M/s. INDIAN OIL CORPORATION LIMITED

Transcription

1 PRE-FEASIBILITY REPORT For Proposed Expansion Project LPG IMPORT FACILITY By M/s. INDIAN OIL CORPORATION LIMITED At Village: Bhitagarh, Paradip, Tehsil: Kujang, District: Jagatsinghpur, State: Odisha Head Office: M/s. INDIAN OIL CORPORATION LIMITED G-9 Indian Oil Bhavan, Ali Yavar Jung Marg, Bandra East, Mumbai GREEN CIRCLE, INC. Integrated HSEQR Consulting Engineers, Scientists & Trainers (MoEF Recognized Environment Laboratory) (An ISO: 9001, 14001, NABL/17025:2005 OHSAS: Certified Organization & GPCB approved Environment Auditor Schedule II) Gujarat High court stay order for QCI NABET No. C/SCA/10311/2012 dated 20/01/2015) Corp. Office & Environmental Research Laboratory Green Empire (Anupushpam), Above Axis Bank, Nr. Yash Complex, Gotri Road, Vadodara (Gujarat) India Tel: ALSO AT E: info@greencircleinc.com BENGALURU RUDRAPUR NEW DELHI HYDERABAD PUNE RAIPUR KOLKATA GOA OVERSEAS AUSTRALIA OMAN KUWAIT AFRICA VIETNAM

2 TABLE OF CONTENTS Sr. No. Particulars Page No. 1 Executive Summary 3 2 Introduction of the Project/Background Information 3 3 Project Description 5 4 Site Analysis 20 5 Planning Brief 21 6 Proposed Infrastructure 23 7 Rehabilitation and Resettlement (R & R) Plan 23 8 Project Schedule & Cost Estimates 23 9 Analysis of Proposal (Final Recommendations) 24 LIST OF TABLES Table. No. Particulars Page No. 1 Employment Details 5 2 Detail of Proposed Project 8 3 Design Basis of Raw Materials 17 4 Water Requirement & Wastewater Generation 17 5 Source of Electricity 18 6 Fuel Requirement 18 7 Environmental Settings 20 8 Land Use Planning 21 LIST OF FIGURES Fig. No. Particulars Page No. 1 Location Map of Proposed Project 6 2 Specific Location & Project Boundary 6 3 Plant Layout 7 Pre-Feasibility Report 2

3 1.0 EXECUTIVE SUMMARY The Indian Oil Corporation, a Central Public Sector Undertaking attached to Ministry of Petroleum and Natural Gas, Govt. of India is planning to expand storage and handling of LPG by setting up LPG Import Facility in the existing LPG Marketing Terminal premises based on the international supply / Indian demand scenario of LPG & its constituents (Propane & Butane). Mounded bullets for bulk Butane & Propane storage (20 Nos. x 2,000 MT) will be set up for storage purpose. It can be seen that deficit of LPG in the country will be increasing year after year and therefore, sufficient LPG import infrastructure is essentially required to meet the demand. In Eastern Region, we have only one LPG import facility at Haldia which is being stretched to almost double the rated capacity. There is also problem of severe draft as well as jetty availability at Haldia affecting smooth supply of LPG. It is, therefore, proposed to construct LPG Import Facility at Paradip within the existing LPG marketing Terminal premises. LPG will be imported in VLGCs at South Oil Jetty constructed by Paradip Refinery where space for putting up Butane / Propane unloading facility is available. Imported Butane / Propane would be transferred to LPG Import Facility through 2 nos. underground pipelines. Imported Butane and Propane will be stored in aboveground mounded storage vessels and sent to market as LPG after blending of Butane & Propane. The proposed expansion project is located at Plot nos. 240, 241, 254, 256, 257, 258, 253, 255, 243, 245, 246, 247, 248, 249, 259, 260, 236, 237, 239, 242, 187, Khata No- 1&3, Bhitargarh area of Jagatsinghpur district in Odisha State. The coordinates of site is N, E. The total area covered by the proposed expansion project is 2,13,269 sq.m of which 37 % (79,237 sq.m) is for greenbelt development. Overall the project will have a positive development in terms employment generation, infrastructure and socio-economic development. The company will roll out CSR activities. 2. INTRODUCTION OF THE PROJECT/BACKGROUND INFORMATION 2.1 Identification of project and project proponent Identification of project The Proposed Expansion of LPG Marketing Terminal is located at Plot nos. 240, 241, 254, 256, 257, 258, 253, 255, 243, 245, 246, 247, 248, 249, 259, 260, 236, 237, 239, 242, 187, Khata No- 1&3, Bhitargarh area of Jagatsinghpur district in Odisha State. The total area of project including proposed expansion is 52.7 Acre Project Proponent Indian Oil Corporation Limited (IOCL), the largest commercial undertaking in India and a Fortune 'Global 500' company, is engaged in the business of refining, transportation and marketing of petroleum products. As a group, IOCL owns and operates ten refineries in India Pre-Feasibility Report 3

