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Project Prefeasibility Report
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 0
Total 240.0 2400.0 2640.0 By Products* 1. Sodium Formate *15.0 *-15.0 Nil 2. Glycerol *25.4 *50.8 *76.2
Total 280.4 2450.8 2716.2 Note: *In existing operations, Sodium Formate is being generated as by product during manufacturing of Epoxidised Soyabean Oil. After proposed project, new manufacturing process of Epoxidised Soyabean Oil will adopted, where Sodium Formate will not be generated. (1) Consolidated Consent and Authorization (CC&A) No: AWH-65840, dated: 30/10/2014 (2) Environment Clearance No.: F.No. J-11011/871/2008- IA II (I), dated: 10/02/2009
Proposed Expansion Project forIncrease in existing production quantities of products. i.e. Synthetic Organic Chemicals
RESOURCES Resource type Requirement Source
Existing Proposed Additional
Total
Land 6761.00 m2 Nil 6761.00m2 No additional land is required for expansion project.
Building 1725.00m2 750.00 m2 2475.00 m2 The existing built up area will be utilized after necessary modifications also some new sheds will be constructed and ETP will have to be modified.
Raw-materials
As given in Chapter-3 section 3.5 - Raw Material for finished products.
The raw materials are available in Local/ Indian market.Andarealso imported from foreign countries. Details are explained in chapter 3
Water Industrial 17.0 KLD Domestic 5.0 KLD
Industrial 30.0 KLD Domestic 3.0 KLD
Industrial 47.0 KLD Domestic 8.0 KLD
Fresh water is/ will be sourced from GIDC water supply
Total 280.4 2450.8 2716.2Note: *In existing operations, Sodium Formate is being generated as by product during manufacturing of Epoxidised Soyabean Oil. After proposed project, new manufacturing process of Epoxidised Soyabean Oil will adopted, where Sodium Formate will not be generated. (1) Consolidated Consent and Authorization (CC&A) No: AWH-65840, dated: 30/10/2014 (2) Environment Clearance No.: F. No. J-11011/871/2008- IAII (I), dated: 10/02/2009
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 4
2.1.2 PROJECT PROPONENT
The company is a private limited and is promoted by 4 directors. Table 2.2: Addresses of Directors
Sr.No. Name of Directors Addresses
1. Mr. Ajay G. Gandhi B-252,25th Floor, Grand Paradi, August KrantiMarg, Mumbai– 400 036.
2. Mr. Pradeep G. Gandhi 21, Vallabh Appts., 87, Bhulabhai Desai Road, Mumbai–400 036.
3. Mr. Shamit A. Gandhi B-252,25th Floor, Grand Paradi, August KrantiMarg, Mumbai – 400 036.
4. Mr. Gulabrai V. Gandhi 21, Vallabh Appts.,87, Bhulabhai Desai Road, Mumbai–400 026
2.2 NATURE OF THE PROJECT The proposed Polymer Compound & Master Batch and Plastic Extruded & Molded Products do not require prior environmental clearance as the process/type of process is not covered under the provisions of EIA-notification-2006 (as amended timely). However, the manufacturing of Plasticizers, Epoxidised Soyabean Oil and Methyl Soyate falls under the item no. “5(f) category” i.e. Synthetic Organic Chemicals and “Category B” as per the EIA notification, since the project is located in GIDC Vapi.However, due to the presence of interstate boundary of D&NH and Daman within 5 km radial periphery, it is to be treated as “Category A” and needs to obtain the prior Environmental Clearance from the Ministry of Environment and Forests MoEF (EIAA).
2.3 NEED OF PROJECT & DEMAND-SUPPLY GAP The proposed products range is having a good demand in the market as per market survey by the company. 2.4 EXPORT POSSIBILITY As per market survey by the company, these proposed products are having a domestic as well as export market.
