LIST OF ANNEXURES SR. NO. NAME OF ANNEXURE€¦ · 4 Mono Butyl Tin Oxide 0.75 MT/MONTH 2273-43-0...
Transcript of LIST OF ANNEXURES SR. NO. NAME OF ANNEXURE€¦ · 4 Mono Butyl Tin Oxide 0.75 MT/MONTH 2273-43-0...
LIST OF ANNEXURES
SR. NO. NAME OF ANNEXURE
I List of Products and Raw materials along with their Production Capacity
II Layout Map of the Plant
III Brief Manufacturing Process Description
IV Details of water consumption & waste water generation
V Details of Effluent Treatment Scheme
VI Details of Hazardous Waste Generation and Disposal
VII Details of Stacks and Vents, Fuel & Energy Requirements
VIII Details of Hazardous Chemicals Storage & Handling
IX Socio-economic Impacts
X Proposed Terms of Reference
XI Plot Allotment Letter
XII Copy of CC&A
ANNEXURE - I ____________________________________________________________________________ LIST OF PRODUCTS ALONG WITH THEIR PRODUCTION CAPACITY WITH RAW MATERIALS
SR. NO.
PRODUCT NAME Existing Capacity
(MT/Month)
Additional Capacity
(MT/Month)
Total Capacity
(MT/Month)
CAS Nos. LD50
1 BEES WAX 25 - 25 8012-89-3 --
2 PETROLIUM JELLY 100 - 100 8009-03-8 --
3 LIQUID PARAFIN 100 - 100 8012-95-1 --
4 EMULSIFYING WAX 50 - 50
8014-38-8 6772-27-0 68439-49-6 9004-99-3 123-94-4 25383-94-7 2197-63-9 9004-95-9
--
5 PETRO WAXES 23 - 23 6472-61-6 --
6 HARD PARAFFIN
WAX 30 - 30 8002-74-2 --
7 MICRO CRYSTALLINE
WAX 30 - 30 63231-60-7 --
8 GLYCERYL MONO
STEARATE 0 25 25 123-94-4 --
9 GLYCERYL COCOATE 0 25 25 8033-99-6 --
10 CEATO STEARYL
STEARATE 0 25 25 93820-97-4 --
11 STEARYL STEARATE 0 25 25 2778-96-3 --
12 CETYL RICINOELATE 0 25 25 --
13 CETYL PALMITATE 0 25 25 540-10-3 --
14 MYRISTRYL MYRISTATE
0 25 25 3234-85-3 --
15 CETYL OLEATE 0 25 25 22393-86-8 --
16
MYRISTYL STEARATE 0 25 25 177661-50-
56 --
17 SODIUM STEAROYL LACTYLATE
0 25 25 2583-94-7 --
18 CANDELILLA WAX 0 15 15 8006-44-8 --
19. COCOA BUTTER 0 10 10 8002-31-1 --
20. SHEA BUTTER 0 10 10 --
21 CARNAUBA WAX 0 15 15 --
22 VEGANCERAS NJ 0 15 15 --
23 VEGANCERAS SBW 0 25 25 --
24 VEGANCERAS DL 0 25 25 --
25 OZOKERITE WAX 0 25 25 --
26 CERESINE WAX 0 25 25 --
27 CHAPSTICK BASE 0 25 25 --
28 HARD FAT 0 25 25 --
29
EMULSIFYING OINTMENT
0 25 25
--
TOTAL 358 490 848
LIST OF RAW MATERIAL Existing Sr. No.
Name of the Raw Materials
Capacity QTY/M
Sr. No.
