SHREE GANESH FATS (P) LTD. -...
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SHREE GANESH FATS (P) LTD.
Pre-Feasibility Report for Environmental Clearance (EC) of Proposed Greenfield Chlor-Alkali Plant of 600 MTD (2×300 MTD) and Captive Power Plant of 32 MW at Landha Village, Tehsil: Saha, District: Ambala, Haryana.
OCTOBER, 2014
Consultant:
K a d a m Environmental
Consultants www.kadamenviro.com
Environment for Development
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 1
SHREE GANESH FATS (P) LTD.
Pre-Feasibility Report for Environmental Clearance (EC) of Proposed
Greenfield Chlor-Alkali Plant of 600 MTD (2×300 MTD) and Captive
Power Plant of 32 MW at Village: Landha, Tehsil: Saha, District:
Ambala, Haryana © Kadam Environmental Consultants (‘Kadam’), October 2014
This report is released for the use of the Shree Ganesh Fats (P) Ltd. Regulators and relevant stakeholders
solely as part of the subject project’s Environmental Clearance process for Proposed Greenfield Chlor-
Alkali plant and Captive Power Plant at Village: Landha, Tehsil: Saha, District: Ambala, Haryana.
Information provided (unless attributed to referenced third parties) is otherwise copyrighted and shall
not be used for any other purpose without the written consent of Kadam.
QUALITY CONTROL
Name of
Publication
EC for Proposed Greenfield Chlor-Alkali plant of 600 MTD (2×300 MTD) and Captive
Power Plant of 32 MW at Village: Landha, Tehsil: Saha, District: Ambala, Haryana
Project Number 1418051306 Report No. 1 Version 1 Released October, 2014
Prepared By Ms. Nazneen Mansuri /Ms. Ishita Garg
Reviewed By Mr. Sangram Kadam/Mr. J.A Rathi
Released By Mr. Sangram A. Kadam
DISCLAIMER
Kadam has taken all reasonable precautions in the preparation of this report as per its auditable quality plan.
Kadam also believes that the facts presented in the report are accurate as on the date it was written. However,
it is impossible to dismiss absolutely, the possibility of errors or omissions. Kadam therefore specifically
disclaims any liability resulting from the use or application of the information contained in this report. The
information is not intended to serve as legal advice related to the individual situation.
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
TABLE OF
CONTENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 1
CONTENTS
1 EXECUTIVE SUMMARY ................................................................................. 6
2 INTRODUCTION OF THE PROJECT ................................................................. 7
2.1 IDENTIFICATION OF PROJECT ............................................................................. 7
2.2 PROJECT PROPONENT .................................................................................... 7
2.3 BRIEF DESCRIPTION OF NATURE OF THE PROJECT ........................................................ 7
2.4 NEED FOR THE PROJECT AND ITS IMPORTANCE TO THE COUNTRY AND OR REGION ....................... 7
2.5 DEMAND-SUPPLY GAP .................................................................................... 8
2.6 IMPORT VS. INDIGENOUS PRODUCTION .................................................................. 8
2.7 EMPLOYMENT GENERATION (DIRECT AND INDIRECT) DUE TO THE PROJECT............................. 8
3 PROJECT DESCRIPTION ............................................................................... 9
3.1 TYPE OF PROJECT ........................................................................................ 9
3.2 LOCATION (MAP SHOWING GENERAL LOCATION, SPECIFIC LOCATION AND PROJECT BOUNDARY &
PROJECT SITE LAYOUT) WITH COORDINATES ..................................................................... 9
3.3 DETAILS OF ALTERNATE SITES CONSIDERED AND THE BASIS OF SELECTING THE PROPOSED SITE. ....... 9
3.4 SIZE OR MAGNITUDE OF OPERATION ................................................................... 10
3.5 PROJECT DESCRIPTION WITH PROCESS DETAILS (A SCHEMATIC DIAGRAM/FLOW CHART SHOWING THE
PROJECT LAYOUT, COMPONENTS OF THE PROJECT ETC, SHOULD BE GIVEN) .................................... 10
3.6 RAW MATERIAL REQUIRED ALONG WITH ESTIMATED QUANTITY, LIKELY SOURCE, MARKETING AREA OF
FINAL PRODUCTS, MODE PF TRANSPORT OF RAW MATERIAL AND FINISHED PRODUCTS. ........................ 16
SALT ............................................................................................................ 16
3.7 RESOURCE OPTIMIZATION/RECYCLING AND REUSE ENVISAGED IN THE PROJECT, ...................... 16
3.8 AVAILABILITY OF WATER ITS SOURCE, ENERGY/POWER REQUIREMENT AND SOURCE SHOULD BE GIVEN 16
3.9 QUANTITY OF WASTES TO BE GENERATED (LIQUID AND SOLID) AND SCHEME FOR THEIR
MANAGEMENT/DISPOSAL ....................................................................................... 16
3.10 SCHEMATIC REPRESENTATIONS OF THE FEASIBILITY DRAWING WHICH GIVE INFORMATION OF EIA
PURPOSE. 19
4 SITE ANALYSIS ......................................................................................... 20
4.1 CONNECTIVITY ......................................................................................... 20
4.2 LAND FORM, LAND USE AND LAND OWNERSHIP ....................................................... 20
4.3 TOPOGRAPHY ........................................................................................... 20
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. ..................................................................................... 20
4.5 EXISTING INFRASTRUCTURE ............................................................................ 21
4.6 SOIL CLASSIFICATION .................................................................................. 21
4.7 CLIMATIC DATA FROM SECONDARY SOURCES ........................................................... 21
4.8 SOCIAL INFRASTRUCTURE AVAILABLE .................................................................. 21
5 PLANNING BRIEF ...................................................................................... 22
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
TABLE OF
CONTENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 2
5.1 PLANNING CONCEPT (TYPE OF INDUSTRIES, FACILITIES, TRANSPORTATION ETC) TOWN AND COUNTRY
PLANNING/ DEVELOPMENT AUTHORITY CLASSIFICATION ...................................................... 22
5.2 LAND USE PLANNING (BREAKUP ALONG WITH GREEN BELT ETC) ........................................ 22
5.3 ASSESSMENT OF INFRASTRUCTURE DEMAND (PHYSICAL & SOCIAL) ................................... 22
5.4 AMENITIES/FACILITIES ................................................................................. 22
6 PROPOSED INFRASTRUCTURE .................................................................... 23
6.1 INDUSTRIAL AREA (PROCESSING AREA) ................................................................ 23
6.2 RESIDENTIAL AREA (NON- PROCESSING AREA) ........................................................ 23
6.3 GREEN BELT ............................................................................................ 23
6.4 SOCIAL INFRASTRUCTURE .............................................................................. 23
6.5 CONNECTIVITY ......................................................................................... 24
6.6 DRINKING WATER MANAGEMENT ...................................................................... 24
6.7 SEWERAGE SYSTEM .................................................................................... 24
6.8 INDUSTRIAL WASTE MANAGEMENT..................................................................... 24
6.9 POWER REQUIREMENT & SUPPLY / SOURCE ............................................................ 24
7 REHABILITATION AND RESETTLEMENT (R & R) PLAN .................................... 25
7.1 POLICY TO BE ADOPTED (CENTRAL/STATE) IN RESPECT OF THE PROJECT AFFECTED PERSONS INCLUDING
HOME OUSTEES, LAND OUSTEES AND LANDLESS. ............................................................... 25
8 PROJECT SCHEDULE & COST ESTIMATES ...................................................... 26
8.1 LIKELY DATE OF START OF CONSTRUCTION AND LIKELY DATE OF COMPLETION......................... 26
8.2 ESTIMATED PROJECT COST ALONG WITH ANALYSIS IN TERMS OF ECONOMIC VIABILITY OF THE PROJECT
26
9 ANALYSIS OF PROPOSAL ........................................................................... 27
9.1 FINANCIAL AND SOCIAL BENEFITS WITH SPECIAL EMPHASIS ON THE BENEFIT TO THE LOCAL PEOPLE. . 27
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
TABLE OF
CONTENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 3
LIST OF FIGURES
Figure 3-1: Process Flow Diagram ................................................................................................ 15
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
TABLE OF
CONTENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 4
LIST OF TABLES
Table 2-1: Details of Management team ......................................................................................... 7
Table 3-1: Co-ordinates of the Proposed Project Site ....................................................................... 9
Table 3-2: Size/Magnitude of Proposed Facilities ........................................................................... 10
Table 3-3: Proposed Production Capacity of Chlor-Alkali plant ........................................................ 10
Table 3-4: Details of Raw material Quantity, Source and Mode of Transport .................................... 16
Table 3-5: Details of Proposed Energy Requirement ...................................................................... 16
Table 3-6: Details of emissions from process and flue gas stacks along with their mitigation methods17
Table 3-7: Details of Hazardous Solid Waste generation from proposed project ............................... 18
Table 3-8: Details of Solid Waste Generation from proposed project ............................................... 18
Table 4-1: Connectivity of Road, Railway and Airport with the site .................................................. 20
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
TABLE OF
CONTENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 5
LIST OF ANNEXURES
Annexure 1: Map Showing General and Specific Location of Project Site .......................................... 29
Annexure 2: Project Boundary Map .............................................................................................. 30
Annexure 3: Site Layout Map ....................................................................................................... 31
Annexure 4: Land Documents ...................................................................................................... 32
Annexure 5: NOC from Department of Town and Country Planning, Haryana .................................. 38
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 6
1 EXECUTIVE SUMMARY
Name of Company Shree Ganesh Fats (P) Ltd.
Category Category “A”
Location of Plant Village Landha, Tehsil Saha, District: Ambala, Haryana
Total Area 5.2 ha (52609.1 m2)
Production Details Chlor alkali plant and Captive Power Plant
Capacity of Proposed Plants Chlor-Alkali: 600 MTD (2×300 MTD)
Power plant: 32 MW
Raw Material Requirement
Salt
Na2CO3
Sodium Sulphite
Flocculent
H2SO4
Coal/Petcoke
Quantity: MTPA
1,60,000
770
140
1
1,500
1,21,968
Water Source Borewell
Total Power Requirement (MW) 32 MW
Total Project Cost Approx. 350 Crore
Project Time Schedule 24 Months from date of issue of EC from MoEF and CTO from SPCB.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 7
2 INTRODUCTION OF THE PROJECT
2.1 Identification of project
The proposed project is a new Greenfield Chlor Alkali plant and Captive power plant. The project falls
under the schedule “Materials Processing”, Project or Activity 4(d), Chlor-Alkali Industry, Category “A”.
This project attracts Public consultation/hearing as per EIA notification, 2006 amended till date.
2.2 Project proponent
Shree Ganesh Group today holds business activities in Edible and Non Edible Oils. From a wide range
of products made available to the consumers and also tailor made for specific requirements.
