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PROPOSAL FOR OBTAINING
TERMS OF REFERENCE
FOR
“PROPOSED COMMON EFFLUENT TREATMENT PLANT" {Category A (due to presence of Bir Bara Ban Wildlife Sanctuary at a distance of 1.16 km towards SE) under
Item ‘7 (h)’ Common Effluent Treatment Plants (CETPs) of Schedule of EIA Notification, 2006 and its
subsequent amendments till date 19th December’ 2018}
Location:-Rectangle No.-24, Khasra No. -25/1, HSIIDC Industrial Estate Hansi Road, Near Vita Plant, Jind, Haryana
Project Capacity:-0.5 MLD; Area: - 2,711.39 Sq.m (0.67 Acre)
Work Order No. – HSIIDC:IA:AMB:2018:2080 Dated:- 24.07.2018
Baseline Data Generation : March’2021 to May’2021(Summer Season)
Project Cost : Rs. 581.76 Lacs
PROMOTER ENVIRONMENTAL CONSULTANT
Haryana State Industrial and Infrastructure
Development Corporation (HSIIDC) Ltd.
HSIIDC Industrial Estate, Near Harihal Chowk,
Narwana-Hisar Road, Narwana
Project In-charge:-Sh. Amandeep (Manager-
Engineer)
E-mail:[email protected]
Gaurang Environmental Solutions Pvt. Ltd.
#102, SNG Shree Ratna Apartment, Peetal Factory,
Jhotwara Road, Bani Park, Jaipur-302016
E-mail: [email protected]
NABET Accreditation: NABET/EIA/2023/RA 0192
dated 01.02.2021 valid up to 19.01.2023.
July’ 2021
Project : Common Effluent Treatment Plant, Jind
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
INDEMNIFICATION
Project : Common Effluent Treatment Plant, Jind
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
INDEMNIFICATION
Utmost care has been taken in preparation of this Report vis a vis proposed “Common
Effluent Treatment Plant” of 0.5 MLD capacity based on Extended Aeration System at
Jind, Haryana promoted by M/s HSIIDC Limited. The data incorporated in the report is
generated through information received from clients in form of their project report
received through e-mail, secondary information, besides stakeholder’s interaction and
inputs. Due care has been taken to represent facts and figures and sources acknowledged.
The purpose of this document is to facilitate environmental appraisal of the proposal and
as such the exercise has been scientifically carried out. The Consultant stand indemnified
against any consequences arising out of any inadvertent omissions.
REVISION HISTORY
Report No. GESPL_259 /ToR/2019/ 53
Type of report For Terms of Reference
Revision No. 01
Issue to HSIIDC Limited
Issue Date 02.07.2021
Project : Common Effluent Treatment Plant, Jind
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
DETAILS OF STUDIES
CONDUCTED FOR THE
PROJECT
Project : Common Effluent Treatment Plant at Jind, Haryana Details of Studies
Conducted for the Project Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
DETAILS OF STUDIES CONDUCTED FOR THE PROJECT
Name of the Project:-Proposed CETP of 0.5 MLD capacity based on Extended Aeration System at
Jind, Haryana
Location:-Rectangle No.-24, Khasra No-25/ 1, HSIIDC Industrial Estate Hansi Road, Near Vita Plant,
Jind, Haryana
Nature of
consultancy
Name and address of the Consultant/
Expert
Approvals, if any from
(NABL/DGMS/IBM/
NRBPT/MOEF/CPCB/others
etc)*, give reference
EIA/ EMP
Organization
Gaurang Environmental Solutions Pvt. Ltd.
#102, SNG Shri Ratna Apartment, Peetal
Factory, Jhotwara Road, Jaipur-302016
E-mail :[email protected]
NABET/ EIA/ 2023/ RA 0192
dated 01.02.2021 valid up to
19.01.2023.
EIA Coordinator Haneesh Panicker
FAE-LU Vinod Kumar Verma
FAE-AP Sanjay Palnitkar
Nidhi Bhardwaj
FAE-AQ Mallikarjun Guttula
Neha Bhargava
FAE-WP Sanjay Palnitkar
Haneesh Panicker
FAE-SC Ratnakumar V Mudliar
FAE-EB Dr. Yati Kachhawa
Ginni Barotia
FAE-NV Sanagapati C. Babu
Mallikarjun Guttula
FAE-SE Gajendra Singh Rathore
FAE-HG Mukesh Suroliya
Vidya Bhushan Trivedi
FAE-GEO Mukesh Suroliya
Vidya Bhushan Trivedi
Project : Common Effluent Treatment Plant at Jind, Haryana Details of Studies
Conducted for the Project Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
FAE-RH Sanjay Palnitkar
Ginni Barotia
FAE-SHW Sanjay Palnitkar
Nidhi Bhardwaj
Environmental
Monitoring &
analysis
Hydro geological
study
Soil Investigation
Mining Plan
Rainwater
Harvesting
Risk Assessment
Architectural Plan
Ground Vibration
Study
Subsidence Study
Services (STP/ETP
design) etc.
Others, such as
project consultants
etc.
* Only Govt. /Statutory Approvals to be mentioned. Put NA where not applicable.
** Team Member
Project : :Common Effluent Treatment Plant, Jind
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd Page
Report Ref: GESPL_259 /ToR/2019/ 53
S. No Particular Page No.
1 SECTION 1 - EXECUTIVE SUMMARY 1
1.1 EXECUTIVE SUMMARY 2
2 SECTION-II INTRODUCTION TO THE PROJECT/
BACKGROUND INFORMATION
5
2.1 IDENTIFICATION OF PROJECT AND PROJECT PROPONENT 6
2.1.1 IDENTIFICATION OF PROJECT 6
2.1.2 PROJECT PROPONENT 6
2.2 BRIEF DESCRIPTION OF NATURE OF THE PROJECT 7
2.3 NEED FOR THE PROJECT AND ITS IMPORTANCE TO THE
COUNTRY AND OR REGION
7
2.4 DEMAND AND SUPPLY GAP 8
2.5 IMPORTS VERSUS INDIGENOUS PRODUCTION 9
2.6 EXPORT POSSIBILITY 9
2.7 DOMESTIC/EXPORT MARKET 9
2.8 EMPLOYMENT GENERATION (DIRECT AND INDIRECT) DUE
TO THE PROJECT
9
3 SECTION-III PROJECT DESCRIPTION 10
3.1 TYPE OF PROJECT INCLUDING INTERLINKED AND
INTERDEPENDENT PROJECTS, IF ANY
11
3.2 LOCATION (MAP SHOWING GENERAL LOCATION, SPECIFIC
LOCATION, AND PROJECT BOUNDARY AND PROJECT SITE
LAYOUT) WITH COORDINATES
11
3.3 DETAILS OF ALTERNATE SITES CONSIDERED AND THE
BASIS OF SELECTING THE PROPOSED SITE, PARTICULARLY
THE ENVIRONMENTAL CONSIDERATIONS GONE INTO
SHOULD BE HIGHLIGHTED
14
3.4 SIZE / MAGNITUDE OF OPERATION 15
3.5 PROJECT DESCRIPTION WITH PROCESS DETAILS (A
SCHEMATIC DIAGRAM/FLOW CHART SHOWING THE
15
Project : :Common Effluent Treatment Plant, Jind
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd Page
Report Ref: GESPL_259 /ToR/2019/ 53
PROJECT LAYOUT, COMPONENTS OF THE PROJECT ETC.
SHOULD BE GIVEN)
3.6 RAW MATERIAL REQUIRED ALONG WITH ESTIMATED
QUANTITY, LIKELY SOURCE, MARKETING AREA OF FINAL
PRODUCT/S, MODE OF TRANSPORT OF RAW MATERIAL
AND
FINISHED PRODUCT
37
3.6.1 RAW MATERIAL 37
3.6.2 PRODUCT 37
3.7 RESOURCE OPTIMIZATION/RECYCLING AND REUSE
ENVISAGED IN THE PROJECT, IF ANY, SHOULD BE BRIEFLY
OUTLINED
38
3.8 AVAILABILITY OF WATER, ITS SOURCE, ENERGY / POWER
REQUIREMENT AND SOURCESHOULD BE GIVEN
38
3.8.1 WATER AVAILABILITY & ITS SOURCE 38
3.8.2 ENERGY / POWER REQUIREMENT& ITS SOURCE 39
3.9 QUANTITY OF WASTES TO BE GENERATED (LIQUID AND
SOLID) AND SCHEME FOR THEIR MANAGEMENT /
DISPOSAL
39
3.9.1 QUANTITY OF LIQUID WASTE TO BE GENERATED & ITS
MANAGEMENT / DISPOSAL
39
3.9.1.1 Domestic Waste Water 39
3.9.1.2 Industrial Waste Water 39
3.9.2 QUANTITY OF SOLID WASTE TO BE GENERATED & ITS
MANAGEMENT / DISPOSAL
40
3.10 SCHEMATIC REPRESENTATIONS OF THE FEASIBILITY
DRAWING WHICH GIVE INFORMATION OF EIA PURPOSE
41
4 SECTION-IV SITE ANALYSIS 43
4.1 CONNECTIVITY 44
4.2 LAND FORM, LAND USE AND LAND OWNERSHIP 44
Project : :Common Effluent Treatment Plant, Jind
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd Page
Report Ref: GESPL_259 /ToR/2019/ 53
4.3 TOPOGRAPHY (ALONG WITH MAP) 45
4.4 EXISTING LAND USE PATTERN (AGRICULTURE, NON-
AGRICULTURE, FOREST, WATER BODIES (INCLUDING AREA
UNDER CRZ)), SHORTEST DISTANCES FROM THE
PERIPHERY OF THE PROJECT TO PERIPHERY OF THE
FOREST, NATIONAL PARK, WILD LIFE SANCTUARY, ECO
SENSITIVE AREA, WATER BODIES (DISTANCE FROM THE
HFL OF THE RIVER), CRZ.
45
4.5 EXISTING INFRASTRUCTURE 46
4.5.1 BASIC AMENITIES 47
4.5.2 INDUSTRIES 47
4.6 SOIL CLASSIFICATION 47
4.7 CLIMATIC DATA FROM SECONDARY SOURCES 48
4.8 SOCIAL INFRASTRUCTURE AVAILABLE 48
5 SECTION –V PLANNING BRIEF 50
5.1 PLANNING CONCEPT (TYPE OF INDUSTRIES, FACILITIES,
TRANSPORTATION ETC) TOWN AND COUNTRY PLANNING/
DEVELOPMENT AUTHORITY CLASSIFICATION
51
5.2 POPULATION PROJECTION 51
5.3 LAND USE PLANNING (BREAKUP ALONG WITH GREEN
BELT (ETC.)