2.5 EMPLOYMENT GENERATION DUE TO PROPOSED PROJECT
The proposed expansion project will provide direct employment opportunity to16 persons the
man-power required for the project will be employed locally from the nearby areas.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 5
CHAPTER – 3
PROJECT DESCRIPTION 3.1 TYPE & LOCATION OF PROJECT
3.1.1 TYPE
The proposed expansion project involves manufacturing of “Synthetic Organic Chemical” falls under the item no. “5(f) category i.e. Synthetic Organic Chemicals and “Category B” as per the EIA notification, 2006 (as amended timely), since the project is located in GIDC Vapi and presence of interstate boundary of D&NH and Daman within 5 km radial periphery it is to be treated as “Category A”, and needs to obtain the prior Environmental Clearance from the MoEF (EIAA).
3.1.2 LOCATION
M/s. Consumers Plastics Pvt. Ltd. falling under Small Scale category proposes expansion in
existing production capacity and addition of new product at Plot No. 16-19, Phase I, GIDC
Estate, Vapi – 396 195.
There is cluster of profuse large-scale, medium scale and small-scale industries, engaged in
manufacturing of various products, bulk drugs, organic pigments, Organic and Inorganic
Chemicals, Pharmaceuticals, Pesticides etc.
The GIDC area has a Disaster management cell set up by Vapi Industrial Association. Common
Effluent Treatment Plant and Common Hazardous Waste Disposal Site is set up by Vapi Waste
&Effluent Management Co. Ltd. Vapi also having the drainage system for the disposal of the
treated effluent from individual industry to the CETP for further treatment and disposal into the
saline region of the Damanganga River.
Location map of the project site is given in the Figure 3.1.
3.4.1.1.1 Chemical Reaction 3.4.1.1.2 Manufacturing Process Epoxidised Soyabean Oil is manufactured by oxidizing Soyabean Oil by Hydrogen Peroxide in presence of catalyst Formic Acid. In this process initially Soyabean Oil is charged in reactor and catalyst Formic acid is added. Then the required quantity of Hydrogen Peroxide is added in six to seven installments with constant stirring.
After the reaction is completed, the mass is transferred to the settling tank where aqueous layer is removed and remaining oily layer is final product Epoxidised Soyabean Oil, which is dried out by heating under vacuum condition. Whereas the aqueous layer is treated with Sodium Hydroxide and after evaporation, used as byproduct Sodium Formate
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 12
3.4.1.2EPOXIDISED SOYABEAN OIL (Proposed Process) 3.4.1.2.1 Chemical Reaction
3.4.1.1.2 Manufacturing Process
In the proposed change in process, we propose giving stage wise washing for remaining organic layer to achieve required reduction in the acidity. The wash water is also diverted to ETP. Finally, the Epoxidised Soyabean Oil will dry in dryer.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 14
3.4.1.3METHYL SOYATE
3.4.1.3.1 Chemical Reaction
3.4.1.3.2 Manufacturing Process Methyl Soyate is manufactured by esterification of Soyabean Oil by Methanol in presence of catalyst. In this process initially Soyabean Oil is charged in reactor and catalyst Sodium Methoxide and Methanol are added. Then the mixture is heated up to 65oC to 75oC with constant stirring, and refluxed.
After completion of esterification reaction, Methyl Soyate is distilled out and remaining oily mass is byproduct Glycerol.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 15
3.4.1.4 Di-Octyl Phthalate (DOP)
3.4.1.4.1 Chemical Reaction
C6H4(CO)2O + 2 (C8H17OH) C6H4(COOC8H17)2 + H2O
148.12 2 x 130.23 390.56 18.02
3.4.1.4.2 Manufacturing Process Esterification / Separation
Esterification is an equilibrium chemical reaction which is carried out as a batch process in the reactor containing an agitator and other equipment – particularly for water separation and removal which is formed during chemical reaction.
