project feasibility report proposed grass-root petroleum...

INDIAN OIL CORPORATION LIMITED, MARKETING DIVISION HEAD OFFICE, PROJECTS GROUP

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Project Feasibility Report

of

Proposed Grass-Root Petroleum Storage & Distribution Terminal

apt

Asanur Village, Vizhupuram,

Tamil Nadu

Prepared by

Indian Oil Corporation Limited,

HO, Indian Oil Bhavan, G-9, Ali Yavar Marg

Bandra (East), Mumbai-400 051


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Table of Contents

Chapter No.

Content Page No.

01. Executive Summary

3-5

02. Project Location and Layout

6-7

03. Objective of Terminal

8

04. Need for the project & Importance in India

9

05. Process Description

10-18

06. Resources

19-20

07. Environment Protection

21

08. Analysis of Proposal and Recommendations

22

Annexure-1 List of Proposed Fire Fighting Equipment

23

Annexure-2 Environmental, Health and Safety Policy of Company

24

Annexure-3 Layout of the Project

26

Annexure-4 Fire Organization Chart 27

Annexure-5 Land Deed Documents 28


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CHAPTER – 1.0

EXECUTIVE SUMMARY


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EXECUTIVE SUMMARY

1.0 Indian Oil Corporation Limited (IOCL) is a premier Public Sector undertaking under the

Ministry of Petroleum & Natural Gas, Govt of India. The Corporation is India's largest

company by sales. Indian Oil is the highest ranked Indian company in the latest Fortune

‘Global 500’ listings, ranked at the 119th position. Indian Oil's vision is driven by creating

new infrastructure & state of the art Marketing network which are world class & also

strengthening the existing marketing network with application of technology in each &

every business process. Indian Oil’s vision is driven by a group of dynamic leaders who

have made it a name to reckon with. IOCL is a Globally Admired Company and has a

Vision of being the Energy of India.

2.0 Indian Oil owns and controls 11 of India’s 23 refineries including commissioning of a new

refinery at Paradip, Odisha during Feb ‘16. The group refining capacity is 80.7 million

metric tonnes per annum (MMTPA)- the largest share among refining companies in India.

It accounts for 35% share of national refining capacity.

3.0 Indian Oil Corporation Ltd. operates a network of 11,220 km long crude oil, petroleum

product and gas pipelines with a capacity of 80.49 million metric tonnes per annum of oil

and 9.5 million metric standard cubic meter per day of gas. Cross-country pipelines are

globally recognized as the safest, cost-effective, energy-efficient and environment-

friendly mode for transportation of crude oil and petroleum products.

4.0 Indian Oil has one of the largest petroleum marketing and distribution networks in Asia,

with over 43,000 marketing touch points. Its ubiquitous petrol/diesel stations are

located across different terrains and regions of the Indian sub-continent. From the icy

heights of the Himalayas to the sun-soaked shores of Kerala, from Kutch on India's

western tip to Kohima in the verdant North East, Indian Oil is truly 'in every heart, in

every part'. Indian Oil's vast marketing infrastructure of petrol/diesel stations, Indane

(LPG) distributorships, SERVO lubricants & greases outlets and large volume consumer

pumps are backed by bulk storage terminals and installations, inland depots, aviation

fuel stations, LPG bottling plants and lube blending plants amongst others. The

countrywide marketing operations are coordinated by 16 State Offices and over 100

decentralized administrative offices.

5.0 The Existing petroleum market of Ullundhurpet and surrounding area is being fed from

petroleum storage locations existing at Chennai, Trichy and Shankari. The Chennai-

Trichy-Madurai Pipeline (CTMPL) of IOCL is already having an intermediate pump station

at Asanur, TN. By providing a pipeline ToP at Asanur which is at a distance of 220 km

from Chennai and 150 km from Shankari, movement of petroleum products by road

would be reduced considerably. This would result in considerable saving in consumption

of fossil fuel, saving in logistic cost to Govt. exchequer and reduce emission / noise

pollution by avoiding movement of petroleum products from far off refinery locations.

6.0 The Terminal operation shall be established keeping in mind the Sustainable

development of the region.


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7.0 Further, Indian Oil Management is committed to contribute towards improving socio

economic status of the surrounding local community.


