MANUFACTURING

PROCESS AND

FLOW DIAGRAM

Manufacturing Process for Sugar

I. Cane Preparation

In order to facilitate easy operation of juice extraction, cane preparation is a prerequisite. During same, first cane is cut into small pieces and then passed through shredder or other cane preparation devices.

II. Juice Extraction

Prepared cane is fed to 1st mill for primary extraction where same is ruptured and juice is extracted. In order to extract further residual juice, rupturing operation is repeated for 3 to 5 times in multiple mills tandum. This juice obtained is termed as secondary juice.

III. Juice Clarification

Extracted juice is weighed and analyzed for P205, CaO. Phosphate level is made up, then juice is heated up to 750C in the juice heater. Heated juice is limed up to pH 9.5 to 9.8 by milk of lime addition and neutralized with blowing SO2 gas up to 7.00 pH. Treated juice is heated further up to boiling point and sent to clarifier for setting. Analysis of clear juice for, pH CaO, colour transmitted is done to understand effectiveness of clarification. The clear juice obtained after settling is sent for evaporation and muddy juice is forwarded for filtration. IV. Muddy Juice Filtration

Muddy juice drawn from clarifier is mixed with bagacillo and sent for filtration in to vaccum filter. The filtrate obtained is treated separately in conventional liming and sulphitation process whereas the solid waste in the form of pressmud is disposed as manure.

V. Evaporation The clear juice obtained from clarifier is thin of about 15 to 16 brix. To concentrate this juice, the process of evaporation is carried out in multiple effects evaporator bodies under the vaccum to obtain thick juice syrup of about 60 to 62 brix. The syrup is bleached in to sulphitation tower by blowing SO2 gas up to pH 5.1 to 5.2. Waste gases recovered in gas absorption tower.

VI. Crystallization Crystallization is process of taking out liquid sugar from syrup and transforming it into uniform granule form. The crystallization process is carried out in three to four boiling step called as there boiling system consisting of four massecuite viz. A, B1, B2 & C. All massecuite system carried out under vaccum in single evaporator body. Each massecuite boiling consist of concentration, seeding, washing and then growing of the crystals. From A massecuite final sugar and AH & AL re-circulated in to process for B1 masseuite boiling. From B massecuite B1 sugar and used for B2 boiling, B2 massecuite product B2 sugar and B2H molasses B2 sugar melted and used for C massecuite boiling C massecuite produced C and final molasses C sugar melted and used for A boiling and final molasses spent for alcohol production. VII. Sugar Formation & Grading Sugar crystals are separated from mother liquor of massecuites by centrifugal machines. Four types of centrifugal machines are used for 4 various massecuite. From A massecuite final sugar is taken out from B1, B2 & C massecuites sugar is melted and reused in process for A massecuites. Boiling sugar obtained from A massecuite is dried, cooled and packed in jute bags after weighment. The bags are then stitched and sent to godown for stacking.

VIII. Steam and Power Generation: In addition to above, steam and power required for manufacturing process are generated in the process. The steam is generated in boiler by using bagasse as fuel. This steam is used for power generation and exhaust obtained is used for process. The excess bagasse is bailed and sent for sale or paper mill. Presently the power is generated according to actual consumption in sugar and distillery unit. IX. Co-product Management

Sugar cane is main raw material for cane sugar production. Bagasse, Press Mud and final molasses are the by-products manufactured. Bagasse is used as fuel for steam generation. Excess bagasse is stored for use in off-season whereas the loose excess is sold in open market. Press mud (filter cake) is used in the distillery's bio-composting plant along with spentwash for manure production. The molasses is stored in steel tanks and used in own distillery for production of alcohol and ethanol. Excess molasses, if any, is sold in open market. Details of storage of by-products and products is given in following table

Manufacturing Process for Co-generation

The existing Co-generation Power Plant of 32 MW have been installed with Double Extraction cum Condensing type steam turbine which operates on steam of 70 kg/cm2pressure with temperature of 5000C.There is boiler of 140 TPH with steam generation of 72 kg/cm2 and 5150C.Bagasse generated from cane crushing, excluding handling losses and bagacillo requirements is available for operation of the high pressure boiler during season of 180 days. Saved bagasse could be used during off season period for about 82 days. The steam utilization in power plant for is also done for auxiliary consumptions namely – at high pressure for soot blowing, Steam Jet Air Ejector (SJAE), gland steam condenser (GSC), at medium pressure for twin HP heater and at low pressure for de-aerator. The auxiliary power consumption, for the power plant, is about 7% to 10% of generation during season and off season periods respectively. The colony power requirement will be met by the co-generation power plant, during season& off-season periods.