With present manufacturing of products ‘Distilled Fatty Acids’ ‘Stearic Acids’ ‘Soap Noodles’ ‘Soaps’
‘Hydrogenated Oils’ all from manufacturing facility in Baddi (Barotiwala), Refined rice bran oils, crude
solvent oils from Ambala (Haryana). The management team includes:
Table 2-1: Details of Management team
S. No. Name Designation
1 Mr. Madan Lal Garg Chairman
2 Mr. Parvind Kumar Garg Managing Director
3 Mr. Vinod Kumar Garg Managing Director
4 Mr. Parmod Kumar Garg Managing Director
5 Mr. Raj Kumar Garg Managing Director
6 Mr. Pragun Garg Director(Operations And Business Development)
2.3 Brief description of nature of the project
The proponent intends to establish a Greenfield Chlor-Alkali plant of 600 MTD (2×300 MTD) and Captive
Power Plant of 32 MW on total plot area of 5.2 ha. The water will be sourced from in-house Borewell.
Coal/Petcoke will be used as raw material for Captive power plant. The Chlor-Alkali process is an
industrial process for the electrolysis of sodium chloride. It is the technology used to produce chlorine
and sodium hydroxide (Caustic Soda), which are commodity chemical required by industry. Usually the
process is conducted on a brine (an aqueous solution of NaCl), in which case NaOH, Hydrogen and
Chlorine results. HCl is produced from H2 and Cl2.
2.4 Need for the project and its importance to the country and or region
The project proponent is involved in other businesses of Chlorination and Hydrogenation which requires
Chlor-Alkali products as raw material. Hence, to cater the need of this raw material and also the
increasing demand of caustic soda in the market the proponent has intended to propose Chlor-Alkali
plant.
The Chlor-alkali industry in India is approximately 65 yrs old. It forms an important component of basic
chemicals industry, comprising around 74% of the basic chemicals production in India. Caustic soda,
chlorine alongside hydrogen and hydrochloric acid comprise the Chlor-alkali industry’s components.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 8
These chemicals find their applications in a number of industries such as textiles, chemicals, paper, PVC,
water treatment, alumina, soaps & detergents, glass, chlorinated paraffin wax, among others. The
demand for the two sub-segments – caustic soda & soda ash, has increased significantly registering a
CAGR of 5.6% and 4.7% respectively, over the past five years.
CARE Research’s report on ‘Indian Chlor-Alkali Industry’ throws light on key aspects that govern the
industry’s present market dynamics, while commenting on the future demand and supply growth in
industry for the next five years, by offering an individual focus on its prime sub-segments.
2.5 Demand-Supply Gap
The Chlor-alkali industry mainly consists of the production of three key products – caustic soda, soda
ash, and chlorine. Together, the alkali chemicals comprised 74% of the total chemicals production in
FY10. According to Alkali Manufacturers’ Association of India (AMAI), the Indian Chlor-alkali market was
estimated at around USD 1.9 billion in FY2010, vis-à-vis global market size of USD 48 billion. Caustic
soda and chlorine are produced together in the ratio of 1:0.89 (also known as Electrochemical Unit or
ECU) through electrolysis of salt. On account of their co-production, the market dynamics for caustic
soda and chlorine are heavily influenced by each other. Internationally, it is chlorine based, whereas, in
India, it is influenced by caustic soda.
Caustic soda finds its application mainly in alumina, textiles, paper, organics, inorganics, soaps &
detergents, etc. The supply of caustic soda can be influenced by the chlorine derivatives markets. If
caustic soda is in surplus, it can be stored safely. Chlorine find its way in market as its uses is in many
industrial sectors. The global demand for caustic soda grows by an average of 3% a year, for chlorine
by an average of 2.2% a year.
2.6 Import vs. Indigenous production
The global caustic soda, chlorine, and soda ash market volume is expected to reach 79.8, 74.2, and
58.1 million tons respectively translating into total revenue of over $60 billion by the year 2017. As of
year 2012, Asia consumes almost half of the combined volume of all the aforesaid products followed by
North America and Europe. The major application segments for chlorine are PVC and organic chemicals,
for caustic soda major applications are pulp and paper and organic and inorganic chemicals. Chlorine
and caustic soda are mainly produced using membrane and diaphragm technology with mercury cell
process in phasing out mode.
The major players in the market are The DOW Chemical Company (U.S.), Occidental Chemical
Corporation (U.S.), Bayer AG (Germany), PPG Industries (U.S.), Tata Chemicals Ltd (India), Shin-Etsu
Chemical Co. Ltd (Japan), Formosa Plastics Corp. (Taiwan), Solvay Chemicals (Belgium), Ineos Chlor
Ltd (U.K.), FMC Corporation (U.S.), Shangdong Haihua Group Co. Ltd (China), and Ciech S.A. (Poland).
2.7 Employment Generation (Direct and Indirect) due to the Project
During the construction phase around 200 workers and during the operational phase around 50 workers
will be required. Local skilled and semi-skilled workers will be engaged during construction phase. The
positives impact include enhanced direct employment for technical/administrative works and indirect
employment opportunities for transporters of raw material like salt, coal/petcoke etc. and finished goods.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 9
3 PROJECT DESCRIPTION
3.1 Type of project
The project is a Greenfield Chlor-Alkali Plant of 600 MTD (2×300 MTD) and Captive Power Plant of 32
MW. The project does not include any interlinked or interdependent projects.
