FORM I
FOR
PROPOSED POLYVINYL CHLORIDE PLANT, POLYMER
MODIFIED BITUMEN PLANT, GAS BASED POWER
PLANT, GAS STORAGE TANKS AND LPG BOTTLING
PLANT WITHIN DIGHI PORT LIMIT AT VILLAGE DIGHI
TALUKA SHRIVARDHAN, DISTRICT RAIGAD,
MAHARASHTRA
PROJECT BY
VERITAS POLYCHEM PVT. LTD.
PREPARED BY
M/S. FINE ENVIROTECH ENGINEERS
120, HIREN INDUSTRIAL ESTATE, MOGUL LANE,
MAHIM,
MUMBAI – 400016
SUBMITTED TO
MINISTRY OF ENVIRONMENT & FOREST & CLIMATE
CHANGE
FORM 1
APPENDIX I
(See paragraph – 6)
I.
Basic Information
Sr.
Item
No.
1. Name of the Project
2.
3.
Details
Proposed Polymer Modified Bitumen
Plant, Polyvinyl Chloride Plant, Gas Based
Power Plant Gas Storage Tanks and LPG
Bottling Plant within Dighi Port Limit at
Village Dighi, Taluka Shrivardhan, District
Raigad.
Google image enclosed as Annexure 1
Polyvinyl Chloride (PVC) – 5(f)
S. No. in the schedule
Polymer Modified Bitumen (PMB) – 5(c)
Gas Based Power Plant - 1(d)
Gas Storage Tanks - 6(b)
Proposed capacity / area / length / 1. Polyvinyl Chloride :1,50,000 MTPA
tonnage to be handled / command area
/ lease area / number of wells to be 2. Polymer Modified Bitumen :3,60,000
MTPA
drilled.
3. Gas Based Power Plant: 18 MW
4. Gas Storage Area: 40,000 m3
(Storage Area comprising of 16 gas
storage tanks, each of capacity 2500
m3 for storage of Vinyl Chloride
Monomer, Propylene, Ammonia, LPG)
5. Gas Pipelines of 2200 RM from Jetty to
Plant for  Bitumen Pipeline of 12” Diameter
 LPG Pipeline of 8’ Diameter
 Vinyl Chloride Monomer of 8’
Diameter
 Propylene of 8’ Diameter
6. LPG Bottling Plant: 300000 MTPA
Total Built-up Area = 78267.80 sq.m.
Total Plot Area = 15.9440 ha
Layout Plan Enclosed as Annexure 2
Sr.
No.
4.
5.
6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
Item
Details
Total Project Cost = 1323.75Crores
New
New/Expansion/Modernization
-Existing Capacity/Area etc.
A
Category of Project i.e., ‘A’ or ‘B’
Does it attract general condition? If yes, No
please specify.
Does it attract specific condition? If No
Yes, please specify.
Location
Plot taken from Dighi Port Limited on
Plot/ Survey/ Khasra No.
Long Lease. NOC from Dighi Port
enclosed as Annexure 3
Dighi
Village
Shrivardhan
Tehsil /Town
Raigad
District
Maharashtra
State
Nearest Railway Station/Airport along  Chhatrapati Shivaji Airport, Mumbai :
with distance in kms.
88 km North.
 Roha Railway Station – 25.32 km
North East.
Nearest
Town,
City,
District Roha: 23 km North East.
Headquarters along with distance in
kms.
Village Panchayats, Zilla Parishad, Shrivardhan Municipal Council
Municipal Corporation, Local body
Veritas Polychem Pvt. Ltd.
Name of Applicant
Veritas Polychem Pvt. Ltd.
Registered Address
Veritas House, 70 Mint Road,
Fort , Mumbai – 400 001
Address for correspondence:
Mr. Nitin Kumar Didwania
Name
Owner / Promoter
Designation (Owner/Partner/CEO)
Veritas Polychem Pvt. Ltd.
Address
Veritas House, 70 Mint Road,
Fort, Mumbai
400 001
Pin Code
022-22755555
Telephone No.
022-22755556
Fax. No.
[email protected]
Email
[email protected]
Sr.
Item
No.
16. Details of Alternate Sites examined, if
any. Location of these sites should be
shown on a toposheet.
17. Interlinked Projects
18. Whether separate application of
interlinked project has been submitted?
19. If yes, date of submission
20.
21.
If no, reason
Details
NA
No
No
No
NA
Whether
the
proposal
involves
approval/clearance under: if yes,
details of the same and their status to
No
be given.
(a) The Forest (Conservation) Act, No
Yes
1980?
(b) The Wildlife (Protection) Act,
1972?
(c) The C.R.Z. Notification, 1991?
22. Whether there is any Government No
Order/Policy relevant/relating to the
site?
No
23. Forest Land involved (hectares)
24. Whether there is any litigation pending No
against the product and/or land in
which the project is propose to set up?
NA
(a) Name of the Court
NA
(b) Case. No.
(c) Orders/Directions of the court, if NA
any and its relevance with the
proposed project.
Capacity corresponding to sectoral activity (such as production capacity for manufacturing,
mining lease area and production capacity for mineral production, area for mineral
exploration, length for linear transport infrastructure, generation capacity for power
generation etc.,
II.
Activity
1. Construction, operation or decommissioning of the Project involving actions,
which will cause physical changes in the locality (topography, land use, changes
in water bodies, etc.)
Sr.
Information/Checklist
Yes/No Details thereof (with approximate
No.
confirmation
quantities /rates, wherever possible)
with source of information data
1.1
1.2
1.3
1.4
1.5
1.6
1.7
1.8
1.9
1.10
1.11
1.12
Permanent or temporary
change in land use, land
cover
or
topography
including
increase
in
intensity of land use (with
respect to local land use
plan)
Clearance of existing land,
vegetation and buildings?
Creation of new land uses?
Pre-construction
investigations
e.g.
houses, soil testing?
Construction works?
bore
Demolition works?
Temporary sites used for
construction
works
or
housing of construction
workers?
Above ground buildings,
structures or Earthworks
including linear structures,
cut and fill or excavations?
Underground
works
including
mining
or
tunneling?
Reclamation works?
Dredging?
Offshore structures?
No
No
Yes
Yes
Yes
No
The proposed project will be developed
within the Dighi Port Limit.
The proposed project will be developed on
vacant land.
Dighi port land has approval for port
related / industrial use.
The detailed Geotechnical Investigation is
being carried out.
Yes construction work will be taken for
setting up of plant
Not Applicable
Yes
Yes workers camp will be provided during
construction phase.