Name of the Raw Materials
Quantity CAS No
1 BEES WAX IP 25 Crud Bees Wax 35 MT/Month --
2 PETROLIUM JELLY
100 1 Micro Crystalline Wax 10 MT/Month 63231-60-7
2 Paraffin Wax 16 MT/Month 8002-74-2
3 White Oil 75 MT/Month 8042-47-5
3 LIQUID PARAFIN
100 1 Mineral Oil 101 MT/Month 8042-47-5
4 EMULSIFYING WAX
50 1 Cetearyl Alcohol (Palm Oil Based)
30 MT/Month 8005-44-5
2 Sodium Laural Sulphate 1.6 MT/Month 151-21-3
3 Cetearyl Alcohol (Palm Oil Based) PS Grade
8 MT/Month 67762-27-0 / 8005-44-5
Ceto macrol-1000-500 5.5 MT/Month --
4 Poly ethiline Glycol – 20 Stearat
1.1 MT/Month 9004-99-3
5 Glyceryl mono stearate 2.6 MT/Month 31566-31-1
6 Poly ethiline Glycol-100 Stearate
2.6 MT/Month 9004-99-3
5 PETRO WAXES 23 1 Slack Wax 26 MT/Month 64742-61-6
6 HARD PARAFFIN WAX
30 2 Paraffin Wax 31 MT/Month 8002-74-2
7 MICRO CRYSTALLINE WAX
30 1 Micro crystalline wax 19 MT/Month 63231-60-7
2 Slack Wax 12 MT/Month 64742-61-6
Proposed Sr. No.
Name of the Products
Capacity QTY/M
Sr. No.
Name of the Raw Materials
Quantity CAS No
8 GLYCERYL MONO STEARATE
25 1 Hydrogenated Palm Stearine
22 MT/Month 68514-74-9
2 Glycerine 3.5 MT/Month 56-81-5
3 Na(OH) Solution 5.0 LTR/MONTH 1310-73-2
9 GLYCERYL COCOATE
25 1 Coconut Fatty Acid
22 MT/Month 61788-47-4
2 Glycerin 3.5 MT/Month 56-81-5
3 Catalyst 0.75 MT/Month --
4 Na(OH) Solution 5.0 LTR/MONTH 1310-73-2
10 CEATO STEARYL STEARATE
25 1 Stearic Acid 12 MT/MONTH 57-11-4
2 Cetostearyl Alcohol
13 MT/MONTH 8005-44-5
3 Catalyst (Con. Sulphuric Acid)
1.25 MT/Month 7664-93-9
4 Mono Butyl Tin Oxide
0.75 MT/MONTH 2273-43-0
11 STEARYL STEARATE
25 1 Stearic Acid 13 MT/MONTH 57-11-4
2 Stearic Alcohol 12 MT/MONTH 112-92-5
3 Catalyst (Con. Sulphuric Acid)
1.25 LTR /Month 7664-93-9
4 Mono Butyl Tin Oxide
0.75 MT/MONTH 2273-43-0
12 CTETYL RICINOELATE
25 1 Cetyl Alcohol 13.25 MT/MONTH 36653-82-4
2 Ricinoelic Acid 12.5 MT/MONTH 141-22-0
3 Catalyst (Con. Sulphuric Acid)
1.25 LTR /Month 7664-93-9
4 Mono Butyl Tin Oxide
0.75 MT/MONTH 2273-43-0
13 CETYL PALMITATE
25 1 Cetyl Alcohol 12.5 MT/MONTH 36653-82-4
2 Palmitic Acid 12.5 MT/MONTH 57-10-3
3 Catalyst (Con. Sulphuric Acid)
1.25 LTR/Month 7664-93-9
4 Mono Butyl Tin Oxide
0.75 MT/MONTH 2273-43-0
14 MYRISTRYL MYRISTATE
25 1 Myristryl Alcohol 12.5 MT/MONTH 112-72-1
2 Myristic Acid 12.5 MT/MONTH 544-63-8
3 Catalyst (Con. Sulphuric Acid)
1.25 LTR /Month 0.75 MT/MONTH
7664-93-9
4 Mono Butyl Tin Oxide
2273-43-0
15 CETYL OLEATE 25 1 Cetyl Alcohol 12.5 MT/MONTH 36653-82-4
2 Oelic Acid 12.5 LTR /MONTH 112-80-1
3 Catalyst (Con. Sulphuric Acid)
1.25 LTR /Month 7664-93-9
4 Mono Butyl Tin Oxide
0.75 MT/MONTH 2273-43-0
16 MYRISTYL STEARATE
25 1 STEARYL ALCOHOL 12.5 MT/MONTH 112-92-5
