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

 

 

The planned 30 MW grid connected cogeneration power plant facility by (CAIL) , will be a Renewabie Energy based grid connected power piant that will be operated for 330 days in a year. All the plant & equipment will be designed for a minimum of 8000 hours of operation in a year.

All the piant and systems shall be designed to achieve the be'st possible efficiency under the specified operating conditions.

2.5    Water, Condensate & Power Balances

Water & condensate, power and bagasse balances both for season and off season operations of the proposed power plant, are given in the following
paragraphs:

Table no. 4: Water & Condensate Balance


 
Sr.No.

Item

Value, TPH

 
 

 

Season

Off season

 
       

1.

Condensate return from sugar mill at around 90° C

71.5

-

2.

Steam to de-aerator

3.0

9.3

3.

Blow down flash steam recovery

0.35

0.357

4.

Condensate return from hot well

11.16

81.2

5.

Make up DM water addition from DM plant      

20.53

15.82

6.

Condensate from HP Heater

13.5

13.5

7.

Condensate from LP Heater

    -

4.5

8.

Desuperheater water addition

0.2

   -

9.

Flow from de-aerator

120.04

120.2

 

The complete plant instrumentation and control system shall be based on DCS philosophy, covering the total functioning requirements of measuring, monitoring, alarming and controlling, logging, sequence interlocks and equipment protection etc.There will be a separate covered, storage yard for bagasse Tor feeding the power plant boiler, with stacking and reclaiming conveyors. The ash handling system will be a combination of submerged belt conveyor for the grate bottom ash and combination of screw and belt conveyors for the rest of the ash handling points.  All the ash will be taken and stored in bins and disposed off in trucks fa. be mixed with sugar mill press mud and distributed to farmers for use as a fertilizer.  

 
 

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