Executive Summary
   
  Chapter 1
Introduction
   
  Chapter 2
Project Description
General
Status of Project
Justification of the Project
Process Details
Steam Power Cycle
Water Condensate
Grid Interface
Raw Material
Product & By product
Water System
Water Requirement
Provision for Pollution Control
Project Implementation
Power Requirement
Waste Water Generation
Spilage, leakage
Boiler Blow Down
Characteristics of waste Water
Effluent Treatment Plant
Effluent Treatment Process
Specification of ETP Plant
Gaseous Emmission
Solid Waste and its Disposal
Noise (Source & Control)
   
  Chapter 3
Environmental Setting of Site
Physical Environment
Aesthetic Environment
Existing Secenario of Co-generation Power Plant
   
  Chapter 4
Environment Impact Prediction
Impact During Construction Phase
Impact during Operation Phase
Impact on Socio-Economic Environment
   
  Chapter 5
Environment Impact Analysis
Matrix Method
Check List Method
Expert Advice
Economic Technique
   
  Chapter 6
Environment Management Plan
Air Pollution Control
Noise Pollution Control
Command Area Development
Monitoring System
Monitoring Facility
   
   
  Annexures
List of Machinery
Study Area
Plot Plan  
Ambient Air Quality Monitored at MPCL  
Meteoroloical Data at MPCL  
Noise Level Monitored Monitored at MPCL  
Ground Water Quality Monitored within Buffer Zone  
Surface Water Quality Monitored Within Buffer Zone  

 Land Use Pattern Within Buffer Zone

 

Soil Quality Monitored Within Buffer Zone

 

Cropping Pattern Within Buffer Zone

 

Demographic Structure Within Buffer Zone

 

Occupational Structure Within Buffer Zone

 

Post Telegraph and Communication Facilities Within Buffer Zone

 

Educational Facilities Within Buffer Zone

 

Health Care Facilities Within Buffer Zone

 

Drinking Water Facilities Within Buffer Zone

 

Flow Diagram of Sugar ETP

 

 

2.3  PROCESS DETAILS

The proposed cogen power plant has been thus designed to be implemented by installing a extraction cum condensing 30 MW turbine.

The cane crushing capacity has been estimated to stabilize to 82 TCH at 22 hours / day basis and 160 days of crushing from 2004 onwards, or around 6.2 lakh MT of cane crushing per year.

Bagasse generation, usage for bagaciiio / handling losses and available for boiler as fuel, have been respectively estimated at 29%, 1% and 28% of cane crushed.

Steam consumption for sugar mill has been taken at total 49 % on cane with 3 % on cine for MP steam" and 46 % on cane for LP steam for process requirements, as per the design of the sugar plant equipment and guarantees offered by the equipment supplier.

Moisture content of wet mill bagasse has been estimated at average 50%.

The cogen power plant will work for 160 season days, with 1 x 120 TPH boiler, 86 kg/cm2 and 515 deg. C and 1 x 30 MW TG sets.

Power consumption for sugar process has been estimated at 27 kwh / TCH

 2.4  Steam & Power Cycle Balances


Table No. 2 Season Steam & Bagasse Balance

 

Sr. no

 

Particulars                             

Value

 
     

1.

 

Crushing rate (TCH)

159

2.

 

No. of hrs/day

22

3.

 

Crushing / day, TCD

3960

4.

 

No. of season, days

160

5.

 

Design Cane crushing, MT

5,59,680

6.

 

Bagasse generation, % cane (TPHJ)

49.29(31.0)

7.

 

Bagasse available as fuel, % cane (TPH)

48.02 (30)

8.

 

Evaporation Ratio, kg/kg

2.35

9.

 

Total Steam generation, TPH

118

10.

 

Total Bagasse consumption, % cane (TPH)

47.2

11.

 

Bagasse saved for offseason, % cane (TPH)

0.817(2876)

12.

 

Steam consumption, TPH

 

13.

 

MP steam (8 kg/cm2a ) from 30 MW STG

 

 

 

 
 

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