UNNATI UDHYOG PVT. LTD. Pre-Feasibility Report...

UNNATI UDHYOG PVT. LTD.

Pre-Feasibility Report - Environmental Clearance for Proposed Greenfield CETP and Incineration Plant at Plot No D-23,24,25,26, UPSIDC Industrial Area, Village Gopalpur, Tehsil Sikandrabad, Distt. Bulandshahar, Uttar Pradesh.

FEBRUARY, 2016

KadamEnvironmental Consultants w w w . k a d a m e n v i r o . c o m

Env i ronmentfor Deve lopment

M/S. UNNATI UDHYOG PVT LIMITED

PRE-FEASIBILITY REPORT – ENVIRONMENTAL CLEARANCE FOR PROPOSED GREENFIELD CETP AND INCINERATION PLANT AT UPSIDC INDUSTRIAL

AREA, SIKANDRABAD, BULANDSHAHAR QUALITY CONTROL

SHEET

KADAM ENVIRONMENTAL CONSULTANTS | FEBRUARY, 2016 II

M/S. UNNATI UDHYOG PVT. LTD.

Pre-Feasibility Report - Environmental Clearance for Proposed Greenfield CETP and Incineration facility at Plot No D-23,24,25,26, UPSIDC Industrial Area, Village Gopalpur, Tehsil Sikandrabad, Distt. Bulandshahar, Uttar Pradesh. © Kadam Environmental Consultants (‘Kadam’), February, 2016

This report is released for the use of the M/s. Unnati Udhyog Pvt Ltd, Regulators and relevant stakeholders solely as part of the subject project’s Environmental Clearance process. Information provided (unless attributed to referenced third parties) is otherwise copyrighted and shall not be used for any other purpose without the written consent of Kadam.

PROJECT DETAILS

Name of Publication

Pre-Feasibility Report for Environmental Clearance for Proposed Greenfield CETP and Incineration Plant at Plot No D-23,24, 25,26 UPSIDC Industrial Area, Village Gopalpur, Tehsil

Sikandrabad, Distt. Bulandshahar, Uttar Pradesh.

Project Number 1522583206 Report No. 1 Version 1 Released February,

2016

Prepared & Managed By

Ishita Garg Released By J.A Rathi

Anand Kunte

CONTACT DETAILS

Vadodara (Head Office)

871/B/3, GIDC Makarpura, Vadodara, India – 390 010.

E: [email protected]; T:+91-265-3001000; F: +91-265-3001069

Delhi / NCR

Spaze IT Park, Unit No. 1124, IIth Floor, Tower B3, Sector 49, Near Omaxe City Centre Mall, Sohna Road, Gurgaon, Haryana, INDIA - 122002.

E: [email protected]; T: +91-124-4242430 to 436; F:+91-124-4242433

DISCLAIMER

Kadam has taken all reasonable precautions in the preparation of this report as per its auditable quality plan. Kadam also believes that the facts presented in the report are accurate as on the date it was written. However, it is impossible to dismiss absolutely, the possibility of errors or omissions. Kadam therefore specifically disclaims

any liability resulting from the use or application of the information contained in this report. The information is not intended to serve as legal advice related to the individual situation.


PRE-FEASIBILITY REPORT - ENVIRONMENTAL CLEARANCE FOR PROPOSED GREENFIELD CETP AND INCINERATION PLANT AT UPSIDC INDUSTRIAL

AREA, SIKANDRABAD, BULANDSHAHAR INTRODUCTION

KADAM ENVIRONMENTAL CONSULTANTS | FEBRUARY, 2016 3

CONTENTS

1 EXECUTIVE SUMMARY ............................................................................... 9

1.1 PLANT FEATURES ........................................................................................ 9 1.1.1 Infrastructure .................................................................................... 9 1.1.2 Utility ............................................................................................. 9

1.2 ENVIRONMENT .......................................................................................... 9 1.3 CONCLUSION ............................................................................................ 9

2 INTRODUCTION ...................................................................................... 10

2.1 IDENTIFICATION OF PROJECT AND PROJECT PROPONENT .............................................. 10 2.2 BRIEF DESCRIPTION OF NATURE OF THE PROJECT .................................................... 10 2.3 NEED FOR THE PROJECT AND ITS IMPORTANCE TO THE COUNTRY AND OR REGION ................... 10 2.4 DEMAND SUPPLY GAP ................................................................................. 10 2.5 IMPORTS VS. INDIGENOUS PRODUCTION .............................................................. 10 2.6 EXPORT POSSIBILITY .................................................................................. 10 2.7 DOMESTIC/EXPORT MARKETS ......................................................................... 10 2.8 EMPLOYMENT GENERATION (DIRECT AND INDIRECT) DUE TO THE PROJECT ........................... 11

