01.project feasibility report - welcome to...
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PRE FEASIBILITY REPORT
FOR
PROPOSED PESTICIDE INTERMEDIATES AND
SPECIALTY CHEMICALS IN EXISTING UNIT
OF
M/s. ACETO CHEM PVT. LTD. (UNIT-II)
PLOT NO. 274/3/1, GIDC ESTATE, PANDESARA,
DIST: SURAT – 394 221, GUJARAT
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CONTENTS
Sr.
No.
Description Page No.
1. Executive Summary 3
2. Introduction of the Project/Background information 9
3. Project Description 10
4. Site Analysis 16
5. Planning Brief 17
6. Proposed Infrastructure 17
7. Rehabilitation and resettlement (R & R) Plan 18
8. Project Schedule & Cost Estimates 19
9. Analysis of Proposal (Final Recommendations) 19
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1.0 EXECUTIVE SUMMARY
1.1 Company Profile
Introduction
M/s. Aceto Chem Pvt. Ltd., established in the year 1976 under the charismatic leadership of Mr.
Jitendra P. Parmar & Mr. Bansilal D. Patel engaged in the manufacturing & marketing of Dyes
Intermediates for Food Color and textiles.
The company has since consolidated its position as major entity. Under the charismatic leadership of
Mr. Jitendra P. Parmar and Mr. Bansilal D. Patel, the company has become a strong force to reckon
with.
In spite of market fluctuations, the company is reporting steady and dynamic progress year after
year. Thanks to our philosophy of believing in team spirit, quality consciousness, innovative
approach, market awareness and foresightedness, we have established a name of repute amongst
our domestic and international clientele.
We started our exports in 1980 and since then gradually expanding our network in various
countries. Currently, we are exporting our products to various European countries besides USA,
Argentina, Brazil, Egypt, South Africa, Japan, Taiwan, Korea, etc.
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1.2 Project Details
Sr.
No. Product Name
Production
Existing Proposed Total
MT/Month MT/Month
1 Nytrosyl Sulphuric Acid (from Sulfur) * 132.08 132.08
2 Nytrosyl Sulphuric Acid (from Sodium Thio
Sulphate Solution and Spent Acid (H2SO4)) ** 468 468
3.1 4-Methoxy Acetophenone 0 60
3.2 4-Methyl Acetophenone
4.1 Diethyl Ketone
0 100 4.2 Methyl Propyl Ketone
4.3 Dipropyl Ketone
4.4 Propiophenone
5 Alpha Nitro Napthalene 0 100
6 Alpha Napthylamine 0 165
7 Phenyl Alpha Naphthylamine (PANA) 0 90
8 Epichlorohydrin Based Polyamide resin 0 116
9 3,5-Dichloroaniline 0 50
10 Bis-(2-Chloroethyl)-amine 0 30
Total 600.08 1311.08
By Products
1 Sulphur 50.74 50.74
2 Sodium Sulphate 242.728 242.728
3 Di Ethyl Ketone Nil 79
4 Acetic Acid Nil 30.5
1.3 Green Belt Development
Company has developed an effective green belt within the factory and on periphery of the factory.
In addition to this, majority of the vacant land shall be planted with trees, shrubs and grasses.
1.4 Power & Fuel Requirement
Fuel
Natural Gas: 82 SCM/day (Existing)
Diesel: 30 Lit/Hr (Existing)
Natural Gas: 82 SCM/day (Total Proposed)
Diesel: 75 Lit/Hr (Total Proposed)
Energy:
90 HP from DGVCL
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1.5 Water Requirement and Wastewater Generation & Treatment
Source of water will be met through Surat Municipal Corporation. Total water requirement will be
65 m3/day (Existing: 25.5 m
3/day + Additional Proposed: 39.5 m
3/day). The total wastewater
generations will be 24.0 m3/day (Existing: 7.0 m
3/day + Additional Proposed: 17.0 m
3/day). Total
24.0 m3/day (14 m3/day Industrial + 10 m
3/day domestic) of effluent shall be generated, out of
which 14 KL/Day waste water generated from process (from manufacturing of 3, 5, DCA), cooling,
washing & Scrubber shall be treated in ETP and the treated effluent shall be reused in to utilities.
