PROPOSED EXPANSION FOR MANUFACTURING OF SPECIALTY...
Transcript of PROPOSED EXPANSION FOR MANUFACTURING OF SPECIALTY...
FORM-1
for
PROPOSED EXPANSION FOR MANUFACTURING
OF SPECIALTY CHEMICALS
IN EXISTING UNIT
of
M/S. WORLD CHEM INDUSTRIES
PLOT NO. C-1B/407/4,
GIDC ESTATE, PANOLI, TAL: ANKLESHWAR,
DISTRICT: BHARUCH-394116, GUJARAT
EIA CONSULTANT
APPENDIX I
FORM 1 (I) Basic Information
Sr.
No.
Item Details
1. Name of the Project/s M/s. World Chem Industries
2. S. No. in the Schedule 5(f)
3. Proposed capacity/area/length/tonnage to
be handled/command area/lease
area/number of wells to be drilled
For Proposed production capacity please refer
Annexure-I
4. New/Expansion/Modernization Expansion
5. Existing capacity/area etc. For existing production capacity please refer
Annexure-I
6. Category of project i.e. ‘A’ or ‘B’ 'A'
7. Does it attract the general condition? If yes,
please specify.
Yes. Located in critically polluted area
(Ankleshwar)
8. Does it attract the specific condition? If yes,
please specify.
-
9. Location
Plot/Survey/Khasra No. Plot No. Plot No. C-1B/407/4,
Village GIDC Estate,Panoli
Tehsil Ankleshwar
District Bharuch
State Gujarat
10. Nearest railway station/airport along with
distance in kms.
Nearest Railway Station: Panoli = 3.80 kms
Nearest Airport: Surat = 55.9 kms
11. Nearest Town, city, District Headquarters
along with distance in kms.
Nearest town: Ankleshwar = 7.0 kms,
Nearest District Head quarter: Bharuch = 16.0
kms
12. Village Panchayats, zilla parishad, Municipal
corporation, Local body (Complete postal
addresses with telephone nos. to be given)
Plot No. C-1B/407/4,
GIDC ESTATE, Panoli, Tal: Ankleshwar,
District: Bharuch-394116, Gujarat
13. Name of the applicant Mr. Bhimashankar VishWanath Patil
14. Registered address M/s. World Chem Industries
Plot No. C-1B/407/4,
GIDC ESTATE, Panoli, Tal: Ankleshwar,
District: Bharuch-394116, Gujarat
15. Address for correspondence:
Name Mr. Bhimashankar VishWanath Patil
Designation (Owner/Partner/CEO) Proprietor
Address M/s. World Chem Industries
Plot No. C-1B/407/4,
GIDC ESTATE, Panoli, Tal: Ankleshwar,
District: Bharuch-394116, Gujarat
Pin Code 394116
E-Mail [email protected]
Telephone No. 02646—272014
Mobile +91 98243 16654/9898078763
Fax No. -
16. Details of Alternative Sites examined, if any
location of these sites should be shown on
a topo sheet.
No
17. Interlinked Projects No
18. Whether separate application of interlinked
project has been submitted?
No
19. If Yes, date of submission Not applicable
20. If no., reason Not applicable
21. Whether the proposal involves
approval/clearance under: If yes, details of
the same and their status to be given.
(a) The Forest (Conservation) Act, 1980?
(b) The Wildlife (Protection) Act, 1972?
(c) The C.R.Z Notification, 1991?
Not applicable, as the project is located in
notified industrial estate.
22. Whether there is any Government
order/policy relevant/relating to the site?
No
23. Forest land involved (hectares) N.A.
24. Whether there is any litigation pending
against the project and/or land in which the
project is propose to be set up?
(a) Name of the Court
(b) Case No.
(c) Orders/directions of the Court, if any
and its relevance with the proposed
project.
No
• Capacity corresponding to sectoral activity (such as production capacity for manufacturing,
mining lease area and production capacity for mineral production, area for mineral exploration, length for linear transport infrastructure, generation capacity for power generation etc.,)
(II) Activity
1. Construction, operation or decommissioning of the Project involving actions, which
will cause physical changes in the locality (topography, land use, changes in water
bodies, etc.)
Sr.
No.
Information/Checklist confirmation Yes
/No?
Details thereof (with approximate
quantities / rates, wherever possible)
with source of information data
1.1 Permanent or temporary change in land
use, land cover or topography including
increase in intensity of land use (with
respect to local land use plan)
No Unit is identically located in notified
area.
1.2 Clearance of existing land, vegetation and
buildings?
No
1.3 Creation of new land uses? No
1.4 Pre-construction investigations e.g. bore
houses, soil testing?
No
1.5 Construction works? No Construction will be carried out as per
plan shown in Annexure-II
1.6 Demolition works? No
1.7
Temporary sites used for construction
workers or housing of construction workers? No
1.8 Above ground buildings, structures or
Earthworks including linear structures, cut
and fill or excavations
Yes Construction will be carried out as per
plan shown in Annexure-II
1.9
Underground works including mining or
tunneling?
No
1.10 Reclamation works? No
1.11 Dredging? No
1.12 Offshore structures? No
1.13 Production and manufacturing Yes List of Products is attached as
Annexure- I and manufacturing process
attached as Annexure-III.
