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 effluent from lime preparation and clarifire houses contains suspended particles and inorganic chemicals as TDS.

Total quantity of effluent due to spillage, leakage, floor and equipment washings will be about 72 M3/day.

2.16   Boiler Blow Down

Boiler feed wafer contains a small concentration of dissolved solids. Antiscaling and stabilizing chemicals are added to the boiler feed water to prevent scale formation, corrosion. As the evaporation continues, concentration of dissolved solids in boiler increases. Therefore solids continues to build up in the boiler, boiler blow down of about 2%of the total evaporation is therefore given from the boiler to control the concentration of dissolved  solids in the boiler water. The quantity of boiler blow down is relatively of-Better quality and therefore advantageously added to the circulating cooling'water channel. The blow down allowed in the boiler is about 24 m3/d.

2.16.1 Laboratory Waste Water

Waste water is generated in the laboratory due to washing and rinsing of apparatus. The chemicals and juice used in the laboratory are ultimately let out to drain along with water as waste water. The effluent is small in quantity and moderately contaminated. Recycle of juice samples and chemicals to factory process will control the quantity and. quality of waste water from the laboratory. The laboratory waste water generated will be about 0.5 m3 /day

2.16.2 Domestic Waste Water

Domestic waste water of about 40 lit/ d, per head is generated in the factory. The effluent is stabilized in septic tanks and overflow is taken to effluent treatment plant for further treatment. The domestic effluent from the factory will be about 12 m3/day

2.16.3 Purge From Barometric Condenser

The vapors from last effect evaporator and pan boiling are cooled in barometric condensers. The vapour compensate alongwith the cooling (quenching) water goes to the cooling tower. Part of the  water is lost as vapour losses and drift in the cooling tower. Excess water from cooling tower channel is discharged as purge effluent. In case of overloading of pan and evaporators the spooling water may become highly contaminated due to entrainments. This water is relatively more contaminated as compared to the cooling water of turbine condenser or of mill bearing. Hence, the purge water from the latter are added to the circulating

 
 

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