3.2 Location (map showing general location, specific location and project boundary
& project site layout) with coordinates
The project site is located at Khasra No.: 15//11, 12,13,18/3,19,20,16//7/2,12/2,13,14,15,16,17,18/1,24
/2,25/1 at Village Landha, Tehsil Saha, and District: Ambala, Haryana. The total plot area is 5.2 ha.
Location map showing general location, specific location of proposed project is given in Annexure 1 Project boundary map is given in Annexure 2. Project site layout map is given in Annexure 3. The
co-ordinates of the project site is given in Table 3-1.
Table 3-1: Co-ordinates of the Proposed Project Site
Code Latitude Longitude
A 30°14'11.38"N 76°51'59.30"E
B 30°14'11.45"N 76°52'2.50"E
C 30°14'13.31"N 76°52'2.67"E
D 30°14'13.29"N 76°52'4.78"E
E 30°14'11.55"N 76°52'4.81"E
F 30°14'11.23"N 76°52'14.98"E
G 30°14'9.10"N 76°52'14.89"E
H 30°14'9.18"N 76°52'12.61"E
I 30°14'7.27"N 76°52'12.45"E
J 30°14'7.29"N 76°52'7.50"E
K 30°14'6.72"N 76°52'7.46"E
L 30°14'6.61"N 76°52'4.90"E
M 30°14'6.00"N 76°52'4.88"E
3.3 Details of alternate sites considered and the basis of selecting the proposed
site.
The proposed project is intended to be establish at Village: Landha, Taluka: Saha, District: Ambala
considering the following points:
Proximity to NH-1 catering 3 states- New Delhi, Himachal Pradesh, and Punjab which are
major market.
Close Proximity of local region like Rohtak, Bahadurgarh, Rewari for chlorine derived products.
Hence need of alternative site identification is not felt.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 10
3.4 Size or magnitude of operation
Capacity of proposed facility is given in Table 3-2
Table 3-2: Size/Magnitude of Proposed Facilities
S. No. Proposed Facility Capacity
1 Chlor Alkali Plant 600 MTD
2 Captive Power Plant 32 MW
3.5 Project description with process details (a schematic diagram/flow chart
showing the project layout, components of the project etc, should be given)
Details of proposed production capacity of Chlor-Alkali plant is given in Table 3-3
Table 3-3: Proposed Production Capacity of Chlor-Alkali plant
S.
No. Products Additional Proposed (MTPA)
1 Caustic Soda (Lye) 1,04,400
2 Chlorine 90,000
3 Hydrochloric Acid (100%) 3,600
4 Hydrogen 3,000
5 Sodium hypochlorite 900
Project Description:
Chlor-Alkali Plant
The process is based on Membrane Cell technology. The main steps in the process to manufacture
caustic soda are
Purification of brine.
Electrolysis.
Concentration and flaking of caustic soda solution.
In the process Hydrogen and Chlorine gas are produced as the co-product.
Brine Purification
General: Brine for ion exchange membrane Chlor-Alkali process is prepared by dissolving salt in the
return brine from the electrolysis plant, and purified in two stages. Primary purification removes
impurities like calcium, magnesium, sulphate, iron, silica etc. to ppm level. Secondary purification is
required to make brine suitable for the ion exchange membrane Chlor-alkali process.
1. Primary Brine Purification
Primary Brine Purification section consists of Salt Handling system, Brine Saturator, Reactor Clarifier,
Clarified Brine Tank and associated facilities.
This process includes Brine saturation, chemicals dosage, reaction and sedimentation. The purpose of
this process is to re-saturate the return brine with raw salt and to remove impurities from the
saturated raw brine.
The return brine is fed from the top of the Brine Saturator and saturated with salt. The salt is
continuously supplied to the top of the saturator by a Belt Conveyor System.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 11
The saturated raw brine overflows from the Brine Saturator and flows into Reactor. Chemicals such as,
sodium carbonate, caustic soda are fed to Reactor.
Calcium, magnesium and other multivalent cations and sulphate anions in the raw brine react with these
chemicals and are changed to suspend solids while the brine is held in the reactor.
pH of the brine is controlled by the addition of caustic-soda to the brine. Then the brine overflows from
the reactor into the Brine Clarifier. Flocculent is fed to the brine line entering the clarifier.
Suspended solids in the brine are removed by settling in the Clarifier provided with water seal & insulated
from the sides. The brine, thus clarified, flows into clarified Brine tank over the weir of Clarifier & is
pumped out and recirculated to the brine system before reactor for better clarification. Slurry is
periodically measured for better control.
A part of slurry is sent to Sludge Filter System. The clarified brine is sent to Secondary Brine purification
section by clarified brine pump.
2. Secondary Brine Purification
Secondary Brine Purification Section consists of Brine Filter and Ion Exchange Resin Column.
The clarified brine is filtered through the filter and flows into filtered Brine tank. Suspended solids
caught on the filter element surface are blown down to Filter Slurry Pit. Filter Slurry in the pit is sent
to centrifuge where most of the brine is recovered and fed back to Return Brine Tank.
Ion Exchange Resin Column packed with special Ion Exchange resin is operated and controlled
automatically from control room.
This specially developed Ion exchange resin can remove multivalent cations harmful to the Ion
exchange membrane. The brine thus purified is fed to Electrolyser and electrolysis is conducted.
ELECTROLYSIS
Electrolysis section consists of bipolar Electrolysers and their associated equipment’s.
