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PROPOSED EXPANSION OF
TPM TO 15750 TPM
PLANT (22 MW TO
M/s. PHILLIPS CARBON BLAC
Survey No. 47, SH
Dist: Kutch
FORM-I
For
EXPANSION OF CARBON BLACK (10950
TPM ) AND CO-GENERATION POWER
PLANT (22 MW TO 32 MW) IN EXISTING PREMISES
of
PHILLIPS CARBON BLACK LTD.
, SH – 46, Village: Mokha, Tal: Mundra
Kutchh-370421, Gujarat
Consultant
0
10950
GENERATION POWER
IN EXISTING PREMISES
Mundra,
1
APPENDIX I
(See paragraph - 6)
FORM 1
(I) Basic Information
Sr.
No.
Item Details
1. Name of the project/s PHILLIPS CARBON BLACK LTD.
2. S. No. in the schedule 5 (C)
3. Proposed capacity/area/length/tonnage to be
handled/command area/lease area/number of
wells to be drilled
Carbon Black = 15750 MT/Month
Co-Generation Power Plant =32 MW
For detail Please refer Annexure – I
Phase - I Carbon Black = 13350 MT/Month
Cogeneration = 26 MW
(50 mt/hr capacity boiler will be installed in 1st
phase)
Phase - II Carbon Black = 15750 MT/Month
Cogeneration = 32 MW
4. New/Expansion/Modernization Expansion
5. Existing Capacity/Area etc. Carbon Black = 10950 MT/Month
Co-Generation Power Plant = 22 MW
6. Category of Project i.e. ‘A’ or ‘B’ ‘A’
7. Does it attract the general condition? If yes,
please specify.
No
8. Does it attract the specific condition? If yes,
please specify.
No
9. Location
Plot/Survey/Khasra No. Survey No. 47
Village Mokha
Tehsil Mundra
District Kutchh
State Gujarat
10. Nearest railway station/airport along with
distance in kms.
Mundra: 14 Km
11. Nearest Town, city, District Headquarters along
with distance in kms.
Mundra: 14 Km
12. Village Panchayats, Zilla Parishad, Municipal
Corporation, local body (complete postal
address with telephone nos. to be given)
Mokha
13. Name of the applicant PHILLIPS CARBON BLACK LTD.
14. Registered Address Duncan House
31, Netaji Subhas Road,
Post Box No. 2229,
Kolkata – 700001
West Bengal
15. Address for correspondence: Survey No. 47, SH-46, Village: Mokha, Taluka:
Mundra, Dist: Kutchh.
PIN: 370421
Gujarat
2
Name Girish Singh
Designation (Owner/Partner/CEO) Chief Projects, Specialty Process & Technology
Address M/s. PHILLIPS CARBON BLACK LTD. Survey No. 47, SH-46, Village: Mokha, Taluka:
Mundra, Dist: Kutchh.
Pin Code 370421
E-mail [email protected]
Telephone No. +91 2838 619203
Fax No. +91 2838 283635
Mobile +91 9099069970
16. Details of Alternative Sites examined, if any.
Location of these sites should be shown on a
topo sheet.
NA
17. Interlinked Projects No
18. Whether separate application of interlinked
project has been submitted?
No
19. If yes, date of submission No
20. If no, reason No
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?
I The C.R.Z. Notification, 1991?
No
22. Whether there is any Government Order/Policy
relevant/relating to the site?
No
23. Forest land involved (hectares) No
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.
I 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.,)
3
(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 there of with approximate quantities
frates, wherever possible) with source of
information data
1.1 Permanent or temporary change in land
use, land cover or topography including
increase intensity of land use (with respect
to local land use plan)
No Proposed expansion is within existing unit
1.2 Clearance of existing land, vegetation and
Buildings?
No --
1.3 Creation of new land uses?
No The project site is located on level ground,
which does not require any major land filling
for area grading work.
1.4 Pre-construction investigations e.g. bore
Houses, soil testing?
No --
1.5 Construction works?
Yes For detail Please refer Annexure – II
1.6 Demolition works? No There will not be any demolition work at the
site.
1.7 Temporary sites used for construction
works or housing of construction workers?
No
1.8 Above ground buildings, structures or
earthworks including linear structures, cut
and fill or excavations
Yes For detail Please refer Annexure – II
1.9 Underground works mining or tunneling?
No
1.10 Reclamation works?
No
1.11 Dredging?
No
1.12 Off shore structures?
No
1.13 Production and manufacturing processes?
Yes For detail Please refer Annexure –III
1.14 Facilities for storage of goods or materials?
Yes Areas for storage of raw materials and
finished products will be developed for the
proposed expansion project.
1.15 Facilities for treatment or disposal of solid
waste or liquid effluents?
Yes Details of the Liquid Effluent is given as
Annexure – V and details of solid waste is
given as Annexure –VI.
1.16 Facilities for long term housing of
operational workers?
No
1.17 New road, rail or sea traffic during
Construction or Operation?
No
4
1.18 New road, rail, air waterborne or other
transport infrastructure including new or
altered routes and stations, ports, airports
etc?
No
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, culverting,
realignment or other changes to the
hydrology of watercourses or aquifers?
No
1.22 Stream crossings?
No
1.23 Abstraction or transfers of water form
ground or surface waters?
No
1.24 Changes in water bodies or the land
surface Affecting drainage or run-off?
No
1.25 Transport of personnel or materials for
construction, operation or
decommissioning?
Yes By road and sea
1.26 Long-term dismantling or decommissioning
or restoration works?
No
1.27 Ongoing activity during decommissioning
which could have an impact on the
environment?
No
1.28 Influx of people to an area either
temporarily or permanently?