51
5.4 ASSESSMENT OF INFRASTRUCTURE DEMAND (PHYSICAL &
SOCIAL)
52
5.5 AMENITIES / FACILITIES 53
6 SECTION-VI PROPOSED INFRASTRUCTURE 54
6.1 PROPOSED INFRASTRUCTURE 55
7 SECTION –VII REHABILITATION AND RESETTLEMENT (R
& R) PLAN
57
7.1 POLICY TO BE ADOPTED (CENTRAL/ STATE) IN RESPECT OF
THE PROJECT AFFECTED PERSONS INCLUDING HOME
58
Project : :Common Effluent Treatment Plant, Jind
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd Page
Report Ref: GESPL_259 /ToR/2019/ 53
***************
OUSTEES, LAND OUSTEES AND LANDLESS LABORERS (A
BRIEF OUTLINE TO BE GIVEN).
8 SECTION –VIII PROJECT SCHEDULE & COST ESTIMATES 59
8.1 LIKELY DATE OF START OF CONSTRUCTION AND LIKELY
DATE OF COMPLETION
60
8.2 PROJECT COST ESTIMATION 60
9 SECTION-IX ANALYSIS OF PROPOSAL 62
9.1 FINANCIAL AND SOCIAL BENEFITS WITH SPECIAL
EMPHASIS ON THEBENEFIT TO THE LOCAL PEOPLE
INCLUDING TRIBAL POPULATION, IF ANY, IN THE AREA
63
Project : Common Effluent Treatment Plant, Jind
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
PRE-FEASIBILITY
REPORT
Project : Common Effluent Treatment Plant, Jind Section -I
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 1
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION – I
Project :Common Effluent Treatment Plant, Jind Section-I
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 2
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION-I
EXECUTIVE SUMMARY
1.1 EXECUTIVE SUMMARY
The concept of effluent treatment, by means, of a collective effort, has assumed
reasonable gravity by being especially purposeful for cluster of small scale industrial
units. Common effluent treatment plant (CETP) not only helps the industries in easier
control of pollution, but also act as a step towards cleaner environment and service to the
society at large. Small scale industries, by their very nature of job cannot benefit much
from economies of scale and therefore the burden of installing & operating pollution-
control equipment, falls heavy on them. Realizing this practical problem, under the policy
statement for abatement of pollution the Government extends the scheme for promoting
combined facilities for treatment of effluent for clusters of small scale industrial units and
also to provide technical support to them. The concerted approach of common effluent
treatment provisions has many advantages. Wastewater of individual industries often
contain significant concentration of pollutants; and to reduce them by individual
treatment up to the desired concentration, becomes techno-economically difficult The
combined treatment provides a better and economical option because of the equalization
and neutralization taking place in the CETP. Other important issues for the merit of
common treatment include scarcity of land at the industry's level and a comparatively
easier availability of professional and trained staff for the operation of CETP, which is
otherwise difficult, at the individual industry level. For the regulatory authorities also,
common treatment facility offers a comparatively easier means of ensuring compliance of
stipulated norms.
HSIIDC had setup Industrial Estate at Jind in the proposed area of 24.93 Acres. Details of
HSIIDC Industrial Estate area is as under:-
Table 1.1: Details of HSIIDC Industrial Estate Area
Particulars Area (Acre)
Industrial Plots 18.38
Green Belt 1.271
Road Area 5.282
Total 24.93
Project :Common Effluent Treatment Plant, Jind Section-I
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 3
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
The industrial plots were allotted with basic Infrastructure facilities. Details of industrial
plots are as under:-
Table 1.2: Details of Plots
Area (Acre) No. of Plots
0.5 14
0.25 20
0.125 43
Others 6
Total 83
The detailed calculation for the effluent discharge has been made and turns out to be
0.264 MLD and accordingly CETP of 0.3 MLD was proposed. It has been revised by the
HSIIDC and it is expected that sum neighboring areas will also get added and the
discharge is likely to increase thus it was proposed by HSIIDC to construct 0.5 MLD
capacity new CETP at Rectangle No.-24, Khasra No-25/ 1, HSIIDC Industrial Estate
Hansi Road, Near Vita Plant, Jind, Haryana. The total plot area for proposed CETP will
be 2,711.39 Sq. m (0.67 Acre). The total capital investment for the proposed CETP will
be Rs. 581.76 Lacs.
There is already 0.1 MLD CETP (up to secondary treatment) situated within HSIIDC IE,
Jind on another site. The same will be dismantled after the commissioning of proposed
0.5 MLD CETP at HSIIDC IE, Jind.
Waste water generated from the associated industries will be collected through dedicated
pipeline system after meeting the Preliminary treatment (based on specific requirements)
discharge standards prescribed by MoEF&CC, CPCB & HSPCB.T he waste water after
treatment shall meet the discharge standards laid down by HSPCB.
The treated water will be utilized in greenbelt development. In addition member
industries will also be permitted to use treated recycled water as per requirement.
The proposed project activity is listed at Category – “B” under item 7 (h) Common
Effluent Treatment Plant as per the EIA Notification, 2006.
However, Due to the presence of Bir Bara Ban Wildlife Sanctuary at a distance of 1.16
km towards SE the project will be categorized as A and considered at MoEF&CC, New
Delhi. Bir Bara Ban Wildlife sanctuary was de-notified and declared as Conservation
Project :Common Effluent Treatment Plant, Jind Section-I
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 4
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
Reserve vide Haryana Govt. Notification No. S.O. 78/C.A.53/72/S.18 and 36-A/2007
dated 11.10.2007. Enclosed as Annexure – I.
As per Wildlife (Protection) Act, 1972 Section [2(24A) “protected area” means a
National Park, a sanctuary, a conservation reserve or a community reserve notified
under sections 18, 35, 36A and 36C of the Act;]. Enclosed as Annexure – II.
In reference to that NBWL application has been applied vide proposal no FP/ HR/ IND/
5881/ 2021 dated 05.07.2021 for requisite clearance. Copy of the same is enclosed as
Annexure-III.
The project details are summarized as under:-
Table 1.3: Project Details
S. No. Particulars Details
1. Total area of Industrial Estate, Jind 1,00,888.13 Sq. m (24.93 Acres)
2. Total area for CETP (sq. m.) 2,711.39 Sq. m (0.67 Acre)
3. Address/ Location/ land details (Khasra
no.)
Rectangle No.-24, Khasra No-25/1, HSIIDC
Industrial Estate Hansi Road, Near Vita Plant,
Jind, Haryana
4. CETP capacity 0.5MLD (500 KLD)
5. Water requirement (KLD) & Source Total Fresh water Demand – 0.8 KLD
Domestic Purposes – 0.6 KLD
Chemical Dosing – 0.2 KLD
Source: HSIIDC IE,Jind
6. Power requirement and source Power demand : 80 kVA
Source: DHBVN
7. Back up source and Fuel DG set -100 kVA (1No.)
Fuel – HSD
Source: Nearby Petrol pump
Consumption – 20 l/hr
8. Employment generation During Construction phase – 30 persons
During Operation phase – 15 persons
Total – 45 persons
*********
Project : Common Effluent Treatment Plant, Jind Section - II
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 5
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION – II
Project: Common Effluent Treatment Plant, Jind Section-II
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 6
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION-II
INTRODUCTION TO THE PROJECT/ BACKGROUND INFORMATION
2.1 IDENTIFICATION OF PROJECT AND PROJECT PROPONENT
2.1.1 IDENTIFICATION OF PROJECT
HSIIDC has proposed Common Effluent Treatment Plant (CETP) having 0.5 MLD
capacity coming up at Rectangle No.-24, Khasra No-25/1, HSIIDC Industrial Estate
Hansi Road, Near Vita Plant, Jind, Haryana to treat waste water from member industries
situated at Industrial Estate, Jind and sum neighboring areas. The rapid growth of
industries in an Industrial Estate. The details of which are as under:-
Name of Industrial Estate Number of Plots Area (Acre)
Jind 83 24.93
2.1.2 PROJECT PROPONENT
In the pursuit of prosperity in Haryana, pioneering role has been played by the Haryana
State Industrial and Infrastructure Development Corporation Limited (HSIIDC). One of
the leading contributors to the wellbeing and progress of the state, HSIIDC has been
instrumental in bringing about a major change in the people of Haryana over the years.
The pioneering zeal of HSIIDC has facilitated the transformations of Haryana from a
primarily agrarian society to one of the most highly industrialized states of modern India.
HSIIDC was setup in 1967 for promoting medium and large-scale industries so as to
ensure balanced regional development of Haryana by acting as an Institutional
Entrepreneur and a financial institution. HSIIDC serves as the single most important
platform for providing services in the following areas:-
HSIIDC is nodal agency of Government of Haryana to develop industries at the
industrial estates after necessary infrastructure developments such as road & drainage
network, water supply and power linkage for the industrial estate.
Providing financial assistance in terms of terms loans, equipment, finance/ leasing
and working capital.
Infrastructural development in the state of Haryana.
Performing agency functions on behalf of the state Government.
Project: Common Effluent Treatment Plant, Jind Section-II
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 7
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
Performing agency functions for entrepreneurs and established industries for
enhancement of capacity/modernization.
Success entrepreneurs will take separate linkage as per the requirement of industry
and environment clearance.
HSIIDC is a Public Limited Company wholly owned by the Government of Haryana, set
up as a catalyst for promoting and accelerating the pace of industrialization in the State.
The corporation provides a wide spectrum of financial services under one roof – the
concept being “Total Financial Support” for its clientele. Being an intrinsically customer
– oriented organization. HSIIDC has often gone beyond in helping to shape to the destiny
and vision of thousands of entrepreneurs. It has generally taken on the role of a trusted
friends and guide, providing crucial support and most important of all, created an
environment where nascent projects are able to attain their function and become vibrant
industries. The details of the project proponent are given below:-
Name of the Promoter HSIIDC Limited
Name and address of
the Promoter
Sh. Amandeep (Manager-Engineer)
HSIIDC Industrial Estate, Near Harihal Chowk,
Narwana-Hisar Road, Narwana
Status of Project Greenfield Project
E-mail Id [email protected]
Contact Number +91-7988707558
2.2 BRIEF DESCRIPTION OF NATURE OF THE PROJECT
It is proposed Common Effluent Treatment Plant (CETP) of 0.5 MLD capacity.
The proposal is to set up the CETP of 0.5 MLD for the effluent from member industries
located in Industrial Estate, Jind and sum neighboring areas. There will be dedicated
closed circuit pipeline network system for the effluent to be received at CETP.
