ANNEXURE - Gujarat Pollution Control Board...M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd.,...

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M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.- Narmada, Gujarat Page 315 ANNEXURE - 10 List of Equipments & Machinery required for distillery unit. PLANT AND MACHINERY FOR DISTILLERY UNIT M/s. Shree Narmada Khand Udyog SahakariMandli Ltd, Dharikheda, Post- Nimbi, Tal- Rajpipla, Dist- Narmada has decided to install 45 KLPD Distillery plant based on fed batch / continuous fermentation system and MPR distillation to produce RS and AA. Alcohol Production 1) Rectified spirit conforming to Indian Standards 323/1959 (94.68 % v/v at 15.6 0 C) 2) Anhydrous alcohol conforming to Indian Standards IS: 15464 (2004) (99.50 % v/v at 15.6 0 C) 3) Impure alcohol 5 % during fuel alcohol production The impure alcohol is also marketable as such in the form of Ordinary denatured spirit. It can be disposed of by blending it with Grade –I, Rectified Spirit in a proportion, which will give Grade –II spirit. This can be sold as special denatured Industrial Alcohol. During the process of distillation, a by-product known as fusel oil separates out. It is a mixture of higher alcohol's. The production of fusel oil is in the range of 0.2 – 0.3 % of alcohol production depending upon quality of molasses and fermentation operations. DESCRIPTION- RS /Fuel Alcohol Production The process of converting molasses to RS can be divided into following sub sections: 1] Feed Preparation and weighing 2] Yeast Propagation and Fermentation 3] Multi-pressure Distillation 1] FEED PREPARATION AND WEIGHING Molasses Stored in a storage tank is first weighed in a tank with load cells so that accurate quantity can be fed to the fermentation section. The weighed molasses then transferred from tank to the dilutor in fermentation section where it is diluted with water and fed to the Fermenter. 2] YEAST PROPAGATION AND FERMENTATION The Yeast from Slant is transferred to Shaker Flasks and grown to the requiredvolume. This “genetically marked” yeast strain is then further propagated, under aseptic conditions, in yeast culture vessel. These vessels are equipped with eductors which are designed to achieve enhanced efficiencies through better sugar / yeast contact by shearing and mixing, efficient oxygen transfer etc. The ready yeast “seed” is then transferred from culture vessel to fermenter. The molasses is diluted by process water. The glucose in the Feed media gets converted to ethanol, in each of the 4 Fermenters operating in Batch mode. A plate heat exchanger and a circulation pump are provided to each fermenter, which will continuously recirculate the Fermenting Wash through PHE for maintaining the Fermenters at 30 deg C.

Transcript of ANNEXURE - Gujarat Pollution Control Board...M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd.,...

M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.- Narmada, Gujarat

Page 315

ANNEXURE - 10 List of Equipments & Machinery required for distill ery unit.

PLANT AND MACHINERY FOR DISTILLERY UNIT M/s. Shree Narmada Khand Udyog SahakariMandli Ltd, Dharikheda, Post- Nimbi, Tal- Rajpipla, Dist- Narmada has decided to install 45 KLPD Distillery plant based on fed batch / continuous fermentation system and MPR distillation to produce RS and AA. Alcohol Production 1) Rectified spirit conforming to Indian Standards 323/1959 (94.68 % v/v at 15.60C) 2) Anhydrous alcohol conforming to Indian Standards IS: 15464 (2004) (99.50 % v/v at 15.60C) 3) Impure alcohol 5 % during fuel alcohol production The impure alcohol is also marketable as such in the form of Ordinary denatured spirit. It can be disposed of by blending it with Grade –I, Rectified Spirit in a proportion, which will give Grade –II spirit. This can be sold as special denatured Industrial Alcohol. During the process of distillation, a by-product known as fusel oil separates out. It is a mixture of higher alcohol's. The production of fusel oil is in the range of 0.2 – 0.3 % of alcohol production depending upon quality of molasses and fermentation operations. DESCRIPTION- RS /Fuel Alcohol Production The process of converting molasses to RS can be divided into following sub sections: 1] Feed Preparation and weighing 2] Yeast Propagation and Fermentation 3] Multi-pressure Distillation 1] FEED PREPARATION AND WEIGHING Molasses Stored in a storage tank is first weighed in a tank with load cells so that accurate quantity can be fed to the fermentation section. The weighed molasses then transferred from tank to the dilutor in fermentation section where it is diluted with water and fed to the Fermenter. 2] YEAST PROPAGATION AND FERMENTATION The Yeast from Slant is transferred to Shaker Flasks and grown to the requiredvolume. This “genetically marked” yeast strain is then further propagated, under aseptic conditions, in yeast culture vessel. These vessels are equipped with eductors which are designed to achieve enhanced efficiencies through better sugar / yeast contact by shearing and mixing, efficient oxygen transfer etc. The ready yeast “seed” is then transferred from culture vessel to fermenter. The molasses is diluted by process water. The glucose in the Feed media gets converted to ethanol, in each of the 4 Fermenters operating in Batch mode. A plate heat exchanger and a circulation pump are provided to each fermenter, which will continuously recirculate the Fermenting Wash through PHE for maintaining the Fermenters at 30 deg C.

