ANNEXURE –

ADDITIONAL ATTACHMENTS

MANUFACTURING PROCESS FLOW CHART

PROCESS FOR ETHYL ALCOHOL HIFERM-GR Fermentation PRAJ Industries, the leading supplier of Distillery plants in India, South Asia, Africa and South Central America, has continuously developed process technologies and engineering for distilleries. Over the last fifteen years, PRAJ has supplied several fermentation and distillation plants, which are essentially designed to suit international norms of spirit quality and fermentation efficiency. The fermentation plant designs include cascade fermentation with cell recycle, cascade fermentation with yeast recycle and cascade fermentation with granulating yeast and gravity settling. On the other hand, plant designs for distillation are multi-pressure types with special facilities to achieve international spirit quality norms with minimum operating costs. PRAJ has dedicated technology development center for the distillery process and engineering developments. As a latest development in the fermentation technology, HIGHFERM - GR fermentation process has evolved. The HIGHFERM - GR technology is designed to specially handle the changing composition of molasses without having the problem of sludge recycle and build up, contamination and resulting low fermentation efficiencies. The technology uses special type of yeast with self-granulating property. This is Saccharomyces cerevesiae yeast with high specific growth rate and productivity. Due to the self-granulating property, the yeast can be separated by gravity settling and treated to wash away contamination. The treated yeast passes through activation step and is recycled back to fermentation. The major drawback of all continuous fermentation processes, which use centrifuge based yeast recycle, is build up of sludge. The yeast centrifuge cannot differentiate between yeast and sludge. Centrifuge separates both yeast and sludge and recycles back to fermentation. This builds up sludge in fermenter and makes the fermentation volume unavailable for fermentation. Moreover the sludge also brings in contamination along with it, which builds in the fermenter. The HIGHFERM - GR fermentation process on the other hand eliminates these limitations and give high fermentation efficiency based on molasses composition and can be flexibly adapted for modernization of existing batch fermentation plants as well as for expansion or for new projects. The sections comprise yeast propagation section, fermentation section with four fermenters, yeast separation & treatment section and yeast activation section. While starting up the plant yeast propagation is done in propagation system. The grown yeast is used to fill up first fermenter and in a similar manner all the other fermenters are filled. When the fermenters are ready for distillation, the fermented wash is subjected to gravity settling for yeast separation. Sufficient residence time is used for completing fermentation. The residence time is dependent on molasses composition. The reactivated and grown yeast is sent to fermentation.

All fermenters are sparged with Air / CO2 generated during fermentation. This helps in maximum recovery of pure CO2 from fermentation. Similarly, it helps in minimum generation of by-products. The CO2 generated in fermentation is scrubbed through the CO2 scrubber, for recovering alcohol in it, before realizing for recovery. This minimizes loss of alcohol. The new HIGHFERM - GR process is designed to minimize the adverse effects of high volatile acidity and sludge in molasses. Similarly the process is designed to minimize effects of contamination. Similarly the effluent volumes are low due to high alcohol concentration in wash. The process does not use recycle of spent-wash as a means to minimize effluent volumes. This is mainly because the recycle of spent wash, as observed in all technologies, had to be stopped or substantially reduced due to high volatile acidity and sludge in the molasses. “ECOFINE-VS” Distillation Process ‘ECOFINE-VS’ distillation scheme has three distillation columns. Three columns operate under different pressure condition. Heat from column operating under high pressure is recycled back to column operating under low pressure to conserve energy. The columns in order of flow are: - 1. Analyzer column - Operated under vacuum 2. Pre-rectifier column - Operated under vacuum 3. Rectifier cum exhaust column - Operated under pressure 4. Fusel oil concentration column. Fermented mash containing 8.0 - 9.0 % v/v alcohol is preheated in the Fermented Mash Preheater and fed at the top of the analyzer column. Analyzer column is fitted with Thermosyphen reboiler. Top vapours of analyzer column are sent to the pre-rectifier column. Rest of the fermented wash flows down the Mash column and is taken out as spent wash from analyzer column bottom. Pre rectifier bottom liquid is preheated with spent lees and fed to rectifier cum Exhaust column. Low boiling impurities are concentrated in the pre rectifier column. A top draw is taken out as impure alcohol from the top of the pre-rectifier column. The wash from this column is sent to rectifier feed tank. Rectifier cum Exhaust column is operated under pressure and heats. Alcohol is enriched towards the top and is drawn out as Rectified Spirit at about 96% v/v concentration. Fusel oil build up is avoided in the rectifier column by withdrawing out side streams (fusel oils). These are sent to the fusel oil concentration column where this fusel oil is decanted. Here these streams are diluted with water and fusel oil rich layer is separated. The fusel oil wash water is recycled back to the column. A top draw is taken out as impure alcohol from the top of the Rectifier column. Benefits of “ECOFINE – VS” Distillation • Operation of analyzer column is under vacuum. This minimizes formation of

byproducts during distillation (like acetal). Hence, the overall quality of spirit is improved. Also, chances of scaling due to invert solubility of certain precipitating inorganic salts of calcium and magnesium are reduced considerably in vacuum distillation.

