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EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
CHAPTER-1
INTRODUCTION
1.0 INTRODUCTION
Modern Industrial Estate comprising of about 620 acres was set up at Kundli by the
Haryana govt. on the side of NH-1 at Haryana-Delhi border to give relief to Delhi
from its increasing industrial pressure. Plots of various categories ranging from 10
Marla plots to two acres have been carved out. In this area different industries related
to footwear, iron & fabrication, plastic goods, pharmaceuticals, chemicals,
confectionary / food processing, auto mobiles ancillaries and electronic & electrical
good etc. have been established. There is an existing CETP of capacity 4 MLD which
was constructed about 15 years ago on approx 28,105 sq. m (7 Acres ) of triangular
shaped land in Phase IV, HSIIDC, Kundli to treat the effluent of this area (Phase I to
IV). The outlet of the treated effluent is being disposed off directly in the drain
running besides the CETP.
Now with the increase in industrial activities in the area (Phase III, IV, IV sector-56),
the quantity of effluent at the CETP is expected to increase and hence it has become
necessary to increase the capacity of the existing system from 4 MLD to 10 MLD.
The proposed up gradation is coming up within the same premises.
Total estimated cost including O&M, Power, Chemicals, Sludge disposal and
Departmental Over head expenses will be Rs. 45.86 Crores and Total Estimated
capital investment will be Rs. 21.02 crores for the proposed CETP up-gradation.
The project falls under “item 7(h) of Schedule of Environment Clearance
Notification dated 14th September, 2006, i.e. Common Effluent Treatment Plant,
under Category –“B”. However, due to presence of Haryana-Delhi interstate
boundary at a distance of 2.3 Km in S direction the proposed project will be treated
as Category “A” project.
As per the EIA Notification and subsequent amendments, “if any of the existing or
proposed member units of the said CETP produces or proposes to produce any product
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
requiring environmental clearance, then the CETP shall need environmental
clearance”. Proposed CETP involves the treatment of waste water from the
Metallurgical Industries which requires Environment Clearance. Therefore, the project
requires a prior environmental clearance from MoEF&CC, New Delhi.
M/s HSIIDC has retained the services of Gaurang Environmental Solutions, Jaipur to
undertake Environmental Impact Assessment (EIA) studies for assessing the impact of
the Up gradation of existing CETP from 4 MLD to 10 MLD capacity on various
environmental parameters in the study area and to prepare an Environment Management
Plan (EMP) for negating the adverse impacts of the project to obtain Environment
Clearance from MoEF&CC, New Delhi.
The application for prior Environmental Clearance (Form-1) was uploaded on dated
07.03.2019. Project was consider in 40th Expert Appraisal Committee (Infra-2) (S. No.
40) Dated 23rd April’ 2019. Project was reconsider for Terms of Reference in in 43rd
Expert Appraisal Committee (Infra-2) (S. No. 43.3.10) Dated 20-22 August’ 2019 and
the project was granted with standard Terms of Reference vide letter no. F. No.10-
23/2019-IA-III Dated 31st October 2019 by MoEF&CC. Copy of Terms of Reference
is enclosed as Annexure I. Baseline studies for the project were carried out during
December’2018 to February’ 2019 (winter season).Public consultation for the project
has been exempted as the proposed up gradation of existing CETP area falls under the
notified industrial area. The industrial area notification gazette is enclosed as
Annexure -VII.
The proposed up gradation of existing common effluent treatment plant will be based
on physical & chemical treatment for removal of excessive inorganic COD, TSS &
BOD beside removal of color & maintenance of equalized & constant PH & Flow rate
prior to biological process i.e. Activated Sludge process based on extended aeration
principal. That after biological Treatment process treated effluent shall be further
treated in pressure Filter, Carbon filter and shall be disinfected with chlorine before
final disposal for reuse being designed on the concept of Zero liquid discharge.
Waste water thus generated by the associated industries will be lifted through
dedicated pipeline system after meeting the pre treatment discharge standards
prescribed by HSIIDC. Waste water generated from Pharmaceutical and chemical
member industry will be treated by themselves and treated water will be discharge as
per standards prescribed by HSPCB and CPCB. The waste water after treatment shall
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
meet the discharge standards laid down by MoEF&CC and HSPCB. It has been
proposed by HSIIDC to reuse treated effluent for irrigation, watering of parks &
greens etc. which will require multimedia filtration with Pressure Filter, Activated
Carbon Filter followed by disinfection for removal of coliforms and helminthes so as
to achieve Zero liquid discharge.
The HSIIDC has always taken lead in providing best possible infrastructure facilities
in all the Industrial Estates. Accordingly it has been decided that Disposal works
Common Effluent Treatment Plant & Disposal of Treated Effluent as per CPHEEO
Norms be designed and got executed at site.
This Environmental Impact Assessment (EIA) report has been prepared to provide
information on the potential environmental, social and economic impacts of the
project. It also aims to make recommendations for mitigation of the potential negative
impacts and enhancement of the positive ones. Baseline data generation including
detailed field survey was carried out and potential environmental impacts of the
project activities were identified, assessed and documented. This report has been
prepared as per the Terms of References (Standard ToR issued by MoEF&CC, New
Delhi), EIA Notification, 2006 & amendments.
1.2 IDENTIFICATION OF PROJECT & PROJECT PROPONENT
1.2.1 Identification of Project
There is an existing CETP of capacity 4 MLD which was constructed about 15 years
ago on approx 28,105 sq. m (7 Acres ) of triangular shaped land in Phase IV,
HSIIDC, Kundli to treat the effluent of this area (Phase I to IV). The outlet of the
treated effluent is being disposed off directly in the drain running besides the CETP.
Now with the increase in industrial activities in the area (Phase III, IV, IV sector-56),
the quantity of effluent at the CETP is expected to increase and hence it has become
necessary to increase the capacity of the existing system from 4 MLD to 10 MLD
capacity (based on extend aeration system) coming up at Phase-IV, Industrial Estate,
Kundli, Sonipat, Haryana.
The proposed project falls under “item 7(h) of Schedule of Environment Clearance
Notification dated 14th September, 2006 and as on date amended on date 17th April’
2015, i.e. Common Effluent Treatment Plant, under Category –“B”. However, due
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
to presence of Haryana-Delhi interstate boundary at a distance of 2.3 Km in S
direction the proposed project will be treated as Category “A” project. As per the
EIA Notification and subsequent amendments, “if any of the existing or proposed
member units of the said CETP produces or proposes to produce any product requiring
environmental clearance, then the CETP shall need environmental clearance”.
Proposed CETP involves the treatment of waste water from the Metallurgical
Industries which requires Environment Clearance. Thus, the project requires
environmental clearance. Project details are summarized as under:-
Table 1.1: Brief details of the project
S.
No.
Particulars Details
1 Project Up gradation of existing CETP from 4
MLD to 10 MLD capacity based on extend
aeration system
2 Promoter HSIIDC Limited
3 Location Phase-IV, Industrial Estate, Kundli,
Sonipat, Haryana
4 Capacity Capacity Existing Proposed Total
CETP 4 6 10
5 Total Plot Area for Industrial
Estates (Phase I, II, III & IV) 620 Acres
6
Total Plot Area
Particula
rs
Existing Proposed Total
Total plot
area
28,105
sq. m
(7 Acres
)
Within the
existing
premises
28,105
sq. m
(7
Acres )
S. No.
Particulars Existing (Sq.m)
Proposed (Sq.m)
Total (Sq.m)
%
1 Plant area 16,196.91 -- 16,196.91 57.63
2 Green Area 5,160.08 -- 5,160.08 18.36
3 Road &
footpaths 2,481.68
--
2,481.68 8.83
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
4 Others Open
area 4,266.33
--
4,266.33 15.18
5 Total 28,105 -- 28,105 100
7 Man Power Particula
rs
Existing Proposed Total
Manpowe
r
13 no 30 during
constructi
on phase
13 –
operati
on
phase
30 –
constru
ction
phase
8 Power Requirement and Source Particular
s
Existing Proposed Total
Power and
Source
275 KW UHBVN Supply
425 KW UHBVN Supply
700 KW UHBVN Supply
D.G. Set 300kVA (200 kVA:1No. + 100 kVA:1No.) Fuel used: HSD
500 kVA (1No.) Fuel used: HSD
3nos. 200kVA:1No. 100kVA:1No 500kVA:1No.
