59
PROJECT PRE-FEASIBILITY REPORT Of PROPOSED EXPANSION PROJECT For SYNTHETIC ORGANIC CHEMICALS MANUFACTURING UNIT At Plot No. 1088/B Lamdapura road, Village: Manjusar, Ta: Savli, Dist: Vadodara, Gujarat Project proponent

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Page 1: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

  

PROJECT PRE-FEASIBILITY REPORT  

Of  

PROPOSED EXPANSION PROJECT For

 

SYNTHETIC ORGANIC CHEMICALS MANUFACTURING UNIT

At   

Plot No. 1088/B Lamdapura road,

Village: Manjusar, Ta: Savli,

Dist: Vadodara, Gujarat

Project proponent

Page 2: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

CHAPT EXE The pro Table 1

PARTIC

NAME OUNIT OCCUPPRODUC

LOCATINATUREPROJEC

 

t Prefeasib

Proposed ex

TER – 1

ECUTIV

oject is sum

1.1: Project

CULARS DET

OF THE M/s

IER Mr. CTS

S.No

Ex1. 2. 3. 4. 5. 6 7. 8.

9. 1011Pr4. 5. 6. Pr7. 8. 9. 10TO*N24

ON PlotE OF CT

Prosim

bility Repo

xpansion pro

VE SUM

marized in

t Summary

TAILS

. Universal Este

Vishwas R. Go

o.

Name of

xisting Produc Methyl An Ethyl Sali Ethyl Ben Amyl Sali Benzyl Sa

Menthyle Amyl Ace Or any oth

of organg Octyl Met0. Octyl Sali1. Octyl Hydroposed produ Homosala Cosmetic Ethyl metroposed produ Octocryle Benzophe Benzophe0. AvobenzoOTAL Note: The comp4/07/2015 for mant No. 1088/B, laposed Expansiilar category of

ort

oject for man

MMARY

the below t

y

er Ltd.

ole, Mr. Mukesh

Products

cts* nithranilate* cylate*

nzoate* cylate* alicylate* Salicylate*

etate* her type of chee esters* thoxycinnamatecylate

droxystearate ucts ate emmolients thoxyCinnamateucts (Repackinene enone-3 enone -4 one

pany has obtainnufacturing of theamdapura road,on Project for I

f products i.e. sy 

nufacturing o

Y

able:

h D.Patel, Mr. D

micals in categ

e

e ng & Reselling

ed consolidatedese products as w, Village: Manjuncrease in exisynthetic organic

of Synthetic O

Dushyant D. Pat

ExisQuan

ory

)

consent & Autwell, but is not mausar, Ta: Savli, sting productionc chemicals

Organic Che

tel

Proposed QuaQuantity

sting ntity After

1.5 1.25 1.6 3.0 8.0 0.5 2.0

--

8 6 2

- - -

- - - -

16 thorization (CC&anufacturing themDist: Vadodaran quantities and

micals  

antity of Produ in MT / Month

r Phase-I Af

NIL

125

5

10

140 &A) no. H 3831m anymore.

a, Gujarat d adding new p

1

uction h

fter Phase-II

NIL

200

5

10

215 5 valid up to

products in the

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Project

Project: 

RESOURResourc

Land

Building

Raw-ma

Water

Power

Fuel

Man-powPOLLUTParamet

Wastewa

Air Emis

t Prefeasib

Proposed ex

RCES ce type Req

Exis369

150

aterials As g

Exis4.6

125

Agrokg/d

wer 35 TION POTENTIter

Exiater Indu

KLDDomKLD

ssions •

bility Repo

xpansion pro

quirement sting

94.48 m2

00.00 m2

given in section

sting KLD

5 KVA

o waste-500 day

IAL & MITIGAT

sting ustrial: 0.60 D mestic: 1.20 D

Non IBR Boiler 1 no.

ort

oject for man

After Phase3694.48 m2

1500.00 m2

n 3.5 - Raw Mat

After Phase29.0 KLD

250 KVA

Agro waste-kg/day Diesel-50 LP50

TION MEASURPoten

After PhaseIndustrial: 7Domestic: 2

• TFH – 2 N6 lakh k.cand 1 of 1kcal/hrs.

• D.G. Set KVA 1 no

nufacturing o

e-I Aft 369

150

terial for finishe

e-I Aft37

250

-8000

PH

Agrkg/dDie55

RES ntial e-I Aft.0 KLD 2.0KLD

IndDom

Nos. 1 of cal/hrs 10 lakh

125 os.

• T6ak

• DK

of Synthetic O

ter Phase-II 94.48 m2

00.00 m2

ed products.

ter Phase-II KLD

0 KVA

ro waste-8000 day

esel-50 LPH

ter Phase-II ustrial: 10.0 KLmestic: 2.2KLD

TFH – 2 Nos. 1 6 lakh k.cal/hrs and 1 of 10 lakhkcal/hrs. D.G. Set 125 KVA 1 nos.

Organic Che

Source

No additexpansioOnly slighinfrastrucThe raw Local/ Inimported Fresh wabore well of supply Sourced f1 D.G. Sas StandbLocal Sup

To be em

Mitigatio

LD D

• The dodisposedsoak pit

• In exiswastewatreated purpose

• After wastewaTreated sent to evaporat

of h

• In existiBoiler isused as

• For proBoiler wThermic kcal/hrs capacitieKVA cap

• Agro waTFH

• Cyclone TFH as A

• Diesel wSet.

• There isfrom theproposed

• Raw Ma

micals  

tional land is n project. ht modification cture will be don materials are

ndian market a from foreign co

ater is sourced and same will for the additionfrom MGVCL et 125 KVA wiby arrangemenppliers.

mployed from loc

n Measures

omestic effluend off through system.

sting operatioater is treatedwater is used .

proposed ater will be tre

effluent from CETP of EIC

ted in evoporatng operations s installed. Ag fuel in non IBRposed expanswill be repla Fluid heater

and 10laes and one D.Gpacities will be iaste will be us

separator will bAPCD. will be used as

s no process e existing pland expansion pro

aterials& Produc

2

required for

in the existing ne. e available in and are also ountries. from in-house be the source nal quantity.

ill be installed t.

cal area

nt is/will be septic tank/

on Industrial in ETP and for gardning

expansion eated in ETP.

ETP will be CL or will be ion unit. one non IBR gro waste is

R Boiler sion non IBR ced by two

rs of 6 lakh akh kcal/hrs G. Set of 125 nstalled.

sed as fuel in

be attached to

s fuel in D.G.

gas emission nt as well as oject. cts are/will be

Page 4: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

Hazardosolid was

Noise

t Prefeasib

Proposed ex

ous & ste

• E(C0

• DR2M

• S(C0

• U5

• DC(3N

Non• F

M Exp

Insi<80

bility Repo

xpansion pro

ETP Waste Cat. 34.3) :

0.04MT/Month Distillation Residue (Cat. 20.3): 3.36 MT/Yr Spent Carbon Cat.35.3 ):

0.05 MT/Month Used Oil (Cat. 5.1): 1.2KL/Yr Discarded Containers 33.3): 120

Nos./Month

n Haz.Waste Fly ash: 13 MT/yr.

pected levels

ide the plant: 0 dB(A)

ort

oject for man

• ETP Was34.3) : 5.5Month

• DistillationResidue (20.3): 80M

• Spent Ca(Cat.35.3 MT/ Yr

• Used Oil (5.1): 2 KL

• DiscardedContainer(33.3): 98Nos./yr

• Inorganic waste (28MT/yr

• Spent sol(20.2): 21

Non Haz.Wa• Fly ash: 2

MT/yr. Expected le

Inside the pdB(A)

nufacturing o

ste (Cat. 5MT/

n (Cat. MT/Yr

rbon ): 0.1

(Cat. L/Yr d rs /Bags

870

process 8.1): 97

vent 0MT/yr. aste

220

• E3M

• DR2

• S(M

• U5

• DC(N

• InwM

• S(2

Non• F

2

vels

lant: <80

Exp

InsdB(

of Synthetic O

ETP Waste (Ca34.3) : 8.5 MT/ Month Distillation Residue (Cat. 20.3): 125 MT/Y

Spent Carbon Cat.35.3 ): 0.1

MT/Month Used Oil (Cat. 5.1): 2.5 KL/Yr Discarded Containers/Bag33.3): 15210

Nos./yr norganic procewaste (28.1): 15MT/yr Spent solvent 20.2): 325 MT/yn Haz.Waste Fly ash: 220MT/yr.

pected levels

ide the plant: <(A)

Organic Che

stored inarea to p

• Good maintain

• Regular carried expansio

t.

Yr

s

ss 55

yr.

• ETP wtransport

• Distillatiostorage, by coNECL/G

• Spent ctransportincinerat

• Used transportregistere

• Discardestorage, selling to

• Fly ashmanufac

• In-organstorage, TSDF

• Spent sactual us

80

• The mgeneratioequipme

• Anti vibbellows applicab

• Acousticbe provid

• Ear plug• Regular

shall be

micals  

n properly desprevent any volahousekeeping

ned in the plant. VOC monito

out afteron.

waste: Collectirtation, disposalon residue: transportation ommon incEPIL.

carbon: Collectrtation and tor. oil: Collectio

rtation, disposaed re-refiners. ed Containers transportationo registered re-h to be socturer ic process was transportation

solvent will besers.

major sourceson in plant

ent machinary abration pads

is provideble. c Enclosure to ded. and Ear muff a maintenancedone.

3

igned storage atilities is/will be . oring will be r proposed

ion, storage, l at TSDF.

Collection, and disposal inerator at

tion, storage, disposal by

on, storage, l by selling to

s: Collection, , disposal by refiners. old to brick

ste: Collection, n, disposal at

e sold to the

s of noise t area are and TFH.

and flexible ed wherever

D.G. Set will

are provided. e lubrication

Page 5: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

CHAPTINTR 2.1 I 2.1.1 ID

M/s. Unin the coin the CLamdap

The unitHydroxyvalid umanufacAnnexu

Now, thcategory

Table 2S. No.

