ANNEXURE

Annexure 1: Production Details

Annexure 2: Site Location Map

Annexure 3: Site Layout Map & Area breakup for Terminal

Annexure 4: Operation Philosophy

Annexure 5: Copy of Consent to Operate

Annexure 6: Storage tank Details

Annexure 7: Water consumption & Waste water generation details

Annexure 8: Fuel consumption details

Annexure 9: Hazardous waste generation details

Annexure 10: Stack details

Annexure 11: Land Possession documents

Annexure 1: Production Details

Table 0-1: Details of Existing & Additional Chemicals Storage

Material

Existing Additional Total

Storage

Capacity

(KL)

Nos. of

Storage

Tanks

Storage

Capacity

(KL)

Nos. of

Storage

Tanks

Storage

Capacity

(KL)

Nos. of

Storage

Tanks

HSD

11000 1 - -

42396 4 13791 1 - -

10805 1 - -

6800 1 - -

MS

9163 1 - -

31952 4 8827 1 - -

6981 2 - -

SKO 8385 2 - -

13615 3 5230 1 - -

LDO 5200 1 - - 5200 1

ATF

16220 2 - -

62072 6

8655 1 - -

7194 1 - -

9783 1 - -

4000 1 - -

EMPTY 180 2 - - 360 2

93-OCTANE 180 1 - - 180 1

ETHANOL 938 2 2000 2 5876 4

Total storage

quantity (KL) 166036 23 4000 2 170036 25

Annexure 2: Site Location Map

Sr. No. Point Latitude Longitude

1 A 28°32'15.97"N 77° 3'37.31"E

2 B 28°32'18.01"N 77° 3'35.83"E

3 C 28°32'26.19"N 77° 3'18.41"E

4 D 28°32'37.89"N 77° 3'27.97"E

5 E 28°32'31.67"N 77° 3'43.50"E

6 F 28°32'29.18"N 77° 3'43.31"E

7 G 28°32'26.39"N 77° 3'40.98"E

8 H 28°32'28.37"N 77° 3'36.88"E

9 I 28°32'21.18"N 77° 3'31.65"E

10 J 28°32'18.92"N 77° 3'35.51"E

11 K 28°32'16.96"N 77° 3'38.70"E

Annexure 3: Site Layout Map

The Total site area is 71 Acres. The area details of the existing facility and the additional facilities are

given below in the Table.

Table 0-2: Area breakup for terminal

S. no. Description Area, m2(Tentative) % of Total Area

1 Storage tank farm area (existing) 53608 18.7

2 Storage tank farm area (additional) 4547 1.6

3 Utility area (FE/PH, PH) 1161 0.4

4 Administrative Building 600 0.2

5 Building Blocks 6515 2.3

6 Parking 240 0.1

7 Roads 5270 1.8

8 Green belt area 16721 5.8

9 Fire water storage area 1325 0.5

10 Loading Unloading area 2446 0.9

11 Misc ( TLF, Open space, scrap yard, lube oil, TT

Parking, Officers coloney etc…) 194894 67.8

Total 287327 100.0

Annexure 4: Operation Philosophy

Delhi Terminal, Bijwasan is a Petroleum Product Storage Terminal of Indian Oil Corporation Limited,

located in New Delhi, the Capital City of Republic of India. The terminal operates in 3 shifts and its

activity involves receipt, storage and distribution of finished petroleum product (Motor Gasolene, Gas

Oil and Aviation Fuel). The product is received from Mathura & Panipat Refineries through cross

country pipelines. There is a provision to receive LDO & Aviation Fuel through Tank Wagons as well.

For storage of various products, Delhi Terminal has 23 Storage Tanks. Delivery of product to various

customers is undertaken through pipelines as well as Tank Lorries. The Terminal also handles Ethanol,

which is mixed in a proportion of 10% by volume with Motor Gasoline for dispatches.

