i1mc41y) qn:c4d'1 ,..,q''''''?lrt:im:::rltq tel: ministry of...

mlaquof fH Cfll GOVERNMENT OF INDIA

qqiC4~Ol CA~ i1MC41Y) qnC4d1 qlrTIMrlTq

MINISTRY OF ENVIRONMENT FORESTSamp CLIMATE CHANGE

Regional Office (WCZ)Ground Floor East WingNew Secretariat Building

Civil Lines Nagpur - 440001Tel 0712-2531319 (0)

0712-2531318 (F)E-mail apccfcentral-ngp-mefgovin

FNo5-2082009(~)1 Date 11052016

To

Scientist EIA Division (Industry-II)Ministry of Environment Forest amp Climate ChangeIndira Paryavaran BhawanAliganj Jorbagh RoadNew Delhi-11 0003

Sub Expansion of sugar mill capacity from 4500 TCD to 12000 TCD 100 KLPD distilleryunit and 30 MW Co-Generation Power Plant at village Pawarwadi Taluka MajalgaonDistrict Seed in Maharashtra by Mis Jay Mahesh Sugar Industries Limited-EC-reg

Ref1 Ministry of Environment Forests amp Climate Change letter no J 11011262015 - IA

II (I) dated 290420152 Ministry of Environment amp Forests IA division letter no J-1101112642007-IA-II(I)

dated 30042009

SirI am directed to invite your kind attention on the above subject and letter under

reference Monitoring report of compliance to conditions stipulated in Environment Clearance

accorded for Expansion of sugar mill capacity from 4500 TCD to 12000 TCD 100 KLPD

distillery unit and 30 MW Co-Generation Power Plant at village Pawarwadi Taluka

Majalgaon District Seed in Maharashtra by Mis Jay Mahesh Sugar Industries Limited is

enclosed herewith It is observed that

Following conditions were not complied

Specific Condition no1l

Lagoon is under construction and PCC work and lining is yet to be carried out

Specific Condition no IV

Only water level measurement has been carried out

Specific Condition no VI

Status of compliance of conditions stipulated in environment clearance and analytical

reports of monitoring were not yet uploaded on to the website Compliance reports and

analytical reports were not submitted to the Regional Office of Ministry

ipitfcHUf cR

MINISTRY OF ENVIRONMENT FORESTS

amp CLIMATE CHANGE

qiTrfTRW

GOVERNMENT OF INDIA

Regional Office (WCZ) Ground Floor East Wing New Secretariat Building

Civil Lines Nagpur - 440001 Tel 0712-2531319(0)

0712-2531318 (F)

E-mail apccfcentral-ngp-mef(5)govin

FNo5-2082009(R^r) Date 11052016

To

Scientist E

IA Division (Industry-ll)

Ministry of Environment Forest amp Climate Change

Indira Paryavaran Bhawan

Aliganj Jorbagh Road

New Delhi-110003

Sub Expansion of sugar mill capacity from 4500 TCD to 12000 TCD 100 KLPD distillery

unit and 30 MW Co-Generation Power Plant at village Pawarwadi Taluka Majalgaon

District Beed in Maharashtra by Ms Jay Mahesh Sugar Industries Limited-EC-reg

1 Ministry of Environment Forests amp Climate Change letter no J 11011262015 - IA

II (I) dated 29042015

2 Ministry of Environment amp Forests IA division letter no J-1101112642007-IA-lll)

dated 30042009

Sir

I am directed to invite your kind attention on the above subject and letter under

reference Monitoring report of compliance to conditions stipulated in Environment Clearance

accorded for Expansion of sugar mill capacity from 4500 TCD to 12000 TCD 100 KLPD

distillery unit and 30 MW Co-Generation Power Plant at village Pawarwadi Taluka

Majalgaon District Beed in Maharashtra by Ms Jay Mahesh Sugar Industries Limited is

enclosed herewith It is observed that

Following conditions were not complied

Specific Condition noll

Lagoon is under construction and PCC work and lining is yet to be carried out

Specific Condition no IV

Only water level measurement has been carried out

Specific Condition no VI

Status of compliance of conditions stipulated in environment clearance and analytical

reports of monitoring were not yet uploaded on to the website Compliance reports and

analytical reports were not submitted to the Regional Office of Ministry

Ref

Specific Condition no VII

Green belt development is in progress Proper post plantation care needs to be

ensured

General Condition no1I

No monitoring is being carried out in buffer zone

General Condition noXI

Six monthly compliance reports were not submitted regularly

General Condition noXV

PA did not inform the Regional Office about the date of financial closure and final

approval of the project by concerned authorities and date of start of land development

work

Following Conditions were partially complied

Specific Condition no I

Distillery unit is under construction

Specific Condition no III

Monthly sampling and trend analysis monitoring reports were not submitted to

Ministry

General Condition no VIII

Data on medical records was not produced during the inspection

General Condition no XIII

PA submitted that clearance letter has been submitted to concerned Panchayatl Zilla

ParishadMunicipal Corporation etc Documentary proof is not available with PA

This issues with the approval of Competent Authority

f~S~~uSuresh KumarAH~pk

Scientist 0

Encl as above

Copy to1 Director RO HQ Ministry of Environment Forest amp Climate Change Government of

India 1st Floor Agni Wing Indira Paryavaran Shawan Jorbagh Road New Delhi-110003

2 Director (Monitoring Cell) Ministry of Environment Forest amp Climate Change IndiraParyavaran Shawan Aliganj Jorbagh Road New Delhi-110003

3 Vice President MsNSL Sugars Limited village Pawarwadi Taluka MajalgaonDistrict Seed in Maharashtra



ensured

General Condition noll







work




Specific Condition no Ill


Ministry




PA submitted that clearance letter has been submitted to concerned Panchayat Zilia



Suresh Kumar Aaapa Scientist D

End as above

Copy to 1 Director RO HQ Ministry of Environment Forest amp Climate Change Government of

India 1st Floor Agni Wing Indira Paryavaran Bhawan Jorbagh Road New Delhi-

110 003

2 Director (Monitoring Cell) Ministry of Environment Forest amp Climate Change Indira

Paryavaran Bhawan Aliganj Jorbagh Road New Delhi-110003

3 Vice President MsNSL Sugars Limited village Pawarwadi Taluka Majalgaon District Beed in Maharashtra

Monitoring the Implementation of Environmental SafeguardsMinistry of Environment Forest amp Climate Change

Regional Office (West Central Zone) NagpurMonitoring Report

Part -IDATA SHEET

1 Project Type River-valley Mining Industry IndustryThermalNuclear Other (Specify)

2 Name of the Project Expansion of sugar mill capacity from 4500 TCO-12000TCD 100 KLPD Distillery unit and 30 MW Co-Generation Power Plant at village Pawarwadi TalukaMajalgaon District Seed in Maharashtra by Ms JayMahesh Sugar Industries Limited

3 Clearance Letter (s) OM No and date FNo J-11 01112642007-IAII (I) dated 300420094 Location

a District (s) Beedb State (s) Maharashtrac Latitude N 19deg 9 200196d Longitude E 76deg 13 10308

5 Address for correspondencea Address of concerned Project Chief Shri S Radha Krishnan

Engineer (with Pin Code amp Telephone Vice PresidentTelex Fax Numbers) NSL Sugars Limitedamp Unit III Jay MaheshAddress of Executive Project Engineer PawarwadiManager (with pin codefax numbers) Taluka Majalgaon

Dist BeedMaharashtraPhone 02443-203590 Fax 02443-202034

6 Salient featuresa Of the Project Enclosed as Annexure-1

b Of the Environmental Management Enclosed as Annexure-2Plan

7 Break up of the Project areaa Submergence Area Forest amp Non

Forestb Others

a Total Plot Area 100 acresb Built - Up Area (Including Road) 502 acresc Open Space available 2300 acresd Green belt area 33 acres

8 Break up of the Project affected population Not applicablewith enumeration of those losinghousesdwelling units only agricultural landonly both dwelling units amp both dwellingunits amp agricultural land amp landlesslaborersartisan

a SC STAdivasisb Others

(Please indicate whether these figures are

Monitoring the Implementation of Environmental Safeguards Ministry of Environment Forest amp Climate Change

Regional Office (West Central Zone) Nagpur Monitoring Report

Part-I DATA SHEET

1 Project Type River-valley Mining Industry Thermal Nuclear Other (Specify)

Industry

2 Name of the Project Expansion of sugar mill capacity from 4500 TCD-12000 TCD 100 KLPD Distillery unit and 30 MW Co- Generation Power Plant at village Pawarwadi Taluka Majalgaon District Beed in Maharashtra by Ms Jay Mahesh Sugar Industries Limited

3 Clearance Letter (s) OM No and date FNo J-1101112642007-IAII (I) dated 30042009 4 Location

a District (s) b State (s) c Latitude d Longitude

Beed Maharashtra N 19deg 9 200196 E 76deg 13 10308

5 Address for correspondence a Address of concerned Project Chief

Engineer (with Pin Code amp Telephone Telex Fax Numbers) amp Address of Executive Project Engineer Manager (with pin codefax numbers)

Shrl S Radha Krishnan Vice President NSL Sugars Limited Unit III Jay Mahesh Pawarwadi Taluka Majalgaon Dist Beed Maharashtra Phone 02443-203590 Fax 02443-202034

6 Salient features a Of the Project

b Of the Environmental Management Plan

Enclosed as Annexure-1


7 Break up of the Project area a Submergence Area Forest amp Non

Forest b Others

a Total Plot Area 100 acres b Built - Up Area (Including Road) 502 acres c Open Space available 2300 acres d Green belt area 33 acres

8 Break up of the Project affected population with enumeration of those losing housesdwelling units only agricultural land only both dwelling units amp both dwelling units amp agricultural land amp landless laborersartisan

a SC STAdivasis b Others


Not applicable

20

12

Financial crisis

based on any scientific and systematicsurvey carried out or only provisional figuresif a survey carried out gives details andyears of survey)

9 Financial Detailsa Project costs as originally planned amp

subsequent revised estimates and the RS300 Croresyear of price reference

b Allocations made for Environmental RS5 CroresManagement Plan with item wise amp yearwise breakup

c Benefit Cost Ratio Internal rate of -Return and the year of assessment

d Whether (c) includes the cost ofEnvironmental Management as shown in -the above

e Actual expenditure incurred on the RS34604 CroresProject so far

f Actual expenditure incurred on the Rs 199 CroresEnvironmental Management Plan so far

10 Forest land requirement Not Applicablea The status of approval for diversion

of Forestland for non-forestry useb The Status of clearing fellingc The status of compensatory

Afforestation programme in the lightof actual field experience

11 The status of clear felling in non-forest areas Not Applicable(such as submergence area of reservoirApproach roads) if any with quantitativeinformation

Status of constructiona Date of commencement (Actual

andor Planned)b Date of completion (Actual andor

Planned)

Sugar amp Co-gen startedconstruction

but distillery is under

13 Reasons for the delay if the project is yet tostart

14 Dates of site visitsa The dates on which the Project was -

monitored by Regional Office onprevious occasions if any

b Date of site visit for this monitoring 11042016Report

15 Details of correspondence with project As underauthorities for obtaining action plan information on status of compliance tosafeguards other than the routine letters forlogistic support for site visit

based on any scientific and systematic survey carried out or only provisional figures if a survey carried out gives details and years of survey)

9 Financial Details a Project costs as originally planned amp

subsequent revised estimates and the year of price reference

b Allocations made for Environmental Management Plan with item wise amp year wise breakup

c Benefit Cost Ratio Internal rate of Return and the year of assessment

d Whether (c) includes the cost of Environmental Management as shown in the above

Rs300 Crores

Rs5 Crores

e Actual expenditure incurred on the Project so far

Rs34604 Crores

f Actual expenditure incurred on the Environmental Management Plan so far

Rs 199 Crores

10 Forest land requirement a The status of approval for diversion

of Forestland for non-forestry use b The Status of clearing felling c The status of compensatory

Afforestation programme in the light of actual field experience

Not Applicable

11 The status of clear felling in non-forest areas (such as submergence area of reservoir Approach roads) if any with quantitative information

Not Applicable

12 Status of construction a Date of commencement (Actual

andor Planned) b Date of completion (Actual andor

Planned)

Sugar amp Co-gen started but distillery is under construction

13 Reasons for the delay if the project is yet to start

Financial crisis

14 Dates of site visits a The dates on which the Project was

monitored by Regional Office on previous occasions if any

b Date of site visit for this monitoring Report

11042016

15 Details of correspondence with project authorities for obtaining action plan information on status of compliance to safeguards other than the routine letters for logistic support for site visit

As under

Vj8

(The monitoring report may obtain thedetails of all the letters issued so far but thelater reports may cover only the lettersissued subsequently)

Letter from RO Reply from PALetter dated 22062009 Status and information No reply from PAcalledLetter dated 08062012 Status and information Letter dated 07072012 Status and informationcalled submittedLetter dated 05042016 Letter sent for siteinspection

(The monitoring report may obtain the details of all the letters issued so far but the later reports may cover only the letters issued subsequently)

Letter from RO Reply from PA Letter dated 22062009 Status and information called

No reply from PA

Letter dated 08062012 Status and information called

Letter dated 07072012 Status and information submitted

Letter dated 05042016 Letter sent for site inspection

sh

100 KLPD Mos~sBased Distillery 30 MW Co-gen Power Plant and ExpltinsiorT-of Sugar Mill from 4500 TCD to 12000 TCD J Final EIAIEMPAt Village Pawarwadi Taluka Majalgaon District Beed (Maharashtra) _ _ __ Re_p_ort---_I

CHAPTER-IIRAW MATERIAL AND

MANUFACTURING PROCESS

21 TYPEANDNEEDOFTHE PROJECT

Adequate State-of-Art project authority may adopt the advance process

technology and latest pollution control system for taking care of water and

air pollution as per the requirement of the Pollution Control Soard through

a new pollution control system

As a process the Environment Impact Assessment study is to be

conducted and impact due to this project during construction as well as

during operation is to be assessed and adequate mitigation measures are

to be suggested for implementation So that adverse impacts if any are

kept under control and within the permissible limits

MIs Jay Mahesh Sugar Industries ltd (JMSll) has planned to expand

capacity of its existing Sugar Mill from 4500 TCD to 12000 TCD and install

a 100 KLPD molasses based distillery to produce Ethanol ENA at village

Pawarwadi Majalgaon Town District Seed Maharashtra Along with this

to meet the power requirement company has proposed for 30 MW co-

generation power plant

As per th~ New EIA Notification dated 14th September 2006 the project

falls in Category A

22 rc CATION OF THE PROJECT

MIs Jay Mahestl ~Jgar Industries Ltd 12

d

100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion of Sugar Mil from 4500 TCD to 12000 TCD At Village Pawarwadi TaluKa Majalgaon District Beed (Maharashtra)

Final ElAEMP Report

CHAPTER-II

RAW MATERIAL AND


21 TYPE AND NEED OF THE PROJECT



air pollution as per the requirement of the Pollution Control Board through







IWs Jay Mahesh Sugar Industries Ltd (JMSIL) has planned to expand



Pawarwadi Majalgaon Town District Beed Maharashtra Along with this



As per the New EIA Notification dated 14th September 2006 the project

falls in Category A

22 LOCATION OF THE PROJECT

IWs Jay Mahampsh Lugar Industries Ltd 12

100 KLPD Molasses BSed Distillery 30 MW Co-gen Power Plant and Expansion 1- -~~I EIAIEJPof Sugar Mill from 4500 TeD to 12000 TCDAt Village Pawarwadi Tltllilky Majalgaon District Seed (Maharashtra) l Report

23 RAW MATERIALS AND UTILITIES REQUIRElvlENT

231 Water Requirement

Total water requirement for the project is 6200 m3day which includes

requirement for Sugar mill Distillery Co-generation power plant and

Colony

23l1 Water Requirement for Sugar Mill

Existing water requirement for 4500 TCD sugarcane is 1140 m3day which

would increase to 1950 m3day after the proposed expansion t012000 TCD

sugarcane

2312 Water Requirement for Distillery

Total water requirement for 100 KLPD molasses based distillery would be

2850 m3day

2313 Water Requirement for Co-generation Plant

Total water requirement for the 30 MW power plant would be 700 m3day

Table - 2Water Requirement (m3day)