Na

Existing1. Me2. Eth3. Eth4. Am5. Be6 Me7. Am8. Or

org9. Oc10.

Oc

11.

Oc

Propose4. Ho5. Co6. Eth

 

t Prefeasib

Proposed ex

TER – 2 RODUC

DENTIFIC

DENTIFICA

iversal Esterommercial prCosmetics inpura road, Ta

t is engagedystearate. Thp to 24/07cturing only

ure-1.

e company y of products

2.1: List of ame of Produc

g Products* ethyl Anithranilahyl Salicylate* hyl Benzoate* myl Salicylate* enzyl Salicylate*enthyle Salicylamyl Acetate* r any other typegange esters* ctyl Methoxycinctyl Salicylate

ctyl Hydroxystea

ed products omosalate osmetic emmolihyl methoxyCin

bility Repo

xpansion pro

CTION

CATION OF

ATION OF T

r Ltd. is a Limroduction of ndustry at itsa.: Savli, Dist

d in manufache company 7/2015 for m

above given

has planneds. The list wis

Products cts

ate*

* ate*

e of chemicals in

namate

arate

ents nnamate

ort

oject for man

N OF TH

F THE PRO

THE PROJE

mited compaPersonal cars manufactut.: Vadodara.

cturing of (1has obtained

manufacturinn three prod

d to increasse products a

n category of

 

nufacturing o

HE PRO

OJECT AN

ECT

any which ware ingredienturing facility . The compa

) Octyl Methd consolidate

ng of 11 vaducts. The e

e its existingand its produ

Exist

of Synthetic O

OJECT

ND PROJE

as establishets, used in valocated at ny is a small

hoxycinnamaed consent &arious produexisting cons

g capacity auction capaci

ProposQ

ting Quantity

1.51.251.63.08.00.52.0

--

86

2

---

Organic Che

ECT PROP

ed in 1994.Tarious types Plot No. 10l scale chem

ate, (2) Octy& Authorizatiucts but present to oper

and add newity are given

sed Quantity oQuantity in MT

After Pha

5 5 6 0 0 5 0 -

8 6

2

- - -

micals  

PONENT

The companyof formulatio88/B, Village

micals manufa

yl Salicylate ion (CC&A) esently the rate-CCA is

w products inin table belo

of Production / Month

ase-I Af

NIL

125

5

4

y is engagedons, primarilye: Manjusaracturing unit.

and (3)Octyno. H 38315company isattached as

n the similarow:

fter Phase-II

NIL

200

5

d y , .

l 5 s s

r

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Project

Project: 

Propose7. Oc8. Be9. Be10.

Av

TOTAL *Note: Tthese pro

2.1.2 P

The coprofessEnviron Below i

Mr.Vish

Mr.Vishin the CBefore after Te

Mr. Mu

Mr. Muindustry

Table 2

Sr. No. 1.

2.

3.  

2.2 The profalls unSeptemindustriEnviron

t Prefeasib

Proposed ex

ed products (Rctocrylene enzophenone-3enzophenone -4vobenzone

he company hasoducts as well, bu

PROJECT P

ompany is sionally quanment are fu

s a brief pro

hwas Gole

hwas Gole hChemicals ireturning to

echnical and

kesh Patel

kesh Patel y. He is in a

2.2: Addres

Name of DMr. Vishw

Mr. Muke

Dushyan

NATURE

oposed expnder item

mber 2006 al area/est

nmental Cle

bility Repo

xpansion pro

Repacking & R

4

s obtained consout is not manufac

PROPONEN

a Limitedalified; they ully complie

ofile of the m

(Director)

has done hndustry. Heo India, he d Marketing

(Director)

is a Chema strategic a

sses of Dire

Directors was R. Gole

esh D.Patel

t D. Patel

OF THE P

pansion prono 5(f) i.e(as amendtate; it is

earance from

ort

oject for man

Reselling)

olidated consent &turing them anym

NT

d firm and take every

ed with.

manageme

is graduatioe has workewas Directo

g aspects in

mical Engineadvisory role

ectors

Addre4, Ka

93, U

3& 4

PROJECT

oject involvee. syntheticded timely).

to be tream EIAA (Mo

nufacturing o

& Authorization (more.

directorsy step to e

nt team.

on in Chemed for over or (R&D) w the compa

eer with ovee in the com

esses ant Flats 7, S

Urmi Society

, Aakashwan

es the prodc organic c Since, the

ated as CaoEF).

of Synthetic O

----

16(CC&A) no. H 38

of the coensure that

mistry. He ha25 years w

with a leadinany.

er 40 yearsmpany.

Suvanapuri S

. Productivity

n Hsg. Comp

uction of sychemicals e project isategory A

Organic Che

- - - -

6 8315 valid up to 2

ompany areall safety

as around 4with renowneng US com

s of experie

Soc. Jetalpur

y Road, Vado

plex. Gotri Se

ynthetic orgas per thes not locateand needs

micals  

10

140 24/07/2015 for m

e well edumeasure to

45 years of ed companpany. He m

ence in the

r Road, Vado

odara 7.

evasi Road,

ganic cheme EIA notifed within as to obtain

5

10

215 manufacturing of

ucated ando Plant and

experienceies in USA

mainly looks

Chemicals

odara 5.

Vadodara

micals whichfication, 14any notifiedn the prior

d d

e . s

s

h 4 d r

Page 7: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

2.3 The prothe prorange hless supthat the 2.4 As per as expCosmet 2.5 The proindirect locally f

t Prefeasib

Proposed ex

NEED OF

oducts are uducts are u

having a gopply of the

e company p

EXPORT

market survport market tics industry

EMPLOYM

oposed expemployme

from the ne

bility Repo

xpansion pro

PROJECT

used in varuser friendlyood demandproduct agaproposed to

POSSIBIL

vey by the due to its

y

MENT GEN

pansion proent to few parby areas.

ort

oject for man

T & DEMA

rious types y confirmind in the maainst its demo have this p

LITY

company, ts applicatio

NERATION

oject will prpersons. Th.

nufacturing o

AND-SUPP

of formulatg with inter

arket& as pemand, to ovproject.

these propoon in vario

N DUE TO

rovide direce man-pow

of Synthetic O

PLY GAP

tions, primarnational ster market svercome thi

osed producous types o

O PROPOS

ct employmwer required

Organic Che

arily in the Ctandards. Tsurvey by this shortage

cts are havof formulat

SED PROJ

ent opportud for the pro

micals  

Cosmetics iThe proposehe company& to get be

ing a dometions, prima

JECT

unityto20 poject will be

6

industry. Aled productsy there is aenefit out of

estic as welarily in the

ersons ande employed

l s a f

l e

d d

Page 8: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

CHAPT

PRO 3.1

3.1.1 T

The prmanufaOrganic

3.1.2 L

M/s. UnSavli, D Savli is Developlocated (Vaishnthis villaincludinarts & c The siteState oDistrict.from stand MuBarodainclude

t Prefeasib

Proposed ex

TER – 3

OJECT D

TYPE & L

TYPE

roposed practuring of nc Chemicals

LOCATION

niversal EstDist: Vadoda

a village pment Corp

in this vilnava), Patelage is tobang the K. J. commerce c

e is approxf Gujarat, a. It is locateate capital,

umbai pass , which petrochem

bility Repo

xpansion pro

DESCR

LOCATION

roject is annew range os.

N

ers Ltd. is lara.

near Vadoporation celage near , Brahmin a

acco. Savli iInstitute of

colleges and

ximately 17after Ahmaded on the b Gandhinagthrough Va

is theicals, engin

ort

oject for man

RIPTIO

N OF PROJ

n expansioof products

ocated at P

odara, Gujanters is vethe Mahisa

and Raj putis also becof Engineerind a homeop

.92 kms SSdabad and Sbanks of thgar. Both t

adodara. It ie larges

neering, che

nufacturing o

ON

JECT

on for incrfalling in th

Plot No.108

arat in Wesery near toagar River.ts, Muslims oming an eng and Tecpathic medic

SW from VaSurat. It is the Vishwamhe railway s also the h

st univeremicals,pha

of Synthetic O

rease in ehe similar ca

8/B, Village

stern India it; the bra. The popualso are pa

educational hnology. Incal college.

adodara - tthe adminismitri river, s

line and nahome of thersity in armaceutica

Organic Che

xisting proategory of p

e: Manjusar

. One of anch of Saulation in Sart of the vilhub with a addition to

the third larstrative headsoutheast oational high

e Maharaja Gujarat.

als, plastics

micals  

oduction caproducts, i.e

r, Lamdapur

the Gujaraantram temSavli comprlage. The m

an educationo this colleg

rgest city indquarters o

of Ahmadabhway conneSayajirao U

Major and Forex.