4 with a total capacity of over 1.3 million BPSD. It also owns and operates a wide network of crude & products pipelines. It has its own Research & Development Centre situated at Faridabad, Haryana, near New Delhi. Indian Oil and its subsidiaries account for a 49% share in the petroleum products market, 31% share in refining capacity and 67% downstream sector pipelines capacity in India. The Indian Oil Group of companies owns and operates 10 of India's 22 refineries with a combined refining capacity of 65.7 million metric tonnes per year. In FY 2012 IOCL sold million tonnes of petroleum products and reported a PBT of Rs billion, and the Government of India earned an excise duty of Rs billion and tax of INR10.68 billion. 2.2 Brief description of nature of project IOCL is has set up (in first phase) new LPG Marketing Terminal at Paradip, Odisha in order to store and distribute LPG production of IOCL Refinery at Paradip. In Phase-II, IOCL is planning to expand storage and handling of LPG by setting up LPG Import Facility in the existing LPG Marketing Terminal premises based on the international supply / Indian demand scenario of LPG & its constituents (Propane & Butane). Mounded bullets for bulk Butane & Propane storage (20 Nos. x 2,000 MT) will be set up for storage purpose. The estimated cost of the project is Rs. 690 crore. The project falls under category B, section 6(b) Isolated storage & handling of hazardous chemicals of EIA notification 2006 and subsequent amendments. Hence Environment Clearance is applicable to the proposed project. 2.3 Need of project and its importance to the country and or region India is presently deficit in LPG and industry is dependent on imports to meet domestic demand. Total LPG imports for and stood at about 5.8 MMT and 6.3 MMT respectively. As per projections made by Petroleum Planning & Analysis Cell (PPAC), LPG demand is projected to grow at a CAGR of 2.6% during XIII Five Year Plan. (Fig. In TMT) Year Demand Considering above demand and available indigenous supply position, the deficit of LPG for the period is projected as under (Fig. In TMT) Year Demand Pre-Feasibility Report 4

5 It can be seen that deficit of LPG in the country will be increasing year after year and therefore, sufficient LPG import infrastructure is essentially required to meet the demand. In Eastern Region, we have only one LPG import facility at Haldia which is being stretched to almost double the rated capacity. There is also problem of severe draft as well as jetty availability at Haldia affecting smooth supply of LPG. It is, therefore, proposed to construct LPG Import Facility at Paradip within the existing LPG marketing Terminal premises. LPG will be imported in VLGCs at South Oil Jetty constructed by Paradip Refinery where space for putting up Butane / Propane unloading facility is available. Imported Butane / Propane would be transferred to LPG Import Facility through 2 nos. underground pipelines. Imported Butane and Propane will be stored in aboveground mounded storage vessels and sent to market as LPG after blending of Butane & Propane. With increased availability of LPG at Paradip through imports, LPG can be moved through upcoming Paradip-Haldia-Durgapur-Barauni-Patna-Muzaffarpur pipeline to LPG bottling plants in West Bengal and Bihar. 2.4 Employment Generation (Direct and Indirect) due to project LPG Import Facility proposed to be set up by M/s. Indian Oil Corporation Ltd. (MD) will generate indirect employment for local people. It will also generate ancillary business to some extent for the local population. In operation phase, the proposed project would require nominal workforce of non-technical and technical persons as given below Table 1: Employment Details Sr. No. Descriptions Existing Proposed Total 1 Regular Employees Contract workers Security Staff Total (approx) PROJECT DESCRIPTION 3.1 Type of Project including interlinked and interdependent projects, if any The site is located near Bittargarh village, Jagatsinghpur district, Odisha State. The proposed site is approx.12 km north of IOC s Paradip Refinery Project (PDRP) site. The plot adjacent to existing IOC s POL terminal at Paradip and is bounded by Paradip Port Trust (PPT) land towards East, PPT s Water Reservoir towards north, IOCL existing POL terminal & BPCL Oil terminal towards south, and Water canal & 8m approach road of Paradip Phosphates Ltd. (PPL) towards west. The proposed site measures 52.7 acres. There is no interlinked project with this proposed unit. 3.2 Location (map showing general location, specific location and project boundary & project site layout) with coordinates. Pre-Feasibility Report 5