9 Water Requirement and Source Particula
rs
Existing Proposed Total
Water
demand
and
3 KLD 0.6 – domestic use 2.4 KLD - chemical dosing
3 KLD - chemical dosing
6 KLD 0.6 – domestic use 5.4 KLD - chemical dosing
source HSIIDC Industrial Water supply
10 Waste Water generation Domestic waste water generation - 0.4 KLD
Total Waste water Quantity for Existing CETP
Capacity – 3927 KLD (3.93 MLD)
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
Total Waste water Quantity for proposed CETP
Capacity – 5252 KLD (5.25 MLD)
11 Estimated Project Cost Total estimated cost including O&M, Power,
Chemicals, Sludge disposal and
Departmental Over head expenses will be Rs.
45.86 Crores and Total Estimated capital
investment will be Rs. 21.02 crores for the
proposed CETP up-gradation.
1.2.2 Identification of Project Proponent
The details of the project proponent are given below:
Name of the
applicant
HSIIDC Limited
Name and address Mr. Arun Garg AGM (IA)
HSIIDC Office, Industrial Estate, Kundli, Distt.- Sonipat
Status of Project Expansion project (Freshly applied for Environmental
Clearance)
Copy of Land document is attached as Annexure II.
1.3 BRIEF DESCRIPTION OF PROJECT
1.3.1 Nature of the Project
The proposed project Up gradation of existing CETP from 4 MLD to 10 MLD
capacity based on extend aeration system coming up at Phase-IV, Industrial Estate,
Kundli, Sonipat, Haryana over an area of 28,105 sq.m.(7 acre).
The proposed project falls under “item 7(h) of Schedule of Environment Clearance
Notification dated 14th September, 2006 and as on date amended on date 17th
April’ 2015, i.e. Common Effluent Treatment Plant, under Category –“B”.
However, due to presence of Haryana-Delhi interstate boundary at a distance of 2.3
Km in S direction the proposed project will be treated as Category “A” project.
As per the EIA Notification and subsequent amendments, “if any of the existing or
proposed member units of the said CETP produces or proposes to produce any product
requiring environmental clearance, then the CETP shall need environmental
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
clearance”. Proposed CETP involves the treatment of waste water from the
Metallurgical Industries which requires Environment Clearance. Therefore, the project
requires a prior environmental clearance from MoEF&CC, New Delhi. Thus, the
project requires environmental clearance.
1.3.2 Size of the Project
Project facilities are as under:
S. No. Project Capacity
1. Common Effluent Treatment Plant (based on
extend aeration system)
Up gradation of existing
CETP from 4 MLD to 10
MLD capacity
1.3.3 Location of the Project
The proposed up gradation is coming up within the existing premises. The existing
CETP is situated at Phase-IV, Industrial Estate, Kundli, Sonipat, Haryana.
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
Figure: 1.1 Location Map
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
Figure: 1.2 Google Map
The latitude longitude of the project site is as under:
1 2
Latitude : 280 53’11.71” N Longitude: 770 7’ 51.32” E
Latitude : 280 53’4.37” N Longitude: 770 7’ 51.43” E
3 4
Latitude: 280 53’4.35” N Longitude: 770 7’42.44” E
Latitude: 280 53’4.88” N Longitude: 770 7’ 42.45” E
The project site falls in Survey of India Toposheet No. 53 H/1, 53 D/13, 53 H/5 and
53 G/4. Geographical location of the project site is shown in Figure-1.3.
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
Figure-1.3: Geographical Location of The Project (10 km)
1.3.4 Project Importance to the Country / Region
Establishment of effluent treatment plants for individual industries especially in the
small scale sector in the various industrial estates in India, to produce the effluent of
desired quality before discharge is not feasible in the Indian context. Firstly, because
it is expensive on both the capital and operating cost front and secondly, there is no
guarantee of performance by the individual industries. Further, the disposal of treated
effluents is also problematic as every individual industry cannot reach the water body
through its own pipeline nor can it purchase land for inland irrigation. Thus,
Government of India floated the idea of Common effluent treatment plant to
overcome these problems. Accordingly Ministry of Environment, Forest & Climate
Change, Government of India instructed the various State Pollution Control Boards to
examine the possibilities of establishing CETP’s in various industrial estates. In
response to the directive issued by the Central Governments, the State Governments
started identifying the various locations for CETP’s. Establishment of CETP has
following advantages:
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
• Saving in Capital and Operating cost of treatment plant. The Common treatment
is always cheaper than small scattered treatment units.
• Contribution of nutrient and diluting potential make the complex industrial waste
more amenable to degradation.
• The neutralization and equalization of heterogeneous waste makes its treatment
techno-economically viable.
• Professional and trained staff can be made available for operation of CETP which
is not possible in case of individual plants.
• Disposal of treated wastewater & sludge becomes more organized.
• Reduced burden of various regulatory authorities in ensuring pollution control
requirement.
Water is our most important resource. The available supply of fresh water is an
absolute deadline beyond which no community, state or nation can ever go. When
humanity runs out of clean water, everything stops. That is the end of road for a man
and his activities. Saving our clean water is thus a must. When untreated or
inadequately treated waste waters are discharged, these have adverse affect on the
body of water into which these wastes are disposed. The type of treatment of waste
water would depend upon the use of effluent itself or of receiving body of water into
which effluent is discharged. The degree of treatment of waste water would further
depend upon the discharge of receiving body of water. If small quantity of waste
water is discharged in a river or into the sea, the degree of treatment would be much
less than if the same quantity of waste water is discharged into a small stream. When
receiving body of water is already polluted because of discharge of waste into it, the
extent of new discharge of waste into it would be limited.
Waste water thus generated by the associated industries will be lifted through
dedicated pipeline system after meeting the pre treatment discharge standards
prescribed by HSIIDC. The waste water after treatment shall meet the discharge
standards laid down by MoEF&CC and HSPCB. Waste water generated from
Pharmaceutical and chemical member industry will be treated by themselves and
treated water will be discharge as per standards prescribed by CPCB. It has been
proposed by HSIIDC to reuse treated effluent for irrigation, watering of parks &
greens etc. which will require multimedia filtration with Pressure Filter, Activated
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
Carbon Filter followed by disinfection for removal of coliforms and helminthes so as
to achieve Zero liquid discharge.
1.4 SCOPE OF THE STUDY
The zone comprising of 10 km radius around the project site is considered as the study
area. The study area map is shown in Figure-1.3. The scope of study broadly includes:
To conduct literature review and to collect data relevant to the study area;
Generate field sampling results of environmental attributes to establish the
baseline environmental status;
Collate and compile secondary data including socio-economic data from
published literature / Government publications;
Estimate pollution loads that would be generated by the proposed project
Evaluate the predicted impacts on various environmental attributes in the study
area by using scientifically developed and widely accepted environmental
impact assessment methodologies
Preparing an Environment Management Plan (EMP) to mitigate the predicted
impacts
To identify critical environmental attributes required to be monitored and
suggest Post Project Monitoring Plan and
To carry out Risk Assessment and prepare suitable Disaster Management Plan
Preparing an EIA report, in line with the standard TOR issued by MoEF&CC,
New Delhi.
To determine existing conditions of various environmental attributes, field
studies have been conducted during December’ 2018 to February’ 2019
covering Winter Season.
The EIA/EMP report has been prepared in line with the Minutes of Meeting
recommended by MoEF&CC, New Delhi. The compliance of Terms of Reference
(regulatory scoping carried out as per TOR) in following Table-1.2.