First Phthalic anhydride and the 2-ethylhexanol are mixed in the reactor in order to form the monoester – mono-2-ethylhexylphthalate. The reaction takes place at about 150oC. Further the reaction mixture is heated to 170-180oC. At this point the catalyst tetrabutyl-titanate is added. Before the addition, care is taken to separate all the water formed during chemical reaction from the system. The evolution of reaction takes place and water formed is continuously & carefully separated in the alcohol water separator. The temperature in the reactor is further increased upto 220-235oC to terminate the Esterification and the Raw DOP is obtained.
Neutralization
After esterification process, neutralization is carried out with Sodium carbonate (caustic soda flakes) wherein small amount of water is added in order to neutralize the traces of monoester.
Distillation
The neutralized DOP is then transferred to the distillation section which consists of a reactor equipped with the stirrer, vapors condenser, cooler and alcohol water separator. The alcohol is distilled first under mild vacuum distillation and at the end with vacuum distillation and steam stripping. Further, DOP is dried under vacuum.
Filtration
In this phase, solids formed during neutralization and hydrolysis of the catalyst is removed by filtration process and finished product is obtained.
Note: Other types of Plasticizers as shown in product list – table are produced using same methodology &equipment using different raw materials.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 25
3.5 RAW MATERIAL FOR FINISHED PRODUCTS The raw materials for the proposed range of products will be indigenously available and will be also imported. Table 3.2: List of Raw Materials
Product Name of Raw Material Requirement (MT/Month) Existing Proposed
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 26
3.5.1 HAZARDOUS CHEMICAL STORAGE & HANDLING Hazardous chemicals are/will be used as raw material in the manufacturing process. Storage, handling & transport of Hazardous Chemicals are given in table 3.3 Table 3.3: Storage, Handling & Transport of Hazardous Chemicals Raw Material Source CAS/CS No Means
of storage
Means of transport
Max. Qty.
stored MT
Raw Material Soyabean Oil Indian/ Imported 801-22-7 Tank By road 40Formic Acid Indian/ Imported 64-18-6 Tank By road 10Hydrogen Peroxide Indian/ Imported 7722-84-1 Tank By road 20Sodium Hydroxide Indian/ Imported 1310-73-2 Bags By road 1Methanol Indian/ Imported 67-56-1 Drum By road 1Sodium Methoxide Indian/ Imported 124-41-4 Bags By road 1Polymer Resin Indian/ Imported -- Bags By road 20Polymer Compound Indian/ Imported -- Bags By road 10Master Batch Indian/ Imported -- Bags By road 2Stabilizer Indian/ Imported -- Bags By road 5HDPE Indian/ Imported 9002-88-4 Bags By road 10Phthalic Anhydride Indian/ Imported 85-84-9 Bags By road 202 Ethyl Hexanol Indian/ Imported 140-76-7 Tank By road 20Normal Butanol (NBA) Indian/ Imported 71-36-1 Tank By road 20Iso-Butanol Indian/ Imported 78-83-1 Tank By road 20Maleic Anhydride Indian/ Imported 108-31-6 Bags By road 10Adipic Acid Indian/ Imported 124-04-9 Drum By road 1
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 27
3.6 RESOURCE OPTIMIZATION & AVAILABILITY The major resources for the proposed project are/will be raw-materials, water, man-power, etc. 3.6.1 LAND & BUILDING REQUIREMENT Total existing plot area is 6761.00 m2 and total existing constructed area is 1725.00 m2. No
additional land will be required for proposed project expansion.
The existing built up area will be utilized after necessary modifications also some new sheds will
be constructed and ETP will have to be modified. After necessary modification & construction,
constructed area will be 2475.00 m2. Plot allotment document is attached as Annexure-3.
3.6.2 EQUIPMENT Some additional equipment will be needed for the proposed expansion. Table 3.4: List of Equipment Sr. No. Equipment Capacity No.Existing 1 SS 316 11 MT 12 SS 316 7 MT 13 SS 316 3.6 MT 14 SS 304 10 MT 15 Vaccum pump --- 16 Filter press --- 1Proposed additional 1 SS 316 15 MT 22 Thermo pack 10 Lakh K cal/Hr. 13 Receiver SS 316 --- 34 Condenser SS 316 --- 2
*Presently, out of 6.0 KLD water used for gardening 3.8 KLD is fresh water and 2.2 KLD is ETP treated water. After the proposed expansion, the total cooling water and gardening water requirement will be met by recycling the ETP treated water.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 29
3.6.5 MAN-POWER REQUIREMENT The total number of man power for existing project is 24 persons, for proposed expansion
project additional 16persons will be required. Hence, the total man-power will be 40.
