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M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-4: Anticipated Environmental Impacts & Mitigation Measures
4.28
Environmental Impact Assessment Report
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-4: Anticipated Environmental Impacts & Mitigation Measures
4.29
Environmental Impact Assessment Report
Figure 4.2 Ground level concentration of SO2
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-4: Anticipated Environmental Impacts & Mitigation Measures
4.30
Environmental Impact Assessment Report
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-4: Anticipated Environmental Impacts & Mitigation Measures
4.31
Environmental Impact Assessment Report
Figure 4.(3) Ground level concentration of NO2
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-4: Anticipated Environmental Impacts & Mitigation Measures
4.32
Environmental Impact Assessment Report
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-4: Anticipated Environmental Impacts & Mitigation Measures
4.33
Environmental Impact Assessment Report
Table 4.5: Predicted 24 hourly short term incremental Concentrations of SPM
Sr. No.
Monitoring Stations
Distance from site
Direction
Base Line Concentration
(µg/m(3)) (98 percentile)
Predicted SPM
Concentration (µg/m(3))
Total SPM Concentrations
implementation of the proposed project
µg/m(3)
1 (A1) Project site -- 0 78.40 0.8 79.2
2 (A2) Becharpura 1.7 Kms NNE 89.75 1.0 90.75
3 (A3) Kamana 2.3 Kms NW 88.91 0.5 89.41
4 (A4)Meghaliyasana 2.7 KMs SW 77.79 0.1 77.89
5 (A5) Basna 4.8 Kms ENE 85.09 0.8 85.89
Table 4.5: Predicted 24 hourly short term incremental Concentrations of SO2
Sr.
No.
Monitoring
Stations
Distance
from
site
Direction
Base Line
Concentration
(µg/m(3))
(98 percentile)
Predicted
SPM
Concentration
(µg/m(3))
Total SPM
Concentrations
implementation of
the proposed project
µg/m(3)
1 (A1) Project site -- 0 25.52 0.1 25.62
2 (A2) Becharpura 1.7 Kms NNE 29.49 0.06 29.55
3 (A3) Kamana 2.3 Kms NW 40.36 0.04 40.4
4 (A4)Meghaliyasana 2.7 KMs SW 36.68 0.04 36.72
5 (A5) Basna 4.8 Kms ENE 28.98 0.007 28.987
Table 4.6 Predicted 24 hourly short term incremental Concentrations of NO2
Sr. No.
Monitoring Stations
Distance from site
Direction
Base Line Concentration
(µg/m(3)) (98 percentile)
Predicted SPM
Concentration (µg/m(3))
Total SPM Concentrations
implementation of the proposed project
µg/m(3)
1 (A1) Project site -- 0 34.96 0.6 35.56
2 (A2) Becharpura 1.7 Kms NNE 39.56 0.5 40.06
3 (A3) Kamana 2.3 Kms NW 44.35 0.3 44.65
4 (A4)Meghaliyasana 2.7 KMs SW 42.88 0.1 48.98
5 (A5) Basna 4.8 Kms ENE 30.72 0.05 30.77
After implementation of the proposed project, these concentrations are found to be well below the
permissible NAAQs norms for rural/residential zone and Industrial zone. Therefore, the proposed
activity will not have any adverse impact on the air environment.
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-4: Anticipated Environmental Impacts & Mitigation Measures
4.34
Environmental Impact Assessment Report
4.3.3 Existing Traffic & Vehicular Pollution
Traffic survey has been carried out on road at project site from. Based on the traffic survey hourly
vehicular traffic has been calculated. Considering worst case scenario, average number of vehicles
observed during 4 hours has been taken as hourly counts. Passenger Car Unit (PCU) has been
calculated by applying PCU factor. Proposed load of trucks due to the movement of raw materials,
fuel and products has been calculated. A design capacity of road has been taken from the Indian
Road Code. Assessment of proposed traffic load is given below in Table 4.7.
From the above table, it can be concluded that even for considering the worst case; there will be
minor increase in vehicular load due to the proposed project. However, the total traffic load even
after the proposed project will be very low compare to the design capacity of roads. Adequate
parking arrangements will be provided within the industrial premises.
As no major increase in traffic due to the proposed project, there will be less chance in increase in
vehicular pollution. However, unit will take adequate measures by instructing transporter for using
only PUC certified trucks/vehicles and carrying out regular service and maintenance of them.
Table 4.7 Assessment of Proposed Traffic Load
Type of Vehicles
Route-2 (SH 56 (2 Lane divided (two way) PCU Factor as per Indian Road Code
Average Vehicles Per Hour
Equivalent PCU (Passenger Car Unit)
per hour
Large Trailer 12 51.8 4.5
Heavy (Bus, Truck, etc) 82 246.0 (3)
Medium (Tractors, light commercial vehicles etc)
1(3)1 195.8 1.5
Light (Car, Jeep, Pickup Van etc.)
20(3) 202.5 1
(3) Wheeler (Rickshaw) 5(3) 52.5 1
2 Wheeler (Scooter, motorcycle, cycle etc)
151 75.5 0.5
Total PCU/hr 824
Width of Road (m) 16
Design PCU per hour 2900
Existing PCU per hour 824
Proposed Load (Trucks/day)
26
Proposed PCU per day 78
As a Worst Scenario taken Proposed PCU per day as
PCU per hour 78
Total PCU per hour after the Proposed Project
902
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-4: Anticipated Environmental Impacts & Mitigation Measures
4.35
Environmental Impact Assessment Report
4.3.4 Socio – Economic Environment
The industry will provide direct and indirect Employment for many of the local population. It will
create employment (20) and helps to improve the social status of the local community.
No Rehabilitation or land acquisition is needed for this industry. This project is not expected to
generate any significant public controversy. Workers including casual workers such as truck drivers
will be provided with basic amenities like safe water supply, low cost sanitation facilities, first aid,
required personal protective equipment, etc. Workers will also be provided with sufficient
infrastructural facilities including drinking water, toilets, sanitation facilities, power, easily accessible
approach roads, communication, etc
Moreover unit would be carrying out CSR activities in nearby villages in the field of public health and
green belt development; which would contribute to improvements the public health in the region to
some extent. Other impacts of the proposed project are:
Any industrial growth will improve economic status of the people either directly or
indirectly.
Creation of employment generation is an another positive impact anticipated from this plant
The development of infrastructure (roads, lighting etc) may not only helpful for
transportation but also to improve aesthetic value of the site.
The proposed green belt plan also generates some employment (labor for plantation
development) and provide hygienic environment.
Non- workers comprises of 61% of the total population in the study area. This intense
unemployment fate can be for extent can be reduced.
Labour quarters will be provided for workers in operation phase of plant.
A slight increase in traffic during construction would result as workers arrive and depart the site and
as materials and equipment are delivered. This temporary traffic increase would represent only
small fluctuations within the normal range.
The Industry will also provide 2.5 % of the project cost, i.e, Rs. 22.5 Lacs, towards the Enterprise
Social Commitment. Socio-economic development activities will be provided after public Hearing.
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-5: Environmental Management Plan
5.1
Environmental Impact Assessment Report
CHAPTER - 5
ANALYSIS OF ALTERNATIVES (TECHNOLOGY & SITE)
As stated in EIA notification dated 14th September, 2006 during scoping stage if analysis of
alternative site is needed than it should be done while selecting site for proposed project. As
it is not suggested during scoping stage Analysis of Alternative has not carried out
Proposed project having total production capacity of 48.29 MT/Month for manufacturing
pharmaceutical ingredients. In case of selecting technology, project proponent will adopt
best available technology for the setting – up proposed manufacturing facilities.
M/s Jayveer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-6: Environmental Monitoring Program
6.1
Environmental Impact Assessment Report
CHAPTER - 6
ENVIRONMENTAL MONITORING PROGRAM
6.1 INTRODUCTION
Environmental monitoring describes the processes and activities that need to take place to
characterise and monitor the quality of the environment. Environmental monitoring is used
in the preparation of environmental impact assessments, as well as in many circumstances
in which human activities carry a risk of harmful effects on environment. All monitoring
strategies and programs have reasons and justifications which are often designed to
establish the current status of an environment or to establish trends in environmental
parameters. In all cases the results of monitoring will be reviewed and analysed statistically.
Environmental monitoring program is designed to understand how the environment
changes over time. Therefore, regular monitoring program of the environmental parameters
is essential to take into account the changes in the environment. The objectives of
environmental monitoring program are;
To verify the results of the impact assessment study in particular with regard to new
development;
1. To follow the trend of parameters which have been identified as critical;
2. To check or assess the efficiency of the pollution control measures;
3. To ensure that new parameters, other than those identified in the impact assessment
study, do not become critical through the commissioning of new installations;
4. To check assumption made with regard to the development and to detect deviations in
order to initiate necessary measures; and
5. To establish a database for future Impact Assessment Studies for new projects.
6.2 ENVIRONMENTAL MONITORING PROGRAM
The attributes, which merit regular monitoring, are air quality both at source and ambient
atmosphere, water and wastewater quality, noise levels, ecological preservation, greenbelt
development, socio-economic aspects, etc. Regular monitoring will be continued with
additional frequency and parameters as per the need after establishment of proposed
project. Environmental monitoring program is given in following Table 6.1.
M/s Jayveer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-6: Environmental Monitoring Program
6.2
Environmental Impact Assessment Report
Table 6.1: Environmental Monitoring Program
Sr. No.
Particulars & Location Monitoring Frequency
Parameters Measurement methodologies Budget &
Procurement Reporting schedules
Emergency procedures
1
Air Pollution In case of emergency, protocol to be followed shall be established and all operating staff shall be trained, accordingly. Inter-locking systems and alarm systems shall be provided at all reasonably possible areas.
Abnormal operations and emergency situations should immediately be brought into the notice of the local regulatory Board / Committee.
A
Stacks Monitoring (All Stacks)
Weekly SO2, IS 11255 (Part 2)1985 (RA 2009) 1 Lakh-2 lakh Weekly to Top Management/
Factory Manager
NO2, IS 11255 (Part 7)2012 (RA 2012)
PM IS 11255 (Part1)1985 (RA 2009)
B
Ambient Air Quality Monitoring (2 Locations within premises)
Twice in a year
PM10, IS 5182 (Part 23) (RA 2006)
Reformed 2012 App. 2 lakh Twice in Year
to Top Management/
Factory Manager
PM2.5, STP No. TRA/STP/AA/02 Based on manual instrument manufactures.
SO2, IS 5182 (Part 2): 2001 (RA 2002)
NOx, IS 5182 (Part 6): 2006 (RA 2002)
VOC IS 5182 (Part 11): 2006
Carbon Monoxide
NDIR spectroscopy
C
Work area monitoring (2 Locations in process plant)
Monthly Volatile Organic
Compounds
IS – 51824
EN -12341
App. 1 lakh Monthly
Top Management/
Factory Manager
2
Water and Wastewater Quality
i Borewell water (Intake source)
Monthly As per IS:
10500
IS 3025 (Part 9): 1984 (RA 2012)
IS 3025 (Part 22): 1986 (RA 2009)
IS 3025 (Part 23): 1986 (RA 2006)
App.
Rs. 20,000/- if out sourced
Monthly
Top Management/
M/s Jayveer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-6: Environmental Monitoring Program
6.3
Environmental Impact Assessment Report
Sr. No.
Particulars & Location Monitoring Frequency
Parameters Measurement methodologies Budget &
Procurement Reporting schedules
Emergency procedures
IS 3025 (Part 15): 1984 (RA 2009) Factory Manager
Effluents
i
Industrial effluent (Untreated & Treated)
High COD & High TDS
Daily pH, COD, BOD,
SS,TDS IS 3025 (Part 9) 1984 (RA 2012)
IS 3025 (Part 22): 1986 (RA 2009)
IS 3025 (Part 23): 1986 (RA 2006)
In- house lab Top Management/
Factory Manager
Monthly General
parameters
App.
Rs. 40,000/- if out sourced
Top Management/
Factory Manager
3
Ambient Noise Levels
i All Prominent places within premises
Twice in a year --
IS 9989: 1991
CPCB guideline
App.
Rs. 10,000/-
Once in Year
to Top Management/
Factory Manager
-
4 Soil (1 within the premises and 1 from vicinity)
Once in a year General
parameters
IS 2720 and Paramerters specified in Book of Department of
Agricuture and cooperation, Ministry of Agriculture
App.
Rs. 20,000/-
Once in Year
to Top Management/
Factory Manager
-
5 ETP sludge Once in a year General
parameters
CPCB guideline App.
Rs. 20,000/-
Once in Year
to Top Management/
Factory
-
M/s Jayveer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-6: Environmental Monitoring Program
6.4
Environmental Impact Assessment Report
Sr. No.
Particulars & Location Monitoring Frequency
Parameters Measurement methodologies Budget &
Procurement Reporting schedules
Emergency procedures
Manager
6 Safety Audit Once in 2 years All safety aspects
Private consultants organization App.
Rs. 200,000/-
Once in Year
to Top Management/
Factory Manager
Availability of First and Antidotes at
appropriate location
7 Occupation health (medical checkups)
Pre, post and regular
Vision, Audiometry, Spirometry, Urine, RBS,
Liver function tests,
Skiagram, (LFT),
Complete blood count, Anemia, etc.
Factory Medical Officer App.
Rs. 20,000/-
(Depends on Numeber of
workers)
8 Greenbelt development Periodic Survival rate and growth
To be developed by Project proponent
- - -
M/s Jayveer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-6: Environmental Monitoring Program
6.5
Environmental Impact Assessment Report
6.3 INFRASTRUCTURAL REQUIREMENT
Project proponent will develop in – house laboratory in which analysis of effluent for basic
parameters like pH, BOD, COD, SS, TDS will be carried out regularly. In addition to this,
regular monitoring will be carried out through NABL approved laboratory.
For the medical facilities, first aid boxes will be provided at prominent places in the premises
and also one MBBS doctor will be appointed for monthly visit in the plant. Moreover, unit
has already tie-up with nearby hospital for medical assistance in case of any emergency.
6.4 DOCUMENTATION AND REPORTING
All the data and reports of monitoring of all parameters as stated in monitoring program will
be properly maintain and timely reviewed by management for taking corrective or
preventive actions. Monitoring reports will be regularly submitted to the concerned
authorities as per their requirements.
6.5 CORPORATE ENVIRONMENT POLICY
Project proponent believe in sustainable development and therefore will provide adequate
environmental control and management system after proposed project and will regularly
and efficiently operate the same.
Project proponent will prepared environment policy duly approved by directors prescribing
standard operating procedures to bring into focus any deviation/violation of environmental
or pollution control norms/conditions. This policy is displayed at various prominent places in
the premises and all the employees are educated about the same.
For performing all the environmental management activities and operating environmental
management systems efficiently, unit has established Environmental Management Cell
governed by director and same will be upgraded for proposed expansion as described
below.
6.6 ENVIRONMENTAL MANAGEMENT CELL (EMC)
For effective implementation of the monitoring program, it is necessary to have a
permanent organizational set-up. Thus, unit has already set-up permanent environmental
management cell (EMC) for the effective implementation and monitoring of environmental
management system as given below.
M/s Jayveer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-6: Environmental Monitoring Program
6.6
Environmental Impact Assessment Report
EMC is monitoring all project activities to ensure the appropriate implementation of all
environmental mitigation activities and to identify areas where environmental management
plan compliance is not satisfied. Responsibilities are assigned to officer from various
disciplines to perform and co-ordinate the activities concerned with management and
implementation of environmental control measures. Director of the company is responsible
for overall environmental management. Environment Manager is responsible to inform all
the matter regarding environmental management including reporting of non compliances /
violations of environmental norms.