No
1.29 Introduction of alien species? No
1.30 Loss of native species or genetic diversity? No
1.31 Any other actions? No
5
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
frates, wherever possible) with source of
information data
2.1 Land especially undeveloped or agricultural
land (ha)
No
2.2 Water (expected source & competing users)
unit: KLD
Yes Water requirement will be met through GWIL.
Water balance is given as Annexure – IV
2.3 Minerals (MT) No
2.4 Construction material – stone, aggregates,
and / soil (expected source – MT)
Yes Construction materials, like steel, cement,
crushed stones, sand, rubble, etc. required for
the project shall 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 Fuel
Existing:
LDO= 30 KL/Month (only for heating & cooling
during startup & stops)
HSD= 4 KL/Month
After Proposed Expansion:
LDO= 40 KL/Month (only for heating & cooling
during startup & stops)
HSD= 6 KL/Month
Energy :
Existing: 7 MW from own CPP
After Proposed Expansion:
Total: 9.5 MW from own CPP
Note: During start up & shut down PGVCL
power will be utilized.
2.7 Any other natural resources (use appropriate
standard units)
No
6
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 there of (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)
No --
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?
Yes Direct/Indirect employment
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 there of (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 –VI
4.4 Other industrial process wastes Yes Please refer Annexure –VI
4.5 Surplus product No
4.6 Sewage sludge or other sludge from effluent
treatment Yes
Please refer Annexure –VI
4.7 Construction or demolition wastes No
4.8 Redundant machinery or equipment Yes Please refer Annexure –VI
4.9 Contaminated soils or other materials No
4.10 Agricultural wastes No
4.11 Other solid wastes Yes Please refer Annexure –VI
7
5. Release of pollutants or any hazardous, toxic or noxious substances to air (Kg/hr)
Sr. No. Information/Checklist confirmation Yes/No Details there of (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 Please refer as Annexure – VII
5.2 Emissions from production processes Yes Please refer as Annexure – VII
5.3 Emissions from materials handling storage or
transport
Yes Please refer as Annexure – VII
5.4 Emissions from construction activities
including plant and equipment
No
5.5 Dust or odors 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 with
source of information data
6.1 From operation of equipment e.g. engines,
ventilation plant, crushers
Yes The Noise level is within the prescribed
limit. At noisy area, adequate preventive
& control measures are 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 is provided in unit
and also local ventilation system is
provided.
6.7 From any other sources No
8
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 there of (with approximate
quantities/rates, wherever possible) with
source of information data
7.1 From handling, storage, use or spillage of
hazardous materials
Yes Please refer as Annexure – VIII
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 and or into water
No
7.4 From any other sources No
7.5 Is there a risk of long term build up of
pollutants in the environment from these
sources?
No
8. Risk of accidents during construction or operation of the Project, which could affect human
health or the environment
Sr. No. Information/Checklist confirmation Yes/No Details there of (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 Please refer as Annexure – VIII
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 there of (with approximate
quantities/rates, wherever possible)
with source of information data
9.1 Lead to development of supporting. Lities, 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,
Yes For detail please refer Annexure – IX
9
10.Environmental Sensitivity
Sr. No.
Areas Name/
Identity
Aerial distance (within 15km.)
Proposed project location boundary
1 Areas protected under international
conventions, national or local legislation for
their ecological, landscape, cultural or other
related value
- No protected area within 10 km from
the proposed expansion project site.
2 Areas which important for are or sensitive
Ecol logical reasons – Wetlands,
watercourses or other water bodies, coastal
zone, biospheres, mountains, forests
Gulf of
Kutchh
Coastal water is 10.8 Km away from
the project site.
3 Area used by protected, important or
sensitive Species of flora or fauna for
breeding, nesting, foraging, resting, over
wintering, migration
- No protected area or sensitive
species within 10 km from the
proposed expansion project site.
4 Inland, coastal, marine or underground
waters
Gulf of
Kutchh
Coastal water is 10.8 Km away from
the project site.
5 State, National boundaries
- State boundary = 235 km
National boundary = 138 km
6 Routes or facilities used by the public for
access to recreation or other tourist, pilgrim
areas
- N.A.
7 Defense installations - N.A.
8 Densely populated or built-up area Mokha Mokha is around 1.9 km from the
proposed expansion project site.
9 Area occupied by sensitive man-made land
uses Hospitals, schools, places of worship,
community facilities)
- N.A.
10 Areas containing important, high quality or
scarce resources (ground water resources,
surface resources, forestry, agriculture,
fisheries, tourism, minerals)
- N.A.
etc.)
• housing development
• extractive industry
• supply industry
• other
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
10
11
LIST OF ANNEXURES
SR. NO. NAME OF ANNEXURE
I List of products with their production capacity
II Layout Map of the Plant
III Brief Manufacturing Process Description with Chemical and Mass Balance
IV Details of Water Consumption Wastewater Generation
V Effluent Treatment Scheme
VI Details of Hazardous /Solid Waste Generation, Handling and Disposal
VII Details of Air pollution Control System (Stack & Vent)
VIII Details of Storage of Hazardous Chemicals
IX Socio-economic Impacts
X Proposed Terms of Reference for EIA studies
12
ANNEXURE – 1
LIST OF PRODUCTS WITH THEIR PRODUCTION CAPACITY
SR.
NO. PRODUCT NAME
EXISTING
CAPACITY
ADDITIONAL
CAPACITY
TOTAL
( MT/MONTH )
1 Carbon Black
10950 Phase – I: 2400
Phase – II: 2400
Phase – I: 13350
Phase – II: 15750
2 Co-generation Power
(waste gas base)
22 MW
Phase – I: 2 MW
Phase – II: 6 MW
Phase – I: 24 MW
Phase – II: 32 MW
LIST OF RAW MATERIALS
SR.
