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PRE-FEASIBILITY REPORT
BALAJI OVERSEAS LUDHIANA, PUNJAB 1 CPTL-EIA
PFR-01-RI 01-02-19
FOR
Manufacturing of Manufacturing of Manufacturing of Manufacturing of
FFFFORMALDEHYDEORMALDEHYDEORMALDEHYDEORMALDEHYDE (37%) (37%) (37%) (37%) ANDANDANDAND PF, MF & UF PF, MF & UF PF, MF & UF PF, MF & UF RESINRESINRESINRESIN
By
M/S M/S M/S M/S BALAJI OVERSEASBALAJI OVERSEASBALAJI OVERSEASBALAJI OVERSEAS VILLAGE HAMBRAN, NEAR MURTI AGRO FOOD,
HAMBRAN ROAD, LUDHIANA, PUNJAB
Prepared by CHANDIGARH POLLUTION TESTING
LABORATORY- EIA DIVISION
PRE-FEASIBILITY REPORT
(QCI/ NABET Certificate No: NABET/EIA/1619/IA 0012) Address: E- 126, Phase- VII, Industrial Area, Mohali, Punjab- 160055.
Contacts: 0172-4669295, 5090312 E-mail: [email protected] / [email protected] Website: www.cptl.co.in
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BALAJI OVERSEAS LUDHIANA, PUNJAB 2 CPTL-EIA
INDEX PFR :-
1.0 INTRODUCTION 7
2.0 THE PROMOTERS & NEED OF PROJECT 5
3.0 PROJECT SITE 6
4.0 PROJECT DESCRIPTION 11
Generals 11
Raw material & product details 11
Final Products 12
Water & Air Pollution 14
Process Description 15
5.0 DESCRIPTION OF THE ENVIRONMENT 22
6.0 ENVIRONMENT IMPACT & MANAGEMENT PLAN 26
7.0 SITE ANALYSIS 29
8.0 PROPOSED INFRASTRUCTURE 30
9.0 REHABILITATION AND RESETTLEMENT (R&R) PLAN 30
10.0 PROJECT SCHEDULE & COST ESTIMATES 31
11.0 ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS) 32
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LIST OF FIGURES
3.1 Key Plan 7
3.2 General Location Plan 8
3.3 Location map on goggle 9
3.4 Layout plan 10
5.1 Flow Chart of ETP 15
LIST OF TABLES
4.1 Raw material & Quantities 11
4.2 Product 12
4.3 Project site & Location 11
4.4 Water Consomption 14
4.5 Waste water Streams & generation 15
5.1 Primary data Description 22
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PRE-FEASIBILITY REPORT 1.0 INTRODUCTION
Earlier, the assessment of the projects was done on Technical feasibility reports and Cost-
Benefit-Ratio which mainly considered financial & technical resources. But no consideration
was given to the environment protection in this evaluation and these flaws became apparent
with continuous deterioration of environment. Thus in order to have more realistic evaluation,
and keeping in view the deteriorating conditions, another dimension was added which is now
called as “Environmental Impact Assessment” (E.I.A.). This forms an integral part of the
project and is taken into account while appraising the project at different stages. Thus in the
new comprehensive approach all considerations like, Technical, Financial & Environmental
are given due weightage.
M/s. BALAJI OVERSEAS is proposing to manufacturing Formaldehyde (37%) and PF, MF,
UF resin @ capacity 100 TPD and 100 TPD respectively at Village Hambran, Near Murti Agro
Foods, Hambran Road, Tehsil & District Ludhiana, Punjab. Methanol and water will be used
as Raw Material for Formaldehyde and Urea, Formaldehyde & caustic for UFR, which is
easily available from the local nearby markets.
As per EIA Notification dated 14th Sep, 2006, the proposed project falls under Category “B”,
Project or Activity 5(f), but since it is located outside the notified Industrial area, the
environmental clearance will be given by the Central Govt. MOEF&CC.