Figure 6.1 Environmental Management Cell:
Director
Plant In-Charge/ Factory Manager
ETP In-Charge
Chemist
Helper
Environment Manager/ Safety Officer
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates (Ahmedabad)
NABET Accredited
Chapter-7: Additional Studies
7.1
Environmental Impact Assessment Report
CHAPTER – 7
ADDITIONAL STUDIES
A. PUBLIC CONSULTATION
All the aspects of the TORs are incorporated in the draft EIA/EMP report, the same
may be submitted to the Gujarat Pollution Control Board (GPCB) for conducting public
hearing/public consultation as per EIA Notification, 2006.
Minutes of Public Consultation / Public Hearing will be included in final EIA report with
suggestions/recommendations, if any after public consultation.
B. RISK ASSESSMENT STUDY
The said study report is presented in next page. 7.2 to 7.75
C. SOCIAL IMPACT ASSESSMENT, R & R ACTION PLAN
The socio-economic study of the study area is carried out and details are presented in
the Chapter-3/Section- 3.9. It may be noted that the proposed project is to be
established on Non Agricultural land. The project site is intended for the industrial
purpose and thus no displacement of villagers/people will take place. Therefore, the
R&R (Rehabilitation & Resettlement)policy/plan is not undertaken. However, the
direct financial and social benefits with special emphasis on the benefit to the local
people will be preferred and the proposed budgets for corporate social responsibility
(CSR) activities are summarized in Chapter- 8 /Section- 8.5.
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates (Ahmedabad)
NABET Accredited
Chapter-7: Additional Studies
7.2
Environmental Impact Assessment Report
7.1 RISK ASSESSMENT & EXECUTIVE SUMMARY OF PROJECT
M/s Jayveer Pharma Chem is proposing to set – up manufacturing facility for Active
Pharmaceutical Ingredients (API) at Survey no.: 1184 and 1187, Village: Basana,
Taluka: Visnagar, District: Mehsana, Gujarat- 384001. The total production capacity of
proposed unit is 48.29 MT/Month.
Site visit was carried out by concerned expert during formation Risk Assessment
report. Detailed discussion regarding plant layout in relation of storage of chemicals
has been carried out with project proponent.
Detailed discussions, Solvent storage facilities (For Methanol and Others) as well as
process safety, Finished product storage go down and tank farm area, Emergency
management plan, Emergency handling facilities, Emergency organization and action
plan with project proponent has been carried out.
In this proposed plant Methanol, Toluene, Hydrochloric Acid, Acetone, O- Xylene will
be used as raw materials and received through road tanker and stored in designated
tank farm area. Flammable solvents receive through road tanker and stored storage
tank farm area as per petroleum Act and Rules. Separate storage area will be provided
for storing Hydrochloric Acid, Hydrogen Cylinder.
Based on storage capacities of chemicals and chemical properties of stored chemicals,
some hazards have been identified and their consequences are modeled using ALOHA.
The threat zone is overlayed on the google image of project for identification of
impact.
The Risk assessment shows that major possible hazards with the plant are (a) Solvent
storage area – tank farm area (b) during the high temperature reaction in reactors
(C)Distillation process of solvent recovery.
Consequences analysis of storage tanks of solvent release scenarios from small hole
spillages and leakages is relatively small and damage distance will be within premises
for most likely occurring event. The impact of such accidental release and leakages can
be reduced by providing all necessary safety measures and risk control measures listed
in this report.
The possibility of major toxic release of chloroform considered very faraway.
Considering the potential for major hazards suggestions are made in the subsequent
chapters for further improvement in the areas of safety, environmental impact,
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates (Ahmedabad)
NABET Accredited
Chapter-7: Additional Studies
7.3
Environmental Impact Assessment Report
Emergency facilities and emergency preparedness plan.
As this is greenfield project at the stage of pre – design and details availability the
conclusion based on Risk Assessment study and information regarding the layout plan
and safety systems.
7.2 Risk assessment study
7.2.1 Objective and Scope
Risk Assessment (QRA) techniques used to determine risk posed to people who work
inside or live near hazardous facilities, and to aid in preparing effective emergency
response plans by delineating a Disaster Management Plan (DMP) to handle onsite
and offsite emergencies.
Scope of the Study:
Hazard Identification - Identifying sources of accidents involving release of
hazardous material in the atmosphere and the various ways (that is scenarios)
they could occur.
Consequence Assessment - Estimating the probable zone of impact of accidents as
well as the scale and/or probability of damages with respect to human beings and
plant equipment and other structures.
Accident Frequency Assessment - Computation of the average likelihood of
accidents.
Risk Estimation - Combining accident consequence and frequency to obtain risk
distribution within and beyond a process plant
7.2.2 Risk Analysis Methodology:
The risk assessment of proposed project is required as part of statutory requirement,
emergency planning. The steps are described as follow:
Hazard Identification
Information on Location, Layout, Process Parameters
Select Most Credible Scenario which can culminate into an accident out of several
major and minor.
Select Worst Case Scenario which has the highest potential to cause an accident
of maximum damage
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates (Ahmedabad)
NABET Accredited
Chapter-7: Additional Studies
7.4
Environmental Impact Assessment Report
Estimate Consequences: in the plant in the form of fire, explosion and toxic
effects
Estimate Frequency of Occurrence
Estimate effect of damage
7.3 Hazard Identification and Risk Analysis
Major components of a system/plant/process are examined to assess their potential
for initiating or propagating an unplanned event/sequence of events, which can be
termed as an accident. While identifying hazards only those areas of plants having
potential risk are used further for risk analysis.
7.3.1 Location, Layout, Process Parameters
The proposed project will be set – up at Survey No. 1187 and 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana, Gujarat. GPS coordinates of the site is situated at
Latitude: 23°37'0.67"N and Longitude: 72°28'37.29"E. Nearest major city is Mehsana
which is about 8 km far from the project site in West direction. State Highway No. 56
is about 3.3 km from the project site in East direction. The google image showing
proposed unit is given in Chapter: 2 Figure No.: 2.2.The project site is intended for
the industrial purpose and thus no displacement of population will take place. There
is no protected area notified under the Wild Life (Protection) Act (1972) & Eco-
sensitive area notified under the Environment (Protection) Act- 1986 exists within 10
km radius areas from the project site.
Detailed plant layout is given in Chapter: 2 Figure No.: 2.2, which provides details of
all internal area (i.e. process area, storage area of solvent and other raw materials ,
tank farm area, drum storage area, utility area, D. G. set etc.. )
Process Parameters: During the manufacturing process of proposed product
temperature will be maintained to tune of 65 to 1050C. No pressurized reaction
involved in any product. In solvent distillation / recovery system temperature of
system will be to tune of 110- 1250C.
7.3.2 Hazard Identification Methods
The proposed project is green filed project in pre- design stage during preparation of
Risk Assessment. Hazard identification method used or the proposed plant is given
below.
o Identification of major hazardous units based on Manufacture, Storage and
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates (Ahmedabad)
NABET Accredited
Chapter-7: Additional Studies
7.5
Environmental Impact Assessment Report
Import of Hazardous Chemicals Rules, 1989 of Government of India (as amended
in 2000); and
o Preliminary Process Hazard Analysis: Hazard associated with raw material
storage, intermediates, by- products, final products, plant machineries and
equipment.
7.3.3 Identification of Hazardous Chemicals used within Premises
List of chemicals to be stored and utilized within the premises falls under
Manufacture, Storage and Import of Hazardous Chemicals Rules, 1989 (Amended in
2000). List of Hazardous Chemicals is given below: Chemical and physical properties
of raw materials are given in Table 7.1.
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates (Ahmedabad)
NABET Accredited
Chapter-7: Additional Studies
7.6
Environmental Impact Assessment Report
Table 7.1 Hazardous Characteristics and Toxicity Of Raw Materials And Products
Sr. No.
Name of the Raw Material
Main Properties Class (As per
petroleum classification)
Antidote
B.P.0C
Boiling
Point
F.P.0C
Flash Point
LEL UEL %
TLV ppm
LD50: mg/Kg
LC50: mg/l
Specific Gravity Water
-1
Vapor Density
Odour threshold
ppm or mg/m
3
1. Methyl Acrylate 80.5 0C
-3.89 0C
(CC) -3
0C
(OC)
2.8 % 25 %
2 (ppm) from ACGIH (TLV)
277 mg/kg
0.96 2.97 20 ppm A ---
2. Mono Methyl amine (30 % solution in methanol)
-6.3 0C Not
available 4.9 % 20.7 %
STEL: 15 (ppm) from ACGIH (TLV
150 mg/L 0.85 0.62 Not available
None ---
3. Sodium Methoxide Powder
Not availa
ble
33 0C
CC 7.3 % 36%
TWA: 3 (mg/m
3)
from ACGIH (TLV)
2037 mg/kg 1.1 1.1 Not available
B ---
4. Chloroform 61 0C Not
Applicable
Not availa
ble
TWA: 10 (ppm) from ACGIH (TLV)
36mg/kg 47702 mg/m
1.48 4.36 85 ppm None N-acetyl-L-cysteine
5 N Methyl 4 piperidone
55-60 0C
58 0C
(CC) --- --- --- --- --- --- B ---
6 Nickle catalyst --- --- --- TWA: 1 (mg/m3)
--- 1.94 --- --- None ---
M/s JayVeer Pharma Chem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
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Sr. No.
Name of the Raw Material
Main Properties Class (As per
petroleum classification)
Antidote
B.P.0C
Boiling
Point
F.P.0C
Flash Point
LEL UEL %
TLV ppm
LD50: mg/Kg
LC50: mg/l
Specific Gravity Water
-1
Vapor Density
Odour threshold
ppm or mg/m
3
from ACGIH (TLV)
7 Hydrogen gas -4230C 565.5
0C 4 %
74% --- --
500 ppm 0.069 21.1
0C --- None ---
8 Thonyl Chloride 76 0C Not
Applicable
1 ppm -- 1.683 4.1 Not Available
None natural oil and one table spoon
sodium or magnesium sulphate with one glass of water. one cup strong tea or
coffee.
9 Sodium hydroxide
1388 0C
323 0C
--- STEL: 2 (mg/m3) from ACGIH (TLV)
---- 2.13 Not available
Not Available
None Sodium Hydro-Carbonate (4% Conc.), Milk, Lime Juice, Milk
of Magnesia
11 Ethyl Chloroformate
94 0C 160C --- --- 270mg/kg 72.5 ppm
1.1 3.7 Not Available
A ---
12 Ammonical methanol (15 to 17 % solution)
--- 14 0C -- --- 5628mg/Kg 83.2mg/l
--- --- --- A ---
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Sr. No.
Name of the Raw Material
Main Properties Class (As per
petroleum classification)
Antidote
B.P.0C
Boiling
Point
F.P.0C
Flash Point
LEL UEL %
TLV ppm
LD50: mg/Kg
LC50: mg/l
Specific Gravity Water
-1
Vapor Density
Odour threshold
ppm or mg/m
3
13 Ranny Nickel Not Availa
ble
Not Available
Not Available
TWA: 1 (mg/m3) from ACGIH (TLV)
Not Available
1.94 Not Available
Not Available
None Unithol (BAL, dimercaprol, 5% solution), Tetacin
calcium (10% solution),
Penicillamine Dextrose (10%) by
intravenous injection. Chillating agent for effect of mercury.
14 2,5, Dichloro nitro Benzene
267 °C 152°C 1.50% 9.20%
Not given 1210 mg/kg
Not Available
Not Available
Not Available
None ---
15 Urea Not availa
ble
Not available
Not available
10 mg/m3, 8-hour TWA from ACGIH
8471mg/Kg 1.323 2.07 Not available
None ---
16 Methanol 64.5°C 12°C (CC) 16°C (OC)
6% 36.5%
STEL: 250 (ppm) from ACGIH (TLV)
5628 mg/kg 64000ppm
0.7915 1.11 100 ppm A 10 mg diazepam through injection
17 Ammonium Chloride
520 0C
Not applicable
Not applicable
STEL: 20 (mg/m3) from ACGIH (TLV)
1650 mg/Kg 1.53 Not available
Not available
None
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Sr. No.
Name of the Raw Material
Main Properties Class (As per
petroleum classification)
Antidote
B.P.0C
Boiling
Point
F.P.0C
Flash Point
LEL UEL %
TLV ppm
LD50: mg/Kg
LC50: mg/l
Specific Gravity Water
-1
Vapor Density
Odour threshold
ppm or mg/m
3
18 HCl 108.50 0C
Not applicable
-- CEIL: 5 (ppm) from OSHA (PEL)
900mg/Kg 1108 ppm
1.16 1.267 0.25 to 10 ppm
None Sodium Hydro-Carbonate (4% Conc.), Milk, Lime Juice, Milk
of Megnesia
19 Ammonia liq. 25% solution
Not availa
ble
Not applicable
25 16
TWA: 25 (ppm) from ACGIH (TLV)
350 mg/kg 2000 ppm
0.898 Not available
5 - 50 ppm as
ammonia
None Skin:wash with lactic Acid, Apply Soframycin
Eye: Benoxynate (Novacin?0.4 % Conc.
Throat : Smelling Ethanol or Ether
20 Nitrogen gas Not Given
Not applicable
-- 2 ppm
Not Available
Not Available
Not available
Not available
None ---
21 Ortho PhenyleneDiamine (OPD)
256.0 -
258.0 °C
136 °C Not available
Not available 366mg/Kg > 91 mg/m3
1.03 3.7 Not available
None ---
22 O- Xylene 144.4°C
17°C (CC)
0.9 6.7
STEL: 651 (mg/m3) from ACGIH (TLV)
Not Available
0.88 3.7 0.05 ppm A Oxygen
23 Methyl Aceto 170°C 67°C 13 Not available 3.228 Not 4.0 Not C ---
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Sr. No.
Name of the Raw Material
Main Properties Class (As per
petroleum classification)
Antidote
B.P.0C
Boiling
Point
F.P.0C
Flash Point
LEL UEL %
TLV ppm
LD50: mg/Kg
LC50: mg/l
Specific Gravity Water
-1
Vapor Density
Odour threshold
ppm or mg/m
3
acetate 14.2 mg/kg 6.6mg/l
available available
24 N Hexane 68.7 -22.5 CC
1.2 7.5
STEL: 1000 (ppm) from ACGIH (TLV)
25000 mg/kg
48000 ppm
0.66 2.97 130 ppm A ---
25 1 bromo 3 chloro propane
145°C 45°C Not available
Not available
930mg/Kg
5668 mg/m3
1.592 Not available
Not available
B ---
26 Acetone 56.2°C 20°C CC
-9°C OC
2.6% 12.8%
STEL: 750 (ppm) from ACGIH (TLV)
5800 mg/kg 44000 mg/m3
0.79 2 62 ppm A ---
27 MethylIso Butyl Ketone
115.9°C
14°C CC
23°C OC
1.4 % 7.5%
STEL: 75 from ACGIH (TLV)
2080 mg/kg 8000 ppm
0.802 3.45 0.1 ppm A ---
28 2,5 Dichloro nitro benzene
267°C 152°C 1.50 9.20
-- 1210 mg/kg
Not available
Not available
Not available
None ---
29 2,5 dichloropara nitro aniline
Not Availab
le
Not Available
Not Available
Not Available 2400 mg/kg >21600
mg/m3/1H
Not Available
Not Available
Not Available
None
Note: * Hazardous chemicals as per MSIHC rule, 2000 Note: CC: Close Cup; OC: Open Cup; N.A.: Not Available.