NO. RAW MATERIAL NAME
EXISTING
CAPACITY
ADDITIONAL
CAPACITY
TOTAL
( MT/MONTH )
1
CBFS 19500 Phase – I: 4286
Phase – II: 4286
Phase – I: 23786
Phase – II: 28072
2
Molasses 66.66 Phase – I: 15
Phase – II: 15
Phase – I: 81.66
Phase – II: 96.66
3
Potassium Nitrate 5.5 Phase – I: 1.0
Phase – II: 1.0
Phase – I: 6.5
Phase – II: 7.5
13
ANNEXURE – 2
PLANT LAYOUT
14
ANNEXURE – 3
MANUFACTURING ACTIVITIES
Manufacturing Process Details
CARBON BLACK is manufactured from highly aromatic hydrocarbon oils, which are thermally cracked
at high temperature in specially designed reactor. The heat for this endothermic thermal cracking is
supplied by either burning of partial Carbon Black feedstock oil or auxiliary fuel oil with process air
inside the reactor itself or both. Carbon Black particles formed are recovered and converted into
pellets for ease of storage, handling and transportation.
The complete manufacturing process has following sections:
Feedstock storage and pumping
Reactor section
Process Bag Collector section
Pelletization and drying section
Vapor Bag Collector section
Conveying and storage section
Packing and dispatch section
Energy Conservation Section (CPP)
Utility section
A brief description of each section is given below to understand the process in totality.
Feedstock Storage And Pumping:
Carbon Black feedstock / auxiliary fuel received from the refineries or from coal tar distillation units
in road tankers are unloaded into the feedstock or auxiliary fuel storage tanks separately. Since the
feedstock is quite viscous in nature, special type of pumps and steam heating of the fluid is required
for ease of handling and pumping.
Feedstock is stored in large CS fixed roof tanks and maintained at about 60-80oC. temp. in the tank
through external steam heating or hot feedstock return from the plant.
Feedstock or auxiliary fuel is supplied to the plant at high pressure through pumps suitable for
handling high viscosity fluids. The feedstock is filtered through a line mesh strainers / filters to
remove extraneous materials.
Feedstock header pressure is maintained by automatic controls by means of suitable control valves
and controlling stations.
Reactor Section:
Various grades of Carbon Black which are mentioned below, can be produced in the oil FURNACE
BLACK PROCESS under varying reaction conditions.
N115 N121 N134 N220 N326 N330 N339 N375 P824 P1201
N550 P435 N650 N660 N774 N762 N772 N765
Preheated feedstock of about 250-350oC. is finally atomized and sprayed inside the reactor through
specially designed nozzles made of special material. The reaction chamber which is lined with high
temperature special refractory is at a temp. of approx. 2000oC - 2500
oC. at a pressure of
0.5kg./sq.cm.
15
Burning of auxiliary fuel and partial burning of feedstock oil in case of HB reactor in presence of air
inside the reactor raise the temp. to 2000 - 2500oooC and provide the endothermic heat for thermal
cracking reaction. The reaction products moving at very high velocities are quenched with water
sprays at predetermined locations inside the reactor to about 900 to 1100oC. Sufficient length of
refractory lined tunnel downstream of the reactors is provided for complete vaporization of quench
water. Energy from this hot stream is recovered by heat transfer from gases laden with carbon black
particles to cold air in a specially designed air pre heater. The hot air at 800-950oC. is used in the
reactor thereby making substantial savings in the fuel requirements in the reactor operation.
Feedstock oil is heated in SS heat exchangers for raising its temp. to 250-350 degree centigrade for
better atomization and hence increasing the process efficiency.
Product gases laden with Carbon Black particles (now hereafter referred as smoke) are cooled down
to 240-260 degree centigrade in a SS ventury cooler and they enter the PBC section for separation of
Carbon Black from gaseous products (a mixture of CO, CO2, CH4, C2H2, N2, H2, Air and water
vapors).
Process Bag Collector Section:
Process Bag Collector is Pulse Jet Filter and comprises of number of modular compartments.
Compartments are housed with very special type of filter bags made of fiber glass / Huyglass /
membrane coated fiber glass. The bags have only top opening and are fixed securely to the cell
plate along with venturi.
Smoke coming from reactor section at 240-260oC. enters the process bag collectors, CB particles are
deposited outside the bags and Clean gas filters off and goes to “off gas header”.
Cleaning of filter bag is done by high pressure air pulse. The deposited CB particles out side the filter
bags drop down into the hopper.
CB material collected in hoppers is conveyed through pneumatic conveying fans and Dense Bag
Collector to a surge tank for pelletizing and drying section. Before conveying, the material passes
through a micro pulverizer, which crushes some hard carbonaceous particles to – 325 mesh.
Off gases collected in the off gas header are sent to pelleting and drying section and energy
conservation section for their 100% utilization and thus eliminate the risk of atmospheric pollution.
Pelletizing and Drying Section:
Carbon Black material collected in a large SS316 L surge tank is sent to a pelletizer at a constant rate
through a variable speed rotary valve where it is mixed with water and molasses solution to form
strong wet pellets.
Pelletizer is specially designed equipment and is equipped with a rotating shaft fixed with sharp edge
pins in a double / triple helix configuration. The close gap between the pins and the inner smooth
surface of pelletizer accompanied by the conveying and rotating action of pins converts the mixture
of CB particles and water in to wet and strong spherical pellets.
These wet pellets are fed into a long rotary SS dryer. Pellets are dried inside the hot rotating dryer
by slow tumbling, agitating and falling action without damaging the pellets. Dryer shell is enclosed in
a refractory / Ceramic lined box all along its length and the heat is supplied by burning of off gases
received from the PBC section in a specially designed refractory lined combustion furnace.
Dry pellets with moisture less than 0.5% exit at the other end of the dryer for storage in the silos.