About 14 KL/Day of Condensate water (is generated only from the manufacturing of Nytrosyl
Sulphuric Acid (from spent sodium thio sulphate solution and Spent H2SO4 (as a raw material)) is
recycled back in to cooling tower.
1.6 Air Pollution Source and Control Management
The source of air pollution due to the project will be Flue gas emission & Process Vents.
FLUE GAS EMISSION
Sr.
No. Stack Attached To Stack Height
Fuel
Consumption Air Pollution Control System
A EXISTING
1. Thermo pack Unit
Cap.: 600 U
Height - 12 Meter Natural Gas
82 SCM/Hr.
As Natural Gas is used as a fuel,
adequate stack height is provided.
2. D. G. Set (Stand By)
Capacity: 250 KVA
HEIGHT - 7 Meter Diesel:
30 Liter/Hr.
As Diesel is used as a fuel, adequate
stack height is provided.
B ADDITIONAL
1. D. G. Set (Stand By)
Capacity: 365 KVA *
HEIGHT - 7 Meter Diesel:
45 Liter/Hr.
As Diesel shall be used as a fuel,
adequate stack height is provided.
* Industry shall remove the existing D. G. Set having capacity of 250 KVA and will install D. G. Set
having capacity of 365 KVA.
C PROPOSED TOTAL
1. Thermo pack Unit Height - 12 Meter Natural Gas: As Natural Gas is used as a fuel,
adequate stack height is provided.
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1.7 Hazardous Waste Management
Cap.: 600 U 82 SCM/Hr.
2. D. G. Set (Stand By)
Capacity: 365 KVA
HEIGHT - 7 Meter Diesel:
45 Liter/Hr.
As Diesel shall be used as a fuel,
adequate stack height is provided.
PROCESS GAS EMISSION
Sr.
No. Vent Attached To
Vent Height &
Diameter Pollutants Air Pollution Control System
A Existing
1. Acidification Vessels
12 Meter SO2
Two Stage Scrubber (i.e. Ventury
Scrubber & Vertical column packed
scrubber) is provided. 2. Acidification Vessels
B Additional
There shall be no change in existing process gas emission.
CAT.
NO.
TYPE OF SOLID /
HAZARDOUS
WASTES
SOURCE OF
WASTE
QUANTITY GENERATED
METHOD OF DISPOSAL
Existing Additional Proposed Total
5.1 Used Oil Plant and
Machinery
0.085 MT/Year
i. e.
100 Liters/Year
Nil 0.085 MT/Year
i. e.
100 Liters/Year
Collection / Storage /
Transportation / sent
to registered recycler
33.1 Discarded
containers /
barrels / liners/
Carboys/bags
Raw
material
packaging
4.8 MT/Year
i. e.
600 Nos/Year
1.6 MT/Year
i. e.
200 Nos/Year
6.4 MT/Year
i. e.
800 Nos/Month
Collection / Storage /
Transportation /
Supplier / sent to
registered recycler
35.3 ETP Sludge From ETP 100 Kg/Year 500 Kg/Year 600 Kg/Year Collection / Storage /
Transportation / sent
to TSDF site for
secured Land Filling
29.5 Catalyst From
Process
Nil 4.1 MT/Month 4.1 MT/Month Collection / Storage /
Transportation /
Given back to
manufacturer for re-
generation
Catalyst shall be generated from the manufacturing of 4 - Methoxy Acetophenone, 4-Methyl Acetophenone &
Alpha Napthylamine.