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The nutrients, biocide, acid and anti-foam agents are fed to the fermenters as per process requirement. The CO2 liberated during fermentation is sent to CO2 Scrubber for recovery of ethanol otherwise being lost in vent. The Fermented Wash is then sent to the Clarification Tank equipped with Lamella Separator. The settled sludge is sent to Sludge Washing Tank for recovery of alcohol. 3] MULTIPRESSURE DISTILLATION (RS) The fermented wash is fed to CO2 stripper column to remove CO2 gas present in wash. Alcohol is stripped off water in stripper column. The top vapors [alcohol + water] are fed to Calendria. Distillate from Calendria is fed to extraction column, The Make DM Water & Recycled Spent Lees from Second Rectifier is used as dilution water. In extraction column most of the high boiling impurities separate from ethanol in presence of water. The bottom ethanol water mixture is pre-heated before being fed to rectifier column. In rectifier column RS is taken out from top tray. The impure spirit from top of CO2 stripper column, rectifier column, fed to fusel oil column. The final impure spirit cut is taken out from the fusel oil column and partly alcohol is recycled to rectifier column. The alcohol containing fusel oil from rectifier column is fed to fusel oil column. Rectification column works under pressure. The CO2 stripper, stripping column, works under vacuum and fusel oil column works under atmospheric condition. The top vapours from rectifier column are condensed in Stripper Reboiler. The alcohol water vapours from stripping column are partly sent to CO2 stripper bottom for heating. The Rectifier column and fusel oil column gets heat from steam. The Distillation process is operated through PLC. 4] PROCESS DESCRIPTION FOR FA (DEHYDRATION – RS TO FA) Rectified Spirit at Azeotropic concentration is pumped by Feed Pump. This pumpcare of the entire backpressure of the system. The pump is in Stainless Steelmaterial of construction for wetted parts complete with flameproof motor andmechanical seal. The rectified spirit will first pass through feed Preheater, which will pass through vaporizer cum super heater which will convert the Rectified Spirit feed to superheated Alcohol vapour stream ready to feed to the Molecular Sieve bottles. The degree of superheat is control via a temperature control loop and the flow rate to the plant is control via flow control loop. The superheated vapours will pass through a Sieve bottle, which is already regenerated, and pressurize to working pressure via. a bleed flow from an operating sieve bottle. After the drying cycle the flow will be shifted to the next Sieve bottle, which is ready after duly regenerated and pressurize. This sequence minimizes the rate of rise and fall of pressure through the molecular sieve. Thus minimizing the attrition of the sieve beads. The sieve column after completion of drying cycle is evacuated to remove the adsorb water through an evacuation system via a condenser. The mixture of Alcohol and water is preheat by Anhydrous Alcohol Vapour in Plate Heat Exchanger before being feed to Recovery Column, which enriches the stream back to Azeotropic composition. The bottom of recovery column get heat from partly by condensing Anhydrous Alcohol Vapour in Plate Heat Exchanger the Anhydrous Alcohol vapours condensed in product cooler. A flow indicator indicates the rate of Anhydrous Alcohol going to the Anhydrous Alcohol receivers. Technical Specifications for 45 KLPD Distillery Plant I) Fermentation Section: It is proposed to have four-fermenter (SS-304) system with facility to empty and clean fermenters on-line (without stoppages). This would require molasses feeding facility to all fermenters with necessary magflow meters (4 Nos.) for molasses & rotameters (4Nos.) for process water.

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Sr. Description Specification

No.

1. MOLASSES DAY TANK 250 MT

2. MOLASSES RECEIVING TANK

Capacity 2.0 M3

Material of construction MS

Quantity 1 No.

3. MOLASSES TRANSFER PUMP FROM DAY RECEIVING TANK

Capacity, Ton/hr 10

Quantity (No) 1 W + 1 SB

Head (MWC) 35

Material of construction CI / CS

(Body/Wetted part)

Type Gear/Screw

4. MOLASSES FILTERS

Quantity 2 sets

Specification MS with SS internals

5. AUTOMATIC MOLASSES WEIGHING SYSTEM WITH TANKS, LOAD CELLS

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Quantity 1 No. Specification 10 Ton per hour WEIGHING TANK (Molasses receiving tank) Capacity 2 MT/ trip Material of Construction MS epoxy WEIGHED MOLASSES TANK Capacity 50 M3 Material of Construction MS epoxy 6. WEIGHED MOLASSES TRANSFER PUMP

Capacity, Ton/hr 10 Quantity (No) 1 W + 1 SB Head (MWC) 35 Material of construction CI / CS (Body/Wetted part) Type Gear/Screw 7. PROCESS MOLASSES MAGNETIC FLOW METER WITH TOTALISER

Specification Suitable for 45 KL Fermentation

8. BIO-CULTURE DEVLOPMENT SECTION CONSISTING OF SERIES OF VESSELS

WITH INCREASING VOLUMES

(Vessel consists of sterilization, cooling arrangement, air sparging facility with all necessary connections for Air, Acid, Nutrients, Necessary fitting and agitators system, sight & light glass assembly etc.) Type Vertical/Cylindrical Material of construction SS-304 Capacity a) Vessel-I 0.30 M3 b) Vessel-II 2.00 M3 c) Vessel-III 10.00 M3 9. MOLASSES DILUTER FOR YEAST VESSELS

Type Static Mixer MOC SS – 304 Quantity 1+1 No. 10. BIO-CULTURE TRANSFER PUMP

(Cell Mass Transfer Pump) Capacity M3 / hr 10 Quantity (No) 1 W + 1 SB Head (MWC) 15 Material of construction Casing and impeller SS-304

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12. MOLASSES BROTH MIXER FOR FERMENTER

Type Static Mixer MOC SS – 304 Quantity 4 No.

13. YEAST ACTIVATION TANKS Quantity 2 Nos. Type Vertical / Cylindrical Material of construction SS 304 Capacity 50 M

3

14. MOLASSES BROTH MIXER FOR YEAST ACTIVATION VESSEL Type Static Mixer MOC SS – 304 Quantity 1 No

15. YEAST ACTIVATION VESSEL TRANSFER PUMP WITH MOTOR Capacity m3/hr 10 M

3

Quantity (No) 1 W + 1 SB Material of construction Casing and impeller SS-304 Type Centrifugal

16. YEAST ACTIVATION COOLERS PLATE HEAT EXCHANGERS Quantity 1 Nos. Type Plate Heat Exchanger (PHE) Material of construction SS-316 plate with EDPM Gasket with 10 % additional plate for spare

17. WASH HOLDING TANK (Clarified wash tank) Quantity 1 Nos. Type Vertical/Cylindrical Material of construction MS EPOXY Capacity 80 M

3

18. DISTILLATION FEED PUMP (Clarified Wash Transfer Pump) Capacity m

3/hr 30

Quantity (No) 1 W + 1 SB Head (MWC) 35 Material of construction Casing and impeller SS-304 Type Centrifugal

19. FERMENTED WASH COOLERS PLATE HEAT EXCHANGERS

Type Centrifugal

11. CONTINUOUS MIXED BIO-REACTORS (FERMENTORS) with air sparger, agitator,

sight and light glass, manholes, level indicators, mechanical pressure relief device & other

necessary fittings & nozzles Quantity 4 Nos. Capacity 290 M3 each Type Vertical/Cylindrical with slopping bottom Material of construction SS-304 Minimum Thickness 4 mm

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Quantity 4 Nos. Type Plate Heat Exchanger (PHE) Material of construction SS-316 plate with EDPM Gasket with 10 % additional plate for spare

20. FERMENTED WASH RECIRCUALTION PUMPS Material of construction With SS-304 Internals Capacity m3/hr 120 Quantity (No) 4 W + 1 SB Head (MWC) 15 Type Centrifugal 21. AIR SPARGING ASSEMBLY FOR VESSELS & FERMENTORS

Quantity 6 Nos. Material of Construction SS-304 22. WASH SETTLING TANK

Capacity 150 M3

Type Cylindrical shell with conical top and slopping bottom MOC MS Epoxy 23. SLUDGE SETTLING TANK