Modern techniques and reliable electronic instruments are used in this section to give a dried
pelleted product of consistent quality at all times and make the process smooth and efficient.
Vapor Bag Collector Section:
Water evaporated due to drying of wet pellets in the dryer along with some powdered material is
removed by a Vapor Fan at the feed end of the dryer. These hot gases are sent to a cylindrical bag
16
filter house called Vapor Bag Collector to remove and collect the CB particles and let out into the
atmosphere very clean, purge gases. Vapor Bag Collector is also equipped with special bags for
filtration of CB particles.
Carbon Black collected in the conical hopper is fed to the conveying line which gets mixed with the
main stream.
Conveying and Storage Section:
Dried pellets coming out at the exit end of the dryer are fed into a bucket elevator made of SS
buckets to carry the material to the top of the silos. The material can be fed into any of the silos via
SS screw conveyors located on the top of silos. These silos are made of MS but epoxy / SS lined from
inside to prevent contamination of product during storage.
Packing & Dispatch Section:
Material stored in the silos is packed in 25kg. paper bags / Bulk Bags through automatic packing
machines. The portable packing machines can be connected to any of the storage silos. Fully
automatic packing machine along with the moving roller conveyors and bag shapers make the
handling of paper bags very fast, convenient and clean. Packed bags are stacked on wooden pellets
in warehouse for storage and subsequent dispatch in trucks to the consumers.
Energy Conservation Section:
Low Btu off gases generated in the manufacturing process of CB in the reactor section and separated
from accompanying CB particles in PBC section are collected in the off gas header. In spite of their
low calorific value, these gases can be utilized to recover their calorific value in a specially designed
boiler system to generate high pressure steam and in a specially designed dryer combustor furnace
to supply the heat energy requirements in the pelletizing and drying section.
The quantum of high pressure steam which can be generated through burning of these off gases
meets the plant requirement of steam and power. Excess power generated is sent to the Grid.
So the benefit of above scheme is being fully taken care of by installing the following system:
1. High pressure boiler system
2. Turbo Generators
3. Power Export
High pressure boiler which can be run on a combination of off gases and fuel oil or Off gas alone
generates high pressure super heated steam at 85 kg./sq.cm.
This high-pressure steam is used to generate sufficient power required for plant consumption
through turbo generator system and excess power is sent to the Grid. The scheme also helps in
eliminating the atmospheric pollution problem which would have been caused had complete
utilization of off gas were not made.
Utilities Section:
Utilities section has following major systems which meet the requirement of various sections at
different locations:
a. Instrumentation Air System.
b. Compressed Air system at 7.0 kg./sq.cm. pressure.
c. Raw water
d. Fire fighting system
e. Cooling water system
f. De Minerlized water system
g. R O System
These systems are provided with necessary equipments eg. Pumps, blowers, compressors, tanks,
towers etc. as necessary.
Figure is a flow diagram for a typical one tread reactor unit.
Figure is a flow diagram for a typical one tread reactor unit.
17
18
There are many reactions occurring in the process after feedstock injection until the point of quenching. Note that the CO2 in the shift reaction and the consumption by CO2 reaction comes from the combustion of fuel in the combustion section of the reactor. These reactions are complicated and only a summary is listed below:
a. Dehydropenation of Oil
CXHY = X/8 C8H + (Y/2 -X/16) H2
Feedstock goes to carbon black plus hydrogen
b. Combustion of Oil
CXHY + (X/2 + Y/4) O2 = xCO + Y/2 H2O
Feedstock plus oxygen goes to carbon monoxide plus water
c. Methane Production
CXHY + (2X - Y/2) H2 = xCH4
Feedstock plus hydrogen goes to methane
d. Acetylene Production
CXHY+((X-Y)/2)H2 = X/2C2H2
Feedstock plus hydrogen goes to acetylene
e. Shift Reaction
CO2 + H2 = CO + H2O
Carbon dioxide plus hydrogen goes to carbon monoxide plus water
Carbon Black Consumption by CO2
8CO2= I6CO+I/2H2
Carbon black + carbon dioxide goes to carbon monoxide + hydrogen
g. Carbon Black Consumption by H2O
CaH + 8H2O = 8 CO + 8 1/2 H2
Carbon black + water goes to carbon monoxide plus hydrogen
h. Acetylene Consumption
4 C2H2 = CsH + 7/2 H2
Acetylene decomposes to carbon black and hydrogen
f.
19
Material Balance - Line-3
Description Unit Value
LINE CAPACITY Mt/d 160.00
CBFS (Primary Feed Stock) Mt/Mt CB 1.56
SFS (Secondary Feed Stock) Mt/Mt CB 0.21
Reactor Stage
Inputs
CBFS (Primary Feed Stock) Mt/d 249.60
SFS (Secondary Feed Stock) Mt/d 33.60
Air NM3/h 25000
NM3/d 600000
Mt/d 776.79
Atomizing Steam (Optional) Mt/d 14.40
Quench Water (DM / RO)) m3/d 200.00
Additive KNO3 mt/d 0.08
Atomizing Air Nm3/h 800
Nm3/day 19200
Mt/d 24.86
1274.47
Output
Carbon Black mt/d 160.00
Off Gas mt/d 1114.47
1274.47
Venturi Cooler Stage
Input
Carbon Black mt/d 160.00
Offgas mt/d 1114.47
Quench Water m3/d 72.00
1346.47
Output
Carbon Black mt/d 160.00
Offgas mt/d 1186.47
1346.47
PBC Stage
Input
Carbon Black mt/d 160.00
Offgas mt/d 1186.47
1346.47
Output
Carbon Black mt/d 160.00
20
Offgas to Dryer Comb. mt/d 189.84
Offgas to Boiler mt/d 996.64
1346.47
Dryer Comb. Stage
Input
Offgas mt/d 189.84
Air (100 % of offgas ) mt/d 243.53
433.36
Output
Flue Gas mt/d 433.36
Pelleting Stage
Input
Carbon Black mt/d 168.00
Water mt/d 167.20
Molasses mt/d 0.80
336.00
Output
Wet Carbon Black 336.00
Rotary Dryer
Input
Wet Carbon Black mt/d 336.00
Flue Gas mt/d 433.36
769.36
Output
Dry Carbon Black Pellets mt/d 160.00
Flow To VBC mt/d 262.67
To dryer Stack mt/d 346.69
769.36
Boiler
Input
Off Gas in mt/d 996.64
Air (100 % of offgas ) mt/d 1278.51
2275.15
Output
Flue Gas to Stack mt/d 2275.15
*****************************************************************************
21
ANNEXURE - IV
WATER CONSUMPTION AND WASTEWATER GENERATION
EXISTING:
ADDITIONAL PROPOSED:
TOTAL AFTER PROPOSED EXPANSION:
SR.