The man-power required for the project is/will be employ locally from the nearby areas. Skilled
as well as unskilled labour will be employed for the project.
3.7 QUANTITY OF WASTE TO BE GENERATED
3.7.1 WASTEWATER GENERATION & MANAGEMENT The category wise bifurcation of the wastewater generation is given in Table 3.7. Table 3.7:Category-wise Wastewater Generation (in KL/D)
S.No. Particulars Waste Water Generation Existing Proposed
Additional Total
1. Domestic 4.0 2.4 6.42. Industrial 3. Process water Nil 43.4 43.44. Cooling (Blow down) 1.0 2.0 3.05. Boiler (Blow down) 0.2 0.4 0.66. Washing 1.0 3.0 4.07. Sub-Total: Industrial 2.2 48.8 51.08. Grand Total 6.2 51.2 57.4
Domestic wastewater generated from the plant is/will be disposed of through septic tank/soak
pit system.
The wastewater from the utility section is given primary treatment. The wastewater after pH
correction is passed through netuch filter and thereafter collected into the collection tank. The
treated water is then utilized for gardening purpose. Hence, there is no discharge of treated
effluent.
There is no industrial wastewater generated from existing industrial activity.
After proposed expansion, industrial effluent generated will be treated in Effluent Treatment
Plant and treated effluent will be reused in cooling & gardening purpose. Hence, there will be no
discharge of treated effluent outside the company premises.
The category wise bifurcation of the waste water generation is given in Table 3.7
3.7.2.3 Fugitive Emission Minor quantity of fugitive emissions will occur during handling of the raw materials. Fugitive emissions are also likely to occur from storage area.
Following measures will be practiced to reduce the fugitive emissions:
• Raw Materials & Products are/will be stored under good storage conditions to prevent any volatilities
• Raw Materials & Products are/will be stored in closed containers • The fugitive emissions in terms of handling losses will get reduced by proper storage
and handling. • Regular monitoring is/will be done of piping and fittings for checking of any leakages. • Hazardous chemicals are/will be stored as per standard criteria. • Good housekeeping maintained in the plant.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 32
3.7.3 HAZARDOUS/NON-HAZARDOUS WASTE MANAGEMENT Hazardous wastes generated will be in the form of ETP waste from Effluent Treatment Plant,
Used oil from gear boxes of the machineries and discarded bags/drums. Company has provided
adequate storage area for proper storage of wastes.
Table 3.9: Details of Hazardous Waste Generation & Disposal
Type of waste & Category
Existing Scenario
Proposed Scenario
Disposal Method
ETP Waste (Cat. 34.3)
0.037 MT/Month 10 MT/Month Company has provided adequate storage area. The ETP waste generated is/will be stored properly and finally disposed of to CSWD site of VWEMCL, Vapi.
Used Oil (Cat. 5.1)
30 L/Year 30 L/Year The used oil is/will be collected & stored separately and reused as lubricant in plant operation.
Discarded bags (Cat. 33.3)
280Nos/Month 11500Nos/Month The discarded bags are/will be stored separately in company premises and are/will be reused for packing / sold to the authorized scrap dealers.
Discarded drums (Cat. 33.3)
2000Nos/Month 2285Nos/Month The discarded drums are/will be stored separately in company premises are/will be returned back to the supplier / sold to the authorized re-conditioners.
3.7.4 NOISE AND ODOUR CONTROL There is/will be no major activities due to which noise would be generated other than
equipment’s, boiler & pumps. However, Noise level generation would be limited to 75dB (A)
within plant. No offensive odour is/will be generated from the process.