Yes
Yes construction work will be taken for
setting up of plant
No
Not Applicable
No
No
Not Applicable
Not Applicable
 Pipeline for transfer of gas and
chemicals will be constructed from
jetty till plant.
Yes
 Intake of sea water & Outfall pipelines
1.13
1.14
1.15
Production and
manufacturing processes?
Facilities for storage
goods or materials?
Yes
of
Yes
Facilities for treatment or
disposal of solid waste or
liquid effluents?
Yes
for Desalination plant.
The production, production capacity,
process details and raw materials are
given as Annexure 4
Separate storage area for goods and
materials will be provided within plant
premises.
Construction Phase:
 Sewage generated during construction
phase will be disposed to septic tank.
 Excavated material generated during
construction phase will be totally
reused in backfilling.
 Other waste’s such as glass, paper and
metal etc. will be sold to recycler.
Other inert waste’s will be disposed
off through local facility.
 Waste’s from labour camp will be
disposed off to local facility.
Operation Phase
 250 kgs of solid waste Municipal
Solid waste generated will be disposed
off to authorized facility.
 Total Sewage Generated (28 KLD)
will be treated in Sewage Treatment
Plant of Capacity 30 KLD and the
treated sewage will be used gardening.
The sludge will be used as manure.

The Effluent generated will be treated
in Effluent Treatment Plant and
treated effluent will be reused for
gardening, flushing, cooling etc.
Water Balance Diagram enclosed as
Annexure 5
1.16
1.17
1.18
Facilities for long term
housing
of
operational
workers?
New road, rail or sea traffic
during
construction
or
operation?
New
road,
rail,
air
waterborne
or
other
No
Not Applicable
No
Not Applicable
No
Not Applicable
1.19
1.20
1.21
1.22
1.23
1.24
1.25
1.26
1.27
1.28
transport
infrastructure
including new or altered
routes and stations, ports,
airports etc?
Closure or diversion of
existing transport routes or
infrastructure leading to
changes
in
traffic
movements?
New
or
diverted
transmission
lines
or
pipelines?
Impoundment,
damming,
culverting, realignment or
other changes to the
hydrology of watercourses
or aquifers?
Stream crossings?
Abstraction or transfers of
water from ground or
surface waters?
Changes in water bodies or
the land surface affecting
drainage or run-off?
Transport of personnel or
materials for construction,
operation
or
decommissioning?
Long-term dismantling or
decommissioning
or
restoration works?
Ongoing activity during
decommissioning
which
could have an impact on the
environment?
Influx of people to an area
in either temporarily or
permanently?
No
Not Applicable
No
Not Applicable
No
Not Applicable
No
Not Applicable
Primarily desalinated water will be used in
the plant. The Water from Maharashtra
Jivan Pradhikaran and Ground water will
be used subject to availability and
permission for the same will be obtained
prior to use of ground water / MJP Water.
Yes
No
Not Applicable
Yes
There will be transportation of
construction material to the project site
during construction phase.
No
Not Applicable
No
Not Applicable
Yes
Construction Phase
During the construction phase about 400
persons will be deployed on the site from
nearby places. Influx of these people will
be temporary in nature.
Operation Phase
During the operation phase about 476
persons will be deployed at the plant.
1.29
1.30
1.31
Introduction
of
alien
species?
Loss of native species or
genetic diversity?
Any other actions?
No
Not Applicable
No
Not Applicable
No
Not Applicable
III. Use of Natural resources for construction or operation of the Project (such as
land, water, materials or energy, especially any resources which are nonrenewable or in short supply)
Sr.
Information/checklist Yes/No Details
thereof
(with
approximate
No.
confirmation
quantities /rates, wherever possible) with
source of information data
2.1 Land
especially
Not Applicable
undeveloped
or
No
agricultural land (ha)
2.2 Water (expected source
Construction Phase
Total Water Requirement during construction
& competing users) unit:
phase will be 23 KLD.
KLD
Domestic use of workers = 8 KLD.
Construction Work = 15 KLD.
Yes
2.3
2.4
Minerals (MT)
Construction material –
stone, aggregates, sand /
soil (expected source –
MT)
2.5
Forests
and
(source – MT)
2.6
Energy
electricity
timber
including
and fuels
No
Yes
Source: Maharashtra Jivan Pradhikaran for
domestic as well as construction use with
prior permission.
Operation Phase
Total Water requirement 3274 KLD
Source: Desalination plant/Kudki Reservoir
(MJP).
Not Applicable
 Stone: 21,800 MT
 Aggregates: 24,000 MT
 Sand: 236,000 MT
 Soil: 15,000 MT
No
Not Applicable
Yes
Electricity
Connected Load: 18010.5 kWh
Demand Load: 17 kWH
(source,
competing
users) Unit: fuel (MT),
energy (MW)
Other Fuel’s
Diesel: 510 liters per month.
LNG : 0.160 MT/MWH
Source:
Gas Based Power Plant of capacity 18 MW
will be set up for fulfill the power
requirement.
2.7
Any
other
resources
appropriate
units)
natural
(use
standard
No
Not Applicable
IV. Use, storage, transport, handling or production of substances or materials,
which could be harmful to human health or the environment or raise concerns
about actual or perceived risks to human health.
Sr. Information/Checklist
Yes/No Details
thereof
(with
approximate
No. confirmation
quantities/rates, wherever possible) with
source of information data
3.1 Use of substances or
materials, which are
hazardous
(as
per
Liquefied gases will be stored. However,
MSIHC rules) to human
storage and handling of hazardous Liquefied
Yes
health
or
the
gases will be as per MSIHC rules.
environment
(flora,
fauna,
and
water
supplies)
3.2 Changes in occurrence
of disease or affect
Not Applicable
disease vectors (e.g.
No
insect or water borne
diseases)
3.3 Affect the welfare of
Not Applicable
people e.g. by changing
No
living conditions?
3.4 Vulnerable groups of
people who could be
Not Applicable
affected by the project
No
e.g. hospital patients,
children, the elderly etc.,
3.5
Any other causes
No
Not Applicable
V. Production of solid wastes during construction or operation or decommissioning
(MT/month)
Sr. Information/Checklist
Yes/No Details
thereof
(with
approximate
No. confirmation
quantities/rates, wherever possible) with
source of information data
4.1 Spoil, overburden or
Not Applicable
No
mine wastes
4.2 Municipal
waste
Construction Phase:
(Domestic
and/or
 Excavated Earth.
Commercial
wastes)
 Solid Waste from labour Camp.