NO.
EXISTING (m3/day)
WATER
CONSUMPTION
WASTE WATER
GENERATION
1. Domestic 50 45
2. Process 604 Nil
3. Boiler 183 50
4. Cooling & Chilling 227 116
5. Washing 100 100
6. Gardening 36 Nil
Total 1200 311
SR.
NO.
PROPOSED SECTION (m3/day)
WATER
CONSUMPTION
WASTE WATER
GENERATION
1. Domestic 10 8
2. Process 500 Nil
3. Boiler 115 44
4. Cooling & Chilling 150 8
5. Washing 20 20
6. Gardening 34 Nil
Total 829 80
SR.
NO.
PROPOSED SECTION (m3/day)
WATER
CONSUMPTION
WASTE WATER
GENERATION
1. Domestic 60 53
2. Process 1104 Nil
3. Boiler 298 94
4. Cooling & Chilling 377 124
5. Washing 120 120
6. Gardening 70 Nil
Total 2029 391
22
WATER BALANCE DIAGRAM:
Total Water: 2029 KL/Day (Fresh: 1691 KL/Day +
Recycled: 338 KL/Day )
Process:
1104
KL/Day Cooling & Chilling:
377 KL/Day
(268 KL/Day
Recycled + 109
KL/Day Fresh)
Boiler (DM,
RO etc):
298 KL/Day
Washing:
120 KL/Day
Gardening:
70 KL/Day
(Recycled:
70 KL/Day)
Domestic
: 60
KL/Day
124
KL/Day
94
KL/Day 120 KL/Day
53 KL/Day: Septic
tank & Soak Pit 338 KL/Day � ETP
338 KL/Day
268
KL/Day
70
KL/Day
120
KL/Day
1104
KL/Day
109
KL/Day
298
KL/Day
0
KL/Day
60
KL/Day
253 KL/Day
Drift &
Evap loss
23
ANNEXURE - V
EFFLUENT TREATMENT PLANT
M/s. Phillips Carbon Black Ltd. shall have an Effluent treatment plant consisting of primary
and tertiary treatment units in existing and proposed ETP. The details of ETP are as follows.
� Effluent Treatment Plant (Line-1):
(A) Effluent Treatment Plant Units
Unit
no. Unit name Unit size
1 Equalization Tank 4.0 MX 3.0 M X (2.5 S.W.D + 0.75 /L + 0.5 F.B.)M
2 Oil & Grease Trap 2.0 M X 1.25 M X (1.7 S.W.D + 0.3 F.B.) M
3 Live Flash Mixer 0.75M X 0.75 M X (0.75 S.W.D + 0.25 F.B.) M
4 Alum Flash Mixer 0.75 M X 0.75 M X (0.75 S.W.D + 0.25 F.B.) M
5 Flocculator Chamber 1.5 M X 1.25 M X (1.5 S.W.D + 0.5 F.B.) M
6 Lamella Tube Settler 1.5 M X 1.25 M X (2.2 S.W.D + 0.3 F.B.) M
7 Cont Liver Platform 2.5 M+1.5 M
8 Intermediate Collection Tank 3.0 MX 3.0 M X (3.25 S.W.D + 0.5 F.B.) M
9 Filter Foundation 3.0 M X 1.5 MX 0.5 M
10 Sludge Drying Bed ( 4 Nos.) 2.0 M X 2.0 M X (1.2 S.W.D + 0.3 F.B.) M
11 Multi Grade Pressure Sand Filter 0.75M DIA X 2.0 M HT
12 Activated Carbon Filter 0.6 M DIA X 2.0 M HT
13 Raw Material Store 3.0 M X 4.0 MX 3.0 M
14 Hazardous Material Storage Room 3.0 MX4.0 MX 3.0 M
(B) Effluent Treatment Scheme:
We have installed Effluent Treatment Plant for the treatment of the wastewater generated
from the Industrial unit. Waste water is treated into Effluent Treatment Plant and around
24
70% treated effluent is recycled for cooling tower, compressors, blowers and remaining is
utilized for gardening and plantation purpose. Details of the same are as under.
Based on the fact that the generated wastewater mainly contains the oil and grease, the
following treatment scheme is given in ETP:
Based on quality of wastewater, we have installed only physiochemical treatment process,
in which the raw effluent is treated with chemicals like lime, alum and polyelectrolyte.
� The raw wastewater is entered into the oil and grease chamber which is provided with
baffle wall to remove oil and grease.
� Then after wastewater is collected into underground equalization tank, which is equipped
with air purging system to keep the particulate matter in suspension.
� An Effluent Transfer Pump is transferred the effluent from Equalization Tank to Flash Mixer
where simultaneously lime dosing takes place.
� From the Flash mixture the effluent is then transferred to the flocculation chamber where
gradual dosing of alum and polyelectrolyte is done. This Mixture is then transferred to
Primary Settling Tank.