Manufacturing Process of Distillery Molasses is the chief raw material used for production of alcohol. Molasses contains about 50% of total sugars, of which 30% to 33% are cane sugars and the rest are reducing sugars. During the fermentation yeast strains, such as the species of Saccharomyces cerevisiae(belonging to fungi class), convert sugar present in the molasses such as sucrose or glucose to alcohol. Sucrose is present as non-reducing fermentable sugar in all sugary raw material e.g. sugarcane and sugar beet juice, syrup and molasses. Before fermentation, yeast enzymatically converts sucrose in to glucose and fructose. Glucose and fructose are reducing monosaccharide and get converted in to ethanol and CO2 within yeast cell Conversion of glucose to ethanol takes place through a series of biochemical reactions called as Embden Mayer Hoff (EMP) pathway. Chemically, this transformation of sucrose to alcohol can be approximated by the following equation. I) C12H22O11 + H2O 2 C6H12O6 Cane Sugar Inversion Glucose II) C6H12O6 C2H5OH + 2CO2 Glucose Fermentation Ethyl Alcohol Carbon dioxide 180 2 X 46 + 2 X 44 100 kg of sugar would theoretically yield 51.11 kg of ethanol and 48.89 kg CO2. Part of glucose is used for yeast growth and by-product formation. Fermentation Process Normally, molasses is made up of water or moisture and solids. Solids are further categorized as organic and inorganic. The organic solids can be classified as fermentable sugars, non-fermentable sugars, volatile acids, nitrogenous matter, caramel, gum and waxes as well as other concentrated components which had been added during sugar processing like polyelectrolyte’s, biocides etc. The volatile acid content has profound effect on yeast performance. The term volatile acids present in molasses are acetic acid, propionic acid, butyric acid, valeric acid and isovaleric acid. The volatile acidity is expressed in terms of acetic acid. Acetic acid affects cell multiplication. As ethanol fermentation is growth-associated product, due to less growth of yeast, alcohol formation rate is decreased. This affects fermentation efficiency and capacity. Butyric acid is more potent to yeast than acetic acid for the same concentration. Saccharomyces is versatile in nature and most preferred yeast to carry out fermentation at industrial scale because of its fast growing and fast fermenting characteristics. Raw material is diluted to appropriate sugar concentration. Yeast is inoculated and fermentation is carried out at optimum temperature, pH, aeration, agitation and supplementary nutrients. The plant has been designed to produce fermented wash for producing 60,000 liters per day of total alcohol based on cane molasses as the feedstock. Fermentation section is based on HIFERM-FERMENTATION continuous / semi continuous fermentation process. The fermentation plant is four-fermenter system. The individual fermenter is equipped with molasses dilution system, aeration for mixing in fermenter, safety system etc. The process utilizes special culture yeast fast fermenting property.

In continuous mode of operation, molasses and process water are added proportionately to maintain desired alcohol concentration in individual fermenter. Fermented wash from last fermenter is passed to Clarified wash tank through Wash settling tank from which it is fed to distillation. In semi continuous mode of operation, molasses and process water are added along with yeast to maintain desired alcohol concentration in individual fermenter. After reaction completion, individual fermenter is harvested. Dedicated molasses weighing system is provided to determine molasses consumption. In spent wash recycle section, spent wash cooler and distribution system is provided. A part of spent wash from distillation section is cooled and recycled to fermentation and used as diluent by replacing process water. CO2 scrubber recovers alcohol from carbon dioxide. Alcohol scrubbed water from scrubber is further sent to clarified wash tank. Air is sparged in yeast culture vessels, activation Vessel and fermenter. Systems for dosing nutrients, sulfuric acid and de foaming agent are provided with appropriate tanks and pumps. Distillation Operation

The Multi-pressure distillation system is designed to produce Rectified Spirit, Extra Neutral Alcohol and Ethanol from fermented wash. Mainly, following columns play important role in the distillation operation. 1. CO2 stripper 2. Stripping 3. Pre-rectifier column 4. Extraction 5. Rectification 6. Refining 7. Fusel oil concentration 8. Evaporator column

