DETAILS OF GREEN BELT DEVELOPMENT - UPL...DETAILS OF GREEN BELT DEVELOPMENT For the period January – 12 to June - 12 1. No. of trees planted before January -12 inside the company

DETAILS OF GREEN BELT DEVELOPMENT

For the period January – 12 to June - 12

1. No. of trees planted before January -12 inside the company premises =

39106 in 20.5 acre.

2. During the above mentioned period:

-No. of trees planted inside company premises = 189 in 0.25 acre area. -Total Trees survived inside company: 189

3. Total trees available inside company: 39295

4. Total area covered : 20.75 acre

5. Total trees per Ha: 4734

EXPENDITURE ON POLUTION CONTROL MEASURE FOR THE PERIOD JANUARY – 12 TO JUNE – 12

A) Operating cost for Air Pollution Control Equipment's

Sr. No. Plant Pollution Control Equipment Expense

1 PCL3 Scrubbers 511961

2 POCL3 Scrubbers 72917

3 Caustic – Chlorine Hypo Scrubber 10289274

4 Caustic – Chlorine Caustic Scrubber 317940

5 White Phosphorus Venture Scrubber 0

6 PCl5 Scrubbers 2002517

7 Mancozeb Scrubbers 4998392

Total cost for operating Air Pollution Control equipment is Rs. 18193001

B) Operating cost for Water Pollution Control Equipment's

Sr. No. Plant Pollution Control Equipment Expense

1 Caustic – Chlorine ETP 1068192

2 PCL3 & POCl3 Plant Scrubber Effluent 722808

3 Power Plant ETP 288832

4 White Phosphorus ETP 0

5 Central ETP ETP 122460

6 RO RO 1548320

7 1 MLD ETP (C-Tech) ETP 9241782

8 MEE MEE 33053352

Total cost for operating Water Pollution Control equipment is Rs. 46045745

C) Operational cost for solid waste disposal

Rs. 9881271 (This includes transferring cost from plant to our internal solid waste storage and

from our site to TSDF, BEIL, Ankleshwar)

Summary of Stack Monitoring Parameters:

Stacks Pollutants Limit Average Maximum Minimum

Power Plant HRSG Stack NOX 50 ppm 28.8 39.7 19.6

Caustic Scrubber WAD 56-TPD Plant HCl 20 mg/Nm3 7.9 10.8 5.9

Caustic Scrubber WAD 100-TPD Plant Cl2 9 mg/Nm

3 1.7 1.7 1.7

HCl 20 mg/Nm3 6.4 8.5 4.8

Caustic Scrubber of HCl Furness 100-TPD Plant HCl 20 mg/Nm3 13.8 16.7 10.9

Caustic Scrubber of Phosphorus Oxy-Chloride

Plant Distillation Column HCl 20 mg/Nm

3 6.0 9.7 4.1

Caustic Scrubber of Distillation Section of PCl3

Plant

HCl 20 mg/Nm3 7.7 10.2 4.4

PCl3 9 mg/Nm3 0.8 1.2 0.5

Caustic Scrubber of Storage Tank & Drum Filling

Section of PCl3 Plant

HCl 20 mg/Nm3 5.6 7.8 3.2

PCl3 9 mg/Nm3 0.5 0.8 0.2

Water Scrubber + Alkali Scrubber of Reactor PCl5

Plant

Cl2 9 mg/Nm3 1.1 1.6 0.4

HCl 20 mg/Nm3 14.3 18.3 11.1

Alkali Scrubber of Mancozeb Plant Reactor D-14

New EDA Scrubber

H2S 45 mg/Nm3 17.9 19.8 15.2

CS2 180 mg/Nm3 127.6 176.0 81.4

Water Scrubber of Wet Spray Dryer of Mancozeb

Plant PM 20 mg/Nm

3 16.5 18.6 14.2

Bag Filter of RVDF of Mancozeb Plant PM 20 mg/Nm3 13.7 17.0 10.2

TPPI - Thermic Fluid Heater

PM 150 mg/Nm3 50.7 66.5 38.4

SO2 100 ppm 9.8 13.4 7.4

NOX 50 ppm 12.4 17.1 9.5

TPPI -Water Scrubber + Ventury Scrubber of Tri-

Phenyl Phosphite Plant Rector(C-2102) HCl 20 mg/Nm

3 8.3 11.4 5.9


Phenyl Phosphite Plant Rector(C-2002A) HCl 20 mg/Nm

3 8.4 10.1 7.0


Phenyl Phosphite Plant Rector(C-2020) HCl 20 mg/Nm

3 7.3 7.3 7.3

Summary of Ambient Monitoring Parameters:

Pollutants Limit Average Maximum Minimum

PM10 100 µg/m3 68.5 84.2 56.2

PM2.5 60 µg/m3 43.1 47.6 38.6

SOX 80 µg/m3 17.4 25.8 12.4

NOX 80 µg/m3 23.4 32.3 14.8

HCl 200 µg/m3 35.9 54.9 7.6

Cl2 100 µg/m3 4.7 4.7 4.7

NH3 400 µg/m3 BDL BDL BDL

HF 160 µg/m3 BDL BDL BDL

H2S 500 µg/m3 BDL BDL BDL

CS2 2000 µg/m3 177.3 306.0 84.6

HC 160 µg/m3 BDL BDL BDL

P2O5 70 µg/m3 BDL BDL BDL

Summary of Effluent Parameters:

Parameters Limits 3rd Party Results NCTL Results

Average Maximum Minimum Average Maximum Minimum

pH 6.5-8.5 -- -- 8 7 -- 8.86 6.84

COD (mg/L) 100 mg/L 89 129 40 116 208 48

SS (mg/L) 100 mg/L 52 78 12 48 218 21

Ammonical

Nitrogen (mg/L) 50 mg/L 12 18 1 13 20 6

UNITED PHOSPHORUS LTD., UNIT NO. 5

JHAGADIA

STATUS CUM COMPLIANCE REPORT FOR ENV. CLEARANCE NO. J – 11011/325/2006 – IA II (I) DTD. 25TH JULY, 2007 FOR VARIOUS PRODUCTS.

Sr.

No.

Condition Status

1 The ministry of Environment & forest has examined the

proposal. It is noted that the proposal is for expansion of

Unit – V at Jhagadia Gujarat. The expansion project

comprise of addition of new units for producing Pesticide

Intermediate & Technical Products and expansion of

existing Chlor-alkali & Captive Power Plants. Company

proposes to produce the following Pesticides

Intermediate Products, Technical Grade Pesticide

Products along with their By – Products

Noted and complied.

Company has started

manufacturing of Mancozeb

and Pendimethyline

Sr.

No.

