EXECUTIVE SUMMARY OF DRAFT EIA REPORT Pharma... · 2016-11-17 · Executive Summary Emmennar Pharma Pvt. Ltd., Unit – III. Prepared By Rightsource Industrial Solutions Pvt. Ltd

EXECUTIVE SUMMARY OF

DRAFT EIA REPORT OF

Emmennar Pharma Pvt. Ltd., Unit – III. For

Modifying of Existing Chemicals Manufacturing

unit to Bulk Drug and Intermediates Manufacturing Unit

AT

Survey Nos: 334 & 335, Turkalkhanapur village,

Hatnoora Mandal, Medak (Dt), Telangana State.

PREPARED BY

Rightsource Industrial Solutions Pvt. Ltd Plot No: 203, H.No:5-36/203, Prashanthi Nagar,

IDA, Kukatpally, Hyderabad – 500072.

Ph: 040-65873137, 23070602, 23075699, 40126589.

Fax: 040-23070602. Mail: [email protected]

Executive Summary Emmennar Pharma Pvt. Ltd., Unit – III.

Prepared By Rightsource Industrial Solutions Pvt. Ltd. Page 1

1. INTRODUCTION Emmennar Pharma Pvt. Ltd. Unit - III, is an established Chemical manufacturing

unit at Survey Nos: 334 & 335, Turkalkhanapur Village, Hatnoora Mandal, Medak

District, Telangana State, in an area of 15.24 Acres (61671.00 SQM).

The company wishes to modify their chemical manufacturing facility to Bulk Drug &

Intermediates manufacturing facility in existing plant area. The company proposes to

invest an additional amount of Rs. 911.33 Lakhs towards its modification and

pollution control equipment.

The Project proposal is to obtain Environmental Clearance from the Ministry of

Environment, Forests and Climate Change (MoEF&CC) and Consent Orders from

SPCB to manufacture proposed products (given in Table-2) with a total production

capacity of 1350.00 MT/Month. Draft EIA report is prepared considering the Terms

of Reference (ToR) issued by MoEF&CC vide F. No. J-11011/23/2014 - IA II (I)

Dated 23rd July 2014. As per Issued TOR - EIA Study was carried out with necessary

Environmental studies & Monitoring. The Environmental monitoring and analysis

were carried out by Savanth Envitech Pvt Ltd, (Having NABL Accreditation and

MoEF & CC Registration) during the period of October 2014 – December 2014 and

Draft EIA Report was prepared and submitting for Public Consultation.

1.1. PROJECT DESCRIPTION The salient features of the unit are furnished below.

TABLE-1: SALIENT FEATURES OF THE PROJECT

Particular Details Name of the project Emmennar Pharma Pvt. Ltd. Unit - III

Location of the project Survey Nos: 334 & 335, Turkalkhanapur Village, Hatnoora Mandal, Medak District, Telangana State.

Latitude & Longitude Latitude : 17041’02.76’’ North Longitude: 78011’ 49.61’’ East

Land acquired for the plant 15.24 Acres (61671 SQM)

Present Land use of the project site Existing Industrial Land

Nearest Habitation Turkalkhanapur - 1.90 KMs (W)

Nearest Town Hatnoora - 6.5 KMs (NNW)

Major urban Settlements Hyderabad - 20 KMs (SSE) Nearest Highway

State Highway SH-17 - (Sangareddy - Narsapur) – 200 Mts (E)



Nearest Railway station Nearest Airport

National Highway NH-9 - (Mumbai - Hyderabad) –13 KMs (NNW) Lingampally Railway Station – 25 KMs (SSE) Rajiv Gandhi International Airport (Shamshabad) - 75 KMs (SE)

Major Industries near the plant site

Aurobindo Pharma Ltd Arch Pharma Ltd. Restile ceramics Ltd Syrex Pharmaceuticals Pvt. Ltd. Covalent Laboratories Pvt. Ltd, Unit -I Hetero Drugs

Water Bodies with in 10 KMs radius

Bhima Cheruvu - 2 KMs (WSW) Mamidi Cheruvu - 2.2 KMs (SE) Manjira River - 4.74 KMs (WNW) Chinthala Cheruvu - 5.2 KMs (NW) Nakka Vagu - 5.5 KMs (SW) Kamuni Cheruvu - 7.5 KMs (S) Chowdary Cheruvu - 9.6 KMs (WSW)

Reserved Forests with in 10 KMs radius

Narsapur RF - 8.7 KMs(ENE)

Naguwaram RF - 8.5KMs (ESE)

2.0 PROCESS DESCRIPTION The manufacturing process of Bulk Drug & Intermediates consists of chemical

synthesis extending to stages of processing involving different types of chemical

reactions. Total production capacity of Existing is 1350.0 TPM of Chemicals and the

present proposal will be 1350 TPM of Bulk drug and Intermediates (Given in Table -

2 & 3). The unit will take adequate control measures for storage and handling of Raw

materials, solvents and cylinders with in factory premises.