They have to submit Form-I along with Pre-Feasibility Report and other relevant documents
for getting Environmental Clearance for proposed project. This pre-feasibility report has,
therefore, been prepared by the consultants to assess the likely impact of the proposed unit on
various factors which may be affected with the implementation of the programme and to
suggest remedial/precautionary measures, if any.
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2.0 PROFILE OF THE COMPANY & PROMOTORS.
M/s Balaji Overseas is a partnership firm having registered office at #10, Rambagh, Agar
Nagar Enclave, Block-A, Ludhiana, Punjab. Company has fallowing partners:
Name and address of Partners
Sh. Subham Bansal
S/O Sh. Subhash Bansal
R/o 10, Rambagh, Agar Nagar Enclave,
Block-A, Ludhiana, Punjab
Sh. Subhash Bansal
S/O Sh. Brij Lal Bansal
R/o 10, Rambagh, Agar Nagar Enclave,
Block-A, Ludhiana, Punjab
Sh. Pawan Kumar
S/O Sh. Brij Lal
R/o Ward No. 04, Near Shivalik,
Model School, Bhucho Mandi,
District Bathinda Punjab
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3.0 PROJECT SITE
The Plant site is located at Village Hambran, Near Murti Agro Food, Hambran Road,
Ludhiana, Punjab. It lies near Long: 75040’25.77” to 75040’28.33”E & 75040’25.60” to
75040’28.27”E and Lat: 30054’54.41” to 30054’54.68”N & 30054’50.72” to 30054’51.69”N
North and is at an Altitude of about 238 m above mean sea level. It is well connected with
Ludhiana through well maintained metalled roads. It is about 18 K.M. from Ludhiana and
2KM from Hambran. The nearest rail head is Ludhiana, which is at a distance of about 2 km
from the site. Key Plan, Location Plan & Google Map of the unit is given in Fig 3.1, 3.2 & 3.3
respectively. Layout Plan of the unit is given in Fig 3.4.
BALAJI OVERSEAS LUDHIANA, PUNJAB
PUNJAB STATE IN INDIA MAP PROJECT SITE ON GOGGLE
PROJECT SITE
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FIGURE – 3.1 KEY – PLAN
INDIA MAP DISTRICT LUDHIANA IN PUNJAB MAP
PROJECT SITE ON GOGGLE LOCATION OF PROJECT SITE IN LUDHIANA MAP
PROJECT SITE
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DISTRICT LUDHIANA IN PUNJAB MAP
LOCATION OF PROJECT SITE IN LUDHIANA MAP
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FIGURE – 3.2 LOCATION – PLAN
BALAJI OVERSEAS LUDHIANA, PUNJAB
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FIGURE – 3.3 GOOGLE IMAGE
PROJECT SITE
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FIGURE – 3.4 LAYOUT PLAN
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4.0 PROJECT DESCRIPTIONS 4.1 GENERAL:
The plant is located at Village Hambran, Near Murti Agro Food, Hambran Road, Ludhiana,
Punjab. Proposed project site has been selected keeping in mind the easy availability of raw
materials. Other infrastructural facilities like Land, Water and Transportation &
Communication etc. are also well established & available at the selected location. No Protected
forest, Reserve forest, ecologically sensitive area, National Park, Biosphere Reserve & Bird
Sanctuary are found with-in 5 km radius of the project site. Salient features of the project is
given in table 4.3
4.2 RAW MATERIALS, PRODUCTS, WATER & QUANTITIES:
Raw materials used for proposed project are given in table 4.1. The details of production is given in table 4.2 1) RAW MATERIAL:
TABLE – 4.1 PRODUCT NAME OF RAW MATERIAL QUANTITY SOURCES
For Formaldehyde (37%)
Methanol (T/D) 45.0 Local market
Water (T/D) 130.0 Ground water
Melamine Formaldehyde
Melamine (T/D) 13.00 Local market
Formaldehyde (T/D) 30.00 Local market
Caustic (T/D) 0.22 Local market
Phenol Formaldehyde
Phenol (T/D) 7.50 Local market
Formaldehyde (T/D) 8.50 Local market
Caustic (T/D) 0.075 Local market
For Urea Formaldehyde
Urea (T/D) 13.00 Own Plant
Formaldehyde (T/D) 30.00 Local Market
Acetic Acid (T/D) 0.11 Local market
Caustic (T/D) 0.11 Local market
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2) PRODUCTS:
TABLE – 4.2
S. NO. NAME QUANTITY
1 Formaldehyde (37%) 100 TPD
2 Melamine Formaldehyde Resin 42.50 TPD
4 Phenol Formaldehyde Resin 15 TPD
5 Urea Formaldehyde Resin 42.50 TPD
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TABLE – 4.3 PROJECT SITE & LOCATION