Products By Products

Quantity in MT/Month Quantity in MT/Month

Items Existing Capacity

Additional

Capacity Overall

capacity

after

expansion

Items Existing

capacity

Additional

capacity

Overall

capacity

after

expansi

on

1 Triphenyl

Phosphite

300 - 300 HCl

(30%)

353 - 353

2 Phosphorus Trichloride

2250 - 2250 - - - -

3 2,4Di Chloropheno

l

166 - 166 Mix

Chloro

phenol

15 - 15

HCl

(30%)

250 - 250

4 Phosphorus Oxychloride

150 - 150 - - - -

5 Phosphorus 900 - 900 Ferrous Phospho

rus

150 - 150

Calcium Silicate

6000 - 6000

6 Phosphorus Acid

150 - 150 HCl(30%)

600 - 600

7 Trinonyl Phenyl

Phosphite

100 - 100

8 Phenyl Di Iso Decyl

Phosphite

100 - 100

9 Amino Tri 200 - 200

Methylene

Phosphoric

Acid

10 Ethylene Diamine

Tetra

Phosphoric

Acid

100 - 100

11 Phosphorus Penta

Chloride

150 150

DVACl Plant

12 DVACl - 300 300 Spent Sulphuric Acid

- 900 900

POCl3 - 400 400

HCL (28%)

- 490 490

Sodium Sulphite

(20%)

- 1200 1200

Pesticides Intermediat

e Products –

Multi

Product

Plant

13 N – Alkylated

Xyledene

- 300 300 Pera Toluene

Sulphoni

c Acid

(PTSA)

- 94 94

OR

HRT Ketone - 200 200

OR

2 – Ethyl 6 – Methyl – n –

n Aniline

- 300 300

OR

MPBAL - 300 300

Caustic Chlorine

Plant

14 Caustic Soda Lye

48% (On

100 % Basis)

4680 10500 15180 Sodium Hypochl

orite

225 525 750

15 Chlorine 3972 8537 12509 - - - -

16 Hydrogen 225 263 488 - - - -

17 Hydrochloric Acid

(30%)

1200 2625 3825 - - - -

Power Plant

18 Electrical Power

50

MW/Hrs

37.6

MW/Hrs.

87.6

MW/Hrs.

Steam 30 MT

/ Hrs.

- 30

MT/Hrs

Pesticides Technical

Products

19 Glyphosate - 1000 1000

20 Pendimethylene

- 200 200

21 Tebuconazole

- 200 200

22 Metalochlor - 200 200

23 Aceflorfen - 500 500 Acetic Acid

(80%)

- 1185 1185

24 Mancozeb - 4000 4000 Sodium Sulphat

e 96% /

Sodium

Sulphat

e

Solution

- 4092/

15680

4092/

15680

25 Acephate - 800 800 Ammonium

Acetate

- 464 464

26 Cypermethrin

- 500 500

27 Permethrin - 300 300 HCl (30%)

- 94.8 94.8

Pesticides Formulation

28 Isopropyl Amine Salt

of

Glyphosate

(liq) –

Formulation

(Kl/Month)

- 2600 2600

29 Ammonium Salt of

Glyphosate

(liq) –

Formulation

(Kl/Month)

- 2600 2600

30 Sodium Salt of

Aceflorofen

–

Formulation

- 1500 1500

CS2 (Carbon Disulfide)

Plant

31 Carbon Disulfide

- 3000 3000

MnSO4 (Manganese

Sulfate)

Plant

32 MnSO4 (31%)

- 10000 10000

2 The unit already has 50 MW CPP and additional 37.5 MW CPP is proposal

to be added. Cooling Towers/ N2 Plant, Compressor, chilling unit,

Biological ET, DM plant, Fire Fighting System etc. shall be added. Total

cost of the expansion is Rs. 473.74 Crores and recurring cost will be Rs.

07.00 Crores. The company has total 8,85,601 sq m (218 acres) of land

and the proposed expansion project will be in the existing premises. Out

of this, about 91,655 sq m is covered as green belt and greenery and an

additional agricultural or forest land is involved in the project site and no

eco-sensitive zone is involved in 7 km area of the project site. However,

about 21 Reserve Forests exist with 10 to 24 km from the site.

Noted

3 The project activities are listed at 4(c) and 5(b) in the schedule of the

EIA Notification, 2006 and are of ‘A’ category. The project is submitted

under the EIA Notification, 2006 for evaluation of the completeness of

Draft EIA/EMP and for additional TORs, if any, as per Para 2.2.1(b) of

the Ministry. The Interim Operational Guidelines dated 13th October

2006 issued by the Ministry, The additional information as desired by

the committee were submitted by the proponent, since the proposed

project is industrial area, it would not need Public Consultation as per

Para 7(i) III, Stage (3) (b) – public construction of EIA Notification

2006.

-

4 Based on the information provided, the Ministry of Environment and

Forests hereby accords environmental clearance to above project under

the provisions of EIA Notification dated 14th September 2006 subject

to the compliance of the following specific and General conditions:

-

5 SPECIFIC CONDITIONS: I The gaseous emissions (SO2, NOx, HCl, Cl2, CH4, P2O5, DMS, H2S, HC,

PCl3, NH4, CS2 AND CO, HC and RSPM from various process units shall

conform to the standards prescribed by the concerned authorities from

time to time. At no time, the emission levels shall go beyond the stipulated

standards. In the event of failure of pollution control system(s) adopted

by the unit, the respective unit shall not be restarted until the control

measures are rectified to achieve the desired efficiency.

Noted and

complied. We have

regular monitoring

internally and

externally .All

parameters are

well within the

limit.

II New standards for pesticides unit, as proposed by the CPCB under the

E(P) A, 1986 shall be followed by the Unit.

Noted and

complied.

III Three new boilers shall be based on Imported Coal/Lignite/ RDF (pellets

or fluff). Fuel for other boilers and D.G. Sets will be Natural Gas, HSD

and FO.

Noted

IV Natural Gas, H2 and Cl2 shall be transported through pipelines. Present

transportation mode of hazardous Chemicals by road shall be switched

over to railway line as soon as it is laid down. All Transportation of

Hazardous Chemicals shall be as per the MVA, 1989

Noted

V 23 additional Stacks shall be provided for dispersion of gaseous emissions.

The height of these shall be as per the Prescribed Stack Height rules

and CPCB guidelines. For process emissions like HCl, Cl2, SO2, PCl3, CS2

etc. Scrubbers shall be provided with each reactor for quenching. Waste

air de-chlorination system shall be provided in the Caustic chlorine Plant,

Vent gases from 2, 4-Dichloro Phenol shall be subjected to two-stage

absorption consisting of DM water and caustic jet. For Chlorine, 2 stages

Scrubber with recovery of Sodium Hypo shall be provided.

Noted and

complied.

Scrubbers

provided for

Mancozeb plant to

control process

emissions.