Quantity 1 Nos. Type Vertical/Cylindrical Material of construction SS-304 Capacity 30 M

3

24. SLUDEG MIXING TROUGH

Capacity m3 2

Quantity (No) 1 No. Material of construction MS 25. SLUDGE TRANSFER PUMP

Capacity m3/hr 2

Quantity (No) 1 W + 1 SB Head (MWC) 25 Material of construction Casing and impeller SS-316 Type Centrifugal 26. AIR BLOWER

Capacity N M3/Hr Suitable for 40 KL plant

Quantity (No) 1 W + 1 SB Material of construction CI Type Water Ring 27. AIR FILTER

Quantity 1 Nos. Type HEPA, CS Frame 28. NUTRIENT TANK

Quantity 1 No. Type Vertical/Cylindrical

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Material of construction SS-304 Capacity 2 M

3

29. NUTRIENT PUMP

Capacity m3/hr 1

Quantity (No) 1 W + 1 SB Head (MWC) 15 Material of construction With SS- 304 Internals Type Centrifugal 30 BIOCIDE TANK

Quantity 1 No. Type Vertical/Cylindrical Material of construction SS-304 Capacity 1 M

3

31 BIOCIDE PUMP

Capacity m3/hr 1

Quantity (No) 1 W + 1 SB Head (MWC) 15 Material of construction With SS- 304 Internals Type Centrifugal

32 DEFOAM TANK Quantity 1 No. Type Vertical/Cylindrical Material of construction SS-304 Capacity 1 M

3

33 DEFOAM PUMP

Capacity m3/hr 1

Quantity (No) 1 W + 1 SB Head (MWC) 15 Material of construction CI / CS (Gear Pump) Type Gear

34 ACID TANK

Quantity 1 No. Type Vertical/Cylindrical Material of construction Carbon steel with FRP Capacity 1 M

3

35 ACID PUMP

Capacity m3/hr 2

Quantity (No) 1 W + 1 SB Head (MWC) 15 Material of construction Alloy 20

36 ALCOHOL VAPORS RECOVERY COLUMN (CO2 Scrubber) Diameter 690 mm No. of trays 3 Nos.

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Material SS-304 Quantity 1 No.

37 WATER HEADER Material - MS Quantity – 1 No.

38 AIR HEADER Material – MS Quantity – 1 No.

39 CO2 HEADER Material – MS Quantity – 1 No.

40 SAFETY SYSTEM FOR FERMENTER Type Cylindrical / Vertical and Mechanical Safety valve Material SS -304 Quantity 4 Nos. 41 CIP SOLUTION TANK

Volume: 10 M3

Material : SS -304 Type : Vertical / Cylindrical Quantity : 1 No. 42 PROCESS WATER PUMP

Capacity m3/hr Suitable for 40 KLPD distillery

Quantity (No) 1 W + 1 SB Head (MWC) 25 Material of construction Casing CI and impeller SS- 316 Type Centrifugal 43 CIP SOLUTION PUMP

Capacity m3/hr 10

Quantity (No) 1 W + 1 SB Head (MWC) 35 44 CONC. ACID TANK

Quantity 1 No. (Vertical/Cylindrical) Material of construction Carbon steel Capacity 3.7 M

3

45 YEAST CREAM TREATMENT TANK Quantity 1 No. (Vertical/Cylindrical) Material of construction SS-304 Capacity 2 M

3

46 Decanter for Post clarification 1 Nos.

Note – All pumps should be provided with double mechanical seal. The pumps in Distillation Section shall be provided with flameproof motors. CIP tank with pumps (1+1Nos.) in fermentation is considered with a view to clean PHE of fermenters/pre-

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fermenters in place from time to time. II) Distillation Section: (Distillation Section–Multi-pressure Distillation System (R.S. Production)

A Columns

Sr. Particulars M.O.C. Qty.

No.

1. Analyzer column SS - 304 1 No.

2. Degasifying column SS – 304 1 No.

3. Aldehyde Column/ Pre-rectifier SS – 304 1 No.

4. Rectifying column R.S. zone D.O. Cu 1 No.

cum exhaust & F.O. zone in SS-304

5. Fusel oil column SS – 304 1 No.

B Condensers/Reboilers/Coolers

Sr. Particulars M.O.C. Qty.

No.

1 Rectifier PCV condenser SS-304 1 No.

2 Rectifier vent condenser SS-304 1 No.

3 Degasifying condenser SS-304 1 No.

Pre-rectifier condenser-I SS-304 1 No.

5 Pre-rectifier condenser -II SS-304 1 No.

6 Pre-rectifier vent condenser SS-304 1 No.

7 FOC condenser I SS-304 1 No.

8 FOC condenser II SS-304 1 No.

9 Alcohol Cooler/product cooler D.O.Cu 1 No.

10 Impure spirit cooler SS-304 1 No.

11 Weak alcohol heater D.O.Cu 1 No.

12 Fusel oil cooler SS-304 2 No.

13 a) Analyzer column reboiler SS-304 1+1No.

b) Analyser reboiler vent condenser SS-304 1 No.

14 Pre- Rectifier (Stripper) column re- SS- 304 1 No.

boiler

15 Rectifier cum exhaust column re- SS- 304 1 No.

boiler

16 FOC column re-boiler SS- 304 1 No.

17 Vent scrubber heat exchanger SS-304 1 No.

C. Miscellaneous

Sr. Particulars M.O.C. Qty.

No.

1 Degasifying Tank SS-304 1 No.

2 Fusel oil De-canter with sight and SS-304 2Nos.

light glass and water sparger

3 Plate heat exchangers SS- 316

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1. F. Wash heater 2 Nos.

2. Rectifier feed heater 1 No.

3. Spentwash cooler 1 No.

4 Jet mixer SS-304 1 No.

5 Hot water tank (Collection tank) M.S. 1 No.

6 Condensate pot MS 1 No.

7 Steam Chest MS 1 No.

With safety valve gauge, glass drain, As per IBR.

and inlet—outlet steam valve,

manhole etc.

8 Fusel oil washing tank SS-304 1 No.

9 Fusel oil collection tank SS-304 1 No.

10 Analyzer flash tank SS-304 1 No.

11 Pre-rectifier draw tank. SS-304 1 No.

12 Rectifier reflux tank SS-304 1 No.

13 HCC bottom equalization tank SS-304 1 No.

14 Water Header M.S. 1 No.

15 Over head water tank M.S. 1 No.

16 IS feed tank SS-304 1 No.

17 Vapour /liquid separator SS-304 2 No.

18 Spent wash/ SS-304 Specify

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Spentless siphon 19 FOC feed preheater SS-304 1 No. 20 Seal pot SS-304 1 No.