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CHAPTER – 2.0

PROJECT LOCATION AND LAYOUT


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Project Location

The proposed facility description of IOCL Greenfield Petroleum Storage Terminal is given below:

Facility : IOCL Petroleum Storage Terminal

Address : Village Asanur, Ullundhurpet, Vizhupuram District

Location : The proposed Terminal is planned at Aanur Village, Ulundhurpet, Vizhupuram District. The nearest Railway station is Kuttakudi railway station (about 8 km). The Terminal is approximately at 200 Km from Chennai Airport.

Geo codes Latitude : 11°36'31.37"N

Longitude : 79°11'32.85"E

Surroundings : East Private Land (Valasai Village, Virdhachalam Taluk)

West SIDCO Developed Plot No. 41, 24m Road and Developed

Plot Nos. 42 to 51

North Private Land (Survey Nos. 356,355, 358, 359, 360, 365/3

Part)

South SIDCO OSR Plot, 15m Road & Developed Plots 103 to 106

Project Layout is given at Annexure-3


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CHAPTER – 3.0

OBJECTIVE OF TERMINAL

THE OBJECTIVE OF THE PROJECT

The project primarily aims at improving the Infrastructure Development for Petroleum Product Storage & Transportation

♦ To develop the storage facility of petroleum product to ensure better availability of petroleum product in the state of Tamil Nadu.

♦ To fulfill the local petroleum products demand of Ulundhurpet & surrounding towns.

The project will contribute towards the socio-economic development of the area. The direct and indirect employment to the local population during the operation of the project for both skilled and unskilled levels will be created thereby the local population will be benefited. The project also envisages the development of planned green belt, which would not only enhance the aesthetic quality of the area but also helps in creating better landscaping. During construction phase, the project will also generate temporary local employment.


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In nutshell, the project would create better infrastructure, better availability of petroleum products, improve livelihood and socio-economic conditions.


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CHAPTER – 4.0

NEED FOR THE PROJECT AND IMPORTANCE TO INDIA

4.1 NEED FOR THE PROJECT The Existing petroleum market of Ullundhurpet and surrounding area is being fed from

petroleum storage locations existing at Chennai, Trichy and Shankari. The Chennai-Trichy-

Madurai Pipeline (CTMPL) of IOCL is already having an intermediate pump station at Asanur, TN.

By providing a pipeline ToP at Asanur which is at a distance of 220 km from Chennai and 150 km

from Shankari, movement of petroleum products by road would be reduced considerably. This

would result in considerable saving in consumption of fossil fuel, saving in logistic cost to Govt.

exchequer and reduce emission / noise pollution by avoiding movement of petroleum products

from far off refinery locations.

4.2 CURRENT DEMAND SCENARIO IOCL projects throughputs for Asanur in 2021-22, 2026-27 and 2031-32. The projected demand numbers are as under:

SN Product Projected Volumes

(TMTPA)

2021-22 2026-27 2031-32

1. MS 112.03 143.32 192.36

2. HSD 246.38 308.10 494.05

4.3 COST OF THE PROJECT The estimated cost of the project is Rs 300 Crores (approx.) 4.4 BUDGETS FOR ENVIRONMENTAL PROTECTION CAPITAL: Rs 35 Crores (approx.); RECURRING: Rs 3 Crores (approx.)


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CHAPTER – 5.0

PROCESS DESCRIPTION

5.1 PROCESS DESCRIPTION

There is no manufacturing process involved in the Terminal.

The process involved can be divided into

� Receipt of finished petroleum products (MS, HSD) through existing cross-country pipelines.

� Unloading of Products (MS & HSD) from Tank trucks occasionally (TLD).

� Receipt of Ethanol through Tank trucks (TLD)

� Receipt of Bio Diesel through Tank trucks (TLD)

� Pump House Operations (PHO)

� Tank Lorry Filling (TLF) operations of MS, Ethanol Blended MS, HSD, Blended Diesel

� Ethanol, Blue Dye & Bio Diesel Dosing

� Storage of petroleum products in storage tanks fabricated as per international standards.

� Dispatch of petroleum products through Tank Lorries.

The entire operation of RECEIPT, STORAGE AND DISPATCH of petroleum products is carried out in a closed system thereby eliminating risk of spillage of products and to achieve enhanced safety.

Typical process flow chart is attached.