TABLE – 1.2
COMPLIANCE TO TERMS OF REFERENCE
S.
No. Terms of References Points Compliance
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
1.
Reasons for selecting the site with
details of alternative sites
examined/rejected/selected on
merit with comparative statement
and reason basis for selection. The
examination should justify site
suitability in terms of
environmental angle, resources
sustainability associated with
selected site as compared to
rejected sites. The analysis should
include parameters considered
along with weight age criteria for
short-listing selected site.
The existing CETP
is located in HSIIDC Industrial area Kundli,
Haryana where the effluent is being
transported through pipeline network.
Proposed up gradation is coming up within the
same premises.
The site is situated in notified industrial area,
considering the environmental and economic
feasibility.
The transport of effluent will be through
pipeline. Thus, it prevents any possibility of
direct contact of untreated effluent with
surface water.
Proximity to effluent generating industries
Uninterrupted power supply.
Availability of power and water
2.
Details of the land use break-up
for the proposed project. Details of
land use around 10 km radius of
the project site.
This is up gradation of existing Common effluent
Treatment Plant at HSIIDC IA, Kundli. The total plot
area of the existing CETP is 28,105 sq.m which is 7
acre. The proposed up gradation is coming up within
the same premises. The land use breakup is as under:-
S. No.
Particulars Existing (Sq.m)
Proposed (Sq.m)
Total (Sq.m)
%
1 Plant area 16,196.91 -- 16,196.91 57.63
2 Green Area 5,160.08 -- 5,160.08 18.36
3 Road &
footpaths 2,481.68
--
2,481.68 8.83
4 Others Open
area 4,266.33
--
4,266.33 15.18
5 Total 28,105 -- 28,105 100
Details of the land use around 10 Km radius of project site mentioned in section- 3.3 of
chapter 3 of EIA Report.
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
3.
Details of member units, its
production capacity, waste
generation, characteristic and
details of primary treatment
provided by the member units.
Preliminary treatment (based on specific
requirements) will be done by member units before
discharging their effluent into the CETP. Waste water
generated from Pharmaceutical and chemical member
industry will be treated by themselves and treated
water will be discharge as per standards prescribed
by CPCB. Details of member industries located in
Phase I, II, III, IV, IV sector-56 are summarized as
under:-
WASTE WATER DETAILS FROM MEMBER UNITS FOR EXISTING CETP (4 MLD)
S. No Types of Industries No of Industries Waste water generation in
KLD
1 Food Processing Unit 32 214
2 Metallurgical 168 1253
3 Plastic tubes 46 234
4 Cement 1 10
5 Chemical 20 227
6 Paper Industry 4 24
7 Agricultural 3 16
8 Wood 5 24
9 Pharmaceutical 14 82
10 Cloths 63 981
11 Rubber 27 222
12 Computer 11 47
13 Warehouse 19 134
14 Packaging, plastic
products & printing
51 349
15 Electronic 20 92
16 Glass 4 58
17 Leather & tanning 2 6
18 Jwellery & accessories 7 57
19 Miscellaneous 20 117
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
Gaurang Environmental Solutions Pvt. Ltd. Report Ref: GESPL/228/2019/EIA/31
HSIIDC Limited Authorized Signatory
WASTE WATER DETAIL FROM MEMBER INDUSTRY FOR PROPOSED CETP (6 MLD)
Total 617 3927
S. No Types of Industries No of Industries Waste water generation in KLD
1 Food Processing Unit 13 285
2 Metallurgical 100 1694
3 Plastic 33 440
4 Cement/ Ceramics 5 64
5 Chemical 09 117
6 Paper Industry 1 12
7 Agricultural 3 47
8 Wood 6 83
9 Pharmaceutical 13 156
10 Textile 71 1020
11 Rubber 12 229
12 Computer 8 107
13 Warehouse 3 52
14 Packaging, plastic products
& printing
32 482
15 Electronic 14 217
16 Glass 1 20
17 Leather & tanning 1 12
18 Jwellery & accessories 3 40
19 Miscellaneous 12 175
Total 340 5252
4. Details on present treatment and
disposal systems. Existing effluent is presently being discharged into
drainage as per HSIIDC Norms.
5.
Details of effluent collection
system from member units level.
Effluent will be collected through closed pipeline
conveyance system. Member industries will
discharge their effluent in the pipeline after meeting
the pre treatment discharge standards prescribed by
HSIIDC.
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
Promoter: HSIIDC Limited Chapter-1 Introduction
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HSIIDC Limited Authorized Signatory
Member industries of CETP will be required to
monitor specified quality parameters and flow rate of
the effluent on daily basis and to submit the
monitoring data to the CETP operator on regular
basis. Continuous flow meters will also be installed at
the outlet of the CETP to monitor the outlet effluent
quantity.
6. Details of hazardous waste
collection, Sill proof arrangement.
As per HWM Rules, 2016 and subsequent
amendments, CETP sludge considered as Hazardous
Waste.
CETP sludge is collected at sludge drying beds which
is properly lined and kept impervious.
7. Examine and submit details of
inlet characteristics.
Effluent will be collected through closed pipeline
conveyance system. Member industries will discharge
their effluent in the pipeline after meeting the pre
treatment discharge standards prescribed by HSIIDC &
will be having following characteristics:
S. No.
Parameters Units Value
1 pH -- 6 - 8.5
2 BOD5 mg/l 450 3 COD mg/l 900 4 TSS mg/l 1200 5 Coliform MPN/100ml 1x107 6 Oil & Grease mg/l 100 7 Temperature oC 18-22 8 NH4- Nitrogen mg/l 45 9 TKN mg/l 40 10 TP as PO4 mg/l 10 11 Chromium mg/l 5 12 COD/ BOD ratio -- 2
8.
Details of the CETP with design
parameters. Layout plan of CETP.
And open spaces.
The proposed project involves up gradation of existing
Common Effluent Treatment Plant (CETP) from 4 to 10
MLD capacities. The CETP is used for the treatment of
waste water generated from Industrial Estates, Phase-IV,
Kundli.
S. Particulars Details
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
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No
1. Capacity 4 to 10 MLD
2. Technology Extend Aeration System
3. Status Proposed Up gradation of existing CETP
4. Waste water generation
Existing – 3927 KLD Proposed – 5252 KLD Total – 9179 KLD
The CETP has been designed for following
parameters:
Influent Sewage Characteristics Parameters Units Value
pH -- 6 - 8.5 BOD5 mg/l 450 COD mg/l 900 TSS mg/l 1200 Coliform MPN/100 ml 1x107 Oil & Grease mg/l 100 Temperature oC 18-22 NH4- Nitrogen mg/l 45 TKN mg/l 40 TP as PO4 mg/l 10 Chromium mg/l 5 COD/ BOD ratio -- 2
Treated effluent Characteristics after secondary Treatment
Parameters Units Value pH -- 7-7.5 BOD5 mg/l ≤10 COD mg/l ≤20 TSS mg/l ≤20 Coliform MPN/100 ml ≤10000 Oil & Grease mg/l ≤5 Temperature oC ≤1 NH4- Nitrogen mg/l ≤2 TP as PO4 mg/l ≤0.1 Chromium mg/l >0.2
Treated effluent Characteristics after Tertiary Treatment
Parameters Units Value pH -- 7-8.5 BOD5 mg/l
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
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COD mg/l
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana
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at the CETP. CETP for storage of Chemicals & Sludge as follows
Description Quantity
Chemical House 01
Sludge Storage Shed 01
13.
Examine and submit details of
sludge / solid waste generated and
method of disposal. MoU in this
regard
Details of sludge / solid waste generated and method
of disposal is mentioned as under. Copy of MoU for
disposal of existing solid waste is enclosed as
Annexure – XVI.
S.
No.
Particulars Category Quantity Mode of
disposal Existing Proposed Total
1. ETP Sludge 34.3 1000 Kg/day
1500 Kg/day
2500 Kg/day
Collection, Storage in HWSA, Transportation and sent to GEPIL site for disposal
2. Domestic solid waste
-- 5.2 kg/day -- 5.2 kg/day Handled by Municipal Corporation, Kundli
14.