6 1. Coordinates of project site : Latitude N, Longitude E Fig. 1: Location Map of Proposed Project Fig. 2: Specific location & Project boundary of proposed site Pre-Feasibility Report 6

7 2. Project site layout Figure 3: Plant Layout 3.3 Details of alternate sites considered and the basis of selecting the proposed site, particularly the environmental considerations gone into should be highlighted Alternative sites have not been considered for proposed project as this is a part of expansion of the existing site Major factors involved in the selection of site are listed below: The project site is located within the premises of existing LPG Marketing Terminal. Site is level ground, which does not require any land filling. Site is well connected by road. Power, water and manpower are already available at existing LPG Marketing Terminal. The site is located near sea and ship unloading facility is already available in form of South Oil Jetty. 3.4 Size or Magnitude of Operation The existing LPG marketing terminal consists of 3 mounded bullets each of 600 MT capacity for storage of LPG. IOCL is planning expansion of existing LPG Marketing Terminal premises by setting up LPG Import Facility having approx. storage capacity of 20,000 MT Butane and 20,000 MT Propane. In 20 nos. mounded bullets of 2,000 MT capacity each. LPG will be produced by blending of Butane & Propane for subsequent dispatch to other locations by road in tank trucks Pre-Feasibility Report 7

8 and by pipeline. Table 2: Detail of Proposed Project Description Existing Capacity Proposed Capacity Bulk LPG storage facility Mounded bullets: 3 Nos. x 600 MT (1800 MT bulk Storage) Mounded bullets: 20 Nos. x 2,000 MT (40,000 MT bulk Butane & Propane Storage) Size of each tank 6.0 M dia., 48.2 M length 8.0 M dia., 90.5 M length Process Description 1.1 Unloading & Handling facilities at South Oil jetty: Each consignment of 10,000 to 20,000 MT refrigerated liquid Propane at -42 C (min.) and Butane at -4 C (min.) shall be unloaded from ship at a rate of 1,000 MT/hr (max.) with the help of ship unloading pumps through two numbers of 14 marine unloading arms. The refrigerated product shall be heated to approx. 15 C by sea water shell and tube heat exchanges & shall be transferred to propose atmospheric Propane / Butane storage tanks at proposed IOCL LPG Import Facility through 2 nos. 16 transfer lines. Booster Pumps may be used for transfer of Butane and Propane through pipelines. 1.2 Pipeline transfer facilities: Both the 16 lines shall be employed for transfer operation of Propane / Butane from Ship. Mass flow meters shall be provided for mass measurement. Adequate safety measures shall be deployed by way of automation and emergency shutdown of unloading and transfer operations by way of motor operated valves etc. in case of any eventuality. Gas detection and fire fighting facilities as per OISD standards shall be provided. 1.3 Receipt & Storage of product at LPG Import Facility: The Propane / Butane unloaded from ship will be stored in 20 nos. pressurised mounded storage bullets 10 nos. each for Propane and Butane. The Mounded Vessels shall be fabricated & installed as per OISD-150. The mechanical design of storage vessel shall be based on following considerations: i. Design Code - ASME SEC. VIII or PD or equivalent duly approved by PESO. A single code shall be adopted for design, fabrication, and inspection and testing. The specific consideration shall be given to a) Internal vapour and hydraulic pressure b) External loadings on the vessel c) Internal vacuum ii. Material - The material of construction for bullets shall be IS:2041 Grade R-355 conforming to design code. Pre-Feasibility Report 8