TABLE- 2: EXISTING PRODUCTS AND QUANTITIES

S. No Product Name Quantity In MT/Day

Quantity In MT/Month

1 Weak Nitric acid (58%) on 100% basis 25 750

2 Concentrated Nitric acid (98%) on 100% basis 20 600

Total 45.00 1350.0



TABLE- 3: PROPOSED PRODUCTS AND QUANTITIES AFTER EXPANSION

S. No Product Name CAS Number

Therapeutic Category /

Application

Quantity In

MT/Month

Quantity In

MT/Day

1 Meta chloro nitro benzene 121-73-3 Drug Intermediate 300.00 10.00

2 Meta chloro anisole 845-89-8 Drug Intermediate 240.00 8.00

3 Diethyl-D(-) Tartarate 13811-71-7 Resoluting Agent 60.00 2.00

4 Triphenyl phosphine 603-35-0 Group Protecting

agent 90.00 3.00

5 Metformin hydrochloride 657-24-9 Hypoglycemic 450.00 15.00

6 Butaphosphan 17316-67-5 Phosphorous Supplement 120.00 4.00

7 Ciprofloxacin Hydrochloride 86483-48-9 Anti Bacterial 90.00 3.00

Total 1350.00 45.00

2.1 RESOURCE REQUIREMENT & INFRASTRUCTURE FACILITIES A) Land Use Details:

Emmennar Pharma Pvt. Ltd, Unit - III is an established facility in an area of 15.24

Acres (61671.00 SQM), and the same land is sufficient for its expansion and there is

no requirement of additional Land and the land usage details are given in Table 3.

TABLE 4: LAND USE DETAILS

S. No Description Area (SQM) % 1. Building Area 41000.00 66.50 2. Roads & Open Area 318.00 0.50 3. Green Belt Area 20353.00 33.0

Total Area 61671.00 100.0

33% of Land Allotted For Green Belt. B) Existing & Proposed Water Consumption Details The existing water consumption is 136.0 KLD, details are given below table.



TABLE- 5: EXISTING WATER CONSUMPTION DETAILS

S. No Purpose Quantity In KLD

1 Process 18.0 2 DM water 20.0 3 Boiler feed 15.0 4 Industrial cooling 63.0 5 Gardening 10.0 6 Domestic 10.0

Total 136.0

The Total water consumption for the proposed project is 195.5 KLD. Water

consumption details are given in below Table. No.6. Water requirement will be met

through Ground Water.

TABLE- 6: PROPOSED WATER CONSUMPTION DETAILS AFTER EXPANSION

S. No Purpose Water

Requirement in KLD

1 Process 70.00 2 Washings 4.00 3 Boiler water Make up 47.00 4 Cooling Towers water Make up 56.00 5 DM Plant 3.00 6 Scrubbing system 1.00 7 Domestic usage 4.5 8 Gardening 10.00 Total 195.5

Out of Total Water consumption of 195.5 KLD an amount of 53 KLD of water

will be recovered by the ZLD system and reused, Hence, Total fresh water

requirement is 142.5 KLD and will be met from Ground Water.

C) Energy Requirement

Power requirement of proposed expansion project will be made available through

Telangana State Southern Power Distribution Corporation Limited [TSSPDCL]. Total

power requirement of proposed plant shall be 1000 KVA.



D) Utilities:

For generation of Steam, the unit is having a 1.5 TPH Coal Fired boiler, existing kept

as standby. In addition to this, the unit is proposing to install another 8.0 TPH Coal

Fired Boiler for its additional steam requirements .The coal requirement will be met

from government allocation or from local authorized sources.

Presently the unit is having 1000 KVA & 250 KVA DG sets for usage during the

power failures. These DG sets are sufficient even for the proposed activity. The

emission details are presented in bellow table No.7, 8 & 9.