3 PROJECT DESCRIPTION ............................................................................ 12

3.1 TYPE OF PROJECT INCLUDING INTERLINKED AND INTERDEPENDENT PROJECTS, IF ANY ................ 12 3.2 LOCATION (MAP SHOWING GENERAL LOCATION, SPECIFIC LOCATION AND PROJECT BOUNDARY &

PROJECT LAYOUT) WITH CO-ORDINATES ...................................................................... 12 3.3 DETAILS OF ALTERNATE SITES CONSIDERED AND THE BASIS OF SELECTING THE PROPOSED SITE, PARTICULARLY THE ENVIRONMENTAL CONSIDERATIONS GONE INTO SHOULD BE HIGHLIGHTED ................ 12 3.4 SIZE OR MAGNITUDE OF OPERATION .................................................................. 12 3.5 PROJECT DESCRIPTION WITH PROCESS DETAILS (SCHEMATIC DIAGRAM/ FLOWCHART SHOWING THE

PROJECT LAYOUT, COMPONENTS OF PROJECT ETC. SHOULD BE GIVEN) ........................................ 12 3.5.1 Process Description-Incinerator ............................................................. 12 3.5.2 Process Description- CETP ................................................................... 14

3.6 RAW MATERIALS REQUIRED ALONG WITH ESTIMATED QUANTITY, LIKELY SOURCE, MARKETING AREA OF

FINAL PRODUCTS, MODE OF TRANSPORT OF RAW MATERIAL AND FINISHED PRODUCT .......................... 16 3.7 RESOURCE OPTIMIZATION/RECYCLING AND REUSE ENVISAGED IN THE PROJECT, IF ANY, SHOULD BE

BRIEFLY OUTLINED ............................................................................................ 16 3.8 AVAILABILITY OF WATER ITS SOURCE, ENERGY/POWER REQUIREMENT AND SOURCE SHOULD BE GIVEN 17

3.8.1 Power Requirement ........................................................................... 17 3.8.2 Fuel Requirement ............................................................................. 17 3.8.3 Water Requirement ........................................................................... 17

3.9 QUANTITY OF WASTES TO BE GENERATED (LIQUID AND SOLID) AND SCHEME FOR THEIR

MANAGEMENT/DISPOSAL ...................................................................................... 17 3.10 SCHEMATIC REPRESENTATIONS OF THE FEASIBILITY DRAWING WHICH GIVE INFORMATION OF EIA

PURPOSE 18

4 SITE ANALYSIS ....................................................................................... 19





4.1 CONNECTIVITY ........................................................................................ 19 4.1.1 By Road ........................................................................................ 19 4.1.2 By Rail .......................................................................................... 19 4.1.3 By Air ........................................................................................... 19

4.2 LAND FORM, LAND USE AND LAND OWNERSHIP ....................................................... 19 4.3 TOPOGRAPHY (ALONG WITH MAP) ..................................................................... 19 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 AREAS, WATER BODIES (DISTANCE FROM THE

HFL OF THE RIVER), CRZ. IN CASE OF NOTIFIED INDUSTRIAL AREA, A COPY OF THE GAZETTE NOTIFICATION

SHOULD BE GIVEN. ............................................................................................ 19 4.4.1 Water Bodies .................................................................................. 19

4.5 EXISTING INFRASTRUCTURE ........................................................................... 19 4.6 SOIL CLASSIFICATION ................................................................................. 20 4.7 CLIMATIC DATA FROM SECONDARY SOURCES ......................................................... 20 4.8 SOCIAL INFRASTRUCTURE AVAILABLE ................................................................. 20

5 PLANNING BRIEF ..................................................................................... 21

5.1 PLANNING CONCEPT (TYPE OF INDUSTRIES, FACILITIES, TRANSPORTATION ETC) TOWN AND COUNTRY

PLANNING/ DEVELOPMENT AUTHORITY CLASSIFICATION ...................................................... 21 5.2 POPULATION PROJECTION ............................................................................. 21 5.3 LANDUSE PLANNING (BREAKUP ALONG WITH GREENBELT ETC.) ........................................ 21 5.4 ASSESSMENT OF INFRASTRUCTURE DEMAND (PHYSICAL & SOCIAL) ................................... 21 5.5 AMENITIES/FACILITIES ................................................................................ 21

