Pre- Feasibility Reportenvironmentclearance.nic.in/writereaddata/Online/TOR/07... · 2019. 3. 7. · Gaurang Environmental Solutions Pvt. Ltd. EIA Coordinator HSIIDC, Kundli, Haryana

Pre- Feasibility Report

Project: Up- gradation of existing 4 MLD to 10 MLD CETP, Kundli, Haryana. Section I/ Executive Summary

Gaurang Environmental Solutions Pvt. Ltd.

EIA Coordinator

HSIIDC, Kundli, Haryana

Authorized Signatory

EXECUTIVE SUMMARY

1.1 IDENTIFICATION OF PROJECT

Pollution from small and medium size industries is a major problem in India. Nearly half of

wastewater generated by the most polluting industries in India comes from the small and

medium size industries.

HSIIDC had acquired land measuring 620 Acres at Kundli, Distt. Sonipat for the proposed

industrial area. A Total No of 10 Marla plots to 2 acres were carved out for setting of

Industrial units of different type of Industries. The various industries present in the Phase I of

Industrial area are as follows:

1. Footwear

2. Iron & fabrication

3. Plastic goods.

4. Pharmaceuticals.

5. Chemicals.

6. Confectionary / food processing Cold Storages.

7. Auto mobiles ancillaries.

8. Electronic & electrical good etc.

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.

1.2 SALIENT FEATURES OF THE PROJECT

S.No Parameter Description

1. Plant Capacity Up-gradation of 4 MLD CETP unit to 10 MLD

2. Total area of the Plant Total area under CETP: 7.0 Acres.

3. Capital Cost The expected capital investment for the proposed up-gradation

project will be 45.86 Crores with 5 Years O&M.

4.

Location Latitude: E 28ᵒ1’6”

Longitude: N 77ᵒ 2’39”

5. Total Water

Requirement/Source

The existing water requirement for 4 MLD CETP unit is 3

KLD. Additional 2 KLD water will be required for the up-

gradation of existing 4 MLD CETP to 10 MLD.

Source: Existing water supply of Industrial Estate, Kundli



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6. Total waste water

Generation and

Management

The ultimate quantity of raw effluent from industries has been

estimated as 10 MLD. The effluent generated from member

units will reach the CETP.

7. Employment Generation

Existing Manpower: 13

Manpower Required during construction will be 30

No additional manpower will be required for up-gradation.

8. Power Supply Existing Power Requirement for the project is 275 KW

Additional Power Requirement for up-gradation 425 KW

Total Power Requirement: 750 KW

Source: UHBVN

9. Power Backup Two D.G set of capacity 300 KVA (200 kVA + 100 kVA) are

already installed for power backup at CETP Kundli. Additional

one DG set of capacity 500 KVA will be installed for CETP up-

gradation project.

Fuel used: HSD

1.3 RAW MATERIAL

Raw material required for construction and setting up of Common Effluent Treatment Plant

are 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.

In addition, raw materials required for the proposed project will be chemicals namely lime,

alum, Ferric Chloride, Polyelectrolyte, Urea, DAP, Chlorine etc. for treatment purpose.

Which are easily available and does not have any significant hazardous effect.

1.4 PRODUCT

The treated effluent is proposed to be used mainly for irrigation, watering of parks, Green

belts etc. or proposed to be disposed of into Drain No. 8 flowing besides the CETP by

gravity. The effluent generated from member units will reach the CETP. The approximate

quantity of such effluent will be 10 MLD.

1.5 CONCLUSION

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.

This project is for establishment of common environmental infrastructure i.e. CETP for

treatment of effluent being generated by its member industries. The imposition of new scale



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of, statutory standards on effluent treatment with water reclamation potential may require, in

addition, a new infrastructural investment on the existing pollution control system of the

individual units. This may be the driving point for the overall participation in the proposed

CETP from industries to bring down drastically the pollution level. The charges to be levied

on new scale on the basis of pollution load, breaking the orthodox style, would equally keep

operational their own equipment. An attempt on water recovery for its recycling in the

proposed CETP design may be an exemplary in the country with a start up in this Zone.

The unit will adopt all measures like; pollution control equipments, effective EMP & DMP to

prevent harm / damage to the environment.

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Project: Up-Gradation of existing 4 MLD to 10 MLD CETP, Kundli, Haryana. Section II/ Project Brief and Background

Information


EIA Coordinator

HSIIDC, Kundli, Sonipat


SECTION II

PROJECT BRIEF AND BACKGROUND INFORMATION

2.1 PROJECT BRIEF

Pollution from small and medium size industries is a major problem in India. Nearly half of

wastewater generated by the most polluting industries in India comes from the small and

medium size industries.

