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ANNEXURE – 1
Satellite image of the Project site showing 10 KM radial area
ANNEXURE – 1
Satellite image of the Project site showing Short View
Annexure-2
PLAN LAYOUT
Annexure – 3
SR.NO.
NAME OF PRODUCTQUANTITY (MT/Month) Category as
per EIAnotification
2006.Existing Proposed
Total afterExpansion
1 Bi Axial Oriented polyester Film 4000 4000 80005(d) Manmade
fibresmanufacturing
2**Polyester chips
(different grades)--- 31000 31000
5(f) syntheticOrganic
3**Mettalized & lacquered Polyester
Film800 2200 3000
5(f) syntheticOrganic
4 Power Plant --- 20 MW 20 MW1(d) thermalpower plan
5 Metalized Polyester Film 2050 NIL 2050 Not required EC
6*Mettealized Laminated Polyester
Film800 --- Removed ---
7*Mettalized & Lacquered Laminated
Polyester Film800 --- Removed ---
8* Mettalic Yarn 400 --- Removed ---
9* M.F. Resin 350 --- Removed ---
10* Epoxy Resin 350 --- Removed ---
11* Lacquers 1000 --- Removed ---
12* Plastic Bobbins (Reels) 90 --- Removed ----
By products
1. Polymer lumps NIL 100 100 ---
2. Tetra Hydro furan(THF) NIL 250 250 ---
3. Fly Ash Bricks NIL 900 900 ---
Note:-1) *product number 6 to 12 will be removed after proposed expansion.2) **Our project is located at outside Notified Industrial Area and our proposed waterconsumption will be more than 25 KL/day and fuel consumption will be more than 25TPD. Therefore, as per EIA notification 2006, and it’s amend we fall category A and wehave applied for EC to MoEF&CC.
(B) LIST OF RAW MATERIAL
SR.NO.
NAME OFPRODUCT
RAW MATERIAL
RAW MATERIAL CONSUMPTION
EXISTING PROPOSEDAFTER
EXPANSIONTOTAL
1.Polyester Chips
(DifferentGrades)
Purified Teteric Acid NIL26660
T/MONTH26660
T/MONTH
Mono Ethylene Glycol NIL10540
T/MONTH10540
T/MONTH
Iso Phthalic Acid NIL500
T/MONTH500 T/MONTH
Di-Ethlyene Glycol NIL150
T/MONTH150 T/MONTH
Butane Diol NIL1400
T/MONTH1400 T/MONTH
2. BOPET filmPolyester Bright Chips
4560T/MONTH
5863T/MONTH
10523T/MONTH
Polyester Mb Chips480
T/MONTH617
T/MONTH1097 T/MONTH
3. Metalized FilmAluminum
52T/MONTH
Nil 52 T/MONTH
Pet Film1998
T/MONTHNil 1998 T/MONTH
4.
Metalized &Lacquered
Polyester Film(Coated Film)
Metalized Poly Film600
T/MONTH1650
T/MONTH2250 T/MONTH
Resins132
T/MONTH363
T/MONTH495 T/MONTH
Dyes20
T/MONTH55 T/MONTH 75 T/MONTH
Solvent20
T/MONTH55 T/MONTH 75 T/MONTH
Chemical20
T/MONTH55 T/MONTH 75 T/MONTH
(1) BI-AXIAL ORIENTED POLYESTER FILM (BOPET):
1) Granules of PET Chips (Film Grade) and Silicon Chips shall be used as Raw Material.
2) Hopper Mixing Process: Granules of PET Chips shall be loaded in Hopper for mixing with
Silicon Chips to get the material fit and ready for melting and blending process.
3) Heating and Melting (Extrusion) Process: On in coming raw material from hopper
vessels, function of this plant starts and by the means heating and than melting process of
PET Chips (Film Grade) converted into Paste foam. This Process calls Mixing and blending.
On completion of this process chips converted in to uneven micron/gauae of films in thick
Paste foam.
4) M.D.O. Treatment: Outcome of above process i.e. uneven Polymer Paste without size,
gauge and micron in thick paste foam, put to heat treatment for regularization of size gauge
as well as micron.
5) T.D.O. Chilling: In this process the Polymer Paste produced from M.D.O. process,
proceeds for chilling process for shaping in proper size, gauge and in proper Micron in Film
Foam.
6) Winding Process: After setting size, gauge and micron in T.D.O. chilling process, prepared
film reach for winding where Rolls of films are prepared.
7) Slitting Process: The ready jumbo Roll of film entered for slitting process for selected and
required marketable size.
8) Recycling Process: In case inferior, damaged, wastage production, it can be recycled and
again this material can be loaded to Re-extrusion for Polymerizing process for heating and
melting for fresh production from wastage Batch.
NOTE: There is no any washing and regeneration of filter is required.