29.6 Spent Acid
(H2SO4)
---- 286 MT/Month Nil 286 MT/Month * Reception / Storage /
Transportation / used
as a raw material for
the manufacturing of
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Nytrosyl Sulphuric Acid
(from Sodium Thio
Sulphate Solution and
Spent Acid (H2SO4))
From
manufacturi
ng of 3,5-
Dichloroanili
ne
Nil 224 MT/Month 224 MT/Month Reuse for the
manufacturing of
Nytrosyl Sulphuric
Acid (from Sodium
Thio Sulphate
Solution and Spent
Acid (H2SO4))
--- Sodium Thio
Sulfate Solution
---- 501 MT/Month Nil 501 MT/Month* Reception / Usage /
Storage /
Transportation / use
as a raw material for
the manufacturing
of Nytrosyl Sulphuric
Acid (from Sodium
Thio Sulphate
Solution and Spent
Acid (H2SO4))
From
manufacturi
ng of 3,5-
Dichloroanili
ne
Nil 384 MT/Month 384 MT/Month Reuse for the
manufacturing of
Nytrosyl Sulphuric
Acid (from Sodium
Thio Sulphate
Solution and Spent
Acid (H2SO4)) / 3, 5
DCA
* Presently, Industry has applied under the Rule 11 [i.e. utilization of the hazardous wastes as a supplementary
resource or for energy recovery, or after processing under Rule 11 of the Hazardous Waste (Management,
Handling & Transboundary) Rules, 2008] for the reception (from actual generator) & usage of Spent H2SO4 &
Spent Sodium Thio Sulphate Solution as a raw material for the manufacturing of Nytrosyl Sulphuric Acid from
Sodium Thio Sulphate Solution & Spent H2SO4 on dated 9/3/2016. Permission for the same is awaited.
Now as per proposed proposal, industry has proposed to manufacture about 50 MT/Day of 3, 5 Di Chloro
Aniline. From the manufacturing of this product Spent H2SO4 and Spent Sodium Thio Sulphate Solution shall be
generate. If industry will manufacture 3, 5 Di Chloro Aniline within premises, in such case industry will receipt
the balance quantity (as per manufacturing of 3, 5, Di Chloro Aniline quantity). If industry will manufacture 50
MT/Day of 3, 5 Di Chloro Aniline, than industry will receipt about balance quantity i. e. 62 MT/Month of Spent
H2 SO4 and 117 MT/Month of Spent Sodium Thio Sulphate Solution from actual generator.
29.4 Spent Solvent
(Anisol)
From the
manufacturi
ng of 4 -
Methoxy
Acetopheno
ne
Nil 161 MT/Month 161 MT/Month Collection / Storage /
Reuse in to next
batch in same
process
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29.4 Spent Solvent
(IPA OR
Methanol)
From
manufacturi
ng of Alpha
Napthylami
ne
Nil 274 MT/Month 274 MT/Month
Collection / Storage /
Reuse in to next
batch in same
process
OR
Spent Solvent
(Aniline OR
ODCB)
From
manufacturi
ng of Alpha
Napthylami
ne
Nil 386 MT/Month 386 MT/Month
If industry will use IPA / Methanol as a raw material for the manufacturing of Alpha Napthylamine, then IPA /
Methanol shall be recovered, accordingly if industry will use Aniline / ODCB, then only Aniline / ODCB shall be
recovered.
29.4 Spent Solvent
(MCB)
From
manufacturi
ng 3,5-
Dichloroanili
ne
Nil 340 MT/Month 340 MT/Month Collection / Storage /
reuse in to next
batch in same
process
29.4 Spent Solvent
(Aniline)
From
manufacturi
ng Phenyl
Alpha
Naphthylam
ine
Nil 56.6 MT/Month 56.6 MT/Month Collection / Storage /
reuse in to next
batch in same
process
29.4 Spent Solvent
(Toluene)
From
manufacturi
ng of 4-
Methyl
Acetopheno
ne
Nil 1329 MT/Month 1329 MT/Month Collection / Storage /
reuse in to next
batch in same
process
29.4 Spent Solvent
(EDC)
From
manufacturi
ng of Bis-(2-
Chloroethyl)
-amine
Nil 28.5 MT/Month 28.5 MT/Month Collection / Storage /
reuse in to next
batch in same
process
29.1 Distillation
Residue
From
Process
Nil 38.5 MT/Month 38.5 MT/Month Collection / Storage /
Transportation / sent
to Cement industries
for co-processing of
CHWIF
Distillation residue generated from the manufacturing of 4-Methoxy Acetophenone, 4-Methyl Acetophenone,
Alpha Napthylamine, Phenyl Alpha Naphthylamine (PANA), 3,5-Dichloroaniline
--- Acetic
Anhydride
From
manufacturi
ng of 4-
Nil 109 MT/Month 109 MT/Month Collection / Storage /
Transportation /
reuse in to next
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2.0 INTRODUCTION OF THE PROJECT/BACKGROUND INFORMATION
2.1 Identification of the project and project proponent. In case of mining project, a copy of mining
lease/letter of intent should be given.