VI Water/ Alkali Two stage Scrubber systems, Mist Eliminator with Koch

filter and Vet Scrubber with Mist Eliminator shall be installed for the

boilers. Thermic Fluid heater, D.G.Sets, The scrubbed water shall be sent

to ETP for further treatment.

Complied

VII Flare system shall be provided for burning of contaminated H2 and Fume

incinerator shall be provided for decomposition of contaminated air/gas

from the plant.

Noted

VIII For CPP, ESP will be provided which will meet SPM limits with in 50

mg/nm3.

Noted

IX All liquid row material shall be stored in storage Tanks and Drums Complied

X Regular monitoring for SO2, NOx, HCl, Cl2,, CH4, P2O5, DMS, H2S, HC,

PCl3, NH3, CS2 and VOC along with SPM and RSPM in the ambient air at

carious probable locations in the plant shall be carried out.

Complied. Company

have regular

monitoring

internally and

externally . All

parameters are

well within limits.

XI The location if ambient air quality monitoring station shall be reviewed in

consultation with the State Pollution Control Board (SPCB) and additional

stations shall be installed, if required in the downwind direction as well as

where maximum ground level concentration are anticipated.

Noted and

complied.

XII Use if toxic solvent like Methylene Chloride (MC) etc. shall be minimized

to the extent possible. Benzene shall not be used as solvent and no

odorous compounds/ gas like Mercaptans or Hydrogen Sulfide shall be

used or formed in any of reactions at the site.

Noted

XIII Bioassay test and toxicity index shall be carried out regularly. Complied

XIV All the storage tanks shall be under negative pressure to avoid any

leakages. Breathers, N2 blanketing and condensers will be provided for all

the storage tanks. Closed handling systems for chemicals and solvents will

be provided. Magnetic seals will be provided for pumps/agitators for

reactors for reduction of fugitive emission, Chilled Brine based

condensers shall be used to prevent VOC emission. Solvent traps shall be

installed wherever necessary.

Complied

XV All venting equipment shall have vapour recovery system. All the pumps

and other equipment’s where there is a likelihood of HC leakages shall be

provided with Leak Detection and Repair (LDAR) system and LEL

indicators and Hydrocarbon detectors. Provision for immediate isolation

of such equipment, in case of a leakage will also be made. The company

shall provide a well defined Leak Detection and Repair (LDAR) programme

for quantification and control of fugitive emissions. The detectors

sensitivity will be in ppm levels.

Complied

XVI Spent solvents shall be recovered as possible & solvent recovery shall be

further increased from the present 95% to at least 98% percent.

Solvent vapours emitted during purification process from purification

tanks as fugitive emissions shall be reduced as far as possible.

Noted and

complied.

XVII Portable monitoring instruments for all relevant gases like Chlorine and

Ammonia shall be provided.

Complied. Chlorine

sensors are

provided.

XVIII Fugitive emissions in the work zone environment, product, raw materials

storage area shall be regularly monitored for all relevant parameters. The

emissions shall conform to the limits imposed by the State Pollution

Boards/Central Pollution Control Board.

Complied.

Online sensors are

provided for

monitoring Fugitive

emissions like

Chlorine, H2S etc.

XIX No ground water shall be used for the project. Water requirement will not

exceed 10,000 m3/day, which will be met through GIDC Water supply.

Complied. Our

water consumption

is well within the

limit.

XX Daily waste water generation will not exceed to 4,575 m3/day. The whole

waste water shall be treated in the proposed two ETPs. One Effluent

Treatment Plant shall consist of primary, secondary and tertiary

treatment units for the proposed Pesticide, CS2 and MnSO4 Plants. The

inorganic stream shall be sent to CETP after the primary treatment. The

Biodegradable stream shall be treated up to tertiary treatment. High

TDS and low COD stream shall taken to MEE System and High Organic

(high COD) stream will be incinerated. The final treated effluent will be

collected in collection sump and discharged through GIDC drainage line.

The effluent generated from the proposed 350 TPD Caustic Chlorine and

enhanced CPP which will be modified. The effluent generated from the

proposed pesticides in the proposed ETP. The treated effluent shall be

sent to CETP of BEAIL for final discharge into the deep sea through

closed pipeline. No free solvent shall go to the ETP.

Complied.

Effluent treatment

plant consisting

primary, Secondary

and tertiary

treatment.

Augmented the

treatment system

with Hypo

treatment to meet

the Ammonical

Nitrogen

XXI Hazardous / Solid Waste generated shall be as per the list and quantities

submitted to this Ministry as per the letter no. UJH/PRO/17/2007 dated

14th May 2007. On-site Incinerator shall be installed to incinerate

incinerable waste. Otherwise the waste shall de sent to the Common

Incinerator of BEIL. Land fillable waste shall be sent to BEIL-TSDF.

Complied.

We have taken

membership of

BEIL and sending

material to BEIL

regularly.

XXII Emissions from the incinerator shall be the prescribed norms for the

incinerators. Monitoring Protocol as prescribed in these standards shall

be followed.

Noted

XXIII Fly ash generated from the CPP will be utilized for Brick manufacturing

and for Cement manufacturing as per the Fly Ash Utilisation Notification.

Noted

XXIV All safety measures suggested in the letter no. UJH/PRO/17/2007 dated

14th May 2007 for the solvent and reactants storage shall be

implemented

Noted & complied

XV The company shall undertake following Waste Minimization measures.

A Metering and control of quantities of active ingredients to minimize

waste.

Noted and

complied

B Reuse of by-products from the process as raw materials or as raw

material substitutes in other processes.

Complied

C Use of automated filling to minimize spillage. Complied

D Use of “Close Feed” system into batch reactors. Complied

E Venting equipment through vapour recovery system. Complied

F Use of high pressure hoses for equipment clearing to reduce wastewater

generation.

Noted

G The project authorities shall strictly comply with the provisions made in

Manufacture, Storage and Import of Hazardous Chemicals Rules, 1989 as

amended in 2000 for handling of hazardous chemicals. Necessary

approvals from Chief Controller of Explosives must be obtained before

commissioning of the expansion project. Requisite On-Site and Off-Site

Disaster Management Plans will be prepared and implemented. Regular

mock drills shall be carried out for both On-Site and Off-Sit plans.

Noted

H The company shall develop rain water harvesting structures to harvest

the run off water for recharge of ground water.

Noted

I Minimum 25% of the total area shall be developed as green belt as per the

CPCB guidelines. Additional 1,12,091 sq.m shall be developed as green belt.

Noted

J Occupational health surveillance of the workers shall be done on a regular

basis and records maintained as per the Factories Act.

Complied

K Training shall be impaired to all employees on safety and health aspects of

chemicals handling. As informed to the Ministry. OHSAS 18001 shall be

continued. Pre employment and routine periodical medical examinations for

all employees shall be undertaken on regular basis. Training to all

employees on handling of chemicals shall be imported.