2.3 NEED FOR THE PROJECT AND ITS IMPORTANCE TO THE
COUNTRY AND OR REGION
Establishment of effluent treatment plants for individual industries especially in the small
scale sector in the various industrial estates in India, to generate the effluent of desired
quality before discharge is not feasible in the Indian context. Firstly, because it is
Project: Common Effluent Treatment Plant, Jind Section-II
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 8
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
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 it can 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, and 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.
The Objective of setting up of CETP is:
To Achieve Economy of scale in waste treatment, thereby reducing the cost of
pollution abatement for individual industry.
To take care of the problem of lack of technical assistance and trained personnel as
needed for skill operation of effluent treatment plant.
To solve the problem of lack of space as the centralized facility can be planned in
advance to ensure that adequate space is available
To reduce the problem of monitoring by the pollution control boards.
To organize the appropriate disposal of treated waste water including reuse and
sludge generated to authorized facility
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.
2.4 DEMAND AND SUPPLY GAP
Govt. of India had sanctioned many Growth Centers in different parts of the country to
provide Industrial Infrastructure for industrialization and creating employments in
backward regions.
Keeping in view the fast industrial development in the area and to meet the growing
demand, it is proposed set up of Common Effluent Treatment Plant (CETPs) where the
effluents, generated from a number of small to medium enterprises in HSIIDC Industrial
Project: Common Effluent Treatment Plant, Jind Section-II
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 9
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
Estate, Jind and sum neighboring areasis suitably treated as per the prescribed procedure
& norms laid down in the regulation.
2.5 IMPORTS VERSUS INDIGENOUS PRODUCTION
Raw material required for treatment of waste water from member industries will be
available from local sources/surrounding area.
2.6 EXPORT POSSIBILITY
Not applicable as company will provide service of effluent treatment comes from its
member industries and final disposal of treated effluent.
2.7 DOMESTIC/EXPORT MARKET
Not applicable, as HSIIDC will provide service of effluent treatment coming from
respective member industries and its final disposal of treated effluent.
2.8 EMPLOYMENT GENERATION (DIRECT AND INDIRECT) DUE TO
THE PROJECT
The proposed project will provide direct employment during construction & operational
phase. Local workers will be hired from the nearby villages based on the requirement and
its fulfillment criteria. The details are given below:-
Table 2.1: Employment Details
S. No. Particulars Numbers
1 Construction Phase 30
2 Operation Phase 15
Total 45
*********
Project : Common Effluent Treatment Plant, Jind Section - III
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 10
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION – III
Project : Common Effluent Treatment Plant, Jind Section - III
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 11
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION-III
PROJECT DESCRIPTION
3.1 TYPE OF PROJECT INCLUDING INTERLINKED AND
INTERDEPENDENT PROJECTS, IF ANY
HSIIDC has proposed Common Effluent Treatment Plant (CETP) of 0.5 MLD capacity
will be constructed on 2,711.39 sq.m (0.67 Acre) area at Rectangle No.-24, Khasra No-
25/1, HSIIDC Industrial Estate Hansi Road, Near Vita Plant, Jind, Haryana.
There is no interlinked project. The proposed project is an individual project.
3.2 LOCATION (MAP SHOWING GENERAL LOCATION, SPECIFIC
LOCATION, AND PROJECT BOUNDARY AND PROJECT SITE
LAYOUT) WITH COORDINATES
The proposed Common Effluent Treatment Plant is coming up atRectangle No.-24,
Khasra No-25/1, HSIIDC Industrial Estate Hansi Road, Near Vita Plant, Jind, Haryana.
The project site falls on Geological Survey of India Toposheet No. 53 C/7. The latitude
and longitude of the project site are as given below:-
Table 3.1: Geographical Coordinates of the Project Site
1.Point 1
Latitude : 29°18'57.07"N
Longitude : 76°17'28.07"E
2.Point 2
Latitude : 29°18'56.16"N
Longitude : 76°17'28.87"E
3.Point 3
Latitude : 29°18'55.34"N
Longitude : 76°17'28.34"E
4.Point 4
Latitude : 29°18'56.29"N
Longitude : 76°17'26.65"E
5.Point 5
Latitude : 29°18'57.14"N
Longitude : 76°17'26.67"E
Project : Common Effluent Treatment Plant, Jind Section - III
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 12
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
Figure 3.1: Location Map
Figure 3.2: Topographical Map of 10 km radius
Project : Common Effluent Treatment Plant, Jind Section - III
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 13
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
Figure 3.3: Map showing location of project site on Google Map
Project : Common Effluent Treatment Plant, Jind Section - III
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 14
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
Figure 3.4: Site Photographs of proposed CETP
3.3 DETAILS OF ALTERNATE SITES CONSIDERED AND THE BASIS
OF SELECTING THE PROPOSED SITE, PARTICULARLY THE
ENVIRONMENTAL CONSIDERATIONS GONE INTO SHOULD BE
HIGHLIGHTED
The Project Proponent has not considered any alternate site; as proposed CETP is coming
up in Rectangle No.-24, Khasra No-25/1, HSIIDC Industrial Estate Hansi Road, Near
Vita Plant, Jind, Haryana. The land available for proposed CETP will be 2,711.39 sq.m
(0.67 Acre) area.
Project : Common Effluent Treatment Plant, Jind Section - III
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Possession of land was taken over by HSIIDC Chandigarh on dated 18.05.1977 and
Mutation of this land was done in favor of HSIIDC on dated 28.10.1987. Land
documents are enclosed as Annexure-IV.
The site is having required infrastructure facilities in form of water, electricity and Road
available for the proposed activities.
3.4 SIZE / MAGNITUDE OF OPERATION
The size and magnitude is as given below:-
Table 3.2: Size/ Magnitude of Operation
Particulars Total
Total area for CETP (sq. m.) 2,711.39 sq.m (0.67 Acre)
CETP capacity 0.5 MLD
3.5 PROJECT DESCRIPTION WITH PROCESS DETAILS (A
SCHEMATIC DIAGRAM/FLOW CHART SHOWING THE
PROJECT LAYOUT, COMPONENTS OF THE PROJECT ETC.
SHOULD BE GIVEN)
Proposed Common Effluent Treatment Plant (CETP) of 0.5 MLD capacity will be
constructed to treat the industrial waste water for the HSIIDC Industrial Estate, Jind and
sum neighboring areas.
The Common Effluent Treatment Plant shall be designed to treat the raw Effluent in a
single stage fully automatic Plant based on Extended Aeration Technology followed by
Tertiary Treatment. The following inlet and outlet effluent characteristics for proposed
CETP are as under:-
Table 3.3: Inlet and Outlet Effluent Characteristics for proposed CETP
INLET PARAMETERS
Description Unit Values
pH 5.5 – 9.0
BOD mg/l 750
COD mg/l 2000
TSS mg/l 1500
Oil and Grease mg/l 100
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OUTLET PARAMETERS
pH 6.5.8.5
BOD mg/l <5
COD mg/l <50
TSS mg/l <5
Oil and Grease mg/l <5
Source:- DPR
TREATMENT OPTIONS
The methods for treatment of sewer effluent ranges from physico, chemicals and
biological as depicted below:-
S. No. Details
a) Physico- Chemicals
I Screen & grit removal
II Sedimentation
III Sludge Thickeners
IV Vacuum Filters
V Centrifuges
b) Biological
I Anaerobic
a) Contact beds
b) UASB (up flow anaerobic sludge blanket)
c) Sludge Digesters
d) Anaerobic Ponds
II Aerobic
a) Moving bed bio reactor
Plasma treatment
b) Suspended
Activated Sludge
Extended Aeration
Aerated Lagoons
Waste Stabilization Ponds (WSP)
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EVALUATION OF TREATMENT PROCESSES
The methods for treatment of sewer effluent ranges from Physico, Chemicals and
Biological as depicted below:-
S. No. Particulars
a) Physico- Chemicals
I) Screen & grit removal
II) Sedimentation
III) Sludge Thickeners
IV) Vacuum Filters
V) Centrifuges
B) Biological
I) Anaerobic
i) Contact beds
ii) UASB (up flow anaerobic sludge blanket)
iii) Sludge Digesters
iv) Anaerobic Ponds
II) Aerobic
a) Moving bed bio reactor
b) Plasma treatment
ii) Suspended
a) Activated Sludge
b) Extended Aeration
c) Aerated Lagoons
d) Waste Stabilization Ponds (WSP)
5.3.2 EVALUATION OF TREATMENT PROCESSES
The following alternatives of sewage treatment have been considered for evaluation of
performance characteristics, land requirement, energy input, equipment requirement and
operational characteristics.
S. No. Particulars
I. Conventional Activated Sludge Process (ASP)
II. Up flow Anaerobic Sludge Blanket (UASB)
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III. Extended Aeration
IV. Waste Stabilization Ponds
V. Facultative Aerated Lagoon.
VI. Moving bed Elio reactor technology (MBBR)
The advantages and disadvantages of various processes are as under:-
S. No. Particulars
A) Facultative / Aerated Lagoon Advantages
1) Aerated lagoons are easy to run
2) In operating Aerated Lagoons less skilled labour is required
Disadvantages
1) Area requirement is large
2) Facultative aerated lagoons have higher civil works cost and lower mechanical and electrical works
cost.
3) Can pollute underground water unless adequate precautions are taken in construction to prevent
seepage
4) Low BOD removal efficiency. Only about 80-85% of BOO removal could be expected.
5) Bad odour spoils the surrounding environment.
Observation: - Not suitable for the present case.
S. No. Particulars
A) UASB (up flow anaerobic sludge blanket)
Advantages
1) Being anaerobic process required lesser power consumption
2) Methane gas which is generated @ 0.08 to 0.1 cum. Per kg of BOD load can be profitably used, if the
effluent BOD loads are high.
3) In this system, reduction of BOD up to 70-75%is'achieved
Disadvantages
1) Being anaerobic in nature, it is susceptible to be able to have the bacteria are more susceptible to
change Raw effluent will have heavy materials and-toxic Compounds, which will inhabit the growth
of bacteria.
2) Moreover as the process in is the development stage and has not been widely adopted.
3) Very careful maintenance is required, any small mistake can reduce the efficiency very low and plant
has to be close down for making it normal in treatment.
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4) No significant operating data is available.
5) UASB is not suitable for industrial-wastes, due to high temperature variation in North india.
6) Treated effluent from this process needs aeration before its final disposal, thus making it costlier then
the aerobic treatment.
Observation: - Not suitable for the present case.
S. No. Particulars
A) Activated Sludge Process
I) Easy to run
II) More suitable for any modification, if required in future.
III) As this is aerobic in nature, thus bacteria are easy to maintain.
