Introduction
There is a large difference between super heated steam temperature, as supplied from boiler to turbine and the condenser temperature, as it leaves the condenser and is recycled to the boiler as a boiler feed water. Now to increase the condensate temperature, on its way back to the boiler and as a consequence to increase the thermal efficiency of the plant, the process of regenerative feed heating is introduced.
In this process small quantity of steam drawn at various
stages of the turbine are allowed to pass through several feed heaters. Whereupon
they condense in the process of either direct heat exchanger or indirect heat
exchanger with the condensate being pumped to the boiler.
Method |
|
Direct
contact feed heating |
Indirect
contact feed heating |
|
Drain pump
method |
|
All drains to
Hot Well method |
|
Cascade
method |
Feed water heater:
A.
Close type heater => They are
basically shell and tube type heat exchanger which operated at higher pressure
then condenser because bleed steam is condensed on the shell side whereas feed water,
acting like circulating cooling water in the condenser, is heated on the tube
side (LP & HP Heater).
B.
Open type heater=> It is one in which the feed water is heated by
direct mixing with the bleed steam of turbine (De-aerator).
Terminal Temperature Difference (TTD)
= saturation temperature of bleed steam - exit water temperature.
- Desuperheating zone.
- Condensing Zone.
- Drain cooling Zone.
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