9 iii. Design Temperature will be (-)42 o C to (+)55 o C. iv. Design Pressure will be 21 kg/cm2 g. v. Other Considerations a) Internal Corrosion Allowance: 1.5 mm (minimum) b) Radiography: Full c) Stress Relieving: 100% irrespective of thickness. d) Earthquake pressure as per IS:1893 e) Hydrotest pressure: As per Design Code Cathodic protection shall be provided to protect the external surface of the bullet from corrosion. Fire safe Remote Operated Valve(s) (ROVs) shall be provided on first flange on liquid line(s) at a minimum distance of 3 m from the vessel. Each vessel has two safety relief valves (SRVs). Each storage vessel shall have minimum two different types of level indicators and one independent high level switch. Each vessel will be provided with one pressure and temperature measuring instrument. 1.4 Blending & Mercaptan dosing at LPG Import Facility: Propane being pumped from propane bullets and Butane from butane bullets shall be blended to form LPG in the blending skid. Blended LPG will be dosed with mercaptan through online automatic dosing system before being sent to market or for pipeline transfer. 1.5 Despatch from LPG Import Facility: Tank truck Loading: Blended LPG will be sent to existing LPG truck loading facility where it can be simultaneously loaded in 8 nos. tank trucks in TLF bays. Mass flow meters are already installed in each TLF bay Pipeline Transfer : Blended LPG after mercaptan dosing will also be sent to different LPG bottling plants in West Bengal and Bihar through upcoming Paradip-Haldia-Durgapur-Barauni-Patna- Muzaffarpur pipeline. 1.6 Utilities: Sea water shall be used for heating of Propane and Butane at Jetty with help of sea water pumps of adequate capacity. At LPG Import Facility, cooling water shall be required for cooling of Process pumps. Existing cooling water pumps and cooling towers shall be used for the purpose. Pre-Feasibility Report 9

10 Instrument air required for pneumatic actuation of remote operated valves and operation of fire fighting deluge valves shall be provided through air compressors along with air dryer & air receiver tank. 1.7 PROCESS PARAMETERS Unloading & handling facilities at South Oil jetty: Ship unloading frequency Ship parcel size, MT Ship berthing time, hrs Unloading by Unloading rate, TPH 3 to 4 Ship s in a month 10,000 to 20,000 (Typical) 25 (Max) 2 Nos of 14 Marine Unloading Arm 1,000 (max) Seawater Intake Pumps Number Type Capacity of each pump m3/hr 1000 Discharge Pressure kg/cm2 (g) Working + 1 S in case of 1000 TPH of Propane unloading / 2W + 2S in case of 1000 TPH of Butane / 3 Working + 1 S in case of 500 TPH Propane and 500 TPH Butane Vertical Submersible Seawater Heat Exchangers Number Type Thermal Capacity of each Heat exchangers 2 Working in case of 1000 TPH of Propane unloading / 1W + 1S in case of 1000 TPH of Butane / 2 Working in case of 500 TPH Propane and 500 TPH Butane Shell and Tube Heat exchanger M kcal /hr for each exchanger Pipeline transfer facilities Unloading through 2 Nos of 16 transfer lines Receipt & Storage facility at LPG Marketing Terminal Storage Capacity of each Bullet : MT 2,000 No. of Mounded Bullet 10 Propane + 10 Butane Size 8 m dia x 90.5 m length (Storing capacity specified above is based on filling up to 85% of vessel diameter.) Pre-Feasibility Report 10