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PICTORIAL DEPICTION OF THE PROCESS FLOW CHART:

TANKFARM FACILITIES


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RECEIPT OF PETROLEUM PRODUCTS

STORAGE OF PETROLEUM PRODUCTS


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5.2 RECEIPT OF PETROLEUM PRODUCTS

The petroleum products viz. MS, HSD will be received from via cross-country pipelines Chennai-Trichy-Madurai Pipeline (CTMPL). The pipeline currently has a pumping station located at Asanur. It is proposed to provide a 12" dia branch pipeline of approx. 700m length from Asanur Pumping Station to the proposed terminal.

5.3 STORAGE FOR PETROLEUM PRODUCTS

Following tankages are proposed to be developed

SN Product Class No of tanks

Type of Tanks

Tank Size Capacity of each tank

Total Tankage

1. MS A 3 IFRVT 30 m dia x 17 m high

10214 KL 30642 KL

2. MS (TTD) A 1 UGHT 3 m dia x 7.5 m long

50 KL 50 KL

3. HSD B 3 CRVT 36 m dia x 15.5 m high

14939 KL 44817 KL

4. HSD (TTD) B 1 UGHT 3 m dia x 7.5 m long

50 KL 50 KL

5. HSD (own use)

B 1 UGHT 3 m dia x 7.5 m long

50 KL 50 KL

6. BIO-DIESEL B 1 CRVT 12 m dia x 14 m high

1500 KL 1500 KL

7. BIO-DIESEL (TTD)

B 2 UGHT 3 m dia x 10.5 m long

70 KL 140 KL

8. Ethanol A 2 IFRVT 14 m dia x 13.5 m high

1685 KL 3370 KL

9. Ethanol (TTD)

A 2 UGHT 3 m dia x 10.5 m long

70 KL 140 KL

10. Transmix A 2 IFRVT 12 m dia x 8 m high

750 KL 1500 KL

11. Sludge B 1 AGHT 12 m dia x 8 m long

750 KL 750 KL

CLASS – A 35,702 KL

CLASS - B 47,307 KL

GRAND TOTAL 83,009 KL

Legends:

a. IFRVT – Internal Floating Roof Vertical Tanks

b. CRVT – Cone Roof Vertical Tanks

c. UGHT – Under Ground Horizontal Tanks

The above tankage shall be developed in line with latest API 650 & OISD regulations.


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5.4 SEPARATION DISTANCES

The minimum separation distances between various facilities, offsite facilities & tanks within a dyke shall be as per provisions of latest version of OISD 118 & OISD 244 Standards.

5.5 DISTRIBUTION OF PETROLEUM PRODUCTS

The petroleum products shall be distributed to various Industries / Petrol Pumps through tank trucks of capacity 9000 Ltrs to 24,000 Ltrs. On an average, 125-150 tank trucks are anticipated to be filled on daily basis. A 8 bay TLF shed with bottom loading facilities for MS and HSD is proposed. The loading facilities shall consist of PD metering system, batch controllers, blending facilities for Ethanol, branded fuels etc. Vapour recovery system to be designed & developed for handling MS. Tank Truck (TT) decantation facility with suitable capacity of Under Ground (U/G) tanks to be provided. 5.6 BRIEF INFORMATION ON OTHER FACILITIES

I. PRODUCT PUMP HOUSE (TWD RECEIPT & TT DISPATCH):

� PUMP HOUSE: 48 M X 6 M with new product pumps. � PUMP HOUSE MANIFOLD: 48 M X 30 M

II. PRODUCT PIPING:

� Set of piping from Pumping Station to the Product Tanks � Set of piping from Product Tanks to the pump house and � Set of piping from pump house to the Tank Lorry Filling (TLF) shed.

III. ELECTRICAL FACILITIES:

� TRANSFORMER & HT BREAKER � NEW MCC PANEL: 1 SET. � DG SETS: 2 nos 750 KVA x 1 nos 500 KVA (Shall be as per connected load & design

requirements) � ELECTRICAL CABLING, LIGHTING, EARTHING.

IV. FIRE FIGHTING FACILITIES:

� 24 M Dia X 14 M High Water Tank Of Capacity 8120 Kl : 3 No � Fire Pumps: 5 no x 700 CUM/ HR x 105 M Head. � Water Sprinkler system on proposed MS & HSD as per prevailing safety guidelines

issued by OISD � Fixed Foam fighting system on proposed Diesel (HSD) and Petrol (MS) tanks as per

prevailing safety guidelines issued by OISD � Centralized Foam Feeding system for Fixed foam pourers & HVLR. � Provision of Fire hydrant piping network for the entire Terminal facilities.