6 PROPOSED INFRASTRUCTURE ................................................................... 22

6.1 INDUSTRIAL AREA (PROCESSING AREA) ............................................................... 22 6.2 RESIDENTIAL AREA (NON-PROCESSING AREA) ........................................................ 22 6.3 EQUIPMENT LIST ...................................................................................... 22 6.4 GREEN BELT ........................................................................................... 23 6.5 SOCIAL INFRASTRUCTURE ............................................................................. 23 6.6 CONNECTIVITY (TRAFFIC AND TRANSPORTATION ROAD/ RAIL/METRO/WATER WAYS ETC) ............. 23 6.7 DRINKING WATER MANAGEMENT (SOURCE & SUPPLY OF WATER) .................................... 23 6.8 SEWAGE SYSTEM ...................................................................................... 23 6.9 SOLID & INDUSTRIAL WASTE MANAGEMENT .......................................................... 23 6.10 POWER REQUIREMENT & SOURCE/ SUPPLY ......................................................... 23

7 REHABILITATION AND RESETTLEMENTS (R& R) PLAN ................................... 24

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) .................. 24

8 PROJECT SCHEDULE AND COST ESTIMATE ................................................... 25

8.1 LIKELY DATE OF START OF CONSTRUCTION AND LIKELY DATA OF COMPLETION (TIME SCHEDULE FOR THE

PROJECT TO BE GIVEN) ........................................................................................ 25





8.2 ESTIMATES PROJECT COST ALONG WITH ANALYSIS IN TERMS OF ECONOMIC VIABILITY OF THE PROJECT

27 8.2.1 Profitability ..................................................................................... 27

9 ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS) ................................. 28

9.1 FINANCIAL AND SOCIAL BENEFITS WITH SPECIAL EMPHASIS ON THE BENEFIT TO THE LOCAL PEOPLE

INCLUDING TRIBAL POPULATION, IF ANY, IN THE AREA ........................................................ 28





ANNEXURES

Annexure 1: General and Specific Location Map ............................................................................ 30

Annexure 2: Project Boundary Map .............................................................................................. 31

Annexure 3: Toposheet ............................................................................................................... 32

Annexure 4: Site Layout Map ....................................................................................................... 33





LIST OF TABLES

Table 3-1: Co-ordinates of Project Boundary ................................................................................. 12

Table 3-2: Unit wise dimensions of CETP ...................................................................................... 15

Table 3-3: Water Consumption Breakup ........................................................................................ 17

Table 6-1: List of Equipments ...................................................................................................... 22

Table 8-1: Project Implementation Schedule ................................................................................. 26

Table 8-2: Project Cost ................................................................................................................ 27





LIST OF FIGURES

Figure 3-1: Block diagram of Incinerator ....................................................................................... 14

Figure 3-2: Block Diagram of CETP ............................................................................................... 16





1 EXECUTIVE SUMMARY

1.1 Plant Features

M/s Unnati Udhyog Pvt Ltd proposes a Greenfield project for combined Common Effluent Treatment Plant (CETP) and Incinerator Facility at plot No 23,24,25,26, Village Gopalpur, Sikandrabad Industrial area, District Bulandshahar, Uttar Pradesh.

The plot is in the industrial area with a total plot area of 6,430 sqm. Aprrox 1200 sqm (19%) of total plot area will be covered under green belt. Total cost of the project will be approx. INR 9.0 Crores.

The project will comprise of CETP of 1 MLD and Common Incinerator Facility of 2 ton/hr (solid and liquid waste) capacity.

1.1.1 Infrastructure

The site is well connected to NH-91 and is accessible through approach roads. Separate storage area will be provided for storing solid and liquid waste. Solid waste will be stacked in three layers. Admin building, laboratory, Chemical storage area for CETP will also be established.

1.1.2 Utility

Power: Total power requirement for proposed project is 2,000 kW and will be supplied by UPPCL. Two DG sets of 250 KVA and 500 kVA capacity will be installed for emergency backup supply.

Fuel: 400kg/hr of HSD will be used for DG sets and process.

Water: Total water requirement for proposed project is 164 KLD out of which 8 KLD of fresh water will be supplied through tankers and remaining water requirement will be fulfilled by treated CETP water after using RO of 150 KLD.

1.2 Environment

Environmental issues associated with proposed CETP and Incinerator includes:

Air emissions: Emissions of SO2, NO2, HC, HF are envisaged from Incinerator. In case of improper quenching, emission of dioxins/furans are also envisaged.

Wastewater: Domestic waste water will be disposed to soak pit. All other process waste water will be sent to CETP. Final disposal of CETP treated water will be done to UPSIDC drain.

Hazardous Waste: CETP sludge will be disposed to Incinerator. Ash from Incinerator will be sent to TSDF site.

1.3 Conclusion

The proposed project will cater the need of the industries by providing CETP and Incineration facility in the area thereby will encourage industrial growth in the region and result in additional revenue for government.





