FINAL TO BE ATTACHED WITH INDENT

Request For Proposal (RFP)

FOR

PRODUCTIONAND SUPPLY OF LIQUID HYDROGEN, LIQUID OXYGENLIQUID NITROGEN AND HIGH PRESSURE GASEOUS

NITROGEN & HYDROGEN AT IPRC, MAHENDRAGIRI

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CONTENTS

A IntroductionB Eligibility criteriaC Bid submission

D TECHNOCOMMERCIAL PART:

CHAPTER – I : PLANT DESCRIPTION, SCOPE OF WORK AND TERMS & CONDITIONS

CHAPTER – II : CONTRACT COSTS

CHAPTER – III : FACILITY DETAILS

CHAPTER – IV : LIST OF EQUIPMENTS

CHAPTER –V : QUALITY ASSURANCE MANUAL

E PRICE PART:

CHAPTER – VI : FORMAT FOR QUOTATION

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A INTRODUCTION:

ISRO Propulsion Complex is the lead centre of ISRO, responsible for the design, development and realization of liquid Rocket engines and stages required for Satellite Launch Vehicle programmes. ISRO PROPULSION COMPLEX (IPRC) at Mahendragiri is responsible for conducting ground testing of various liquid Rocket engines & stages for qualification, acceptance, development studies etc. and the integration of stages for launch and test purposes. Ground testing programmes require various key facilities for supporting these tests.

Integrated Liquid Hydrogen Plant (ILHP), one among the key facilities, is responsible for

Production of purified Liquid Hydrogen and supply of Ultra high pure Liquid Hydrogen to meet the requirement of GSLV launch to Satish Dhawan Space Centre, Sriharikota Range (SDSC, SHAR).

Production and supply of Cryogenic Liquids like Liquid Hydrogen, Liquid Oxygen, Liquid Nitrogen and High pressure gases.

It is proposed to handover the plant to the successful Bidder, produce cryogenic fluids and high pressure gases and supply to the DEPARTMENT as and when required. This involves operation and maintenance of the following major facilities/system/unit of the PLANT in round the clock basis by the Bidder:

1. Liquid Hydrogen Plant.2. Liquid Hydrogen Purification System.3. Air Separation Unit-I & II.4. High Pressure GN2& GH2 Supply System.5. Liquid Hydrogen pumping system.6. Cryogenic Storage tanks/tankers.7. Utility Systems like DM Plant, CW System, IA system, Effluent

Treatment Plant etc.8. Analytical Laboratory.9. Electrical Substations & DG sets at Plant.10.Main Receiving Station (MRS) with DG sets.

B ELIGIBILITY CRITERIA FOR THE BIDDER:

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1) The bidder should have “minimum five (05) years experience in Operation & Maintenance of Liquid Hydrogen plant and Air Separation Units involving steam reformer, purification and liquefaction of Liquid Hydrogen, Handling of Liquid Nitrogen, Liquid Oxygen & Liquid Hydrogen and generating gases at High Pressure”. The bidder has to submit self attested copies of Work Orders / Agreements / Invoices / Performance Certificates towards proof of this. The Bidder should be financially sound and have annual turnover of minimum Rs 160 lakhs (Rupees one hundred and sixty lakhs) during the last 3 Financial years (FY 2012-13, FY 2013-14, FY 2014-15) and made profit during this period. The bidder has to submit self-attested copies of the Audited Accounts for these three years.(Balance sheet and Profit & Loss account)

2) Bidder shall possess a valid license to carryout electrical works like operation and maintenance of substation including DG sets up to 11KV level supply (‘EA’ grade license of Tamil Nadu Government or equivalent.) issued by electrical license board.

In case the bidder doesn’t possess the valid electrical license, they should submit an undertaking to obtain such valid electrical license and produce to IPRC before commencement of work / mobilization of men and material.

4) The Party/Firm should be registered with the competent authorities, so as to meet statutory requirements of Provident Fund, Labour Department., E.S.I. etc and shall submit the copies of the following for evaluation of ELIGIBILITY CRITERIA of the tenders:ESIC Code Allotment Letter PAN Card Provident Fund Registration Certificate Registration certificate with labour commissioner, Central Government.Work Completion Certificate for similar work in Last 5 Years Work Order Copies for similar work in Last 5 Years. Any Other relevant Documents with respect to the statutory taxes & duties as applicable.Audited account (Balance sheet, Profit/Loss account).

C BID SUBMISSION

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1.0 Refer Attachment -1 for Guidelines EGPS bidding and Attachement-2 for PTE Tender conditions.

2.0 A Pre Bid meeting will be held 30 days before bid submission date at IPRC, Mahendragiri. After tendering, before submission of bid, the bidder may visit the site to fully acquaint himself about the condition in regard to accessibility of site, nature and extent of working condition of site and locality including stocking of materials, tools etc., conditions affecting accommodations and movement of labour, etc., required for the satisfactory execution of the contract. Plant visit and pre bid meeting shall be planned on the same day.

3.0 No price or rate or cost in any nature shall be quoted /mentioned in the Techno commercial Part. It shall be quoted only in the Format for Quotation given Price Part.

4.0 The tender should be submitted in two parts as techno commercial Bid and price bid. Techno commercial part should comprise

Compliance of Eligibility Criteria given in tender with complete documentary proof.

Compliance of RFP and statement showing acceptance of techno commercial part and price part of RFP.

D TECHNO COMMERCIAL PART:

CHAPTER – IPLANT DESCRIPTION, SCOPE OF WORK AND TERMS & CONDITIONS

CONTENTS

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Article 1 DefinitionArticle 2 Plant location and layoutArticle 3 Scope of the BidderArticle 4 Scope of the DepartmentArticle 5 Details of the plantArticle 6 Joint Co-Ordination CommitteeArticle 7 DocumentationArticle 8 Handing over the plantArticle 9 ISO CertificationArticle 10 SafetyArticle 11 Quality Assurance and Inspection of the products Article 12 Terms and Conditions Article 12.1 Statutory Rules and RegulationsArticle 12.2 Taxes & DutiesArticle 12.3 Fixation and Review of Naphtha Consumption NormsArticle 12.4 Price for the Sale to third Agency Article 12.5 InsuranceArticle 12.6 Security DepositArticle 12.7 Secrecy Article 12.8 Force MajeureArticle 12.9 Settlement of DisputeArticle 12.10 ArbitrationArticle 12.11 Effective date and period of ContractArticle 12.12 TerminationArticle 12.13 NoticesArticle 12.14 Authorized RepresentativesArticle 12.15 ChangesArticle 12.16 Entire AgreementsArticle 12.17 MiscellaneousArticle 12.18 Limitation of LiabilityArticle 12.19 Applicable Law and Infringement there ofArticle 12.20 Integrity Pact

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LIST OF ANNEXURES TO CHAPTER – I

Annexure 1.1 Plant LayoutAnnexure 1.2 Assay of Liquid HydrogenAnnexure 1.3 Assay of Liquid NitrogenAnnexure 1.4 Assay of Liquid OxygenAnnexure 1.5 Assay of Gaseous NitrogenAnnexure 1.6 Assay of Gaseous HydrogenAnnexure 2 Documentation and Operating manualAnnexure 3 Details of buildings and Equipments insured for the fire policyAnnexure 4 Bank guarantee for security depositAnnexure 5 Proforma for integrity PactAnnexure 6 Approvals and statutory clearanceAnnexure 7 Tentative list of Inventory of plant including all allied facilities

which will be handed over to BIDDER by the Department and the stock position at the time of handing over.

Annexure 8 List of Approvals & Statutory clearance to be renewed by the Bidder.

ARTICLE 1.0 DEFINITION

This CONTRACT conveys the final Contract between the DEPARTMENT and the BIDDER on the terms and conditions and is a complete and exclusive statement of the terms of the CONTRACT.

WHEREVER used hereinafter in this Contract, the following expression shall have the following meaning:

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“DEPARTMENT ” means the President of India, acting through the Government of India, Department of Space, represented by the Director, ISRO Propulsion Complex (IPRC), Indian Space Research Organization (ISRO), Department of Space (DOS) Mahendragiri post, Tirunelveli District, Tamilnadu State, Pincode-627 133, INDIA.

“SDSC - SHAR” means Satish Dhawan Space Centre, Sriharikota.

“IPRC” means ISRO Propulsion Complex.

“PARTY” means the BIDDER or DEPARTMENT .

“Parties” means BIDDER and DEPARTMENT .

“AGENCY” means THIRD PARTIES PROCURING THE CRYO FLUIDS.

“LH2” means LIQUID HYDROGEN.

“LOX” means LIQUID OXYGEN.

“LIN” means LIQUID NITROGEN.

“GH2” means GASEOUS HYDROGEN.

“GN2” means GASEOUS NITROGEN.

“GOX” means GASEOUS OXYGEN.

“lit” means liters used for measuring Liquid products.

“Cu m” means Cubic meter used for measuring Gaseous products.

“PLANT” means the INTEGRATED LIQUID HYDROGEN PLANT comprising of the complete set of equipments and machineries required for the production, storage, transportation and supply of required quantities of LH2, LOX, LIN and High pressure GN2 & GH2 conforming to the specification and Main Receiving Station with DG sets.

“PROPOSAL” means the offer of the BIDDER submitted to the DEPARTMENT consisting of the technical as well as the commercial details and specification, amendments and clarifications offered by BIDDER up to the date of signing of this Contract.

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“MONTH” means the continuous period commencing from a particular date in a calendar month and ending of the day immediately prior to the corresponding date in the following month.

“WEEK” means a continuous period of seven DAYS commencing from and inclusive of a particular day.

“DAY” means a calendar day.

“CONTRACT OR AGREEMENT” means this AGREEMENT entitled CHAPTER I through CHAPTER VI hereby specified, signed and concluded between the DEPARTMENT and the BIDDER.

“JCC” means Joint Coordination Committee defined in Article 6.0 of chapter-I of this RFP.

“EFFECTIVE DATE” or “EFFECTIVE” means the date upon which this CONTRACT shall become effective.

Unless otherwise indicated, reference in this CHAPTER-I to Articles shall be references to articles of this CONTRACT and words indicating the singular may also include the plural and vice versa as the context requires.

ARTICLE 2.0 PLANT LOCATION AND LAYOUT

2.1 TITLE OF THE PLANT/FACILITY AND OWNER OF PROPERTY:

The Land, Building, Plant, Analytical equipments and Instruments, Utilities and all other equipments and machineries of the DEPARTMENT described in chapter III & IV of this proposal shall be utilized by the BIDDER for the purpose of producing LH2, LOX, LIN and High pressure GH2 & GN2 primarily for the supply to the DEPARTMENT and the surplus if any, with the approval of DEPARTMENT for marketing. The site, equipment

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and machineries belong to and are owned by the DEPARTMENT. But at no time the title or ownership of these facilities shall rest with the BIDDER either legally or contractually, implied or otherwise. All the insurance policies and other related matters should be undertaken by the BIDDER and in the name of Director, IPRC.

2.2 LOCATION

The plant is located at ISRO Propulsion Complex, Mahendragiri which is situated at about 25 kilometers from Nagercoil in Tirunelveli District of Tamilnadu. The site is on the Madurai- Kanyakumari National Highway (NH 7). The nearest Railway Station is Nagercoil on the Southern Railway. The Integrated Liquid Hydrogen Plant is located at a distance of about 1.5 km from the existing main gate of IPRC and Main Receiving Station with DG sets is located in another area at a distance of about 0.4 km from the existing main gate of IPRC.

2.3 PLANT LAYOUT

The PLANT Layout is given in Annexure - 1.1. And the details are given in chapter III. The entire facility is housed in an area of about 15 acres (240 M X 230 M). All the major processing units like Naphtha reformer, Hydrogen gas purifier, Liquid hydrogen cold box, Liquid Hydrogen purification system, Air separation unit, Control room, Analytical Laboratory, Storage tanks and Transport Tankers are located inside the plant battery limit. Utility units like process/DM water plant, Instrument air unit, Cooling water system etc., and auxiliary facilities like fire fighting section, effluent treatment plant, Security, Maintenance shop, Office building etc, are located outside the battery limit. The plant area is connected to the other ISRO facilities in the complex by an approach road.

ARTICLE 3.0 SCOPE OF THE BIDDER

3.1 The Bidder shall undertake the entire responsibility for operation, maintenance and repairs of PLANT including utility units and transport tankers with prime movers on round the clock basis maintaining raw material (Naphtha) consumption of 0.52 Kg/lit of LH2, procurement of raw materials, Production & supply of cryogenic fluids (LH2, LIN, LOX and High pressure GN2& GH2) as and when required, transfer of

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cryogenic liquid between tankers, analysis of inter streams, product and others samples, Effluent treatment and disposal at identified areas inside plant, procurement of plant spares, arranging AMCs for equipments, maintenance services and Transportation and delivery of cryogenic fluid to Department’s sites at Mahendragiri as well as outside Mahendragiri. Maintenance of Fire protection system, Fire hydrant and incipient firefighting shall also form part of the scope.

3.2 The BIDDER shall mobilize their man-power, at least to the minimum requirement of human resources as given in appendix-1 of chapter –II, to carry out the shift operations, maintenance works, special maintenance works etc., as per the scope contained in this article and provide them with all welfare measures and Insurance coverage. The team shall carry out entire scope of the Bidder given in this Article 3.0 of this chapter I. All the equipments are to be maintained in house utilizing the manpower deployed by the bidder. Generally AMC shall be entered for the special equipments given in Article 3.0 & Appendix-4 of chapter–II. Tentative list of maintenance services which can be availed from outside parties is given in Article 3.0 & Appendix-4 of chapter –II. Any other requirements of AMC & maintenance services shall be addressed in JCC and decided. The BIDDER shall also provide his employees with all statutory amenities, conforming to the various Regulations and shall be solely liable for their staff and other labourers, either engaged directly or on sub-contract or daily wages, including payment of wages and providing facilities and amenities and complying with the payment of wages Act, workman’s compensation Act and all other laws applicable and incidental to the deployment of man (which expression shall include women also) employed or engaged by them. The entire scope of work will involve operation of the various units of the plant as and when required by Department and production & supply of LIQUID HYDROGEN, LIQUID NITROGEN AND LIQUID OXYGEN & HIGH PRESSURE GASES and overhauling, repair & maintenance. This involves deployment of operation team in addition to maintenance team for overhauling, repair & maintenance during non-production time or during planned shut down time.3.3 Grass cutting and bush clearance, Maintenance of internal security and safety are also the responsibilities of the Bidder.

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3.4 The BIDDER shall be responsible to pay the license fees, permit fees etc., for obtaining and to renew the same, for the operation of the plant and tankers used for transportation of products. The tentative list of approvals and statutory clearance to be renewed by the Bidder on annual basis is given in Annexure-8.

3.5 The BIDDER shall carry out operation and maintenance works on all facilities (at plant) including

1. Liquid Hydrogen Plant. 2. Liquid Hydrogen Purification System.3. Air Separation Unit-I & II.4. High Pressure GN2& GH2 Supply System.5. Liquid Hydrogen pumping system.6. Cryogenic Storage tanks/tankers.7. Utility Systems like DM Plant, CW System, IA system, Effluent

Treatment Plant etc.8. Analytical Laboratory.9. Electrical Substations & DG sets at Plant.

The BIDDER shall carry out operation of the Main Receiving Station (MRS) along with the 3 nos of DG sets and carry out the minor maintenance. The supply of diesel, spares and consumables for the DG sets and substation at MRS shall be the responsibility of the Department .The supply of spares and consumables for the facilities at plant except DG sets and substation at MRS shall be the responsibility of the BIDDER. Tentative list of spares which can be availed from outside parties given in Article 3.0 & Appendix-3 of chapter –II. Any other requirement shall be addressed in JCC and decided. 3.6 The bidder shall be responsible for the security/insurance of their staff working at site. DEPARTMENT shall not be responsible in any manner in case of any accident/ disputes amongst the employees of Bidder.3.7 Bidder should follow all safety norms and provide necessary safety equipments at his own cost. In case of any accident during the operation & maintenance of the equipment leading to injuries /damaged to human beings equipments and / or loss of life, the Bidder shall be fully responsible for settlement of all claims and indemnify DEPARTMENT against any claims arising out of such incidents.

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3.8 The Bidder shall be responsible to provide group accidental insurance to its employees and in case of any accident occurring to any of the employees engaged by the Bidder, no compensation shall be payable by the DEPARTMENT . The Bidder on demand from DEPARTMENT shall have to produce the copy of the valid insurance policy, covering the names of the employees engaged by him. The Bidder shall also be responsible for the safety of his employees and in case of any safety threat from public, natural calamity or otherwise causing harm to his employees, DEPARTMENT will not be liable for any compensation to the Bidder and his employees.

3.9 The Bidder shall be responsible for Procurement and supply of Chemicals, Oil & Consumables, Tyres, Spares, AMC, statutory fees and providing Maintenance Services and related administrative support.

3.10 The Bidder shall provide an exclusive light vehicle of category like Tata sumo Mahindra Bolero etc… at the plant on round the clock basis for internal transportation of men and material and it is a mandatory safety requirements. The drivers included in human resources to be deployed as per appendix-1 of chapter-II shall be utilized for operation of the exclusive light vehicle and movement of tankers on round the clock basis.

3.11 The Bidder shall be responsible to provide administrative support like transport for their men and materials, Staff Welfare measures, Communication Expenses including telephone charges & postage/ courier charges, Office Maintenance including printer cartridges, computer maintenance, paper & stationeries, General Administration etc….DEPARTMENT will not provide food, transport, accommodation (except office space at plant) and STD Telephone for the Bidder & his team in connection with O & M of the plant. The administrative expenses and overheads defined in article 1.1 of chapter-II shall include the above, all others required for carrying out the scope of contractor defined in this article 3.0 and overhead expenses for arranging AMC as per appendix-4 of chapter-II and arranging statutory inspection and payment of statutory fees as per appendix-5 of chapter-II. This shall include all overhead expenses for arranging inspection of Naphtha storage tank from-District collector and obtaining Naphtha purchase license (once in 2 years) from District collector, Tirunelveli, arranging inspection of Boiler from inspector of Boiler, Madurai every year and arranging renewal of license from PESO, Chennai. However the

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overhead expenses for Procurement and supply of Chemicals, Oil & Consumables, Tyres, Spares, and providing Maintenance Services is covered in article 3.0 of chapter-II.

ARTICLE 4.0 SCOPE OF THE DEPARTMENT

4.1The DEPARTMENT shall provide water, electricity and Diesel for running DG sets required for the operation and maintenance of the plant at free of cost. The DEPARTMENT shall put their best effort to ensure uninterrupted power supply to ILHP. The Department shall take care of the incoming HT feeder for power supply.

4.2 The DEPARTMENT shall arrange necessary security of the plant.

4.3 All the necessary approvals of Local Authorities and all the necessary clearance and licenses that may be required for operating the plant including LH2 Tanker, LOX Tanker and LIN Tankers shall be provided by the DEPARTMENT. Necessary license from the Ministry of petroleum for the procurement of Naphtha shall be provided by the DEPARTMENT. The list of approvals and statutory clearance are given in Annexure-6. The DEPARTMENT shall assist the BIDDER for the renewals of the licenses. However the Bidder shall be responsible to pay the license and permit fees for their renewal during the period of this CONTRACT as indicated in the Article 3.0 0f Chapter –I.

4.4 The DEPARTMENT shall provide Plant, Equipments/ machineries and Analytical Laboratory Equipments and other infra structural facility required for the plant operation and maintenance as per the details given in chapter III & IV.

4.5 The Department shall pass on any technology developed by it to improve the plant performance, provide additional equipment to realize increase in production and reduction in consumption of raw materials and shall demonstrate the know-how jointly with the Bidder.

4.6 The Department shall inspect the product and conduct quality control checks as and when required.

4.7 Hydrogen gas required for Hydrogen plant start up shall be taken from the charged cylinder skid available at the plant or from the LH2 tanker.

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4.8 REPAIR/REFURBISHMENT.Considering the fact that the age of the plant crossed 20 years, if any

repair/refurbishment of the plant Unit/equipment/machinery, is considered essential during the contract, proposal shall be submitted to JCC. Depending upon the urgency of the requirements, JCC will decide either one of following mode of implementation.

Department may provide materials for repair/refurbishment, execution shall be carried out by the Bidder through outside sources. The cost for execution shall be mutually agreed upon before execution through JCC.

Bidder shall procure the materials & carry out the repair/refurbishment in total. In such case Bidder shall submit a proposal to JCC before implementation.

Department may carry out the repair/refurbishment in total.

ARTICLE 5.0 DETAILS OF THE PLANT

5.1 Design plant Specification

Production capacity with 24 hours of production per day and 300 production days per annum:

Sl.No

Unit Fluid Production capacity Tonnes/annum

Purity % by volume

Production rate

Specification

1 Liquid Hydrogen (LH2)plant

LH2 150 99.995 300 lit/hr Annexure 1.2

2 Air Separation Unit-I

LIN

LOX

2495

600

99.8

99.75

477 lit/hr

75 lit/hr

Annexure 1.3& 1.4

3 Air Separation Unit-II

LIN 5100 99.8 1000 lit/hr Annexure 1.3

High Pressure GN2 supply system

GN2 5100 99.8 400 Nm3/hr Annexure 1.5

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4 High Pressure GH2 supply system

GH2 96 99.995 150 Nm3/hr Annexure 1.6

5.2 STORAGE CUM TRANSPORTATION CAPACITY

(a) One storage and feed system for feed naphtha of 60,000(sixty thousand) lit volumetric capacity as per the specifications contained in chapter III of this Contract.

(b) One storage tank for process feed water of 10,000(Ten thousand) lit of volumetric capacity as per the specifications contained in chapter III of this Contract.

(c) One storage and transfer system for LIN of 43,000 (Forty three thousand) lit of volumetric capacity as per the specifications contained in chapter III of this Contract.

(d) One storage and transfer system for LOX of 26,000 (Twenty six thousand) lit of volumetric capacity as per the specifications contained in chapter III of this Contract.

(e) 3 (three) numbers storage cum transport tankers for LH2 each of 41,600 (forty one thousand six hundred) lit of volumetric capacity as per the specifications contained in chapter II of this Contract.

(f) 2 (Two) Number transport tankers for LIN each of 13,000 (Thirteen thousand) lit of volumetric capacity as per the specifications contained in chapter III of this Contract.

(g) One transport tanker for LOX of 13,000 (thirteen thousand) lit volumetric capacity as per the specifications contained in chapter III of this Contract.

(h) 2 (Two) Numbers transport tankers for LIN/LOX each of 6000 (Six thousand) lit of volumetric capacity as per the specifications contained in chapter III of this Contract.

(i) 1 (one) number storage tank for LH2 of 125,000 (One lakh twenty five thousand) lit of volumetric capacity as per the specifications contained in chapter III of this Contract.

(j) 2 (two) numbers storage tanks for LIN/LOX each of 75,000 (seventy five thousand) lit of volumetric capacity as per the specifications contained in chapter II of this Contract.

(k) 2 (two) numbers storage cum transport tankers(Air Liquid make) for LH2 each of 40,000 (forty thousand) lit of volumetric capacity& Two numbers of LIN/LOX tankers of 10,000 lit volumetric capacity as per the specifications contained in chapter III of this Contract.

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(l) 1(one) number storage cum transport tanker (Gardner Cryogenics make) for LH2/LHe each of 41,600 (forty one thousand six hundred) lit of volumetric capacity as per the specifications contained in chapter III of this Contract.

5.3 CONSUMPTION RATES:

The Design consumption rates of raw materials and utilities are:Naphtha : 110kg/hrDM water (Boiler feed) : 550kg/hrDM water circulation for cooling : 160cu. m/hrInstrument Air : 110NM3/hrPower : 2000KVA

5.4 FACILITY DESCRIPTION

The Integrated Liquid Hydrogen plant consists of various facilities/major systems/units. The detailed description of each one of these facilities/major systems/units including buildings and list of individual Equipments and systems are given in chapter III. The list of individual equipments / systems is given in chapter IV.

ARTICLE 6.0 JOINT CO-ORDINATION COMMITTEE (JCC)

A Joint Co-ordination Committee (JCC) consisting of seven nominees of the DEPARTMENT and five nominees of the BIDDER shall be constituted by the Director, IPRC. The JCC shall meet at least once in six months and the venue shall be IPRC.JCC is only a recommending body and decisions /recommendation shall be implemented with the approval of Director, IPRC if it is applicable as per the contract and with the approval of the Department in case of amendments.

This Co-ordination Committee shall:

Monitor PLANT operation, production schedule, ISRO’s off take, sales if any to third party and man power utilization.

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Resolve any issues arising out of the administration, security, insurance, operation and maintenance of the PLANT.

Any deviation or any modifications called for towards operation of the plant and or logistics shall be first projected to the Joint Coordination Committee before implementation.

Any augmentation to the PLANT, existing establishment etc. should be discussed in the JCC meeting before proceeding with such proposals.

Decide on the quantity and cost of following to ensure uninterrupted Operation & maintenance of the plant.i. Repair/Refurbishment requirements of plant and prime movers & trailers of

tankers as per article 4.4 of chapter II.ii. Procurement and supply of Chemicals, Oil & Consumables, Tyres, Spares, AMC,

statutory fees and providing Maintenance Services as per Article 3.0 of chapter-II

iii. Major maintenance requirement of prime movers & trailers of tankers as per article 4.4 of Chapter-II.

iv. Fixation and review of Naphtha consumption norms as per article 12.3 of this chapter- I

ARTICLE 7.0 DOCUMENTATION.

The major documents consisting of the equipment details specifications, and operating manuals are given in Chapter-IV. The operating personnel shall follow the various instructions given in the operating manual. It will be handed over at the time of award of contract. The Bidder shall maintain the data acquired by Distributed Control System in Electronic form for Air separation plants, printed log sheets duly approved by DEPARTMENT for recording hourly readings of operational parameters of entire plant with different equipment / panels etc. and maintenance documents in compliance with ISO requirements. The detailed operation & maintenance log sheet & data shall be provided by the Bidder to the DEPARTMENT at end of each month and also as & when desired by the DEPARTMENT. The Bidder shall maintain data of plant Operation & Maintenance, list of deviations, log books, shift register, safety register etc. as per the format approved by the

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Department. The inventory of spares, chemicals and consumables, oil & naphtha, diesel, products shall be maintained on daily basis with details of Receipt and consumption details.

The Bidder shall provide adequate number of operational and maintenance staff as mentioned in the RFP and shall display the name of the person on duty along with name of Bidder, Supervisor and Engineer In charge on a Board easily visible inside plant control room. The Bidder shall maintain IN time and OUT time punching of all operational and maintenance staff at the plant entrance. The data shall be provided by the Bidder to the DEPARTMENT at the end of each month and also as & when desired by the DEPARTMENT.

ARTICLE 8.0 HANDING OVER THE PLANT

At the time of handing over the plant in case of awarding the contract, the inventory of plant including all allied facilities shall be checked jointly by the Department and the Bidder and operating condition and technical details recorded and signed by the authorized representatives of the Department and the Bidder. Any inventory added to the plant by the Bidder/ the Department during the period of the agreement shall also be recorded separately. These records shall be the document to check the inventory at the time of either completion or termination of the contract. The tentative list of inventory of the plant including all allied facilities to be handed over to BIDDER by the Department and format for the stock position at the time of handing over is given in Annexure - 7.

ARTICLE 9.0 ISO CERTFICATION

The Plant is ISO 9001-2008 certified. The BIDDER shall maintain documents as per the divisional quality manual prepared and approved based on ISO 9001-2008 requirements. The Bidder shall comply with ISO 9001-2008 requirements and co operate with teams of internal audit and external audit.

ARTICLE 10.0 SAFETY

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The Bidder is responsible for safety of the plant and their personnel. The Bidder shall ensure process safety as given in the operating manuals and safety documents. The Bidder shall identify one safety focal point with PG Diploma in safety well versed in Operation & Maintenance safety of the PLANT. The Bidder shall strictly follow the safety instruction of Department and maintain safety register. Bidder shall coordinate with Department’s safety division for safety audit & safety review and implement their suggestions for improving safety of the plant.

ARTICLE 11.0 QUALITY ASSURANCES AND INSPECTION OF THE PRODUCTS.

11.1 FOR ISRO’s OFF-TAKE

Quality assurance of the product shall be performed by the BIDDER in accordance with the Quality assurance system given in the Quality assurance manual and related procedures shall be carried out by the DEPARTMENT for its take off. The indicators provided in the DEPARTMENT’s tankers shall be used for measuring the quantity. The measurement shall be carried out at the plant immediately after filling and before the tankers leave the premises. At ILHP premises each tanker load meant for the DEPARTMENT shall leave plant premises only after the acceptance certificate is issued by the DEPARTMENT. All the Documents shall be written in English language and metric system of measurements shall be used exclusively in this CONTRACT. Liters for liquid products and normal Cum. for gaseous products shall be used.

ARTICLE 12.0 TERMS AND CONDITIONS

12.1 Statutory rules and regulations:

12.1.1The Bidder shall comply with all the statutory rules and regulations like provisions of the Minimum Wages Act, Electricity Act and the Regulations, Boiler Act and the Regulations, Contract Labour Act and rules framed there under and other laws including labour laws affecting contract labour that may be brought into force from time to time.

12.1.2 The Bidder must ensure, the payment of prevailing State Government monthly minimum rates of wages promulgated by the Labour Commissioner, TamilNadu/Central govt.

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12.1.3 The Bidder shall employ qualified/trained persons for operation & maintenance of the equipment and shall be fully responsible to obtain such license for taking up the above work as prescribed by the state / local bodies/ELECTRICITY BOARDS / Pollution control board/OTHER STATUTORY REGULATIONS both for execution and operation & maintenance and will be responsible for the same from time to time during the term of the contract. Bidder shall be responsible for any periodic statutory inspection to be carried out on the equipment, necessary test report and certificate, rectification of defects pointed during such inspection etc. A failure to comply with this clause by the Bidder will render him liable for payment of all penalties imposed by the staff / local bodies and the inspection and/or subsequent rectification will be carried at their risk and cost.

12.2 TAXES & DUTIES

The Department shall pay all the applicable statutory taxes and duties mentioned in the Price bid of chapter –VI. Additional taxes if any imposed and found applicable during the period of the contract will be reimbursed subject to clearance by the Department at actual against documentary evidence. For third party sales if any, the BIDDER is responsible to collect the necessary taxes and duties from the buyer and pay to the concerned Government authorities. For the purpose of this Article the BIDDER as referred to therein shall include any sub-Bidders employed, any distributing agencies for any entity engaged by the BIDDER.

The statutory deductions on account of Income tax shall be made as per the extant provisions contained in the Indian Income Tax Act, 1961 and tax deducted-at-source certificate will be issued to the Bidder.

Excise Duty Exemption Certificate will be provided by Department only for the supply of items consigned to IPRC Mahendragiri against pro forma invoice submitted by the Bidder.

Custom Duty Exemption Certificate will be provided by Department for those imported items consigned to IPRC Mahendragiri against pro forma invoice submitted by the Bidder.

It is the responsibility of Bidder to avail Custom Duty and Excise Duty Exemption.

12.3 FIXATION AND REVIEW OF NAPHTHA CONSUMPTION NORMS

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The Naphtha consumption norm shall be 0.52 kg/lit of LH2 produced. Naphtha consumption shall be reviewed and re-fixed as per the following procedure, for the operation with existing NEA and DR Hydrogen compressors.

a. From maintenance to maintenance shall be the period to be considered generally for fixing Naphtha consumption norm. “Maintenance” means the complete gas side overhauling of the Hydrogen gas compressor. The main NEA compressor shall be taken up for overhauling if the collection rate of LH2 is reduced to 200 lit./hr. due to wear of the sealing elements of the Hydrogen compressor.

b. The average consumption of Naphtha (Total Naphtha consumed ÷ LIQUID HYDROGEN produced) during the above said period shall be worked out and the same shall be the basis for the subsequent period of operation.

c. The calculated average naphtha consumption norm shall have a tolerance limit of ±5%. Any increase /decrease outside this tolerance limit of ± 5% shall be jointly analyzed and, the reasons for the deviation will be identified by the DEPARTMENT and the BIDDER. If the reasons are attributable to the Department for exceeding the positive (+) tolerance limit, the Bidder shall be suitably compensated. If the reasons are attributable to the Bidder, the Bidder shall not be compensated. In case the negative (-) tolerance exceeds the limit due to the reasons attributable to the Department and/or the Bidder, the value shall be taken for the subsequent period of operation. However in either case the decision shall be taken with the recommendation of JCC

d. While fixing specific consumption for the subsequent period of operation the following shall be adhered.

i. If the average consumption worked out is within the tolerance limit, the same shall be consumption norm for subsequent period.

ii. In case the tolerance limit of ±5% is exceeded, the reasons shall once again be jointly reviewed. If there is increase in consumption norm in any of the batches due to unforeseen malfunction, operating condition, failure or other, then the specific consumption for that particular batch shall be ignored. The specific consumption for the previous batch shall be taken in to calculation for fixing the average consumption norm. However incase of any event, which are of recurring type, the same shall be considered for fixing the new consumption norm.

22

e. Normally the average consumption of Naphtha shall be worked out as envisaged above (a to d).However consequence to any modification/ improvement/ augmentation to the plant the consumption norm may be improved. In such occasion the stable operation of the plant shall be monitored and subsequently the consumption norm achieved during this period shall be adopted, and shall be ratified by the JCC, with retrospective effect and shall be implemented from the stable period of operation of plant.

f. In case of Specific Naphtha consumption norm calculated in any batch is more than 0.52kg/lit of LH2 and the increase due to Major break down of equipment not attributable to lack of operation and maintenance on the part of contractor, production of Liquid Hydrogen less than 3 full tanker loads excluding Gaseous Hydrogen supply from Reformer unit and long power shut down of 6 hours or more affecting Liquid Hydrogen production shall be discussed in JCC and decided.

12.4 PRICE FOR THE SALE TO THIRD AGENCY

The BIDDER shall market excess production if any, at a price with the approval of the DEPARTMENT to third agencies and the sales value shall be paid to the DEPARTMENT by the BIDDER. The prices for the sale of LH2/LOX/LIN to third agencies if any shall be fixed after taking in to account the prevailing market price and the production cost. It is specifically agreed that the BIDDER shall extend their full cooperation to the DEPARTMENT by way of exploring the market potential and in fixing the price. Regarding sale of LH2/LOX/LIN to third agencies if any, the service charges shall be mutually discussed and decided.

12.5 INSURANCE

The Bidder shall arrange insurance to cover the cost of the plant as a whole and the insurance shall cover for Earth quake, fire, terrorism of buildings, STFI (Storm, Tempest, Flood & Inundation) of plant and machineries, motor policy for cryogenic tankers and public liability. The motor policy for LH2/LOX/LIN cryogenic tankers going on public road shall be comprehensive insurance policy. Department will contact the public sector insurance companies & obtain competitive offers, finalize if required or

23

advise for renewal of such finalized policy for subsequent years in case of same scope and communicate the insurance company & premium amount to the bidder and Bidder shall take the insurance policy. The insurance premium payable shall be paid at actual against documentary evidence. The insurance policy shall be in favor of the Department and the original policy deposited with the Department and shall be renewed periodically by the Bidder. The compensation, if any, paid by the insurance company in case of any claim, shall be paid to the Bidder by the Department once the repair/ replacement is completed. JCC shall also finalize the mode of payment of insurance premium and the mode of handing over the money received by the DEPARTMENT from the insurance company to the Bidder to meet the expense for the repair/replacement. For the purpose of taking the insurance, the breakup of the capital cost is given in Annexure-3. The Bidder shall arrange their own insurance cover at bidder’s cost for their personal involved in the operation of the plant.