S. No.
Particulars Details
A. LOCATION DETAILS
1. Location
A. Village Hambran
B. Tehsil Ludhiana
C. District Ludhiana
D. State Punjab
2. Latitude 30054’54.41” to 30054’54.68”N 30054’50.72” to 30054’51.69”N
3. Longitude 75040’25.77” to 75040’28.33”E 75040’25.60” to 75040’28.27”E
4. Topo-sheet No.
H43J9
5. Project Area 3135 M2
C. PRODUCTION CAPACITY Formaldehyde (37%)- -100.00TPD
Melamine Formaldehyde Resin - 042.50TPD Phenol Formaldehyde Resin -015.00TPD Urea Formaldehyde Resin -042.50TPD
D. ENVIRONMENTAL SETTINGS
5. Nearest Village Hambran
6. Nearest City Ludhiana City, approx. 17 km in east direction from the project site
7. National Highway/State Highway/ Express Highway
NH-95 (Ludhiana-Moga) is about 7km south-east direction from the project site.
8. Nearest Railway Station Ludhiana Railway Station, approx. 17 km in east direction.
9. Nearest Airport Ludhiana (Sahnewal) Airport approx. 28 km in east and Chandigarh Airport approx. 110 km in east direction from the project site.
10. National Parks/ Wild Life Sanctuaries/ Biosphere Reserves within 5 km radius
No, National Parks/ Wild Life Sanctuaries/ Biosphere Reserves within 5 km radius.
11. Reserved / Protected Forest within 5 km radius (Boundary to boundary distance)
No Reserved Forests exists within 5 km radius.
12. Nearest water bodies Sirhind canal is about 3km towards south side and Satluj river is about 7km in north
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side 13. Source of Water Ground water Corporation Limited)
14. Seismic Zone Seismic Zone – IV
D. COST DETAILS
15. Capital Cost of the project Rs. 04.00 Cr
16. Total cost for Environmental
Management Plan (EMP) Rs 0.15 Cr
3) WATER & AIR POLLUTION
WATER:-
The water requirement of the unit will be met from ground water through tube well. The daily
requirement of fresh water will be about 250 m3. The details of water consumption of fresh