Disposal:
 Excavated Earth will be reused for
backfilling.
 Solid waste from workers camp will be
disposed off through Authorized
Agency.
Yes
Operation Phase:
Solid Waste such as paper, plastic, empty
cartons and waste from pantry / canteen
waste will be generated during operation
phase.



4.3
4.4
4.5
4.6
4.7
Hazardous wastes (as
per Hazardous Waste
Management Rules)
Other industrial process
wastes
Surplus product
Sewage sludge or other
sludge from effluent
treatment
Construction
or
demolition wastes
The municipal waste generated will be
segregated as wet waste, recyclable
waste, inert waste etc.
Wet waste and inert waste disposed of
too authorized agency.
Recyclable waste will be sold to
authorized recycler.
Yes
Details of Hazardous waste generation &
disposal are given in Annexure 6
No
Not Applicable
No
Not Applicable
STP sludge of 82 kg/day will be generated.
Yes
No
Not Applicable
4.8
4.9
4.10
4.11
Redundant machinery
or equipment
Contaminated soils or
other materials
Agricultural wastes
Other solid wastes
No
Not Applicable
No
Not Applicable
No
No
Not Applicable
Not Applicable
VI. Release of pollutants or any hazardous, toxic or noxious substances to air
(Kg/hr)
Sr. Information/Checklist
Yes/No Details
thereof
(with
approximate
No. confirmation
quantities/rates, wherever possible) with
source of information data
There will be stack emissions from
5.1 Emissions
from
combustion of NG and fuel oil in
combustion of fossil fuels
machineries such as Boiler, DG, Power Plant
from
stationary
or
etc. The emission will be controlled by
mobile sources
Yes
provision of Air Pollution Control
Equipments such as Scrubber, Dust
Collectors, Bag Filters etc.
The stack details enclosed as Annexure 7
There will be emissions from production
5.2 Emissions
from
Yes
activity. The adequate stacks/ vents will be
production processes
provided. The emission will be controlled by
provision of Air Pollution Control
Equipments such as Scrubber, Dust
Collectors, Bag Filters etc.
There will be generation of fugitive
5.3 Emissions
from
emission from storage and handling of
materials
handling
Yes
materials.
including
storage or
transport
There will be emission of dust and other
5.4 Emissions
from
gaseous material during construction
construction
activities
activities due to operation of construction
including plant and
Yes
material, construction vehicle, handling of
equipment
materials.
5.5 Dust or odours from
handling of materials
Not Applicable
including construction
No
materials, sewage and
waste
5.6 Emissions
from
Not Applicable
No
incineration of waste
Not Applicable
5.7 Emissions from burning
No
5.8
of waste in open air (e.g.
slash
materials,
construction debris)
Emissions from any
other sources
No
Not Applicable
VII.Generation of Noise and Vibration, and Emissions of Light and Heat
Sr. Information/Checklist
Yes/No Details
thereof
(with
approximate
No. confirmation
quantities/rates, wherever possible) with
source of information data with source of
information data
Noise levels are expected to increase during
6.1 From
operation
of
Yes
construction phase due to operation of
equipment e.g. engines,
construction equipment, movement of
ventilation
plant,
vehicles and other construction activities at
crushers
the project site. During construction phase
noise levels will be addressed by providing
mufflers and earplugs to the persons
working at the project site and by putting
barrier tin sheets around the construction site
to reduce noise in the surrounding areas.
There will be noise generation due to
6.2 From
industrial
or
Yes
operation of plant machineries, handling of
similar processes
materials, vehicle movement etc. during
operation phase which will be addressed by:
 Providing noise barriers in the form of
Green Belt around the premises.
 Proper
maintenance
of
plant
machineries.
 Proper equipment’s for loading and
unloading of vehicles.
There will be generation of noise from
6.3 From construction or
construction activities. However, it will be
demolition
controlled by:
 Provision of noise barriers at the project
site.
 Maintenance of construction machineries
Yes
and vehicles.
 Construction work will be carried out only
during day time.
 Transportation of construction material
only during non-peak hour etc.
NA
6.4 From blasting or piling
No
6.5
From construction
operational traffic
or
Yes
Noise levels are expected to increase during
construction phase due to operation
movement of vehicles carrying construction
materials and other construction vehicles
such as excavators, bulldozers etc. This will
be controlled by:

6.6
6.7
From lighting or cooling
systems
From any other sources
No
Proper signage will be installed to reduce
honking.
 Provision of separate entry exit for
vehicles.
 Transportation of construction material
only during non-peak hour etc.
Not applicable.
No
Not anticipated.
VIII.Risks of contamination of land or water from releases of pollutants into the
ground or into sewers, surface waters, groundwater, coastal waters or the sea
Precautions
will
be
taken
during
7.1 From handling, storage,
transportation, loading/unloading etc. MSDS
use or spillage of
No
will be followed.
hazardous materials
Wastewater generated during operation phase
7.2 From
discharge
of
No
will be treated in ETP and the treated water
sewage or other effluents
will be reused for Gardening, Flushing etc.
to water or the land
Under no circumstances treated or untreated
(expected mode and
liquid waste will be poured with marine water.
place of Discharge)
7.3 By
deposition
of
Air Pollution Control equipment will be
pollutants emitted to air
No
provided at source to prevent emissions in air.
into the land or into
water
Not Applicable
7.4 From any other sources
No
7.5 Is there a risk of long
term build
up of
Not Applicable
pollutants
in
the
No
environment from these
sources?
IX. Risk of accidents during construction or operation of the Project, which could
affect human health or the environment.
Sr. Information/Checklist
Yes/No Details
thereof
(with
approximate
No. confirmation
quantities/rates, wherever possible) with
source of information data
8.1
8.2
8.3
From
explosions,
spillages, fires etc from
storage, handling, use or
production of hazardous
substances.
From any other causes.
Could the project be
affected
by
natural
disasters
causing
environmental damage
(e.g. floods, earthquakes,
landslides,
cloudburst
etc)?
No
Disaster and risk management plan will be
prepared and implemented.
No
Yes
Not applicable
The project will be designed by taking into
consideration these factors as per relevant
codes and standards. The proposed project
site has not reported any kind of natural
disasters like earthquake, floods. Tsunami etc.
However, a proper DMP will be prepared and
executed in case of any such eventualities.