The control measures to be taken for reduction in noise levels are as below:
Ear Plugs and Ear muffs are provided to the workers in Utility Section.
Anti-vibration pads are/will be provided wherever applicable.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 34
CHAPTER – 4
SITE ANALYSIS 4.1 CONNECTIVITY
The Industry is located at Plot No. 16-19 GIDC Vapi, Dist. Valsad. This proposed expansion
project will be accommodated in the existing site. The site is very well connected by national
highway and railway. Efficient transport facilities will be available nearby the project site.
4.2 LAND FORM, LAND USE & LAND OWNERSHIP 4.2.1 LAND FORM The proposed expansion project will be accommodated in the existing site located in GIDC Vapi. 4.2.2 LAND USE PATTERN It is a developed industrial estate for industrial development.
4.2.3 LAND OWNERSHIP The plot is located in GIDC Vapi. The company has obtained it on lease from GIDC. 4.3 TOPOGRAPHY
The Topography of the region consists of flat topped, highly dissected plateaus and dyke ridges
running in a west to east direction. The Main River (Damanganga) in the catchment area flows
in incised meanders forming steep geomorphologic ally ‘V’ shaped valleys with steep sides. The
entire catchment has a rectangular and trellis pattern of drainage depicting the influence of the
structures on the drainage development. The piedmonts at the base of the steep plateaus and
dyke ridges are covered with thin soils, which support agriculture in very few areas. The river
valley, wherever flat, has good quality soil and is mostly cultivated based on the availability of
water. The river valley fills with thick alluvium provides the only area for cultivation.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 35
4.4 SALIENT FEATURES The salient features of the project site are given in the table below: Table 4.1: Salient Features of the Project Site Particulars Details Co-ordinates 20°21'2.76"N, 72°54'47.79"E Village Vapi Town≈ 2.50 km (NW) Taluka/ Tehsil Pardi District Valsad Nearest Water body Damanganga River Nearest Highway N.H.- 8≈ 0.42 km Nearest Railway station & Railway line Vapi Railway Station ≈ 2.43 km (NW) Nearest Airport/ Airbase Daman Coast Guard ≈ 11.40 km (NW) State/ National borders Daman & Dadra Nagar Haveli(D&NH) Protected Area/ Sanctuaries None within 15 km CRZ applicability Not applicable Seismicity Seismic Zone III Note: All the above mentioned distances are the aerial distance from the project site.
4.5 EXISTING INFRASTRUCTURE The plot is located in the industrial estate. It has been developed for industrial purpose. Existing
infrastructure includes provisions of water, power, storage facilities for raw-material and
products and production, utility sheds and administrative office
4.6 CLIMATE & METEROLOGY The climate is characterized by oppressive summer dampness in the atmosphere nearly
throughout the year, heavy south–west monsoon rainfall and a mild winter. The year can be
divided into four seasons. The winter season from December to February is followed by the
summer season from March to May. The South-West monsoon season is from June to
September. The post-monsoon season constitutes the months of October and November.
The Table 4.2 indicates the summary of meteorological pattern at the nearest observatory of
Indian Meteorological Department (IMD), Dahanu and is taken from the book “Climatological
tables of Observatories in India (1951 - 1980)” published by IMD.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 36
Table 4.2: Summary of Meteorological Data at nearest IMD Station –Dahanu.