Purpose Existing ProposedRequirement Requirement

Sugar Mill 1140 1950

Distillery - 2850

Power Plant - 700

Colony if any 340 700--I

To ai 1480 6200 I~--- --- p bullbullbullbull

Source Pm-feasibility Report

MIsJay Mahesh Sugar Industries Ltd 15

-----bull

-

--

-

100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion of Sugar Mill from 4500 TCD to 12000 TCD At Village Pawarwadi TaUampz Majalgaon District Seed (Maharashtra)

Final EIAEMP Report

jd

23 RAW MATERIALS AND UTILITIES REQUIREMENT




Colony

2311 Water Requirement for Sugar Mill


would increase to 1950 m3day after the proposed expansion to12000 TCD

sugarcane



2850 m3day



Table - 2

Water Requirement (m3day)

Purpose Existing Requirement

Proposed

Requirement


Distillery - 2850

Power-Plant - 700

Colony If any 340 700

Total 1480 6200

rs

mmf

Source Piq~feasibility Report

Mis Jay Mahesh Sugar Industries Ltd 15

mm

-bullbullbull

100 KLPD Molasses Ss-Zd Distillery 30 MW Co-gen Power Plant and Expansion 1of Sugar Mill from 4500 TeD to 12000 TCDAt Village Pawarwadl TaluK Majalgaon District Beed (Maharashtra) I

Fmal EINEMPReport

232 Water balance

A Water Input

Raw Water consumed = 6200 m3day

Water Contained in cane= 8400m3day

Total Water lnput = 14600 m3day

B Water Output

Water Contained in Bagasse = 1800 m3day

Water discharged with spent wash = 650 m3day

Water contained in Press mud =300 m3day

Water Evaporated in cooling water system distillery == 800 m3day

Water Evaporated in Spray pond of sugar plant =5000 m3day

Water lost as steamvapours due to leakages etc = 170 m3day

C Waste Water generated = A - B = 5880 m3day

24 MANPOWER

The total manpower required will be as follows

Table - 3

Total ManpowerExisting Requirement Proposed Total

Requirement Requirement

Sugar Mill 350 50 400

Distillery - 75 75+-- ----~ --- ---

I Power Plant 20 I 20I - I

I----------- J------- --

Total I 350 145 i 495I --_ --- I - - - -Source Pre-feasibilily riI[Jort

--------------------~-------- -bull-----s Jay MaheshSugar Irvtustries Ltd 16

Imdash

gtbull

-

p

Itei

100 KLPD Molasses Based Oistiltcry 30 MW Co-gen Power Plant and Expansion of Sugar Mill from 4500 TCD to 12000 TCD At Village Pawarwadi Taluks Majalgaon District Seed (Maharashtra)

Final EIAEMP Report

232 Water balance

A Water Input



Total Water Input = 14600 m3day

B Water Output




Water Evaporated in cooling water system distillery = 800 m3day


Water lost as steamvapours due to leakages etc =170 m3day


MANPOWER 24


Table - 3

Total Manpower

Hiiiwt Existing Requirement Proposed Total



Distillery - 75 75

IIIIM Power Plant - 20 20

Total 350 145 495

Source Pre-feasibility Report

Ws Jay Mahesh Sugar Industries Ltd 16

100 KLPD Molasses Based Distillery 30MVi f~-g-emiddotn--=P-ow-e-r-PC-Ia-n---t-amiddotn-d--=-Ex-p-a-ns---io-n-----------~middotlFinal EIAJEMP Iof Sugar Mill from 4500 TeD to 12000 TeD I

At Village Pawarwadi Taluka Majalgaon Distnct Beed (Maharashtra) Report IL-~~ __ ---- __ ~--~-~--~~ __ ~~ --~ __ -------

For employment in unskilled category preference will be given to local

people Employment in skilled category will be done from outside if the

skilled labour force is not available in local areas

241 Power

The total power requirement for the existing plant is 4 MW which would

increase to 13 MW (During Season) and 4 MW (During Off-Season) after

the proposed project Power requirement would be met from proposed co-

generation plant 135 TPH steam from high pressure boiler will be fed to

back pressure turbine to generate 30 MW power which will fulfill the

process steam requirement of Sugar mill and distillery 40 TPH steam from

existing low pressure boiler will be used for boiler feed water heating and

distillery

Two D G Sets of 1000 KVA capacity is proposed to be installed for the

complete power back up in addition to the existing two D G Sets of 160

KVA and 625 KVA capacity each Details are given in table below

Table - 4Power Requirement

Purpose Existing requirement Total requirement

Sugar Mill 4MW 10MW

Distillery - 125 MW

Power Plant - 15 MW(during season)

25 MW (during off season)

Colony - 025 MW

Total 4MW 13 MW(During Season)

I 4 MW (During Off-Season)____-l ---



-------bullbull-

bullbullbull

100 KLPD Molasses Based Distillery 30 MW Co-cjen Power Plant and Expansion of Sugar Mill from 4500 TCD to 12000 TCD At Village Pawarwadi Taluka Majalgaon District Beed (Maharashtra)

Final EIAEMP Report




241 Power








distillery




Table - 4

Power Requirement


Sugar Mill 4 MW 10 MW

Distillery - 125 MW

Power Plant 15 MW(during season)


Colony - 025 MW

Total 4 MW 13 MW(During Season)

4 MW (During Off-Season)



bull100 KLPD MO3sses Based Distillery 30 MW Co-qen Power Plant and Expa- sionof Sugar Mill from 4500 TCD to 12000 TCDAt Village Pawarwadi Taluka Majalgaon District Beed (Maharashtra)

Final EIAEMPReport

Table - 5

Details of DG Set-----_ ---

S No of Capacity Height of No of Fuel FuelNo DG sets stacks stack used consumption

1 1 160 KVA 25m 1 HSD 0756 KUday(Existing)

~1 625 KVA 50m 1 HSD 2750 KUdaymiddot

(Existing)

3 2 1000 KVA 7 m each 1 HSD 8500 KUday

(Proposed)


The fuel consumption is when the DG set runs at rated capacity However

these DG sets are installed for emergency use only and will be required to

run for about 10-15 days only in a year when the turbine is not running

2411 Details ofFuel Used

Bagasse coming out of sugar milling plant is utilised as fuel for boiler For

the proposed project daily consumption will be about 1500 TPD and steam

generated from this boiler will be utilized for generation of power in a

steam turbine

2412 Source of Fuel

Table - 6Fuel Source

Raw Source Distance Mode ofMaterial Transportation

Bagasso Captive generation from own Within the Bagasse conveyors

I sugar mill premises

i I

Road TankersDiesel I Oil dealers depots 25Km ____1__ --

MIsJay MaheshSugar Industries Ltd 18

100 KLPD Mofasses Based Distillery 30 MW Co-gen Pover Plant and Expansion of Sugar Mill from 4500 TCD to 12000 TCD A Village Pawarwadi Taluka Majalgaon District Beed (Maharashtra)

Final EIVEMP Report

Table - 5

Details of DG Set

s

No

No of

DG sets

Capacity Height of

stacks

No of

stack

Fuel

used

Fuel

consumption

1 1 160 KVA

(Existing)

25m 1 HSD 0 756 KLday

2 1 625 KVA

(Existing)

50m 1 HSD 2750 KUday

3 2 1000 KVA

(Proposed)

7 m each 1 HSD 8500 KLday





2411 Details of Fuel Used




steam turbine

2412 Source of Fuel

Table - 6

Fuel Source

Raw

Material

Source Distance Mode of

Transportation

Bagasse Captive generation from own

sugar milt

Within the

premises

Bagasse conveyors

Diesel Oil dealers depots 25 Km Road Tankers

Ms Jay Mahcsh Sugar Industries Ltd 18

-2

100KLPDMolasses Based Distillery 30 MW Co-gen Power Plant and Expansion Finalof Sugar Mill from 4500 TCD to 12000 TCDAt Village PawarwadiTaluka Majalgaon District Beed (Maharashtra) EIAJEMPReport

CHAPTER-VIIIENVIRONMENTAL MANAGEMENT PLAN

81 INTRODUCTION

The Environmental Management Plan consists of the set of mitigation

management monitoring and institutional measures to be taken during

implementation and operation to eliminate adverse environmental impacts

or reduce them to acceptable levels The present environmental

management plan addresses the components of environmental affected

during construction of the plant and by the different activities forming part

of the processes of manufacturing of Insecticides

The aims of EMP are

gt Overall conservation of environment

Minimization of waste generation and pollution

gt Judicious use of natural resources and water

raquo Safety welfare and good health of the work force and populace

Ensure effective operation of all control measures

raquo Vigilance against probable disasters and accidents

gt Monitoring of cumulative and long time impacts


82 POST-PROJECT OPERATIONS

Detailed study of the pre-project commissioning environment as also the

likely (and predicted) implications after the plant commissioning suggests

that the following preventivecontrol measures are considered necessary

to reduce the adverse impact to the utmost practicable limit


1~

cr

u

u

i^

1-

iBfMa An^6Û^-2-

100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion of Sugar Mill from 4500 TCD to 12000 TCD At Village Pawacwadi Taluka Majalgaon District Beed (Maharashtra)

Final

EIAEMP Report

CHAPTER-VIII

ENVIRONMENTAL MANAGEMENT PLAN

81 INTRODUCTION








The aims of EMP are


gt Minimization of waste generation and pollution


gt Safety welfare and good health of the work force and populace

gt Ensure effective operation of all control measures

gt Vigilance against probable disasters and accidents








Ms Jay Mahesh Sugar Industries Ltd 146

100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansionof Sugar Mill from 4500 TCD to 12000 TCDAt Village Pawarwadi Taluka Majalgaon District Beed (Maharashtra)

Final

EIAIEMP Report

821 Air Environment

Two main source of air pollution are 0 G Sets and boilers The sources of

air pollution are not having much significance as OG sets will operate only

during emergencies and major power generation coming from own Steam

Turbines The clean agro based fuel Bagasse is utilized for production of

Steam The emission from boiler and all DG set will be taken care by

providing adequate stack heights as per the CPCB regulations DG set

will be used in case of emergency situations However the required stackheight will be provided

---

--Two OG Sets of 160 KVA amp 625 KVA are already operating in the

existing plant and two sets of 1000 KVA (each) are proposed to be

installed for emergency operation The safe stack height calculated is as

under --

a) DG set Capacity = -160 KVA --H h + 02 J 160 -=

= h + 25

Hence a safe stack height around 25 meters above the roof

b) DG set Capacity = 625 KVA

H = h + 02 J 625

= h + 5


c) OG set Capacity = 1000 KVA -bullbull~-

-----

-

-~-

11-56

= h + 632

Hence a safe stack height around 7 meters above the roof is provided for

the DG sets of 1000 KVA (each) respectively Details are given in table

below

MIs Jay Mahesh Sugar Industries Ltd 147

o

O

n

100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion of Sugar Mill from 4500 TCD to 12000 TCD At Village Pawarwadi TaluKa Majalgaon District Beed (Maharashtra)

Final EIAEMP Report

x

821 Air Environment

Two main source of air pollution are D G Sets and boilers The sources of

air pollution are not having much significance as DG sets will operate only





will be used in case of emergency situations However the required stack

height will be provided

Two DG Sets of 160 KVA amp 625 KVA are already operating in the



under -

a) DG set Capacity - 160 KVA

H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5


c) DG set Capacity = 1000 KVA

h + 632



below

W

ltw

ma w


I

100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion Finalof Sugar Mill from 4500 TeD to 12000 TCDAt Village Pawarwadi Taluka Majalgaon District Seed (Maharashtra) ElAlEMP Report

TABLE 58Details of Boiler and D G set

Is Sources Nos Capacity Type and Stack PollutionNo Quantity Height

of Fuel1 Boiler

1 135 TPH Bagasse 65m ESPProposed 1500 TPD

2 20TPH Bagasse 65 m each WetExisting each 500 TPD scrubber

2 DG Set 2 1 X160 HSD 25mExisting KVA 0756 above

KUday roof level

1 X 625 HSD 50m AdequateKVA 2750 above stack

KUday roof level heightI 3 DG Set 2 HSD 70m and

2 x1000 85 KUday each acoustic

Proposed KW aboveenclosure

roof levelSource Pre-feasibility Report

8211 Sugar Mill

There are no pollutants emitted from the process into air as there are no

such emission points present in the process of manufacture The process

uses sulphur-di-oxide gas for sulphitation of juice As an abundant

precaution an absorber is installed in the vent of the sulphiter and the rawjuice passes through this scrubber and then it goes to the sulphiter So if

any sulphur dioxide remains unabsorbed in the sulphiter the same will get

absorbed in the raw juice in the scrubber

8212 Thermal Power Plant

Electro Static Precipitator ie ESP will be installed to the boiler flue gas

exhaust to the stack This ESP is designed with 2 chambers containing the

charging and discharging electrodes for full steam generation capacity of

the boiler This ESP is adequate to keep the SPM level in flue gas below

the prescribed level of 150 ppm


100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion of Sugar Mill from 4500 TCD to 12000 TCD At Village Pawarwadi Taluka Majalgaon District Beed (Maharashtra)

Final EIAEMP Report

TABLE 58

Details of Boiler and D G set

Source Pre-feasibllity Report

8211 Sugar Mill




precaution an absorber is installed in the vent of the suiphiter and the raw

juice passes through this scrubber and then it goes to the suiphiter So if

any sulphur dioxide remains unabsorbed in the suiphiter the same will gat








s No

Sources Nos Capacity Type and Quantity of Fuel

Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD

65 m each Wet scrubber

2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level

Adequate stack height and acoustic enclosure

1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level


bull100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion Finalof Sugar Mill from 4500 TCD to 12000 TCDAt Village PawarwadiTaluka Majalgaon District Seed (Maharashtra) EIAIEMPReport

8213 Distillery

There are no visible sources of air pollution However carbon dioxide gas

is evolved during fermentation process and is discharged into atmosphere

As this carbon dioxide gas could carry some ethanol vapours with it it is

scrubbed with water in a scrubber Water containing traces of ethanol is

recycled back into the process However following practices would be

adopted

1 Development of Green Belt within the premises of the plant will help

in attenuating the pollutants emitted by the plant

2 Ambient air quality and stack emission would be regularly

monitored to ensure that ambient air quality standards and

suggested limits on stack emission loads would be met honestly at

all the time

3 The ambient air monitoring will be carried out regularly in the work

zone and surrounding areas which shows that ambient air levels of bull

the contaminants are well below the stipulated norms

4 From the foregoing account it is quite clear that there shall be no

significant effect on the air quality The only regular aerial emissions

are due to burning of fuel All the S02 NOxbull SPM generated

through burning assume to be discharge to only one stack of the

boiler or incinerator

822 Water Environment


requirement for sugar mill distillery co-generation power plant and colony

Details of waste water management are given below


--

-

100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion of Sugar Mill from 4500 TOO to 12000 TCD At Village Pawarwadi Taluka Majalgaon District Beed (Maharashtra)

Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time


zone and surrounding areas which shows that ambient air levels of




are due to burning of fuel All the SO2 NOx SPM generated






Details of waste water management are given below ^

flU

Mis Jay Mahesh Sugar Industries Ltd 149 W

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100 KLPD Molasses Based Distillery 30 MW Co-qen Power Plant and Expansion Finalof Sugar Mill from 4500 TCD to 12000 TCDAt VillagePawarwadiTalukaMajalgaonDistrictSeed (Maharashtra) EIAIEMPReport

8221 Sugar Mill

To treat the liquid effluents from sugar mill 750 m3day effluent treatment

plant is already installed for the 4500 TCD capacity One more effluent

treatment plant with a capacity to treat 250 m3hr effluents will be installed

for the additional 7500 TCD sugarcane capacity

8222 Power Plant

About 1 m3 Ihr liquid effluent will be generated from boiler as boiler blow

down The same will be treated along with the sugar mill effluent in the

effluent treatment plant Treated effluent will be used for green belt

development

Mis Jay Mahesh Sugar Industries ltd 150

1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill



treatment plant with a capacity to treat 250 nrVhr effluents will be installed


8222 Power Plant

About 1 m3 hr liquid effluent will be generated from boiler as boiler blow

down The same will be treated along with the sugar mill effluent In the


development

L

U

IWs Jay Mahesh Sugar Industries Ltd 150

1^6

REIAIEMP ReportProposed 100 KLPD Molasses Based Distillery 30 MW Co-gen PowerPlant and Expansion of Sugar Mill from 4500 TPD to 12000 TPDAt Village Pawarwadi Majalgaon Town District Beed (Maharashtra)