11 1.7.6 Despatch Facilities at LPG Marketing Terminal Tank Trucks Loading to Loading temperature, ºC Loading by No. of loading Station Pumping Rate, MT/hr 150 Pipeline Transfer Loading to Loading temperature, ºC Loading by Pumping Rate, MT/hr Un-insulated road tankers. 15 / Ambient LPG / Propane / Butane transfer pumps Existing 8 bays TLF 12 dia. Existing LPG transfer pipeline to Refinery for onward pumping into Paradip-Haldia-Durgapur- Barauni-Patna-Muzaffarpur pipeline 15 / Ambient LPG / Propane / Butane transfer pumps 400 (Approx.) Propane / Butane Transfer Pump: Type Flow, m3/hr MOC Vertical Can Type with double mechanical seal 220 (2W + 1S) Each for Propane & Butane LTCS 1.8 Space for facilities at South Oil Jetty : Space for Unloading arms Propane / Butane Unloading arms shall be installed in the space allotted for future loading arms. Adequate space is available in South Oil Jetty Space for Sea water shell and tube heat exchangers : Approx. 10 m x 8 m space is required for installing sea water shell and tube heat exchangers with associated piping and instrumentation for heating the cryogenic propane and butane to approx. 15 deg C. Space is available in back-up area of Jetty Space for Sea water intake pumps : Approx. 16 x 12 m space is required for installing sea water intake pumps for heating the cryogenic propane / butane. These pumps are to be located on the fire water jetty. For this purpose existing building is to be extended by 12 m towards the back-up area side Space for Electrical panels : Approx. 4 m x 2 m space is required for accommodating the LT panels for the sea water intake pumps which will be available after extension of fire pump house building. Pre-Feasibility Report 11

12 1.8.5 Space for DG set : Approx. 8.5 m x 3.5 m space is required for accommodating 1,000 KVA DG sets Space for Control Room : Space for instrument panels and consoles are available Space for N2 Bottles : Presently N2 bottles are located in the jetty for polypropylene unloading arms. Same can be shared for the Propane / Butane unloading arms. Alternatively N2 bottles for Propane / Butane unloading arms can be located along with the present facility. 1.9 LPG evacuation pipeline from Import Terminal to Paradip to Durgapur Pipeline Reconnaissance survey was carried out in Paradip by TCE along with IOCL, LPG Engineering to identify the possible pipeline routes. Options of pipeline routing depend on the location of the Main Pumping Station of Paradip Durgapur Pipeline. Hence detailed discussion were held with IOCL, Pipeline division / IOCL, Refinery division / IOCL, LPG Engineering and TCE for identifying the various options available LPG evacuation to Durgapur / Haldia. 3.6 Raw Material required along with estimated quantity, likely source, marketing area of final product/s, mode of transport of raw material and Finished product. Butane & propane will be imported through sea vessels at South Oil Jetty, transported to LPG Import facility through underground pipeline and stored in mounded type storage vessels. Table 3: Design Basis of Raw Materials Sr. No. Parameter Propane Butane 1.0 Product Specification 1.1 Composition (wt %) Propane Iso-Butane N-Butane Other Resource optimization/recycling and reuse envisaged in the project, if any, should be briefly outlined. The sources of waste water from the proposed terminal are from canteen facilities and office building. The waste water is treated in sewage treatment plant and is reused for gardening and other activities like toilet flushing and cleaning purposes. Zero discharge is proposed for the terminal project. There is no process effluents generated. Hence impact on water quality from the proposed project is insignificant. Pre-Feasibility Report 12

