Pre-Feasibility Report For Amendment in Existing EC ......I Site & 10 km study area II Layout plan III NIPL certificate from ICT . Prefeasibility Report for Proposed Expansion IG Petrochemicals

Pre-Feasibility Report

For

Amendment in Existing EC- Increase in Benzoic Acid production by process improvement

Category 5 (e)-A

Prepared By

M/s IG Petrochemicals Limited T-2, M.I.D.C Taloja,

Dist.: Raigad – 410208, Maharashtra, India

Tel.: 022 - 39289102 Web site: www.igpetro.com

http://www.igpetro.com/

TABLE OF CONTENTS: Index

List of Tables

List of Figures

Executive Summary ______________________________________________________________________________ 1

Introduction of the Project / Background Information ___________________________________ 4

Identification of the project and Project Proponent ______________________________________ 4

Brief Description of Nature of the Project: __________________________________________________ 5

Need of project with description for region and country _________________________________ 6

Export Possibility _______________________________________________________________________________ 6

Employment Generation due to Project (Direct and indirect) ___________________________ 6

Project Description_______________________________________________________________________________ 7

Type of Project including interlinked or interdependent projects, if any _____________ 7

The location justification for the project – __________________________________________________ 8

Lay-Out ___________________________________________________________________________________________ 8

Project Description with Processes Details: ________________________________________________ 8 Benzoic acid Recovery ___________________________________________________________________________________ 8 Note on increase in BA production _____________________________________________________________________ 8 Reasons for Increase in BA production: ________________________________________________________________ 9

Resource Optimization: _______________________________________________________________________ 11 Availability of Resources (Water, Energy/Power Requirement): ___________________________________ 11

Manpower: ______________________________________________________________________________________ 11

Steam / Process heat Requirement: ________________________________________________________ 11 DG set: ___________________________________________________________________________________________________ 11

Waste Generation and its treatment, disposal ____________________________________________ 11

Site Analysis ______________________________________________________________________________________ 12

Connectivity_____________________________________________________________________________________ 12

Land form, Land use and Land ownership _________________________________________________ 12

Topography _____________________________________________________________________________________ 12 Wind _____________________________________________________________________________________________________ 12 Temperature & Humidity ______________________________________________________________________________ 13 Rainfall ___________________________________________________________________________________________________ 13

Existing land use pattern _____________________________________________________________________ 13

Existing Infrastructure ________________________________________________________________________ 13

Planning Brief ____________________________________________________________________________________ 14

Planning Concept ______________________________________________________________________________ 14

Proposed Infrastructure _______________________________________________________________________ 15

Industrial area __________________________________________________________________________________ 15

Residential Area________________________________________________________________________________ 15

Green Belt _______________________________________________________________________________________ 15

Social Infrastructure __________________________________________________________________________ 15

Water Management ____________________________________________________________________________ 15

Waste water Management ____________________________________________________________________ 15

Rehabilitation and Resettlement (R & R Plan) ____________________________________________ 16

Project schedule and cost estimates _________________________________________________________ 17

Time schedule of the Project _________________________________________________________________ 17

Estimated project cost (Economic Viability of the Project) _____________________________ 17

Analysis of Proposal (Final recommendations) ___________________________________________ 18

Financial and Social Benefits _________________________________________________________________ 18

List of Tables

Table 1-1 Growth milestones ............................................................................................................................................. 1

Table 1-2 Proposed production quantities ................................................................................................................... 2

Table 2-1 Proposed production quantities ................................................................................................................... 4

Table 3-1 Details Of Nearest Infrastructure Facilities.............................................................................................. 7

