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Pre Feasibility Report for proposed LPG Bottling Plant at Bhaunti, PO-
Panki, Tehsil: Kanpur Nagar, District: Kanpur, Uttar Pradesh.
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Pre Feasibility Report for proposed 3 x 1,450 MT capacity mounded
LPG storage vessel, at BPCL, Kanpur POL Depot , Bhaunti, PO-Panki,
Kanpur Nagar, Kanpur, Uttar Pradesh.
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Pre Feasibility Report for proposed LPG Bottling Plant at Bhaunti, PO-
Panki, Tehsil: Kanpur Nagar, District: Kanpur, Uttar Pradesh.
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1. INTRODUCTION 1.1 GENERAL
Bharat Petroleum Corporation limited (BPCL), the project proponent, is a fortune 500 oil
refining, exploration and marketing PSU with Navratna status company. BPCL is engaged
in refining and marketing of petroleum products. The company is India's one of the
largest commercial enterprises.
Oil marketing companies have projected an increase in demand of Liquefied Petroleum
Gas (LPG) in future due to increase in its domestic use. The demand is likely to increase
substantially over the years to come. Even in the present scenario it is very difficult to
meet the market demand of Kanpur and adjoining areas by Bharat Petroleum
Corporation Limited. As per directive of the Ministry of Petroleum and Natural Gas,
Government of India, different Oil companies are required to augment / construct new
facilities to meet the growing demand.
In line with the requirement envisaged and to ensure fulfillment of demand, Bharat
Petroleum Corporation Limited proposes to construct new LPG Bottling Plant facility at
it’s existing BPCL Kanpur POL Depot, near Bhaunti, PO-Panki, Tehsil: Kanpur Nagar,
Kanpur District in Uttar Pradesh State with a storage capacity of 3 X 1,450 MT. This
proposed plant shall meet the short supply of LPG Cylinders in the area and also decrease
BPCL’s dependence on other oil companies. This will also meet the present and future
house hold demands of people.
2 PROJECT DESCRIPTION
BPCL proposes to provide NEW 90,000 MTPA LPG Bottling Plant conforming to OISD 144
with LPG Storage in the form of 4,350 MT (3 x 1,450 MT) Mounded Storage Vessels which
will be distributed through LPG Cylinders in Kanpur and nearby areas.
2.1 PROJECT LOCATION
Bharat Petroleum Corporation Limited will install the 3 x 1450 MT LPG storage mounded
vessel along with other associated facilities in existing Kanpur POL Depot. The Land is
located in Bhaunti village, PO: Panki, Tehsil: Kanpur Nagar, District: Kanpur which is
about 4.38 kms away from Panki Railway station. LPG Plant plot Area is approx. 11.74 Ha.
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Pre Feasibility Report for proposed LPG Bottling Plant at Bhaunti, PO-
Panki, Tehsil: Kanpur Nagar, District: Kanpur, Uttar Pradesh.
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Particulars
Area (Ha)
Percentage (%)
Plant Area, Office Area, and housing (all covered area) 3.02 25.72%
Paved Area ( Road, Corridor, Parking and drainage) 2.12 18.06%
Green Belt Area 3.70 31.52%
Open Area 2.90 24.70% Total Plot Area 11.74 100
2.1.1 Connectivity
Nearest Railway Station – Panki R.S. 4.38 km towards E
Nearest Airport – Kanpur Airport (Chakeri Air Force Station), Nearest Town- Kanpur
14.15 Km
Nearest City – Kanpur 14.15 km
Nearest District – Kanpur Dehat 26.95 km WSW
District Headquarter- Kanpur Dehat 26.95 km WSW
2.2 COMPOUND WALL, GATES AND FENCING
A 3M high compound wall with 0.6M high concertina wire fencing on top of the wall is
proposed. One no. of 6M wide Main Gate with one wicket gate for plant with security
office and Emergency Gate of 6M wide has been proposed.
2.3 KERB WALL FENCING
To segregate the licensed area, 0.6 M height kerb wall with 1.2 meter high chain link
fence shall be provided at appropriate places.
2.4 STORAGE VESSEL:
3 Nos. x 1450 MT capacity Mounded Storage Vessels have been considered. The bullets
shall be of dia. 8.00 M and 65.0 M length. However, actual dimensions shall be as per
approved design of the successful vendor. CCOE approval shall be obtained for the
proposed bullets. Also calibration of bullets shall be got approved from approved
calibration agencies by the vendor.