• Analyzer column with Hyperstate trays ensure high turbulence on tray, this minimizes chances of scaling. Also, this special construction of trays and access to each tray helps in easier maintenance of column intervals.

• Pre- Rectification column ensures proper removal of sulfur compounds / Mercaptans for ensuring a good odor to alcohol. This column also reduces the load of lower boiling volatile compounds passing on to rectifier cum exhaust column.

• Vacuum distillation system requires low steam consumption i. e.1.8 Kg / liter of total alcohol of EQRS quality as against 2.0 –2.2 Kg / liter of total alcohol of normal quality in atmospheric distillation.

• System designed for maximum heat integration for optimum utilization of energy.

• Minimum no. of condensers. Forced circulation multi-pass condensers with optimum tube side velocities.

• Use of Thermo siphon reboilers in analyzer column helps in maintaining uniform temperature profile across the column. Also avoids excess spent wash volume generation.

• Energy saving by recovery of Steam condensate from Thermo siphon reboiler of analyzer column.

• Effective separation of fusel oils from decanter.

VISHWASRAO NAIK SAHAKARI SAKHAR KARKHANA LTD.

Process Flow Chart of Sugar Production

Un – satisfactory

Phosphate Dosing Collect Juice in Receiving Tank

Juice Flow Measurement

Vapour line juice heating

Raw Juice Heating

Gauge

Less

Stream/ Vapour valve setting

MOL Addition

Monitor & Verify temp & pH

Satisfactory

A

Clear Juice

Light/ Heavy Filtrate

A

Sulphered Juice heating

Monitor temp of juice

Stream/ Vapour valve setting

Juice Clarification Juice sulphieter

Vacuum Filter

Muddy Juice

Monitor pH

B

Feedback addition at reaction tank

Less Composting

Filter cake

Less

B OK

Monitor temp

Less Stream/ Vapour valve setting

Juice Evaporation

Monitor Brix & temp

Adjust – a) Steam b) Vacuum c) Juice flow

Satisfactory

Syrup Sulphitation

Monitor pH

Pan Storage tank C

SO2

Addition

NO

C

‘A’ Masseccute Boiling

Air - cooled crystalliser

Centrifugal

Curing

Hopper

Grader

M.30/S.30 Sugar

Weighing & Bagging

Gowdown

Magma

Dry seed Magma

Melter

Pan Storage tank

Molasses D ‘A’ Heavy

‘A’ Light

Pan Storage tank

D

Pan Boiling B Pan

‘B1 ’Massecute

Air cooling crystallizer

Centrifugal

B1 Heavy

B- Seed ‘A’ Pan

Melter

B1 Sugar

Syrup Tank

Pan Boiling ‘B2’ Massecute

Water -Cooled Crystilizer

Centrifugal E

B2 Heavy

Melter

Syrup

B1 Sugar

..

E

Pan Boiling ‘C’ Pan

Water - cooled vertical crystaliser

Centrifugal Final Molasses

Storage Tank

Delivery to Distillery

Fore ‘C’ Sugar

Magma

Centrifugal

Melter

Syrup tank

‘C’ Light ‘C’ after sugar

CERTIFICATES & OTHER DOCUMENTS

WATER BUDGET & WATER PERMISSION LETTER

123

MASS BALANCE FOR THE 30 KLPD DISTILLERY UNIT

BY

M/S. VISHWASRAO NAIK SAHAKARI SAKHAR KARKHANA LIMITED

ALCOHOL- 24 MT (30 KL)

FUSEL OIL – 0.06 KL

SPENT WASH- 200 KL

SPENT WASH- 210 KL

AIR

BACTERIAL CULTURE 40 Kg

PRESS MUD 40 MT CO2+WATER VAPOUR

FERMENTED WASH 350 KL

CONDENSATE – 42 KL SPENT LEES 60 KL

WATER 225 KL

FERMENTER

DISTILLATION

SPENT WASH STORAGE TANK CAPACITY OF 30 DAYS GENERATION

COMPOST YARD

CO2 -23 MT

MOLASSES 110 MT (Vol. 75 KL)

ADDITIVES 0.12 MT

STEAM 42 MT

24,812 MT BIO-COMPOST

TO ETP OF SUGAR FACTORY FOR TREATMENT ALONG WITH SUGAR EFFLUENT.