2 Myristic Acid 12.5 MT/MONTH 544-63-8
17 SODIUM 25
STEAROYL LACTYLATE
18 CANDELILLA WAX
25 1 Crude Candelilla wax
27.5MT/MONTH 8006-44-8
19 COCOA BUTTER
25 1 Crude Cocoa Butter
27.5MT/MONTH 8002-31-1
20 SHEA BUTTER 25 1 Crude Shea Butter 27.5MT/MONTH 194043-92-0
21 CARNAUBA WAX
25 1 Crude Carnauba wax
27.5MT/MONTH 8
0
1
5
-
8
6
-
9
22 VEGANCERAS NJ
15 1 Vegetable wax 7.5MT/MONTH 8001-39-6
2 Sunflower Oil 7.5MT/MONTH 8001-21-6
23 VEGANCERAS SBW
25 1 Ceto Steryl Alcohol
12.5 MT/MONTH 67762-27-0
Stearic Acid 12.5 MT/MONTH 57-11-4
Vegetable wax 5.0 MT/MONTH 8001-39-6
24 VEGANCERAS DL
25 1 Castor oil 12.5MT/MONTH 8001-79-4
2 SG 12.5MT/MONTH --
25 OZOKERITE WAX
25 1 Paraffin wax 12.5MT/MONTH 8002-74-2
2 Microcrystalline wax
12.5MT/MONTH 84136-31-2
26 CERESINE WAX 25 1 Paraffin wax 12.5MT/MONTH 8002-74-2
2 Microcrystalline wax
12.5MT/MONTH 63231-60-7
27 CHAPSTICK BASE
25 1 Coconut Oil 12.4 MT/MONTH 8001-31-8
2 Microcrystalline Slack Wax
12.4MT/MONTH 63231-60-7
3 Paraffin Wax 0.05 MT/MONTH 8002-74-2
4 Ozokerite Wax 0.05 MT/MONTH 84136-31-2
5 Candelilla wax 0.05 MT/MONTH 8006-44-8
6 Carnauba Wax 0.05 MT/MONTH 8015-86-9
7 Sunflower Wax 0.05 MT/MONTH 1286686-34-7
28 HARD FAT 25 1 GLYCERYL MONO STEARATE
22.5 MT/MONTH 123-94-4
2 CAPRILYC CAPRIC TRIGLYCERIDE
2.5 MT/MONTH 73398-61-5
29 EMULSIFYING OINTMENT
25 1 Emulsifying Wax 7.5 MT/MONTH --
2 White Soft Paraffin
12.5 MT/MONTH 8002-74-2
3 Liquid Paraffin 5.0 MT/MONTH 8012-95-1
ANNEXURE - II ___________________________________________________________________________ LAYOUT OF MAP OF THE PLANT
ANNEXURE - III ___________________________________________________________________________ MANUFACTURING PROCESS, CHEMICAL REACTION & MASS BALANCE Existing: 1. Manufacturing Process:
This is a simple blending process where selected waxes and oils are blended in the blending
vessel with continuous stirring for 2 hours.
Upon completion of the blending, new wax compound is formed.
There are no bye products or waste materials generated in this process.
Mass Balance:
Process Flow Diagram of Bees Wax:
Process Flow Diagram of Petroleum Jelly:
Process Flow Diagram of Liquid Paraffin:
Process Flow Diagram of Emulsifying Wax:
Process Flow Diagram of Petro wax:
Process Flow Diagram of Hard Paraffin wax:
Process Flow Diagram of Microcrystalline wax:
Proposed: 2. Esters (240 MT/Year i.e. 20 MT/Month) - Proposed
a. Manufacturing Process:
In Esters manufacturing process basic reaction involves substitution of a hydroxyl group with
an alkyl. Typically acids are organic acids like oleaic acid, linolic acid etc. and the alkyl group
is contributed by alcohols, phenols etc. The reactions are typically catalyzed.