7

apacity ande. Synthetic

ra road, Ta

t Industriample is also

rises Baniamain crop ofnal campus

ge there are

n the Indianof Vadodaraad, 139 km

ecting DelhUniversity of

industries

d c

:

l o a f s e

n a m

i f s

Page 9: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

Figure

 

t Prefeasib

Proposed ex

3.1: Projec

bility Repo

xpansion pro

ct Site

ort

oject for man

nufacturing oof Synthetic OOrganic Chemicals   8

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Project

Project: 

Figure

t Prefeasib

Proposed ex

3.2: Satelli

bility Repo

xpansion pro

ite Image o

ort

oject for man

of the Proje

nufacturing o

ect Site

of Synthetic OOrganic Chemicals   99 

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Project

Project: 

Figure

Table 3

S. No. 1. 2. 3. 4.

t Prefeasib

Proposed ex

3.3: Proje

3.1: Area St

DescrTotal Built-uGreenOpen

bility Repo

xpansion pro

ct Site layo

tatement

ription Plot Area up area nbelt area Area

ort

oject for man

out

nufacturing oof Synthetic OOrganic Chemicals  

Approx

10

x. Area (m2)3694.481500.00600.00

1594.48

Page 12: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.2 The prostudy frequiremavailabproposeHence o Some m

. 3.3 The tota

3.4 It is notand rawand octsections MoreovAvoben

t Prefeasib

Proposed ex

DETAILS

oposed expfor site selment of theility is veryed project. only existin

more benefi

Site is very

Proximity to

Availability

SIZE & MA

al magnitud

PROJECT

teworthy thaw-material fotyl salicylates.

ver, some onzone) are o

bility Repo

xpansion pro

OF THE A

pansion is tlection has

e proposed y helpful to

These togg site is con

ts of the ex

y well conne

o Raw Mate

of power fr

AGNITUD

de of operat

T DESCRIP

at the compfor manuface. Details o

of the prodonly to be p

ort

oject for man

ALTERNAT

to be carries been conexpansion

o avoid insgether justifnsidered for

xisting site a

ected by roa

erial supplie

rom MGVCL

E OF OPE

tion after pro

PTION WIT

pany is propcturing of itsof both exis

ucts (viz. Opurchased, r

nufacturing o

TIVE SITE

ed out in thnducted. Thproject. Fu

stallation offy the use r the propos

are shown b

ad.

ers

L.

ERATION

oposed exp

TH PROC

posing chans existing 2 ting and pro

Octocrylenerepacked an

of Synthetic O

E

he existing he presentrther the exf many infof existing

sed project.

below.

pansion will

ESS DETA

nge in procenos. of prooposed pro

e, Benzophnd sold out.

Organic Che

industrial pt land is axisting infrafrastructure g premises .

be 2400 M

AILS

ess in termsoducts, viz. ocess are p

enone-3, B.

micals  

plot. So noadequate toastructure &

& machinfor propos

T/A.

s of changeoctylmetho

provided in s

Benzopheno

11

o alternativeo cater the& machineryery for the

sed project

e of catalystoxycinamatesubsequent

one -4, and 

e e y e .

t e t

d

Page 13: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.4.1 E

 3.4.1.1

3.4.1.1. 

3.4.1.1. Into an is heatepress. Recove

3.4.1.1.

t Prefeasib

Proposed ex

Existing Pr

OCTYL ME

.1 Chemica

.2 Manufact

S.S. Reacted to 190 CMother liq

ered 2-ethyl

.3 Material B

bility Repo

xpansion pro

oducts Sce

ETHOXYCI

l Reaction

turing Proce

tor para Ani0 - 200C0 fouor is disthexyl aceta

Balance

ort

oject for man

enario

NAMATE (

ess

sic Aldehydor 48 hours.tilled undeate is recyc

nufacturing o

EXISTING

de, catalyst . Then massr high vac

cled in the n

of Synthetic O

PROCESS

& 2-ethyl hs is cooled

cuum to geext batch.

Organic Che

)

exyl acetateto 70C0 -80et 98% oc

micals  

e are charg0C0& filter thctyl methox

12

ged. & masshrough filterxycinamate

s r .

Page 14: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.4.1.1

3.4.1.1. 

3.4.1.1. Into anchargedfilter thmethox

3.4.1.1.

t Prefeasib

Proposed ex

OCTYL ME

.1 Chemica

.2 Manufact

n S.S. Read. & mass ishrough filtexycinamate.

.3 Material B

bility Repo

xpansion pro

ETHOXYCI

l Reaction

turing Proce

ctor para As heated tor press. MRecovered

Balance

ort

oject for man

NAMATE (

ess

Anisic Alde 190 C0 - 20

Mother liquod 2-ethyl he

nufacturing o

PROPOSE

ehyde, inor00C0 for 48or is distillxyl acetate

of Synthetic O

D PROCES

rganic catal8 hours. Theed under is recycled

Organic Che

SS)

lyst & 2-eten mass is chigh vacuu in the next

micals  

thyl hexyl acooled to 7um to get t batch.

13

 

acetate are0C0 -80C0&98% octy

e & l

Page 15: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.4.1.2

3.4.1.2. 

 

3.4.1.2. Into a gare charaise tedistillati

3.4.1.2.

 

t Prefeasib

Proposed ex

OCTYL SA

.1 Chemica

.2 Manufac

glass lined rarged. & maemp, to 150on tank. Cr

.3 Material B

bility Repo

xpansion pro

ALICYLATE

l Reaction

cturing Proc

reactor saliass is slowl0°c for 8 horude is distil

Balance

ort

oject for man

E (EXISTING

cess

cylic acid (1ly heated to

ours & samplled under h

nufacturing o

G PROCES

1100 kgs), o 120°c & hple is givenhigh vacuum

of Synthetic O

SS)

catalyst (60hold for 3 hn to check Gm to get 99%

Organic Che

0 kgs) 2-ethours. ApplyG.C. Then % octyl salic

micals  

hyl hexanol y low vacuucrude is tracylate.

14

 

(1140 kgs)um & slowlyansferred to

 

) y o

Page 16: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.4.1.2

3.4.1.2.

3.4.1.2. Into a gslowly hgiven tovacuum

3.4.1.2.

t Prefeasib

Proposed ex

OCTYL SA

.1 Chemica

.2 Manufact

glass lined rheated to 1o check GC

m to get 99%

.3 Material B

bility Repo

xpansion pro

ALICYLATE

l Reaction

turing Proce

reactor met20C0& hold

C. Then cru% octyl salic

Balance

ort

oject for man

E (PROPOS

ess

thyl salicylad for 3 hourude is transcylate.

nufacturing o

SED PROCE

te, catalyst rs. Slowly rasferred to d

of Synthetic O

ESS)

and 2-ethyaise temp, tdistillation ta

Organic Che

yl hexanol ato 150 C0 foank. Crude

micals  

are chargedor 8 hours &is distilled

15

d. & mass is& sample isunder high

s s h

Page 17: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.4.1.3 3.4.1.3. 

 3.4.1.3. Into a g180 C0 the reac2-ethyl

3.4.1.3.

t Prefeasib

Proposed ex

OCTYL HY

.1 Chemica

.2 Manufact

glass line refor 24 hou

ction & slowhexanol is <

.3 Material B

bility Repo

xpansion pro

YDROXYST

l Reaction

turing Proce

eactor 12HArs & water

wly apply va<2.0% stop

Balance

ort

oject for man

TEARATE

ess

AS, catalysis removed

acuum & thep the vacuum

nufacturing o

sts& 2-ethyd. Check theen under him and heat

of Synthetic O

l hexanol ae acid valuegh vacuum. Cool down

Organic Che

are chargede. If the ac

m remove 2-n to 80®c &

micals  

d. & mass isid value is ethyl hexan

& filter produ

16

 

s heated to<1.5% stop

nol. If GC ofuct.

o p f

Page 18: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.4.2  3.4.2.1

3.4.2.1. 

 3.4.2.1. Into an heated down to99% pu

3.4.2.1.

t Prefeasib

Proposed ex

Proposed

HOMOSAL

.1 Chemica

.2 Manufact

S.S. Reactto 180˚C fo

o 80˚C & trurity & color

.3 Material B

bility Repo

xpansion pro

Products S

LATE

l Reaction

turing Proce

tor methyl sor 24 hoursransfer crudrless produc

Balance

ort

oject for man

Scenario

ess

salicylate, cs & check Gde to distillact.

nufacturing o

catalyst & hGC. If methyation unit. C

of Synthetic O

homo Menthyl salicylateCrude is dis

Organic Che

hyl alcohole is <1.5% sstilled in Co

micals  

are chargestop the reaolumn distill

17

ed& mass isaction. Cooation to get

s l t

Page 19: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

 3.4.2.2

 3.4.2.2.

3.4.2.2. Into (20chargedtemp. <check ucatalystpurity ounit. 3.4.2.2.

t Prefeasib

Proposed ex

ETHYLE M

.1 Chemica

.2 Manufact

00 ltr) glassd. Mass is c< 30°C. Reunreacted pt. Organic a

of ethyl met

.3 Material B

bility Repo

xpansion pro

METHOXYC

l Reaction

turing Proce

s lined reacooled to 1action mixt

p-anisic aldeand water lathoxycinnam

Balance

ort

oject for man

CINNAMAT

ess

actor paraan0°C. 16 kgsture is keptehyde whicayer is sepamate. Wate

nufacturing o

E

nisic aldehys catalyst ist stirring arch is <1.0%arated. Org

er layer is ta

of Synthetic O

yde (40 kgs added oveound 30°C

%. 25% acetganic layer iaken for dis

Organic Che

s), & ethyl er the periofor 3 hour

tic acid is ais taken forstillation in

micals  

acetate (1od of 2 hours. Sample added to ner distillation distillation/e

18

120kgs) arers. Keepingis taken to

eutralize theto get 98%

evaporation

e g o e

% n

Page 20: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.4.2.3

 

3.4.2.3.

3.4.2.3. Into (2030°C. Rwhich isminor lofrom filtobtaine 3.4.2.3.

t Prefeasib

Proposed ex

Cosmetic

.1 Chemica

.2 Manufact

00 ltr) glass Reaction ms sent to Eoss occurretration unit

ed.

.3 Material B

bility Repo

xpansion pro

Emollients

l Reaction

turing Proce

lined reactixture is ke

ETP. Then ed. Sample

where proc

Balance

ort

oject for man

s

ess

tor carboxylept stirring it is taken is taken to cess waste

nufacturing o

ic acid, alcoaround 30°into high vacheck for G is separate

of Synthetic O

ohol & cata°C for 3 hoaccum dist

GC and cooled. Finally

Organic Che

alyst are chaours. Aqueoillation. Alcled down. T98% pure

micals  

arged. Keepous layer iscohol is sepThen mixturcosmetic e

19

ping temp.<s separatedparated andre is passedmollients is

< d d d s

Page 21: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.5 The rawalso imp Table 3

 

3.5.1 Hazardhandlin

Table 3

Raw Ma

Raw MaP-Anisi2-EthylMethyl 2-Ethyl12 H.S

Octyl Methox

Octyl S

Octyl H

Homos

Ethyl methox

t Prefeasib

Proposed ex

RAW MAT

w materials ported.