1. Electrolyser
Electrolyser consists of number of bipolar type cell frames with the metal anode and the activated
cathode, the Ion exchange membrane, press unit for mounting cell frames, sub-headers for feeding
anolyte and catholyte, sub-headers, and oil pressure unit which supplies oil to oil cylinders.
Cell frames holding the Ion Exchange membrane in between are fixed by the oil cylinder installed at
the end of the press unit. This structure ensures no leakage of electrolytes because uniform pressure
can be applied to gasket surface and cell frame of metal structure ensures no electrolyte leakage
caused by deformation even after a long period of operation.
2. Anolyte Circulation
Anolyte circulation system is composed of Anolyte Circulation Tank and anolyte circulation pump.
Anolyte is fed into each of anode compartment of cell frames through subheaders and hoses, and
recirculated to Anolyte circulation Tank. Purified brine is fed to maintain anolyte concentration within a
designed level. A part of the anolyte, is taken out from Anolyte Circulation Tank to Depleted Brine
Tank by overflow.
Anolyte Circulation system is designed to ensure steady and uniform distribution of anolyte to each
cell and to cope-up with any change in electrolysis conditions such as production rate change.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 12
The diluted brine collected in Depleted Brine Tank is sent to De-chlorination Tower for removal of
Chlorine gas. Chlorine gas generated in electrolyser is separated in Anolyte Circulation Tank and sent
to Chlorine gas cooling, drying and compression section.
3. Catholyte Circulation
Catholyte Circulation System is composed of Catholyte Circulation Tank, Catholyte Circulation Pump
and Catholyte Cooler.
Catholyte is circulated through cathode compartment of cell frames to Catholyte Circulation Tank by
Catholyte Circulation Pump, and a part of it is taken out from Catholyte Circulation Tank to Caustic
Soda Tank and sent out to caustic evaporation section. To keep the concentration of caustic soda at
designed level, demineralised water is fed to catholyte inlet sub-header. Hydrogen gas generated in
Electrolyser is separated from the catholyte in catholyte Circulation Tank and sent to Hydrogen Gas
Cooling and Compression Section. Heat generated in electrolyser is removed by cooling water in
Catholyte Cooler.
DE- CHLORINATION OF RETURN BRINE
De-chlorination section is composed of De-Chlorination Tower, De-Chlorination Tower Cooler, Ejector,
Ejector Cooler and associated facilities. Return brine, (depleted brine) from Electrolysis Section is
saturated with chlorine.
In the tower, chlorine is stripped together with water vapor, and passed through De-chlorination
Tower cooler. The vapor are condensed there and the chlorine gas is sucked by the steam ejector to
Ejector Cooler.
Steam is condensed there and the chlorine gas is then introduced to chlorine gas product main line.
The depleted brine dechlorinated through De-chlorination tower, still contains small amount of free
chlorine which can cause damage to the filter elements in Brine Filters and damage ion exchange resin
in Ion Exchange Resin Columns. Sodium sulfite is added to kill free chlorine. Return brine is then fed
to Return Brine Tank & pumped to salt saturator.
Caustic Concentration
The caustic soda concentration system consists of triple effect falling film evaporators operating on
backward feed flow scheme. 30% caustic solution 80 0C is fed to third effect evaporator. Vapors are
separated from solution and concentrated solution of third effect evaporator is pumped to second
effect evaporator after passing through two heat exchangers in series. In the second effect
evaporator, flash evaporation of liquor takes place and liquor is further heated by steam and vapors
are separated in second effect evaporator to concentrate liquor.
The concentrate from the second effect evaporator is pumped through first effect evaporator after
passing through two heat exchangers in series. Steam at 11 kg/cm2a pressure is used to attain
required concentration of caustic.
Chlorine Liquefaction & Bottling
1. Chlorine Gas Washing and Cooling
Chlorine Gas coming out of Anolyte circulation tank contains water vapor saturated at about 900C
and has little amount of Sodium Chloride as entrainment. Gas is first washed by process water in a
direct contact scrubbing packed tower. Condensate is sent to dechlorination tower. The process water
is in turn cooled by cooling tower.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
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KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 13
Cooled gas is then passed through a packed tower having chilled process water circulation at 160 C so
as to cool the gas to reduce water vapors load.
Chlorine gas temperature is generally around 15-20 deg C as cooling below 9-10 0C will result into
formation of Chlorine hydrate. Cooled gas is then dried with direct spray of sulfuric acid in packed
towers.
2. Chlorine Gas Drying
The cooled chlorine gas is led to chlorine Gas Drying Tower. The moisture of chlorine gas is absorbed
into sulfuric Acid of 98% concentration fed into the two stage chlorine gas drying tower, and gets
diluted to 70% by absorption of moisture from chlorine gas. Chlorine Gas Drying Tower has a
cooler to cool circulating sulfuric Acid. The Dry Chlorine gas is sent for compression.
3. Chlorine Gas Compression
Dry chlorine gas from chlorine Gas Drying Section is compressed to 4 kg/cm2 (a) by using Acid Ring
type Compressor.
4. Chlorine Gas Liquefaction and Filling
Chlorine gas from compressor is sent to chlorine Gas Liquefaction Unit to be condensed by the Freon
22 refrigerant. The unliquefied gases along with inert gas from Liquefier are sent to HCI Synthesis unit
for burning with Hydrogen to produce HCl.