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Pre Feasibility Report for proposed LPG Bottling Plant at Bhaunti, PO-
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2.5 FILLING CUM EMPTY CYLINDER SHED
Shed size of 37.5M X 65M with 12 M X 15 M Fingers (2 nos.) loading / unloading
platform shall be provided for stacking empty cylinders and filling facilities.
Filling of LPG Cylinders will be done by 1x 48 station Electronic carousel which shall have
all the required upstream and downstream facilities( like cylinder washing/drying/in-
line check scales, GD/PT units, correction units, cap hammering unit, washer replacement
loop etc) complying with all guidelines and statutory norms. Additionally, adequate
number of on-line valve change machines (without evacuation) shall be installed to take
care of the valve leak detected cylinders.
One number electronic check scale (platform type) of 50 kg capacity to be provided at
unloading bay for random checking of new & pressure tested cylinders as per QAP.
Manual Filling Facility:
One conveyor line shall be provided for filling of 19/35and 47.5 Kg cylinders with facility
for Online dosing for BMCG.
In the above line a separate inline filling station shall be provided to fill 5 Kg cylinders.
Scale accuracy of 10 gm.
Special type heavy duty reversible conveyer shall be provided for safe and easy handling
of these cylinders.
Online Cylinder Purging facility shall be provided with capacity 1600 cylinders/hr.
The list of equipments is as under.
A. 1 x 48 Station Electronic Carousel with Dynamic check scale, WCU, VLD & OLD.
B. Cylinder Washing Unit to wash empty cylinders
C. Automatic Valve Changing Machine
D. Purging unit
E. Chain / Roller conveyor system with drive units
F. One Hot Air Sealing System
G. Vapour Extraction System
H. CVT
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I. Test Bath
2.6 FILLED CYLINDER STORAGE SHED
Shed of size 45 M X 37.5 M with 12 M X 15 M Finger loading platform ( to accommodate
2 lorries at a time.) will be provided.
Filling shed & filled cylinder shed are interconnected by 6.0 M wide gangway for
conveyors. Similarly, gangway connection of 7 M wide shall be provided between filing
shed and valve change shed. Statistical quality control loop (SQC) with roller conveyor
will be provided with an inline check scale and CVT. All the loading/unloading fingers and
gangway shall be provided with sprinkler coverage.
2.7 INHOUSE PRESSURE TESTING FACILITY
Separate shed of 35 X 15M size shall be provided to house PT facility with LPG vent pipe
from 2 X 10 head test bench extending to a point having 30 mtr clear distance all around.
PT shed to be located adjacent to Valve Change Shed. Adequate provision of conveyors
shall be considered for movement of cylinders.
Following equipments shall be integral to the PT facilities:
Cylinder Washing tank
Valve screwing & unscrewing machine
Tilting type 2 X 10 head Test bench with closed air and water vessels of suitable
capacity
Pneumatic testing facility with air compressor capable of providing 12 kg/cm2 air
pressure
Painting booth with blower
Flameproof/Intrinsically safe platform type electronic weighing scale of up to 250
kg capacity.
Ultrasonic cleaning and valve salvaging machines shall be provided.
The above system will be semi automatic.
In addition to the above, open hard standing will be provided for stacking the cylinders
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Pre Feasibility Report for proposed LPG Bottling Plant at Bhaunti, PO-
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2.8 CHAIN CONVEYOR SYSTEM
As per the requirement of Electronic carousel, the speed of chain conveyor system shall
be between 12 – 22 M/Min. On the Introduction line and Ejection line, the speed should
be minimum 22 M/Min and 18M/Min up to the test bath. A layout will be developed
showing the position of OLD/VLD and the location of test bath and HAS. The ratings &
numbers of Drive Units will be provided commensurate with the new electronic carousel.
One Telescopic Chain Conveyors and one Manual Chain Conveyor each for loading and
unloading Fingers shall be provided. This is adequate to cater to the requirement of 24
Stn. Electronic Carousel.