Identification of the project
Proposed Pesticide Intermediates and Specialty Chemicals in Existing Unit
Identification of the project proponent
Presently following are the directors of the company:-
1. Mr. Bansilal D. Patel
2. Mr. Jitendra P. Parmar
2.2 Brief description of nature of the Project
Proposed Pesticide Intermediates and Specialty Chemicals in Existing Unit
2.3 Need for the project and its importance to the country and or region
The objective is to be achieved by:
• Consolidating Business.
• By constantly upgrading the product range.
• Continuously reducing the Costs & improving Quality.
• To generate local employment
2.4 Demands-Supply Gap
Based on our informal survey of the market with our current customers and various traders, we have
found that there is a big potential for the range of the products we are planning. These products will
be an addition to the current range of our products.
2.5 Imports vs. Indigenous production
Based on the current cost of indigenous raw materials and the non availability of some materials, we
will have to import some of the key raw materials as they are not available indigenously. This will
Methyl
Acetopheno
ne
batch in same
process
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make us very competitive against imported finished products and we will be able to increase the
export of our finished products.
2.6 Export possibility
There is export potential of our proposed products.
2.7 Domestic/Export Markets
There is export potential as well as demand in local market.
2.8 Employment Generation (Direct and Indirect) due to project.
Employment would be as per prevailing norms of state government for skilled and unskilled people
for the proposed expansion project.
3.0 Project Description
3.1 Type of Project including interlinked and interdependent projects, if any.
Proposed Pesticide Intermediates and Specialty Chemicals in Existing Unit.
Category: A-5 (b) & 5(f)
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3.2 Location (map showing general location, specific location and project boundary & project site
layout) with coordinates.
Map showing general location
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Layout
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3.3 Details of alternate sites considered and the basis of selecting the proposed site, particularly
the environmental considerations gone into should be highlighted.
Major factors involved in the selection of site are listed below:
• Site is very well connected by road
• Proximity to Raw Material suppliers
• Availability of sufficient land free from cultivation
• Availability of power evacuation facilities
• Availability of water for industrial use
Modern infrastructure support and amenities at par with industrial estates in other global markets,
including:
� Efficient transport facilities within the industrial estate and to & fro the city area.
� Environment-friendly zone.
� Uninterrupted power supply.
3.4 Size or Magnitude of Operation
Please refer Annexure-I of Form-I.
3.5 Project Description with process details (a schematic diagram/flow chart showing the project
layout, components of the project etc. should be given)
Please refer Annexure-III in Form-I.
3.6 Raw material required along with estimated quantity, likely source, marketing area of final
products. Mode of transport of raw materials and finished products.
Please refer Annexure-I in Form-I
3.7 Resource optimization/recycling and reuse envisaged in the project, if any, should be briefly
outlined.
Out of total 28 KL/Day of effluent ...
1. About 14 KL/Day of Condensate water (generated only from the manufacturing of Nytrosyl
Sulphuric Acid (from spent sodium thio sulphate solution and Spent H2SO4 (as a raw material)) is
recycled back in to cooling tower.
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And remaining 14 KL/Day waste water generated from process (from manufacturing of 3, 5, DCA),
cooling, washing & Scrubber shall be treated in ETP and the treated effluent shall be reused in to
utilities.