REBOILER

124

DETAILS OF RAW - MATERIALS, CHEMICALS, AND PRODUCTS OF

THE PROPOSED 30 KLPD DISTILLERY PROJECT

1. Capacity - 30 KLPD, 2. Working Days – 270 Days / Year

Particulars Consumption/ Production per

Month

Consumption / Production per

Year

Remarks

Raw materials

Molasses (Consumption)

3600 MT 32400 MT Basis 45% F.S. @ 110 MT/Day

Yeast Test Tube Culture

Test Tube Culture

----

Chemicals

Diammoniumphosphate (DAP)

1.2 MT 10.8 MT Stored in Fermentation House transported in Sacks.

Antifoaming Compound 3.5 MT 31.5 MT Stored in 200 Lit. Capacity Barrels/Antifoam oil tank

Utilities

Steam at 120-122 0C (Consumption)

2520 MT

22680 MT

84 MT/day

Process and Cooling water, Makeup water etc. (Consumption)

8640 M3 77760 M3 288 M3/day

Washing water and Lab. water (Consumption)

150 M3 1350 M3 5 M3/day

Boiler 210 M3 1890 M3 7 M3/day

Domestic water (Consumption)

300.0 M3 2700 M3 10 M3/day

Products/By-products

Ethanol 900 KL 8100 KL 30 KLPD

Rectified Spirit 900 KL 8100 KL 30 KL /Day

Extra Neural Alcohol 333 KL 3000 KL 11.1 KLPD

Fusel oil 1.8 MT 17 KL 0.06 MT /Day

Process Emissions

CO2+ Air@ 23 M.T. per Day

690 MT 5520 MT Location -Fermentation House

Effluent Generated

Spent wash 6840 M3 61560 M3 228 M3/day

Spent lees 1350 M3 12150 M3 45 M3/day

Domestic effluent 180 M3 1620 M3 6 M3 / day

123

DETAILS OF RAW - MATERIALS, CHEMICALS, AND PRODUCTS OF

THE PROPOSED 60 KLPD DISTILLERY PROJECT

1. Existing Capacity - 30 KLPD, 2. Working Days – 270 Days / Year

Particulars Consumption/

Production per Month

Consumption /

Production per Year

Consumption/

Production per Month

Consumption /

Production per Year

Remarks

30 KLPD 60 KLPD 30 KLPD 60 KLPD Raw Materials

Molasses (Consumption)

3600 MT 32400 MT 7200 MT 64800 MT Basis 45% F.S.@ 110

MT/Day

Basis 45% F.S.@220M

T/Day Yeast Test tube

Culture Test Tube

Culture Test Tube

Culture Test Tube

Culture ----

Chemicals

Diammoniumphosphate (DAP)

1.2 MT 10.8 MT 2.4 MT 21.6 MT Stored in Fermentation

House transported in

Sacks.

Stored in Fermentatio

n House transported in Sacks.

Antifoaming Compound

3.5 MT 31.5 MT 7 MT 63 MT Stored in 200 Lit. Capacity Barrels/Antifo

am oil tank

Stored in 200 Lit.

Capacity Barrels/Antifoam oil tank

Utilities

Steam at 120-122 0C(Consumption)

2520 MT

22680 MT

5040 MT 45360 MT 84 MT/Day 168 MT/Day

Process and Cooling water,

Makeup water etc. (Consumption)

8640 M3 77760 M3 17280 M3 155520 M3

288 M3/day

576 M3/day

Washing water and Lab. water (Consumption)

150 M3 1350 M3 300 M3 2700 M3 5 M3/day 10 M3/day

Boiler 210 M3 1890 M3 420 M3 3780 M3 7 M3/day 14 M3/day

Domestic water (Consumption)