Careful design shall be planned on floor keeping operational and aesthetics aspects in
mind. Further, conveyors shall be designed to offer high efficiency at designed load with
help of high efficiency motors/helical or direct mount gear boxes etc. Auto on-off
operation of loop conveyers at correction, valve & O-ring change and evacuation
conveyors to be provided.
Telescopic conveyors to be provided for unloading/loading of empty/filled cylinders to
and from box lorry with photoelectrical type auto sensing/tripping system.
All electric motors shall be of high efficiency “ Eff 1 “ grade .
2.9 LPG PUMP / COMPRESSOR SHED
The pump house will be of size 16 M x 8 M. 2 nos. LPG pumps (100 Cu.M / hr, 160 M
Head) will be provided for bottling.
2 no. LPG compressor (150 CFM) will be provided for unloading of bulk tank lorries. One
no. LPG Loading pump of 50 M3/hr, 80 M Head shall be provided for loading Bulk LPG.
Suitable capacity cooling tower with cooling water pumps as per requirement to be
provided.
2.9 ADMIN. / AMENITY BUILDING / PLANNING ROOM
20 M X 15M double story building will be provided to accommodate office space,
conference rooms, canteen, amenities etc with internal partitions / furniture.
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15 M X 10 M single story building will be provided for planning room including Dress
change room/Toilet.
2.10 SECURITY CABIN / PLANNING ROOM/ CHANGE ROOM
10 M x 15 M double story building to be provided at the main gate.
2.11 ENGINEERING/CONSUMABLES STORES
Engineering cum Consumables Stores of 12 M X 8 M has been proposed. This would be a
shed with false ceiling for store keeper. A field toilet with emergency eye wash facility is
also being provided adjacent to the stores.
2.12 MCC & HT Room
20 M X 8 M building will be provided to house HT (Vacuum type) Breaker / LT panel etc.
meeting operational and statutory requirements.
Transformer shall be indoor type located behind the MCC Room in a 5 M X 5 M enclosure
with minimum safety distance as per IE Rules. Transformer shall be provided with AVR
on HT side , in case necessary to eliminate unwanted power consumption due to voltage
fluctuation. Suitable APFC panel to maintain plant power factor above 0.95 shall be
ensured.
Separate arrangement bypassing main LT breaker shall be provided to maintain power
supply to critical areas (i.e. plant lighting, siren, fire control panel & road barriers etc) in
case of emergency shutdown of plant.
2.13 DG SET
DG Sets of capacity 2 x 480 KVA & 1x 160KVA having acoustic enclosures will be
provided adjoining to MCC room in 20M x 6M shed. 2x480 KVA set will be used for full
load plant operation while 160 KVA unit will take care of light load and emergency power
requirement.
Provision of Diesel Tanks for supply of Diesel to the DG sets will be made outside the
shed. The stack height to DG sets will be provided as per CPCB guidelines.
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Pre Feasibility Report for proposed LPG Bottling Plant at Bhaunti, PO-
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2.14 HT ROOM
HT room of 4 M X 5 M. Location shall be frozen in consultation with state electricity
board.
2.15 CYCLE /CAR SHED
Cycle Shed of size 15 M X 2.5M and Car Shed of size 15.0Mx5.5M will be provided.
2.16 INSPECTION PLATFORM
At least 1.5M wide and 6m long inspection cum counting platforms will be provided in
front of security gate, to check LPG packed lorries.
2.17 WEIGHBRIDGE
50 MT capacity electronic way bridge with SAP interface shall be provided. ¼ th Capacity
Dead weights shall be provided for calibration/testing.
2.18 TANK LORRY GANTRY
8 Bay TLD gantry of size 16 M X 5.5 M for Unloading of tank lorry with MFM on common
header to facilitate automation. All unloading bays will be provided with suitable loading
arms with break-away type coupling and Earthing interlocks.
2.19 TRUCK PARKING AREA/DRAINAGE SYSTEM
Approximately 2500 Sq M bituminized area will be developed inside the plant boundary
for parking of 30 nos. Trucks/lorries. Provision of Solar powered illumination shall be
explored to illuminate the area as part of BPCL’s RE policy.
Open Drainage system will be provided covering admin/tank lorry parking area.