2 INTRODUCTION

2.1 Identification of Project and project Proponent

As per the EIA notification dated 14th September, 2006, as amended till date, the proposed project falls under the Project / Activity: 7(d) – Common Hazardous waste treatment, storage and disposal facilities (TSDFs) and 7(h) - Common Effluent Treatment Plants (CETPs). The project shall be treated as category “A”.

M/s Unnati Udhyog Pvt. Ltd. is currently engaged in transportation and disposal of waste to recyclers under directorship of Mr. Rajeev Goel.

2.2 Brief Description of Nature of the Project

The proposed project is a Greenfield CETP and Incineration Facility project at village Gopalpur, Tehsil Sikandrabad, District Bulandshahr, Uttar Pradesh.

2.3 Need for the Project and its Importance to the Country and or Region

The area has various small and medium scale industries of paints, printing & dyeing, automobiles, sugar, pesticides etc. These industries generates huge amount of waste water and incinerable waste.

As there is no CETP and incineration facility in the area, the industries either send their waste to distant treatment facilities or they dispose in an unscientific manner.

Hence, the proposed project will cater the need of the industries by providing CETP and Incineration facility in the area.

2.4 Demand Supply Gap

The area has different category of industries generating incinerable waste and waste water. Due to lack of treatment facilities in the area, the industries are disposing the waste in an unscientifically manner. The proposed project will cater the need of the area.

2.5 Imports vs. Indigenous Production

Not applicable.

2.6 Export Possibility

Not applicable.

2.7 Domestic/Export Markets

Not applicable.





2.8 Employment Generation (Direct and Indirect) due to the project

During the construction phase, around 50 workers and during operational phase around 30 workers including contractors will be required. Local skilled and semi-skilled workers will be engaged during construction phase.



AREA, SIKANDRABAD, BULANDSHAHAR SITE ANALYSIS


3 PROJECT DESCRIPTION

3.1 Type of Project including interlinked and interdependent projects, if any

As per the EIA notification dated 14th September, 2006, as amended till date, the proposed project falls under the Project / Activity: 7(h) - Common Effluent Treatment Plants (CETPs) and 7(d) – Common Hazardous waste treatment, storage and disposal facilities (TSDFs) which shall be treated as category “A”.

3.2 Location (map showing general location, specific location and project boundary & project layout) with co-ordinates

The project is located at Plot No D-23, 24, 25, 26, UPSIDC Industrial area, Village Gopalpur, Sikandrabad, Bulandshahar, Uttar Pradesh.

Location map showing general & specific location of proposed project is given in Annexure 1. Project boundary map is given in Annexure 2. The co-ordinates of the project site are presented in Table 3-1.

Table 3-1: Co-ordinates of Project Boundary Code Latitude Longitude

1 28°29'41.45"N 77°39'16.08"E

2 28°29'40.44"N 77°39'19.20"E

3 28°29'39.67"N 77°39'19.03"E

4 28°29'37.78"N 77°39'19.82"E

5 28°29'39.34"N 77°39'15.21"E

3.3 Details of alternate sites considered and the basis of selecting the proposed site, particularly the environmental considerations gone into should be highlighted

Alternative sites were reviewed & finally the proposed site was selected as it is within industrial area and best suited for the application of CETP’s and Incinerator.

3.4 Size or Magnitude of Operation

Total plot area of the project is 6,430 sqm. The proposed project includes CETP of 1 MLD capacity and Incinerator of 2 ton/hr capacity (solid & liquid waste).

3.5 Project Description with process details (Schematic diagram/ flowchart showing the project layout, components of project etc. should be given)

3.5.1 Process Description-Incinerator

The system comprises of following units:





Liquid Waste Storage tank

Primary Combustion chamber of wastes

Secondary Combustion chamber

Cyclonic Collector

Quencher

Ventury Scrubber with Tank

Flue gas wet scrubber with tank

Moisture separator

Duct Lines with manhole for cleaning

ID Fan (Exhaust Fan)

FD Fan

Pumps

Chimney having height of 30 mtr.