13 3.8 Availability of water its source, energy/power requirement and source should be given Water Source The source of water for the proposed project shall meet through Bore wells. Total water requirement for the proposed expansion project will be KLD (Existing KLD & Proposed-12 KLD) KLD sewage will be treated in existing STP (Capacity-10.5 KLD). No trade effluent generate from the operation. Details of water consumption and waste water generation are tabulated in Table 3. Table 4: Water Requirement & Wastewater Generation Sr. No. Type of use Water Consumption (KLD) Waste Water Gen. (KLD) Existing Proposed Total Existing Proposed Total 1 Domestic Plant Cooling Gardening/Floor 4 washings and Fire water makeup TOTAL ELECTRICITY & FUEL REQUIREMENTS Electricity shall be obtained from Paradip Refinery. HSD shall be used as a fuel for D.G sets. The total power & fuel requirement for the proposed project is given in Table 4 & Table 5. Table 5: Source of Electricity Sr. No. Source Existing Proposed 1. Paradip Refinery 881 KVA 319 KVA 2. D.G Set (Stand By) 1 X 750 KVA & 1 X 320 KVA 1 X 750 KVA Table 6: Fuel Requirement Sr. No Name of Equipment Name of Fuel & Requirement Capacity Type of Emission Stack Height (M) from Ground Level Stack Diameter (M) 1 DG Set HSD & 90 L/hr 2 x 750 KVA CO2, NOx, SOx DG Set HSD & 30 L/hr 320 KVA CO2, NOx, SOx Pre-Feasibility Report 13

14 3.9 Quantity of wastes to be generated (liquid and solid) and scheme for their management/ Disposal Waste Water generation & Management plan The sources of waste water from the proposed terminal are from canteen facilities and office building. The waste water is treated in sewage treatment plant and is reused for gardening and other activities like toilet flushing and cleaning purposes. Zero discharge is proposed for the terminal project. There is no process effluents generated. Hence impact on water quality from the proposed project is insignificant Solid & Hazardous waste generation & Management plan Solid commercial waste from office building and biodegradable waste from canteen will be segregated. It is proposed to use the biodegradable waste for the gardening purpose after vermi composting. Sewage waste will be treated in existing sewage treatment plant and the sludge will be recycled back to the aeration tank. The impact of solid waste on the environment is insignificant. The Management of Hazardous waste will be done as per Hazardous Waste Management Rules Pre-Feasibility Report 14

15 3.10 Schematic representations of the feasibility drawing which give information of EIA purpose. Project Concept and Site identification Form-I, Pre-feasibility project report with proposed TOR to MoEF (EAC) Scoping by EAC/SEAC (Site visit by sub group of EAC/SEAC, if necessary) TOR approved by EAC/SEAC Draft EIA report to SPCB by project proponent EC-rejected by SPCB on the recommendation of SEAC Summary EIA and Form-I display on the website by SPCB Display on the SPCB website Public consultation process by SPCB Proceedings of public consultation Appraisal and recommendation by EAC/SEAC Display at Panchayat, ZP, DM/DC/Dy. Com & on the SPCB website To proponent for submission of final EIA report/supplementary report to draft EIA Approval by SEIAA Referred back to SEAC under communication to the project proponent Rejected Approved Display on SPCB website & project proponent website Post EC monitoring Submission of half yearly compliance report to MoEF/RO- MoEF Display of compliance report on MoEF /SPCB website Pre-Feasibility Report 15

16 4.0 SITE ANALYSIS 4.1 Connectivity Site is very well connected by road and railway. Availability of water, power, etc. Table 7: Environment Settings Sr. No. Particulars Details Distance (km) 1 Nearest Village Bauripalanda village Nearest Town/City Jagatsinghpur Nearest Railway Station Paradip Railway Station Nearest Hospital Vivekanand Hospital Nearest Highway NH-5A Nearest Airport Bhubaneshwar airport Nearest Water Body Mahanadi Nearest Port Paradip Port Land Form, Land Use and Land Ownership About 52.7 Acres of land is already available for LPG Marketing Terminal. Land required for LPG Import Facility project has already been earmarked. The land has been taken from Paradip Port Trust on long term lease. Project area is low lying non-agricultural barren land, which was filled up approx. 3.0 m during construction of LPG Marketing Terminal. The present project site is level land. 4.3 Topography (along with map). The topography of the site is plain. Refer Annexure I. 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. The project area is low lying non-agricultural barren land; there is no national park, wild life sanctuary, eco sensitive areas within 10 Km from the proposed project boundary. CRZ is not applicable to the proposed project. Pre-Feasibility Report 16