2.20 PCVO CREW REST ROOM/BARRIER GATE
A room of sizes 10M X 4M will be provided nearer to tank lorry parking area for the use
of PCVO crew. Toilet / Wash room will be provided as per requirement. Suitable
broadcast arrangement shall be made for relaying safety messages/films for enhancing
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Pre Feasibility Report for proposed LPG Bottling Plant at Bhaunti, PO-
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PCVO crew awareness. Solar powered systems shall be explored to illuminate the area as
part of BPCL’s RE policy.
4 Nos of Lifting barrier gate will be provided. 2 nos near to time office and 1no at
emergency gate/ 1no at Tank lorry parking area.
2.21 FIRE PROTECTION FACILITIES
a. Fire water storage; 2 Nos. above ground vertical water tanks each of capacity 2600
KL as per OISD requirement will be provided. (Actual FW calculation to be
attached).
b. Fire water pump house (shed) : - Pump house of size 25M X 8M (200 M2) will be
provided to accommodate 3 Nos. diesel driven fire water pump sets of 616 KL/HR
and two no. electric motor driven jockey pumps of 10 KL capacity shall be
provided. The room shall be provided with OHT (Over head trolley) suitable to
handle the equipments load.
c. Fire hydrant system: - Fire hydrant ring main covering all facilities will be provided
as per the OISD requirements. Double hydrants (with hose boxes, hoses & nozzles)
and fire water monitors as per the stipulations in the OISD-144 will be provided.
Long range Fire Monitors shall be provided in critical areas with remote operation.
d. MV Spray system: As per OISD norms for Fire Protection System.
e. Fire Extinguishers: Shall be provided as per OISD norms
f. Deluge Valves: Auto reset type deluge valves having manual quick bypass system as
per OISD norms shall be provided with fire protection wall. Provision for activation
of DV shall be for auto and manual modes (local & remote panel) as per OISD-144.
g. All the isolation valves used in Fire fighting system should be of rising stem type.
h. MCP: Manual Call Points at strategic locations as enumerated in OISD-144 shall be
provided to raise alarm (siren) and also shut down LPG operations ,in case of
emergency with suitable hooter on annunciation panel at fire water pump house.
2.22 GAS MONITORING SYSTEM
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Pre Feasibility Report for proposed LPG Bottling Plant at Bhaunti, PO-
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Gas monitoring system with infra red / Catalytic type sensors shall be provided as per
revised OISD standard-144. Mimic & repeater panels shall be provided at FWPH (Fire
Water Pump House) /Control room and security gate.
2.23 AIR COMPRESSOR / RECEIVER / DRYER
Two nos. 350 CFM ( to be reviewed with OEM) Screw type integrated Air-compressors
along with refrigerated Air dryers and air receivers of capacity 350 CFM shall be
provided to cater to the requirement of instrument air for carousel, pneumatics, ROV etc.
One no of 100 CFM Air compressor shall be used for PT, pneumatics, ROVs, Fire
protection system etc.
Shed of Size 8 M x 8 M shall be provided for housing these equipments adjacent to DG
Sets.
2.24 ELECTRICAL SYSTEM
Incoming supply will be taken from State Electricity Board preferably through an
independent feeder to ensure uninterrupted power supply from grid.
2.25 TRANSFORMER
800 KVA transformer with provision for Automatic Voltage Regulator (AVR based on
roller contact technology with permissible voltage vaiation of +/-1% and 98% plus
efficiency) on HT side will be provided in the plant.
2.26 MAXIMUM DEMAND
MAXIMUM DEMAND expected is 500 KVA.
2.27 ELECTRICAL FITTINGS
All electrical fittings will be as per the area classification (refer OISD-113) and prevalent
IE Rules. All Motors to be of Eff 1 Grade.
2.28 MAIN INSTRUMENT CONTROL PANEL (MIC)
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Flame proof ROV control panel shall be provided at LPG Pump House with parallel
display at FWPH /Control room.
2.29 BORE WELL
Two no. of bore well shall be provided for storing and pumping drinking water shall be
made.
2.30 ROADS
Bituminized Roads 6.0 m wide and arterial roads connecting the main roads having width
of 3.5M shall be provided inside the plant.
2.31 PLANT SECURITY SYSTEM
Provision of following facilities shall be ensured:
1. Handheld metal detector for frisking
2. Door Frame Metal detector
3. Mirror trolley
4. Integrated Biometric Access Control System
5. Digital Surveillance through CCTV cameras with memory back-up for 30 days. All
critical areas i.e. Admin Bldg, Filling shed, LPG Pump House, Tank Farm, TLD Gantry ,
Parking and Gate areas to be covered under constant surveillance.