HSIIDC had acquired land measuring 620 Acres in the year 2000 at Kundli, Dist. Sonipat for

the proposed industrial area. Plots of various categories ranging from 10

Marla plots to two acres have been carved out.

The area was planned for mixed type of Industrial use these include

i. Footwear

ii. iron & fabrication

iii. Plastic goods

iv. Pharmaceuticals

v. Chemicals

vi. Confectionary/food processing

vii. Auto mobiles ancillaries

viii. Electronic & electrical good etc.

The Polluting industries such as Electroplating chromium plating, Nickel Polishing,

Coal burning boiler etc have not been allowed to come up in the area.

There is an existing 4 MLD CETP unit to cater the effluent generation from the industries of

Phase IV of Kundli Industrial area. Increasingly rapid urbanization and industrialization are

causing more rapid rise in the pollution of water. Looking at this HSIIDC has planned an up-

gradation of 4 MLD CETP units to 10 MLD. This 10 MLD CETP unit will cater the waste

water generation from industries of Phase of Kundli Industrial area. The existing land area for

4 MLD CETP unit is 7.0 Acres. No additional land will be required for the up-gradation

project.

The total capital investment for the proposed CETP up-gradation will be 45.86 Crores with 5

years O&M. The proposed common effluent treatment plant will be based on Extended

Aeration Process. The treatment system involves Raw effluent Collection (BY HSIIDC )

followed by Primary Treatment (Fine Screening, Grit removal, Oil Removal, and


Information


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Equalization) followed by Physico Chemical Treatment & Secondary biological Treatment

(Activated Sludge Process -Extended aeration), and finally tertiary followed by

Chlorination/disinfection.

The project is for common effluent treatment plant to treat the effluent being generated from

the industries located in the Phase IV of Kundli Industrial area. Waste water thus generated

by the associated industries will be collected through pipeline network for treatment. The

waste water after treatment shall meet the discharge standards laid down by MoEF & CC &

HSPCB. The treated effluent is proposed to be used mainly for irrigation, watering of parks

green belts etc. or proposed to be disposed of into Drain no. 8 flowing besides the CETP by

gravity. Communication for the permission for discharge has been already started.

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

Treat Plant & Disposal of Treated Effluent (Including Rising Main) as per CPHEEO Norms

be designed and got executed at site.




Category – “B”. However, due to presence of Haryana-Delhi interstate boundary at a distance


2.1.1 BACKGROUND OF THE PROJECT PROPONENT

The details of the project proponent are given below:

Name of the applicant HSIIDC, Kundli, Sonipat

Name and address Mr. Arun Garg Senior Manager (IA)

HSIIDC Office, Industrial Estate, Rai, Distt.- Sonipat

Status of Project Expansion project (Freshly applied for Environmental Clearance)

2.2 NEED FOR THE PROJECT AND ITS IMPORTANCE

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


Information


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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.

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 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. At present 4 MLD capacity CETP

is functional for treated effluent of HSIIDC, Indl. Estate Kundli, Phase IV.


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The treated effluent is being disposed off in drain no. 8 flowing beside the CETP.

2.3 DEMAND-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 industrial area Kundli, Sonipat is

suitably treated as per the prescribed procedure & norms laid down in the regulation.

2.4 IMPORTS VS INDIGENOUS PRODUCTION.

Raw material available from local sources/surrounding area or industries.

2.5 EXPORT POSSIBILITY

Not applicable as company will provide service of effluent treatment comes from its member

industries and final disposal of treated effluent.

2.6 DOMESTIC / EXPORT MARKETS

Not applicable as company will provide service of effluent treatment comes from its member

industries and final disposal of treated effluent.

2.7 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. The total manpower required

will be as follows:

1. Existing Manpower in 4 MLD CETP Unit: 13. No additional manpower will be

required after up-gradation.

2. Manpower required during Construction Phase: Will be arranged by Construction

Contractor from nearby areas.

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Project: Up-gradation of existing 4 MLD to 10 MLD CETP, Kundli, Haryana. Section III/ Project Description


EIA Coordinator


`Authorized Signatory

SECTION III

PROJECT DESCRIPTION

3.1 TYPE OF PROJECT




Category – “B”. However, due to presence of Haryana-Delhi interstate boundary at a distance


The project is for common effluent treatment plant to treat the effluent being generated from

the industries located in the Kundli Industrial area. Kundli is situated at about 20 Km from

National Capital Delhi on NH-1 i.e Delhi- Amritsar highway on Delhi – Chandigarh broad

gauge rail link. It is located at 28ᵒ-1’-6” latitude & 77ᵒ -2’-39” longitude. It is located at 15

km from the District Headquarter at Sonipat. 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.7.0 acres of triangular shaped

land in Phase IV, HSIIDC, Kundli to treat the effluent of this area. 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 I to V), 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.