Complied

L Usage of PPEs by all employees/ workers shall be ensured. Complied

M The company shall strictly follow all the recommendations mentioned in

the Charter on Corporate Responsibility for Environmental Protection

(CREP).

Complied

N The company shall harvest surface as well as rainwater from the rooftops

of the buildings proposed in the expansion project and storm water drains

to recharge the ground water and use the same water for various

activities of the project to conserve fresh water.

Noted

O All the recommendations made by the consultants in respect of

environmental management and risk mitigation measures relating to the

project shall be implemented.

Complied

P The company shall undertake all relevant measures as indicated during the

Public Hearing for improving the Socio-economic conditions of the

surrounding area. CSR activities will be undertaken by involving local

villages and administration.

Complied

Q The company shall undertake eco-developmental measures including

community welfare measures in the project area for the overall

improvement of the environment. The eco-development plan should be

submitted to the SPCB within three months of receipt of this letter for

approval.

Noted

GENERAL CONDITIONS

I The project authorities shall strictly adhere to the stipulations made by

the State Pollution Control Board.

Complied

II No further expansion or modifications in the plant shall be carried out

without prior approval of the Ministry of Environment and Forests. In

case of deviations or alterations in the project proposal from those

submitted to this Ministry for clearance, a fresh reference shall be made

to the Ministry to assess the adequacy of conditions imposed and to odd

additional environmental protection measures required, if any.

Noted and

complied.

We have obtained

Consent to

Establish (NOC)

from GPCB for

products mix

change and applied

for Consent to

operate(CC&A) .

NOC copy is

attached in

Annexure -1 for

your ready

reference.

III At no time, the emissions shall exceed the prescribed limits. In the event

of failure of any pollution control system adopted by the unit, the unit

shall be immediately put out of operation and shall not be restarted until

the desired efficiency has been achieved.

Noted and

Complied.

IV The project authorities shall strictly comply with the rules and

regulations under Manufacture, Storage and Import of Hazardous

Chemicals Rules, 1989 as amended in October, 1994 and January, 2000.

Authorization from the SPCB shall be obtained for collection, treatment,

storage, and disposal of hazardous wastes.

Complied

V The over all noise levels in and around the plant area shall be kept well

within the standards by providing noise control measures including

acoustic hoods, silencers, enclosures etc. on all sources of noise

generation. The ambient noise levels shall conform to the standards

prescribed under Environment (protection) Act,1986 Rules, 1989 viz. 75

dBA (day time) and 70 dBA (night time).

Complied

VI The project proponent shall also comply with all the environmental

protection measures and safeguards recommended in the EIA/EMP

report.

Complied

VII A separate Environmental Management Cell equipped with full fledged

laboratory facilities shall be set up to carry out the Environmental

Management and Monitoring functions.

Complied

VIII The project authorities shall earmark separate funds of Rs. 43.09 Crores

to implement the conditions stipulated by the Ministry of Environment

and Forests as well as the State Government along with the

implementation schedule for all the conditions stipulated herein. Rs. 07.00

crores will be the annual recurring expenditure for environmental

protection measures. The funds so provided shall not be diverted for any

other purpose.

Noted and being

complied

IX The implementation of the project vis-à-vis environmental action plans

shall be monitored by the concerned Regional Office of the Ministry /

SPCB / CPCB. A six monthly compliance status report shall be submitted

to monitoring agencies.

Complied

X The project proponent shall inform the public that the project has been

accorded environmental clearance by the Ministry and copies of the

clearance letter are available with the SPCB/Committee and may also be

advertised within seven days from the date of issue of the clearance

letter at least in two local newspapers that are widely circulated in the

region of which one shall be in the vernacular language of the locality

concerned and a copy of the same shall be forwarded to the concerned

Regional Office of the Ministry.

Complied

XI The project authorities shall inform the Regional Office as well as the

Ministry, the date of financial closure and final approval of the project by

the concerned authorities and the date of start of the project.

Complied

XII The Ministry may revoke the right to stipulated additional conditions, if

found necessary. The company in a time bound manner will implement

these conditions.

Noted

XIII The above conditions will be enforced, inter-alia under the provisions of

the Water (Prevention & Control of Pollution) Act, 1981, the Environment

(Protection) Act, 1986 Hazardous Waste (Management and Handling)

Rules, 2003 and the Public Liability Insurance Act, 1991 along with their

amendments rules.

Noted

UNITED PHOSPHORUS LTD., UNIT NO. 5 JHAGADIA

STATUS CUM COMPLIANCE REPORT FOR ENV. CLEARANCE NO. J-

11011/42/95-A.II (1), DTD. 17TH. MAY, 1996 OF 100 TPD CHLOR-ALKALI PLANT

Sr. No.

Condition Status

1 To adhere GPCB and state Govt. stipulation Complied as per CCA No. 10067 Dated 25th February 2008 valid up to 18.12.2012

2 To intimate MoEF about any project coming up in the premises

Complied. As and when new projects are coming up, we will intimate MOEF. We have obtained Consent to Establish (NOC) from GPCB for products mix change and applied for Consent to operate(CC&A) . NOC copy is attached in Annexure -1 for your ready reference.

3 Gaseous (CL2, SO2, Nox, HC) and particulate emission from the various process vents and storage tanks should conform to the standards.

Complied Parameters are within limits.

4 Three AAQ to install • Stack emission to monitor regularly

• To submit AAQ + Stack report to MoEF once in six

month with statistical analysis and interpretation

• 3 AAQ installed for monitoring of PM10,PM2.5, SO2,NOX & CL2.

• CL2,HCl Monitored in Hypo & HCl stacks

• Results are being submitted in half yearly reports. It is well within stipulated norms.

5 Fugitive emission monitoring and data recorded Chlorine sensor is to be installed in the chlorine

storage area at lower level between the tanks

16 Cl2 sensors at strategic locations & monitored on DCS.

6 • Liquid effluents coming out of the plants should be confirmed to the standard prescribed by the GPCB

• Recycling and reuse of the treated waste water should be maximized

• Complied • Steam condensate of

Caustic Evaporation reused in Brine make up & Cooling tower make up

7 • Adequate measures for the control noise levels below 85dB.

• Employees to be provided with PPE.