TABLE- 7: DETAILS OF UTILITIES FOR EXISTING & PROPOSED

S. No Description Capacity Existing Proposed

after Expansion Dropped Continued

1

Coal fired boilers

1.5TPH (Stand By) - Continued -

0.6 TPH waste Heat recovery Boiler

Dropped - -

8.0TPH - Proposed

2

DG Sets

1 X 1000 KVA - Continued - 1 X 250 KVA - Continued -

3 Cooling Towers

1X500 TR - Continued - 1X400 TR - Continued -

4 Electricity supply from TSSPDCL.

250 KVA - Continued

1000 KVA - - Proposed

Fuel

5 Coal Proposed - 20.0 TPD (8.0 TPH Boiler ) Stand By - 3.75 TPD (1.5 TPH Boiler)

6 Diesel 200 Liters/Day

TABLE- 8: EMISSION CHARACTERISTIC DETAILS OF PROPOSED BOILER

AFTER EXPANSION

Particulars Units 8.0 TPH

Coal fired Boiler (Proposed)

Type of Fuel -- Indian Coal Coal Consumption TPD 20.0 Ash Content % 47 Sulphur Content % 0.8 Nitrogen Content % 1.07



Particulars Units 8.0 TPH

Coal fired Boiler (Proposed)

No. of Stacks No 1.0 Height of Stack m 32 Diameter of Stack m 0.7 Temperature of Flue Gas oC 120 Velocity of Flue Gas m/s 9.0 Particulate Matter at outlet of Bag filter (Based on 115 mg/Nm3 at outlet)

gm/sec 0.32

Sulphur dioxide emission gm/sec 1.85 Oxides of Nitrogen emission gm/sec 2.48

Pollution control Equipment -

Cyclone separator followed by suitable pack

of Bag filters

Existing 1.5 TPH coal fired boiler is kept as standby.

TABLE- 9: STACK EMISSION DETAILS OF EXISTING DG SETS

Capacity In KVA

Emission of SPM

in mg/Nm3

Emission Of SO2 in mg/Nm3

Emission of NOx in mg/Nm3

Stack dia. In m

Flue Gas Temp. in OC

Stack Height in m

Flue gas Velocity In m/sec.

250 KVA (Existing) 65.0 110.0 135.0 0.30 290 8 18.50

1000KVA (Existing) 160.0 380.0 470.0 0.30 290 10 46.40

E) Pollution Control Equipment: i) Cyclone separator: The denser particles which are carried away by boiler flue

gases will get separated in the cyclone separator and collected in the bottom of the

cyclone separator at a definite interval.

ii) Bag Filter: The boiler flue gases from cyclone separator enter into pack of bag

filters, where particulate matter will be separated leaving as cake on bags surface.

They are cleared by shaking or vibrating by pulse jet causing the filter cake to be

loosened and to fall in the Hopper.

iii) Boiler Stack: The adequate stack height (30-32 mts) will be provided for

pollutants (SO2, NOx, PM & CO) dispersed in a very large area so that ground level

concentration is within CPCB permissible limits.



iv) Scrubbers: Two scrubbers of 2-Stage are proposed to scrub the process

emissions, the packing media in the scrubber is 25mm poly propylene rings.

3. BASELINE ENVIRONMENTAL STATUS

3.1 Study Area Included In Environmental Setting

Studies were carried out in about 10 km radius area from the site with respect to

meteorology, flora, fauna, land and socio-economies of the area. Further sampling

and analysis of air quality, water quality, noise level and soil quality were carried out.

The air quality, water quality, noise level and soil quality in the study area is

evaluated based on this physical sampling and analysis.

The base line data were monitored during the study period of October 2014 –

December 2014. The study team conducted site surveys and field experiments for

gathering the information on air quality, water quality, noise quality and soil quality.

3.2 CLIMATE OF THE STUDY AREA

A. Temperature:

During the study period the minimum and maximum temperatures were recorded as

18.0 °C and 36.2°C respectively.

B. Relative Humidity:

During study period at project site during study period, the minimum relative humidity

was recorded as 40.3 % and maximum as 77.6 %.

C. Rainfall

No rainfall during the study period at project site. The normal annual rainfall in the

District is 932.70 mm (Source: Directorate of Economics and Statistics).

D. Wind Pattern during Study Period

The analysis of the average wind pattern shows predominant winds from SE, NE,

ESE and ENE with wind frequencies of 16.4, 8.5, 8.2 and 6.9 % respectively. The

calm conditions were prevailed for 25.2 % of the total time. Average wind speed 2.45

m/s.