IV) Can achieve desired values of efficiency.
V) Process is dependent on power and will stop in case of power failure.
Disadvantages
a) Only drawback is high power requirement for supply of oxygen as compared
to any other system suggested.
b) Improved version of this process is available.
Observation: - Not suitable for the present case, as better option is available.
A. Extended Aeration
The conventional system represents early development of activated sludge process. Over
the years, several modifications to this system have been developed to meet specific
treatment objectives by modifying the process-variables like loading rates, the mixing
regime and flow scheme. A better alternate is the modified version of this process in
shape of extended aeration process detailed below:-
S. No. Particulars
A) Advantages
I) High degree of treatment-Efficiency 90% BOD removal.
II) The excess Sludge does not require separate digestion and can be directly dried a beds.
III) Sludge production is minimum
B) Disadvantages
I) Long aeration time
II) Higher power consumption
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III) Less F/M ratio
Observation:-
Extended aeration process is advantageous over other sewage treatment methods as its results give
very high efficiency to the extent of 90%, cost effective with clear, sparkling and odourless
effluent and low pump head requirement, its operation is simple and requires no skilled
manpower. Hence is recommended for adopting in this project.
S. No. Particulars
B) Moving Bed Reactor
A) Advantages
I) Sensitivity to small power breakdowns is low
II) Sludge re-circulation not needed and the system is self sustaining.
III) Land requirement is about 60% of conventional system.
IV) Low power consumption
V) High degree of treatment.
VI) High degree of coil form removal
VII) Less chlorine dosing required
B) Disadvantages
I) Installation cost is quite high.
II) It requires highly skilled technical manpower for its operation and maintenance.
III) Presently being tried for smaller units up to 1.50 MLD as prefabricated treatment plant
for individual industry or group housing.
Observation:-
It is a new technique, not much of experience and performance is available on larger plants at
present. Needs highly skilled staff to operate and maintain. Further no significant operating data is
available towards its performance and costing. Hence is not recommended.
FINAL RECOMMENDATIONS
After detailed discussions on various technical options available for treatment of waste
water the final recommendations of the extended aeration process. Recommendations
have been made keeping in view the capacity of treatment plant, its location, cost
economics, environmental impact, technical capacity of manpower available for
maintenance and other technological restrictions and options. Accordingly, the proposed
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common effluent treatment plant for this Industrial Estate, Jind, has been designed on
extended aeration process.
EFFLUENT TREATMENT SCHEME
Waste Water Treatment Technology
In view of the facts detailed in Introduction part, it can be concluded that when
characteristics of raw waste water, the intended use and quality of receiving waters and
their assimilative capacity are known, the extent or degree of treatment needed for the
waste can be determined. Different types of treatment provide different percentage
removal of BOD and suspended solids. In general, the treatment plants are classified as
preliminary, primary, intermediate, secondary and tertiary. The general yard stick for
evaluating the performance of sewage treatment plants is the degree of reduction in BOD,
suspended solids and total coliforms.
(a) Preliminary Treatment: This treatment removes coarser solids. Where dilution is
adequate preliminary treatment consisting of screening of waste water protects the
appearance of receiving body of water and preliminary treatment is considered sufficient
when effluent is disposed of into an open sea. The provision of grit removal arrangement
is also important for the proper functioning and protection of subsequent treatment units.
(b) Primary Treatment: Primary treatment consists of sedimentation only. This treatment
removes 45 to 60% of suspended solids, 30 to 45% of BOD and 40 to 60% of total
coliforms. In case treatment of lesser degree can satisfy the requirement, the size of
treatment plant can be smaller.
(c) Intermediate Treatment (Chemical Treatment) : The treatment removes 60 to 80% of
suspended solids, 45% to 65% of BOD ad 60 to 90% of total coliforms. This treatment is
accomplished by the addition of chemicals prior to sedimentation. This treatment is
quite expensive and is thus rarely adopted where the need of such a high degree
treatment is only seasonal or for a short period.
(d) Secondary Treatment: It is a biological treatment which may consist of standard
trickling filters, high rate trickling filters, single or double stage, activated sludge plants,
stabilization ponds, single cell or two cells. These treatments are expected to remove 75
to 95% of suspended solids, 70 to 90% BOD and 80 to 98% of total coliform depending
upon the type and capacity of the treatment.
(e) Tertiary Treatment: This treatment is done to polish the effluent received from
secondary treatment units to improve the quality of effluent further for reuse. Tertiary
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treatment is needed only when such greater reuse of waste is contemplated or where the
situation dictates the higher quality of effluent. Tertiary treatment may include processes
like rapid sand filtration, carbon absorption, ammonia stripping, coagulation and
flocculation and ion exchange etc. Evidently the cost of such a treatment is prohibitive
and may hardly prove economically viable particularly in developing countries except in
certain extremely critical situations.
In order to select the treatment method, cost factor is the prime consideration. The cost
of the treatment plant would include the cost of installation, cost of maintenance and
operation. The other factors which deserve consideration are cost of construction and
maintenance, location, land availability and topographical conditions.
TREATMENT PROCESS
Receiving Chamber
The raw sewage from the Industrial Units of Jind will be channelized into the Receiving
Chamber through the incoming sewer line. Accordingly, the bed level of the Receiving
Chamber has been kept lower than the Invert Level of the incoming sewer.
DESIGN OF COMMON EFFLUENT TREATMENT PLANT UNITS BASED ON
EXTENDED AERATION TECHNOLOGY
The flow scheme of the extended aeration process and its mixing regime are similar to
that of the completely mixed process except that primary setting is omitted. The process
employs low organic loading, long aeration time, high MLSS concentration and low F/M.
The BOD removal efficiency is high. Because of long detention in the aeration tank, the
mixed liquor solids undergo considerable endogenous respiration and get well stabilized.
The excess sludge does not require separate digestion and can be directly dried on sand
beds. Also the excess sludge production is a minimum.
The oxygen requirements for the process is higher and the running costs are also
therefore high. However, operation is rendered simple due to the elimination of primary
settling and separate sludge digestion. The method is, therefore, well suited specially for
small and medium size communities and zones of a larger city.
In small plants intermittent operation of extended aeration systems may be adopted,
intermittent aeration cycles are : (i) closing of inlet and aerating the sewage, (ii) stopping
aeration and letting the contents settle and (iii) letting in fresh sewage which displaces an
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equal quantity of clarified effluent sludge is wasted from the mixed liquor. To handle
continuous flows a number of units may be operated in parallel.
Further the process is similar to the conventional plug-flow process except that it operates
in the endogenous respiration phase of the growth curve, which requires a law organic
loading and long aeration time. Because of the long STRs (20 to 30d) aeration equipment
design is controlled by mixing needs and not oxygen demand. The process is used
extensively for pre-engineered plants for small communities. Generally, primary
clarification is not used. Secondary clarifiers are designed at lower hydraulic loading
rates than conventional activated-sludge clarifiers to better handle large flow rate
variations typical of small communities. Although the bio-solids are well stabilized,
additional bio-solids stabilization is required to permit beneficial reuse. The
characteristics and design parameter of extended aeration technology are as under:
Flow
Regime
MLSS
Mg/ l
MLVSS
/ MLSS
F/M HRT
hrs
Vol.
Loading
kg BOD/
m3
SRT
(days)
Qr\
/ Q
BOD
Removal,
%
KgO2/ kg
BOD5
removal
Air
Requirem
ent/ kg.
BOD, m3
Complete
Mix
3000
to
5000
0.6 0.10 to
0.18
12
to
24
0.2
to
0.4
10
to
25
0.5
to
1.0
0
95
to
98
1.0
to
1.2
100
to
135
The Treatment flow diagram consists of mainly three streams i.e. the main Treatment
Stream, Chemical Treatment and Sludge Re-handling. The units of each stream are as
under:-
A. Units of Main Treatment Stream
i) Receiving Chamber
ii) Screens (Mechanical and Manual)
i) Oil and Grease removal
ii) Raw effluent sump
iii) Equalization Tank
iv) Flash mixtures
v) Clariflocculator
vi) Aeration Unit
vii) Secondary Clarifier
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viii) Pressure Filters & Activated Carbon Filter
ix) Disposal of Treated Effluent
B. Chemical Treatment
i) Ferrous Sulphate, Lime, Polyelectrolyte solutions of required concentrations will
be added in the flash mixture before clariflocculator.
ii) DAP and Urea solutions of required concentration will be added before aeration
tank in the distribution box / receiving chamber.
iii) Farrous Chloride solution of required concentration will be added after secondary
clarifier.
C. Sludge Re-handling
The sludge from the clariflocculator shall be taken directly to combined sludge sump,
whereas the biological sludge from secondary the clarifier shall be pumped into
combined sludge sump. The sludge from the combined sludge sump shall be pumped into
sludge thickener, from where it will be taken to centrifuge / sludge drying beds.
Polyelectrolite solution of required consideration shall be added in the thickened sludge.
Brief Description/Design characteristics of main units of extended aeration technology
are as under :-
Receiving Chamber
The Receiving Chamber is proposed to act as a wastewater receiving structures from the
terminal pumping station (TPS) / Outfall Sewer; It will have a hydraulic retention time
(HRT) of 30 – 60 seconds at peak flow.
Coarse Screen
The coarse screens are provided at main pumping station before collecting tank. The
maximum velocity of flow through screens is 1.2 mtr per second.
Equalization Tank
The equalization tank shall be design for hydraulic retention time for 8 hrs of average
flow.
Flash Mixtures
Flash mixture is designed for 60-120 seconds hydraulic retention time. The purpose of
flash mixture is to mix the chemicals uniformally in the flow.
Clariflocculators
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Clariflocculators takes care of the Primary Sedimentation of the sewage and also reduces
the organic load on secondary treatment units. While inorganic suspended solids are
removed before clariflocculators in grit chamber, the organic are residual solids, free oil
and grease and other floating material are removed in the clariflocculator, which are
located after screens and equalization tank. The efficiency of primary clariflocculator is
nearly 30% and the specific gravity of organic suspended solid vary from 1.01. to 1.20.
Aeration Tank
An activated sludge plant essentially consists of the following
i) Aeration tank – containing microorganisms in suspension, in which the reaction
takes place.
ii) Activated sludge – recirculation system.
iii) Excess sludge wasting and disposal facilities
iv) Aeration systems to transfer oxygen.
v) Secondary sedimentation tank to separate and thicken activated sludge.
The main variables of the activated sludge process are the loading rate , the mixing
regime and the flow scheme. The extended aeration process employs low organic
loading, long aeration time, high MLSS concentration and low F/M ratio. The BOD
removal efficiency is high. Because of long detention time in aeration tank, the mixed
liquor solids undergo considerable endogenous respiration and get well stabilized.