3.2(a): List

HAZARDO

ous chemicg & transpo

3.2(b): Stor

aterial/ finished

aterial ic Aldehyde lHexylacetateSalicylate

lHexanol .A.

Product

xycinnamate

Salicylate

HydroxyStear

salate

xyCinnamate

bility Repo

xpansion pro

TERIAL FO

for the pro

of Raw Ma

OUS CHEMI

cals are/willort of Hazar

rage, Hand

d goods

e

Nam

P-An2-EthCata

SalicMeth2-EthCata

rate 12 H2-EthCata

MethHomCata

e

P-AnEthylCataAceti

ort

oject for man

OR FINISH

oposed rang

aterials

ICAL STOR

l be used ardous Chem

ling & Tran

Source

Local/ImLocal/Im

me of Raw M

nisic Aldehydhyl Hexylacelyst

cylic acid hyl Salicylatehyl Hexanollyst

.S.A. hyl Hexanollyst

hyl Salicylateo Menthyl Allyst

nisic Aldehydl Acetate lyst ic acid (25%

nufacturing o

HED PROD

ge of produ

RAGE & HA

as raw matemicals are gi

nsport of H

CAS

Local 123-1Local 103-0

ported 119-3ported 104-7Local 106-1

Material

de etate

e

e lcohol

de

)

of Synthetic O

DUCTS

cts will be i

ANDLING

erial in the iven in table

Hazardous C

No

1-5 09-3 36-8 76-7 4-9

ReExisting

4.03712.470.004

3.474

4.4230.001

1.50.84

0.0001

Organic Che

indigenousl

manufactue 3.2(b).

Chemicals

Means ofstorage

DrumsDrumsDrumsDrumsDrums

equirement (g After Ph77 14

4-31

541 0

---

----

micals  

y available

ring proces

f e

Means of transport

s Truck s Truck s Truck s Truck s Truck

(MT/Month) hase I Aft63.07

194.95 8.03

Or -

80.13 92.15 0.02

Or 93.75 52.5

0.0063 Or

77.38 97.62 0.060

And 3.64

10.91 0.91 3.18

20

and will be

ss. Storage

Max. Qty. stored MT

5 10 10 15 5

ter Phase II100.92311.9312.84

-128.41147.44

0.04

150.0084.000.10

123.81156.19

0.1

3.6410.910.913.18

e

,

Page 22: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

Raw Ma

Homo Ethyl AAcetic ProductOctyl MOctyl SOctyl HHomosEthyl m

3.6 The ma 3.6.1 Total exwill be carried

3.6.2 Some a Table 3 Sr. No.Existin1 2 3 4 5 6 7 8 9 10 11 12 13. Propos1 2 3 4 5

t Prefeasib

Proposed ex

aterial/ finished

Menthyl AlcoAcetate acid ts MethoxycinnaSalicylate HydroxyStearsalate methoxyCinna

RESOURC

ajor resourc

LAND & B

xisting plot required forout. Land P

EQUIPMEN

additional eq

3.3: List of

. Equipmng

Glass liSS 316 SS 316 SS 316 SS 316 SS 316 SS 316 SS 316 SS 316 SS 316 AdvancNutche Non IBR

sed additionVacuumSS 316 SS 316 ThermicDeep Fr

bility Repo

xpansion pro

d goods

ohol

amate

rate

amate

CE OPTIM

es for the p

UILDING R

area is 369r proposed Possession

NTS

quipment w

Equipmen

ments

ne Reactor (Reactor (3 KDistillation VDistillation VReactor (1.5Reactor (2 K(1 KL) Reactor (4 KReactor (5 KReactor (6 K

ced ContinuoFilter

R Boiler nal

m pumps Reactor (5 KReactor (6 K

c fluid heaterreezer Chillin

ort

oject for man

Source

ppppp

MIZATION

proposed pr

REQUIREM

94.48 m2andproject expDocument

will be neede

ts

(3 KL) KL) Vessel (800LVessel (2 KL5 KL) KL)

KL) KL ) KL)

ous Distillatio

KL ) KL) r (6& 10lakh.ng Unit

nufacturing o

CAS

Local 79-20Local 141-7Local 64-19

roduct 5466-roduct 118-6roduct 29710roduct 118-5roduct 5466-

& AVAILA

roject are/w

ENT

d total constpansion. Miis attached

ed for the p

L) )

n Unit

k.cal/hrs.)

of Synthetic O

No

0-9 78-6 9-7

-77-3 60-5 0-25-6 56-9 -77-3

ABILITY

ill be raw-m

tructed areanor constru as Annexu

roposed ex

Organic Che

Means ofstorage

DrumsDrumsDrums

DrumsDrumsDrumsDrumsDrums

materials, wa

a is 650.44 uction and fure-2.

xpansion.

micals  

f e

Means of transport

s Truck s Truck s Truck

s Truck s Truck s Truck s Truck s Truck

ater, man-p

m2. No addfabrication w

21

Max. Qty. stored MT

5 5

10

10 10 10 10 2

ower, etc.

ditional landwork will be

No

1211221111111

122121

d e

Page 23: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.6.3 Total po250 kVA In exist8000 kgfuel in D Table 3 

Sr. No.

Power1

Fuel 1

 

3.6.4 For exisfrom in be 29.0well. The catTable 3 Table 3

S.No.

1. 2. 3. 4. 5. 6. 7. 8. 9.

 

t Prefeasib

Proposed ex

POWER A

ower requirA, sourced

ing 500 kg/g/day Agro D.G. Set.

3.4: Details

Particulars

r Power Requiremen

Fuel & it’s consumption

WATER RE

sting projechouse, bor

0 KLD after

tegory wise3.5

3.5: Catego

Particula

Domesti Gardenin Industria Process Boiler Cooling ( washing Sub-Tota Grand To

bility Repo

xpansion pro

ND FUEL R

ement for efrom Madhy

/day Agro wwaste will

of Power &

RequiremExistingScenario

nt 125 kVA

n Agro was500 kg/d

EQUIREME

ct, water is rre well. Totaphase l and

e bifurcation

ory-wise Wa

ars

c ng al

(Make-up)

al: Industriaotal

ort

oject for man

REQUIREM

existing projya Gujarat V

waste is usebe used in

& Fuel

ment g o

P

2

ste @ ay

A8D

ENT

required for al fresh watd 37.0 KLD

n of the wa

ater Requi

al

nufacturing o

MENT

ject is 125 kVij Compan

ed as fuel foproposed T

Phase I

250 kVA

Agro waste @8000 kg/dayDiesel@ 50 L

domestic, pter requiremafter phase

ater require

rement (in

Existin

of Synthetic O

kVA and aftny Ltd. (MG

or non IBR Thermic flui

Phas

250

@

LPH

Agro8000DiesLPH

process andment for exie II which w

ment is giv

KL/D)

Reqng scenario

1.40.0

0.21.02.00.03.24.6

Organic Che

ter proposeVCL)

boiler. Afteid heaters.

se II

kVA

o waste @ 0 kg/day el@ 50

d utility purpisting projec

will be sourc

ven in the W

quirement (Ko After Pha40

200026

micals  

ed expansio

er proposedDiesel will

Source

Madhya GuCompany L(MGVCL.) Local Suppl

pose, whichct is 4.6KLDced from in

Water Balan

KLD) ase I Aft

2.5 1.5

3.1 NIL

20.4 1.5

25.0 29.0

22

n it will be -

d expansionbe used as

ujarat Vij td

liers.

h is sourcedD which wilhouse bore

nce Data in

ter Phase II2.82.0

5.0NIL

25.22.0032.237.0

-

n s

d l

e

n

Page 24: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.6.5 The totproject The maSkilled Table 3

Phase

ExistinDuring

Phase During

Phase During

3.7

3.7.1 The cat Table 3

S.No.

1. 2. 3. 4. 5. 6. 7. 8.

 

t Prefeasib

Proposed ex

MAN-POW

tal number additional 2an-power reas well as u

3.6: Man Po

of project

ng operations

I operations

II operations

QUANTITY

WASTE WA

tegory wise

3.7:Categor

Particu

Domes Indust Proces Cooling Boiler ( Washin Sub-To Grand

bility Repo

xpansion pro

WER REQUI

of man po20 persons equired forunskilled lab

ower Requ

Type Labou

ManaSkilledUn-sk

ManaSkilledUn-sk

ManaSkilledUn-sk

Y OF WAS

ATER GEN

bifurcation

ry-wise Wa

ulars

stic trial ss water g (Blow down(Blow down) ng otal: IndustrTotal

ort

oject for man

IREMENT

ower for exwill be requ

r the projecbour will be

irement

of ur

gerial d killed

gerial d killed

gerial d killed

STE TO B

NERATION

of the wast

astewater G

n)

rial

nufacturing o

xisting projeuired. Hencect is/ will b employed

GeneralM

353

353

355

E GENERA

& MANAG

te water ge

Generation

Existing S

of Synthetic O

ect is 35 pe the total me employedfor the proje

No.1st S

ATED

EMENT

neration is

(in KL/D)

WasteScenario

1.2

0.20.20.2NIL0.61.8

Organic Che

persons, forman-power d locally froect.

. of workersShift

M

...35

...67

...68

given in Ta

e Water GeneAfter Pha

micals  

r proposedwill be 55 om the nea

s 2nd Shift

M

... 3 5

... 6 7

... 6 8

ble 3.7.

eration ase I Aft

2.0

3.1 2.4 NIL 1.5 7.0 9.0

23

expansion

arby areas

3rd ShiftM

...35

...67

...68

ter Phase II2.2

5.03.0NIL2.0

10.012.2

n

.