3.8 Availability of water its source, energy/power requirement and source should be given.
Power & Fuel Requirement
Fuel
Natural Gas: 82 SCM/day (Existing)
Diesel: 30 Lit/Hr (Existing)
Natural Gas: 82 SCM/day (Total Proposed)
Diesel: 75 Lit/Hr (Total Proposed)
Energy:
90 HP from DGVCL
Water Source
The entire water requirement will be met through Surat Municipal Corporation (SMC).
3.9 Quantity of wastes to be generated (liquid and solid) and scheme for their
management/disposal.
Liquid Waste:
Source of water will be met through SMC. Total water requirement will be 65 m3/day (Existing: 25.5
m3/day + Additional Proposed: 39.5 m
3/day). The total wastewater generations will be 24.0 m
3/day
(Existing: 7.0 m3/day + Additional Proposed 17.0 m
3/day). Total 24.0 m3/day (14 m
3/day Industrial +
10 m3/day domestic) of effluent shall be generated, out of which 14 KL/Day waste water generated
from process (from manufacturing of 3, 5, DCA), cooling, washing & Scrubber shall be treated in ETP
and the treated effluent shall be reused in to utilities. About 14 KL/Day of Condensate water
(generated only from the manufacturing of Nytrosyl Sulphuric Acid (from spent sodium thio sulphate
solution and Spent H2SO4 (as a raw material)) is recycled back in to cooling tower.
Solid Waste:
Please Annexure- VI in Form-I.
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3.10 Schematic representations of the feasibility drawing which give information of EIA purpose.
RECONNAISSANCE SURVEY OF EXISTING PLANT ANNUAL REPORT
MARKET ASSESSMENT
FINANCIAL REPORT
PROJECT REPORT
INTRODUCTION
MONITORING OF AIR, WATER & SOIL QUALITY & NOISE
LEVELS. DATA ON METEOROLOGY SOCIO-ECONOMIC
STATUS & BASIC AMENITIES. SITE VISITS BY AND
INTERVIEWS WITH LOCALS
BASELINE
ENVIRONMENTAL
STATUS
ENVIRONMENTAL INFORMATION CENTRE
CENTRAL GROUND WATER BOARD
GUJARAT POLLUTION CONTROL BOARD (GPCB)
PUBLIC HEALTH ENGINEERING DEPT.
AGRICULTURE DEPARTMENT
FOREST DEPARTMENT
IRRIGATION DEPARTMENT
EMPLOYMENT EXCHANGE
HEALTH CENTER
CENSUS DEPT.
INDIAN METEOROLOGICAL DEPT.
SOCIOECONOMIC
STATUS &
INFRASTRUCTURE
PROPOSED
EXPANSION PLANT
FACILITY DESCRIPTION
IMPACTS
METHODOLOGY OF
IMPACT
ASSESSMENT
IDENTIFICATION & ASSESSMENT OF IMPACTS
EVALUATION OF IMPACTS BY MATRIX METHOD
SOURCE OF INFORMATION OVERVIEW OF
E. I. A. STUDIES
ACTIVITIES
ENVIRONMENTAL
MANAGEMENT PLAN
DESCRIPTION OF EFFLUENT TREATMENT PLAN, AIR
POLLUTION CONTROL, HAZARDOUS WASTE
MANAGEMENT, GREEN BELT DEVELOPMENT
MONITORING PROGRAM
RISK ANALYSIS
STUDIES &
DISASTER
MANAGEMENT PLAN
SAFETY, HEALTH & ENVIRONMENTAL POLICY, GUIDELINES BY
DIRECTOR GENERAL OF FACTORY SAFETY, MINISTRY OF LABOR. CONSEQUENCE ANALYSIS
PREPARATION OF DISASTER MANAGEMENT PLAN
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4.0 Site Analysis
4.1 Connectivity
• Site is very well connected by road & rail
• Availability of power evacuation facilities
• Availability of water for industrial use
4.2 Land Form, Land Use and Land Ownership
It will be incorporated in EIA Studies.
4.3 Topography (along with map)
We will incorporate topography in EIA Studies.