Details of water requirement,
source and water balance chart.
Particulars Existing Proposed Total
Water
demand
3 KLD 0.6 – domestic use 2.4 KLD - chemical dosing
3 KLD - chemical dosing
6 KLD 0.6 – domestic use 5.4 KLD - chemical dosing
Source HSIIDC Industrial Water supply
Details of the water requirement along with water
balance chart are mentioned in section – 2.4.3 of
Chapter 2 in EIA Report.
The flow diagram of Water Balance is shown in Fig.
2.5 of Chapter – 2 in EIA Report.
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15.
Details of green belt. 5160.08 sq. m. (18.36%) of plant area will be under green
cover as per CPCB norms.
Total Plot Area : 28,105 sq. m.
Total Green Area : 5160.08 sq. m. (18.36%)
Tree Required : Total Plot area /80
: 28,105/80
: 351.31 (says 351)
Tree Provided : 370 nos.
S. No Botanical Name Common
Name
Total
1 Azadirachta indica Neem 72
2 Dalbergia sissoo Shisham 74
3 Cassia Fistual Amaltash 76
4 Ficus Religiosa Peepal 70
5 Ficus Benghalensis Bargad 78
Total 370
Details of green belt development is mentioned in section
10.3.8 of chapter-10 in EIA Report.
16.
Details of performance
monitoring, lab facility with
technical persons.
Laboratory facility is available with technical staff,
Organizational structure mentioned in the report.
CETPs’ organizational chart including the details of
laboratory personals have been mentioned in Chapter
6 of EIA Report.
17.
Details of litigation pending
against the project, if any, with
direction /order passed by any
Court of Law against the Project
should be given.
There is no litigation pending against project.
Affidavit regarding the same is enclosed as
Annexure-XIII.
18.
The cost of the Project (capital
cost and recurring cost) as well as
the cost towards implementation of
EMP should be clearly spelt out.
Environmental management plan Budget
Capital Cost – 99 lacs
Recurring Cost – 11.8 lacs
The detail for the same is mention in chapter – 10 in
EIA Report.
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19. Details of water meters for inflow
and outflow monitoring etc.
Magnetic flow meter has already been installed at
Inlet & outlet of the CETP.
20.
Any further clarification on
carrying out the above studies
including anticipated impacts due
to the project and mitigative
measure, project proponent can
refer to the model ToR available
on Ministry website
http://moef.nic.in/Manual/CETPs.
Complied with
Addition ToR
I Importance and benefits of the
project.
Importance and benefits of the project is mentioned
in section 1.3.4 of chapter-1 in EIA Report.
ii
A chapter on Quantification and
Characterization of inlet
characteristic including
methodology adopted.
Quantification and Characterization of inlet
characteristic is elaborated in Section – 2.6 of
Chapter-2 of EIA Report.
iii Process flow diagram of the
proposed CETP.
Process flow diagram is mentioned in figure 2.6 of
chapter 2 in EIA Report.
iv Layout plan of CETP. Layout plan of CETP is mentioned in figure-2.4 of
chapter – 2 in EIA Report.
v Cost of project and time of
completion.
Total estimated cost including O&M, Power,
Chemicals, Sludge disposal and Departmental Over
head expenses will be Rs. 45.86 Crores and Total
Estimated capital investment will be Rs. 21.02 crores
for the proposed CETP up-gradation.
The implementation schedule for the up gradation of
existing CETP project is twenty four months from the
date of sanction.
vi Area earmarked for CETP. The existing CETP plant is situated in 28,105 sq.m (7
acre) area. There will be up gradation of existing CETP
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capacity from 4 MLD to 10 MLD. The up gradation is
coming up with in the same premises. Thus, there will
be no additional land required.
vii
Method for conveyance of effluent
from the individual industrial unit
to CETP.
Effluent will be collected through closed pipeline
conveyance system. Member industries will
discharge their effluent in the pipeline after meeting
the pre treatment discharge standards prescribed by
HSIIDC. Waste water generated from Pharmaceutical
and chemical member industry will be treated by
themselves and treated water will be discharge as per
standards prescribed by HSPCB and CPCB.
Member industries of CETP will be required to
monitor specified quality parameters and flow rate of
the effluent on daily basis and to submit the
monitoring data to the CETP operator on regular
basis. Continuous flow meters will also be installed at
the outlet of the CETP to monitor the outlet effluent
quantity.
viii
Explore the option to recycle the
treated effluent to individual
industrial unit instead or
discharging outside.
It has been proposed by HSIIDC to reuse treated
effluent for irrigation, watering of parks & greens etc.
which will require multimedia filtration with Pressure
Filter, Activated Carbon Filter followed by disinfection
for removal of coliforms and helminthes so as to
achieve Zero liquid discharge.
ix Reuse and Recycle option of
treated effluent.
It has been proposed by HSIIDC to reuse treated
effluent for irrigation, watering of parks & greens etc.
which will require multimedia filtration with Pressure
Filter, Activated Carbon Filter followed by disinfection
for removal of coliforms and helminthes so as to
achieve Zero liquid discharge.
x
List of hazardous waste to be
handled and their source along
with mode of transportation.
Detail about hazardous waste generated, handled and
their source along with mode of transportation is as
under:-
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S.
No.
Particulars Category Quantity Mode of
disposal Existing Proposed Total
1. ETP Sludge 34.3 1000 Kg/day
1500 Kg/day
2500 Kg/day
Collection, Storage in HWSA, Transportation and sent to TSDF site for disposal
xi
Other chemicals and materials
required with quantities and
storage capacities.
The details about raw materials and chemicals are
mentioned in section – 2.7.2 of chapter – 2 in EIA
Report.
xii
Details of temporary storage
facility for storage of hazardous
waste at project site.
In existing unit, sludge generated from CETP has
been storage in closed room with proper ventilation
and sent to GEPIL site for disposal. After up
gradation sludge storage will be maintain the same.
xiii
Details of pre-treatment facility of
hazardous waste at proposed
incinerator site.
Not Applicable as this is a up gradation of Common
Effluent Treatment Plant project
xiv
Details of air Emission, effluents,
hazardous/solid waste generation
and their management.
Details of air Emission, effluents, hazardous/solid
waste generation and their management are
mentioned in Chapter -4 of EIA Report.
xv Hazard identification and details of
proposed safety systems.
Details for the same is elaborated in chapter-7 of EIA
Report.
xvi
Layout maps of proposed Solid
Waste Management Facilities
indicating storage area, plant area,
greenbelt area, utilities etc.
Not Applicable as this is a common effluent
treatment plant.
xvii Disaster Management Plan. Disaster Management Plan is elaborated in chapter -7
of EIA Report.
xviii Status of court case pending
against the project.
There is no court case pending against the project.
xix Plan for Corporate Environment
Responsibility (CER) as specified
Total Project cost -21.02 Cr.
CSR – 1% (as per Brownfield project) – 21 lac
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under Ministry’s Office
Memorandum vide F.No. 22-
65/2017-IA.III dated 1st May,
2018 shall be prepared and
submitted along with EIA Report.
Detail about same is elaborated in chapter-8 of EIA
Report.
xx
A tabular chart with index for
point wise compliance of above
ToRs.
Noted and Complied with
General Guidelines
i The EIA document shall be printed
on both sides, as for as possible.
Noted and Complied with
ii All documents should be properly
indexed, page numbered.
Noted and Complied with
iii Period/date of data collection
should be clearly indicated.
Monitoring has been done during December’ 2018 to
February’ 2019 covering winter season.
iv
Authenticated English translation
of all material provided in
Regional languages.
Noted and Complied with
v
The letter/application for EC
should quote the MoEF&CC File
No and also attach a copy of the
letter prescribing the ToR.