Page 25: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

Fig-3.4

Fig-3.4

t Prefeasib

Proposed ex

(a): Water

(b): Water

bility Repo

xpansion pro

r Balance D

Balance D

ort

oject for man

Diagram (in

iagram (in

nufacturing o

n KLD) for E

KLD) for P

of Synthetic O

Existing Sc

Phase - I

Organic Che

cenario 

micals   24

Page 26: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

Fig-3.4

3.7.2 The ten Table 3

Sr. No.

1. 2. 3. 4. 5. 6.

 

3.7.3 In existand thegardeni

After prsystemmainten

t Prefeasib

Proposed ex

(c): Water

WASTE WA

ntative wast

3.8: Charac

. pH SuspeChemiBiocheOil & GTotal D

WASTE WA

ting operatioe industrial ing.

roposed ex. For the nance and m

bility Repo

xpansion pro

Balance D

ATER CHA

ewater cha

cteristics o

Parameter

nded Solids cal Oxygen D

emical OxygeGrease Dissolved So

ATER TRE

ons, the doeffluent is

xpansion theindustrial

modification

ort

oject for man

iagram (in

ARACTERIS

racteristic o

f Wastewa

r

(SS) Demand (COen Demand (

olids (TDS)

EATMENT &

omestic effluprovided p

e domestic effluent f

ns will be m

nufacturing o

KLD) for P

STICS

of effluent is

ter

OD) (BOD)

& DISPOSA

uent is dispprimary trea

effluent wifrom the pade in the e

of Synthetic O

Phase – II

s given belo

Untre

AL

posed throuatment and

ill be disposproposed pexisting ETP

Organic Che

ow in Table

Charaeated Efflue

6.0-8200-40

800-100250-30

<140000-5000

ugh septic td the treate

sed throughproduction P.

micals  

No. 3.8.

acteristics ent Treat8.5 00 00 00 10 00

tank/ soaksed effluent

h septic tanactivities,

25

ed Effluent6-8

<100<250<100<10

<2100

s pit systemis used for

nk/ soak pitnecessary

m r

t y

Page 27: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

The efflcollectio

After nebottom the primand theevapora The salTSDF s ETP Sc Fig-3.5

Fig-3.5

 

t Prefeasib

Proposed ex

luent cominon cum neu

eutralizationof the prim

mary settlinge effluent fration unit.

ts/ residue site.

cheme:

(a): Existin

(b): Propo

bility Repo

xpansion pro

ng from the utralization t

n, the effluemary settlingg tank will brom this ta

from evapo

ng ETP flow

osed ETP fl

ort

oject for man

process, wtank and ne

ent will be pg tank will bbe passed tnk will eith

oration unit

w diagram

low diagram

 

nufacturing o

washing andeutralization

pumped out be diverted through mixer be sent

along with E

m

of Synthetic O

d cooling town will be car

to the priminto the slu

x bed filter ato CETP o

ETP primar

Organic Che

wer blow doried out.

mary settlingudge dryingand diverteof EICL or

ry sludge w

micals  

own will div

g tank; sludgg bed. The d into the hwill be eva

ill be dispos

26

erted to the

ge from theoverflow of

holding tankaporated in

sed through

e

e f k n

h

Page 28: PROJECT PRE-FEASIBILITY REPORTenvironmentclearance.nic.in/writereaddata/Online/TOR/0_0_03_Jul... · PROJECT PRE-FEASIBILITY REPORT ... separator will b PCD. ill be used as no process

Project

Project: 

3.7.4  

3.7.4.1 There is

3.7.4.2 In existboiler. CFor proof 6 lakAdditioncase ofemissio Table 3

Partic

ExistinNon IB

PropoThermheaterone of k.cal/hof 10 lakcal/hrD.G. SKVA (S

PropoThermheaterone of k.cal/hof 10 lakcal/hrD.G. SKVA (S

3.7.4.3 Minor qemissio

t Prefeasib

Proposed ex

AIR EMISS

Process

s/will be no

2 Utility Em

ting scenarCyclone sepposed expa

kh k.cal/hrs&nally a D.Gf power faons and con

3.9: Details

ulars

ng scenarioBR boiler.

osed Scenarmic fluid r 2 No.- 6 lakh rs and one akh rs.

Set 125 Stand by)

osed Scenarmic fluid r 2 No.- 6 lakh rs and one akh rs.

Set 125 Stand by)

3 Fugitive

quantity of ons are also

bility Repo

xpansion pro

SIONS & CO

Emission

process em

mission

io, the comparator is pansion IBR &10 lakh k.c. Set of 12

ailure and Dntrol measu

of Utility E

Fuel

o Agro waste

rio for PhaseAgro waste

Diesel

rio for PhaseAgro waste

Diesel

Emission

fugitive emo likely to oc

ort

oject for man

ONTROL

n

missions fro

mpany has orovided as aboiler will bcal/hrs. Agr5 KVA will

Diesel will ures are men

Emission

Fuel

e 500 K

e I e 8000

50 LP

e II e 8000

50 LP

missions wilccur from st

nufacturing o

omthe manu

one non IBair pollution

be replaced ro waste wilbe installedsed as fuelntioned in th

Quantity

Kg/day

0 Kg/day

PH

0 Kg/day

PH

l occur durtorage area

of Synthetic O

ufacturing a

BR boiler. An control me by two thel be used ad as standbl in the D.Ghe below ta

ring handlin.

Organic Che

ctivities.

Agro waste easure with rmic fluid h

as fuel in theby unit and

G. Set. The dable no. 3.9.

APCD

Cyclone separator

Cyclone separator

Cyclone separator

ng of the ra

micals  

is used asthe boiler. eaters havie thermic fluwill be util

details rega.

EmissNorms

PM<15SO2< 1NOx<

PM<15SO2< 1NOx<

PM<15SO2< 1NOx<

PM<15SO2< 1NOx<

PM<15SO2< 1NOx<

aw materia

27

s fuel in the

ng capacityuid heatersized only inarding utility

sion s

50 mg/Nm3 100 ppm 50 ppm

50 mg/Nm3 100 ppm 50 ppm

50 mg/Nm3 100 ppm 50 ppm

50 mg/Nm3 100 ppm 50 ppm

50 mg/Nm3 100 ppm 50 ppm

als. Fugitive

e

y . n y

e

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Project

Project: 

Followin

• •

• • •

3.7.5 Hazardused oiof the h

Table 3

Type o& CateETP W(Cat. 3

Distillatresidue(Cat.36

Spent c(Cat 35

In orgaproces(Cat. 2

Used O(Cat. 5

DiscardContainbags (Cat. 3

Spent s(Cat. 2

t Prefeasib

Proposed ex

ng measure

Raw Materunder goodRaw MaterThe fugitiveand handlinRegular moHazardous Good hous

HAZARDO

ous wastesl Company

hazardous w

3.10: Detail

of waste egory

S

Waste 4.3)

E

tion e 6.4)

P

carbon 5.3)

P

anic s waste 8.1)

P

Oil .1)

M

ded ners/

3.3)

Rs

solvent 0.2)

P

bility Repo

xpansion pro

es will be pr

rials & Prodd storage coials & Produe emissionsng. onitoring is/w chemicals ekeeping w

OUS/NON-H

s generatedhas provide

waste and it

s of Hazard

Source

ETP

Process

Process

Process

Maintenance

Raw materiastorage

Process

ort

oject for man

racticed to r

ducts are/wonditions to ucts are/wils in terms

will be doneare/will be

will be maint

HAZARDOU

is in the foed adequatts managem

dous Wast

Existing

0.04 MT/Mont

3.36 MT/

0.05 MT/Mont

....

e 1.2 KL/Y

l 120 Nos/Mon

....

nufacturing o

reduce the f

will be storeprevent anl be stored of handling

e of piping astored as ptained in the

US WASTE

orm of ETP te storage ament is give

te Generati

After

th 5.5 MT/M

/Yr 80 MT

th 0.1 MT/M

97 MT

r 2.0 KL

nth 9870

210 M

of Synthetic O

fugitive emi

ed in propey volatilitiesin closed co

g losses wi

and fittings per standarde plant.

MANAGEM

waste, Distarea for propn in below t

ion & Dispo

Phase l A

Month 8 M

T/Yr 12

Month 0 M

T/Yr 15

L/Yr 2

Nos./Yr 15

MT/Yr 32

Organic Che

issions:

erly designas ontainers ll get reduc

for checkind criteria.

MENT

tillation residper storagetable 3.10

osal

After Phase l

.5 MT/Month

25 MT/Yr

.1 MT/Month

55 MT/Yr

.5 KL/Yr

5210 Nos./Y

25MT/Yr

micals  

ated storag

ced by prop

g of any lea

due, spent of wastes.

ll Dispos

Collectiotransportdisposal site. Collectiotransportand disincineratNECL/GCollectiotransportand disincineratCollectiotransportdisposal site. Collectiotransportdisposal to regisrefiners.