V. OTHER CIVIL FACILITIES:

� Room for the Transformer and HT Breaker � Fire Pumps � MCC room � Dyke walls for proposed product tanks � Roads and Storm water drains for the new product tank farms


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� Driveway around TLF shed

VI. AUTOMATION OF ENTIRE TERMINAL: � Tank Farm Management system: These shall comprise of automation of receipt of

products from TW siding. � Valve Automation system: All the Tank Body Valves and exchange pit valves shall be

automated including remote operation with necessary safety interlocks. Further, the tank body Valves shall be fitted with Remote Operated Shut Off Valves (ROSOV) to be closed by a safety PLC in case of emergency. The same shall be in line with international SIL 2 requirements.

� Radar gages on all tanks: Each tank shall be provided with 2 nos SIL 2 certified Radar gauges for automatic level measurement. The gauges shall function in remote for the tank inventory and tank shut down procedures.

� Automatic Overspill Protection Switch: In addition to the dual redundant radar gauges on each tank, an independent SIL 3 certified Level switch shall be provided for shut of the tank in case of reaching high level alarm.

� Tank Lorry Filling System: The entire process of filling of the Tank Lorries shall be automated along with necessary safety interlocks

� Access Control System: The system shall permit only authorized personnel to carry out the operations within the Terminal. The access shall be both role and application based system.

� Control Room with equipment: The control room shall monitor and log all events pertaining to the operation of the Terminal on real time basis.

� OTHERS: � MOVs for the tank farm dyke valves for remote operation & real time indication

on status of valves � Push Button Stations outside Tank body valves for remote switching off of the

product tank body valves. � Emergency Shut Down Procedures for various Terminal operation activities.

(i) Ethanol/ Bio-Diesel/ Branded fuels Dosing: Design and provision of suitable dosing

system for Ethanol with MS, Bio-Diesel with HSD with feasibility of varying the blending ratio from 5% to 15% to be provided. Similarly design & provision of suitable dosing system for branded fuels with feasibility of changing the dosing ratio (in ppm) to be provided

(ii) Bio diesel handling facilities: Suitably designed for online dosing to be provided. (iii) Non Plant Facilities: All the ancillary facilities like security, perimeter wall with fencing,

gates, internal fencing, internal roads, pavements, driveway, security, Administrative block, Workmen change room, Control room, S & D room, Locker shed, Calibration facility, sludge pits, Effluent Treatment Plant, Scrap yard, PPE/First Aid room MCC rooms, DG sets and rooms, Electrical substation, TT parking area, TT rest room Storage sheds for revenue store/Engg materials.

Design Considerations for increased Safety: A. All Tanks are atmospheric & are designed as per IS 803 & API 650 guidelines. B. Design of tanks is considering wind pressure & seismic activity. C. Tank shell plate calculations are based on Joint efficiency factor of 0.85 with corrosion

allowance of 1.5 mm. D. Steel plates used for tank fabrication are as per IS 2062 Grade B. E. All material used for piping/flanges confirm to relevant API/ASTM & ANSI standards.


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F. Tanks shall be provided with Breather/ Conservation valves & Emergency vents as per API 650/ API 2000 requirements.

G. Tanks are provided with double seal (primary & secondary) to prevent escape of vapour & exposure to atmosphere as per API 650 guidelines.

H. All electrical equipments/motors/switches etc used inside hazardous area are either intrinsically safe or Ex proof as per relevant zone classifications.

I. Body earthing & grid system is ensured for all product tanks & pipelines to discharge static charges effectively & to prevent any generation of heat/spark. Continuity between various pipe sections & valves are ensured.

J. Roads inside the hazardous area of Installation are restricted to vehicles required for operational, maintenance and safety/security reasons and allowed only with proper safety fittings and ensure the same by well established checking procedure at the entry gate.

K. Road widths, gradient and turning radii at road junctions are ensured to facilitate movement of the largest fire-fighting vehicle envisaged in the event of emergency.

L. Vehicles with spark ignition engine only are allowed inside hazardous area. Vehicles with internal combustion engine (compression ignition) & with PESO (Petroleum and Explosive Safety Organization) approved spark arrestor fitted on the vehicle.