The excess sludge does not require separate digestion and can be directly dried on sand
beds. The excess sludge production is a minimum.
The volume of aeration tank is calculated for selected value of sludge retention time
(SRT), by assuming a suitable value of MLSS concentration Tank can also be designed
from F/M and MLSS concentration according to equation given as below F/M – Q S0 /X,
V.
It is seen that economy in reactor volume can be achieved by assuming a large value for
X. However, it is seldom taken to be more than 5000 g/m3. A common range is between
1000 and 4000 g/m3. Considerations which govern the upper limit are initial and running
cost of sludge recalculation system to maintain a high value of MLSS, limitations of
oxygen transfer equipment to supply oxygen at required rate in a small reactor volume,
increased solids loading on secondary clarifier which may necessitate a larger surface
area to meet limiting solid flux, design criteria for the tank and minimum HRT for the
aeration tank for stable operation under hydraulic surges.
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Except in the case of extended aeration plants and completely mixed plants, the aeration
tanks are designed as long narrow channels. This configuration is achieved by the
provision of round-the-end baffles in small plants when only one or two tanks units are
proposed and by construction as long and narrow rectangular tanks with common
intermediate walls in large plants when several units are proposed. In extended aeration
plants other than oxidation ditches and in complete mix plants the tank shape may be
circular or square when the plant capacity is small or rectangular with several side inlets
and equal number of side outlets, when the plant capacity is large.
The width and depth of the aeration channel depends on the type of aeration equipment
employed. The depth controls the aeration efficiency and usually ranges from 3 to 4.5 m,
the latter depth being found to be more economical for installations treating more than 50
MLD. Beyond 70 MLD duplicate units are preferred. The width controls the mixing and
usually kept between 5 and 10 m. Width-depth ratio should be adjusted to be between 1.2
to 2.2. The length should not be less than 30 or not ordinarily longer than 100 m in a
single section length before doubling back. The horizontal velocity should be around 1.5
m/min. Excessive width may lead to settlement of solids in the tank. Triangular baffles
and fillets are used to eliminate dead spots and induce spiral flow in the tanks. Tank
freeboard is generally kept between 0.3 and 0.5 m.
Due consideration must be given in the design of aeration tanks to the need for
intermediate walls should be designed for empty conditions on either side. The method of
dewatering should be considered in the design and provided for during construction.
The inlet and outlet channels of the aeration tanks should be designed to maintain a
minimum velocity of 0.2 meter per second to avoid deposition of solids. The channels of
conduits and their appurtenances should be sized to carry the maximum hydraulic load to
the remaining aeration tank units when anyone is out of operation.
The inlet should provide for free fall into aeration tank when more than one tank unit or
more than one inlet is proposed. The free fall will unable positive control of the flows
through the different inlets. Outlets usually consist of free fall weirs. The weirs length
should be sufficient to maintain a reasonably constant water level in the tank. When
multiple inlets or multiple tanks are involved, the inlets should be provided with valves,
gates or stop planks to enable regulation of flow through each inlet.
Tertiary Treatment consisting of Pressure Sand Filter & Activated Carbon Filter
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As it is proposed to use the treated effluent for meeting out demands of horticulture,
washing, air conditioning, flashing and other Industrial Uses, tertiary treatment has to be
given so as to make the effluent worthy of the proposed use. For this purpose, it is
proposed to have filtration consisting of Pressure Sand Filter and Activated Carbon filter.
These filters shall be supplied clarified effluent from SST and shall have top level as that
of the feeding pipe to avoid overflow in the filters.
Filtration through these units is by gravity down wards, through a bed of filtering media
consisting of coarse material of crushed coconut shell / charcoal anthracite and final
silica. The under drainage system consist of piped grit system, comprising of central pipe
/ channel with lateral system of pipes having nozzles. The system should conform to IS
8149 (part-2). The dual filter is complete with filter operation gallery, pipe gallery, back
wash arrangement with storage, pumps, blowers etc.
I) Sludge Thickener
Sludge thickening or dewatering of sludge becomes necessary, within a reasonable time,
to have solid contents as high as possible for reducing the volume of sludge. Sludge
thickening is important to
(i) Allow increased loading to sludge digesters, thickening reduces the volume and
thus increases effective sludge digester capacity,
(ii) Increases feed solid concentration to vaccum Filters,
(iii) Reduces cost of transportation of sludge,
(iv) Economics cost of land requirement and handling costs when sludge is required to
be carted to disposal sites
(v) Saves cost of fuels when sludge incineration is contemplated.
The thickening or concentration of sludge withdrawn from settling tanks can generally be
increased by resettling it with or without stirring. The arms stir the sludge slowly, some
of the entrapped gases and also some of the water is released. The process of Thickening
results in saving in unit cost.
There are three processes of thickening which are generally practices,
(a) Gravity thickening,
(b) Air flotation
(c) Centrifugation.
The process of thickening is especially desirable at activated sludge plants, which usually
produce sludge with low solid content.
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Gravity Thickening:
It is a most common method of thickening of sludge. Gravity thickening is adopted both
for primary sludge or combined primary and activated sludge. Independent dealing with
activated sludge is not successful. When activated sludge exceed 40% of total sludge,
method of gravity thickening of combined sludge does not prove effective and under this
situation it becomes necessary to consider other methods of thickening of activated
sludge.
There are two types of gravity filters, continuous flow or fill and draw type with or
without addition of chemicals. The working becomes efficient with the use of slowly
revolving stirrer.
The size of the thickener is based on either solids or liquid loading. Continuous flow
tanks are deep circular tanks with about 3 m side water depth, with central feed and over
flow at the periphery. Liquid loading rate of 20,000 to 25,000 lpd/m2 is recommended.
The adoption of liquid loading less than 12000 lpd/m2 may give rise to odour problems.
The following solid surface loading rates are recommended:-
Primary sludge : 90-140 kg/d/ m2
Mixtures of Primary and trickling filter : 50-60 kg/d/ m2
Mixture of Primary and activated sludge : 30-50 kg/d/ m2
With these loadings it is practicable to produce thickened solid concentrations of the
following orders:-
Primary sludge : 5 to 10%
Primary and trickling filters : 7 to 9%
Primary and activated sludge : 5 to 8%
Activated sludge : 2.5 to 3.0%
When slow revolving stirrers are provided particularly in the sludge with gas, efficiencies
are improved. The sludge blanket upto 1m depth governs the concentration of under flow
solids beyond which there is negligible influence of the blanket. Sludge detention time of
24 hours is recommended to achieve maximum compaction. Lesser detention time is
required to be adopted during peak conditions in order to keep the sludge blanket depth
adequately below the overflow weir to prevent carry over of excessive solids.
The important aspects, which deserve considerations are to ensure necessary provision
(i) To regulate the quantity of dilution water required
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(ii) Sufficient capacity of pumping to maintain desired solid concentration, continuous
feed and under flow pumping,
(iii) Torque over load protection
(iv) Sludge blanket detection.
Design Consideration
Side water depth : 3m
Liquid loading rate : 20000 – 25000 lpd/m2
Solid surface loading rate : 30 – 50 kg/d/m2
Detention time : 24 hours
The sludge from the primary chemical and excess secondary sludge sump duly blended
shall be taken in to sludge thickener. The same shall be designed as per the following
parameters:-
Thickeners:-
General
Type Circular with mechanical scrapper
Quantity One unit each
Design
Chemical + Secondary Sludge Solids loading,
Kg/M^2/Day
≤ 30
Surface loading, M^3/m^2/day 12000
Side water depth, mm ≥ 4000
Sludge drain pipe mm Ø ≥ 200
Slope 1 in 8 towards center
Thickeners Mechanism
Type Central driven
Width, M 1.2
There shall be 1.2 M wide platform all around the thickener with stair for approach with
CI posts & 40 mm Ø MS PVC coated railing & encapsulated PVC footrests of size 35
mm x 35 mm shall be fixed inside the thickener.
The supernatants shall be collected in the launders outside / inside the periphery of the
tank & Thickened sludge shall be collected in a sludge tank of suitable size.
Thickener Mechanism (Central Driven Fixed Full Bridge Type):-
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The Thickener Mechanism shall be suitable for installation in RCC tank of specified size.
The mechanism shall comprise of the following main components:
Bridge Superstructure spanning the tank diameter
Drive assembly complete with drive head, chain & sprocket, geared motor etc
Feed well
Center Shaft
Cone scraper
Rake arms
Tie rods for rake arms
Plow blades & Squeegees
Weir plate
Brief Technical Specification:-
Bridge Superstructure:-
The bridge shall span the entire diameter of the tank. The width of the walkway shall be
minimum 1.2 M. The bridge shall rest on the thickeners wall at both the end. The bridge
shall be of truss type welded steel construction with walkway of gratings/ chequerred
plates for full of the bridge and center platform. The truss bridge shall be provided with
one row of handrail.
Drive Assembly with Drive Head :-
The central drive head shall rest on the bridge at the center. The drive head shall be
coupled to a geared motor through chain & sprocket and shall support the center shaft at
the bottom for rotating the rake arms.
Feed Well :-
The fixed feed well shall be hung from the bridge superstructure. The inlet feed pipe shall
run under the bridge up to the feed well.
Centre Shaft :-
The centre shaft shall be of SS welded ERW pipe and shall be attached to the output shaft
of the drive head. The center shaft shall be bolted to the drive head at top and shall
support the rake arms at the bottom through a torque frame.
Cone Scraper :-
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A cone scraper shall be attached to the bottom of the center shaft and shall serve to stir
the sludge in the bottom hopper.
Rake Arms & Tie Rods :-
Two sets of rake arms shall be attached to the center shaft torque cage in diametrically
opposite direction through a hinged connection. The rake arms shall be attached to the
center shaft through tie rods with provision for adjustment of inclination of the rake arms.
Each rake arm shall be provided with the plow blades at the bottom and adjustable
renewable squeegees for scraping of sludge.
Weir Plate :-
V – notch weirs of size 5 mm thick x 150 mm wide shall be provided along the periphery
of thickeners for uniform draw – off of the overflow. The weir plate shall be fixed to the
tank wall by means of plate washers.
Inclusions
All civil works along with anchor bolts, inserts etc.
All electrical, instrumentation & cabling including motor starters.