6. Perimeter surveillance
7. Sufficient High mast illumination in parking as well as for plant.
2.32 VAPOUR SEAL
Suitable vapour seals to be provided in storm water drain at the following areas:
Drains around filling & filled cylinder sheds
Bulk storage
Boundary
2.33 COMMUNICATION SYSTEM
Following systems to be provided:
Intrinsically Safe Paging System
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PA System for announcement at gate
Inter-com at all working stations/points as per advice
Walkie-talkie for designated staff(VHF/UHF)
Display of carousel performance at TC cabin & Planning
2.34 ENVIRONMENTAL INITIATIVES
Admin Building and main gate shall be tastefully landscaped with provision for
gardening and plantation. About 3.7 hectares of land will be used for green belt
development.
The location shall have suitable Rain Water Harvesting (RWH) System for ground
recharge as well as arrangement to replenish collected water from sump.
Effluent Treatment Plant (ETP) shall also be provided meeting Pollution norms.
Energy efficient lighting (i.e. LED / Induction type) shall be provided
Administrative and planning sections will be designed for abundant natural light
and air. Additionally, LED based illumination shall be explored to reduce
dependence on DG & EB power.
Solar heating system shall be provided for Staff Canteen
3 PROCESS PARAMETERS & DESIGN BASIS
A) The proposed LPG bottling Plant at BPCL Kanpur shall be designed based on the
following statutory codes / standards: -
1. OISD STANDARD 144 LATEST REVISION
2. OISD STANDARD 150 LATEST REVISION
3. SMPV (U) RULES – 2016
4. GAS CYLINDER RULES – 2016
5. ASME / API / BIS CODES PERTAINING TO LPG
6. FACTORIES ACT – 1948
7. ELECTRICAL INSTALLATION UNDER ELECTRICITY RULES --1956
B) Basic process parameters of the new LPG Plant has been mentioned in the below Table
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3.1.
Table 3.1
PROCESS PARAMETERS PLANT CAPACITY 90000 MTPA Plant
PLANT LAYOUT & FIREFIGHTING SYSTEM
Conforms to OISD-144 / OISD 150 /OISD 116
LIQUID TO BE HANDLED LPG as per IS –4576
CYLINDER CAPACITY TO BE FILLED
Domestic cylinder (14.2 Kg) Small numbers commercial cylinders( 19 Kg, 35 kg,47.5 ) as well as 5 Kg cylinders. Hippo Cylinders
PRODUCT RECEIPT Product will be received through road tankers and pipeline
CYLINDER STORAGE 2 Shed concept 1. Empty Cylinder & Cylinder filling shed (65 m X
37.7m) – 5800 Cylinders. 2. Filled cylinder storage shed (45 m X 37.5 m) – 5000
Cylinders.
PROPERTY LAND DEMARCATION
Compound wall 3M height with 0.6M barbed wire strand / concertina fencing on top as per our standard drg.
LICENSED AREA DEMARCATION
0.6M height wall with 1.2 M height chain link fencing on front side and tank truck parking partition shall be Boundary Wall.
NO OF TANK LORRY UNLOADING BAYS
8 bays Tank lorry gantry
CAPTIVE POWER GENERATING SETS
2 X 480 KVA DG for plant and 1 No. 125 KVA DG for yard light and jockey pump.
TRANSFORMER 800 KVA with AVR
LORRY PARKING AREA Paver blocks of 2500 M2 area will be provided.
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FILLING/TESTING EQUIPMENTS
CYLINDER WASHING / DRYING UNIT
1 No.
CAROUSEL SYSTEM Electronic Carousel with auto tare wt reader 48 station with OLD/VLD along with 3 no online auto filling machines for 19kg/5kg, two nos. stationery filling machines with pre-filling/CVT/Testbath/Check scale for 35.0/ 47.5 kg cylinder filling & one no. stationery filling machine with pre-filling/CVT for Hippo cylinders
WEIGHT CORRECTION UNIT
Dynamic check scale
TEST BATH Inline
SINGLE CVT FOR SQC,VCM,MANUAL M/C
4 No.
CVT VERIFIER 1 No.