Mitigation Measures proposed for risk reduction during operation:

A. All product tank dyke wall/enclosure designed with 110% of the largest tank capacity.

� As per OISD standards, all tanks are provided with an enclosure wall to contain any leak from the tanks or in case of failure/rupture of the tank shell.

� The dyke provided is designed to contain the 110% of volume of the largest tank & a free board of 200 mm to prevent any overflow of spilt oil.

� The dyke enclosure designed as mentioned above facilitates to fight fire caused by a pool of oil.

B. All product tanks to be provided with 2 nos exclusive SIL 2 certified Radar gauges & 1 no additional over spill protection device to avoid any overflow of tanks.

� All the proposed & existing product storage tanks shall be provided with 2 nos separate radar gauges with SIL 2 certification, which is an internationally accepted standard.

� Provision of 2 separate radar gages & monitoring of the same from control room/ PLC system helps to avoid any overflow of product. The radar gauges are linked to the control room & shall give audio visual alarms at the control room in case of the product level reaches higher than the specified level.

� In addition to the above, 1 no exclusive & independent Automatic Overspill Protection device is hard wired to the Remote Operated Shut Off Valve & Safety PLC of the automation system. When the product level in the storage tanks rise beyond a pre-defined & safe filling capacity, the Automated Overspill Protection System (AOPS) is triggered & it overrides all operations & logics built in the system to implement total shut down of the operations & closure of all valves of all tanks.

� The above safety features prevent any overflow of petroleum product from the storage tanks.

C. All product tanks to be provided with fire & fail safe Remote Operated Shut Off Valves.

� All body valves of tanks shall be provided with Fire Safe & Fail Safe Pneumatic actuated Remote Operated Shut Off Valves (ROSOV).


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� The ROSOVs shall be interlinked with the SIL 2 certified radar gauges, AOPS & Safety PLC. Upon the product level reaching the set trip point of a tank, the ROSOVs shall automatically close overriding all operational logics.

D. All body valves of tanks to be provided with Remote Open & Close facility outside the dyke enclosure to operate during emergencies.

� All valves of tanks shall be provided with an open & close push button just outside the tank enclosure.

� The same shall be used to close a particular valve of a tank in case of exigencies, thereby eliminating man entry in to hazardous zone (dyke area) during spillage etc.

� This system shall save human lives during emergencies & hazards due to proximity to petroleum vapour.

E. Fire water storage planned for 2 simultaneous contingencies with full coverage of fire hydrant facilities to the entire plan area & positioning of fire fighting equipments as per OISD standards & MB Lal recommendations.

� Permanent fire water storage & fire hydrant system to cover the entire Terminal operating area shall be provided.

� The water storage & pumping facilities shall be designed to cater 2 simultaneous emergencies inside the Terminal.

F. High Volume Long Range remote operated monitors to be provided for all Class A STORAGE tanks.

� In case of a fire, fire fighting can be done from the proposed High Volume Long Range Monitors (HVLR).

� The HVLRs shall have motorized valves with provision to operate from control room. � As per OISD 117, fixed type HVLR & Mobile type HVLR with 1000/ 2000 US GPM

capacity are being proposed for the Terminal to cover tank farm fires.

G. Hydro carbon detection system to be provided for all tanks, drain valve & manifold in Class A service.

� To detect any leak & potential fire hazard, Hydro-Carbon Detection (HCD) system is proposed for all tanks with Class A service, tank enclosure drain valves & product piping manifolds.

� The proposed HCD system shall be linked to the control room & shall alert the Control room officer with audio visual alarm when the concentration of the petroleum vapour exceed beyond pre-defined limits.

� The following equipment are being planned for the Terminal as part of the HCD system.

• Point type Infra Red (IR) sensor – at each drain valve in tank farm.

• Open path IR sensor (range: 0 to 40 m & 0 to 120 m) – at valves & manifold of Class A product.

• Portable Gas detector – 1 no.

• Test filter – 1no.

H. Fixed water spray & fixed foam pourer system has been provided for all Class A Tanks & for Class B tanks above 18 m diameter. The same shall also be extended for the proposed tankage.


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� As per OISD 117, fixed water spray & fixed foam pourer system is existent for all

product tanks storing Class A product & for Class B tanks with diameter more than 18 m.