Side stream generated in these processes are non toxic and biodegradable. The
biodegradability of esters is one of the main plus points. Side stream is generally glycerin.
The plant will be suited for multipurpose ester production. The volume expected is in the
range of 240 MT/Year of finished products.
List of Products
Cetyl Palmitate
Stearyl Stearate
Cetyl Oleate
Myristyl Myristate
Ceto Stearyl Stearate
Cetyl Recinoleate
Glycerol Mono Stearate
Glyceryl Cocoate
Myristyl Stearate
Sodium Stearoyl Lactylate
Ester
Process Type 1:
INPUT QTY (Kgs) OUTPUT QTY (Kgs) REMARK
Vegetable Oils 1564.00 Ester 1000.00 Product
Alcohols# 582.00 Recover alcohol 515.00 recycle
Process waste 631.00 To Incinerator/
co-processing
Total 2146.00 Total 2146.00
Process Type 2:
INPUT QTY (Kgs) OUTPUT QTY (Kgs) REMARK
Fatty acid* 1089.00 Ester 1000.00 Product
Alcohols#
380.00 Recover alcohol 272.00 recycle
Process waste 51.00 To Incinerator/
co-processing Waste water 146.00 To ETP
Total 1469.00 Total 1469.00
Note: * Fatty acid can be anyone of Oleic acid, Lenolic acid, Palmitic acid, Stearic acid, Lauric
acid, Coconut fatty acid, Myristic acid, Caprylic Capric acid, 2-Ethyl hexanoic acid,
Trimellitic anhydride, Benzoic acid, Recinoleic acid
# Alcohol can be anyone of the list provided in Table below:
List of Alcohols
Sr. No.
Material Sr. No.
Material
1. Ethanol 2. Tridecanol
3. 2-Ethyl hexanol 4. Isotridecanol
5. Isopropanol 6. Cetyl alcohol
7. Trimethylolpropane 8. Stearyl alcohol
9. Pentaerythritol 10. Myristyl alcohol
11. Neopentyl glycol 12. Monoethylene glycol
13. Glycerol 14. Myristyl alcohol
15. Cetostearyl alcohol 16. C12-15 alcohol
17. Isodecanol
LIST OF RAW MATERIALS
Name of the product
Raw Materials
RM
Consumption (MT/MT)
RM
Consumption
(MT/Month)$
Esters (Proposed) (240 MT/Year)
Vegetable Oils 1.564 31.28
Fatty Acids 1.089 21.78
Alcohols# 0.582 11.64
$ Indicates the quantity of raw materials calculated based on annual production of the respective products. # indicates use of anyone alcohol from the list of alcohols.
CHEMICAL REACTIONS
C16H34O + C16H32O2 C32H64O2 + H2O Cetyl Alcohol Palmitic Acid Cetyl Palmitate Water C18H38O + C18H36O2 C36H72O2 + H2O Stearyl Alcohol Stearic Acid Stearyl Stearate Water C16H34O + C18H34O2 C34H66O2 + H2O Cetyl Alcohol Oleaic Acid Cetyl Oleate Water C14H30O + C14H28O2 C28H56O2 + H2O Myristyl Alcohol Myristic Acid Myristyl Myristate Water
CH3(CH2)nOH + C18H36O2 + H2O Ceto Stearyl Alcohol Stearic Acid Ceto Stearyl Stearate Water C16H34O + C18H34O3 C34H66O3 + H2O Cetyl Alcohol Ricinoleic Acid Cetyl Ricinoleate Water C3H8O3 + C18H36O2 C21H42O4 + H2O Glycerin Stearic Acid Glycerol Mono Stearate Water C3H8O3 + Coconut Fatty Acid + H2O Glycerin Glyceryl Cocoate Water C14H30O + C18H36O2 C32H64O2 + H2O Myristyl Alcohol Stearic Acid Myristyl Stearate Water 2C3H6O3 + C18H36O2 + NaOH C24H43NaO6 + 3H2O Lactic Acid Stearic Acid Sodium Hydroxide Sodium Stearoyl Lactylate Water
3. WAX BLENDS
b. Manufacturing Process:
This is a simple blending process where selected waxes and oils are blended in the
blending vessel with continuous stirring for 2 hours.