300.0 M3 2700 M3 600 M3 5400 M3 10 M3/day 20 M3/day

124

Particulars Consumption/

Production per Month

Consumption /

Production per Year

Consumption/

Production per Month

Consumption /

Production per Year

Remarks

30 KLPD 60 KLPD 30 KLPD 60 KLPD Products/By-

products

Ethanol 600 KL 5400 KL 1200 KL 10800 KL 20 KLPD 40 KLPD

Rectified Spirit 900 KL 8100 KL 1800 KL 16200 KL 30 KL /Day 60 KL/Day

Extra Neural Alcohol

900 KL 8100 KL 1800 KL 16200 KL 30 KLPD 60 KLPD

Fusel oil 4.5 KL 40.5 KL 4.5 KL 40.5 KL 4.5 KL/M 4.5 KL /M

Pharma grade Alcohol

--- --- 1800 KL 16200 KL ---- 60 KLPD

Process Emissions

CO2+ Air@ 23 M.T. per Day

690 MT 6210 MT 1380 MT 12420 MT Location -Fermentation

House

Location -Fermentatio

n House Effluent

Generated

Spent wash 6840 M3 61560 M3 13680 M3 123120 M3

228 M3/day 456 M3/day

Spent lees 1350 M3 12150 M3 2700 M3 24300 M3 45 M3/day 90 M3/day

Domestic effluent 180 M3 1620 M3 360 M3 3240 M3 6 M3 / day 6 M3 / day

No. Unit Size Capacity M3 Remark

1 Screen Chamber 3 M x 2 M x 1.2 M 7.2 Existing

2 Oil & Grease 3 M x 2 M x 1.2 M 7.2 Existing

3 Primary Holding Tank 6.5 M x 6.5 M x 2.7 M 105.63 Existing

4 Equalisation Tank 11 M x 11 M x 3.5 M 363 Existing

5 Reaction Tanks 2 M x 2 M x 2.5 M (Two Units) 20 Proposed

6 Primary Settling Tank 8 M Dia x 2.7 M SWD 135.65 Proposed

7 1st Stage Aeration Tank 21 M x 16 M x 3 M 840 Proposed

8 Secondary Settling Tank-I 8 M Dia x 2.7 M SWD 135.65 Existing

9 2nd Stage Aeration Tank 21 M x 10 M x 3 M 525 Proposed

10 Secondary Settling Tank-II 8 M Dia x 2.7 M SWD 135.65 Proposed

11 Holding Sump 21 M x 11M x 3 M 577.5 Proposed

12 Treated Water Tank 22 M x 12 M x 2.2 M 528 Existing

13 PSF& ACF --- 40 M3/Hr, Each Proposed

14 SDBs 11 M x 8.3 x 1.3 M ( 2 Nos.) --- Existing

Oil &

Grease

Trap Reaction Tanks (2 Nos.)

Influent

Primary

Settling

Tank

1st Stage

Aeration Tank

Secondary

Settling

Tank- I

2nd

Stage

Aeration Tank

Secondary

Settling

Tank- II

Holding Sump

PSF

Treated Water Tank Treated water for

Gardening / Irrigation

Sludge Drying Beds (SDBs)

Excess Sludge

Return Sludge

Legends:-

Existing Units

Proposed Units

Block Diagram of ETP provided at Vishwasrao Naik S.S.K. Ltd., Yashwantnagar, Chikhali, Tal.: Shirala, Dist.: Sangli.

Primary

Holding

Tank

Screen

Chamber

ACF

Equalization

Tank

Return Sludge

Excess Sludge

Excess Sludge

VISHWASRAO NAIK SAHAKARI SAKHAR KHARKHANA LTD., TAL. – SHIRALA, DIST. – SANGALI

EXISTING 30 K.L.P.D. MOLASSES BASED DISTILLERY Daily Requirement of Water

419 KL/Day (*276 + #143)

Condensate 116 KL

Fermentation Dilution *255 KL

Vaccum pump *20 KL

Cooling Tower make-up

#84

Cooling Blow Down 15 KL

290 K.L Spent wash (18% Solid)

276 KL to

CPU

Bio - Digester

Composting

116 KL Conc,Spent Wash Contains 60% Solids

Note: * - Recycled water from CPU unit. # - Fresh water

Effluent 30 KL

75 KL Spent Lees

Fermentation Dilution 255 KL

Recycle for, vacuum Pump, lab& washing 21 KL

Lab & Washing

5KL (#4+*1)

Air Blower # 30 KL

Effluent 20 KL

Effluent 5 KL

Fusel oil decanter &

Alcohol scrubber # 15 KL

Effluent 15 KL

85 KL

Molasses 110 MT

R.O. Unit 58 KL To sugar

ETP

Domestic #10 KL

10KL Treatment in Septic tank followed by Soak Pits

VISHWASRAO NAIK SAHAKARI SAKHAR KHARKHANA LTD., TAL. – SHIRALA, DIST. – SANGALI

TOTAL 60 K.L.P.D. MOLASSES BASED DISTILLERY

Daily Requirement of Water

848 KL/ Day

(*697 + #151)

Condensate 403 KL

Molasses 220MT +

Fermentation Dilution *520 KL

(Total 740 KL)

Vaccum pump

#40 KL

Cooling Tower make-up

*168

Cooling Blow Down 15 KL 576 K.L Spent wash

(18% Solid)

697 KL to

CPU

Multiple Effect

Evaporators (MEE)

Incineration

173 KL Spent Wash Contains 60% Solids

Note: * - Recycled water from CPU unit. # - Fresh water

Effluent 30 KL

164 KL Spent Lees

Fermentation Dilution 520 KL

Cooling Tower make-up, Lab & Washing 177 KL

Lab & Washing

10 KL (*9+#1)

Air Blower #30 KL

Effluent 40 KL

Effluent 10 KL

Effluent 30 KL

130 KL

Incineration Boiler

# 50 KL

Effluent 5 KL

Fusel oil decanter &

Alcohol scrubber # 30 KL

Application for Consent/ Authorisation

Sir,I/We hereby apply for*

1. Consent to Establish/Operate/Renewal of consent under section 25 and 26 of the Water (Prevention & Control of Pollution) Act, 1974 asamended.