� The system shall be extended to the proposed tanks & shall cool the surface area of tank on fire & protect the nearby tanks from heat radiation & fire due to auto-ignition.

� The fixed foam pourer system shall apply foam solution to the surface of fire to create smothering effect & extinguishing of fire.

I. MOVs & Flow switch shall be provided for all water draw off lines.

� In order to have effective monitoring of water draining from product tanks, a flow switch shall be installed on all drain valves of all tanks to alert the Control room.

� Proposed Class A tank shall be constructed as internal floating roof tank.

In order to prevent exposure of petroleum vapour to open environment, the proposed tank on Class A service shall be constructed as an internal floating roof tank with an Aluminum floating deck & a fixed roof. This shall act as an additional safety feature & shall minimize fires due to lightning etc

J. Manual call points shall be provided at strategic places within the Terminal.

� Manual call points are proposed at strategic places inside the Terminal to raise alarm in case of any exigency.

K. Receipt & delivery operation shall be done based on in built logic developed in SCADA with site specific interlocks.

� Tank operations like receipt & delivery shall be based on pre-defined logic & controlled by PLC & SCADA systems.

� This shall prevent wrong operations & risks like overflow of tanks.

L. Tank truck bottom loading shall have interlocks to monitor grounding of the truck, position of the loading arm & over flow protection system. Tank truck operation shall be designed as Bottom loading system with the following interlocks to avoid fire hazards.

� Grounding interlock – To stop loading in the absence of proper grounding & to prevent fire due to static electricity.

� Position sensor/ level switch on loading arm – The batch controller commences tank truck loading based on the feedback from loading arm’s position sensor is inserted in to the tank truck compartment. Similarly, the batch controller shall stop loading based on a feedback from a level switch of loading arm to prevent any overflow of tank truck.

M. Separate Safety PLC planned for interlinking of all safety features & for ensuring total shut down of the plant.

N. CCTV system shall be provided as per security guidelines applicable & shall be linked with Safety PLC.


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CHAPTER – 6.0

Resources

6.1 Water Requirements

Description Remarks

1. Utilities and Human Consumption 8,000 Litres per day

2. Process Requirement Nil

3. Fire Fighting Demand (as per OISD 117) 8120 KL for 4 hours of fighting

4. Horticulture/ Green Belt Demand 5,000 Litres per day

Description Quantity Treatment

Effluent to be generated 6500 LPD Septic Tank & Soak pits

Domestic Sewage to be generated 7 kg/ day Disposal through municipal authorities

Sludge/ Hazardous Waste to be generated

4-5 MT per year

Disposal through CHWTSDF & Bio-remediation

Solid Waste to be generated 50 kg/ day Vermi composting & manure for gardening

6.2 Source (s) for meeting water demand

It is proposed to 2 nos sink bore wells for meeting the requirements of the Terminal. Out of the 2 bore well, one shall be exclusively used for domestic & human consumption. The balance 1 bore well shall be used for topping up of the Fire Water storage tanks as & when consumed for regular monthly Mock Drills.

6.3 Fire Hydrant Storage Facilities (No. of Tanks with height/ dia/ capacity) and distance from Tank Farm, POL Gantry

Details provided above.

6.4 Energy Requirements and Source, Power Back-up facilities.

It is envisaged to have HT power connection from TANGEDCO. The approximate power requirement would be supply with a load of 1500 kW & with 1500 kVA contract demand Details of power back up facilities proposed by IOCL is provided above.

6.5 Requirement of Building Material/ Construction Material

The approximate quantities of major building materials for construction of the Petroleum Terminal are as given below:


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� Filling Earth: 2,50,000 CUM

� Sand: 25,000 CUM

� Bricks: 20 Lacs

� Cement Concrete: 15000 CUM

� Steel: 10000 MT

6.4 Human Resources/ Manpower

(a) Permanent Staff (Organization chart): 10 Officers, 15 Workmen

(b) Temporary Staff: Skilled-30; Semi-skilled: 30; TT Crew: 250 nos

Proposed Fire Organization Chart is enclosed.