4.4 Existing land use pattern (agriculture, non-agriculture, forest, water bodies (including area
under CRZ)), shortest distances from the periphery of the project to periphery of the forests,
national park, wild life sanctuary, eco sensitive areas, water bodies (distance from HFL of the
river), CRZ. In case of the notified industrial area, a copy of the Gazette notification should be
given.
It will be incorporated in EIA Studies.
4.5 Existing Infrastructure
Existing Infrastructures facilities are listed below:
Site is very well connected by road
Proximity to Raw Material suppliers
Availability of sufficient land free form cultivation.
Availability of power evacuation facilities
4.6 Soil Classification
It will be incorporated in EIA Studies.
4.7 Climatic data from secondary sources.
Primary source: our own weather station & Secondary Sources: Indian Meteorological Department,
Ahmedabad.
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4.8 Social infrastructure available.
Depending on the growth of the company the required social infrastructure will be provided.
5.0 Planning Brief
5.1 Planning Concept (type of industries, facilities, transportation etc) Town and Country
planning/Development authority classification.
Type of Industry: Proposed Pesticide Intermediates and Specialty Chemicals in Existing Unit
Facility: Canteen, Administration, Transportation, OHC
5.2 Population Projection
It will be incorporated in EIA Studies.
5.3 Land use planning (breakup along with green belt etc.)
Plot Area: 2700 m2
Total Factory area: 1413 m2
Green belt area: 540 m2
Total Open Area: 747 m2
5.4 Assessment of Infrastructure Demand (Physical & Social)
It will be incorporated in EIA Studies.
5.5 Amenities/Facilities
It will be incorporated in EIA Studies.
6.0 Proposed Infrastructure
6.1 Industrial Area (Processing Area)
Processing Area (Processing Zone, ETP Area and Utility Area): 1413 m2
6.2 Residential Area (Non Processing Area)
Non Processing Area (Green belt, Raw material storage area, Finished storage area, road, Open
Area): 1287 m2
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6.3 Green Belt
Company has developed an effective green belt within the factory and on periphery of the factory.
In addition to this, majority of the vacant land shall be planted with trees, shrubs and grasses.
6.4 Social Infrastructure
Depending on the growth of the company the required social infrastructure will be provided.
6.5 Connectivity (Traffic and Transportation Road/ Rail/Metro/ Water ways etc)
Site is very well connected by road & railway.
6.6 Drinking water Management (Source & Supply of water)
Water requirement will meet through SMC.
6.7 Sewerage System
Sewage pipes are laid in entire company for the removal and disposal of mainly non-harmful liquid
wastes from the offices, canteen and domestic waste coming from different sections. These liquid
wastes is treated and disposed by septic tank and soak pit.
6.8 Solid Waste Management
Please refer Section 1.7, Page No. 7 in Pre-Feasibility Report.
6.9 Power Requirement & Supply/Source
Energy:
90 HP from DGVCL
7.0 Rehabilitation and Resettlement (R & R) Plan
7.1 Policy to be adopted (central/state) in respect of the project affected including home ousters,
land ousters and landless laborers (a brief outline to be given)
There is no habitation on the proposed expansion project area and it is industrial land which is
purchased by company for development of Company, so that R & R policy is not applicable to this
project.
There shall be no displacement of any population in project area.
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8. Project Schedule & Cost Estimates
8.1 Likely date of start of construction and likely date of completion (Time schedule for the project
to be given).
We shall start construction after getting environmental clearance and consent to establish. We shall
start production upon making application for CCA.
8.2 Estimated Project cost along with analysis in terms of economic viability of the project.
Total costs of the project will Rs. 50 Lakh. Capital cost of air & water pollution control system and
environmental monitoring equipments will be Rs. 5 Lakh.
9. Analysis of Proposal (Final Recommendations)
9.1 Financial and social benefits with special emphasis on the benefit to be local people including
tribal population, if any, in the area.
• Employment would be as per prevailing norms of state government for skilled and unskilled
people for the proposed project.
• Social Welfare shall be done.
• Cordial relation with the industry shall be established and representation shall be made to
villagers for help for creation of facilities related to health, education, etc.