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The Toxicity level of hazardous chemicals as per Manufacture, Storage and Import of Hazardous Chemical (Amendment) Rules, 2000 (MSIHC) is
shown as below:
Sr. No Toxicity Oral Toxicity LD50 (mg/Kg) Dermal Toxicity LD50 (mg/Kg) Inhalation Toxicity LD50 (mg/Kg)
1 Extremely Toxic <5 <40 <0.5
2 Highly Toxic >5- 50 >40-200 >0.5-2
3 Toxic >50-200 >200-1000 >2-10
7.3.4 Storage Details of Raw Material and Products:
Details of the raw materials and products with storage are given in Table 7.2A & 7.2B.
Table 7.2 A: Storage tank details for Raw Material storage
Sr. No.
Raw Materials Product
Qty Consumed per Month
(Kg)
Mode of storage
Capacity of storage
unit (MT)
No. of units
Total Storage
(MT)
Threshold Quantity
as per MSIHC rule (MT)
Inventory
1. Hydrogen
N – Methyl 4 Chloro Piperidine (NMCP)
125 Isolated
Storage area 9 m3 - 1.5
2 ton
4 D-7 [5 - Chloro 1 - (4 - Piperidyl)
2 –Benzimidazolonone] 1500
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Sr. No.
Raw Materials Product
Qty Consumed per Month
(Kg)
Mode of storage
Capacity of storage
unit (MT)
No. of units
Total Storage
(MT)
Threshold Quantity
as per MSIHC rule (MT)
Inventory
D-2 [1 – (3 – Chloropropyl) -1- Dihydro – 2 –1-1 – Benzimidazolone]
6000
2. Toluene
N – Methyl 4 Chloro Piperidine (NMCP)
3000 Tank
(SS 316) 12 1 12
10,000 >30
D-7 [5 - Chloro 1 - (4 - Piperidyl) 2 –Benzimidazolonone]
7000
3. Caustic Lye
N – Methyl 4 Chloro Piperidine (NMCP)
800
MS tank 12 1 12
-
15
D-7 [5 - Chloro 1 - (4 - Piperidyl) 2 Benzimidazolonone]
6600
D-2 [1 – (3 – Chloropropyl) -1- Dihydro – 2 –1-1 – Benzimidazolone
2550
4 Chloro 2 Amino Phenol (4 CAP)
12000
4.
Methanol
D-7 5-chloro-1-(4-piperidyl)- 2 – benzimidazolonone
2000 Tank
(SS 316) 12 1 12
7000 >30 Chlorzoxazone (5-chloro-3-h benzooxa-zolonone)
or 5-chloro-2-benzoxazolione 5000
5.
D-7 5-chloro-1-(4-piperidyl)- 2 – benzimidazolonone
2000 Tank
(HDPE) 12 2 24
20 day
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Sr. No.
Raw Materials Product
Qty Consumed per Month
(Kg)
Mode of storage
Capacity of storage
unit (MT)
No. of units
Total Storage
(MT)
Threshold Quantity
as per MSIHC rule (MT)
Inventory
HCl (28-30%)
D-2 1 – (3- chloropropyl)-1- dihydro-2-1-1- benzimida-zolone
6400 -
chlorzoxazone (5-chloro-3-h benzooxa-zolonone)
or 5-chloro-2-benzoxazolione 15000
4-cap (4-chloro 2 –amino phenol)
6000
6.
Acetone
D-2 1 – (3- chloropropyl)-1- dihydro-
2-1-1- benzimida-zolone
2500 Tank
(SS 316) 12 1 12
10000
>30
7.
O-Xylene
D-2 1 – (3- chloropropyl)-1- dihydro-
2-1-1- benzimida-zolone
4500 Tank
(SS 316) 12 1 12
10000
>30
8. Mixed solvent 2.5 Dichloro Paraphenylene
Diamine 5000
Tank (SS 316)
12 1 12 10000
>30
9
Chloroform
N-methyl – 4- piperidone 12000 Tank
(SS 316) 12 1 12
-
>30 N-methyl – 4- chloro – piperidine (nmcp)
2500
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Table 7.2 B: Storage Details of Raw Materials
Sr. No.
Raw Materials Product Qty Per
Month
Mode of storage Drums/ tanks/ bags &
Material of Construction
Capacity of
storage unit (Kg)
No. of Units
Total Storage
(Kg)
Inventory
1. Methyl Acryalate
N-methyl – 4- Piperidone
10750 Kg Drum 210 20 4200 15
2. Mono Methyl Amine
(30% Solution in Methanol) 6075 Kg Drum 210 15 3150 15
3. Sodium Methoxide Powder 3400 Kg Bag 50 34 1700 15
4. N-Methyl – 4 – Piperdone N-methyl – 4- chloro – Piperidine
(nmcp)
2000 Kg Drum 210 10 2100 30
5. Nickle Catalyst 80 Kg Bag 50 2 100 >30
6. Thionyl Chloride 3200 Kg Drum 210 10 2100 20
7. N-Methyl – 4- Piperidone
D-7
5-chloro-1-(4-piperidyl)- 2 –
benzimidazolonone
2250 Kg Drum 210 10 2100 30
8. Ethyl Chloro Formate 2700 Kg Drum 210 12 2520 30
9. Ammonical Methanol (15 To 17 % Solution)
2700 Kg Drum 210 13 2730 30
10. Ranny Nickle Catalyst 150 Kg Bag 50 3 150 30
11. 2,5,Dichloro Nitro Benzene 2700 Kg Drum 210 13 2730 30
12. Urea 1500 Kg Bag 50 15 750 15
13. Ammonium Chloride 2400 Kg Drum 210 10 2100 30
14. NH3 Liq. 25 % Soln 6000 Kg Drum 210 15 3150 15
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Sr. No.
Raw Materials Product Qty Per
Month
Mode of storage Drums/ tanks/ bags &
Material of Construction
Capacity of
storage unit (Kg)
No. of Units
Total Storage
(Kg)
Inventory
15. Carbon 300 Kg Bag 50 3 150 15
16. Ortho Phenylene Diamine
(OPD) D-2
1 – (3- chloropropyl)-1- dihydro-2-1-1-
Benzimida-zolone
2000 Kg Drum 210 10 2100 30
17. Methyl Aceto Acetate (MAA) 3000 Kg Drum 210 10 2100 15
18. 1-Bromo-3-Chloro Propane
(BCP) 2800 Kg Drum 210 10 2100 20
19. Tebac (Catalyst) 40 Kg Bag 50 2 100 30
20. D-2 Dompiridone 5- chloro -1-(1-l3-l2-oxo-
1-benximidazolinyl) Propyl) -4-piperidyl)-2-
benzimidaz
2640 Kg Bag 50 26 1300 15
21. D-9 3000 Kg Bag 50 20 1000 3
22. M.I.B.K. (Methyl Iso Butyl
Ketone) 1000 Kg Drum 210 5 1050 30
23. Ammonium Chloride 3500 Kg Drum 210 10 2100 20
24. 4-CAP Chlorzoxazone (5-chloro-3-h benzooxa-
zolonone) or 5-chloro-2-
benzoxazolione
10000 Kg Bag 100 25 2500 4
25. Urea 12792 Kg Bag 100 30 3000 5
26. Carbon 240 Kg Bag 50 5 250 30
27. 2,5 Dichloro Nitro Benzene
(2,5 DCNB) 4-cap
(4-chloro 2 –amino phenol)
19950 Kg Drum 210 25 5250 8
28. Platinum / Carbon Catalyst 165 Kg Bag 50 3 150 25
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Sr. No.
Raw Materials Product Qty Per
Month
Mode of storage Drums/ tanks/ bags &
Material of Construction
Capacity of
storage unit (Kg)
No. of Units
Total Storage
(Kg)
Inventory
29. 2.5 Dichloro
Para nitro aniline 2.5dichloro paraphenylene diamine
12000 Kg Bag 50 120 6000 15
30. Pd/Co catalyst 85 Kg Bag 25 4 100 >30
31. N- Haxane
D-2 1 – (3- chloropropyl)-1- dihydro-2-1-1-
Benzimida-zolone
445 Drums 210 5 1050 2
32. M.I.B.K
Dompiridone Chloro – 1 – (1 – (3 –
(2 – Oxo – 1 – Benzimidazolinyl)
Propyl) – 4 – Piperidyl) – 2-
Benzimidaz
1000 Drums 210 10 2100 5
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Table 7.2C: Storage Details Products
Sr. No.
Name of the product Physical
State
No. of container and size
No. MT
1. N - Methyl 4 Piperidone (NMP) Liquid 80 2
2. N – Methyl 4 Chloro Piperidine (NMCP) Solid 50 1.25
3. D-7 5-Chloro 1-(4- Piperidyl) 2-Benzimidazolonone Solid-Powder 200 5
4. D-2 1–(3-Chloropropyl)-1-Dihydro–2–1-1-Benzimidazolone Solid 100 2.5
5. Dompiridone Chloro–1–(1–(3–(2–Oxo–1– Benzimidazolinyl) Propyl)–4–Piperidyl)–2- Benzimidaz
Solid 50 1.25
6. Chlorzoxazone (5 – Chloro – 3 – H Benzooxa- zolonone) OR 5 – Chloro – 2 – Benzoxazolione Solid 50 1.25
7. 4 Chloro 2 Amino Phenol (4 CAP) Solid 100 0.5
8. 2.5 Dichloro Peraphenylene Diamine Solid 100 2.5
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7.3.5 Identification of Hazard Associated with Storage of Raw Materials
Table 7.3: Identification Hazard Associated with Storage of Raw Materials and control measures
Sr. No.
Material stored
Hazard Rating Systems
Type of hazard / Risk
involved Causes Effect Control Measures proposed
(1)
Methanol (12 KL Tank farm area) and other
solvent tank
TLV – 200 PPM (8-hr TWA) STEL-250 PPM NFPA Ratings: Health: 1 Flammability: 3
Fire /Explosion
Glands/seal leaks in valves, pumps
Hose/pipe failure, leakage from flanged joints carrying Methanol
Loading and unloading process
Nearby ignition sources
Fire due to Bottom nozzle failure
Damage of storage tank Pump discharge nozzle failure
Unloading road tanker hose rupture
Highly Flammable
Toxic by inhalation
Toxic when contact with Skin
Toxic if swallowed
Danger of very serious irreversible effects.
Dyke wall shall be provided to all above ground storage tank.
Separate from strong oxidant. Fire hydrant system shall be installed. Safety shower and eye washer shall be
installed near storage area. Flame proof Electrical fittings shall be
provided at flammable storage area. Proper selection of MOC for chemicals
storage tank. Earthing/bonding shall be provided for
static charges. Flame arrestor shall be provided on
flammable material storage tank vent. Level gauge and level measurement
instrument shall be provided on material storage tank.
Stored away from the plant and safe distance shall be maintained.
Safety permit system shall be followed for loading, unloading of hazardous
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Material stored
Hazard Rating Systems
Type of hazard / Risk
involved Causes Effect Control Measures proposed
chemical. Fencing, caution note, hazardous
identification board should be provided.
Authorized person permitted in storage tank area and register will be maintained.
(2) Hydrochloric Acid (30%)
(12 KL)
TLV : 500 ppm Health: 2
Flammability: 1 Reactivity: 0
Corrosive and Toxic
DISCHARGE from 1) Piping not correctly secured which may fail under pressure 2) Joint failure. 3) Gasket failure. LEAKS & SPRAYS: flange failure
Highly corrosive to most metals with evolution of hydrogen gas, which is highly explosive when mixed with air
Non-flammable,
but reacts with
most metals
with evolution
of hydrogen
which may
cause fire nor
explosion with
1) Easy Access. 2) Bulk Tanks (clearly identified). 3) Spillage area. 4) Bund. 5) Shower and eye wash/bath 6) First aid equipment. 7) Water hose. 8) Respirators. Note: a) Equipment must be
correctly maintained. b) Personnel must be trained to operate the safety equipment. c) Safety equipment must be visible from all points.
VENT AND OVERFLOW ARRANGEMENT
Gaskets should comprise chemically resistant natural rubber or PTFE.
Centrifugal pumps of rubber lined cast iron or suitable plastic construction are recommended.
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Sr. No.
Material stored
Hazard Rating Systems
Type of hazard / Risk
involved Causes Effect Control Measures proposed
air
PTFE should be used for packed glands
Mechanical seals of corrosion resistant material may be used.
Plastic valves. Neutralise spill area with lime or soda
ash and flush area with water. Do not get water inside containers. In case of large spillages Keep upwind
and out of low areas. Contain spill with earth, sand, or
absorbent material, which does not react with spilled material.
Level indicator and pressure relief systems.
3 (Drums and Bags of other
Raw material
storage area )
- Fire & Explosion Leak. Release of toxic vapors. Reaction of incompatible chemicals. Collapse of containers
Storing incompatible substances together;
Incorrect labelling/delivery of raw materials, intermediates and products;
Introduction of
Domino effects (e.g. thermal radiation from fires);
Toxic substance dispersion
Loss of material Contamination
of land & water in case of major
At least one emergency entrance point Impervious floor Smoke alarms High quality electrical installation Eye wash bottles. Stocks of absorbent materials for
dealing with spills Stocks of sandbags to form temporary
containment barriers Non sparking tools in warehouses
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Material stored
Hazard Rating Systems
Type of hazard / Risk
involved Causes Effect Control Measures proposed
ignition sources into segregated areas containing flammable, combustible and explosive substances (e.g. smoking, mobile equipment and vehicles, power tools);
Poorly managed inventory control and identification systems for hazardous chemicals stored in drums;
Poor house keeping.
Insufficient recording of chemical inventories at each location on site
leakages
storing highly flammable liquids Adequate level of natural or artificial
lighting Constructed of essentially non-
combustible materials Bunding to a height of 1m Fitted with in rack foam/water
sprinkler system Fire resistant doors Site floodlighting Perimeter lighting A emergency generator Direction of leaks to common
sumps/manifolds; sufficient warning signs in place to
inform employees and visitors of the potentially, hazardous environments they are approaching (no smoking signs, flammable area, intrinsically safe zone.
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Material stored
Hazard Rating Systems
Type of hazard / Risk
involved Causes Effect Control Measures proposed
4 Chloroform Storage
Health:2 Flammability: 0 Reactivity:0
Toxic effect DISCHARGE from 1) Piping not correctly secured which may fail under pressure 2) Joint failure. 3) Gasket failure.
LEAKS & SPRAYS: flange failure
Toxic by
inhalation
Toxic when
contact with
Skin
Toxic if
swallowed
Toxic gas
dispersion
In presence of excess moisture, strong alkalis, sunlight and high temperatures Chloroform decomposes to highly toxic phosgene and hydrochloric acid.
Chloroform are not compatible with
mild steel storage and handling
equipment. The use of stainless steel—
lined mild steel, nickel clad steel, or
stainless steel of the 300 series.
Precautionary measures should be
taken to ensure that moisture does not
contaminate the solvent. To minimize
evaporation losses, a completely
sealed storage tank is recommended.
Positive displacement rotary pumps
are recommended for chloroform
service.
Submerged centrifugal pumps may be
used in storage tanks designed for
atmospheric service.
Piping may be of steel or black iron,
preferably with welded or flanged
joints.
Lubricant for threaded joints must be
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Material stored
Hazard Rating Systems
Type of hazard / Risk
involved Causes Effect Control Measures proposed
of a type resistant to chloroform, such
as white lead, graphite and glycerine
pastes or fluorocarbon tape.
Dyke provision to storage area of tank
Safety boards should be displayed on
the tank
Good ventilation must be provided.
A. Identification of Process hazards:
Name of
hazardous
process and
operation
Material in the
process /
operation
Type of hazard possible
toxic gas release / fire /
explosion / run away
reaction / rupture, etc.
Causes
Control Measures to be provided
Reactor
Vessel
Methanol
And other
solvents
Acetone
Acetonitrile
Mechanical hazards e.g.
pressure release, leaks,
burns, noise, .equipment
or utility failure.