• Engineering Control measures to reduce noise

• Monitoring done monthly. Range is from 70 to 75dB

• Ear muffs & ear plugs are provided to the person working in high noise area like H2 compressor, & air compressor

• Acoustic enclosures provided

8 Occupational health surveillance program with respect to exposure to chlorine, thermal stresses and noise pollution.

Complied. We are doing half yearly

medical check up. We are also doing full body medical check up by external expert agency once in two years. All records are maintained

9 • Green belt of adequate width & density covering 25 acres of land should be developed

• Treated effluent to be used for green belt development

• Complied • Presently we have about

39295 trees • Sewage water is used for

gardening

10 • Educate the neighboring people for accidental release of chlorine

• To install wind sock • Necessary approval from CCE & Chief Inspector of

Factories

• Complied. • Disclosure of Information

on Cl2 to general public is given in book let thriceand also conducted awareness program in the year 1999 & 2005

• We have installed 14wind socks inside the factory

• Obtained CCE approval

for CL2 Storage, filling in toners, hydro testing. Also for H2 filling & storage.

• Maps of plant approved & inspected by Chief Inspector of Factories(Director – Industrial Safety & Health, Gujarat State)

11 Hazardous waste handling as per rules 1989 Complied Yearly return submission is

done for solid waste generation & disposal to GPCB

12 To follow hazardous chemicals Mfg./Storage/Handling / import Rules1989-1994

Complied. MSIHC guidelines followed

for e.g On site emergency plan, MSDS etc.

13 To set up laboratory for collection & analysis of sample

Complied Laboratory is in operation &

regular analysis is being done for waste water, stacks & ambient air, ground water etc.

14 Set up Environment management cell Internal Environment management cell comprising of Unit Head, plant head, SHE Head & Corporate Environmenthead is in operation for close monitoring. The environment cell verifies environmental performance and involves in environmental audit

15 • Funds earmarked during project for Env. protection • Year wise expenditure to be submitted to MoEF

• Complied. • Project has been

commissioned since 1997 with compliance of all environment related protection

• Statement of expenditure submitted half yearly.

16 Six monthly - Half yearly report submission to MoEF • Being submitted regularly

UNITED PHOSPHORUS LTD., UNIT NO. 5 JHAGADIA

STATUS CUM COMPLIANCE REPORT FOR ENV. CLEARANCE NO.

J.13011/26/96-1A.II, DTD. 24TH. DEC., 1996 OF 50 MW COMBINED CYCLE CO. GENERATION POWER PLANT.

Sr. Sr. Sr. Sr. No.No.No.No.

ConditionConditionConditionCondition StatusStatusStatusStatus

1 All the conditions stipulated in the GPCB NOC No. PC/NOC/-BRCH-1611/9518 should be implemented

Complied for effluent quantity & quality norms

2 An area of 103 acres only to be acquired for power plant including green belt development

Complied. Power plant is included in the area of 103 acres

3 Three stack of height 30m, 35m, 7m for Gas Turbine, HRSG, DG sets should be installed

Installed & commissioned

4 Ambient air quality should be regularly monitored and results should be submitted to the MoEF every six months

We are submitting results half yearly to MOEF along with Half yearly EC compliance report.

5 Sulfur content in Naphtha should not exceed 0.15%

Condition is not applicable now as we have switched over from Naphtha to Natural Gas from June 2002 and consent has been obtained

6 Nox control system should be installed to ensure that Nox emission should not exceed 50 ppm

Nox is well within norms.

7 To use effluent for green belt development It is being used

8 Water used for plant should be restricted to 6480 KL/Day

It ranges from 1200 to 1500 KL/Day

9 • Adequate measured for Noise control below -85 dB

• To give PPE to employees

• Enclosures provided to control noise

• People use ear muffs & ear plugs

10 Green belt development @ 1500-2000 trees / hectares

Presently we have about 39295trees in 20.75 Acres.

11 Land fill site provided No solid waste generation from power plant. Power Plant fuel is Natural Gas.

12 To build thermal proof wall between Naphtha tanks and switch yard

Not applicable as we have switched over from Naphtha to Natural Gas.

13 Sludge from common sludge tank to be incinerated and disposed in the land fill site

No such sludge is generated which requires incinerator

14 Full cooperation should be extended to the statutory authority during their visit

Noted the point

15 Funds earmarked for Env. protection during project

Project has been commissioned since 1997 with compliance of all environment related protection

16 Environment monitoring committee should be constitute

As our plant is commissioned since long Internal Environment management cell comprising of Unit Head, plant head, SHE Head & Corporate Environment head is in operation for close monitoring.

After implementation of the project, we have constituted a monitoring committee and the last meeting was conducted in September - 2002

We have carried out a meeting involving various stakeholders including the monitoring members in September 2005 in connection with information on the change over of fuel from naphtha to natural gas as we are working on CDM project.

17 Any deviation or alternation in project need fresh reference to the ministry

There was no deviation during project. However subsequently raw material change from Naphtha to Natural Gas in 2002

Mahabal Enviro Engineers Pvt. Ltd. Engineers, Consultants, Environmental Monitoring Laboratory, Contractors

Plot No. 13/14, Opp. Patel Petrol Pump, Chhindawara Road, Koradi, Dist-Nagpur- 441 111

Phone: 91-07109-326999, 0712-2612162, Tle Fax: 0712-2612212, E-mail: [email protected]

QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010

Effluent Sample Analysis Report

Report No. ME-BH-0333-120113-SA-UPL-5-JH Date: 13.01.2012

Name and Address of Customer

United Phosphorus Limited, UNIT-V, 746 & 750, G.I.D.C; Jhagadia, GUJARAT - 393110

Order Reference No. 4510051816 Dated 19.05.2011

Sample Description / Type

Industrial Effluent/Grab

Sample Collectedby

Laboratory

Sampling Location ETP Outlet (Treated Effluent)

Sample Quantity/Packing

20 L X 1 No. PVC Can

Date of Sampling 04.01.2012 Date of Receipt of Sample

07.01.2012

Sampling Procedure

IS:3025(Part I) 1987 RA1998

Date of Start of Analysis

09.01.2012 Date of Completion of Analysis

12.01.2012

Sr. No.

Parameters Unit Results GPCB LIMIT

Method Reference

1. pH - 7.12 5.5 to 8.5 APHA, 21st Ed., 2005, 4500 - H+

2. Temperature oC 26.0 40 oC IS 3025, Part 9:1983, RA 2002

3. Colour Hazen 10.0 100 APHA, 21st Ed., 2005, 2120 – B,C

4. Total Residual Chlorine

mg/L N.D 1.0 IS-3025, Part 26:1986, RA 2003 Eds 2.1(2004-02)

5. Total Dissolved Solids (TDS)

mg/L 9964 2100 APHA, 21st Ed., 2005, 2540 - C

6. Total Suspended Solids (TSS)

mg/L 12.0 100 APHA, 21st Ed., 2005, 2540 - D

7. Oil and Grease mg/L




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010

Report No. ME-BH-0333-120131-SA-UPL-5-JH Cont… 22. Copper as Cu mg/L < 0.03 2.0 APHA, 21st Ed., 2005, 3500-Cu - B

23. Chromium Hexavalent as Cr6+

mg/L < 0.02 0.1 APHA, 21st Ed., 2005, 3500-Cr - B

24. Total Chromium as Cr

mg/L < 0.02 2.0 APHA, 21st Ed., 2005, 3111 – B

25. Mercury as Hg mg/L < 0.0008 0.01 APHA, 21st Ed., 2005, 3112 – B

26. Arsenic as As mg/L 0.011 0.2 IS 3025, Part 37:1988, RA 2003

27. Cadmium as Cd mg/L 0.019 2.0 APHA, 21st Ed., 2005, 3111 – B

28. Total Heavy Metal mg/L < 2 7.0 By Calculation

29. Percentage Sodium (% Na)

% 93.4 60 MERI HANDBOOK

Remarks: N.D. – Not Detectable

.----------------------------------------------------------End------------------------------------------ for Mahabal Enviro Engineers Pvt. Ltd.