X. Factors which should be considered (such as consequential development) which
could lead to environmental effects or the potential for cumulative impacts with
other existing or planned activities in the locality
Sr. Information/Checklist
Yes/No Details
thereof
(with
approximate
No. confirmation
quantities/rates, wherever possible) with
source of information data
9.1 Lead to development of
supporting
facilities,
ancillary development or
development Stimulated
by the project which
could have impact on the
environment e.g.:
Not Applicable
No
 Supporting
infrastructure
(roads,
power
supply, waste or
Not Applicable
No
waste
water
The project will have positive impact of
Yes
treatment, etc.)
supply industries, due to procurement of raw
 Housing
materials etc. required for production.
development
- Extractive industries
- Supply industries
9.2
 Other
Lead to after-use of the
site, which could have
No
--
9.3
9.4
an impact on the
environment
Set a precedent for later
developments
Have cumulative effects
due to proximity to
other
existing
or
planned projects with
similar effects
No
--
No
Not applicable.
III. Environmental Sensitivity
Sr.
Areas
Name/
Aerial distance (within 15 km.) Proposed
No.
Identity
project location boundary
1
Areas protected under
international
conventions, national or
Phansad wildlife sanctuary located at a
local legislation for their
Yes
distance of 11 km towards the North East.
ecological,
landscape,
cultural or other related
value
2
Areas
which
are
important or sensitive
for ecological reasons –
Proposed project is located within Dighi Port
Wet-lands, watercourses
Yes
situated near Rajpuri Creek.
or other water bodies,
coastal zone, biospheres,
mountains, forests
3
Areas used by protected,
important or sensitive
species of flora or fauna
Not Applicable
No
for breeding, nesting,
foraging, resting, over
wintering, migration
The proposed project situated at intertidal
4
Inland, coastal, marine
Yes
zone and falls under CRZ I and IV.
or underground waters
5
State,
National
Not Applicable
No
boundaries
6
Routes or facilities used
Murud Jangira Fort: 2 km East across the
by the public for access
Yes
creek.
to recreation or other
tourist, pilgrim areas
Not Applicable
7
Defense installations
No
Roha: 23 km
8
Densely populated or
Yes
9
10
11
12
built-up area
Areas
occupied
by
sensitive man-made land
uses (hospitals, schools,
places
of
worship,
community facilities)
Areas
containing
important, high quality
or
scarce
resources
(ground water resources,
surface
resources,
forestry,
agriculture,
fisheries,
tourism,
minerals)
Areas already subjected
to
pollution
or
environmental damage.
(Those where existing
legal
environmental
standards are exceeded)
Areas susceptible to
natural hazard which
could
cause the
project
to
present
environmental problems
(Earthquakes,
subsidence, landslides,
erosion, flooding or
extreme
or
adverse
climatic conditions)

Dr. A.R. Undre English High School &
Junior College, Diveagar: 13 km South.
Sir S. A. High School, Murud: 4.60 North
East
Yes

No
Not Applicable
No
Not Applicable
No
The project will be designed by taking into
consideration these factors as per relevant
codes and standards. The proposed project site
has not reported any kind of natural disasters
like earthquake, floods. Tsunami etc.
However, a proper DMP will be prepared and
executed in case of any such eventualities.
“I hereby given undertaking that the data and information given in the application and
enclosures are true to the best of my knowledge and belief and I am aware that if any of the
data and information submitted is found to be false or misleading at any stage, the project will
be rejected and clearance give, if any to the project will be revoked at our risk and cost.
Date: 06.07.2017
Place: Mumbai, Maharashtra
ANNEXURE 1
GOOGLE IMAGE SHOWING LOCATION OF PROJECT SITE OF VERITAS POLYCHEM PVT. LTD.
ANNEXURE 2
LAYOUT PLAN
ANNEXURE 3
NOC FROM DIGHI PORT
ANNEXURE 4
PRODUCTS, RAW MATERIALS REQUIREMENT & PROCESS DESCRIPTION
Sr. no
Product
Quantity
Unit
1.
Polyvinyl Chloride
1,50,000
MTPA
2.
Polymer Modified Bitumen
3,60,000
MTPA
3.
Gas Based Power Plant
18
MW
4.
Gas Storage
m3
6.
LPG Bottling Plant
40,000
(Storage Area comprising of 16 gas
storage tanks, each of capacity 2500
m3 for storage of Vinyl Chloride
Monomer, Proplylene, Ammonia,
LPG)
300000
5.
Gas Pipelines of 2200  Bitumen
Running meter from Jetty to
 LPG
Plant for-
MTPA
12” diameter
8” diameter
 Vinyl Chloride Monomer
8” diameter
 Propylene
8” diameter
PROJECT DESCRIPTION
The Project comprises of a 150,000 MTPA Polyvinyl Chloride (PVC) manufacturing plant
and a 360,000 Polymer Modified Bitumen (PMB) plant, 16 mounded bullets for storage of
gases with a 18 MW captive gas based power plant at Dighi Port, Maharashtra. The brief
description of Project is given below:
POLY VINYL CHLORIDE PLANT
VPPL proposes to buy a PVC plant form Petroliam Nasional Berhad (Petronas) in Malaysia.
This plant is capable of producing suspension grade PVC (grades K57, K67 and K70). The
manufacture of suspension grade PVC is envisaged through vinyl chloride monomer (VCM)
route, where VCM is polymerized to produce the PVC slurry using agitators and additives.
The license for the plant shall be provided by Ineos Technologies, UK., the world’s largest
PVC technology provider having long standing experience in the related field.
Poly Vinyl Chloride (PVC) is the most versatile thermoplastic forming on one extreme,
highly rigid products such as pipes and profiles and on the other, highly flexible products
such as soft leather cloth & flexible footwear. The basic structure of this polymer is
(C2H3Cl)n. The degree of polymerization varies from 300 to 1500. The chlorine content in
PVC is about 57% by weight which makes it less dependent on hydrocarbon content.
Review of Process Technology
There are mainly four polymerization routes for the manufacture of PVC. They are as
follows :
Process Route
Suspension Polymerization
Emulsion Polymerization
Bulk or Mass Polymerization
% of World Production
80
10
8-10
It can be seen from above that suspension polymerization is the most prevalent technology in
the world today. The leading licensors for this technology are Ineos Technologies (UK) and
Oxy Vinyl Corporation (US) In this process Vinyl Chloride Monomer (VCM) droplets are
dispersed in water medium aided with suspending agents and agitation in the Reactors/
polymerizers. Polymerization of VCM to PVC takes place in this medium initiated by
peroxide catalyst. Multiple batch reactors discharge into a continuous polymer separation and
finishing line. The polymer slurry from the reactors is first separated from unconverted VCM
by degassing and steam stripping. Water is separated from the polymer by means of
centrifuging followed by drying.