Liquefied chlorine enters Chlorine Storage Tank from where it is transferred by means of compressed
dry air to chlorine bottling section. Part of liquid Chlorine is vaporised and sent to nearby customers
through pipeline.
5. Waste Chlorine Neutralization / Sodium Hypochlorite Section
Waste chlorine gas, only in case of plant emergency is led to the Sodium Hypochlorite Unit. Chlorine
Gas during start up and plant tripping is fed to the absorption tower. This unit consists of packed
tower in which caustic solution is circulated to absorb waste chlorine. Temperature of the liquid is
controlled by heat transfer through plate type heat exchanger with chilled water.
After a desired strength of sodium hypochlorite is reached, the solution is sent to a Hypo Reactor.
Here it is reacted with fresh chlorine to produce marketable quality Sodium Hypochlorite.
6. HCL Synthesis
The HCI Synthesis unit consists of combustion furnace fitted with absorbers. The chlorine gas reacts
with Hydrogen to form HCI gas which is cooled and absorbed in DM water. The flow rate of DM water
is adjusted to obtain 30-33% HCI Solution. The flow rates of Chlorine and Hydrogen are controlled by
flow controllers. Safety Interlocking provisions are made which get actuated by flame protection
device. The Hydrochloric Acid Solution is collected in a product tank from where is pumped to HCI
Storage Tanks.
7. Hydrogen Bottling and Storage
Hydrogen gas is compressed and filled in hydrogen cylinders banks of the customers and also stored
in cylinder banks.
Chemical Reaction:
2 NaCl(aq) + 2 H2O(l) H2(g) + Cl2(g) + 2NaOH(aq)
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FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 14
Power Plant
Process Description
Coal/Petcoke will be used as a fuel source for the Power plant. Basic process involves steam
generation by combustion of coal in boiler. Steam is used to run turbine for power generation.
The process flow diagram is given in Figure 3-1.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
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KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 15
Figure 3-1: Process Flow Diagram
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FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
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KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 16
3.6 Raw material required along with estimated quantity, likely source, marketing
area of final products, mode pf transport of raw material and finished products.
The major raw materials are industrial salt and power. Details of raw material along with the Quantity,
Source and Mode of Transport is given in Table 3-4
Table 3-4: Details of Raw material Quantity, Source and Mode of Transport
S.
No. Raw Material
Proposed
Quantity
(MTPA)
Source Mode of
Transport
1 Salt 1,60,000 Ambala storage areas originally
from Rajasthan and Gujarat Damper/trucks
2 Na2CO3 770 Local Market Trucks
3 Sodium Sulphite 140 Local Market Trucks
4 Flocculent 1 Local Market Trucks
5 H2SO4 1,500 Local Market Tanker
6 Coal/Petcoke 1,21,968 Imported/Indigenous Trucks
3.7 Resource optimization/recycling and reuse envisaged in the project,
The process waste water will be treated with R.O technology and will be recycle back into the process.
Most energy efficient technology will be selected.
3.8 Availability of water its source, energy/power requirement and source should
be given
Water: The water will be extracted from inhouse borewell with prior permission from CGWA.
Power: The details of energy requirement is given in Table 3-5
Table 3-5: Details of Proposed Energy Requirement
S. No. Unit Proposed Quantity (MW)
1 Coal/Petcoke based Power Plant 32
Emergency Power:
D.G set of 3 Nos. will be used for back-up or emergency usage of 600 KVA.
3.9 Quantity of wastes to be generated (liquid and solid) and scheme for their
management/disposal
Gaseous Emissions
The main sources of Gaseous Emission from proposed project will be:
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Stack attached to power plant
Waste Chlorine absorption system (Hypo Plant)
HCl plant
Details of anticipated air emissions from Process and Flue gas are given in Table 3-6.
Table 3-6: Details of emissions from process and flue gas stacks along with their mitigation methods
S.
No.
Stack
Attached to
Stack
Height
(m)
Stack
Diameter
(m)
Exit
Velocity
(m/s)
Pollutants Mitigation
measures
Process Stacks
1. HCl plant 30 0.15 1 HCl Water/Caustic
scrubber
2.
Sodium
Hypo
chlorite
plant
30 0.3 1.2 Cl2 Caustic
scrubber
Flue Gas Stack
1 Boiler of
CPP 60 3 12
SO2 Adequate
Stack height NOx
PM ESP
3 D.G Set
30 1 20.6 SO2, NOx,
PM
Adequate
Stack height 4 D.G Set
5 D.G Set
Liquid Effluent
The waste water generated from the process will be treated using R.O technology and the permeate
of R.O will be recycle back into the process while if required MEE will be used to treat R.O reject,
hence the plant will be a Zero liquid discharge unit.
Solid Waste Generation
Brine sludge is generating during brine purification process in membrane based pollution free Chlor
alkali plant. It contains Inorganic solids of Calcium carbonate, Magnesium hydroxide. Natural sea salt
(produced in Gujarat), our basic raw material, contains impurities like calcium. Magnesium & Sulfate.
We precipitate out these impurities as Calcium carbonate, Magnesium hydroxide and Barium sulfate as
per standard brine purification process followed worldwide. None of these impurities are hazardous.
Brine sludge is not Hazardous in nature.
Details of solid waste generated is given in Table 3-7
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FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 18
Table 3-7: Details of Hazardous Solid Waste generation from proposed project
S. No Waste Name Category Proposed Quantity
Per Annum Disposal Method
1 Discarded
Bags 33.3
1,02,000
(Nos.)