Upon completion of the blending, new wax compound is formed.
There are no bye products or waste materials generated in this process.
List of Products
Candelila Wax
Cocoa Butter
Shea Butter
Carnauba wax
Veganceras NJ
Veganceras SBW
Veganceras DL
Ozokerite wax
Ceresine wax
Chapstick Base
Hard Fat
Emulsifying Ointment
B. Process Flow Diagram
Waxes oils
Wax Blend
Reactor
Process Type 1:
INPUT QTY (Kgs) OUTPUT QTY (Kgs) REMARK
Waxes and oils 1000 Wax Blend 950 Product
Process skinning loss
100 Handling loss
Total 1000 Total 1000
List of waxes and oils
LIST OF RAW MATERIALS
Name of the product
Raw Materials
RM
Consumption (MT/MT)
RM
Consumption
(MT/Month)$
WAX BLENDS(existing )(190mt/annum)
waxes 1.10 33.11
Sr. No.
Material Sr. No.
Material
1. Crude Candelilla wax 2. Crude Cocoa Butter
3. Crude Shea Butter 4. Crude Carnauba Wax
5. Vegetable Wax 6. Sunflower Wax
7. Cetostearyl Alcohol 8. Stearic Acid 9. Castor oil 10. Ester gum
11. Paraffin Wax 12. Microcrystalline Wax 13. Coconut Oil 14. Ozokerite wax
14 Glyceryl Monostearate 15. Caprilyc Capric Triglyceride
16 Emulsifying Wax 17. White Soft Paraffin
18. Liquid Paraffin
Annexure -4 ___________________________________________________________________________ Details of Water Consumption and Wastewater generation Water Consumption and Wastewater generation (Existing)
Note: No change in Water Consumption and Wastewater generation in proposed scenario. Industrial wastewater is treated in ETP and treated wastewater is used in gardening. Domestic waste water is treated in septic tank & disposed in soak pit.
SR. NO.
SECTION (m3/day)
WATER CONSUMPTION
WASTE WATER GENERATION
1. Domestic 1.7 0.7
2. Process 0.6 0.2
3. Boiler 2.1 0.4
4. Cooling & Chilling 1.1 0.3
5. Washing 1.7 1.5
6. Gardening 0.0 0.0
Total 5.5 3.1
Water Balance (KL/Day):
All figures are in KL/day
Fresh Water: 5.5 KL/Day
Domestic: 1.7 Industrial: 3.8
0.7 KL/Day Septic tank & soak pit
Process: 0.6 Washing: 1.7 Boiler: 2.1 Cooling: 1.1
Process: 0.2 Washing: 1.5 Boiler: 0.4 Cooling: 0.3
ETP
Reuse in Gardening
Annexure -5: ___________________________________________________________________________ Details of ETP PROCESS DESCRIPTION: ETP (EFFLUENT TREATMENT PLANT)
The details of ETP are as follows.
Wastewater is collected in Collection tank and Equalization cum Neutralization Tank (ENT-
01) where the continuous addition and stirring of Caustic solution is done to maintain
neutral pH of wastewater from Caustic Dosing Tank (LDT-01) as per requirement by gravity.
Mixer is provided at bottom of the ENT-01 to keep all suspended solids in suspension and to
provide proper mixing by Mixing Mechanism (M-01).
Then after, neutralized wastewater is pumped to Primary Settling tank (PST-01). Alum and
Polyelectrolyte is dosed from Alum Dosing Tank (ADT-01) and Polyelectrolyte Dosing Tank
(PEDT-1) respectively by gravity into PST-01 to carry out coagulation by using a Mixer. Then
after, coagulated wastewater is settled in Primary Settling tank (PST-01). Clear supernatant
from PST-01 shall be sent to aeration tank and then pass through filter press. Clear
supernatant is reused for gardening purpose.