Pipe lines and valve fittings

One Belt Conveyor for Solid Waste Feeding into Solid PCC

Combustion burners for PCC for liquid and Solid Waste PCC

Electrical Panel Board

Fuel Day tank

An incinerator is designed to achieve complete combustion of the waste with maximum extraction of heat from exhaust gases and extensive cleaning of the exhaust gases to ensure only minimal amounts of harmful substances released into the atmosphere. The supply and movement of the waste through the chamber is automated and adjustable. There is an adjustable forced supply of air as insufficient air will lead to incomplete combustion while excess air makes it difficult to achieve the required temperatures. The air is usually drawn in from the storage area containing dust and odour in it and is destroyed in the combustion process ensuring no odour and dust escape from the building. A controllable amount of secondary fuel such as natural gas is supplied to ensure required temperature is attained. The chamber is designed to keep exhaust gases at required temperature for a sufficiently long time. The chamber has an ash collection and removal system. Ash from the combustion chamber is first cooled with water and then sorted and graded and used as a building aggregate. Flue gases from combustion chamber enter into quencher where low TDS/raw water is injected to quench the temperature from 900°C to 300°C. After quenching, flue gas passes through cyclone, bag filter and scrubbers to reduce the temperature further and removal of contaminants. The flue gas is released to the atmosphere through exhaust (ID) fan.





The Block diagram of the Incinerator is given in Figure 3-1

Figure 3-1: Block diagram of Incinerator

3.5.2 Process Description- CETP

The CETP units are described below:

Equalization Tanks

The prime purpose of equalization tank is to have constant load. Equalization tank shall be provided with coarse bubble aeration grid. Aeration grid will be provided at the bottom and air will be supplied via Blower in order to have adequate mixing in the tanks. Mixing of lime batch wise is also carried out in equalization tank as a part of coagulation process.

Flash Mixing Tank

After addition of lime in the Equalization tank, alum is added and flash mixing is carried out in Flash mixing tank. Alum is used as a coagulant for the removal of suspended and colloidal particles. Agitators are provided with RPM 100 so as to carry out Flash Mixing.

Flocculation Tank

Flocculation Tank is provided for the formation of Flocs of alum and the colloidal particles. Slow mixing with Flocculator RPM 10-15 is carried out and the Flocs are allowed to form. Polyelectrolyte is added in the flocculation tank for the enhancement in the floc formation and to improve the binding of the flocs.

Primary Settling Tank

A primary settling tank is provided for settlement of the chemical flocculated sludge generated from the Flocculation tank. The sludge from the bottom shall be sent to sludge collection sump. Overflow from the settling tank will be sent via gravity into Aeration Tank. A PVC Tube settler media will be installed in the tank.

Ist stage Aeration Tank

Aeration tank is provided for removal of organics using biodegradation with MLSS concentrations of around 3000 mg/l. Diffused aeration system with Air blowers will be provided in the tank for air supply.





Secondary Settling Tank

A Secondary settling tank is provided for settlement of the biological sludge generated from the aeration tank and its recirculation. The sludge from the bottom shall be sent to sludge collection sump / re-circulated to the aeration tank for maintaining the sludge concentration. Overflow from the settling tank will be transferred to aeration tank 2.

IInd Stage Aeration Tank

Aeration tank II is provided for further removal of organics using biodegradation with MLSS concentrations of around 3000 mg/l. Diffused aeration system with air blowers will be provided in the tank for air supply.

Final Settling Tank

A Final settling tank is provided for settlement of the biological sludge generated from the Aeration Tank II and its recirculation. The sludge from the bottom shall be wasted to sludge collection sump / re-circulated to the aeration tank for maintaining the sludge concentration. Overflow from the settling tank will be transferred to Intermediate Collection Tank.

Intermediate Collection Tank

An intermediate collection tank is provided for intermediate collection and for disinfection treatment (using NaOCl dosing) of the biologically treated waste waters. The tank also acts as intermediate storage of treated waste water for further pumping to tertiary Treatment system.

Pressure Sand Filter

A Pressure sand filter consisting of sand and gravel bed in a pressure vessel is considered for final filtration and adsorption of residual organics and colloidal suspended solids. The filter vessel will be of MSEP of capacity of 50cu.m per hr and operation: 20 hrs.

Activated Carbon Filter

An Activated carbon filter consisting of activated carbon and gravel bed in a pressure vessel is considered for final filtration and removal of color. The filter vessel will be of MSEP of capacity of 50cu.m per hr and operation: 20 hrs.

Final Collection Tank

A final collection is provided for collection of final treated outlet of the ETP. The pumps required to transfer the effluent will be in Clients scope.

Decanter Centrifuge

The primary sludge and biological sludge will be stored into the sludge collection sump. From this sump, the sludge will further dewater through decanter.