FLOW DIAGRAM OF MANUFACTURING PROCESS :
BI-AXIALLY ORIENTED POLYESTER FILM ( BOPET FILM ):
PET Chips& silicon Chips
Mixed Up
PET Chips (Film grade)
Heating &Melting.Chips converted into thick Paste
Foam
Heating to thick Paste Foam for
regularization size Gauge & Micron
Chilling to thick Paste Foam for
regularization size Gauge & Micron
Damaged & wastage production is
reuse back in the process
Ready BOPET Film wound up &
prepared in a Jumbo Roll Foam
Ready BOPET Film in Jumbo Foam
slitting & cutting in marketable
size & as per requirement
Re-cycle
(2) METALLISED FILM:
a) A Pet Film and Aluminum are basic raw material for manufacturing Metallized Polyester Film.
b) Initially, the aluminum layer is deposited on Pet Film in a high vacuum Chamber of the
vacuum metalliser. The vacuum metaliser has a series of vacuum pumps, which evacuate the
chambers of the metallising.
c) The chamber has unwinder / main chill roll / unwinder and aluminum evaporation system
comprising of evaporation at 1400Oc. The Polyester Film is passed on to the chill roll maintained
between a temperature of 15 OC to -15 OC and aluminum is deposited on the film. Above
temperature is maintained by Brain Solution internally.
d) The dazzling reflection effect of the metallic yarn is due to the aluminum layer on the
polyester film. Finally, the metallised film special product is wound on the rewinder.
Flow diagram of metalized film:
Pet film
Vacuum metalizer coating of
aluminum filmAluminum
Chiller (cooling)
Wounding
Packing & dispatch
(3) Metalized & Lacquered Polyester Film (Coated Film):
a) This is a process of lamination to the Metallised Poly. Film produced earlier to prevent the
Metallised Poly. Film from abrasion and oxidation during the yarn cutting / cloth processing.
b) In this process, simply the Metallised Poly. Film is either coated on both side by passing the
film through mixture of resin, solvent and chemical under normal temperature.
c) Finally, coated Metallised Poly. Film is passed through drier maintained at 180 Oc to obtain
laminated film which known as Metallised and Lacquered Polyester Film.
Metalized film
Coating& mixing
Resin
Solvent
Chemical
Drying
Packing &
dispatch
(4) POLYESTER CHIPS (DIFFERENT GRADES)
Manufacturing Process of Polyester Chips:-
We are going to manufacture Polyester Chips as per following process under Continuous
Process manufacturing.
PTA Slurry Making:-
Purified Terephthalic Acid (PTA) in power form charged in Hopper and conveyed to the plant
under 0.5 kg pressure to the slurry preparation reactor. Mono Ethylene Glycol (MEG) is charged
under the close condition to pump from MEG storage yard to PTA slurry making reactor. PTA
and MEG mixed in the PTA slurry reactor and transfer through mass flow meter to esterification
reaction.
Esterification Reaction:-
Under the continuous process from one side slurry of PTA received under gradual heating up to
250oC to start Polymerization reaction. The reacted mass is passed through etherification stage-
II having temperature of 250 to 260 o C and from Monometer during the process. During this
process water is generated as by product and transfer to effluent treatment plant for the
treatment.
During the esterification reaction, Antimony Trioxide is added as catalyst to accelerate the rate
of reaction.
Prepolymerization:-
During the continuous process, monometer mass from esterification stage is passed through
prepolymerization stage between 260 to 280oC and at the same time delustering agent as
Titanium dioxide (TiO2) is added in the reaction mass. Under this stage, mixture of Oligomer and
polymer are formed.
Polycondensation:-
Under continues process, Oligomer in molten form is filtered through S.S. Candle Filter and
received the mass for final condensation. The final polycondensation reaction is carried out
between 280 to 290oC and after achieving the desired viscosity, the molten polymer mass is
passed through cutter to form the required size of Polyester Chips.
Drying of the Chips:-
Preferred size of chips dried in dryer and passed through classifier and transfer to intermediate
storage vessel.
Storage & Dispatch:-
The manufactured chips are checked for various physic-chemical parameter and the approved
chips are stored in chips silo. Finally it is packed in jumbo bags and dispatch to the various
customers or it can dispatch in tanker load.
POLYESTER CHIPS (BOTTLE GRADES)
1. Feeding and Conveying System for Amorphous Chips:-
The raw chips (amorphous chips) are fed into the amorphous chips silo by feeding & conveying
system from feeding hopper. And then the atmosphere chips are been sent into the pre-bin
hopper of SSP system through the second conveying system from silo. The conveying process
from silo to pre-bin is automatic controlled by level sensor on pre-bin.