HSIIDC has planned an up-gradation of 4 MLD CETP unit to 10 MLD. This 10 MLD CETP

unit will cater the waste water generation from industries of Phase IV of Kundli Industrial

area. The existing land area for 4 MLD CETP unit is 7.0 Acres. No additional land will be

required for the up-gradation project. The total capital investment for the proposed CETP up-

gradation will be 45.86 Crores with 5 years O&M.



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3.2 LOCATION

The existing common Effluent Treatment Plant (CETP) at HSIIDC, Kundli, District Sonipat,

Haryana. The site of the existing CETP is in HSIIDC, Kundli, Phase IV, a triangular plot of

28105 sqm area (7 acres) of land. The key plan for total area is enclosed. The important

levels and brief characteristics of the site are as hereunder:

1. The Ground level of the CETP is 201.5m

2. Ground water table at the proposed site is at ground level.

3. Size & invert level of the outfall sewer 800ø, at 196.0 M.

4. Soil bearing capacity report 0.6 MT / cm2

5. There is an existing drain No.8 flowing adjacent to the proposed CETP Site

where treated effluent is to be finally disposed after filtration, active carbon

filter and chlorination if not reused.

6. HFL level of the above said drain 202.50

7. The peak factor has been adopted as 3.0 since almost all the industries are

single shift units and accordingly physical treatment units shall be design for

peak flow whereas the biological and Tertiary Treatment unit shall be design

for average flow. The adoption of peak flow at 3.0 will avoid surcharging of

sewers resulting in minimum silting of sewers.

The plan clearly showing the project site and study area of 15 km radius is shown in Figure

3.1.



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Figure 3.1 (i) Topographical Map showing the project site and 15 km buffer area



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Figure 3.2: Location Map Showing the Project Site



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Figure 3.3: Google Image showing the Project site



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Figure 3.4: Plant Layout

3.3 DETAILS OF ALTERNATIVE SITES CONSIDERED

Not applicable as the proposed project is Up-gradation of existing 4 MLD CETP to 10 MLD

3.4 SIZE OR MAGNITUDE OF OPERATION

S. No Treatment facility Existing Capacity Proposed Capacity

1 Common Effluent Treatment plant 4 MLD 10 MLD

3.5 PROJECT DESCRIPTION WITH PROCESS DETAILS

The size of CETP was planned & designed at the time of developing this area on the basis of

average discharge of effluent from the area. The detailed capacity requirement calculation



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were made while planning the Industrial area, where in it was proposed to construct 2

modules of 5 MLD capacity i.e. Total 10 MLD capacity CETP. Based on the same one

module had been construction and accordingly 2nd

module is proposed to be constructed

along with Tertiary treatment for the total 10 MLD capacity Kundli Industrial Estate.

At present 4 MLD capacity CETP is functional for treated effluent of Indl Estate Kundli. 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.

3.5.1 RAW EFFLUENT CHARACTERISTICS

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

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:

S. No. Influent Sewage Characteristics

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

S.

No.

Treated effluent Characteristics

after secondary Treatment

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



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7 Temperature, Co. ≤1

8 NH4- Nitrogen, mg/ L ≤2

9 TP as PO4, mg/ L ≤0.1

10 Chromium mg/L >0.2

S.

No.

Treated effluent Characteristics

after Tertiary Treatment

1 pH 7-

8.5

2 BOD5, mg/ L



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The suspended matter shall be removed by physico-chemical treatment whereas the removal

of bio-degradable soluble organic matter shall be achieved in the biological treatment. As

factor of safety, filtration and disinfection has been provided as polishing treatment. Flow

meters for flow measurement and instrumentation with PLC and SCADA is proposed to be

provided.

The existing and proposed treatment units are mentioned below:

S. No Unit Name Existing Nos.

and Capacity

Proposed Nos.

and Capacity

Total

Capacity

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



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3.5.2.1 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

Receiving Chamber (16.5MLD, Existing)

Mechanical Coarse Screen Chamber (3 nos.)

(1 working mechanical + 1 stand by mechanical)

Effluent Inlet Sump (circular, Existing)

Mechanical fine screen, Oil and Grease trap

(Proposed 3 nos.)

Flash Mixer

(Dosing of Ferrous, alum and lime)

Flocculator

(Existing primary clarifier will be converted to flocculator)

Primary Clarifier (existing)

Aeration Tank (2 existing, 2 proposed)

Secondary clarifier (1 existing and 1 proposed)

Pressure Sand filters

Activated Carbon Filter

Gaseous chlorination for disinfection

Centrifugal decanter for dewatering

Disposal of Dried sludge to TSDF site

Treatment Scheme & Flow Chart



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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.

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



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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.

- Ground water pollution potential.

- Odour, aerosol spray, mosquito nuisance.

- Effect on near by 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.



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- 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.

- Energy conservations.

- Energy/ power generations.