Harish Mendhi Technical Manager AUTHORISED SIGNATORY ---------------- ---------------------------------------------------------------------

Note: 1. The result listed refers only to the tested sample(s) and applicable parameter(s). 2. This report is not to be reproduced except in full, without written approval of the

laboratory.

Page 2 of 2




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010

Stack Emission Monitoring Report





Sample Description / Type Stack Emission Sample Collected by Laboratory

Sampling Location 1. Power Plant Turbine Stack 2. Power Plant HRSG Stack Sample Quantity/Packing

50 mL X 2 No. PVC Bottle and 1 X 1 No. Thimble


10.01.2012

Sampling Procedure As per IS: 11255



16.01.2012

Stack No. 1 2

Stack attached to Power Plant Turbine Stack Power Plant HRSG Stack

Material of construction M.S. M.S.

Stack height above ground level (Meter) 30.0 35.0

Stack diameter(Meter) 3.0 3.0

Stack shape at top Round Round

Type of fuel N.G. N.G.

Flue gas Temperature (0C) Not 135

Flue gas Velocity (m/sec) In 14.1

Total gas quantity (Nm3/hr) Operation 262066

Parameter Unit Results GPCB Limit Method Reference

Particulate Matter mg/Nm3 -- BDL 150 IS 11255 (Part 1):1985 RA-2003

Sulphur Dioxide (SO2) ppm -- BDL 100 IS 11255 (Part 2):1985 RA -2003

Oxides of Nitrogen (NOx) ppm -- 29.2 50 IS 11255 (Part 7):2005

Remarks : BDL – Below Detectable Limit

--------------------------------------------End------------------------------------- for Mahabal Enviro Engineers Pvt. Ltd.

Harish Mendhi Technical Manager AUTHORISED SIGNATORY -------------------------------------------------------------------------------------------------------

Note : 1. The result listed refers only to the tested sample(s) and applicable parameter(s). 2. This report is not to be reproduced except in full, without written approval of the laboratory.

Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010







Stack Emission Sample Collectedby Laboratory

Sampling Location 1. Caustic Scrubber WAD 56-TPD Plant 2. Caustic Scrubber WAD 100-TPD Plant 3. Caustic Scrubber HCl Furness 56-TPD Plant 4. Caustic Scrubber HCl Furness 100-TPD Plant


50 mL X 3 No; 100mL X 3No. PVC Bottle

Date of Sampling

06.01.2012 Date of Receipt of Sample

10.01.2012

Sampling Procedure As per IS: 11255 and IS: 5182



16.01.2012

Stack No. 1 2 3 4

Stack attached to

Caustic Scrubber of WAD 56-TPD Plant


Caustic Scrubber of HCl Furness 56-TPD Plant


Material of construction H.D.P.E. H.D.P.E. F.R.P. F.R.P.

Stack height above ground level (Meter) 30 30 30 30

Stack diameter(Meter) 0.2 0.15 0.15 0.25

Stack shape at top Round Round Round Round

Type of fuel Process

Scrubber Process

Scrubber Process

Scrubber Process

Scrubber

Flue gas Temperature (0C) 30 30 Not 45

Flue gas Velocity (m/sec) 4.6 8.1 In 5.6

Total gas quantity (Nm3/hr) 512 507 Operation 927

Parameter Unit Results GPCB Limit

Method Reference

Chlorine (Cl2) mg/Nm3 BDL BDL -- BDL 9 IS 5182 (Part 19):1982, RA 2003

Hydro Chloride Vapours (HCl) mg/Nm

3 10.8 5.2 -- 14.8 20

Jecob M.B. The Analytical Toxicology of Industril Inorganic Poisons-Inter Science Publishers, Newyork, USA-2367





Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010







Sampling Location 1. Di-Choloro Phenol Plant 2. Phosphorus Oxi-Chloride Plant 3. Phosphorus Acid Plant


50 mL X 1 No. PVC Bottle


10.01.2012




16.01.2012

Stack No. 1 2 3

Stack attached to

Water & Caustic Scrubber of DCP Plant Reactor

Caustic Scrubber of Phosphorus Oxy-Chloride Plant Distillation Column

Water & Caustic Scrubber OR Ventury Scrubber of H3PO4 Scrubber Reactor

Material of construction H.D.P.E. H.D.P.E. H.D.P.E.

Stack height above ground level (Meter) 30.0 30.0 30.0

Stack diameter(Meter) 0.15 0.2 0.15

Stack shape at top Round Round Round

Type of fuel Process Scrubber Process

Scrubber Process

Scrubber

Flue gas Temperature (0C) Not 30 Not

Flue gas Velocity (m/sec) In -- In

Total gas quantity (Nm3/hr) Operation -- Operation


Method Reference

Sulphur Dioxide (SO2)

mg/Nm3 -- -- -- 40 IS 11255 (Part 2):1985 RA -2003 Oxides of Nitrogen (NOx) mg/Nm

3 -- -- -- 25 IS 11255 (Part 7):2005

Chlorine (Cl2) mg/Nm3 -- -- -- 9 IS 5182 (Part 19):1982, RA 2003


3 -- 6.4 -- 20





Note : 1. The result listed refers only to the tested sample(s) and applicable parameter(s). 2. This report is not to be reproduced except in full, without written approval of the laborator

Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010







Sampling Location

1. Caustic Scrubber of Distillation Section of PCl3 Plant

2. Caustic Scrubber of Storage Tank & Drum Filling Section of PCl3 Plant

3. Water Scrubber + Alkali Scrubber of Rector PCl5 Plant


50 mL X 5 No; 100mL X 3 No. PVC Bottle


10.01.2012

Sampling Procedure As per IS: 11255 and OSHA: 6402



16.01.2012

Stack No. 1 2 3

Stack attached to

Caustic Scrubber of Distillation Section of PCl3 Plant

Caustic Scrubber of Storage Tank & Drum Filling Section of PCl3 Plant

Water Scrubber + Alkali Scrubber of Rector PCl5 Plant






Scrubber Storage Scrubber

Process Scrubber

Flue gas Temperature (0C) 30 30 30

Flue gas Velocity (m/sec) -- -- --

Total gas quantity (Nm3/hr) -- -- --


Method Reference

Chlorine (Cl2) mg/Nm3 BDL BDL 1.6 9 IS 5182 (Part 19):1982, RA 2003


3 4.4 4.9 17.6 20


Phosphorus Tri-Chloride Vapours (PCl3) mg/Nm

3 0.8 BDL -- 9 OSHA Method No.6402, 1985





Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010

Ambient Air Quality Monitoring Report Report No.: ME-BH-0334-120113-SA-UPL-5-JH Date: 13.01.2012