List of Annexures

Sr. No. Description

I Site & 10 km study area

II Layout plan

III NIPL certificate from ICT

Prefeasibility Report for Proposed Expansion IG Petrochemicals Limited, Taloja

EXECUTIVE SUMMARY

I G Petrochemicals Ltd. (IGPL) is an established market leader in Phthalic Anhydride (PAN) with strong recognition and excellent plant facilities of international standards. Phthalic Anhydride (PAN) is used in industries such as flexible PVC, plastics, paints, construction, transportation and marine. Phthalic Anhydride (PAN) is also used in manufacturing plasticizers, which are most essential in making PVC products, shoe soles, cables, pipes and hoses, leather cloth, films for packaging and other products. It is also used to manufacture alkyd resins used in paints and in the production of unsaturated polyester

resins for building materials, plastic products, textile industries and printing inks Being a "value driven" company, the values are a part of individual and collective objectives for continuous business excellence. IGPL commenced production in the year 1992 with a view to become one of the leading players in the petrochemicals industry. Today, we are the largest producer of PAN in India. Our dynamic spirit to go beyond the normal realms of success and our relentless will to be the market leader has been the hallmarks of our pursuit of excellence. IGPL is promoted by the Dhanuka Group in technical collaboration with Lurgi GmbH, Germany.

The plant is located at MIDC, Taloja in Raigad District, Maharashtra, India, 50 Km from Jawaharlal Nehru Port Trust (JNPT), Maharashtra, thus enabling us to provide unsurpassed customer service to versatile and diversified market since 1992. Equipped with one of the largest capacity at a single location, the Company has the ability to cater to local and international market. Our evolution of growth is captured in the following table

Table 1-1 Growth milestones

Year Description

1988 Incorporated as 100% EOU in technical collaboration with Lurgi GmbH, Germany.

1992 – 1993 Started production with initial capacity of 45,000 MTPA (PA 1)

1997 – 1998 Brownfield expansion of 50,000 MTPA (PA 2)

2006 – 2007 Debottlenecking of capacity by 26,100 MTPA

2008 – 2009 Converted from EOU to DTA

2013 – 2014 Brownfield expansion of 53,000 MTPA (PA 3) with recovery of Benzoic acid 1000 TPA from residue/effluent & 2.5 MW Captive Power to grid. Total PA Licensed Capacity of 169,110 MTPA


Proposed additional production capacities are:

Table 1-2 Proposed production quantities

Name of products Existing

capacity as per CTO (TPA)*

Existing capacity as per

EC (TPA)#

Proposed Add. capacity (TPA)

Total (TPA)

Phthalic anhydride (PAN)

1,69,110 53,000 -- 2,22,110

Benzoic acid 1,000 500 250 1750 Maleic Anhydride 6,500 1,160 -- 7660 Di ethyl phthalate

(DEP) -- 12,600 -- 12,600

Di methyl phthalate (DMP)

Power (Export to grid)

2.5 MW -- -- 2.5 MW

By- products Sodium sulphate -- 900 -- 900

Phthalic acid -- 800 -- 800 Monoester salts -- 3,000 -- 3,000

(*) Existing Consent to operate Formate 1.0/BO/CAC-Cell/EIC No. NM-5370-14/1st CAC/4700 date 24th April 2015 valid upto 28th February 2018 (#) As per Existing Environment Clearance letter No. J-11011/73/2016-IA II (I), dated 18th July 2017

The plant is at existing plot no T-2 which is at Taloja MIDC area, Dist Raigad, Maharashtra. The total Plot area is 100,876 sq m. Since majority of existing plant/land area (>80%) is in plot T-2, the applications are generally made showing plot T-2. The Google image of the existing and proposed area is at Annexure – I Layout Plan for expansion is attached as Annexure–II. The Land is already in use as “Industrial” (all plots are in MIDC Chemical zone) thus there is no change in land use. MIDC has provided basic infrastructure like Electrical Power, water supply, the internal

road network, external approach road (connecting site to NH4 and Mumbai-Pune Expressway), CHWSTDF (Common Hazardous Waste Storage Treatment and Disposal Facility), and underground effluent line connected to CETP. There is no sensitive establishment in the vicinity such as health resort, hospital, archaeological monuments, Wild Life sanctuaries, National Parks etc. To treat both effluents Industrial & Domestic, the combined Effluent Treatment Plant (ETP) provided shall be suitably enhanced to treat entire effluent quantity.


This unit is registered under Factories Act. All the significant risks identified are controlled through Engineering/Operational/PPE controls. Trained First Aid and Fire Fighting team are available in every shift. Also qualified Safety Officer is employed by the company. Company is accredited ISO 9001: 2008 and ISO 14001: 2004. Firefighting system is installed as per MIDC guidelines. The industry will manufacture additional products as mentioned in chapter 2 below. This will not disturb the present land use. Sufficient greenbelt is developed & maintained as required.