3.3 SAMPLING LOCATION DETAILS

Total eight locations were selected for Base line status. Air, Water & Noise results

are presented in Table 7, 8 & 9 respectively.

3.4 AMBIENT AIR QUALITY

The ambient air monitoring was carried out for 24 hours a day, twice a week for 12

week per location in the study area. Ambient Air Quality Monitoring (AAQM) was

carried out at eight locations during period of October 2014 – December 2014.

Particulate Matter (PM10): Maximum value of 67.40 μg/ m3 was recorded at Bodupatla.

Particulate Matter (PM2.5): Maximum value of 23.92 μg/ m3 was recorded at Kasal.

Sulphur Dioxide (SO2): Maximum value of Sulfur dioxide of 13.91 μg/ m3

obtained near the sampling location of Kasal.

Oxides of Nitrogen (NOx): A maximum value of 19.49 μg/ m3 was prevailing

at the time of sampling at Hatnoor sampling station.

Carbon Monoxides (CO): Maximum value of Carbon Monoxide of 0.46 mg/

m3 obtained near the sampling location of Daulatabad.

Volatile Organic Compounds (VOCs)

Volatile Organic Compounds (VOCs) concentration in study area was found to be Below Detectable Limit of I ppm

Benzene

Benzene concentration in study area was found to be Below Detectable Limit

of 5 ppm

Poly Aromatic Hydro carbons (PAH)

PAH concentration in study area was found to be Below Detectable Limit of I

ppm



TABLE- 10: THE MAXIMUM, MINIMUM & 98TH PERCENTILE VALUES FOR ALL THE

SAMPLING LOCATIONS

Code Name of Sampling Location

PM 10(µg/M3) PM 2.5(µg/M3) SO2(µg/M3) NOX(µg/M3) CO (mg/M3)

Min Max 98 th Min Max 98 th Min Max 98 th Min Max 98 th Min Max 98 th A1 Plant Site 51.14 64.21 64.17 16.81 22.55 22.54 9.31 12.65 12.43 11.54 16.97 16.77 0.12 0.51 0.44 A2 Turkhalkhanpur 49.31 63.53 63.21 17.42 21.97 21.82 9.67 13.10 12.98 12.81 18.11 17.89 0.12 0.29 0.29 A3 Chintalcheruvu 50.32 62.59 61.98 15.89 20.30 19.98 9.21 13.51 13.20 14.25 18.72 18.61 0.12 0.41 0.37 A4 Gandlamasnur 49.34 61.27 60.80 19.32 22.52 22.35 9.78 12.83 12.83 11.97 16.83 16.83 0.12 0.36 0.35 A5 Bodupatla 52.80 67.53 67.40 18.63 23.54 23.23 9.70 12.90 12.87 11.49 18.47 18.12 0.12 0.35 0.35 A6 Kasal 51.55 66.55 66.22 18.92 24.84 23.92 10.20 14.50 13.91 11.62 17.28 16.96 0.12 0.36 0.36 A7 Hatnura 40.34 65.54 64.68 15.35 22.65 22.19 8.40 12.58 11.69 12.84 19.67 19.49 0.12 0.54 0.45 A8 Daulatabad 45.48 65.63 65.32 15.36 22.69 21.69 7.94 10.99 10.90 14.52 18.62 18.25 0.12 0.47 0.46

CPCB Standards’ 100.00 60.00 80.00 80.00 2.00



3.5 WATER QUALITY

Water sampling and subsequent analysis was carried out to determine both the

groundwater and surface water quality of the study area.

Ground water samples are collected at 8 locations and surface water samples was

collected at 8 locations in the study area. These samples were analyzed for physical

and chemical parameters to ascertain the Baseline status in the existing surface

water and ground water bodies.

TABLE- 8: WATER ANALYSIS RESULTS

S. No Parameters Ground water Surface water

Min Max Min Max

1 pH 6.84 8.74 7.61 9.33

2 Total dissolved solids (mg/l) 432.17 1155.57 318.05 930.8

3 Total hardness (mg/l) 280.00 480.00 290.00 560.00 4 Chlorides (mg/l) 90.00 519.80 44.90 249.90 5 Fluoride (mg/l) <0.5 <0.5 0.55 0.76 6 Sulphates (mg/l) 26.54 153.40 22.5 78.6

3.6 NOISE ENVIRONMENT

Noise level monitoring was carried out at eight locations during the period of

October 2014 – December 2014.