Reaction hazards due to
failure to control
Release of Heat and
Flammable gases
Fire, Toxic gas release and
Explosion
Failure of agitator, heating
and cooling system in the
Raw Materials quantity must be controlled either
volumetrically or gravimetrically.
Process control devices must be installed
includes the use of sensors, alarms, trips and
other control systems that either take automatic
action or allow for manual intervention to
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Name of
hazardous
process and
operation
Material in the
process /
operation
Type of hazard possible
toxic gas release / fire /
explosion / run away
reaction / rupture, etc.
Causes
Control Measures to be provided
exotherms, incompatible
materials, side reactions.
Environmental hazards
such as air pollution,
odour problems, spills
etc.
Toxicity and health
effects Flammability
hazards due to explosive
mixture, static charge,
autoignition etc.
reactor
Failures of external boiler,
condenser and piping system
prevent the conditions for uncontrolled reaction
occurring.
High Temperature indicator valve and alarm
system must be provided
Auto cut off system must be provided after
reaching of predetermined maximum safe
temperature.
Pressure gauge is must provided.
Safety Control valve is must be provided.
The Vessel Emergency Relief vent should
discharge to a suitably designed catch pot or
should be so positioned that people working in
the area and members of the public will not be in
danger if the contents of the vessel are
discharged.
Use skilled worker
Proper selection of MOC
Mechanical seal in all pumps and reactors
Transportation of finished product from vessel to
storage tank through close pipe.
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Name of
hazardous
process and
operation
Material in the
process /
operation
Type of hazard possible
toxic gas release / fire /
explosion / run away
reaction / rupture, etc.
Causes
Control Measures to be provided
Solvent
recovery
System
Methanol, Mix -
Xylene and
Other solvents
Explosion/fire release of
toxic material
Failure of the cooling system
resulting in the reduction of
condenser capacity which
might cause the emission of
volatile organic compounds
to the atmosphere.
In the presence of an ignition
source, a fire with serious
consequence.
Level control failure
Loss of heat transfer due to
fouling, accumulation of
noncondensables, or loss of
cooling medium
Blockage of packing/trays
leading to excessive pressure
drop in column
Level control failure.
Failure of safety system
An alarm and safety valve are required to
indicate any choking and release of any pressure.
In case of vacuum distillation vacuum failure
alarm, inert gas purging
safety valve or explosion vent should be provided
to take care of any accidental pressure
All electric fitting should be flameproof including
lighting
Flame arrester, smoke detector should be
provided spark/flame detectors with alarm
Flammable substances should be processed at
low temperature (below flash point) and
pressure. Dip feed pipe, slow and controlled
addition (e.g. niddle valve), inert blanketing,
vacuum, spark/flame avoidance, , no-smoking
habit, good ventilation and training to workers
are necessary.
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Name of
hazardous
process and
operation
Material in the
process /
operation
Type of hazard possible
toxic gas release / fire /
explosion / run away
reaction / rupture, etc.
Causes
Control Measures to be provided
Boiler Heat burns
Thermal radiation
Explosion
Heat burns
Leaking safety and or safety
relief valves
Malfunctioning of Water
level indicator
Steam leaks (steam systems)
High stack temperatures
(excess of 350ºF)
Condensate dripping down
stack or out the front of the
boiler
Constantly resetting of
controllers and safety devices
Annual inspections
Safety interlocks to be provided
Installation of pressure reducing valves is must.
Safety and pressure gauge valves fitted
Properly supported and protected against
corrosion
Water level indicators installation is must.
Testing of Jackets and joints of tubes regularly
All necessary measures should be taken to control
corrosion
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B. General hazards and controls
Type of
Emergency
Identification
of Area Possible Causes Possible Results
Material
handling In Plant
Flammable, eye irritating &
accidently leakages Fire and health Hazards
7.3.6 Credible Accident Scenarios and Worst Case Scenarios
Maximum Credible Accident (MCA) scenario indicates most believable, reasonable,
likely or possible accident scenario and damage distance based on it. MCA scenario
takes into account the effect of control measures also. It considers the malfunctioning
of the control system, opening of safety valve/failure of safety valve, leakages from
flange joint, pipe line etc. and failing of some safety devise.
Worst-case scenario (rarely possible) is defined as the release of the largest quantity
of a regulated substance from a single vessel or process line failure that results in the
greatest distance to an end point, eg catastrophic failure. It considers the failure of all
control systems and release of the whole mass resulting in maximum damage.
Based on the storage and properties of the chemicals at the proposed resin
manufacturing unit, the some typical scenarios relevant for MCA analysis is given in
the following Table.
Table -7.4: Scenarios Considered for MCA Analysis
Sr.
No.
Chemical Storage
Quantity
Pool Fire Flash fire Toxic
Dispersion
Worst case
scenario
BLEVE
1 Methanol 12 KL √ √ √ √
2 Toluene 12 KL √ √ √ √
3 O - Xylene 12 KL √ √ √ √
4 Acetone 12 KL √ √ √ √
5 Chloroform 12 KL - - √ √
The above table indicates that major material storage is flammable liquid. Fires could
occur due to presence of ignition source at or near the source of leak or could occur
due to flashback upon ignition of the traveling vapour cloud.
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Tank fires may occur due to the ollowin nition i rim eal lea leadin to rim eal
fire and escalating to full-fledged tank fire.
Li htin i a ma or ource o i nition o tan ire and O er low rom tan leadin to
spillage and its subsequent ignition, which flashes back to the tank leading to tank
fire. The chance of overflow should be less unless operator has grossly erred.
Spillage due to overflow may result in a dyke fire if ignition occurs after sufficiently
long period.
For radiation calculations, pool fire is important and the criteria of 4.5 kW/m2
elected to ud e accepta ility o the cenario . he a umption or calculation
are t i not continuou expo ure t i a umed that no ire detection and miti ation
measures are initiated
For Chlorine leakage from valve of tonner is considered for discharge of chemical in
atmosphere and threat zone predicted using ALOHA by considering heavy gas
modeling
7.4 Consequence Modeling
Hazardous incidents start with a discharge of a flammable or toxic material from its
normal containment. Discharge can take place from a crack or fracture of process
vessels or pipe work, an open valve or from an emergency vent. The release may be in
the form of gas, liquid, or two phase flashing of gas-liquid.
7.4.1 Damage Criteria:
The storage and unloading at the storage facility may lead to fire and explosion
hazards. The damage criteria due to an accidental release of any hydrocarbon arise
from fire and explosion.
A. Fire Damage
Table 7.6 tabulates the damage effect on equipment and people due to thermal
radiation intensity whereas; the effect of incident radiation intensity and exposure
time on lethality is given in Table7.6.
Table 7.5: Damage Due to Incident Radiation Intensities
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Sr. No.
Incident Radiation
(kW/m2)
Type of Damage Intensity
Damage to Equipment Damage to People
1 37.5 Damage to process equipment 100%lethality in1 min. 1% lethality in 10sec.
2
25.0
Minimum energy required to ignite wood at indefinitely long
exposurewithout aflame
50% Lethalityin1 min. Significant injury in 10 sec.
3
19.0
Maximum thermal radiation intensity allowed on thermally
unprotected adjoiningequipment
--
4
12.5
Minimum energy to ignite with a flame; melts plastic tubing
1% lethality in 1min.
5
4.5
--
Causes pain if duration is longer than
20sec,howeverblisteringis un-likely (First degree burns)
6
1.6
-- Causes no discomfort on long
exposures
Source: Techniques for Assessing Industrial Hazards by World Bank.
Table 7.6: Radiation Exposure and Lethality
Radiation
Intensity(kW/m2)
Exposure Time
(seconds)
Lethality (%)
Degree of Burns
1.6
--
0 No Discomfort even
after long exposure
4.5 20 0 1st 4.5 50 0 1st 8.0 20 0 1st 8.0 50 <1 3 rd 8.0 60 <1 3 rd
12.0 20 <1 2 nd 12.0 50 8 3 rd 12.5 -- 1 -- 25.0 -- 50 --
37.5 -- 100 --
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B. Damage due to explosion
Explosion is a sudden and violent release of energy accompanied by the generation of
pressure wave and a loud noise. The rate of energy release is very large and has
potential to cause injury to the people, damage the plant and nearby property etc.
BLEVE – fireball A Boiling Liquid Expanding Vapour Explosion (BLEVE) occurs when there
is a sudden loss of containment of a pressure vessel containing a superheated liquid or
liquefied gas. It is sudden release of large mass of pressurized superheated liquid to
atmosphere. The primary cause may be external flame impinging on the shell above
liquid level weakening the vessel and leading to shell rupture. Calculations are done for
diameter and duration offer ball and the incident thermal flux.
Pool fires and jet fires are common fire types resulting from fires over pools of liquid or
from pressurized releases or gas and/or liquid. They tend to be localised in effect and
are mainly of concern in establishing potential for domino effects and employee safety.
ALOHA Models are used to calculate various components - burning rate, pool size,
flame height, In jet fire modelling the steps followed for the thermal effects are
calculation of the estimated discharge rate, total heat released, radiant fraction/source
view fraction, transmissivity and thermal flux and thermal effects.
Vapour cloud explosion: When gaseous flammable material is released a vapour cloud
forms and if it is ignited before it is diluted below its lower explosive limit, a vapour
cloud explosion or a flash fire will occur. Insignificant level of confinement will result in
flash fire. The vapour cloud explosion will result in overpressures. Table 7.6 tabulates
the damage criteria as a result of peak over pressure of a pressure wave on structures
and people.
Table 7.7: Damage Due to Peak Over Pressure
Human Injury StructuralDamage
Peak Over Pressure (bar)
Typeof Damage PeakOver Pressure (bar)
Typeof Damage
5 -8 100%lethality 0.3 Heavy(90%damage) 3.5 -5 50% lethality 0.1 Repairable (10%damage) 2 -3 Threshold lethality 0.03 Damage of Glass
1.33 - 2 Severelung damage 0.01 Crack ofWindows
1 - 11/3 50%Eardrumrupture
- -
Source: Marshall, V.C. (1977)' Howlethal are explosives and toxic escapes'.
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C. Effect due to toxic gas release
Various approaches are used to determine the consequences of toxic gases:
• DLH
• ERPG
DLH (“ mmediate Dan er to Li e or Health”) i the maximum concentration rom which
escape is possible within 30 minutes without any escape-impairing symptoms or
irreversible health effects.
7.4.2 Details of Model Used for Consequence Analysis
ALOHA provide output as amount of chemical discharged from the source as well as
its concentration in air it takes into account different levels of concentrations for a
specified chemical.
Software used for calculation- ALOHA (AREAL LOCATIONS OF HAZARDOUS
ATMOSPHERES) ALOHA is a computer program designed especially for use by people
responding to chemical accidents, as well as for emergency planning and training.
ALOHA can predict the rates at which chemical vapors may escape into the
atmosphere from broken gas pipes, leaking tanks and evaporating puddles. It can
then predict how a hazardous gas cloud might disperse in the atmosphere after an
accidental chemical release.
ALOHA provides output as amount of chemical discharged from the source as well as
its concentration in air it takes in to account different levels of concentrations for a
specified chemical. Different concentration levels are given below:
ERPG 1: is the maximum airborne concentration below which it is believed that
nearly all individuals could be exposed for up to 1 hour without experiencing other
than mild transient adverse health effects or perceiving a clearly defined,
objectionable odor.
ERPG 2: is the maximum airborne concentration below which it is believed that
nearly all individuals could be exposed for up to 1 hour without experiencing or
developing irreversible or other serious health effects or symptoms which could
impair an individual's ability to take protective action.
ERPG 3: is the maximum airborne concentration below which it is believed that
nearly all individuals could be exposed for up to 1 hour without experiencing or
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developing life-threatening health effects.
IDLH: The Immediately Dangerous to Life or Health (IDLH) level. A chemical's IDLH is
an estimate of the maximum concentration in the air to which a healthy worker
could be exposed without suffering permanent or escape-impairing health effects.
Input data for aloha are as below:
Weather Data:
Average Wind Speed: 5 m/sec & 1.5 m/sec
Average Ambient Temperature: 350C, 220C
Average Humidity: 44%, 66%
Atmosphere Stability Class: D (windy day time), F (Extreme calm, night time)
Chemical Properties:
Chemical properties of each hazardous chemical stored within premises is given in Table
No.: 7.2
Storage Details:
Storage quantity and type of storage of chemicals is given in Table No.: 7.3
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Table 7.8: Consequence analysis and Damage Distance (Failure of raw material storage tanks)
Name of Chemical
Type of Impact Flammable (Distance in meter) Toxic Dispersion
Pool Fire (meter)
Fire Ball (BLEVE) Worst Case
Scenario (meter)
Flash fire (Flammable Area of
Vapor Cloud) (meter)
ERPG(3)/ IDLH ERPG(2) ERPG(1)
Radiation Intensity(kW/m2)
37.5 25 4.5 37.5 25 4.5 UEL LEL
Fatalities 100% 50% 100%
50% - -
Wind Speed
Stability Class
Methanol (12 KL x 1)
4 D 10 10 15 62 93 253 15 meters --- (43080
ppm = 60% LEL =
Flame Pockets)
19 meters --- (7180 ppm =
10% LEL)
15 meters --- (6000 ppm =
IDLH)
24 meters --- (2100 ppm
= AEGL-2 [60 min])
65 meters --- (530 ppm = AEGL-1 [60 min])
2 F 10 10 15 69 99 266 19 meters --- (43080
ppm = 60% LEL =
Flame pockets)
36 meters --- (7180 ppm =
10% LEL)
28 meters --- (6000 ppm =
IDLH)
47 meters --- (2100 ppm
= AEGL-2 [60 min])
106 meters --- (530 ppm =
AEGL-1 [60 min])
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Name of Chemical
Type of Impact Flammable (Distance in meter) Toxic Dispersion
Pool Fire (meter)
Fire Ball (BLEVE) Worst Case
Scenario (meter)
Flash fire (Flammable Area of
Vapor Cloud) (meter)
ERPG(3)/ IDLH ERPG(2) ERPG(1)
Radiation Intensity(kW/m2)
37.5 25 4.5 37.5 25 4.5 UEL LEL
Fatalities 100% 50% 100%
50% - -
Wind Speed
Stability Class
Chloroform (12 KL x 1)
4 D - - - - - - - - 107 meters --- (500 ppm =
IDLH)
494 meters --- (50 ppm = ERPG-2)
1.2 kms --- (10 ppm)
2 F - - - - - - - - 136 m (500 ppm =
IDLH)
590 m (50 ppm =
ERPG-2)
1.8 Km (10 ppm)
Worst case (Direct source Leakage of 1 Ton)
430 meters --- (500 ppm =
IDLH)
1.1Km (50 ppm =
ERPG-2)
2.1 Km (10 ppm)
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Name of Chemical
Type of Impact Flammable (Distance in meter) Toxic Dispersion
Pool Fire (meter)
Fire Ball (BLEVE) Worst Case
Scenario (meter)
Flash fire (Flammable Area of
Vapor Cloud) (meter)
ERPG(3)/ IDLH ERPG(2) ERPG(1)
Radiation Intensity(kW/m2)
37.5 25 4.5 37.5 25 4.5 UEL LEL
Fatalities 100% 50% 100%
50% - -
Wind Speed
Stability Class
Acetone (12 KLx1)
4 D 10 10 14 96 128 325 10 15600 ppm =
60% LEL = Flame
Pockets
19 (2600 ppm = 10% LEL)
<10m LC50:46400
ppm)
14 meters --- (IDLH:
2500 ppm)
102 meters --- (200 ppm =
AEGL-1)
2 F <10 <10 <13 101 134 339 14 meters --- (15600
ppm = 60% LEL =
Flame Pockets)
49 meters --- (2600 ppm =
10% LEL)
LOC was never exceeded --- (46400 ppm)
50 meters --- (2500 ppm)
257 meters --- (200 ppm =
AEGL-1 [60 min])
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Name of Chemical
Type of Impact Flammable (Distance in meter) Toxic Dispersion
Pool Fire (meter)
Fire Ball (BLEVE) Worst Case
Scenario (meter)
Flash fire (Flammable Area of
Vapor Cloud) (meter)
ERPG(3)/ IDLH ERPG(2) ERPG(1)
Radiation Intensity(kW/m2)
37.5 25 4.5 37.5 25 4.5 UEL LEL
Fatalities 100% 50% 100%
50% - -
Wind Speed
Stability Class
Toluene (12 KLx1)
4 D 10 10 16 119 153 375 11 meters --- (6600 ppm =
60% LEL = Flame
Pockets)
20 meters --- (1100 ppm =
10% LEL)
21 meters --- (500 ppm =
IDLH)
28 meters --- (300 ppm = ERPG-2)
132 meters --- (50 ppm = ERPG-1)
2 F 10 10 15 125 160 390 14
meters -
-- (6600
ppm =
60% LEL
= Flame
Pockets)
36 meters --- (1100 ppm =
10% LEL)
38 (500 ppm =
IDLH)
49 (300 ppm =
ERPG-2)
221 (50 ppm = ERPG-1)
Note
*** The concentration of HCl stored will be in range of 30 to 33%, as it will be solution and ALOHA cannot allow to model tank source for
consequence analysis of solutions, a puddle of HCl has been selected to model toxic dispersion scenario after HCl leakage from tank.