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CHAPTER 7.0

ENVIRONMENT PROTECTION

ENVIRONMENT PROTECTION

a. Green belt in line with MoEF guidelines shall be provided around the periphery of the Terminal. The green belt will be maintained in an excellent condition.

b. Mechanized oil water separators & Effluent Treatment Plant will be provided. The oil content of the discharge from oil water separator shall be less than the prescribed limits of 10 PPM.

c. Floating roof tanks will be provided with Internal floating roof, Mechanical shoe primary seal & wiper type secondary seal with minimum vapour recovery of at least 96% as per MoEF norms.

d. Cone roof tanks shall be provided with Breather/ Conservation vents to reduce fugitive emissions.

e. The DG sets shall be acoustically insulated resulting in reduction of noise as per limits prescribed by Central Pollution Control Board. The exhaust pipe from DG sets shall be taken above the building as per Central Pollution Control norms.

f. All conditions & pre-requisites of water and air consents together with certificate to handle hazardous products issued by State Pollution Control Board shall be strictly adhered to.

g. Geo-technical studies of the soil shall be carried out & design of facilities shall be as per bearing capacity of the soil.


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CHAPTER – 8.0

ANALYSIS OF PROPOSAL & RECOMMENDATION

� The entire project is being proposed on approximate 75 acre land acquired from Tamil Nadu Small Industries Development Corporation Ltd. (TNSIDC) at SIDCO Industrial Estate, Asanur.

� There would be negligible impact in the buffer zone due to the proposed project

� Project being capital in nature shall contribute to the socio economic development, strengthening of the facilities in & around Vizhupuram.

� Plant shall be operated keeping in mind Sustainable development of the region.

� IOCL Management is committed to contribute towards improving socio economic status of surrounding local community.

Considering the above overwhelming positive impacts, there shall be overall development of the area.

Hence it is requested that Environmental Clearance be granted for the project submitted.


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ANNEXURE-1

LIST OF PROPOSED FIRE FIGHTING EQUIPMENT 1. Fire Water storage Static Tank: 3 x 8120 KL 2. Fire Fighting pump sets: 5 x 700 KL/Hr x 105 m Head 3. Jockey pump sets: 2 x 72 KL/ Hr x 110 m head 4. U/G Tank of 100 KL capacity with pumps & provision to receive water from outside: 1 set 5. Bore well pumps: 3 nos 6. Well spread fire hydrant piping layout for the entire plant: approx 4000 m 7. Remote operated & Fixed High Volume Long Range Foam cum water monitor: 7 nos 8. Trolley mounted High Volume Long Range Foam cum water monitor: 2 nos 9. Medium Expansion Foam Generator (Fixed): 4 nos 10. Medium Expansion Foam Generator (Portable): 2 nos 11. 3% AFFF Tanks (9000 litre): 3 nos 12. ATC Foam for Alcohol fire: 1 KL 13. Hydro-carbon Gas Detectors (OP Type): 6 Nos 14. Hydro-carbon Detectors (Point Type): 14 Nos 15. Portable Gas Detector: 1 no 16. Explosimeter: 1 no 17. Oxygen meter: 1 no 18. Fire proximity suit: 1 no 19. SCABA with spare O2 cylinder: 1 set 20. Wheeled Portable Water cum Foam monitor – 2 nos 21. Fixed water spray system for Storage Tanks: 11 nos 22. Fixed Foam Pourer System for Storage Tanks: 13 nos 23. Fixed Water monitors: 45 nos 24. Double Hydrant points on stand post: 75 nos 25. Jet Nozzle: 5 nos 26. Universal Nozzle: 5 nos 27. Foam Branch Pipe: 5 nos 28. Stretcher with blanket: 2 nos 29. First Aid Box: 2 nos 30. Shock resistant Rubber Hand Gloves: 2 pair 31. Oil Sorbent Booms: 2 nos 32. 75 kg DCP Fire Extinguisher: 15 nos 33. 25 kg DCP Fire Extinguisher: 15 nos 34. 10 kg DCP Fire Extinguisher: 135 nos 35. 2.5 & 4.5 kg CO2 Fire Extinguisher: 60 nos 36. Safety Hand lamp: 2 nos 37. Leak arrestor kit with clamps: 1 set Note: Any other additional firefighting equipment for which need is felt during design & detailed engineering will be appropriately added to be compliant with the provisions of OISD 117 & OISD 244


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Annexure-2

Environmental, Health and safety Policy of Company


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Annexure-3: Project Layout


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Annexure-4

Fire Organization Chart

Fire Chief Ch Terminal Manager

Alternate Incharge Manager (Operations)