During monitoring period, noise levels varied between 61.54 dB (A) to 65.81 dB (A)

during day time in the study area respectively.

Noise levels varied between 51.28 dB (A) to 55.74 dB (A) during night time in the

study area respectively.

The noise level varied at the same place at different times due to fluctuations in

traffic movements as well as commercial and domestic activities going on in the

study area but it was under the permissible limit as prescribed by CPCB.



TABLE- 9: NOISE LEVELS OF THE STUDY AREA

S. No Name of the place

Day Time In Leq

Night Time In Leq

CPCB NORMS

(Day time)

CPCB NORMS

(Night time) 1. Plant Site 65.81 55.74

75dB (A) 70dB (A)

2. Turkhalkhanapur 61.58 51.28 3. Chintala cheruvu 64.75 54.80 4. Gandlamchanur 61.54 52.35 5. Bodupatla 63.32 55.28 6. Korpol 63.99 55.26 7. Hatnoora 62.40 54.84 8. Daulathabad 65.07 55.47

3.7 SOIL ENVIRONMENT

On data obtained, the soil quality at around the site is appropriate and normal in

terms of soil contaminants.

3.8 LAND USE/ LAND COVER OF THE STUDY AREA

Land use / Land cover map is prepared by visual interpretation of high-resolution

satellite data (Satellite Imagery: 14-02-2014) and with the help of Survey of India

Topographic maps on 1: 50,000 scale. Two seasons’ data (Rabi year 2014) is used

for the delineation of different units. The units are confirmed by the ground truth/field

visits.

TABLE-10: LAND USE / LAND COVER OF THE STUDY AREA

S. No LANDUSE Area in SQM

Area in Percentage (%)

1 Built- Up Land 24.120 7.7 2 Water bodies 20.574 6.6 3 Crop Land 208.390 66.3 4 Forest 12.246 3.9 5 Wastelands 48.670 15.5

Total 314 100

3.9 DEMOGRAPHIC AND SOCIO-ECONOMIC PROFILE

This Detailed Study of the Base-Line Data of Socio-Economic Aspects – including,

Population, Gender ratio, Rural & Semi-Urban Demographic distribution, Literacy

Rate, Education, Medical & Health facilities, Employment rate and other



Developmental Indices of 8 Villages, falling within 10 Kms of the Project-Influence

area and especially, that of ‘Turkalkhanapur’ Village, where the project site is located

– are obtained from Primary Sources.

The total population of the study area is 25,949 in which 51.67% with

male population and 48.33% with female population while, the Demographic

distribution is 73.13% & 26.87% for Rural & Semi-Urban areas, respectively.

The Average Literacy rate in the study areas is 61.98% while the rate

of Illiteracy is at an alarmingly high i.e, 51.79% for Women and 25.15% for

Men Populations.

The total population of the study area is 25,949 out of which 11,684 are

employed, 13,276 are Other Non-Working Population while 989 are

Unemployed or still Employable.

All the Villages, in the study area, are electrified – both for Domestic Purpose

and common facilities like, Street Lights, Public Water Pumping, etc. and also

are provided with Domestic Water.

4.0 IDENTIFICATION, PREDICTION & MITIGATION MEASURES

4.1 Expected Air Environment (Expected Process Emissions Details):

The Predicted Process emission is CO2, which is liberated from manufacturing

process of proposed products.

TABLE-15: EXPECTED PROCESS EMISSION DETAILS

S. No Name of the Gas Quantity In Kg/Day Treatment Method Non- Polluting Process Emission Details

1 Carbon dioxide 981.56 Dispersed into atmosphere



4.2 PROPOSED PROCESS EMISSION CONTROL SYSTEM Scrubbers with 300 mm (Diameter) X 3 meters (Height) & 300mm (Diameter) X 3

meters (Height) capacities will be installed for control of process emissions. The

Schematic diagram of emission control system is given below.

FIGURE-1: SCHEMATIC DIAGRAM OF PROPOSED EMISSION CONTROL SYSTEM

The Particulate matter generated from 8.0 TPH Boiler will be controlled by using

cyclone separator followed by bag filters. The sulphur dioxide (SO2) and oxides of

nitrogen (NOX) from boiler will be dispersed in to atmosphere by providing adequate

stack height of 32 meters for effective dispersion and dilution.