Yr Collectiotransportdisposal to regisrefiners. Spent sto the ac

28

e area and

per storage

akages.

carbon andThe details

al Method

on, storage, tation and

to TSDF

on, storage, tation sposal by tion at EPIL.

on, storage, tation sposal by tion on, storage, tation and

to TSDF

on, storage, tation,

by selling stered re-

on, storage, tation,

by selling stered re-

solvent sell ctual users.

d

e

d s

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Project

Project: 

3.7.6 There icomprewithin pgenerat

The co

3.7.7 The foll

• Theperi

• Theburnburn

• Gogare

• Thethe

• The• Fire• Eme• Fire• Wor 3.7.8 E The compollutioenvironresponsresponslegislati

t Prefeasib

Proposed ex

NOISE AN

is/will be nessors, TFHplant. The etor. No offe

ontrol measuEar Plugs aAnti vibratioAcoustic EnRegular ma

HEALTH A

owing key s

e industry isiodical med

e industry hnol, dettol, ns, eye injuggles, Glovprovided to

e industry isindustry.

e industry hae buckets arergency ala

e extinguishrk place mo

ENVIRONM

mpany has n control ement in acsibilities of sible for maive requirem

bility Repo

xpansion pro

D ODOUR

no major acH & pumpsequipments nsive odour

ures to be tand Ear muon pads andnclosure to aintenance

AND SAFET

safety meas

s responsibical examinhas providetincture iodries and ees, Gum b

o the workers taking all

as providedre provided arm will be iers will be i

onitoring wil

MENTAL HE

an environequipment,

ccordance wregulating

aintaining thment.

ort

oject for man

CONTROL

ctivities due. However,resulting in

r is/will be g

aken for redffs are provd flexible beD.G. Set w& lubricatio

TY MEASU

sures shall

ble for healnation of its ed first aiddine, eyes aelectrical shooots, Helmrs. precautiona

d good lightito withstannstalled forinstalled whl be done o

EALTH & S

ment cell in emissionswith the mothe safety

he records o

nufacturing o

L

e to which Noise leve

n noise gengenerated fr

duction in nvided to the ellows is pro

will be providon shall be d

RES

be impleme

lth and safeemployees box conta

and eardropocks.

mets, Skin C

ary measur

ing and vennd the fire orr the commuherever necon regular b

SAFETY CE

n order to kes from theonitoring pr

measures of all data,

of Synthetic O

noise wouel generatio

neration is/wrom the pro

noise levels workers in

ovided wheded. done.

ented in the

ety of the w and the he

aining cottops. This is t

Cream, Ear

res to contr

ntilation arrar explosion unication focessary. asis.

ELL

eep a closee sources rogram. Th

inside thedocuments

Organic Che

uld be genon would bwill be Air cocess.

are as beloUtility Sectrever applic

e proposed

workers. Thealth recordon, bandagto cure the

plugs, Face

rol the haza

angements. condition.r the emerg

e watch on tand the q

he cell is ae plant cam and inform

micals  

nerated othbe limited tocompressor

ow: tion. cable.

project:

he industrys are mainte, soframyinjuries fro

e Masks, a

ardous asso

gency condi

the performquality of slso entruste

mpus. The mation in line

29

er than Airo 80 dB(A)and Diese

y is doing atained. cine tubesm chemica

and clothing

ociated with

ition.

mance of thesurroundinged with thecell is alsoe within the

r ) l

a

, l

g

h

e g e o e

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Project

Project: 

3.7.9 P The comnot posrecogni

Table 3

Compo

Drinkin

Waste

Air-amb

Stack m

Noise m

t Prefeasib

Proposed ex

POST PRO

mpany hasssible to ezed/approv

3.11: Post P

onents

ng water

water

bient

monitoring

monitoring

bility Repo

xpansion pro

OJECT MON

developedestablish sved agencie

Project Mo

Param

IS-105

BOD,

SPM,

SPM, dB (A)

ort

oject for man

NITORING

d in-house fsuch facilities. The prop

nitoring Pl

meters

500:1991

COD, pH, TS

SOx, NOx. V

SO2, NOx

)

nufacturing o

PLAN

facilities for es, the sa

posed post-

an

SS, TDS

VOC

of Synthetic O

r monitoringame will b-project mon

Frequencyhouse mon

--

Daily (At all ETP) --

--

--

Organic Che

g certain cobe done bynitoring plan

of in nitoring

stages of

micals  

omponents. y appointinn is given b

Frequency party monit

Once in a m

Once in a m(treated andQuarterly

Quarterly

Once in a m

30

Where it isng externaelow:

of third toring

month

month d untreated)

month

s l

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Project

Project: 

CHAPT

SITE 4.1 C The IndVadodais very availab

4.2 L 4.2.1 L The pro 4.2.2 L It is a outside

4.2.3 L The plo 4.3 The topeasternresidenmodernRoad. TeasternVilas Pafortified

t Prefeasib

Proposed ex

TER – 4

E ANAL

CONNECT

dustry is locara. This pro

well connele nearby th

LAND FOR

LAND FORM

oposed expa

LAND USE

non-agriculnotified ind

LAND OWN

ot is owned

TOPOGRA

pography ofn regions. Ttial comple

n buildings. The eastern

n region alsalace and t city of Vad

bility Repo

xpansion pro

LYSIS

TIVITY

cated at Plooposed expected by nhe project s

RM, LAND

M

ansion is to

PATTERN

tural land adustrial area

NERSHIP

by the com

APHY

f VadodaraThe westernexes, railwa

The businn region hoo contains he General

dodara.

ort

oject for man

ot No. 1088/pansion pronational higite.

D USE & LA

o be carried

and develoa.

pany. Land

a is divided n region of tay station,

ness districtouses bazasome of th Post Office

nufacturing o

/B, Lamdapoject will be hway and

AND OWN

out in the e

ped industr

ownership

into two dithe city pos

shopping t centers aars, various

he landmarke. The easte

of Synthetic O

pura road, Vaccommodrailway. Ef

NERSHIP

existing indu

rial facility

document

istinct regiossesses a n

malls, muat Alkapuri, s shrines aks such as ern bank of

Organic Che

Village: Mandated in thefficient tran

ustrial facilit

at existing

is attached

ons, viz. wenumber of eultiplexes, b

Old Padraand various

Nyay Mandf river Vishv

micals  

njusar, Ta: e existing sinsport facili

ty.

industrial u

as Annexu

estern regioeducational business da Road and

shanty buidir, Mandvivamitri also

31

Savli, Dist.te. The siteties will be

unit located

ure-2.

ons and theinstitutionsistricts andd R C Duttildings. The and Laxmhouses the

: e e

d

e ,

d t e i

e

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Project

Project: 

4.4 The sal Table 4 ParticuCo-ordVillage Taluka/DistrictNearesNearesNeares

Neares

State/ NProtectCRZ apSeismiNote: A

4.5 E The ploinfrastru 4.6 C The clithroughdivided summeSeptem

The TaIMD, Va

t Prefeasib

Proposed ex

SALIENT

ient feature

4.1: Salient

ulars inates

/ Tehsil t st Water bodst Highway st Railway sta

st Airport/ Air

National bordted Area/ Sapplicability city

All the above

EXISTING

ot is locateducture is de

CLIMATE

mate is chhout the yea

into four ser season mber. The po

able 4.2 indadodara pu

bility Repo

xpansion pro

FEATURE

es of the pro

t Features o

y

ation & Railw

rbase

ders anctuaries

e mentioned d

INFRAST

d in villageeveloped by

& METER

haracterizedar, heavy sseasons. Tfrom Marcost-monsoo

icates the blished by I

ort

oject for man

ES

oject site are

of the Proje

way line

distances are

TRUCTURE

e: Manjusary the compa

ROLOGY

d by oppresouth–west The cold seh to May.

on season c

summary oIMD.

nufacturing o

e given in th

ect Site

DetailsCenter: ManjusaSavli VadodaMahi RiState hiSamlayaVadodaVadodaAhmedaNone wNo No Seismic

e the aerial d

E

r outside noany itself.

essive summonsoon

eason from The south

constitutes t

of meteorolo

of Synthetic O

he table be

22°28'02.92ar

ara ver≈ 9.37 kmghway ≈ 1.1a railway sta

ara Railway Sara Airport ≈ abad Airport

within 10 kms

c Zone – III (distance from

otified indus

mmer damprainfall and Decemberh-west mothe months

ogical patte

Organic Che

low:

2"N, 73°12'22

m (NW) 6 km (W)

ation ≈ 10.10 Station ≈ 17.915.34 km (SS≈ 89.00 km

(Moderate) m the project

strial area.

pness in thd a mild winr to Februansoon seaof October

ern at the n

micals  

2.43"E

(ENE) 92 km SSW SE) (NW)

site.

The entire

he atmosphnter. The yary is followason is fro

and Novem

nearest obs

32

e necessary

here nearlyyear can bewed by them June to

mber.

servatory of

y

y e e o

f

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Project

Project: 

Table 4

LocationAerial DHeight oMonth

JanuaryFebruaryMarch April May June July August SeptembOctober NovembDecembSeasonaPeriod

SummerWinter MonsoonPost monsoonAnnual Tor MeanNote: Wmonsoon

(Source: B

4.6.1. The sumdecreasdecreasrain to twith thetemperatempera

t Prefeasib

Proposed ex

4.2: Summa

n: At the PhysicDist from Projeof installation:

Tem

Maxy 30.3y 33.0

37.140.240.937.132.731.5

ber 33.2 36.0er 34.3er 31.4al Average Val

Tem

AvgMax

r 39.4031.56

n 33.62

n 35.15Total

n 34.80

Winter: Decemben: October & NoBook “Climatolog

TEMPERA

mmer seasoses during ses during tthe area. Te mean daature recordature as 30

bility Repo

xpansion pro

ary of Mete

cs Department,ct Site: Approx 34 m above Mmperature

(oC)

x. Min. 3 12.0 0 13.8 1 18.4 2 22.9 9 26.5 1 27.0 7 25.7 5 25.0 2 24.3 0 21.3 3 16.7 4 13.4 lues mperature

(oC)

g. x.

Avg. Min.

0 22.60 56 13.06 62 25.50 8

5 19.00 60 20.60 7

er, January & Fovember gical tables of O

ATURE

on from Mamonsoons

the winter. The winter maily maximded at 12.0.3oC and m

ort

oject for man

eorological

MS Universityx.16 Km SSW SL,

RelativeHumidity

(%Mor. Eve

67 3361 2553 2053 2064 2776 5188 7290 7486 6372 4464 4170 40

Relative Humidity

(%) Avg. Mor.

Avg. Eve.