The fusel oil column concentrates the heads and fusel oil and recovers alcohol. In CO2 column non-condensable gasses remove from the top. The plant is operated from control room through PLC system. The CO2 stripper, extraction and refining columns work at the pressure below the atmospheric whereas the rectifier and fusel oil columns work above atm. pressure. The rectifier column, fusel column & pre-rectifier columns are indirectly heated by steam. The pressurized vapours from the top of rectifier column supply thermal energy to the re-boiler of stripper column. The top vapours of pre-rectifier column supply the thermal energy to the re-boiler of extraction column and also to the re boiler of the refining column. The stripper column top and middle vapours supply direct heat to CO2 column. 1. CO2 Stripper Column

The fermented wash after clarification and yeast separation is pumped to the column through the Beer heater & plate heat exchanger by adjusting wash flow through flow meter. The fermented wash fed to the top of column and the vapours coming from the stripper column heat the wash. The hot wash is fed to stripper column. The non condensable gasses escapes from the top of the column and condensed in the condenser. The condensate get recycled back to the column. The non condensable gasses are connected to vacuum pump.

2. Stripper Column

Hot fermented wash from CO2 column is fed to stripper column. Spent wash at the bottom of the column is circulated by axial flow pump and passed through re-boiler and is taken out from bottom by pump. The heat recovered from outgoing spentwash through is used to heat incoming fermented wash. The alcohol vapors coming out from top of this column and fed to the pre-rectifier column under ENA mode. Otherwise, they are fed to the extraction column for operations under RS mode through pump. The spent lees from the bottom of the column are free from alcohol and are used for heating by passing through. The bottom liquid is pumped and partly fed to extraction column.

3. Pre Rectifier Column

The steam flow control valve is adjusted to get required reflux and temperature to the column. Subsequently, the bottom level of the column is checked and adjusted up to 50% and thereafter the level control valve is set on auto mode. Also, the level of reflux tank is checked. During the operation, the concentration of reflux, product and fusel oil draw is checked periodically. Then the RS draw valve is gradually opened. 4. Extraction Column

The column is designed to separate all low boiling impurities; aldehydes, esters and sulfur compounds from the feed alcohol. Addition of process water or spent less or chemicals dosing increases volatility of low boiling compound with respect to ethanol in solution containing of water. In this process the impurities of ethanol water mixture get removed at the bottom of the column. Then the impurities go on the top portion of the column. The dilution water/spent lees get heated by passing through PHEs. The top vapour from the column is condensed in main condenser and vent condenser and reflux is sent to the column through glass tube rotameter. Partly the fusel oil and other impurities are fed to FOC and the vent is connected to vacuum system. The bottom liquid containing alcohol water mixture is fed to rectifier column. 5. Rectifier Column

Rectification column is provided to accommodate the alcohol. It takes some time to build up the required alcohol profile in the column. Here, it is extremely essential to observe the temperature difference of alcohol draw plate and fusel oil draw plate which are required to be near the designed temperature. From this column, the alcohol is fed to refining column by opening the product control valve. 6. Refining Column

The refining column is mainly designed for polishing the product by removing traces of volatile impurities and maintaining aroma and flavors to meet the premium quality norms. The pure alcohol is removed from bottom of the column & after cooling it is pumped to ENA day storage section. 7. Fusel Oil Column

The impurities from rectifier column &pre-rectifier column are concentrated in this column. The concentrated heads are taken out from top of the column. Spent lees from the bottom of column are passed through PHE to recover the heat. Concentrated fusel oil is drawn from middle portion of the column and sent for decantation. Subsequently, the fusel oil is sent to the FO storage tank.

8. Fusel Oil Decanter The fusel oil comes from fusel oil column, cooled in cooler and fed to fusel oil decanter. In decanter, fusel oil is washed to remove traces of alcohol by adding process water. The fusel oil layer is taken out as by-product and the bottom liquid is recycled back to fusel oil column for further recovery. A question was asked during PH about spentwash. Consultant answered to this question as spent means waste and wash is a term used in distillery for discharges from fermentation, distillation section, etc. Thus, spent wash indicates nothing but waste discharge from a distillery, which is generated after recovery of alcohol through distillation of fermented wash. This spent wash is having dark brown colour when in fresh condition and contains considerable organic matter due to which it is good for bio-methenation. A query was raised during public hearing about type of process used for alcohol production. It was replied by consultant that continuous fermentation followed by multi-pressure vacuum distillation process is adopted in existing distillery and same shall be followed under expansion project

MPCB CONSENT TO

OPERATE ORDER

8th CAC meeting of 2017-2018 (Book-let no 13 of Consent to operate cases) dated 09.02.2018 Page 1 of 33

MAHARASHTRA POLLUTION CONTROL BOARD

Minutes of 8th Consent Appraisal Committee Meeting of 2017-2018 held on 09.02.2018 at 3.00 p.m. at MHADA Office, Grihanirman Bhavan,

Kalanagar, Bandra (East), Mumbai, Maharashtra 400051.