The predicted ground level concentrations when added to Baseline scenario, the

overall scenario levels of PM, SO2 and NOX are well within the permissible limits as

specified by CPCB.

4.3 Existing & Proposed Effluent Water Details

The existing waste water generation is 22.0 KLD, proposed waste water generation

will be 97.00 KLD which is from process, floor & reactor washes, cooling tower blow

down, boiler blow down, scrubber, DM plant and domestic usage. The effluent

generation and its HTDS & LTDS effluent details are given below.



TABLE-16: EXISTING EFFLUENT GENERATION DETAILS

S. No Outlet Description Max Daily Discharge Point of Discharge

1

Trade Effluents - 12.0 KLD + Domestic effluents after septic tank - 10.0 KLD*

22.0 KLD

Forced evaporation in the FE system.

The condensate first forerun to distillate for recovery of solvent at onsite & to use

The secondary condensate to re-use for makeup.

Total 22.0 KLD

TABLE-17: PROPOSED EFFLUENT GENERATION DETAILS AFTER EXPANSION

S. No Purpose Effluent

Generation In KLD

1 Process 68.00 2 Washings 4.00 3 Boiler Blow down 7.00 4 Cooling towers Blow down 10.00 5 Scrubbing system 1.00 6 DM Plant regeneration 3.00 7 Domestic 4.00

Total 97.0

TABLE-18: PROPOSED HTDS & LTDS EFFLUENT DETAILS AFTER EXPANSION

Unit HTDS KLD

LTDS KLD

Effluent Generation

in KLD Treatment Method

Process 36.0 32.0 68.0 HTDS Effluent after neutralization, filtration sent to MEE. LTDS effluents along with MEE condensate will be sent to Biological treatment and finally to RO system RO Rejects to MEE system and RO permeate to reuse; MEE residue to ATFD for drying.

Washings 0.00 4.00 4.00 Boiler Blow Down 7.00 0.00 7.00 Cooling towers Blow Down 0.00 10.00 10.00

Scrubber System 1.00 0.00 1.00

DM Plant 3.00 0.00 3.00

Domestic 0.00 4.00 4.00 Septic tank followed by soak pit Total 47.0 50.0 97.0



Effluent Treatment / Disposal: Zero Liquid Discharge (ZLD) concept consisting of

steam stripper (5000 litrs/hr), MEE system (5000 ltrs/hr), ATFD (875 ltrs/hr),

Biological Treatment and RO (5000 ltrs/hr) will be installed to treat the effluents

generated from plant and to reuse the treated water.

The MEE System with 100 KLD Capacity & RO system with 100 KLD Capacity will

be installed for treatment of effluents generated from plant operations.

The details of MEE system given in Draft EIA Report Chapter-10.

4.4 Noise Environment

The main sources of noise pollution in the plant are Boilers, Reactors, DG Sets,

compressors and other Noise generating units. Vehicular movements during

operation phase for loading / unloading of raw materials and finished products and

transporting activity may also increases the noise levels.

All the noise generating equipments like motor’s, gear boxes and compressors are

regularly maintained with lubricating material to avoid noise generation. All the DG

sets are providing with acoustic enclosures. A thick greenbelt will be developed

along the periphery of the plant boundaries to minimize the noise pollution from the

source.

4.5 Land Environment

The proposed plant activities are unlikely to alter the land-use pattern in the project

site. The unit will take adequate measures for storage, handling and disposal of

hazardous waste. Hence, there will be no significant adverse impact on land

environment.

4.6 Ecological Environment

Detailed flora and fauna studies were carried in the study area. As per baseline

studies, there are no endangered, threatened & protected plants and animal species

were recorded in the study area. Hence, no significant adverse impact is envisaged

on ecology.



4.7 Existing & Proposed Hazardous and Solid Waste Details

The Hazardous & Solid waste generated and disposal methods from existing and

proposed project are given below.

TABLE- 19: EXISTING HAZARDOUS & SOLID WASTE GENERATION AND

DISPOSAL

S. No Description Quantity of Hazardous

wastes Disposal Option

HAZARDOUS WASTES WITH DISPOSAL OPTION:

1 ETP sludge / FE salts

500 Kg/Day

TSDF; Dundigul, Rangareddy District for land filling after stabilization.