1.14 Facilities for storage of goods or materials? Yes Facilities for storage of raw materials &
products will be developed as shown in
Annexure-II.
1.15
Facilities for treatment or disposal of solid
waste or liquid effluents?
Yes Detail of the Liquid effluent treatment
in Annexure- IV.
Detail of solid Waste and Hazardous
waste disposal attached in Annexure- V.
1.16
Facilities for long term housing of
operational workers?
No
1.17 New road, rail or sea traffic during
construction or operation?
No The project is identically situated in
GIDC's Notified (Industrial) Area. It is
having well connectivity with Road as
well as Railways.
1.18 New road, rail, air waterborne or other
airports etc?
No Existing transportation system is
adequate.
1.19 Closure or diversion of existing transport
routes or infrastructure leading to changes
in traffic movements?
No
1.20 New or diverted transmission lines or
pipelines?
No
1.21
Impoundment, damming, converting,
realignment or other changes to the
hydrology of watercourses or aquifers?
No
1.22 Stream crossings? No
1.23
Abstraction or transfers or the water form
ground or surface waters?
No Water Source : GIDC Water Supply.
1.24
Changes in water bodies or the land surface
affecting drainage or run-off?
No The project is located in G.I.D.C., Panoli
1.25
Transport of personnel or materials for
construction, operation or
decommissioning?
No By road only.
1.26 Long-term dismantling or decommissioning
or restoration works?
No No such work will be involved.
1.27 Ongoing activity during decommissioning
which could have an impact on the
environment?
No
1.28
Influx of people to an area in either
temporarily or permanently?
No
1.29 Introduction of alien species? No
1.30 Loss of native species of genetic diversity? No
1.31 Any other actions? No
2. Use of Natural resources for construction or operation of the Project (such as land,
water, materials or energy, especially any resources which are non-renewable or in
short supply):
Sr. No Information/checklist confirmation Yes/
No?
Details there of (with approximate
quantities/rates, wherever possible)
with source of information data
2.1 Land especially undeveloped or agriculture
land (ha)
No The project site is located in GIDC,
Panoli.
2.2 Water (expected source & competing
users) unit: KLD
Yes Source: GIDC water supply
For water consumption for proposed
expansion, please refer Annexure - IV
2.3 Minerals (MT) No
2.4
Construction material -stone, aggregates,
sand / soil (expected source MT)
Yes Construction materials, like steel,
cement, crushed stones, sand, rubble,
etc. required for the project will be
procured from the local market of the
region.
2.5 Forests and timber (source - MT) No
2.6
Energy including electricity and fuels
source, competing users) Unit: fuel (MT),
energy (MW)
Yes Power required from…
DGVCL is : 60 HP
Fuel :
Existing: Nil
Proposed total: Natural Gas: 30 M3/Hr.
The Detail regarding fuel consumption is
shown in Annexure VI.
2.7 Any other natural resources (use
appropriates standard units)
No
3. Use, storage, transport, handling or production of substances or materials, which
could be harmful to human health or the environment or raise concerns about
actual or perceived risks to human health.
Sr.
No.
Information / Checklist confirmation Yes/
No?
Details thereof (with approximate
quantities / rates wherever possible)
with source of information data
3.1 Use of substances or materials, which are
hazardous (as per MSIHC rules) to human
health or the environment (flora, fauna,
and water supplies)
Yes
Please refer Annexure : VII
3.2 Changes in occurrence of disease or affect
disease vectors (e.g. insect or water borne
diseases)
No
3.3 Affect the welfare of people e.g. by
changing living conditions?
No
3.4
Vulnerable groups of people who could be
affected by the project e.g. hospital
patients, children, the elderly etc.,
No
3.5 Any other causes No
4. Production of solid wastes during construction or operation or decommissioning
MT/month)
Sr.
No.
Information/Checklist confirmation Yes/
No?
Details thereof (with approximate
quantities / rates, wherever possible)
with source of information data
4.1 Spoil, overburden or mine wastes No
4.2
Municipal waste (domestic and or
commercial wastes) No
4.3
Hazardous wastes (as per Hazardous Waste
Management Rules)
Yes Please refer Annexure: V
4.4 Other industrial process wastes Yes Please refer Annexure: V
4.5 Surplus product Yes Not applicable
4.6
Sewage sludge or other sludge from
effluent treatment
No
4.7 Construction or demolition wastes No
4.8 Redundant machinery or equipment No
4.9 Contaminated soils or other materials No
4.10 Agricultural wastes No
4.11 Other solid wastes No
5. Release of pollutants or any hazardous, toxic or noxious substances to air (Kg/hr)
Sr.
No.
Information/Checklist confirmation Yes/
No?
Details thereof (with approximate
quantities/rates, wherever possible)
with source of information data
5.1 Emissions from combustion of fossil fuels
From stationary or mobile sources
Yes For details Please refer Annexure – VI
5.2 Emissions from production processes Yes For details Please refer Annexure – VI
5.3 Emissions from materials handling Yes For details Please refer Annexure – VI
including storage or transport
5.4 Emissions from construction activities
including plant and equipment
No
5.5
Dust or odours from handling of materials
including construction materials, sewage
and waste
No
5.6 Emissions from incineration of waste No
5.7 Emissions from burning of waste in open
air (e.g. slash materials, construction
debris)
No
5.8 Emissions from any other sources No
6. Generation of Noise and Vibration, and Emissions of Light and Heat:
Sr.