water uses and generation will be given in TABLE 4.4
TABLE 4.4
S. No.
COMPONENT CONSUMPTION (KLD)
GENERATION (KLD)
DISPOSAL
1 Process 130 5 Sent to ETP for treatment
2 Boiler 25 3(Boiler Blow down) Sent to ETP for treatment
3 Cooling 70 3(Purge water) Sent to ETP for treatment
4 Domestic 15 12(Waste water) Sent to ETP for treatment
5 Washing 10 7(Trade effluent) Sent to ETP for treatment
Waste Water: 30KLD of waste water from the project will be taken to E.T.P. through
underground delivery system and treated to tertiary level. Treated water will be partly used for
tree plantation, and the rest will be again reuse for cooling purpose. There will be no discharge
of waste water from the project and it will be a zero discharge industry. The stream wise
quality characteristics of waste water will be given in TABLE 4.5 Schematic Flow chart of
ETP is given in FIGURE 4.1
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TABLE 4.5
WASTE WATER STREAMS & GENERATION PARAMETERS UNITS PROCESS DOMESTIC/W
ASHING STEAM BOILER
RO COOLING WATER
COMPOSITE TOTAL/ STANDARDS
QUANTITY KL/DAY 5 19 3 0.5 3 25 25 pH - 3.5-5.0 6.5-7.5 6.0-6.8 7.0-7.5 6.5-7.0 6.5-7.5 6.0-8.5 TSS MG/L 50-80 250-400 30-50 20-40 60-90 100-200 <2100 COD MG/L 6500-10000 500-750 50-70 30-50 70-100 2500-500 <250 TDS MG/L 8000-9500 250-400 2500-4500 1000-
2000 1500-2500 1500-2000 <2100
FIGURE 4.1 FLOW CHART OF ETP
AIR POLLUTION: The flue gas emission will be the main source of air pollution. There will be not any type of
process gas emissions during the manufacturing process. Flue gas emission will take place
from stack attached to Steam Boiler (600kg/hr). High Speed diesel will be utilized as fuel.
There will also a provision of D. G. Set (350 KVA) as a stand-by source to the main power
supply. High Speed Diesel (HSD) will be used as fuel in D. G. Set.
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4.3 PROCESS DESCRIPTION:
1. PROCESS OF FORMALDEHYDE
Formaldehyde is the oxidation/dehydrogenation product of methanol with oxygen in the
presence of silver catalyst. Please refer to the attached Process Flow diagram.
1. feed methanol, air, water
Catalyst: Silver
2. A fixed quantity of methanol and water is introduced into a mixer(F03) from where
this mixture is taken into an evaporator (F04).
3. Pre-heated Air is also introduced into the evaporator and Pre-heated Recycled Tail
Gas is fed just above the evaporator through a Tail Gas Mixer (F06).
4. A temperature of 70oC is maintained by heating with steam through the steam coil
(F05) which facilitates the evaporation of methanol.
5. The air, methanol vapour, water molecules and Tail Gas mixture is then further
heated to 120ºC. in the Super heater (F07).
REACTION
The superheated vapour is then introduced into the Reactor I (F09) and then comes
down to the Catalyst bed in Reactor II (F10) where, in presence of silver catalyst
maintained at a temperature of 650º.C, the oxidation/dehydrogenation reaction takes
place as per the following chemistry:
CH3OH = HCHO + H2 Endothermic Reaction
H2 + 1/2 O2 = H2 O Exothermic Reaction
CH3OH + 1/2 O2 = HCHO + H2O Net Exothermic Reaction
Several side reactions also happen to produce formic acid, carbon dioxide and carbon
monoxide. The endeavor is to minimize these side reactions. The catalyst bed
temperature is maintained at around 640 to 650º C by controlling the composition of
Reactor feed gas.
The Reaction is net Exothermic. In the Reactor II(F10) itself, which is also a waste heat
boiler, the temperature of the product gasses is brought down to 180º C and then further
cooled to about 95ºC in the Re-boiler (F11). This is achieved by circulating the Solution
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in the Evaporator in the Re-boiler which cools down the Product gasses to about 95º c
and itself is heated up to 70º C thus saving on energy.
With Tail Gas Recycle incorporated in the design, Surplus steam to the extent of 200-
250 kg/ton of produced Formaldehyde is available for export which can be used in the
heating of the Resin Kettle.
ABSORPTION
The reaction gas containing Formaldehyde, un-reacted Methanol and water vapour is
then directed to Absorption Column-I (F16) and the Formaldehyde gases are absorbed
by the circulating Formaldehyde solution. The absorption of Formaldehyde is an
exothermic process and the circulating Formaldehyde solution is cooled in the Plate
Heat Exchanger (HE1).A part of the circulation is taken out as product.
The Absorber-I is packed with Structure Packing with a high efficiency of contact and
coupled with the efficient cooling system provided results in very efficient absorption
of the Formaldehyde in the absorber.