12.6 SECURITY DEPOSIT.

The Bidder shall furnish security deposit for an amount equivalent to 10% of total annual contract cost valid during the period of the contract towards the performance of the contract by providing bank guarantee from any nationalized/scheduled bank approved by RBI in favor of the Department. The bank guarantee shall be submitted by the Bidder with in fifteen days from the date of signing of the CONTRACT. The format for the bank guarantee is given in Annexure-4. In case of non-performance of the Bidder or irreparable damages caused to the plant on the part of the Bidder, the security deposit will be revoked by the DEPARTMENT.

12.7 SECRECYAny details and data furnished to the BIDDER out of or in connection with this

AGREEMENT shall be treated as confidential and shall not be divulged by the BIDDER to any third party or otherwise made public without prior written consent of the DEPARTMENT. Likewise any details and data furnished by the BIDDER to the DEPARTMENT out of or in connection with this AGREEMENT shall be treated as confidential and shall not be divulged by the DEPARTMENT to any third party or otherwise be made public without prior written consent of the BIDDER. The BIDDER and

24

DEPARTMENT shall not disclose the terms and conditions of this AGREEMENT to third parties without prior written consent of the other PARTY except as required under any law for the time being in force or due to any statutory requirement.

The foregoing provisions of confidentiality shall not end on termination of this AGREEMENT. However, they do not apply to information and data which were already in DEPARTMENT `s possession prior to disclosure thereof, and were not acquired from the BIDDER, or technical information and data that is in the public domain.

12.8 FORCE MAJEURE

Neither the DEPARTMENT nor the BIDDER shall be considered in default in performance of the obligations under the terms of this agreement, from the happening of the event and the notice to be served if such performance is prevented or delayed for any causes beyond the control of the party affected, such as war, hostilities, revolution, riots, civil commotion, strikes, lock-outs, epidemic fire, accidents, floods, earthquake or because of any law and order, proclamation or regulation or ordinance of any Government or Sub division thereof or because of any Act of God, provided notices in writing of any such cause with necessary evidence that the obligation under the agreement thereby affected or prevented or delayed is given within 30 days. As soon as the cause of Force Majeure ceases to exist, the party whose ability to perform its obligation has been affected, shall notify and establish the other party, the actual delay occurred with documents to substantiate the same.

12.9 SETTLEMENT OF DISPUTE

Any dispute or difference including those considered as such by only one of the parties arising out of or in connection with this CONTRACT shall be, to the extent possible, settled amicably between the parties represented by the CONTRACT managers. In case the contract managers could not resolve the issues, the same shall be presented to the Joint Coordination Committee (JCC) for sorting out the issues. In case, if amicable settlement cannot be reached, then all disputes shall be referred to arbitration by a person decided upon by the Secretary, Department of Space, Bangalore, in consultation with the Chairman/CMD of Bidder.

12.10 ARBITRATION

25

In the event of a dispute or difference arising of or in connection with this AGREEMENT which cannot be resolved by amicable settlement within 90 days after the formal written notice of the dispute / disagreement by one party to the other, the same shall be referred to and arbitrated. The arbitrator shall be appointed by the secretary, Department of Space, Govt. of India in consultation with Chairman/CMD of Bidder. In case an acceptable person as arbitrator is not possible, then the Arbitration shall be as per the Arbitration and conciliation Act of India 1996. Either party shall give notice to the other regarding its intention to refer the matter to the arbitration.

12.11 EFFECTIVE DATE AND PERIOD OF CONTRACT

The contract shall become effective from the date of signing the agreement and shall be valid for a period of 5 (five) years. However, if the DEPARTMENT so wishes, the agreement shall be extended by a further period of 5 years on the same agreed terms and conditions at the end of 5 years period. Department reserves the right to extend the contract after 5 years from the date of signing of the contract or close the contract without assigning any reason.

12.12 TERMINATION

The DEPARTMENT may, on giving 90 days written notice of the default to the BIDDER, terminate the Contract in whole or in part, in any of the circumstances in which the BIDDER fails to fulfill the contractual obligations contained in this Contract. In the event of the DEPARTMENT terminating the Contract in whole or in part as provided in this ARTICLE ,the DEPARTMENT reserves the first option to purchase the raw materials from the BIDDER on mutual agreed price. In case the DEPARTMENT is not procuring the same, the BIDDER is free to sell the same to third parties within a stipulated period with written consent of the DEPARTMENT. In the event the DEPARTMENT does not terminate the Contract (due to the Bidders default, as provided in this ARTICLE, the BIDDER shall continue with and complete the contractual obligations after correcting the default .The BIDDER may, on giving 90 days written notice, terminate the Contract in whole or in

26

part, in any of the circumstances in which the DEPARTMENT fails to fulfill the contractual obligation contained in this Contract.

Before the termination comes into effect, the DEPARTMENT has the right to ascertain the physical and operating efficiency of the PLANT. The findings of the DEPARTMENT shall be reviewed by the Joint-Co-ordination Committee to settle any outstanding issues.Upon termination of the CONTRACT, the DEPARTMENT shall not be liable to accept any

liabilities of the BIDDER, legal or otherwise including that of the BIDDER’S personnel, sub Bidders etc.Upon termination, the BIDDER shall not dispose of the plant or any of the equipment,

machinery, utilities, communication and transport facilities deployed by the DEPARTMENT as well by the BIDDER for the operation and maintenance of the PLANT and for the distribution and marketing of the products to the DEPARTMENT as well as to the third agencies before the details are referred and decided by the Joint Coordination Committee for appropriate decision. For any damages / shortages / losses noticed on the list of the inventory, on completion of the valid CONTRACT period or on termination of the CONTRACT, the BIDDER shall compensate the DEPARTMENT in full, subject to normal wear and tear.

12.13 NOTICES

Any notice required or authorized to be given by either PARTY to the other shall be in writing and shall be dispatched by registered airmailed letter sent to the Chairman/CMD of Bidder and Director, IPRC as set forth herein below.The post mark date shall be considered as the official date of notice. For reasonable cause, such as mail strikes, other forms of reasonable notice may be used and shall constitute notice.

12.14 AUTHORISED REPRESENTATIVES

The CONTRACT managers of the BIDDER and the DEPARTMENT shall be the authorized representative/s who shall have the full authority to act on behalf of the BIDDER/DEPARTMENT respectively for the purpose of this Contract.

12.15 CHANGES

27

The BIDDER is not allowed to do any changes or modification in the PLANT without prior concurrence and written permission of the DEPARTMENT. Any changes necessitated by changes in laws, regulations, codes and standards shall be deemed as changes requested by DEPARTMENT and shall be carried out after detailed discussions and mutual AGREEMENT.12.16 ENTIRE AGREEMENTS

The agreement made between the DEPARTMENT and the BIDDER contains the entire understanding between the PARTIES in respect of the subject of the AGREEMENT and may be amended or altered in future only in writing, duly executed by authorized representative of each of the PARTIES. There are no terms, obligations, covenants, representations, or conditions other than those contained in this AGREEMENT. No variation or modification of this AGREEMENT or waiver of any of the terms and provision hereof shall be deemed valid unless made in writing and signed by both the PARTIES here to. The BIDDER conveys the final AGREEMENT between the DEPARTMENT and the BIDDER on the terms and conditions and is complete exclusive statement of the terms of the CONTRACT. The AGREEMENT shall be prepared in DUPLICATE and both shall form the authenticated document.

12.17 MISCELLENEOUS

If any stipulation or stipulations of this AGREEMENT should be or should become void in whole or in part, this shall not affect the validity of the AGREEMENT as a whole. Both PARTIES shall in such case be obliged to make an arrangement to replace any possible inoperative stipulation by another stipulation which shall be valid and which shall best suit the economical purpose of said inoperative stipulation. Additional cost resulting from recommendations or requirements imposed by the DEPARTMENT, other than those already covered in this AGREEMENT, shall be paid by the DEPARTMENT. The possible effects on additional cost, Delay in delivery or changes of guaranteed product specifications and liabilities resulting from such recommendations or requirements, shall be agreed upon by the PARTIES on case to case basis.

28

The failure of either PARTY hereafter at any time to enforce any of the terms, provisions or conditions of this AGREEMENT shall not be constructed as a waiver of the same or of the rights of either PARTY to enforce the same on any subsequent occasion.Neither of the PARTIES shall transfer or assign their respective rights and obligations under this AGREEMENT to third parties without the prior permission of the other PARTY in writing, excepting assignments which may be made by BIDDER for refinancing and credit insurance purposes. In the event of any assignment, the assigner and assignee shall be jointly and severally liable. The AGREEMENT shall be prepared in DUPLICATE, each of which is considered as ORIGINAL.

12.18 LIMITATION OF LIABILITY

The BIDDER shall take complete responsibility towards the operations and maintenance of the PLANT, including all the manpower required for this purpose. The DEPARTMENT has neither any commitment nor any liability what so ever towards these requirements, except those identified specifically under article 4.0. The BIDDER expressly indemnifies the DEPARTMENT from any type of claims from the BIDDER’S personnel or any of his sub-Bidder, deployed/employed for the PLANT activities. Due to the negligence on the part of the contractor in not following the documents, Safety rules & Standards etc..the BIDDER shall be liable. In addition to the liabilities mentioned in this RFP, the liabilities of bidder shall include the following:12.18.1 The BIDDER is legally bound and liable for all the liabilities and legally responsible for the discharge of the responsibilities, connected with the scope of the operation of this CONTRACT. Any litigation, either directly or indirectly connected with the discharge of the scope by the BIDDER during the contract period or after termination, incidental to plant operation during the validity period of the contract shall continue to rest with the BIDDER. The BIDDER shall not transfer, sub-let or assign scope of operation of the PLANT, maintenance, distribution and marketing of the product to another company or their subsidiary without the written consent of the DEPARTMENT.12.18.2 The facilities, buildings and other inventory including utilities assigned to the BIDDER are meant for the discharge of the scope of the CONTRACT by the BIDDER and the BIDDER shall have no right whatsoever to sell or transfer any of the listed inventories to any of their companies or to third parties or to put them to use for any other purpose.

29

12.18.3 The Bidder shall make good all the damages caused to the system or part of it of the plant due to faulty and negligent operation. And at the end of contract period, the Bidder shall hand over plant and all equipment in the contract scope in good working condition. Any material required for making good the damages shall be brought by the Bidder at his own cost and risk, and such material shall be of proper brand and of good quality. In case the damages cannot be made good, the DEPARTMENT will recover the cost of the damaged system or part of it of the plant from the bidder.

12.18.4 The BIDDER has all the rights of an assignee for discharging the scope of work specified in this CONTRACT during the validity of this CONTRACT. All the rights of the BIDDER Ipso facto shall cease on the date completion of 5 (five) years from the effective date of contractor on the date of termination of the CONTRACT unless otherwise the CONTRACT is renewed as per Article-12.11.

12.19 APPLICABLE LAW AND INFRINGEMENT THERE OF

The contract shall be governed by and interpreted and construed in accordance with the laws of India. The BIDDER shall indemnify the DEPARTMENT and be so solely responsible for infringement of any law of the states in force during the tenure of the Agreement by the Bidder.

12.20 INTEGRITY PACTIf the value of any procurement is above 10.00 crores (Rupees ten crores only), it

would be mandatory to sign the Integrity pact with the tenderer/contractor as per proforma given in Annexure-5. In witness Where of the parties set to this agreement on………….day of……………2016

1. For & on behalf of 2. For & on behalf of The President of India, BIDDER

Represented by Represented by

Director, IPRC BIDDER

WITNESS WITNESS

30

1. 1.

2. 2.

31

32

ANNEXURE 1.2

ASSAY OF LIQUID HYDROGEN

A) Assay

- Hydrogen (H2) – percent (%) : 99.995Volume, minimum, by difference

- Parahydrogen % by volume minimum : 95.00 (Balanceortho hydrogen)

B) IMPURITIES

-Total gases – PPM by volume max. : 50.00-Nitrogen, moisture and volatile hydrocarbonscombined PPM by volume maximum. : 9.00-oxygen plus Argon – PPM volume max. : 1.00-Helium –PPM by volume max. : 39.00-Carbon monoxide plus carbon dioxidePPM by volume max. : 1.00

C) PARTICULATES 10 microns nominal filter at plant outlet.

33

ANNEXURE 1.3

ASSAY OF LIQUID NITROGEN

A) Assay

- Nitrogen percentage by volume min : 99 .8

B) IMPURITIES - Argon PPM by volume max. : 1000- Water PPM by volume maximum. : 5- Oxygen PPM by volume max. : 50- Hydro carbons –PPM by volume max. : 5- Hydrogen PPM by volume max. : 5

C) PARTICULATES 10 microns nominal filters to be provided at the outlet of the tank.

34

ANNEXURE 1.4

ASSAY OF LIQUID OXYGEN

A) Assay

- Liquid oxygen (LOX) percent (%) by : 99.75Volume, minimum

B) IMPURITIES - Argon percentage by volume max. : 0.0 to 0.05- Nitrogen, percentage by volume : 0.0 to 0.05- Water PPM by volume : 1 to 5- Carbon monoxide PPM by volume max. : 5- Volatile hydrocarbons (mostly propane, propylene

and heavier saturates ) PPM by volume max. : 2.00- Acetylinichydrocarbons PPM by volume : 0.05 to 0.1

C) PARTICULATES 10 microns nominal filters to be provided at the out let of the tank

ANNEXURE 1.5

35

ASSAY OF GASEOUS NITROGEN

A) Assay

- Nitrogen percentage by volume min : 99 .8

B) IMPURITIES - Argon PPM by volume max. : 1000- Water PPM by volume maximum. : 5- Oxygen PPM by volume max. : 50- Hydro carbons –PPM by volume max. : 5- Hydrogen PPM by volume max. : 5

- Oil content mg/m3 by volume max. : 3

C) PARTICULATES 10 microns nominal filters to be provide at the outlet.

ANNEXURE 1.6

ASSAY OF GASEOUS HYDROGEN

36

A) Assay

- Hydrogen (H2) – percent (%) : 99.995Volume, minimum, by difference

B) IMPURITIES

-Total gases – PPM by volume max. : 50.00-Nitrogen, moisture and volatile hydrocarbonscombined PPM by volume maximum. : 9.00-Oxygen plus Argon – PPM volume max. : 1.00-Helium –PPM by volume max. : 39.00-Carbon monoxide plus carbon dioxidePPM by volume max. : 1.00-Oil content.mg/m3 max : 3.00

C)PARTICULATES 10 microns nominal filter at outlet.

ANNEXURE – 2

DOCUMENTATION AND OPERATING MANUAL

I. DOCUMENTATIONS SUPPLIED BY LINDE37

A.1.OPERATING MANUAL (UNIT (100/200) 1. WHR, REFORMER, COMPRESSOR VOL.3 FILE 2.2 2. PSA CONTROL SYSTEM VOL .3 FILE 2.1.1 3. PSA CONTROL SYSTEM VOL .3 FILE 2.1.2 4. PSA CONTROL SYSTEM VOL .3 FILE 2.1.3 5. PSA CONTROL SYSTEM VOL .3 FILE 2.1.4 6. OPERATION AND START UO VOL.3 FILE – 1

B.1.ACCEPTANCE DOCUMENTS (UNIT (100/200) 1. WHR (WASTE HEAT RECOVERY) FILE 1.2.2 2. WHR FILE 1.2.3 3. WHR FILE 2.1.4 4. H2 – PSA VALVES FILE 1.1.1 5. H2 – PSA VALVES FILE 1.1.2 6. REFORMER COMPRESSOR FILE – 1.3 7. WHR – FILE 1.2.1 C.1.ENGINEERING DOCUMENTS (UNIT (100/200) 1. PROCESS DESIGN FILE 1/2

2. EQUIPMENT AND COMPONENTS FILE 3A.2.OPERATING MANUAL (UNIT 300/400)

1. OPERATIONING / MAINTENANCE COMPRESSOR CO301 VOL.3 FILE2.2

2. OPERATING AND START UP MANUAL VOL.3 FILE 13. INSTRUMENTATION – OPERATION AND MAINTENANCE VOL.3 FILE 2.4

4. VACUUMPUMPS, LOX/LIN TANK VOL.3 FILE2.3 5. H2 TRAILER DO401 C VOL.3 FILE 2.1.3 6. H2 TRAILER DO401 B VOL.3 FILE 2.1.2 7. H2 TRAILER DO401 A VOL.3 FILE 2.1.1

B.2. ACCEPTANCE DOCUMENTS (UNIT (300/400)1. EQUIPMENTS AND COMPONENTS FILE 1.2.2

38

2. EQUIPMENTS AND COMPONENTS FILE 1.53. EQUIPMENTS AND COMPONENTS FILE 1.2.34. INSTRUMENTATION FILE 1.7 5. ERECTION FILE 36. EQUIPMENTS AND COMPONENTS FILE 1.2.17. EQUIPMENTS AND COMPONENTS FILE 1.3.18. EQUIPMENTS AND COMPONENTS FILE 1.3.29. EQUIPMENTS AND COMPONENTS FILE 1.410. EQUIPMENTS AND COMPONENTS FILE 1.111. VALVES FILE 1.6

C.2 ENGINEERING DOCUMENTS1. INSTRUMENTATION BASIC DATAS FILE 1.2.12. PROCESS DESIGN FILE 1.13. EQUIPMENTS AND COMPONENTS FILE 3.2.2

4. EQUIPMENTS AND COMPONENTS FILE 3.45. EQUIPMENTS AND COMPONENTS FILE 3.16. EQUIPMENTS AND COMPONENTS FILE 3.2.17. EQUIPMENTS AND COMPONENTS FILE 3.3.18. EQUIPMENTS AND COMPONENTS FILE 3.59. EQUIPMENTS AND COMPONENTS FILE 3.3.210. PIPING PLAN, ISOMETRIC FILE 4.111. INSTRUMENT DETAILS FILE 1.2.212. MECHANICAL DESIGN FILE 213. VALVES FILE 5

14. PIPING PLAN ISOMETRIC FILE 4.2

A.3 OPERATING MANUAL (UNIT 500)1. AIR PRECOOLING, MOL SIEVE, EXP. TURBINE, OIL UNIT VOL.3 FILE 2. SPEC. OF INSTRUMENTS VOL.3 FILES 3.13. AIR COMPRESSOR VOL.3 FILE 2.14. CONTROL SYSTEMS AND WIRING DRAWING VOL.3,FILE 4.25. CONTROL VALVES VOL.3, FILE 3.26. PROCESS AND OPERATION FILE 1

39

7. PROGRAMMABLE CONTROLLER VOL.3 FILE 4.1

B.3 ACCEPTANCE DOCUMENT 1. VALVES FILE 1.62. EQUIPMENTS AND COMPONENTS FILE 1.13. EQUIPMENTS AND COMPONENTS FILE 1.24. EQUIPMENTS AND COMPONENTS FILE 1.35. EQUIPMENTS AND COMPONENTS FILE 1.46. EQUIPMENTS AND COMPONENTS FILE 1.5

C.3 ENGINEERING DOCUMENT (UNIT 500) 1. VALVES FILE 5

2. EQUIPMENTS AND COMPONENTS FILE 3.53. EQUIPMENTS AND COMPONENTS FILE 3.34. EQUIPMENTS AND COMPONENTS FILE 3.45. EQUIPMENTS AND COMPONENTS FILE 3.26. EQUIPMENTS AND COMPONENTS FILE 3.17. MECHANICAL DESIGN FILE 28. PROCESS DESIGN AND INSTRUMENT FILE 1.2/FILE 1.19. PIPING PLAN, ISOMETRIC FILE

II. DOCUMENTS SUPPLIED BY LPT

1. CIVIL BASIC ENGINEERING 2. MECHANICAL DESIGN AND FABRICATION OF EQUIPMENTS3. PLOT PLAN AND PIPING LAYOUT4. PIPNG ISOMETRICS5. PIPE SPECIFICATIONS AND MTO6. STEEL STRUCTURE7. DESIGN AND DRAWINGS8. QUALITY ASSURANCE MANUALS – EQUIPMENTS

40

9. QUALITY ASSURANCE MANUAL – PIPING COMPONENTS10. INSTRUMENTATION – DETAILED ENGINEERING11. INSTRUMENTS/ INSTRUCTION MANUALS12. DETAILED ENGINEERING13. VENDOR’S DRAWINGS AND MAINTENANCE MANUALS14. FIRE FIGHTING SYSTEMS15. LIST OF RECOMMENDED SPARES

III. OTHER DOCUMENTS

1. A REPORT ON NAPHTHA TRANSFER SYSTEM (NO. ILHP /100/92/01)

2. INSTRUMENT AIR SYSTEM (NO. ILHP /100/92/02)

3. DM PLANT MANUAL (NO. ILHP /100/92/03)

4. COOLING WATER SYSTEM(NO. ILHP /100/92/04)

5. REPORT ON LOX/LIN TANKERS (NO. ILHP /500/92/02)6. INSTRUMENTATION SYSTEM

I. NO. LPSC .LMF / IDA / TR / 356 / 93II. NO. LPSC .LMF / IDA / TR / 377 / 93

III. NO. LPSC .LMF / IDA / TR / 392 / 94IV. NO. LPSC .LMF / IDA / TR / 401 / 94V. NO. LPSC .LMF / IDA / TR / 398 / 94

VI. NO. LPSC .LMF / IDA / TR / 397 / 94VII. NO. LPSC .LMF / IDA / TR / 420 / 94

7. REPORT ON EFFLUENT TREATMENT PLANT (NO. ILHP /600/92/01)8. REPORT ON FIRE FIGHTINGSYSTEM (NO: ILHP /600/92/02)9. D.G SET MANUAL (NO. ILHP /600/92/03)10. LHPS DOCUMENTS11. ASU CHILLER PLANT MANUAL12. 62.5 KV DG SET MANUALS13. GH2 HOFER COMPRESSOR – SL NO : 06239514. GN2 HOFER COMPRESSOR – SL NO : 070010 – FILE : 1/3

41

15. GN2 HOFER COMPRESSOR – SL NO : 070010 – FILE : 2/316. GN2 HOFER COMPRESSOR – SL NO : 070010 – FILE : 3/317. D.R COMPRESSOR PRIMARY – SL NO : MAS 45175 A18. D.R COMPRESSOR BOOSTER – SL NO : MAS 45175 B19. CAMERON TURBO AIR COMPRESSOR –TA 2000 : CFI MANUAL20. CAMERON TURBO AIR COMPRESSOR –TA 6000 : CFI MANUAL21. BOC CRYO STAR TURBINE : 1579 FILE:1/222. BOC PLANT OPERATION MANUAL COPY23. 125 KL GARDENER TANK – 6319 – 06. 24. LH2 PUMPING SYSTEM – 1 NO

Annexure -3DETAILS OF BUILDINGS AND EQUIPMENTS TO BE INSURED:All figures in rupees lakhs

SL: NO BLOCKSUM TO BE INSURED

BLDG P&M

1Naphtha steam reformer section , naphtha storage system including stock of naphtha

- 800.82

2 H2 compressor 18.00 382.40

3 Control room equipments , 32.8 276.36

42

Instrumentation , Analytical lab

4 Process pipe lines other than water - 107.32

5Captive power plant, DG set power lines, cables / racks, electrical system, sub station

29.50 637.97

6 Transformer (2 Nos) - 40.00

7DM Plant , Instrument air compressor pumps house

13.38 40.24

8Cooling water lines, raw water lines , fire water lines, hydrants

- 147.49

9 Air separation unit 8.52 114.70

10 O2, N2 PROCESS BLOCK - 188.80

11 LOX storage system - 12.44

12 LIN storage system - 16.55

13 Cooling tower - 2.83

14Water supply UG water storage process water storage and cooling water storage

12.00 18.39

15 Effluent treatment 12.78 -

16 Fire station security time office, site office 12.90 4.01

17 Workshop , stores 12.427.69

(incl.stocks)

18 Vehicles / tankers parking sheds 16.3 -43

19Spares like CPI rings for H2 compressor, spares for Air compressor, MSLD,TMP etc…

- 300.00

20 A/C plant and AHU 3.00 9.44

21 Barbed wire fencing 4.50 -

22 LH2 Purification system 6.00 152.38

23Ashok Leyland DG set sets in captive power plant

- 5.36

24 Chilling plants - 15.89

25 Air separation unit II 70.00 1000.00

26Dresser Rand (Primary & Booster) & 2NOS of Hofer Hydrogen Compressors including shed.

18.32 250.00

27 Hofer Nitrogen Compressor 1 No 8.00 250.00

28 Air Liquide LH2 Tanker 2 Nos - 1000.00

29 LIN/ LOX Storage Tank 75 KL 3 Nos - 225.00

30 Start up Nitrogen Compressor 8.00 20.00

31 LH2 Pumping System - 150.00

32 125 KL LH2 Tank – 1 NO - 600.00

33 Gardener LH2 tanker – 1 NO - 400.00

34 Gardener LH2 tanker – 3 NOS - 600.00

44

(D0401A, D0401B, D0401C)

35

LIN/LOX Tankers

13 KL – 3 Nos,

10 KL – 2Nos

-

-

300

40

Total 278.12 8116.08

Grand total 8394.20

45

Annexure -4 Bank Guarantee for Security Deposit

PROFORMAFOR BANK GUARANTEE(From indigenous suppliers)

(On non-judicial stamp paper of appropriate value)

1. WHEREAS on the......................... (day, month &year), M/s. ............................................... (name &address of the firm), a company registered under Companies Act and having its registered office at .........................(herein after referred to as 'The Contractor'),entered in to a Contract bearing No...................dated.. . . . . . . . . . . . . . . . . . (here-in after referred to as 'The Contract')with the President of India (here-in after referred to as 'The Government') for Production and Supply Of Liquid Hydrogen, Liquid Oxygen, Liquid Nitrogen And High Pressure Gaseous Nitrogen & Hydrogen w h i c h i n v o l v e s o p e r a t i o n a n d m a i n t e n a n c e of the INTEGRATED LIQUID HYDROGEN PLANT comprising of the complete set of equipments and machineries required for the production, storage, transportation and supply of required quantities of LH2, LOX, LIN and High pressure GN2 & GH2 conforming to the specification and Main Receiving Station with DG sets referred as PLANT a s p e r t h e s a i d C o n t r a c t a g r e e m e n t (here-in after referred to as ( ‘ O p e r a t i o n a n d M a i n t e n a n c e o f ‘ Plant’).

2. AND WHEREAS under the terms and conditions of the Contract, an amount of`...........(Rupees.......................only)representing 10% of total annual contract cost valid during the period of the contract`............(Rupees .........................only)form of a bank Guarantee is to be furnished by the Contractor t o t h e Government a s S e c u r i t y D e p o s i t ( S D ) f o r d u e p e r f o r m a n c e o f t h e c o n t r a c t o n t h e e v e n t n o n e x e c u t i n g o f t h e c o n t r a c t b y t h e c o n t r a c t o r i n l i k e w i t h t h e c o n t r a c t t e r m s t h e s e c u r i t y d e p o s i t s h a l l b e f u r n i s h e d .

3. Hereby agree and undertake to pay as demand and without any demur to the accounts officer, ISRO Propulsion Complex, Mahendragiri on behalf of the Government (here-in referred as the “Accounts Officer”), a sum not exceeding Rs………….an unsatisfactory performance of the Contract by the Contractor.

4. WE, .......................... (Bank) undertake to pay to the Government any money so demanded not withstanding any dispute or disputes raised by the Bidder, in any suit or proceedings pending before any Court of Law or Tribunal relating there to, our liability under this present guarantee bond being absolute and un equivocal. The payment so made by us under this

46

bond shall be valid discharge of our liability for payment there under and the Bidder shall have no claim against us for making such payment. 5. WE, .............................. (Bank)hereby further agree that the decision of the said Accounts Officer as to whether the Contractor has committed any breach of any terms and conditions of the contract or not and as to the amount of damage, by the said Accounts Officer as damage a loss suffered by the Government an account of such breach would be final and binding on us (The Bank). 6. AND WE, the..................... (Bank) hereby agree that our liability hereunder shall not be discharged by virtue of any agreement between the Government and the Contractor whether with or without our knowledge and/or consent or by reason of the Government showing any indulgence or forbearance to the Contractor whether as to payment, time or performance, or any other matter whatsoever relating to the Contract which, but for this provision, would amount to discharge of the surety under the law. 7. OUR GUARANTEE shall remain in force until..............(Two months beyond the Contract period)and unless a claim under the guarantee is lodged with us on or before the above date, all right of the Government under the guarantee shall be forfeited and we shall be relieved and discharged from all our liabilities there under.PlaceDate

…………………………..………………………….(Signature of the Authorized Officer of the Bank)

……………………………………………………………………………………

(Name and designation of the officer)

Seal

Name, Address of the Bank (Head Office) with Phone/FaxNos.

Name & Address of the Branch with Phone/Fax Nos.

Annexure-5PROFORMA FORINTEGRITY PACT

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If the value of any procurement is above 10.00 crores (Rupees ten crores only), it would be mandatory to sign the Integrity pact with the tenderer/contractor

This Integrity Pact is made and executed on this the ……………………………..day of …………………….. (month & year), at ………………….(place) by…………………………………….. (name of the Centre/Unit) hereinafter referred to as “The Principal”

and……………………………………… (name of the tender/prospective tender) hereinafter referred to as “The Tenderer/ Contractor”.

1. Preamble1.1 The Principal intends to award, under laid down organizational procedures, a contract for ………………………………………………………………….. (details of the goods, services, etc.).1.2 The Principal values full compliance with all relevant laws of the land, rules, regulations, economic use of resources and of fairness/transparency in its relations with the Tenderers / Contractors. In order to ensure transparency, equity and competitiveness in public procurement, the Principal has evolved a code of Integrity under which its official or a Tenderer/Contractor participating in a procurement process is prohibited to –

(a) make any offer, solicit or accept any bribe, reward or gift or any material benefit, either directly or indirectly, in exchange for an unfair advantage in the procurement process or to otherwise influence the procurement process;

(b) make any omission, or misrepresentation that may mislead or attempt to mislead so that a financial or other benefit may be obtained or an obligation avoided;

(c) resort to collusion, bid rigging or anti-competitive behaviour that may impair the transparency, fairness and progress of the procurement process;

(d) improperly use the information provided by the Centre/Unit to the tenderer/contractor with an intent to gain unfair advantage in the procurement process or for personal gain;

(e) carry out any financial or business transaction between the Tenderer/Contractor and any official of the Centre/Unit;

(f) resort to any coercion or any threat to impair or harm, directly or indirectly, any party or its properly to influence the procurement process; and

(g) obstruct any investigation or audit of a procurement process.

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1.3 In order to ensure the adherence to the above Code of Integrity, the Principal will appoint an Independent External Monitor (IEM) who will monitor the process and the execution of the contract for compliance with the principles mentioned above.1.4 In case of any violation of the above Code of Integrity by the Tenderer/Contractor, the Principal shall take appropriate measures, including –

(a) exclusion of the Tenderer/Contractor from the procurement process:(b) calling off pre-contract negotiations and forfeiture or encashment of

Earnest Money deposit, if any;(c) recovery of payments made by the Centre/Unit along with interest

thereon at bank rate;(d) cancellation of the relevant contract and recovery of compensation for

loss incurred by the Centre/Unit;(e) debarment of the Tenderer/Contractor from participation in future

procurements of the Department for a period not exceeding two years.2. Commitments of the Principal2.1 The Principal commits itself to (i) follow the Code of Integrity given in pare 1.2 above, (ii) take all measures necessary to prevent corruption, and (iii) specifically observe the following principles:

(a) No employee of the Principal. Personally or through family members, or others, will in connection with the tender for, or the execution of a contract, take a promise for or accept, for self or third person, any material or immaterial benefit which the person is not legally entitled to.

(b) The Principal will, during the tender process, treat all tenderers with equity and reason. The Principal will, in particular, before and after the tender process, provide to all tenderers the same information and will not provide to any tenderer confidential/additional information through which the tenderer concerned could obtain an advantage in relation to the process or the contract execution.

(c) The Principal will exclude from the process all known prejudiced persons.2.2 If the Principal obtains information on the conduct of any of its employees which is a criminal offence under the Indian Penal Code (45 of 1860)/Prevention of Corruption Act, 1988 (49 of 1988), or if there be a substantive suspicion in this regard, the Principal will inform its Vigilance Officer (VO) or the Chief Vigilance

49

Officer (CVO) of the Department of Space, and, in addition, can initiate disciplinary action under the relevant service rules.3. Commitments of the Tenderer(s)/Contractor(s)3.1 Tenderer/Contractor commits himself to follow the Code of Integrity given in para 1.2 above and take all measures necessary to prevent corruption. He specifically commits himself to observe the following principles during his participation in the tender process and during the contract execution:(a) The Tenderer/Contractor will not, directly or through any other person or firm,

offer, promise or give to any of the Principal’s employees involved in the tender process or the execution of the contract or to any third person any material or other benefits which he/she is not legally entitled to, in order to obtain, in exchange, any advantage of any kind whatsoever during the tender process or execution of the contract.

(b) The Tenderer/Contractor will not enter with other Tenderers/Contractors into any undisclosed agreement or understanding, whether formal or informal. This applies in particular to prices, specifications, certifications, subsidiary contracts, submission or non-submission of tenders or any other actions to restrict competitiveness or to introduce cartelization in the tendering process.

(c) The Tenderer/Contractor will not commit any offence under the relevant Indian Penal Code (45 of 1860)/Prevention of Corruption Act, 1988 (49 of 1988), Further, the Tenderer/Contractor will not use improperly, for purposes of competition or personal gain, or pass on to others, any information or document provided by the Principal as part of the business relationship, regarding plans, technical proposals and business details, including information contained or transmitted electronically.

(d) The Tenderer/Contractor of foreign origin shall disclose the name and address of the Agents/Representatives in India, if any. Similarly, the Tenderer/Contractor of Indian Nationality shall furnish the name and address of their foreign principals, if any. Further, details as mentioned in the “Guidelines on Indian Agents of Foreign Suppliers” shall be disclosed by the Tenderer/Contractor.

(e) The Tenderer/Contractor shall, when presenting his tender, disclose any and all payments he has made or is committed to or intends to make to agents, brokers or any other intermediaries in connection with the award of the contract.

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(f) The Tenderer/Contractor, on a specific request by the principal, shall provide necessary information/documents whatsoever sought for by the Principal or allow access to the relevant record, documents, accounting record, books of accounts, financial statements, etc., of the Tenderer/Contractor.