Unit wise dimensions are provided in Table 3-2

Table 3-2: Unit wise dimensions of CETP

S. No Description No of units Dimension

1. Equalization Tank 2 17.4 x 8.7 x 3.8m SWD + 0.5m F.B

2. Flash Mixer 1 2.1 x 2.1 x 1.8m SWD + 3.0m F.B

3. Flocculator 1 2.8 x 2.8 x 1.6m SWD + 0.3m F.B





S. No Description No of units Dimension

4. Primary Settling tank 1 6.0 x 5.0 x 2.15m SWD + 0.3m F.B + 3.0m H.B +

0.3 m S.B

5. 1st stage aeration tank 1 24.0 x 8.4 x 5.0 SWD + 0.5m F.B

6. Secondary settling tank 1 6.5 x 5.7 x 2.15m SWD + 0.3m F.B + 3.25m H.B

+ 0.3m S.B

7. 2nd stage aeration tank 1 18.0 x 9.0 x 5.0m SWD + 0.5m F.B

8. Secondary settling tank 1 6.5 x 5.7 x 2.15m SWD + 0.3m F.B + 3.25m H.B

+ 0.3 S.B

9. Intermediate Collection tank 1 7.0 x 6.0 x 3.5m SWD + 0.3m F.B

10. Pressure sand filter 1 50 m3/hr

11. Activated Carbon Filter 1 50 m3/hr

12. Final Collection Tank 1 20.8 x 14.0 x 4.0m SWD + 0.3m F.B

Block diagram of CETP is provided in

Figure 3-2: Block Diagram of CETP

3.6 Raw Materials required along with estimated quantity, likely source, marketing area of final products, mode of transport of raw material and finished product

The proposed project envisages only treatment facility for effluents and hazardous waste received from various industries. Provision of Chemical Storage will be made in the Chemical Storage Building.

3.7 Resource optimization/recycling and reuse envisaged in the project, if any, should be briefly outlined

Resource Optimization / recycling and reuse are not envisaged in the project.





3.8 Availability of water its source, Energy/power requirement and source should be given

3.8.1 Power Requirement

Total power requirement for the project is proposed to be 2,000 KW and will be supplied by Uttar Pradesh Power Corporation Ltd (UPPCL).

Power backup: DG Sets of 1x250 kVA +1x500 kVA capacities will be used in case of emergency.

3.8.2 Fuel Requirement

400 kg/hr of HSD will be used for DG sets and incineration process.

3.8.3 Water Requirement

Total water requirement for the proposed project is 164 KLD. Fresh water requirement of 8 KLD will be met by tankers. Remaining water requirement will be fulfilled by CETP treated water after using RO of 150 KLD. Water consumption breakup is given in Table 3-3.

Table 3-3: Water Consumption Breakup

S. No. Water Consumption Description Quantity

(KLD)

Waste Water Generation

(KLD)

Effluent Treatment &

Disposal Facility

1 Treated water from CETP

Lime, Alum & Nutrient Dosing 16 16 To CETP

Filter Backwash 20 20 To CETP

Sub-total (a) 36 36

2 RO water

Gas Quencher 55 0 Evaporation loss

Spray Drier 30 0 Evaporation loss Scrubber 15 10 To Spray drier

Sub-total (b) 100 10

3 RO Reject Floor and Vehicle Washing 20 20 To CETP

Sub-total (c) 20 20

4 Fresh water

Greenbelt 6 0 - Domestic 1 0.8 Septic tank

Laboratory 1 0.5 To CETP Sub-total (d) 8 1.3

Total water

Requirement (a+b+c+d)

164 67.3

3.9 Quantity of wastes to be generated (liquid and solid) and scheme for their Management/disposal

Solid Waste

Incinerator ash and CETP sludge will be sent to landfill facility.

Liquid Waste

The scrubber water discarded occasionally will be treated in CETP.

Domestic waste water will be disposed in soak pit via septic tank.





3.10 Schematic representations of the feasibility drawing which give information of EIA purpose

Air: Emissions will be controlled by using adequate APCM.

Waste water: Scrubber media will be treated in CETP. Treated effluent from CETP will be disposed to UPSIDC drainage system.

Hazardous waste: Incinerator Ash and CETP sludge will be sent to TSDF site.

Incineration Process Liquid & Solid Waste

Incinerator Ash

Scrubber media

SO2, NOx, PM, HCL, H2S, HF, VOC, Total Dioxins/Furans

CETP Liquid

Effluent

Sludge

Treated Effluent





4 SITE ANALYSIS

4.1 Connectivity

4.1.1 By Road

The site is connected via internal roads to NH-91 at a distance of 1.3 km in SW direction.

4.1.2 By Rail

Ajaibpur railway station is located at an aerial distance of ~6.5 Km in SW direction and Dadri railway station at a distance of 12.5 km in NW direction from the project site.

4.1.3 By Air

Nearest airport from project site is IGI Airport, New Delhi located at an aerial distance of ~ 56 Km in West direction.