Inlet piping and sludge outlet piping
Material of Construction
Tank RCC – M30
Feed Wall SS – 304
Bridge MSEP
Rake Arm SS – 304
Vertical shaft / Center Cage SS – 304
Blades SS – 304
V-notch weir SS – 304
Squeegees Neoprene
Walkway MS Chequerred Plate / Grating
Handrail 40 NB MSPVC Coated
Vertical Post CI
Scum skimmer SS – 304
Scum box SS – 304
Scum baffle SS – 304
Anchor Bolt
Fasteners – Under Water SS – 304
Project : Common Effluent Treatment Plant, Jind Section - III
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Fasteners – Above Water SS – 304
Sludge Drying Beds
This method can be used in all places where adequate land is available and dried sludge
can be used for soil conditioning. Where digested sludge is deposited on well – drained
bed of sand and gravel, the dissolved gases tend to buoy up and float the solids leaving a
clear liquid at the bottom, which drains through the sand rapidly. The major portion of
the liquid drains off in a few hours, after which drying commences by evaporation. The
sludge cake shrinks producing cracks which accelerates evaporation from the sludge
surface. The areas having greater sunshine, lower rain fall and lesser relative humidity,
the drying time may be about two weeks while in other areas, it could be four weeks or
more. Covered beds are not generally necessary. With the provision of sludge digester &
sludge thickeners, the number of drying days reduces from 7-2 and accordingly area of
sludge drying beds gets reduced to 15-20%.
Design Criteria
The sludge drying process is affected by weather, sludge characteristics, system design
(including depth of bed) and length of time between scraping and lifting of sludge
material. High temperature and high wind velocity improve drying while high relative
humidity and precipitation retard drying.
Area of Beds
The area needed for dewatering and drying the sludge is dependent on the volume of the
sludge, cycle time required to retain sludge of dewatering, drying and removal of sludge
and making the sand bed ready for next cycle of application and depth of application of
sludge on drying bed. The cycle time between two drying of sludge on drying beds
primarily depends on the characteristics of sludge including factors affecting its ability to
allow drainage and evaporation of water, the climatic parameters that influence
evaporation of water from sludge and moisture co0ntent allowed in dried sludge. The
cycle time may vary widely, lesser time required for aerobically stabilized sludge than for
anaerobicaly digested sludge and for hot and dry weather conditions than for cold and / or
wet weather conditions. The area of land required for sludge can be quite substantial with
value of 0.1 – 0.25 m2 / capita. The average cycle time for drying may range from few
days to two weeks in warmer climate and upto 3 to 6 weeks in unfavorable conditions.
By the provision of sludge digester bed, the no of sludge drying beds gets reduced by
50%.
Project : Common Effluent Treatment Plant, Jind Section - III
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Bed Specifications
A sludge drying bed usually consists of a bottom layer of gravel of uniform size over,
which is laid a bed of clean sand. Open jointed tiles under drains are laid in the gravel
layer to provide positive drainage as the liquid passes through the sand and gravel.
Gravel
Graded gravel is placed around the under drains in layers upto 30 cm with a minim of 15
cm above the top of the under drains. At least 3 cm of the top layer shall consist of gravel
of 3 to 6 mm sizes.
Sand
Clean sand of effective of size 0.5 to 0.75 mm and uniform coefficient not greater than
4.0 is used. The depth of sand may vary from 20 to 30 cm. The finished sand surface
shall be level.
Under drains
Under drains are made of vitrified clay pipes of tiles of at least 10-cm dia laid with open
joints. However, other suitable materials may also be used. Under drains shall be placed
not more than 6 m apart.
Walls
Walls shall preferably be of masonry and extend at least 40 cm above and 15 cm below
sand surface. Outer walls should be kerbed to prevent washing outside soil on to beds.
Dimensions
Drying beds are commonly 6 to 8 m wide and 30 to 45 m long. A length of 30 m away
from the inlet should be exceeded with a single point of wet sludge discharge, when the
bed slope is about 0.5%. Multiple discharge points may be used with large sludge beds to
reduce the length of wet sludge travel.
Sludge Inlet
All sludge pipes and sludge inlets are so arranged to easily drain and have a minimum of
200 mm dia terminating at least 30 cm above the sand surface. Splash plates should be
provided at discharge points to spread the sludge uniformly over the bed and to prevent
erosion of the sand.
Tertiary Treatment with Filtration, Color removal and Disinfection
Project : Common Effluent Treatment Plant, Jind Section - III
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Since it is proposed to use treated effluent for reuse it is mandatory to provide tertiary
treatment consisting of the following units to achieve desired treated effluent parameters
as prescribed by Central Pollution Control Board and National Green Tribunal.
I. Secondary Treated effluent sump with treated effluent pumps for storage of
secondary treated effluent and pumping the same to pressure filters.
II. Pressure sand filters for reduction in BOD, COD & TSS
III. Activated carbon filters for removal of color and smell.
The Secondary Treated effluent shall flow in to Pressure filters to be followed by
Activated Carbon Filter before final discharge for reuse.
SLUDGE TREATMENT
Sludge generated from Physico-chemical treatment and biological treatment is collected
in separate sludge sumps. Mechanical mixers are provided to keep the sludge in
suspended form. Separate Belt Filter Press for Chemical Sludge and Centrifuge for
Biological Sludge respectively are considered to dewater the sludge to the required solid
concentration. Screw pumps are used to pump the sludge from sludge sump to filter press
and Belt Press. Dewatering polymer is dosed into the sludge to improve its dewatering
characteristics.
CHEMICAL STORAGE and HANDLING BUIDLING
Chemical Storage Building is provided for 30 days storage and handling of various
chemicals utilized in the effluent treatment plant.
SLUDGE STORAGE
Separate sludge storage areas for biological sludge and chemical sludge are provided for
5 day storage of sludge
DISPOSAL OF TREATED EFFLUENT
The treated water will propose to be used greenbelt development. In addition member
industries will also be permitted to use treated recycled water as per requirement.
Project : Common Effluent Treatment Plant, Jind Section - III
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
Figure 3.5: Process Chart of Common Effluent Treatment Plant
Project : Common Effluent Treatment Plant, Jind Section - III
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
Figure 3.6: Plant Layout
Project : Common Effluent Treatment Plant, Jind Section - III
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
3.6 RAW MATERIAL REQUIRED ALONG WITH ESTIMATED
QUANTITY, LIKELY SOURCE, MARKETING AREA OF FINAL
PRODUCT/S, MODE OF TRANSPORT OF RAW MATERIAL AND
FINISHED PRODUCT
3.6.1 RAW MATERIAL
Raw material required for construction and setting up of Common Effluent Treatment
Plant will be cement, steel, aggregates & sand for civil works. Waste water will be
collected through dedicated pipeline system from associated industries. Sludge generated
from CETP will be disposed off to the TSDF site via GPS enabled trucks (GEPIL).
In addition, raw materials required for the treatment of waste water will be namely Lime,
Polymer, Urea, DAP, FeSO4, Hydrochloric Acid etc for treatment purpose. Which are
available at local market/nearby areas. The consumption of raw materials along with
storage is as under:-
Table 3.4: Raw Material and its Consumption and Storage
S. No. Chemical QTY per Day Storage QTY for 3 days
1 Lime for Coagulation & pH Correction 27.50 Kg/day 90 Kg/day
2 Polymer for Flocculation 0.91 Kg/day 4 Kg/day
3 Dewatering Polymer for Primary Sludge 0.37 Kg/day 2 Kg/day
4 Dewatering Polymer for Biological Sludge 0.09 Kg/day 0.50 Kg/day
5 Hydrochloric Acid 1.97 l/day 6 l/day
6 Urea 2.12 Kg/day 7 Kg/day
7 DAP 0.72 Kg/day 3 Kg/day
8 FeSO4 16.50 Kg/day 50 Kg/day
Source: DPR
3.6.2 PRODUCT
Waste water thus generated by the associated industries will be collected through
dedicated pipeline system after meeting the pre-treatment discharge standards prescribed
by HSIIDC. The approximate quantity of such effluent will be 131 KLD.
The treated water will propose to be used greenbelt development. In addition member
industries will also be permitted to use treated recycled water as per requirement.
Project : Common Effluent Treatment Plant, Jind Section - III
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
3.7 RESOURCE OPTIMIZATION/RECYCLING AND REUSE
ENVISAGED IN THE PROJECT, IF ANY, SHOULD BE BRIEFLY
OUTLINED
The proposed CETP project is to be upgraded with Zero Liquid Discharge (ZLD), hence
the treated water would be recovered and recycled for industrial purposes and green belt.
3.8 AVAILABILITY OF WATER, ITS SOURCE, ENERGY / POWER
REQUIREMENT AND SOURCESHOULD BE GIVEN
3.8.1 WATER AVAILABILITY & ITS SOURCE
This is a proposed common effluent treatment plant. There water will be required for
domestic and chemical dosing purposes.
Total fresh water demand for proposed unit will be 0.8 KLD, Out of which 0.6 KLD
water will be required for domestic and 0.2 KLD for chemical dosing purposes. Water
demand will be met from HSIIDC Industrial Estate, Jind. Water requirement and Water
balance are shown as under:-
Table 3.5: Water Requirement
S. No. Details Total
a. Industrial
Chemical Dosing 0.2 KLD
b. Domestic 0.6 KLD
Fresh 0.8 KLD
Recycled --
c. Green belt and recirculate to member
industries (Recycled- CETP treated
water)
117 KLD
Total
Fresh
0.8 KLD
Recycled 117 KLD
Project : Common Effluent Treatment Plant, Jind Section - III
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
Figure 3.7: Water Balance
3.8.2 ENERGY / POWER REQUIREMENT& ITS SOURCE
S. No. Particulars Unit Total Source
1 Power kVA 80 DHBVN
2 DG Set (capacity and number) kVA 100 kVA–1 no. From Manufacture
3 HSD (for DG Set) l/hr 20 l/hr Local Traders
3.9 QUANTITY OF WASTES TO BE GENERATED (LIQUID AND
SOLID) AND SCHEME FOR THEIR MANAGEMENT / DISPOSAL
3.9.1 QUANTITY OF LIQUID WASTE TO BE GENERATED & ITS
MANAGEMENT / DISPOSAL
3.9.1.1 Domestic Waste Water
Domestic wastewater to the tune of 0.5 KLD will be pumped into CETP lead no
discharge.