HAZARDOUS WASTES WITH RECYCLING OPTION: 1 Waste Oil 1200 Ltrs/year Authorized Agencies

2 Used lead acid battries 6 Nos/ 2 years

Return to dealer / manufacture on buy back basis

TABLE- 20: PROPOSED HAZARDOUS WASTE & SOLID WASTE GENERATION, DISPOSAL DETAILS AFTER EXPANSION

S. No Name of the Hazardous Waste

Quantity Kg/Day Disposal Method

1 Organic waste 3412.00 Sent to Cement Industries 2 Spent Carbon 198.00 Sent to Cement Industries 3 Solvent Distillation Residue 84.00 Sent to Cement Industries 4 Inorganic Waste 5016.00 Sent to TSDF 5 MEE Salts 6082.60 Sent to TSDF 6 ETP Sludge 50.00 Sent to TSDF

7 Used Oils 600

Litres / Annum

TSPCB Authorized Agencies for Reprocessing/Recycling

8 Detoxified Containers & Container Liners

500 Nos/ Month

After Detoxification sent back to suppliers/TSPCB Authorized Parties

9 Used Lead Acid Batteries 4 Nos / Annum

Send back to suppliers for buyback of New Batteries

Solid Waste Details 10 Ash from boiler 9400.00 Sent to Brick Manufacturers



4.8. Risk Assessment and Disaster Management Plan

The Risk assessment studies have been conducted for identification of hazards, to

calculate damage distances and to spell out risk mitigation measures. The details

are discussed in detail in Chapter – 7 of Draft EIA Report.

5.0 ENVIRONMENTAL MANAGEMENT PLAN 5.1 ENVIRONMENT MANAGEMENT PLAN FOR CONSTRUCTION PHASE Adequate and effective environment protection measures will be planned and

designed to minimize the impacts due to activities related to pre-construction

(preparatory phase) of the project, machinery installation and commissioning stages

and end with the induction of manpower and start up. The impacts identified during

the construction phase are mainly due to site preparation, foundation work, material

handling, and construction of buildings and installation of the machinery.

All possible care will be taken to reduce the noise levels due to construction activity.

Also, noise prone activities shall be restricted to the extent possible during night

particularly during the period of 10 PM to 6 AM in order to have minimum

environmental impact.

5.2 ENVIRONMENT MANAGEMENT PLAN FOR OPERATIONAL PHASE

A) Air Pollution Management

Gaseous emissions from reactions shall be scrubbed in a two stage scrubber

to control the gaseous emissions into the atmosphere.

Fugitive emissions will be reduced by providing vent condensers to the

storage tanks and all the reactors are will be provided with primary and

secondary condensers with cooling water and chilled brain circulation

respectively to avoid fugitive emissions and solvent losses which ensures

the recovery up to 95% and also controlled by closed operations and suitable

handling methods.

Adequate stack height of 32 meters will be provided to the proposed boiler for

effective dispersion of pollutants’ and stack monitoring facilities for the

periodic monitoring of the stack flue gases to verify the compliance of the

stipulated norms.

To prevent the particulate matter delivering from the boilers will be arrested by

providing Cyclone separator followed by Bag filters.



B) Water Pollution Management

The HTDS effluents will be collected and treated in steam stripper, MEE system &

ATFD. Condensate along with LTDS effluent will be sent to biological treatment

including R.O system for treatment and reuse. There will be no discharge of effluent

outside the plant premises. The unit will be treated as ZLD unit. Salts from ATFD

and sludge from the ETP will be sent to TSDF for land fill.

C) Noise Pollution Management

Extensive oiling, lubrication and preventive maintenance will be carried out for

the machineries and equipments to reduce noise generation.

Green Belt Development around plant boundaries and within plant in an area

of 5.0 Acres (20353.0 SQM).

A thick Greenbelt along the periphery of the compound wall arrests the Noise

pollution from the plant.

D) Hazardous & Solid Waste Management

The hazardous and solid wastes generated from the industry will be from solvents

distillation, Process, ETP, Boilers, MEE, discarded containers and bags which will

properly stored in a hazardous waste storage area with leachate collection system

and then transported and properly disposed.

The entire organic residues will be disposed to cement industries for incineration and

Inorganic residues sent to TSDF for secure land fill.

E) Green Belt The industry proposed to develop greenbelt of 5 to 10m width on all sides of the

industry in an area of 5.0 Acres (20353.0 SQM) from the total area of 15.24 Acres

(61671.0 SQM) of land, with an amount of Rs.6,00,000 /- for greenbelt. The amount

will be spent during the period of Three years. First year amount will be Rs.3,00,000

for plantation. Second year amount will be Rs.2,00,000/- for development of plants.