No.
Information/Checklist confirmation Yes/
No?
Details there of (with approximate
Quantities /rates, wherever possible)
With source of information data
6.1
From operation of equipment e.g. engines,
ventilation plant, crushers
Yes The Noise level will be within the
prescribed limit. At noisy areas
adequate preventive & control
measures will be taken. No significant
noise, vibration or emission of light &
heat from the unit.
6.2 From industrial or similar processes Yes -do-
6.3 From construction or demolition No
6.4 From blasting or piling No
6.5 From construction or operational traffic No
6.6 From lighting or cooling systems
Yes Adequate Lighting will be provided in
unit and also local ventilation system
will be provided.
6.7 From any other sources No
7. Risks of contamination of land or water from releases of pollutants into the ground
or into sewers, surface waters, groundwater, coastal waters or the sea:
Sr.
No
Information/Checklist confirmation Yes/
No?
Details thereof (with approximate
quantities / rates, wherever possible)
with source of information data
7.1
From handling, storage, use or spillage of
hazardous materials
Yes All the raw materials will be stored
separately in designated storage area
and safely as per details given in
Annexure: VII.
7.2
From discharge of sewage or other
effluents to water or the land (expected
mode and place of discharge)
No
7.3
By deposition of pollutants emitted to air
into the land or into water
No
7.4 From any other sources No
7.5 Is there a risk of long term build up of No
pollution in the environment from these
sources?
8. Risks of accident during construction or operation of the Project, which could
affect human health or the environment:
Sr.
No
Information/Checklist confirmation
Yes/
No?
Details thereof (with approximate
quantities / rates, wherever possible)
with source of information data
8.1 From explosions, spillages, fires etc from
storage, handling, use or production of
hazardous substances
Yes For detail please refer Annexure – VII
8.2 From any other causes No
8.3 Could the project be affected by natural
disasters causing environmental damage
(e.g. floods, earthquakes, landslides,
cloudburst etc)?
No
9. Factors which should be considered (such as consequential development) which
could lead to environmental effects or the potential for cumulative impacts with
other existing or planned activities in the locality
Sr.
No.
Information/Checklist confirmation Yes/
No?
Details thereof (with approximate
quantities / rates, wherever possible)
with source of information data
9.1 Lead to development of supporting.
laities, ancillary development or
development stimulated by the project
which could have impact on the
environment e.g.:
* Supporting infrastructure (roads, power
supply, waste or waste water treatment,
etc.)
• housing development
• extractive industries
• supply industries
• other
No For detail please refer Annexure – VIII
9.2
Lead to after-use of the site, which could
have an impact on the environment
No
9.3 Set a precedent for later developments No
9.4 Have cumulative effects due to proximity
to Other existing or planned projects with
similar effects
No
(III) Environmental Sensitivity
Sr.
No
Information/Checklist confirmation Name
/
Aerial distance (within 25 km).
Proposed Project Location
Identity Boundary.
1 Areas protected under international
conventions national or local legislation
for their ecological, landscape, cultural or
other related value
-- The site is located in Notified
Industrial Area of GIDC Estate, Panoli
Dist Bharuch, Gujarat.
2 Areas which are important or sensitive
for Ecological reasons - Wetlands,
watercourses or other water bodies,
coastal zone, biospheres, mountains,
forests
-- The site is located in Notified
Industrial Area of GIDC Estate, Panoli,
Dist Bharuch, Gujarat.
3 Areas used by protected, important or
sensitive species of flora or fauna for
breeding, nesting, foraging, resting, over
wintering, migration
-- Site is located in Notified Industrial
Area of GIDC Estate, Panoli
4 Inland, coastal, marine or underground
waters
No
5 State, National boundaries No
6 Routes or facilities used by the public for
to recreation or other tourist, pilgrim
areas.
-- N.A.
7 Defense installations -- N.A.
8 Densely populated or built-up area --
9 Areas occupied by sensitive man-made
land community facilities)
-- N.A.
10 Areas containing important, high quality
or scarce resources (ground water
resources, surface resources, forestry,
agriculture, fisheries, tourism, tourism,
minerals)
-- N.A.
11 Areas already subjected to pollution or
environmental damage. (those where
existing legal environmental standards
are exceeded)
-- N.A.
12 Areas susceptible to natural hazard which
could cause the project to present
environmental problems (earthquakes,
subsidence, landslides, erosion, flooding
or extreme or adverse climatic
conditions)
-- N.A.
LIST OF ANNEXURES
SR. NO. NAME OF ANNEXURE
I List of products with their production capacity
II Layout Map of the Plan
III Brief Manufacturing Process Description
IV Details of Water Consumption Wastewater Generation and Treatment
V Details of Hazardous /Solid Waste Generation, Handling and Disposal
VI Details of Stacks and Vents
VII Details of Hazardous Chemicals Storage & Handling
VIII GIDC Plot Allotment Letter
IX Membership of Common Effluent Treatment Plant
X GIDC Water Supply Letter
XI Topo Sheet
XII Socio-economic Impacts
XIII Proposed Terms of Reference for EIA studies
Annexure-I
List of Products & its production capacity
Note: Product No. 1 shall be discontinued after expansion.