8223 Distillery

Effluent discharged from the distillery process commonly known as spent

wash is one of the most polluting effluents with very high values of BODand COD

The company management has viewed the treatment technology to be

adopted and wishes to go for an environmental friendly option ie

concentration and incineration This will have the following advantages

bull This option is more environmental friendly

bull The steam generated from the incinerator will be used as fuel in

boiler

The treatment scheme is a five effect including Finisher Evaporation Plant

for spent wash evaporation Basic working principle includes

bull Shell amp Tube type evaporators with highly efficient liquid distributor

working on the principle of falling film and forced circulation

evaporation will be used with shell amp tube type Preheater for

preheating of feed stream which serves the purpose of energy

conservation

bull Steam will be fed to the first effect evaporator shell side and to the

finisher shell side at the given pressure and temperature as theheating medium

bull The feed solids considered are 1625 ww TS

The feed follows the flow path as

bull The product is obtained at 55-58 ww TS

bull A shell amp tube type surface condenser is employed for condensing

the vapors generated Cooling water is used as the cooling

medium

bullbull s Jay Mahesh Sugar Industries Ltd 152

o

0

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Proposed 100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion of Sugar Milt from 4500 TPD to 12000 TPD REIAEMP Report At Village Pawarwadi Majalgaon Town District Beed (Maharashtra)

8223 Distillery


wash is one of the most polluting effluents with very high values of BOD

and COD






boiler







conservation


finisher shell side at the given pressure and temperature as the

heating medium






medium


))

~)

Proposed 100 KLPD Molasses Based Distillery 30 MW Co-gen PowerPlant and Expansion of Sugar Mill from 4500 TPO to 12000 TPOAt Village Pawarwadi Majalgaon Town District Seed (Maharashtra)

REIAIEMP Report

bull The pure and the process condensate are collected in receiving

vessels

bull Highly efficient operating pumps will be provided for pumping the

required fluid

bull The operation of the plant is under vaccum which is created with

the help of a water ring type vaccum pump

bull The plant is having high level of automation to get consistent outputat required concentration

The waste water of 1200 tonsday from the distillation called the molasses

alcohol slops generate has a solid content of about 12 and the organic

particle content of about 9 to 10 Molasses alcohol slops is concentrated

in a multi effect evaporator to a concentration of about 55 to 60 of solid

content then is piped to a storage tank as fuel of 260 tonday The

condensate from No 1 effect will be recycled as boiler feed water to boiler

and condensate from the last three effects can be used for dilution

The Boiler burning concentrating slops will burn CoalRice Husk during

start up to raise the furnace and bed temperature to 900 degCThen the

concentrated slops will be injected in by a high pressure pump at a rate of

108 Uhr and is sprayed to be burn in the boiler When burning only slops

the steam output can reach 186 tonshr For effectively burning of slop

30 makeup fuel (Rice HuskCoal) is required The total output of Boiler

with slop and Rice Husk can reach 25 Tonshr In this way 16 Thr of Rice

husk of 3200 Kcallkg heat value to be added The Flue gas from the

burning of slops first pass the ash separator in the furnace outlet where

the part of coarse ash is separated pass the special design back end

boiler bank to release the heat and heat the boiler water then pass the

ash separator and 10 fan to discharged into the air The Coarse ash from

the burning and ash collected by the scrubber can be recovered as

materials for fertilizer for its 11-17 K20 content


--bull-bull-

^ Proposed 100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion of Sugar Mill from 4500 TPD to 12000 TPD REIAEMP Report At Village Pawarwadi Majalgaon Town District Beed (Maharashtra)


vessels


required fluid



bull The plant is having high level of automation to get consistent output

at required concentration








The Boiler burning concentrating slops will burn CoatRice Husk during

start up to raise the furnace and bed temperature to 900 0CThen the


108 thr and is sprayed to be bum in the boiler When burning only slops




husk of 3200 Kcalkg heat value to be added The Flue gas from the




ash separator and ID fan to discharged into the air The Coarse ash from


materials for fertilizer for its 11-17 K2O content

V

V


laquo

Proposed 100 KLPD Molasses Based Distillery 30 MW Co-gen PowerPlant and Expansion of Sugar Mill from 4500 TPD to 12000 TPDAt Village Pawarwadi Majalgaon Town District Seed (Maharashtra)

REIAEMP Report

The Biological Energy of the organic particles in the slops can be

converted to the Thermal Energy after burning which is used in the boiler

and produce steam of 186 Thr and 64 Thr of steam is produced by Rice

Husk at 45 Kgcm2 This steam is superheated in the separate fired

superheater to 440degC The SH steam is sent to a back pressure Turbine

to generate power of 22 MW (approx) Part of the Exhaust steam can be

used as the heat media in concentration where the condensate is

produced and can be used as boiler feed water Part of the steam can be

used as heat media for alcohol production saving the energy consumption

in production

The waste water is concentrated and then burned The Thermal energy

from the burning can be used for concentration and alcohol production

Steam is recycling and ash can be reused as a material for fertilizer for its

11-17 K20 content

TABLE 59Performance Parameters

SNo Description Units Technical Data

1 Feed rate to TPH 3772evaporator

2 Total solids in fess OOWNV 1625

3 Product rate TPH 1114

4 Feed temperature DC 55

5 Water Evaporation TPH 2658Rate

6 Total Solids in OOWMf 5558 Product

7 Total Steam TPH 886Required


)

Proposed 100 KLPD Molasses Based Distillery 30 MW Co-gen Power Plant and Expansion of Sugar Mill from 4500 TPD to 12000 TPD At Village Pawarwadi Majalgaon Town District Beed (Maharashtra)

REIAEMP Report





superheater to 440 0C The SH steam is sent to a back pressure Turbine


used as the heat media in concentration where the condensate Is



in production




11-17 K2O content

TABLE 59

Performance Parameters


1 Feed rate to

evaporator

TPH 3772

2 Total solids in fess WW 1625


4 Feed temperature 0C 55

5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886

M$ Jay Mahesh Sugar Industries Ltd 3 54

Proposed 100 KLPD Molasses Based Distillery 30 MWCo-gen PowerPlant and Expansion of Sugar Mill from 4500 TPD to 12000TPDAt Village Pawarwadi Majalgaon Town District Seed (Maharashtra)

REIAIEMP Report

TABLE 60Specification and Requirement of Units for Spent wash

Evaporation Plant1 I Cooling WaterSoft Water

a) cooling water recirculation rate stand aloneevaporation plant ( 31oc max3G kgcm2 (g)delta T=10 deg

copy during molasses as feed stock

Cooling water make up for evaporation

Soft water for vacuum and other pumps

2 Steams

Saturated and regulated steam at constant pressure of 15 plusmn 005kgc2 (g) should be provided at the inlet of stream header for standalone evaporation plant

3 Electricity for main Connected load (kwh) Operating loadplant (kwh)

A Based on molasses 5500 5000as feed stock

-bull

---

-bull

--bull--

MIs Jay Mahesh Sugar Industries Ltd )55


REIAEMP Report

TABLE 60

Specification and Requirement of Units for Spent wash Evaporation Plant

1 Cooling WaterSoft Water

a) cooling water reclrculation rate stand alone

evaporation plant ( 31oc max(30 kgcm2 (g)

delta T=10 deg




2 Steams

Saturated and regulated steam at constant pressure of 15 + 005

kgc2 (g) should be provided at the inlet of stream header for stand

alone evaporation plant

3 Electricity for main

plant

Connected load (kwh) Operating load

(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V

Nils Jay Mahesh Sugar Industries Ltd 155

v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL

-----------[VACUUM PUMP bull

DIAGRAM OF NATURAL CONCENTRATION BURNING SYSTEM

823 Solid Waste Environment

There are three types of solid wastes

Ash will be generated from steam boilers and spent wash incinerator

Secondly bio-degradable sludge will be generated from effluent treatment

plant which will be dried in sludge drying beds This dried sludge and ash

will be mixed with press mud from sugar mill and used as manure



REIAEMP Report

PREOCESS DIAGRAM

SrEAMTURflCtf CWlMNEr ETOM Tc WATER ASre FiJUE GAS

| Q^jTa t ekvmdash[ sr-LTiEFrccT rvAPC^nof -t [ cojcc on m ytf ftKlta nrm fa xampi scwu-me f

I crcoNoeltsî|~gt |_QCraquorx [ Cjyu tJfecT conoehsaji

| PROCESS DIAGRAM [ I fOTASSICFtmilUEw

-CIASBAM

VACUUM PmiP

COKDpoundM5Ch XX5LNC TO-AIR

J bullt^plusmn-rr i COLD WATER PCW CVCUNOCOOtPJG WATER PUMP j r MAKEUP

I I WATER Imdash^^WCE^SATEPUUP SjERnHpoundTpoundRU^-poundm

U uimdash4imdashi K WASTPWATGR STEAM r~ U U 1 (mdashj [ hO TAN

rzin s

TANK turbine

STEAM FOR PROCESS

SLOPS BUHNINS LER ADOED FUEL

FECO WATER PUMP YCTON

CONCENTRATED SiOPS TANK

c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN








IWS Jay Mahesh Sugar Industries Ltd 156

Proposed 100 KlPD Molasses Based Distillery 30 MW Co-gen PowerPlant and Expansion of Sugar Mill from 4500 TPD to 12000 TPDAt Village Pawarwadi Majalgaon Town District Beed (Maharashtra)

REIAIEMP Reportn)

Press Mud

The quantity of press mud that will be generated from the clarification of

raw juice will be about 35 of sugarcane processed So with the

proposed capacity of 12000 TeD of sugar mill 420 MT press mud will be

generated every day based on a season of 180 days total press mud

generated would be 75000 MT This press mud as it is a very good

manure as it contains a lot of nutrients and will be used as a fertilizer in

growing sugarcane

Sludge from ETP

There will be some excess sludge generated in effluent treatment plant

from primary clarifier and aerobic through secondary clarifier The same

shall be dried in sludge drying beds The water coming out from the sludge

beds will be recycled back to the effluent treatment plant Dried sludge will

be used as manure as it is in the agricultural fields around the industry

AshTo generate 135MTIhr steam in the boiler about 6222 MTIhr bagasse will

be burnt in the boiler This bagasse contains about 1 ash ie about 620

kghr The same will be discharged from the boiler furnace bottom As itwill be hot it will be cooled with water and then collected This boiler ash

will be used along with press to produce manure

824 NoiseOdour Environment

There is no danger of noise pollution from Mis Jay Mahesh Sugar

Industries Ltd The green belt will (plantation of dense trees across

the boundary) help in reducing noise levels in distillery plant as a

result of attenuation of noise generated due to plant operations and

transportation

bull D G set will be kept in acoustic enclosure

bull It is proposed to monitor the ambient odour level and work zone

odour level by sensing

Mis Jay MaheshSugar Industries Ltd 157

bull

Proposed 100 KLPD Molasses Based Distillery 30 MW Co-gen Power ~ Plant and Expansion of Sugar Mill from 4500 TPD to 12000 TPD REIAEMP Report

At Village Pawarwadi Majalgaon Town District Beed (Maharashtra)

Press Mud



proposed capacity of 12000 TCD of sugar mill 420 MT press mud will be




growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V


from primary clarifier and aerobic through secondary clarifier The same -J s-

shall be dried in sludge drying beds The water coming out from the sludge _ bullv



Ash

To generate 135MThr steam in the boiler about 6222 MThr bagasse will


kghr The same will be discharged from the boiler furnace bottom As it

will be hot it will be cooled with water and then collected This boiler ash



There is no danger of noise pollution from Ms Jay Mahesh Sugar




transportation

mdash 1 D G set will be kept in acoustic enclosure

It is proposed to monitor the ambient odour level and work zone



mdashi ^

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REIAIEMPReport

Program to Create awareness for odour attenuation and mitigation

program would be under taken

bull Earmuffs would be used while running the equipments of the plant

825 Green Belt Development

Green belt will be developed inside the factory premises covering a total

area of about 33 acres(33) of the total plot area The unit will also

develop the nearby area around the industry for greenbelt The inter-

spaces between plants will be laid with shrubs It is proposed to double

the tree density in the future Taking into consideration the nature of

pollutants availability of space and dominant wind directions

Recommendations given by expert committee on plantation requirements

in the premises of the plant would be fully implemented This will help in

reducing the concentration of pollutants and will also be effective in

attenuating noise levels

MIs Jay Mahesh Sugar Industries Ltd has social obligation to recreate the

environmental status by providing thick green cover to suppress fugitive

emission and provide aesthetic beauty Trees form the important part of

the biosphere in the Ecosystem

A layout of green belt or tree plantation ar~und the proposed project of

MIs Jay Mahesh Sugar Industries Ltd which will help to arrest the

particulate matter in the area and hence attenuate the pollution to a greatextent

The following characteristics would be taken into consideration while

selecting plant species for green belt development and tree plantation

bull Fast growing and tall trees

bull They should have large leaf area index

bull They should not have any noticeable effect on the plant yield due to

gaseous pollutants

bull The planting should be in appropriate alternate rows around the

proposed site to prevent lateral pollution dispersion


)

o


REIAEMP Report



Earmuffs would be used while running the equipments of the plant




mdash_ develop the nearby area around the industry for greenbelt The inter-


bdquo the tree density in the future Taking into consideration the nature of

_ ^ pollutants availability of space and dominant wind directions





Ms Jay Mahesh Sugar Industries Ltd has social obligation to recreate the




A layout of green belt or tree plantation around the proposed project of

Ms Jay Mahesh Sugar Industries Ltd which will help to arrest the

particulate matter in the area and hence attenuate the pollution to a great

extent



Fa^t growing and tall trees

They should have large leaf area index

They should not have any noticeable effect on the plant yield due to

gaseous pollutants

The planting should be in appropriate alternate rows around the


Ms Jay Mahesh Sugar industries Ltd 158 t

STATUS OF COMPLIANCE TO CONDITIONS OF ENVIRONMENTAL CLEARANCEOM No J-11 01112642007- IA II (I) dated 30042009

S No Condition Compliance Status

A - Specific conditionsI The effluent generated from the sugar

plant and the boiler blow down aftertreatment shall be used for green beltdevelopment The treated effluentshall conform to the prescribedstandards The spent wash from thedistillery unit shall be concentrated in amultiple effect evaporator andincinerator in the bagasse fired boilerto achieve zero discharge

Partly compliedEffluent generated from the sugar plant andboiler blow down is used for irrigation purposein the 70 hectares of agricultural land owned bythe project the after necessary treatmentDistillery unit is under construction

ii The spent wash shall be stored inimpervious pucca lagoons The spentwash lagoons shall have proper liningwith HOPE and shall be kept in propercondition to prevent ground waterpollution As per the CPCBrecommendation storage for theconcentrated spent wash shall notexceed 5 days capacity The capacityfor storage of treated effluent for thesugar unit shall not be more than 15days

Not compliedThe distillery unit is under construction Lagoonis under construction PCC work and lining isyet to be carried out

iii Adequate numbers of ground waterquality monitoring stations by providingpiezometers around the plant andproject area shall be set up Samplingand trend analysis monitoring must bemade on monthly a basis and reportsubmitted to State Pollution ControlBoard and this Ministry

Partly compliedAs per the monitoring report ground waterquality is monitored at 5 locations Howeverlocation details were not given in the monitoringreportMonthly sampling and trend analysismonitoring reports were not submitted toMinistry

iv The company shall carry out hydrogeological study of the area and reportsubmitted to the Ministry within a year

Not CompliedPA only carried out water level measurement

v Particulate emissions from the135TPH bagasse fired boiler and 2X20 TPH boilers shall be controlled byinstallation of ESP and wet scrubberrespectively The emissions shall bedispersed through stack of 65m heightThe DG sets shall be provided withacoustic enclosures to mitigate noisepollution and gaseous emissions shallbe dispersed through stack height asper CPCB standards