Third year amount will be Rs. 1,00,000/- for maintenance and development. A list of

plants suitable for greenbelt and to the local agro climatic conditions is given in the

Draft EIA report.

F) Solvent Recovery

The solvents like Diethyl ether, THF, Toluene, Methanol, n- Butanol, n- Propane,

Acetone, Ethyl Alcohol will be recovered up to 95% by using distillation and the

remaining 5% will be the loss.



5.3 ENVIRONMENT MANAGEMENT CELL Emmennar Pharma Pvt. Ltd., Unit – III will provide a dedicated Environmental

Management Cell with trained staff to look after the proper environmental

management of the proposed plant including operation & maintenance of all

facilities.

5.4 ENVIRONMENT MONITORING PROGRAM

Regular monitoring of environmental parameters is of immense importance to

assess the status of environment during project operation. The regular monitoring

will be carried out with the MoEF&CC Registration / NABL Accredited Laboratory.

6. PROPOSED ROOF WATER HARVESTING Rainwater harvesting is a mechanism involved in collecting, storing and using. A

rainwater harvesting system comprises various stages – flow of rainwater through

pipes or drains, filtration and storage in tanks for reuse or recharge. Roof top area

is considered for harvesting rainwater for this project and other areas are excluded

due to possibility of chemical contamination. Roof top rainwater harvesting is one

of the appropriate options for augmenting ground water recharge/ storage in urban

areas where natural recharge is considerably reduced due to increased urban

activities and not much land is available for implementing any other artificial

recharge measure.

FIGURE-2: PROPOSED ROOF WATER HARVESTING STRUCTURE



7. EMP BUDGET

The unit has proposed for 174.0 Lakhs as capital cost and 24.0 Lakhs as recurring

cost for environment pollution control measures.

TABLE- 21: PROPOSED BUDGETS FOR ENVIRONMENTAL MANAGEMENT PLAN [EMP] AFTER EXPANSION

S. No Particulars Proposed

Capital Cost (Rs. Lac)

Recurring Cost

(Rs. Lac)

1 Pollution Control Equipment (Scrubbers, Cyclone separator, Bag filter , Sampling port arrangements etc.,)

10.0 2.0

2 ZLD System (MEE , RO, necessary modification of ETP system)

150.0 16.0

3 Rain Water Harvesting (Roof top water collection pit and Roof top water towards the rain water harvesting pit)

6.0 0.0

4 Green Belt Development (Plantation and Maintenance) 5.0 1.0

5 Health & Safety (PPEs, Medical Surveillances Expenses etc.,) 3.0 2.0

6 Environmental Monitoring (Air, Water, Noise, VOCs, Boiler Stack flue gases, DG sets stack monitoring expenses etc.,)

0.0 3.0

Total 174.0 24.0

8.0 SOCIO-ECONOMIC DEVELOPMENT

It is predicted that socio-economic impact due to this project will positively increase

the chance of more employment opportunities for local peoples. There are no

Resettlement and Rehabilitation issues involved in this project. The project

infrastructures will be of use to people of the area. The revenue of the village will be

definitely increasing due to the project.

9.0 PROJECT BENEFITS

Proposed expansion project will result in considerable growth and up liftments of

local community in the nearby villages by providing the employment. The proposed

project will generate direct and indirect employment to the nearby villages and the

unavailable technical persons will be recruited from outside.



10.0 CONCLUSION

Emmennar Pharma Pvt. Ltd., Unit – III has committed to implement all the pollution

control measures to protect the surrounding environment – adapting Zero-Liquid-

Discharge System for all its Effluents, by controlling process emissions and Safe-

Disposal of all Solid Wastes – generated either as process wastes or packing

wastes.

The project can definitely improve the regional, state and national economy.

Industrial growth is an indication of all-round Socio-Economic Development – by

generating local Employment and Business Opportunities. The implementation of

this project will definitely improve the physical and social infrastructure of the

surrounding area.

Documents

EXECUTIVE SUMMARY OF DRAFT EIA REPORT Pharma... · 2016-11-17 · Executive Summary Emmennar Pharma Pvt. Ltd., Unit – III. Prepared By Rightsource Industrial Solutions Pvt. Ltd