Prefeasibility Report for Proposed Expansion IG Petrochemicals Limited

INTRODUCTION OF THE PROJECT / BACKGROUND INFORMATI ON

Identification of the project and Project Proponent

It is proposed to recover Benzoic acid from Scrubber Effluent water & waste residues during PA purification process. Proposed additional quantities are as below:

Table 2-1 Proposed production quantities

Name of products Existing

capacity as per CTO (TPA)*

Existing capacity as per

EC (TPA)#

Proposed Add. capacity (TPA)

Total (TPA)

Phthalic anhydride (PAN)

1,69,110 53,000 -- 2,22,110

Benzoic acid 1,000 500 250 1750 Maleic Anhydride 6,500 1,160 -- 7660 Di ethyl phthalate

(DEP) -- 12,600 -- 12,600

Di methyl phthalate (DMP)

Power (Export to grid)

2.5 MW -- -- 2.5 MW

By- products Sodium sulphate -- 900 -- 900

Phthalic acid -- 800 -- 800 Monoester salts -- 3,000 -- 3,000

(*) Existing Consent to operate Formate 1.0/BO/CAC-Cell/EIC No. NM-5370-14/1st CAC/4700 date 24th April 2015 valid upto 28th February 2018 (#) As per Existing Environment Clearance letter No. J-11011/73/2016-IA II (I), dated 18th July 2017 IGPL is promoted by the Dhanuka Group through Mysore Petro Chemicals Ltd & other group companies in technical collaboration with Lurgi GmbH of Germany. The Management

team comprises qualified & dedicated professionals. Promoters/ Directors and their background are as follows:

➢ Mr. M M Dhanuka (Chairman): B.E. (Chem), aged 67 years, is a Promoter of the Company and is associated with the company since inception and is also a Promoter & Managing Director of Mysore Petro Chemicals Ltd, a group concern.

➢ Mr. Nikunj Dhanuka (Managing Director): B. Com, MBA aged 47 years is a Promoter of the Company. He has vast experience in finance, banking and all major


functions of the Company and is a Promoter & Director of Mysore Petro Chemicals Ltd, a group concern.

➢ Mr J K Saboo (Executive Director): B. Com, LLB. Aged 61 years. He is associated with the company since 1991 and has more than 35 years’ experience in petrochemical industry. He is in charge of the Taloja Plant and looks after the overall activities of the plant.

➢ Shri Rajesh Muni: B.Com (Hons.), F.C.A. Aged 63 years he is an Independent & Non-Executive Director and associated with IGPL since 2002. He is a senior partner of M/s. R.R. Muni & Co and has more than 30 years of experience in auditing and taxation areas. He was also the President of Bombay Chartered Accountants’ Society.

➢ Dr. A K A Rathi: M.E. (Chem), Ph.D (Chem) and Diploma in Management and

Integrated Coastal Zone Management. Aged 66 years he is an Independent & Non-Executive Director associated with IGPL since 2009. He has worked in Industries Department as Chief Technical Advisor and as Director (Environment) in Forest and Environment Department in the Government of Gujarat. He was associated with Faculty of Planning and Public Policy, CEPT University, Ahmedabad, Gujarat. He has contributed a number of articles on various aspects of industrial development, management, safety and environment in different journals, periodicals etc. and is a visiting professor to various engineering and management colleges.

➢ Shri P H Ravikumar: B.Com., CAIIB, ACIB (Lond.), FCISI (Lond.) (Hons.)Aged 64 years is a retired Banker and is an Independent & Non-Executive Director associated with IGPL since Oct, 2012. He has vast knowledge and experience in corporate banking functions, treasury, retail, agri business verticals and also

associated with Commodity and Derivatives exchanges. ➢ Dr. Vaijayanti Pandit: M.A. in Political Science, Diploma in Journalism and Mass

Communications and Ph.D in Management Studies Aged 64 years she is an Independent & Non-Executive Director associated with IGPL since March, 2015. She has built up a vibrant organization of woman entrepreneurs, managers, professionals from 1982-99. She was Secretary of Indian Merchants Chambers for the period 1999-2006 and was also a Director of Federation of Indian Chambers of Commerce and Industry (FICCI) from 2006-12, which is India’s leading apex industry body.