……….

The Consent Appraisal Committee meeting of the Board was held on 09.02.2018. Following members of the Consent Appraisal Committee were

present:

1. Shri Milind Mhaiskar, Chairman

Vice President & CEO, MHADA and

Chairperson, MPCB, Mumbai.

2. Shri. P. Anbalagan Member

Member Secretary, MPC Board, Mumbai

3. Shri. Padmakar Nandusekar Member

Technical Advisor (Environment), MIDC, Mumbai

4. Shri. P. K. Mirashe Member Conveyor

Assistant Secretary (Technical), MPC Board, Mumbai

Additional Chief Secretary, Home (Transport) Dept., Mumbai could not attend the meeting. Leave of absence was granted to them.

Following Officer of MPCB were present for the meeting:

1. Shri. V. M. Motghare, JD(APC), MPCB, Special Invitee

2. Shri. Y. B. Sontakke, JD(WPC), MPCB, Special Invitee

3. Shri A. R. Supate, PSO, Mumbai, Special Invitee

4. Shri. N. N. Gurav, Regional Officer (HQ), Mumbai, Special Invitee

Chairman of the committee welcomed the members of the committee and allowed proceeding of the meeting to start. The minutes of 7thConsent

Appraisal Committee meeting held on 11.12.2017 for 1st consent to operate and consent to establish (booklet no 10, 11) respectively and held on 12.12.2017

for renewal of consent (booklet no 12) circulated vide letter no. NO.BO/CAC-CELL/TB/B-133 dtd. 09.01.2018 were confirmed.

8th CAC meeting of 2017-2018 (Book-let no 13 of Consent to operate cases) dated 09.02.2018 Page 23 of 33

Sr.

No.

Application

unique

number

Name of Industry Decision on grant of

consent

Consent

granted up

to

Remarks/Discussion (1)

of Rs. 25 lakh obtained towards compliance of

conditional direction after receipt of verification report

from SRO.

Consent shall be issued after ;-

1] Confirmation regarding 100% recycle of effluent.

2] Submission of consent fee towards re-validation of

consent to establish as it was expired 2 months before

the application for 1st CtoO.

28. MPCB-

CONSENT-

0000033438

Technocraft Industries

(India) Limited C-5, C-

2/1-2 MIDC, Murbad,

Dist. Thane.

APPROVED

1st consent to Operate

for expansion with

increase in water

consumption, effluent

quantity and

amalgamation with

existing consent

31.12.2020 It was decided to grant 1st consent to Operate for

expansion with increase in water consumption, effluent

quantity and amalgamation with existing consent to

manufacture RUBBER GASKETS / WASHER-

10,00,000 No/D (31.5 MT/M)

1. This consent is issued with the overriding effect of

the earlier consent granted by the Board vide

consent dated 31.05.2016.

We may impose the condition that industry shall not be

allowed to treat the RO reject in the MEE at sister

concern industry located in Murbad MIDC, plot no A-

4/1.

It was also decided to return the BG of Rs. 5 lakh & BG

of Rs. 2 lakh obtained towards compliance of CtoE

condition and installation of STP as industry has

complied the same.

Consent shall be issued after –Verification report about

installation of dedicated MEE at plot no. C-5, C-2/1-2

MIDC, Murbad, Dist. Thane.

29. MPCB-

CONSENT-

0000034874

Gangamai Industries

and Constructions Ltd.

(GIACL) 222,223,224

Najik Babhulagaon

Shevgaon, Dist.

APPROVED

1st Consent to Operate

for expansion and

amalgamation with

31.08.2019 Committee noted that industry has obtained

Environmental Clearance for 30 KLPD vide letter dated

18.10.2017. Industry has provided bio-metanizaton plant

followed by MEE to achieve zero liquid discharge.

8th CAC meeting of 2017-2018 (Book-let no 13 of Consent to operate cases) dated 09.02.2018 Page 24 of 33

Sr.