To authorized
vendors
2 Used Oil 5.1 250 Lt To authorized re-
refiners.
Table 3-8: Details of Solid Waste Generation from proposed project
S. No Waste Name Proposed
Quantity MTPA Disposal Method
1 Brine Sludge 3,630 To Secured landfill site
2 Fly ash 6,566.4 As per Fly ash notification will be given to brick
making units
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3.10 Schematic representations of the feasibility drawing which give information of
EIA purpose.
Government of India, as per its policy has given emphasis on Sustainable Development. While it is
supporting the industrial growth, the environmental protection has been made the integrated criteria
for this support. In line with this policy, Ministry of Environment & Forests has defined elaborated
‘Environmental Clearance (EC)’ framework under The Environment (Protection) Act, 1986
(Environmental Impact Assessment Notification, 2006) for establishing/expanding an
industry/development project. The EC process takes into consideration local conditions, public concerns,
effectiveness of impact assessment and proposed mitigation measures in sustaining environmental
equilibrium. The base documentation/study report, called Environmental Impact Assessment (EIA)
detailing baseline conditions, environmental impacts, mitigation measures and management plan is
required to be prepared for start of EC process. Prior Environmental Clearance is required from
concerned authorities for all projects detailed in the ‘Schedule’ as given in the ‘Notification date 14th
September, 2006’. The projects listed as category A or B under EIA notification require submission of
EIA report as per approved TOR for appraisal by expert committee for EC.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 20
4 SITE ANALYSIS
4.1 Connectivity
Table 4-1: Connectivity of Road, Railway and Airport with the site
S. No Routes Distance in ~km
Direction
Roads
1 NH -1 1.5 WSW
2 NH -73 12 NE
3 SH -31 3.9 S
4 SH -4 5.9 SSW
5 SH -7 7.9 SSW
6 SH -5 8 SSW
Railway
1 Mohri 2.7 NNW
2 Dukheri 6.7 NE
3 Kesari 7.0 ENE
4 Shahabad 7.7 SSW
5 Tandwal 11.5 ESE
6 Ambala Cantonment R.S 11.3 NW
Airport
1 Chandigarh 49.1 NNW
2 Patiala 49.4 NNW
4.2 Land Form, Land Use and Land Ownership
The total plot area of the plant is 5.2 ha. The proposed project is to be carried out at village Landha,
Tehsil Saha, District Ambala, Haryana. The site is an undeveloped land and is owned by Shree Ganesh
Fats (P) Ltd. The land documents are attached as Annexure 4. No Objection certificate is obtained
from the department of Town and Country Planning, Haryana for setting up of Industrial unit on the
given Khasra Nos. which is attached as Annexure 5
4.3 Topography
The district area is occupied by Indo-Gangetic alluvium, the area is traversed and drained by seasonal
streams namely Tangri, Beghna and Markanda. Physiographically the area is flat terrain. However a
little part in the extreme northeastern area of the district is occupied by Siwalik hills, and falls in the
zone of “Dissected Rolling Plain”. The area slopes towards southwest with an average gradient of
1.5m/km. The general elevation in the district varies between 245m to 300m above MSL.
4.4 Existing land use pattern (agriculture, non-agriculture, forest, water bodies
(including area under CRZ)), shortest distances from the periphery of the
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project to periphery of the forests, national park, wild life sanctuary, eco
sensitive areas, water bodies (distance from HFL of the river), CRZ.
The existing land is an undeveloped land which does not include agricultural, forestry, water bodies
(including CRZ) and there are no forests, national parks, wild life sanctuary, eco sensitive areas, water
bodies (distance from HFL of the river), CRZ within the study area.Error! Reference source not
found.
4.5 Existing Infrastructure
The proposed project is a new Greenfield project and there are no existing infrastructures on the site.
4.6 Soil Classification
The soils are non-calcareous and sandy loam on the surface, and loam to clayey loam at depth, and
placed under the classification of soil as Udipsamments/Udorthents.
4.7 Climatic data from secondary sources
The climate of Ambala district can be classified as subtropical monsoon, mild & dry winter, hot
summer and sub-humid. The hot weather season starts from mid-March to last week of the June
followed by the south west monsoon which lasts upto September. The transition period from
September to November forms the post monsoon season. The winter season starts late in November
and remains upto first week of March. The normal annual rainfall of the district is 1076 mm. The mean
maximum temperature is 40.8°C (May & June) and mean minimum is 6.8°C (January).
4.8 Social Infrastructure available
Key infrastructure such as primary health centers, schools, bank, places of worship and social/
community facilities such as market, playground etc are available in nearby area of proposed site.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 22
5 PLANNING BRIEF
5.1 Planning Concept (type of industries, facilities, transportation etc) Town and
Country Planning/ Development Authority Classification
The proposed is Chlor-Alkali Plant. This will be the first chemical industry in this area. Within a radius of
1 km storage godowns/sheds, poultry farm etc are located. The project area does not falls within any
controlled area declared by Department of Town and Country Planning, but falls within Urban area
Ambala. No Objection certificate is obtained from the department of Town and Country Planning,
Haryana for setting up of Industrial unit on the given Khasra Nos. which is attached as Annexure 5.
5.2 Land use planning (breakup along with green belt etc)
The green belt area of 1.7 ha (17,360 sqm) i.e 33% of total plot area. Processing area includes:
Storage area, plant area, administrative buildings, parking area, canteen etc.