COMBAT TEAM AUXILIARY TEAM RESCUE TEAM COMMUNICATION TEAM

Shift In charge - Leader Maintenance Officer - Leader Finance Officer - Leader S & D Officer - Leader

Members

Safety Officer - Alt.Leader

Site Engineer

PL Officer

Mechanical Contract Workers

TT Calibration Officer

TLF Officer

Members

QC//Etahnol Officer - Alt.Leader

TLF Officer - (TT Evacuation)

Electrical Contract Workers

TLF Staff

TLF P/H Staff

Security Guards - 2 Persons

Members

Lab Officer – Alt. Leader

Finance Employees (WCWs)

PL Staff

Locks Section Staff

TT Calibration Staff

Security Guards - 2 persons

Members

WCW (S&D Staff) – Alt. Leader

Admin Building Contract Workers


• Stop immediately filling operations &

remove hoses from tank wagons & TTs

after closing the valves. •

Rush to the scene of fire with available

fire extinguishers & try to extinguish the

fire immediately.

• Rush to the spot with available hoses

& nozzles & start fire fighting as per the

instructions of the Fire Chief.

• All operations to be stopped, tank

valves to be closed, electric mains to

be switched off.

• If necessary all filled TTs should be

allowed to go through the emergency

exit gate. Half filled TTs should not

go out without documents.

• Organize supply of fire fighting

equipments as well as personnel to

the Fire Combat team as per the

orders of Fire Chief.

• Replace all fire fighting equipments

that are exhausted after the fire is

brought under control.

• Help the incident controller

(Fire chief) & the combating

team in rescuing operations of

the victims.

• Give First Aid to the affected

persons.

• Keep all the cash & other

important documents in the

locker/ cabinets locked.

• Ensure all unwanted people

are sent out of the terminal

• Inform about the incident to

Industry Members, Local Police and

State Govt Agencies like Fire

Brigade, Factories Dept , nearest

Hospital (as per priority displayed)

and DGM (O), TNSO

• Coordinate with DSP (Rural) & DCP

(Traffic) for ease of flow of traffic

en route for Fire Brigade &

Ambulance to reach the site.

• Coordinate in shifting the injured

persons to hospital

Note:

1.In the absence of leader,deputy leader will lead the team.

Responsibilities

Proposed Fire Organisation Chart - During 1st,2nd and General Shift

Asanur Terminal, Tamil Nadu

2.After normal working hours,the shift in charge will act as the Chief Controller and carry out the necessary activities till the nominated Chief Controller or Site Controller reaches

the site.


Manger (Ops) – 1 person – Leader PL Officer - Leader TLF Officer Finance Officer – 1 person - Leader

Members

Staff

Security Guards – 4 persons

Members

Security Guards – 2 persons

Electriction - 1 Person

Members

Staff

Security Guard - 1 Person

Members

Security Guard - 1 Person


• Rush to the scene of fire with available

fire extinguishers & try to extinguish the

fire immediately

• Rush to the spot with available hoses &

nozzles & start fire fighting as per the

instructions of the Fire Chief.

• Organize supply of fire fighting

equipments as well as personnel to the

Fire Combat team as per the orders of

Fire Chief.

• Replace all fire fighting equipments

that are exhausted after the fire is

brought under control.

• Help the incident controller

(Fire chief) & the combating team

in rescuing operations of the

victims.

• Give First Aid to the affected

persons.

• Inform about the incident to CTM,

DGM (O),TNSO ,Industry Members,

Local Police , State Govt Agencies like

Fire Brigade, Factories Dept , nearest

Hospital (as per priority displayed)

• Coordinate with DSP (Rural) & DCP

(Traffic) for ease of flow of traffic en

route for Fire Brigade & Ambulance to

reach the site.

• Coordinate in shifting the injured

persons to hospital.

Note:

1.In the absence of leader,deputy leader will lead the team.

2.After normal working hours,the shift in charge will act as the Chief Controller and carry out the necessary activities till the nominated Chief Controller or Site Controller reaches

the site.

Responsibilities

Ch Terminal Manager

Asanur Terminal, Tamil Nadu

Proposed Fire Organisation Chart - During Off Shift Hours

Fire-in-Chief cum Combat Team Leader


Page 28 of 28

Annexure-5

Land Deed Documents