PVC produced through the Emulsion polymerization process is mainly used as latex or paste
in specialty applications. In Europe manufacture of PVC started with the emulsion process.
The process is similar to the suspension process except that large amounts of emulsifying
agents are used which result in very fine PVC particles. Consequently, separation of these
fine PVC particles from water cannot be done by centrifuging action. Hence this technology
employs spray dryers to separate water from the fine PVC particles.
Production capacity
Plant capable of manufacturing K-57, K-66,K-70 grades of suspension PVC. Low K value
and High K Value grades also can be produced. The plant is capable to produce the full range
of PVC grades for fulfilling most market requirements. 150,000 MTPA expandable to
200,000 MTPA within the same infrastructure without any further expansions. The plant at
present is assumed to be working for 300 days in a year of suspension grade PVC.
Raw materials
Sr. no.
Raw Material
Quantity
1.
Vinyl Chloride Monomer
15,000 m³
2.
Water (De-Mineralized)
25,000 m³
3.
Suspending Agent (Poly Vinyl Alcohol)
50 MT
4.
Initiator (Peroxy Compound)
30 MT
5.
Alpha Methyl Styrene
40 MT
Unloading, storage & Feeding system for VCM
VCM is a colourless liquid with a characteristic sweet odour. It is highly reactive, though not
with water, and may polymerise in the presence of oxygen, heat and light. Its vapours are
both toxic and flammable. Aluminium alloys, copper, silver, mercury and magnesium are
unsuitable for vinyl chloride service. Steels are, however, chemically compatible.
Unloading condition
Unloading at
Unloaded by
Pressure at ship pump flange, kg/cm2g
Unloading Carrier
:
:
:
:
Dighi Port
Marine Unloading arm
30.0 (min)
7500 CBM
Each consignment of 7500 cbm pressurised liquid VCM shall be unloaded from ship with the
help of ship unloading pumps through one numbers of 8” marine unloading arm & shall be
transferred to proposed VCM storage bullets at VPPL gas storage Terminal.
Pipeline transfer facilities
8“ lines shall be employed for transfer operation of VCM from Ship. Two mass flow meters,
one at jetty end & one at tank end shall be provided for mass measurement & input to leak
detection system. The motorized operated valve shall be provided at jetty for emergency
shutdown operation in case of leak.
Receipt & Storage facility at Gas Storage Terminal
The VCM from ship will be transferred & stored in 6 nos of pressurized VCM bullets at 10.5
kg/cm2. 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 CCOE. 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 is SA 537 CL.II, the selected material
conforms to design code.
iii. Design Temperature is (-) 27 oC to + 55 oC.
iv. Design Pressure is 25 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
 The 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 (SRV). Each storage vessel shall have minimum
two different types of level indicators and one independent high level switch.
 Each vessel is provided with one pressure and temperature measuring instrument. The
pressure gauge shall be provided with isolation valves.
Process Description
Preparation and charging of de-mineralized water
Part of de-mineralized water from de-mineralized water tank is used in polymerization
charging, bearing seal priming, sealing, agitator/ pump seal flushing, reactor rinsing etc.. Part
of cold de-mineralized water cooled by cooling water is stored in cold de-mineralized water
tank and used for buffer preparation, catalyst preparation and additive preparation.
Preparation and feeding of addition agents
All the chemical agents of polymerization, such as initiators, dispersants, buffering agents,
de-foaming agents, Shortstops (terminators), etc. are prepared and stored in their own
reservoirs. When the polymerization reaction occurs, chemical agents are sent to polymerizer
by pumps according to specified quantity in the recipe and specified procedure.
Polymerization
De-mineralized water, dispersants, buffers and initiators are automatically added into the
polymerization reactor in a closed state according to PVC production process recipe for the
type and amount of raw materials and the feeding program of DCS settings. Polymerization
starts when the initiators are automatically added. By automatically adjusting the level of
cooling water, the reaction temperature is maintained. Polymerization reaction takes place in
accordance with the required temperature curves; the polymerization reaction heat is
measured by a microcomputer to calculate the monomer conversion rate. When the
conversion rate is met, the terminators are automatically added into polymerization reactor to
terminate polymerization, PVC slurries automatically discharged to the Vessel. After PVC is
blowdown, the reactor wall shall be rinsed with water of appropriate pressure.
Shortstop (Terminator) System
This process adopts two shortstop systems for two different purposes, and adopts different
shortstops. One is for normal production stop of each batch operations; the other is for
emergency, during mechanical or power failure.
Vacuum System
Vacuum system shall be adopted to draw out air from all equipment of the unit contacting
VCM to ensure safety of the unit after maintenance.
VCM recovery System
Un-reacted VCM from polymerization reactor and stripping outlet trough shall pass through
the VCM Recovery unit in order to be used for utilization in the polymerizer.
PVC slurry stripping
PVC slurry stripping process shall be provided to efficiently remove and recover residual
vinyl chloride monomer from PVC resin. The PVC from the blowdown vessel enters the
stripping tower. In the stripping tower PVC slurry shall make heat exchange with cooling
water in a countercurrent flow. After stripping, the PVC slurry shall be stored in bin and sent
to PVC drying section. The VCM after stripping tower passes through the top stripping tower
condenser then to gas-liquid separator and finally sent to VCM recovery section.
PVC Centrifuge and drying
This section is composed of dewatering, finished product drying, screening and gas
conveyance. PVC slurry after stripping enters centrifuge. After de-watering in the centrifuge,
wet PVC resin is fed in dryer. Warm air shall be used to dry wet PVC resin. Then after, the
PVC enters the vortex type cyclone dryer for drying of critical moisture content. The dried
PVC powder shall be separated with the air flow by the cyclone separator set. Finished PVC
product after screening shall be delivered to PVC intermediate silo and it goes into packaging
process by mixing pump.
Part of the mother liquor from the PVC centrifuge goes to stripping tower for flushing the
tower, and part of it goes to PVC mother liquor treatment and recycle system.
PVC Packaging and Product ware house
PVC material from finished product silo is measured and bagged into 25kg/bag by
quantitative semi-automatic packaging machine. After packaging, the packed PVC will be
transported to PVC ware house by forklift.
Process Flow Diagram
Brief process flow diagram is indicated below. Detailed process flow diagram is attached as
Annexure.
