7.1 public consultation - welcome to · pdf file7.1 public consultation ... is an important...
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ADDITIONAL STUDIES7
136
7.1 PUBLIC CONSULTATION
The proposed project site is situated in Chincholi MIDC area. Hence, as per Environmental
Impact Assessment (EIA) Notification No.S.O.1533 (E) dated 14th
September 2006; and
amendment there at the proposed project does not requires conducting of public hearing. The
EIA report has been complied by incorporating required information with regards to the
project as mentioned in the Terms of Reference (TORs) issued by EAC to Sri Krishna
Pharmaceuticals Ltd (SKPL), MIDC Chincholi, Tal.: Mohol, Dist.: Solapur during 3rd
EAC
meeting held on 18.01.2016.
7.2 RISK ASSESSMENT REPORT
Under proposed manufacturing facility, bulk drug & intermediates will be manufactured by
batch production and will be carried out on campaign basis. General production process for
proposed products consist of
1. Various organic reactions in 2 to 3 stages in various solvent mediums 2. Recovery of solvents by batch distillation for recycles and reuse of solvents. 3. Layer separations and recovery of crystallized product by centrifuge. 4. Drying operation to get the final product.
7.3 HAZARD IDENTIFICATION
7.3.1 Classification of Chemicals:
In a chemical industry for primary hazard identification, classification of different chemicals
is an important factor. The classification of chemicals to be used by SKPL is presented in
following table-
Table 7.1 Classification of Chemicals used in SKPL
Group of
Chemical
Group
Members
Handling Spill Emergency Storage
Flammable
Liquids
OPDA
MAA
O-Xylene
BCP
Toluene
MIBK
Methanol
Ammonia
DMF
Acetone
PNBA
Iron power
Control of
electrostatic
charges.
Non-sparking
tools.
Containment
Inertisation.
Spill control
material
Eye/skin/
breathing PPE
Fire safety
training.
Contain
spill.
Prevent
mixing with
water
sources.
Refer TREM
card.
Arrest leak
by closing the
valve if is
safe to do so.
Contact local
police/
supplier
Take vehicle to
safe area
without
endangering life
Place warning
signs around the
vehicle.
Prevent crowd
approach to the
vehicle.
Contact local
police/supplier
Assist
emergency team
as per the need.
Ventilated place
Containment
Leak detectors
Absence of
oxidizers
Fire protection
system
Non sparking
tools
FLP fixtures as
per IS
Hot work
permits system.
Spill control
material.
Flame arrester
for storage tanks
ADDITIONAL STUDIES7
137
Group of
Chemical
Group
Members
Handling Spill Emergency Storage
Reactive
Chemicals
Caustic Lye
(48%)
MIBK
Thionyl
chloride
H2SO4
Iron power
Refer MSDS
before
handling
Avoid
incompatible
materials
around
handling area.
Ensure
inertisation
Make
available
compatible
fire
extinguishers.
Avoid
shocks/drops
and rolling
while
handling
containers.
Ensure
inertisation
while
charging in to
reactors.
Contain spill.
Prevent
mixing with
water
/moisture
Refer TREM
card.
Arrest leak by
closing the
valve if is
safe to do so.
Contact local
police/
supplier
Take vehicle to
safe area
without
endangering life
Place warning
signs around the
vehicle.
Prevent crowd
approach to the
vehicle.
Contact local
police.
Assist
emergency team
as per the need.
Refer MSDS for
compatibility
before storage.
Store air reactive
materials under
nitrogen.
Store water
reactive
materials away
from water/
moisture/
Aqueous
solutions.
Use visible sign
boards for
warning about
hazards and
cautions for
responders.
Make available
compatible fire
extinguishers.
Do not store the
materials in
flammables
storage area.
Avoid
shocks/drops
and rolling
while handling
containers.
Ensure water
layer above
Raney/Ni
catalyst all the
times
Oxidizers Conc. HCl
(30%)
Acetic acid
H2SO4
Refer MSDS
before
handling
Avoid
incompatible
materials
around
handling area.
Ensure
inertisation
Make
available
compatible
Contain spill.
Prevent
mixing with
flammables
combustibles
Refer TREM
card.
Arrest leak
by closing the
valve if is
safe to do so.
Contact local
police/
Take vehicle to
safe area
without
endangering life
Place warning
signs around the
vehicle.
Prevent crowd
approach to the
vehicle.
Contact local
police
Assist
Do not store
with flammables
and
combustibles
Do not store
with reducers.
Exclusive
storage place
advisable.
ADDITIONAL STUDIES7
138
Group of
Chemical
Group
Members
Handling Spill Emergency Storage
fire
extinguishers.
Avoid
shocks/drops
and rolling
while
handling
containers.
supplier
emergency team
as per the need.
Corrosive
Liquids
Conc. HCl
(30%)
Acetic acid
H2SO4
Chlolro
Sulphonic
Acid
Wear full
gloves,
respirator
with face
shield and
body
protection
while
handling.
Ensure
neutralizing
agents
nearby.
Contain spill.
Prevent
mixing with
flammables/c
ombustibles
Refer TREM
card.
Arrest leak
by closing the
valve if is
safe to do so.
Contact local
police/
supplier
Wear all the
PPE kept in
vehicle
before
handling
spill.
Spread
neutralizing
agent like
Calcium
oxide/ash
liberally on
the spill.
Take vehicle to
safe area
without
endangering life
Place warning
signs around the
vehicle.
Prevent crowd
approach to the
vehicle.
Contact local
police/supplier
Assist
emergency team
as per the need.
Consider
secondary
containment.
Store on non-
corrosive
surface
Consider local
exhaust system
Store away
from azides,
sulphides, and
hydrosulphides
and metal
powders.
Separate
organic acids
and In-organic
acids.
Segregate
water reactive
corrosive
liquids from
water moisture
and aqueous
solutions.
Keep
neutralizing
agents nearby.
Store
containers on
sand bed.
Display board
at the entrance
to avoid use of
water or water
based
extinguishers
during fire
fighting.
ADDITIONAL STUDIES7
139
7.3.2 Risk Prone Areas
Based on classification of chemicals the hazard prone areas have been identified as follows-
Reaction and separation Sections
Storage of chemicals in tanks or respective vessels
Handling of the materials or the process equipment by the operator or worker.
Transportation of the products and raw materials.
Underground Storage tank.
7.3.2.1 Reaction and Separation Sections
Major hazard in this section is of fire, explosion leading to toxic release. Extent of the
damage depends on the hazardous properties of the reactants, reaction and separation
conditions. Minimum risk is of most importance and this can be achieved by selecting an
intrinsically safe process and optimizing operating process parameters near to the
atmospheric conditions. But this is not possible most of the time. Hence, it is necessary to
install safe guards and build in perfect operating procedure that will minimize chances of
accident to the minimum. Also types of reaction taking place during the process are of prime
importance. It may be exothermic or endothermic. The same will be followed for the
expansion product facilities.
Exothermic Reactions.
HAZOP studies will be carried out for potentially dangerous and hazardous reactions in the
manufacturing of products. The reaction includes the chlorination in the production of folic
acid in stage II. All safety features will be designed to mitigate the risk and hazard to
minimum. For controlling exothermic reaction