Tank farm Receivers & Storage Tanks for Rectified spirit

Sr.

Particulars Working

MOC Qty

No. Capacity

1 Rectified spirit receivers 50 M3 MS 3 Nos.

2 Impure spirit receivers 10 M3 MS 3 Nos.

3 Rectified spirit storage tank 500 M3 MS 3 Nos.

4 Impure spirit storage tank 100 M3 MS 1 No.

5 Fusel oil storage tank 10 M3 MS 1 No.

Flow meter with Totalizer for issue to be

2 Nos.

6 (One for R.S. (Pure) and one for

approved by Weight & Measure Dept.

IS/TA)

J. Pumps with flameproof motor & double mechanical seal

Sr. Particulars M.O.C. Qty.

No.

1. R.S. pump (From receiver to storage tank to SS -304 1+1 Nos

issue)

2. I.S./TA pump (From receiver to storage tank SS -304 1+1 Nos.

to issue)

3. Fusel oil feed pump (from storage tank to SS -304

1+1 Nos.

issue)

IV) Technical Specifications for 45 KLPD Anhydrous Alcohol plant (MSDH SYSTEM)

Sr. Equipment Name Specifications

No.

1. Absorber bed with packing and MOC- SS-304

internals- 2 to 3 Nos. Qty.-2-3Nos.

2. Regeneration Column MOC- SS-304

Quantity –1No.

3. Regeneration Column Reboiler MOC- SS-304

Quantity –1No.

4. Feed Preheater MOC- SS-304

Quantity –1No.

5. Regeneration Pre-heater MOC- SS-304

Quantity –1No.

6. Product Condenser MOC- SS-304

Quantity –1No.

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7. Product Cooler MOC- SS-304

Quantity –1No.

8. Regeneration Condenser MOC- SS-304

Quantity –1No.

9. Regenerating Cooler MOC- SS-304

Quantity –1No.

10. Super heater MOC- SS-304

Quantity –1No.

11. Regeneration Drum MOC-SS-304

Qty.-1No.

12. Vacuum eductor Pumps- Pump- MOC-Water ring type

1+1 Nos. Quantity -1+1 Nos.

Water ring type with

flame-proof motors/starter/push

button

13. Feed Pumps with flame-proof MOC-SS-304Quantity. -2Nos

motors/starter/push button

14. Regeneration Pumps with flame MOC-SS-304

proof motors/Starter/push button Quantity.-2Nos

15. Product Storage Pumps with MOC-SS-304

flame proof motors/Starter/push

Quantity.-2Nos

button

16 Rectified Spirit Receiving Tank MOC-MS

with vent condenser, flame Quantity-1No.

arrester & L.T.

Material of construction -MS

Capacity-1.0Lac Lits.

Thickness- Shell/Bottom/Top-

8/8/6mm

17. Flow meters with totalizers 1No.

18. Piping valves & Instrumentation

a. Piping

Alcohol

Water

Steam

b. Valves

Alcohol

Water

Steam

19. Instrumentation: -

As per the process requirement, necessary No. Of Flow meters, Rotameters,

Electronic Temperature Indicators, Level indicators, Pressure gauges & SYKES

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Hydrometers, Thermometers etc. should be supplied with necessary instrument

board along with airtight chamber with A.C. room for instrument panel (details

of each instrument should be submitted)

20. Supply of Electrical Material such as cables, starters push button:- Electrical

Motors – Kirloskar/ Siemens make, Starters/Button –

21. a) Cooling Tower Make-Paharpur

MOC-Wooden

Quantity -1No.

b) Water circulation pump with Make –KSB/Flow Serve

motor Type -Centrifugal

MOC –CI

22. Pump for makeup Water for Included in R.S. plant

cooling tower with Motor/Starter/

push bottom etc.

23. Water softening plant for cooling Included in R.S. plant

tower make up along with feed

pump – motor/starter/push button

etc.

24. Instrument air compressor Included in R.S. plant

25. Motor control center Included in R.S. plant

26. Water Chilling plant with MOC -To be specified

compressor pump

Quantity –1No.

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27. PC with printer 1No.

28. Software package for SCADA & 1No.

control loops in detail

29. Air dryer Heatless air dryer with filters –1No.

30. Rectifier Condenser outlet PHE Cap-2.1 M3/hr

Quantity. -1No.

Receivers & Storage Tanks for Anhydrous Alcohol

Sr. No. Title MOC

Receivers

1 Absolute Alcohol Receivers – 3 Nos. (Cap. 50 M3, each) MS

Thickness -Shell/Bottom/Top - 8 / 8 / 6 mm

2 Rectified Spirit feed tanks - 1Nos. (Cap. 150 M3) MS

Thickness -Shell/Bottom/Top - 10 / 8 / 6 mm

Storage Tanks

3 Absolute Alcohol Storage Tank – 3 No., (Cap. 500 M3) MS

Thickness -Shell/Bottom/Top – 10 / 8 / 6 mm

4 Fire Arresters for Absolute Storage tank - 2 Nos.

5 Moisture traps for Receivers & Storage tanks– 5Nos.

Flame proof pumps - Receivers & Storage tanks for Anhydrous Alcohol

1. Anhydrous Alcohol pump Type: Centrifugal

(From receiver to storage tank) MOC- SS-304 Capacity – To be specified Head MLC -To be specified Motor KW –To be specified Quantity – 1+1Nos.

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Annexure - 11

Toposheet

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Annexure - 12 Meteorological Data

1. Average Hourly Met Data

Wind Direction (degree) Wind Speed (m/sec) Temp.

(0K)

Satbility

Class

Mixing Height

(M)

1 45 1.01 291.1 6 300

2 45 2.2 290 6 250

3 45 1.49 290.6 6 200

4 1.5 2.4 289.4 6 150

5 1.5 1.4 287.1 5 100

6 270 1.2 290 5 50

7 45 1.6 292.9 5 100

8 337.5 2.3 295.6 4 400

9 45 2.4 300.2 4 500

10 270 1.2 301.2 3 800

11 45 1.1 303.6 2 1200

12 315 1.4 305.4 2 1200

13 45 1.7 305.1 1 1100

14 315 2.88 304.6 1 1100

15 1 1.9 304.2 2 1000

16 225 1.6 303.8 2 900

17 45 1.9 303.1 3 500

18 45 2.8 301.6 4 500

19 22.5 1.1 300.7 5 450

20 337.5 1 299.8 5 400

21 1 1.5 297.5 5 350

22 337.5 0.6 296.4 6 300

23 1 1.2 293 6 300

24 360 1 292.4 6 300

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2. Hourly Met data for the Study Period (October 2017 to December 2017)

Date Time Air Temperature RH Wind Speed

Wind Dir.