Location: Dahanu Gujarat ( Lat: N 19o 58’, Long: E 72o 43’) Aerial Dist from Project Site: Approx.37 Km SSW Height of installation: 29 m above MSL, Month Temperature
(oC) Relative Humidity
(%) Cloud Cover
(Oktas) Mean Wind
Speed (km/h)
Pre-dominant Wind
Direction
Rainfall (mm)
Max. Min. Mor. Eve. Mor. Eve. January 27.7 16.5 67 69 1.3 1.1 11.3 N 0.2 February 28.3 17.4 66 69 1.1 0.8 11.7 N 0.2 March 30.3 20.7 68 67 1.4 1.1 12.9 N 0.1 April 32.2 24.0 74 69 2.1 1.4 13.7 W 0.1 May 33.1 26.8 77 73 3.8 2.3 15.5 W 5.2 June 32.2 26.3 85 80 6.1 5.6 17.7 SW 522.1 July 30.1 25.0 89 84 7.1 6.8 22.6 SW 771.7 August 29.5 24.7 88 83 6.9 6.7 22.6 W 502.3 September 30.0 24.0 87 79 5.4 4.9 14.6 W 319.1 October 32.1 23.1 77 72 2.8 2.4 10.0 E 44.4 November 32.1 20.5 67 71 1.9 1.9 9.4 N 17.1 December 29.8 18.0 67 71 1.6 1.5 10.0 N 0.3 Seasonal Average Values Period Temperature
(oC) Relative Humidity
(%) Cloud Cover
(Oktas) Mean Wind
Speed (km/h)
Avg. PDW Direction
Total Rainfall (mm)
Avg. Max.
Avg. Min.
Avg. Mor.
Avg. Eve.
Avg. Mor.
Avg. Eve.
Summer 31.9 23.8 73.0 69.7 2.4 1.6 14.0 W 5.4 Winter 28.6 17.3 66.7 69.7 1.3 1.1 11.0 N 0.7 Monsoon 30.5 25.0 87.3 81.5 6.4 6.0 19.4 SW 2115.2 Post monsoon 32.1 21.8 72.0 71.5 2.4 2.2 9.7 N/E 61.5 Annual Total or Mean
30.7 21.9 74.7 73.1 3.1 2.7 13.5 W 2182.8
Note: Winter: December, January & February, Summer: March, April & May, Monsoon: June, July, August & September, Post monsoon: October & November (Source: Book “Climatological tables of Observatories in India (1951 - 1980)” published by IMD)
4.6.1. TEMPERATURE
The summer season from March to May is a one of continuous increase in temperatures which
decreases during monsoons, increases slightly during the post-monsoon season and again
decreases during the winter.
4.6.2. HUMIDITY
The climate of the region is characterized by a humid summer because of the closeness to
coastline. Humidity is usually high during the monsoon months, with average relative humidity
generally exceeding 80%. Humidity decreases gradually during the post-monsoon months and
for rest of the year i.e. the period of December to April, the average relative humidity ranges
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 38
Figure 4.1: Village Map of Study Area
4.7.1 EDUCATIONAL FACILITIES
As per Census 2001 Educational facilities are available and the literacy rate is above 72% within
5 km periphery. All the villages have a minimum of one primary school.
4.7.2 MEDICAL FACILITIES As per census 2001, Details of medical facilities available in the study area are given below.
Table 4.3: Details of Medical facilities
Sr.No. Particulars Observed values in 5 km radius1 Dispensaries 02 Primary Health Centers 13 Primary Health sub centre 84 Allopathic Hospital 05 Allopathic dispensary 26 Maternity and Child welfare Centre 17 Community Health Workers 4
(Source: Primary Census Abstract – Census of India, 2001)
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 39
CHAPTER – 5 PLANNING BRIEF 5.1 PLANNING CONCEPT The proposed project is located at GIDC Vapi. Major raw materials are/will be sourced locally.
RM cost as many input suppliers are located nearby which will bring reduction in transportation
cost. The region is well planned with all the basic infrastructural facilities like internal roads,
water supply, arrangements for power, streetlights, solid waste disposal sites etc.
5.2 POPULATION PROJECTION As per census 2001, the average household size is around 4 persons. The demographic profile
of study area presented below.