Figure 1-Process flow diagram for PVC manufacturing
2. POLYMER MODIFIED BITUMEN (PMB) PLANT
Bitumen, one of the commercial products of petrochemical refinery, is primarily used in road
construction, the tar roads to be specific. PMB is a specific type of bitumen which has higher
tensile strength than normal bitumen. Locally, PSU’s such as IOCL, BPCL, and HPCL
produce VG30 grade of bitumen. The manufacturing process of PMB entails heating normal
bitumen (VG30 grade bitumen) with styrene butadiene styrene (SBS) or ethyl vinyl acetate
(EVA) at about 180 Deg C in large Blenders. SBS or EVA is thermoplastic additive which
binds with the bitumen when heated at high temperatures to produce PMB.
Raw Materials
Sr. no.
Raw Material
Quantity
1.
Bitumen
15,000 m³
2.
SBS (Polymer)
200 MT
3.
EVA (Polymer)
200 MT
Design Basis
 Plant Capacity :- 1000 Tons / Day
 Bitumen Class :- Class 60 – 70 and Class 80 – 100
Bitumen Property Table:Properties
Penetration at 25°C, 0.1mm
Class 80 - 100
Class 60 - 70
80
100
60
70
Softening point, °C
45.0
52.0
45.0
52.0
Flash point, °C
276
-
276
-
Viscosity at 60°C (Poise)
140
-
260
-
Viscosity at 170°C (Poise)
0.45
-
0.65
-
Process Description
Unloading & Handling facilities at Dighi jetty:
Bitumen shall be unloaded from ship at a with the help of ship unloading through one
numbers of 12” marine unloading arm & shall be transferred to proposed storage tanks at
VPPL.
Pipeline transfer facilities
12“ lines shall be employed for transfer operation of Bitumen from Ship. Two mass flow
meters, one at jetty end & one at tank end shall be provided for mass measurement & input to
leak detection system. The motorised operated valve shall be provided at jetty for emergency
shutdown operation in case of leak.
Unloading through
1 No of 12” transfer line
Receipt & Storage facility
The Bitumen from ship will be transferred & stored in 2 nos of storage tank with a storage
capacity of 2500 Cu.M. each.
Bitumen is stored in Conical Roof & inverted cone at bottom storage tanks. Each inlet line is
provided with motorized valve which has provision to open / close by hand in case of power
break-off. These tanks shall have one nozzle for inlet & one for pump recycle inlet, also one
outlet nozzle for PMB blender pump suction header. Tanks are provided with LP steam
supply & condensate return line to keep required temperature inside storage tank.
Inlet nozzle of recycle line is provided with jet mixer to mix the content in the tank &
maintain uniform density. Tanks are equipped with temperature & pressure transmitter which
are connected to level indicator. Level indicator will indicate level of tank after considering
temperature & pressure in the tank. High level switch is also provided.
Combining Agent
Combining agents are sometimes added to PMBs to improve their performance properties
and shelf life and will comply with the requirements of the AAPA Guide to the safe use of
SBS.
Polymer
The common generic polymer types used for the manufacture of PMBs are Styrene
Butadiene Styrene (SBS), Polyethylene’s and Ethylene Vinyl Acetate (EVA).
Mixing
All polymer maintained at elevated temperatures for long periods will be subject to three
competing reactions: increase in molecular weight leading to gelation, caused by cross
linking of the unsaturated bonds; a similar, oxygen induced, polymerization; and breakdown
reactions. Additionally bitumen are subject to hardening on prolonged high temperature
exposure. All of these reactions can be minimized by maintaining close control of operating
temperatures and residence times in the mixing equipment. Additional measures that will
reduce any tendency to polymerize by nitrogen blanketing of the mixing vessel. Component
materials have to be thoroughly mixed to ensure production of a homogeneous PMB. Critical
elements that are common to all processes include procedures for proportioning of materials,
temperature control, mixing time and conditions, and maintenance and cleanliness of
equipment.
Storage of the Finished Product
2 nos. of Tanks for the storage of finished product with a storage capacity of 2500 cbm will
be designed to minimize deterioration in storage, with strict control of temperature, minimal
surface area to reduce oxidation, and provision for mixing or circulation to ensure that the
product remains homogenous in storage.
Polymer Modified Bitumen is stored in Conical Roof & inverted cone at bottom storage
tanks. Each inlet line is provided with motorized valve which has provision to open / close by
hand in case of power break-off. These tanks shall have one nozzle for inlet & one for pump
recycle inlet, also one outlet nozzle for drum filling pump suction header. Tanks are provided
with LP steam supply & condensate return line to keep required temperature inside storage
tank.
Inlet nozzle of recycle line is provided with jet mixer to mix the content in the tank &
maintain uniform density. Tanks are equipped with temperature & pressure transmitter which
are connected to level indicator. Level indicator will indicate level of tank after considering
temperature & pressure in the tank. High level switch is also provided. The heating system
will be designed such that the PMB is not exposed to high contact temperatures around the
heating elements or flues for prolonged periods. Prolonged exposure of PMBs to heating
elements may result in deterioration and carbonization of the binder. Tanks will be provided
with good circulation of the PMB around heating elements or flues, either through the use of
mechanical stirrers and/or by circulating the tank contents with a pump. The tank heating
system commonly used for PMB storage uses heat transfer oil and automated temperature
controls to limit overheating.
Loading Gantry
All supply lines throughout the plant, including loading equipment to be designed and
procedures will be established as to avoid contamination during change of product or
cleaning of supply lines. The use of oils such as kerosene, diesel, or gas oil for flushing lines
will be avoided. Where lines need to be flushed, it will be done with hot bitumen or finished
product. Any oils used for flushing or cleaning of supply lines will be collected and disposed
of separately and will not be added to products or components in storage or delivery vehicles.
Bitumen Barrel Filling and Packing Facility
The Polymer Modified Bitumen will have a mechanized and semi auto with a capacity of
6000 Drums per day. Facilities for receipt and storage of Bulk Bitumen and all
infrastructures required for Bitumen handling including tank truck unloading arrangement.
Bitumen process flow diagram
3. GAS STORAGE TERMINAL
VPPL proposes to construct 16 mounded bullets which would be used for storage of
chemicals at high pressure. Each of these bullets would have a capacity of 2500 m3
aggregating to storage capacity to 40,000 cum. Out of these 16 tanks, 6 are proposed to be
utilized for storage of VCM, the raw material for PVC production. The remaining 10 tanks
would be utilized for trading other chemicals viz:- LPG & propylene.