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Figure 7.1: Methanol BLEVE (Worst case scenario 12KL Tank)
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Figure 7.2 Methanol Toxic Dispersion (12 KL Tank)
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Figure 7.3 Chloroform Toxic dispersion (12 kl tank)
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Figure 7.4 Chloroform Toxic dispersion (12 KL tank)
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Figure 7.5 Chloroform tank leakages (12 KL)
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Figure 7.5 Acetone Worst Case Scenario (Total Rupture Tank :12 KL)
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Figure: 7.6 Acetone Pool Fire (Full rupture of Connecting pipe )
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Figure: 7.7 Acetone Toxic dispersion (Full rupture of Connecting pipe/valve)
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Figure: 7.8 Toluene BLEVE (12KL tank: Worst Case Scenario)
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Figure: 7.9 Toluene Pool fire (12KL tank: Maximum Credible Accident)
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Figure: 7.10 Toluene Toxic dispersion (12KL tank: Maximum Credible Accident) (2F)
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Figure: 7.11 Toluene Toxic dispersion (12KL tank: Maximum Credible Accident) (4D)
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Figure: 7.11 Toluene BLEVE (12KL tank: Worst Case scenario) (4D)
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Figure: 7.11 Toluene Pool fire (12KL tank: MCA) (4D)
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7.5 Failure Frequency
Fire under a tank may lead to the instantaneous release of the complete inventory of
the tank. Various causes of failure may lead to a fire under a tank:
Leakage of the connections under the tank followed by ignition. This event only
occurs for tanks loaded with flammable substances. The frequency is equal to 1
× 10-5 per year for atmospheric tanks. (Reference Purple book: Guidelines for
quantitative risk assessment)
The best available estimates of leak frequencies for atmospheric tanks are
summarised in Table 7.10.
Reference: Storage incident frequencies International Association of Oil and Gas
Producers (UK: HSE)
Table7.9: Atmospheric Storage Tank Leak/ tank fire Frequencies
Type of Tank Type of Release Leak Frequency(per tankyear )
Fixed/ floating roof Liquid spill outside tank 2.8 × 10-3
Tank rupture 3.0 × 10-6
Atmospheric storage tank Fire Frequency
Type of Fi r e Fi x e d Roof Tank (per tank year)
Internal explosion & full surface fire
9.0 × 10-5
Internal explosion without
fire
2.5 × 10-5
Vent fire 9.0 × 10-5
Small bund fire 9.0 × 10-5
Large bund fire
(full bund area)
6.0 × 10-5
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7.6 Estimation of Effect of Damage / Impact Identification
Consequence analysis of hazardous chemicals stored in large quantities as well as in tanks within premises shows that area prone to fire and explosion is mainly storage area of Methanol and chemicals storage/ware house where drums of hazardous raw material will be stored. The maximum intensity of heat radiation will be due to worst case scenario i.e total rupture of Methanol 10 MT tank. In case of flammable chemicals stored in drum, Acetone and Acetonitrile has been considered for prediction of damage distance by considering single drum worst case scenarios. From the toxic dispersion modeling of Chlorine toner and Ammonia cylinder maximum damage distance will be 154 meter and 322 meters from source of leakage. Threat zone distance given below are considered for Temperature 220C, Velocity: 1.5m/sec, Humidity 71%, Atmospheric stability Class: F considering winter night time. Percentage fatality from different incident outcome cases and level of concerns are given below:
Table7.10: Estimation of Effect of Damage / Impact Identification &
Chemical (12 KL)
Incident outcome
case
Level of concern
Threat zone
Distance meter
% fatality
(pfi)
Likely hood of
occurrence
Magnitude of Impact/Damage
Methanol
Pool fire 25 kW/m2
10 50% Possible Moderate
BLEVE 25 kW/m2
93 50% Unlikely high
Chloroform Toxic dispersion
IDLH 500 ppm
136 - ikely high
Acetone Pool fire 25 kW/m2
10 50% Unlikely high
BLEVE 25 kW/m2
134 50% Possible Moderate
Toluene Pool fire 25 kW/m2
10 50% Possible Moderate
BLEVE 25 kW/m2
160 50% Possible Moderate
Magnitude of impact will be higher in case of pool fire of Methanol tank storage
area
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Figure 7.1 to 7.10 shows the map of threat zone corresponding to different
chemicals and its incident outcome cases. All the threat zones in the proposed unit
are super imposed on google image. All scenarios of different release indicate that
individual risk is found to be a maximum at locations within premises as well as
outside of premises for toxic dispersion only. The reason for high individual risk at
this location is due to considering BLEVE scenario as worst case scenario resulting
from the catastrophic failure of storage tank of solvent. Abroadly acceptable level of
individual risk as per the ALARP (As low as reasonably practicable) concept of HSE,
UK is 10-6/year.
7.7 Summary
The present risk assessment study corresponding to quantity of solvents stored
within premises shows that proposed unit of M/s Jayveer Pharma Chem has higher
potential for damage to those inside compare to outside the industry because of
storage of Methanol, chloroform storage and loading and unloading from tanker
solvents.
There are many other hazardous raw material drums will be stored in drum storage
area, where possibility of fire and explosion will higher during loading, undloading
transportation and handling of drums.
It may be noted that in dispersion modeling, the wind direction and air temperature,
atmospheric stability are found to be the deciding factors for the threat zones.
Fire modeling shows that the hazardous distances for Methanol storage tank
extended up to 266 meters in worst case scenario, In case of pool fire it is within 15
meters which might prevented by effective fire-fighting arrangements to be
provided after commissioning of poject.
A maximum threat zone of chloroform considering 1 ton leakage is approximately
430 meter (500 IDLH).
7.8 Proposed Risk Reduction Measures /Safety Measures
A. Tank farm area:
Storage tank of Methanol, Sulphuric Acid, Hydrochloric Acid should be installed
away from the plant area.
Automatic sprinkler system for the flammable material tanks (over ground
tanks only) may be provided as knock on effect in case of fire is possible.
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Containment dykes with proper sloping and collection sumps should be
provided so that any spillages in the bulk storage and other handling areas shall
not stagnate and shall be quickly lead away to a safe distance from the source
of leakage. This reduces the risk of any major fire on the bulk storages and the
risk to the environment shall be minimized/ eliminated.
Inspection of the storage tanks as per prefixed inspection schedule for
thickness measurement, joint and weld efficiency etc.
Pro i ion o lameproo electrical ittin / equipment’ .
Proper maintenance of earth pits.
Strict compliance of security procedures like issue of identity badges for
outsiders, gate passes system for vehicles, checking of spark arrestors fitted to
the tank lorries etc.
Strict enforcement of no smoking.
Periodic training and refresher courses to train the staff in safety fire fighting.
Employee training and education is carried out.
Structural fireproofing in the process area could be considered as a safety
measure in the light of probable spill and fires in the area.
B. Safety measures of storage and handling Nickel catalyst;
Raney nickel catalyst (active) is highly pyrophoric when it gets dried up on
exposure to air/ atmosphere/ oxygen. It should therefore always be kept under
demineralised/ distilled water.
The containers of the catalyst should be stored in a cool and ventilated place
protected from direct exposure to sunlight.
Protective gloves, shoes and goggles must be used while transferring catalyst
from containers to the reaction vessel.
Hydrogen gas continuously evolves from the catalyst slurry. Smoking cigarette/
bidi and lighting matchstick/ lighter should be strictly prohibited while opening
the containers of thecatalyst.
The catalyst slurry should be manually stirred using a thick wooden stick to
restore it in suspension for easy and smooth transfer.
Care should be taken while transferring catalyst so as to avoid/ minimise
spillage of the catalyst. Skilled personnel should be employed for handling the
catalyst.
In the event of spillage of small quantity, the spilled material may be
deactivated by using a 0.5 % solution of potassium permanganate followed by
flushing the area with sufficient water.
In the event of spillage of significant quantity, the spilled catalyst slurry should
be collected back manually and put in a polythene bag thereafter be packed in
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a plastic or M. S. container and retrieval of the spilled catalyst should be
flushed with water. A 0.5 % solution of potassium
Permanganate [kmno4] may also be used as an additional measure.
In the event of contact with skin, the skin should be washed immediately with
running water.
Dry with a clean towel and apply a soothing ointment (viz soframycin).
Empty polythene bags and containers after transfer of catalyst should be
washed profusely with water before scrapping them.
Great care should be taken in deciding temperature and pressure condition
and selection of solvent for the hydrogenation reaction.
Nickel is a costly metal. Do not therefore discard even such of the spent Raney
Nickel Catalysts which cannot be reactivated any more.
C. General Safety measures to be taken:
Emergency drills should be carried out periodically to ensure preparedness must
continue.
Wind indicator should be provided at the highest level of the plant to know the
wind direction.
Many operations involve use of highly toxic/flammable materials and these
needs to be documented as SOPs. These must be made and kept updated on
priority.
Extensive training on use of Self Contained Breathing apparatus (SCBAs) must be
ensured for emergency control.
Raw materials are either toxic or flammable, therefore important to ensure that
these materials are stored in closed, well ventilated totally safe areas. A fire
alarm system (heat and smoke detection) should be provided for the storage
area where the material is stored as toxic fumes arise on combustion.
Loose drums of waste materials, often solvent laden, must be removed from the
working areas and close watch kept.
Proper Earthing needs to be provided through plug type systems or through the
agitators/liquid.
Ventilation should be provided for any enclosed are where hydrocarbon or toxic
vapors may accumulate. Several such areas were noticed- these may be surveyed
and tackled accordingly.
All personnel should be trained in handling emergency situations and should be
apprised of their role in handling emergency situation and to ensure adequacy of
the emergency procedures simulated exercise should be carried out. This was
found wanting.
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Flame arrestor should be provided.
Adequate number of caution boards highlighting the hazards of chemicals should
be provided at critical locations.
Monitoring of occupational hazards like noise, ventilation, chemical exposure
etc. is carried out regularly and its record is maintained.
Good housekeeping, use of PPE, Engineering controls, Enclosure processes,
scrubber system, display of safety boards, SOP of loading / unloading, local
exhaust ventilation, safety shower etc. are important safety measures have taken
to keep these chemicals within TLV.
Appropriate personal protective equipment is provided & ensure the usage of
them.
Workers is trained for safe material handling of hazardous chemicals.
Prepare & display the safe operating procedure for hazardous chemicals storage,
handling & transporting or using.
Local Exhaust ventilation and scrubber should be installed where it is required to
reduce fumes, vapors, temperature and heat stress.
Reduce the level of physical activity by sharing workload with other or by using
mechanical means.
D. FIRE safety devices should be PROVIDED to protect from any malfunctioning of
plant equipment.
Water storage of adequate capacity to meet the requirements of water for
firefighting purposes.
Fire hydrants and automatic sprinkler system. Diesel driven pumps and headers
to supply water to fire hydrant network.
Adequate Portable fire extinguishers, sand bucket, wheeled fire & safety
equipment should be provided at the required places.
Fire proof electric fitting is mandatory.
Equipment required for personal safety like blankets, gloves, apron, gum boots,
face mask helmets, safety belts, first aid boxes etc. are provided. Proximity suits
and self-contained breathing apparatus to be provided.
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Table7.11: Details of proposed fire safety measures
Sr.
No. Type Capacity Qty**
1. Water storage tank (For Fire) 1.5 KL 1
2. Jockey Pump 250 RPM 1
3. 200 Liter Capacity Mobile Foam Unit 200 Lit 01 Nos
4. Dry chemical Powder 2 Kg. 10 Nos.
5. Dry Chemical Powder 6 Kg. 6 Nos.
6. Capacity Dry Chemical Powder type Fire
Extinguishers 9 Kg. 3 Nos.
7. Capacity Foam type Fire Extinguisher. 50 Kg 1 Nos
8. Capacity Co2 type Fire Extinguisher. 3 Kg 03 Nos
9. Capacity Co2 type Fire Extinguisher. 4.5 Kg 02 Nos
10. Capacity Co2 type Fire Extinguisher 6.5 Kg 02 Nos
Note: **Numbers of cylinders and type may change after commissioning of the project
depending on requirement of NOC from fire department.
7.9 Occupational Health Surveillance Programme
7.9.1 Introduction:
The Factories Act, 1948 and the rules framed thereunder provide for pre-employment
and periodical medical examinations of workers employed in industries with
hazardous processes and dangerous operations under section 41-C and section 87
respectively.
All Chemical listed in table no. 7.2 to which workers will be exposed. There are solvent
stored within premises which may cause adverse health impact due to regular
exposure. Pre-employment medical checkup and periodically medical examination
will be done. Liver function testis will be carried out during pre-placement and
periodical examination. In addition to the above, following safety equipment will be
provided.
7.9.2 Action plan for Occupational Health and safety for workers:
Monitoring of occupational hazards like noise, ventilation, chemical exposure etc.
will be carried out regularly and its record will be maintained.
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Good housekeeping, use of PPE, Engineering controls, Enclosure processes, display of
safety boards, SOP of loading / unloading, local exhaust ventilation, safety shower
etc. All necessary safety measures will be taken to keep all chemicals within TLV.
Appropriate personal protective equipment will be provided & ensure the usage of
them.
Workers will be trained on safe material handling of hazardous chemicals.
Prepared & display the safe operating procedure for hazardous chemicals storage,
handling & transporting or using.
Periodical medical examination of the workers & Liver Function Testes will be done.
Register (form no.37) for work place air monitoring will be done regularly.
Employee training and education will be carried out regularly.
Control the noise at source by substitution, isolation, segregation, barriers will be
done.
Local Exhaust ventilation will be installed where it is required to reduce fumes,
vapors, temperature and heat stress.
Periodic Health Check-up includes: 1. Complete clinical check-up. 2. X-ray of chest. 3. Vision testing. 4. Blood routine, sugar and cholesterol. 5. Urine routine. 6. ECG for workers above 40 years. 7. Indirect laryngoscopy for workers above 40 years. 8. Spirometer for workers employed in dusty, and smoky environment. 9. Audiometry for those, working in noisy environment.
Statutory requirement:
Health Records (Rule 68R): Once in every 6 months or immediately after his medical
examination whichever is earlier.