2. Pre-Crystallizing System:-
The added IPA in PET bottle grade chips results in the melting point decreasing and the
crystallization rate declining, the trend to stick (agglomeration) is increased when heating for
crystallizing. In the process of crystallization, amorphous chips are continuously fed into the
crystallizer by rotary valve and the hot gas entre into the pre-crystallizer from bottom. The hot air
move and heat chips to remove surface moisture make chips get crystallizing.
As special design, the amorphous chips are spread around and surrounded by air and
crystallized chips quickly when entering crystallizer. It is efficacious to prevent chips
agglomerate.
The hot air circulating in crystallizing system is controlled by the fan and heater, which ensure
the suitable quantity flow and temperature. The circulating airs also take away the fines /dust
which are removed in the dust cyclone.
A small quantity of circulating air must be discharged in case of big humidity. The discharged
gas is balanced by the complementing of fresh air.
System Characteristic:-
Jet fluid crystallizer, high quality to prevent agglomeration.
Without mechanical agitation, not produce dust.
Rapidly remove the water on surface of chips.
Efficiently remove the dust of chips.
3. Pre-Heating (annealer) System:-
System Description
Crystallized chips are fed into the pre-heater in which the chips are heated (annealing) to SSP
temperature by nitrogen. The crystallizing degree, molecule weight of PET chip from crystallizer
needs increase and annealing before polymerization in high tempuras. The molecular weight
increase and annealing before polymerization in high tempuras. The molecular weight increase
and AA decrease also continuously under protection of nitrogen purification system. The roof
structure can make the nitrogen evenly distribution and decrease chips contact pressure and
reduce the effect of gravity from chips. Preventing chips agglomeration.
The level sensor is installed on the top of reactor, which can control the level and adjust
capacity. When there is large fluctuation, it can alarm and control the operation of crystallization
to protect the equipment.
System Feature:-
Taken roof structure, lower pressure from gravity, long heating time, the chips can
contact with hot wind enough.
Without mechanical agitation, no pellet deformation
Chips flow uniformity
Multi area temperature control, easy process control
No need for equipment maintenance
4. Hot chips Conveying System:-
In order to lower the height of the building, we transfer the heated chips into the SSP react
tower by a hot state conveyor. The hot state conveying use hot nitrogen and the conveying is
controlled by the level sensor in the SSP reactor tower automatically.
System Feature:-
Hot nitrogen protection, no loss of temperature
Effect mixture in conveying
5. Solid State Poly-Condensation System:-
After being transported to the SSP reactor tower, the molecular weight of chip increase
continuously under the protection of purified nitrogen. The nitrogen from purifying system take
away moisture, hydrocarbon (like AA, glycol), oligomers and other by-product from reaction. The
gas velocity, temperature and flow quantity are keep as a good condition for product.
At lower area in tower, the low temperature nitrogen exchange heat with hot chips. It can cool
the chips to control speed of and stop reacting and save energy. SSP is a high temperature
reaction without oxygen and moisture and enough chips staying time must be ensured to get the
best reacting.
System Feature:-
Taken column reactor, save space and cost.
Low temperature nitrogen come from bottom of react tower, save energy.
Without mechanical agitation, no pellet deformation.
Chips flow uniformity.
No need for equipment maintenance.
6. Cooling System:-
The temperatures of product form SSP reactor is some high and required to rapid stop reacting.
Though the fluid bed cooling system to decrease temperature and SSP course. The molecular
weight become steady and can be storage or package. The cooling system uses atmosphere air
to reduce making cost. Rapid
System Feature:-
Taken fluid bed cooler, cooling quickly and evenly
Without mechanical agitation, no dust produce
Taking atmosphere air, reducing making cost.
Effectively remove the dust of chips.
7. Product Conveying System(With Buffer Production)
The chips after cooling are final product. The will be transport to storage silo for packing. The
system is the conveying to transport.
Some time some product are not as required (as beginning) but the SSP course is a long and
continuous course, we also need the transport system to transport the chips to faliur storage
silo.
Material balance
REG
:2
74.
87
TOET
PFINISHERREACTOR
MEG 58.89 KG
MEG 270 KG
1050.8
REG 115.28
REG 159.59
PREPOLYMENSER
REACTORS
PR
OC
ESS
CO
LOU
MN
PASTE PREPARATION
PTA: 860
ESTERIFIER REACTOR1463.76
H2O
:186.4
7A
UT
OD
EH
YD
RA
TE
,1
.49
CE
C22
5
H2O
,186.4
7A
CT
UA
LD
EH
YD
RA
TE
,
1.4
9
EC
,0.9
3
POLYMER1000 KG
ANNEXURE – 4
FACILITIES FOR STORAGE OF GOODS/MATERIAL
Sr.No.
Title Area (m2)
1. Finished product Area 10000
2. Raw material storage area 5000
3. Process Area 18000
4. Hazardous Waste Storage Area 1000
5. Office 500
6. Parking 4000
7. Open 14090
8. Boiler Area & Thermopack 15000
9. Green Belt 35000
10 Total Plot Area 102590
Annexure 5
Source: - Gujarat Water Infrastructure Ltd.