Design Basis
LPG – Composition – mole %
Designation
Straight Run LPG
Cracked LPG
Sp. Gr. @ 15 Deg C
0.51 – 0.58
0.51 – 0.58
Viscosity @ ST, CST
0.18 – 0.40
0.18 – 0.40
Water content in LPG
200 ppm
200 ppm
(As Caustic Solution)
(As Caustic Solution)
RSH – H (wppm)
10 (Max)
5 (Max)
Re Entry – S + RSH – S,
wppm (Max)
40
40
Caustic (NaOH)
Traces
Traces
Total Sulphur Presence, ppm
150 (Max)
150 (Max)
Liquid Propylene: - Composition wt%
Designation
Composition, Wt. %
PROPYLENE
Case - 1
Case – 2
Ethylene
0.02
0.093
Ethane
1.089
0.233
Propylene
95.196
95.198
Propane
3.69
4.470
Properties of Propylene
Water Content in Propylene
200 ppm (As Caustic Solution)
As H₂S, RSH & COS, wppm (max)
5, 10 , 10 Respectively
Sp. Gr. @ 15 Deg C
0.515 – 0.522
Viscosity @ ST, CST
0.15 – 0.38
Total Sulfur Presence, ppm
25 (Max)
Caustic (NaOH)
Traces
Unloading condition
Parameter
Unloading at
Unloaded by
LPG
Dighi Port
Marine Unloading arm
Pressure at ship pump flange, kg/cm2g
Unloading Carrier
30.0 (min)
7500 cbm
Propylene
Dighi Port
Marine Unloading
arm
30.0 (min)
7500 cbm
Process Description
Unloading & Handling facilities at Dighi jetty:
Pressurized liquid LPG and propylene shall be unloaded from ship with the help of ship
unloading pumps through two numbers of 8” marine unloading arm & shall be transferred to
proposed LPG and propylene Bullets at VPPL gas storage Terminal.
Pipeline transfer facilities:
Both the 8“ lines shall be employed for transfer operation of LPG and propylene from Ship.
Two mass flow meters, one at jetty end & one at tank end shall be provided for mass
measurement & input to leak detection system. The motorised operated valve shall be
provided at jetty for emergency shutdown operation in case of leak.
Receipt & Storage facility at Gas Storage Terminal
The LPG from ship will be transferred & stored in 2 nos of pressurised LPG bullets at 14.5
kg/cm2 and Propylene from ship will be transferred & stored in 8 nos of pressurised
propylene bullets at 23.0 kg/cm2 .
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 CCOE. 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 is SA 537 CL.II, the selected material
conforms to design code.
iii. Design Temperature is (-) 27 oC to + 55 oC.
iv. Design Pressure is 25 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
 The 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 (SRV). Each storage vessel shall have minimum two
different types of level indicators and one independent high level switch.
 Each vessel is provided with one pressure and temperature measuring instrument. The pressure
gauge shall be provided with isolation valves.
Despatch Facilities at Gas storage Terminal
LPG & Propylene truck Loading:
LPG and propylene will be sent to truck loading facility.
Process Parameters
Unloading & handling facilities at Dighi jetty:
Ship unloading frequency
Max. 2 Vessels in a week
Unloading by
2 Nos of 8” Marine Unloading Arm
Pipeline transfer facilities
Unloading through
2 Nos of 8” transfer line/
Receipt & Storage facility at LPG Marketing Terminal
Storage Capacity of Bullet cu.m  8 Propylene bullets with storage capacity of 2500 M³ in
each bullet

No. of Mounded Bullet
Size
2 LPG bullets with storage capacity of 2500 M³ in each
bullet
2 LPG + 8 Propylene
One mound consisting of eight (8) Propylene bullets (each
70m long & 7.4m dia. Propylene storage capacity of 2500
M³) shall be constructed and One mound consisting of two
(2) bullets (Each 63m long & 7.4m dia. LPG storage
capacity 2500
VCM / Propane / Butane Transfer Pump:
Liq. VCM from bottom outlet of all the VCM bullets is pumped to the PVC plant by two (2)
VCM transfer pumps out of the two pumps, one is standby.
Liq. LPG from the bottom outlet is pumped to marketing area by two (2) LPG transfer pumps
out of two pumps, one LPG pump shall be used for Recirculation and another pump is
common standby.
Two Propylene pumps (1+1) of similar draw suction of liq. Propylene from bottom of the
Propylene Bullets and send the product to marketing area.
VCM Transfer Pump
Type
: Vertical Canned Type with double mechanical seal
Flow, MT/hr
: 25 (1W + 1S) Each for LPG & Propylene
MOC
: LTCS
LPG Transfer Pump
Type
Flow, m3/hr
MOC
: Vertical Canned Type with double mechanical seal
: 100 (1W + 1S)
: LTCS
Propylene Transfer Pump
Type
Flow, m3/hr
MOC
: Vertical Canned Type with double mechanical seal
: 100 (1W + 1S)
: LTCS
Dispatch Facilities at Gas Terminal
Loading to
Loading temperature, ºC
Loading by
No. of loading Station
Pumping Rate, MT/hr
: Un-insulated road tankers.
: 15
: LPG / Propylene transfer pumps
: 4 bay Tanker Loading Facility
: 100
4. GAS BASED CAPTIVE POWER PLANT
VPPL proposes to setup a 17MW gas based power plant for captive consumption. The gas
required for the production of power is proposed to be sourced from GAIL through gas
pipelines including the Metering Station, which shall be within the boundary limit of the
plant. There is already a pipeline connecting Dabhol and Panvel passing through Mangaon.
GAIL will lay the pipeline up to the plot area including metering station located within the
boundary limit of plant. Alternatively, LNG can also be procured using the local transport /
can be imported at the port and can be re-gassified from the third party contractor.
Raw Materials
Sr. no.
1.
Raw Material
Quantity
0.168 MT/MWH
LNG
Direct pipeline from GAIL
2.
Water (De-Mineralized)
Common 25,000 M³
Process flow diagram
5. LPG Bottling Plant
Veritas have also proposed an LPG bottling plant of 300,000 MTPA. LPG will be coming to
the unit by road in trucks or imported LPG by vessel at Dighi Port. This will be stored in
bullets and then filled in various cylinders within the plant and sold to the customers. The
proposal is only storage and bottling of LPG.
Demand – Supply Gap
LPG is a growing market in India and every year the demand is increasing from 6 to 10%.
Veritas will provide energy solutions to the nearby industries for better safety and cost
optimization Company has seen the interest of industrial customers in the Konkan area for
conversion from conventional fuels to LPG.
Type of the Project
The proposed project is new LPG bottling facility to bottle 300,000 MTPA. The proposed
project falls under the schedule 6 (b) as per the EIA notification dated September 14, 2006
and its amendments. There is no interlinked project. The project falls under the Category B.