Note:In Existing scenario unit has got Consolidated Consent & Authorisation- Gandhinagar-
Gujarat forFormulation/Blending/mixing only.
Unit shall manufacture listed products after getting Environmental Clearance (MoEF-Delhi)&
Consolidated Consent & Authorisation- SPCB-Gujarat.
Sr.
No. Product name
Existing
Quantity
MT/Month
Total Proposed
Quantity
MT/Month
1 Penta Erythritol Tetra Oleate 20 --
2 Turkey red oil
(CAS No. 8002-33-3)
65
60
3 Glycerol monostearate
(CAS No. 31566-31-1)
20
4 Sorbitan Mono Sterate
(CAS No. 1338-41-6)
30
5 Sorbiton Mono Oleate
(CAS No. 1338-43-8)
30
6 Sorbitan Tri Streate
(CAS No. 26658-19-5)
20
7 Sorbitan Monolaurate
( CAS No. 1338-39-2)
20
8 Anti Foam- Polyol Fatty Acid Ester
(CAS No. 65381-09-1)
20
9 CADAPA- Coco Amido Propyl Amine --
300
10
Coco Amido Propyl Betaine (CAPB)
( CAS No.61789-40-0)
--
11
Coco Mono Ethanol Amide (CMEA )
(CAS No. 68140-00-1) --
12
Coco Diethanolamide (CDEA)
(CAS No. 68603-42-9) --
Total 360
List of Raw Material & its consumption
Sr.
No. Product name Raw Materials
Qty.
MT/Month
1 Penta Erythritol Tetra Oleate - --
2 Turkey red oil Caster Oil 31.19
Sulphuric Acid 5.61
Caustic Lye 10.73
3 Glycerol monostearate Steric Acid 53.23
Glycerian 9.92
Catileyst 0.48
4 Sorbitan Mono Sterate Steraic Acid 56.25
Sorbitoal 24.50
Hypo 0.25
Hydrogen Peroxide 0.13
Catlyest 0.23
5 Sorbiton Mono Oleate Fatty Acid 51.06
Sorbitoal 24.26
Hypophosphorous Acid 0.19
Hydrogen Peroxide 0.19
Caustick flakes 0.24
6 Sorbitan Tri Streate Steraic Acid 42.857
Sorbitoal 23.571
Hypophosphorous Acid 0.343
Hydrogen Peroxide 0.407
Caustic Flakes 0.171
7 Sorbitan Monolaurate dcfa /lauric 47.50
Sorbitoal 30.00
Hypophosphorous Acid 0.27
Hydrogen Peroxide 0.38
Caustick flakes 0.33
Nitrogen Gas 0.50
8 Anti Foam Fattay Acid 37.90
PEG-400 19.56
PPG-2000 4.89
S.V.Cat 0.10
List of Raw Material & its consumption (Cont…)
9
CADAPA Coconut Oil 117.65
Dimethylamino
propylamine 88.24
Sodium Methoxide 0.21
10
Coco Amido Propyl Betaine CADAPA 72
Caustic flakes 10.91
mca 32.73
11 Coco Mono Ethanol Amide
Coconut Oil 212.24
Mono Ethanol Amine 16.24
Sodium Methoxide 0.41
Nitrogen Gas 1.22
12 Coco Diethanolamide
Coconut Oil 150.83
Diethylamine 45.25
Caustic Potosh 3.02
Nitrogen Gas 0.90
Annexure-II
Plan Lay Out
Annexure-III
Manufacturing Process & Mass Balance
1.0 TURKEY RED OIL ( CAS No. 8002-33-3)
Process:-
1:- Add Castor oil + Sulphuric acid …………………………………………....room temp.
2) slowly add sulphuric acid…….
3:- Start Stirring at 6 hr……………………………………………….room temp.
4:- Neutrize by Caustic flkas or lye
5:- Yield 90% for 80 % TRO
Mass Balance
Caster Oil 0.52 Turkey Red OIL 1
Sulphuric Acid 0.09
Caustic Lye 0.18
Water 0.21
Total 1 1
2.0 GLYCEROL MONO STEARATE (CAS No. 31566-31-1)
Process:-
1:- Add STERAIC ACID / Glycerian / HYPOPHOSPHEROUS ACID At…...room temp.
2)…….Heating Start & stirring Start……
3) Start Nitrogen at……………………………………………...100c.
4) Add Hyposphorus acid at………………..120c
5) Add caustic soda flakes at……………….120c
6:- Maintain for 30-35 Minutes at……………………………….240-242c.
7:- Cooled batch at………………………………………………..200c.
8:- Transfer next reactor ………………………70c
9:- Flaker…….. at 70c Temp .
10:- pack in 25kg Bag
Chemical Reaction
Mass Balance:
Input Ton Output Ton
Steric Acid 0.89 Glycerol monostearate 1
Glycerian 0.17 WASTE WATER 0.060
Catileyst 0.01
Total 1.06 1.06
3.0 SORBITAN MONO STERATE (CAS NO 1338-41-6)
Process:-
1:- Add STERAIC ACID / SORBITOL / HYPOPHOSPHEROUS ACID At…...room temp.
2)…….Heating Start & stirring Start……
3) Start Nitrogen at……………………………………………...100c.