The unabsorbed gas from the Absorption Column-I is absorbed in the Absorption
Column(F17) which is packed with Pall Rings. Finally, the gas is washed with pure
Chilled DM water at the upper part of the Column-III (F18), provided with bubble cap
trays, and then exhausted as tail gas to the atmosphere.
The Exhaust gasses now contain only Nitrogen, Hydrogen, Carbon Dioxide, Carbon
Monoxide and traces of Formaldehyde and Methanol which is lead out to the
atmosphere. The waste gas containing Hydrogen can be burnt or incinerated to generate
steam for use in the Resin section if so desired.
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PROCESS FLOW CHART DIAGRAM
Air, Methanol Water Silver Catalyst Air (A/M=1.8̃1.95)
Water
Formaldehyde (37%)
Vaporization of
Methanol & water With Air
Catalytic reactor 200·C initiated
externally and maintain exothermically
Absorption tower
three stages
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2. UREA FORMALDEHYDE RESIN:
MANUFACTURING PROCESS:
� First all the raw materials Urea & Formaldehyde will be added in Limped reaction
vessel.
� pH will be adjusted to pH 9.0.
� Stirring & heating will be done up to 95 °C for 50 Minutes.
� Heating will be continued until tolerance (10:40) is achieved.
� pH will be adjusted to 9 by adding Caustic.
� Cooling will start
� Urea Formaldehyde Resin will be ready for Packing.
Chemical Reaction:
Process Flow Chart
Stirring and Heating up to
95°°°°C for 50 Minutes
Cooling
Urea Formaldehyde Resin
Limped Reaction Vessel
pH adjusted to 9
pH adjusted to 9 Caustic
pH adjusted to 9 pH adjusted to 9
Urea
Formaldehyde
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3. MELAMINE FORMALDEHYDE RESIN:
MANUFACTURING PROCESS
� First all the raw materials melamine, formaldehyde & caustic will be added in Limped
reaction vessel.
� Stirring & heating will be done up to 95 °C for 1 Hr.
� Cooling down to 40 °C
� Melamine Formaldehyde Resin will be ready for Packing.
Chemical Reaction:
4. PHENOL FORMALDEHYDE RESIN:
MANUFACTURING PROCESS
� First all raw materials like phenol, formaldehyde & caustic will be added into closed
vessel.
� Stirring & heating will be done up to 60 °C. After 60°C stop heating.
� Reflux is done for 30 minutes up to 98 °C.
� Vacuum distillation will be started.
� Water will be removed from the vessel as per the batch size.
� Cooling down to 40°C.
� Methanol will be added for dilution purpose.
� Phenol Formaldehyde Ready for Packing.
Limped Reaction Vessel
Stirring and Heating up to
95°°°°C for 1 hr
Cooling at 40°°°°C
Melamine Formaldehyde
Resin
Melamine
Formaldehyde
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CHEMICAL REACTION:
Process Flow Diagram
H – CHO
OH
CH2OH
OH
Fas
Phenol Phenol Formaldehyde Resin
Limped Reaction Vessel
Stirring and heating up to 60 °°°°C
Reflux for 30 Minutes
Vacuum Distillation
Cooling
Dilution
Phenol Formaldehyde Resin
Phenol Formaldehyde Caustic Flakes
Water
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5.0 DESCRIPTION OF THE ENVIRONMENT
5.1 INTRODUCTION:
The main objectives of describing the environment, which may be potentially affected, are (i)
to assess present environmental quality and the environmental impacts and (ii) to identify
environmentally significant factors that could preclude project development.
This chapter contains information on existing environmental scenario for the following
parameters.