Brief Description of Nature of the Project:

Proposed project is for Increase in production of Benzoic acid beyond the capacity for which EC was granted and will be effected by way of process improvement viz

• Better recovery of Benzoic Acid from scrubber water due to better control of crystallizer unit

• Increase in conversion of Benzoic Acid during purification of Phthalic Anhydride. Recovery of Benzoic Acid from scrubber solution at the time of applying for EC was about 50% and the production quantity was estimated based on the results observed during


laboratory trails and reported at 1000 TPA. Due enhanced recovery & purity from effluents/residues, it will be possible to recover Benzoic acid capacity upto 1250 TPA. Due to above, company proposes to apply as per newly inserted clause 7 (ii) (a) vide SO No. 3518 (E) dt 23.11.2016

Need of project with description for region and country

Benzoic acid is an important organic intermediate used in number of organic synthesis reactions. Salts of benzoic acid are used as food preservatives and benzoic acid is an important precursor for the industrial synthesis of many other organic substances. Benzoic acid is also used in manufacture of Phenols and Benzoate plasticizers. Benzoic acid also has number of medicinal uses such as topical antiseptics, expectorants, analgesics and

decongestants. Benzoic acid is a general purpose organic chemical and available quite cheaply but has plenty of uses and hence used immensely in Organic chemical industry.

Export Possibility

Based on market growing demand projections there is great opportunity for export.

Employment Generation due to Project (Direct and indirect)

The proposed project will not generate additional manpower.


PROJECT DESCRIPTION

Type of Project including interlinked or interdependent projects, if any

It is modernization project of petrochemicals of existing facility. Location of the Project

Table 3-1 Details Of Nearest Infrastructure Facilities

Sr. No Destination App. Distance of Project Site

1 Nearest National Highway

NH-4 4 km

2 Nearest Airport

Mumbai 28 km

3 Nearest Railway Station

Taloje Panchnand 4.5 km

4 Nearest Port

JNPT sea port 30 km

The proposed project is on the existing location at plot no. T-2 and the adjacent acquired plot T- 2 (part) at MIDC Industrial Estate, Taloja, Dist Raigad Maharashtra.

The Geographical Location of this Industry is at coordinates, 190 05’ 27”N and 730 7’41”E at elevation above Mean sea level of 25 meters. This site is in premises of MIDC which is meant for these types of Industries.

GPS Location on Google Imagery of the proposed site is attached for as (Annexure I). Land Form: Land is on plain contour, it is flat terrain. Land Ownership: Land ownership is with project proponents (IG Petrochemicals limited).

Existing Land use Pattern: The Land is reserved for Industrial use & presently project expansion site is at the same plot. MIDC Taloja is a multi-product industrial estate Existing Infrastructure: Presently there is an existing Infrastructure at the site. Infrastructure like water, electricity, telephone facility, roads already available as this is an existing Industrial area.


There is no sensitive establishment in the vicinity such as health resort, hospital, archaeological monuments, Wild Life Sanctuaries, National Parks etc.

The location justification for the project –

NOT APPLICABLE since project is already operational and application is made for enhanced recovery of Benzoic acid from effluents and residues.

Lay-Out

Refer Annexure II for the plant site layout plan.

Project Description with Processes Details:

Benzoic acid Recovery

Organic residue from forerunning columns of PA-1, PA-2 & dehydrated molten material from crystallizer plant will be fed to Benzoic acid recovery column. The scrubber from wash water containing Phthalic Anhydride (PA) & Benzoic acid (BA)

crystals will be subjected for lower temperature thereby partly crystallizing the two

products. The cooling will be achieved by evaporating water from the wash water solution

at reduced pressure. The remaining solution will then be fed to vacuum rotary filter

thereby separating the wash water and BA+PA crystals (cake). The cake of crystals thus

formed of BA+PA crystals is melted for recovery in a BA recovery column.

The remaining wash water will then be taken for MA recovery to neighboring sister

concern M/s Mysore Petrochemicals Ltd.

Organic residue from forerunning column & cake from Crystallization will be fed to Benzoic

acid recovery column.