3.2 The Tenderer/Contractor will not instigate third persons to commit the offences outlined above or be an accessory to such offences.4. Disqualifications from tender process and exclusion from future contracts

If the Tenderer/Contractor, before award or during execution, has committed a transgression through a violation of para 3 above or in any other form such as to put his reliability or credibility in question, the Principal is entitled to disqualify the Tenderer/Contractor from the tender process or take action as per the procedure mentioned in the “Guidelines on Banning of business dealing”

5. Compensation for Damages5.1 If the Principal has disqualified the Tenderer/Contractor from the tender process prior to the award according to para 4 above. The Principal is entitled to demand and recover the damages equivalent to Earnest Money Deposit.5.2 If the Principal has terminated the contract according to para 4 above, or if the Principal is entitled to terminate the contract according to para 4 aboe, the Principal shall be entitled to demand and recover from the Tenderer/Contractor liquidated damages of the Contract value or the amount equivalent Performance Bank Guarantee.6. Previous Transgression6.1 The Tenderer/Contractor shall declare that no previous transgression occurred in the last three years with any other company in any country conforming to the anti-corruption approach or with any other Public Sector Enterprise/Government Department in India that could justify his exclusion from the tender process.6.2 If the Tenderer/Contractor makes incorrect statement on his subject, he can be disqualified from the tender process and action taken as per the procedure mentioned in “Guidelines on Banning of business dealing”.7. Equal treatment of all Tenderer(s)/Contractor(s)/Subcontractor(s)

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7.1 The Tenderer/Contractor undertake(s) to demand from all subcontractor(s) a commitment in conformity with his Integrity pact, and to submit it to the Principal before signing of the contract/release of order.7.2 The Principal will enter into agreements with identical conditions as this one with all Tenderers, Contractors and Subcontractors for the subject procurement.7.3 The Principal will disqualify from the tender process all Tenderers/Contractors who do not sign this Integrity Pact or violate its provisions.8. Criminal charges for violation by Tenderer/Contractor/Subcontractor

If the Principal obtains knowledge of conduct of a Tenderer, Contractor or Subcontractor, or of an employee or a representative or an associate of a Tenderer, Contractor or Subcontractor which constitutes corruption, or if the Principal has substantive suspicion in this regard, the Principal will inform the same to the Vigilance Officer of the Principal, who will take further necessary action in the matter.9. Independent External Monitor/s9.1 In terms of para 1.3 above, the Principal will appoint competent and credible Independent External Monitor (IEM) for this Integrity Pact. The task of the IEM is to review independently and objectively, whether, and to what extent, the parties comply with the obligations under this agreement.9.2 The IEM is not subject to instructions by the representatives of the parties perform his functions neutrally and independently. He reports to the Head of the Principal’s Office.9.3 The Tenderer/Contractor accepts that the IEM has the right to access, without restriction, to all documentation of the Principal including that provided by the Tenderer/Contractor relating to the subject procurement. The Tenderer/Contractor will also grant the IEM upon his request and demonstration of a valid interest, unrestricted and unconditional access to his documentation relating to the subject procurement. The above condition shall also be applicable to sub-contractor/s. The IEM is under contractual obligation to treat the information and documents of the Tenderer/Contractor/Subcontractor(s) with confidentially.9.4 The Principal will provide to the IEM sufficient information about all meetings among the parties related to the subject procurement provided such meetings could have an impact on the contractual relations between the Principal and the

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Tenderer/Contractor. The parties offer to the Monitor the option to participate in such meetings.9.5 As soon as the IEM notices, or believe to notice, a violation of this Pact, he will so inform the Principal and request the Principal to discontinue or take corrective action, or to take other relevant action. The IEM can in this regard submit non-binding recommendations. Beyond this, the IEM has no right to demand from the parties that they act in a specific manner or refrain or tolerate action.9.6 The IEM will submit a written report to the Head of the Principal’s Office within four weeks from the date of reference or intimation to him by the Principal and, should the occasion arise, submit proposals for correcting problematic situations.9.7 If the IEM has reported to the Head of the Principal’s Office a substantiated suspicion of an offence under the relevant Indian penal Code/Prevention of corruption Act, and the Head of the Principal’s Office has not, within a reasonable time, taken visible action to proceed against such offence or reported it to the Chief Vigilance Officer of the Department, the IEM may also transmit this information directly to the Central Vigilance Commission, with a copy to the Chief Vigilance Officer of the Department.10. Duration of the Integrity Pact10.1 This integrity Pact shall be treated as part and parcel of Purchase Order/ Contract, if any, placed by the Principal on the Tenderer/ contractor. The validity of this Integrity Pact begins when both parties have legally signed it. It expires for the successful Tenderer/ Contractor 12 (twelve) months after the last payment under the contract, and for all other Tenderers/ Contractors, 6 (six) months after the contract has been awarded.10.2 If any claim is made/ lodged during the periods aforementioned, the same shall be binding and continue to be valid despite the lapse of this Integrity Pact as specified above, unless it is discharged/determined by the Head of the principal’s office.11. Other provisions11.1 This integrity Pact is subjected to Indian Law, and the place of performance & jurisdiction shall be the place where the Principal’s Office is located.11.2 Changes and supplements as well as termination notice need to be made in writing.

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11.3 If the Tenderer/Contractor is a partnership firm or a consortium, this Integrity Pact must be signed by all partners or consortium members.11.4 Should one or several provisions of this Integrity Pact turn out to be invalid, the reminder of this pact would remain valid. In this case, the parties will strive to come to an agreement to their original intensions.11.5 In the event of any contradiction between the Integrity Pact and its Annexures, the clause in the Integrity Pact only will prevail.

………………………………… ……………………................................(For & on behalf of the Principal) (For & on behalf of Tenderer/Contractor)(Office seal) (Office seal)

Place: ………………………….Date: …………………………..

Witness 1: Witness 2:(Name & Address) (Name & Address)

Annexure-6

APPROVALS & STATUTORY CLEARANCE

The following documents will be handed over to the BIDDER at the time of Acceptance of the plant

PESO license for naphtha storage Clearance from Chief Inspector of Boilers, Tamilnadu. PESO license for LOX&LIN Storage tanks. PESO license for 13 KL LOX/LIN transport tankers. Letters of consent from TNPCB under water and Air pollution act. Copy of the concurrence obtained from Ministry of petroleum and natural gas

for Naphtha supply. PESO exemption for LH2 tankers. Registration certificates for the tankers

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License from Naphtha Storage & use from District authorities.

ANNEXURE-7

LIST OF INVENTORY OF PLANT INCLUDING ALL ALLIED FACILITIES

100.00.00 REFORMER SECTION

200.00.00 PRESSURE SWING ADSORBER UNIT

300.00.00 H2 LIQUEFACTION UNIT

400.00.00 LH2 TANKERS

500.00.00 ASU- PHASE I

600.00.00 UTILITIES- PHASE I

700.00.00 FIRE FIGHTING, SAFETY & ETP

800.00.00 INSTRUMENTATION SYSTEM

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900.01.00 SHORT BREAK DG SET

900.02.00 MAIN SUPPLY SUB STATION AT ILHP

900.03.00 DG SET PANEL & ELECTRICAL INSTALLATION AT ILHP SUB STATION PHASE I

900.04.00 LIGHTING. LOADS. FITTING PANELS AND OTHERS

900.05.00 AIR CONDITIONING

1000.00.00 CIVIL

01.00 ASU BUILDINGS- PHASE I

02.00 BUILDINGS

03.00 SANITORY AND PH WORKS

1100.00.00 LOX/LIN TANKERS- PHASE I

1200.00.00 ANALYTICAL LAB

1300.00.00 MAIN RECEIVING STATION AT MAHENDRAGIRI

2000.00.00 LIQUID HYDROGEN PURIFICATION SYSTEM

2100.00.00 CHILLER WATER PLANT

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2200.00.00 25M3 COOLING WATER SYSTEM

2300.00.00 5KL, 10KL TANKERS WITH ACCESSORIES

2400.00.00 GC FOR CO2 ANALYSIS

2500.00.00 UPS FOR ANALYTICAL LAB

3000.00.00 GH2 HOFER COMPRESSOR WITH MOTOR

3100.00.00 DR H2 COMPRESSOR PRIMARY & BOOSTER WITH MOTOR

3200.00.00 N2 START UP COMPRESSOR WITH MOTOR

3300.00.00 GN2 HOFER COMPRESSOR WITH MOTOR

3400.00.00 CP 11 CAMERON TURBO AIR COMPRESSOR WITH MOTOR

3500.00.00 CP 12 RECYCLE COMPRESSOR WITH MOTOR

3600.00.00 CRYO STAR TURBINE WITH BOOSTER COMPRESSOR

3700.00.00 BOC COLD BOX

3800.00.00 INOX LIN STORAGE TANK 75 KL

3900.00.00 INOX LOX STORAGE TANK 75 KL

4000.00.00 125 KL LH2 STORAGE TANK

4100.00.00 BLUE STAR CHILLER PLANT WITH PANEL

4200.00.00 CHILLED WATER CIRCULATION PUMP UNIT

4300.00.00 170037 (TN 72 Q 4109) LH2 TANKER

4400.00.00 170038 (TN 72 Q 4101) LH2 TANKER

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4500.00.00 TN 72 AZ 2216 LIN/LOX TANKER 10KL

4600.00.00 TN 72 AZ 2219 LIN/LOX TANKER 10KL

4700.00.00 BOTLYBOI COOLING TOWER

4800.00.00 150m3 COOLING WATER PUMP WITH MOTOR

4900.00.00 PLC CONTROL PANEL FOR GH2 HOFER COMPRESSOR

5000.00.00 PLC CONTROL PANEL FOR GN2 HOFER COMPRESSOR

5100.00.00 PLC CONTROL PANEL FOR N2 START UP COMPRESSOR

5200.00.00 PLC CONTROL PANEL FOR DR PRIMARY & BOOSTER COMPRESSOR

5300.00.00 ASU II 690KW MOTOR VCB CONTROL PANEL WITH PROTECTION RELAYS

5400.00.00 ASU II MCB AND MCC PANEL

5500.00.00 N2 HOFER COMPRESSOR PANEL AND ACB

5600.00.00 DR COMPRESSOR POWER AND CONTROL MCC PANEL WITH ACB

5700.00.00 TR I INCOMING PANEL WITH ACB

5800.00.00 NUMERIC UPS FOR ASU II CONTROL PANEL 2 NOS

5900.00.00 NUMERIC UPS FOR ASU II LAB

6000.00.00 SCADA SYSTEM ASU I (2 NOS)

6100.00.00 PLC PANEL WITH SCADA ASU II (2NOS)

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6200.00.00 INCOMER II VCB PANEL WITH PROTECTION RELAYS

6300.00.00 ASU II MV PANEL WITH 2NOS ACB

6400.00.00 TRANSFORMER – I MV PANEL WITH 4ACB

6500.00.00 TRANSFORMER – II MV PANEL WITH OUTGOING 4ACB

AIR SEPARATION UNIT II DR GH2 COMPRESSOR (PRIMARY & BOOSTER) , CHILLED WATER COOLED GH2 HEAT EXCHANGER AND CHILLED WATER PLANT II (BLUE STAR)HIGH PRESSURE GH2 HOFER COMPRESSORHIGH PRESSURE GN2 HOFER COMPRESSORN2 START UP COMPRESSOR125 KL LH2 STORAGE TANK40 KL AIR LIQUIDE LH2 TANKERS- 2 NOS (170037 & 170038 WITHOUT PRIME MOVERS) 40 KL GARDNER LH2 TANKER (630306) -1 NO (WITHOUT PRIME MOVER)75 KL INOX MAKE LIN TANK -1 NO

STOCK POSITION AT THE TIME OF HANDING OVER ON ----------

LIN LEVEL IN STORAGE TANK : -------------

LIN IN TANKERS : -------------

LOX LEVEL IN STORAGE TANK : -------------

LOX IN TANKERS : -------------

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NAPHTHA LEVEL IN STORAGE TANK : -------------

NAPHTHA IN TANKERS : -------------

ENERGY METER READING : -------------

CHEMICALS AND CONSUMABLES : -------------

Annexure-8

TENTATIVE LIST OF APPROVALS & STATUTORY CLEARANCE TO BE RENEWED BY THE BIDDER

PESO license for Naphtha Storage.

Clearance from Chief Inspector of Boilers, Tamil Nadu.

PESO license for LH2/ LOX/LIN storage tanks.

PESO license for LH2/ LOX/LIN transport tankers.

Taxes & Permits and F.C for transport tankers.

All fees and charges to TNPCB except the consent fee.

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License for Naphtha Storage from district authorities.

CHAPTER – IISTRUCTURE OF CONTRACT COSTS

1.0 Operation & Maintenance Cost2.0 Variable Cost3.0 Procurement and supply of Chemicals, Oil & Consumables, Tyres,

Spares, AMC, statutory fees and providing Maintenance Services: 4.0 Transportation Elements of ILHP O & M Contract

5.0 Escalation6.0 Terms of Payment

List of Appendix:

Appendix-1 Details of human resources to be deployed in round the clock operation.

Appendix-2 Procedure for Calculation of Actual consumption of Naphtha incurred for GH2 supply from Reformer Unit.

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Appendix-3 Tentative List of replacement spares, consumables gaskets etc to be procured and supplied by the bidder

Enclosure-1 Tentative List of Mechanical sparesEnclosure-2 Tentative List of Electrical SparesEnclosure-3 Tentative List of Instrumentation Spares Enclosure-4 Tentative List of Spares for Safety system Enclosure-5 Tentative List of Process, Mechanical, Instrumentation and

Analytical lab log book Appendix-4 Tentative list of special equipments for which AMC

shall be enteredAppendix-5 Tentative list of statutory fees to be paid by the bidderAppendix-6 Tentative list of maintenance services which can be

availed from outside parties to be procured and supplied by the bidder

Appendix-7 Tentative list of chemicals, oil & other consumables to be procured and supplied by the bidder.

CHAPTER – IISTRUCTURE OF CONTRACT COSTS

1.0 OPERATION & MAINTENANCE COST1.1 Fixed Cost

Sl. No Description Cost in Rs lakhs/year.

Operation and maintenance of the plant in round the clock basis(Minimum deployment of human resources as per details given in Appendix-1)The fixed cost towards human resources shall include:

To be quoted by the bidder in the

format given ‘CHAPTER-VI’

1.1.1 Towards Basic Salary*

1.1.2 Other allowances including PF, Group insurance etc…

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1.1.3 Administrative expenses and overheads cost towards Operation and maintenance of the plant*

* Subjected to escalation every year as per article no 5.1 of this chapter- II (The fixed cost towards Basic Salary and Administrative expenses and overheads cost)1.2 Plant Insurance cost

1.2 Plant Insurance cost (As defined in Article No 12.5 of chapter I)

At actual

2.0 VARIABLE COSTa) Liquid HydrogenTowards Naphtha (0.52kg/lit x Avg price of Naphtha per kg for every batch)Average price of Naphtha during Jan 2016 is Rs 43.12/kg.The Specific Naphtha consumption norm is 0.52kg/lit of LH2. It is essential to ensure operation and maintenance of the plant by the bidder to achieve the Specific Naphtha consumption norm of 0.52kg/lit of LH2. It shall be subjected to review as per article 12.3 of chapter-I. The quantity of LH2 in litres shall be measured with level transmitters fitted on the tankers filled and its calibration chart. However in case of supply of LH2 directly to Liquid Hydrogen Purification System the quantity of LH2 in litres shall be calculated by (hours of supply) x (average hourly production rate). Average hourly production rate of LH2 shall be calculated based on either preceding 72 hrs of operation or subsequent 72 hrs of operation. b) Liquid Oxygen : No variable cost is payable for production & supply.c) Liquid Nitrogen : No variable cost is payable for production & supply.d) Gaseous Hydrogen Supply from Reformer Unit: Against payment towards actual consumption of Naphtha incurred as per the procedure given in Appendix-2 of this chapter II.

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3.0 Procurement and supply of Chemicals, Oil & Consumables, Tyres, Spares, AMC, statutory fees and providing Maintenance Services:

Department will decide the list of Chemicals, Oil & Consumables, Tyres, Spares, AMC and Maintenance Services and its cost required for the plant. It shall be addressed in JCC and decided.

All the equipments are to be maintained in house utilizing the manpower deployed by the bidder. Generally AMC shall be entered for the special equipments given in Appendix-4 of this chapter–II of RFP. Tentative list of spares & maintenance services which can be availed from outside parties is given in Appendix-3 & Appendix-6 of chapter –II of RFP respectively. Tentative list of statutory fees to be paid by the bidder is given in Appendix-5. Tentative list of chemicals, oil & other consumables to be procured and supplied by the bidder is given in Appendix-7. Any other requirements of Chemicals, Oil & Consumables, Tyres, Spares, AMC, statutory fees and providing Maintenance Services shall be addressed in JCC and decided.

3.1 General conditions for Procurement and supply of Chemicals, Oil & Consumables, Tyres, Spares, AMC And providing Maintenance Services: The Bidder shall procure the items by obtaining competitive offers wherever

applicable. The Bidder shall procure the items by following our general purchase terms &

conditions given in Attachment No. - 1 & 2 where ever applicable and deviations if any shall be addressed and finalized in JCC. The decision of Department shall be final.

3.2 Bidders are requested to Quote the overhead expenses in % of cost as given below in the format given in chapter V of price bid. The bidders may quote for overhead expenses in the format given in chapter V of price bid towards administrative expenses & overheads including local transportation

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charges from Nagercoil/Valliyur/Tirunelveli to IPRC Mahendragiri for the following: Procurement and supply of Tyres , Chemicals, Oil & Consumables, and

Spares as detailed in Appendix 3 of CHAPTER II of RFP as given below: With individual unit rate of Tyres , Chemicals, Oil & Consumables,

and Spares costing less than Rs. 25,000 per item in % invoice of cost of Tyres , Chemicals, Oil & Consumables, and Spares supplied .

With individual unit rate of Tyres , Chemicals, Oil & Consumables, and Spares costing from Rs. 25,000 to 1,00,000 per item in % of invoice cost of Tyres , Chemicals, Oil & Consumables, and Spares.

Arranging maintenance services from outside parties as given in Appendix 4 in % of invoice cost of maintenance services availed.

costing less than Rs. 25,000 per service . costing from Rs. 25,000 to 1,00,000 per service.

3.3 Procurement and Supply of Capital Spares costing more than Rs. 1,00,000& providing maintenance services costing more than 1,00,000.

Department will decide the list of capital spares, and the maintenance services and its cost required for the plant. It shall be addressed in JCC and decided. Bidder shall procure and supply the Capital Spares costing more than Rs. 1,00,000& providing maintenance services costing more than Rs. 1,00,000. based on the request by Department. The landed cost of capital spares & providing maintenance services shall be paid at actual as decided by DEPARTMENT in JCC & approved Director, IPRC if it is applicable as per the contract and with the approval of the Department in case of amendments against the documentary evidence with CISF gate entry seal and accepted & certified Material Inspection cum receipt voucher (MIRV) for capital spares.

4.0 TRANSPORTATION ELEMENTS OF ILHP O & M CONTRACT4.1 OPERATIONAL TRANSPORT CHARGES FOR INTERNAL TRIPS

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4.1.1 For delivery within Mahendragiri and movement of tankers within ILHP the cost towards diesel shall be paid based on mileage in ghat section of IPRC, Mahendragiri and Km readings of prime movers and certified trip sheets.

Sl. No Description

Mileage in Km/lit applicable to ghat section of IPRC, Mahendragiri.

1. 40KL Gardner Liquid Hydrogen Tanker 1.0

2. 13KL Liquid Oxygen/Liquid Nitrogen Tankers 2.0

3. 6KL Liquid Oxygen/Liquid Nitrogen Tankers 3.0

4. 40 KL Air Liquide Tankers 2.0

5. 10 KL LIN/LOX Tankers 3.04.1.2 For delivery within Mahendragiri, 2.67 lit/trip of diesel cost is payable towards diesel cost of light vehicle stationed at the plant by the bidder.4.1.3 The movement of tanker shall be approved and certified and a separate log book shall be maintained. Diesel price at kavalkinaru on the date of transportation will be considered.

4.1.3 Movement of tankers within ILHP shall include the following requirements: Movement of LIN/LH2/LOX tankers from the filling area after filling and parking

of new tanker for filling on round the clock basis. Movement of tankers within the plant for transfer of LH2/LIN/LOX, Analysis

purpose, filing LIN shield of LH2 Tankers, Reformer start up, leak testing, movement of air liquide tanker to reduce evaporation loss etc.

4.2 DETAILS OF TANKERS

Sl No Tanker No Fluid Capacity

Prime mover make & model

Year of Built

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1 TNK8332 LIN/LOX 6KL Ashok Leyland Comet 1985

2 TN74G0001 LIN/LOX 6KL Ashok Leyland Comet 1988

3 TN72G0079 LIN/LOX 13KL Ashok Leyland Tuskar Turbo 1993

4 TN72G0080 LIN/LOX 13KL Ashok Leyland Tuskar Turbo 1993

5 TN72G0085 LIN/LOX 13KL Ashok Leyland Tuskar Turbo 1993

6 TN72AZ2216 LIN/LOX 10KL Ashok Leyland Tarus 2007

7 TN72AZ2219 LIN/LOX 10KL Ashok Leyland Tarus 2007

8 TN72V0217 LH2 40KL Ashok Leyland Hippo 1993

9 TN72V0245 LH2 40KL Ashok Leyland Hippo 1993

10 TN72V0246 LH2 40KL Ashok Leyland Hippo 1993

11 TN72Q4109 LH2 40KL Air Liquide Tusker Turbo Tractor 3516

2006

12 TN72Q4101 LH2 40KL Air Liquide Tusker Turbo Tractor 3516

2006

4.3 OPERATIONAL TRANSPORT CHARGES FOR OUTSIDE TRIPS

SL.NO DESCRIPTION

6KL-2NO 13 KL-3NO 10KL-2NOS 40 KL-3NO (Gardner/ Air Liquide)

40KL-2NOS (Air Liquide)

LIN/LOX Tankers LH2Tankers

TNK8332 TN74G001

TN74G0079 TN74G0080

TN72AZ2216TN72AZ2219

TN72V0217 TN72V0245

TN72Q4109 TN72Q4101

67

TN74G0085 TN72V0246 and others

and others

1 Basic cost towards DIESEL (Mileage)

(3km/lit) (2.25km/lit)(3.5km/lit)

(1.5km/lit), 1.7 km/lit for hippo of Air

Liquide tankers

(2.25km/lit), 2.2 for artik

2 Operational incidental expenses

To be quoted by the bidder in the CHAPTER-VI

TOTAL (RS PER KM) For deliveries outside Mahendragiri, the cost towards diesel shall be paid

based on mileage and the distance. The bidder shall quote operational incidental expenses.

operational incidental expenses for LIN/LOX Tankers:

The operational incidental expenses shall include incidental expenses for taking care of en route expenses of tankers like air checking, attending to puncture of tyre, hose leak & brake binding, bulb changing, oil top up etc.

operational incidental expenses for LH2 Tankers:

LH2 Transportation is to be carried out at maximum speed of not more than 40 km/hr with police escort. Also TATA sumo or equivalent vehicle is to be engaged as pilot, scout and escort for LH2 transportation. For every trip, one pilot vehicle is to engaged and one scout & one escort per tanker is to be engaged.

The operational incidental expenses shall include in addition to the incidental expenses for taking care of en route expenses of tankers,

68

incidental expenses for transportation crew with escort police personnel. The cost towards engaging following shall be quoted separately

One Diesel mechanic as part of transportation crew. Additional driver

The table showing details are given in article no 2.0 of Chapter VI. The distance for transportation between IPRC and outside places are

given below: IPRC, Mahendragiri – SDSC-SHAR & Back = 1660 Km

(Round trip will be 6 days excluding halting). IPRC, Mahendragiri –LPSC (Valiamala)/VSSC & Back = 230 Km

(Round trip will be 1 day Excluding halting). IPRC, Mahendragiri – ASL Saggonda &Back =2620 Km

(Round trip will be 10 days Excluding halting).NOTE:

1. Set of tyres for Prime movers & Trailers of tankers shall be procured by the Bidder with the approval of Department and replaced as and when required.

2. SUMO or equivalent running charges will be allowed for LH2Transportation at the mileage of 8km/lit for the actual number of vehicles engaged for pilot, scout, and escort.

3. For LH2Transportation to SDSC – SHAR, Scout will be allowed for 1850 km, First Pilot will be allowed for 1750 km and 1660 Km for others. In addition Halting charges is payable per day excluding the day of arrival and departure.Halting charges per day ________ (To be quoted by the bidder in the CHAPTER-VI)

VARIATION:Base diesel price =………….IPRC shall allow variation in respect of the difference in fuel charges as per the following formula for tankers and SUMO running charges.

= (New rate of fuel- Base Diesel Price) x Distance in KM Mileage

69

4.4 FIXED TRANSPORTATION CHARGES

SL.NO

DESCRIPTION

TANKER

6KL-2NO

(LIN/LOX)

13KL-3NO

(LIN/LOX)

40KL-3NO

(LH2)

10KL-2NOS

(LIN/LOX)

40KL- 2NOS

LH2

TNK8332 TN74G001

TN74G0079 TN74G0080 TN74G0085

TN72V0217 TN72V0245 TN72V0246

TN72AZ 2216

TN72AZ 2219

TN 72Q 4109

TN72Q 4101 and others if any

I TAXES, PERMITS & INSPECTION FEES

1 TAX

At actual against documentary evidence

2 GREEN TAX

3 NATIONAL PERMIT

4 WORKMAN COMPENSATION AND ACCIDENT INSURANCE

5 QUALITY INSPECTION FEES AND INSPECTION EXPENSES

II OVERHEADS AND MINOR MAINTENANCE

( To be quoted by the bidder in the CHAPTER-VI)

6a Overhead Expenses for arranging FC & Quality inspection in Rs per year

6b Expenses towards Minor maintenance, battery charging, oil service including oil filter

70

replacement, grease service, fuel filter replacement, Hose replacement etc. in Rs per year

III MAJOR MAINTENANCE Department shall decide the list of replacement spares and services required. It shall be paid at actuals against documentary evidence from authorized service provider.

Supply of Paint and painting of the Tankers and prime movers is covered in maintenance.Over head Expenses for arranging FC and Quality Expenses shall include

Diesel for movement of tankers from IPRC, Mahendragiri to Regional Transport Office (RTO), Vallioor (20 Kms).

Quality Inspection fee for testing of the Cryogenic tankers in presence of authorized Inspector certified by Petroleum and Explosive Safety Organization (PESO), Nagpur.

Incidental Expenses for arranging FC.NOTE:

1. Taxes (Sl No: 1 to 5) shall be paid against documentary evidence.2. The charges mentioned on Sl No: 6 shall remain fixed for 5 years.

5.0 ESCALATION.

5.1 Fixed cost:

Fixed cost towards salary given in article 1.1.1 of this chapter –II shall be subjected to escalation once in a year as per CPI for industrial workers (all India average Base 2001= 100 published by Reserve bank of India) to cover the additional expenses on account of escalation. (Fixed cost towards salary x

CPI ( IW )CPI base Index(Monthof effectivedate of contract )).

71

Fixed cost towards administrative expenses, overheads given in article 1.1.3 of this chapter –II shall be subject to escalation once in a year as per the WPI.(All commodities Base 2004-05 = 100, published by Reserve bank of India) (Fixed cost towards administrative expenses & overheads

x WPIWPI base Index (Monthof effective date of contract )

)

5.2 VARIABLE COST:5.2.1 NaphthaThe escalation due to variation in the price of naphtha shall be applied for every batch of LH2 production. The cost towards naphtha in the variable cost as per article No 2.0(a) of this chapter II, shall be calculated based on the average landed price of naphtha as per IOCL invoices including transportation charges using standard practice of FIFO (First in First out inventory accounting).5.3 Chemicals, Oil & Consumables, Tyres, Spares, AMC, Statutory fees And Maintenance Services:

The cost towards Chemicals, Oil & Consumables, Tyres, Spares, and Maintenance Services shall be paid at actual plus quoted Over head expenses and the cost towards AMC & Statutory fees shall be paid at actual as decided by DEPARTMENT in JCC & approved by Director, IPRC if it is applicable as per the contract and with the approval of the Department in case of amendments against the documentary evidence with CISF gate entry seal and accepted & certified Material Inspection cum receipt voucher (MIRV) for Chemicals, Oil & Consumables, Tyres & Spares by contract manager of DEPARTMENT for every 3 months to make payment.

6.0 TERMS OF PAYMENT

6.1 FIXED COST

72

The Bidder shall submit the invoice for fixed cost per month [cost for one year divided by 12] on the last working day and the DEPARTMENT shall release the fixed charges payable for every month before the 10th of the succeeding month. If the plant or part of the plant is shut down for more than 7 Days in a month due to the fault of the BIDDER, then the fixed cost towards Basic Salary, Other allowances including PF, Group insurance etc…& Administrative expenses and overheads (excluding Plant Insurance cost) is payable proportional to the number of days of operation in that particular month. In case, there is dispute regarding the cause of shutdown, then the same shall be discussed in JCC and settled as per the recommendation of JCC. In case of any further dispute, then the matter shall be referred to Director, IPRC for a final settlement. The decision of Director, IPRC shall be final.

6.2 VARIABLE COST

The DEPARTMENT shall release 100% payment of the variable cost within 15 days of acceptance of the product based on analysis report for each tanker.

6.3 Transportation charges and other charges: The delivery charges for supplying to all ISRO centers/units, Fixed transportation charges, Batch wise settlement of variable cost of LH2 towards Naphtha, variable cost for gaseous Hydrogen supply from Reformer unit etc shall be paid within 30 days from the date of delivery/supply and submission of invoice with verified/certified documents to the satisfaction of DEPARTMENT.6.4 The cost towards Chemicals, Oil & Consumables, Tyres, Spares, and Maintenance Services shall be paid at actual plus quoted Over head expenses and the cost towards AMC, Statutory fees shall be paid at actual once in 3 months and within 30 days upon submission of invoice with verified/certified documents to the satisfaction of DEPARTMENT. The landed cost of capital spares & providing maintenance services shall be paid at actual on case by case basis.

73

6.5 The cost towards plant Insurance shall be paid at actual within 30 days upon submission of original insurance policy with verified/certified documents to the satisfaction of DEPARTMENT.6.6 Any delay in arriving at the revised price shall not affect the delivery of the products and the payment shall be made by the DEPARTMENT as per the pre-revised price, and the difference if any shall be adjusted subsequently.

74

Annexure-1

Details of human resources to be deployed by the bidder in round the clock operation:SL.NO

DESCRIPTION QUALIFICATION MINIMUM EXPERIENCE IN YEARS

PREFERRED AREA OF EXPERIENCE IN OPERATION & MAINTENANCE OF

NO OF MAN POWER

I Process Operation and Maintenance

1 Manager Operation B.E Mechanical 15 Steam reformer and Hydrogen Liquefier, Air separation Plant, High pressure compressors, cryogenic fluid transfer and routine maintenance.

1

2 Shift In charge DME/BE 10/5 Steam reformer and Hydrogen Liquefier, Air separation Plant, High pressure compressors, cryogenic fluid transfer and routine maintenance.

4

3 Process Operator &

DME/BSc.Chem /DChem.E

5 Steam reformer and Hydrogen Liquefier, Air separation Plant, High pressure compressors, cryogenic fluid transfer and routine maintenance.

6

4 Field operator DME/BSc.Chem /DCE

2 Steam reformer and Hydrogen Liquefier, Air separation Plant, High pressure compressors, cryogenic fluid transfer and routine maintenance.

4

5 Process operation & Safety

BSc. Chem/DCE with PG Diploma in safety

5 safety related Process & Plant operation

1

6 Air separation Plant I & II /Utilities

DME 5 Air separation plant 7

7 Air separation Plant I & II /Utilities

DME 1 De-mineralized water plant , Effluent treatment plant, Air Compressor, Cooling water system

4

Process Subtotal 27

II Specialist Maintenance Team

75

8 Maintenance In charge

DME 15 Rotary equipment, Stationery equipment and vacuum system & Stock inventory management.

1

9

Special Maintenance team

DME with IBR certificate holder.

5 1

10 ITI Fitter 10 1

11 ITI welder/third party certified welder

10 Welding and fittings & assembly works.

1

11 Diesel Mechanic ITI Diesel Mechanic 15 Automobile & Diesels 1

Maintenance Subtotal 5

III Analytical Lab

12 Analyst B.Sc Chemistry. 10 Gas Chromatograph analysis, water analysis

3

Subtotal 3

IV Instrumentation

13 Engineer In-charge Instrumentation

DECE/DEEE / BSc PHYSICS

15 Process plant Instrumentation Procurement of spares and Inventory control

1

14 Shift In charge/ Operator

DECE/DEEE/ Diploma in Instrumentation

5 Process plant Instrumentation 3

15 Maintenance Technician/Instrumentation

DECE/DEEE/Diploma in Instrumentation

5 Field maintenance of Instrumentation

1

Instrumentation Subtotal 5

V Electrical

16 Engineer In-charge, Electrical

DEE/B.E (Electrical). 15/8 O & M of substation and DG set

1

17 Shift In charge – Electrical (Plant)

DEEE, License holder for 11kva

8 4

76

18 Shift In charge – Electrical MRS substation & Plant maintenance

DEEE License holder for 11kva

4 7

Electrical Subtotal 12

VI Administrative In charge

Graduate 15 Overall administration 1

19 Driver HVD 5 Driving of LH2/LIN/LOX articulated Tankers

4

20 Attendant 3 Housekeeping 1

Transportation Subtotal 6

Total 58

Typical Deployment of human resources in round the clock operation when Hydrogen plant & Air separation unit 1 & unit 2 are running:

S.No Description General shift

Per shift For 3 shift

Weekly rest

Total

I Process and Mechanical

1 Manager, operations 1 - - - 1

2 Shift in-charge(Hydrogen plant)

1 3 1 4

77

3 Process operator(Reformer unit including LH2 transfer operations)

- 2 6 1 7

4 Field operator(Reformer unit Including LH2 transfer operations)

- 1 3 1 4

5 Air separation unit I & unit II (Including transfer operations)

- 2 6 1 7

6 Utilities (Deminralizer plant, Instrument air system & cooling water system)

- 1 3 1 4

Total 27

II Specialist Maintenance Team

7 Maintenance in charge 1 - - - 1

8 Special Maintenance Team 3 - - - 3

9 Diesel mechanic 1 - - - 1

Sub total 5

III Analytical lab

10 Analyst - 1 [ only for two shift]

2 [ only for two shift]

1 3

IV Instrumentation

11 Instrumentation In charge 1 1

12 Shift In charge - 1 3 1 4

Sub total 5

V Electrical

13 Electrical In- charge 1 - - - 1

14 Shift In-charge (ILHP) - 1 3 1 4

78

15 Shift In-charge (MRS) - 2 6 1 7

Sub total 12

VI Transportation & Administration

16 In-charge 1 - - - 1

17 Driver - 1 3 1 4

18 Housekeeping (Attendant) 1 - - - 1

Total 58

Appendix-2

Procedure for Calculation of Actual consumption of Naphtha incurred for GH2 supply from Reformer Unit.

The actual consumption of naphtha incurred shall be calculated based on the initial and final level measurement of ILHP naphtha storage tank. This shall include any interruption due to power failure occurring during the supply time.

In case of LH2 production and GH2 supply from Reformer unit

The naphtha consumption for LH2 production shall be calculated based on either preceding 24hrs of operation or subsequent 24hrs of operation. The format for calculation in excel sheet is given in Appendix 2a.