2. Consent to Establish/Operate/Renewal of consent under Section 21 of the Air (Prevention and Control of Pollution) Act, 1981, asamended.

3. Authorization/renewal of authorization under rule 5 of the Hazardous Wastes (Management and Handling) Rules, 1989, as amended inJanuary,2000, in connection with my/our/existing/proposed/altered/ additional manufacturing/processing activity from the premises as perthe details given below.

Consent Information

UAN No:MPCB-CONSENT-0000027359

Industry Information

Consent To: IIN No.: Submit to:Renewal (Normal) SRO - Sangli

Type of institution: Industry Type: Category: Scale:Industry R15 Distillery including

Fermentation industryRed L.S.I

EC Reqd. EC Obtained EC Ref. No.No No -

Whether construction-buildup area is more than 20,000sq.mtr.(Existing Expansion Unit)

Yes

General Information

1. Name, designation, office address with Telephone/Fax numbers, e-mail of the Applicant Occupier/Industry/Institution / Local Body.

Name AddressShree Ramchandra Shivajirao Patil Yashwantnagar, Chikhali, Tal.: Shirala, Dist.: Sangli

Designation TalukaManaging Director Shirala

Area DistrictYashwantnagar, Chikhali Sangli

Telephone Fax9970700165 02345231006

Email Pan Numbersharad.etp@gmail.com AAAAV0215B

2. (a) Name and location of the industrial unit/premises for which the application is made (Give revenue Survey Number/Plot numbername of Taluka and District, also telephone and fax number)

Industry nameM/s. Vishwasrao Naik Sahakari Sakhar Karkhana Ltd.(Distillery Unit)

Location of Unit Survey number/Plot NumberYashwantnagar, Chikhali 182, 224, 223, 175, 189, 183, 162

Taluka DistrictShirala Sangli

(b) Details of the planning permission obtained from the local body/Town and Country Planning authority/Metropolitan Developmentauthority/ designated Authority.

Planning permission Planning AuthorityNOC from Gampanchayat Chikhali, Tal. - Shirala, Dist. - Sangli Garamvikas Adhikari & Sarpanch,Tal. - Shirala, Dist. - Sangli

Name of the local body under whose jurisdiction the unit is located and Name of the licence issuing authority

Name of Local Body Name of the licence issuing authorityGampanchayat Chikhali, Tal. - Shirala, Dist. - Sangli Garamvikas Adhikari & Sarpanch,Tal. - Shirala, Dist. - Sangli

3. Names,addresses with Telephone and Fax Number of Managing Director / Managing Partner and officer responsible for mattersconnected with pollution control and/or Hazardous waste disposal.

Name of Managing Director Telephone numberMr.Ramchandra Shivajirao Patil 9970700165

Fax number Officer responsible for day to day business02345231006 Mr. Sharadkumar Patil

4. (a.) Are you registered Industrial unit ? Yes

Registration number Date of registrationSAN/PGR/ (A) 2 dated 04.05.1967 May 4, 1967

5. Gross capital investment of the unit without depreciation till the date of application (Cost of building, land, plant and machinery). (Tobe supported by an affidavit/undertaking on Rs.20/- stamp paper, annual report or certificate from a Chartered Accountant for proposedunit(s), give estimated figure)

Gross capital (in Lakh) * Verified * Consent Fee 1505.44 CA Certificate 50000.00

6. If the site is located near sea-shore/river bank/other water bodies/Highway, Indicate the crow fly distance and the name of the waterbody, if any.

Distance From Distance(Km) * NameSH/NH 21.30 National Highway 4

River 3.00 Warna

Human Habitation 0.50

Religious Place 0.00 --NA--

Historical Place 0.00 --NA--

Creek/Sea 0.00 --NA--

6b. Enter Latitude and Longitude details of site

Latitude Longitude165618 740518.35

7. Does the location satisfy the Requirements Under relevant Central/State Govt. Notification such as Coastal Regulation Zone.Notification on Ecologically Fragile Area, Industrial Location policy, etc. If so, give details.

Location Approved IndustryArea

Sensitive Area If Yes, Name Of Area Industry Location withReference to CRZ

NA No No NA

8. If the site is situated in notified industrial estate,

Details(a) Whether effluent collection,treatment and disposal system hasbeen provided by the authority.

No NA

(b) Will the applicant utilize thesystem, if provided.

No NA

(c) If not provided, details of proposedarrangement.