Medical Examination & FMO (Rule 68T & U):
1. Pre-employment and six monthly periodical examinations are required. 2. Report of above examinations shall be in form No. 32. 3. First employment only after fitness certificate in form No. 33, Appeal regarding unfit,
shall lie with the Certifying Surgeon (CS) whose opinion shall be final.
4. The worker required to undergo medical examination will not refuse it.
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7.9.3 Possible Health Effect from Aromatic chemicals/solvents stored within premises
As mentioned in above stated occupational health and surveillance programme,
industry will appointed Factory Medical Officer (MBBS with Associate Fellow of
Industrial Health (AFIH) Certification) for periodical, pre-employed medical
monitoring of all workers. Project proponent will take all necessary measures as
stated in topic no. 7.9.2 to reduce exposure to workers
Table7.12: Common Chemical used within premises and their Health Effects and
Medical Monitoring
Hazardous
substance or
chemical group
Compounds Target organs Potential health
effects
Medical monitoring
Aromatic
Hydrocarbons
Methanol
Toluene
O-Xylene
Blood
Bone
marrow
Central
Nervous
System
Eyes
Respiratory
system
Skin
Liver
Kidney
Central
Nervous
System
depression:
Decreased
alertness,
Headache,
Sleepiness,
Loss of
consciousness.
Defatting
dermatitis.
Medical examination
with focus on liver,
kidney, nervous
system, and skin.
Laboratory testing:
Complete blood count
(CBCb) Platelet count
Measurement of
kidney and liver
function.
Following test are
performed
CBC
Urine R/M
RBS
SGPT
S. Creat
PFT
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7.9.4 Treatment Facilities Provided to workers affected by accidental Spillage of
Chemicals
Regular safety inspection is highly recommended to keep equipment up to date and
ensure all procedures are being followed correctly. Chemical Plant Safety
Precautions to Avoid Accidents and Injuries
o Gas detectors system as described in above section of chlorine and ammonia
o Fire extinguishers
o Frequent training on safety procedures
o Perform hydrostatic tests to check pressure safety equipment
o Protective eyewear
o Eye-washing equipment for splashes
o Safety valves to regulate pressure
o Ventilation and respiration for fumes
o Adequate number of Personal protective equipment to revent contact with
skin by wearing neoprene gloves, lab coat, and resistant apron. Glasses or a
face shield will be provided if splashing may occur.
o Washing facility: In case of contamination of chemicals
o Drinking water
o First aid facility at prominent location within premises
o Antidots of chemicals will be provided within premises.
o Emergency accident Warning Devices
o Regular Maintenance and Inspection of process machineries
Medical Arrangement:
First Aid Boxes have been provided at various strategic locations. Requisite number
employees are trained about First Aid, Liaison with nearest hospitals. Details of available
antidotes of raw materials is given in table no.7.11.
7.9.5 Minimization of the Manual Handling of Hazardous Substance
Employers and employees should examine their workplaces to detect any unsafe or
unhealthful conditions, practices, or equipment and take corrective action. Provide
flameproof electrical motor & transfer chemicals through the pipelines. Use
specially designed pallets to hold, move raw materials, finished products through
work areas. Minimize lifting of raw materials, heavy loads by using appropriate
platforms, trolleys etc. Avoid the moving, manual handling of hazardous material.
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Table7.13: DO’S and DONT’S
A. (Handling of Chemicals)
Do’ Dont’
Know the hazards of the chemical before
handling.
Know the antidotes for chemical, which you
are handling.
Do keep material safety data sheet in
locations where chemicals are being handled
and study it.
Use appropriate personal protective
equipment like gloves, aprons, and respirator;
face shield etc. depending upon nature of the
work.
Label every chemical that you use and tightly
close the container.
Use eye wash fountain / safety shower in case
of splash of chemicals in the eye or body for
at least 15 minutes.
Segregate toxic, flammable chemicals and
keep them under control.
In addition to draining and closing valves,
lines should be blanked before taking up
maintenance work.
Provide proper ventilation at the chemical
handling area to limit their concentration
within prescribed level.
Do not store the chemicals that are
incompatible with other chemicals.
Do not spill the chemicals.
Do not dispose chemical without
neutralizing.
Do not keep large inventory of
chemicals.
Do not allow empty containers of
hazardous chemicals to be used by
others.
Do not use compressed air for
transferring chemicals.
Do not stand near chemical transfer
pump while it is in operation with
temporary hose connection.
Pouring of chemicals by hand or doing
siphoning by mouth should never be
adopted.
Chemicals drums should never be
moved without protection.
Do not attempt to neutralize the acid /
alkali on the skin. Use water only.
Do not use solvent for cleaning hands.
B. Material Handling
Do’ Don’t
Use proper lifting tool and tackle having
adequate capacity.
Only authorized persons should operate
material handling equipments.
Each tool, tackle or equipment should have
number and safe working load (SWL) marked
Do not use the equipment for the
purpose other than its design intention.
Do not allow personnel to move
underneath lifted load.
Do not load the equipment above its
safe working load.
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Do’ Don’t
on it.
Assess weight of the material, distance to be
carried and hazards etc. before lifting the
load.
Inspect and test all the lifting tools and tackles
regularly as per Factory Rules.
Wear Personal Protective Equipments while
handling of material.
Wherever possible, mechanized material
handling shall be adopted.
While lifting a load physically, keep the load
as near as possible to the body with feet
properly placed for body balance.
Bend knees, keep back straight, keep the load
closed to the body and lift the load.
Do not use makeshift arrangements for
lifting equipment without inspection
and test.
Do not use defective tool and tackles.
Keep the tools & tackles free from
adverse effect of atmosphere by
applying suitable protective coating.
The angle between the legs of two leg
sling should not exceed 90 degree.
Do not allow male and female adult to
lift a load manually higher than 55 kgs
and 30 kgs respectively.
Do not hold the load with tip of the
fingers; grasp the load firmly with palm.
C. Fire Prevention
Do’s Don’ts
Follow ‘NO SMOK NG’ i n.
Deposit oily rags and waste combustible material
in the identified containers and dispose them
suitably.
Fire Hose used for any other purpose should be
permanently marked and taken out of fire
hydrant system.
Keep minimum inventory of flammable and
combustible substances.
Take permission before breaking or removal of
fire barrier and ensure subsequent relocation of
fire barrier.
Check periodically the operability of fixed fire
fighting system.
Attend any abnormality / deficiency with fire
protection system promptly.
Provide earthling or bonding to prevent
accumulation of static charges to tanks where
Do not leave flammable material like
acetone, kerosene etc. used as
cleaning agent at the work area.
Do not over tighten fire hydrant
valves with F-lever.
Do not allow wild grass growth
around storage of the gas cylinders
and switchyard.
Do not obstruct accessibility to the
fire related equipment.
Do not destroy the inspection tag
provided with the fire equipment.
Do not misuse fire-fighting
equipment other than intended
purpose.
Do not store the flammable material
in the open container.
Do not use instruments that are not
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flammable chemicals are stored / handled.
Use instruments that are intrinsically safe in
explosive atmosphere.
intrinsically safe in the explosive
atmosphere.
D. House Keeping
Do’s Don’ts
Assign places for everything and maintain things
at assigned places.
Clean the area after completion of work.
Use aisle space free for personnel and material
movement.
Ensure adequate illumination and ventilation for
the job.
Drop paper, plastic, glass, metal and bio-medical
waste in a separate bin kept for this purpose.
Know the location where emergency equipment
such as first aid box, fire fighting equipment,
SCBA, Stretchers are kept.
Arrest all types of spills such as chemical, water,
oil, air / gas, steam etc. and clean up the area
immediately.
Ensure exits are indicated / painted for use
during emergency.
Do not leave combustible materials
in the work area.
Do not smoke in the area of work.
Do not allow dust bin to overflow.
Do not generate extra waste.
Do not disturb the safety equipment
from assigned location.
Do not block emergency switches
and on/off switches of the
equipment by storming of materials
in front of work.
Do not leave cleaning agent like
acetone, isopropyl alcohol, kerosene
etc. at the work area after
completion of work.
Do not block fire exit point by storing
materials or by means.
Do not leave a spillage unattended.
7.10 Disaster Management Plan
7.10.1 Disaster
Disaster , A disaster is a catastrophic situation in which the day-to-day patterns of life
are, in many instances, suddenly disrupted and people are plunged into helplessness
and suffering and as a result need protection, clothing,, shelter, medical and social
care and other, necessities of life.
Advance emergency planning and proper training of every employee in the
'emergency function is very essential to make emergency control measures more
effective. There are two types of emergency control plans (1) On site emergency plan
and (2) Off site emergency or disaster plan.
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7.10.2 Statutory Provisions:
Section 41B(4) of the Factories Act, 1948 requires an on site emergency plan and
detailed disaster control measures for the safety of the factory workers and the
general public living in the vicinity of the factory. The occupier is required to inform
the workers and the public about the safety measures to be taken in the event of an
accident.
Rule 13, 14 and Schedule II & 12 of the Manufacture; Storage and Import of Hazardous
Chemicals Rules, 1989 and Rule 5,7,9 and 10 of the Chemical ' Accidents (Emergency
Planning, Preparedness and Response) Rules, 1996 also provide for on-site and off-site
emergency plans
7.10.3 On-Site Emergency Plan :
Objectives of the Plan
1. To protect persons and properly of your factory in case of all kinds of accidents,
dangerous occurrences (Rule 103, Gujarat Factories Rules), emergencies and
disasters happening in or affecting your plant at any time.
2. To inform people and surroundings about above happening if it is likely to adversely
affect them.
3. To inform authorities including helping agencies (doctors, hospitals, fire, police,
transport etc.) in advance, and also at the lime of actual happening.
4. To identify, assess, foresee and work out various kinds of possible hazards, their
places, potential and damaging capacity and area in case of above happenings.
Review, revise, redesign, replace or reconstruct the process, plant, vessels and
control measures if so assessed.
5. To work out a plan with detailed instructions to cope up with above happenings,
based on your personnel, equipment and records. Necessary requirements shall be
added if not already available. Levels of hazardous substances shall be minimised to
the extent possible. Establish machinery for rescue and recuperation operations,
total loss control and prevention of harms and recurrence of above happenings.
Ensure that absolute safety and security is achieved within the shortest time.
7.10.4 Site Plan of the Factory and Surrounding:
Proposed unit has prepared a plan of the factory premises and surroundings showing
therein the areas of various hazards such' as fire, explosion, toxic release etc., and also
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location of assembly points, equipment room, personal protective equipment room,
telephone room, first aid or, emergency control room, main gate, emergency gates, normal
wind direction, north direction.
The same has been given in Chapter No.2; Figure No.2.4 of EIA report
7.10.5 Types of Overall Emergencies
In the risk assessment study topic no. 7.3 describes all type of hazards are listed along with
its causes in or near plant. Fire (small and big), explosion, toxic exposure, strike, storm, flood
and other hazardous possible situations shall be described with reasons. Sources of hazard
from outside or neighboring plants, tanks, structure etc. shall be mentioned. From the
consequence analysis table no.7.15 for storage area and drums following emergency
situation can be arise.
Table 7.14 Type of overall emergencies
Sr.
No.
Type of emergency
including disaster
(Major class)
May arise due to
At (Place)
People and
area likely to
be affected
1 Fire
Methanol spillage or leakages
at storage tank
Leakages: Pipeline, pumps
and valves carrying
Methanol
Leakages and spillages in
drums storage area for raw
materials and products
Fire in road tanker of
Methanol during loading of
methanol
Storage area
of raw
materials
Tankers
carrying
Methanol
Plant
Operator,
Labors,
workers
Admin staff
2 Explosion
Failure of the safety
valve/pressure relief
valve, corrosion of critical
parts of the boiler, or low
water level.
Boiler
3 Release of Toxic
Gas/Vapour
Leakages from valve or
tonner or Chlorine or from
cylinder of Ammonia.
Storage area
of Chlorine
tonner and
Ammonia
4 Spillage of Loading and unloading Tank farm
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Sr.
No.
Type of emergency
including disaster
(Major class)
May arise due to
At (Place)
People and
area likely to
be affected
flammable liquid
/gas
area, process
area
5 Deliberate Sabotage,
Terrorism, Air Raid
etc.
- -
6 Natural Calamities: -
Lightening, Storm,
Earthquake, Flood
etc.
- -
7 Collapsing of
structure
Overturning of
tanker containing
flammable / toxic
substances
- -
7.10.6 Assessment of In-plant Hazards
Detailed hazard assessment of in-plant and control measures provided in topic no.7.3, table
no.7.3 & 7.4 of EIA report. Storage Hazards and Controls, Process Hazards and Controls are
described in same topic.
7.10.7 Emergency Control System:
A. Emergency Organizations and Functions
The organizational set-up necessary for chain of commands during emergency situation,
which may arise in the premises. The system is described in following Subsections.
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Organizational Set-up
Members of above teams will be available during all shifts and holidays. Protective
equipment, lifting gears, fire control points etc.; will be provided in sufficient numbers and
their locations will be well informed. Necessary vehicles will be kept ready to shift persons
'in case of emergency.
B. Emergency Control Room (Safety officer room)
The place identified as Emergency Control Center is considered as safety officer room.. The
facilities available at the Emergency Control Center shall include:
i. Internal Telephone& External Telephone:
Address and Telephone numbers of the Factory Inspectorate, Gujarat Pollution Control
Board, Police, Fire Brigade, Hospitals and OEP Team Members
ii. Manual Fire/Emergency Siren
iii. Siren Actuation Switch
iv. Important Address and Telephone Numbers
v. Emergency Vehicles
vi. Confined Space Entry Procedure
vii. List of Antidote/actions to be taken in case of hazardous chemical/materials.
viii. Material Safety Data Sheets of chemicals
ix. A copy of On-Site Disaster Management Plan
x. Plant layout-indicating storage of hazardous materials, layout of fire
Hydrants/extinguishers, entrances/exits, roads etc.
Plant Manager
EHS/Safety Officer
Supervisor Plant Chemist
Director
Skilled workers Security staff
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xi. Portable P.A. System, Manual Siren, flood lights, Torches, Pickaxe, Saw, Nylon
Ropes.
xii. Fire Blankets / Fire Proximity Suit, Breathing Apparatus, First Aid Box etc.
xiii. List of employees with address, telephone number, blood group etc.
All communications after General Shift working hours and on Sundays/ Holidays are to be
routed through the Security Gate Office.
C. On – site facilities for emergency control
Fire Emergency: Trained personnel will be employed in all the shifts. The responsibilities and
duties include:
To fight the fire with available internal firefighting equipment and to stop leakage of
liquid etc.
To provide personal protective equipment to the team.
To cordon the area and inform incident controller or site main controller about the
development of emergency.
To train the persons (essential workers) to use personal protective equipment and fire-
fighting equipment.
D. Fire Fighting Facilities to be provided on - site:
1. Fire Buckets / Fire Extinguishers : details is given in table no.: 7.12
2. Fire Alarm Sirens
It will be provided to alert all the employees inside the premises about the situation of
an emergency.
3. Sand Buckets
5 nos. of sand buckets will be provided within the industrial premises in case of
emergency fire.
4. Oxygen Cylinder
Oxygen cylinder will be provided for emergency.
E. Assembly Points:
The assembly points for gathering workers / Admin staff is fixed and clearly marked as per
the wind direction on plant layout as well as on site.In case of emergency some locations are
considered as Assembly Points. Depending on the wind direction and location of
emergency, Assembly Point is declared. The employees should run across the wind
direction and not against the wind direction.
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7.10.8 General Procedures and responsibilities:
Mock drill:Mock drills are carried out regularly to familiarize the staff with their roles, fire
protection equipment/system installed in the plant and use of personnel protective
equipment. Senior officials
Wind Socks: Wind direction is determined with the help of installed windsocks.