79

__

Actual consumption of naphtha measured at ILHP storage tank

Naphtha consumption for LH2 production

Naphtha incurred for GH2 supply

=

Appendix-2a

DETAILS OF GH2 SUPPLIED FROM THE STEAM REFORMER UNIT OF ILHP

CASE1 SIMULTANEOUS LH2 PRODUCTION AND GH2 CHARGING

DATE  TIME (Hrs) NAPHTHA LEVEL

CHARGING FROM TO INITIAL FINAL DIFF.  FACILITY Hr Min Hr Min mm mm mm

ContinuedCONSUM. NAPHTHA LH₂ LEVEL LH₂ LH₂ PRODUCTION

DURING CONSUM FINAL INITIAL PRODUCTION CONVERT INTOTRANSFER kg % & Liters (Liters) EQUAL. OF GH₂

ContinuedGH₂ NAPHTHA NAPHTHA COST PAYABLE

CHARGING CONSUMPTION COST/KGNm³ FOR 1

Nm³for GH₂

(kg) kg/hr Rs Rs

CASE2 GH2 SUPPLIED FROM THE STEAM REFORMER UNIT OF ILHP FOR tankers WARMINGUP

NO

STARTED TIME (Hrs) TANK PR No NAPHTHA LEVEL

DATE FROM TO   of INITIAL FINAL DIFF.&

COMPLETED DATE Hr

Min Hr Min Kpa

CYCLES mm mm mm

Continued

80

CONSUM.DURING

TRANSFER

NAPHTHA LH₂ LEVEL LH₂ LH₂

PRODUCTION GH₂

CONSUM FINAL INITIAL PRODUCTION CONVERT INTO CHARGING

kg % & Liters (Liters) EQUAL. OF GH₂ Nm³

Continued

NAPHTHA NAPHTHA COST PAYABLECONSUMPTION COST/KG

FOR 1 Nm³ for GH₂ (kg) kg/hr Rs Rs

CASE3 GH2 SUPPLIED FROM THE STEAM REFORMER UNIT OF ILHP

NO DATE  TIME (Hrs) NAPHTHA LEVEL

CHARGING FROM TO INITIAL FINAL DIFF.  FACILITY Hr Min Hr Min mm mm mm

ContinuedCONSUM. NAPHTHA GH₂ NAPHTHA

DURING CONSUM CHARGING CONSUMPTIONTRANSFE

R kg Nm³ FOR 1 Nm³ for GH₂ (kg) kg/hrContinued

NAPHTHA COST PAYABLECOST/KG  

Rs Rs

81

Appendix-3

Tentative list of Replacement Spares, Consumables, Gaskets etc to be procured and supplied by the bidder .

The summary of Mechanical spares, Electrical spares, Instrumentation spares and Safety spares are given in the following tables. The detailed list is given in Enclosure 1.

Table I: SUMMARY OF MECHANICAL SPARES

SL.NO DESCRIPTION

1 LIN,LOX HOSE AND PIG TAIL HOSE

2 BEARING

3 BELT

4 RUPTURE DISK

5 DM PLANT VALVE

6 GASKETS

7 LIN,LOX TANKER VALVE

8 NAPHTHA TRNSFER PUMP 2 NOS

9 NAPHTHA FEED PUMP 2NOS

10 BOILER FEED PUMP 2NOS

82

11 HYDRAZINE PUMP

12 COOLING WATER PUMP 160m³ 2 NOS

13 RAW WATER PUMP 2 NOS

14 VACUUM PUMP COOLING WATER PUMP

15 VACUUM PUMP 2 NOS

16 ETP PUMP

17 COOLING TOWER

18 REFORMER BLOWER

19 FIRE WATER PUMP

20 FIRE JACKY PUMP

21 CHILLER COMPRESSOR

22 INSTRUMENT AIR COMPRESSOR 2 NOS

23 RECYCLE COMPRESSOR

24 H₂ COMPRESSOR

25 ASU I TURBINE

26 STUD & NUTS

27 BOILER

28 SEALANT,WASTE,WELDING SPARES

TOTAL (for one year)Table II: SUMMARY OF ELECTRICAL SPARES

SL.NO DESCRIPTION

1 62.5 KVA DG SET - 1

2 62.5 KVA DG SET - 2

83

3 LIGHTS

4 BCH MOTOR STARTER

5 HRC FUSE

6 POWER CONTACTOR

7 TIMER

8 AUXILLARY CONTACTOR

9 DIGITAL METERS

10 OVER LOAD RELAY

11 ACB

12 VCB

13 MOTOR

14 MCCB

15 SWITCH DISCONNECTOR

TOTAL (for one year)

Table III: SUMMARY OF INSTRUMENTATION SPARES:

SL.NO DESCRIPTION

1 SPARES (for one year)

Table IV: SUMMARY OF SAFETY SPARES:

SL.NO DESCRIPTION

1 SPARES (for one year)

84

Table V: PROCESS, MECHANICAL, INSTRUMENTATION AND ANALYTICAL LAB, ELECTRICAL LOG BOOKS:

SL.NO DESCRIPTION

1 PROCESS,MECHANICAL,INSTRUMENTATION AND ANALYTICAL LAB LOG BOOK (for one year)

2 ELECTRICAL LOG BOOKS

TOTAL:

SL. NO DESCRIPTION

I MECHANICAL SPARES

II ELECTRICAL SPARES

III INSTRUMENTATION SPARES

IV SUMMARY OF SAFETY SPARES

V PROCESS, MECHANICAL, INSTRUMENTATION AND ANALYTICAL LAB, ELECTRICAL LOG BOOKS:

85

Enclosure-1TENTATIVE LIST OF DETAILS OF MECHANICAL SPARES 1. LIN, LOX TRANSFER HOSE AND PIG TAIL HOSE (Per year)

SL.NO DESCRIPTION QTY

1

LIN, LOX TRANSFER HOSE Stainless steel (Double Braid) Hose having inner corrugation out of SS 316 and Outer Wire Braiding out of SS 304 Size: 1.1/2" ID in length of 2500 mm having 1.1/2" BSP female. Swivel fittings St. at both ends. Working Pressure: 53 bar Permanent Bend Radius: 172 mm Flexing Bend Radius: 325 mm Temp. : -196 Deg C to 600 Deg C

3

2

PIG TAIL HOSE Bengal make 1-1/4" NB X 1630 mm X 445 mm Long SS 321 Hose with SS 304 wire double braided assembly complete with one side1-1/4" NB SS 304 Swivel flange ASA 600 LBS Swivel flange over SS 304 Stub & other end1-1/2" NB SS 304 Swivel flange ASA 600 LBS over SS 304 Stub

3

2. BEARING (SKF MAKE) (For Two years)

SL.NO DESCRIPTION BEARINGN

UMBERQTY

1 Naphtha Transfer Pump 6306 4

2 Naphtha Transfer Motor 6308 4

3 Naphtha Feed Pump 7304 4

86

4 Naphtha Feed Pump Motor 6205 ZZ 4

5 BFW Pump 30206 4

6 BFW Pump Motor 6208 ZZ 4

7 Hydrazine Dosing Pump 30205 2

8 Hydrazine Dosing Pump Motor 6208 ZZ 2

9 Recycle Compressor

NU 209 ECP 2

NU 307 ECP 2

NU 211 ECP 2

6009 2

NA 22025 2

10 Recycle Compressor Motor

 

6208 2

6308 2

11Reformer Blower (Ventapp make)

6210 1

NU 2210ECJ 1

12 Reformer Blower (Almonard make) 6311 2

13 Reformer Blower Motor 6208 C3 2

14Chiller Compressor Motor

 

6206 1

6208 1

15 Evaporator Column Chilling Pump 6208 1

16 3309 A/C3 2

87

N₂ Vacuum Pump6309 2

NU 2212 ECP 2

17 N₂ Vacuum Pump Motor A 6316 C3 2

18 N₂ Vacuum Pump Motor B 6215 C3 2

19 A/C Compressor Motor6208 ZZ 3

6206 ZZ 3

20 AHU Blower 6312 C3 1

21 AHU Blower MotorNU 309 1

6209 1

22 160 m³ Cooling Water PumpNU 309 2

7309 B 4

23 160 m³ Cooling Water Pump Motor NU 318 C3 1

24160 m³ Cooling Water Pump Motor

NU 215 C3 2

6215 C3 2

25DM Water Degasser Pump

 

3304 2

6304 2

26 25 m³ Cooling Water PumpNU 2209 2

3309 2

27 25 m³ Cooling Water Pump Motor6208 2

6308 2

28 Fire Fighting Pump NU 315 C3 1

29 Fire Fighting Jockey Pump Motor 6308 ZZ 1

88

6208 ZZ 1

30 Fire Fighting Jockey Pump Motor6309 1

6209 1

31 Raw Water Pump6309 2

6207 2

32 Raw Water Pump Motor6306 2

6206 2

33 Degasser Blower 6205 2

34 ETP Reformer Effluent Pump6305 2

7305 2

35 ETP Reformer Effluent Pump Motor 6305 1

36 Oil Effluent & Irrigation Pump 6203 2

37 Cooling Tower Motor6309 ZZ 4

6209 ZZ 4

38 Blue star Chiller Pump6206 ZZ 2

6207 ZZ 2

3. BELT (CONTINENTAL MAKE) (For Two years)

SL.NO

DESCRIPTION BELT NUMBER

QTY

1 A/C Plant Compressor Motor C 2720/C 105 12

2 LHPS A/C Compressor Motor B 1620/B-62 8

3 GH₂ Compressor Blower B 100 B 2580 3

89

L

4 Chiller Plant Compressor Motor C 2545/C 98 4

5

Lab A/C Compressor Motor

B 1850/B 71 2

B 46 1

6 Instrument Air Compressor SPC 4000 4

7 A/C Plant AHU I B 96 2

8 A/C Plant AHU II B 71 2

9 LHPS A/C AHU B 61 24. RUPTURE DISK (For one year)

SL.NO DESCRIPTION QTY

1

13 KL LIN/LOX TANKERS (G-79,80,85)DRSV316/316/TFE Tension loaded pre bulged slotted Composite Rupture with vacuum support-support rings & soft gasket Burst Pressure: 12.0000 BAR(G)Burst Temperature : 22.0 deg C Burst Tolerance :+/5%

6

2

6 KL LIN TANKER (G0001) DRSV316/316/TFE Tension loaded pre bulged slotted Composite Rupture with vacuum support-support rings & soft gasket Burst Pressure: 26.0000 BAR(G)Burst Temperature : 22.0 deg C Burst Tolerance :+/5%

2

90

3

6 KL LIN TANKER (TNK 8332) DRSV316/316/TFE Tension loaded pre bulged slotted Composite Rupture with vacuum support-support rings & soft gasket Burst Pressure: 19.0000 BAR(G)Burst Temperature : 22.0 deg C Burst Tolerance :+/5%

2

5. DM PLANT VALVE (BHARAT INDUSTRIAL SYSTEMS) (For Three years)

SL.NO DESCRIPTION SIZE QTY

1 Diaphragm valve

60 NB 2

50 NB 4

40 NB 5

25 NB 5

20 NB 2

2

Diaphragm 40 NB 5

20 NB 5

25 NB 5

6. GASKETS (For Three years except Boiler Gasket)

SL NO MATERIALS SIZE QTY

1FEED PRE HEATER DOME: (4.8 X 438 X (OD) X 418) S.S 304 SPIRAL WITH ASBESTOS

4.8 X 438 X 418 2

2 S.S 304 SPIRAL WOUND WITH ASBESTOS 4.5 X 125 X 157 2

3 NAPHTHA EVAPORATOR IRON JACKETED (IJA)

3.5 X 386 X 426 2

91

IRON JACKETED ASBESTOS 3.5 X 394 X 426 2

4

ECONOMIZER FLANGE SIDE 3.5 X 52.6 X 91.6 2

S.S JACKETED ASBESTOS 3.5 X 126 X 100 4

S S 304 WOUND SPIRAL GASKET 3.5 X 356 X 336 2

S.S 304 WOUND SPIRAL GASKET 3.5 X 73 X 107.9 2

5

WATER COOLER CAF – OIL 3.2 X 438 X 409 2

CAF – OIL 2 X 117 X 157 2

6

NAPHTHA CONDENSOR CAF – OIL RES 2 X 400 X 438 2

CAF – OIL RES 2X 273 X 293 2

7BOILER GASKET MAN HOLE - 2

HAND HOLE - 4

8 SS304/GL/SS304 IR & OR

2”-300# 20

2 ½” -300# 20

3”– 300# 20

9 SS304/GL/SS304 IR & OR1 ½”– 300# 20

1 ¼” -300# 20

10 NITRILE RUBBER GASKETS SHEET 1000X1000X4 1

11

1 mm TUFFLAN GASKET SHEET 1000x1000x1 1

2 mm TUFFLAN GASKET SHEET 1000x1000x2 1

3 mm TUFFLAN GASKET SHEET 1000x1000x3 1

12 GRAPHITE SHEET 1000x1000x1 1

92

1000x1000x2 1

1000x1000x3 1

13SPITMAN STYLE 20 CAF JOINTING SHEET

1525mmX1650 mmX1mm 2

1525mmX1650 mmX2mm 2

1525mmX1650 mmX3mm 2

14SPITMAN STYLE 59(GRAY COLOUR) CAF JOINTING SHEET

1525mmX1650 mmX1mm 2

1525mmX1650 mmX2mm 2

1525mmX1650 mmX3mm 1

15 TEFLON SHEET

1000mmX1000 mmX0.5mm 2

1000mmX1000 mmX1mm 2

1000mmX1000 mmX1.5mm 2

1000mmX1000 mmX2mm 2

1000mmX1000 mmX3mm 1

16 ASBESTOS ROPE

6 mm 5

10 mm 5

12 mm 5

17 GRAPHITE METALIC ROPE6 mm 5 Box

8 mm 5 Box

93

18 PURE TEFLON ROPE 2 Box

19 PURE GRAPHITE SHEET

1000x1000x1 2

1000x1000x2 2

1000x1000x3 2

20 FULL THREADED STUD WITH TWO NUTS

12/40 19

12/65 24.4

16/40 31

16/65 34.6

7. LIN /LOX TANKERS (For Three years)

SL. NO MATERIAL QUANTITY

1 GASKET (METTALIC TEFLON 150 GLASS) 1 1/2" 25

2G.G BRONZE CRYOGENIC GLOBE VALVE (40mm) WORKING PRESSURE 17.3 Kg/Cm2 AT 195°C

3

8. NAPHTHA TRANSFER PUMP (2 NOS) (For Three years)

TAG NO MODEL NO. TYPE MAKE FLOW RATE

ILHP/619&620 D-211044001 CCR32 -200R6M2L3

STORK PUMPINDIA LTD 19 m³/hr

SL NO PART NO ITEM MATERIAL OF CONSTRUCTION

QTY

94

1 140 LEG STEEL 2

2 300 GASKET CAF 2

3 310,320 PLUG SS 316 2

4 1200SHAFT SLEEVE SS 316 2

5 1210 BUSH SS 316 2

6 1230 SEAL COVER STEEL 2

7 1420 NIPPLE STEEL 2

8 1300 GASKET CAF 2

8 1320 GASKET CAF 2

10 1340 GASKET CAF 2

11 1800 STUD STEEL 2

12 1820 CAB NUT SS 316 2

13 1860 KEY SS 316 2

14 2110BEARING COVER C.I 2

15 2120, 2125 OIL BUFFLE BRONZE

2

16 2140 OIL LEVELER STEEL 2

17 2150 PLUG SS 316 2

18 2160 GASKET CAF 2

19 2220 DEFLECTOR STEEL 2

20 2300INTERNAL CIRCLIP STEEL 2

21 2340ADJUSTING RING STEEL 2

95

22 2350DISTANCE SLEEVE STEEL 2

23 2351MECHANICAL SEAL CEROMIC 1

9. NAPHTHA FEED PUMP (2 NOS) (For Three years)

TAG NO MODEL NO. SERIAL NO MAKE FLOW RATE

P 0101&101R 4 WDD –2250/36 4720/97 SWELORE CONTROLVOLUME PUMP 212 Lit/hr

10. BOILER FEED WATER PUMP (2 NOS) (For Three years)

96

SL NO CODE NO DESCRIPTION MATERIAL

1 203A WORM SHAFT OIL SEAL 20357

2 214 SLIDE BALL SEAT EN9

3 403 PISTON BALL SEAT EN9

4 405 CONNECTING BALL EN9

5 406 DISTANCE PIECE MS

6 407 DISTANCE PIECE LOCK NUT MS

7 409 OIL SEAL 385410

8 619 GLAND PACKING PTFE

9 621 DELIVERY VALVE SEAT(I) SS 316

10 622 DELIVERY VALVE SEAT(II) SS 316

11 623 SUCTION VALVE SEAT(I) SS 316

12 624 SUCTION VALVE SEAT(II) SS 316

13 625 VALVE SS 316

TAG NO MODEL NO. SERIAL NO MAKE FLOW RATE

P 102& 102R WH 3000/54 3190/92-93 SWELORE CONTROLVOLUME PUMP 915 Liter/hr

SL NO

CODE NO DESCRIPTION MATERIAL QTY

1 512 VALVE SS316 4

2 510SUCTION VALVE SEAT (I) SS316 2

3 509DELIVERY VALVE SEAT (II) SS316 2

4 504 GLAND PACKING PTFE 2

5 407DISTANCE PIECE LOCK NUT MS 2

6 406 DISTANCE PIECE MS 4

7 405 CONNECTING BALL EN9 2

8 404 BALLSEAT COVER EN9 4

9 403 PISTON BALL SEAT EN9 2

10 203AWORM SHAFT OIL SEAL 305010 2

11 409 OIL SEAL 456510 2

12 401 SLEEVE CI 1 11. HYDRAZINE DOSING PUMP (For Three years)

TAG NO MODEL NO. SERIAL NO MAKE

P 0103 WDD 1125/10 3141/92-93 SWELORE

97

SL NO CODE NO DESCRIPTION QTY

1 203A OIL SEAL 1 SET

2 409 OIL SEAL  1 SET

3 619 GLAND PACKING 1 SET

4 622 DELIVERY VALVE SEAT 1 NO

5 624 DELIVERY VALVE SEAT 1 NO

6 621 DELIVERY VALVE 2 NO'S

7 623 SUCTION VALVE 1 NO

8 624 SUCTION VALVE SEAT 1 NO

9 625 SUCTION VALVE SEAT 1 NO

12. COOLING WATER PUMP160m³ (2 NOS) (For Three years)

MAKE: KIRLOSKAR

SL NO PART NO PART

DESCRIPTIONMOC DESCRIPTION

QTY

1 18002684PUMP SHAFT (FOR REINFORCED B

ASTMA 322 - 4140 ANNEALED

1

2 19000012CASING WEARING RING (SUCTION)

CI IS 210 – FG 260 2

3 19100012CASING WEARING RING (DELIVERY)

CI IS 210 - FG 260 2

4 19200110 IMPELLER RING (SUCTION SIDE)

LT BR IS 318 -LTB2 2

5 19300110 IMPELLER RING (DELIVERY SIDE)

LT BR IS 318 -LTB2 2

98

6 22700012 LANTERN RING CI IS 210 - FG 260 2

7 31100556 SHAFT SLEEVE P.S

ST AISI - 41 OH 300 BHN 2

8 35000012 THROAT BUSH CI IS 210 - FG 260 1

9 24000012 BEARING HOUSING

CI IS 210 - FG 260 1

10 43002345 GLAND PACKING CHAMPION -1094 OR EQ 1

11 SUBSOG SET OF GASKETS NAM 37 1

12 SUBSOO SET OF OIL SEALS

NTR RBR ST SPRING 1

13 SUBSOR SET OF 'O' RINGS NE RUBBER 1

14 SUBSOF SET OF FASTNERS

STD MS - CL (270/276) 1

13. RAW WATER PUMP (2 NOS) (For Three years)MAKE: JOHNSONFLOW RATE: 10 m³/hr

SL NO PART NO DESCRIPTION MATERIAL QTY

1 140 LEG STEEL 1

2 300 GASKET CAF 1

3 310,320 PLUG SS 316 1

4 1200 SHAFT SLEEVE SS 316 1

5 1210 BUSH SS 316 1

99

6 1230 SEAL COVER STEEL 1

7 1420 NIPPLE STEEL 1

8 1300 GASKET CAF 1

9 1320 GASKET CAF 1

10 1340 GASKET CAF 1

11 1800 STUD STEEL 1

12 1820 CAB NUT SS 316 1

13 1860 KEY SS 316 1

14 2110 BEARING COVER C.I 1

15 2120, 2125 OIL BUFFLE BRONZE 1

16 2140 OIL LEVELER STEEL 1

17 2150 PLUG SS 316 1

18 2160 GASKET CAF 1

19 2220 DEFLECTOR STEEL 1

20 2300 INTERNAL CIRCLIP STEEL 1

21 2340 ADJUSTING RING STEEL 1

22 2350 DISTANCE SLEEVE STEEL 1

23 2351 MECHANICAL SEAL

CEROMIC 2

100

14. VACUUM PUMP -COOLING WATER PUMP (For Three years)MAKE: STROKE PUMP IND LTDFLOW: 17.5m³/hr

SI NO MATERIAL

1 SHAFT

2 SEAL (MECHANICAL)

3 OIL SEAL

4 SPIDER - COUPLING (NO 95)

15. N2 VACUUM PUMP 302 A & 302B(For Three years)MAKE: AREZENEM GERMANYCAPACITY: 38.90M³/min (302 A)CAPACITY: 16.60M³/min (302 B)

SI NO MATERIAL

1 COUPLING

2 SPIDER (C226) 2Nos

16. ETP PLANT (For Three years)MAKE: JOHNSON PUMPFlow Rate: 10m³/hr

SI NO DESCRIPTION

1 OIL SEAL

2 SHAFT

3 GLAND PACKINGOIL EFFLUENT PUMP (For Three years)MAKE: JOHNSON PUMP

SI NO DESCRIPTION

101

1 OIL SEAL

2 SHAFT

3 GLAND PACKING

AGITATORMAKE: ELCON

SI NO DESCRIPTION

1 OIL SEAL

17. COOLING TOWER (4 NOS) (For One year)MAKE: UNITED COOLING TOWERSMODEL: UFC 300

SI NO DESCRIPTION QTY

1 6' SPRINKLER 1

2 PVC FILLS HONEY COMB TYPE COLOUR: TRANSPARENT BLUE

SIZE: 600 X300mmX150m 1 No= 1 CFT NOTE: 250 CFT FILLS REQUIRED FOR 1 NO COOLING TOWER

250 CFT

18. REFORMER BLOWER (For Three years)MAKE: VENTAPP

SI NO DESCRIPTION

1 COUPLING (95 mm)

2 SPIDER (95 - R)19. FIRE WATER PUMP 171 m3 /hr (For Three years)

102

MAKE: MATHER & PLATTFLOW: 170 m³

SI NO

PART NO

PART DESCRIPTION

MOC DESCRIPTION

QTY

1 18002684

PUMP SHAFT (FOR REINFORCED B

ASTMA 322 - 4140 ANNEALED

1

2 19000012

CASING WEARING RING (SUCTION)

CI IS 210 - FG 260 1

3 19100012

CASING WEARING RING (DELIVERY)

CI IS 210 - FG 260 1

4 19200110

IMPELLER RING (SUCTION SIDE)

LT BR IS 318-LTB2 1

5 19300110

IMPELLER RING (DELIVERY SIDE)

LT BR IS 318-LTB2 1

6 22700012

LANTERN RING

CI IS 210 - FG 260 1

7 31100556 SHAFT

SLEEVE P.S

ST ST AISI - 41 OH 300 BHN

1

8 35000012 THROAT BRUSH

CI IS 210 - FG 260 1

9 24000012 BEARING HOUSING

CI IS 210 - FG 260 1

10 43002345 GLAND PACKING

CHAMPION -1094 OR EQ

1

103

11 SUBSOG SET OF GASKETS NAM 37 1

12 SUBSOO SET OF OIL SEALS

NTR RBR ST SPRING 1

13 SUBSOR SET OF 'O' RINGS

NE RUBBER 1

14 SUBSOF SET OF FASTENERS

STD MS - CL (270/276)

1

20. FIRE JOCKEY PUMP (For Three years)MAKE: MATHER & PLATTFLOW: 170m³

SI NO MATERIAL

1 OIL SEAL

2 SHAFT

3 GLAND PACKING

4 SLEEVE

21. ACCKL COMPRESSOR (MODEL: SMC4-100)(For Three years)

SL. NO PART DESCRIPTION QTY

1 CRANK SHAFT 6H C 55 1

2 NUT FOR CRANK SHAFT 1

3 WASHER FOR CRANK SHAFT 1

4 CONNECTING ROD 1

5 CONNECTING ROD LOCKING PLATE 1

6 UNLOADING PISTON 1

104

7 PACKING UNLOADER PISTON (TEFLON RING) 1

8 UNLOADER PISTON RETAINER 1

9 DIS. VALVE STOPPER 1

10 OIL PUMP ELEMENT 1

11 OIL PUMP BODY BUSH 1

12 CYLINDER LINER 1

13 BEARING SLEEVE MOTOR SIDE 1

14 BEARING SLEEVE OIL PUMP 1

15 C.R.BEARINGS (CRANK PIN METAL) 1

16 PISTON RING (1 SET) 1

17 OIL SCRAPING 5RING (1 SET) 1

18 PISTON 1

19 PISTON PIN 1

20 DIS.VALVE REED 1

21 SUC.VALVE REED 1

22 SUCTION FILTER 6HS - 55 1

23 OIL FILTER 1

24 DEMISTER ASSY 1

25 VALVE SEAT 4 HC/5HC - 1

105

55

26 GROOVED PIN 1

27 UNLOADING LIFT PIN 1

28 UNL.SPRING 6HC -- R4 - 18 - 117 1

29 RELIEF Hd.SPRING R4 - 1 -671 1

30 SUC. & DIS. SPRING R4 - 16 -763 1

31 SPRING REV. RETAINER R 414-1213 1

32 SPRING OIL PUMP R4 - 14 - 1217 1

33 SPRING UNL.LIFT PIN R4 - 18 -158 1

34 SIGHT GLASS 1

35 SIGHT GLASS ADOPTER 1

36 OIL PRESSURE CONTROL VALVE 1

37 SHAFT SEAL ASSEMBLY 1

38 SHAFT SEAL COVER 1

39 RING FOR SHAFT SEAL 1

40 CRANK CASE HEATER 1

41 O' RING SET 1

42 GASKET SET 6HC55 (FULL SET) 1

106

22. INSTRUMENT AIR COMPRESSOR MAKE: KIRLOSKAR PNEUMATIC CO.LTDFLOW: 2.7 Nm³/minHIGH PRESSURE SIDE: (For One year)

SL NO PART NUMBER

DESCRIPTION/ CUSTOMER PART NO

QTY

1 72771034050 PISTON RING 6

2 72770038750 GUIDE RING 4

3 72480039750

SEALING RING(ROD PACKING) 3 PIECES

6

4 72481033150

SEALING RING(ROD PACKING) 6 PIECES

6

SL NO PART NUMBER

DESCRIPTION/ CUSTOMER PART NO

QTY

1 72480034050 PISTON RING 4

2 72480034051 GUIDE RING 4

3 72480100550

SEALING RING(ROD PACKING) 3 PIECES

6

4 72480100750

SEALING RING(ROD PACKING) 6 PIECES

6

SL NO PART DESCRIPTION/ QTY

107

NUMBER CUSTOMER PART NO

1. 72480100450 PRESSURE BREAKER 2

2. 72480031350 OIL WIPER RING 2

3. 72460065350 VALVE PLATE 5

4. 72460065450 CUSHION PLATE 5

5. 72460067350 VALVE SPRING 25

6. 72770066450 VALVE PLATE 5

7. 72770062150 CUSHION PLATE 5

8. 79991269550

O' RING SILI 35.5X29.500X3.0000XC 5

9. 70910071250 FILTER ELEMENT 2

10. 70122212000 OIL SEALING JOINT 10

11. 70910071500 SEALING JOINT 10

12. 70910070500 SEALING JOINT 10

13. 7241010550 SEAL OIL 10

14. 910071250 OIL FILTER 2

15. 2770060050 SUCTION VALVE ASSY H.P 1

16. 2770070050 DELIVERY VALVE ASSY H.P 1

108

17. 72460020550 PACKING 2

18. 74260030450 CROSS HEAD NUT 2

19. 72460031650 PISTON ROD NUT 1

20. 72770020550 PACKING 2

21. 72770076550 COPPER RING 4

22. 79991289250

O' RING NITR -X79.300X5.7000XC 8

23. 72460021850 PACKING 8

24. 72520032050 CROSS HEAD BUSH 4

25. 72520040850

OIL SEAL MOM 75-100-12 1

26. 72520051150 WASHER THRUST 2

27. 72480031350 OIL WIPER RING 4

28. 72480039550 GARTER SPRING 4

29. 72520056350 SAFETY PLATE 62

30. 72480065150 VALVE SEAT 1,780

31. 72460065650

BOLT SPECIAL M12X1.5XDRG CH 145

32. 72460061350

LOCATING PIN REF 2500061350 62

109

33. 72460060950 NUT CASTLE 122

34. 72460061150 CIRCLIP 62

35. 72480075150 VALVE SEAT 1,780

36. 72480075250 VALVE GUARD 1,285

37. 72460065350 VALVE PLATE 579

38. 72460065450 CUSHION PLATE 451

39. 19 2460067350 VALVE SPRING 122

40. 72460075650

STUD SPECIAL M12X1.5XDRG CH 122

41. 72770061850 VALVE SEAT 2

42. 72770062050 VALVE GUARD 2

43. 72770066450 VALVE PLATE 8

44. 72770062150 CUSHION PLATE 8

45. 72770061750 BOLT 2

46. 72770062450

WASHER PLAIN STEEL 8X0.55 10

47. 79990954850

CYLINDRICAL PIN DIA 3.00 X10L 4

48. 95 2480095250 VALVE PUSHER 2

110

49. 72770071050 VALVE SEAT 2

50. 70910071250 FILTER ELEMENT 2

51. 70122212000 OIL SEALING RING 2

52. 70910071500 SEALING JOINT 2

53. 72410110550 SEAL OIL 1

54. 79991212800

O RING NEOP -X1.487"X0.103"XC 1

55. 72480100450 PRESSURE BREAKER 2

56. 79991269550

O RING SILI 35.5X29.500X3.000XC 20

57. 72770076550 COPPER RING 8

58. 72770076650 COPPER RING 8

59. 72460021850 PACKING 8

60. 72460071350 SEALING RING ID 91.0 10

23. RECYCLE COMPRESSOR (For One year)HOFER NO: 2NosMAKE: ANDREAS HOFER

SI NO MATERIAL

1 SPIDER 2 NOS

111

24. H2 COMPRESSOR (For One year)MAKE: NEUMAN & ESSARFLOW: 1000 m³/hr

SI NO MATERIAL

1 BRASS RING 76 X 86 (5 NO'S)

2 BRASS RING 65 X 75 (5 NO'S)

25. ASU - I TURBINE

MAKE ATLAS COPCO

CAPACITY 3410 Nm3/hr

SPEED 35,800 rpm

TURBINE CARBON SEAL (For One year)

SI NO MATERIAL Qty

1 CARBON SEAL  

26. STUD & NUTS (For Five years)

Part No Description SizeMaterial

Specification

Quantity

FEED PRE-HEATER

7 STUDS5/8" UNC X 190lg

SA 193 GR 87 29

8 NUTS(HEX)

5/8 " UNC X STD

HEAVY HEX SA 193 GR 4

58

9 JACK SCREW

M 16 X 85 lg

IS 1367 C.L.4.6

2

112

(Full thread)

16 STUDS3/4" UNC X 145 lg

SA 193 GR 87 21

17 NUTS3/4" UNC

STD SA 194 GR.4 42

32A

BOLT WITH NUT/

WASHER

M8 X 25 lg /M8 STD

CADMIUM PLATED/SS

2/TWO

41

NUT(HEX) FOR TIE

ROD M8 STDIS 1367 -

CL.4.016

NAPHTHA EVAPORATOR

11 STUDS3/4" UNC X 175 lg

SA.193 - B 7 20

12 NUTS(HEX)3/4" UNC

STD SA.194 - 4 40

16 JACK SCREWM16 X 80

lg C.S 4

22 STUDS5/8" UNC X 80 lg

SA 193 - B 7 8

23 NUTS(HEX)5/8" UNC

STD SA 194 - 4 16

25G STUDS5/8"UNC X 80 lg

SA 193 - B 7 4

25H NUTS(HEX)5/8" UNC

STD SA 194 - 4 8

36A NUTS(HEX) M 10 STD IS 1367 C.L.4.0 4

37PULLING EYE BOLT

20ø X 275 D. Lg C.S 2

113

59BOLT WITH NUT(HEX)

M 8 X 25 lg

CADMIUM PLATED 2

60 WASHER M 8 S.S 2

*

STUDS WITH 2 NUTS FOR P.NO 11, 12

3/4" UNC X 165 lg

SA 193-67/SA 194

- 45

*STUDS WITH 2 NUTS FOR P.NO 22,23,25G,25H

5/8" UNC X 80 lg

SA 193 - B7/SA 194

-45

ECONOMIZER

7 STUDS 5/8"UNC X 150 lg

SA - 193 GR - B7 40

8 NUTS(HEX) 5/8" UNC STD

SA - 194 GR - 2 H 80

13 STUDS 5/8"UNC X 85 lg

SA - 193 GR - B7 8

13A STUDS 5/8"UNC X 85 lg

SA - 193 GK - B8 8

14 NUTS(HEX) 5/8" UNC STD

SA - 193 GR- 2H 16

14A NUTS(HEX) 5/8" UNC STD

SA - 194 GR - B8 16

18 STUDS 3/8"UNC X 110 lg

SA - 193 GR - B8 32

19 NUTS(HEX) 3/4"UNC STD

SA 194 GR - B8 64

*

STUD WITH TWO NUTS FOR P.NO 7,8

5/8"UNC X 150 lg

A 193 GR . B7/

A 194 GR . 2H

5

* STUD WITH 5/8"UNC A 193 GR . 5

114

TWO NUTS FOR P.NO 13A,14A X 85 lg

B8/ A 194 GR .