- Carbon Credit as per KYOTO Protocol.

Cost considerations: -

Finally the selected process, overall cost that is capital & operating has to be determined in

order to arrive at the optimum solution.

- Land purchase cost.

-Engineering, design & supervision charges.

-Civil constructions, equipments supply & erection cost.

-Interest charges on loan.

-Amortization & interest charges on capital borrowings.

-Direct operation & maintenance cost of staff, chemicals, fuel & electricity, transport,

maintenance & repair, insurance & over heads.



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3.5.3. 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 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.



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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 flocs. Though a flocculator

is designed for 30 min HRT but the existing structure will provide an HRT of 55 min which



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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 flow by gravity into existing and new aeration

tank designed on extended aeration process for biological treatment using Surface Aerators,

fine bubble diffusers through Air blowing mechanism, biological sludge recycling for

maintaining MLSS & addition of Urea & DAP for N: P ratio maintenance.

Secondary Clarifier:- This biologically treated effluent treated effluent shall flow by gravity

into secondary clarifier for removal of excess MLSS. There is an existing 1 no. Secondary

Clarifier of 18.50m dia. x 3.0m SWD + 0.5FB.

For 10 MLD upgradation of the CETP of CETP one new Secondary Clarifier is proposed of

size 30.8m dia. x 3.5 m SWD + 0.5 FB.

The treated effluent from both the existing and newly proposed Clarifier will be flow through

gravity to Treated effluent Sump having a storage capacity of 2 hours HRT for 10 MLD

capacity.

D. Tertiary Treatment with , Filtration, Color removal and Disinfection

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



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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 filter for removal of color and smell.

IV. Gaseous Chlorination for disinfection of treated water.

The Secondary Treated effluent shall flow in to deep bed Dual media Pressure filters to be

followed by Activated Carbon Filter and chlorination before final discharge for reuse.

E. DISPOSAL OF SLUDGE

For proper disposal of sludge generated in the whole process it is proposed to install

centrifuge for dewatering and disposal of the same in hazardous sludge disposal sites

earmarked.

The biological sludge shall be collected in a separate sump with Horizontal/ vertical (Non-

Clog) pumps for lifting biological sludge for recycling to aeration tank & to combine cum

primary sludge sump for excessive sludge. The super tenant from thickener shall flow back in

to existing MPS by gravity & thickened sludge shall be collected into another thickened

sludge sump from where it shall be pumped on centrifuge & ultimate disposal as dry sludge

for land filling or as per norm of the Pollution control Board at the site proposed for the same.

The filtrate from sludge drying beds shall flow back by gravity in to existing MPS. The

tentative Process flow & instrumentation is attached along with this for reference purpose

only.

3.5.4 DETAILS OF PROPOSED UNITS:-

The capacity of major components of CETP have been designed for following capacities:-

Sl. No. Particulars : Capacity

1 Coarse Screen : 30 MLD

2 Raw effluent Sump. : 10 Minute for 30 MLD

3 Pump House for raw effluent lifting.

a) Pumps for raw effluent lifting pumps. : 417 M^3/ Hr. 4(3 W+1 SB) with

15 MWC head.

4 Grit chamber. : 30 MLD

5 Receiving chamber. : 30 MLD

6 Mechanical Screen : 30 MLD

7 Collection cum Distribution Box. : 30 MLD

8 Extended Aeration Reactor : 10 MLD

9 Collection cum Distribution channel/ Box. : 10 MLD



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10 Secondary Treated Effluent Collection Sump. : 60 Minute

13 Centrifuge : 10 MLD

14 Pressure Filtration : 10 MLD

15 Activated Carbon Filter : 10 MLD

16 Disinfection. : 10 MLD

The sizes of major treatments units and other contingent works shall be as under:-