Procedure on Noticing an Emergency
If anybody notices any situation, which may lead to a disaster, should be immediately
inform the Shift In-charge / site controller / Incident Controller / Fire & Safety Supervisor
/ Security.
Take charge of the situation as Incident Controller.
Rush to the site of emergency to get the correct picture and then to Emergency Control
Center for speedy control over the situation by making an arrangement for raising the
alarm.
On arrival of Team members, he shall assign duties as required and activate the On-Site
Emergency Plan.
Ensure safety of the plant and the personnel in the plant. He will make an assessment of
the emergency and decide on external assistance.
Communicate and Coordinate among the Incidents Controller/ Site Controller/ Factory
manager/ fire safety supervisor etc. and is final authority on all matters related with
management of emergency such as:
Firefighting
Welfare and rescue operations.
Arrange for Civil/Mechanical/Electrical work during emergency.
Transport.
EHS/SAFETY OFFICER & Security staff:
Rush immediately to the scene of the fire/emergency, select and set out appropriate
fire/emergency equipment. He will take the below mentioned actions at the earliest
opportunity, if the fire/emergency is not controlled.
He will
Call the security personnel from their residences for additional manpower if required.
Regulate entry and exit of personal required for controlling the fire/emergency.
Restrict exit of personal required for controlling the fire/emergency.
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Arrange for Personnel Protective Equipment required for the emergency.
Call, the local Fire Brigade, Police in case of necessity in consultation with the Incident
controller.Arrange transport facilities for removal of causalities to dispensary / hospital.
Take responsibility of law and order.
Keep detailed records of the incident and progress of operations to fight the emergency.
Plant manager:
He will rush to the Emergency Control Centre and collect the information from the Incident
Controller. Further he will,
Announce the location of the Assembly Point after getting information from Incident
Controller / site controller. Take the list of persons to be communicated internally and
externally.
Maintain liaison with the press, government agencies i.e. Police, Fire Brigade etc. and
the neighborhood regarding the emergency under instructions from Incident Controller.
Courteously Receive officers from the State Government or neighbors to the
Administration Block only and inform to Incident Controller that they can be taken care
off.
Take all the steps required for the welfare such as providing tea, snacks, emergency
temporary Medical Center in consultation with the incident controller/site controller.
Disclose all the necessary information in the plant and media so as to avoid rumors and
Confusion. Also be responsible for the head counts at the Assembly Points.
Supervisor/ shift in charge& security:
Proceed to the scene; establish contact with firemen and incident controller to
supplement efforts in fire fighting.
Assist in searching casualties and help to remove them to the medical center. Organize
outside assistance in fire fighting and rescue operations if required.
Mobilize personal protective equipment and safety appliances and assist personnel
handling emergency in using them.
Keep and check on any new development of unsafe situation and report the same to Site
Main Controller. Effectively cordon off the emergency area and will prevent
unauthorized people entering the scene.
Permit the Fire tenders or Ambulance requisitioned by Incident Controller to the plant.
Ensure that vehicles and trolleys are sent out of the plant premises.
Ensure that all the employees are conducted out of plant and assembled at Assembly
Point.
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Control Traffic Movement. Remove tankers, tanker drivers outside. Entry of
unauthorized public to be prevented.
Arrange for vehicles for shifting casualties and essential workers to safe assembly points.
Collect and preserve evidence to facilitate future inquiries.
7.11 Offsite Emergency Preparedness Plan
Offsite emergency plan would follow the onsite emergency plan. When the consequences of
an emergency situation go beyond the plant boundaries, it becomes an offsite
emergency.As the off-site emergency plan is to be prepared by the Government, a Central
Control Committee or Group shall be formed under the Chairmanship of the area head. For
example we assume a district structure and District Collector (is the Chairman of the District
Control Committee (DCC). Other officers from police, fire, factory, medical, engineering,
social welfare, publicity, railway, telephone, transport and requisite departments shall be
incorporated as members.
The roles of the various parties who is directly involved in the implementation of an offsite
plan are described below. Depending on local arrangements, the responsibility for the
offsite plan would either rest with the plant management or with the local authority.
Figure 7.12: Off-Site Emergency Plan
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Aspects Proposed to be considered in the Offsite Emergency Plan
The main aspects, which should be included in the emergency plan, are:
Organization: Detail of command structure, warning systems, and implementation
procedures, emergency control centres. Names and appointments of incident controller,
site main controller, their deputies and other key personnel.
Communications: Identification of personnel involved, communication centre, call signs,
network, list of telephone numbers.
Specialized Knowledge: Details of specialist bodies, firms and people upon whom it may be
necessary to call e.g. those with specialized fuel knowledge, laboratories.
Voluntary Organizations: Details of organizers, telephone numbers, resources etc.
Fuel Information: Details of the hazardous substances stored and a summary of the risk
associated with them.
Meteorological Information: Arrangements for obtaining details of weather forecasts and
weather conditions prevailing at that time
Humanitarian Arrangements: Transport, evacuation centres, emergency feeding, treatment
of injured, first aid, ambulances and temporary mortuaries.
Public Information :Arrangements for (a) Dealing with the media press office; (b) Informing
relatives Assessment of Emergency Plan
Arrangements for: Collecting information on the causes of the emergency; and Reviewing
the efficiency and effectiveness of all aspects of the emergency plan.
Role of the Emergency Co-ordinating Officer
The various emergency services would be coordinated by an Emergency Coordinating
Officer (ECO), who is designated by the district collector. The ECO would liaison closely with
the Factory Manager/Safety officer. The ECO has been equipped with address and phone
numbers of important agencies.
a. Role of the Local Authority
The duty to prepare the offsite plan lies with the local authorities. The emergency planning
officer (EPO) appointed should carry out his duty in preparing for a whole range of different
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emergencies within local authority area. This liaison should ensure that plan is continually
kept up to date. It is responsibility of the EPO to ensure that all those organizations which
has been involved offsite in handling the emergency, know of their role and are able to
accept it by having for example, sufficient staff and appropriate equipment to cover their
particular responsibilities. Rehearsals for offsite plans should be organized by the EPO.
b. Role of Police
Formal duties of the police during an emergency include protecting life and property and
Controlling traffic movements. Their functions should include controlling bystanders,
evacuating the public, identifying the dead and dealing with casualties, and informing
relatives of death or injury.
c. Role of Fire Authorities
The control of a fire should be normally the responsibility of the senior fire brigade officer
who would take over the handling of the fire from the site incident controller on arrival at
the site. The senior fire brigade officer should also have a similar responsibility for other
events, such as explosions. Fire authorities in the region should be appraised about the
location of all stores of flammable materials, water and foam supply points, and firefighting
equipment. They should be involved in onsite emergency rehearsals both as participants
and, on occasion, as observers of exercises involving only site personnel.
d. Role of Health Authorities
Health authorities, including doctors, surgeons, hospitals, ambulances and so on, should
have a vital part to play following a major accident, and they should form an integral part of
the emergency plan. For major fires, injuries should be the result of the effects of thermal
radiation to a varying degree, and the knowledge and experience to handle this in all but
extreme cases may be generally available in most hospitals.
Major off site incidents are likely to require medical equipment and facilities additional to
tho e a aila le locally, and a medical "mutual aid” cheme hould exi t to ena le the
Assistance of neighboring authorities to be obtained in the event of an emergency.
e. Role of Government Safety Authority
This will be the factory inspectorate available in the region. Inspectors are likely to satisfy
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themselves that the organization responsible for producing the offsite plan has made
adequate arrangements for handling emergencies of all types including major emergencies.
They may wish to see well documented procedures and evidence of exercise undertaken to
test the plan. In the event of an accident, local arrangements regarding the role of the
factory inspector will apply. These may vary from keeping a watch, to a close involvement in
advising on operations.
Table No.7.16 Offsite Action Plan
Sr.
No.
Action Required to be taken to
Mitigate Disaster by Aid giving
agency
Responsible
Agencies for
Taking action
Equipment/Material facilities
required at site to mitigate
Emergency
A
1
Arrangements for evacuation
Rescue of persons from zone of
influence to predetermined camps
Police
Department
Self-Breathing apparatus
With spare cylinder
Chemical gas mask with
spare canister
Vehicle with PA system
Transportation for evacuation
of people
2 Caution to public by
announcement
3 Traffic control by cordoning
of the area
4 Law & order
5 Request to railway authority for
keeping the nearest railway gate
open & to stop the trains at the
nearest railway station
B Control of fire District Fire
Brigade
Self-breathing apparatus with
spare cylinders
Foam /water fire tenders
Gas mask with spare canisters
Limewater
Neck to toe complete
asbestos suit, PVCh and gloves,
gumboots, safety goggles
Mobile scrubbing system
Along with suction
arrangement.
1 Scrubbing of the flashed off gas
Cloud with water curtain
2 To rescue trapped persons
3 If fire is big, keep surrounding
Are a cool by spraying water
4 Communication to State
Electricity Board to continue or
cut off electric supply
5 Communication to water supply
Department for supplying water
C Medical facilities for affected
persons(first aid and treatment)
Hospital and
Public health
Ambulance with onboard
resuscitation unit, first aid,
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No.
Action Required to be taken to
Mitigate Disaster by Aid giving
agency
Responsible
Agencies for
Taking action
Equipment/Material facilities
required at site to mitigate
Emergency
stretchers
D Identification of concentration of
Gas in zone of influence
Pollution
Control Board
Gas detector
E Removal of debris and damaged
structures
Municipal
corporation
Provide bulldozers
Provide cranes
F
1
Monitor the incoming and out
Going transports
Transport
department
Provide traffic police at site
Provide emergency shifting
vehicles at site
Provide stock of fuel for
vehicles.
2 Arrange emergency shifting of
affected persons and non
Affected person to specified area
3 Arrange diesel/petrol for needed
vehicles
G
1
Give all information related to
Meteorological aspects for safe
handling of affected area for living
beings
Meteorological
Department
Provide wind direction and
velocity instruments with
temperature measurements
2 Forecast important weather
Changes ,if any
Mobile van for
Meteorological parameter
measurements
H
1
Representatives of all
departments are in the local is
group; therefore they are expected
to render services available with
them. Since it is a group of experts
with authority, the mitigating
measures can be implemented
speedily. The representative’ from
locals are also there so that
communication with local people is
easy and quick.
Local Crises
Group
Must have all resources at hand,
specially disaster management
plan and its implementation
method.
All relevant information
Related to hazardous industry
shall available with crisis group
Newspaper editor shall be a part
of the group so that right and
timely media release can be
done
2 The district emergency or
Disaster control officer/collector
shall be the president and he shall
do mock drill etc. So that action can
be taken in right direction in time
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No.
Action Required to be taken to
Mitigate Disaster by Aid giving
agency
Responsible
Agencies for
Taking action
Equipment/Material facilities
required at site to mitigate
Emergency
I
1
Collector shall be the President
Of District Crisis Group therefore all
district infrastructure facilities are
diverted to affected zone
District Crisis
Group
All necessary facilities
available at district can be made
available at affected zone
Control of law and order
situation 2 All other functions as mentioned
For local crisis group
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Chapter-8: Project Benefits
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Environmental Impact Assessment Report
CHAPTER - 8
PROJECT BENEFITS
8.1 General:
The proposed project is to manufacture active pharmaceutical ingredients. The current growth in
new medical technologies is spurring the demand for APIs worldwide today especially with the
increased importation of raw pharmaceutical ingredients from emerging markets. According to
different surveys, countries such as India and China, which now supply over 40% of APIs used in the
U.S. will double that figure to a whopping 80% in just the next 10 years. The API industries in India
include domestic and in-house consumption as well as exports. API manufacturers in India are trying
to strengthen their marketing in regulated markets by different means viz., by focusing on the
improvement of production yields; especially of critical products, through process modification, by
increasing the productivity of high volume products through capacity re-balancing, by increasing
sales in international market etc. Manufacturing standards in India are compliant with many
international regulations. In addition, improvements in the technological capabilities of the country
have enabled many manufacturers to venture into the highly regulated markets of the US and
Europe. Proposed project will have benefits in form of increase in employment opportunity,
infrastructural development, socio-economic development etc. as described below under respective
points;
8.2 EMPLOYMENT POTENTIAL
Proposed project will have employment potential for about 30 persons, skilled & unskilled, for the
operation and maintenance in efficient way. Secondary jobs and indirect employment are also
bound to be generated to provide day-to-day needs and services to the work force and industrial
activity. The employed people will be benefited financially as this financial growth will fulfil their
economic requirements, which in turn will increase their living standard.
8.3 IMROVEMENT IN PHYSICAL & SOCIAL INFRASTRUCTURE
Proposed project has basic infrastructure facilities such as proximity to man power, electricity, water
supply, transportation, telecommunication systems As far as the project premises is concerned, unit
will prepare labor rooms for about its 8 employees with sufficient facilities including drinking water,
toilets, sanitation facilities, power, communication, etc. In addition to these, benefits due to CSR
activities, if any CSR activities will be related with such facilities.
8.4 OTHER TANGIBLE BENEFITS
Employment & trade opportunities will be generated with proposed project. Thus, these
considerable employment & trade opportunities will eventually result in appreciable economic
benefits to the local people & businesses/contractors. Proposed project will also contribute revenue
to the State exchequer in form of applicable tax. Indirect contribution to the State exchequer will be
there due to Income by way of registration of trucks, payment of road tax, income tax from
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individual as well as taxes from associated units. Thus, the proposed project will help the
Government by paying different taxes from time to time, which is a part of revenue and thus, will
help in developing the area. The country shall also benefit from increase in excise and vat revenues.
The CSR activities by the company can be considerably beneficial for the health, education,
upliftment of poor people, welfare of women & labors, assistance to the disabled people etc. These
all together with the economic benefits of the proposed project will result in further benefits in
terms of the literacy level, primary and middle level education and on health facilities.
8.5 CORPORATE SOCIAL RESPONSIBILITY (CSR)
Proposed Expansion project will generate employment for about 30 persons, skilled & unskilled, for
the operation and maintenance in efficient way. In addition to this, unit will try to generate indirect
employment for many people of nearby villages.
Unit will spend annually minimum 2.5 % of its net profit for carrying out various CSR activities as
stated below;
Provision of drinking water and sanitation facilities in schools.
Provision of education aids & scholarship to poor students.
Contribute in religious and social programs in nearby villages.
Organize medical camp and providing support for the development and maintenance of the
health facilities.
Plantation along the road side and development of garden/greenbelt in nearby villages.
Organize various camps for awareness programs regarding health and sanitation, Cleanliness in
surrounding, greenbelt development.
Participate and cooperate in animal husbandry camp.
In addition to this, unit will spend 2.5% amount (Rs. 22.5 lacs) of the project cost in 3 years after
commencement of production. Detailed planning of spending this amount in various activities in
nearby villages is given below;
Table No.: 8.1 Budgetary allocation for CSR Activity
Type of Activities
Total amount to be spent (Rs. In Lacs) Total
1st Year 2nd Year 3rd Year
Tree Plantation in nearby villages 1.0 1.0 1.0 3.0
Development of Medical facilities in Hospital
2.0 2.0 2.0 6.0
Vocational Training Skill Development in nearby collage
1.5 1.5 1.5 4.5
Donation in Schools / distribution of education aids
1.5 1.5 1.5 4.5
Drinking & sanitation facilities in schools of nearby villages
0.5 0.5 0.5 1.5
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Type of Activities
Total amount to be spent (Rs. In Lacs) Total
1st Year 2nd Year 3rd Year
Organization of medical camps and various training programs
1.0 1.0 1.0 3.0
Total 7.5 7.5 7.5 22.5
These CSR activities by the company will be considerably beneficial for the health, education,
upliftment of poor people, welfare of women & labors, assistance to the disabled people etc.