INLINE CHECK SCALE 2 nos inline check scales of capacity 600 cylinders/hr and 10 gms LC each would be provided one before SQC loop and another before purging unit for new LPG cylinders.
PURGING FOR NEW CYLINDER
Online Auto purging facility with capacity of 1600 cylinders per hrs.
HOT AIR SEALING SYSTEM
1 or 2 No. in line with production capacity of carousel
VALVE CHANGING MACHINE
Online – 2 nos.
AUTO CAPING UNIT 1 NO.
PORTABLE HOT AIR SEALING M/C
2 NO.
AUTO SQC SYSTEM 1 NO
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MAJOR EQUIPMENTS
LPG COMPRESSOR 2 Nos. LPG Compressor of 150 CFM Cap.
LPG FILLING PUMP 2 Nos. pump (1 main & 1 stand by) having Cap. 100 m3/hr, head of 160 M.).
AIR COMPRESSOR 2 Nos. (350 CFM) + 1 No 100 CFM for PT shed.
AIR DRYER 2 No. (400 CFM)
FIRE WATER PUMP 3 Nos. – 616KL / Hr, head 105 M
JOCKEY PUMP 2 No. of 10 KL per hr cap.
DG SET- 480 KVA 2No.
DG SET - 125 KVA 1No.
TRANSFORMER 800 KVA
1 No.
HT BREAKER 1 No.
FACILITIES
ADMIN / AMENITY / TIME OFFICE BUILDING
300 Sq. M. (Double storied)
TIME OFFICE 15 MX 6 M
SECURITY OFFICE 3.0 MX 5.0 M
CYCLE / SCOOTER PARKING SHED 120 Sq.M. area of size 20 x 6 M.
FIRE WATER TANK 17.03 M Dia. X 11.5 M High X 2 Nos. (Capacity: 5200 KL each) , should have water storage for four hours fire fighting for largest risk area.
FIRE WATER PUMP SHED 25 M X 8 M
AIR COMPRESSOR / RECEIVER / DRIER SHED
10 M X 6 M
D G Platform 12 M X 6 M
( The above three sheds are combined in one block )
MCC / MLDB / LT ROOM 20 M X 6 M
ENGINEERING STORE 15 M X 6 M
( The above two RCC Buildings are combined in one block )
2 POLE STRUCTURE 1 No.
TRANSFORMER YARD 10 M X 10 M
TRIVECTOR ROOM(optional) 3 MX 3 M
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INSPECTION PLATFORM 6 M X 1.5M
FILLING / EMPTY CYLINDER SHED 65 M X 37.5 M
FILLED CYLINDER SHED 45 M X 37.5 M
LOADING / UNLOADING FINGERS 15 M X 12 M X 2nos
LPG MOUNDED BULLETS 3 Nos. – 1450 MT Each
LPG PUMP SHED 16 M X 8 M
BULK UNLOADING BAY 16 M X 5.5 M – 8 Nos.
HIGH MAST TOWER 30 M High (4 Nos.)
TANK LORRY PARKING AREA with Paver blocks
2500 Sq.M. (Approximately)
PCV CREW REST ROOM 10 M X 4 M
WEIGH BRIDGE 1 No. OF 50 MT (16 x 3 M size)
SERVICE WATER PUMPS 2 Nos.
CATHODIC PROTECTION ROOM 3M X 3M
COOLING TOWER 1
CHANGE ROOM FOR STAFF 4*6 Meters.
Toilets block 3*6 Meters.
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4 PROCESS FLOW DIAGRAM OF LPG PLANT
5 SAFETY PHILOSOPHY
LPG is a common material used extensively in households as well as industry. If its
characteristics are understood well and proper precautions as stipulated in various codes
and standards are followed, it is an easy and safe material to handle. Accordingly, in most
of the developed / developing countries, where LPG is consumed in million tons / year,
specific codes and standards are available for storing and handling of LPG.
