Use
a Vent Condenser to Recover Flash Steam Energy
When the pressure of saturated condensate
is reduced, a portion of the liquid "flashes" to low pressure steam.
Depending on the pressures involved, the flash steam contains approximately
10% to 40% of the energy content of the original condensate. In
most cases, including condensate receivers and deaerators, the flashing
steam is vented and its energy content lost. To preserve the energy
content lost in venting the flashed steam, a heat exchanger can
be placed in the vent to recover this energy. The following table
indicates the energy content of flash steam at atmospheric pressure.
(Source: US Department of Energy)
|
Energy Recovery Potential of
a Vent Condenser
|
|
Pipe Diameter (Inches)
|
Energy Content, MMBtu/year*
|
|
Steam Velocity, feet/min
|
|
200
|
300
|
400
|
500
|
600
|
|
2
|
90
|
140
|
185
|
230
|
280
|
|
4
|
370
|
555
|
740
|
925
|
1,110
|
|
6
|
835
|
1,250
|
1,665
|
2,085
|
2,500
|
|
10
|
2,315
|
3,470
|
4,630
|
5,875
|
6,945
|
* Assumes continuous operation, 70° F makeup water, and condensed
steam at 100° F.
Example
Consider a vent pipe with the following conditions:
| Velocity of flash steam: |
_300 feet per minute |
| Diameter of vent pipe: |
_4 inches |
| Hours of operation: |
_8,000 hours per year (hr/yr) |
| Boiler efficiency: |
_80% |
| Cost of fuel: |
_US $8.00 per million Btu ($8.00/MMBtu) |
Download the original US Department of Energy PDF document.
A vent condenser could condense the flash steam, transfer its thermal
energy to incoming makeup water, and then return it to the boiler.
Energy is recovered in two forms: hotter makeup water and clean,
distilled condensate ready for productive use in your operation.
Referring to the table above, the potential energy recovered from
the flashed steam is 555 MMBtu, based on 8,760 hours of annual operation.
Correct this value for actual operating hours and boiler efficiency:
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