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PPRREE--FFEEAASSIIBBIILLIITTYY RREEPPOORRTT

For Proposed Expansion Project

LLPPGG IIMMPPOORRTT FFAACCIILLIITTYY

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 - 400051

GREEN CIRCLE, INC.

Integrated HSEQR Consulting Engineers, Scientists & Trainers

(MoEF Recognized Environment Laboratory)

(An ISO: 9001, 14001, NABL/17025:2005 OHSAS: 18001 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-390 021 (Gujarat) India |Tel: 0265-2371269

www.greencircleinc.com E: [email protected] ALSO AT

BENGALURU RUDRAPUR NEW DELHI HYDERABAD PUNE RAIPUR KOLKATA GOA

OVERSEAS

AUSTRALIA OMAN KUWAIT AFRICA VIETNAM

http://www.greencircleinc.com/

Project: Proposed Expansion of LPG Import Facilities, Paradip, Odisha

Project Proponent: M/s. Indian Oil Corporation Ltd.

Pre-Feasibility Report 2

TABLE OF CONTENTS

LIST OF TABLES

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

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

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




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 20°17’24”N, 86°37’40”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.

2.1.1 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.

2.1.2 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




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 75.66 million tonnes of

petroleum products and reported a PBT of Rs. 37.54 billion, and the Government of India earned

an excise duty of Rs.232.53 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 2011-12 and 2012-13 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 2016-17 2017-18 2018-19 2019-20 2020-21 2021-22

Demand 21831 22597 23271 23868 24342 24770

Considering above demand and available indigenous supply position, the deficit of LPG for the

period 2021-22 is projected as under –

(Fig. In TMT)

Year 2016-17 2017-18 2018-19 2019-20 2020-21 2021-22

Demand -6635 -6961 -6955 -7262 -7503 -7772




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 12 8 20

2 Contract workers 10 15 25

3 Security Staff 10 0 10

Total (approx) 32 23 55

3.0 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.




1. Coordinates of project site : Latitude - 20°17’24”N,

Longitude - 86°37’40”E

Fig. 1: Location Map of Proposed Project

Fig. 2: Specific location & Project boundary of proposed site




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




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 - 5500 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.




iii. Design Temperature will be (-)42 oC to (+)55 oC.

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:

1.5.1 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.

1.5.2 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.




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

1.7.1 Unloading & handling facilities at South Oil jetty:

Ship unloading frequency 3 to 4 Ship’s in a month

Ship parcel size, MT 10,000 to 20,000 (Typical)

Ship berthing time, hrs 25 (Max)

Unloading by 2 Nos of 14” Marine Unloading Arm

Unloading rate, TPH 1,000 (max)

1.7.2 Seawater Intake Pumps

Number

3 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

Type Vertical Submersible

Capacity of each pump m3/hr 1000

Discharge Pressure kg/cm2 (g) 3.0

1.7.3 Seawater Heat Exchangers

Number

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

Type Shell and Tube Heat exchanger

Thermal Capacity of each Heat

exchangers 14.25 M kcal /hr for each exchanger

1.7.4 Pipeline transfer facilities

Unloading through 2 Nos of 16” transfer lines

1.7.5 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.)




1.7.6 Despatch Facilities at LPG Marketing Terminal

Tank Trucks

Loading to Un-insulated road tankers.

Loading temperature, ºC 15 / Ambient

Loading by LPG / Propane / Butane transfer pumps

No. of loading Station Existing 8 bays TLF

Pumping Rate, MT/hr 150

Pipeline Transfer

Loading to

12” dia. Existing LPG transfer pipeline to Refinery for

onward pumping into Paradip-Haldia-Durgapur-

Barauni-Patna-Muzaffarpur pipeline

Loading temperature, ºC 15 / Ambient

Loading by LPG / Propane / Butane transfer pumps

Pumping Rate, MT/hr 400 (Approx.)