B8

*

STUD WITH TWO NUTS FOR P.NO 18,19

3/4"UNC X 110 lg

A 193 GR . B8/

A 194 GR . B8

5

*

STUD WITH TWO NUTS FOR P.NO 13,14

5/8"UNC X 85 lg

A 193 GR . B7/

A 106 GR . 2H

5

7 STUDS 5/8" UNC X 145 lg

SA 193 GR B7 24

8 NUTS 5/8" UNC STD

SA 197 GR 2H 48

9 JACK SCREW M 16 X 90 lg

IS 1367 CL : 4.6 2

16 STUDS 3/4" UNC X 110 lg

SA 193 GR B8 16

17 NUTS(HEX) 3/4" UNC STD

SA 194 GR B8 32

*STUD WITHTWO NUTS P.NO 7,8

5/8" UNC X 145 lg

SA 193 GR B7

SA 194 GR 2H

5

*STUD WITHTWO NUTS P.NO 7,9

5/8" UNC X 145 lg

SA 193 GR B8

SA 194 GR B8

5

9 STUD /BOLT5/8" UNC X 120 lg A 193 GR B7 20

10 NUTS5/8" UNC

STD A 194 GR 4 40

16 STUD /BOLT5/8" UNC X 180 lg

A 193 GR 5B 7 16

115

17 NUTS5/8" UNC

STD A 194 GR 4 32

22 STUD /BOLT5/8" UNC X 75 lg A 193 GR B7 16

23 NUTS5/8" UNC

STD A 194 GR 4 24

*STUD WITH TWO NUT P.NO 9,10

5/8" UNC X 120 lg

A 193 GR B7/

A 194 GR 45

*STUD WITH TWO NUT P.NO 16,17

5/8" UNC X 140 lg

A 193 GR B7/

A 194 GR 45

*STUD WITH TWO NUT P.NO 22,23

5/8" UNC X 180 lg

A 193 GR B7/

A 194 GR 45

*STUD WITH TWO NUT P.NO 33,34

5/8" UNC X 75 lg

A 193 GR B7/

A 194 GR 45

33

STUD/BOLT (FOR CONN A1,A2)

5/8" UNC X 75 lg A 193 GR B7

8

34 NUTS (FOR CONN A1,A2)

5/8" UNC STD A 193 GR 4 16

BOILER

SI NOBOLT

DIAMETER mm

NUT SIZE mm

LENGTH mm

(inches)

QTY ESTIMATED AMOUNT

1 20 30 100(4") 44

2 16 27 90(3.5") 268

3 16 24 90(3.5") 76

4 12 19 65(2.75") 68

116

5 12 19 75(3") 52

6 18 32 146(5.75") 4

7 16 27 125(5") 16

8 16 27 100(4") 8

9 19 30 115(4.5") 12

10 19 30 125(5") 12

11 12 19 140(5.5") 44

12 mm &16 mm STUD

11/2"& 21/2" 26

27. BOILER (For Three years)

MAKE REKUPARATOR

CAPACITY 537 Kg/hr

WORK PRES 27.0BAR

SI NO DESCRIPTION QUANTITY

1

CAST STEEL GATE VALVE CLASS 300#, FLANGED ENDS SIZE : 1/2" WITH IBR CERTIFICATE

3 NO'S

2

CAST STEEL GATE VALVE CLASS 300#, FLANGED ENDS SIZE : 1" WITH IBR CERTIFICATE

3 NO'S

117

28. Sealants, Cotton, Welding Spares, waste etc. (For One year)

SL.NO DESCRIPTION QTY

1 ANABOND 202 (10g) 100

2 ANABOND 666 (50g) 50

3 ANABOND THREAD SEAL (4ml)

50

4 ARALDITE 25

5 M SEAL (100g) 50

6 TEFLON TAPE (12mmx10m)

50 BOX

7 RUSTOLIN (250ml) 20

8 HS HACKSAW BLADE 50

9 COTTON WASTE 500

10 O₂ CYLINDER 5

11 ARGON CYLINDER 3

12

ARC WELDING ROD CARBON STEEL (SIZE = 3.15)

5(PACK)

13ARC WELDING ROD E 7018 (SIZE = 2.15) 2(PACK)

14

ARC WELDING ROD CARBON STEEL (SIZE = 2.5)

5(PACK)

15

ARC WELDING ROD ESAP E309MO 16 (SIZE = 2.5)

1(PACK)

16 ARC WELDING ROD CAST IRON ROD

1(PACK)

118

(SIZE = 3.15)

17TIG WELDING 309 L (SIZE = 2mm) 3 Kg

18TIG WELDING 308 L (SIZE = 2mm) 3 Kg

19

(TEFLON TAPE, GLYCERIN,POLYTHENE SHEET ETC)

1

Enclosure-2TENTATIVE LIST OF ELECTRICAL SPARES62.5 KVA DG SET -1

SL.NO DESCRIPTION QTY

1 Batteries for DG sets, UPS, prime movers etc. 10

1A Battery charger 1

2 Radiator Fan Belt 2 (sets)

3 Oil Filter 4

119

4 Fuel Filter 4

5 Air Filter1 1

6 Air Filter2 1

7 Oil Pressure Transducer 1

8 Self Motor 1

9 Dynamo 1

62.5 KVA DG SET -2

SL.NO DESCRIPTION QTY

1 12v Battery 88AH 1

2 Radiator Fan Belt 1

3 Oil Filter 6

4 Fuel Filter (Primary &Secondary) 6(sets)

5 Air Filter1 2

6 Air Filter2 2

7 Oil Pressure Sensor 1

8 Self Motor 1

9 Dynamo 1LIGHTS

SL.NO DESCRIPTION QTY

1 125W HPMV LAMP 10

2 70W SV LAMP 4

120

3 40W TUBE LIGHT 150

4 40W TUBE LIGHT COPPER CHOKE

100

5 40W TUBE LIGHT STARTER & HOLDER WITH BASE

50

6 2SQMM 3CORE FLEXBLE CABLE

1 COIL

7 20W CFL 20

8 150W HPSV LAMP 15

9 INSULATION TAPE 150

10 150W HPSV CHOKE 10

11 125W HPMV CHOKE 10

12 70W CHOKE 3

13 IGNITOR FOR 150W SV LAMP 10

14 EARTHING COPPER 4 KGBCH MOTOR STARTER

SL.NO DESCRIPTION QTY

1 7.5HP DOL 1

2 10HP DOL 1

SL.NO DESCRIPTION QTY

1 2POLE MCBs 10

121

2 3POLE MCBs 10

3 4POLE MCBs 5HRC FUSES

SL.NO DESCRIPTION QTY

1 NS 2,4,6,10AMPS (each 10 nos) 50

2 NS 16,25,32AMPS (each 10 nos) 30

3 3NA 6,10,16AMPS 20

4 3NA 25,3NA 32 12

6 3NA 63 15

7 3NA 100 10

8 3NA 125 7

9 3NA 250 10

10 3NA 400 6

11 3NA 800 6

12 THYRISTOR HRC FUSE(SITAR)63AMPS

3

POWER CONTACTOR

SL.NO DESCRIPTION QTY

1 3TF 16 AMPS 3

2 32AMPS 3

122

3 40AMPS 3

4 63AMPS 3

5 100AMPS 2

6 150AMPS 1

7 ML1.5 2

8 ML2 2

9 ML3 3

10 ML4 2

11 ML6 2

12 630AMPS TC CONTACTOR COIL

1

TIMER

SL.NO DESCRIPTION QTY

1 ON DELAY TIMER 4

2 OFF DELAY TIMER 4

3 SINGLE PHASING PREVANTOR 5AUXILLARY CONTACTOR

SL.NO DESCRIPTION QTY

1 110V,220V,415V AC(2NO,2NC) 6

2 24V,110V DC (2NO,2NC) 3

123

DIGITAL METERS

SL.NO DESCRIPTION QTY

1 VOLTMETER 2

2 AMMETER 2

3 MULTIFUNCTION METER (V,A,HZ,PF,W,KWH)

1

OVER LOAD RELAY (SIEMENS / L&T) (for three years)

124

ACB (for three years)

SL.NO DESCRIPTION QTY

1 1000A,1250A,1600A CLOSING,SHUNTCOIL,UNDER VOLTAGE COIL

2

2 HAND SPRING CHARGE UNIT MECHANISM 2

3 SAFETY SHUTTERS (1000A,1250A 3POLE) 1

4 SAFETY SHUTTERS (1600A 4POLE) 1

5 SAFETY SHUTTERS 1

125

SL.NO DESCRIPTION QTY

1 3-5 AMPS 2

2 4-10 AMPS 2

3 10-16 AMPS 3

4 13-20 AMPS 3

5 22-32 AMPS 3

6 30-50 AMPS 2

7 50-90 AMPS 1

8 60-120 AMPS 1

9 120-150 AMPS 1

10 160-230 AMPS 1

11 50-200 AMPS 1

(2000A,3200A 4POLE)

6 LAMINATION BLOCK (1000A,1250A 3POLE) 1

7 LAMINATION BLOCK (2000A 4POLE) 1

8 LAMINATION BLOCK (3200A 4POLE) 1VCB (for three years)

SL.NO DESCRIPTION QTY

1 VCB CLOSING & SHUNT COIL WITH MECHANISM,UNDER VOLTAGE COIL 1

2 AUXILLARY SWITCH(2NO,2NC) LIMIT SWITCH 2

3 VACUUM INTERRUPTER 2

MOTOR TERMINAL & COOLING FAN (for two years)

SL.NO DESCRIPTION QTY

1 MOTOR TERMINAL 100HP 2

2 40HP 1

3 10,15HP 10

4 3HP TO 10HP 15

5 MOTOR COOLING FAN (Up to 20 HP) 1

MCCB & ELMCBs (for three years)

SL.NO DESCRIPTION QTY

1 100A 3POLE MCCB 1

2 200A 3POLE MCCB 1

126

3 4POLE ELMCB 40 AMPS 30 mA 1

4 4POLE ELMCB 63 AMPS 100 mA 1

5 4POLE ELMCB 40 AMPS 100 mA 1

6 4POLE ELMCB 63 AMPS 300 mA 1

SWITCH DISCONNECTOR (for two years)

SL.NO DESCRIPTION QTY

1 32AMPS 3

2 63AMPS 1

3 125AMPS 1

4 250 AMPS 1

Enclosure-3

TENTATIVE LIST OF INSTRUMENTATION SPARES (per year)

SL NO DESCRIPTION MAKE &

MODEL NOSPECIFICATIO

NQTY

127

1 BATTERY 1.5V EVERADEY,DURACELL 1.5V,TYPE"AA" 20

2 BATTERY 9V EVERADEY,DURACELL 9 V BATTERY 10

3 EXTENSION BOARD REPUTED COMPANY

230VAC,5A,5FEET LENGTH 4

4 PANEL TUBE LIGHT,CHOKE CROMPTON

230VAC,2 FEET LENGTH 3

5 3 PIN PLUG, SOCKETS KUNDAN,ANCHOR

230 VAC,5A,10A RATINGS 10

6 TERMINAL BLOCKS REPUTED COMPANY

SUITABLE FOR 1.5 SQ.MM CABLE 300

7 MCB L&T,ANCHOR2A,5A,10A ETC. 15

8 CABLE FOR WIRINGKUNDAN,FINOLEX,V-GUARD

1.0 SQ.MM MULTISTRAND CABLE

100 MT

9 ELECTRICAL INSULATION TAPE

REPUTED COMPANY 50

10 6 MM PVC TUBE REPUTED COMPANY

100 M

1 UPS BATTERY (emergency spare)

EXIDE, AMARON 12V,42AH 5

2 POSITIONER FOR ILP VALVES

HTP POSITIONER,I.L.LTD, PALGHAT

INPUT:0.2 TO 1.0 BAR,SUPPLY 1.4 KSC,PORTS CONNECTION: 1/4 " NPT(F) 2

3 I/P FOR SAMSON VALVES MODEL:4765 AIR SUPPLY MAX;4BAR, INPUT:4 TO 20

2

128

MA,PORT SIZE:1/4" NPT(F)

4 RTD PROBE ALTOP   2

5 THERMOCOUPLE PROBE ALTOP 2DETAILS OF INSTRUMENTATION SPARES (For 2 years)

SL NO DESCRIPTION MAKE &

MODEL NO SPECIFICATION QTY

1 3/2 SOLENOID VALVE 24VDC,EX.PROOF

ROTEX: TYPE 30125-1.8-2R/ AVCON M45-1-RD/FLP-IIC/F

MEDIUM:AIR, PRESSURE: 10 BAR MAX,IN/OUT PORT SIZE: 1/4" (NPT)F.

2

23/2 SOLENOID VALVES 230 VAC ,FOR AIR COMP,DRYER

JANATICS: DS2 COMPACT VALVE

MEDIUM:AIR, PRESSURE: 10 BAR MAX,IN/OUT PORT SIZE: 1/4" (NPT)F.

2

3SOLENOID VALVES 230 VAC ,FOR CHILLER UNIT AND AHU

MKC-2, TYPE 180

230 VAC ,1/4 " SAE FLARE 2

4 OLD CHILLER LOAD/UNLOAD SOV

SPORLAN-MKG2, TYPE180

230 VAC, 15 WATTS 1

5 BLUE STAR CHILLER TEMP. SENSOR BLUE STAR

THERMISTER TEMPERATURE SENSORS.

2

6 PRESSURE SWITCH FOR LH2 PLANT

INDFOS: TYPE: B7-31-S

MEDIUM: NAPHTHA, N2,AIR ETC., PORT SIZE: 1/4"(NPT)F

2

7 PRESSURE SWITCH FOR INST AIR COMP.

SWITZER :GH902

MEDIUM:AIR,PRESSURE:10 BAR

2

129

MAX,INPUT PORT SIZE: 1/4" (NPT)F.

8ON/OFF PUSH BUSH BUTTON WITH LED LAMP 24VDC

BHARTIA CUTLER HAMMER:LED LSU 24VAC/DC

24V DC LED BULB. 5

9 INDICATION LAMPBHARTIA CUTLER HAMMER

24 V AC/DC LED INDICATOR

5

10 SMOKE DECTOR APOLLO/ EURO:ES-01

IONISATION, PHOTOELECTRIC TYPE SMOKE DETECTORS. OPERATING VOLTAGE: 17 TO 30 VOLTS.

4

11 FIRE ALARM PANEL BATTERY, 12VDC EXIDE BATTERY

12VOLTS 7.5 AH 2

12 MOTOROLA WALKIE-TALKIE BATTERY

HNN9008A-1332-AK47

7.2 V NICKEL METAL HYDRIDE BATTERY FOR MOTOROLA GP338 WALKIE TALKIE

2

13 I/P CONVERTOR BELLS BCE69F

INPUT:4 TO 20 MA,OUT PUT: 0.2 TO 1.0 BAR ,AIR SUPPLY :1.4 BAR

2

14 AIR FILTER REGULATORPLACKA: FPR-1/SHAVO NORGREN: 11-2 SN

MEDIUM: AIR, PRESSURE: 10 BAR MAX,IN/OUT PORT SIZE: 1/4" (NPT)F.

6

15 MTL BARRIERMTL 788R+,728,707+

SAFETY BARRIER 700 SERIES.

6

16 CONTROLLER EEPROM BELLS SOFTWARE 4

130

CONTROLSEEPROM FOR BMOS 6110 CONTROLLER

17 PRESSURE GAUGE WIKA: 232.50

DIAL SIZE:100MM, PROCESS CONNECTION:1/2"(NPT-F), LAMINATED SAFET GLASS.

15

18 TEMP. GAUGE WIKA : S 5550

BIMETAL THERMOMETER,PROCESS CONNECTION;G1/2 B.STEM DIA:6MM

10

19 ANN. BULBS 24VDC OMAX MAKEE10,PIN TYPE,24VDC

3 BOX

20 COOLING FANS FOR PANEL ebm NADI:

TYPE-4650Z

COOLING FAN 230VAC, 19WATTS.

4

21 COPPER/S.S.TUBE,FITTINGS AND FERRULES

REPUTED MANUFACTURER

6MM,12 MM SS TUBE.1/4 " ,3/8",1/2 ",6MM SS FITTINGS.

22FUSES 0.1A, 0.2A, 0.4A, 1A, 2A ETC.)

REPUTED MANUFACTURER

GLASS FUSES OF DIFFERENT RATINGS 0.1,0.2 1A,2A,4A,6A ETC.

23 SOLDERING IRON,LEAD AND FLUX

REPUTED MANUFACTU _

24 SIEMENS PLC LITHIUM BATTERY

TYPE-C ,LITHIUM BATTERY

3.6 VOLT LITHIUM BATTERY

1

25 PSA VALVES ACTUATOR DIAPHRAGMS

SAMSON ACTUATOR DIAPHRAGM FOR 240 CM2

AND 350 CM2

ACTUATOR DIAPHRAGM 240 AND 350 CM2

3

131

26 PRESSURE GAUGES CHILLER UNIT BLUE STAR

PROCESS CONNECTION 1/8 " (M) ,MEDIUM-FREON,SIZE-2"

8

Enclosure -4 IV TENTATIVE LIST OF SPARES FOR SAFETY SYSTEM

PERSONAL PROTECTIVE EQUIPMENTS (FOR 10 YEARS)

SL.NO DESCRIPTION For 1st

yearFor 9 years

QTY (NOS/SETS)

1 HELMETS 54 108 162

2 EAR MUFF 54 300 354

3 EAR MUFF 10 20 30

4 GOGGLES 54 100 154

132

5 FACE SHEILD HELMET

3 9 12

6 WELDING SHEILD 2 5 7

7 APRONS (CHEMICAL USE)

3 9 12

8 DUST MASK 50 180 230

9 BOILER SUIT 2 4 6

10 ASBESTOS GLOVES 10 36 46 SET

11 LEATHER GLOVES 4 36 40 SET

12 CRYO-APRAM GLOVES

2 4 6 SET

13 HOT GLOVES 2 4 6

14 SAFETY SHOES 54 216 270 SET

15 GUM BOOTS 2 4 6 SET

16 AIR PURIFYING RESPIRATORS (HEPA)(CARTRIDGE CHANGEIBLE TYPE)

3 3 6

17 CARTRIDGE (CHEMICAL)

- 27 27

18 BARRIGAURD 1 2 3 COILS

Enclosure-5

133

V TENTATIVE LIST OF PROCESS, MECHANICAL, INSTRUMENTATION AND ANALYTICAL LAB LOG BOOK

SL.NO DESCRIPTION NO.OF PAGES

NO.OF BOOK

1CONTROL ROOM LOG BOOK 200 10

2300/400 UNIT CONTROL ROOM 200 10

3300/400 UNIT FIELD 200 10

4100/200 UNIT CONTROL ROOM 200 10

5 100/200 UNIT FIELD 200 10

6DR COMPRESSOR CONTROL ROOM 200 10

7DR COMPRESSOR FIELD 200 10

8GH₂ HOFER COMPRESSOR CONTROL ROOM 200 10

9GH₂ HOFER COMPRESSOR FIELD 200 10

10GN₂ HOFER COMPRESSOR CONTROL ROOM 200 12

11GN₂ HOFER COMPRESSOR FIELD 200 12

12CHILLER PLANT I 200 12

13CHILLER PLANT II 200 7

14DM PLANT 200 12

15ETP 200 12

16TANKER READING 200 4

17ASU I 200 12

18ASU II CONTROL ROOM 200 12

19ASU II FIELD 200 12

134

20ASU II PRODUCTION 200 10

21GN₂ STRAT UP COMPRESSOR 200 10

22DPR 200 10

23BATCH PRODUCTION 200 4

24QUARTALY PRODUCTION REPORT 200 1

25DAILY MAINTENANCE REPORT 100 1

26MONTHLY MAINTENANCE REPORT 200 12

27ANNUAL MAINTENANCE REPORT 200 1

28MAINTENANCE REPORT 200 1

29MAINTENANCE NOTE BOOK 200 1

30SAFETY VALVE REPORT 200 5

31PLANT START UP CHECK LIST 200 8

32GH₂ HOFER START UP CHECK LIST 200 5

33LAB LOG BOOK 200 4

34LAB WATER ANALYSIS BOOK 200 8

35LAB ANALYSIS BOOK 200 5

36INSTRUMENTATION LOG BOOK 200 5

37INSTRUMENTATION REPORTS 200 7

38GN₂ HOFER START UP CHECK LIST 200 8

39LIN,LOX LH₂ TRANSPORT CHECK LIST 200 3

40PLANT WORK PERMIT 100 1

41SAFETY DAILY MONTHLY REPORT 100 6

135

42ASU II DPR 100 4

43BOX FILE - 30

44SMALL FILE - 30

45A4 PAPER - 12

ELECTRICAL LOG BOOK DETAILS

SL.NO DESCRIPTION NO.OF PAGES

NO.OF BOOK

1SUB STATION LOG BOOK 200 12

2SUB STATION READING 200 6

362.5 KVA DG READING LOG BOOK 200 12

4A/C PLANT READING 200 12

5MRS LOG BOOK 200 5

6MRS EB READING 200 5

7MRS DG I & II LOG BOOK 200 5

8200 KVA DG LOG BOOK 200 5

9SUB STATION MONTHLY 200 2

10TRANSFORMER MAINTENANCE QUARTELY 200 2

11TRANSFORMER MAINTENANCE HALFYEARLY 200 2

12CABLE MAINTENANCE 200 2

13EARTH BIT MAINTENANCE 200 2

14MOTOR MAINTENANCE YEARLY 200 2

15SWITCH GEAR MAINTENANCE 200 2

16PANEL MAINTENANCE 200 2

17DG MAINTENANCE 200 2

136

18LONG SIZE NOTE 100 10

Appendix-4

Tentative list of special equipments for which AMC shall be entered.

SL.NO Description Party Visit per Year

1 Centac Air Compressor- 1 No

Ingersoll rand (i) pvt ltd, Chennai

6 days over 4 visits

2 Dubas – 10 Kva UPS – 1 No Dubasengg, Bangalore

3

3A 62.5 kVA DG Set – Engine: Cummins

JN Machineries, Tirunelveli.

12

3B 62.5 kVA DG Set– Engine: Greaves

Gen services, Madurai

6

4 Overhead Cranes-5 nos Elmec Engg.pvt ltd, Nagercoil

2 visits per crane

5 Riello - 15 kVA UPS- 4 Units

Riello, Chennai 3 visits

6 A/C Plant –Make :Batliboi-3 units of each 15 tons

National coolers On call basis, approx 4 per

year

7 40 tons Chiller water Plant –Make: Accel

Bright Engineers, Tirunelveli

On call basis, approx 4 per

year

8 PLC Maintenance LH2 Plant, ASU I

Proficient automation and controls, Kochi

On call basis, approx2 per

year

137

9 Numeric - 10 Kva UPS- 3 Units

Numeric, Tirunelveli 3

10 ASU II,PSA Modicon PLC Sun automation,Chennai

On call basis, approx.2 per

year

Appendix-5

Tentative list of statutory fees to be paid by the bidder.

Sl.no Description

1 Boiler Inspection fee ( Every year) - Inspector of Boiler, Madurai

2 Naphtha Storage Tank ( 3 years) License from PESO, Chennai

3Pollution Control Board(Every year) -statutory fee, Water cess, ambient air quality survey etc except consent fee.

4

PESO Licenses ( 3 years) for LIN/LOX Storage Tank-2 Nos

LIN/LOX Tankers – 3 Nos

Other Tank/Tankers as applicable.

5 Naphtha Purchase License (2 years) – District Collector, Tirunelveli

138

Appendix-6

Tentative list of maintenance services which can be availed from outside parties to be procured and supplied by the bidder.

Sl.No

Maintenance Service Unit Qty per year Remarks

1 Motor Rewinding NOS Upto 3.7 KW – 5 nos

Different Motors of capacity up to 75 KW

3.7 to 30 KW – 5 nos

31 to 75 KW one in 5 year

2 Grass Cutting m2 15,000 Grass cutting in and around the plant area is to

139

be carried out as and when it grows.

3 Painting charges [excluding supply of paint]

a) Pipe line m2

1,200

Pipeline, structures and buildings are to be painted once in two years. Tankers are to be painted every year.

b) Plant Equipments, Tank, Vessels, Structures etc

m2

8,500

c) Tankers with prime movers.(Letter writing included as 50 m2per tanker)

m2 3,116

d) Masonry wall and roof

m2 12,000 m2

4 Cleaning ETP solar pit m3 450 Removal of effluent from the evaporator pit and storing in safe place.

5 Overhauling& reconditioning charges of 62.5 km DG set

No 2 nos (once in 5000 hrs)

DG sets are to be overhauled once in 5000 hrs. It is once in 4 years based on current operation mode.

6 a Welding Inch dia 200

6b TPI charges Per day 3

6c Radiography charges Per day 6

6d Heat treatment charges Per day 6

140

6e Mobilization charges for welding , Radiography and Heat treatment if arranged from out station,

Per visit 3

7

7A

Servicing / calibration of Instruments/ controller

BMOS BDE6110 Controller, BDE 4300 indicator servicing

Nos 3 (To be serviced at Bluebells controls, Chennai)

7B

Test equipments calibration – buden berg pressure calibrator, nagman make pressure calibrator, yew make current/voltage source, decade resistance box and digital multimeter

Nos 4

To be serviced at ERTL, Trivandrum, North lab (I) Pvt Ltd, Chennai

7C 24 volt power supply units and siemens plc power supply servicing

Nos5

To be serviced at APLAB, Trivandrum, Krishna Electronics, Chennai

8

Renewal of Reformer Tube including welding& radiography

Package

Once in 5 years

Engaging 40 tonnes, 50 m boom length crane for a day, cutting &dismantling old reformer tube, installation of new reformer tube welding & Radiography with BVQI Inspection. In order to take out the Reformer

141

tube – 3 nos, asbestos roof is to be removed and put back.

9 a] Metal spray and Dynamic Balancing of Turbine impeller and shaft

No 1 (Once in a year)

Re build up of shaft/ Impeller by metal spray technique and dynamic balancing. b] Metal spray

and Dynamic Balancing of Impellers and shaft of centrifugal compressors

No

3 (Once in three years)

10 Fabrication cost a) Lathe works

Machine hours

250 ( rough)Fabrication of components and adaptors as and when required.50 (finishing)

b) Milling works 100

c) Drilling works 100

11 Insulation Including Materials and providing Vapour barrier (for 2years).

a) Foam m2 10

b) Glasswool m2 20

a) Thermocoal m2 10

12 Fire extinguisher testing & refilling charges

No Dry chemical powder

2 kg – 6

4 Kg – 9

10 kg - 11

142

Co2

2 kg – 4

4.5 kg- 4

22.5 kg- 1

13 NDT services

a) Measurement of Thickness of pipe line vessels

No of points

5000

b) Radiography Inch dia +

Mobilization

100

c) Other NDT services like etching &taking replica Inch dia

+ Mobiliza

tion25

14 Scaffolding works for servicing of equipment & vessel

m3 40

15 Industrial cleaning of equipments, vessels, Tank, Tankersetc and touching up of paint if required

Frame volume in m3

680 Removal of oil spillage and other waste, Cleaning by wiping of surfaces, mobbing with solvent/cleaning agent, water washing if applicable

143

Appendix - 7

Tentative list of chemicals, oil & other consumables to be procured and supplied by the bidder.

144

145

List of Chemicals

List of Oil List of Consumables

HCLNaOHN2H4

(Hydrazine)H2 SO4

GE Chemicals:

BL 5323BD 1500MS 6209AZ 8104NX 1100NX 1104

HYPO

ASU Compressor (SS 32)Naphtha and BFW Pump (SS 32)ASU Turbine (SS 46)Recycle Compressor (SS 46)Cooling Water Pump and Cooling Tower fan (SS 100)Inst. Air Compressor (SS 68)Vacuum Pump (SS 100)H2 Compressor (SS 100)Fire Water Engine (Pride 40)62.5 KVA DG set-1 (Premium Blue)62.5 KVA DG set-2 (Greaves Maxtherm)A/c Compressor-1 (Seetal 50)

A/c Compressor-2 (Freezol)

Turbine ASU II ( Servo prime 46

LP)

CP 11/CP12 oil( Servo prime 46)

DR compressor oil(Servo 220)

N2 Hofer compressor oil (Servo

68)

Start up N2 compressor -SS 100

Teflon sealsGreaseCotton WasteAdhesivesGasketsRefrigerants (A/C & Chiller plant)Servogem 2 grease

CHAPTER-III

FACILITY DETAILS

CONTENTS

Article – 1 Naphtha transportation systemArticle – 2 Naphtha Transfer SystemArticle – 3 Naphtha Storage SystemArticle – 4 Naphtha Feed SystemArticle – 5 Steam Reforming UnitArticle – 6 PSA UnitArticle – 7 Process Water Storage SystemArticle – 8 Process Water Feed SystemArticle – 9 Hydrogen Compressor SystemArticle – 10 Hydrogen Cold BoxArticle – 11 Valve BoxArticle – 12 Hydrogen Receiving StationArticle – 13 Hydrogen Storage Cum Transport TankersArticle – 14 Air Separation UnitArticle – 15 Liquid Oxygen StorageArticle – 16 Liquid Nitrogen StorageArticle – 17 Main Receiving Station.Article – 18 LIN Transfer SystemArticle – 19 LOX and LIN Transportation TankersArticle – 20 Instrument Air CompressorArticle – 21 DM Water PlantArticle – 22 Cooling Water SystemArticle – 23 Captive Power PlantArticle – 24 Analytical LabArticle – 25 Sub StationArticle – 26 Central Control RoomArticle – 27 Effluent Treatment PlantArticle – 28 Water Supply systemArticle – 29 Power Supply System

146

Article – 30 Fire Hydrant and Fire Fighting SystemArticle – 31 Communication FacilitiesArticle – 32 62.5KV DG Set Power Supply SystemArticle – 33 25m³ Cooling Water SystemArticle – 34 ASU Chiller Water PlantArticle – 35 LHPSArticle – 36 ASU IIArticle – 37 Dresser rand Hydrogen compressor (Primary & Booster) Article – 38 High Pressure GH2 Hofer compressor systemArticle – 39 High Pressure GN2 Hofer compressor systemArticle – 40 N2 Start up compressor-systemArticle – 41 125 KL LH2 storage Tank System Article – 42 40 KL Air Liquide LH2 Trailer 170037,170038 (2Nos)Article – 43 40 KL LHe/LH2 Trailer 630306 Article – 44 75 KL INOX LIN Storage TankArticle – 45 75 KL INOX LOX Storage TankArticle – 46 10 KL LIN/LOX Transportation TankersArticle – 47 10KW HeaterArticle – 48 LH2 Pumping System.Article – 49 Yard Piping.

Note: The documents referred in this chapter and listed in Annexure-2 of Chapter-I will be handed over.

ARTICLE -1: NAPHTHA TRANSPORTATION SYSTEM (NTS)Gaseous Hydrogen required for the production of liquid Hydrogen is manufactured using naphtha feed stock. Naphtha is supplied by M/S. Indian Oil Corporation in IOCL charted Tanker to the ILHP site. The storage facility for naphtha at IOCL at Narimanam has the necessary provision for road tanker loading.

ARTICLE- 2: NAPHTHA TRANSFER SYSTEM

147

The naphtha transported in the tanker is transferred into a storage tank located within the safety zone using pump transfer system. The transfer system consists of two centrifugal pumps and the related pipe lines. At a time only one pump will be in operation while the other will be on standby. To ensure the smooth operation and changeover of one pump to the other, necessary valves and fittings are provided. The major items included are:

- A flexible hose of length 3 m and size 2” NB with end connection, one end flanged to tanker and other end threaded (3” BSP)

- A reducer- Check valves- A filters- Suction valves- Centrifugal pumps with motors- Pressure gauges with isolation valves

Details of the system and operations are described in Doc.No.ILHP/100/92/01

ARTICLE -3: NAPHTHA STORAGE SYSTEMNaphtha transported from Narimanam is transferred in to a 60,000 lit capacity storage tank. The transfer line mentioned in Article-2 connects the tanker to the storage tank through a pump. Storage tank has the necessary level reaches high value, the globe valve in the transfer line gets closed by an electrical signal from the level switch. If the level goes below the lower set point then the operator will get a alarm in the control room. Details are available in Doc. Operating Manual, Unit 100/200. Volume 3, file 1. ARTICLE -4: NAPHTHA FEED SYSTEM

The liquid Naphtha which is used as feed and fuel in the reformer plant is stored in the Naphtha storage tank. Naphtha vapour generated in the tank due to heat input from the atmosphere is fed in to the condenser where the vapour are condensed and liquefied. Thus the loss of naphtha due to atmospheric heating is maintained at an absolute minimum level. The naphtha is pumped from the tank to a pressure of 1960 kpa (g) and the liquid naphtha enters the evaporator where the evaporation process occurs. The heat required for the evaporation is supplied by the hot process

148

gas leaving the reformer. During the start up period, required quantity of heat is supplied by an electrical heater. Naphtha leaving from the evaporator is divided into streams; the smaller stream is fed to the reformer furnace and used as fuel while the other stream is the main feed for H2 production. The feed gas is mixed with recycle hydrogen from the compressor. Sulphur carried in the naphtha is hydrogenated in the desulphurization reactor and hydrogen sulphide is removed in adsorber bed. The sulphur free Naphtha vapor gets heated up in exchanger and enters the reformer tubes. Full Details are narrated in Document – Operating Manual Unit 100/200, Vol.3,File 1.

ARTICLE -5: STEAM REFORMING UNIT

The feed free from sulphur in a desulphurization unit is then mixed with process steam generated in the flue gas boiler. The mixture is superheated in the feed super heater and fed into the reformer. The pre-heated mixture of naphtha and steam is distributed evenly into the three reformer tubes via flexible pigtails and reforming of feed steam mixture takes place in the heated high-alloy reformer tubes.The reformer tubes are filled with Nickel based catalyst. The burner assembly consists of a vertical firing induced draft burner complete with wind box, quarl, burner head, manual air damper, igniter location tube, viewing port and flame scanner connections. Flue gas fan is located near the flue gas stack maintaining a negative pressure inside the reformer furnace. The pressure difference between the combustion chamber and the atmosphere gives the necessary driving force for the flow of air in to the combustion chamber. The air passes through the manually adjustable air damper at the back of the wind box and the through the burner head, which is located within the wall of the combustion chamber, before entering the combustion zone. During start up Hydrogen gas stored in a 4x1 m³ cylinder skid is fed into the reformer unit. The cylinder skid is mounted on foundation surrounded by dyke wall and provided with necessary valves, regulator, pipe lines, instruments and fittings. Details of the unit are described in Document – Operating Manual Unit 100/200 Vol.3, File 1.

ARTICLE -6: PSA UNIT

149

The hydrogen purification is carried out in a Pressure Swing Adsorption (PSA) Unit. The PSA unit of four adsorbers, which are filled with activated alumina, activated carbon, and molecular sieve. While one adsorber is under process mode, the other three adsorbers will be under depressurization, purging and pressurization mode respectively. The purge gas from the PSA unit is fed into a buffer vessel. This purge gas is returned to the reformer furnace and used as fuel. Details are available in Document. - Operating Manual. Unit 100/200. Vol.3, File1

ARTICLE -7: PROCESS WATER STORAGE SYSTEM

The de mineralized water for the process is collected in a storage tank of 10 m³ capacity. In order to avoid any contamination of the DM water especially due to corrosion of the container, the storage tank is fabricated out of SS304. Also there will be a nitrogen blanket to prevent oxygen getting dissolved in the DM water. The tank is provided with safety valves, pressure gauges, regulators etc. the 2 meter in diameter and with a height of 3.2 meter is designed and fabricated as per ASME Sec Div.I. Details of the system are mentioned in Document. No ILHP/100/92/01

ARTICLE -8: PROCESS WATER FEED SYSTEM

The water from the tank is pumped using a boiler feed water pump and suction side is connected to the BFW tank. The hydrazine required for the elimination of dissolved oxygen is stored in a drum and pumped into the BFW tank using a dozing pump. The boiler feed water is preheated in an economizer before being supplied to boiler. The boiler is equipped with level controller and the flow of BFW to the boiler is regulated by the level controller. The process steam is added to the reformer feed stock at upstream of the feed super heater, while the vent steam is sent to the atmosphere through a silencer. A continuous boiler blow-down is provided to maintain the BFW quality in the boiler system. The blow-down water is directly cooled with cooling water in the blow-down drum and then released to the sewer system. All inflammable gases are collected in common vent header and routed to the vent stock. Details are described in Doc.-Operating Manual, Unit 100/200, Vol 3, File1.

ARTICLE -9: HYDROGEN COMPRESSOR SYSTEM

150

The hydrogen liquefaction is realized by a high pressure Joule Thomson process with vacuum nitrogen pre-cooling. The five stage compressor raises the pressure upto 120 bar (abs). This compressor is designed to circulate 1240 Nm3/hr, of gas in a closed cycle. The liquid hydrogen production rate is equivalent to the feed steam from PSA unit. The major portion of the feed to the compressor suction comes from the liquefier as return cold gas. The feed from PSA enters the compressor only after the second stage. Details are described in Document- Operating Manual, unit 300/400 vol.3, File 2-2

ARTICLE -10: HYDROGEN COLD BOX

The high pressure gas from the compressor passes through a filter and it is splitted into streams before entering the cold box. Both the streams are cooled in the two heat exchanger housed inside the cold box against the return cold box against the return cold vacuum nitrogen gas and low pressure hydrogen gas. Then the streams are recombined and pass through the guard absorbers to remove trace of impurities, if any. The next stage is vacuum nitrogen bath where pre cooling as well as ortho-para conversion take place (first phase). H2 gas is then cooled to in heat exchangers against the cold return H2 gas and the stream is once again split into two. The larger part (approx.12.5 mol/s) is throttled to approx. 20kpa (g) and gets liquefied. The LH2 bath vessel receives the liquid hydrogen. The smaller part (approx.2.9 mol/s) is throttled to approx. 900kpa (g), and after passing through the final ortho Para convertor, exchange the heat in LH2 bath vessel bringing down the temperature to 21.4k.Details are explained in Document–Operating manual, Unit 300/400.3, File 1.