Sample Description / Type Ambient Air Sample Collected by Laboratory

Sampling Location Nr. U.G.Tank Sample Quantity/Packing

30 mL X 8 No; 100mL x 1 No. PVC Bottle, 1 No. Filter Paper and 2L X 1 No. Bladder


07.01.2012

Sampling Procedure As per CPCB Guidelines and IS: 5182



12.01.2012

Meteorological Data/ Environmental Conditions

Avg. Wind Velocity km/hr

Prominent Wind Direction Relative Humidity

(%) Temperature

(0C)

3.9 NE - SW Max Min Max Min 54 31 30 11

Location Nr. U.G.Tank Duration of Survey 24 hrs

Sr. No.

Parameter Result Unit GPCB Limit

Method Reference

1. Respirable Suspended Particulate Matter (RSPM)

58.4 µg/m3 100 CPCB Guidelines

2. Oxides of Sulphur (SOx) 12.36 µg/m3 80 CPCB Guidelines

3. Oxides of Nitrogen (NOx) 14.8 µg/m3 80 CPCB Guidelines

4. Hydro Chloride Vapour (HCl) 36.7 µg/m3 200 Jecob M.B. The Analytical Toxicology of Industril Inorganic Poisons-Inter Science Publishers, Newyork, USA-2367

5. Chlorine (Cl2) BDL µg/m3 100 IS 5182 (Part 19):1982, RA 2003

6. Ammonia (NH3) BDL µg/m3 400 APHA Method No. 401, 2nd Edition

7. Hydrogen Flouride (HF) BDL µg/m3 160 IS 5182, Part 13:1991

8. Hydrogen Sulphide (H2S) BDL µg/m3 500 IS 5182, Part 7:1999

9. Carbon Di-Sulphide (CS2) 247 µg/m3 2000 IS 5182 Part 20 1999

10. Hydrocarbon (H.C.) BDL µg/m3 160 IS 5182, Part 17:1979

11. Phosphorus Pent-oxide Fumes (P2O5) BDL µg/m3 70 APHA 25ST Edition 4500, P - D


----------------------------------------------------------End------------------------------------------ for Mahabal Enviro Engineers Pvt. Ltd. Harish Mendhi Technical Manager AUTHORISED SIGNATORY

---------------- --------------------------------------------------------------------- Note: 1. The result listed refers only to the tested sample(s) and applicable parameter(s). 2. This report is not to be reproduced except in full, without written approval of the laboratory.

Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010

Noise Level Monitoring Report

Report No.: ME-BH-0340-120118-SA-UPL-5-JH Date: 18.01.2012


United Phosphorus Limited, UNIT-V, 746 & 750, G.I.D.C; Jhagadia, GUJARAT – 393110



Noise Level Sample Collected by

Laboratory

Sampling Location As mentioned bellow Sample Quantity/ Packing

Not Applicable


Not Applicable

Sampling Procedure

Noise Level Meter

Location Unit Results Norms

dB(A) Leq DAY NIGHT

Fencing Wall East Side (Nr. C-Tech. ETP)

dB(A) Leq

74.5 71.2

Day(06.00-22.00) – 75

Night(22.00-06.00) - 70

Fencing Wall North Side (Nr. Raise Plant)

67.9 64.9

Fencing Wall South Side (Nr. Secondary Brine)

74.1 70.3

Fencing Wall West Side (Nr. Salt Yard)

66.3 60.1

--------------------------------------------End------------------------------------- For Mahabal Enviro Engineers Pvt. Ltd.

Harish Mendhi Technical Manager AUTHORISED SIGNATORY

------------------------------------------------------------------------------------------------------- Note: 1. The result listed refers only to the tested sample(s) and applicable parameter(s). 2. This report is not to be reproduced except in full, without written approval of the laboratory.

Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010

Noise Level Monitoring Report

Report No.: ME-BH-0341-120118-SA-UPL-5-JH Date: 18.01.2012





Noise Level Sample Collected by

Laboratory

Sampling Location As mentioned bellow Sample Quantity/ Packing

Not Applicable


Not Applicable

Sampling Procedure

Noise Level Meter

Location Unit Results Norms

dB(A) Leq DAY NIGHT

Primary Brine

dB(A) Leq

78.5 73.4

TLV - 90

Secondary Brine 77.1 71.2

H2 Compressor 86.2 80.1

Cl2 Compressor 87.3 83.9

Utility Block – Mechanical 95.5 97.3

WP-CO Pump 65.3 62.5

Power Plant GT 85.8 85.7

Utility – MNZ 89.1 87.6

D – 14 Tank- MNZ 80.2 79.1

SPD-Panel Room – MNZ 73.4 73.1

Security Gate 75.1 71.4

1 MLD ETP– C-Tech Blowers 78.2 74.5

Belt Filter Vacuum Pump - MNZ 87.4 83.2

--------------------------------------------End------------------------------------- For Mahabal Enviro Engineers Pvt. Ltd.

Harish Mendhi Technical Manager AUTHORISED SIGNATORY

------------------------------------------------------------------------------------------------------- Note: 1. The result listed refers only to the tested sample(s) and applicable parameter(s). 2. This report is not to be reproduced except in full, without written approval of the laboratory.

Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010







Sampling Location 1. Alkali Scrubber of Mancozeb Plant Reactor D-14

2. Water Scrubber of Wet Spray Dryer of Mancozeb Plant

3. Bag Filter of RVDF of Mancozeb Plant

Sample Quantity/Packing 1 X 1 No. Thimble


10.01.2012




16.01.2012

Stack No. 1 2 3

Stack attached to Alkali Scrubber of Mancozeb Plant Reactor D-14 New EDA Scruber

Water Scrubber of Wet Spray Dryer of Mancozeb Plant

Bag Filter of RVDF of Mancozeb Plant

Material of construction S.S. M.S. M.S.