4.2 Land Form, Land Use and Land ownership

The site has been purchased by proponent from Uttar Pradesh State Industrial Development Corporation Ltd (UPSIDC). The landuse of the site is industrial.

4.3 Topography (along with map)

The entire area is covered by Indo-Gangetic alluvium of Quaternary age. Physiography, the area is flat terrain and gradient is very gentle sloping towards south western direction. Project site shown on Toposheet (Bulandshahr, Uttar Pradesh) is shown in Annexure 3

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 areas, water bodies (distance from the HFL of the river), CRZ. In case of notified industrial area, a copy of the Gazette Notification should be given.

4.4.1 Water Bodies

Upper Ganga Canal is at distance of ~7.0 km in NE direction and Khatana distributary is at a distance of 3.0 km in NW direction from project site.

4.5 Existing Infrastructure

The proposed site is a Greenfield project and does not have any existing infrastructure.





4.6 Soil Classification

The soil ranges from pure sand to stiff clays and including all combination of the two extreme litho units. The pure sand is called Bhur and clay is called Matiar. The mixture of sand and clay in equal proportion forms Dumat or loam, a good agriculture soil. Several subcategories of Dumat are possible depending upon the contents of clay and sand. The bad land patches (Kallor) which are ingested with Reh at places do not support any vegetation growth. Alluvial soils occurring in flood plain of rivers is called Kemp which yield good crops. Kankars invariably associated with clay and at times retards ground water movement.

4.7 Climatic Data from Secondary Sources

Based on the available long-term climatological tables (1961 – 1990) published by India Meteorological Department (IMD) of Meerut, average temperature and relative humidity are 22.3°C and 68% respectively. 1st Pre-dominant wind direction is noted from West to East (21 %). 2nd pre-dominant wind direction is from East to West (14%).

Above mentioned climatic conditions will be considered during designing stage.

4.8 Social Infrastructure Available

The social infrastructure like health centre, schools, place of worship and community facilities is located at Sikandrabad at a distance of ~ 6.0 km in SE direction.



AREA, SIKANDRABAD, BULANDSHAHAR PLANNING BRIEF


5 PLANNING BRIEF

5.1 Planning concept (type of industries, facilities, transportation etc) Town and Country Planning/ Development Authority Classification

Basic facilities of infrastructure like admin building, processing area, storage area, internal roads etc. shall be developed on the project site. Transportation of effluent and hazardous waste will be carried out through internal roads and finally through NH-91.

5.2 Population Projection

Sikandrabad has population of 81,028 of which 42,152 are males while 38,876 are females as per report released by Census India 2011. Population of Children with age of 0-6 is 12244 which is 15.11 % of total population. Female Sex Ratio is of 922 against state average of 912. Literacy rate is 65.71 % with male literacy around 73.35 % while female literacy rate at 57.49 %.

5.3 Landuse Planning (breakup along with greenbelt etc.)

Site layout of the proposed project is shown in Annexure 4

5.4 Assessment of Infrastructure Demand (Physical & Social)

Assessment of infrastructure demand will be done during social survey to be performed at the time of EIA.

5.5 Amenities/Facilities

Basic Amenities like public transport, water supply, telecommunications, educational institutions, hospitals etc. are available in Sikandrabad at a distance of ~ 6.0 km in SE direction.



AREA, SIKANDRABAD, BULANDSHAHAR PROPOSED

INFRASTRUCTURE


6 PROPOSED INFRASTRUCTURE

6.1 Industrial Area (Processing Area)

The industrial area shall comprise of following sections:

1. Incinerator plant area 2. Storage area 3. CETP area

6.2 Residential Area (Non-Processing Area)

Non-processing area will consist of:

1. Administration building 2. Truck parking area 3. Security cabin 4. Laboratory 5. Weigh bridge room

6.3 Equipment List

Equipment List is provided in Table 6-1.

Table 6-1: List of Equipments

S.No Name of Equipment

1. MS Rotary Kiln Shell, with SS Ends. Tires, Rollers, Bearings, Pad blocks & base frames.

2. Inlet Breaching & base frames

3. Discharge Breaching & base frames 4. Secondary Combustion Chamber 5. Quenching (by air) chamber 6. Refractory and Insulation brick and dam casting 7. Burners (2 Nos.) + 1 Spare gun 8. BMS control panel for rotary & Secondary burners 9. Solid Waste (cylindrical) Ram Feeder 10. Liquid Waste feeding arrangement 11. Ash scrapper conveyer collection system with Motor & Gear box 12. Mist Eliminator 13. Packed bed for Scrubber 14. Bag filter with all assessors 15. SS cyclone Separator 16. Inter connecting ducts 17. Booster ID Fan 18. Induced Draft Fan 19. Pumps for Scrubbers water circulation 20. Self-supported MS Chimney



AREA, SIKANDRABAD, BULANDSHAHAR PROPOSED

INFRASTRUCTURE


6.4 Green Belt

Approx 1200 sqm (~19%) of total plot area will be developed as greenbelt as shown in Annexure 4.