NA

9.

(a) Total plot area (in squear meter) (b) Built up area and (in squear meter) (c) Area available for the use oftreated sewage/ trade effluent forgardening/irrigation. (in squear meter)

185600 35600 118956

10. Month and year of commissioning of the Unit.

2003-03-01

11. Number of workers and office staff

Workers staff Hrs. of shift Weekly off26 11 8 Sunday

12.

(a) Do you have a residentialcolony Within the premisesin respect of Which thepresent application is Made?

No NA

(b) If yes, please state population stayingNumber of person staying Water consumption Sewage generation Whether is STP provided?

0 0 No

(c) Indicate its location and distance with reference to plant site.Number of person staying Water consumptionNA 0

13. List of products and by-products Manufactured in tonnes/month, Kl/month or numbers/month with their types i.e.Dyes, drugs etc.(Give figures corresponding to maximum installed production capacity

Products Name and Quantity

ProductName

UOM ProductName

Existing Consented ProposedRevision

Total Remarks

DistilleryincludingFermentationIndustry

KL/M Rectified spirit 900 900 0 900 --

DistilleryincludingFermentationIndustry

KL/M AbsoluteAlcohol

600 600 0 600 --

DistilleryincludingFermentationIndustry

KL/M Fusel Oil 4.5 4.5 0 4.5 --

Products Name and Quantity

Product Name UOM Quantity RemarksNA --NA-- 0 NA

14. List of raw materials and process chemicals with annual consumption corresponding to above stated production figures, intonnes/month or kl/month or numbers/month.

Name of Raw Material UOM Quantity HazardousWaste

HazardousChemicals

Remarks

Molasses MT/M 3600 No No NA

Urea MT/M 1 No No NA

De- Foaming Oil MT/M 3 No No NA

Steam MT/M 2500 No No NA

15. Description of process of manufacture for each of the products showing input, output, quality and quantity of solid, liquid andgaseous wastes, if any from each unit process.

For Manufacturing Process Refer Uploaded Documents.

Part B : Waste Water aspects

16. Water consumption for different uses (m3/day)

Purpose Consumption EffluentGeneration

Treatment Remarks Disposal Remarks

Domestic Pourpose 10 8 Septic Tank &Soak Pit

NA --NA-- NA

Water gets Polluted& Pollutants areBiodegradable

225 (200 + 60)=260 OTHERS @210KL spentwash forwardedto Reboiler &spent lees@60KL isforwarded tosugar ETP.

Others @200KL spent washused forcomposting.@60m3/DSpent lees isforwarded to sugarETP & used forgarden

Water getsPolluted,Pollutantsare notBiodegradable &Toxic

0 0 --NA-- 0 --NA-- NA

IndustrialCooling,spraying inmine pits or boilerfeed

100 11.75 Primary +Secondary +Tertiary

Effluentgenerated fromFermentercooling,condensercooling is@7m3/D & otherefflunent fromLab &

On Land forGardening

@11.25m3/D effluentgenerated fromcooling, Lab &washing is used forgardening in ownfactory premi

Others 5

17. Source of water supply, Name of authority granting permission if applicable and quantity permitted.

Source of water supply Name of authority granting permission Qauntity permittedWarana River Irrigation Department, Government of

Maharashtra452.27

18. Quantity of waste water (effluent) generated (m3/day)

Domastic Boiler Blowdown Industrial Cooling water blowdown8 0 271.25 7

Process DM Plants/Softening Washing Tail race discharge from260 0 4.25 0

* 19. Water budget calculations accounting for difference between water consumption and effluent generated.

For Water Budget ReferUploaded documents.

20. Present treatment of sewage/canteen effluent (Give sizes/capacities of treatment units).

Capacity of STP (m3/day)0

Treatment unit Size (mxm) Retention time (hr)NA 00 00

21. Present treatment of trade effluent (Give sizes/capacities of treatment units) (A schematic diagram of the treatment scheme withinlet/outlet characteristics of each unit operation/process is to be provided. Include details of residue Management system (ETP sludges)

Capacity of ETP (m3/day)630

Treatment unit Size (mxm) Retention time (hr)Screen chamber 7.2 0.04

Oil & Grease Tank 7.2 0.04

Primary Holding Tank 126.75 2

Collection Tank 80.41 5.09

Equalization Tank 423.5 27

Aeration Tank 2957.33 15

Secondary Clarifier 145.69 2

Holding Sump 742.46 47.02

Sludge Drying Bed (2 Nos) 118.69 360

22.

(i) Are sewage and trade effluents mixed together? No

If yes, state at which stage-Whether before, intermittently or after treatment. NA

23. Capacity of treated effluent sump, Guard Pond if any.

Capacity of treated effluent sump (m3) NA

Effluent sump/Guard pond details No NA

If yes, state at which stage-Whetherbefore, intermittently or aftertreatment.