� The sludge from Primary Settling Tank is transferred to the Sludge Drying Beds through
sludge sump. The sludge after drying is disposed off to secured Landfill site.
� Leachate from the Sludge Drying Beds is collected and directed to equalization tank for
further treatment.
25
.
.
Oil & Grease
Trap
Equalization
Tank Live fresh mixer Flocculation
chamber
lime Alum
Primary settling
Tank
Sludge Pump
Sludge Drying
beds.
Multi Grade
Pressure Sand
Filter
Activated Carbon
FilterTreated Water
Collection Tank
Reuse in Gardening and
Process
Treated Water Collection Tank
Leachate
Leachate
(C) Schematic Flow Diagram of Effluent Treatment Scheme:
26
Effluent Treatment Plant (Line-2):
(A) Effluent Treatment Plant Units
Sr.
No. Unit Qty.
Hydraulic
Volume,
(m3)
Overall Size
(m)
1. Oil & Grease Trap 1 12.0 4.0 x 2.0 x1.5 SWD+1.5 FB
2. Collection cum
Equalization Tank 2
48.0
(Each) 4.0 x 4.0 x3.0 SWD+1.5 FB
3. Chemical Solution Tanks 3 1.0
(Each) 1.0 x 1.0 x1.0 SWD+0.5 FB
4. Flash Mixing Tank 1 3.0 1.8 x 1.5 x1.1 SWD+0.4 FB
5. Flocculation Tank 1 10.0 2.25 x 2.25 x2.0 SWD+0.4 FB
6. Primary Clarifier 1 126.0 8.0 Φ x 2.5 SWD+0.3 FB+0.6 SD
7. Sludge collection tank 1 9.0 3.0 x 2.0 x 1.5 SWD+0.5 FB
8. Primary Treated effluent
collection tank 1 48.0 4.0 x 4.0 x 3.0 SWD+0.5 FB
9. Final Treated Effluent
Collection Tank 1 48.0 4.0 x 4.0 x 3.0 SWD+0.5 FB
10. Sludge Drying Beds 8 4.5 (Each) 3.0 x3.0 x 1.5
11. Leachate collection tank 1 2.4 1.2 x 2.0 x 1.0 SWD+1.5 FB
(B) Effluent Treatment Scheme:
Effluent Treatment Plant consists of primary with physico-chemical treatment followed by
sludge settling and tertiary treatment to achieve the discharge norms prescribed by GPCB
for the treated effluent. The detailed effluent treatment scheme is given hereunder.
� OIL AND GREASE TRAP
The wastewater generated from various processes is first passed through oil & Grease
chamber where emulsified oil, grease and other floating matter is removed/skimmed off
manually.
� COLLECTION CUM EQUALIZATION TANK
After removal of oil and floating matter, effluent is collected in collection cum equalization
tank through network of pipe by means of gravity. The effluent is thoroughly mixed by
27
supplying compressed air through aeration grid placed at the bottom of the tank. Lime is
added to the effluent as a coagulant in this tank. The effluent is then pumped to the Flash
Mixing Tank.
� CHEMICAL DOSING TANKS
The chemical dosing tanks are provided for the preparation of chemical solution required
for the primary treatment such as hydrated lime, alum and polyelectrolyte.
� FLASH MIXING TANK
Alum solution is added to the effluent in the flash mixer. Here coagulants are properly
mixed with the effluent by means of stirrer. Effluent is then flow by gravity into the
Flocculator.
� FLOCCULATOR
Polyelectrolyte solution is added as a flocculent in this tank. It helps to form large and dense
flocs of settlable solids which can easily settle. From here all the mass is taken by gravity
into the primary clarifier.
� PRIMARY CLARIFIER
The effluent from flocculation tank is flow by gravity to Primary clarifier. Here the effluent is
retained for certain period in a relatively quiescent state. Thus, chemical flocs are settled
down at the tank bottom. The settled sludge from bottom is drained to the sludge drying
bed.
� PRIMARY TREATED WATER COLLECTION TANK
The clear supernatant effluent from clarifier tank overflow is collected here for further
polishing tertiary treatment. From this tank, effluent is pumped to the Pressure Sand Filter
by means of high pressure pump.
� PRESSURE SAND FILTER
Pressure Sand Filter consists of graded quartz free sand supported on gravel and pebble
bed. This acts as a packing material and also protect the under drainage system. Here
remaining suspended solids are removed from the effluent. Pressure sand filter needs to be
cleaned periodically to remove accumulated solids. This is done by backwashing the filter
28
using fresh water in reverse flow sequence. The backwash water flows back to collection
cum equalization tank for treatment.
� ACTIVATED CARBON FILTER
Activated Carbon Filter consists of bed made of coconut shell based activated carbon. The
carbon bed is provided over the sand bed and is supported on gravel and pebble bed. This
acts as a packing material and protect the under drainage system. The effluent from the
outlet of pressure sand filter is passed through activated carbon filter where final polishing
of the effluent is done to remove the suspended solids, color, odour and other organic
impurities. Activated carbon filter needs to be cleaned periodically to remove accumulated
solids. This is done by backwashing the filter using fresh water in reverse flow sequence. The
backwash water flows back to collection cum equalization tank for treatment.
� FINAL TREATED WATER COLLECTION TANK
Treated effluent from tertiary treatment is collected in this tank and is utilized for land
irrigation within premises.
� SLUDGE DRYING BEDS
The settled sludge at the bottom of primary clarifier tank is drained into Sludge drying beds.
Here water from the sludge is filtered through the bed and filtrate is taken back to the
collection cum equalization tank for further treatment. The sludge after drying is collected
and stored in to hazardous water storage area and ultimately disposed of at hazardous
waste disposal site.