The column works on batch mode under vacuum. After achieving the top cut purity benzoic

acid shall be recovered as pure product.

At the end of distillation operation the distillation still mainly containing Phthalic

Anhydride shall be recycled to recover Phthalic Anhydride through normal distillation

process.

Note on increase in BA production

Phthalic Anhydride is manufactured by partial oxidation of O-Xylene with air in presence of

catalyst in a fixed bed tubular reactor. Benzoic acid is one of the side reaction products


while converting O-Xylene to Phthalic Anhydride. Formation of Benzoic Acid at reactor

outlet based on O-Xylene feed is about 0.75%.

There are three stages whereby Benzoic acid is separated from the organic streams as

below:

➢ Goes along with crude PA and Separation during PA Purification: While separating

Phthalic Anhydride from the gas stream, small amount of Benzoic Acid condenses along

with crude Phthalic Anhydride & flows to storage vessels. In the first stage of purification,

crude Phthalic Anhydride is subjected to thermal pretreatment where chemicals are dozed

to achieve required Phthalic Anhydride product quality. In the thermal treatment, Phthalic

Acid which is in the range of about 1.0% in crude Phthalic anhydride partly converts to

Benzoic acid and conversion of Phthalic Acid to Benzoic Acid depends on dehydration of

Phthalic Acid to Phthalic Anhydride during thermal treatment & the temperatures in

thermal pretreatment to achieve required quality of pure Phthalic Anhydride at desired

through put.

➢ Removed in Scrubber and recovered from scrubber effluent: Off gas containing

Phthalic Anhydride, Maleic Anhydride, Benzoic Acid & other organic impurities is

scrubbed in three stage scrubber for dissolving organics before letting clean off gas to

atmosphere. Scrubber water containing mainly Maleic Acid & Benzoic Acid/Phthalic Acid

as well as other organic Acids is sent to Benzoic Acid recovery plant where scrubber

solution temperature is reduced to about 15-18oC in crystallizers. Solubility of Benzoic

Acid & Phthalic Acid reduces with reduction of temperature & thus Phthalic Acid &

Benzoic Acid crystalizes. The slurry is filtered in rotary pressure filter & the solids mainly

containing Benzoic Acid & Phthalic Acid is dehydrated & sent to BA recovery column.

Recovery of Benzoic Acid from scrubber solution based on lab trials which was about 50%

and the quantity was estimated based on the results observed during laboratory trails.

Reasons for Increase in BA production:

At the time of applying for initial permissions (Environmental clearance /consent to

establish), theoretical generation of benzoic acid was estimated based on above facts.

There is an improvement in BA recovery in plant due to following:

➢ Conversion of Benzoic Acid in thermal pretreatment has increased by about 0.1%

which has resulted in increasing Benzoic Acid recovery from 56 to 82 kg/hr.

➢ Recovery of Benzoic Acid from the scrubber solution is observed to be higher about

60% & thus production of Benzoic acid has increased from 58 kg/hr to 70 kg/hr.

➢ Additionally, Benzoic Acid column is designed to get purity of 99.5%, whereas

presently, we are maintaining purity of about 96% which results in increasing

production of about 3.5%. Considering 98% recovery & 96% purity, Benzoic Acid per

hour will be 152 kg/hr.


➢ Benzoic acid can be purified by recrystallization from water because of its high solubility in hot water and poor solubility in cold water. This process usually gives a yield of around 65%

Thus, the Benzoic acid production in existing and proposed production scenario is as

under:

Process step Existing

(as per CTO) in kg/hr Proposed post

expansion in kg/hr Remarks

Recovery from PA purification

56.1 82

From scrubber soln

58.2 70

TOTAL 116.7 152 For 8000 hours

annually 934 TPA 1216 TPA

Say approximately 1000 TPA 1250 TPA Additional due to higher recoveries in BA column

NIPL certificate from Institute of Chemical Technology is enclosed as Annexure III.


Resource Optimization:

The resource optimization shall be carried out at the site and with existing operation at site to reduce wastage and minimum transport needs.

Availability of Resources (Water, Energy/Power Requirement):

1) Power: No additional power requirement for proposed project.