S. No. PARTICULARS SIZE/CAPACITY QTY.

1 Receiving chamber 3800x2000x1500SWD 1

2 Mechanical coarse screen 6000x1170x700SWDx300FB 3

3 Raw effluent sump 10000x7500x5000H 1

4 Raw Pump House 25500x7500x5000H 1

5 Raw effluent lifting pumps 417m^3/Hr.@15MWC 4

6 Receiving Chamber 1500x1500x2000SWD 1

7 Mechanical fine screen 4000x1000x650SWD+450FB 2

8 Oil & grease trap 10300x20600x1000SWD 2

9 Equalization sump chamber 2700x3750SWDx500FB 2

10 Equalized effluent lifting pumps 208.3m^3/Hr.@6MWC 3

11 Flash mixer 2550 x1700x2550SWD+400FB 1

12 Flash mixer agitator 1.12HP 1

13 Ferrous sulphate solution tanks 1960x1960x1950SWD+400FB 2

14 Ferrous metering pumps 0.32M^3/Hr.@10MWC 2

15 Ferrous chloride solution tanks 1260x1260x1260SWD+400FB 1

16 Ferrous metering pumps 0.08M^3/Hr.@10MWC 2

17 Lime solution tanks 2160x2160x2150SWD+400FB 2

18 Lime screw pumps 0.50m^3/Hr.@10MWC 2

19 Poly. Tanks for Flocculates 1710x1710x1710SWD+400FB 2

20 Poly. Metering pumps 0.30m^3/Hr.@10MWC 2

21 Poly. Tanks for centrifuges 1150x1150x1150SWD+400FB 2

22 Poly. Metering pumps 0.10m^3/Hr.@40MWC 2

23 Chemical store 120M^2 1

24 Primary Clarifier

a) Flocculation basin 13000ø x 3000SWD+400FB 1

b) Settling basin 21200ø x 3130SWD 1



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25 Aeration Tanks 4

a) Existing Tank 13000x43000x3000SWD+600FB 2

b) Proposed Tank 22000x43000x3000SWD+600FB 2

26 Air blowers for Aeration Tanks 2900m^3/[email protected]/cm^2g 3

27 Chemical Sludge Sump 33.11M^3 1

28 Chemical Sludge Pump 7.36 m^3/Hr.@20 MWC 2

29 Biological Sludge Sump 141.18M^3 1

30 Return activated sludge pumps 416.67 m^3/Hr.@10 MWC

3

31 Excess Activated Sludge Pumps 6.88 m^3/Hr.@ 20 MWC 2

32 Secondary Clarifiers 36200øx3500SWD 2

a) Existing 18500ø x3000SWD 1

b) Proposed 30800ø x3500SWD 1

33 Centrifuge for Chemical Sludge 7.36M^3/Hr. 1

34 Centrifuge for Biological Sludge 6.88M^3/Hr. 1

35 Centrifuge for Feed Pumps 6.88M^3/Hr.@20MWC 2

36 DAP solution tanks 1300x1300x2600SWD+300FB 1

37 DAP metering pumps 0.10m^3/Hr.@15MWC 2

38 Urea solution tanks 1980x1980x1970SWD+400FB 1

39 Urea metering pumps 0.20m^3/Hr.@15MWC 2

40 Treated effluent sump 27400x9200x4000SWD+500FB 2

41 Treated effluent pumps 203.33m^3/Hr.@3Kgf/cm^2g 3

42 Pressure sand filters 2800øx1750SWD+500FB 8

43 Activated carbon filters 2800øx2520SWD+500FB 8

44 Air Blowers 521m^3/Hr.@40Kgf/cm^2g 2

45 Gaseous Chlorination 3 Kg / Hr. 2

46 Chlorine Tonners - 6

Building sizes

1

Chemical store including tertiary L.T

Panel, M.C.C Panel,

(Ground Floor :)

20000x15000x5000HT 1

2 Chemical feeding, office & lab First : 20000x15000x5000HT 1

3 Wet sludge pump house 9000x6000x4000HT 1

4 Centrifuge building (Double Storied) 9000x5000x4000HT



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5 D.G set platform 30M^2 1

Figure 3.5 : Process Flow Sheet

3.6 RAW MATERIAL (Quantity and Source), PRODUCT AND MODE OF

TRANSPORT

3.6.1 Raw Material

Raw material required for construction and setting up of Common Effluent Treatment Plant

are 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

600 Kg/day.



EIA Coordinator



In addition, raw materials required for the proposed project will be chemicals namely lime,

FeSO4, Polymer, HCl, Urea, DAP, Chlorine etc for treatment purpose.

3.6.2 Product

The effluent generated from member units will reach the CETP via pipelines. The treated

water will be further used for horticulture, cooling towers, washing, flashing etc, and surplus

into the existing effluent channel adjacent to existing CETP site and connected with

Shahabad River.

3.7 SOURCE OPTIMIZATION/RECYCLING AND REUSE ENVISAGED IN THE

PROJECT

This is a common effluent treatment plant. Thus, recycle and reuse is not envisaged in the

proposed project.

3.8 AVAILABILITY OF WATER, ENERGY / POWER REQUIREMENT AND

SOURCE

3.8.1 Water Demand

The total water requirement will be 5 KLD. The water will be sourced from existing water

supply of Industrial Area Kundli.

3.8.2 Power Demand

Existing Power Requirement for the project is 275 KW. Additional Power Requirement for

up-gradation 425 KW. Total Power Requirement: 750 KW Source: UHBVN

Two D.G set of capacity 300 KVA (200 kVA + 100 kVA) are already installed for power

backup at CETP Kundli. Additional one DG set of capacity 500 KVA will be installed for

CETP up-gradation The fuel used for DG set will be HSD Diesel with low sulphur content.