DD/MM/YYYY HH:MM °C % mtrs/sec °

01-10-17 0:59 16.53 23.52 0 255

01-10-17 1:59 16.02 24.57 0.28 45

01-10-17 2:59 14.52 27.16 0.86 163

01-10-17 3:59 12.64 30.65 1.26 93

01-10-17 4:59 12.31 31.98 1.75 134

01-10-17 5:59 11.76 33.83 1.07 153

01-10-17 6:59 11.8 38.04 0.54 162

01-10-17 7:59 14.66 29.73 1.1 0

01-10-17 8:59 19.93 14.92 3.03 237

01-10-17 9:59 22.55 20.3 2.05 0

01-10-17 10:59 24.46 19.97 2.68 272

01-10-17 11:59 26.76 18.79 3.4 45

01-10-17 12:59 27.79 15.8 6.43 0

01-10-17 13:59 28.64 14.59 6.22 270

01-10-17 14:59 29.17 13.17 6.27 270

01-10-17 15:59 29.42 13.55 5.82 274

01-10-17 16:59 29.15 14.5 0 284

01-10-17 17:59 28.44 15.72 5.26 301

01-10-17 18:59 27.39 16.92 4.47 292

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21-11-17 18:59 30.46 14.05 3.54 265 21-11-17 19:59 28.53 16.52 2 208 21-11-17 20:59 26.14 20.85 0.49 45 21-11-17 21:59 24.56 23.83 0.14 0 21-11-17 22:59 23.1 26.29 0.35 0 21-11-17 23:59 21.93 29.19 1.07 0 22-11-17 0:59 21.29 30.89 3.05 1 22-11-17 1:59 20.73 33.36 3.1 215 22-11-17 2:59 20.95 37.48 3.38 45 22-11-17 3:59 20.3 43.98 4.75 215 22-11-17 4:59 20.32 47.6 0 237 22-11-17 5:59 18.99 53.2 0 236 22-11-17 6:59 18.85 55.68 0 235 22-11-17 7:59 20.48 53.24 5.85 0 22-11-17 8:59 22.42 48 5.1 0 22-11-17 9:59 24.01 40.89 0 286 22-11-17 10:59 25.65 33.76 3.59 308 22-11-17 11:59 27.12 30.43 0 284 22-11-17 12:59 27.94 29.04 0 0 22-11-17 13:59 29.02 24.92 1.21 276 22-11-17 14:59 29.77 24.35 2.49 313 22-11-17 15:59 30.21 22.34 2.98 45 22-11-17 16:59 30.24 22.48 0.3 94 22-11-17 17:59 29.81 23.22 0 174 22-11-17 18:59 28.97 25.03 0 236 22-11-17 19:59 27.78 24.3 0 232 22-11-17 20:59 25.94 27.06 0 262 22-11-17 21:59 24.66 30.58 1.05 291 22-11-17 22:59 24.49 27.93 1.68 291 22-11-17 23:59 23.79 23.32 0.75 0 23-11-17 0:59 22.83 24.85 1.75 120 23-11-17 1:59 21.35 28.13 3.29 114 23-11-17 2:59 19.52 32.77 3.38 151 23-11-17 3:59 17.66 38.69 2.68 45 23-11-17 4:59 16.66 41.95 3.91 204 23-11-17 5:59 16.22 44.97 2.96 200 23-11-17 6:59 16.59 44.39 0 197 23-11-17 7:59 19.47 35.59 0 256 23-11-17 8:59 23.02 29.93 3.54 228 23-11-17 9:59 25.57 25.17 0 223 23-11-17 10:59 26.93 22.79 0.91 258 23-11-17 11:59 29 18.99 0.63 171

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23-11-17 12:59 30.47 15.03 0.05 157 23-11-17 13:59 31.17 13.8 0.47 1 23-11-17 14:59 31.95 22.18 3.47 132 23-11-17 15:59 31.78 29.3 3.31 36 23-11-17 16:59 31.78 22.18 3.31 61 23-11-17 17:59 31.66 13.24 2.78 76 23-11-17 18:59 30.88 15.06 2.54 97 23-11-17 19:59 29.17 18.4 2.33 111 23-11-17 20:59 27.13 21.88 1.38 115 23-11-17 21:59 25.51 26.8 0 145 23-11-17 22:59 23.81 29.07 0.72 215 23-11-17 23:59 24.39 21.67 2.26 0 24-11-17 0:59 23.36 21.37 2.29 229 24-11-17 1:59 22.18 22.65 2.08 276 24-11-17 2:59 20.99 24.25 2.26 1 24-11-17 3:59 20.31 24.99 3.03 227 24-11-17 4:59 19.29 26.65 3.59 161 24-11-17 5:59 18.62 28.1 4.17 45 24-11-17 6:59 18 30.88 0 223 24-11-17 7:59 20.18 29.56 3.4 45 24-11-17 8:59 22.61 28.94 3.52 45 24-11-17 9:59 25.98 24.39 2.61 290 24-11-17 10:59 28.22 21.49 0.84 0 24-11-17 11:59 30.21 18.75 0.12 24 24-11-17 12:59 31.39 15.41 0.21 134 24-11-17 13:59 32.4 22.18 0.09 130 24-11-17 14:59 32.83 23.1 0.68 171 24-11-17 15:59 32.91 22.18 0 271 24-11-17 16:59 33.24 22.18 0.23 123 24-11-17 17:59 32.44 28.5 0.07 152 24-11-17 18:59 31.57 22.18 1.52 162 24-11-17 19:59 29.43 23 1.17 128 24-11-17 20:59 28.02 22.18 0.68 154 24-11-17 21:59 26.79 20.4 0 155 24-11-17 22:59 24.77 15.87 1.75 45 24-11-17 23:59 22.57 18.63 0 224 25-11-17 0:59 20.82 22.18 3.86 215 25-11-17 1:59 19.68 24.22 4.14 45 25-11-17 2:59 18.31 27.21 5.24 205 25-11-17 3:59 18.06 27.42 5.87 45 25-11-17 4:59 18.84 25.2 0 221 25-11-17 5:59 17.59 27.87 5.36 45