56.66 22.33 66.00 32.66 85.00 65.00

68.00 42.50 70.00 43.00

ebruary, Summ

Observatories in

arch to May, increasesThe south-

months are um temper0oC. Janua

mean daily m

nufacturing o

l Data at ne

, Vadodara Guj

e y )

Cloud Co(Okt

e. Mor. E3 1.1 5 0.9 0 1.1 0 1.1 7 1.7 1 4.5 2 6.5 4 6.7 3 4.3 4 1.5 1 1.3 0 1.3

Cloud Cove

(Oktas

Avg. Mor.

Avg

Eve1.30 1.01.10 1.15.50 5.0

1.40 1.32.70 2.5

mer: March, Apr

n India (1951 - 1

y is a one os slightly du-west monsgenerally p

rature recory is the co

minimum tem

of Synthetic O

earest IMD

jarat ( Lat: N 22

over tas)

MeanS

(kEve.

1.1 0.9 1.2 1.2 0.7 3.4 6.4 6.5 4.0 1.4 1.3 1.3

er s)

Mean WSpe

(mg.

e. 3 50 37 7

5 30 5

ril & May, Mons

1980)” published

f continuouuring the poon from Jpleasant. Morded at 40oldest montmperature o

Organic Che

Station –V

2o18’, Long: E 7

n Wind Speed km/Hr)

PreWind

4.0 4.1 4.2 4.8 8.7

10.3 8.4 7.1 5.1 3.0 3.0 3.6

ind eed

m/s)

Avg. PDDirecti

5.90 NW,S3.90 7.72 S

3.00 CA

5.50 S

soon: June, July

d by IMD)

s increase post-monsoune to Sep

May is gener0.9oC and th with the observed as

micals  

Vadodara

73o15’)

e-dominant d Direction

R

NE CALM CALM

NW SW SW SW SW SW

CALM CALM

NE

DW ion

Total R

SW NE SW

ALM

SW

y, August & Sep

in temperaon season tember brinrally the homean dailymean daily

s 12.0oC.

33

Rainfall (mm)

1.2 0.6 2.2 0.9 4.4

146.8 297.6 284.7 141.7 22.0 16.2 4.4

Rainfall (mm)

2.50 2.06

217.70

19.10 922.70

ptember, Post

tures whichand again

ngs copiousottest monthy minimumy maximum

h n s h m m

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Project

Project: 

4.6.2. The climcoastlingeneralfor restaround

4.6.3. During Cloud cmostly c

4.6.4. About 9June toobserve

4.6.5. The anand moseason season slightly

4.7 S The infr

4.7.1 E As per are give

t Prefeasib

Proposed ex

HUMIDITY

mate of thene. Humiditylly exceedint of the yea20-70%.

CLOUD CO

the South-cover decreclear.

RAINFALL

95% of the o Septembeed from the

WIND PAT

nual resultaonsoon, the experience experiencemoderate d

SOCIAL IN

rastructure

EDUCATIO

census 200en below.

bility Repo

xpansion pro

e region is y is usuallyng 85%. Huar i.e. the p

OVER

-west monseases durin

L

annual raier, July bedata is 922

TTERN

ant vector fe winds bloe a changee calm windduring winte

NFRASTR

available in

ONAL FACI

01, Out of 1

ort

oject for man

characterizy high durinumidity decperiod of De

soon monthg the post

nfall is receing the mo

2.70 mm.

for wind dirow mostly fe in directiods. The winer and post

RUCTURE

n the study a

LITIES

136 villages

nufacturing o

zed by a hg the monsreases gradecember to

hs, the skiemonsoon m

eived durinonth with h

rection showfrom the sen, with the d speed is monsoon s

area denote

s, all villages

of Synthetic O

umid summsoon monthdually durin

o April, the

es are usuamonths. In t

ng the southhighest rain

ws winds bea i.e. the winds blowhigh during

seasons.

es the econ

s have edu

Organic Che

mer becaushs, with aveng the post-average re

ally heavilythe rest of

hwest monfall. The av

blowing fromNW or SW

wing from Ng monsoon

omic well-b

cational fac

micals  

se of the clerage relativ-monsoon m

elative humi

y clouded othe year th

soon seasoverage ann

m SW. DuriW direction. NE. The posand summe

being of the

cilities, deta

34

loseness tove humiditymonths andidity ranges

or overcasthe skies are

on i.e. fromnual rainfal

ng summerThe winter

st-monsooner seasons

region.

ails of which

o y d s

. e

m l

r r n ,

h

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Project

Project: 

Table 4

Sr.No 1. 2. 3. 4. 5.

(Source: P

4.7.2 As per c

Table 4

Sr.No.1 2 3 4 5 6 7

(Source: P 

t Prefeasib

Proposed ex

4.3: Details

ParticularPrimary SMiddle ScSecondarySenior SeCollege

Primary Census

MEDICAL

census 200

4.4: Details

ParticulaDispensaPrimary HPrimary HAllopathicAllopathicMaternity Communi

Primary Census

bility Repo

xpansion pro

of Educat

rs Schools chools y School

econdary Sch

s Abstract – Cen

FACILITIES

01, Details o

of Medica

rs ries Health CenteHealth sub cec Hospital c dispensary and Child wty Health Wo

s Abstract – Cen

ort

oject for man

ional facili

hool

nsus of India, 20

S

of medical f

al facilities

ers entre

welfare Centreorkers nsus of India, 20

nufacturing o

ties

001)

facilities ava

e

001)

of Synthetic O

ailable in the

Organic Che

Observed v

e study area

Observed v

micals  

values in Sa

a are given

values in Sa

35

avli Taluka131

02371

below.

avli Taluka57

4311

1111

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Project

Project: 

CHAPTPLA 5.1 The prolargest are/will reductiofacilitiesdisposa 5.2 As per of study Table 5

Sr. No1 2 3 4 5 6 7 8

(Source: P

5.3 A The tota 5.4 A This is land or So ther 5.5 A 5.5.1 D As per c

t Prefeasib

Proposed ex

TER – 5 ANNING

PLANNIN

oposed procity in the be sourced

on in transs like internal sites etc.

POPULAT

census 200y area withi

5.1: Distrib

o. PTNAMMFFS

Primary Census

AREA STA

al area of th

ASSESME

an expansbuilding is

re will be no

AMENITIE

DRINKING W

census 200

bility Repo

xpansion pro

G BRIE

G CONCE

oject is locaIndian Sta

d locally. RMportation cnal roads,

TION PRO

01, the avern Savli Talu

ution of po

Particulars Total PopulatNo. of HouseAvg. househoMale populatMale populatFemale popuFemale popuSex ratio s Abstract – Cen

ATEMENT

he plot is 36

NT OF INF

ion project required fo

o demand of

S/FACILIT

WATER FA

01 following

ort

oject for man

EF

EPT

ated at Maate of GujaM cost as most. The rewater supp

OJECTION

rage houseuka is prese

opulation

tion eholds old size (perstion tion (in %) ulation ulation (in %)

nsus of India, 20

694.48m2 ou

FRASTRU

which is toor the propof major cha

TIES

ACILITIES

drinking fa

nufacturing o

anjusar, Savarat, after Amany input segion is weply, arrange

hold size isented below

son)

)

001)

ut of which

CTURE D

o be develoosed projecnge in phys

cilities are a

of Synthetic O

vli. The neAhmedabadsuppliers aell planned ements for

s around 5 pw.

constructed

EMAND (P

oped in thect except fesical infrastr

available in

Organic Che

arest city id and Surat.re located nwith all th

r power, st

persons. Th

Observed

d area of the

PHYSICAL

existing prew installatioructure and

study regio

micals  

s Vadodara. Major rawnearby whice basic infreetlights, s

he demogra

values in Sa

e plant is 65

L & SOCIA

remises. Noons and mo social infra

on.

36

a- the thirdw materialsch will bringfrastructurasolid waste

aphic profile

avli Taluka23792946963

5.07125292

52.66112637

47.34899

50.44m2

AL)

o additionaodificationsastructure.

d s g l

e

e

l .

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Project

Project: 

Table 5

Sr. No1 2 3 4 5 6 7 8 9 10

(Source: P

 5.5.2 As per c 5.5.3 As per and tele Table 5

Sr. No1 2 3 4

(Source: P

 

5.5.4 T As per Taluka railway;is 100%

5.5.5 A As per foot pat

t Prefeasib

Proposed ex

5.2: Drinkin

o. ParticulaTap Well wateTank watTube weHand pumRiver waCanal Lakes Spring Other dri

Primary Census

POWER SU

census 200

COMMUNI

census 200ephone con

5.3: Commu

o. ParticulaPost OfficPost andTelephonCommerc

Primary Census

 

TRANSPOR

census 200and most

; railway line% electrificat

APPROAC

census 200th.

bility Repo

xpansion pro

ng Water Fa

ars

er ter ll water mp ter

nking water s Abstract – Cen

UPPLY FAC

01, all the vi

CATION&

01, Distributnnections in

unication &

ars ce telegraph of

ne connectiocial Bank

s Abstract – Cen

RT FACILIT

01, Bus serpreferable e is availabtion in the a

H TO VILLA

01, 109 villa

ort

oject for man

acilities

sources nsus of India, 20

CILITIES

llages have

BANKING

tion of facili the study a

& Banking

ffice n

nsus of India, 20

TIES

rvice is avamode of t

ble in 4 villagarea.

AGES

ages have p

nufacturing o

001)

e power sup

FACILITIES

ities such aarea are illu

Facilities

001)

ailable in allransport in ges. 136villa

paved road

of Synthetic O

pply facilities

S

as post officstrated in ta

the villagethe region

ages are co

d, 98 village

Organic Che

Observed v

s in the stud

ce, post & teable below.