3.9 WASTE GENERATION AND MANAGEMENT

3.9.1 Solid

Spent oil from DG Set and sludge from CETP will be generated during the operation phase.

S.

No.

Particulars

Category

Category Quantity Mode of Disposal

1. ETP Sludge 34.3 600 Kg/day TSDF site

2. Used oil 5.1 -- Collection, Storage,

Transportation

& disposal.



EIA Coordinator



3.9.2 Waste water

The effluent generated from member units will reach the CETP via pipelines. The

approximate quantity of such effluent will be 10 MLD.

3.10 SCHEMATIC REPRESENTATIONS OF THE FEASIBILITY DRAWING

WHICH GIVE INFORMATION OF EIA PURPOSE

Figure:- Master Plan of Industrial Area, Kundli, Sonipat

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Project: Up-gradation of existing 4 MLD to 10 MLD CETP, Kundli, Haryana. Section IV/ Site Analysis


EIA Coordinator



SECTION – IV

SITE ANALYSIS

4.1 CONNECTIVITY


Haryana. The site of the existing CETP is in HSIIDC, Kundli, Phase IV District Sonipat,

Haryana, which has all possible amenities that are feasible for industrial projects viability.

Particular Details

Airport Indira Gandhi International Airport, 36.5 Km, South direction

Nearest National Highway,

State Highway, Major

District road

NH-1 : 1.2 Km, WSW

SH-57 : 10.6 KM, E

Railway Station Rathdhana Railway Station, 6.2 Km, SW direction

Sonipat Railway station: 16,0 KM, NW

Water Bodies

Water Bodies:

Drain No. 8 : Nearest to the site, N

Naahri Mukhya Vitrika : 3.6 KM, W

Harsana Vitrika : 4.7 Km, NW

Yamuna River : 8.3 KM, ESE

Alipur Dem : 9.8 KM, E

Bawana Vitrika : 12.2 Km, SW

4.2 LAND FORM, LAND USE AND LAND OWNERSHIP

Presently, the Existing 4 MLD CETP is situated on 7.0 Acres of land within HSIIDC

Industrial Area, Kundli, District Sonipat, which is earmarked for CETP to treat the effluent

being generated by member units of Industrial Area. The existing land use of the project site

is already earmarked for Industrial Use. The land ownership of industrial area, kundli is

reserved with HSIIDC.

4.3 TOPOGHRAPHY

The area forms a part of the Indo-Gangetic plains and exhibits flat terrain with general slope

from North to South. The area is devoid of any prominent topographic features. However, a

natural depression exists in North & Northwest of Gohana (290 08’22”N & 76

042’55”E). The



EIA Coordinator



maximum elevation of the plain is 230 m above msl. Topographically the district can be

divided into the following units.

1. Active flood plains along the present day course of the river Yamuna in eastern part of the

district

2. Abandoned flood plains of recent past. These are generally bordering the active flood

plains and are wider, low lying flat tracts.

3. Upland plains representing the relatively older river deposits. The western Yamuna canal

has been roughly aligned along the ridge formed by upland plains.

Source: http://en-in.topographic-map.com/places/Sector-59-E-Block-TDI-City-Kundli-N.H.-1-Sonipat-Haryana-131028-India-6096387/

4.4 EXISTING LAND USE PATTERN

The Land use pattern of the existing CETP remains same. The additional construction/ up-

gradation of CETP will be same as it is already earmarked as Industrial Category.

4.5 EXISTING INFRASTRUCTURE OF SITE

Physical infrastructure

Physical infrastructure is an important aspect of a city. It determines the quality of life to a

large extent. Physical infrastructure deals with

Water supply

Electricity

http://en-in.topographic-map.com/places/Sector-59-E-Block-TDI-City-Kundli-N.H.-1-Sonipat-Haryana-131028-India-6096387/



EIA Coordinator



Solid waste

Water supply

The total water requirement will be 5 KLD. The water will be sourced by existing water

facility within HSIIDC Industrial Area, Kundli.

Electricity


up-gradation 425 KW. Total Power Requirement: 750 KW.Source: UHBVN



CETP up-gradation project. Fuel used: HSD

Solid waste

The sludge from CETP will be generated during the operation phase.

4.6 SOIL CLASSIFICATION

Psammaquents and Haplaquepts- These soils are found in Yamuna Plains.

Haplaquept- These soils are non saline, alkalinity hazards are classified as typic ustochrepts

but water logged soils with loam to clay loam texture showing the effect of glazing, are

classified as aeric/ typic Haplaquepts. Areas as aeridic soil moisture have soils classified as

camborthics and torropsamments.