Type of fuel Process Scrubber Process Stack Process Stack


Flue gas Velocity (m/sec) In 8.7 In

Total gas quantity (Nm3/hr) Operation 72143 Operation


Method Reference

Particulate Matter

mg/Nm3 -- 18.6 -- 20 IS 11255 (Part 1):1985 RA-2003 Hydrogen Sulphide (H2S)

mg/Nm3 -- -- -- 45 IS 11255 (Part 4):1985 RA-2003 Carbon Di-Sulphide (CS2)

mg/Nm3 -- -- -- 180 IS 11255 (Part 4):1985 RA -2003





Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010









Date of Sampling 20.01.2012 Date of Receipt of Sample 24.01.2012


Date of Start of Analysis 24.01.2012

Date of Completion of Analysis 28.01.2012

Stack No. 1 2


















Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010














Date of Completion of Analysis

28.01.2012

Stack No. 1 2 3 4

Stack attached to









Type of fuel Process Scrubber

Process Scrubber

Process Scrubber

Process Scrubber





Method Reference



3 6.3 4.8 -- 11.3 20






Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010







Sampling Location 1. Alkali Scrubber of Mancozeb Plant Reactor D-14

2. Water Scrubber of Wet Spray Dryer of Mancozeb Plant

3. Bag Filter of RVDF of Mancozeb Plant

Sample Quantity/Packing 50 ml X 2 No. PVC Bottle




Date of Completion of Analysis

28.01.2012

Stack No. 1 2 3

Stack attached to Alkali Scrubber of Mancozeb Plant Reactor D-14 New EDA Scruber

Water Scrubber of Wet Spray Dryer of Mancozeb Plant

Bag Filter of RVDF of Mancozeb Plant

Material of construction S.S. M.S. M.S.




Type of fuel Process Scrubber Process Stack Process Stack

Flue gas Temperature (0C) 28 Not Not

Flue gas Velocity (m/sec) -- In In

Total gas quantity (Nm3/hr) -- Operation Operation


Method Reference

Particulate Matter

mg/Nm3 -- -- -- 20 IS 11255 (Part 1):1985 RA-2003 Hydrogen Sulphide (H2S)

mg/Nm3 BDL -- -- 45 IS 11255 (Part 4):1985 RA-2003 Carbon Di-Sulphide (CS2)

mg/Nm3 169 -- -- 180 IS 11255 (Part 4):1985 RA -2003





Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010














Stack No. 1 2 3

Stack attached to









Scrubber Process

Scrubber





Method Reference



3 -- -- -- 25 IS 11255 (Part 7):2005



3 -- 6.4 -- 20





Note : 1. The result listed refers only to the tested sample(s) and applicable parameter(s). 2. This report is not to be reproduced except in full, without written approval of the laboratory

Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010







Stack Emission Sample Collected by Laboratory

Sampling Location







Sampling Procedure

As per IS: 11255



Stack No. 1 2 3

Stack attached to










Process Scrubber





Method Reference

Chlorine (Cl2) mg/Nm3 BDL BDL BDL 9 IS 5182 (Part 19):1982, RA 2003


3 6.2 7.2 13.8 20








Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010

Effluent Sample Analysis Report






Industrial Effluent/Grab

Sample Collectedby

Laboratory

Sampling Location ETP Outlet (Treated Effluent)


20 L X 1 No. PVC Can


07.02.2012

Sampling Procedure

IS:3025(Part I) 1987 RA1998



13.02.2012

Sr. No.

Parameters Unit Results GPCB LIMIT

Method Reference

1. pH - 7.45 5.5 to 8.5 APHA, 21st Ed., 2005, 4500 - H+

2. Temperature oC 26.0 40 oC IS 3025, Part 9:1983, RA 2002

3. Colour Hazen 65.0 100 APHA, 21st Ed., 2005, 2120 – B,C

4. Total Residual Chlorine

mg/L N.D 1.0 IS-3025, Part 26:1986, RA 2003 Eds 2.1(2004-02)

5. Total Dissolved Solids (TDS)

mg/L 9290 2100 APHA, 21st Ed., 2005, 2540 - C

6. Total Suspended Solids (TSS)

mg/L 45.0 100 APHA, 21st Ed., 2005, 2540 - D

7. Oil and Grease mg/L




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010

Report No. ME-BH-0362-120229-SA-UPL-5-JH Cont… 22. Copper as Cu mg/L < 0.03 2.0 APHA, 21st Ed., 2005, 3500-Cu - B

23. Chromium Hexavalent as Cr6+

mg/L < 0.02 0.1 APHA, 21st Ed., 2005, 3500-Cr - B

24. Total Chromium as Cr

mg/L < 0.02 2.0 APHA, 21st Ed., 2005, 3111 – B

25. Mercury as Hg mg/L < 0.0008 0.01 APHA, 21st Ed., 2005, 3112 – B

26. Arsenic as As mg/L 0.009 0.2 IS 3025, Part 37:1988, RA 2003

27. Cadmium as Cd mg/L 0.007 2.0 APHA, 21st Ed., 2005, 3111 – B

28. Total Heavy Metal mg/L < 2 7.0 By Calculation

29. Percentage Sodium (% Na)

% 90.9 60 MERI HANDBOOK

Remarks: N.D. – Not detected

.----------------------------------------------------------End------------------------------------------ for Mahabal Enviro Engineers Pvt. Ltd.

Harish Mendhi Technical Manager AUTHORISED SIGNATORY ---------------- ---------------------------------------------------------------------

Note: 1. The result listed refers only to the tested sample(s) and applicable parameter(s). 2. This report is not to be reproduced except in full, without written approval of the

laboratory.

Page 2 of 2




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010










17.02.2012




23.02.2012

Stack No. 1 2


















Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010











Date of Sampling

13.02.2012 Date of Receipt of Sample

17.02.2012

Sampling Procedure As per IS: 11255 and IS: 5182



23.02.2012

Stack No. 1 2 3 4

Stack attached to










Scrubber Process

Scrubber Process

Scrubber Process

Scrubber





Method Reference



3 8.4 4.8 -- 12.7 20






Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010











17.02.2012




23.02.2012

Stack No. 1 2 3

Stack attached to









Scrubber Process

Scrubber





Method Reference



3 -- -- -- 25 IS 11255 (Part 7):2005



3 -- 9.7 -- 20





Note : 1. The result listed refers only to the tested sample(s) and applicable parameter(s). 2. This report is not to be reproduced except in full, without written approval of the laborator

Page 1 of 1




QF / 5.10/1 – B Amend. No. 00 Dt. 01.08.2010







Sampling Location







17.02.2012

Sampling Procedure As per IS: 11255 and OSHA: 6402



23.02.2012

Stack No. 1 2 3

Stack attached to










Process Scrubber





Method Reference

Chlorine (Cl2) mg/Nm3 BDL BDL 1.6 9 IS 5182 (Part 19):1982, RA 2003


3 5.3 3.2 14.9 20







Note : 1. The result listed refers only to the tested sample(s) and applicable parameter(s). 2. This report is not to be reproduced except in full, w

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