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25-11-17 6:59 17.37 29.88 5.47 227 25-11-17 7:59 20.14 35.02 0 234 25-11-17 8:59 23.57 40.4 0 235 25-11-17 9:59 26.15 35.76 0 224 25-11-17 10:59 28.54 29.65 2.24 218 25-11-17 11:59 30.42 22.88 0.14 203 25-11-17 12:59 31.86 18.53 0.35 204 25-11-17 13:59 32.88 14.48 0 221 25-11-17 14:59 33.41 13.28 4.7 231 25-11-17 15:59 33.72 23.18 0 237 25-11-17 16:59 33.94 23.18 0 237 25-11-17 17:59 33.25 13.44 5.12 230 25-11-17 18:59 32.54 15.09 4.07 228 25-11-17 19:59 30.5 17.06 0 222 25-11-17 20:59 27.65 20.67 0 219 25-11-17 21:59 25.7 24.97 3.22 228 25-11-17 22:59 26.04 26.17 4.96 228 25-11-17 23:59 26.27 27.49 6.22 230 26-11-17 0:59 25.53 28.79 6.62 0 26-11-17 1:59 24.35 33.47 5.96 45 26-11-17 2:59 22.99 42.33 5.57 264 26-11-17 3:59 21.76 47.79 6.61 45 26-11-17 4:59 20.78 50.3 0 257 26-11-17 5:59 19.96 51.64 0 259 26-11-17 6:59 19.64 52.55 0 45 26-11-17 7:59 20.23 50.76 0 0 26-11-17 8:59 21.63 46.43 0 258 26-11-17 9:59 23.94 38.91 0 45 26-11-17 10:59 26.11 33.07 6.85 228 26-11-17 11:59 28.18 28.17 6.83 45 26-11-17 12:59 30.05 22.3 0 231 26-11-17 13:59 31.97 15.64 6.78 231 26-11-17 14:59 32.54 13.23 6.29 0 26-11-17 15:59 32.98 23.18 5.78 0 26-11-17 16:59 32.84 25.7 4.84 259 26-11-17 17:59 32.24 23.18 4.33 0 26-11-17 18:59 31.32 23.18 3.03 230 26-11-17 19:59 30.26 14.6 1.87 215 26-11-17 20:59 29.15 13.86 3.1 216 26-11-17 21:59 27.97 17.03 0 221 26-11-17 22:59 26.76 20.43 3.68 231 26-11-17 23:59 25.36 22.58 4.26 0

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27-11-17 0:59 23.81 25.64 4.01 45 27-11-17 1:59 22.25 29.41 3.52 45 27-11-17 2:59 20.93 33.19 3.1 236 27-11-17 3:59 19.45 35.85 3.29 218 27-11-17 4:59 17.63 38.72 0 329 27-11-17 5:59 17.04 39.98 0 327 27-11-17 6:59 16.67 40.26 4.21 261 27-11-17 7:59 18.12 42.82 4.87 266 27-11-17 8:59 19.17 46.05 5.05 292 27-11-17 9:59 20.92 45.01 4.45 306 27-11-17 10:59 23.08 37.94 1.17 301 27-11-17 11:59 25.14 33.26 0 308 27-11-17 12:59 26.91 30.39 0.26 275 27-11-17 13:59 28.76 21.04 0.49 63 27-11-17 14:59 30.23 14.96 1.75 91 27-11-17 15:59 30.84 13.52 1.24 70 27-11-17 16:59 31.21 23.18 0 45 27-11-17 17:59 30.66 23.18 0.49 109 27-11-17 18:59 29.95 23.18 0.44 163 27-11-17 19:59 28.37 14.32 1.38 131 27-11-17 20:59 26.45 15.83 1.35 107 27-11-17 21:59 25.09 17.84 1.84 308 27-11-17 22:59 22.77 21.03 2.52 130 27-11-17 23:59 22.53 18.97 2.47 69 28-11-17 0:59 21.31 19.65 1.54 68 28-11-17 1:59 19.22 23.6 1.38 1 28-11-17 2:59 17.67 27.07 2.59 45 28-11-17 3:59 16.91 27.82 4.31 270 28-11-17 4:59 16.99 26.93 4.63 45 28-11-17 5:59 16.51 28.6 6.24 274 28-11-17 6:59 17.12 28.45 0 222 28-11-17 7:59 19.61 25.74 5.68 294 28-11-17 8:59 23.43 20.12 5.26 263 28-11-17 9:59 27.07 15.44 0 286 28-11-17 10:59 29.62 14.4 2.26 292 28-11-17 11:59 30.31 23.18 0.28 45 28-11-17 12:59 31.05 23.18 0.54 45 28-11-17 13:59 32.01 23.18 2.56 175 28-11-17 14:59 32.38 23.18 4.12 104 28-11-17 15:59 32.56 23.18 3.17 76 28-11-17 16:59 32.46 23.18 3.89 107 28-11-17 17:59 32.03 23.18 0 145

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28-11-17 18:59 31.21 23.18 2.43 110 28-11-17 19:59 29.68 13.93 1.56 134 28-11-17 20:59 27.27 16.75 1.52 99 28-11-17 21:59 25.95 18.7 0.75 272 28-11-17 22:59 26.07 18.44 1.38 291 28-11-17 23:59 25.78 16.9 3.42 271 29-11-17 0:59 24.24 19.28 4.33 287 29-11-17 1:59 23.52 20.57 4.96 288 29-11-17 2:59 22.67 20.94 0 277 29-11-17 3:59 22.46 21.65 6.03 262 29-11-17 4:59 20.87 24.81 4.56 288 29-11-17 5:59 18.78 27.52 4.96 237 29-11-17 6:59 17.91 30.3 5.82 296 29-11-17 7:59 20.8 27 4.75 291 29-11-17 8:59 24.2 22.82 0 277 29-11-17 9:59 27.13 21.77 2.91 299 29-11-17 10:59 29.57 16.66 0 284 29-11-17 11:59 30.84 14.24 0.07 256 29-11-17 12:59 32.06 23.18 0 221 29-11-17 13:59 32.49 23.18 0.37 215 29-11-17 14:59 33.44 24.8 0.47 203 29-11-17 15:59 33.57 23.18 0.65 1 29-11-17 16:59 33.43 26.3 0 223 29-11-17 17:59 33.26 23.18 0 222 29-11-17 18:59 32.62 23.18 4.89 45 29-11-17 19:59 30.93 23.18 4.68 237 29-11-17 20:59 28.27 13.41 2.94 236 29-11-17 21:59 25.94 15.41 2.5 231 29-11-17 22:59 24.84 16.78 3.03 215 29-11-17 23:59 24.09 18.36 4 0 30-11-17 0:59 22.57 21.38 4.82 0 30-11-17 1:59 22.5 30.13 5.03 45 30-11-17 2:59 22.79 37 6.45 235 30-11-17 3:59 22.27 46.24 6.52 45 30-11-17 4:59 21.26 53.2 6.34 0 30-11-17 5:59 19.98 57.66 0 221 30-11-17 6:59 19.34 58.46 5.8 45 30-11-17 7:59 20.6 52.98 4.52 258 30-11-17 8:59 23.12 41.06 0 286 30-11-17 9:59 25.94 31.7 3.36 45 30-11-17 10:59 28.9 25.69 0 219 30-11-17 11:59 31.19 17.5 1.82 215