No.

Application

unique

number

Name of Industry Decision on grant of

consent

Consent

granted up

to

Remarks/Discussion (1)

Ahmednagar existing consent in view of above it was decided to grant 1st consent to

operate for 30 KLPD distillery and amalgamation with

existing 30 KLPD distillery and 120 KLPD ethanol unit,

by imposing following conditions;

1. Industry shall submit Bank Guarantee of Rs. 5 lakh

towards O & M of pollution control systems and

compliance of consent conditions.

Consent will be issued after submission of NOC of

CGWA/Irrigation department for water uses.

30. MPCB-

CONSENT-

0000035295

Indiabulls Real Estate

Company Pvt. Ltd C.S

No 613 & 612 Lower

Parel Division,

Elphinstone Mill

Mumbai

APPROVED

1st Consent to Operate

for MCGM car parking

30.09.2022 It was decided to grant 1st Consent to Operate (Part) for

MCGM Parking on Total Plot Area 34,383 sq. mtrs. and

construction BUA of 91,195 sq. mtrs. (Out of Total

Construction BUA of 3,60,099 sq. mtrs. of entire project

as per amended EC dated 3.07.2017) by imposing

following condition(s);

1. PP shall re-valid and amend Consent to Establish as

per amended EC dated 3.7.2017.

2. PP shall submit affidavit in Board’s prescribed

format within 15 days regarding compliance of

conditions of Environmental Clearance (EC) and

Consent to Establish.

3. PP shall submit the affidavit within 15 days in the

prescribed format regarding the part of the built up

area/ building for which application for 1st Consent

to Operate (Part) is made and that the same is

included in the Environmental Clearance accorded.

4. Project Proponent shall submit the BG of Rs. 25

lakhs towards O & M of pollution control system.

5. PP shall achieve the treated domestic effluent

standard for the parameter BOD- 10 mg/lit.

6. The treated effluent shall be 60% recycled for

secondary purposes such as toilet flushing, air

conditioning, cooling tower make up, firefighting

etc. and remaining shall be connected to the

sewerage system provided by local body.

Consent shall be issued after:

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-0000034874

Industry Information

Consent To: IIN No.: Submit to:Operate SRO - Ahmednagar

Type of institution: Industry Type: Category: Scale:Industry R60 Distillery ( molasses / grain

/yeast based)Red 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 AddressSHRI A.L.MORE HARINAGAR , NAJIKBABHULGAON

Designation TalukaVICE PRESIDENT SHEVGAON

Area DistrictNAJIK BABHULGAON Ahmednagar

Telephone Fax9921997399 02429-217251

Email Pan Numbergangamaisugar_ind@rediffmail.com AABCG2199Q

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 nameGangamai Industries and Constructions Ltd. (GIACL)

Location of Unit Survey number/Plot NumberNajik Babhulagaon 222,223,224

Taluka DistrictShevgaon Ahmednagar

(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 Grampanchayat Najik Babhulgaon Sarapanch Grampanchayat Najik Babhulgaon

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 authorityGrampanchayat Najik Babhulgaon Sarapanch Grampanchayat Najik Babhulgaon

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 numberRanjeet P Mulay 02429217255

Fax number Officer responsible for day to day business02429217251 I.B.Inamdar

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

Registration number Date of registrationNo. 11-119930 DT.19-5-1999 May 19, 1999

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 4164.00 CA Certificate 75000.00

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 1.63 Ahmednagar-Paithan Highway

River 13.00 Dhora

Human Habitation 2.00

Religious Place 0.00 --NA--

Historical Place 0.00 --NA--

Creek/Sea 0.00 --NA--

6b. Enter Latitude and Longitude details of site

Latitude Longitude19224728 75170072

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)

270661 100945 186691

10. Month and year of commissioning of the Unit.

2014-12-27

11. Number of workers and office staff

Workers staff Hrs. of shift Weekly off0 0 8 Sunday

12.

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

Yes 150 houses are present in a residential colony within the premises.