No NA

24. Mode of disposal of treated effluent With respective quantity, m3/day

(i) into stream/river (name ofriver)

0 (ii) into creek/estuary (nameof Creek/estuary)

0

(iii) into sea 0 (iv) into drain/sewer (ownerof sewer)

0

(v) On land for irrigation onowned land/ase land. Specifycropped area.

The treated effluent is used for gardening in own factorypremises.

(vi) Connected to CETP NA

(vii) Quantity of treatedeffluent reused/ recycled,m3/day Provide a locationmap of disposalarrangement indicating theoutler(s) for sampling.Treated effluent reused /recycled (m3/day)

0

25. (a) Quality of untreated/treated effluents (Specify pH and concentration of SS, BOD,COD and specific pollutants relevant to theindustry. TDS to be reported for disposal on land or into stream/river.

Untreated Effluent

pH 3.9-4.5

SS (mg/l) 15,000 - 20,000

BOD (mg/l) 60,000 - 80,000

COD (mg/l) 1,20,000-1,40,000

TDS (mg/l) 80,000 – 90,000

Specific pollutant ifany

Name Value

1 NA 0

Treated Effluent

pH --

SS (mg/l) --

BOD (mg/l) --

COD (mg/l) --

TDS (mg/l) --

Specific pollutant ifany

Name Value

1 NA 0

(b) Enclose a copy of the latest report of analysis from the laboratory approved by State Board/ Committee/Central Board/CentralGovernment in the Ministry of Environment expected characteristics of the untreated/treated effluent

Refer uploaded documents for monitoring reports.

26. Fuel consumption

Fuel Type UOM Fuel Consumption TPD/LKD Calorific value--NA-- --NA-- 0 0

Ash content Sulphur content Quantity Other (specify)0 0 1 --

27. (a) Details of stack (process & fuel stacks: D. G. )

(a) Stack number(s) (b) Stack attached to (c) Capacity (d) Fuel TypeNA NA NA NA

(e) Fuel quantiy (Kg/hr.) (f) Material of construction (g) Shape(round/rectangular)

(h) Height, m (above groundlevel)

0 0 0 0

(i) Diameter/Size, in meters (j) Gas quantity, Nm3/hr. (k) Gas temperature ℃ (l) Exit gas velocity, m/sec.

0 0 0 0

(m) Control equipmentpreceding the stack

(n) Nature of pollutantslikely to present in stackgases such as CI2, Nox, SoxTPM etc.

(o) Emissions control systemprovided

(p) In case of D.G. Set powergeneration capacity in KVA

0 0 0 Steam required for Distilleryoperations is taken from sugarfactory boiler.

27. (B) Whether any release of odoriferous compounds such as Mercaptans, Phorate etc. Are coming out from any storages or processhouse.

NA

28. Do you have adequate facility for collection of samples of emissions in the form of port holes, platform, ladder\etc. As per CentralBoard Publication “Emission regulations Part-III” ( December, 1985 )

Poart hole No Details NA

Platform No Details NA

Ladder No Details NA

29. Quality of treated flue gas emissions and process emissions. Quantity of treated flue gas emissionsand process emissions.

Sr.No.

Stack attached to Parameter Concentration mg/Nm3 flow (Nm3/hr)

1 NA NA 0 0

(Specify concentration of criteria pollutants and industry/process-specific pollutants stack-wise. Enclosea copy of the latest report of analysis from the laboratory approved by State Board/Central Board/Central Government in the Ministry of Environment & Forests. For proposed unit furnish expectedcharacteristics of the emissions..

Refer uploaded documents for monitoring reports.

Part - D: Hazardous Waste aspect

30. Information about Hazardous Waste Management as defined in Hazardous Waste (Management & Handling ) Rules, 1989 asamended in Jan.,2000. Type/Category of Waste as per

Waste (Annually) Schedule ICat No Type Qty Min20.3 20.3 Distillation residue 25

Max Method of collection Method of reception Method of storageManually Manually Manually

Method of transport Method of treatment Method of disposal NA -- Used for composting

Waste (Annually) Schedule II31. Details about use of hazardous waste

Name of hazardouswaste/Spent chemical

Quantity used/month Party from whom purchased Party to whom sold

20.3 Distillation Residue 750 NA NA

32.

a. Details about technical capability and equipments available with the applicant to handle the Hazardous Waste

NA

b. Characteristics of hazardous waste(s) Specify concentration of relevant pollutants. Enclose a copy of the latest reportof analysis from the laboratory approved by State Board/Central Board/Central Govt. in the ministry of Environment &Forests. For proposed units furnish expected characteristicsNA

33.

Copy of format of manifest/record Keeping practiced by the applicant.NA

34.