3.9.1.2 Industrial Waste Water
Waste water thus generated by the associated industries will be collected through
dedicated pipeline system after meeting the pre-treatment discharge standards prescribed
10%
losses
Industrial Effluent
131 KLD
Preparation of
Dosing Chemicals
0.2 KLD Total Fresh Water
0.8 KLD Domestic use
0.6 KLD
Waste Water
0.5 KLD
0.4 KLD
CETP 0.5 MLD
Capacity
500 KLD
Effluent
TreatedWater
118 KLD
Recycle
117 KLD
Conveyance
Loss
1 KLD
Green Belt and recirculate
to member industries
HSIIDC IE Jind
Project : Common Effluent Treatment Plant, Jind Section - III
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
by HSIIDC. The approximate quantity of such effluent will be 131 KLD. The treated
water will proposed to be recirculate for industrial uses by member industries, green
belts/plantation. Waste water quantity from member industries are as under:-
Table 3.6: Waste Water Quantity from Member Industries for Proposed CETP (0.5 MLD)
S. No. Type of Industry Number Discharge (KLD)
1 Misc 20 42.82
2 Food Processing 4 1.1
3 Plastic 3 0.9
4 Stone 1 0.3
5 Cotton 5 84.3
6 Paper 2 0.5
7 Paint 1 0.6
8 Polymer 1 0.1
9 Metal 1 0.2
10 Fabric 2 0.2
11 Steel 1 0.1
Total 41 131.12 says131
3.9.2 QUANTITY OF SOLID WASTE TO BE GENERATED & ITS
MANAGEMENT / DISPOSAL
1. Hazardous Waste Generation
Table 3.7: Hazardous Waste Generation
S. No. Particulars Category Quantity
(Kg/day)
Mode of Disposal
1 ETP Sludge 35.3 80
Collection, Storage in HWSA,
Transportation and will be sent to TSDF site
via GPS enabled Trucks for disposal.
(GEPIL, Faridabad)
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2. Solid Waste Generation
Table 3.8: Solid Waste Generation
S. No. Particulars Quantity
Mode of Disposal
1. Domestic solid waste 7.5Kg/day Will be handled by Municipal Council, Jind
2. Construction Waste 15 Ton Construction waste will be reused as early as
possible in the construction and for landfilling
during landscaping of project site.
3.10 SCHEMATIC REPRESENTATIONS OF THE FEASIBILITY
DRAWING WHICH GIVE INFORMATION OF EIA PURPOSE
The proposed project activity is listed at Category – “B” under item 7 (h) Common
Effluent Treatment Plant as per the EIA Notification, 2006. Due to the presence of Bir
Bara Ban Wildlife Sanctuary at a distance of 1.16 km towards SE the project will be
categorized as A and considered at MoEF&CC, New Delhi.
Project : Common Effluent Treatment Plant, Jind Section - III
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
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Project : Common Effluent Treatment Plant, Jind Section - IV
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION-IV
Project : Common Effluent Treatment Plant, Jind Section - IV
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION-IV
SITE ANALYSIS
4.1 CONNECTIVITY
HSIIDC Limited has proposed common effluent treatment plant of 0.5 MLD
capacities. The proposed CETP site has all possible amenities that are feasible for
infrastructure projects viability.
Table 4.1: Connectivity
S.
No.
Name Distance (Km) Direction
(From project site)
Nearest Railway Station
1 Jind Railway Station 1.2 N
Nearest Airport
2 Karnal Airport 85 NE
Nearest Highway
3 SH - 12 0.25 ESE
SH-10 1.4 SSE
SH-14 7.55 ENE
Narwana Road 4.0 N
Bhiwani-Jind Road 3.0 SE
4.2 LAND FORM, LAND USE AND LAND OWNERSHIP
Land Form: Proposed Common Effluent Treatment Plant (CETP) of 0.5 MLD capacity
will be constructed on 2,711.39 Sq. m (0.67 Acre) area, which is an notified industrial
area (HSIIDC, Jind)
Land use: The proposed land use breakup is summarized as under:-
Table 4.2: Land use Breakup
S. No. Particulars Area (Sq. m.) %
1 Plant Area 1,220.13 45.0
2 Road/Paved Area 189.80 7.0
3 Green Belt 894.76 33.0
4 Open area 406.70 15.0
Total 2,711.39 100
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Land Ownership
Possession of land was taken over by HSIIDC Chandigarh on dated 18.05.1977 and
Mutation of this land was done in favor of HSIIDC on dated 28.10.1987. Land
documents are enclosed as Annexure-IV.
4.3 TOPOGRAPHY (ALONG WITH MAP)
Haryana is essentially a plain area: 94 percent below 300 meters. The plain spreads
between the hilly tract in the northeast and the sand dune sprinkled desert topography in
the south and southwest. The outliers of the Aravall is make their appearance in the
southern part of the state. The Haryana Plain is a vast surface of flat to rolling terrain and
extends southward to the northern boundary of the alluvial bed of the Ghaggar. It covers
over 65 percent of the area of the District. The elevation of the surface from east to west
varies from 190 to 210 meters above the mean sea level. The most diagnostic feature of
the Haryana Plain is the presence of palaeo channels which set the occurrence of sand
dunes in this terrain unit apart from those in the dune tract. The plain is traversed by
numerous dune complexes and shifting sands.
4.4 EXISTING LAND USE PATTERN (AGRICULTURE, NON-
AGRICULTURE, FOREST, WATER BODIES (INCLUDING AREA
UNDER CRZ)), SHORTEST DISTANCES FROM THE PERIPHERY
OF THE PROJECT TO PERIPHERY OF THE FOREST, NATIONAL
PARK, WILD LIFE SANCTUARY, ECO SENSITIVE AREA, WATER
BODIES (DISTANCE FROM THE HFL OF THE RIVER), CRZ.
Existing Land use:-This is a proposed Common effluent treatment plant. The land is
vacant and situated in Notified Industrial Esate, Jind.
The details of Forests, National Park, Wild Life Sanctuary, Eco Sensitive Area, Water
Bodies within 15 km area are as mentioned below:-
S. No. Particulars Distance (Km) Direction
(From Project Boundary)
P.F/R.F
1. P.F/R.F. None within 15 km
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The proposed expansion project falls in notified Industrial area. Copy of the Gazette
Notification is enclosed as Annexure –V.
4.5 EXISTING INFRASTRUCTURE
The proposed CETP is coming up in an industrial land, which is vacant. The area is well
connected by SH-12, which is 0.25 km towards ESE. SH-10, which is 1.4 km towards
SSE. The study area is having facilities for primary educational and health care, drinking
water, post and telegraph offices, approach roads etc.
National Park
1. None within 10Km radius -- --
Wildlife Sanctuary
1. Bir Bara Ban Wildlife Sanctuary 1.16 SE
Bir Bara Ban Wildlife sanctuary was de-notified and declared as
Conservation Reserve vide Haryana Govt. Notification No. S.O.
78/C.A.53/72/S.18 and 36-A/2007 dated 11.10.2007. As per Wildlife
(Protection) Act, 1972 Section 2(24A) says” “protected area” means a
National Park, a sanctuary, a conservation reserve or a community reserve
notified under sections 18, 35, 36A and 36C of the Act
Eco Sensitive Area
1. Eco Sensitive Area None within 15 km
Water Bodies
1. Hansi Branch 1.0 SE
2. Sirsa Kheri Minor 9.4 SSW
3. Bararikhera Minor 9.7 SSE
4. Siwani Feeder 11.0 SE
5. Jind Distributary 12.9 SE
6. Khanda Minor 14.3 SSW
7. Sundar Subbranch 14.6 SSE
Source: - All distance are taken with respect to Toposheet.
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
4.5.1 BASIC AMENITIES
The details of basic amenities like schools, hospitals and medical center located in 10.0
km of project site is given as under:-
Table No. 4.3: Basic Amenities
S. No. Particulars Distance (Km) & Direction
(From Project Boundary)
Medical facility
1. Govt. Hospital 1.8, NNW
2. Govt. Veterinary dispensary, Jalalpur 2.3, WNW
3. Civil Hospital, Jind 3.8, ESE
Schools
1. 4. Govt. School Jalalpur Khurd 0.7, WNW
2. 5. Govt. Sen. Sec. School, Sabjimandi 1.8, ENE
Place of Worship
3. 6. DurgaMandi 0.5,W
4. 7. Hanuman Temple 1.0, NE
5. 8. Kedarnath Temple 2.0, E
*Source: - All distances are taken with respect to Toposheet.
4.5.2 INDUSTRIES
The proposed CETP is coming up within the notified industrial Estate, Jind. There are
many established industries like food, plastic, paper, cotton, lead, metal, paint steel etc
with well-developed infrastructure facilities within study area.
4.6 SOIL CLASSIFICATION
Soil is formed almost entirely of alluvium, the state is situated towards the depressions of
the rivers Ganges and Indus. It is a broad level plain standing nearly on the watershed
between the basins of the two rivers. It is a vast ground of moist land. In the whole of the
region except the flood plains of the Yamuna and the Ghaggar, the alluvium is of the old
type containing sand, clay, silt and hard calcareous concentrations about the size of nuts
known as 'Kankars'.
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In the Khaddar the deposits of the alluvium are the recent type. They consist of coarse
sand and some silt regularly deposited by the rivers and small mountain streams of the
Indo-Gangetic watershed.
In the south-western part, a great deal of wind-blown sand has been piled up in the form
of sand dunes. These dunes are sometimes many meters high and extend many kilometers
in length. The alluvium is covered by sand, making the region as arid and unproductive
as a desert.
The only part useful for cultivation in this region is Tals, where due to some reason or the
other sand does not collect.
4.7 CLIMATIC DATA FROM SECONDARY SOURCES
The climate of the district is characterized by the dryness of the air with an intensely hot
summer and a cold winter. The cold season starts by late November and extends to about
the middle of March. It is followed by hot season, which continues to about the end of
June when the southwest monsoon arrives over the district. The period from July to
September is the southwest monsoon season. Rainfall: The normal annual rainfall of the
district, based on the record for the period 1901-1980 is 567 mm recorded in 30 rainy
days in a year. There is no meteorological observatory in the district, so the
climatological data of the nearby observatory at Delhi has been taken as representative of
the climatological conditions of the district. About 76% of the annual rainfall is recorded
during the southwest monsoon from June-September. July is the wettest month of the
year with 7.5 rainy days and 169 mm rainfall. During the period 1901-80, deficient to
scanty rainfall was recorded in 18 years. The probability of occurrence of rainfall in the
range 400- 700 mm is 0.65. January is the coldest month with mean daily maximum
temperature 21.3oC and mean daily minimum temp 7.3oC. May is the hottest month with
mean daily maximum temp 26.6oC. In May and June, the maximum temperature
sometimes reaches about 47oC.
4.8 SOCIAL INFRASTRUCTURE AVAILABLE
The well-established social infrastructure like hospitals, temple, schools, roads, and
others similar are available/ existing within 15 km radius which is tabulated in point no
4.5 of PFR.