29
ETP FLOW DIAGRAM
30
Characteristics of Effluent
Date of Sampling : 24/06/2015
Sr. No Parameters Result of Phase-I
Plant
Result of Phase-II Plant GPCB Norms
Raw
Inlet
Treated
Outlet
Raw
Inlet
Treated
Outlet
1. pH 6.67 7.32 7.1 7.34 6.5 to 8.5
2. Temperature, °C 32 32 32 32 40
3. Color, Pt.Co. Scale 1 1 1 1 100
4. Suspended Solids, mg/L 172 90 233.2 85 100
5. Total Dissolve Solids, mg/L 1744.25 2080.4 2530 2030 2100
6. COD, mg/L 144.312 94.312 268.088 88.624 100
7. BOD3, mg/L 45.20 25.42 40.49 22.29 30
8. Chlorides, mg/L 1408.358 587.106 1462.525 592.52 600
9. Sulphates, mg/L 268.875 236.61 243.063 162.4005 1000
10. Oil & Grease, mg/L 8.0 2.0 7.2 1.0 10
11. Ammonical Nitrogen, mg/L 50.4 10.08 42.56 12.88 50
12. Total Chromium, mg/L BDL BDL BDL BDL 0.2
13. Hexavelent Chromium,
mg/L
BDL BDL BDL BDL 0.1
14. Copper, mg/L BDL BDL BDL BDL 1.0
15. Iron, mg/L BDL BDL BDL BDL 1.0
16. Phenolic compounds,
mg/L 1.2 0.7 1 0.54
1.0
17. Sodium Absorption Ratio 22.71 19.34 29.87 19.2 26
18. % Na 58.28 55.88 57.36 52.01 60 %
31
ANNEXURE-VI
DETAILS OF HAZARDOUS & SOLID WASTE GENERATION & DISPOSAL
SR.
NO.
NAME OF
WASTE
WASTE
CATEGORY
EXISTING QTY.
MT/YEAR
ADDITIONAL
QTY.
MT/YEAR
TOTAL MODE OF DISPOSAL
1 Used Oil I-5.1 1.56 0.64 2.20 Collection, Storage,
Transportation, reuse
in process/sent to
GPCB registered
recycler
2 Spent Acid from
Batteries
I-36.3 0.024 0.00 0.024 Collection, Storage,
Transportation,
Disposal by Authorized
way
3 Chemical Sludge
from Waste water
treatment
I-34.3 27.00 8 35 Collection, Storage,
Transportation,
Disposal at TSDF site
of SEPPL.
4 Oily Sludge
Emulsion
I-4.1 6.0 0 6 Collection, Storage,
Transportation,
Disposal at Common
Incineration site of
SEPPL – Bhachau
5 Used Batteries 17 0.1
(CCA
Amendment
Applied)
0 0.1 Collection, Storage,
Transportation, and
Disposal as per lead
batteries rules.
6 Discarded Drum /
Barrels/
Containers / Bags/
Liners
33.3 8
(CCA
Amendment
Applied)
4 12 Collection, Storage,
Transportation, sent to
GPCB Approved
recycler
32
7 Plastic Waste X-9 0.5
(CCA
Amendment
Applied)
0.5 1 Collection, Storage,
Transportation, sent to
GPCB Approved
recycler.
8 Spent Ion
Exchange Resin
34.2 0.4
(CCA
Amendment
Applied)
0.2 0.6 Collection, Storage,
Transportation,
Disposal at TSDF site.
9 Oily Cotton Waste
/Leather Hand
Gloves / Cotton
Hand Gloves
33.2 0.4
(CCA
Amendment
Applied)
0.1 0.5 Collection, Storage,
Transportation, and
Disposal by
incineration at SEPPL –
Bhachau.
10 E-Waste 18.5 0.5
(CCA
Amendment
Applied)
0.2 0.7 Collection, Storage,
Transportation, sent to
GPCB Approved
Recycler
11 Waste Insulation
Material
- 1
(CCA
Amendment
Applied)
0.5 1.5 Collection, Storage,
Transportation, and
Disposal by
incineration at SEPPL –
Bhachau
33
ANNEXURE-VII
DETAILS OF AIR POLLUTION CONTROL SYSTEM
1) Flue Gas Stack (Existing)
Note: Process Flare Stack is used only in case of emergency.
2) Process Stack (Existing)
SR.
NO.
PROCESS STACK
ATTACHED TO
HEIGHT FROM
GROUND (m)
DIAMETER
(m)
AIR POLLUTION
CONTROL SYSTEM
EXPECTED
POLLUTANTS
1 VBC- 1 50 1.0 Bag Filter SPM,SOx, NOx
2 VBC- 2 50 1.0 Bag Filter SPM, SOx, NOx
3 Dryer -1 50 1.1 Bag Filter SPM, SOx, NOx
4 Dryer -2 50 1.1 Bag Filter SPM, SOX, NOx
3. Flue Gas Stack (Proposed):
4. Process Stack (Proposed)
SR.
NO.
PROCESS
STACK
ATTACHED TO
HEIGHT
FROM
GROUND (m)
DIAMETER
(m)
AIR
POLLUTION
CONTROL
SYSTEM
EXPECTED
POLLUTANTS
1 VBC- 3 50 1.0 Bag Filter SPM, SOX, NOx
2 Dryer -3 50 1.1 Bag Filter SPM, SOx, NOx
SR.
NO. STACKS ATTACHED TO
HEIGHT FROM
GROUND LEVEL (m)
CONSUMPTION
OF FUEL
(KL/hr)
DIAMETER
(m)
EXPECTED
POLLUTANTS
1 Process Plant –Flare stack 50 NIL 1.0 SPM, SOx, NOx
2 CPP 16MW–Boiler Chimney 80 Nil 2.5 SPM, SOx, NOx
3 CPP 6MW–Boiler Chimney 80 Nil 1.8 SPM, SOx, NOx
SR.