4) Add Hyposphorus acid at………………..120c
5) Add caustic soda flakes at……………….120c
6:- Maintain for 30-35 Minutes at……………………………….240-242c.
7:- Cooled batch at………………………………………………..200c.
8:- Transfer next reactor ………………………70c
9:- Flaker…….. at 70c Temp .
10:- pack in 25kg Bag
Chemical Reaction
Mass Balance
Input Ton Output Ton
Steraic Acid 0.938 Sorbitan Mono Sterate 1
Sorbitoal 0.408 Waste Water 0.25
Hypo 0.004 Solid waste 0.11
Hydrogen Peroxide 0.002
Catlyest 0.004
Total 1.36 1.36
4.0 SORBITON MONO OLEATE (CAS NO 1338-43-8)
Process:-
1:- Add DISTILLED FATTY ACID + SORBITOL + OLEIC ACID… At…...room temp.
2)…….Heating Start & stirring Start……
3) Start Nitrogen at……………………………………………...100c.
4) Add Hyposphorus acid at………………..120c
5) Add caustic soda flakes at……………….120c
6:- Maintain for 30-35 Minutes at……………………………….240-242c.
7:- Cooled batch at………………………………………………..200c.
8:- Transfer next reactor ………………………70c
9:- Fliter…….. at 70c Temp .
10:- pack in drum or IBCs
Chemical Reaction:
Mass Balance
Input Ton Output Ton
Fatty Acid 0.851 Sorbiton Mono Olite 1
Sorbitoal 0.404 Waste Water 0.234
Hypophosphorous Acid 0.003 Solid Waste 0.032
Hydrogen Peroxide 0.003
Caustick flakes 0.004
Total 1.266 1.266
5.0 SORBITAN TRI STREATE (CAS NO 26658-19-5)
Process:-
1:- Add STERAIC ACID / SORBITOL / HYPOPHOSPHEROUS ACID At…...room temp.
2)…….Heating Start & stirring Start……
3) Start Nitrogen at……………………………………………...100c.
4) Add Hyposphorus acid at………………..120c
5) Add caustic soda flakes at……………….120c
6:- Maintain for 30-35 Minutes at……………………………….240-242c.
7:- Cooled batch at………………………………………………..200c.
8:- Transfer next reactor ………………………70c
9:- Flaker…….. at 70c Temp .
10:- pack in 25kg Bag
Chemical Reaction
Mass Balance
Input Ton Output Ton
Steraic Acid 0.714 Sorbitan Tri Streate 1
Sorbitoal 0.393 Waste Water 0.107
Hypophosphorous Acid 0.006 Solid Waste 0.015
Hydrogen Peroxide 0.007
Caustic Flakes 0.003
Total 1.123 1.123
6.0 SORBITAN MONOLAURATE (CAS NO 1338-39-2)
Process:-
1:- Add DISTILLED COCNUT FATTY ACID + SORBITOL + LAURIC ACID… At…...room temp.
2)…….Heating Start & stirring Start……
3) Start Nitrogen at……………………………………………...100c.
4) Add Hyposphorus acid at………………..120c
5) Add caustic soda flakes at……………….120c
6:- Maintain for 30-35 Minutes at……………………………….240-242c.
7:- Cooled batch at………………………………………………..200c.
8:- Transfer next reactor ………………………70c
9:- Fliter…….. at 70c Temp .
10:- pack in drum or IBCs
Chemical Reaction
Mass Balance
Input Ton
Output Ton
dcfa /lauric 0.792
sorbitan monolaurate 1
Sorbitoal 0.500
Waste Water 0.250
Hypophosphorous Acid 0.004
Solid Waste 0.066
Hydrogen Peroxide 0.006
Caustick flakes 0.006
Nitrogen Gas 0.008
Total 1.316
1.316
7.0 ANTI FOAM
Process:-
1:- Add RBFA / PEG-400 / HYPOPHOSPHEROUS ACID At…...room temp.
2)…….Heating Start & stirring Start……
3) Start Nitrogen at……………………………………………...100c.
4) Add Hyposphorus acid at………………..120c
5) Add caustic soda flakes at……………….120c
6:- Maintain for 30-35 Minutes at……………………………….200-205c.
7:- Cooled batch at………………………………………………..200c.
8:- Transfer next reactor ………………………70c
9:- Discharge…….. at 70c Temp .
10:- pack in 220 kg Drum
Mass Balance
Input ton Output ton
Fattay Acid 0.632 Anti Foam 1
PEG-400 0.326 Waste Water 0.041
PPG-2000 0.081
S.V.Cat 0.002
Total 1.041 1.041
8.0 CADAPA
Process:-
1:- Add COCONUT OIL / CAUSTIC SODA FLKES/ DIMETHLYlAMINO PROPYLAMINE
At…...room temp.
2)…….Heating Start & stirring Start……
3) Start Nitrogen at……………………………………………...100c.
4:- Maintain for 2 Hrs. at……………………………….130c.
5:- Cooled batch at………………………………………………..130c.
6:- Transfer next reactor ………………………70c
7:- Discharge…….. at 70c Temp .