Noted and Complied with
vi
The copy of the letter received
from the Ministry on the ToR
prescribed for the project should
be attached as an Annexure to the
final EIA-EMP Report.
Noted and Complied with
vii
The Final EIA-EMP report
submitted to the Ministry must
incorporate the issues mentioned
in ToR. The index of the final
EIA-EMP report, must indicate the
Noted and complied with
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specific chapter and page no of the
EIA-EMP report where the
specific ToR prescribed by the
Ministry have been incorporated.
Questionnaire related to the project
(posted on MoEF&CC website)
with all sections duly filled in shall
also be submitted at the time of
applying for EC.
viii Grant of ToR does not mean grant
of EC
Noted and Complied with
1.5 STRUCTURE OF THE REPORT
This EIA Report has been structured as follows:
Chapter 1: Introduction: Provides a background to the project, identification of the
project and project proponent, brief description of the project, details of the project
proponent, scope of the study and structure of this report.
Chapter 2: Project description: Provides details of project, infrastructure required,
technology and process description of bio medical waste management, information on
the needs and desirability of the project and sources of pollution with pollution
control measures.
Chapter 3: Description of the Environment: Provides description of the receiving
Environment details, the specialist study baseline conditions identified for the project
within 10 km radius from the project site.
Chapter 4: Anticipated Environmental Impact and Mitigation Measures:
describe the EIA methodology and impacts identified during the EIA process,
providing the anticipated impacts during the various project phases.
Chapter 5: Analysis of alternatives: provides the different site and technology
alternatives which were considered for the project.
Chapter 6: Environment Monitoring program: provides the monitoring schedule
and implementation plan during the construction and operation phase of the project.
Chapter 7: Additional Studies: has the information about risk and hazard
assessment and details of disaster management plan.
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Chapter 8: Project benefits: associated with the proposed project are discussed in
this chapter.
Chapter 9: Environmental Cost Benefit Analysis: Description of the
Environmental benefits of the project
Chapter 10: EMP: Description of the administrative aspects of ensuring that
mitigative measures are implemented and their effectiveness monitored, after
approval of the EIA
Chapter 11: Summary & Conclusion
Chapter 12: Disclosure of Consultants engaged.
**********
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CHAPTER-2
PROJECT DESCRIPTION
This chapter deals with the technical details of the Up gradation of existing CETP from 4 MLD
to 10 MLD capacity based on extend aeration system, process and technology description and
details of infrastructure.
2.1 TYPE OF PROJECT
There is an existing CETP of capacity 4 MLD which was constructed about 15 years ago
on approx 28,105 sq. m (7 Acres ) of triangular shaped land in Phase IV, HSIIDC,
Kundli to treat the effluent of this area (Phase I to IV). The outlet of the treated effluent
is being disposed off directly in the drain running besides the CETP.
Now with the increase in industrial activities in the area (Phase III, IV, IV sector-56), the
quantity of effluent at the CETP is expected to increase and hence it has become
necessary to increase the capacity of the existing system from 4 MLD to 10 MLD. The
proposed up gradation is coming up within the premises.
The proposed project falls under “item 7(h) of Schedule of Environment Clearance
Notification dated 14th September, 2006, i.e. Common Effluent Treatment Plant,
under Category –“B”. However, due to presence of Haryana-Delhi interstate
boundary at a distance of 2.3 Km in S direction the proposed project will be treated
as Category “A” project.
As per the EIA Notification and subsequent amendments, “if any of the existing or
proposed member units of the said CETP produces or proposes to produce any
product requiring environmental clearance, then the CETP shall need environmental
clearance”. Proposed CETP involves the treatment of waste water from the
Metallurgical Industries which requires Environment Clearance. Therefore, the project
requires a prior environmental clearance from MoEF&CC, New Delhi.
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2.2 NEED FOR THE PROJECT
Establishment of effluent treatment plants for individual industries especially in the
small scale sector in the various industrial estates in India, to produce the effluent of
desired quality before discharge is not feasible in the Indian context. Firstly, because it
is expensive on both the capital and operating cost front and secondly, there is no
guarantee of performance by the individual industries. Further, the disposal of treated
effluents is also problematic as every individual industry cannot reach the water body
through its own pipeline nor can it purchase land for inland irrigation. Thus,
Government of India floated the idea of Common effluent treatment plant to
overcome these problems. Accordingly Ministry of Environment, Forest & Climate
Change, Government of India instructed the various State Pollution Control Boards to
examine the possibilities of establishing CETP’s in various industrial estates. In
response to the directive issued by the Central Governments, the State
Governments started identifying the various locations for CETP’s.
Establishment of CETP has following advantages:
• Saving in Capital and Operating cost of treatment plant. The Common
treatment is always cheaper than small scattered treatment units.
• Contribution of nutrient and diluting potential make the complex industrial
waste more amenable to degradation.
• The neutralization and equalization of heterogeneous waste makes its treatment
techno-economically viable.
• Professional and trained staff can be made available for operation of CETP
which is not possible in case of individual plants.
• Disposal of treated wastewater & sludge becomes more organized.
• Reduced burden of various regulatory authorities in ensuring pollution control
requirement.
Water is our most important resource. The available supply of fresh water is an
absolute deadline beyond which no community, state or nation can ever go. When
humanity runs out of clean water, everything stops. That is the end of road for a man
and his activities. Saving our clean water is thus a must. When untreated or
inadequately treated waste waters are discharged, these have adverse affect on the
body of water into which these wastes are disposed. The type of treatment of waste
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water would depend upon the use of effluent itself or of receiving body of water into
which effluent is discharged. The degree of treatment of waste water would further
depend upon the discharge of receiving body of water. If small quantity of waste
water is discharged in a river or into the sea, the degree of treatment would be much
less than if the same quantity of waste water is discharged into a small stream. When
receiving body of water is already polluted because of discharge of waste into it, the
extent of new discharge of waste into it would be limited.
The project is for common effluent treatment plant to treat the effluent being
generated from the industries located in the industrial estate ((Phase I to IV – existing
CETP, Phase III, IV, IV sector-56 – proposed CETP). Waste water thus generated by
the associated industries will be lifted through dedicated pipeline system after meeting
the pre treatment discharge standards prescribed by HSIIDC. The waste water after
treatment shall meet the discharge standards laid down by MoEF&CC and HSPCB. It
has been proposed by HSIIDC to reuse treated effluent for irrigation, watering of
parks & greens etc. which will require multimedia filtration with Pressure Filter,
Activated Carbon Filter followed by disinfection for removal of coliforms and
helminthes so as to achieve Zero liquid discharge.
2.3 LOCATION OF THE PROJECT
The project site is coming up at Phase-IV, Industrial Estate, Kundli, Sonipat, Haryana.
The general location map of the project is shown in Figure 2.1, which provides a
regional location map of the proposed site relative to its surroundings. The site is
located near National Highway NH-1, which is about 1.2 Km towards WSW from the
site. SH-57, which is about 10.6 Km towards E from the site. Site will be enforced
with secured entrance procedures. The entire footprint of the site will be fenced off
with security fencing.
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Figure 2.1: General Location Map
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Figure 2.2: Google Map
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Figure 2.3: HSIIDC Industrial Estate Layout Plan showing Transportation of
Waste Water
Details
Phase I Industrial plots: 106 nos.
Phase II Industrial Plots: 92 nos.
Phase –III (EPIP) Industrial Plots: 189 nos.
Phase-IV Industrial Plots: 656 nos.
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Figure 2.4: Plant Layout
The details of environmental setting are given in Table-2.1.