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30-11-17 12:59 32.74 13.86 0 223 30-11-17 13:59 33.55 23.18 1.91 204 30-11-17 14:59 34.33 23.18 0 222 30-11-17 15:59 34.71 29.8 3.03 235 30-11-17 16:59 34.67 23.18 0 221 30-11-17 17:59 34.4 23.18 2.05 232 30-11-17 18:59 33.69 23.18 1.49 234 30-11-17 19:59 31.07 23.18 1.96 0 30-11-17 20:59 28.59 14.49 2.75 45 30-11-17 21:59 26.92 17.06 2.94 275 30-11-17 22:59 25.4 19.93 3.75 273 30-11-17 23:59 24.21 22.3 4.98 0 01-12-17 0:59 23.04 24.82 4.94 237 01-12-17 1:59 21.44 28.26 0 220 01-12-17 2:59 20.29 31.49 0 45 01-12-17 3:59 19.43 35.54 0 235 01-12-17 4:59 19.17 43.66 0 45 01-12-17 5:59 18.84 53.24 0 0 01-12-17 6:59 18.41 57.98 0 0 01-12-17 7:59 19.51 56.86 6.2 45 01-12-17 8:59 21.76 49.34 5.85 237 01-12-17 9:59 24.56 37.46 5.43 45 01-12-17 10:59 27.9 26.03 2.87 234 01-12-17 11:59 30.46 19.73 0 221 01-12-17 12:59 31.54 15.76 1.82 208 01-12-17 13:59 32.83 16.4 2.5 206 01-12-17 14:59 33.48 23.18 3.36 45 01-12-17 15:59 33.53 23.18 0 220 01-12-17 16:59 33.52 20.1 0 223 01-12-17 17:59 33.48 23.18 0 219 01-12-17 18:59 32.56 23.18 4.68 233 01-12-17 19:59 30.47 23.18 3.96 231 01-12-17 20:59 27.64 13.41 3.75 231 01-12-17 21:59 25.06 16.59 3.26 233 01-12-17 22:59 24.14 18.41 5.52 45 01-12-17 23:59 23.84 19.7 6.71 230 02-12-17 0:59 23.05 21.78 0 231 02-12-17 1:59 21.72 24.24 0 236 02-12-17 2:59 21.05 28.09 0 223 02-12-17 3:59 20.54 35.18 0 229 02-12-17 4:59 19.4 44.46 0 236 02-12-17 5:59 18.46 56.15 0 221

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02-12-17 6:59 18.26 59.42 0 224 02-12-17 7:59 19.94 50.04 0 232 02-12-17 8:59 23.28 33.91 6.92 237 02-12-17 9:59 26.25 23.8 6.31 0 02-12-17 10:59 28.81 18.7 5.59 45 02-12-17 11:59 31.32 13.93 4.28 45 02-12-17 12:59 32.53 29.3 0 223 02-12-17 13:59 33.11 13.8 2.89 1 02-12-17 14:59 33.9 13.99 4.21 204 02-12-17 15:59 34.01 13.45 6.92 0

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02-12-17 17:59 31.1 13.7 0.28 45 02-12-17 18:59 32.26 15.02 0.86 163 02-12-17 19:59 30.67 17.78 1.26 93 02-12-17 20:59 29.06 20.5 1.75 134 02-12-17 21:59 27.17 24.25 1.07 153 02-12-17 22:59 25.77 24.78 0.54 162 02-12-17 23:59 25.02 27.84 1.1 0 03-12-17 0:59 20.47 30.43 3.03 237 03-12-17 1:59 20.4 37.3 2.05 0 03-12-17 2:59 20.69 46.54 2.68 272 03-12-17 3:59 20.17 53.5 3.4 45 03-12-17 4:59 19.16 57.96 6.43 0 03-12-17 5:59 17.88 58.76 6.22 270 03-12-17 6:59 17.24 53.28 6.27 270 03-12-17 7:59 18.5 41.36 5.82 274 03-12-17 8:59 21.02 32 0 284 03-12-17 9:59 23.84 25.99 5.26 301 03-12-17 10:59 26.8 17.8 4.47 292 03-12-17 11:59 29.09 14.16 0 305 03-12-17 12:59 30.64 23.48 0 312 03-12-17 13:59 31.45 23.48 0 313 03-12-17 14:59 32.23 30.1 0 313 03-12-17 15:59 30.6 23.48 0 0 03-12-17 16:59 31.2 23.48 0 20 03-12-17 17:59 32.3 23.48 0 29 03-12-17 18:59 31.59 23.48 0 39 03-12-17 19:59 28.97 14.79 1.63 56 03-12-17 20:59 26.49 17.36 1.59 78 03-12-17 21:59 24.82 20.23 1.96 64 03-12-17 22:59 23.3 22.6 0.37 79 03-12-17 23:59 22.11 25.12 0 79

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04-12-17 0:59 22.44 28.56 0.98 101 04-12-17 1:59 20.84 31.79 4.82 125 04-12-17 2:59 19.69 35.84 4.14 123 04-12-17 3:59 18.83 43.96 3.75 127 04-12-17 4:59 18.57 53.54 0 147 04-12-17 5:59 18.24 58.28 3.47 100 04-12-17 6:59 17.81 57.16 2.98 161 04-12-17 7:59 18.91 49.64 0 195 04-12-17 8:59 21.16 37.76 4.05 267 04-12-17 9:59 23.96 26.33 3.26 272 04-12-17 10:59 27.3 20.03 0 219 04-12-17 11:59 29.86 16.06 0.49 31 04-12-17 12:59 30.94 16.7 1.24 62 04-12-17 13:59 32.23 23.48 1.45 66 04-12-17 14:59 32.88 23.48 1.96 73 04-12-17 15:59 32.93 20.4 0.4 121 04-12-17 16:59 32.92 23.48 0.61 84 04-12-17 17:59 32.88 23.48 1.47 39 04-12-17 18:59 31.96 23.48 2.29 66 04-12-17 19:59 29.87 13.71 1.28 124 04-12-17 20:59 27.04 16.89 1.4 91 04-12-17 21:59 24.46 18.71 1.35 73 04-12-17 22:59 23.54 20 0.86 113 04-12-17 23:59 23.24 22.08 1.19 119 05-12-17 0:59 22.45 24.54 1.66 111 05-12-17 1:59 21.12 28.39 2.78 110 05-12-17 2:59 20.45 35.48 2.17 117 05-12-17 3:59 19.94 44.76 0 196 05-12-17 4:59 18.8 56.45 3.75 273 05-12-17 5:59 17.86 59.72 4.98 0 05-12-17 6:59 17.66 50.34 4.94 237 05-12-17 7:59 19.34 34.21 0 220 05-12-17 8:59 22.68 24.1 0 45 05-12-17 9:59 25.65 19 0 235 05-12-17 10:59 28.21 14.23 0 45 05-12-17 11:59 30.72 29.6 0 0 05-12-17 12:59 31.93 14.1 0 0 05-12-17 13:59 32.51 14.29 6.2 45 05-12-17 14:59 33.3 13.75 5.85 237 05-12-17 15:59 33.41 23.48 5.43 45 05-12-17 16:59 33.31 14 2.87 234 05-12-17 17:59 32.72 15.32 0 221