1. Land Environment
2. Meteorology
3. Air Environment
4. Noise Environment
5. Water Environment
6. Soil Environment
7. Biological Environment
8. Socio-economic Environment
5.2 ENVIRONMENTAL BASELINE DATA COLLECTION: Baseline data for the proposed unit will be collected during pre monsoon Season (March to
May, 2019) to assess the present scenario of the area. Detail of site is given in topo sheet
Figure 5.1. Primary data will be collected by monitoring & surveying of various
environmental components/ parameters in the core zone during the study period (March to
May, 2019); details of which are given in Table - 5.1.
TABLE-5.1 PRIMARY DATA
S. NO. PARAMETERS DESCRIPTION 1 Meteorology Meteorological parameters on hourly basis at project site.
Parameters: Temperature, Relative humidity, Wind Speed
& Wind Direction.
2 Air Ambient air quality monitoring (24 hourly), twice a week.
Parameters are PM10, PM2.5, SO2, NO2 & CO.
No. of Locations: 1 (Project site)
3 Noise Noise level monitoring (Day & Night time), once in a
season.
No. of Locations: 8 locations in core and buffer zone.
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4 Water Ground water sampling, once in a season.
No. of Locations: 8 locations in core and buffer zone.
Tested for physical and chemical parameters.
5 Soil Soil sampling, once in a season.
No. of Locations: 6 locations in core and buffer zone.
6 Biological Factors Biodiversity survey, once in a season.
Location: Core and buffer zone.
7 Socio-economic Environment
Socio-economic survey, once in a season.
Location: Core and buffer zone.
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FIGURE- 5.1 TOPO SHEET
PROJECT SITE
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5.2.1 METEOROLOGY:
Meteorology plays a vital role in affecting the dispersion of pollutants, once discharged into
the atmosphere. The principal variables include horizontal convective transport (average wind
speed and direction), vertical convective transport (atmospheric stability) and topography of
the area.
Meteorological characteristics of an area are very much important in assessing possible
environmental impacts and in preparing environmental management plan. The climate of the
district can be classified as tropical steppe, semi-arid and hot which is mainly characterized by
general dryness except for a short period during southwest monsoon season, intensely hot
summers and cold winters. There are four seasons in a year namely the cold season from
November to March, hot season from April to June, south west monsoon season from the last
week of June to the middle of September and the post monsoon season from September till the
beginning of November. During cold season, a series of western disturbances affect the climate
of the district. During the summer months i.e. from April to June, weather is very hot, dry and
uncomfortable. The weather becomes humid and cloudy during July to September due to
penetration of moist air of oceanic origin into the atmosphere.
The normal annual rainfall of the district is 670 mm, which is unevenly distributed over the
area in 31days. The south west monsoon which contributes 72%, sets in last week of June and
withdrawn in middle of September. July and August are the rainiest months. Rest 28% of
annual rainfall occurs in the non-monsoon months in the wake of western disturbances and
thunder storms. The micro-meteorology of the project site is given in Table 5.2
TABLE-5.2 MICRO-METEOROLOGY OF SITE
Period TEMPERATURE
(oC)
RELATIVE
HUMIDITY
(%)
WIND
SPEED
(km/h)
RAIN
FALL
(mm) Max. Min.
2014 46 3 64 4 670
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6.0 ENVIRONMENTAL IMPACT AND MANAGEMENT PLAN
PARTICULARS DETAILS
Impact on Air
Construction/Operational
Phase
Fugitive/Flue gas emissions from proposed plant will be on
account of process emissions from stacks attached to proposed
reactor/boiler. The mitigation measure adopted as under:
� The main raw material brought in and dispatched by
road in covered enclosures.
� All the vehicle owners will have valid PUC Certificate
� All vehicles are loaded up-to prescribed limit during
transportation.
� Dust suppression on haul roads will be done at regular
intervals.
� Proper pollution control equipments like Cyclone &
wet scrubber will be installed by the proponent.
Air Quality Management:
Emissions Management � A stack of 30m height will be equipped with Multi-
cyclone installed with the boiler to control the
particulate and gaseous emissions due to combustion of
fuel.
� All the roads are asphalted to control the fugitive dust
emissions
� Proper servicing & maintenance of vehicles is/will be
carried out.