Partly CompliedESP has been installed for the 135 TPHbagasse fired boiler 2X20 TPH boilers Wetscrubber has not been installed Stack height of65 meters has been installed

STATUS OF COMPLIANCE TO CONDITIONS OF ENVIRONMENTAL CLEARANCE OM No J-1101112642007- IA II (I) dated 30042009


A - Specific conditions i The effluent generated from the sugar

plant and the boiler blow down after treatment shall be used for green belt development The treated effluent shall conform to the prescribed standards The spent wash from the distillery unit shall be concentrated in a multiple effect evaporator and incinerator in the bagasse fired boiler to achieve zero discharge

Partly complied Effluent generated from the sugar plant and boiler blow down is used for irrigation purpose in the 70 hectares of agricultural land owned by the project the after necessary treatment Distillery unit is under construction

ii The spent wash shall be stored in impervious pucca lagoons The spent wash lagoons shall have proper lining with HDPE and shall be kept in proper condition to prevent ground water pollution As per the CPCB recommendation storage for the concentrated spent wash shall not exceed 5 days capacity The capacity for storage of treated effluent for the sugar unit shall not be more than 15 days

Not complied The distillery unit is under construction Lagoon is under construction PCC work and lining is yet to be carried out

iii Adequate numbers of ground water quality monitoring stations by providing piezometers around the plant and project area shall be set up Sampling and trend analysis monitoring must be made on monthly a basis and report submitted to State Pollution Control Board and this Ministry

Partly complied As per the monitoring report ground water quality is monitored at 5 locations However location details were not given in the monitoring report Monthly sampling and trend analysis monitoring reports were not submitted to Ministry

iv The company shall carry out hydro geological study of the area and report submitted to the Ministry within a year

Not Complied PA only carried out water level measurement

V Particulate emissions from the 135TPH bagasse fired boiler and 2X 20 TPH boilers shall be controlled by installation of ESP and wet scrubber respectively The emissions shall be dispersed through stack of 65m height The DG sets shall be provided with acoustic enclosures to mitigate noise pollution and gaseous emissions shall be dispersed through stack height as per CPCB standards

Partly Complied ESP has been installed for the 135 TPH bagasse fired boiler 2X20 TPH boilers Wet scrubber has not been installed Stack height of 65 meters has been installed

vi The company shall upload the status Not Compliedof compliance of the stipulated Status of compliance of conditions stipulated inenvironmental clearance conditions environment clearance and analytical reports ofincluding results of monitored data on monitoring were not yet uploaded on to theits website and shall update the same websiteperiodically It shall simultaneously be Compliance reports and analytical reports weresent to the Regional office of MOEF not submitted to the Regional Office of Ministrythe respective Zonal office of CPCBand the State Pollution Control BoardThe criteria pollutant levels namelySPM RSPM S02 NOx (ambientlevels as well as stack emissions) orcritical sectoral parameters indicatedfor the project shall be monitored anddisplayed at a convenient locationnear the main gate of the company inthe public domain

VII Green belt in 33 of the plant area Not Compliedshall be provided to mitigate the Green belt development is in progress Propereffects of fugitive emissions all around post plantation care needs to be ensuredthe plant and compost yard as per theCPCB guidelines in consultation withthe local DFO

viii Company shall adopt rainwater Compliedharvesting measures to recharge the Rainwater harvesting measures have beenground water implemented

B - General Conditionsi No further expansion or modifications

in the plant shall be carried out without PA agreed to comply withprior approval of the Ministry ofEnvironment and Forests

ii Ambient Air Quality Monitoring Stations Not compliedshall be set up in the down wind Ambient air quality monitoring is done at onlydirection as well as where maximum one location No monitoring is done in bufferground level concentration of SPM zoneS02 NOx are anticipated inconsultation with the State PollutionControl Board

iii Adequate number of influent and Compliedeffluent quality monitoring stations Monitoring of water quality is carried out at ETPshall be set up in consultation with the inlet and outletState Pollution Control Board Regularmonitoring should be carried out forrelevant parameters

iv The industry shall ensure that the Compliedtreated effluent and stack emissions Stack monitoring is being carried out A sensorfrom the unit are within the norms has been installed in the stack for monitoring ofstipulated under the EPA rules or stack emissionsSPCB whichever is more stringent Incase of process disturbancesfailure ofpollution control equipment adopted bythe unit the respective unit shall beshut down and shall not be restarteduntil the control measures are rectified

vi The company shall upload the status of compliance of the stipulated environmental clearance conditions including results of monitored data on its website and shall update the same periodically It shall simultaneously be sent to the Regional office of MOEF the respective Zonal office of CPCB and the State Pollution Control Board The criteria pollutant levels namely SPM RSPM S02 NOx (ambient levels as well as stack emissions) or critical sectoral parameters indicated for the project shall be monitored and displayed at a convenient location near the main gate of the company in the public domain

Not Complied Status of compliance of conditions stipulated in environment clearance and analytical reports of monitoring were not yet uploaded on to the website Compliance reports and analytical reports were not submitted to the Regional Office of Ministry

vii Green belt in 33 of the plant area shall be provided to mitigate the effects of fugitive emissions all around the plant and compost yard as per the CPCB guidelines in consultation with the local DFO

Not Complied Green belt development is in progress Proper post plantation care needs to be ensured

viii Company shall adopt rainwater harvesting measures to recharge the ground water

Complied Rainwater harvesting measures have been implemented

B - General Conditions i No further expansion or modifications

in the plant shall be carried out without prior approval of the Ministry of Environment and Forests

PA agreed to comply with

ii Ambient Air Quality Monitoring Stations shall be set up in the down wind direction as well as where maximum ground level concentration of SPM S02 NOx are anticipated in consultation with the State Pollution Control Board

Not complied Ambient air quality monitoring is done at only one location No monitoring is done in buffer zone

iii Adequate number of influent and effluent quality monitoring stations shall be set up in consultation with the State Pollution Control Board Regular monitoring should be carried out for relevant parameters

Complied Monitoring of water quality is carried out at ETP inlet and outlet

iv The industry shall ensure that the treated effluent and stack emissions from the unit are within the norms stipulated under the EPA rules or SPCB whichever is more stringent In case of process disturbancesfailure of pollution control equipment adopted by the unit the respective unit shall be shut down and shall not be restarted until the control measures are rectified

Complied Stack monitoring is being carried out A sensor has been installed in the stack for monitoring of stack emissions

to achieve the desired efficiencyvi The overall noise levels in and around Complied

the plant area shall be kept well within Enclosures have been provided for noisethe standards by providing noise generating sourcescontrol measures including acoustic Distillery unit of the project is still in constructionhoods silencers enclosures etc on allsources of noise generation Theambient noise levels should conformto the standards prescribed under EPARules 1989 viz 75 dBA ( day time)and 70 dBA ( night time)

vii The project proponent shall also Partly Compliedcomply with all the environmental Environmental protection measures pertaining toprotection measures and safeguards Sugar Plant have been implementedrecommended in the EIA EMP report Green belt development is not upto the mark

viii Occupational health surveillance Partly Compliedprogramme shall be undertaken as A health clinic has been provided in the plantregular exercise for all the employees premises First aid facilities are existing in theThe first aid facilities in the health clinic Data on medical records was notoccupational health centre shall be produced during the inspectionstrengthened and the medical recordsof each employee shall be maintainedseparately

ix A separate environmental Compliedmanagement cell equipped with full Separate environment cell has been set up withfledged laboratory facilities must be set laboratory facilityup to carry out the environmentalmanagement and monitoring functions

x The project authorities shall provide Compliedrequisite funds for both recurring and PA submitted that Rs193 Crores have beennon-recurring expenditure to spent for environment protection measuresimplement the conditions stipulated by Rs 65 lakhs have been spent on the green beltthe Ministry of Environment and development during 2014-15Forests as well as the Stategovernment along with theimplementation schedule for all theconditions stipulated herein The fundsso provided shall not be diverted forany other purpose

xi The project proponent shall also Not Compliedsubmit six monthly reports on the PA did not submit the six monthly compliancestatus of compliance of the stipulated reports regularlyEC conditions including results ofmonitored data (both in hard copies aswell as bye-mail) to the respectiveRegional Office of MoEF therespective Zonal Office of CPCB andthe State Pollution Control Board

xii The implementation of the project vis- Not pertaining to PAa-vis environmental action plans willbe monitored by Ministrys RegionalOffice at BhopalState PollutionControl BoardCentral PollutionControl Board

to achieve the desired efficiency vi The overall noise levels in and around

the plant area shall be kept well within the standards by providing noise control measures including acoustic hoods silencers enclosures etc on all sources of noise generation The ambient noise levels should conform to the standards prescribed under EPA Rules 1989 viz 75 dBA ( day time) and 70 dBA ( night time)

Complied Enclosures have been provided for noise generating sources Distillery unit of the project is still in construction

vii The project proponent shall also comply with all the environmental protection measures and safeguards recommended in the EIA EMP report

Partly Complied Environmental protection measures pertaining to Sugar Plant have been implemented Green belt development is not upto the mark

viii Occupational health surveillance programme shall be undertaken as regular exercise for all the employees The first aid facilities in the occupational health centre shall be strengthened and the medical records of each employee shall be maintained separately

Partly Complied A health clinic has been provided in the plant premises First aid facilities are existing in the health clinic Data on medical records was not produced during the inspection

ix A separate environmental management cell equipped with full fledged laboratory facilities must be set up to carry out the environmental management and monitoring functions

Complied Separate environment cell has been set up with laboratory facility

X The project authorities shall provide requisite funds for both recurring and non-recurring expenditure to implement the conditions stipulated by the Ministry of Environment and Forests as well as the State government along with the implementation schedule for all the conditions stipulated herein The funds so provided shall not be diverted for any other purpose

Complied PA submitted that Rs193 Crores have been spent for environment protection measures Rs 65 lakhs have been spent on the green belt development during 2014-15

xi The project proponent shall also submit six monthly reports on the status of compliance of the stipulated EC conditions including results of monitored data (both in hard copies as well as by e-mail) to the respective Regional Office of MoEF the respective Zonal Office of CPCB and the State Pollution Control Board

Not Complied PA did not submit the six monthly compliance reports regularly

xii The implementation of the project vis- a-vis environmental action plans will be monitored by Ministrys Regional Office at Bhopal State Pollution Control BoardCentral Pollution Control Board

Not pertaining to PA

xiii

Xiv

xv

A copy of the clearance letter shall besent by the proponent to concernedPanchayat Zilla ParishadMunicipalCorporation Urban local Body andthe local NGO if any from whosuggestions representations if any were received while processing theproposal The clearance letter shallalso be put on the website of thecompany by the proponentThe Project Proponent shall informthe public that the project has beenaccorded environmental clearance bythe Ministry and copies of theclearance letter are available with theState Pollution Control BoardCommittee and may also be seen atWebsite of the Ministry ofEnvironment and Forests athttpenvfornicin This shall beadvertised within seven days from thedate of issue of the clearance letterat least in two local newspapers thatare widely circulated in the region ofwhich one shall be in the vernacularlanguage of the locality concernedand a copy of the same shall beforwarded to the Regional officeThe Project Authorities shall inform theRegional Office as well as the Ministrythe date of financial closure and finalapproval of the project by theconcerned authorities and the date ofstart of land development work

Partly compliedPA submitted that clearance letter has beensubmitted to concerned Panchayatl ZillaParishadMunicipal Corporation etcDocumentary proof is not available with PA

CompliedInformation about Environment Clearance waspublished in two news papers on 02052009

Not CompliedPA did not inform the Regional Office about thedate of financial closure and final approval of theproject by concerned authorities and date ofstart of land development work

xiii A copy of the clearance tetter shall be sent by the proponent to concerned Panchayat Zilla ParishadMunicipal Corporation Urban local Body and the local NGO if any from who suggestions representations if any

were received white processing the proposal The clearance letter shall also be put on the website of the company by the proponent

Partly complied PA submitted that clearance letter has been submitted to concerned Panchayat Zilla ParishadMunicipal Corporation etc Documentary proof is not available with PA

Xiv The Project Proponent shall inform the public that the project has been accorded environmental clearance by the Ministry and copies of the clearance letter are available with the State Pollution Control Board Committee and may also be seen at Website of the Ministry of Environment and Forests at httpenvfornicin This shall be advertised within seven days from the date of issue of the clearance letter at (east in two local newspapers that are widely circulated in the region of which one shall be in the vernacular language of the locality concerned and a copy of the same shall be forwarded to the Regional office

Complied Information about Environment Clearance was published in two news papers on 02052009

XV The Project Authorities shall inform the Regional Office as well as the Ministry the date of financial closure and final approval of the project by the concerned authorities and the date of start of land development work

Not Complied PA did not inform the Regional Office about the date of financial closure and final approval of the project by concerned authorities and date of start of land development work

Scientist ^TTT

SUKEt-H i-1 - ^^DAPA TT^ TT ji

^Tlt ^ ^ Regional Ci-ice i^Z)

vffTT^V NagP - 44l^1

SUMMARY NOTE

1 Implementation of Conditions It is observed thatFollowing conditions were not compliedSpecific Condition no IILagoon is under construction and PCC work and lining is yet to be carried outSpecific Condition no IVOnly water level measurement has been carried outSpecific Condition no VIStatus of compliance of conditions stipulated in environment clearance and analyticalreports of monitoring were not yet uploaded on to the websiteCompliance reports and analytical reports were not submitted to the Regional Officeof MinistrySpecific Condition no VIIGreen belt development is in progress Proper post plantation care needs to beensuredGeneral Condition no1INo monitoring is being carried out in buffer zoneGeneral Condition noXISix monthly compliance reports were not submitted regularlyGeneral Condition noXVPA did not inform the Regional Office about the date of financial closure and finalapproval of the project by concerned authorities and date of start of land developmentworkFollowing Conditions were partially compliedSpecific Condition no IDistillery unit is under constructionSpecific Condition no IIIMonthly sampling and trend analysis monitoring reports were not submitted toMinistryGeneral Condition no VIIIData on medical records was not produced during the inspectionGeneral Condition no XIIIPA submitted that clearance letter has been submitted to concerned Panchayatl ZillaParishadMunicipal Corporation etc Documentary proof is not available with PA

Other Observationsa Permission from the CGWB for ground water abstraction expired in 2013

Application for the renewal of the permission submitted in 2015 and thesame is pending with CGWB

b Housekeeping needs to be improved

PA submitted that all the above non compliances are due to frequent change ofmanagement of the plantPA also submitted that Mis NSL Limited will take all necessary steps to comply withthe conditions stipulated in the Environment ClearanceConsent to operate has been obtained only for 7000 TCD of sugar 30 MWcogeneration power plant where as EC was granted for 12000 TCD of sugar mill 30MW cogeneration power plant and 100 KLPD distillery unit

2 Review wrt to MOEFs letter dated 3052012 The above mentioned report isprepared after site visit on 11042016 for the extension of validity of EnvironmentClearance issued to expansion of sugar mill capacity from 4500 TCD to 12000 TCD100 KLPD distillery unit and 30 MW co-generation plant of Mis Jay Mahesh Sugars

SUMMARY NOTE

1 Implementation of Conditions It is observed that Following conditions were not complied Specific Condition noll Lagoon is under construction and FCC work and lining is yet to be carried out Specific Condition no IV Only water level measurement has been carried out Specific Condition no VI Status of compliance of conditions stipulated in environment clearance and analytical reports of monitoring were not yet uploaded on to the website Compliance reports and analytical reports were not submitted to the Regional Office of Ministry Specific Condition no VII Green belt development is in progress Proper post plantation care needs to be ensured General Condition noll No monitoring is being carried out in buffer zone General Condition noXl Six monthly compliance reports were not submitted regularly General Condition noXV PA did not inform the Regional Office about the date of financial closure and final approval of the project by concerned authorities and date of start of land development work Following Conditions were partially complied Specific Condition no I Distillery unit is under construction Specific Condition no Ill Monthly sampling and trend analysis monitoring reports were not submitted to Ministry General Condition no VIII Data on medical records was not produced during the inspection General Condition no XIII PA submitted that clearance letter has been submitted to concerned Panchayat Zilla ParishadMunicipal Corporation etc Documentary proof is not available with PA