8:- pack in 220 kg Drum
Chemical Reaction
Mass Balance
Input Ton Output Ton
Coconut Oil 0.59 CADAPA 1
Dimethylamino
propylamine 0.44
Dimethylamino propylamine
recovery 0.03
Sodium Methoxide 0.00
Total 1.03 1.03
9.0 COCO AMIDO PROPYL BETAINE (CAS NO 61789-40-0)
Process:-
1) 1:- Add CADAPA/CAUSTIC FLAKES/MONO CHLORO ACETIC ACID/ WATER
At…...room temp.
2)…….Heating Start & stirring Start……
3:- Maintain for 1HR Minutes at……………………………….90c.
4:- Cooled batch at………………………………………………..70c.
5:- Discharge…….. at 70c Temp .
06:- pack in 220 kg Drum
Chemical Reaction:
Mass Balance
Input Ton Output Ton
CADAPA 0.36 CAPB 1
Caustic flakes 0.05 Water vapour 0.03
mca 0.16
DM water 0.45
Total 1.03 1.03
10.0 COCO MONO ETHANOL AMIDE ( CAS NO 68140-00-1)
Process:-
1) 1:- Add COCNUT OIL/MONO ETHANOL AMINE SODIUM METOXIDE
At…...room temp.
2)…….Heating Start & stirring Start……
3:- Maintain for 1HR at……………………………….130c.
4:- Cooled batch at………………………………………………..70c.
5:- Flaker…….. at 58c Temp .
06:- pack in 25 kg Bag
Chemical Reaction
Mass Balance
Input Ton Output Ton
Coconut Oil 1.06 CMEA 1
Mono Ethanol Amine 0.08 Glycerol Monostearate 0.15
Sodium Methoxide 0.00
Nitrogen Gas 0.01
Total 1.15 1.15
11.0 COCO DIETHANOLAMIDE (CAS NO 68603-42-9)
Process:-
1) 1:- Add COCNUT OIL/DIETHLY AMINE/ SODIUM METOXIDE
At…...room temp.
2)…….Heating Start & stirring Start……
3:- Maintain for 1HR at……………………………….140c.
4:- Cooled batch at………………………………………………..70c.
5:- Discharge…….. at 70c Temp .
06:- pack in 220 kg Drum
Chemical Reaction:
Mass Balance
Input Ton Output Ton
Coconut Oil 0.75 CDEA 1
Diethylamine 0.23
Caustic Potosh 0.02
Nitrogen Gas 0.00
Total 1.00 1
ANNEXURE-IV
Details of Water Consumption, Wastewater Generation and Treatmant
Existing
NOTE:
� Domestic wastewater is discharged through Septic Tank/ Soak Pit System.
Sr. No. Category Water Consumption
(KL/Day)
Waste Water Generation
(KL/Day)
1. Domestic 0.650 0.300
2. Industrial
Process 0.750 Nil
Boiler Nil Nil
Cooling 0.100 Nil
Washing --- ---
Total Industrial 0.850 Nil
3. Other (Gardening) 1.000 Nil
Total (Domestic +Industrial) 2.500 0.300
DETAILS OF WATER CONSUMPTION AND WASTEWATER GENERATION
TOTAL PROPOSED
NOTE:
*DILUTE STREAM: 1.0 KLD( from Washing & Process) will be treated in ETP & Sent to CETP ( M/s.
Panoli Enviro Technology Ltd.) through tanker.
** CONCENTRATED STREAM: 0.333 KLD-from process will be treated in ETP & sent to Common
Spray Dryer Facility of M/s. Panoli Enviro Technology Ltd. through tanker.
Sr.
No.
Category Water Consumption
(KL/Day)
Waste Water
generation
(KL/Day)
Mode of discharge
1. Domestic 2.5 2.0 Septic Tank & Soak pit
2. Industrial
Process
1.0
0.833
0.333**
* Concentrated Stream from
process will be treated in ETP
& sent to Common Spray
Dryer Facility of M/s. Panoli
Enviro Technology Ltd.
0.5*
* Dilute stream: 0.5 KLD will
be Treated in ETP & send to
CETP of M/s. Panoli Enviro
Technology Ltd.
Boiler Nil Nil --
Cooling 1.0 NIl --
Washing 0.5 0.5 * Dilute stream: 0.5 KLD will
be Treated in ETP & send to
CETP of M/s. Panoli Enviro
Technology Ltd.
Total Industrial
2.5 1.333
3 Other (Gardening) 1.0 Nil
Total (Domestic + Industrial) 6.0 2.0 (Dom) + 1.333 (Ind)
= 3.333
WATER BALANCE
0.833
Raw Water: 6.0 KL/Day
Dom: 2.5 KL/Day
Process
1.0 KL/Day
Cooling
1.0 KL/Day
Washing
0.5 KL/Day
Septic Tank & Soak
Pit: 2.0 KL/Day
Ind: 2.5 KLD Green Belt : 1.0 KL/Day
Nil KL/Day
Common Spray Dryer
(M/s. PETL)
0.333 KL/Day
ETP
CETP (M/s. PETL)
1KL/Day ETP
0.5 KL/Day 0.5 KL/Day
CONCENTRATED EFFLUENT
IN WORST SITUATION EFFLUENT CHARACTERISTICS
(For Concentrated effluent)
Parameter Raw Effluent
(0.7 KL/Day)
pH 6.5 - 9.5
Oil and Grease, mg/L 2.0
COD, mg/L 25000
BOD3, mg/L 1000
Suspended Solids, mg/L 180
The above characteristics effluent will be allow in to ETP for primary treatment & send to Common
Spray Dryer (M/s. PETL) through Tanker.