6.5 Social Infrastructure

Described in Chapter 4, Section 4.8

6.6 Connectivity (Traffic and transportation road/ rail/metro/water ways etc)

Described in Chapter 4, Section 4.1

6.7 Drinking Water Management (Source & Supply of Water)

Fresh water requirement of 8 KLD for domestic & gardening purposes will be met through tankers.

6.8 Sewage System

Domestic waste water shall be disposed to soak pit.

6.9 Solid & Industrial Waste Management

Described in Chapter 3 , Section 3.9

6.10 Power Requirement & Source/ Supply

Described in Chapter 3, Section 3.8.1



AREA, SIKANDRABAD, BULANDSHAHAR R & R PLAN


7 REHABILITATION AND RESETTLEMENTS (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)

Not Envisaged as the proposed project site is within industrial estate.



AREA, SIKANDRABAD, BULANDSHAHAR PROJECT SCHEDULE &

COST ESTIMATE


8 PROJECT SCHEDULE AND COST ESTIMATE

8.1 Likely date of start of construction and likely data of completion (Time Schedule for the project to be given)

The construction is likely to start after getting Environmental Clearance and NOC/CTE from EAC and SPCB. The EIA studies are likely to get completed in 14-16 months.

Project implementation schedule describing various activities from finalization of site to project commissioning is tabulated in

M/S. UNNATI UDHYOG PVT LIMITED PRE-FEASIBILITY REPORT - ENVIRONMENTAL CLEARANCE FOR PROPOSED GREENFIELD CETP AND INCINERATION

PLANT AT UPSIDC INDUSTRIAL AREA, SIKANDRABAD, BULANDSHAHAR PROJECT SCHEDULE & COST

ESTIMATE


Table 8-1: Project Implementation Schedule

Act

ivit

y

Feb-

16

Mar

-16

Au

g-16

Oct

-16

Nov

-16

Dec

-16

Jan-

17

Mar

-18

Form 1 submission

ToR presentation at MoEF

Draft EIA Preparation & Submission to SPCB

Presentation at MoEF

Receipt of EC

Application for NOC

NOC receipt

Execution & Commissioning




COST ESTIMATE


8.2 Estimates project cost along with analysis in terms of economic viability of the project

The project cost is estimated to be INR 9.0 Crore. Summary of project cost is shown in Table 8-2.

Table 8-2: Project Cost S.No. Particulars Amount (INR in Crores)

Civil Cost 4.0

Mechanical, Electrical & Instrumentation cost 1.5

1 Total CETP Cost (a) 5.5

2 Incinerator Cost (b) 3

3 Others (c) 0.5

TOTAL PROJECT COST (a+b+c) 9.0 Cr

8.2.1 Profitability

Since the project will cater to the need of industries for disposal of effluent and hazardous waste in the region, it will encourage industrial growth in the region and result in additional revenue for government.




COST ESTIMATE


9 ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS)

9.1 Financial and social benefits with special emphasis on the benefit to the local people including tribal population, if any, in the area

The proposed project will attribute to following social and financial benefits:

Will help small scale industries from huge treatment cost. Treated water after RO, can be used in various industrial process, thereby reducing raw water

intake. Direct and indirect employment to semi skilled people. Labour force from nearby area.



AREA, SIKANDRABAD, BULANDSHAHAR ANNEXURES


ANNXURES


PLANT AT UPSIDC INDUSTRIAL AREA, SIKANDRABAD, BULANDSHAHAR ANNEXURES


Annexure 1: General and Specific Location Map




Annexure 2: Project Boundary Map




Annexure 3: Toposheet




Annexure 4: Site Layout Map

CONTACT DETAILS

Vadodara (Head Office)

871/B/3, GIDC Makarpura, Vadodara, India – 390 010.

E: [email protected]; T:+91-265-3001000; F: +91-265-3001069

Delhi / NCR

Spaze IT Park, Unit No. 1124, IIth Floor, Tower B3, Sector 49, Near Omaxe City Centre Mall, Sohna Road, Gurgaon, Haryana, INDIA - 122002.

E: [email protected];T: +91-124-4242430 to 436; F:+91-124-4242433

Kadam Environmental Consultants w w w . k a d a m e n v i r o . c o m

Env i ronmentfor Deve lopment

UNNATI UDHYOG PVT. LTD. Pre-Feasibility Report...

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