Water required for domestic and industrial purpose for proposed project activity will be procured from
Gujarat Water Infrastructure Ltd.
Water consumption and Waste water generation for the Existing and Proposed activity at the
different usages is as under:
WATER CONSUMPTION :-
Sr.No.
Category
Water Consumption (KL/day)
Existing
Due toremoval
ofexistingproducts
ProposedTotal AfterExpansion
1. Domestic 22 -- 21 43
2. Gardening NIL -- 50 50
A TOTAL 22 -- 71 93
Industrial
1. Process 1 -- 158 159
2. Boiler -- -- 120 120
3.Cooling Tower (Make-
up)*337 -- 226 563
4. Washing 0.1 -- 79.8 79.9
5. D.M. NIL -- 10.0 10.0
B TOTAL 338.1 -- 593.8 931.9
GRAND TOTAL (i + ii) 360.1 NIL 664.8 1024.9
WASTE WATER GENERATION:-
Sr.No.
Category
Waste Water Generation (KL/day)
Existing
Due toremoval of
ExistingProducts
ProposedTotal AfterExpansion
1. Domestic 19 -- 17 36
A TOTAL 19 -- 17 36
Industrial
1. Process 1.0 -- 288 289
2. Boiler NIL -- 40 40
3. Cooling Tower (Make-up)* 70 -- 65 135
4. Washing 0.1 -- 69.8 69.9
5. D.M. NIL -- 10 10
B TOTAL 71.1 -- 472.8 543.9
GRAND TOTAL (i + ii) 90.1 NIL 489.8 579.9=580
WATER BALANCE DIAGRAM:-
WATER BALANCE DIAGRAM FOR EXISTING UNIT
Basis: KL/Day
Recycle
Fresh Water360.1
Industrial338.1
Domestic22
Process1.0
Cooling337
Washing0.1
1.0 70 0.1
0.1 KL Natural Evaporated
U/G Septic tank19
ETP
ETP
WATER BALANCE DIAGRAM FOR AFTER EXPANSION (EXISTING +
PROPOSED) OF UNIT
Basis: KL/Day
Recycle
Fresh Water1024.9
TOTAL931.9
Domestic43
Gardening50
DM10
Process159
Boiler120
10
289 40
Washing79.9
Cooling563
69.9 135
579.9 ETP580.1
480
RO 580RO Permeate480
Coal & Fly ashHandling
55
MEE100
MEECondensate 55
U/G SepticTank
36
Decanter/Centrifuge0.5
MEE SALT0.30 T/day
Evaporated44.5
RO Reject100
0.2MEECon.
Detail of Proposed ETP
The high COD effluent shall treat mixed with low COD stream at ETP and further treatment as under:
1) Oil/grease separation: The effluent does not contain any oil/grease. But, during maintenance of
equipment the spilled oil/grease get mix with water effluent the same so separated in oil/grease
separation which shall provide at inlet of collection tank.
2) Collection tanks: Untreated effluent of plant is collected in a common tank and is homogenizing by
all through baffle wall arrangement.
3) Neutralization Tank: Diffused air system shall install in neutralization tank. Here, during chemicals
& polyelectrolyte shall be added to achieve neutralization and flocculation.
Details of proposal ETPDesign Flow Rate Q = 581 M3/Day
SR.NO.
NAME OF PROPOSEDUNITS
SIZENO OFUNITS
CapacityIn M3
DetentionTime
1. Stripper 20 M3/hr 1 20 M3/hr 0.822. Oil & Grease separator 10 M3 1 10 M3 0.413. Collection tank 350 M3 each 2 700 M3 28.964. Primary clarifier 60 M3 each 2 120 M2 4.965. Buffer tank 24 M3 each 1 24.0 M3 0.996. UASB (Up flow Anaerobic
Sludge Blanket540 M3 each 1 540 M3 22.34
7. Sludge settling tank 5 M3 each 2 10.0 M3 0.418. Aeration tank 225 M3 each 2 450 M3 18.629. Secondary clarifier 80 M3 each 2 160.0 M3 6.6210. Secondary water
collection tank96 M3 each 1 96.0 M3 3.97
11. Tertiary clarifier 50 M3 each 2 100.0 M3 4.1312. Treated water tan 50 M3 each 1 50.0 M3 2.0613. Decanter 5 M3/hr 1 5 M3/hr 0.2014. Sludge drying bed 50 sq. ft each 2 100 sq. ft 4.1315. Sand filter 15 M3/hr each 2 30 M3/hr 1.2416. Carbon filter 15 M3/hr each 2 30 M3/hr 1.2417. RO system 29 M3/hr 1 1 0.04118. MEE 100 M3/day 1 100 M3/day 4.13
4) Primary Clarifier: The effluent from neutralization tank them feed to primary clarifier. The
suspended solids get settle as sludge at the bottom of primary clarifier. The over flow of primary clarifier
is collected in buffer tank.