The above characteristic effluent is given primary treatment in Effluent treatment plant.
DILUTE EFFLUENT
EFFLUENT WASHING CHARACTERISTICS (For Dilute effluent)
Parameter Raw Effluent
(0.7 KL/Day)
pH 6.5 - 9.5
Oil and Grease, mg/L 2.0
COD, mg/L 5000
BOD3, mg/L 1400
Suspended Solids, mg/L 160
The above characteristics effluent will be allow in to ETP for primary treatment & send to Common
ETP (M/s. PETL) through Tanker.
The above characteristic effluent is given primary treatment in Effluent treatment plant.
Primary Treatment
For study of primary treatment on effluent i.e. neutralization, flocculation and settling, effluent
sample was treated with Lime as neutralizing agent and FeSO4 as flocculating agent. Various
parameters were studied such as lime dose, FeSO4 dose, settling time, influent and effluent
suspended solids and COD.
The summary of the result is tabulated herewith in Table .
Table Summary of Primary Treatment Study
Initial COD: 500 mg/L
Run 1 Run 2 Run 3
Effluent Sample taken, ml 500 500 500
Lime Dose mg/L 100 150 275
FeSO4 Dose mg/L 50 65 85
COD after neutralization with FeSO4 mg/L 2500 2250 2612
% reduction of COD 50 55 48
Observation:
1. Reduction of 55 % in COD load is found at primary treatment level with Lime dose of 150
mg/L and FeSO4 dose of 65 mg/L.
After primary treatment, characteristic of effluent is as under:
Parameter Treated effluent
(Dilute Stream) FETP inlet Norms
pH 8.1 6.5 to 8.5
Oil and Grease, mg/L 1.0 <10
COD, mg/L 2450 <3500
BOD3, mg/L 845 <1000
Suspended Solids, mg/L 40 <100
Phenolic Compounds, mg/L BDL 1
The primary treated effluent conforming to above standards shall be sent to CETP, Panoli.
BRIEF DESCRIPTION OF EFFLUENT TREATMENT PLANT:
Process Description of Effluent Treatment Plant
The details of ETP are as follows.
First all non-toxic and biodegradable streams of wastewater shall be collected in
Equalization cum Neutralization Tank (ENT-01) where the continuous addition and stirring of
Lime solution is done to maintain neutral pH of wastewater from Lime Dosing Tank (LDT-01)
as per requirement by gravity. Pipe grid is provided at bottom of the ENT-01 to keep all
suspended solids in suspension and to provide proper mixing by air supplied through air
blowers (B-01).
Then after, neutralized wastewater shall be pumped to Flash Mixer (FM-01). Alum and
Polyelectrolyte shall be dosed from Alum Dosing Tank (ADT-01) and Polyelectrolyte Dosing
Tank (PEDT-1) respectively by gravity into FM-01 to carry out coagulation by using a Flash
Mixer. Then after, coagulated wastewater shall be settled in Primary Settling tank (PST-01).
Clear supernatant from PST-01 shall be collected in Intermediate Sump (IS-01).
Treated effluent from IS-01 then passed through Dual Media Filter (DMF-01) to remove
remaining SS from effluent. Then clear Water shall be collected in treated effluent Sump
(TES-01) before sent to common effluent treatment plant for further treatment.
Sludge settled in PST-01 shall be sent to Sludge Drying Beds (SDBs-A/B) where, dewatering
shall be carried out before storage in HWSA and ultimate disposal to TSDF. Leachate from
SDBs-A/B shall be pumped back to ENT-01 for further treatment.
All High COD streams of wastewater shall be collected in Collection Tank (CT-01) then
pumped to Common spray dryer for future treatment.
SIZE OF TANKS
S.N. Name of unit Size No. MOC/ Remark
Stream I (LOW COD stream) 1 KLD
1 Equalization cum Neutralization Tank (ENT-
01) 2 KLD 1 RCC M25
2 Primary Settling Tank(PST-01) 1 KLD 1 MSEP
3 Treated Effluent Sump (TES-01) 10 KLD 1 RCC M25
4 Lime Dosing Tank (LDT-01) 100 lit 1 HDPE
5 Alum Dosing Tank (ADT-01) 100 lit 1 HDPE
6 Poly Dosing Tank (PDT-01) 50 lit 1 HDPE
7 Sludge Drying Beds (SDBs-A/B) 2.0 x 3.0 2
Bk. Mas. With PCC
Bedding+ filling
Media
Stream II (High COD stream) 0.333 KLD
8 Collection Tank (CT-01) 10 KLD 1 RCC M25
RCC M25 = REINFORCED CEMENT CONCRETE (M 25 GRADE)
PCC = PLAIN CEMENT CONCRETE
HDPE = HIGH DENSITY POLY ETHELINE
BK.MAS. = BRICK MASONARY
ETP FLOW DIAGRAM
ANNEXURE-V
DETAILS OF HAZARDOUS WAST GENERATION & DISPOSAL
Sr.No
.
Type of
Hazardous
Waste
Hazardous
Waste
Category
Existing Qty.
MT/Month
Total proposed
Qty.
MT/MONTH
Mode of disposal
1. Discarded
Containers/
Bags/Liners
33.1 5 Nos
45 Nos.
50 Nos
200 nos.