1.7.7 Propane / Butane Transfer Pump:

Type Vertical Can Type with double mechanical seal

Flow, m3/hr 220 (2W + 1S) Each for Propane & Butane

MOC LTCS

1.8 Space for facilities at South Oil Jetty :

1.8.1 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.

1.8.2 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.

1.8.3 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.

1.8.4 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.




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.

1.8.6 Space for Control Room :

Space for instrument panels and consoles are available.

1.8.7 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 %)

1.1.1 Propane 97 1.3

1.1.2 Iso-Butane 1.3 24.4

1.1.3 N-Butane 0.4 73.6

1.1.4 Other 1.3 0.7

3.7 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.




3.8 Availability of water its source, energy/power requirement and source should be given.

3.8.1 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 39.74 KLD (Existing-27.74 KLD &

Proposed-12 KLD). 9.45 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 5.5 5.0 10.5 4.95 4.5 9.45

2 Plant 3.0 3.0 6.0 0.0 0.0 0.0

3 Cooling 0.24 1.0 1.24 0.0 0.0 0.0

4

Gardening/Floor

washings and

Fire water

makeup

19.0 3.0 22.0 0.25 0.30 0.55

TOTAL 27.74 12.0 39.74 5.2 4.8 10.0

3.8.2 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

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

9 0.200

2 DG Set HSD & 30 L/hr 320 KVA

CO2,

NOx,

SOx

9 0.150

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




3.9 Quantity of wastes to be generated (liquid and solid) and scheme for their management/

Disposal

3.9.1 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.

3.9.2 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

2008.




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

Public consultation

process by SPCB

Proceedings of public

consultation

Appraisal and

recommendation by EAC/SEAC

Approval by SEIAA

Rejected Approved

Display

on the

SPCB

website

EC-rejected by SPCB on the

recommendation of SEAC

Summary EIA and Form-I display

on the website by SPCB

To proponent for submission of final

EIA report/Supplementary report to

draft EIA

Referred back to SEAC under

communication to the project

proponent

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

Display at Panchayat, ZP,

DM/DC/Dy. Com & on the SPCB website




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 0.6

2 Nearest Town/City Jagatsinghpur 31.5

3 Nearest Railway

Station

Paradip Railway

Station 2.0

4 Nearest Hospital Vivekanand Hospital 2.15

5 Nearest Highway NH-5A 1.7

6 Nearest Airport Bhubaneshwar airport 120

7 Nearest Water

Body Mahanadi 4.6

8 Nearest Port Paradip Port 5

4.2 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.




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 oC 22.4 oC

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 28106 numbers. About 26.45% of the population belongs

to Schedule caste and 15.74 % belongs to Schedule tribe category. Out of total population of

28106 , literacy population is 17441, comprising 10944 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 13541 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 250 --

2. Canteen/Amenities/Labour Rest Room 132 --

3. Stores Building 280 --




4. S&D and Control Room 125 ----

5. Electrical Sub-station/PMCC/DG Sets 536 --

6. Fire Pump / Air Compressor House 450 --

7. Driver’s Rest Room 110 --

8. Water Treatment Plant 100

9. Two Wheeler/Car Parking 200 --

10. Main Security Room 25 --

11. Security Kiosk at Inner Gate 9

12. Sewage Treatment Plant 100

13. Truck Parking Area 7,600 --

14. Fire Water Tanks 760 --

15. Own Use HSD Storage 300 --

16. Weigh Bridge (2 nos.) 96 --

B Plant Shed/Building

1. LPG Mounded Vessels (3 x 600 MT) 2,500 --

2. Butane Mounded Vessels (10 x 2,000 MT) -- 10,000

3. Propane Mounded Vessels (20 x 2,000 MT) -- 10,000

4. TLF (8 Bays) 720 --

5. LPG Pump House / Cooling Tower 410 --

5. Blending Skid -- 100

Total Area (A+B) 14,703 20,100

C Green Belt 79,237 --

D Open Space and Roads/ Driveways, etc 98,229 1,000

Total Area 1,92,169 21,100

5.4 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




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 3.9.2 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.

6.10 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.




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.

Date post:	07-May-2018
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