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05-12-17 18:59 31.66 18.08 1.82 208 05-12-17 19:59 30.07 20.8 2.5 206 05-12-17 20:59 28.46 24.55 3.36 45 05-12-17 21:59 26.57 25.08 0 220 05-12-17 22:59 25.17 28.14 0 223 05-12-17 23:59 20.37 30.63 0 219 06-12-17 0:59 20.3 37.5 4.68 233 06-12-17 1:59 20.59 46.74 3.96 231 06-12-17 2:59 20.07 53.7 3.75 231 06-12-17 3:59 19.06 58.16 3.26 233 06-12-17 4:59 17.78 58.96 5.52 45 06-12-17 5:59 17.14 53.48 6.71 230 06-12-17 6:59 18.4 41.56 0 231 06-12-17 7:59 20.92 32.2 0 236 06-12-17 8:59 23.74 26.19 0 223 06-12-17 9:59 26.7 18 0 229 06-12-17 10:59 28.99 14.36 0 236 06-12-17 11:59 30.54 23.68 0 221 06-12-17 12:59 31.35 23.68 0 224 06-12-17 13:59 32.13 30.3 0 232 06-12-17 14:59 32.51 23.68 6.92 237 06-12-17 15:59 32.47 23.68 6.31 0 06-12-17 16:59 32.2 23.68 5.59 45 06-12-17 17:59 31.49 23.68 4.28 45 06-12-17 18:59 28.87 14.99 0 223 06-12-17 19:59 26.39 17.56 2.89 1 06-12-17 20:59 24.72 20.43 4.21 204 06-12-17 21:59 23.2 22.8 0 271 06-12-17 22:59 22.01 25.32 0.23 123 06-12-17 23:59 22.34 28.76 0.07 152 07-12-17 0:59 20.74 31.99 1.52 162 07-12-17 1:59 19.59 36.04 1.17 128 07-12-17 2:59 9.6 44.16 0.68 154 07-12-17 3:59 18.47 53.74 0 155 07-12-17 4:59 8.9 58.48 1.75 45 07-12-17 5:59 17.71 57.36 0 224 07-12-17 6:59 18.81 49.84 3.86 215 07-12-17 7:59 21.06 37.96 4.14 45 07-12-17 8:59 23.86 26.53 5.24 205 07-12-17 9:59 27.2 20.23 5.87 45 07-12-17 10:59 29.76 16.26 0 221 07-12-17 11:59 30.84 16.9 5.36 45

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07-12-17 12:59 32.13 23.68 5.47 227 07-12-17 13:59 32.78 23.68 0 234 07-12-17 14:59 32.83 20.6 0 235 07-12-17 15:59 32.82 23.68 0 224 07-12-17 16:59 32.78 23.68 2.24 218 07-12-17 17:59 31.86 23.68 0.14 203 07-12-17 18:59 29.77 13.91 0.35 204 07-12-17 19:59 26.94 17.09 0 221 07-12-17 20:59 24.36 18.91 4.7 231 07-12-17 21:59 23.44 20.2 0 237 07-12-17 22:59 23.14 22.28 0 237 07-12-17 23:59 22.35 24.74 5.12 230 08-12-17 0:59 21.02 28.59 4.07 228 08-12-17 1:59 20.35 35.68 0 222 08-12-17 2:59 19.84 44.96 0 219 08-12-17 3:59 10.8 56.65 3.22 228 08-12-17 4:59 17.76 59.92 4.96 228 08-12-17 5:59 17.56 50.54 6.22 230 08-12-17 6:59 19.24 34.41 6.62 0 08-12-17 7:59 22.58 24.3 5.96 45 08-12-17 8:59 25.55 19.2 5.57 264 08-12-17 9:59 28.11 14.43 6.61 45 08-12-17 10:59 30.62 29.8 0 257 08-12-17 11:59 31.83 14.3 0 259 08-12-17 12:59 32.41 14.49 0 45 08-12-17 13:59 31.7 13.95 0 0 08-12-17 14:59 30.1 23.68 0 258 08-12-17 15:59 30.2 14.2 0 45 08-12-17 16:59 29.9 15.52 7.3 228 08-12-17 17:59 31.56 18.28 6.83 45 08-12-17 18:59 29.97 21 0 231 08-12-17 19:59 28.36 24.75 6.78 231 08-12-17 20:59 26.47 25.28 6.29 0 08-12-17 21:59 25.07 28.34 5.78 0 08-12-17 22:59 24.9 27.9 4.84 259 08-12-17 23:59 24.5 27.1 4.33 0

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Annexure - 13 Environmental Monitoring Reports

Soil Monitoring Results

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Air Quality Monitoring Reults

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M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.- Narmada, Gujarat

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M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.- Narmada, Gujarat

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Noise Monitoring Results

M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.- Narmada, Gujarat

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M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.- Narmada, Gujarat

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Surface Water Monitoring Results

M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.- Narmada, Gujarat

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M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.- Narmada, Gujarat

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Ground water Monitoring Results

M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.- Narmada, Gujarat

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M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.

Data Related to Occupational Health & Safety

M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.

ANNEXURE - 14 Data Related to Occupational Health & Safety

Rajpipla (Nandod), Dist.- Narmada, Gujarat

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Data Related to Occupational Health & Safety

M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.

M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.

Rajpipla (Nandod), Dist.- Narmada, Gujarat

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M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.

M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.

Rajpipla (Nandod), Dist.- Narmada, Gujarat

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M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.

M/s Shree Narmada Khand Udyog Sahakari Mandli Ltd., Dharikheda, Tal.- Rajpipla (Nandod), Dist.

Rajpipla (Nandod), Dist.- Narmada, Gujarat

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