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CHAPTER - 9
ENVIRONMENTAL COST BENEFIT ANALYSIS
The study on Environmental Benefit Analysis is to be done only if it is required during scoping stage
as stated in above stated EIA notification. During scoping stage ToR points issued by SEIAA, Gujarat
vide letter no.: SEIAA/GUJ/TOR/5(F)/269/2017 dated 24th April 2017 has not included point of
Environmental Cost Benefit Analysis, therefore this analysis is not carried out .
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Chapter-10: Environmental Management Plan
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CHAPTER - 10
ENVIRONMENTAL MANAGEMENT PLAN
10.1 INTRODUCTION
Environmental Management Plan provides methods and procedures which an organization will use
to meet its objectives with respect to Pollution Control. Cost of measures for pollution prevention
activities is treated as an integral component of the project cost.
The proposed Environment Management Plan of the proposed unit will be composed of the following:
Summary of the potential impacts of the proposal
Description of recommended mitigation measures
Description of monitoring programme to ensure compliance with relevant standards and residual impacts
Allocation of resources and responsibilities for plan implementation
Implementation schedule and reporting procedures
contingency plan when impacts are greater than expected The Management Action Plan aims at controlling pollution at the source level to the possible extent
with the best available technology followed by treatment measures before they are discharged. The
recycling and re-use of industrial waste not only reduces the waste generated but can be an economic
gain to the industry.
10.2 ENVIRONMENTAL MANAGEMENT PLAN FOR THE PROPSOED PROJECT
The EMP for the proposed project has been prepared for the various environmental attributes like Air,
Water, Land, Noise, ecology, socio-economic etc. and the same is given below in Table 10.1.
Table 10.1: Environmental Management Plan
Activity Source of Pollution Type of Pollutant Environment Management
Plan/Mitigation Measures
1. Water Environment
A. Manufacturing process
Generation of
effluent from production activities
Generation of
high TDS, BOD, COD effluent, RO reject
High COD & TDS stream, Low
COD stream will treated sent to ETP consisting of primary treatment units. Primary treatment will include neutralization of effluent. Neutralized effluent will be sent to M/s Chhatral Environmental Management System Pvt. Ltd., Chhatral for final disposal. Unit will become member of facility after obtaining Environmental Clearance.
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Activity Source of Pollution Type of Pollutant Environment Management
Plan/Mitigation Measures
B. Domestic usages of
water
Generation of
domestic effluent
SS, COD
domestic effluent
Domestic effluent will be
disposed off through septic tank/soak pit system.
2. Air Environment
A. Steam Boiler & thermic Fluid heater
Flue gas emission from stack attached to steam boiler
Emission of SPM, SO2, NO2.
Industry will install cyclone separator followed by bag filter to the common stack attached to Thermic Fluid Heater and boiler and adequate stack height will be provided.
B. Loading and unloading activities of raw material and products
Fugitive emissions from process, spillages and leakages
Vapours of raw materials, solvent and products
Industry will installed closed system for proposed products, so there will be very less chances of any fugitive emission
All the raw material and products will be handled as per MSDS and SOP will be prepared for handling , storage and transportation
All necessary personal protective equipment will be provided to workers handling hazardous chemicals
3. Solid and Hazardous Waste
Manufacturing process Manufacturing process
Process wastes, residues
Distillation residue
ETO sludge
Unit will provided isolated storage area with covered top and RCC flooring for the storage of hazardous waste.
Unit will become member of TSDF site for disposing ETP sludge
Unit will install incineration system or become member of common incineration facility.
4. Noise and Vibration
Power generation D.G. Sets Process
Equipment Boiler
Noise generation
Low noise D.G. set with acoustic enclosures will be installed
Timely oiling, lubrication and preventive maintenance will be carried out for the machineries and equipment to reduce noise generation.
5. Occupational Safety and Health
Manufacturing activities Handling and VOC and All necessary PPE will be
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Activity Source of Pollution Type of Pollutant Environment Management
Plan/Mitigation Measures
storage of different hazardous chemicals, High Temperature and pressure
fugitive emissions
provided. Pre-employment and
periodical medical examinations will be carried
Workers and medical records will be maintained as per Gujarat Factories Rules (GFR).
Register (Form No. -37, GFR) for work place air quality monitoring will be maintained.
6. Disaster Management
Manufacturing Activity Natural Disaster
Emergency situation arising due to fire, explosion, sudden leakage of liquid/gas
Natural calamities like earthquake/ Flood
- All necessary disaster control measures will be implemented
Regular mock drill to be carried out
Fire fighting equipment and other safety appliances will kept ready for use during disaster/emergency situation including natural calamities like earthquake/flood.
7. Transportation Systems
Raw material and product transportation
Vehicular Exhaust
Emission of SPM, SOx, VOC, NOx.
Spillage of chemicals/substances
Proper parking places should be provided for the trucks and other vehicles to avoid any congestion or blocking of roads
Spillage of chemicals/substances on roads inside the plant may lead to accidents. Proper road safety signs both inside and outside the plant should be displayed for avoiding road accidents.
10.3 CLEANER PRODUCTION TECHNOLOGIES
A number of practices are implemented by the industry to reduce waste generation and material losses.
Typical practices include process optimization, production scheduling, materials tracking and inventory
control, special material handling and storage procedures, preventive maintenance programs, and waste
stream segregation. General practices to be adopted are listed below:
Waste Minimization Options For Pharmaceutical Facilities: Material Substitutions:
Aqueous-based cleaning solutions are also being used more frequently for equipment cleaning instead of
solvent-based solutions (U.S. EPA, 1991)
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Process Modifications:
Process modifications are alterations to or modernization of existing processes to reduce waste generation.
Process modifications can involve re-designing chemical transfer systems to reduce spillage and other material
losses. For example, in batch operations, each loading and unloading of the reactors and other equipment
increases the risk of chemical spills and solvent vapor releases. Batch operations often require more frequent
reactor clean outs using significant volumes of cleaning solution and solvents. With continuous operations, the
reactor is loaded once and solvents and reactants are fed into the reactor continually, thereby reducing the
risk of pollutant releases (US EPA, 1991).
Process changes that optimize reactions and raw material use can reduce waste and releases to the
environment (US EPA, 1995). Modifications as simple as careful monitoring of reaction parameters
(temperatures, pH, etc.) can dramatically improve manufacturing efficiency.
Good Operating Practices:
One of the easiest and most economical ways to achieve source reduction is to implement good operating
practices. Pharmaceutical companies already follow a list of Good Manufacturing Practices (GMP) guidelines
outlined by the FDA
Management Commitment:
Good operating practices start with on-site commitment and understanding of the need and methods for
pollution prevention, from top management levels to the plant floor. Without facility-wide efforts to reduce
pollution, source reduction may not be successful (US EPA, 1991).
Employee training:
An employee training program is essential to the success of a source reduction program. Employees should be
trained in safe handling of equipment, chemicals, and wastes. They should also be informed of any potentially
harmful health effects of the hazardous chemicals they handle. As well as being trained in proper operation of
equipment and chemical handling, employees should be trained in spill cleanup and methods for detecting
chemical releases (US EPA, 1991).
Maintenance programs:
Maintenance programs should target both preventive and corrective maintenance of equipment. This means
that equipment should be regularly checked and cleaned to insure its proper functioning, and damaged
equipment should be repaired quickly.
Inventory control:
The wide range of chemicals used in the pharmaceutical industry makes it essential to instigate an efficient
inventory tracking system, such as a “first-in, first-out” policy and chemicals must be properly labeled with
their name, date of purchase, and date of expiration. This helps to insure that older, un-used chemicals do not
have to be needlessly discarded (US EPA, 1991).
Spill prevention and storage:
Spill and leak prevention are critical to pollution prevention. Tightly secured storage tanks are a key to avoiding
spills. Containers should have good valves with tight stopping devices to avoid the spilling or dripping of
hazardous chemicals. Storage containers should have legible signs indicating the contents of the container,
health hazard warnings (where necessary), and spill cleanup procedures in case of emergencies. Large drums
can be raised above the ground to avoid corrosion. An organized storage area facilitates fast and easy removal
of chemicals, as well as reduction and cleanup of spills (U.S. EPA, 1991).
M/s Jayveer Pharmachem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-10: Environmental Management Plan
10.5
Environmental Impact Assessment Report
Recycling, Recovery, and Reuse & Solvent Minimization:
Recycling and recovery provides the pharmaceutical industry a great opportunity to reduce the volume and
toxicity of spent solvents. Solvents are used for a wide range of applications, from synthesis, extraction, and
purification of active ingredients to cleaning process equipment. The types of solvent recovery employed
include distillation, evaporation, decantation, centrifugation, and filtration. However, limitations exist with
both on and off-site recycling and recovery since several types of solvents (including water), reactants, and
other contaminants may be present. These materials must be extracted to allow the solvent to be reused
either in a pharmaceutical process or in another process. Additionally, special techniques and equipment must
be used to break azeotropes formed during the chemical reactions.
10.4 RAIN WATER HARVESTING
Rainwater Harvesting is generally putting back rainwater in to the underground formation, where it will be
stored in underground reservoirs (Aquifer) so that we can draw it whenever we need it.
Need for Rainwater Harvesting
To reduce ground water pollution
To augment the ground water storage and decline of water level
To improve the quality of ground water
To reduce the soil erosion
The harvested rain water can be used for flushing, washing, gardening, irrigation, fire fighting, etc. Rain water
is the purest form for water available to us.
Advantages of Rainwater Harvesting
Provides self sufficiency at least reduces load on water supply
Reduces the cost of pumping of ground water as it raises ground water table
Improves quality of ground water through dilution when recharge to ground water
Reduces soil erosion in alluvium area
Rainwater harvesting systems are simple which can be adopted by individuals.
Unit proposes to manufacture activate pharmaceutical ingredients which will require some hazardous
chemicals as raw material. Due to handling and storage of such chemicals, unit is planning to store rain water
and use the same for activities like washing, cooling, etc. Calculation of rain water to be harvested based on
yearly rainfall and runoff is given in Table 10.2.
Table 10.2: Details of Rain Water Harvesting
Particular Details
Roof top area Gardening area Road area Open area
Annual rainfall (mm) 709
No. of rainy days per year 30
Catchment area available (sq.mt.) 3232 5342 3130 3939
Coefficient of runoff 0.7 0.5 0.6 0.2
Area wise volume of rain water can be
harvested (Kilo Liter/year) 2262.4 2671 1878 787.2
Total volume of rain water can be
harvested (KL/year) 7598.6
Average volume of rain water can be
harvested (KL/day) during 30 rainy days 253
M/s Jayveer Pharmachem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-10: Environmental Management Plan
10.6
Environmental Impact Assessment Report
Particular Details
Roof top area Gardening area Road area Open area
Volume of storage tank to be provided
by unit for rain water storage (KL) 100
Total Fresh water requirement by unit
(KL/year) 7150
Unit will provide rain water storage tank of about 100 Kilo Liter and stored water will be used for cooling,
washing, gardening etc. as per requirement.
10.5 GREENBELT DEVELOPMENT
The main objective of the green belt is to provide a barrier between the plant and the surrounding areas. The
green belt helps to check soil erosion, make the eco-system more sustainable, make the climate more
conductive and restore water balance. The green belt helps to capture the fugitive emissions and to attenuate
the noise generated in the plant apart from improving the aesthetics of the plant site.
Out of total plant area 15653.00 sq.mt, unit will develop greenbelt in 5342 sq.mt. (34.0%) area. The tolerant
species with diversity will be planted which will help in suppression of fugitive dust, attenuate noise levels and
provide aesthetic background. The green belt development program will go simultaneously in phased manner
along with the civil activities. Details of the proposed plant species are given in the Table 5.3.
Table 10.3: Details of Plant Species in Greenbelt
Common Name of Trees/Plants Scientific Name Number of Species
Neem / Limbado Azadirachta indica 150
Gulmohar Delonix regia 50
Asopalav Polyalthia longifolia (Sonn.) Thw. 80
Kesudo, Khakharo Butea monosperma (Lam.) Taub. 50
Pili karan Thevetia peruviana 10
Lal Karen Nerium indicum 10
Tulsi Ocimum sanctum 10
Lawn -- --
Total Species 360
Proposed Five Years Program for Greenbelt Development
Plantation details 1st
Year 2nd
Year 3rd
Year 4th
Year 5th
Year Total
No. of plants 90 83 65 65 57 360
Yearly %age 25% 23% 18% 18% 16% 100%
10.6 BUDGET FOR ENVIRONMENT PROTECTION
A capital investment towards the environmental protection, control & mitigation measures is about Rs. 119 Lac for the proposed project. The unit keeps provision for adequate funds aside to meet with regular expenses for the environmental control measures. Recurring cost for environmental management for the existing as well as proposed project. Unit will regularly and efficiently operate environmental management systems and keep provision for fund for meeting expenses for the same. Estimated recurring cost for environmental management is given in Table 10.4.
M/s Jayveer Pharmachem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. Associates, Ahmedabad, Gujarat
Chapter-10: Environmental Management Plan
10.7
Environmental Impact Assessment Report
Table 10.4: Recurring Cost for Environmental Management
Particulars
Capital Cost
(Rs. In Lac /
Annum)
Recurring Cost
(Rs. In Lac /
Annum)
Remark
Air Pollution Control 60 15 Cost of scrubbers, Bag filters, stack
installation, VOC control system
attached to reactors
Water Pollution Control 120 50 Primary treatment at site and
disposal at Common Spray Dryer,
M/s Chhatral Environmental
Management System Pvt. Ltd.
CEMSPL.
Noise pollution 2 0.5 As per the requirement, equipment
maintenance
Hazardous / solid waste
management
20 11 Disposal at CHWIF/TSDF site and
Membership
Green Belt Development 2 0.5 Tree Plantation and maintenance
charges
Occupational Health & Safety 4 0.5 Cost of required PPE, First-Aid,
Antidotes, Medical Check-up
Statutory Compliance and
miscellaneous
2 0.5 -
Total 210 78
M/s Jayveer Pharmachem Survey No. 1187 & 1184, Village: Basana,
Taluka: Visnagar, District: Mehsana 384001
T. R. ASSOCIATES,
AHMEDABAD, GUJARAT CHAPTER-2: PROJECT DESCRIPTION
11.1
ENVIRONMENTAL IMPACT ASSESSMENT REPORT
`CHAPTER -11 DISCLOSURE OF CONSULTANTS
11.1 Declaration for Involvement in EIA Study
Project Details
Name & address
M/s JayVeer Pharma Chem
Survey No. 1187 & 1184, Becharpura-Chitrodipura Road,
Village: Basana, Taluka: Visnagar, District: Mehsana
384001, Gujarat
Status Proposed project
Type Bulk Drug manufacturing
Category as per EIA Notification 5(f) ‘B’
NABET sector 21
EIA Consultant Details
Name & address
T. R. Associates
C-605/A, Ganesh Meridian, Opp. Kargil Petrol Pump, S.G.
Highway, Ahmedabad, Gujarat.
Contact No.: 98253 71099
trassociates@ymail.com, adm.trasociastes@gmail.com
Status
NABET Accredited Environmental Consultants
Valid up to 17/03/2019
Certificate No.: NABET/EIA/1619/RA 033
Details of Laboratory engaged in EIA Study
Name & address
Aavanira Biotech (P) Ltd.
Kinetic Innovation Park, D-1 Block, Plot No. 18/1 Part,
MIDC Chinchwad, Pune, Maharashtra.
aavanira.bio@gmail.com
Status NABL Accredited vides Certificate No. T-3189 dated 14-
11-2014 valid upto 13-11-2018
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