5.1 LPG INSTALLATIONS - CODES & STANDARDS
Codes and standards which are generally followed for LPG installations are as follows:
1. NPPA (National Fire Protection Association of USA) Standards
- NFPA-58 : Standard for the Storage and Handling of Liquified
Petroleum Gases
- NFPA-59 : LP-Gases at Utility Gas Plants
2. API (American Petroleum Institute) Standards
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- API-2510: Design & Construction of LPG installations
3. IP (Institute of Petroleum) Standards .
- IP-9: Liquified Petroleum Gas - Large Bulk Storage of Pressurised
and Refrigerated LPG
4. The Static and Mobile Pressure Vessels (Unfired) Rules, 2016 of India
(SMPV Rules)
5. OISD (Oil Industry Safety Directorate) Guidelines
- OISD RP - 158 : Recommended Practices on Storage and Handling of Bulk
Liquified Petroleum Gas (LPG), 1997. (This is being followed by Public Sector
Refineries and Oil Industry in India. It is currently a guide and not a mandatory
code or standard).
LPG storage tanks take any other pressurised vessels may be designed as per any of the
following well known international or local codes / standards:
- ASME, Section VIII, Division I
- ASME, Section VIII, Division II
- BS 5500
- IS 2825
5.2 MOUNDED STORAGE FOR LPG
LPG is normally stored in above ground storage mainly spheres and cylindrical tanks,
namely, bullets & Horton spheres, the advantage being their accessibility for regular
inspection and maintenance which is important for such storage for hazardous service.
But these storages are susceptible to fire impingement and can give rise to Boiling
Liquid Expanding Vapour Explosions (BLEVE).
The reason for selecting mounded or buried bullets for LPG storage is to protect
them from direct flame impingement caused by any eventual fire in the
surroundings and thus prevent initiation of the sequence of events leading to an
occurrence of BLEVE.
The mounded storage concept basically originated from Europe and specialized codes
exist in Germany such as:
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DIN 4681 Tl : Statutory Steel Pressure Vessels for Liquified Petroleum Gases for Earth
Covered Installations, Dimensions and Equipment.
During construction phase, a slight increase in the ambient noise levels is anticipated.
This impact will be temporary and limited to the construction phase. Hence no
permanent impact on this account is expected.
During the operational phase, no major social impact in the general area is expected.
There will be no change in the occupational structure of the workforce. As there will be
no emissions into air, no liquid effluents and no solid wastes no negative impact on the
health of the inhabitants in and around the project site is expected.
5.3 Water Resources
The total water requirement for the project and further during operation of plant i.e.
regular domestic use, fire fighting storage, drinking purpose etc. shall be done through
two bore Well within our premises.
5.4 Water Quality and Aquatic Ecology
The proposed LPG plant will not generate any process effluent. The only wastewaters
from the plant will be domestic effluent. The domestic wastewater will be treated
through septic tank followed by a soak pit. Water used for firefighting drills will be used
for gardening & water harvesting etc.
Hence no permanent impact will be caused on the environment on this account.
5.5 Air Quality
The dust from earthworks, vehicular emissions and the usage of D.G. set in case of power
failure are the only sources of air pollution from the site.
Power supply will be met by Uttar Pradesh State Electricity Board (UPSEB). There is no
requirement of steam hence no boiler and no emissions due to utilities. Since the
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Pre Feasibility Report for proposed LPG Bottling Plant at Bhaunti, PO-
Panki, Tehsil: Kanpur Nagar, District: Kanpur, Uttar Pradesh.
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proposed facilities plan to receive, store and dispatch LPG there are no process emissions
as well.
Adequate heights of the stacks for atmospheric emissions help dispersing and diluting
pollutants to within the prescribed limits. In view of the above mentioned point there
will be no impact on the air quality. There will be no significant effects on air quality in
the context of human health.
During construction phase, a slight increase in noise is anticipated. This impact will be
temporary and limited to the construction phase. After the construction phase no major
increase in the noise level is expected. Hence no permanent impact on this account is
expected.
5.7 Environmental Hazards
The project proponents have designed all the safety aspects in planning, designing and
operation of the plant as per international practice. Such safety aspects are adequate to
take care of any hazard associated with the project.
5.8 Terrestrial Ecology
Any construction activity brings a significant change to the site top soil and some
components of the local terrestrial ecosystem. However, the adverse impacts are
restricted to the project construction site and to some extent its immediate vicinity. The
selected site is plain and leveled and will involve excavation and site preparation.
Rare or endangered species of flora and fauna do not exist in and around the proposed
site. Adequate green belt will be planted which will provide improved vegetation
habitat.