ARTICLE -11: VALVE BOX

In the valve box, the stream coming through LH2 bath down to a pressure of 40kpa (g) and the liquid is fed into the LH2 storage cum transport tankers by means of special flexible hoses meant for H2 application. The valve box will terminate with two discharge coupling ends for drain and two other ports for the return cold vapours. Details are narrated in Document. - Manual, Unit 300/400, File 1.

ARTICLE -12 HYDROGEN RECEVING STATION

151

The liquid hydrogen produced in the plant is drawn in to the LH2 transport tankers parked near to the valve box. Form the valve box LH2 is drained to the tanker using the flexible hose. The cold vapors from the tanker are taken back to the liquefier. In the receiving station, two tankers can be parked at a time and can be filled one after the other without delay as two outlet points are available from valve box. There are totally three LH2 storage cum transport tankers available each mounted on the gooseneck flat bed trailer connected to hippo haulage. A deluge system is provided in the receiving station.

ARTICLE -13: HYDROGEN STORAGE CUM TRANSPORT TANKERS

The liquid hydrogen in the cold box of the liquefier unit is drained through a valve box system to 11,000 gallon vacuum insulated LN2 shielded tanker. There are two tankers planned to park in the loading station and these tankers are meant for storage tank as well as for transport of liquid hydrogen. This dewar is cylindrical in shape and housed in a standard 8’ wide x 8½’ high x 40’ long inter model frame. These tankers are mounted by Mahindra make trailer and will be hauled by Ashok Leyland Hippo vehicle. There are three units complete with tankers, trailer and prime mover. The detailed specification and the relevant drawing for the tanker units are given in Doc.-Operating Manual,Unit 300/400, volume 3, File 2.1.1. Along with the details of the chassis and prime movers.

ARTICLE -14 AIR SEPARATION UNIT

In this system, Dust free air is compressed in a 3 stage turbo compressor to a pressure of 9.8 bar and purified in a molecular sieve unit. The molecular unit consists of two absorber, so that the regeneration can be done parallel. The purified air goes to a main heat exchanger in a cold box where it splits into two. The major stream is expanded in an expansion turbine which supplying the refrigeration. The smaller stream which is cooled by means of the refrigeration produced in the expander is fed to the dual pressure column distillation unit. In this unit major constituent of air namely Nitrogen and Oxygen get separated. The liquid oxygen is drawn from the bottom of upper column (low pressure column) and filled in a LOX storage tank. The liquid nitrogen is drawn from the outlet of a condenser immersed in a LOX located at re boiler part of the distillation unit. (High pressure column).

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The system consists the following sub system

Air filter for dust removal Air compressor -3 stage dry running turbo compressor with inter coolers after

coolers, separators, instrumentation, gear unit, oil system emergency shutdown switch and local panel and HV motor.

Pre cooling system which one evaporation cooler. Two cooling water pumps, chilled water cooler (Tube and shell type), water separator with level indicator.

Molecular sieve adsorber with Twin adsorber vessel, two electric heater insulated (Installed Power -70 KW, power requirement – 16KW), silencer for outgoing regeneration gas of the adsorber and instrument air filter. The switching over after regeneration period is done automatically by the PLC.

Control panel – the automatic microprocessor based control system is installed in a cabinet, located near to the cold box. A programmable logic controller (S TYPE PLC) is the main item of this cabinet. The PLC is manufactured by SIEMENS.

Automatic analyzers – one for the purpose of Nitrogen product with a range of 0 – 10/100/1000 vppm Oxygen, one for Oxygen product purity range of 99-100 % Oxygen and one for Oxygen content (0-100%).

Manually operated analyzer and for determination of water vapour content with drager tube.

Cold box – All cryogenic equipments are housed in a self supporting carbon steel container. The box is constantly purged with residual gas so as to maintain a slightly positive pressure which prevents the increase of moisture cold box which comprises of main heat exchanger (fin type), Rectification columns, condenser/reboiler, Expansion turbine, Interconnecting piping, cryo valves and control equipment.

oil unit consists of oil vessel, oil pump with motor, oil cooler, oil filter, oil separator and Lubrication vessel.

Details of this system is elaborated in Operating Manual Unit 500, Vol.3, File 1.

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ARTICLE – 15 LIQUID OXYGEN STORAGE

The liquid oxygen produced in the distillation unit of ASU is filled in the 26 m³ LOX storage tank located near the cold box. This tank is a double wall vacuum insulated tank and is equipped with control devices and measuring instruments for fully automatic operation. There is a top filling and bottom discharge line for the filling/ transfer purpose. A pressurization coil is provided for pressure build up in the tank. The liquid level is measured by a differential pressure gauge with necessary additional provision for connecting a transmitter and to measure the pressure in the tank, a pressure gauge is provided. The inner vessel has two safety valves. The vessel is designed according to the pressure vessel code,

ARTICLE -16: LIQUID NITROGEN STORAGE

The liquid nitrogen produced in the distillation unit of ASU in the 43 m³ LIN storage tank located adjacent to the cold box. This tank is a vacuum insulated double wall vessel and is equipped with control devices and measuring instruments for automatic operation. There is a top filling and bottom discharge line for the filling/ transfer purpose. A pressurization coil is provided for pressure build up in the tank. The liquid level is measured by a differential pressure gauge with additional connection for transmitter and the tank pressure is measured using a pressure gauge. The inner vessel has two safety valves. The vessel is designed according to the pressure vessel code.

ARTICLE -17: MAIN RECEIVING STATION

Main Receiving Station is located near IPRC main gate. It receives 11 KV power supply from 110 KV substation at IPRC and distribute to IPRC facilities. It has 2 nos of 1000 KVA HT DG sets and 1 no of 200KVA DG set with required distribution panels, change over panel, synchronization control & breakers. It distributes both LT & HT power supply to ILHP plant & other facilities at IPRC as given in Article 29.

ARTLCLE -18: LIN TRANSFER SYSTEM

The liquid Nitrogen from storage tank is transferred to LIN transport tanker by pressurizing the LIN storage tank. This is made possible with the help of a

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pressurization coil provided in the tank. The transfer line includes SS pipe linefrom LIN tank discharge coupling and flexible hose to connect the LIN transport tanker.

ARTICLE –19: LOX AND LIN TRANSPORTATION TANKERS

There are three numbers of transportation tankers of capacity 13,000 liters each and two transportation tankers of capacity 6,000 liters each for transporting LOX/LIN. All the tankers vacuum insulated. The 13,000 lit. Tankers are mounted on semi trailer and the free end will be connected to prime mover by means of fifth wheel coupling. The smallest tankers are in built one standard chassis with prime mover. The prime mover is provided with driver’s cabin. The details of the tankers are given in Doc.No.ILHP/500/92/02

ARTICLE -20: INSTRUMENT AIR COMPRESSOR

The compressor is to meet the instrument air required for the operation of the various pneumatic valves/solenoid valves. The system is having mainly two air compressor, two air drier units, and an air receiver. At the downstream line of air receiver, dome loaded/spring loaded pressure regulators are provided to keep a constant command pressure. The piping components include non-return valves, filters, globe valve, reducer, ball valves and pressure gauges. One of the compressors will be running while the other will be standby. Details of the system are designed in Doc.No.ILHP/100/92/02

ARTICLE -21: DM WATER PLANT

The DM water plant produce boiler feed water as well as cooling water (makeup). The quality of boiler feed water is much stringent and hence requires a mixed bed deionizer whereas for cooling water. pH should be less than of BFW. Hence from the two bed ionizer the cooling water make up is sent to a cation polisher instead of a mixed bed unit to bring the PH value to 7.6 and fed to the cooling water make up storage tank. To meet the requirement of boiler feed water at the rate of 1.0 m³/hr and cooling water at the rate of 5m³/hr, the plant is designed with a capacity of 144 m³ per day. The maximum number of regeneration/day is two and regeneration time will be approximately 3 hours for both the mixed and two bed units. The plant

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could produce approx.100 m³ DM water in 18 hours. At the outlet of mixed bed unit, an online conductivity meter with an alarm is introduced to monitor continuously the conductivity. Whenever conductivity goes up, there will be an alarm in the control room. At the same time signal from conductivity meter will ensure the shut off the delivery valve to storage and open the bye pass to drain. Similarly whenever level in the BFW storage tank goes up, there will be an alarm at the control room and at the same time shut off the delivery valve and the bye pass valve will get opened to drain. DM water plant requires inlet pressure of 4.5 bar (g) maximum. Details of the system are in Doc.No.ILHP/100/92/03. The raw water analysis is given I Annexure – 2.1. The boiler feed water quality is given in Annexure – 2.2. The specification for the cooling water make up is given in Annexure -2.3

ARTICLE 22: COOLING WATER SYSTEM

The system is designed to handle 160 m³ /hr. Demineralised water is used for cooling water system and this water is taken from DM plant. Water at the rate of 5m³/hr is taken from the plant. There are three cooling towers connected to water circulation pump through a sump. A stand by pump is also included. Cooled water from the sump is taken to the pump through suction pipes. Hot returning from individual equipments is collected in a header and sent to all the towers. Water is sprayed through nozzles and sent to all the towers. Water is sprayed through nozzles and sent through atmospheric air draft. Water collected in the sump is taken for further circulation. Pressure and temperature are measured at inlet and exit points. The above details are described in Doc.ILHP/100/92/04

ARTICLE - 23: CAPTIVE POWER PLANT

The facility includes a DG set of 1250 KVA, 0.8 P.F. located near substation building. This Unit restores power supply within 500 milliseconds once the main power supply fails. The major units are

a) Diesel engine – supercharged, water cooled engine suitable for generating required power at 1500 rpm. Basic power is 1730 HP. The engine includes fuel–pump injectors, speed regulators, oil filters/ coolers, air filters etc. safety

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features like engine oil pressure switch, over speed detectors, fuel pressure switch etc. are provided in the system.

b) Instrument on engine board – Tachometer oil pressure gauge, diesel level indicators, water temp, gauge etc.

c) Engine water cooling devicesd) Engine preheating devices, pre lubricating devicese) Alternator

Rating: 415 V, 3 phase, 50Hzn, 1000KW, 1250KVA, 0.8 p.f. 1500rpm. Insulation F, protection IP 21

f) Accessories - Exhaust silencers with flanges - Anti vibration dampers - Lead acid battery for starting - Fuel tank, 990 lit capacity - Fuel cooler - Maintenance tools

g) Automatic electric control and monitoring cabineth) Power distribution paneli) Cooling towerj) General – raw water pumps, control cables, power cables, exhaust pipe, earthing station/ connectionk) Necessary spares for the DG set.l) The details are described in Doc.ILHP/100/92/05

ARTICLE -24: ANALYTICAL LABAnalytical lab consists of:

- Custom built gas chromatograph fitted with thermal conductivity detector with a sensitivity of 1 ppm for trace gases, gas sampling and column switching valves, silica jel and molecular sieve column connected in series for LH2 analysis.- Custom built gas gas chromatograph fitted with thermal conductivity detector With a sensitivity of 1 ppm for trace gases, flame ionization detector with a sensitivity of

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0.02 ppm for hydrocarbons. Mechanizer gas sampling, switching valves and appropriate columns for LOX and LN2 analysis.

- Data station to handle both the aforesaid gas chromatographs comprising interface, software and indigenous PC with printer.- Spares and accessories for the aforesaid systems.- Trace oxygen analyzer (Electro chemical type)-Percentage level oxygen analyzer

o Trace level Oxygen analyzer(Electrolytic type)(ppb sensitivity)

o Trace level moisture analyzer(ppm sensitivity)(Electrolytic type)

o Calibration gas standardso GC accessories

(Gas sampling bottles)(Syringes etc)

- C/H analyzer (To analyze C/H ratio naphtha)- Sulphur content analyzer- Chloride, dissolved oxygen analyzer (To analyze chloride and dissolved oxygen in boiler feed water and cooling water)- Atomic Absorption spectrometer to analyze heavy metals in naphtha and hardness in boiler feed cooling water -UV/ visible spectrometer- O-P content analyzer-RVP apparatus to analyze RVP in Naphtha -conductivity meter to analyze -pH meter to measure pH of cooling water- Nephelometer to measure turbidity of cooling water -Hot plate with magnetic stirrer -Heating mantle-Water baths 2 nos.

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-Hot plate 2 nos.-Stainless steel sampling cylinders for withdrawing samples-4 nos.-Hot air oven -Electronic analytical balance (200 gm. Capacity)-Electronic top loading balance (2kg. capacity)-Glass wares -Lab work benches and minor equipments

ARTICLE-25: SUB STATION The area substation for the power supply includes two transformers and the necessary control panels with U.P.S back up for control circuits. All the motor control panels for utilities are kept inside the substation. The major units at substation includes. - HT Panel consisting 6 nos of VCB

(One for incomer feeder 1 and one for incomer feeder 2, one each for ASUs (2nos), Transformers(2nos))

- LT distribution panels (motors and lighting)- Changeover panels- UPS panels (master, salve and static voltage regulator)- Chargers (float and boost) for control volt batteries - Heat tracer distribution panel - Heater control panel - Control voltage Batteries - U.P.S Batteries.The details are described in Document No. ILHP/100/92/06

ARTICLE -26: CENTRAL CONTROL ROOM

The central control room is air conditioned and provide with false flooring. All major process parameters are monitored and controlled in the control room. Two CCTVSs are provided to cover the important areas like LOX transfer area, LH2 filling area, reformer top etc. An alarm annunciator system is provided in the control room as well as in the fire station with hooter sound. The instrumentation system at ILHP caters to unit 100 (GH2 production), unit 200 (GH2 purification), unit 300 (H2

liquefaction), unit 400 (Storage of LH2, LIN, LOX) and unit 500 (Air separation unit)

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for the production of LOX and LIN. central control room at ILHP consists of six control panels equipped with BMOS controllers, indicators, auto manual stations alarm annunciator and panel mate plus. All inputs and outputs to and from field are marshelled through a barrier rack containing an array of input and output barriers and signal convertors for thermocouple /RTD inputs in the field. In another two panels two places two PLCs (Siemens PLC model NO. S5-135U and MODICON PLC model No.968 – 640) are installed. Siemens PLC is used to control the system of unit 100,300 and 400. Modicon PLC is used to control the system of unit 200. Auxiliary analog output from controller and digital output from ON/OFF manual switch are fed to Siemens PLC/MODICON PLC which in turn gives alarm, ON/OFF command and trip signals. A separate Siemens PLC (S5-153U) is installed in ASU control room to control the process of unit 500. Production level of LOX and LIN as well as the status of the plant are provided in the central control room. The details of important instruments used in ILHP are indicated briefly in the respective Doc of the individual sub system and in the following Documents.

- User manual – Measurement rack -1(No. LPSC/LMF/IDA/TR/356/93)- User manual – command rack – 2 & 2A(No. LPSC/LMF/IDA/TR/377/93)- User manual – safety rack – 3(No. LPSC/LMF/IDA/TR/392/94) - User manual - Alarm annunciator(No. LPSC/LMF/IDA/TR/401/94)- user manual – Alarm annunciator rack at fire station(No. LPSC/LMF/IDA/TR/398/94)-User manual Auxiliary system (No.LPSC/LMF/IDA/TR/397/94)- General description of Instrumentation system for supporting facilities (No.LPSC/LMF/IDA/TR/420/94)

ARTICLE -27: EFFLUENT TREATMENT PLANT

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During the plant operation the effluents generated and subjected to proper treatment before being disposed. To treat the liquid effluents a dedicated unit is established along with ILHP. The various liquid effluents obtained are classified in to our categories namely.Acidic effluentWash waterSteam reformer effluent Oil effluent The specification and treatment procedures are described in Document No. ILHP/600/92/01

ARTICLE – 28: WATER SUPPLY SYSTEM

The water supply to ILHP is from bore wells. In the utilities building, there is a 25m3

capacity sump for domestic water, 150m3 capacity sump for process water and a 700m3 storage for fire water.

ARTICLE – 29: POWER SUPPLY SYSTEM

Power supply was tapped from 110 KV double circuit line of TNEB (Arumuganeri- SR Pudur feeder) passing through IPRC campus and fed into 110/11KV EHV substation of IPRC where 110 KV supply was stepped down to 11 KV supply. From 110 KV substation to MRS two dedicated feeders (11 KV underground cables) were provided for further distribution i.e one for IPRC facilities and other one exclusively for ILHP. From MRS to ILHP substation, one main and standby feeders (11 KV underground cable) were provided for drawing power from MRS to substation- ILHP. 11 KV power further distributed to ASU motors and also stepped down for further distribution of LT loads.

ARTICLE -30: FIRE HYDRANT AND FIRE FIGHTING SYSTEM

Necessary fire product system is installed at ILHP.This includes- First aid and fire extinguishers- Fire hydrant system

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- Deluge and sprinkler system- Fire detection system- Smoke detection system- Manual fire call points- Camp fire station- Fire action boardsThere is a fire water storage of 700m3 capacity available at the utilities area at ILHP. There are 19 fire hydrant points (250 gpm, 63mm outlet) provided at various important areas. Fire at the following area will be controlled with automatic deluge/sprinkler system and using hose line from fire hydrants and fire tender if necessary.- LH2 filling area- LH2 taker parking shed- LOX and LIN filling area- Storage tanks for LOX and LINFire in the control room and substation will be detected by automatic smoke detector system. In addition to built fire fighting system a dedicated fire tender is also provided. Details are available in Doc. No. ILHP/800/92/02.

ARTICLE -31: COMMUNICATION FACILITIES:

The control is connected to various locations of the plant by means of public address system. Telephones are provided at the following places.- SECUIRITY BUILDING- SITE OFFICE- CENTREL CONTROL ROOM- ASU CONTROL ROOM- SUB STATION- SERVICE BUILDING- ETP- ANALYTICAL LAB Two sets of walk-talkies are provided in the control room for communication between other points at site.

ARTICLE -32: 62.5 KVA DG SET POWER SUPPLY SYSTEM

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In order to maintain un interrupted power supply to the critical loads of unit 100/200, this power supply system is introduced.The system consists of 2 Nos. of 62.5KVA DG set, accessories and related power panels and switches. During operation 1 set will be in line and other will be available as stand by. The critical loads of unit 100/200 like reformer Blower Boiler feed water pumps etc are connected to this DG set supply and un-interrupted power supply during entire period of operation of the plant is ensured. Since these loads are running continuously on DG set supply, the power interruption in EB power supply is not affecting the operation of critical loads. The details are available in 62.5 KVA DG set manuals.

ARTICLE –33: 25 m³ COOLING WATER SYSTEM

The cooling water system is designed to handle 25m³ /hr, of cooling water exclusively to meet the requirements of unit 100/200. This system consists of 25m³ centrifugal pumps, suction filters, swing check valves, pressure gauges, Isolation valves and necessary piping connecting the sump to the header at Battery limit of the plant. During operation one set of pump and valves & fitting will be in line and other set will be a standby. This cooling water is supplied to syn gas cooler syn gas and to Naphtha condenser for cooling naphtha and returns to the cooling towers. The details are given in 25 m3 cooling water pump manuals.

ARTICLE – 34: ASU CHILLER WATER PLANT

The chiller water plant in ASU is in corporate to attain lower inlet temperature at the inlet of molecular sieve unit for better adsorption of impurities. The system consists of compressor, Brine pumps, Cooling water pumps, Heat exchanger and related accessories and power/ operation panels & controls. The systems have two circuits namely Brine circuit and Freon (Refrigerant) circuit. Compressor, expansion device, Heat exchanger and accessories form the Freon circuit and produce the refrigerant effect and cool the Brine water. Brine pumps, Heat exchanger and accessories forms the Brine circuit which circulates the Brine water through the process air Heat exchanger. There is a cooling water system with pumps, cooling

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towers and accessories for cooling the compressor and Freon circuit. The details are given in chiller water plant manuals.

ARTICLE – 35: LHPS

Liquid Hydrogen Purification plant (LHPS) is supplied by GK to purify LH2 from ILHP to the specification of GK requirement and the system is installed at ILHP.The purification is carried out using Liquid Phase Adsorber filled with silica get providing the sorption of micro impurities from Liquid Hydrogen and purification of LH2 from fine dispersed solid phase of impurities. The O-P reactor converts ortho hydrogen in to para hydrogen. To prevent the formation of para phase in the Adsorber a heat exchanger sub-cooler is incorporated in the purification circuit. A part of liquid purified hydrogen boils in the heat exchanger sub- cooler at 1.15bar (g) LH2from ILHP under pressure at 2.4bar (a) and at a temperature of 23.7K enters at purification unit 62A10. The LH2 enters heat exchanger sub cooler 62A01 where it is cooled to a temperature of 21.5K at the expense of boiling of about 10% of purified Liquid Hydrogen at pressure of 1.15bar(a)Sub cooler LH2 is purified from impurities in Adsorber 62A03 and converted from ortho hydrogen into para hydrogen in O-P reactor 62A04 (from 95% to 98% of para from). In this case, it is heated to a temperature of 23K, cleaned from possible mechanical impurities in filter 62F01 and filled from the purification unit in to the filling trucks.The LH2 purified in LHPS is constantly analyzed by on-line gas chromatograph at the analytical lab. The details are given in the set of LHPS Documents.

ARTICLE – 36: AIR SEPARATION UNIT II

1.1 PROCESS & BRIEF TECHNICAL DESCRIPTION OF THE EQUIPMENTS

Dry air from the header (provided by DEPARTMENT) air is compressed in main air compressor (CP-11) to about 5 to 6 bar (a), cooled in after cooler AC-11. This air is fed to recycle compressor to higher pressure and cooled in after cooler AC-12. Air is then fed to booster blower of expansion turbine (CP-13), where the pressure is further raised. It is then cooled in after cooler AC-13 and fed to main exchanger.Air is cooled in main Exchanger (HE-11) to about (-) 140deg C from where it is partly taken out to expansion turbine (ET-35), where air is expanded to about 5 bar (a).

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The expansion turbine is coupled with booster blower CP-13 to recover the energy produced in expansion turbine. Expanded air from expansion turbine is partly sent to HP column (CP-25) and remaining to main exchanger (HE-11) to recover the cold. The recycle air is fed to suction of recycle air compressor (CP-12) the remaining part of air is cooled further to its liquefaction temperature and fed to MP column (CP-25).IN HP COLUMN (CP-25) the air is distilled to produce liquid Nitrogen of 99.98% purity at top and rich liquid containing 30% Oxygen at bottom. Rich liquid is passed through RL filter D-37 to remove any dangerous hydrocarbons it may contain, sent through sub cooler (HE-10) and sent to LP column.LIN MODE

In this mode liquid Nitrogen is taken through sub cooler (HE-10) and taken out as product at medium pressure. When liquid Nitrogen is required at low pressure poor liquid is taken in to LIN separator after expansion in valve. The flashed vapors are recovered and mixed with outgoing waste gases. The liquid Nitrogen is tapped off at low pressure.Rich liquid fed in to the LP column (CP-30) trickles down the LP column. Produces a bath of liquid Oxygen, vaporizes in reboiler condenser RB-31 and finally leaves LP column as waste Nitrogen. Waste Nitrogen after through sub cooler goes through main exchanger and shall be used for regeneration or vented.

GAN LOX MODE:In this mode gas Nitrogen is taken out from HP column (CP-25) warmed in main exchanger and used as product. Poor liquid, Rich liquid taken out from HP columns, are sub cooled and fed to LP column (CP-30). LOX product is taken out from bottom of reboiler condenser (RB-31) sub cooled and delivered as product.

3.2.2 LIST OF MAIN EQUIPMENT

ASU II consists of following main equipment Main air compressor with after cooler -1 set Recycle air compressor with after cooler -1 set Brazed aluminum main exchanger -1 No Brazed aluminum reboiler condenser -1 No

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Brazed aluminum sub cooler - 1 No Expansion turbine with booster air blower -1 set HP/LP column -1 set LIN separator -1 set Carbon steel cold box enclosing

Columns, exchangers etc. -1 No RL adsorber -1 No Thawing heater -1 No Drain disposal vessel -1 No Field instruments -1 Lot DCS/PLC control system -1 set Control cabling -1 Lot Piping/valves etc -1 Lot

ARTICLE – 37: DR GH2 COMPRESSOR (PRIMARY & BOOSTER), CHILLED WATER COOLED GH2 HEAT EXCHANGER AND CHILLED WATER PLANT II (BLUE STAR)The compressor is dry running horizontal reciprocating foundation mould compressor. The primary compressor consists of 2 stages to compress GH2 from 1.2 bar (a) to 7.5 bar (a). The flow rate is 420Nm3/hr. The secondary compressor further increases the pressure in three stages. Also 80 Nm3/hr of GH2 from PSA is added and the total flow rate becomes 500 Nm3/hr at 120 bar (a) outlet. The compressor has its own control panel installed at control room.The chiller plant supplies chilled water for cooling cylinder jacket of Hydrogen compressors, GH2 Heat Exchanger at cold box inlet and air inlet of molecular sieve of ASU. Chilled water Heat Exchanger cools GH2 from 315K to 285K at cold box inlet.

ARTICLE – 38 : HIGH PRESSURE GH2 HOFER COMPRESSORMAKE : Andreas Hofer, GermanyCONFIGURATION : Diaphragm compressor MODEL: MKZ 280-60

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The system is designed to take Gaseous Hydrogen either from steam reformer unit of ILHP or Gaseous Hydrogen produced by conversion of Liquid Hydrogen in atmospheric evaporator in case steam reformer is not running. The pressure is increased to 120 bar in reciprocating compressor and finally to 440 bar (a) in GH2

Hofer compressor. (The Gas is supplied through 4000m of ½” piping to other facilities like Main Engine Test Stand/Steering Engine Test and/TPT/CST/TCT.)

ARTICLE – 39: HIGH PRESSURE GN2 HOFER COMPRESSORMAKE : Andreas Hofer, GermanyCONFIGURATION : Reciprocating compressor with Final Diaphragm compressor MODEL : 180 TK 400/MKZ 350-50

The system is designed to take Gaseous Nitrogen tabbed from Air Separation Unit (ASU I or II) or GN2 produced by conversion of Liquid Nitrogen in atmospheric evaporator in case of ASU is not running. The pressure is increased from 4 bar (a) to 440 bar (a) (The Gas is supplied through 4000m of 1” piping to other facilities like Main Engine Test Stand/Steering Engine Test and/TPT/CST/TCT.)

ARTICLE – 40 : N2 START UP COMPRESSORMAKE : M/s Kirloskar, PuneCONFIGURATION : Two Stage reciprocating, Non Lubricating (dryRunning) Water

cooled compressionThe compressor can handle dry Gaseous Nitrogen as well as atmospheric air.

It is used to compress air to 7bar (a) and increase the air supply to Air Separation Unit (ASU I or ASU II). SPARE PARTS MANUAL FOR MODEL NO: KHOSLA 2EHA2TERGT

ARTICLE – 41:125 KL LH2 Storage Tank

MAKE : M/s Gardner Cryogenics, USACONFIGURATION : Horizontal Cylinder Tank with Super Insulation and Liquid Nitrogen Shield.

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The tank is connected with vent stack provided with continuous Gaseous Nitrogen purging and flame arrestor. The details are given in Gardner Manual No: DM-06-6023, SERIAL NO: 6319-06ARTICLE – 42 :40 KLAIR LIQUIDE TANKER – 2 NOS

MAKE : Air liquide, France (Cryolor, France)The Hydrogen storage cum transfer which can be used for higher pressure up to 12bar (a). The tankers being service No 170037 & 170038 are added as part of Augmentation of LH2 storage. The tankers are Horizontal, cylindrical tank with super insulation and Liquid Nitrogen Shield. The two tankers 35m3 normal capacity are meant for storage as well as for transport of liquid Hydrogen. This Dewar is cylindrical in shape and housed in a standard 8’ wide x 8½’ high x 40 long inter model frame. These tankers are mounted on PL Haulwel make trailer and will be hauled by Ashok Leyland vehicle. There are two units complete with tanker, trailer and prime mover. The detailed specification and the relevant drawing for the tanker units are given in the Document no Trailer 5/170038 file no. E 9169.DCC.002.

ARTICLE – 43: 40 KL GARDNER LH2TANKER 630306 – 1NoMAKE : M/s GARDNER CRYOGENICS, USAThe Hydrogen storage cum transfer can be used for higher pressure up to 6.0bar (a). The tanker being service No 630306 is added as part of Augmentation of LH2

storage. The tankers are Horizontal, cylindrical tank with super insulation and Liquid Nitrogen Shield. The tankers 40m3 normal capacity are meant for storage as well as for transport of liquid Hydrogen. This Dewar is cylindrical in shape and housed in a standard 8’ wide x 8½’ high x 40 long inter model frame. These tankers are mounted on PL Haulwel make trailer and will be hauled by Ashok Leyland vehicle. There are two units complete with tanker, trailer and prime mover. The detailed specification and the relevant drawing for the tanker units are given in the Document no operation & spare part manual: 6303-06.

ARTICLE – 44:75 KL INOX MAKE LIN TANK – 1 NO

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The liquid Nitrogen produced in the distillation unit of ASU II is filled in the 75m3 LIN storage tank located opposite to the cold box. This tank is a Perilite filled vacuum insulated double wall vessel and is equipped with safety devices and measuring instruments. There is a top filling and bottom discharge line for the filling/transfer purpose. A pressurization coil is provided for pressure build up in the tank. The liquid level is measured by a differential pressure gauge with additional connection for transmitter and the tank pressure is measured using a pressure gauge. The inner vessel has two safety valves. The vessel is designed according to the ASME pressure vessel code. Details are available in Document no H7904A. JOB NO. 0502/1.This is made possible with the help of a pressurization coil is provided in the tank. The transfer line includes SS pipe line from LIN tank discharge coupling and flexible hose to connect the LIN transport tanker.

ARTICLE – 45:75 KL INOX MAKE LOX TANK – 1 NOThe liquid oxygen produced in the distillation unit of ASU II is filled in the 65m3 LOX storage tank located opposite the cold box. This tank is a perilite filled double wall vacuum insulated tank and is equipped with safety devices and measuring instruments. There is a top filling and bottom discharge line for the filling/transfer purpose. A pressurization coil is provided for pressure build up in the tank. The liquid level is measured by a differential pressure gauge with necessary additional provision for connecting a transmitter and to measure the pressure in the tank, a pressure gauge is provided. The inner vessel has two safety valves. The vessel is designed according to the ASME pressure vessel code. The total specification and drawing are available in the document H7904A. JOB NO. 0502/2.

ARTICLE – 46: LOX AND LIN TRANSPORTATION TANKERThere are two numbers of transportation tankers of capacity 10,000 liters each for transporting LOX/LIN. The tankers are vacuum insulated. The tankers are in built one standard chassis with prime mover. The prime movers are provided with driver’s cabin Tanker No TN 72 AZ 2216&TN 72 AZ 2219. The details of the tankers are given in OPERATION & MAINTENANCE MANUAL MODEL NO: T12K 17.5K

ARTICLE – 47:10KW HEATER

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The heater is used to heat the GN2 in the startup of LH2 plant. The hot GN2 is used to heat the D.S Reformer and feed Naphtha pipe line.

ARTICLE – 48:LH2 PUMPING SYSTEM.LH2 pumping system is established at ILHP for pumping LH2and supply high pressure GH2 to facilities through yard piping. The system is located in side merlon for safety. The system includes a LH2 pump with 8 lit/min capacity, a high pressure atmospheric evaporator and related SI piping for connecting LH2 tanker, vent stack and high pressure discharge line. LH2 is supplied from LH2 tanker through SI lines, pumps out to 500 bar. High pressure liquid hydrogen get evaporated inatmospheric evaporator and high pressure GH2 charged to facilities through yard piping line.

ARTICLE – 49: YARD PIPING.High pressure GN2 and GH2 supply systems of ILHP are charging the high pressure GN2/GH2 to the test facilities through yard piping laid through jungles between ILHP and MET/TCT. Yard piping consisting of SS lines for supplying GH2 and GN2 separately as follows: 1. 1” NB 160 sch line for supplying GN22. ½” NB 160 sch line for supplying GH2

Distance between ILHP & MET yard line is approximately 3 km. Yard line is connected with compressor discharge at ILHP and connected with MET facilities & having all welded joints in yard section. GH2 line has a branch that connects HGP with valves near MET. GH2 line has a branch connecting CHPI. GH2 is charged up to 400 bar to MET,TCT,SET CST &CFT. GN2 is charged up to 400 bar to MET,TCT, TPT, CST& CFT.

ANNEXURE-2.1

SPECIFICATION OF RAW WATER

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pH : 7.6

CHLORIDE : 46PPM

HARDNESS : 140PPM

IRON : 0.1PPM

SILICA : 72PPM

ANNEXURE-2.2

SPECIFICATION OF BOILER FEED WATER

171

Pressure : Minimum 2 bar (g)Maximum 2 bar (g)

Temperature :25-30˚CTDS :2.5 ppm max.Chloride :2 ppm max.Fe :0.03 ppm max.Turbidity :Clear of colourlessO2 :6 ppm max.pH :9 to 10Silica :1 ppm max.Organic content :1 ppm max.

ANNEXURE-2.3

SPECIFICATION OF COOLING WATER

172

pH :7.6Total hardness :14.42 ppm max.Chlorides :117.09 ppm max.Fe2O3 :3.06 ppm max.Turbidity :5.05 ppm max.M-Alkali :70.06 ppm max.SiO2 :10.1 ppm max.EC :787 micro siemen/cm

CHAPTER IVLIST OF EQUIPMENTS

1. EQUIPMENT / MACHINERIES

173

174

SL NO DESCRIPTION ILHP TAG NO.

1 TURBO AIR COMPRESSOR WITH PANELS HT MOTOR (WITH INTER COOLERS)

ILHP/M/501

2 LUBE OIL PUMP UNIT FOR AIR COMPRESSOR ILHP/M/502

3 PRE COOLING PUMP UNIT ILHP/M/503

4 PRE COOLING PUMP STAND BY UNIT ILHP/M/504

5 EXPANSION TURBINE ILHP/M/505

6 OIL PUMP UNIT FOR EXPANSION TURBINE ILHP/M/506

7 AIR FILTER ILHP/E/501

8 SILENCER – SUCTION TO COMPRESSOR ILHP/E/502

9 SILENCER – DISCHARGE TO COMPRESSOR ILHP/E/503

10 SILENCER – COLD BOX OUT ILHP/E/504

11 SILENCER – M.S. UNIT OUT ILHP/E/505

12 AFTER COOLER OF AIR COMPRESSOR ILHP/E/506

13 CHILLER – HEAT EXCHANGER ILHP/E/507

14 EVAPORATIVE COOLER ILHP/E/508

15 MOL.SIEVE UNITS (2 BEDS) ILHP/E/509 A/B

16 HEATER UNIT ILHP/E/510

17 COLD BOX ILHP/E/511

18 LN2 SEPARATOR ILHP/E/512

19 PLC PANEL WITH PLC S7 ILHP/E/513

20 NAPTHA FEED PUMP UNIT ILHP/M/101

21 NAPTHA FEED PUMP STAND BY UNIT ILHP/M/102

22 BFW FEED PUMP UNIT ILHP/M/103

23 BFW FEED PUMP UNIT (STAND BY) ILHP/M/104

24 H2 RECYCLE COMPRESSOR UNIT ILHP/M/105

25 H2 RECYCLE COMPRESSOR UNIT (STAND BY) ILHP/M/106

26 BLOWER – REFORMER BOX ILHP/M/107

27 HYDRAZINE DOZING PUMP UNIT ILHP/M/108

28 NAPTHA HEATER ILHP/E/101

29 NAPHTHA EVAPORATOR ILHP/E/102

30 NAPHTHA PRE HEATER ILHP/E/103

31 DESULPHURISATION REACTOR ILHP/E/104

TANKS/ TANKERS / CYLINDERS

175

176

SL NO DESCRIPTION ILHP TAG NO.