Table-2.1 Environmental Setting of the Site
S. No. Particulars Details
1
“Up gradation of existing Common Effluent Treatment Plant from 4 MLD to 10 MLD
capacity”
Khasra No Phase-IV, Industrial Estate, Kundli
Village --
District Sonipat
State Haryana
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S. No. Particulars Details
2
Coordinates
1 2
Latitude : 280 53’11.71” N Longitude: 770 7’ 51.32” E
Latitude : 280 53’4.37” N Longitude: 770 7’ 51.43” E
3 4
Latitude: 280 53’4.35” N Longitude: 770 7’42.44” E
Latitude: 280 53’4.88” N Longitude: 770 7’ 42.45” E
3 Plant site elevation above MSL 214 m above MSL
4 Geographical location in Survey
of India toposheet
Toposheet No. 53 H/1, 53 D/13, 53 H/5 and 53 G/4
5 Plant site topography Plain
6 Present land use at the site
The proposed up gradation project shall be executed on
the existing land only which is already under the
industrial use. Hence, there will be no change in the land
use.
7 Nearest highway • National Highway NH-1 - 1.2 Km towards WSW
• SH-57 - 10.6 Km towards E
8 Nearest railway station • Narela Railway Station - 6.2 Km towards SW
• Sonipat Railway station – 16.0 Km towards NW
9 Nearest airport Indira Gandhi International Airport - 36.5 Km towards
S
10 Nearest village Sonipat - 15 km towards NW
11 Villages within 1 km radius None
12 Hills/valleys None
13 Archaeologically important
places None
14
Protected areas as per Wildlife
Protection Act,1972 (Tiger
reserve, Elephant reserve,
Biospheres, National parks,
Wildlife sanctuaries, community
reserves and conservation
reserves)
None within the study area
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S. No. Particulars Details
15 Reserved / Protected Forests
• Mamupur P.F. - 3.1 km towards SSW
• Ogha R.F - 9.3 km towards SW
• Bawana R.F - 10.0 km towards SW
• Niwara R.F -12.0 km towards NNE
16 Water Bodies
• Drain No. 8 - Nearest to the site towards N
• Naahri Mukhya Vitrika - 3.6 KM towards W
• Harsana Vitrika - 4.7 Km towards NW
• Yamuna River - 8.3 Km towards ESE
• Alipur Dem - 9.8 Km towards E
• Bawana Vitrika - 12.2 Km towards SW
17 Seismicity Seismic Zone-IV as per IS 1893 (Part I): 2002 High
Damage Risk Zone
18 Defence Installations None
19 List of Industries in the
surrounding
There are footwear, iron & fabrication, plastic goods,
pharmaceuticals, chemicals, confectionary / food
processing, auto mobiles ancillaries and electronic &
electrical good etc. have been established.
20 Soil type Sandy loams to loamy sands
21 Depth of water table *Pre-monsoon depth to water level - 1.57-24.84 mbgl
*Post-monsoon depth to water level - 0.64 m-22.46 m
22 Major crops Wheat, Rice, Maize, Gram
23 Socio-economic factors No R&R issues involved
2.4 SIZE OR MAGNITUDE OF OPERATION
The There is an existing CETP of capacity 4 MLD which was constructed about 15
years ago on approx 28,105 sq. m (7 Acres ) of triangular shaped land in Phase IV,
HSIIDC, Kundli to treat the effluent of this area (Phase I to IV). The outlet of the
treated effluent is being disposed off directly in the Drain No. 8 running besides the
CETP.
Now with the increase in industrial activities in the area (Phase III, IV, IV sector-56),
the quantity of effluent at the CETP is expected to increase and hence it has become
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necessary to increase the capacity of the existing system from 4 MLD to 10 MLD.
Details of project facilities are as under.
TABLE-2.2 Details of The Proposed Facilities
S. No. Parameter Description
1 Total Plot Area for Industrial
Estates (Phase I, II, III & IV) 620 Acres
2 Total plot area for CETP 28,105 sq.m.(7 acre)
3 Land-Use
The proposed up gradation project shall be
executed on the existing land only which is
already under the industrial use. Hence, there will
be no change in the land use.
4 Project Capacity Up gradation of existing common effluent
treatment plant from 4 MLD to 10 MLD
5 Power Requirement
Particulars Existing Proposed Total
Power and
Source
275 KW
425 KW 700 KW
D.G. Set 300kVA (200 kVA:1No. + 100 kVA:1No.) Fuel used: HSD
500 kVA (1No.) Fuel used: HSD
3nos. 200kVA:1No. 100kVA:1No 500kVA:1No.
6 Source of Power
Source:- UHBVN Supply
HSD – 15 ltr/hr – existing
25 ltr/hr – proposed
7 Employment
Particulars Existing Proposed Total
Manpower 13 no
operation
phase
30 during
constructio
n phase
13 –
operatio
n phase
30 –
construct
ion
phase
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S. No. Parameter Description
8 Water Requirement
Particular
s
Existing Proposed Total
Water
demand
3 KLD 0.6 – domestic use 2.4 KLD - chemical dosing
3 KLD - chemical dosing
6 KLD 0.6 – domestic use 5.4 KLD - chemical dosing
9 Source of Water HSIIDC Industrial Water supply
10 Waste water generation
Domestic waste water generation - 0.4 KLD
Total Waste water Quantity from Phase I to IV,
Kundli IE for Existing CETP Capacity – 3927 KLD
Total Waste water Quantity from Phase III, IV, IV
sector-56 Kundli, IE for proposed CETP Capacity
– 5252 KLD
11 Project Cost
Total estimated cost including O&M, Power,
Chemicals, Sludge disposal and Departmental
Over head expenses will be Rs. 45.86 Crores and
Total Estimated capital investment will be Rs.
21.02 crores for the proposed CETP up-gradation
2.4.1 Infrastructure
This is up gradation of exiting Common Effluent Treatment Plant project. The existing
unit already has all the basic amenities like adequate industrial sheds, sanitation facilities,
drinking water arrangements, Restrooms, Canteen, first aid facility etc. HSIIDC has
established its own water supply arrangement for the Industrialist at HSIIDC IE Kundli.
There will be no separate designated temporary sites for construction workers.
2.4.2. Land Requirement
The proposed up gradation project shall be executed on the existing land only. The
total plot area of the project is 28,105 sq.m, which is 7 acre. The ownership of the
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land is with HSIIDC (IE) itself. Land documents is given as Annexure II. The land
use break up is provided below in Table-2.3.
TABLE-2.3 Land Use Breakup
S. No.
Particulars Existing (Sq.m)
Proposed (Sq.m)
Total (Sq.m)
%
1 Plant area 16,196.91 -- 16,196.91 57.63
2 Green Area 5,160.08 -- 5,160.08 18.36
3 Road &
footpaths 2,481.68
--
2,481.68 8.83
4 Others Open
area 4,266.33
--
4,266.33 15.18
5 Total 28,105 -- 28,105 100
2.4.3 Water Requirement
Total fresh water requirement for existing project is 3 KLD. For domestic purposes
0.6 KLD water will be required. HSIIDC has established its own water supply
arrangement for the Industrialist at HSIIDC IE Kundli. There will be use of some
water for the preparation of sensitive dosing chemicals to be used in the treatment
process to an extent of 2.4 KLD. After up gradation man power will be same, thus
water demand for domestic purposes will remain same. There will be use of some
water for the preparation of sensitive dosing chemicals to be used in the treatment
process to an extent of 3 KLD. The flow diagram of existing and proposed Water
Balance is shown in Fig. 2.5 (a) and Fig. 2.5 (b):-
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana Promoter: HSIIDC Limited Chapter-2 Project Description
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HSIIDC Limited Authorized Signatory
Figure – 2.5 (a) Existing Water Balance
Figure – 2.5 (b) Proposed Water Balance
393 KLD (10% losses)
Industrial Effluent 3927 KLD
Preparation of Dosing Chemicals 2.4 KLD
Total Fresh Water 3 KLD
Domestic use 0.6 KLD
Septic Tank Soak Pit 0.4 KLD
CETP 4 MLD Capacity
4,000 KLD Effluent
Treated Water
3,534 KLD
Recycle = 3,463
KLD
Conveyance Loss (2 %) =
71 KLD
Green Belt Development / industrial use for member industry
Phase I, II, III & IV
525 KLD (10% losses)
Industrial Effluent 5252KLD
Preparation of Dosing Chemicals 3
KLD Total Fresh Water 3 KLD
CETP 6 MLD Capacity
6000 KLD Effluent
TREATED
WATER 4727 KLD
Recycle
4632 KLD
Conveyance Loss (2 %) =
95 KLD
Green Belt Development/ industrial use for member industry
Phase III, IV and IV sector 56
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana Promoter: HSIIDC Limited Chapter-2 Project Description
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2.4.4 Power Requirement
Power requirement for the project is as under:-
Particulars Existing Proposed Total
Power and
Source
275 KW
UHBVN Supply
425 KW
UHBVN Supply
700 KW UHBVN
Supply
D.G. Set 300kVA
(200 kVA:1No.