Source: Central Ground Water Report Sonipat

4.7 CLIMATE FROM SECONDARY SOURCES

Sonipat experiences semiarid, continental, sub tropical and monsoon type climate. During

summer months of April, May and June temperature can rise to as high as 45°C. The climate

is usually very hot and dry during this time. During the summer months very often sandy dust

cyclone can be seen occurring. People are advised to stay indoors as it might affect the skin

of the body and get also get into eyes too. Rainy season is from the month of July to

September brings some relief to the people residing there from the extreme hot climate of the

summer months. The region experiences heavy rain during this time. This area receives

average rainfall of 800mm per year. The region is under the grip of chilling cold between the

months of October till March. The coldest months however are December and January when

the temperature can dip to as low as 2°C. Heavy woolen cloths are needed to keep oneself

warm from the chilling cold waves.



EIA Coordinator



4.7 SOCIAL INFRASTRUCTURE AVAILABLE

Habitation of Sonipath is densely populated with available social infrastructure viz: Primary,

secondary schools, dispensary, hospitals, Mandir, Masjid, Church etc.

Medical Facilities: Available in Sonipath.

Post & Telegraph Offices: Available in District Sonipath.

Educational Institutions:

TDI International School : 0.7 KM, NE

Govt. Sr. Sc. School : 1.7 KM, WSW

Govt. Girls Sr. Sc. School : 1.6 KM, N

Worship Places:

Shiv Temple : 0.4 Km, ESE.

Om Kareswar Temple : 1.2 KM, N

On the basis of the preliminary site visit, the infrastructure available was identified. Further

after the grant of TOR, available infrastructure (baseline data) will be encompassed, along

with socio economic observations and submitted at the time of final presentation regarding

EIA/EMP.

**************

PROJECT: Upgradation of existing 4 MLD to 10 MLD Common

Effluent Treatment Plant, Kundli, Haryana. Section V/ Planning Brief

SECTION V

PLANNING BRIEF

5.1 PLANNING CONCEPT

Kundli Industrial Area is well planned to cater industrial development of Haryana Delhi

Border in Sonipat by Haryana State Industrial & Infrastructural Development Corporation ,

Government of Haryana, to reduce load on Delhi. The existing CETP unit was setup for the

treatment of Waste water of various industries ranging from different sectors located in the

HSIIDC area of Kundli. Waste water will be transported to CETP through dedicated pipeline

network. The expected capital investment for the proposed CETP plant is 45.86 crores with 5

Years of O&M.

5.2 POPULATION PROJECTION

The project will employ mostly workers from nearby villages. There will not be any increase

in population due to the project.

5.3 LAND USE PLANNING (Break up along with green Belt, etc.)

Land Use: The open space inside the CETP area will suitably landscape and covered with the

vegetation of indigenous variety. Green Belt area will be developed as per the CPCB

guidelines. The total land of existing CETP is 7.0 Acres. There is no additional land will be

required to upgrade the existing 4 MLD capacity CETP to 10 MLD capacity CETP.

5.4 ASSESSMENT OF INFRASTRUCTURE DEMAND (Physical & Social)

Social Demand

The proposed CETP falls in Free Enterprising Zone therefore all facilities / amenities like

medical, educational, housing, transportation, communication, shopping etc are available

nearby places. Since, local workers will be employed for this purpose therefore; no long term

infrastructure will be required.

Physical Demand

Water supply

The total water requirement will be 5 KLD. The water will be sourced by existing water

facility within HSIIDC Industrial Area, Kundli.

PROJECT: Upgradation of existing 4 MLD to 10 MLD Common

Effluent Treatment Plant, Kundli, Haryana. Section V/ Planning Brief

Electricity


up-gradation 425 KW. Total Power Requirement: 750 KW.Source: UHBVN




Solid waste

The sludge from CETP will be generated during the operation phase.

******************

Project: Up-gradation of existing 4 MLD to 10 MLD CETP, Kundli, Haryana. Section VI/ Proposed Infrastructure


EIA Coordinator



SECTION VI

PROPOSED INFRASTRUCTURE

6.1 INDUSTRIAL AREA (processing area)

The existing CETP has bene established in an area of 7.0 acres. Being a CETP, adequate

infrastructural facilities such as office space, laboratory, storage area as well as treatment

units comprising Preliminary, primary, secondary, tertiary treatment based on extend aeration

system. New unit will make use of the facilities for land, storage of raw material and

handling, additional water & power demand, and use of road and rail network for

transportation.

6.2 RESIDENTIAL AREA (non processing area)

The plant does not have any residential facility for the workers and employee.

6.3 GREEN BELT

Adequate and proper Green belt has already been developed according to CPCB guidelines.

Plants of the various species has been planted within the plant area.

6.4 SOCIAL INFRASTRUCTURE

Social infrastructure viz: Primary, secondary schools, dispensary, hospitals, Mandir, Masjid,

Church etc. are present near the project site & within the Industrial Area, Kundli.