136LH2 TANKERS WITH AL HIPPO PRIME MOVERS (3 NOS.) – (CAPACITY 41 m3 EACH)

ILHP/T/401 A/B/C

137 LOX STORAGE TANK (26 m3) – 1 NO ILHP/T/402

138 LIN STORAGE TANK (43 m3) – 1 NO ILHP/T/403

139LIN TRANSPORTATION TANKER WITH AL, TURBO TUSKER (2 NOS. – 13,000LIT EACH)

ILHP/T/404

140LOX TRANSPORTATION TANKER WITH AL, TURBO TUSKER (1 NOS. –

13,000LIT)ILHP/T/405 A/B

141 LIN TRANSPORTATION TANKER WITH PRIME MOVER (2 NO. 6000 LIT) ILHP/T/406 A/B

142 NAPHTHA STORAGE TANK (60,000) LIT ILHP/T/102

143 BOILER FEED WATER TANK (12m3) ILHP/T/103

144 H2 CYLINDER SKID, 1 m3, 250 BAR (4 NOS.) ILHP/A/101

145 HELIUM CYLINDERS (10 NOS.) ILHP/A/401

146 ELECOFLUX – 02 PPM ANALYSER ILHP/A/501

147 SERVOMEX – 02% PPM ANALYSER ILHP/A/502

148 MAGNOS 4G – 02 PPM ANALYSER ILHP/A/503

149 CALIBRATION GAS CYLINDERS (5 CYLINDERS) ILHP/A/504

150 A/C. UNIT SPLIT A/C FOR ASU I PLC ROOM ILHP/A/505

151 OVER HEAD TRAVELLING CRANE ILHP/A/506

152 FLUE GAS ANALYSER ILHP/A/101

153 METHANE ANALYSER ILHP/A/201

154 CALIBRATION GAS CYLINDERS FOR METHANE ANALYSER ILHP/A/202

155 OVER HEAD TRAVELLING CRANE ILHP/A/303

156 S.S FLEXBLE HOSES FOR LOX/LIN TANKERS (3 NOS.) ILHP/A/401

157 VACUUM INSULATED HOSES FOR LH2 TANKER (4 NOS.) ILHP/A/402

158 WALKIE TALKIE (4 NOS.) ILHP/A/803

THE LIST OF ADDITIONAL EQUIPMENTS HANDED OVER TO BIDDER.

177

178

SL NO DESCRIPTION ILHP TAG NO.

1LIQUID HYDROGEN PURIFICATION SYSTEM

ILHP/AD/LHPS

2 25M3 PUMP ILHP/M/AD/01

3 25M3 PUMP STAND BY ILHP/M/AD/02

4 COOLING TOWER III ILHP/M/AD/03

5 COOLING TOWER III FAN ILHP/M/AD/04

6 CHILLER PLANT COMPRESSOR ILHP/M/AD/05

7CHILLER PLANT COMPRESSOR CW PUMP

ILHP/M/AD/06

8CHILLER PLANT COMPRESSOR BRINE PUMP ST.

ILHP/M/AD/07

9 62.5 KVA DG SET (POWERICA) ILHP/E/AD/01

1062.5 KVA DG SET STAND BY (GREAVES)

ILHP/E/AD/02

11POWER PANEL FOR 62.5 KVA DG SET

ILHP/E/AD/03

12 STAND BY POWER PANEL ILHP/E/AD/04

135KL LH2TRANSPORT TANKER (WITHOUT PRIMOVER)

ILHP/T/AD/01

1410KL LH2TRANSPORT TANKER (WITHOUT PRIMOVER)

ILHP/T/AD/02

AUGUMENTATION MACHINERIES AND EQUIPMENTS

SL NO DESCRIPTION ILHP TAG NO.

1 GH2 HOFER COMPRESSOR WITH MOTOR -500 BAR ILHP/2015/AU/01

2 DRESSER RAND H2 COMPRESSOR WITH MOTOR (PRIMARY -1 BOOSTER-1) ILHP/2015/AU/02

3 N2 START UP COMPRESSOR KIRLOSKAR (PNEUMATIC) ILHP/2015/AU/03

4 GN2 HOFER COMPRESSOR WITH SIEMENS MOTOR -500 BAR ILHP/2015/AU/04

5 CP 11 CAMERON TURBO AIR COMPRESSOR WITH MOTOR TA 2000 ILHP/2015/AU/05

6 CP 12 CAMERON RECYCLE COMPRESSOR WITH MOTOR TA 6000 ILHP/2015/AU/06

7 CRYO STAR TURBINE WITH BOOSTER COMPRESSOR ILHP/2015/AU/07

8 BOC COLD BOX ILHP/2015/AU/08

9 INOX LIN STORAGE TANK 75 KL ILHP/2015/AU/09

10 INOX LOX STORAGE TANK 75 KL ILHP/2015/AU/10

11 125 KL LH2 STORAGE TANK ILHP/2015/AU/11

12 BLUE STAR CHILLER PLANT WITH ILHP/2015/AU/12

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PANEL 2NOS

13 CHILLED WATER CIRCULATION PUMP UNIT 2NOS ILHP/2015/AU/13

14170037 (TN72 Q4109) AIR LIQUIDE LH2 TANKER WITH PRIME MOVER ILHP/2015/AU/14

15170038 (TN72 Q4101) AIR LIQUIDE LH2 TANKER WITH PRIME MOVER

ILHP/2015/AU/15

16 630306 GARDNER LH2 TANKER ILHP/2015/AU/16

17 TN 72 AZ 2216 LOX TANKER 10 KL ILHP/2015/AU/17

18 TN 72 AZ 2219 LOX TANKER 10 KL ILHP/2015/AU/18

19 BOTLIBOI COOLING TOWER 1NO ILHP/2015/AU/19

20 150m3 COOLING WATER PUMP WITH MOTOR ILHP/2015/AU/20

21 PLC CONTROL PANEL FOR GH2 HOFER COMPRESSOR ILHP/2015/AU/21

22 PLC CONTROL PANEL FOR GN2 HOFER COMPRESSOR ILHP/2015/AU/22

23 PLC CONTROL PANEL FOR N2START UP COMPRESSOR ILHP/2015/AU/23

24 PLC CONTROL PANELS FOR DR PRIMARY & BOOSTER COMPRESSOR

ILHP/2015/AU/24

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25ASU II 690KW MOTOR VCB CONTROL PANEL PROTECTION RELAYS ILHP/2015/AU/25

26 ASU II ACB AND MCC PANEL ILHP/2015/AU/26

27 N2 HOFER COMPRESSOR PANEL AND ACB ILHP/2015/AU/27

28 DR COMPRESSOR POWER AND CONTROL MCC PANEL WITH ACB ILHP/2015/AU/28

29 TR.I INCOMING PANEL WITH ACB ILHP/2015/AU/29

30 NUMERIC UPS FOR ASU II CONTROL PANEL 2NOS ILHP/2015/AU/30

31 NUMERIC UPS FOR ASU II LAB 1NO ILHP/2015/AU/31

32 SCADA SYSTEM ASU I 2NOS ILHP/2015/AU/32

33 PLC PANEL WITH SCADA ASU II 1NO ILHP/2015/AU/33

34 INCOMER II VCB PANEL WITH PROTECTION RELAYS ILHP/2015/AU/34

35 TRANSFORMER – 1 MV PANEL WITH 4 NOS ACB ILHP/2015/AU/35

36 ASU –II MV PANEL WITH 2 NOS. ACBS ILHP/2015/AU/36

37 TRANSFORMER – II MV PANEL OUTGOING – 4NOS ACB. ILHP/2015/AU/37

181

LISTS OF EQUIPMENTS AND MATERIALS1. MAJOR EQUIPMENTS:

Sl No. Equipments as per Contract

1. Gas Chromatograph fitted with TCD, GSV, SV and Columns

2. Gas Chromatograph fitted with FID, GSV, SV and Columns

3. Dual Channel integrator

4. SHAW type moisture analyzer

5. Trace level Oxygen analyzer

6. Para Hydrogen analyzer

7. Visible Spectrometer

2. MINOR EQUIPMENTS

Sl No. Equipments as per contract

1. Bomb Calorimeter

2. RVP Apparatus

3. Conductivity meter

4. pH meter

5. Nephelometer

6. Hot Air Oven

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7. Electronic Analytical balance

8. Electronic Top loading balance

9. SS Sampling Cylinders

3. MATERIALS (CONSUMABLE)

Sl No. Consumables

1. Laboratory Glass wares

2. Laboratory Chemicals

3. Water bath

4. Heating mantle

5. Hot plate

6. Gas sampling bulbs, 500ml. capacity

7. Super syringe 500 ml. capacity

8. Gas tight syringe

9. Calibration gas standards

SL NO. NEW EQUIPMENTS

1. Gas Chromatograph (GC- PDID/ FID)

Model: Chemitto GC 1000

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2. Gas Chromatograph (GC- PDID/ FID/ TCD)

Model: Trace - GC 2000

2. Gas Chromatograph (GC- PDID)

Model: Trace GC Ultra

3. Gas Chromatograph (GC- TCD & FID)

Model: Trace GC Ultra

4. Oxygen Analyzer (ppm Level)

Model: Delta F- 150

5. UV- Visible Spectrophotometer

Model: Perkin Elmer Lambda 650

6. On- line CO2 Analyzer

Model: S 700

7. On- line Oxygen Analyzer (ppm level)

Model: Delta F- 300

8. On- line Oxygen Analyzer (% level)

9. On- line SHAW Super Dew moisture meter

Detailed list of equipments, machineries. Fittings, instruments, etc., will be prepared and signed by the respective CONTRACT Managers and this document on inventory will form the authenticated record.

184

CHAPTER –V

QUALITY ASSURANCE MANUAL

CONTENTS

ARTICLE - 1 : GENERAL APPROACHARTICLE - 2 : ANALYSIS OF NAPHTHAARTICLE - 3 : ANALYSIS OF BOILER FEED WATER (BFW)ARTICLE - 4 : ANALYSIS OF COOLING WATER (CW)ARTICLE - 5 : ANALYSIS OF INTERMEDIATEARTICLE - 6 : ANALYSIS OF LIQUID HYDROGEN (LH2)ARTICLE - 7 : ANALYSIS OF LIQUID OXYGEN (LOX)ARTICLE - 8 : ANALYSIS OF LIQUID NITROGEN (LIN)ARTICLE - 9 : SAMPLING METHODARTICLE - 10: LIST OF EQUIPMENTS AND MATERIALS

ARTICLE -1: GENERAL APPROACH

The analytical methodologies to be followed for the quality control and acceptance plan will be mainly based on ASTM/IP, England/ Linde and MIL standards. A brief outline of the methodologies for various raw materials, intermediate streams and end products are described in this chapter

ARTICLE -2: ANALYSIS OF NAPHTHA

2.1 SPECIFICATIONDistillation range : IBP 50 deg. C min50% 130 deg, C : FBP 180 DEG. COlefins : 1.5%by Vol. MaxAromatics : 20% by Vol. MaxTotal sulphur : 500 ppm by wt. AverageRVP at 37.8 deg. C : 0.7Kg/cm2 MaxC/H ratio : 6.5Max

185

Lead : 3 ppm by wt. MaxOrganic chloride : 0.5 ppm by wt. MaxArsenic : 1 ppm by wt. MaxCopper Vanadium : NilSodium Mercury : NilResidue on evaporation : 5 mg/100ml.MaxWater : No free waterDensity at 15 deg. C : 0.66 to 0.77 gm /ccMol.wt : 90 to 120Calorific value LHV : 10,200 Kcal/kg

2.2 METHODS OF ANALYSIS

Distillation range shall be determined as per IP -123/84, ASTM D-86-87 method.

Olefins aromatics shall be determined by calculation based on bromine no and boiling range as per IP – 129/64 method.

Total sulphur shall be determined by lamp method as per IP – 107/86, ASTM D 1266 -7 - method.

RVP shall be determined by using RVP apparatus as per IP/69/78,ASTM D 323

C/H ratio shall be determined by calculation as per ISI 1448-P-7 method.

Lead shall be determined by a chemical method as per IP-224/68.

Organic chloride shall be determined by a chemical method or shall be obtained from the Naphtha supplier.

Arsenic, Copper, Vanadium, Sodium and mercury content shall be obtained from the Naphtha supplier.

Residue on evaporation shall be determined by an evaporation method.

Water content shall be obtained from the supplier. Density shall be determined as per IP-160/68, ASTM-D-1298-67

method.

186

Calorific value shall be determined by using a bomb calorimeter as per ISI method.

ARTICLE -3: ANALYSIS OF BOILER FEED WATER

3.1 SPECIFICATION

Pressure : Minimum 2 bar, Maximum 2 barTemperature : 25-30 DEG. CResistivity : 100,000 ohms TDS : 2.5 ppm maxChloride : 2ppm max

Fe : 0.03ppm maxTurbidity : clear of colourlessO2 : 6 ppm maxpH : 9 to 10Silica : 1 ppm maxOrganic content : 1ppm max

3.2 METHOD OF ANALYSISResistivity shall be determined by a conductivity meter.Total hardness shall be determined calorimetrically using water test kit.Total solids shall be determined by a conventional evaporation method.Chloride shall be determined calorimetrically using water test kit.Fe2o3 shall be determined calorimetrically using invisible spectrometer calorimetric. Determination is done as per the method mentioned in the Vogel using ophenanthroline reagent. Turbidity shall be determined using a Nephelometer. Dissolved Oxygen shall be determined as per Linde method.

ARTICLE -4: ANALYSIS OF COOLING WATER4.1 SPECIFICATIONpH : 7.6Total hardness : 14.42 ppm maxChlorides : 117.09 ppm max

187

Fe2o3 : 3.06 ppm maxTurbidity : 5.05 ppm maxM – Alkali : 70.06 ppm maxSio2 : 10.1 ppm maxEC : 787 micro simen /cm4.2. METHOD OF ANALYSISThe pH shall be determined by a pH meter.Total hardness shall be determined calorimetrically using water test kit. Chlorides shall be determined by a turbidity method.Fe2O3 shall be determined calorimetrically by using o-phenanthroline reagent as per Vogel method. Turbidity shall be determined by a Nephelometer.M-Alkali shall be determined calorimetrically by using water test kit.SiO2 shall be determined calorimetrically as per the method in Vogels book of quantitative inorganic analysis.

ARTICLE -5: ANALYSIS OF INTERMEDIATE

The intermediate streams like reformer gas, purge gas, fuel gas, and flue gas containing CO, CH4, 02, C02 and H2 at different leaves will be a gas chromotogragh fitted with a thermal conductivity detector and a flame ionization detector.

ARTICLE – 6: ANALYSIS OF LH2

6.1 SPECIFICATION HYDROGEN : MIN.99.995% PARA CONTENT : > 95%WATER : MAX. 1VPPM NITROGEN : MAX. 5VPPM

CH4 : MAX.1VPPMHELIUM : MAX. 39 VPPM

Carbon monoxide, Carbon dioxide, nitrogenMoisture and volatile Hydrocarbons combined : MAX.9VPPM

6.2. METHODS OF ANALYSIS Hydrogen content:

188

The percentage of hydrogen shall be determined by difference by subtracting all the impurities present from 100.

Moisture content: Moisture content shall be determined by a Shaw type moisture analyzer

having 1 ppm sensitivity.Oxygen content: Oxygen content shall be determined by an electrochemical type oxygen

analyzer having 1 ppm sensitivity. OTHER GASEOUS IMPURITIES: Nitrogen, Methane, Helium, Argon, carbon dioxide and other volatile

hydrocarbons shall be determined by a custom built gas chromatograph fitted with a thermal sieve column. The thermal conductivity detector must have 1 ppm sensitivity for all the components mentioned above. Para content shall be determined by an Ortho-Para content analyzer.

ARTICLE -7: ANALYSIS OF LIQUID OXYGEN7.1 SPECIFICATIONOxygen % by volume : >98.75Argon % by volume : max. 0.5Nitrogen % by volume : max. 0.05Water ppm by volume : max.5Carbon dioxide by volume : max. 5Volatile hydrocarbon mostlyPropane, propylene and heavierSaturates ppm by volume. : max. 2Acetylene ppm by volume : max.0.1

7.2 METHOD OF ANALYSISOxygen content shall be determined by difference by subtracting total impurities from 100. Other gaseous impurities (Argon, Nitrogen, carbon dioxide volatile hydro carbon and acetylene) shall be determined by a gag chromatograph fitted with a thermal conductivity detector having as sensitivity of not less than 1 ppm and a flame ionization detector with a sensitivity of not less than 0.02 ppm.

189

ARTICLE -8: ANALYSIS OF LIQUID NITROGEN

8.1 SPECIFICATIONNitrogen and argon % by volume :min. 99.99Argon ppm by volume :max. 10.00Water ppm by volume :max. 5.00Oxygen ppm by volume :max. 50.00Hydrocarbons ppm by volume :max.5.00Hydrogen ppm by volume :max.5.00

8.2. METHOD OF ANALYSIS Nitrogen content shall be determined by difference by subtracting the total

impurities from 100. Water content shall be determined by SHAW type moisture analyzer with 1 ppm sensitivity.Other gaseous impurities (Argon, oxygen, hydrocarbon and Hydrogen) shall be determined by a gas chromatograph fitted with thermal conductivity and flame ionization detectors having not less than 1ppm sensitivity

ARTICLE -9: SAMPLING METHODS The frequency of sampling of various intermediate streams and products shall be as per the schedule in Linde’s operation manual. The intermediate streams shall be sampled from the respective sample points using 500ml.SS sample container. The sample container must be purged well with the samples before it is filled. The sample container and the sample hoses have ¼ ‘’ BSP male end fittings. Suitable end fittings must be provided at the sample points to withdraw the samples. For withdrawing the flue gas samples Hamilton super syringe or gas sampling bulbs mode of glass be used.The products LH2,LOXand LN2 shall be sampled in accordance with the method given in MIL-S-27626-D (USAF)

ARTICLE -10 LISTS OF EQUIPMENTS AND MATERIALS 10.1 MAJOR EQUIPMENTS:

Gas chromatograph fitted with TCD, GSV, SV and columns

190

Gas chromatograph fitted with FID, GSV, SV and columns.Dual Channel integrator SHAW type moisture analyzer Trace level Oxygen analyzer Para Hydrogen analyzer Visible spectrometer

10.2 MINOR EQUIPMENTS Bomb calorimeterRVP apparatusConductivity meterpH meterNephelometerHot air ovenElectronic analytical balanceElectric top loading balanceSS Sampling cylinders

10.3 MATERIALS (CONSUMABLE)Laboratory glass waresLaboratory chemicalsWater bathHeating mantleHot plateGas sapling bulbs, 500ml. capacitySuper syringe 500 ml. CapacityGas tight syringeCalibration gas standards

PRICE PART CHAPTER-VI

FORMAT FOR QUOTATION

191

1.0 OPERATION & MAINTENANCE COST

The charges payable by the Department for fulfilling the scope of the Contract shall be quoted in the following format by the Bidder. No other payment shall be entertained except as given in the format.1.1 FIXED COST:

Sl. No Description Cost in Rs lakhs/year.

1.1.1

Operation and maintenance of the plant in round the clock basis(Minimum deployment of human resources as per details given in Appendix-1)

The fixed cost towards man power shall include ,Towards Basic Salary

1.1.2 Other allowances including PF, Group insurance etc…

1.1.3 Administrative expenses and overheads cost towards Operation and maintenance of the plant

2.0 Operational Transport charges for outside trips For deliveries outside Mahendragiri, the cost towards diesel shall be paid based on

192

mileage and the distance. The bidder shall quote operational incidental expenses.

Note: Operational incidental expenses shall be quoted as defined in article 4.0 of Chapter II.

Table showing details of Operational incidental expenses for transporting one LH2 tanker

Description Unit Unit cost in Rs

Driver** Per day/per person

Diesel Mechanic (One person per trip)

Per day/per person

Food Allowance for crew with 4 Per day/per

193

SL.

NODESCRIPTION

6KL-2NO 13 KL-3NO 10KL-2NOS 40 KL-3NO (Gardner/ Air Liquide)

40KL-2NOS (Air Liquide)

LIN/LOX Tankers LH2Tankers

TNK8332 TN74G001

TN74G0079 TN74G0080 TN74G0085

TN72AZ2216TN72AZ2219

TN72V0217 TN72V0245 TN72V0246 and others

TN72Q4109 TN72Q4101 and others

1 Operational incidental expenses in Rs per KM

2 Halting charges per day for SUMO/equivalent engaged for pilot, scout, and escort ___________ Rs per day

nos police person

en route accommodation charges and at halting places.

Per day/per person

Accommodation charges at ISRO Guest house at SDSC,SHAR*

At actuals* At actuals*

Oil & Lubricants, En route water and air check up

per trip+

Spare driver for light vehicle (One person per trip)

Per day/per person

Communication per trip+

Overheads and miscellaneous expenses

percentage of total cost

+One trip shall be maximum 8 days for trip to SDSC SHAR and 13 days for trip to ASL Saggonda. *Will be reimbursed At actuals against production of documentary evidence.**Department will decide the no of persons for every transportation. Generally drivers at

the plant will be utilized for transportation of tankers. In case drivers are required at the plant, Department will advise to engage drivers on trip basis based on the above rate.

194

3.0 Fixed transportation charges

195

196

SL.

NO

DESCRIPTION

LIN/LOX TANKERS LH2 TANKERS

6KL-2NOS 13KL-3NOS 10KL-2NOS 40KL-3NOS 40KL- 2NOS

TNK8332 TN74G001

TN74G0079 TN74G0080 TN74G0085

TN72AZ2216TN72AZ2219

TN72V0217 TN72V0245 TN72V0246

TN72Q4109 TN72Q4101

a Overhead Expenses for arranging FC, Quality inspection in Rs per year as defined in article 4 of Chapter II.

b Expenses towards Minor maintenance, battery charging, oil service including oil filter replacement, grease service, fuel filter replacement, Hose replacement etc. in Rs per year as defined in article 4of Chapter II.

4.0 OVER HEAD AND MISCELLANEOUS EXPENSES:

Sl.no Description Figures in %

1 Procurement and supply of Tyres , Chemicals, Oil & Consumables, and Spares as detailed in Appendix 3 of CHAPTER II of RFP towards administrative expenses & overheads including local transportation charges from Nagercoil/Valliyur/Tirunelveli to IPRC Mahendragiri for the following:

With individual unit rate of Tyres , Chemicals, Oil & Consumables, and Spares costing less than Rs. 25,000 in % invoice of cost of Tyres , Chemicals, Oil & Consumables, and Spares supplied .

2 With individual unit rate of Tyres , Chemicals, Oil & Consumables, and Spares costing from Rs. 25,000 to 1,00,000 in % of invoice cost of Tyres , Chemicals, Oil & Consumables, and Spares.

3 Arranging maintenance services from outside parties as given in Appendix 4 in % of invoice cost of maintenance services availed towards administrative expenses & overheads including local transportation charges from Nagercoil/Valliyur/Tirunelveli to IPRC Mahendragiri for the following:

197

Costing less than Rs. 25,000 per service.

4 Costing from Rs. 25,000 to 1,00,000 per service.

Probable list of parties to whom attention is to be invited about PT advertisement:LIST OF PARTIES:

1) M/s.SPIC SMO (A Division of SPIC LTD, Chennai – 600 032) SPIC House 88 Mount Road Guindy Chennai 600032 India Telephone +91 44 22355447 Fax +91 44 22350015 E-mail:  admn.smo@spic.co.in E-mail-ebalu@spic.co.in

O & M SERVICES AND ENGINEERING SERVICES GROUPS:

MOHAN. SGM (ENGINEERING)SPIC SMO ( A Division of SPIC LTD, Chennai – 600 032)SPIC House88 Mount Road GuindyChennai 600032IndiaTelephone +91 44 2235 3179Fax +91 44 22350015E-mail:mohan@spic.co.in

2) Asiatic Oxygen Limited Kolkatta

3) The Andhra Sugars Limited Saggonda

198

Attachment-1General Guidelines

1. Last minute request for the extension of the due date w.r.t. any technical issue at Vendor’s/Supplier’s side will not be considered.

2. You may submit your quotation online well in advance instead of waiting till the last date to ensure that Internet problem and network condition does not cause problem.

3. The documents solicited from vendor should be submitted online. 4. The suppliers have to provide the Open Authorization as per schedule defined. Their bids will not be

valid if this is not submitted online on or before the Open Authorization closing date.5. Vendor should regularly see the e-mail being sent from e-procurement portal for initiating appropriate

action. Conditions for online submission of Tenders

01. It is mandatory for interested parties to register as vendors in our e-procurement portal https://eprocure.isro.gov.in for participating in online e-Procurement process of ISRO. Only registered vendors can submit their offers online in our e-Procurement portal.

02. To register as vendors please refer to the help documents listed in the illustrative demo section on the home page of the e-procurement link mentioned above. They may approach help desk (contact details provided on the home page) for any technical help for registration and subsequent process.

03. Bidders shall arrange themselves all resources, including Digital Signature Certificates (DSC) and Internet Connections at their own cost, for participating in online tendering.

04. Vendors can download the tender details and submit their offers online using their vendor accounts (obtained during registration) in our portal. Help documents/demos for tender download and bidding processes are given on home page.

05. The tender should be submitted online by selecting ISRO Propulsion Complex link provided in the Centres/Units page of ISRO e-procurement portal before the due date and time as specified in the tender.

Procedure for seeking clarifications/help for the tender1. All enquiries regarding the tenders and submission of offers shall be online and only through our e-

Procurement portal. 2. Vendors may approach help desk e-mail id and phone number given on the home page for any

technical help (e-mail: support.isro@nextenders.com and Ph: 020-30187500/ 25315555 & 09167969601).

Procedure for reporting technical issues, if any, in online submission1. In case bidder encounters any technical snag pertaining to e-procurement system while acting on the

tender, computer screen shot of the error message with date & time stamp on the web-browser along with the query shall be e-mailed by the bidder to the help desk (as mentioned above) for problem resolution at least 24 hours before the due date and time of the tender.

2. The time taken to ascertain, evaluate and suggest a solution for the problem reported by vendor may vary from case to case. Hence vendors are advised to submit the bid well in advance before closing date and time to avoid last minute issues.

3. IPRC shall not be responsible for failure of vendors in submitting bids online caused due to technical reasons at vendor end such as network or power failures, computer failure, internet-browser, mistakes / errors in filling the bids on line by vendor etc.

4. Queries by vendors on technical problems on the last day of tender will not be binding on IPRC/ISRO

199

for resolving/addressing. IPRC will not be responsible for non-submission of bids for those cases. Terms & conditions for extension of Tender Due Date

1. The Server Date & Time as appearing on our website https://eprocure.isro.gov. in shall only be considered for the cut-off date and time for receipt of tenders.

2. Request, if any, for extension of tender due date shall reach IPRC at least 4 working days in advance of due date and time for consideration. IPRC is not bound by such requests to extend the due date unless it feels necessary.

3. The e-procurement system does not permit submission of any offer after closing date and time of the e-tender. Hence, there is no scope for any late or delayed offer in the on-line bidding process.

4. Requests for extension of due date and time citing technical issues in online submission of offers will not be entertained.

5. In case there is complete breakdown of e-Procurement system on the last day of the tender for any reason then IPRC may extend the date for submission after their own assessment.

Reworking on Submitted bids1. Vendors have to note that once rework is initiated, the status of the earlier submitted bid becomes

invalid till the bidding process is completed once again. During the process of rework earlier submitted bid data becomes invalid and will not be available for opening. If rework is initiated then vendor has to complete the entire process of bid submission once again within the due date and time for a valid bid submission.

2. IPRC will not be responsible for non submission of bids resulting due to failure of vendor to once again complete the process of bid submission before due date after reworking of submitted bid is initiated.

3. Please note that unsolicited clarifications / changes / modifications sought by the vendors after submitting their bids will not be considered.

Procedure for filling offers online1. Vendors may please note that in case of two-part tender, the price details shall be mentioned

only in the price-bid template. If the price details either in part or full are indicated in the technical bid, the bid will be disqualified.

2. Vendors may note that in e-procurement system submission of bid is a two-step process. After submission of their bids, vendors have to wait for bid sealing by IPRC purchase officer. Following that vendors have to submit open authorization in the e-procurement system to enable the purchase officer to open the bid. If open authorization is not completed by the vendor then purchase officer will not be able to open the bid and the bid becomes invalid.

Using Digital Certificates for online submission 1. Vendors may note that digital keys of class-III USB tokens, which supports both digital signing and

encryption are to be used for bidding in IPRC e-procurement system. 2. Vendors may note that they have to use the same digital key with which they submitted the

bid to give open authorization. If vendors use different key for open authorization, the system will not accept the open authorization and the bid becomes invalid.

3. In case the digital key which is used during bid submission expires before giving open authorization, then vendor has to first login with the new key and use the expired key for completing open authorization process for the bid.

Uploading files in to E-procurement portal1. Vendors may please note that the maximum file size that can be uploaded per attachment in

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e-procurement system is 4 MB. If the document is more than 4 MB then the document is to be split into multiple documents of size less than 4 MB and upload into attachments (preferably in pdf format). Literature / Technical data should accompany the quotation.

2. Similarly, if the number of files to be uploaded is more than the number of attachments allowed in the tender then group the files into folders such that the number of folders is less than the number of attachments. Further zip/archive the folders and upload as attachments. However, the attachment size should still be less than 4 MB.

3. Vendors may note that documents including Literature / Technical data are to be uploaded through e-procurement system only.

4. Offers sent through post, telegram, fax, email, courier will not be considered. Partially completed / incomplete tenders shall not be considered.

Offer validity1. The offer should be valid for a minimum period of 120 days from the date of opening of the bids (Technical

bid in case of 2-part tender). 2. Offers sent through post, telegram, fax, e-mail, courier will not be considered. Partially completed /

incomplete tenders shall not be considered.

Terms for Technical-bid & Price-bid applicable for supply of spares & providing services

1. The goods / material offered should be strictly as per our specifications. Change(s) in specifications, if any, should be clearly indicated by the supplier in his quotation. The supplier should also indicate make/type No. of the materials / equipments offered. Vague terms such as Best Indian, Best Indigenous and Imported make should not be used.

2. Only authorized dealers/agents or their accredited representatives for original manufacturers have to submit the quotation with documentary evidence.

3. Indian Agents while quoting on behalf of their principals shall attach necessary authorization letter from their Principals along with the bid.

4. In a tender, either the Indian Agent on behalf of the Principal/OEM or Principal/ OEM itself can bid but both cannot bid simultaneously for the same item/product in the same tender.

5. If an Indian agent submits bid on behalf of the Principal/OEM, the same Indian agent shall not submit a bid on behalf of another Principal/OEM in the same tender for the same item/product.

a) Facility of after sales service to be confirmed with details. b) Permanent Account Number (PAN) allotted by Income-Tax authorities shall be furnished with documentary proof. Otherwise, documentary proof for having applied for PAN should be provided. Also PAN should be in the name of Company/Firm, if quoted by the Company/Firm and in the name of Individual, if quoted by individual.

c) Service Tax Registration No.

d) TIN No. / TAN No.

e) Local office in Tirunelveli / Nagercoil is preferable.

Note: (b) to (e) are applicable for Indian Companies only. 6. In case of imported items (stores), Ex-Works/FOB/FCA prices should be indicated. In case of indigenous

stores the quotation should be on FOR-Destination / Door delivery basis.7. Delivery period should be specified. For delayed deliveries and for delays in installation (wherever

applicable), IPRC reserves the right to levy Liquidated Damages @ 0.5% per week or part thereof subject to

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a maximum of 10% of PO value. 8. For indigenous stores, the applicable rates of Excise Duty, Sales Tax/VAT and Service Tax etc., should be

clearly mentioned. Terms like Tax/Excise Duty as applicable etc., will not be accepted. Please note that IPRC will not provide Form C/D. Excise Duty Exemption Certificate (EDEC) will be provided for the items covered under Ministry of Finance, Department of Revenue under Notification No. 10/97 Central Excise Dated 01.03.1997 as amended by Notification No. 16/2007 Central Excise Dated 01.03.2007 or Notification No. 64/95-CE dated 16.03.1995 as amended by Notification No. 7/08-CE dated 01.03.2008.

41. ISRO PROPULSION COMPLEX (IPRC) is exempted from payment of Customs Duty under Notification No. 21/2002-Customs dated 01.03.2002 as amended by Notification No. 12/2012 Customs dated 17.03.2012. For imported items IPRC will provide Customs Duty Exemption Certificate.

9. Guarantee / Warranty : as applicable10. IPRC reserves the right to accept or reject any quotation in full or part thereof by recording the reasons. 11. In case the vendor falls in the category of Small Scale Industries(SSIs), who are registered with NSI, Public

Sector Undertakings (PSUs) and Micro & Small Enterprises (MSMEs) the same shall be mentioned in their quote for evaluation.

12. Payment as per clause no 6 of chapter II of RFP

Document to be submitted for payment for imported item.The Sight Draft/Letter of Credit will be operative on presentation of the under mentioned documents;a) Original Bill of Lading / Airway Bill

b) Commercially certified invoices describing the stores delivered, quantity, unit rate and their total value in triplicate. The invoice should indicate the discounts, if any, and Agency Commission separately.

c) Packing List showing individual dimensions and weight of packages. d) Country of Origin Certificate shall be mentioned in the Invoice itself.

e) Test Certificate.

f) Declaration by the Seller that the contents in each case are not less than those entered in the invoices and the quality of the Stores are guaranteed as per the specifications asked for by the Purchaser.

g) Warrantee and guarantee certificates Bank charges to respective accounts. 13. PERFORMANCE BANK GUARANTEE : The Supplier shall guarantee the successful and satisfactory

performance/commissioning of equipment/machinery under the conditions specified in the Purchase Order. As a performance security, the SUPPIER shall furnish a performance bank guarantee (format enclosed) from Nationalized Bank/Scheduled Bank for an amount equal to the sum of 10% of the order value ensuring the due performance of equipment/machinery in accordance with all the specifications and terms specified in the Purchase Order herein valid for the warranty period. On due performance, the performance bank guarantee shall be automatically cancelled and returned to the Supplier within 30 days after expiry of the Warranty period. The performance bank guarantee shall have claim period of six months.

14. FORCE MAJEURE :(a) If at any time during the execution of work, the performance in whole or in part by either party of any

obligation under the work is prevented or delayed by reasons of any war, hostility, acts of the public enemy/terrorist, civil commotion, sabotage, fire, flood, earth quake, epidemics, quarantine restrictions, tsunami, strikes, lock-outs, or acts of God (hereinafter referred as Eventualities) and if notice is given by either party to the other within 21 days from the date of occurrence thereof, neither party shall for such eventuality be entitled to terminate the work nor shall any party have any claim for damages against the other in respect of such non-performance or delay in performance. The performance under the work shall be resumed as soon as practicable after such eventualities have come to an end and the decision

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of the Department whether the performance has been resumed or not shall be final and conclusive.