Other Observations a Permission from the CGWB for ground water abstraction expired in 2013

Application for the renewal of the permission submitted in 2015 and the same is pending with CGWB


PA submitted that all the above non compliances are due to frequent change of management of the plant PA also submitted that Ms NSL Limited will take all necessary steps to comply with the conditions stipulated in the Environment Clearance Consent to operate has been obtained only for 7000 TCD of sugar 30 MW cogeneration power plant where as EC was granted for 12000 TCD of sugar mill 30 MW cogeneration power plant and 100 KLPD distillery unit

2 Review wrt to MOEFs letter dated 3052012 The above mentioned report is prepared after site visit on 11042016 for the extension of validity of Environment Clearance issued to expansion of sugar mill capacity from 4500 TCD to 12000 TCD 100 KLPD distillery unit and 30 MW co-generation plant of Ms Jay Mahesh Sugars

Limited located at village Pawarwadi Taluka Majalgaon In Seed district ofMaharashtra

3 Court Cases and show causeclosure notices PA submitted the undertakingsthat

a There are no court cases pending against the projectb There are no show cause notices issued by MPCB

4 Uploading of compliance on web site With regard to uploading of EC andcompliance of conditions along with analytical reports on the web site of the companyPA did not upload the compliance and analytical reports in company website Ministrymay like to take up this matter with PA during the final presentation

~-~~~~~bScientist 0

litflf ~ 3WrrSUREf-HKiJM~ iillAPA

lt~-7 )YgtC jO-T D

qlff~ ~f~(~~~0~~(ql~Mirlltry of EfI~rv~rltnt ~u-t r ~nateChange~~ ~~ (11l~~ ~ IA~)

Regional Cffict (WeZ)~Nagpur-44(001

Limited located at village Pawarwadi Taluka Majalgaon in Beed district of Maharashtra

3 Court Cases and show causeclosure notices PA submitted the undertakings that

a There are no court cases pending against the project b There are no show cause notices issued by MPCB

4 Uploading of compliance on web site With regard to uploading of EC and compliance of conditions along with analytical reports on the web site of the company PA did not upload the compliance and analytical reports in company website Ministry may like to take up this matter with PA during the final presentation

M-Afcb Scientist D

^T SUKSSH KUMAR ADAPA

SC w- IT bullgt ^ WTcTZT

WrJjtrjf pf Enlaquo4iTgt-riHnt ^ CLnate Charge famptw ^Tfr-rr ate)

Regional Office (WCZ) -nIMxiVaCDLT-440001

gtis

MAHARASHTRA POLLUTION CONTROL BOARDTel 240104372402078124014701Fax 24024068 124023515Website httpmpcbgovinE-mail mpcbvsnlnet

Kalpataru Point 2nd - 4th FloorOpp Cine Planet CinemaNear Sion Circle Sion (E)Mumbai - 400 022

MAHARASHTRA

RedlLSI Date ICf 1 11120150 FormatiOIBOICAC-CEllIEIC NoAD-17177-15IRICAC- 14SG4

0MI s NSL Sugar Ltd Unit - HI(Formerly known as Jay Mahesh Sugar Industries Ltd)Gut No 85186 PawarwadiTal Majalgaon Dist Beed

Subject Renewal of Consent to Operate of 7000 TCD Sugar amp 30 MW Co-generation unit

under RED categoryRef 1 Consent to operate granted by the Board vide no BGCAC-CELLEIC AD-

15875-140ICAC-7112 dtd 250620152 Minutes of CAC meeting held on 03112015 bull bullbullbull

Your appllcation CR1507000016Dated 30062015For Renewal of Consent to Operate of 7000 TCD Sugaramp 30 MW Co-generation unit underRED category under Section 26 of the Water (P~evention amp Control of Pollution) Act1974 amp under Section 21 of the Air (prevention amp Control of Pollution) Act 1981 andAuthorization under Rule 5 of the Haxard ous Wastes (M H amp T M) Rules 2008 isconsidered and the consent is hereby granted subject to the following terms andconditions and as detailed in the schedule I II III amp IV annexed to this order

r bull fJf

1 The consent is granted for a period from 01082015 to 31072016

2 The actual total investment ofrhe industry is Rs 34604 Cr(As per C A Certificate submitted by industry)

3 The Consentis vafid for the manufacture of -

Sugar 239402 Molasses 94503 Pressmud 73504 Bagasse 58800II

Electric Power (Cogeneration) 30MW5(Th~poundm~_crushmg Capacltv of Sugar Industry shall not exceed 7000 TeD)

4 1974 Act fOrlIIIIIlriiiiililll

270 CMD 100 recycleAs per amp 311 CMD on land forSchedule J

--7-t------t---- ---- ___~+-_Irriampa_t1_O_D_--- --i_+--_- As per On land for irrigation

Schedule -I

l Tradeeffluent

2 Domesticeffluent

Mis NSL Sugar ua UnitI SRO jalnaIIRL12884000 08

MAHARASHTRA POLLUTION CONTROL BOARD

Tel 240104372402078124014701 Fax 24024068 24023515

Website httpmpcbgovin E-mail mpcbvsnlnci

MAHARASHTRA Kalpataro Point 2nlt1 - 4h Floor Opp Cine Planet Cinema Near Sion Circle Sion (E) Murabai - 400 022

RedLSI^ Date QI]20I5

Consenyfto Format lOBOCAC-CELLETCNoAD-l777-i5 RCAC- (q

Ms NSL Sngar Ltd Unit - III Formerly known as Jay Mahesh Sugar Industries Ltd) Gut No 8586 Pawarwadi Tal Majalgaon Dist Seed

i-v

Subject

Ref

Renewal of Consent to Operate of 7000 TCD Sugar amp 30 MW Co-generation unit under RED category ^ bull

1 Consent to operate granted by the Board vide no B0CAC-CELLEICAD- I5875-I40CAC-7112 dtd 25062015 2 Minutes of CAC meeting held on 03112015

Your application CR1507000016 Dated 30062015 For Renewal of Consent to Operate of 7000 TCD Siigar amp 30 M W Co-generation unit under RED category under Section 26 of the Water (Prevention amp Control of Pollution) Act 1974 amp under Section 21 of the Air (Prevention amp Control of Pollution) Act 1981 and Authorization under Rule 5 of the Hazardous Wastes (M H amp T M) Rules 2008 is considered and the consent is Hereby granted subject to the following terms and conditions and as detailed in the Schedule 111 III amp IV annexed to this order

1

2

3

The consent is grantedToTa period from 01082015 to 31072016

The actual total investment of the industry is Rs 34604 Cr (As per C A Certificate submitted by industry)

_ SfÔ g product By-Prodact Name Maximum Quantity in MTM vl A Sugar 23940

2f v Molasses 9450 Pressmud 7350

4 Bagasse 58800 5 Electric Power (Cogeneration) I 30 MW

(The cane crushing Capacity of Sugar Industry7 shall not exceed 7000 TCD)

4 Conditions under Water (PampCP) 1974 Act for discharge of effluent

n Permitted quantity of

discharge ICMD) Standards to he achieved

1 Trade effluent

581 (Sugar 311 + Co-gen

270)

As per Schedule -I

270 CMD 100 recycle amp 311 CMD on land for irrigation

2 Domestic effluent

30 As per Schedule -1

On land for irrigation

Ms mi Sugar Ltd Unit- SUO Jo In aIRL12834000

5

6 Conditions under Hazardous Waste (M H amp T M) Rules 2008 for treatment and disposalof hazardous wasticiJ

I

FlyIBoiler Ash 140 MTD

Use as manure

l

Sludge fromwaste watertreatment

30 MTD2

8 This Board reserves the right to review amend suspend revoke etc this consent and thesame shall be binding on the industry

9 This consent should not be construed as exemption from obtaining necessaryNOCpermission from any other Government agencies

10 Industry shall comply the directions issued by CPCB for online monitoring system

nConsent is issued without prejudice to the directions issued and being issued by epCB

For and on behalf of the

Copy to1 Regional Officer - MPCB Aurangabad - He is directed to forfeit BG of Rs 5 Lakh submitted

towards 0 amp M of pollution control system is to beforfeited as JVS results are exceeding theConsented limit

2 Sub -Regional Officer - Jalna MPCB He is directed to ensure the compliance of theconsent conditions

3 Chief Accounts Officer MPCB Mumbai4 CCICAC desk- for record amp website updation purposes

Mis NSL Sugar ua UllitmiddotllI SRO Jalna1118f1112884000 Page2of8

y msgmM

5 Conditions under Air (Pamp CP) Act 1981 for air emissions

no Descrijptjon of staclt source dumber of Stack Standards to he achieved

l Boilers (20 TPH 20 TPH amp 135 i TPH)

i As per Schedule - II

2 DG Set 1250 KVA 1 As per Schedule -11 3 DG Set 750 KVA l i As per Schedule - II 4 DG Set 625 KVA I As per Schedule - II 5 DG Set 250 KVA i As per Schedule - II

6 Conditions under Hazardous Waste (M H amp T M) Rules 2008 for iTeatment and disposal of hazardous waste

1 TypeolWaste Category Duantitv UOME msmsposAMl

i - bull

Used Spent Oil 51 100 LitrsM Reuse-inown boiler as fuel

7 Non-Hazardous Solid Wastes $rgt2sfo lype of Waste iCtaanfity txeanneot Disposal

LandfillSale to Bricks 1 1 FlyBoiler Ash 140 MTD

manufacturers and used for compost production

2 Sludge from waste water treatment

30 MTD j |

-V Use as manure

8 This Board reserves the right to review amendsuspend revoke etc this consent and the same shall be binding on the industry

9 This consent should not bq^cSShstrued as exemption from obtaining necessary NOCpermission from any other Government agencies


11 Consent is issued without prejudice to the directions issued and being issued by CPCB bullr

fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn

For and on behalf of the aharashtra Pollution Control Board

(Dr T AnbalagSi IAS) Member Secretary

Sr No Amount (Rs) DD No Date Drawn On

1 Rs 692189- | 233388 ( 05062015 | SBI Bank |

Copy to 1 Regional Officer - MPCB Aurangabad - He is directed to forfeit BG ofRs 5 Lakh submitted

towards OampM of pollution control system is to be forfeited as JVS results are exceeding the Consented limit

2 Sub -Regional Officer - Jalna MPCB He is directed to ensure the compliance of the consent conditions

3 Chief Accounts Officer MPCB Mumbai 4 CCCAC desk- for record amp website updation purposes

Ms NSL Sugar Ltd Unit-Ill SROaInalRLl2884000 Page 2oS

I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv

F] rndu4 colleG] The

thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The

M sNS~Sugar ud Unit-III

Schedule-Ionditions for compliance of Water Pollution Control

cr your application you have provided Effluent Treatment Plant with designacity 1400 CMD

Applicant shall operate the effluent treatment plant (ETP) to treat the tradeent so as to achieve the following standards prescribed by the Board or underAct 1986 and Rules made there under from time to time whichever isgent

Parameters Standards prescribed by Boardro

Limiting Concentration in mgl except for pHI pH 55-902 Oil amp Grease 103 BOD (3 days 270C) 1004 Sul hare J (JUO I

i Suspended Solids 1006 COD 2507 Chloride 6008~T~0~t=a=LD==is~so~l~ve~d~S~o~l=iru~~~~ ~2~1~OO~ ~treated effluent 311 CMD generated from Sugar unit shall be disposed on land f ration on 153 acres of own land las per the bilateral agreement with farmers Incase treateduntreated effluent shall find its way outside the factory premis stfy or indirectlye effluent of270 CMD generated from Co-gen shall be 100 recycle in proces

P conditions for Sugar FactoryOperation of ETP shall be started at least one month before starring of canecrushing to achieve desired MLSS So as to meet prescribed standards fromday one the operation of millWaste water generation shall be maintained as 100 liters per ton of canecrushedIndustry-shall achieve zero discharge into in land surface water bodies15 days storage capacity tank shall be provided for treated effluent to take careof no demand for irrigation my shall maintain properly the arrangement provided for covering the effluentction system and to avoid the ingress of Bagasse other materialunit shall operate ETP even after completion of the crushing season soany effluent generated during washing amp maintenance is dischargedproper treatment

unit shall optimize water use in industrial process amp maintain records ofr consumption amp waste water generationcr your consent application for the 30 CMD sewage generation you haveded septic tank amp soak pit for the treatment of sewage

Applicant shall operate the sewage treatment system to treat the sewage so ashieve the following standards

Snspended Solids Not to exceed 100 mglBOD 3 days 27degC Not to exceed 100 mgl

treated sewage shall be disposed on d for gardeninglirrigation

SIlOjalnoIRLIZ884000 Page308

-

Schedule-I I) Terms amp Conditions for compliance of Water Pollution Control

1) A] As per your application you have provided Effluent Treatment Plant with design Capacity 1400 CMD

BJ The Applicant shall operate the effluent treatment plant (ETP) to treat the trade effluent so as to achieve the following standards prescribed by the Board or under EP Act 1986 and Rules made there under from time to time whichever is stringent

2)

Sr No

Parameters Standards prescribed by Board

Limiting Concentration in mg1 except for pH

01 PH 55-90 02 Oil amp Grease 10

03 BOD (3 days 27oC) 100 )

04 Sulphate 1000 05 Suspended Solids 4 ioo 06 COD 1 250

07 Chloride 600

08 Total Dissolved Solids -a 2100

C]

D]

El

The treated effluent 311 CMD generated from Sugar unit shall be disposed on land fc irrigation on 153 acres of own land as per the bilateral agreement with fanners In n any case treateduntreated effluent shall find its way outside the factory premise directly or indirectly Trade effluent of270 CMD generated from Co-gen shali he 100 recycle in process

n

in iv

CREP conditions for Sugar Factory lt i Operation of ETP shall be started at least one month before starting of cane

crushing to achieve desired MLSS So as to meet prescribed standards from day one the operation of mill Waste watergeneration shall be maintained as 100 liters per ton of cane crushed- Industiyjshall achieve zero discharge into in land surface water bodies 15 days storage capacity tank shall be provided for treated effluent to take care

^ of nd demand for irrigation F] r Industry shall maintain properly the arrangement provided for covering the effluent t collection system and to avoid the ingress of Bagasse other material

GJ The unit shall operate ETP even after completion of the crushing season so that any effluent generated during washing amp maintenance is discharged after proper treatment

HJ The unit shall optimize water use in industrial process amp maintain records of water consumption amp waste water generation

A] As per your consent application for the 30 CMD sewage generation you have provided septic tank amp soak pit for the treatment of sewage

B] The Applicant shall operate the sewage treatment system to treat the sewage so as to achieve the following standards (1) Suspended Solids Not to exceed 100 mg1 (2) BOD 3 days 270C Not to exceed 100 mg1

CJ The treated sewage shall be disposed on^jajid for gardeningirrigation

er MA NSL Sugar Ltd Unit-Ill SROJalnalRi12884000 Page 3o8 C

Vd

iX1

)

3) The industry shall have bilateral agreement with the farmers on whose land the treatedeffluent is used for irrigation purposes and a copy of the agreements with validity shall besubmitted to the RegionalSub- Regional Office of the Board

4) The industry shall create Environmental Cell by appointing an Environmental EngineerChemist and Agriculture expert for looking after day to day activities related toEnvironment and irrigation field where treated effluent is used for irrigation

5) CONDITIONS FOR MOLASSES STORAGE

(i) The molasses shall be properly collected and stored in steel tanks which shall beleak proof At no stage of handling of molasses there shall be leakage or spillageThe capacity of tanks for storage of molasses shall be such that it will take care ofbumper production of sugar non-lifting of molasses etc ltAll the area on which molasses are stored and handled should be provided withdrain for diverting the spills to the treatment plant molasses tank Suitablearrangements for accidental discharges of molasses from Ihe tanks shall beprovided to contain the same within factory premisesDestruction of molasses and its disposal shall not be done without specificpermission in writing from the authorized offioerof the Board Intimation ofintention to destroy or dispose of the molasses shall be given to the Board atleast 15(fifteen) days in advance by registered post under intimation to the Sub-Regionalofficer and Regional officer of the Board under whose jurisdiction the factory issituatedThe storage tanks shall be kept in goodsoriditions all the year round with adequatemaintenance The tanks size and capacity per em height total capacity in tonnesshall be displayed prominently near ton the tankThe above conditions shallbe in addition to and not in derogation of the provisionscontained in the Bombay Molasses Rules 1955 and Maharashtra MolassesStorage and Supply Regulation 1965