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

10 6 Yes

(c) Indicate its location and distance with reference to plant site.Number of person staying Water consumptionHarinagar 0.5

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 Ethanol 900 900 0 900 --

DistilleryincludingFermentationIndustry

KL/M ENA 900 900 0 900 --

Products Name and Quantity

Product Name UOM Quantity RemarksFusel Oil KL/A 17 --

Compost MT 14820 Qty of compost 14820MT/season genrated

CO2 Gas MT/M 690 --

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

Yeast --NA-- 00 No No Test Tube Culture

Anitifoaming Compound Kg/M 3500 No No --

Urea Kg/M 1200 No No --

Bleaching Powder Kg/M 60 No No --

Sulphuric Acid Kg/M 3000 No No --

Caustic Soda Kg/M 200 No No --

Formaline Ltrs 100 No No --

Molasses MT/M 3600 No No --

DAP MT/M 1200 No No --

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.

Refer Manufactring Process at uploaded documents.

Part B : Waste Water aspects

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

Purpose Consumption EffluentGeneration

Treatment Remarks Disposal Remarks

Domestic Pourpose 00 00 --NA-- NA --NA-- --

Water gets Polluted& Pollutants areBiodegradable

245 240 OTHERS @245 M3/Dwaterconsumtion forprocess in which20m3/D is freshwate & 225m3/Discondensatewater.

Recycle #- Fresh Water, *- CondensateWater

Water getsPolluted,Pollutantsare notBiodegradable &Toxic

00 00 --NA-- NA --NA-- --

IndustrialCooling,spraying inmine pits or boilerfeed

70 5 OTHERS 70M3/D waterconsumption forcooling is freshwater. Effluentgented to thetune of 5 M3/D &spentl

Recycle #- Fresh Water, *- CondensateWater

Others 00

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 permittedJayakwadi Dam Jayakwadi irrigation 197.22

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

Domastic Boiler Blowdown Industrial Cooling water blowdown0 0 240 5

Process DM Plants/Softening Washing Tail race discharge from240 0 0 0

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

Refer uploaded documents fordetailed water budget.

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 0 0

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)0

Treatment unit Size (mxm) Retention time (hr)MEE 600 1

CPU 700 60

Biocomposting - 8 Acres Land 0 0

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) 9000

Effluent sump/Guard pond details Yes --

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

Yes --

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.

0 (vi) Connected to CETP 0

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

200

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 5-6

SS (mg/l) --

BOD (mg/l) 1500-1800

COD (mg/l) 2800-3000

TDS (mg/l) 1500-1800

Specific pollutant ifany

Name Value

1 -- NA

Treated Effluent

pH 7

SS (mg/l) --

BOD (mg/l) 30

COD (mg/l) 100

TDS (mg/l) 500

Specific pollutant ifany

Name Value

1 -- NA

(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 detailed water budget.

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 Steam for expansion activities is

taken from existing boiler indistillery.

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

(a) Stack number(s) (b) Stack attached to (c) Capacity (d) Fuel TypeNA NA 0 NA

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

(h) Height, m (above groundlevel)

0 NA NA 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

NA NA NA NA

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..

For existing unit industry conduct monitoring of environmental attributes viz. AAQM, Noise monitorin

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 MinNA 0

Max Method of collection Method of reception Method of storageNA NA NA

Method of transport Method of treatment Method of disposal NA NA NA

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

NA 0 NA NA

32.

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

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)For existing unit industry conduct monitoring of environmental attributes viz. AAQM, Noise monitorin

35.

Are you using any imported hazardous waste. If yes, give details.No

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 factory0

(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).Refer uploaded documents for O & M Cost.

41.

To which of the pollution control equipment, separate meters for recording consumption of electric energy are installed ?Yes, electric energy meters are provided to treatment facillity.

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 220 MT/M -- 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?Yes

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

Open Space Availability Plantation Done On Number of Trees Planted86042.19 Square meter 61350 Square meter(71 %) 10000

46.

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

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.Yes, The Industry requires Public Hearing and Environmental Clearance (EC) from Ministry of Environment, Forests and Climate Change(MoEFCC), New Delhi

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

(c) Whether Environmental Statement submitted ? If submitted, give date of submission.Environment statement for existing unit submitted for the year 2016-17. Uploaded for your reference.

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 : A. L. MOREDesignation : VICE PRESIDENT

Additional Information

Air Pollution

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

Separate EM Provided No Other Emission Sources --

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 Details

CHWTSDF Details

Member of CHWTSDF CHWTSDF Name Remarks

Cess Details

Cess Applicable Cess Paid If Yes, UpToYes No Jan 1 1900 12:00:00:000AM

Legal Actions

LegalActionTaken

Legal Record Of Company Legal Action Details Remarks

No

CERTIFICATES AND

OTHER DOCUMENTS