+ 100 kVA:1No.)
500 kVA
(1No.)
3nos.
200kVA:1No.
100kVA:1No
500kVA:1No.
Fuel HSD: 15 l/ hr/ DG
set
HSD: 25 l/ h HSD: 15 l/ hr/ DG
set (200 kVA
100 KVA – 2 nos )
HSD: 25 l/ h DG
Set (1no. 500 kVA)
2.4.5 Manpower
Local workers will be hired from the nearby villages. The details of the existing and
proposed manpower are as under:-
Particulars Existing Proposed Total
Manpower 13 no 30 during
construction
phase
13 – operation
phase
30 – construction
phase
2.5 PROPOSED SCHEDULE AND APPROVAL FOR
IMPLEMENTATION
2.5.1 Proposed Schedule for Implementation
The implementation schedule for the proposed project is twenty four months from the
date of sanction.
2.5.2 Approval for Implementation
EIA for Up gradation of existing CETP from 4 MLD to 10 MLD capacity at Kundli, Sonipat, Haryana Promoter: HSIIDC Limited Chapter-2 Project Description
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The ground activities will be started after receipt of Environment Clearance from
MoEF&CC, New Delhi and subsequent Consent to Establish from Haryana State
Pollution Control Board.
2.6 TECHNOLOGY AND PROCESS DESCRIPTION OF COMMON
EFFLUENT TREATMENT PLANT
At present 4 MLD capacity CETP is functional for treated effluent of Indl Estate Kundli
(Phase I to IV). The treated effluent is being disposed off in drain no. 8 by pumping
system through 200 mm dia PVC pipe line. At present, the average inflow is approx. 4
MLD & will reach 5 MLD within a year. Presently, the Indl. Estate sector-38 Ph-I has
fully been developed and in Mega Food Park area, the maximum number of plots are
under construction. The present arrangement will be inadequate and needs to be
upgraded to treat the maximum discharge of 10 MLD.
The existing treatment process which has been adopted for the 4 MLD CETP which is
functioning is Extended Aeration process. The upgradation of the treatment plant has
been proposed using the similar treatment process so that there is a parity with the
existing system as well as the existing structures can be used to 5 the maximum
possible extent. Detailed design report has been prepared using the existing
Equalization tanks, Aeration system and Secondary clarifier system, which will be
augmented with new units which are necessary and compatible with the existing
structures has been mentioned hereunder. Moreover, Extended Aeration process which
is most technically and financially viable treatment process, has been recommended for
adoption as the treated effluent parameters even after secondary treatments meets the
Pollution Control Board norms at the lowest power consumption. The methods range
from physico- chemical to biological & in the latter group from aerobic to anaerobic.
RAW EFFLUENT CHARACTERISTICS
Member industries of CETP will be required to monitor specified quality parameters
and flow rate of the effluent on daily basis and to submit the monitoring data to the
CETP operator on regular basis. Continuous flow meters will also be installed at the
outlet of the CETP to monitor the outlet effluent quantity.
The effluent characteristics of mix type industrial units has been assessed as under for
designing of CETP. It is presumed that most of the industrial unit shall have their own
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treatment plants & shall have consent from Haryana state Pollution Control Board to
discharge treated effluent in to the common sewers. The values given in Table below,
are considered in design:
Influent Sewage Characteristics
S. No. Parameters Units
1 pH 6 - 8.5
2 BOD5, mg/ L 450
3 COD, mg/ L 900
4 TSS, mg/ L 1200
5 Coliform, MPN/100ml 1x107
6 Oil & Grease mg/L 100
7 Temperature, Co. 18-22
8 NH4- Nitrogen, mg/ L 45
9 TKN, mg/ L 40
10 TP as PO4, mg/ L 10
11 Chromium mg/L 5
12 COD/ BOD ratio 2
Treated effluent Characteristics after secondary Treatment
S. No. Parameters Units
1 pH 7-7.5
2 BOD5, mg/ L ≤10
3 COD, mg/ L ≤20
4 TSS, mg/ L ≤20
5 Coliform, MPN/100ml ≤10000
6 Oil & Grease mg/L ≤5
7 Temperature, Co. ≤1
8 NH4- Nitrogen, mg/ L ≤2
9 TP as PO4, mg/ L ≤0.1
10 Chromium mg/L >0.2
Treated effluent Characteristics after Tertiary Treatment
S. No. Parameters Units
1 pH 7-8.5
2 BOD5, mg/ L
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6 Oil & Grease mg/L
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1. Raw effluent intake & bar screen chamber
1 @ 30.0MLD Nil 30.0MLD
2. Collection cum-Pumping tank
2 @ 5.0MLD Nil 10.0MLD
3. Grit Chamber Nil 1 @ 30 MLD 30MLD
3. Receiving Chamber Nil 1 @ 30.0MLD 30 MLD
4. Mechanical Fine Screen Nil 1 @ 30.0MLD 30.0MLD
5. Collection cum Distribution Box
Nil 1 @ 30.0MLD 30.0MLD
6. Equalization Tank 1 @ 10.0MLD Nil 10.0MLD
7. Flash Mixer Nil 1 @ 10.0MLD 10.0MLD
8. Flocculator (Existing Primary Clarifier to be converted)
10.0MLD Nil 10.0MLD
9. Primary Clarifier Nil 10.0MLD 10.0MLD
10. Extended Aeration Reactor 2 @ 10.0MLD 2 @ 10.0MLD 40.0MLD
11. Secondary Clarifier 1 @ 10.0MLD 1 @ 10.0MLD 20.0MLD
12. Collection cum Distribution channel
1 @ 10.0MLD Nil 10.0MLD
13. Secondary Treated Effluent Collection Sump.
60 minutes as its retention Time
Nil 60 minutes as its retention
Time
14. Centrifuge 3 @ 10.0MLD Nil 30MLD
15. Pressure Filtration 1 @ 10MLD Nil 10 MLD
16. Activated Carbon Filter 1 @ 10 MLD Nil 10.0MLD
17. Disinfection. 1 @ 10.0MLD Nil 10.0MLD
Selection of Treatment Process
The existing treatment process which has been adopted for the 4 MLD CETP which is
functioning is Extended Aeration process. The up-gradation of the treatment plant has
been proposed using the similar treatment process so that there is a parity with the
existing system as well as the existing structures can be used to the maximum possible
extent. Detailed design report has been prepared using the existing Equalization tanks,
Aeration system and Secondary clarifier system, which will be augmented with new
units which are necessary and compatible with the existing structures has been
mentioned hereunder. Moreover, Extended Aeration process which is most technically
and financially viable treatment process, has been recommended for adoption as the
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treated effluent parameters even after secondary treatments meets the Pollution
Control Board norms at the lowest power consumption.
Some Waste Water Treatment Methods & their Characteristics:-
The methods range from physico- chemical to biological & in the latter group from
aerobic to anaerobic. The quick overview for the same is given as hereunder: -
Treatment Methods Biological Physical Chemical Aerobic Anaerobic Suspended Growth Attached Growth Suspended
Growth Attached Growth
Activated Sludge Trickling Filters UASB Moving Bed Bio Reactors
Screening & Grit Removal
Extended Aeration Rotating Bio Reactors
Anaerobic ponds.