6.5 CONNECTIVITY


Haryana. The site of the existing CETP is in HSIIDC, Kundli, Phase IV District Sonipat,

Haryana, which has all possible amenities that are feasible for industrial projects viability.

Particular Details

Airport Indira Gandhi International Airport, 36.5 Km, South

direction

Nearest National

Highway, State

Highway, Major District

road

NH-1 : 1.2 Km, WSW

SH-57 : 10.6 KM, E

Railway Station Rathdhana Railway Station, 6.2 Km, SW direction

Sonipat Railway station: 16,0 KM, NW



EIA Coordinator



6.6 WATER MANAGEMENT (source & supply of water)

Water Requirement:

The total water requirement will be 5 KLD. The Source of water supply will be existing

water supply of Industrial Estate, Kundli.

6.7 SEWERAGE SYSTEM

The domestic waste water will be routed to septic tank followed by soak pit.

6.8 INDUSTRIAL WASTE MANAGEMENT

The effluent generated from member units will reach the CETP via pipelines. The

approximate quantity of such effluent is 10 MLD.

The ultimate quantity of raw effluent from industries has been estimated as 10 MLD

assuming water demand of 4500 gallons/ per acre as per prevalent practice including

domestic sewage for the entire existing industrial estate developed by the HSIIDC. At present

4 MLD Common Effluent Treatment Plant is under operation which needs to be upgraded to

10 MLD capacity.

Capacity Computation of CETP.

i) Total Area of Industrial estate, Kundli (Phase I to V). 620 Acres

ii) Sewage inflow from 620 acres area @ 4500 gallons /

acre with 0.8 Interception factor.

10133280 Litres/Day

Total Average Flow 10.13 MLD

Proposed Capacity of CETP 10.00 MLD

and requires no skilled manpower. Hence, is recommended for adopting in this project.

6.9 SOLID WASTE MANAGEMENT

Used oil from DG Set and sludge for CETP will be generated during the operation phase.

S. No. Particulars Category Category Quantity Mode of Disposal

1. ETP Sludge 34.3 600 Kg/day TSDF Site

2. Used oil 5.1 -- As per the norms.



EIA Coordinator



6.10 POWER REQUIREMENT & SUPPLY/ SOURCE


up-gradation 425 KW. Total Power Requirement: 750 KW. Source: UHBVN




**************

Project: Up-gradation of existing 4 MLD to 10 MLD CETP, Kundli, Haryana. Section VII/ Rehabilitation &

Resettlement Plan


EIA Coordinator



SECTION VII

REHABILITATION & RESETTLEMENT (R&R) PLAN

7.1. REHABILITATION & RESETTLEMENT (R&R) PLAN

There is no habitation on the proposed project land. It 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: Up-gradation of existing 4 MLD to 10 MLD CETP, Kundli, Haryana.. Section VIII/ Project Schedule &

Cost Estimates


EIA Coordinator



SECTION – VIII

PROJECT SCHEDULE & COST ESTIMATES

8.1. PROJECT SCHEDULE & COST ESTIMATES

Likely date of start of construction and likely date of completion (time schedule for the

project to be given) Estimated project cost along with analysis in terms of economic viability

of the project. Sewage treatment plant is normally designed to meet the requirement of 30

years period after completion. The expected time for completion of allotment of work is

approximately 18 months after getting Clearances.

The likely date of completion / time required for the fabrication and erection of the

one storage vessel would take one and a half year, from the grant of clearances. The

proposed vessel will be operationalised after successful erection.

The project cost is Rs. 45.86 Crores with 5 Years O&M and chemical cost.

*************

Project: Up-gradation of existing 4 MLD to 10 MLD CETP, Kundli, Haryana. Section IX/ Analysis of Proposal


EIA Coordinator



SECTION – IX

ANALYSIS OF PROPOSAL

This project is for establishment of common environmental infrastructure i.e. CETP for

treatment of effluent being generated by its member industries. The imposition of new scale

of, statutory standards on effluent treatment with water reclamation potential may require, in

addition, a new infrastructural

Investment on the existing pollution control system of the individual units.

This may be the driving point for the overall participation in the proposed CETP from

industries to bring down drastically the pollution level. The charges to be levied on new scale

on the basis of pollution load, breaking the orthodox style, would equally keep operational

their own equipment. An attempt on water recovery for its recycling in the proposed CETP

design may be an exemplary in the country with a start up in this Zone.

There will be social benefits from the proposed unit; the underlying benefit through the

proposed project aims to:

The appropriate amount will be allocated towards the company’s CER activities.

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Documents

Pre- Feasibility Reportenvironmentclearance.nic.in/writereaddata/Online/TOR/07... · 2019. 3. 7. · Gaurang Environmental Solutions Pvt. Ltd. EIA Coordinator HSIIDC, Kundli, Haryana