Table 5.1: Distribution of population
Sr. No. Particulars Observed values in 5 km radius1 Total Population 2171332 No. of Households 514033 Avg. household size (person) 4.224 Male population 1270535 Male population (in %) 58.516 Female population 900807 Female population (in %) 41.498 Sex ratio 709.00
(Source: Primary Census Abstract – Census of India, 2001)
5.3 AREA STATEMENT The total area of the plot is 6759.68m2 out of which constructed area of the plant is 1722.60 m2. After additional construction in existing land area constructed area will be 2427.60 m2. 5.4 ASSESMENT OF INFRASTRUCTURE DEMAND (PHYSICAL & SOCIAL) This is an expansion project which is to be developed in the existing premises. No additional
land is required for the proposed project except few installations and modifications. So there will
be no demand of major change in physical infrastructure and social infrastructure.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 40
5.5AMENITIES/FACILITIES 5.5.1 DRINKING WATER FACILITIES All the villages have potable water supply through taps and also potable water is sourced from wells and tube wells as secondary source. 5.5.2 POWER SUPPLY FACILITIES As per census 2001, all the villages have power supply facilities in the study area. 5.5.3 COMMUNICATION& BANKING FACILITIES As per census 2001, the information collected clearly indicates that the infrastructural facilities
are provided by respective government agencies for the development of this area. For
communication purposes, post office and phones are available in most of the villages. The
villages having non-availability of these facilities within 5km distance.
5.5.4 TRANSPORT FACILITIES As per census 2001, bus service is available in all the villages of the study region within 5 km
area and is the most preferable mode of the transport in the region Second option for transport
is auto rickshaw.Villages connected with paved roads.
5.5.5 APPROACH TO VILLAGES As per census 2001, most of the villages have paved road in the study region.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 41
CHAPTER – 6
PROPOSED INFRASTRUCTURE 6.1 INDUSTRIAL AREA The total area of the plot is 6761.00 m2 out of which constructed area of the plant is 1725.00 m2
and proposed construction 750.00 m2 will be done in existing area. The total production capacity
will be 2716.2 MT/month with byproducts after proposed project.
6.2 RESIDENTIAL AREA In the said proposal no residential area has been proposed for workers and/or for staff. 6.3 GREENBELT In existing operation company has developed a healthy green belt in1600 m2 area. Maximum
possible open land will be allotted for green belt development.
6.4 SOCIAL INFRASTUCURE Existing infrastructure will be sufficient to accommodate the existing load from the proposed
project which is very low.
6.5 CONNECTIVITY This proposed expansion project will be accommodated in the existing site. The site is very well
connected by national highway and railway. Efficient transport facilities will be available nearby
the project site.
6.6 DRINKING WATER MANAGEMENT Drinking water is/will be sourced from GIDC Water supply.
6.7 SEWERAGE SYSTEM Domestic wastewater generated from the existing and proposed project is/will be disposed of
through septic tank/Soak pit system, which is @4.0 KL/D for existing plant and @6.4 KL/D after
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 43
CHAPTER – 7
REHABILITATION &RESETTLEMENT (R &R) PLAN 7.1 POLICY TO BE ADOPTED The proposed project is to be developed in the existing premises.Hence, no displacement of
any population is proposed for the project. Therefore, detailed Social Impact Assessment
studies or R&R action study has not been proposed.
Project: Proposed expansion project for manufacturing of Synthetic Organic Chemicals 44
CHAPTER – 8
PROJECT SCHEDULE & COST ESTIMATES 8.1 TIME SCHEDULE OF THE PROJECT At present we are not proposing any additional production at the site. It will start only after
getting all the statutory permission from respective authorities.
8.2 ESTIMATED PROJECT COST The company has made budgetary provision for the recurring expenses for the environmental
issues and Environment Protection has also been considered in planning the cost projection.
The existing cost projection is 97.2Lakh and after proposed project expansion project the
estimated cost bifurcation table is given below:
Table 8.1: Total Capital Cost Projection
Sr. No. Purpose Proposed Expansion Cost (Rs. in Lakhs)
1. Land Nil2. Building 203. Plant & Machinery 2504 Electrification and Administrative set-up 105. ETP 50
Air pollution control device 106. Safety instruments 57. Chartered services/ Government fees 5 TOTAL 350