Submerged Bio Reactors.
Coagulation
Aerated Lagoons Land treatment. Flocculation Waste Stabilization ponds.
Roof Zone Reed Beds
Settling
Sequential Batch Reactor.
Vermistabilization Sludge Thickening.
Membrane Bio Reactor.
Moving Bed Bio Reactors
Sludge dewatering
Submerged Bio Reactors.
Filtration.
Colour Removal Chlorination De chlorination Ion Exchange softening
or Demineralization. Ultra Filtration Reverse Osmosis
Sewage Treatment Processes may be generally classified as Primary, Secondary &
Tertiary. The general yard stick of evaluating a performance of sewage treatment plants
is the degree of reduction of BOD as such & total coliforms.
The selection of process will depend upon whether primary, secondary or tertiary
treatment is required to meet with the parameters prescribed by the respective pollution
control boards or local bodies whichever is stricter. In addition environment impact &
other consideration in planning treatment facilities are required to be considered for
selection of processes are illustrated as here under: -
a) Environment Impact Considerations: -
- Downstream hydrology & aquatic ecosystem.
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- Ground water pollution potential.
- Odour, aerosol spray, mosquito nuisance.
- Effect on nearby land use & land values.
- Rehabilitation of effected people.
- Discharge Standards.
- Toxic in food chain.
- Nitrates & Chemical pollution of water resources.
- Bathing water quality.
- Health of plant operators/ farm workers.
- Plant operation & maintenance aspects.
- Green belt & land escaping.
b) Engineering & Site considerations: -
- Selection of design period.
- Sufficiency of site area available.
- Topography of the general area to be served, location of pumping station & contours
at the available site.
- Available hydraulic head, high flood level, level of the irrigation land or HFL of the
available drain/ water body receiving the treated effluent.
- Ground water depth & land disposal facility of treated effluent.
- Soil Bearing Capacity & type of strata at the proposed site.
c) Process performance, energy, operation & maintenance: -
Process considerations involve below mentioned factors which affect the choice of
treatment methods & design criteria: -
- Waste water flow & characteristics.
- Degree of treatment required.
- Performance fluctuations, sustainability & reliability.
- Land availability.
- Power availability.
- Operating equipments requirements & its indigenous availability.
- Skilled staff availability.
- Extent of sludge production & disposal requirements.
- Loss of head through plant & available head.
- Ease of stage wise extension of plant with time.
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- Energy conservations.
- Energy/ power generations.
- Carbon Credit as per KYOTO Protocol.
Proposed Treatment Process:
It is stipulated that the proposed CETP shall be based on physical & chemical treatment
for removal of excessive inorganic COD, TSS & BOD5 beside removal of color &
maintenance of equalized & constant PH & Flow rate prior to biological process i.e.
Activated Sludge process based on extended aeration principal. That after biological
Treatment process Treated effluent shall be further treated in pressure Filter, Carbon
filter and shall be disinfected with chlorine before final disposal in drain.
A. Physical Treatment
The existing system has structures which needs to be improvised with new structures to
meet the requirement of the CETP.
The adequacy of the existing structures has been checked only those modifications/
additional structures are proposed which are essentially required.
However, the replacement of existing electromechanical equipment’s has been
proposed since the same has outlived its performance period and the material of
construction has been used as Mild Steel which has been corroded.
The details of the structures included in the CETP is given below:
Inlet Pipe: - The existing inlet pipe is of size 800 mm diameter. The invert of the inlet
pipe is 196.0 m. The inlet pipe has been found to be adequate to discharge peak flow (3
times the average flow) at a velocity of 0.7 m/sec.
Receiving chamber:- The existing Receiving chamber is of size 3m x 1m x 5.5 m
depth. The chamber is capable of accommodating flow for 30 seconds. Hence no
additional Receiving chamber has been proposed.
Coarse Screen chamber:- The existing coarse screen chamber is of size 6m x 4m x 5
m deep. It is proposed to convert the existing Screen chamber to mechanical coarse
screen chamber. The present structure can be modified by constructing concrete
partition walls to accommodate 3 nos. mechanical Coarse Screen (2W mechanical + 1
SB mechanical ) suitable for channel size 6.0 m x 1.16 m x 0.7 SWD + 0.3 FB.
Effluent Inlet Sump:- At present there is a circular Effluent Inlet chamber which is
pumping effluent directly to the Equalization Chamber. The size is 10m dia. + 3 m
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SWD. The existing size is adequate to accommodate effluent for HRT 10 min at peak
flow of 30 MLD. The Effluent Inlet sump will be utilized to pump effluent to the fine
screen chamber.
Replacement of existing submersible pumps with non-clog submersible sewage pumps
as here under have been proposed: - 417 M^3/ Hr. @ 15MWC, 4Nos. (3W+1SB).
Non clog submersible sewage pumps have been proposed keeping in view the depth of
the incoming sewer and high water table.
Mechanical fine screen, oil and grease trap:- There is no existing fine screen
chamber with oil and grease trap. Therefore a new mechanical Fine screen chamber 3
nos (2 W+1 SB) is proposed with oil and grease trap to accommodate flow of 10 MLD
with 3.0 peak factor.
Equalization Tank:- There is an existing Equalization tank of size 27 m diameter and
SWD 3.75 m. The tank can accommodate average flow of 416.67 m3/hr for 5 hours. It
is proposed to utilize the existing Equalization tank as there will be intermittent
discharge of different characteristics from mix of industries. It is proposed to install air
diffusing system like aspirators in the Equalization tank to enhance the oxidation
process of the pollutants. Thereafter the equalized effluent shall be pumped in to the
flash mixer. Replacement of all existing effluent pump has been proposed in the DPR
as the capacity of the pumps has been enhanced for 10 MLD plant.
B. Chemical Treatment
Flash Mixer:- At present there is no flash mixer is installed. The equalized effluent is
being pumped to the existing primary clarifier. It is proposed to construct a flash mixer
of size 2.55m x1.70m x 1.5m SWD + 0.40m FB. The equalized effluent will be pumped
into the flash mixer for mixing of ferrous alum & lime. It is proposed to convert the
existing Primary Clarifier of 13m dia. and 3.0 m SWD into a Flocculator. The
coagulated effluent from the Flash mixer shall flow into the Flocculator with concentric
flocculation unit after addition of fast settling chemical viz. Polyelectrolyte.
Flocculator:- A separate Primary Clarifier has been proposed to be built besides the
existing one. The same has been proposed because the existing Primary clarifier is
inadequate to handle the effluent of 10 MLD. As mentioned above the existing Primacy
clarifier – 1 no. will be converted into a flocculator. In the Flocculator, the effluent
mixed with ferrous sulphate, ferrous chloride and Lime solution in the flash mixer will
result in formation of flocs. Addition of polyelectrolyte is also proposed to thicken the
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flocs. Though a flocculator is designed for 30 min HRT but the existing structure will
provide an HRT of 55 min which will add efficiency to the system. The size of the
Flocculator designed for HRT 55 minutes is 13 m dia. x 3 m SWD.- 1 no.
Primary Clarifier:- A clarifier is a settling zone where the flocs formed at the
flocculator settles. A new Primary clarifier is proposed besides the existing structure to
allow clarification of the incoming effluent. The size of the Clarfication unit is circular
tank of 21.2 m diameter and 3.0 m SWD. This physically & Chemically treatment shall
remove colour, oil & Grease, correct PH, remove TSS at least by 70% & COD/ BOD5
by 50/ 30% respectively.
Effluent Characteristics after primary Treatment.
BOD5, mg/L 360.00
TSS , mg/L 540.00
COD, mg/ L 675.00
C. Biological Treatment
Aeration Tank:- At present there are two nos. of rectangular Aeration tank of size
43m x 13m x 3m SWD. The existing tanks are inadequate to handle 10 MLD effluent.
Hence it is proposed to provide further 2 nos. Aeration tank of length 43m x 22m x
3m SWD. This physically & Chemically treated effluent shall fl