Monitoring Management Ambient air quality and stack emission will be regularly
monitored to ensure that ambient air quality standards and
suggested limits on stack emission loads would be met
honestly at all the time.
Impact on water
Construction/Operational phase
Water requirement of the plant will be met from ground water.
Roof top (Office Block) rain water will be recharged to
compensate for ground water with-drawl. The proposed plant
would have “Zero Effluent discharge”.
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� Waste water from different streams will be treated in ETP and used for greenbelt development/ re-use for cooling.
Water Management � Domestic waste water generated from the plant will be
treated in Septic Tank. And treated water will be used
in green belt development.
� Portable water to labour for drinking purpose.
� Rain water conservation.
Impact on Noise
Operational Phase The expected noise levels of some of the equipment like
Pumps (82-95 dB (A), DG sets (100-120 dB (A).
With the mitigation measures the noise levels will be further
restricted within very short distance from the source point.
The operators/personnel working near the noise sources in the
Plant has been provided with earmuffs and earplugs
Green belt will be developed around the plant premises which
act as noise abatement measures. Regular monitoring of noise
level is being carried out and corrective measures in concerned
machinery to be adopted accordingly.
Noise Management � There is no danger of noise pollution from plant. The
green belt (plantation of dense trees across the
boundary) helps in reducing noise levels in distillery
plant as a result of attenuation of noise generated due to
plant operations and transportation.
� Earmuffs will be used while running the equipments of
the plant.
� D.G sets will be provided with acoustic to control the
noise level within the prescribed limit.
� A high standard of maintenance will be practiced for
plant machinery and equipments, which helps to avert
potential noise problems.
� Personal Protective Equipment like earplugs and
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earmuffs will be provided to the workers exposed to
high noise level.
� Regular monitoring of noise level will be carried out.
Solid/Hazardous Waste Management Management � Entire solid/hazardous waste generations from the process
will be stored & disposed off as per norms. The details are
given in table:-
S. No
WASTE CATEGORY QUANTITY DISPOSAL
1 ETP Sludge 35.3 0.5TPA Sent to TSDF Site 2 Used /spent
oil 5.1 0.2TPA Sold to authorized
recyclers
Green belt Management Management
� Green belt development in and around the plant site helps
to attenuate the pollution level.
� Out of the total plant area approx. 33% land will be
developed and maintained as green belt.
� Green belt will be developed as per Central Pollution
Control Board (CPCB) guidelines.
� Native species will be planted in consultation with the
local DFO.
Odor Management Management
� The remedial measures will be taken such as better house-
keeping by regular steaming of all equipments.
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BALAJI OVERSEAS LUDHIANA, PUNJAB 29 CPTL-EIA
7.0 SITE ANALYSIS (i) Connectivity
The proposed plant will be located at Village Hambran, Near Murti Agro Foods, Tehsil &
District Ludhiana, Punjab. It has an easy access to raw material availability and other
infrastructural facilities e.g. land, power, water, transport and communication, approach
through road & access distances from the nearest highway, railway station etc. The site is well
connected with communication facilities like telephone, fax, wireless and telex and as such, no
constraints are envisaged in this aspect also.
(ii) Land from Land use and land ownership
The proposed project will be set up in an area of 1.82 Acres. The proposed land use break up is
given in Table 7.1
Table7.1
LAND BREAKUP DETAILS
S.no. Type Of Use Area in acres 1 Built up area at GF 1.05 2 Open area 0.13 3 Parking area 0.04 4 Green Belt and Open area 0.60 TOTAL LAND 1.82 acre
(iii) Topography
The topography of the area is plain. (iv) Existing land use pattern
Project area is the industrial land as per master plan of Ludhiana. Project proponent already
obtained CLU.
PRE-FEASIBILITY REPORT
BALAJI OVERSEAS LUDHIANA, PUNJAB 30 CPTL-EIA
8.0 PROPOSED INFRASTRUCTURE
(i) Industrial Area (processing area) It is an approved focal point and project proponents have already purchased land for proposed
project.