Collection, Storage,
Transportation, Reuse/ Sale
to Authorized Vendor.
2. Used
Oil/Spent Oil
5.1 0.09 KL
0.200 KL Collection, Storage,
Transportation, Reuse or sale
to authorized reprocessors.
3. ETP Sludge 35.3 -- 1.0 Collection, Storage,
Transportation, disposal at
nearest TSDF site.
4 Process
Waste
-- 6.35 Collection, Storage,
Transportation, disposal at
nearest TSDF site or send to
Cement Industries for Co
Processing.
ANNEXURE-VI
DETAILS OF STACK AND VENTS
EXISTING (FLUE GAS EMISSION)
No Any Flue Gas /Process Gas Emission
PROPOSED (FLUE GAS EMISSION)
Sr.
No.
Stack
attached
to
Stack
Height
(Meter)
Fuel Fuel
Consumption
Concentration of
Pollutants
1. Thermic
Fluid Heate
4 Lac KCal
12 Natural Gas 30 M3/ Hr. PM:< 150 mg/Nm
3
SOX:<100 ppm
NOX:<50 ppm
ANNEXURE-VII
STORAGE DETAILS OF HAZARDOUS CHEMICALS
Sr.
No.
Raw Materials Storage (MT) Type of
Storage
No. of
Tank
1.0 Sorbitol 10KL HDPE Tank 1
2.0 Coconut Oil 10 KL HDPE Tank 2
3.0 Fatty Acid 10 Kl SS Tank 1
ANNEXURE-VIII
Plot Alotment Letter
ANNEXURE-IX
Membership of Common Effluent Treatment Plant (M/S. PANOLI ENVIRO TECHNOLGY LTD.)
ANNEXURE-X
GIDC: WATER SUPPLY LETTER
ANNEXURE-XI
TOPO SHEET
ANNEXURE-XII
SOCIO - ECONOMIC IMPACTS
1) EMPLOYMENT OPPORTUNITIES
The manpower requirement for the proposed expansion project is being expected to
generate some permanent jobs and secondary jobs for the operation and maintenance of
plant. This will increase direct / indirect employment opportunities and ancillary business
development to some extent for the local population.
This phase is expected to create a beneficial impact on the local socio-economic
environment.
2) INDUSTRIES
Required raw materials and skilled and unskilled laborers will be utilized maximum from the
local area. The increasing industrial activity will boost the commercial and economical status
of the locality, to some extent.
3) PUBLIC HEALTH
The company regularly examines, inspects and tests its emission from sources to make sure
that the emission is below the permissible limit. Hence, there will not be any significant
change in the status of sanitation and the community health of the area, as sufficient
measures have been taken and proposed under the EMP.
4) TRANSPORTATION AND COMMUNICATION
Since the existing factory is having proper linkage for the transport and communication, the
development of this project will not cause any additional impact.
In brief, as a result of the expansion there will be no adverse impact on sanitation,
communication and community health, as sufficient measures have been proposed to be
taken under the EMP. The proposed expansion is not expected to make any significant
change in the existing status of the socio - economic environment of this region.
ANNEXURE-XIII
PROPOSED TERMS OF REFERENCE FOR EIA STUDIES
1. Project Description
• Justification of project.
• Promoters and their back ground
• Project site location along with site map of 10 km area and site details providing various
industries, surface water bodies, forests etc.
• Project cost
• Regulatory framework
• Project location and Plant layout.
• Existing infrastructure facilities
• Water source and utilization including proposed water balance.
• Product spectrum (proposed products along with production capacity) and process
• List of hazardous chemicals with their toxicity levels.
• Mass balance of each product along with the batch size
• Existing environmental scenario
2. Description of the Environment and Baseline Data Collection
• Micrometeorological data for wind speed, direction, temperature, humidity and rainfall
in 5 km area.
• Study of Data from secondary sources.
• Other industries in the impact area
• Prevailing environment quality standards
• Existing environmental status Vis a Vis air, water, noise, soil in 5 km area from the project
site. For PM10, PM2.5, SO2, NOx.
• Ground water quality at 5 locations within 5 km.
• Complete water balance
3. Socio Economic Data
• Existing socio-economic status, land use pattern and infrastructure facilities available in
the study area were surveyed.
4. Impacts Identification And Mitigatory Measures
• Identification of impacting activities from the proposed project during construction and
operational phase.
• Impact on air and mitigation measures including green belt
• Impact on water environment and mitigation measures
• Soil pollution source and mitigation measures
• Noise generation and control.
• Solid waste quantification and disposal.
• Control of fugitive emissions
5. Environmental Management Plan
• Details of pollution control measures
• Environment management team
• Proposed schedule for environmental monitoring including post project
6. Risk Assessment
• Details on storage facilities
• Process safety, transportation, fire fighting systems, safety features and emergency
capabilities to be adopted.
• Identification of hazards
• Consequence analysis through occurrence & evaluation of incidents
• Recommendations on the basis of risk assessment done
• Disaster Management Plan.
7. Information for Control of Fugitive Emissions
8. Post Project Monitoring Plan for Air, Water, Soil and Noise.
9. Occupational Health and Safety Program for the Project.
10. Information on Rain Water Harvesting
11. Green Belt Develop