2) Water: No additional fresh water requirement for proposed project. The proposal will result in enhanced recovery of Benzoic acid and will thus result in reduced organic load to ETP thereby enhancing ETP performance and lower quantity of

residue for disposal. Above effluent shall be treated at “existing upgraded ETP at IGPL and shall be sent to CETP Taloja after the treatment.

Manpower:

No additional manpower shall be required for the proposed project.

Steam / Process heat Requirement:

No additional fuel requirement for proposed project.

DG set:

There is no proposal to add any new DG set.

Waste Generation and its treatment, disposal

No change from existing EC/ Consent to Operate.


SITE ANALYSIS

Connectivity

This proposed IG Petrochemicals expansion facility shall be located at its existing Plot T-2 and acquired adjacent plot at MIDC Taloja in Raigad district, Maharashtra.

Land form, Land use and Land ownership

Land Form: Land is on plain contour, it is flat terrain.

Land Ownership: Land ownership is with project proponents.

Topography

The project site is located on a relatively level terrain at an average elevation of 15 m above MSL and forms part of catchment area of Kasardi/Kalundri river. Mountain ranges in the area run in the North – South direction. The Malang gadh is located to the North east (having height of 437m) which stretches down south (612m high- 5-6km to the east) and to the South east (medium sized peaks about 400 m high, 6-7 km away). There is another range (Parsik hill) located about 6-7km to the west also running in North-South direction and separating the MIDC Taloja from Navi Mumbai/MIDC, TTC.

The area has a coastal climate with monsoon occurring between June to September. Like any other coastal area, wind speed, relative humidity is moderate to high and temperature variation is minimal. Micrometeorological information for IGPL, Taloja was collected by installing a micro meteorological station at project site. Data was collected for wind speed, wind direction, temperature, relative humidity and rainfall. Whereas the first two parameters viz. wind speed and direction play a vital role in dispersion of pollutants the later ones i.e. humidity and precipitation are important to find amount of deposition for the region.

Wind

The data on wind patterns are pictorially represented by means of wind rose for Winter Jan-Feb 2014 in figure below. The winds were moderate and are predominantly from directions between north and east. Macro level wind patterns seem to be affected by the presence of Arabian sea to the South west and the mountain ranges which deflect the winds. Calm conditions were recorded during the monitoring period. Overall


meteorological and topographical condition indicates good dispersion characteristics at Taloja.

Temperature & Humidity

Overall climate of this region is equable with high rainfall in monsoon season and very few days of extreme temperatures. The mean annual temperature ranges from 300C to 330C. The maximum temperature of the hottest month in this area varies from 35oC – 40oC in April-May while minimum temperature of coldest month varies from 15oC to 20oC. Extremes of temperatures, like 46-48oC in summer and 10-120C in winter, may be experienced for a day or two in respective season. The area has humid climate. Relative humidity varies from 25% to 85%. Driest days being in winter and wettest ones

experienced in July.

Rainfall

The monsoon in this region extends from June to September with an average annual rainfall of 2500 – 3000mm.

Existing land use pattern

The existing land is used for the existing facility is for manufacture of petrochemicals and its byproducts.

Existing Infrastructure

Existing Infrastructure: Presently there is an operative plant / well developed

Infrastructure at the site.

4.6 Soil Classification

District Raigad is one of the coastal districts of Konkan region of Maharashtra, spread over an area of 7152 km2. It shows variation in topography from high altitudinal Sahyadri hill ranges to coastal plains. The soils of the district are formed from the predominating rock formation i.e. Deccan Trap. According to the topographical situation and location, soils in Raigad district are grouped as Forest, Varkas, Rice, Khar or Salt, Coastal Alluvial and

Laterite soils. District receives average 3029mm annual rainfall mostly contributed by southwesterly monsoon. These climatic and edaphic conditions support different types of forests.