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
*********
Project : Common Effluent Treatment Plant, Jind Section - V
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION –V
Project : Common Effluent Treatment Plant, Jind Section - V
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Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION -V
PLANNING BRIEF
5.1 PLANNING CONCEPT (TYPE OF INDUSTRIES, FACILITIES,
TRANSPORTATION ETC) TOWN AND COUNTRY PLANNING/
DEVELOPMENT AUTHORITY CLASSIFICATION
The CETP unit is proposed for the treatment of waste water of member industries located
in the Industrial Estate, Jind and sum neighboring area. Waste water will be transported
to CETP through dedicated pipeline network.
Raw material required for treatment of waste water from member industries will be
procured from nearby areas. Transportation of Raw Material will be done through road
only as it is well-connected. The land for the project is in favor of HSIIDC Limited.
5.2 POPULATION PROJECTION
Jind district occupies 7th position in population size during 2011. In terms of density Jind
ranks at 15th position with a density of 494, whereas during 2001 the density was 440.
The Sex Ratio of the district is 871 females over thousand males in 2011 and the child
sex ratio is 838 females over thousand males. The percentage of Scheduled Caste
Population to Total Population in the district is 21.2% and it ranks at 9th position whereas
during 2001 it was 19.8%. The literacy rate in 2011 is 71.4%. The literacy rate has also
shown an increase amongst female population. During 2001 it was 48.5% and it reached
60.8% during 2011. The Work Participation Rate (WPR) of Jind district is 39.2% in
comparison to 35.2% of the State. The Work Participation Rate of Males in Jind is
51.7%, whereas the Female work Participation Rate is 25%. The proposed expansion
project will provide employment to 45 persons of whom 30 persons are for construction
Phase and 15 persons for operation phase. It is likely that the population of the project
area will not be significantly impact.
5.3 LAND USE PLANNING (BREAKUP ALONG WITH GREEN BELT
ETC.)
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The total land area under green belt will be 894.76 Sq. m. (33%).The main aim of the
green belt development is to improve the ecosystem to a maximum possible extent by
designing the green cover with the same native species.
Greenbelt with in project site/ core zone will be developed for proposed project for 4-5
years while buffer zone plantation will be continued up to 5 years. Estimated budget for
same is as follows:-
Total Plot Area : 2,711.39Sq. m
Greenbelt area : 894.76Sq.m
Total trees required : 2,711.39/80 = 33.89 Nos.
Total trees provided : 50
Trees for proposed project =50 trees will be planted.
A total of 50 trees for the next 5 years will be planted for the green area development
in the close proximity of the proposed project.
Table 5.1: Green Belt Development Programme
S. No. Botanical Name Common Name Total
1 Azadirachta indica Neem 5
2 Dalbergia sissoo Shisham 5
3 Cassia fistula Amaltash 10
4 Alstonia scholaris Devil Tree 10
5 Grevillea robusta Silk Oak 10
6 Eucalyptus tereticornis Safeda 5
7 Albizialebbeck Siris 5
Total 50
The detailed green belt programme along with budgetary allocation will be elaborated in
EIA/ EMP Report
5.4 ASSESSMENT OF INFRASTRUCTURE DEMAND (PHYSICAL &
SOCIAL)
On the basis of the preliminary site visit, the infrastructure demands in the villages are
assessed on the basis of need and priority. The health infrastructure, drinking facilities are
Project : Common Effluent Treatment Plant, Jind Section - V
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 53
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
the primary requirements analyzed. The lack of modern and specialist facilities in
hospitals needs improvement. The assessment will be identified in the socio-economic
survey, after the grant of TOR and final assessment will be submitted in final
presentation of EC.
5.5 AMENITIES / FACILITIES
In the preliminary site visit it was found that requiments of women upliftment and
increase in working population. After ToR will be obtained during the detailed survey
which will include consultations with the likley stakeholders. The required facilities will
be updated. This is a tentative budget with facilities to be provided. Provision for the
same has been made as given below: -
Table 5.2: Amenties/ Facilities
S.No. Activities Capital Cost
(Rs. In Lacs)
Recurring Cost
(Rs. In Lacs)
1. Drinking Water Facility 2.00 0.50
2. Sanitation Facilities 1.00 0.50
3. Education 2.00 2.00
4. Training/ Camps etc 1.00 1.00
5. Miscellaneous 1.00 1.00
Total 7.00 5.00
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Project : Common Effluent Treatment Plant, Jind Section - VI
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 54
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION-VI
Project : Common Effluent Treatment Plant, Jind Section - VI
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 55
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION-VI
PROPOSED INFRASTRUCTURE
S. No. Particulars Details
1. Industrial Area 2,711.39 Sq. m (0.67 Acre)
2. Residential Area
(Non Processing Area)
No residential area is proposed. Preference would be given to suitable
local people for employment.
3. Green Belt 894.76 (33%)
4. Social Infrastructure Social infrastructure available within 10-15 km from project site.
5. Connectivity S. No. Highways Distance (Km) & Direction
(From Project Boundary)
1. SH-12 0.2, ESE
2. SH-10 1.4, SSE
3. Bhiwani-Jind Road 3.0, SE
4. Narwana Road 4.0, N.
5. SH-14 7.5, ENE
*Source: - All Distances are taken with respect to Toposheet.
6. Drinking Water
Management
Adequate drinking water facilities will be provided.
Source of water for domestic purposes and chemical dosing will be
managed by HSIIDC, IE, Jind itself.
7. Sewerage System Industrial waste water
Waste water thus generated by the associated industries will be
collected through dedicated pipeline system after meeting the pre-
treatment discharge standards prescribed by HSIIDC. The approximate
quantity of such effluent will be 131 KLD. The treated water will
proposed to be recirculate for industrial uses by member industries,
green belts/plantation.
Domestic waste water
Domestic wastewater to the tune of 0.5 KLD will be generated the
same will be pumped into CETP lead no discharge.
8. Industrial Waste
Management
Sludge from CETP will be generated during the operation phase.
Hazardous Waste Generation
Particulars Category Quantity
(Kg/day)
Mode of Disposal
ETP Sludge 35.3 80 Collection, Storage in
9. Solid Waste Management
Project : Common Effluent Treatment Plant, Jind Section - VI
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 56
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
HWSA, Transportation and
will be sent to TSDF site via
GPS enabled Trucks for
disposal. (GEPIL, Faridabad)
Solid Waste Generation
Particulars Quantity
Mode of Disposal
Domestic solid
waste
7.5Kg/
day
Will be handled by Municipal
Council, Jind
Construction
Waste
15 Ton Construction waste will be reused
as early as possible in the
construction and for landfilling
during landscaping of project site.
10. Power Requirement &
Supply / Source
Phase Demand Expected Source
Operational Phase 80 kVA DHBVN
D. G. Set 100 kVA (1 No.) From Manufacture
Fuel (For DG Set)
Fuel (HSD) 20 l/ hr Local Traders
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Project : Common Effluent Treatment Plant, Jind Section - VII
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 57
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION –VII
Project : Common Effluent Treatment Plant, Jind Section - VII
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 58
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION -VII
REHABILITATION AND RESETTLEMENT
(R & R) PLAN
7.1 POLICY TO BE ADOPTED (CENTRAL/ STATE) IN RESPECT OF THE
PROJECT AFFECTED PERSONS INCLUDING HOME OUSTEES, LAND
OUSTEES AND LANDLESS LABORERS (A BRIEF OUTLINE TO BE GIVEN).
There is no habitation on the proposed project land and is an industrial land. Thus, R & R
policy is not applicable to this project. There shall not be displacement of any population
in proposed project land. The execution of CETP will boost the commercial and
economical status of the locality up to some extent
.
***********
Project : Common Effluent Treatment Plant, Jind Section - VIII
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 59
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION -VIII
Project : Common Effluent Treatment Plant, Jind Section - VIII
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 60
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION -VIII
PROJECT SCHEDULE & COST ESTIMATES
8.1 LIKELY DATE OF START OF CONSTRUCTION AND LIKELY
DATE OF COMPLETION
Proposed Common Effluent Treatment Plant of 0.5 MLD capacity will be completed
within twelve months of getting Environment Clearance from MoEF&CC and consents
from HSPCB.
Table 8.1: Expected Time Schedule for the Project
Activities Completed
activities
Months
1 2 3 4 5 6 7 8 9 10 11 12
Submission of
Terms of
Reference
Application
July’2021
Terms of
Reference
Baseline Study March to May’
2021
Submission of
Final EIA/ EMP
report for EC
Environmental
Clearance
8.2 PROJECT COST ESTIMATION
The total capital investment for the proposed CETP will be 581.76 Lac.
Table 8.2: Expenditure Proposed for Environmental Protection Activities
S. No. Particulars Capital Cost
(Rs. In Lacs)
Recurring Cost
(Rs. In Lacs)
1 Environmental Monitoring
(Air, Stack, Water, Noise, Soil etc.)
0.0 5.0
2 Air Pollution Control System 0.50 0.1
Project : Common Effluent Treatment Plant, Jind Section - VIII
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 61
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
3 Water Pollution and Rain Water Harvesting
Structure
5.0 0.5
4 Occupational Health 1.5 0.50
5 Green Belt Development 10.0 1.0
6 Monitoring laboratory 50.0 5.0
7 Online monitoring system 60.0 6.0
Total 127.0 18.1
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Project : Common Effluent Treatment Plant, Jind Section - IX
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 62
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION-IX
Project : Common Effluent Treatment Plant, Jind Section - IX
Promoter : HSIIDC Limited
Gaurang Environmental Solutions Pvt. Ltd. Page 63
Report Ref: GESPL_259 /ToR/2019/ 53 Rev. No. 01
SECTION-IX
ANALYSIS OF PROPOSAL
9.1 FINANCIAL AND SOCIAL BENEFITS WITH SPECIAL EMPHASIS
ON THEBENEFIT TO THE LOCAL PEOPLE INCLUDING TRIBAL
POPULATION, IF ANY, IN THE AREA
Due to proposed CETP project, it is expected that employment will increase for people
who reside nearby project area. Approximately 45 persons will get employment (30
people during Construction phase and 15 people during Operation Phase). Ancillary units
will also be benefitted in the project area. The local economy will be uplifted in the
project area. Locals will get employment their expenditure and saving power will
increase which will result in better living standards. Due to green belt development,
aesthetic value of local environment will improve. Detailed Environmental management
plan will be submitted during EIA stage.
***********
GAURANG ENVIRONMENTAL SOLUTIONS PVT.LTD.
SIMPLIFYING SUSTAINABILITY
Accredited EIA Consultant Organization by NABET, QCI, New Delhi at S. No. 71 in list of
Accredited EIA Consultant Organizations (as on June’ 2021)
#102, SNG Shree Ratna Apartment, Peetal Factory, Banipark, Jhotwara Road, Jaipur-302016
E-mail: [email protected]