5) Buffer Tank: The effluent collected in buffer tank shall mix with lime as dosing chemical to maintain
the pH in Anaerobic
6) USAB: The BOD/COD load of effluent is treated in presence of biomass under anaerobic condition.
Methane is generated as gas which is further used as flame. Reduction of 70 to 80 % COD/BOD load
of effluent is achieved in USAB.
7) Sludge settling Tank: The over flow of USAB contain active biomass along with the effluent. The
bio mass is collected as sludge and recycled back to tower through buffer tank.
8) Aeration Tank: The overflow of USAB shall feed to the aeration tank. The aeration tank contain the
microorganism and enough shall be provided through the aerators. The further degradation of organic
matter shall be gone. The BOD and COD reduction shall be obtain 80 to 85%.
9) Secondary Clarifier: The overflow of Aeration tank contains the biomass which shall feed in
secondary clarifier where the active biomass is collected as sludge. The port of it shall recycled back to
Aeration tank and port shall dry in sludge drying bed.
10) Tertiary clarifier: The overflow of secondary clarifier contains some deed/active biomass along
with it. It is treated with polyelectrolyte in tertiary clarifier and all the suspended bio mass settled at
bottom of tertiary clarifier. The overflows effluent achieves the required norms for further disposal and
reuse.
11) Decanter: The bottom sludge from secondary/tertiary clarifier shall feed to decanter. It shall require
for separation solids from water. The solids are packed in 25 kgs bags and sent to TSDF site for safe
disposal. The leachate shall recycled back for treatment.
12) Recycling system of treated water.
Treated water after tertiary treatment shall give RO treatment for reuse and zero discharge.
a) The coal storage water sprinkler system
b) In house manufacturing of bricks from fly ash generated from coal fired TFH and CPP.
c) Biomass quantity will be treated in pray dryer / MEE and solids collected will be disposed off to TSDF
site.
The treated effluent shall be passing through sand filter and carbon filter and then feed to RO plant.
The RO treatment effluent shall reuse back @480 KL and reject @100 KL shall be transfer to MEE.
The MEE condensate shall be reuse in coal & Fly Ash handling and MEE salt that dispose to TSDF site
after giving transfer in decanter.
ETP FLOW DIAGRAM
1. Oil and grease separator
2. Collection tank
3. Primary Clarifier
4. Buffer Tank
5. UASB (Up flow Anaerobic Sludge Blanket)
6. Sludge settling Tank
7. Aeration Tank
8. Secondary clarifier
9. Secondary water collection tank
10. Tertiary clarifier
11. Treated water tank
12. Decanter
13. Sludge drying Bed
14. Sand Filter
15. Carbon Filter
16. RO system
17. MEE
Permeate to coating
Spray dryer/MEE
Bricks from fly ash
Recycle
1
2 3 4 5 6
891011
12
1314, 15 &16
MEE
Effluent fromhigh CODstripper
7
Effluent fromLow CODstripper
Annexure – 6
Details Of Emission In To Air & Its Control System
FUEL CONSUMPTION:
Sr.No.
Name ofFuel
Use in toCONSUMPTION
ExistingAfter
ExpansionProposed
Total AfterExpansion
1 CoalThermopacks
and boilers52 MT/Day - 52 MT/Day 600 MT/Day 600 MT/Day
2High
SpeedDiesel
D.G Sets710
Liter/hour- 710
Liter/hour--- NIL
STACK DETAILS
STACK ATTACHED TO Details of APCMStackHeightExisting Proposed
AfterExpansion
Existing ProposedAfter
ExpansionTFH – 1(capacity4000 U)
--- RemovedTrima Cyclone
separator &Bag filter
--- NIL 40 Mts
TFH – 2(capacity1500 U)
--- RemovedMulti Cyclone
separator--- NIL
30 MtsTFH – 3(capacity2500 U)
--- RemovedMulti Cyclone
separator--- NIL
Boiler(capacity 4
T/Hr)--- Removed
Multi Cycloneseparator
--- NIL
---
Boiler-I(Turbine Type)
(capacity 40T/Hr)
Boiler-I(Turbine
Type)(capacity 40
T/Hr)
--- ESP ESP
65 Mts
---
Boiler-II(Turbine Type)
(capacity 40T/Hr)
Boiler-II(Turbine
Type)(capacity 40
T/Hr)
--- ESP ESP
--- TFH – 1 TFH – 1 --- ESP ESP 65 Mts
(capacity14000 U)
(capacity14000 U)
---TFH – 2(capacity14000 U)
TFH – 2(capacity14000 U)
--- ESP ESP
---TFH – 3(capacity14000 U)
TFH – 3(capacity14000 U)
--- ESP ESP
D.G Set(capacity
3300 KVA)(Standby)
--- RemovedAs per
AdequateStack height
--- NILNot
Available
D.G Set(capacity750 KVA)(Standby)
--- RemovedAdequate
Stack height--- NIL
NotAvailable
D.G Set(capacity750 KVA)(Standby)
--- RemovedAdequate
Stack height--- NIL
NotAvailable
Note: We will dismantle existing Boiler, Thermopack & D.G. Sets after proposed expansion.