Observed v

es of the stun. Second onnected w

es mud road

micals  

values in Sa

dy region.

elegraph of

values in Sa

udy region option for tith paved ro

d and 73 vi

37

vli Taluka 92936155

126403024

ffice, banks

avli Taluka937

7013

within Savltransport isoads. There

llages have

,

i s e

e

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Project

Project: 

CHAPT

PRO 6.1 The totThe tota 6.2 In the s 6.3 Maximuwill also 6.4 Existingproject 6.5 This proconnecthe proj

6.6 Drinking

6.7 Domestthroughafter ph

6.8 IndustriETP wiexplaine

t Prefeasib

Proposed ex

TER – 6

OPOSED

INDUSTR

al area of tal productio

RESIDEN

said proposa

GREENBE

um possibleo be consult

SOCIAL IN

g infrastructwhich is ve

CONNECT

oposed expted by natioject site.

DRINKING

g water is/w

SEWERAG

tic waste wh septic tanhase I and 2

INDUSTR

al effluent ill be will bed in Chapt

bility Repo

xpansion pro

D INFR

RIAL AREA

the plot is 3on capacity

TIAL ARE

al no Reside

ELT

e open landted for sele

NFRASTU

ture will beery low.

TIVITY

pansion projonal highwa

G WATER

will be sourc

GE SYSTE

water generank/Soak pit 2.2 KLD afte

RIAL WAST

generated e sent to Eter 03, Sect

ort

oject for man

RASTRU

A

3694.48 m2

will be 2580

EA

ential area

d is/will be action of spe

UCURE

e sufficient

ject will be ay and railw

MANAGE

ced from in

EM

ated from thsystem, wh

er phase II.

TE MANAG

after propoEICL/CETP tion 3.7.3 an

nufacturing o

UCTUR

2 out of whi0 MTA after

has been p

allotted for ecies for the

to accomm

accommodway. Efficien

EMENT

house bore

he existing hich is @ 1

GEMENT

osed projecor will be

nd 3.7.5.

of Synthetic O

RE

ich construcr proposed

proposed for

green belt e developme

modate the

ated in the nt transport

e well for the

and propos1.20KL/D fo

ct will be treevaporated

Organic Che

cted area oproject.

r workers a

developmeent of the g

existing loa

existing sitt facilities w

e proposed

sed projector existing p

eated in ETd in evapor

micals  

of the plant

nd/or for sta

ent. If requirgreenbelt.

ad from the

te. The site will be availa

project.

is/will be dplant and @

TP, treated ration unit.

38

is 1500m2

aff.

red, experts

e proposed

is very welable nearby

disposed off@ 2.0 KL/D

water fromDetails are

.

s

d

l y

f D

m e

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Project

Project: 

6.9 Solid wand disarea for Table 6

Type owaste CategoETP W(Cat. 3

Distillatresidue(Cat.36

Spent c(Cat 35

In orgaproces(Cat. 2

Used O(Cat. 5

Discardcontainbags (Cat. 3

Spent s(Cat. 2

6.10 Total po250KVA

t Prefeasib

Proposed ex

SOLID WA

astes genecarded conr proper sto

6.1: Solid w

of & ory

So

Waste 4.3)

ET

tion e 6.4)

Pr

carbon 5.3)

Pr

anic s waste 8.1)

Pr

Oil .1)

M

ded ners/

3.3)

Rst

solvent 0.2)

Pr

POWER R

ower requireA, sourced f

bility Repo

xpansion pro

ASTE MAN

rated are intainers from

orage of was

waste gene

ource

TP

rocess

rocess

rocess

Maintenance

aw material torage

rocess

REQUIREM

ement for efrom Madhy

ort

oject for man

NAGEMEN

n the form om storage ostes. Details

ration and

Existing

0.04 MT/Month

3.36 MT/Y

0.05 MT/Month

....

1.2 KL/Yr

120 Nos/Mont

....

MENT & S

existing projya Gujarat V

nufacturing o

NT

of ETP wastf raw maters of solid w

disposal

After P

h 5.5 MT/

Yr 80 MT/Y

h 0.1 MT/Mo

97 MT/Y

2.0 KL/Y

h 9870 No

210 MT

OURCE O

ect is 125 KVij Compan

of Synthetic O

te, spent carials. Compaste genera

Phase l Af

/Month 8.5

Yr 12

nth 0.1 M

Yr 15

Yr 2.5

os/Yr 15

T/Yr 32

OF SUPPLY

KVA and aftny Ltd. (MGV

Organic Che

arbon, Distilany will proation are giv

fter Phase l

5 MT/Month

5 MT/Yr

1 T/Month

5 MT/Yr

5 KL/Yr

210Nos/Yr

5 MT/Yr

Y

ter proposeVCL)

micals  

lation residovide adequven in table

l Dispos

Collectiotransportdisposal site. Collectiotransportand disincineratNECL/GCollectiotransportand disincineratCollectiotransportdisposal site. Collectiotransportdisposal to regisrefiners. Collectiotransportdisposal to regisrefiners. Spent sto the ac

ed expansio

39

ue, used oiuate storagee 6.1.

al Method

on, storage, tation and

to TSDF

on, storage, tation sposal by tion at EPIL.

on, storage, tation sposal by tion on, storage, tation and

to TSDF

on, storage, tation,

by selling stered re-

on, storage, tation,

by selling stered re-

solvent sell ctual users.

on it will be -

l e

-

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Project

Project: 

CHAPT

REH 7.1 The proany postudies

t Prefeasib

Proposed ex

TER – 7

HABILI

POLICY T

oposed proopulation is

or R&R act

bility Repo

xpansion pro

ITATIO

TO BE ADO

oject is to bproposed

tion study h

ort

oject for man

ON &RE

OPTED

be developefor the pr

has not bee

nufacturing o

ESETT

ed in the exroject. Thern proposed

of Synthetic O

TLEME

xisting premrefore, deta.

Organic Che

NT (R

mises.Hencailed Socia

micals  

&R) PL

ce, no displal Impact A

40

LAN

acement ofAssessment

f t

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Project

Project: 

CHAPT

PRO 8.1 At presgetting 8.2 The comissues Green bwill be a Table 8

Sr. No.

1. 2. 3. 4 5.

6. 7. 8.

Table 8

Sr. No.

1.

2. 3. 4. 5. 6.

t Prefeasib

Proposed ex

TER – 8

OJECT

TIME SCH

sent we areall the statu

ESTIMAT

mpany hasand Envirobelt develoapproximate

8.1: Total C

. Purpose

Land Building Plant & MElectrificEnvironmETP Air polluSafety inChartereGreen bTOTAL

8.2: Recurr

. Purpos

EnvironAPCD eAir polluFees forEnv. Mo

Safety in Environ Green b Medical TOTAL

bility Repo

xpansion pro

SCHED

HEDULE O

e not propoutory permis

ED PROJE

made budonment Protpment is alely Rs. 668

Capital Cos

e

Machinery cation and Adment Protect

tion control dnstruments ed services/ elt developm

ring cost pr

e

ment Protectetc.) ution control r Common donitoring expnstruments mment & safet

belt maintena surveillance

ort

oject for man

DULE &

OF THE PR

osing any assion from r

ECT COST

dgetary provtection has lso conside.25 Lakhs.

st Projectio

dministrativetion (includin

device

Governmentment

rovision fo

tion (includin

device isposal facilienses

maintenancety training ance e

nufacturing o

& COST

ROJECT

additional prespective a

T

vision for thalso been

ered. The e

on

e set-up g ETP, APC

t fees

or EHS

ng ETP,

ties

e

of Synthetic O

T ESTI

production aauthorities.

he recurringconsidered

estimated pr

CaExisting

120.0080.00

300.005.00

CD etc.) 5.001.000.500.500.25

512.25

RecExisting

5.00

0.501.000.500.250.250.250.508.25

Organic Che

IMATE

at the site.

g expensesd in planninroject cost

apital Cost g Prop

addit000 10

000055 1

curring Costg Prop

addit0

00055505

micals  

ES

It will star

for the envng the costafter propo

(Rs. in Lakhposed tional

0.00 20.00 00.00 10.00

20.00 3.00 1.00 1.00 1.00

56.00

t per annumposed tional 10.00

1.00 10.00

1.50 1.00 1.00 0.50 1.00

26.00

41

rt only after

vironmentat projectionosed project

hs) Total

120.00100.00400.0015.00

10.004.001.501.501.25

668.25

(in Lakhs)Total

15.00

1.5011.002.001.251.250.751.50

34.25

r

l . t

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Project

Project: 

CHAPT

ANA 9.1 M/s. UnVadodaCare InUniverscompan

Finally contribu

For thebenefit

 

t Prefeasib

Proposed ex

TER – 9

ALYSIS

FINANCIA

niversal Esara. Currentngredients isal has builny focuses o

in the daysuted to the e

proposed as Corpora

bility Repo

xpansion pro

S OF PR

AL & SOCI

sters Ltd. tly Universan India. Wit its reputaon providing

s of acute Dearning of F

project, theate Social R

ort

oject for man

ROPOS

IAL BENE

is located al Esters haith stringention as a pg quality pro

Deficit of FForeign Exc

e company Responsibilit

nufacturing o

SAL

EFITS

at Plot Nos become o

nt quality stapreferred suoducts to th

oreign Excchange in H

intends to ty.

of Synthetic O

. 1088/B, Vone of the leandards an

upplier to cohe Personal

hange in oHard Curren

donate 2%

Organic Che

Village: Maneading mannd good maompanies al Care indus

ur Country,cy.

% of the cap

micals  

njusar, Ta: nufacturers anufacturingall over the stry.

, Universal

pital cost fo

42

Savli, Distof Personag practicesworld. The

Esters has

or the socia

: l ,

e

s

l

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Annexure – 1: Existing CC&A  

 

 

 

A1

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A2

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A3

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A4

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A5

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Annexure – 2: Land Ownership Document  

 

A6

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A7

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A8

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A9

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A10

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A11

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A12

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A13

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A14

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A15

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A16