At Bijwasan terminal product inlet is through Mathura Jalandhar pipeline which has commenced on

27th

April 1982 & is around 763 kms in length. This pipeline runs around 147 kms from Mathura to

Delhi with a capacity of about 3.70 MMTPA. Storage capacity of terminal is 165720 KLs with 23 tanks

storing different products. On an average 400 T/T were loaded per day with the help of TLF Gantry

with 30 loading bays & 23 pumps for different products at the terminal

The Terminal is operated in accordance with the provisions of licenses and consents granted by

regulatory departments viz. Departments of Petroleum & Explosives Safety Organization, Directorate

of Factories, Manufacture, Storage & Import of Hazardous Chemical Rules & Pollution Control Board

etc. as per the applicable regulatory statutory acts and rules of Govt. of India.

1.1.1 Activities at Terminal

Tank Lorry Loading - MS, HSD, SKO, ATF, LDO

Tank Lorry Unloading : MS, 93 Octane, SKO, Ethanol

Ethanol blending, at TLF

Loading of additive to the additive tank and blending at TLF

Pipeline Receipt through Cross Country Pipeline – MS, HSD, SKO & ATF

Receipt through Tank Wagon (Intermittent) – ATF, LDO

Inter tank transfer

Tank Water Draining Operation

Sampling of Product from Tank after every receipt

Emptying out of Tank at fixed interval for Maintenance/ Cleaning for Quality Control adherence

Opening of Strainers for Cleaning of Strainer’s Filters at fixed interval.

Maintenance and Repair of various Equipments Viz. Pumps, Motors, Fire Engines, Air

Compressors etc.

Process Flow Diagram of the operation at Terminal is enumerated as under:

Figure 3.1: Process Flow Diagram

1.1.2 Ethanol blending process

Nominate the ETHANOL Tank (TK-21 or TK-22) for MS- Ethanol blending at TLF.

Nominate the ETHANOL Pump (E1 OR E2) for pumping ETHANOL to TLF through the nominated

ETHANOL Tank (TK-21 or TK-22).

Carry out gauging of the tanks and upload the gauges in SAP.

Check line up of the nominated tanks & pumps or pump sequence for TLF Operation, by opening

valves which are numbered for Operating sequence as below.

Figure 3.2: Ethanol blending process

Annexure 5: Copy of Consent to Operate

Annexure 6: Storage tank details

S. No. Tank No. Material Physical

State

Hazard

Involve

Storage

Capacity (KL)

Type of Tank

(CR/FR/UG

/AG/SB)

Height (m) Dia (m)