PLANNING BRIEF

Planning Concept

• Plot is at well-established MIDC Taloja area • Purified Water supply from MIDC • Road facility with illumination. • Infrastructure facilities available established MIDC site • Integration with the existing manufacturing facility

5.2 Population Projection

Raigad District is a district in the state of Maharashtra, India. It is in the Konkan region. The district was renamed after Raigad, the fort that was the former capital of the Maratha leader Shivaji Maharaj, and is located in the interior regions of the district, in dense forests on a west-facing spur of the Western Ghats of Sahyadri range. In 2011 the district had a population of 2,635,394, compared to 2,207,929 in 2001. In 2011 urban dwellers had increased to 36.91% from 24.22% in 2001. The district is bounded by Mumbai Harbour to the northwest, Thane District to the north, Pune District to the east, Ratnagiri district to the south, and the Arabian Sea to the west. It includes the large natural harbor of Pen-Mandwa, which is immediately south of Mumbai harbour, and forming a

single landform with it. The northern part of the district is included in the planned metropolis of Navi Mumbai, and its port, the Jawaharlal Nehru Port. The district includes towns / cities of Panvel Alibag, Mangaon, Roha, Pen, Khopoli, Kharghar, Taloja, Khalapur, Uran, Patalganga, Rasayani, Nagothana, Poladpur, Alibag, Karjat and Mahad. The largest city both in area and population is Panvel. The district also includes the isle of Gharapuri or Elephanta, located in Uran which has ancient Hindu and Buddhist caves. 5.3 Assessment of Infrastructure Demand (Physical and Social):

For proposed project there will be increase in production of the chemicals. There will be no major demand of expansion of physical infrastructure and social infrastructure.

https://en.wikipedia.org/wiki/Districts_of_Maharashtra

https://en.wikipedia.org/wiki/Maharashtra

https://en.wikipedia.org/wiki/India

https://en.wikipedia.org/wiki/Konkan

https://en.wikipedia.org/wiki/Raigad_fort

https://en.wikipedia.org/wiki/Maratha

https://en.wikipedia.org/wiki/Shivaji_Maharaj

https://en.wikipedia.org/wiki/Western_Ghats

https://en.wikipedia.org/wiki/Mumbai_Harbour

https://en.wikipedia.org/wiki/Thane_District

https://en.wikipedia.org/wiki/Pune_District

https://en.wikipedia.org/wiki/Ratnagiri_district

https://en.wikipedia.org/wiki/Arabian_Sea

https://en.wikipedia.org/wiki/Mumbai_harbour

https://en.wikipedia.org/wiki/Navi_Mumbai

https://en.wikipedia.org/wiki/Nhava_Sheva


PROPOSED INFRASTRUCT URE

Industrial area

IGPL, MIDC Taloja proposed to increase capacity of synthetic organic chemicals manufacturing facility based on demand and market projection.

Residential Area

No Residential area has been proposed within the plant site.

Green Belt

In and around the IGPL plant site, green plantation has been carried out to balance green belt and along the boundary of the plot.

Social Infrastructure

The proposed project will generate indirect employment. Thus the project shall have a positive impact on the employment pattern of the region. Economic status of the local population will improve due to increased ancillary / business opportunities, thereby making positive impact.

Water Management

No additional water required for proposed project. The project shall be maintained fresh water requirement as per existing consent to operate. The water supply will be through MIDC from Barvi Dam.

Waste water Management

Effluent shall be treated in Existing ETP.


REHABILITATION AND R ESETTLEMENT (R & R PLAN)

The proposed activities are in the existing and acquired neighboring plot of the company

which is located in Taloja MIDC area. It does not require acquisition of Land and the

Infrastructure so there will be no any kind of activity of Rehabilitation and Resettlement

carried out.


PROJECT SCHEDULE AND COST ESTIMATES

Time schedule of the Project

Since this is an modernization of existing project, hence there is no infrastructure

requirement for the increase in benzoic acid production.

Estimated project cost (Economic Viability of the Project)

The project is due enhanced recovery from effluents/residues. Modifications in Crystallizer unit will be required nominal cost of Rs. 1 crore.


ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS)

Financial and Social Benefits

The global growing demand for shall give boost to financial economy for the company and to the nation. It will also benefit the society by way of employment and ancillary industries development.


Annexure I

Site & study area of 1 km

Site & study area of 10 km


ANNEXURE II

Proposed Layout Plan


ANNEXURE III

NIPL certificate from Institute of chemical Technology

Documents

Pre-Feasibility Report For Amendment in Existing EC ......I Site & 10 km study area II Layout plan III NIPL certificate from ICT . Prefeasibility Report for Proposed Expansion IG Petrochemicals