6) The Applicant shall provide Specific Water Pollution control system as per the conditionsofEP Act 1986 and rule madethere under from time to time Environmental Clearance CREP guidelines if applicable

(ii)

(iii)

(iv)

(v)

(vi)

II) Conditions under Water (prevention amp Control of Pollution) CESS A~t 1977 asamendedThe Applicant shall comply with the provisions of the Water (Prevention amp Control ofPollution) Cess Act 1977 and as amended by installing water meters filing water cess

i~ Ferm-I and other ons as contained in the said act

Ms NSLSuqar Ltd Unit-Ill SROJalnaIRL12884000 Page4of8

TTiirijStfjBBi raquoMTgirfisa

3)

4)

5)

6)

ID

The industry shall have bilateral agreement with the farmers on whose land the treated effluent is used for irrigation purposes and a copy of the agreements with validity shall be submitted to the RegionalSub- Regional Office of the Board

The industry shall create Environmental Cell by appointing an Environmental Engineer Chemist and Agriculture expert for looking after day to day activities related to Environment and irrigation field where treated effluent is used for irrigation

CONDITIONS FOR MOLASSES STORAGE

(i) The molasses shall be properly collected and stored in steel tanks which shall be leak proof At no stage of handling of molasses there shall be leakage or spillage

(ii) The capacity of tanks for storage of molasses shall be such that it will take care of bumper production of sugar non-lifting of molasses etc

(iii) All the area on which molasses are stored and handled should be provided with drain for diverting the spills to the treatment plant xnolassps tank Suitable arrangements for accidental discharges of molasses from The tanks shall be provided to contain the same within factory premises

(iv) Destruction of molasses and its disposal shall not bexdone without specific permission in writing from the authorized officerW the Board Intimation of intention to destroy or dispose of the molasses shall be given to the Board atleast 15 (fifteen) days in advance by registered post under intimation to the Sub-Regional officer and Regional officer of the Board under whose jurisdiction the factory is situated

(v) The storage tanks shall be kept ingopdeoriditions all the year round with adequate maintenance The tanks size and capacity per cm height total capacity in tonnes shall be displayed prominently near on the tank

(vi) The above conditions shalfbein addition to and not in derogation of the provisions contained in the BombayMolasses Rules 1955 and Maharashtra Molasses Storage and Supply Regulation 1965

The Applicant shall provide Specific Water Pollution control system as per the conditions of EP Act 1986 and rule made there under from time to time Environmental Clearance CREP guidelines if applicable

Conditions under Water (Prevention amp Control of Polhition) CESS Act 1977 as amended A

The Applicant shall comply with the provisions of the Water (Prevention amp Control of Pollutiorl) Cess Act 1977 and as amended by installing water meters filing water cess returns iri Form-I and other provisions as contained in the said act

k-

1 2

Industrial Cooling boiler feed etc 260 Domestic purpose 50

3 Processing whereby water gets polluted amp pollutants are easily biodegradable

835

4 Processing whereby water gets polluted amp pollutants are not easily biodegradable and are toxiq^

mdash

MA NSL Sugar Ltd Unit-Ill SRO ]alnalRL12884000 Page 4olaquo

w

72-2

---------~

Terms amp conditions for compliance of Air Pol1ution Control

1 As per your application you have provided the Air pollution control (APC) system andalso erected following stack (5) to observe the following fuel pattern-

2 ESP 72 Bagasse 1449MTDay

3

4 Acoustic 7~O HSD 20KLDKVA enclosure 1 400

5 DG Set 750 Acoustic 60 HSD 17 KLDKVA enclosure 1 340

6 DG Set 625 Acoustic50 1 280KVA enclosure

7 DG Set 250 Acoustic 50 1 140KVA enclosure

2 The Applicant shall provide ESP IBag ft1~erl Wet scrubber to the Bagasse fired boiler andDust Collector to Sugar bagging seCtttm-as an Air Pollution control equipments OR as perthe conditions of EP Act 1986 and rule made there under from time to time IEnvironmental Clearance I CREP guidelines

3 The applicant shall operate and maintain above mentioned air pollution control system soas to achieve the level ofpollutants to the following standardsrParticul~te J1ytter _~ltt to exceedJ 150 mgN=m=-3 _

4 The Applicant shall obtain necessary prior permission for providing additional controlequipment with necessary specifications and operation thereof or alteration orreplacement alteration well before its life come to an end or erection of new pollutioncontrol equipment

5 The Board reserves its rights to vary all or any of the condition in the consent if due toany technological improvement or otherwise such variation (including the change of anycontrol equipment other in whole 0 in pa~

Mis NSL Sligar Ltd Unit-III SRO Jaillall1RL112884000

Schedale-II

Terms amp conditions for compliance of Air Pollntion Control

1 As per your application you have provided the Air pollution control (APC) system and also erected following stack (s) to observe the following fuel pattem-

Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day

I Boiler (135 TPH) |

2 Boiler (20 TPH) (Standby)

ESP 72 Bagasse 1449 MTDay 02 gt-5796

3 Boiler (20 TPH) (Standby) bull X V

-A--

4 DG Set 1250 KVA

Acoustic enclosure 70 HSD 20 KlD 00 400

5 DG Set 750 KVA

Acoustic enclosure 60 HSD 17XLD 1 340

6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W

2 The Applicant shall provide ESPBag filter Wet scrubber to the Bagasse fired boiler and Dust Collector to Sugar bagging sectibn as an Air Pollution control equipments OR as per the conditions of EP Act -4986 and rule made there under from time to time Environmental Clearance CREPgiiidelines

3

4

5

The applicant shall operate and maintain above mentioned air pollution control system so as to achieve the leêbof pollutants to the following standards

Paniculate matter Not to exceed 150 mgNm3 1

The Applicantshall obtain necessary prior permission for providing additional control equipmentv with necessary specifications and operation thereof or alteration or replacementalteration well before its life come to an end or erection of new pollution coiitrol equipment

The Board reserves its rights to vary all or any of the condition in the consent if due to any technological improvement or otherwise such variation (including the change of any control equipment other in whole or in part is necessary)

Ms NSL Sugar Ltd Unit-ltlSROjalnalRil2884000 Xv

PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story

Schedule-illDetails of Bank Guarantees

nscntEOR)

AmtofBGImposed

Purpose of BG forfeitureAmountofBGforfeited from the

im osed BGbull As JVS results of trade effluent amp

~iO Rs 50 Lakh I ~~acI(monitoring -are exceeding_---J L --Llhe Consentelt Iimitsc ~

BG

o amp M for achievingconsented

CompliaiiceP~riod

ent Amt oiBGTsubmissionOR) _ Imposed Period

Rs100Lacs

Purpose of BG

15days

standards ofEffluent f--==~~o--_--i 31072016o amp M for achievingconsented ~stanilards of Stackemission

Validity lDate

30112016

niiiii SRO JalnaIRL12884000 Page6of8

Tm T

Schedule-Ill Details of Bank Guarantees

BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed

Amount ofBG forfeited from the

imposed BG

Purpose of BG forfeiture

1 C to R Rs 50 Lakh Rs 50 Lakh

bull As JVS results of trade effluent amp stack monitoring are exceeding the Consented limits X

NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period

Purpose of BG Compliance Period

Validity Date

2 C to R Rs 100 Lacs 15 days

0 amp M for achieving consented standards s^-of Effluent I

v

31072016 30112016 0 amp M for achieving consented standards of Stack emission

C

tS

-----~---------

Schedule-IVGeneral Conditions

The applicant shall provide facility for collection of environmental samples and samples of tradeand sewage effluents air emissions and hazardous waste to the Board staff at the terminal ordesignated points and shall pay to the Board for the services rendered in this behalfIndustry should monitor effluent quality stack emissions and ambient air quality monthlyThe applicant shall provide ports in the chimney(s) and facilities such as ladder platform etc formonitoring the air emissions and the same shan be open for inspection toland for use of theBoards Staff The chimney(s) vents attached to various sources of emission shall be designatedby numbers such as S-l S-2 etc and these shall be painted displayed to facilitate identification

4) Whenever due to any accident or other unforeseen act or even such emissions occur or isapprehended to occur in excess of standards laid down such information shall be forthwithReported to Board concerned Police Station office of Directorate of Health ServicesDepartment of Explosives Inspectorate of Factories and Local Body In casect~oeurobullfailure ofpollution control equipments the production process connected to it shall be stJilpep

5) The applicant shall provide an alternate electric power source sufficient to operate all pollutioncontrol facilities installed to maintain compliance with the terms and conditions of the consentIn the absence the applicant shall stop reduce or otherwise control production to abide by termsand conditions of this consentThe firm shall submit to this office the 30rh day of SeptembeL~everyyear the EnvironmentalStatement Report for the financial year ending 31t March inthtltijescribedForm-Vas per theprovisions of rule 14 of the Environment (Protection) (SecondAmendment) Rules 1992The industry shall recyclereprocessreuserecover Hazardcus Waste as per the provisioncontain in the HW (MHampTM) Rules 2008 which caTbe recycled processed reused recoveredand only waste which has to be incinerated shall gQJojncineration and waste which can be usedfor land filling and cannot be recycledreproc_ess~deic should go for that purpose in order toreduce load on incineration and landfill siteenvironmentThe industry should comply with the I-I~ar~QusWaste (M H amp TIvf) Rules 2008 and submitthe Annual Returns as per Rule 5(6) amp ~2(2) of Hazardous Waste (M H amp TM) Rules 2008 forthe preceding year April to March in F~ftnJV by 30tiJ June of every yearAn inspection book shall be open~dah~ made available to the Boards officers during their visitto the applicant ~r The applicant shallmake an apglication for renewal of the consent before the date of theexpiry of the consent - Industry shall strictly CQ~ply with the Water (PampCP) Act 1974 Air (PampCP) Act 1981 andEnvironmental ProtectionAtt 1986 and industry specific standard under EP Rules 1986 whichare available on MPCBwebsite (wwwmpcbgovin)The industry shall constitute an Environmental cell with qualified staffpersonnelagency to seethe day to dayenc0OJpliance of consent condition towards Environment Protectionseparate~r~inagesysteJ shall be provided for collection of trade ~nd sewage effluents Termi~almanholes shall be provided at the end of the collection system WIth arrangement for measunngthe flow No effluent shall be admitted in the pipessewers downstream of the terminalmanholes No effluent shall find its way other than in designed and provided collection systemNeither storm water nor discharge from other premises shall be allowed to mix with the effluentsfrom the factoryThe applicant shall install a separate meter showing the consumption of energy for operation ofdomestic and industrial effluent treatment plants and air pollution control system A registershowing consumption of chemicals used for treatment shall be maintainedConditions for DG SetNoisefrom the DG Set should be controlled by providing an acoustic enclosure or by treatingthe room acousticallyIndustry should provide acoustic enclosure for control of noise The acoustic enclosure acoustictreatment of the room should be designed for mini 25 dB (A) insertion loss or for meeting

1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)

Page 70f8Mis NSLSugar Ltd Unit-lit SROjalnallRt12884000

SchedlaquoiegtIV Gencraj Conditions

1) The applicant shall provide facility for collection of environmental samples and samples of trade and seivage effluents air emissions and hazardous waste to the Board staff at the terminal or designated points and shall pay to the Board for the services rendered in this behalf

2) Industry should monitor effluent quality stack emissions and ambient air quality monthly 3) The applicant shall provide ports in the chimney(s) and facilities such as ladder platform etc for

monitoring the air emissions and the same shall be open for inspection toand for use of the Boards Staff The chimney(s) vents attached to various sources of emission shall be designated by numbers such as S-l S-2 etc and these shall be painted displayed to facilitate identification

4) Whenever due to any accident or other unforeseen act or even such emissions occur or is apprehended to occur in excess of standards laid down such information shall be forthwith Reported to Board concerned Police Station office of Directorate of Health Services Department of Explosives Inspectorate of Factories and Local Body In case of failure of pollution control equipments the production process connected to it shall be stopped

5) The applicant shall provide an alternate electric power source sufficient to operate all pollution control facilities installed to maintain compliance with the terms and conditions of the consent In the absence the applicant shall stop reduce or otherwise control production to abide by terms and conditions of this consent

6) The fern shall submit to this office the 30th day of September evefy year the Environmental Statement Report for the financial year ending 31 March in- thc prescribed Form-V as per the provisions of rule 14 of the Environment (Protection) (Second Amendment) Rules 1992

7) The industry shall recydereprocessreuserecover Hazardous Waste as per the provision contain in the HW (MHampTM) Rules 2008 which can be fecycled processed reused recovered and only waste which has to be incinerated shall goto incineration and waste which can be used for land filling and cannot be recycledreprocessed etc should go for that purpose in order to reduce load on incineration and landfill siteenvironment

8) The industry should comply with the Hazardous Waste (M H amp TM) Rules 2008 and submit the Annual Returns as per Rule 5(6) amp 22(2) of Hazardous Waste (M H amp TM) Rules 2008 for the preceding year April to March in Fqrn-W by 30th June of every year

9) An inspection book shall be opened and made available to the Boards officers during their visit to thampapplicant

10) The applicant shall make an application for renewal of the consent before the date of the expiry of the consent iS

11) Industry shall strictly cojftply with the Water (PampCP) Act 1974 Air (PampCP) Act 1981 and Environmental ProtectionACt 1986 and industry specific standard under EP Rules 1986 which are available on MPCB website (wwwmpcb go v in)

12) The industry shall constitute an Enviionmental cell with qualified staffpersonnelagency to see the day to day compliance of consent condition towards Environment Protection

13) Separate drainage system shall be provided for collection of trade and sewage effluents Terminal manholes shall be provided at the end of the collection system with arrangement for measuring the flow No effluent shall be admitted in the pipessewers downstream of the terminal manholes No effluent shall find its way other than in designed and provided collection system

14) Neither storm water not discharge from other premises shall be allowed to mix with the effluents from the factory

15) The applicant shall install a separate meter showing the consumption of energy for operation of domestic and industrial effluent treatment plants and air pollution control system A register showing consumption of chemicals used for treatment shall be maintained

16) Conditions for DG Set a) Noise from the DG Set should be controlled by providing an acoustic enclosure or by treating

the room acoustically b) Industry should provide acoustic enclosure for control of noise The acoustic enclosure acoustic

treatment of the room should be designed for minimuî 25 dB (A) insertion loss or for meeting

the ambient noise standards whichever is on higher side A suitable exhaust muffler withinsertion loss of 25 dB (A) shall also be provided The measurement of insertion loss will be doneat different points at 05 meters from acoustic enclosureroom and then average

c) Industry should make efforts to bring down noise level due to DG set outside industrialpremises within ambient noise requirements by proper sitting and control measures

d) Installation of DG Set must be strictly in compliance with recommendations of DG Setmanufacturer

e) A proper routine and preventive maintenance procedure for DG set should be set and followed inconsultation with the DO manufacturer which would help to prevent noise levels of DO set fromdeteriorating with use

f) DG Set shall be operated only in case of power failureg) The applicant should not cause any nuisance in the surrounding area due to operation of DG

Seth) The applicant shall comply with the notification of MoEF dated 17052002 regardingnoise limit

for generator sets nm with diesel p c17) The industry should not cause any nuisance in surrounding area 18) The industry shall lake adequate measures for control of noise levels from itSown sources within

the premises so as to maintain ambient air quality standard in respedofJOiSe-to less than 75 dB(A) during day time and 70 dB (A) during night time Day time isreckon~d in between 6 amand 10 pm and night time is reckoned between 10 pm and 6 am

19) The applicant shall maintain good housekeeping ~20) The applicant shall bring minimum 33 of the avaitablew~eb land under green coverage

plantation The applicant shall submit a yearly statemenhby 30th September every year ona vailable open plot area number of trees surviving asort3lamptMarch of the year and number oftrees planted by September end