Operating Condition

Press Kg/Cm2 Temp ºC

1 TK1 HSD Liquid Flammable 11000.00 CR 13.75 M 36.00 Atmospheric Ambient

2 TK2 HSD Liquid Flammable 13791.00 CR 14.00 M 36.00 Atmospheric Ambient

3 TK3 HSD Liquid Flammable 10805.00 CR 14.00 M 32.00 Atmospheric Ambient

4 TK4 MS Liquid Flammable 9163.00 FR 12.93 M 32.00 Atmospheric Ambient

5 TK5 MS Liquid Flammable 8827.00 FR 12.48 M 32.00 Atmospheric Ambient

6 TK6 SKO Liquid Flammable 5230.00 CR 14.33 M 22 Atmospheric Ambient

7 TK7 LDO Liquid Flammable 5200.00 CR 14.34 M 22 Atmospheric Ambient

8 TK8 HSD Liquid Flammable 6800.00 CR 13.41 M 26 Atmospheric Ambient

9 TK9 ATF Liquid Flammable 16220.00 CR 14.93 M 38 Atmospheric Ambient

10 TK10 ATF Liquid Flammable 16220.00 CR 15.00 M 38 Atmospheric Ambient

11 TK11 MS Liquid Flammable 6981.00 FR 16.50 M 24 Atmospheric Ambient

12 TK12 MS Liquid Flammable 6981.00 FR 16.50 M 24 Atmospheric Ambient

13 TK13 ATF Liquid Flammable 8655.00 CR 14.75 M 28 Atmospheric Ambient

14 TK14 ATF Liquid Flammable 7194.00 CR 14.55 M 26 Atmospheric Ambient

15 TK15 ATF Liquid Flammable 9783.00 CR 14.55 M 30 Atmospheric Ambient

16 TK16 SKO Liquid Flammable 8385.00 CR 15.00 M 28 Atmospheric Ambient

17 TK17 SKO Liquid Flammable 8385.00 CR 15.00 M 28 Atmospheric Ambient

18 TK18 EMPTY Liquid Flammable 180.00 SB 16.25 M(L) 3.75 Atmospheric Ambient

19 TK19 EMPTY Liquid Flammable 180.00 SB 16.25 M(L) 3.75 Atmospheric Ambient

20 TK20 93-OCTANE Liquid Flammable 180.00 SB 16.25 M(L) 3.75 Atmospheric Ambient

21 TK21 ETHANOL Liquid Flammable 938.00 CR 12.00 M 10 Atmospheric Ambient

22 TK22 ETHANOL Liquid Flammable 938.00 CR 12.00M 10 Atmospheric Ambient

23 TK24 ATF Liquid Flammable 4000.00 CR 14.70 M 20 Atmospheric Ambient

Annexure 7: Water consumption & Waste water generation details

Water will be sourced through Tankers. As the terminal is providing only storage and handling

services, there is no additional water requirement for processing or operation, water is required only

for gardening and domestic purpose. Terminal’s existing water requirement is 50 KLD. After addition

of two new tanks, domestic water consumption will not increase. So after proposed expansion water

consumption will remain same as 50 KLD.

Table 0-3: Water Consumption Details

S. No. Description Water Consumption in KLD

Existing Additional Total

1 Processing 0 0 0

2 Gardening 10 0 10

3 Domestic 40 0 40

Total 50 0 50

There will not be any generation of industrial effluent. Domestic wastewater will be disposed off in

soak pit through septic tank. Break up of wastewater generation along with disposal mode is given

in following table

Table 0-4: Wastewater Generation and disposal

S. No. Description Wastewater Generation in KLD

Disposal Mode Existing Additional Total

1 Industrial Operation 0 0 0 -

2 Gardening 0 0 0 -

3 Domestic 20 0 20 To send to

Septic Tank

Total 20 0 20

Annexure 8: Fuel consumption details

Table 0-5: Fuel Consumption details

Sr. No. Stack Attached to Capacity Stack Nos. Type of Fuel used Fuel consumption

Existing

1 DG set 2 x 750 KVA +

1 x 500 KVA 5 HSD

140 Ltr/hr. at full

load

2 Fire water Engine

pumps 8 x 616 m

3 8 HSD

35 Ltr/hr. at full

load

Additional

No flue gas stack will be added after additional tankage

Annexure 9: Hazardous waste generation details

Table 0-6: Hazardous waste Generation and disposal

S. No. Hazardous

Waste

Hazardous

Waste Category

Quantity in MTPA Management

Existing Proposed Total

1 Used Oil 5.1 60 liters 0.00 60 liters Disposed to

authorized agency

2 Tank cleaning

Sludge 3.3 0.6 0.02 0.62 Internal Bio- remedial

Annexure 10: Stack details

Table 0-7: Stack details

Sr.

No. Stack Attached to Capacity Stack Nos.

Stack Height,

m

Stack Top

Dia, m

Existing

1 DG set As a backup

during emergency

2 X 750 KVA 4 7 6 inch

1 X 500 KVA 1 7 6 inch

2 Fire water Engine

pumps 8 X 616 m3 8 7 6 inch

Proposed

No flue gas stack will be added after proposed expansion

Annexure 11: Land possession documents