(b) Provided further that if the performance in whole or in part of any obligation under the work is prevented or delayed by such eventuality for a period of exceeding 60 days, the Department may at their option terminate the Contract provided also if the work is terminated under this clause, the Department will be at liberty to take over from the Supplier at a price fixed by the Department which shall be final, all unused, un-damaged, and acceptable material, bought-out components and stores in course of erection and commissioning in the possession of the Supplier at the time of such termination of such portion thereof as the Department may deem fit excepting such material, bought-out components and stores as the Supplier may with the concurrence of the Department elect to retain.

15. Sales Tax/VAT and / other duties / levies where legally leviable and intended to be claimed should be distinctly shown separately in the tender. We will not issue any Concessional Form for availing Sales Tax concession as per extent orders. Hence, full percentage of tax shall be applicable.

Make, Model No., Catalogue, Client list, details of order from ISRO Centres/Units for similar items, Warranty/guarantee shall be mentioned in the offer. Specifications:- Stores offered should strictly conform to our specifications. Deviations, if any should be clearly indicated by the tenderer in your quotation. The tenderer should also indicate the Make/Type number of the stores offered and provide catalogues, technical literature and samples, wherever necessary along with the quotations. Test Certificates wherever necessary should be forwarded along with supplies. Whenever options are called for in our specifications, the tenderer should address all such options. Wherever specifically mentioned by us, the tenderer could suggest changes to specifications with appropriate response for the same.

The purchaser shall be under no obligation to accept the lowest or any tender and reserves the right of acceptance of the whole or any part of the tender or portions of the quantity offered and the tenderer shall supply the same at the rates quoted.

The Purchaser reserves the right to place order on the successful tenderer for additional quantity up to 25% of the quantity offered by them at the rates quoted.

Samples if called for, should be submitted free of all charges by the tenderer and the Purchaser shall not be responsible for any loss or damage thereof due to any reason whatsoever. In the event of non-acceptance of tender will have to remove the samples at his own expense.

Approximate net and gross weight of the items offered shall be indicated in your offer, if dimensional details are available the same should also be indicated in your offer.

All amounts shall be indicated both in words as well as in figures. Where there is difference between amounts quoted in words and figures, amount quoted in words shall prevail.

Wherever the tenderer is asked to submit sample for evaluation of tenders, the same shall be submitted along with your quote.

Wherever the tenderer asked to quote the charges separately for evaluation on commercial aspect as mentioned below, it shall be quoted separately otherwise the offer would be liable for rejection.

a. Installation charges

b. Third Party Inspection charges

c. Testing charges

d. Training charges

e. Erection & Commissioning charges

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IPRC reserves the right to accept the tender as a whole or part there of. Hence, acceptance of part order shall be confirmed in the offer. If offer is silent on this point, it will be presumed that part order is acceptable to you.

Deviations, if any, to our specification shall be explicitly spelt out.

Important Note:

All vendors should note that the entries for rate, taxes & duties, freight and any other levy shall be entered only in the relevant fields as provided in the financial offer form. In case, any entry is made by the vendor outside the relevant field, same shall be ignored by the system while evaluating the offers and will be ranked accordingly and PO will be placed ignoring such levies.

GENERAL TERMS AND CONDITONS OF CONTRACT1.Definitions :- a) The term shall mean the President of India or his successors or assigns.

b) The term shall mean, the person, firm or company with whom or with which the Order for the supply of stores is placed and shall be deemed to include the Contractor successors, representatives, heirs, executers and administrators unless excluded by the contract.

c) The term shall mean, what Contractor agrees to supply under the contract as specified in the Purchase Order including erection of Plant & Machinery and subsequent testing should such a condition be included in the Purchase Order.

d) The term Purchase Order shall mean, the communication signed on behalf of the Purchaser by an Officer duly authorized intimating the acceptance on behalf of the purchaser on the terms and conditions mentioned or referred to in the said communication accepting the Tender or offer of the Contractor for supply of stores or plant, machinery or equipment or part thereof.

2.Guarantee and Replacement

a) The Contractor shall guarantee that the stores supplied shall comply fully with the specifications laid down, for material, workmanship and performance.

b) For a period of twelve months after the acceptance of the stores, if any defects are discovered therein or any defects therein found to have developed under proper use, arising from faulty stores design or workmanship, Contractor shall remedy such defects at his own cost provided he is called upon to do so within a period of 14 months from the date of acceptance thereof by the Purchaser who shall state in what respect the stores or any part thereof are faulty.

c) If in the opinion of the Purchaser, it becomes necessary to replace or renew any defective stores, such replacement or renewal shall be made by the Contractor free of all costs to the Purchaser provided the notice informing the Contractor of the defect is given by the Purchaser in this regard within the said period of 14 months from the date of acceptance thereof.

d) The Contractor fail to rectify the defects, the Purchaser shall have the right to reject or repair or replace at the cost of the Contractor the whole or any portion of the defective stores.

e) The decision of the Purchaser not withstanding any prior approval or acceptance or inspection thereof on behalf of the Purchaser, as to whether or not the stores supplied by the Contractor are defective or any defects has developed within the said period of 12 months as to whether nature of the defects requires renewal or replacement, shall be final, conclusive and binding on the Contractor.

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f) To fulfil guarantee conditions outlined in clause 4 (a) to (e) above, the Contractor shall, at the option of the Purchaser furnish a Bank Guarantee (as prescribed by the Purchaser) from a Bank approved by the Purchaser for an amount equivalent to 10% of the value of the contract along with first shipment documents. On the performance and completion of the contract in all respects, the Bank Guarantee will be returned to the Contractor without any interest.

All the replacement stores shall also be guaranteed for a period of 12 months from the date of arrival of store at purchaser site.

h) Even While the 12 months guarantee applies to all stores in case where a greater period is called for by our specifications, then such a specification shall apply in such cases the period of 14 months referred to in para 4 (b) & (c) shall be asked for guarantee period plus two months.

3.Packing, Forwarding & Insurance

The Contractor will be held responsible for the stores being sufficiently and properly packed for transport by rail, road, sea or air to withstand transit hazards and ensure safe arrival at the destination. The packing and marking of packages shall be done by and at the expense of the Contractor. The Purchaser will not pay separately for transit insurance all risks in transit being exclusively of the Contractor and the Purchaser shall pay only for such stores as are actually received in good condition in accordance with the contract.

4. Despatches

The Contractor is responsible for obtaining a clear receipt from the transport authorities specifying the goods despatched. The consignment should be despatched with clear Railway Receipt / Lorry Receipt. If sent in any other mode it is at the risk of the Contractor. Purchaser will take no responsibility for short deliveries or wrong supply of goods when the same are booked on said to contain basis. Purchase shall pay for only such stores as are actually received by them in accordance with the contract.

5. Acceptance of stores

a) The stores shall be tendered by the Contractor for inspection at such places as may be specified by the Purchaser at the contractor own risk, expense and cost.

b) It is expressly agreed that the acceptance of the stores contracted for is subject to final approval by the Purchaser, whose decision shall be final. c) If, in the opinion of the Purchaser all or any of the stores that do not meet the performance or quality requirements specified in the purchase order, they may be either rejected or accepted at a price to be fixed by the Purchaser and his decision as to rejection and the prices to be fixed shall be final and binding on the Contractor.

d) If the whole or any part of the stores supplied are rejected in accordance with Clause No. 8 (c) above, the Purchaser shall be at liberty with or without notice to the Contractor, to purchase in the open market at the expense of the Contractor, stores meeting the necessary performance and quality contracted for in place of those rejected, provided that either the purchaser or the agreement to purchase from another supplier is made within six months from the date of rejection of the stores as aforesaid.

6. Rejected stores

Rejected stores will remain at destination at the contractor risk and responsibility, if instructions for their disposal are not received from the Contractor within a period of 14 days instructions from the date of receipt of the advice of rejection, the Purchaser or his representative has, at his discretion the right to scrap or sell or consign the rejected stores to contractor address at the contractor entire risk and expense Freight being payable by the Contractor at actuals.

7. Delivery

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a) The time for and the date of delivery of the stores stipulated in the purchase order shall be deemed to be essence of the contract and delivery must be completed on or before the specified dates.

b) Should the Contractor fail to deliver the stores or any consignment thereof within the period prescribed for such delivery, the Purchaser shall be entitled at his option either.

I. to recover from the Contractor as agreed liquidated damages and not by way of penalty, a sum of 10% of the price of any stores which the contractor has failed to deliver as aforesaid each month or part of a month during which the delivery of stores may be in arrears, or

II. to purchase elsewhere, without notice to the Contractor on the account and at the risk of the Contractor the stores not delivered or others of a similar description (where others exactly complying with the particulars, are not in the opinion of the Purchaser readily procurable, such opinion being final) without cancelling the contract in respect of the consignment (s) not yet due for delivery, or

III. to cancel the contract of a portion thereof and if so desired to purchase or authorize of stores not so delivered or others of a similar description (where others exactly complying with the particulars are not in the opinion of the Purchaser readily procurable such being final) at the risk and cost of the Contractor.

In the event of action being taken under sub-clause (ii) & (iii) of clause 10 above, the Contractor, shall be liable for any loss which the Purchaser may sustain on that account, provided that the re-purchase, or if there is an agreement to re purchase then such agreements is made within six months from the date of such failure. But the Contractor shall not be entitled to any gain on such re-purchase made against default. The manner and method of such re-purchase shall be at the discretion of the Purchaser, whose decision shall be final. It shall not be necessary for the Purchaser to serve a notice of such re-purchase on the defaulting Contractor. This right shall be without prejudice to the right of the Purchaser to recover damages or breach of contract by the Contractor.

8. Recovery of sums due

Whenever any claim for the payment of whether liquidated or not, money arising out of under this contract against the Contractor, the Purchaser shall be entitled to recover such sum by appropriating. In part or whole the security deposited by the Contractor, if a security is taken against the contract. In the event of the security being insufficient or if on security has been taken from the Contractor, then the balance or the total sum recoverable, as the case may be, shall be deducted from any sum then due or which at any time thereafter may become due to the Contractor under this or any other contract with the Purchaser. Should this sum be not sufficient to cover the full amount recoverable, the Contractor shall pay to the Purchaser on demand the remaining balance due. Similarly, if the Purchaser has or makes any claim, whether liquidated or not, against the Contractor under any other contract with the Purchaser, the payment of all moneys payable under the contract to the Contractor including the security deposit shall be with-held till such claims of the Purchaser are finally adjudicated upon and paid by the Contractor.

9. Indemnity

The Contractor shall warrant and be deemed to have warranted that all stores supplied against this contract are free and clean of infringement of any Patent, Copyright or Trademark, and shall at all times indemnify the Purchaser against all claims which may be made in respect of the stores for infringement of any right protected by Patent Registration of design or Trade mark and shall take all risk of accidents or damage which may cause a failure of the supply from whatever cause arising and the entire responsibility for sufficiency of all means used by him for the fulfilment of the contract.

10. ArbitrationRefer clause no12.10 of chapter no I of RFP

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11. Counter Terms and Condition of SuppliersWhere counter terms and conditions / printed or cyclostyled conditions have been offered by the supplier, the same shall not be deemed to have been accepted by the Purchaser, unless specific written acceptance thereof is obtained.

12. Security for Purchaser MaterialsRefer clause no12.6 of chapter no I of RFP

13. INSPECTION AND ACCEPTANCE TESTS:

The purchaser representatives shall also be entitled at all reasonable times during manufacture to inspect, examine and test on the Contractor premises the material and workmanship of all stores to be supplied under this contract and if part of the said stores is being manufactured on other premises, the contractor shall obtain for the purchaser representative permission to inspect, examine, and test as if the equipment were being manufactured on the contractor premises. Such inspection, examination and testing shall not release the contractor from the obligations under this contract. For tests on the premises of the contractor or of any of his sub-contractors, the contractor shall provide free of cost assistance, labour, materials, electricity, fuel and instruments as may be required or as may be reasonably needed by purchaser representative to carry out the tests efficiently.

When the stores have passed the specified test, the purchaser representatives shall furnish a certificate to the effect in writing to this Contractor. The contractor shall provide copies of the tests certificates to the purchaser as may be required.

14 CONTRACTORS DEFAULT LIABILITY:

Refer clause no12.18 of chapter no I of RFP

15. LANGUAGE AND MEASURES

Refer clause no11.1 of chapter no I of RFP

Attachment-2GOVERNMENT OF INDIADEPARTMENT OF SPACE

INDIAN SPACE RESEARCH ORGANISATIONISRO PROPULSION COMPLEX (IPRC)

MAHENDRAGIRI, TIRUNELVELI DISTRICTTAMILNADU 627 133, INDIA

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TERMS AND CONDITIONS FOR SUBMISSION OF QUOTATIONAGAINST PUBLIC TENDER THROUGH E-PROCUREMENT

I. Conditions for online submission of tenders

01. It is mandatory for interested parties to register as vendors in our e-procurement portal https://eprocure.isro.gov.in for participating in online e-Procurement process of ISRO. Only registered vendors can submit their offers online in our e-Procurement portal.

02. To register as vendors please refer to the help demos listed on the home page of the e-procurement link mentioned above. They may approach help desk (contact details provided on the home page) for any technical help for registration and subsequent process.

03. Bidders shall arrange themselves all resources, including Digital Signature Certificates (DSC) and Internet Connections at their own cost, for participating in online tendering.

04. Vendors can download the tender details and submit their offers online using their vendor accounts (obtained during registration) in our portal. Help demos for tender download and bidding processes are given on home page.

05. The tender should be submitted online in the IPRC Centre link before the due date and time as specified in the tender schedule in the portal.

II. Procedure for seeking clarifications/help for the tender

06. All enquiries regarding the tenders and submission of offers shall be online and only through our e-Procurement portal.

07. Vendors may approach help desk e-mail id and phone number given on the home page for any technical help (e-mail: support.isro@nextenders.com and Ph: 020-30187500).

III. Procedure for reporting technical issues, if any, in online submission

08. In case bidder encounters any technical snag pertaining to e-procurement system while acting on the tender, computer screen shot of the error message with date & time stamp on the web-browser along with the query shall be e-mailed by the bidder to the help desk (as mentioned above) for problem resolution at least 24 hours before the due date and time of the tender.

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09. The time taken to ascertain, evaluate and suggest a solution for the problem reported by vendor may vary from case to case. Hence vendors are advised to submit the bid well in advance before closing date and time to avoid last minute issues.

10. IPRC shall not be responsible for failure of vendors in submitting bids online caused due to technical reasons at vendor end such as network or power failures, computer failure, internet-browser, mistakes / errors in filling the bids on line by vendor etc.

11. Queries by vendors on technical problems on the last day of tender will not be binding on IPRC/ISRO for resolving/addressing. IPRC will not be responsible for non-submission of bids for those cases.

IV. Terms & conditions for extension of Tender Due Date

12. The Server Date & Time as appearing on our website https://eprocure.isro.gov. in shall only be considered for the cut-off date and time for receipt of tenders.

13. Request, if any, for extension of tender due date shall reach IPRC at least 4 working days in advance of due date and time for consideration. IPRC is not bound by such requests to extend the due date unless it feels necessary.

14. The e-procurement system does not permit submission of any offer after closing date and time of the e-tender. Hence, there is no scope for any late or delayed offer in the on-line bidding process.

15. Requests for extension of due date and time citing technical issues in online submission of offers will not be entertained.

16. In case there is complete breakdown of e-Procurement system on the last day of the tender for any reason then IPRC may extend the date for submission after their own assessment.

V. Reworking on Submitted bids:

17. Vendors have to note that once rework is initiated the status of the earlier submitted bid becomes Pending till the bidding process is completed once again. During the process of rework earlier submitted bid data becomes invalid and will not be available for opening. If rework is initiated then vendor has to complete the entire process of bid submission once again within the due date and time for a valid bid submission.

18. IPRC will not be responsible for non submission of bids resulting due to failure of vendor to once again complete the process of bid submission before due date after reworking of submitted bid is initiated.

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19. Please note that unsolicited clarifications / changes / modifications sought by the vendors after submitting their bids will not be considered.

VI. Procedure for filling offers online:

20. Vendors may please note that in case of two-part tender, the price details shall be mentioned only in the price-bid template. If the price details either in part or full are indicated in the technical bid, the bid will be disqualified.

21. Vendors may note that in e-procurement system submission of bid is a two-step process. After submission of their bids, vendors have to wait for bid sealing by IPRC purchase officer. Following that vendors have to submit open authorization in the e-procurement system to enable the purchase officer to open the bid. If open authorization is not completed by the vendor then purchase officer will not be able to open the bid and the bid becomes invalid.

VII. Using Digital Certificates for online submission

22. Vendors may note that digital keys of class-III USB tokens, which supports both digital signing and encryption are to be used for bidding in IPRC e-procurement system.

23. Vendors may note that they have to use the same digital key with which they submitted the bid to give open authorization. If vendors use different key for open authorization, the system will not accept the open authorization and the bid becomes invalid.

24. In case the digital key which is used during bid submission expires before giving open authorization, then vendor has to first login with the new key and use the expired key for completing open authorization process for the bid.

VIII. Uploading files in to E-procurement portal:

25. Vendors may please note that the maximum file size that can be uploaded per attachment in e-procurement system is 4 MB. If the document is more than 4 MB then the document is to be split into multiple documents of size less than 4 MB and upload into attachments (preferably in pdf format). Literature / Technical data should accompany the quotation.

26. Similarly, if the number of files to be uploaded is more than the number of attachments allowed in the tender then group the files into folders such that the number of folders is less than the number of attachments. Further zip/archive the folders and upload as attachments. However, the attachment size should still be less than 4 MB.

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27. Vendors may note that documents including Literature / Technical data are to be uploaded through e-procurement system only.

28. The offer should be valid for a minimum period of 120 days from the date of opening of the bids (Technical bid in case of Two Part Tender)

29. Offers sent through post, telegram, fax, email, courier will not be considered. Partially completed / incomplete tenders shall not be considered.

IX. Offer validity

30. The offer should be valid for a minimum period of 120 days from the date of opening of the bids (Technical bid in case of 2-part tender).

31. Offers sent through post, telegram, fax, e-mail, courier will not be considered. Partially completed / incomplete tenders shall not be considered.

X. Terms for Technical-bid & Price-bid wherever applicable including supply of spares and providing services.

32. The goods / material offered should be strictly as per our specifications. Change(s) in specifications, if any, should be clearly indicated by the supplier in his quotation. The supplier should also indicate make/type No. of the materials / equipments offered. Vague terms such as Best Indian, Best Indigenous and Imported make should not be used.

33. Only authorized dealers/agents or their accredited representatives for original manufacturers have to submit the quotation with documentary evidence.

34. Indian Agents while quoting on behalf of their principals shall attach necessary authorization letter from their Principals along with the bid.

35. In a tender, either the Indian Agent on behalf of the Principal/OEM or Principal/ OEM itself can bid but both cannot bid simultaneously for the same item/product in the same tender.

36. If an Indian agent submits bid on behalf of the Principal/OEM, the same Indian agent shall not submit a bid on behalf of another Principal/OEM in the same tender for the same item/product. 37. a) Facility of after sales service to be confirmed with details. b) Permanent Account Number (PAN) allotted by Income-Tax authorities shall be furnished with documentary proof. Otherwise, documentary proof for having applied for PAN should be provided. Also PAN should be in the name of Company/Firm, if quoted by the Company/Firm and in the name of Individual, if quoted by individual. c) Service Tax Registration No.

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d) TIN No. / TAN No. e) Local office in Tirunelveli / Nagercoil is preferable. Note: (b) to (e) are applicable for Indian Companies only.

38. In case of imported items (stores), Ex-Works/FOB/FCA prices should be indicated. In case of indigenous stores the quotation should be on FOR-Destination / Door delivery basis.

39. Delivery period should be specified. For delayed deliveries and for delays in installation (wherever applicable), IPRC reserves the right to levy Liquidated Damages @ 0.5% per week or part thereof subject to a maximum of 10% of PO value.

40. For indigenous stores, the applicable rates of Excise Duty, Sales Tax/VAT and Service Tax etc., should be clearly mentioned. Terms like Tax/Excise Duty as applicable etc., will not be accepted. Please note that IPRC will not provide Form C/D. Excise Duty Exemption Certificate (EDEC) will be provided for the items covered under Ministry of Finance, Department of Revenue under Notification No. 10/97 Central Excise Dated 01.03.1997 as amended by Notification No. 16/2007 Central Excise Dated 01.03.2007 or Notification No. 64/95-CE dated 16.03.1995 as amended by Notification No. 7/08-CE dated 01.03.2008.

41. ISRO PROPULSION COMPLEX (IPRC) is exempted from payment of Customs Duty under Notification No. 21/2002-Customs dated 01.03.2002 as amended by Notification No. 12/2012 Customs dated 17.03.2012. For imported items IPRC will provide Customs Duty Exemption Certificate.

42. Guarantee / Warranty period as applicable shall be indicated, along with the quote. Guarantee/Warranty shall commence from the date of installation and acceptance of the complete equipment supplied under the contract/purchase order. 43. IPRC reserves the right to accept or reject any quotation in full or part thereof by recording the reasons.

44. In case the vendor falls in the category of Small Scale Industries(SSIs), who are registered with NSI, Public Sector Undertakings (PSUs) and Micro & Small Enterprises (MSMEs) the same shall be mentioned in their quote for evaluation.

45. PAYMENT: 100% through RTGS within 30 days from the date of receipt and acceptance of items at our site is the normal payment for Indigenous supply.

46. PERFORMANCE BANK GUARANTEE: Refer clause no 12.6 of chapter-I

47. FORCE MAJEURE :

(a) If at any time during the execution of work, the performance in whole or in part

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by either party of any obligation under the work is prevented or delayed by reasons of any war, hostility, acts of the public enemy/terrorist, civil commotion, sabotage, fire, flood, earth quake, epidemics, quarantine restrictions, tsunami, strikes, lock-outs, or acts of God (hereinafter referred as Eventualities) and if notice is given by either party to the other within 21 days from the date of occurrence thereof, neither party shall for such eventuality be entitled to terminate the work nor shall any party have any claim for damages against the other in respect of such non-performance or delay in performance. The performance under the work shall be resumed as soon as practicable after such eventualities have come to an end and the decision of the Department whether the performance has been resumed or not shall be final and conclusive.

(b) Provided further that if the performance in whole or in part of any obligation under the work is prevented or delayed by such eventuality for a period of exceeding 60 days, the Department may at their option terminate the Contract provided also if the work is terminated under this clause, the Department will be at liberty to take over from the Supplier at a price fixed by the Department which shall be final, all unused, un-damaged, and acceptable material, bought-out components and stores in course of erection and commissioning in the possession of the Supplier at the time of such termination of such portion thereof as the Department may deem fit excepting such material, bought-out components and stores as the Supplier may with the concurrence of the Department elect to retain.

48. Sales Tax/VAT and / other duties / levies where legally leviable and intended to be claimed should be distinctly shown separately in the tender. We will not issue any Concessional Form for availing Sales Tax concession as per extent orders. Hence, full percentage of tax shall be applicable.

49. Make, Model No., Catalogue, Client list, details of order from ISRO Centres/Units for similar items, Warranty/guarantee shall be mentioned in the offer. Specifications:- Stores offered should strictly conform to our specifications. Deviations, if any should be clearly indicated by the tenderer in your quotation. The tenderer should also indicate the Make/Type number of the stores offered and provide catalogues, technical literature and samples, wherever necessary along with the quotations. Test Certificates wherever necessary should be forwarded along with supplies. Whenever options are called for in our specifications, the tenderer should address all such options. Wherever specifically mentioned by us, the tenderer could suggest changes to specifications with appropriate response for the same.

50. The purchaser shall be under no obligation to accept the lowest or any tender and reserves the right of acceptance of the whole or any part of the tender or portions of the quantity offered and the tenderer shall supply the same at the rates quoted.

52. Samples if called for, should be submitted free of all charges by the tenderer

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and the Purchaser shall not be responsible for any loss or damage thereof due to any reason whatsoever. In the event of non-acceptance of tender will have to remove the samples at his own expense.

53. Approximate net and gross weight of the items offered shall be indicated in your offer, if dimensional details are available the same should also be indicated in your offer.

54. All amounts shall be indicated both in words as well as in figures. Where there is difference between amounts quoted in words and figures, amount quoted in words shall prevail.

55. Wherever the tenderer is asked to submit sample for evaluation of tenders, the same shall be submitted along with your quote.

56. Wherever the tenderer asked to quote the charges separately for evaluation on commercial aspect as mentioned below, it shall be quoted separately otherwise the offer would be liable for rejection.

a. Installation chargesb. Third Party Inspection chargesc. Testing chargesd. Training chargese. Erection & Commissioning charges

57. IPRC reserves the right to accept the tender as a whole or part there of. Hence, acceptance of part order shall be confirmed in the offer. If offer is silent on this point, it will be presumed that part order is acceptable to you.

58. Deviations, if any, to our specification shall be explicitly spelt out.

Important Note: All vendors should note that the entries for rate, taxes & duties, freight and any other levy shall be entered only in the relevant fields as provided in the financial offer form. In case, any entry is made by the vendor outside the relevant field, same shall be ignored by the system while evaluating the offers and will be ranked accordingly and PO will be placed ignoring such levies.

GENERAL TERMS AND CONDITONS OF CONTRACT

1. Definitions :- a) The term shall mean the President of India or his successors or assigns. b) The term shall mean, the person, firm or company with whom or with which the Order for the supply of stores is placed and shall be deemed to include the Contractor successors, representatives, heirs, executers and administrators unless excluded by the contract. c) The term shall mean, what Contractor agrees to supply under the contract as

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specified in the Purchase Order including erection of Plant & Machinery and subsequent testing should such a condition be included in the Purchase Order. d) The term Purchase Order shall mean, the communication signed on behalf of the Purchaser by an Officer duly authorized intimating the acceptance on behalf of the purchaser on the terms and conditions mentioned or referred to in the said communication accepting the Tender or offer of the Contractor for supply of stores or plant, machinery or equipment or part thereof.

2. Guarantee and Replacementa) The Contractor shall guarantee that the stores supplied shall comply fully with the specifications laid down, for material, workmanship and performance. b) For a period of twelve months after the acceptance of the stores, if any defects are discovered therein or any defects therein found to have developed under proper use, arising from faulty stores design or workmanship, Contractor shall remedy such defects at his own cost provided he is called upon to do so within a period of 14 months from the date of acceptance thereof by the Purchaser who shall state in what respect the stores or any part thereof are faulty. c) If in the opinion of the Purchaser, it becomes necessary to replace or renew any defective stores, such replacement or renewal shall be made by the Contractor free of all costs to the Purchaser provided the notice informing the Contractor of the defect is given by the Purchaser in this regard within the said period of 14 months from the date of acceptance thereof. d) The Contractor fail to rectify the defects, the Purchaser shall have the right to reject or repair or replace at the cost of the Contractor the whole or any portion of the defective stores. e) The decision of the Purchaser not withstanding any prior approval or acceptance or inspection thereof on behalf of the Purchaser, as to whether or not the stores supplied by the Contractor are defective or any defects has developed within the said period of 12 months as to whether nature of the defects requires renewal or replacement, shall be final, conclusive and binding on the Contractor. f) To fulfill guarantee conditions outlined in clause 4 (a) to (e) above, the Contractor shall, at the option of the Purchaser furnish a Bank Guarantee (as prescribed by the Purchaser) from a Bank approved by the Purchaser for an amount equivalent to 10% of the value of the contract along with first shipment documents. On the performance and completion of the contract in all respects, the Bank Guarantee will be returned to the Contractor without any interest. g) All the replacement stores shall also be guaranteed for a period of 12 months from the date of arrival of store at purchaser site. h) Even While the 12 months guarantee applies to all stores in case where a greater period is called for by our specifications, then such a specification shall apply in such cases the period of 14 months referred to in para 4 (b) & (c) shall be asked for guarantee period plus two months. 3. Packing, Forwarding & InsuranceThe Contractor will be held responsible for the stores being sufficiently and properly packed for transport by rail, road, sea or air to withstand transit hazards and ensure safe arrival at the destination. The packing and marking of packages shall be done

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by and at the expense of the Contractor. The Purchaser will not pay separately for transit insurance all risks in transit being exclusively of the Contractor and the Purchaser shall pay only for such stores as are actually received in good condition in accordance with the contract. 4. DespatchesThe Contractor is responsible for obtaining a clear receipt from the transport authorities specifying the goods despatched. The consignment should be despatched with clear Railway Receipt / Lorry Receipt. If sent in any other mode it is at the risk of the Contractor. Purchaser will take no responsibility for short deliveries or wrong supply of goods when the same are booked on said to contain basis. Purchase shall pay for only such stores as are actually received by them in accordance with the contract.

5. Acceptance of storesa) The stores shall be tendered by the Contractor for inspection at such places as may be specified by the Purchaser at the contractor own risk, expense and cost. b) It is expressly agreed that the acceptance of the stores contracted for is subject to final approval by the Purchaser, whose decision shall be final.c) If, in the opinion of the Purchaser all or any of the stores that do not meet the performance or quality requirements specified in the purchase order, they may be either rejected or accepted at a price to be fixed by the Purchaser and his decision as to rejection and the prices to be fixed shall be final and binding on the Contractor. d) If the whole or any part of the stores supplied are rejected in accordance with Clause No. 8 (c) above, the Purchaser shall be at liberty with or without notice to the Contractor, to purchase in the open market at the expense of the Contractor, stores meeting the necessary performance and quality contracted for in place of those rejected, provided that either the purchaser or the agreement to purchase from another supplier is made within six months from the date of rejection of the stores as aforesaid.

6. Rejected storesRejected stores will remain at destination at the contractor risk and responsibility, if instructions for their disposal are not received from the Contractor within a period of 14 days instructions from the date of receipt of the advice of rejection, the Purchaser or his representative has, at his discretion the right to scrap or sell or consign the rejected stores to contractor address at the contractor entire risk and expense Freight being payable by the Contractor at actuals.

7. Deliverya) The time for and the date of delivery of the stores stipulated in the purchase order shall be deemed to be essence of the contract and delivery must be completed on or before the specified dates. b) Should the Contractor fail to deliver the stores or any consignment thereof within the period prescribed for such delivery, the Purchaser shall be entitled at his option either.

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I. to recover from the Contractor as agreed liquidated damages for supply of spares and providing services and not by way of penalty, a sum of 10% of the price of any stores which the contractor has failed to deliver as aforesaid each month or part of a month during which the delivery of stores may be in arrears, or

II. to purchase elsewhere, without notice to the Contractor on the account and at the risk of the Contractor the stores not delivered or others of a similar description (where others exactly complying with the particulars, are not in the opinion of the Purchaser readily procurable, such opinion being final) without cancelling the contract in respect of the consignment (s) not yet due for delivery, or

III. to cancel the contract of a portion thereof and if so desired to purchase or authorize of stores not so delivered or others of a similar description (where others exactly complying with the particulars are not in the opinion of the Purchaser readily procurable such being final) at the risk and cost of the Contractor. In the event of action being taken under sub-clause (ii) & (iii) of clause 10 above, the Contractor, shall be liable for any loss which the Purchaser may sustain on that account, provided that the re-purchase, or if there is an agreement to re purchase then such agreements is made within six months from the date of such failure. But the Contractor shall not be entitled to any gain on such re-purchase made against default. The manner and method of such re-purchase shall be at the discretion of the Purchaser, whose decision shall be final. It shall not be necessary for the Purchaser to serve a notice of such re-purchase on the defaulting Contractor. This right shall be without prejudice to the right of the Purchaser to recover damages or breach of contract by the Contractor.

8. Recovery of sums due

Whenever any claim for the payment of whether liquidated or not, money arising out of under this contract against the Contractor, the Purchaser shall be entitled to recover such sum by appropriating. In part or whole the security deposited by the Contractor, if a security is taken against the contract. In the event of the security being insufficient or if on security has been taken from the Contractor, then the balance or the total sum recoverable, as the case may be, shall be deducted from any sum then due or which at any time thereafter may become due to the Contractor under this or any other contract with the Purchaser. Should this sum be not sufficient to cover the full amount recoverable, the Contractor shall pay to the Purchaser on demand the remaining balance due. Similarly, if the Purchaser has or makes any claim, whether liquidated or not, against the Contractor under any other contract with the Purchaser, the payment of all moneys payable under the contract to the Contractor including the security deposit shall be with-held till such claims of the Purchaser are finally adjudicated upon and paid by the Contractor.

9. IndemnityThe Contractor shall warrant and be deemed to have warranted that all stores

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supplied against this contract are free and clean of infringement of any Patent, Copyright or Trademark, and shall at all times indemnify the Purchaser against all claims which may be made in respect of the stores for infringement of any right protected by Patent Registration of design or Trade mark and shall take all risk of accidents or damage which may cause a failure of the supply from whatever cause arising and the entire responsibility for sufficiency of all means used by him for the fulfillment of the contract.

10. Arbitration Refer clause no12.10 of chapter no I of RFP

12. Security for Purchaser MaterialsSuccessful tenders will have to be furnished in the form of a bank guarantee or any other form as called for by the Purchaser towards adequate security for the materials / property provided by the Purchaser for the due execution of the Contract.

13. INSPECTION AND ACCEPTANCE TESTS: The purchaser representatives shall also be entitled at all reasonable times during manufacture to inspect, examine and test on the Contractor premises the material and workmanship of all stores to be supplied under this contract and if part of the said stores is being manufactured on other premises, the contractor shall obtain for the purchaser representative permission to inspect, examine, and test as if the equipment were being manufactured on the contractor premises. Such inspection, examination and testing shall not release the contractor from the obligations under this contract. For tests on the premises of the contractor or of any of his sub-contractors, the contractor shall provide free of cost assistance, labour, materials, electricity, fuel and instruments as may be required or as may be reasonably needed by purchaser representative to carry out the tests efficiently. When the stores have passed the specified test, the purchaser representatives shall furnish a certificate to the effect in writing to this Contractor. The contractor shall provide copies of the tests certificates to the purchaser as may be required.

14 CONTRACTORS DEFAULT LIABILITY: Refer clause no12.18 of chapter no I of RFP

21. PACKINGa) The Contractor whatever applicable shall pack and cover all stores for sea / air shipment as applicable in a manner suitable for export to a tropical humid climate, in accordance with internationally accepted export practice and in such a manner so as to protect it from damage and deterioration in transit by road rail or sea for space qualified store. The contractors shall be held responsible for all damages due to improper packing. b) The contractor shall ensure that each box/unit of shipment is legible and properly marked for correct identification. The failure to comply this requirement shall make the contractor liable for additional expenses involved.

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c) The contractor shall notify the Purchaser of the date of shipment from the port of embarkation as well as the expected date of arrival of such shipment at the designated port of arrival. d) The contractor shall give complete shipment information concerning the weight, size, content of each packages etc. e) Transhipment of equipment shall not be permitted except with written permission of the purchaser. f) Apart from the despatch documents negotiated through Bank, the following documents shall also be airmailed to the purchaser within 7 days from the date of shipment by sea and within 3 days in case of air consignments.

a) Commercial Bill of Lading/Air Way Bill/Post Parcel Receipt (two non-negotiable copies)

b) Invoice (3 copies) c) Packing List (3 copies) d) Test Certificate (3 copies) e) Certificate of Origin shall be declared in the Invoice itselfContractor shall also ensure that one copy of the packing list is enclosed in

each case.

22. ARBITRATION Refer clause no12.10 of chapter no I of RFP

23. LANGUAGE AND MEASURESAll documents pertaining to the contract including specifications, schedule

notices, correspondence, operating and maintenance instructions drawings or any other writings shall be written in English language. The metric system of measurement shall be used exclusively in the contract.

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