Effluent Treatment Plant (Dimension): SIZE OF TANKS
SR. NO. NAME OF THE UNIT CAPACITY NUBER OF UNIT
01 COLLECTION TANK 5 KL 01
02 EQUILIZATION TANK 5 KL 01
03 AERATION MOTOR 7.5 HP (WITH GEAR BOX) 01
04 FEEDING PUMP 5 HP 01
05 FILTER PRESS 30 PLATE (CLOTH FILTER) 01
Annexure -6 ___________________________________________________________________________Details of hazardous waste generation, storage & disposal
Note: No change in hazardous waste in proposed scenario.
SR.
NO.
NAME OF
WASTE
WASTE
CATEGORY
EXISTING
CAPACITY
PROPOSED
CAPACITY
TOTAL QTY.
MODE OF DISPOSAL
1 ETP Waste 35.3 6 MTA 0 6 MTA Collection, Storage,
Transportation & disposal in
TSDF of M/s. BEIL.
2 Process Waste 26.1 4.8 MTA 0 4.8 MTA Collection, Storage,
Transportation & incineration
at CHWIF of M/s. BEIL or sent
for co-processing in cement
industries.
3 Discarded
Containers
33.1 12,000
No./Y
0 12,000 No./Y Collection, Storage,
Transportation,
Decontamination & reuse or
given to registered vendors.
Annexure -7 ___________________________________________________________________________
Details of flue gas & proposed pollution control equipment
1) Flue Gas Stack
Note: Existing utility sufficient for manufacturing additional new products. * Fuel will be changed from fire wood to agro waste briquette in baby boiler.
2) Process Stack
SR. NO.
PROCESS STACK
ATTACHED TO
HEIGHT FROM
GROUND (m)
DIAMETER (m)
AIR POLLUTION CONTROL SYSTEM
EXPECTED POLLUTANTS
N. A. No process vent is required in existing and proposed scenario.
SR. NO.
STACKS ATTACHED TO HEIGHT FROM
GROUND LEVEL (m)
CONSUMPTION OF FUEL
(KL/hr)
DIAMETER (m)
EXPECTED POLLUTANTS
1 Baby Boiler & Thermic Fluid Heater
11 4.58 SCM/Hr Natural Gas
0.2 PM 150 mg/NM3 SO2 100 ppm NOx 50 ppm
2 Baby Boiler 11 10.41 KG/Hr
Fire Wood* 0.2
3 85 KVA (Stand-by DG set) 9 0.625 Lit/Hr.
Diesel
0.12
Annexure -8
Storage Details of Hazardous Chemicals
Sr.
No.
Name of the
Material
Kind of Storage Max.
quantity to
be stored
(MT)
Storage
condition
i.e. temp.,
pressure
Tank
Dimensions in
(m)
Dyke
Dimensions
1. Glycerine Drum 7 MT Room
temperature
NA NA
2. Fatty Acid Drum 10 MT Room
temperature
NA NA
3. Alcohol Drum 10 MT Room
temperature
NA NA
Annexure – 9
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 proposed 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 scenario is not expected to make any significant change
in the existing status of the socio - economic environment of this region.
Annexure-10 __________________________________________________________________________ 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.
Existing infrastructure facilities
Water source and utilization including proposed water balance.
List of Products & their capacity
Details of manufacturing process of proposed products
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 10 km area.
Existing environmental status Vis a Vis air, water, noise, soil in 10 km area from the project site.
Ground water quality at 8 locations within 10 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 • Objectives, Philosophy 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 • Recommendations on the basis of risk assessment done • Disaster Management Plan. 7. Information for Control of Fugitive Emissions
8. Information on Rain Water Harvesting
9. Green Belt Development plan
Annexure-11 __________________________________________________________________________ Plot Allotment Letter
Annexure-12 __________________________________________________________________________ Copy of CC&A