ANNEXURE-7
HAZARDOUS WASTE:
Sr.No.
Waste Source Schedule-I
Quantity
FacilityExisting Proposed
Total AfterExpansion
1 Used OilThermo
packSch-I5.1
0.90 1.12
MT/Year
Collection,Storage,
Transportation,Disposal by
selling toRegistered Re-
refiners,approved by
GPCB/CPCB orreused as
lubricant formachinery within
the factory.
2 ETP Sludge ETPSch-I35.3
4MT/Year
146MT/Year
150MT/Year
Collection,Storage,
Transportation,Disposal at TSDFsite approved by
GPCB.
3DiscardedContainer
RawMaterial
Sch-I33.1
8.50MT/Year
6.5MT/Year
15.0MT/Year
Collection,Storage,
Transportation,Disposal by
selling toRegistered facility
approved byGPCB.
4Evaporated
saltMEE
Sch-I35.3
---110
MT/Year110
MT/Year
Collection,Storage,
Transportation,Disposal at TSDF
approved byGPCB.
5Waste
ResidueProcess
Sch-I20.3
30MT/Year
-30MT/Year
NIL
Collection,Storage,
Transportation,Disposal at
CHWIF approvedby GPCB.
6
Wasteresidue
contaminatedoil
process --2.40
MT/Year0.6
MT/Year3.0
MT/Year
Collection,Storage,
Transportation,Disposal at
CHWIF approvedby GPCB.
ANNEXURE – 8
DETAILS OF RISK OF ACCIDENTS DURING OPERATION & ITS MITIGATION FOR THE PROJECT THATCOULD AFFECT HUMAN HEALTH & ENVIRONMENT
Environmental Impact & It’s Mitigation Measures
ActivityEnvironmental
AttributeCause
Impact Characteristic
Nature Duration Reversibility Mitigation Measures
MANUFACTURING OF PRODUCT
Handling &
Charging of
Raw
Material /
Product
Air, Land &
Soil
Charging of
liquid raw
material
Direct
Negative
Long
Term
Reversible Charging of liquid material should be through pipeline
Proper collection system will be provided for theleakage & spillage of hazardous chemical bypreparing dyke wall & acid proof RCC flooring withspillage collection tank.Loading & Unloading equipments inspected &maintained regularly.Trained and experience operator will be employed.
The personnel will be periodically and regularlytrained in handling & using fire extinguishers etc.
Handling of
finished product
Direct
Negative
Long
Term
Reversible The management should ensure provision of properstorage facility & proper usage of PPE’s
OPERATION OF UTILITIES
Operation ofBoiler &Thermopack
Air, Noise,Land & Soil
Air emission dueto coal
combustion
Direct
Negative
Long
Term
Reversible Provision of adequate stack height as per CPCBguidelines for adequate dispersion of pollutantgases.Provision of ESP as air pollution control system.
Noise generationdue to
operation ofblower
Regular maintenance and inspection.
The engine oil must be checked at regular intervals.
Used oil generated from generator will be collectedand stored in a storage area and disposal will bedone appropriately so as to prevent anyenvironmental hazards.
Land/soilcontamination
due to oil spillage
ActivityEnvironmental
AttributeCause
Impact Characteristic
Nature Duration Reversibility Mitigation Measures
STORAGE FACILITIES FOR THE LIQUID MATERIALS
Storage facilities
for all the liquid &
solid materials
Air, Water
& Land
Spillages of
material
Direct
Negative
Long
Term
Irreversible Independent dykes will be provided forhazardous chemicals storage to containleakages. Floors of the dyke area haveimpervious finish. Dyked enclosure shallbe able to contain the complete contents ofthe largest tank in the dyke in case of anyemergency.
NFPA label (hazard identification) capacityand content will be displayed on storagetank.Efficient Level system in tank shall beprovided to avoid over flow of tank.
Dangerous substance should be handledand stored under the supervision of acompetent person who is familiar with therisks and the precautions to be taken.Proper and sufficient fire fightingarrangement will be provided in and aroundthe storage.Proper labeling, handling and housekeepingshall be maintained.