Project Location
The plot of land is acquired from Dighi Port, as stated above. A number of other industrial
undertakings are being planned and under execution in the nearby notified industrial areas.
Magnitude of Operation
S. No.
1
2
3
4
5
6
Proposed Packing
Composite Cylinder 2 Kg
Composite Cylinder 5 Kg
12 Kg
17 Kg
33 Kg
Bulk Supply
Quantity (No./ Month)
7,500,000
9,000,000
6,250,000
5,294,118
909,091
1,800 Tankers (18 MT each)
Bottle filling System
As mentioned above the filling station will fill the cylinders and the composite cylinders with
the capacities mentioned above. In the filling station the empty cylinders (various capacities)
will be fed to the automated chain conveyor system. The conveyor system will be routed
through the following units for completing the filling process:
 Empty cylinder weight scale with CVT
 Cylinder washing unit
 Electronic filling machines (60 No.s)
 Online electronic cylinder weight scale unit
 Digital compact valve tester unit (DCVT)
 In line Test bath
 Hot air sealing unit
The filled LPG cylinders will be conveyed and stored in the filled cylinder storage shed. If
any cylinders are rejected from the online electronic check scale unit then it will be directed
to the manual weight correction unit where the weight correction will be done manually and
then it will be routed to the automated conveyor for subsequent process. If any filled cylinder
fails in the DCVT and in line test bath unit, then the defective cylinders will be directed to
evacuation rack for evacuation and repairing work. The evacuated LPG from rejected
cylinders will be collected in an evacuation vessel and then will be transferred to the storage
bullets. The emptied cylinder will be purged using the purging unit. The liquid LPG will be
supplied to the filling heads through LPG vane pumps. The LPG pumps suction and
discharge lines will be designed with all safety requirements.
Fire Fighting Details for the Bottling Unit
Fire Fighting System Description
Following are the type of fire protection systems for proposed LPG bottling plant:
 Automatic Fire Water Pumping System consisting of one Main Pump, one Standby Pump
& one jockey pump.
 External Hydrant & Water Monitor System covering the entire proposed bottling unit area
for manual firefighting.
 Medium Velocity Water Spray System for Cylinder filling sheds, Filled storage sheds,
Tank truck gantry (four bays), LPG Pump / Compressor shed, Fire Detection & Alarm
System covering the entire proposed unit area.
 Portable Fire Extinguishers.
 Personnel Health & Safety Equipment.
Design Basis for Pumps for the Unit
Spray density of 10LPM/m2 is considered as per OISD: 169 clause 4.4.2.
Highest Water Requirement for water spray system is 4000 LPM for cylinder filling shed.
As per OISD: 169 clause 4.4.2. (iii), the fire water system in the plant shall be designed to
meet the highest fire water flow requirement of a single largest risk of any cases at a time
plus 72 Cu. M per hour for operating 2 hydrant points.
6. PIPELINE FROM JETTY TO PLANT AREA
8“ lines of 2200 RM length shall be employed for transfer operation of VCM from Ship.
Two mass flow meters, one at jetty end & one at tank end shall be provided for mass
measurement & input to leak detection system. The motorized operated valve shall be
provided at jetty for emergency shutdown operation in case of leak.
Both the lines shall be employed for transfer operation of LPG and propylene from Ship. Two
mass flow meters, one at jetty end & one at tank end shall be provided for mass measurement
& input to leak detection system. The motorised operated valve shall be provided at jetty for
emergency shutdown operation in case of leak.
12“ lines shall be employed for transfer operation of Bitumen from Ship. Two mass flow
meters, one at jetty end & one at tank end shall be provided for mass measurement & input to
leak detection system. The motorised operated valve shall be provided at jetty for emergency
shutdown operation in case of leak.
Service gas
12” Bitumen pipe line from jetty to terminal
Material
:
A 106 Gr.B seamless
Pipe sch./thk.
:
Sch. STD
Design/dimensions
:
ANSI B 36.10
Lengths
:
In 5 to 6 m lengths
End finish
:
Bevelled end as per ANSI B 16.25
Pressure Rating
:
Class 150#
Service
8” LPG pipe line from jetty to gas terminal
Material
:
A 106 Gr.B seamless
Pipe sch./thk.
:
Sch. 40
Design/dimensions
:
ANSI B 36.10
Lengths
:
In 5 to 6 m lengths
End finish
:
Bevelled end as per ANSI B 16.25
Pressure Rating
:
Class 300#
Service
8” VCM pipe line from jetty to gas terminal
Material
:
A 106 Gr.B seamless
Pipe sch./thk.
:
Sch. 40
Design/dimensions
:
ANSI B 36.10
Lengths
:
In 5 to 6 m lengths
End finish
:
Bevelled end as per ANSI B 16.25
Pressure Rating
:
Class 300#
Service gas
8” Propylene pipe line from jetty to terminal
Material
:
A 333 Gr.6 seamless
Pipe sch./thk.
:
Sch. STD
Design/dimensions
:
ANSI B 36.10
Lengths
:
In 5 to 6 m lengths
End finish
:
Bevelled end as per ANSI B 16.25
Pressure Rating
:
Class 300#
Typical cross section of piping on sleepers
Layout plan for LPG & Propylene unloading & transfer
Layout plan for LPG & Propylene unloading & transfer
ANNEXURE 5
WATER BALANCE DIAGRAM
ANNEXURE 6
HAZARDOUS & NON-HAZARDOUS WASTE GENERATION & DISPOSAL
Sr.
no.
Description
1
2
3
Biological ETP Waste
Garbage
Canteen Waste
4
Insulation waste
5
6
7
8
9
10
11
Rejected Filter / Scrap
Spent / Lube Oil
Sludge and Filter Contaminated with Oil
Discarded Containers / Barrels
Industrial Batteries
Chemical Sludge
Water Treatment / Phosphate Sludge
Quantity
NON-HAZARDOUS WASTE
30 TPA
80 TPA
10 TPA
12 TPA
HAZARDOUS WASTE
4 TPA
10 TPA
3 TPA
10,000 Nos/ Annum
15 Nos/ Annum
50 TPA
5 TPA
Disposal
Reuse as Manure in gardening
 The municipal waste generated will be
segregated as wet waste, recyclable waste,
inert waste etc.
 Wet waste and inert waste disposed of too
authorized agency.
 Recyclable waste will be sold to authorized
recycler.
Will be given to MPCB authorized recycler
Common Treatment facility
Common Treatment facility