17 4.5 Existing Infrastructure This is an existing project located near Bittargarh village, Jagatsinghpur district, Odisha state. 4.6 Soil Classification Soil investigation was done during construction of LPG marketing Terminal. 4.7 Climatic data from secondary sources. Proposed project site is fall under seismic zone III. Regional Climatology Parameters Maximum Minimum Temperature 30.9 o C 22.4 o C Relative humidity (RH) 86% (July and August) 70 % (December) Rainfall 345 mm (August) 6.5 mm (February) Wind Speed 23.9 km/hr 10 km/hr 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 Expansion at existing LPG Marketing Terminal 5.2 Population Projection The total population in the study area is numbers. About 26.45% of the population belongs to Schedule caste and % belongs to Schedule tribe category. Out of total population of 28106, literacy population is 17441, comprising no s of male & 6497 nos of female and Illiteracy population is 10665, comprising 4950 nos of male & 5715 nos of female. The survey results shows, the literate population is higher than the illiterate population. The non working population in the study area is found to be Nos. 5.3 Land use planning (breakup along with green belt etc.) Table 8: Land Use Planning Sr. No. Details of Land Existing Area (In Sq. Mt) Proposed Area (In Sq. Mt) A Non-Plant Shed/Building 1. Administrative Building Canteen/Amenities/Labour Rest Room Stores Building Pre-Feasibility Report 17

18 4. S&D and Control Room Electrical Sub-station/PMCC/DG Sets Fire Pump / Air Compressor House Driver s Rest Room Water Treatment Plant Two Wheeler/Car Parking Main Security Room Security Kiosk at Inner Gate Sewage Treatment Plant Truck Parking Area 7, Fire Water Tanks Own Use HSD Storage Weigh Bridge (2 nos.) B Plant Shed/Building 1. LPG Mounded Vessels (3 x 600 MT) 2, Butane Mounded Vessels (10 x 2,000 MT) -- 10, Propane Mounded Vessels (20 x 2,000 MT) -- 10, TLF (8 Bays) LPG Pump House / Cooling Tower Blending Skid Total Area (A+B) 14,703 20,100 C Green Belt 79, D Open Space and Roads/ Driveways, etc 98,229 1,000 Total Area 1,92,169 21, Assessment of Infrastructure Demand (Physical & Social) On the basis of the preliminary site visit, the infrastructure demand in the villages was assessed on the basis of need and priority. Employment would be as per prevailing norms of state government for skilled and unskilled people for the proposed project activity. 5.5 Amenities/Facilities Proper site services such as First Aid, Canteen, Drinking Water, etc. will be provided to the workers. 6.0 PROPOSED INFRASTRUCTURE 6.1 Industrial Area (Processing Area) Processing Area: 21,100 Sq.m. 6.2 Residential Area (Non Processing Area) Non Processing Area: Nil Pre-Feasibility Report 18

19 6.3 Green Belt Green belt area: 79,237 Sq.m. (Existing) 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) Road and Railway are close to the working site. There is no proposal to make any new kind of connectivity. 6.6 Drinking water Management (Source & Supply of water) Water for drinking and operations will be met from Borewells. 6.7 Sewerage System Domestic waste water will be treated in existing STP. 6.8 Industrial Waste Management Please refer Solid & Hazardous waste generation & Management plan 6.9 Solid Waste Management The excavated earth will be used for levelling and filling of low lying area Power Requirement & Supply/Source Electricity shall be obtained from Paradip Refinery. The total power requirement for the proposed project is 1200 KVA. 7.0 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 labourers Not applicable because the proposed project is expansion of existing LPG Marketing Terminal. 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). The proposed expansion project is to be carried out in the existing facility of LPG Marketing Terminal. Likely time schedule for completion of project is 30 months. 8.2 Estimated Project cost along with analysis in terms of economic viability of the project. Total cost for proposed project activity is Rs. 690 crore. Pre-Feasibility Report 19

20 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. The project will be beneficial to people as the company progress and expands its activity gradually. Through CSR activity company management will be committed to improve infrastructural facilities for the local people in fields of Education, Medical, and Transportation etc. The local people especially tribal population will benefit by way of indirect employment opportunities which will improve the socioeconomic environment of the area. Pre-Feasibility Report 20