TRANSPORTATION OF ALL THE RAW MATERIALS, FINISHED PRODUCTS AND HAZARDOUS WASTES
Transportation
of all the raw
materials, finished
products and
hazardous wastes
Air,
Water, Noise
& Land
Vehicular
movement
& its emission
Direct
Negative
Short
Term
Reversible Paved roads will be maintained. Necessaryrepairs will be done immediately if the road isdamaged.The speed of vehicles will be limited to less than10 km/hr for heavy vehicles to prevent dustgeneration.
Spillage of
raw material,
Direct
Negative
Long
Term
Reversible The truck drivers should be trained intransportation of materials having knowledge inspill control and other emergency actions.
finished
product and
hazardous
waste during
transportation
The vehicles used for transporting materialsshould follow the applicable guidelines given inThe Motor Vehicles Act.Only P.U.C. certified vehicle will be used & avoidusage of old age truck.Trucks will not be over loaded and should bemaintained to the body level.
MSDS of all the raw materials and finishedproducts should be made available to the driver& Off-site Emergency team as and whenrequired.Adequate tree plantation should be carried out.
ANNEXURE-12
CC&A COMPLIANCE REPORT
SR.NO.
CONSENT CONDITION STATUS
Name of unit SUMILON POLYESTER LIMITEDPlot No.: 43/P , N.H. 8, Village: Varsana, taluka: Anjar, Dist: Kutch-370201
1 CC&A order no. & Issue Date AWH-94666, Dated: 19 /07 /20182 Validity of CC&A 07/04/2023
Name of Product i) Bi- Axial Oriented Polyester Filmii) Ii) Metalized Polyester Film
Production Capacity i) 2500 MT/Month ii) 1250 MT/Month
SR.NO.
CONSENT CONDITION STATUS & CORECTIVE& PREVENTIVE ACTION
3 CONDITIONS UNDER THE WATER ACT3.1 The quantity of the Industrial effluent to be generated from the manufacturing
process and other ancillary industrial operation shall be NIL. The entire wastewater generated from the process shall be utilized in the cooling Process withinplant premises.
Complied
3.2 The quantity of Sewage Effluent from the factory shall not exceed 1.2 KL/day. Complied3.3 Domestic effluent shall be disposed off through septic tank/soak pit system Complied4 CONDITIONS UNDER THE AIR ACT
4.1 The following shall be used as fuel in the Thermic Fluid Heater and DG set, asfollowing rates.
Sr. No. Fuel Quantity1) Coal 36 MT/Day2) High Speed Diesel 410 Liter/hour
Complied
4.2 The applicant shall install & operate air pollution control system in order to achieveflue gas emission norms as prescribed below.
StackNo.
Stackattached to
Stackheightinmeter.
Air pollutionControlMeasure
Parameter Permissiblelimit
1 ThermicFluidHeater-4000U
40.00 Trimacycloneseparatorwith BagFilter
PM
SO2
NOx
150 mg/Nm3100 ppm50ppm
2 D.G. SET-3300 KVA(stand by)
30.00 NOx+HCCOPMSmokelimit(LightAbsorptionCoefficient)
< 4.0 g/kW-hr< 3.5 g/kW-hr< 0.2 g/kW-hr< 0.7 mˉ¹
Complied
4.3 There shall be no process gas emission from the manufacturing activities andother ancillary operations.
Complied
SR.NO.
CONSENT CONDITION STATUS & CORECTIVE& PREVENTIVE ACTION
4.4 The concentration of the following parameters in the ambient air within thepremises of the industry shall not exceed the limits specified hereunder as perNational Ambient air Quality Standards issued by MoEF&CC dated 16
thNovember-
2009SrNo.
Pollutant Time weightedAverage
Concentration inAmbient air inμg/m³
1 Sulphur Dioxied(SO2) Annual24 Hours
5080
2 Nitrogen Dioxied (NOx) Annual24 Hours
4080
3 Particulate Matter(size lessthan 10μm) OR PM10
Annual24 Hours
60100
4 Particulate matter (size lessthan2.5μm) OR PM2.5
Annual24 Hours
4060
.
Complied
4.5 The level of Noise in ambient air within the premises of industrial unit shall notexceed following levels:Between 6 am to 10 pm : 75 dB (A)
Between 10 pm to 6 am : 70 dB (A)
Complied
5 Authorization under hazardous waste [management & Transboundry Movement] Rules , 2016 & amended5.1 Authorization NumberAWH-94666 and shall valid upto 27/04/2023 Complied5.2 SUMILON POLYESTER LIMITED, is hereby granted an authorization to operate
facility for following hazardous wastes after expansion on the premises situated atPLOT NO.: 43/P, N.H. 08, VILLAGE VARSHAMEDI, TALUKA: ANJAR, DIST:KUTCH
Sr.No.
Waste Quantityper Annum
Category Facility
1 Used Oil 0.600 MT 5.1 Collection, storagetransportation and disposal byselling out to Registeredrecyclers/re-processors orReuses as lubricant withinplant premises.