5.3 Assessment of Infrastructure Demand (Physical & Social)
Key infrastructure such as primary health centers, schools, bank, places of worship and social/
community facilities such as market, playground etc are available in nearby area of proposed site.
5.4 Amenities/Facilities
Approach road from highway is adequate to take load of transportation. State Electrical transmission
lines are available in the near vicinity Basic amenities like public transport, water supply,
telecommunications, educational institutions, hospitals etc. are available in nearby area. Facilities for
water requirement will be met through existing Borewell.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 23
6 PROPOSED INFRASTRUCTURE
6.1 Industrial Area (Processing area)
Salt storage area
Brine sections
Cell house
Utilities
Cooling towers
Chlorine bottling area
Liquid Chlorine storage area
Caustic soda evaporation and storage area
HCl plant, Hypo plant
Hydrogen compression and Bottling area
Hydrogen holder
Hypo, HCL storage
Chemical storage
Boilers
ESP
Effluent treatment plant
DM water plant
D.G House
Transformers and Rectifiers
6.2 Residential Area (Non- Processing Area)
Water reservoir
Weighbridge
Security cabins
Workers restroom,
Parking/Vehicle Shed
Canteen
Administrative Block
Workshop
6.3 Green Belt
The green belt area of 1.7 ha (17,360 sqm) i.e 33% of plot area will be provided.
6.4 Social Infrastructure
Civic/infrastructural facilities like public transport, water supply, telecommunications, educational
institutions, hospitals etc. are available in nearby areas.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
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KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 24
6.5 Connectivity
Adequately described in point 4.1.
6.6 Drinking Water Management
The water will be abstracted from in-house Borewell with prior permission from CGWA. The domestic
water requirement is ~3 KLD. Drinking water for workmen will be procured locally.
6.7 Sewerage System
The domestic effluent will be disposed off in soak pit via septic tank.
6.8 Industrial Waste Management
The process waste water generated will be treated using R.O technology and the permeate of R.O will
be recycle back into the process and MEE will be used to treat R.O reject, hence the plant will be a
Zero liquid discharge unit.
The industrial Hazardous solid waste like discarded bags will be given to authorized vendors and used
oil to authorized refineries. The other process solid waste like brine sludge will be sent to secured
landfill site. The solid waste of MEE will also be sent to secured landfill facility. Fly ash will be given to
brick making units.
6.9 Power Requirement & Supply / source
The power requirement for proposed project will be 32 MW which will be procured from Captive Power
Plant. D.G sets (3 Nos.) of 600 KVA will be installed as backup.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 25
7 REHABILITATION AND RESETTLEMENT (R & R) PLAN
7.1 Policy to be adopted (Central/State) in respect of the project affected persons
including home oustees, land oustees and landless.
Rehabilitation and Resettlement (R&R) plan is not applicable for the proposed project.
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EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 26
8 PROJECT SCHEDULE & COST ESTIMATES
8.1 Likely date of start of construction and likely date of completion
The construction is likely to start after getting Environmental Clearance from regulating authority. This
process may take 12-14 months. Then after NOC from pollution Control Board is required.
Construction work will start, technology selection and detailed engineering will be simultaneously done
with EC process. Construction and execution work will be completed in 12-14 months.
8.2 Estimated project cost along with analysis in terms of economic viability of the
project
The total investment is envisaged to INR 350 crores. The project is economically viable as Cl2 and
Caustic are in high demand with chemical and other process industries. There is huge demand of
these chemicals with good returns.
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
PRE-FEASIBILITY
REPORT
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 27
9 ANALYSIS OF PROPOSAL
9.1 Financial and social benefits with special emphasis on the benefit to the local
people.
Project process technology is well established and supplied on turnkey basis by international
process houses.
The project is being established by well-known technology having industrial background and
has financial support from parent industry. Bank loans are also available.
This will generate employment opportunity for skilled and semi-skilled work force.
Local people around 200, non-skilled or semi-skilled will get daily work during construction
phase.
During operational phase, around 50 skilled persons (Engineers, technicians, Arts and
commerce graduates) will get opportunity to work in administration process and safety or
maintenance sections.
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA ANNEXURES
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 28
ANNEXURES
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA ANNEXURES
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 29
Annexure 1: Map Showing General and Specific Location of Project Site
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE: LANDHA,
TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA ANNEXURES
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 30
Annexure 2: Project Boundary Map
SHREE GANESH
FATS (P) LTD.
EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE: LANDHA,
TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA ANNEXURES
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014 31
Annexure 3: Site Layout Map
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
OTHER
DOCUMENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014
Annexure 4: Land Documents
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
OTHER
DOCUMENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
OTHER
DOCUMENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
OTHER
DOCUMENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
OTHER
DOCUMENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
OTHER
DOCUMENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014
SHREE GANESH
FATS (P) LTD. EC FOR PROPOSED CHLOR-ALKALI PLANT AND CPP AT VILLAGE:
LANDHA, TEHSIL: SAHA, DISTRICT: AMBALA, HARYANA
OTHER
DOCUMENTS
KADAM ENVIRONMENTAL CONSULTANTS |OCTOBER 2014
Annexure 5: NOC from Department of Town and Country Planning, Haryana
CONTACT DETAILS
Vadodara (Head Office)
871/B/3, GIDC Makarpura, Vadodara, India – 390 010.
E: [email protected]; T:+91-265-3001000; F: +91-265-3001069
Delhi / NCR
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E: [email protected]; T/F : 0124-424 2430-436
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