21) The non-hazardous solid waste arising in thebullractpry premises sweepings etc be disposed ofscientifically so as not to cause any nuisance IpQ11ution The applicant shall take necessarypermissions from civic authorities for dispos~1prspIid waste

22) The applicant shall not change or alter thehlttl)ltity quality the rate of discharge temperature orthe mode of the eflluentcmissions~or hizardous wastes or control equipmentgt provided forwithout previous written permission ofehe Board The industry will not carry out any activity forwhich this consent has not been gfiUlt~dlwithout prior consent of the Board

23) The industry shall ensure thafflgitive emissions from the activity are controlled so as to maintainclean and safe environment-in and around the factory premises

24) The industry shall mbmirltqmhterly statement in respect of industries obligation towards consentand pollution control ccinpliances duly supported with documentary evidences (format candownloaded from MRbB official site)

25) The industry shall submit official e-mail address and any change will be duly informed to theMPCB

26) The indqstryvshall achieve the National Ambient Air Quality standards prescribed videGovernment of India Notification dt 16112009 as amended

27) The Board reserves its rights to review plans specifications or other data relating to plant setupfor the treatment of waterworks for the purification thereof amp the system for the disposal ofsewage or trade effluent or in connection with the grant of any consent conditions The Applicantshall obtain prior consent of the Board to take steps to establish the unit or establish anytreatment and disposal system or an extension or addition thereto

28) The industry shall ensure replacement of pollution control system or its parts after expiry of itsexpected life as defined by manufacturer so as to ensure the compliance of standards and safety ofthe operation thereof (l

----oooorer

Mis NSL Sugar LtdUnit-lit SROJalnaiJIRILI12884000 Page 8q(8

the ambient noise standards whichever is on higher side A suitable exhaust muffler with insertion loss of 25 dB (A) shall also be provided The measurement of insertion loss will be done at different points at 05 meters from acoustic enclosureroom and then average

c) Industry should make efforts to bring down noise level due to DG set outside industrial premises within ambient noise requirements by proper sitting and control measures

d) Installation of DG Set must be strictly in compliance with recommendations of DG Set manufacturer

e) A proper routine and preventive maintenance procedure for DG set should be set and followed in consultation with the DG manufacturer which would help to prevent noise levels of DG set from deteriorating with use

f) DG Set shall be operated only in case of power failure g) The applicant should not cause any nuisance in the surrounding area due to operation of DG

Set y- h) The applicant shall comply with the notification of MoEF dated 17052002 regardingnoise limit

for generator sets run with diesel 17) The industry should not cause any nuisance in surrounding area 18) The industry shall take adequate measures for control of noise levels from itlown sources within

the premises so as to maintain ambient air quality standard in respect -pf noise to less than 75 dB (A) during day time and 70 dB (A) during night time Day time isrfeckoned in between 6 am and 10 pm and night time is reckoned between 10 pm and 6 am gt

19) The applicant shaii maintain good housekeeping j-I 20) The applicant shall bring minimum 33 of the available- open land under green coverage

plantation The applicant shall submit a yearly stateihenH^y 30th September every year on available open plot area number of trees surviving as off 3J March of the year and number of trees planted by September end

21) The non-hazardous solid waste arising in thqjactpfy premises sweepings etc be disposed of scientifically so as not to cause any nuisance pdllution The applicant shall take necessary permissions from civic authorities for disposal-of splid waste

22) The applicant shall not change or alter thequantity quality the rate of discharge temperature or the mode of the effluentemissions or hazardous wastes or control equipments provided for without previous written permission of the BoardThe industry will not carry out any activity for which this consent has not been gfahtedwithout prior consent of the Board

23) The industry shall ensure thabfygitive emissions from the activity are controlled so as to maintain clean and safe environraent ra ahd around the factory premises

24) The industry shall submirquarterly statement in respect of industries obligation towards consent and pollution control compliances duly supported with documentary evidences (format can downloaded from MPpB Official site)

25) The industry shall suhlnit official e-mail address and any change will be duly informed to the mpgb

26) The industry shall achieve the National Ambient Air Quality standards prescribed vide Government of India Notification dt 16112009 as amended

27) The Board reserves its rights to review plans specifications or other data relating to plant setup for the treatment of waterworks for the purification thereof amp the system for the disposal of sewage or trade effluent or in connection with the grant of any consent conditions The Applicant shall obtain prior consent of the Board to take steps to establish the unit or establish any treatment and disposal system or an extension or addition thereto

28) The industry shall ensure replacement of pollution control system or its parts after expiry of its expected life as defmed by manufacturer j of standards and safety of the operation thereof

s Ms NSL Sugar Ltd Unit-l SRO jahaSRLimmO Page Sof 8

SUGARSSustainable food Fule amp Power

NSL Sugars LimitedUnit III Jay MaheshRegd Off PawarwadiTqMajalgaon DistBeedMaharashtraINDIAOff(02443) 20359091Fax 02443-202034Emailjmsilnslsugarscomweb wwwnslsugarscomTin No 27830948879 VCCIN NOU15429KA1999PLC026121

Ref No NSLSLAdmL)7 2016-17 Date- 28th April 2016

TO WHOM SO EVER IT MAY CONCERN

This is to certify that there are no show cause notices issued by MPCB or pending against ofNSLSugars Limited Unit III Jay Mahesh till date

Signature 1tvU w ~ II)

~ Designation- v~ce President

AGroup Company s7NSL Icon 8-26842A Road No12 Banjara Hills Hydrabad - 500 034 INDIA Ph 91 -40 - 30514444 $y-

m

SUGARS Sustainable food Fule amp Power

RefNo NSLSLAdmV 2016-17

NSL Sugars Limited

Unit III Jay Mahesh

RegdOffPawarwadi TqMajalgaon DistBeed MaharashtraINDIA Off(02443) 20359091 Fax 02443-202034 Email jmsilnslsugarscom web wwwnslsugarscom

Tin No 27830948879 VC C1N NOU 15429KA1999PLC026121

Date- 28th April 2015


This is to certify that there are no show cause notices issued by MPCB or pending against of

NSL Sugars Limited Unit III Jay Mahesh till date

Signature

Designation vice President

Unf

sh

fGroup Company gt70 -

NSL Icon 8-26842A Road No12 Banjara Hills Hydrabad - 500 034 INDIA Ph 91 -40 - 30514444


NSL Sugars LimitedUnit III Jay MaheshRegd Off Pawa rwad iTqMajalgaon DistBeedMaharashtraINDIAOff(02443) 20359091Fax 02443-202034Emailjmsilnslsugarscomweb wwwnslsugarscomTin No 27830948879 VIGGIN NOU15429KA 1999PLG026121

Ref No NSLSLAdmvrry 2016-17 Date- 28th April 2016


This is to certify that there are no court cases pending against of NSLSugars Limited Unit IIIJay Mahesh till date

hlXft~V)

~(gnature

Designation - Vice President

AGroup Company 1f-NSL Icon 8-26842A Road No12 Banjara Hills Hydrabad - 500 034 INDIA Ph 91 -40 - 30514444 ]


NSL Sugars Limited

Unit 111 Jay Mahesh

RegdOffPawarwadi TqMajalgaon DistBeed MaharashtraINDIA Off(02443) 20359091 Fax 02443-202034 Email jmsilnslsugarscom web wwwnslsugarscom Tin No 27830948879 VC CIN NOU15429KA1999PLC026121

RefNo NSLSLAdmA^^2016-17 Date- 28th April 2016


This is to certify that there are no court cases pending against of NSL Sugars Limited Unit

Jay Mahesh till date

gnature

Designation Vice President

f

U

1

Is NO

m fGroup Company

NSL Icon 8-26842A Road No12 Banjara Hills Hydrabad - 500 034 INDIA Phi 91 -40 - 30514444



ensured

General Condition no1I







work




Specific Condition no III


Ministry




PA submitted that clearance letter has been submitted to concerned Panchayatl Zilla



f~S~~uSuresh KumarAH~pk

Scientist 0

Encl as above

Copy to1 Director RO HQ Ministry of Environment Forest amp Climate Change Government of

India 1st Floor Agni Wing Indira Paryavaran Shawan Jorbagh Road New Delhi-110003

2 Director (Monitoring Cell) Ministry of Environment Forest amp Climate Change IndiraParyavaran Shawan Aliganj Jorbagh Road New Delhi-110003

3 Vice President MsNSL Sugars Limited village Pawarwadi Taluka MajalgaonDistrict Seed in Maharashtra



ensured

General Condition noll







work




Specific Condition no Ill


Ministry




PA submitted that clearance letter has been submitted to concerned Panchayat Zilia



Suresh Kumar Aaapa Scientist D

End as above

Copy to 1 Director RO HQ Ministry of Environment Forest amp Climate Change Government of

India 1st Floor Agni Wing Indira Paryavaran Bhawan Jorbagh Road New Delhi-

110 003

2 Director (Monitoring Cell) Ministry of Environment Forest amp Climate Change Indira

Paryavaran Bhawan Aliganj Jorbagh Road New Delhi-110003

3 Vice President MsNSL Sugars Limited village Pawarwadi Taluka Majalgaon District Beed in Maharashtra



Part -IDATA SHEET











Forestb Others







Part-I DATA SHEET


Industry













Forest b Others





Not applicable

20

12

Financial crisis















Planned)














Rs300 Crores

Rs5 Crores


Rs34604 Crores


Rs 199 Crores




Not Applicable


Not Applicable



Planned)



Financial crisis




11042016


As under

Vj8





No reply from PA




sh





















falls in Category A



d


Final ElAEMP Report

CHAPTER-II

RAW MATERIAL AND



















falls in Category A








Colony




sugarcane



2850 m3day






Distillery - 2850

Power Plant - 700





-----bull

-

--

-


Final EIAEMP Report

jd





Colony




sugarcane



2850 m3day



Table - 2



Proposed

Requirement


Distillery - 2850

Power-Plant - 700


Total 1480 6200

rs

mmf



mm

-bullbullbull


Fmal EINEMPReport

232 Water balance

A Water Input




B Water Output








24 MANPOWER


Table - 3




Distillery - 75 75+-- ----~ --- ---


I----------- J------- --



Imdash

gtbull

-

p

Itei


Final EIAEMP Report

232 Water balance

A Water Input




B Water Output








MANPOWER 24


Table - 3

Total Manpower




Distillery - 75 75


Total 350 145 495








241 Power








distillery






Sugar Mill 4MW 10MW

Distillery - 125 MW



Colony - 025 MW





-------bullbull-

bullbullbull


Final EIAEMP Report




241 Power








distillery




Table - 4

Power Requirement



Distillery - 125 MW



Colony - 025 MW






Final EIAEMPReport

Table - 5





(Existing)


(Proposed)









steam turbine

2412 Source of Fuel





i I




Final EIVEMP Report

Table - 5

Details of DG Set

s

No

No of

DG sets

Capacity Height of

stacks

No of

stack

Fuel

used

Fuel

consumption

1 1 160 KVA

(Existing)


2 1 625 KVA

(Existing)


3 2 1000 KVA

(Proposed)










steam turbine

2412 Source of Fuel

Table - 6

Fuel Source

Raw

Material


Transportation


sugar milt

Within the

premises

Bagasse conveyors



-2



81 INTRODUCTION








The aims of EMP are















1~

cr

u

u

i^

1-

iBfMa An^6^U^-2-


Final

EIAEMP Report

CHAPTER-VIII


81 INTRODUCTION








The aims of EMP are
















Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent

Mis NSL Sugar ua UnitI SRO jalnaIIRL12884000 Page 108


Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |





Ms NSL Sugar Ltd Unit-Ill SROaInalRLl2884000 oS

I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

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2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

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(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



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mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company




Part -IDATA SHEET











Forestb Others







Part-I DATA SHEET


Industry













Forest b Others





Not applicable

20

12

Financial crisis















Planned)














Rs300 Crores

Rs5 Crores


Rs34604 Crores


Rs 199 Crores




Not Applicable


Not Applicable



Planned)



Financial crisis




11042016


As under

Vj8





No reply from PA




sh





















falls in Category A



d


Final ElAEMP Report

CHAPTER-II

RAW MATERIAL AND



















falls in Category A








Colony




sugarcane



2850 m3day






Distillery - 2850

Power Plant - 700





-----bull

-

--

-


Final EIAEMP Report

jd





Colony




sugarcane



2850 m3day



Table - 2



Proposed

Requirement


Distillery - 2850

Power-Plant - 700


Total 1480 6200

rs

mmf



mm

-bullbullbull


Fmal EINEMPReport

232 Water balance

A Water Input




B Water Output








24 MANPOWER


Table - 3




Distillery - 75 75+-- ----~ --- ---


I----------- J------- --



Imdash

gtbull

-

p

Itei


Final EIAEMP Report

232 Water balance

A Water Input




B Water Output








MANPOWER 24


Table - 3

Total Manpower




Distillery - 75 75


Total 350 145 495








241 Power








distillery






Sugar Mill 4MW 10MW

Distillery - 125 MW



Colony - 025 MW





-------bullbull-

bullbullbull


Final EIAEMP Report




241 Power








distillery




Table - 4

Power Requirement



Distillery - 125 MW



Colony - 025 MW






Final EIAEMPReport

Table - 5





(Existing)


(Proposed)









steam turbine

2412 Source of Fuel





i I




Final EIVEMP Report

Table - 5

Details of DG Set

s

No

No of

DG sets

Capacity Height of

stacks

No of

stack

Fuel

used

Fuel

consumption

1 1 160 KVA

(Existing)


2 1 625 KVA

(Existing)


3 2 1000 KVA

(Proposed)










steam turbine

2412 Source of Fuel

Table - 6

Fuel Source

Raw

Material


Transportation


sugar milt

Within the

premises

Bagasse conveyors



-2



81 INTRODUCTION








The aims of EMP are















1~

cr

u

u

i^

1-

iBfMa An^6^U^-2-


Final

EIAEMP Report

CHAPTER-VIII


81 INTRODUCTION








The aims of EMP are
















Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv









er MA NSL Sugar Ltd Unit-Ill SROJalnalRi12884000 o8 C

Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


12

Financial crisis















Planned)














Rs300 Crores

Rs5 Crores


Rs34604 Crores


Rs 199 Crores




Not Applicable


Not Applicable



Planned)



Financial crisis




11042016


As under

Vj8





No reply from PA




sh





















falls in Category A



d


Final ElAEMP Report

CHAPTER-II

RAW MATERIAL AND



















falls in Category A








Colony




sugarcane



2850 m3day






Distillery - 2850

Power Plant - 700





-----bull

-

--

-


Final EIAEMP Report

jd





Colony




sugarcane



2850 m3day



Table - 2



Proposed

Requirement


Distillery - 2850

Power-Plant - 700


Total 1480 6200

rs

mmf



mm

-bullbullbull


Fmal EINEMPReport

232 Water balance

A Water Input




B Water Output








24 MANPOWER


Table - 3




Distillery - 75 75+-- ----~ --- ---


I----------- J------- --



Imdash

gtbull

-

p

Itei


Final EIAEMP Report

232 Water balance

A Water Input




B Water Output








MANPOWER 24


Table - 3

Total Manpower




Distillery - 75 75


Total 350 145 495








241 Power








distillery






Sugar Mill 4MW 10MW

Distillery - 125 MW



Colony - 025 MW





-------bullbull-

bullbullbull


Final EIAEMP Report




241 Power








distillery




Table - 4

Power Requirement



Distillery - 125 MW



Colony - 025 MW






Final EIAEMPReport

Table - 5





(Existing)


(Proposed)









steam turbine

2412 Source of Fuel





i I




Final EIVEMP Report

Table - 5

Details of DG Set

s

No

No of

DG sets

Capacity Height of

stacks

No of

stack

Fuel

used

Fuel

consumption

1 1 160 KVA

(Existing)


2 1 625 KVA

(Existing)