2 DiscardedContainer
1.50 MT 33.3 Collection, storage,decontamination,transportation and disposal byselling to registered recycler.
Complied
5.3 The authorization is granted to operate a facility for collection, storage, within thefactory premises transportation and ultimate disposal of Hazardous wastes bysending to TSDF site.
Complied
5.3 The authorization is subject to the conditions stated below and such otherconditions as may be specified in the rules from time to time under theEnvironment (Protection) Act – 1986.
Complied
5.4 TERMS AND CONDITIONS OF AUTHORISATION:1. The authorized person shall comply with the provisions of the Environment(Protection) Act, 1986 and the rules made there under.2. The authorization or its renewal shall be produced for inspection at therequest of an officer authorized by the State Pollution Control Board.3. The person authorized shall not rent, lend, sell, transfer or otherwisetransport the hazardous and other wastes except what is permitted through thisauthorization.
Complied
SR.NO.
CONSENT CONDITION STATUS & CORECTIVE& PREVENTIVE ACTION
4. Any unauthorized change in personnel, equipment or working conditionsas mentioned in the authorization order by the persons authorized shall constitutea breach of this authorization.5. The person authorized shall implement Emergency Response Procedure(ERP) for which this authorization is being granted considering all site specificpossible scenarios such as spillages, leakages, fire etc. and their possible impactand also carry out mock drill in this regard at regular interval of time.6. The person authorized shall comply with the provisions outlined in theCentral Pollution Control Board guidelines on “Implementing for EnvironmentalDamages due to Handling and Disposal of Hazardous Waste and Penalty”7. It is the duty of the authorized person to take prior permission of theGujarat Pollution Control Board to close down the facility.8. The imported hazardous and other wastes shall be fully insured for transitas well as for any accidental occurrence and its clean-up operation.9. The record of consumption and fate of the imported hazardous and otherwastes shall be maintained.10. The hazardous and other waste which gets generated during recycling orreuse or recovery or pre-processing or utilization of imported hazardous or otherwastes shall be treated and disposed of as per specific conditions of authorization.11. The imported or exporter shall bear the cost of import or export andmitigation of damages if any.12. An application for the renewal of an authorization shall be made as laiddown under these rules.13. Any other conditions for compliance as per the guidelines issued by theMinistry of Environment, Forest and Climate Change or Central Pollution ControlBoard from time to time.14. Annual return shall be filed by June 30
thfor the period ensuring 31
stMarsh
of the year.5. GENERAL CONDITION
5.1 Unit shall develop green belt within premises as per the CPCB guidelines.However, if the adequate land is not available within premises, the unit shall tie upwith local agencies like gram panchayat, school, social forestry office etc. for theplantation at suitable open land in nearby locality and submit an action plan ofplantation for next three years to GPCB.
CompliedNo change.
5.2 Adequate plantation shall be carried out along THE PERIPHERY OF THEINDUSTRIAL Premises in such a way that the density of plantation is at least 1000trees per acre of land and a green belt of 10 meters width is developed.
Complied
5.3 The applicant shall have to submit the returns in prescribed form regarding WaterConsumption and shall have to make payment of Water Cess to the Board underWater Cess Act-1977.
Complied
5.4 In case of change ownership / management the name and address of the newOwners/partners/directors/proprietor should immediately be intimated to the Board.
Complied
5.5 The applicant shall however, not without the prior consent of the board bring intoUse any new or altered outlet for the discharge of effluent, or gaseous emission orSewage waste or Hazardous waste from the proposed industrial plant. Theapplicant is required to make application to this Board for this purpose in theprescribed Forms under the provisions of the Water Act-1974, The Air Act-1981and the Environment (Protection) Act-1986.
Complied
5.6 The overall noise level in and around the plant area shall be kept well within thestandards by providing noise control measures including engineering control likeacoustic insulation hoods silences enclosures etc. on all sources of noisegeneration. The ambient noise level shall conform to the standards prescribedunder the Environment (Protection) Act, 1986 & Noise Pollution (Regulation and
Complied
SR.NO.
CONSENT CONDITION STATUS & CORECTIVE& PREVENTIVE ACTION
Control) Rules, 2000.
5.7 Applicant is required to comply with the manufacturing, Storage and import ofHazardous Chemicals Rules-1989 framed under the Environment (Protection) Act-1986.
Complied
5.8 If it is established by any competent authority that the damage is caused due totheir industrial activities to any person or his property in that case they are obligedto pay the compensation as determined by competent authority.
Complied
5.9 Applicant shall have to comply with all the guidelines/ directive issued/ beingissued by MoEF & CC/ CPCB/ DoEF from time to time.
Complied
5.10 Environmental cell shall be setup and shall be responsible for the totalEnvironmental management.
Complied
5.11 Monitoring inrespect to Air, Water, Noise level shall be carried out and results shallbe submitted to GPCB on quarterly basis.
Complied
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