(ii) Residential Area (Non processing area)
There is no requirement of residential colony, because local labor will be preferred to provide
employment opportunities.
(iii) Green Belt
Total land area of the proposed project is 1.82 acre. The greenbelt will also be developed at the
site in an estimated area of 0.6 acre. Adequate green belt provision as per CPCB guideline has
already been considered for proposed project development. Further, unpaved areas if any,
within the plant boundary will be provided with grass cover which will also improve the plant
aesthetics.
(iv) Social Infrastructure
Proposed project will result in growth of the surrounding areas by increased direct and indirect
employment opportunities in the region including ancillary development and supporting
infrastructure.
(v) Connectivity
The plant site is well connected to National Highway NH-95(~7.0 km in south direction). The
nearest railway station is Ludhiana and nearest airport is Ludhiana (Sahnewal) & Chandigarh.
The site is suitably located with respect to availability of raw material, water, road network,
skilled/semi skilled/unskilled and professional manpower etc. All communication facilities
such as telephone, telefax & internet are available in the vicinity of the plant site.
(vi) Industrial Waste management The project would be based on “ZERO DISCHARGE”. 9.0 REHABILITATION AND RESETTLEMENT (R & R) PLAN
No agricultural land and habitation is present in the land and there is no displacement involved.
Hence, no Land Acquisition, Resettlement and Rehabilitation is envisaged for this project.
PRE-FEASIBILITY REPORT
BALAJI OVERSEAS LUDHIANA, PUNJAB 31 CPTL-EIA
10.0 PROJECT SCHEDULE AND COST ESTIMATES
(i) Likely date of start of Construction and likely date of completion
(Implementation schedule) :
The construction of the project shall commence soon after receipt of Environment Clearance
from MOEF&CC, GOI, New Delhi. The project execution schedule shall be another 10
months after obtaining environment clearance.
(ii) Estimated Project Cost
The project cost estimated to be Rs 400 Lacs and the breakup is as follows.
Table 10.1 DETAILS OF PROJECT COST
Total Fixed Cost Cost (Rs. In Lacs)
Land & Development cost 47.00
Building and infrastructure 50.00
Plant & Machinery including erection, contingency APCD,ETP expenses
295.00
Misc Expenses 8.0
Total 400.00
Profit and Cost Benefit Analysis
Profit and cost benefit analysis can be estimated as the Raw Material cost per kg of product.
PRE-FEASIBILITY REPORT
BALAJI OVERSEAS LUDHIANA, PUNJAB 32 CPTL-EIA
11.0 ANALYSIS OF PROPOSAL & CSR ACTIVITIES
M/s Balaji Overseas will create direct & indirect employment opportunities to the people
residing in the surrounding area. The management will also recruit the locals by giving them in
plant training and making them permanent employee. Different types of people are being
recruited based on their basic qualification as skilled, unskilled or semiskilled.
Considering from the financial point of view, proposed project will help to generate additional
government revenues from taxes, duties and levies. Additional benefit of the project also
includes considerable growth of the industrial and commercial activities in the state.
Proposed project will result in growth of the surrounding areas by increased direct and indirect
employment opportunities in the region including ancillary development and supporting
infrastructure. Special emphasis on Financial and Social benefits will be given to the local
people including tribal population, if any, in the area. Development of social amenities will be
in the form of medical facilities, education to underprivileged and creation of self help groups.
The company will also propose to take up more activity on account of social corporate activity
for proposed project. These activities are as under:
Sr. No.
NAME OF VILLAGE ACTIVITY PROPOSED COST (Lacs)
1 Hambran Tree Plantation, Environment awareness camp
Rs. 2.5
2 Chakk Bhatian Construction of one classroom in the Middle School of village and its upkeep
Rs. 2.0
No adverse effect on environment is envisaged as proper mitigation measures will be taken
up for the same.
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