3 2 1000 KVA

(Proposed)










steam turbine

2412 Source of Fuel

Table - 6

Fuel Source

Raw

Material


Transportation


sugar milt

Within the

premises

Bagasse conveyors



-2



81 INTRODUCTION








The aims of EMP are















1~

cr

u

u

i^

1-

iBfMa An^6^U^-2-


Final

EIAEMP Report

CHAPTER-VIII


81 INTRODUCTION








The aims of EMP are
















Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash

MA NSL Sugar Ltd Unit-Ill SRO ]alnalRL12884000 olaquo

w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company






No reply from PA




sh





















falls in Category A



d


Final ElAEMP Report

CHAPTER-II

RAW MATERIAL AND



















falls in Category A








Colony




sugarcane



2850 m3day






Distillery - 2850

Power Plant - 700





-----bull

-

--

-


Final EIAEMP Report

jd





Colony




sugarcane



2850 m3day



Table - 2



Proposed

Requirement


Distillery - 2850

Power-Plant - 700


Total 1480 6200

rs

mmf



mm

-bullbullbull


Fmal EINEMPReport

232 Water balance

A Water Input




B Water Output








24 MANPOWER


Table - 3




Distillery - 75 75+-- ----~ --- ---


I----------- J------- --



Imdash

gtbull

-

p

Itei


Final EIAEMP Report

232 Water balance

A Water Input




B Water Output








MANPOWER 24


Table - 3

Total Manpower




Distillery - 75 75


Total 350 145 495








241 Power








distillery






Sugar Mill 4MW 10MW

Distillery - 125 MW



Colony - 025 MW





-------bullbull-

bullbullbull


Final EIAEMP Report




241 Power








distillery




Table - 4

Power Requirement



Distillery - 125 MW



Colony - 025 MW






Final EIAEMPReport

Table - 5





(Existing)


(Proposed)









steam turbine

2412 Source of Fuel





i I




Final EIVEMP Report

Table - 5

Details of DG Set

s

No

No of

DG sets

Capacity Height of

stacks

No of

stack

Fuel

used

Fuel

consumption

1 1 160 KVA

(Existing)


2 1 625 KVA

(Existing)


3 2 1000 KVA

(Proposed)










steam turbine

2412 Source of Fuel

Table - 6

Fuel Source

Raw

Material


Transportation


sugar milt

Within the

premises

Bagasse conveyors



-2



81 INTRODUCTION








The aims of EMP are















1~

cr

u

u

i^

1-

iBfMa An^6^U^-2-


Final

EIAEMP Report

CHAPTER-VIII


81 INTRODUCTION








The aims of EMP are
















Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company






















falls in Category A



d


Final ElAEMP Report

CHAPTER-II

RAW MATERIAL AND



















falls in Category A








Colony




sugarcane



2850 m3day






Distillery - 2850

Power Plant - 700





-----bull

-

--

-


Final EIAEMP Report

jd





Colony




sugarcane



2850 m3day



Table - 2



Proposed

Requirement


Distillery - 2850

Power-Plant - 700


Total 1480 6200

rs

mmf



mm

-bullbullbull


Fmal EINEMPReport

232 Water balance

A Water Input




B Water Output








24 MANPOWER


Table - 3




Distillery - 75 75+-- ----~ --- ---


I----------- J------- --



Imdash

gtbull

-

p

Itei


Final EIAEMP Report

232 Water balance

A Water Input




B Water Output








MANPOWER 24


Table - 3

Total Manpower




Distillery - 75 75


Total 350 145 495








241 Power








distillery






Sugar Mill 4MW 10MW

Distillery - 125 MW



Colony - 025 MW





-------bullbull-

bullbullbull


Final EIAEMP Report




241 Power








distillery




Table - 4

Power Requirement



Distillery - 125 MW



Colony - 025 MW






Final EIAEMPReport

Table - 5





(Existing)


(Proposed)









steam turbine

2412 Source of Fuel





i I




Final EIVEMP Report

Table - 5

Details of DG Set

s

No

No of

DG sets

Capacity Height of

stacks

No of

stack

Fuel

used

Fuel

consumption

1 1 160 KVA

(Existing)


2 1 625 KVA

(Existing)


3 2 1000 KVA

(Proposed)










steam turbine

2412 Source of Fuel

Table - 6

Fuel Source

Raw

Material


Transportation


sugar milt

Within the

premises

Bagasse conveyors



-2



81 INTRODUCTION








The aims of EMP are















1~

cr

u

u

i^

1-

iBfMa An^6^U^-2-


Final

EIAEMP Report

CHAPTER-VIII


81 INTRODUCTION








The aims of EMP are
















Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company







Colony




sugarcane



2850 m3day






Distillery - 2850

Power Plant - 700





-----bull

-

--

-


Final EIAEMP Report

jd





Colony




sugarcane



2850 m3day



Table - 2



Proposed

Requirement


Distillery - 2850

Power-Plant - 700


Total 1480 6200

rs

mmf



mm

-bullbullbull


Fmal EINEMPReport

232 Water balance

A Water Input




B Water Output








24 MANPOWER


Table - 3




Distillery - 75 75+-- ----~ --- ---


I----------- J------- --



Imdash

gtbull

-

p

Itei


Final EIAEMP Report

232 Water balance

A Water Input




B Water Output








MANPOWER 24


Table - 3

Total Manpower




Distillery - 75 75


Total 350 145 495








241 Power








distillery






Sugar Mill 4MW 10MW

Distillery - 125 MW



Colony - 025 MW





-------bullbull-

bullbullbull


Final EIAEMP Report




241 Power








distillery




Table - 4

Power Requirement



Distillery - 125 MW



Colony - 025 MW






Final EIAEMPReport

Table - 5





(Existing)


(Proposed)









steam turbine

2412 Source of Fuel





i I




Final EIVEMP Report

Table - 5

Details of DG Set

s

No

No of

DG sets

Capacity Height of

stacks

No of

stack

Fuel

used

Fuel

consumption

1 1 160 KVA

(Existing)


2 1 625 KVA

(Existing)


3 2 1000 KVA

(Proposed)










steam turbine

2412 Source of Fuel

Table - 6

Fuel Source

Raw

Material


Transportation


sugar milt

Within the

premises

Bagasse conveyors



-2



81 INTRODUCTION








The aims of EMP are















1~

cr

u

u

i^

1-

iBfMa An^6^U^-2-


Final

EIAEMP Report

CHAPTER-VIII


81 INTRODUCTION








The aims of EMP are
















Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)

0f8Mis NSLSugar Ltd Unit-lit SROjalnallRt12884000






































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


-bullbullbull


Fmal EINEMPReport

232 Water balance

A Water Input




B Water Output








24 MANPOWER


Table - 3




Distillery - 75 75+-- ----~ --- ---


I----------- J------- --



Imdash

gtbull

-

p

Itei


Final EIAEMP Report

232 Water balance

A Water Input




B Water Output








MANPOWER 24


Table - 3

Total Manpower




Distillery - 75 75


Total 350 145 495








241 Power








distillery






Sugar Mill 4MW 10MW

Distillery - 125 MW



Colony - 025 MW





-------bullbull-

bullbullbull


Final EIAEMP Report




241 Power








distillery




Table - 4

Power Requirement



Distillery - 125 MW



Colony - 025 MW






Final EIAEMPReport

Table - 5





(Existing)


(Proposed)









steam turbine

2412 Source of Fuel





i I




Final EIVEMP Report

Table - 5

Details of DG Set

s

No

No of

DG sets

Capacity Height of

stacks

No of

stack

Fuel

used

Fuel

consumption

1 1 160 KVA

(Existing)


2 1 625 KVA

(Existing)


3 2 1000 KVA

(Proposed)










steam turbine

2412 Source of Fuel

Table - 6

Fuel Source

Raw

Material


Transportation


sugar milt

Within the

premises

Bagasse conveyors



-2



81 INTRODUCTION








The aims of EMP are















1~

cr

u

u

i^

1-

iBfMa An^6^U^-2-


Final

EIAEMP Report

CHAPTER-VIII


81 INTRODUCTION








The aims of EMP are
















Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer

Mis NSL Sugar LtdUnit-lit SROJalnaiJIRILI12884000 q(8




























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company







241 Power








distillery






Sugar Mill 4MW 10MW

Distillery - 125 MW



Colony - 025 MW





-------bullbull-

bullbullbull


Final EIAEMP Report




241 Power








distillery




Table - 4

Power Requirement



Distillery - 125 MW



Colony - 025 MW






Final EIAEMPReport

Table - 5





(Existing)


(Proposed)









steam turbine

2412 Source of Fuel





i I




Final EIVEMP Report

Table - 5

Details of DG Set

s

No

No of

DG sets

Capacity Height of

stacks

No of

stack

Fuel

used

Fuel

consumption

1 1 160 KVA

(Existing)


2 1 625 KVA

(Existing)


3 2 1000 KVA

(Proposed)










steam turbine

2412 Source of Fuel

Table - 6

Fuel Source

Raw

Material


Transportation


sugar milt

Within the

premises

Bagasse conveyors



-2



81 INTRODUCTION








The aims of EMP are















1~

cr

u

u

i^

1-

iBfMa An^6^U^-2-


Final

EIAEMP Report

CHAPTER-VIII


81 INTRODUCTION








The aims of EMP are
















Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company



Final EIAEMPReport

Table - 5





(Existing)


(Proposed)









steam turbine

2412 Source of Fuel





i I




Final EIVEMP Report

Table - 5

Details of DG Set

s

No

No of

DG sets

Capacity Height of

stacks

No of

stack

Fuel

used

Fuel

consumption

1 1 160 KVA

(Existing)


2 1 625 KVA

(Existing)


3 2 1000 KVA

(Proposed)










steam turbine

2412 Source of Fuel

Table - 6

Fuel Source

Raw

Material


Transportation


sugar milt

Within the

premises

Bagasse conveyors



-2



81 INTRODUCTION








The aims of EMP are















1~

cr

u

u

i^

1-

iBfMa An^6^U^-2-


Final

EIAEMP Report

CHAPTER-VIII


81 INTRODUCTION








The aims of EMP are
















Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent

Mis NSL Sugar ua UnitI SRO jalnaIIRL12884000 8


Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


-2



81 INTRODUCTION








The aims of EMP are















1~

cr

u

u

i^

1-

iBfMa An^6^U^-2-


Final

EIAEMP Report

CHAPTER-VIII


81 INTRODUCTION








The aims of EMP are
















Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company



Final

EIAIEMP Report

821 Air Environment








---




under --


= h + 25



H = h + 02 J 625

= h + 5



-----

-

-~-

11-56

= h + 632



below


o

O

n


Final EIAEMP Report

x

821 Air Environment












under -


H = h + 02 V 160

h + 25



H = h + 02 V 625

h + 5



h + 632



below

W

ltw

ma w


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


I




of Fuel1 Boiler




KUday roof level






8211 Sugar Mill















Final EIAEMP Report

TABLE 58



8211 Sugar Mill














s No


Stack Height

Pollution

1

(

Boiler

1

Proposed

135 TPH Bagasse

1500 TPD

65 m ESP

2

Existing

20 TPH

each

Bagasse

500 TPD


2 DG Set 2

Existing

1 X160 KVA

HSD

0756 KLday

25 m above

roof level


1 X 625 KVA

HSD

2750 KUday

50 m above

roof level

3 DG Set 2

Proposed 2x1000

KW

HSD

85 KLday

70 m each

above roof level



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company



8213 Distillery






adopted






all the time














--

-


Final

EIAEMP Report

8213 Distillery

O

o

o






adopted






all the time













flU


^1 9gt


8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company



8221 Sugar Mill





8222 Power Plant




development


1

n

o

u

u

l

L

U

L

u


Final

ElAEMP Report

8221 Sugar Mill





8222 Power Plant




development

L

U


1^6


8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company



8223 Distillery








boiler







conservation








medium


o

0

n

n

u

l

u

u

U

L_


8223 Distillery



and COD






boiler







conservation



heating medium






medium


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


))

~)


REIAIEMP Report


vessels


required fluid


























--bull-bull-



vessels


required fluid


























V

V


laquo


REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company



REIAEMP Report










in production




11-17 K20 content











)


REIAEMP Report










in production




11-17 K2O content

TABLE 59



1 Feed rate to

evaporator

TPH 3772




5 Water Evaporation

Rate

TPH 2658

6 Total Solids in

Product

WW 5558

7 Total Steam

Required

TPH 886



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company



REIAIEMP Report







2 Steams




-bull

---

-bull

--bull--



REIAEMP Report

TABLE 60





delta T=10 deg




2 Steams





plant


(kwh)

A Based on molasses

as feed stock

5500 5000

V

V- -bullbullpi

mdashltlaquo V


v -4M

V

V

Sto-


REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company



REIAIEMP Report

PREQCESS DIAGRAM

ODED FUEL











REIAEMP Report

PREOCESS DIAGRAM





-CIASBAM

VACUUM PmiP





rzin s

TANK turbine

STEAM FOR PROCESS




c SCRLfflBfcR

JvAJ ID FAN

tO FAN ID FAN










REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company



REIAIEMP Reportn)

Press Mud







growing sugarcane

Sludge from ETP















transportation





bull



Press Mud







growing sugarcane

Sludge from ETP

a v

- Mi V

m Sm

V






Ash











transportation





mdashi ^

U

u

u

u

u

-J

I


REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company



REIAIEMPReport



























gaseous pollutants




)

o


REIAEMP Report






















extent






gaseous pollutants












































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company










































































xiii

Xiv

xv












Scientist ^TTT




SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


SUMMARY NOTE







SUMMARY NOTE











~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company






~-~~~~~bScientist 0


lt~-7 )YgtC jO-T D







M-Afcb Scientist D





gtis



MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company




MAHARASHTRA







r bull fJf









Schedule -I

l Tradeeffluent

2 Domesticeffluent



Tel 240104372402078124014701 Fax 24024068 24023515






i-v

Subject

Ref




1

2

3










1 Trade effluent


270)

As per Schedule -I


2 Domestic effluent




5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


5


I


Use as manure

l


30 MTD2











y msgmM








i - bull






30 MTD j |

-V Use as manure





fx ^

bull- bull1 gt - r

-On mdash N

f-Zfr - -1

rnn




1 Rs 692189- | 233388 ( 05062015 | SBI Bank |






I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


I I) TermsampC

1) A] AspCap

BJ TheeffluEPstrin

SN

00000000

C] Theirriganydirec

D Trad

E1 eREI

ii

iiiiv


thatbull after

HJ Thewate

2) A] Altppro vi

B] Theto ac(1)(2)

C] The














-




2)

Sr No




03 BOD (3 days 27oC) 100 )


07 Chloride 600


C]

D]

El


n

in iv










Vd

iX1

)






(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company







(ii)

(iii)

(iv)

(v)

(vi)





3)

4)

5)

6)

ID













k-

1 2



835


mdash


w

72-2

---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


---------~




3










Schedale-II



Sr bull No

System iliiiiiiS

sw

metei Quantity s m

sect0)- Kg Day





-A--

4 DG Set 1250 KVA


5 DG Set 750 KVA


6 DG Set 625 KVA

Acoustic enclosure

50 HSD 14 KLD 1 280

7 DG Set 250 i KVA

Acoustic enclosure

50 HSDV 07 KLD 1 140

W


3

4

5






PogeSofS

BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


BGHi

Sr CoNo (eto

1 CtoR

NEW

Sr ConsNo (eto E

2 CtoR

Ms NSL Sugar Ltd U

story


nscntEOR)

AmtofBGImposed




BG


CompliaiiceP~riod


Rs100Lacs

Purpose of BG

15days


Validity lDate

30112016


Tm T


BG History

Sr No

Consent (C to EOR)

Amt of BG Imposed


imposed BG




NEW BG Cv

Sr No

Consent (Cto EOR)

Amt of BG Imposed

Submission Period


Validity Date



v


C

tS

-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


-----~---------





1)

2)3)

6)

7)

8)

9)

10)

11)

12)

13)

14)

15)

16)a)

b)







































----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company




















----oooorer





























m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company










m



NSL Sugars Limited

Unit III Jay Mahesh







Signature


Unf

sh








hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company







hlXft~V)

~(gnature




NSL Sugars Limited

Unit 111 Jay Mahesh






gnature


f

U

1

Is NO

m fGroup Company


i1mc41y) qn:c4d'1 ,..,q''''''?lrt:im:::rltq tel: ministry of...

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