Details of self-monitoring (source and environment system)Ambient Air Quality Monitoring, Noise Monitoring & Effluent Sample Analysis is routinely being done

35.

Are you using any imported hazardous waste. If yes, give details.NA

36.

Copy of actual user Registration/certificate obtained from State Pollution Control Board/Ministry of Environment &Forests, Government of India, for use of hazardous waste.NA

37.

Present treatment of hazardous waste, if any (give type and capacity of treatment units)NA

38. Quantity of hazardous waste disposal

(i) Within factory25

(ii) Outside the factory (specify location and enclose copies of agreement.)0

(iii) Through sale (enclosed documentary proof and copies of agreement.)0

(iv) Outside state/Union Territory, if yes particulars of (1 & 3 ) above.0

(v) Other (Specify)0

Part - E: Additional information

39.

a. Do you have any proposals to upgrade the present system for treatment and disposal of effluent/emissions and/orhazardous waste.No

b. If yes, give the details with time- schedule for the implementation and approximate expenditure to be incurred on it.NA

40.

Capital and recurring (O & M) expenditure on various aspect of environment protection such as effluent, emission,hazardous waste, solid waste, tree- plantation, monitoring, data acquisition etc. (give figures separately for itemsimplemented/to be implemented).About 5 Lakhs spent every year for O & M of Effluent treatment plant.

41.

To which of the pollution control equipment, separate meters for recording consumption of electric energy are installed ?NA

42.

Which of the pollution control items are connected to D.G. Set (captive power source) to ensure their running in theevent of normal power failureNA

43. Nature, quantity and method of disposal of non- hazardous solid waste generated separately from the process of manufacture and waste treatment.(Give details of area/capacity available in applicant’s land)

Type Quantity UOM Treatment Disposal Other DetailsYeast sludge 5 MT/Day -- Used for Bio-composting --

44. Hazardous Chemicals – Give details of Chemicals and quantities handled and Stored.

(i) Is the unit a Majot Accident Hazard unit as per Mfg.Storage Import Hazardous Chemicals Rules ?NA

(ii) Is the unit an isolated storage as defined under the MSIHC Rules ?NA

(iii) Indicate status of compliance of Rules 5,7,10,11,12,13 and 18 of the MSIHC Rules.NA

(iv) Has approval of site been obtained from the concerned authority?NA

(v) Has the unit prepared an off-site Emergency Plan? Is it updated ?NA

(vi) Has information on imports of Chemicals been provided to the concerned authority?NA

(vii) Does the unit possess a policy under the PLI Act?NA

45. Brief details of tree plantation/green belt development within applicant’s premises ( in hectors )

Open Space Availability Plantation Done On Number of Trees Planted118956 Square meter 41634 Square meter(35 %) 7400

46.

Information of schemes for waste Minimization, resource recovery and recycling - implemented and to be implemented,separately.NA

47.

(a) The applicant shall indicate whether Industry comes under Public Hearing, if so, the relevant documents such as EIA,EMP, Risk Analysis etc. shall be submitted, if so, the relevant documents enclosed shall be indicated accordingly.NA

(b) Any other additional information that the applicants desires to giveNA

(c) Whether Environmental Statement submitted ? If submitted, give date of submission.Environmental Statement for the year 2016-17 would be submitted online.

48.

I/We further declare that the information furnished above is corect to the best of my/our knowledge.

49.

I/We hereby submit that in case of any change from what is stated in this application in respect of raw materials,products, process of manufacture andtreatment and/or disposal of effluent, emission, hazardous wastes etc. In quality and quantity; a fresh application forConsent/Authorization shall be made anduntil the grant of fresh Consent/Authorization no change shall be made.

50.

I/We indertake to furnish any other information within one month of its being called by the Board

Yours faithfullySignature :Name : Mr. Ramchandra Shivajirao PatilDesignation : Managing Director

Additional Information

Air Pollution

Sr No. Air Pollution Source Pollutants APCS Provided Remark1 NA NA NA --

Separate EM Provided Yes Other Emission Sources NA

Measures Proposed NA Foul Smell Coming Out No

Air Sampling Facility Details NA

D.G. Set Details

Description Capacity(KVA) RemarksNA 0 --

Hazardous Waste Generation

Hazardous Waste Quantity UOM Treatment Disposal Other Details20.3 Distillation residue 2.50 MT/A -- Used for composting. Hazardous waste for the

year 2016-17 would besubmitted online.

CHWTSDF Details

Member of CHWTSDF CHWTSDF Name Remarks

Cess Details

Cess Applicable Cess Paid If Yes, UpToYes Yes Oct 31 2016 12:00:00:000AM

Legal Actions

LegalActionTaken

Legal Record Of Company Legal Action Details Remarks

No