NO. STACKS ATTACHED TO
HEIGHT FROM
GROUND LEVEL (m)
CONSUMPTION
OF FUEL
(KL/hr)
DIAMETER
(m)
EXPECTED
POLLUTANTS
1 Process Plant –Flare stack 50 Nil 1.5 SPM, SOx, NOx
2 CPP 8 MW–Boiler Chimney 80 Nil 1.8 SPM, SOx, NOx
34
Total:
1) Flue Gas Stack
2) Process Stack
SR.
NO.
PROCESS STACK
ATTACHED TO
HEIGHT FROM
GROUND (m)
DIAMETER
(m)
AIR POLLUTION
CONTROL SYSTEM
EXPECTED
POLLUTANTS
1 VBC- 1 (Existing) 50 1.0 Bag Filter SPM, SOx, Nox
2 VBC- 2 (Existing) 50 1.0 Bag Filter SPM, SOx, Nox
3 Dryer -1 (Existing) 50 1.1 Bag Filter SPM, SOx, Nox
4 Dryer -2 (Existing) 50 1.1 Bag Filter SPM, SOx, Nox
5 VBC- 3 (Proposed) 50 1.0 Bag Filter SPM, SOx, Nox
6 Dryer -3 (Proposed) 50 1.1 Bag Filter SPM, SOx, Nox
SR.
NO. STACKS ATTACHED TO
HEIGHT FROM
GROUND LEVEL (m)
CONSUMPTION
OF FUEL
(KL/hr)
DIAMETER
(m)
EXPECTED
POLLUTANTS
1 Process Plant –Flare stack
(Existing)
50 Nil 1.0 SPM, SOx, NOx
1 Process Plant –Flare stack
(Proposed)
50 Nil 1.5 SPM, SOx, NOx
3 CPP 16 MW–Boiler Chimney
(Existing)
80 Nil 2.5 SPM, SOx, Nox
4 CPP 6 MW–Boiler Chimney
(Existing)
80 Nil 1.8 SPM, SOx, Nox
5 CPP 8 MW–Boiler Chimney
(Proposed)
80 Nil 1.8 SPM, SOx, Nox
35
Flue Gas/Process Stack Analysis Report
1st
Analysis Results
Sr. No.
Parameters GPCB limit Results
Flare Stack Boiler
(6 MW)
Boiler
(16MW)
D.G. Set
1. Particulate Matter 150 mg/NM3 127 141 79 121
2. SO2 100 ppm 19.87 25.56 38.35 4.56
3. NOx 50 ppm 11.3 12.64 10.87 3.35
2nd
Analysis Results
Sr. No.
Parameters GPCB limit Results
Drier 1
Drier 2
VBC 1
VBC 2
1. Particulate Matter 150 mg/NM3 140 79 85 77
2. SO2 100 ppm 42 47 57 50
3. NOx 50 ppm 8.9 7.8 9.7 8.1
36
ANNEXURE – VIII
DETAILS OF HAZARDOUS CHEMICALS (EXISTING + PROPOSED)
Sr.
No
.
Name of
the
Material
Type of
Hazard
Kind of
Storage
Max.
quantity
to be
stored
(MT)
Storage
condition
i.e. temp.,
pressure
Tank
Dimensions in
(m)
Dyke
Dimensions
(m)
1 Caustic
Soda
Health
Hazard
Horizontal
cylindrical
Tank
17 Ambient &
Atmospheric
2.4 mtr dia x 3.77
mtr lenght
6.25 x 3.27 x 0.23
2 Hydrochlo
ric Acid
Health
Hazard
Horizontal
cylindrical
Tank
13 Ambient &
Atmospheric
2 mtr dia x 4.15
mtr lenght
6.51 x 6.35 x 0.23
3 CBSF OIL Fire
Hazard
Fixed Roof
Cylindrical
32400 80 &
Atmospheric
1. 9000 KL
x2 = dia
25 x ht
18 mtr
2. 2300
KLx6 =
dia 13 x
ht 18
mtr
3. 600 kl x1
= dia 8.0
x ht 11
mtr
90 x 90 x 1.2 mtr
4 LDO Fire
Hazard
Fixed Roof
Cylindrical
136 Ambient &
Atmospheric
dia 5.4 x
ht 6.0
mtr
5 HSD Fire
Hazard
Fixed Roof
Cylindrical
35 Ambient &
Atmospheric
dia 3.0 x
ht 5.0
mtr
37
ANNEXURE – IX
SOCIO - ECONOMIC IMPACTS
1) Employment Opportunities
The manpower requirement for the proposed 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.
38
ANNEXURE-X
______________________________________________________________________
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 5 km area and site details providing various industries,
surface water bodies, forests etc.
• Project cost
• Project location and Plant layout.
• Water source and utilization including proposed water balance.
• Product spectrum (proposed products along with production capacity) and process
• List of hazardous chemicals.
• Mass balance of each product
• Storage and Transportation of raw materials and products.
2. Description of the Environment and Baseline Data Collection
• Micrometeorological data for wind speed, direction, temperature, humidity and rainfall in 5 km
area.
• Existing environmental status Vis a Vis air, water, noise, soil in 5 km area from the project site. For
SPM, RSPM, 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.
5. Environmental Management Plan
• Details of pollution control measures
• Environment management team
• Proposed schedule for environmental monitoring including post project
6. Risk Assessment
• Objectives and methodology of 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
• Disaster Management Plan.
39
7. Information for Control of Fugitive Emissions
8. Post Project Monitoring Plan for Air, Water, Soil and Noise.
9. Information on Rain Water Harvesting
10. Green Belt Development plan
