In a boiler drum exist water and steam at saturation
pressure and saturation temperature. Furthermore, the water is mixed with steam
bubbles in different sizes. If one opens the valve to a steam consumer then the
pressure in the boiler drum falls and hence the steam bubbles expand and the
water level rises despite the fact that the water mass actually decreases. On
the other hand, pumping in cold feed water will cause the steam bubbles to
collapse and the water level falls when the water quantity actually increases
in the steam drum. These shrinks and swell phenomena will complicate the
control of the boilers steam drum level.
For a boiler with large amount of water and relatively low steam production a
single water level transmitter on the steam drum is sufficient for the level
controller to maintain a level with acceptable variation.
Far more sophisticated methods are required for boilers with
high steam production and relatively small water volume.
This classic method works as follow:
The outlet steam mass-flow is measured and the inlet feedwater mass-flow
is adjusted to the very same amount. The level transmitter is merely used to
tune up the system so the water level lies within the limits.
Thus, the input to the setpoint of the feedwater flow controller is the sum of
the outlet steam flow signal and the reversed water level controllers signal
minus 12 mA (or 9 psi if it is a pneumatic system).
Add to the monthly maintenance list:
- Check the process impulse piping between the steam outlet line and the
steam flow transmitter. Fur deposit is very common in the orifices
measuring holes.
- Check the process piping between the steam drum and the water level
transmitter. Condensate has to accumulate in the tubing before the transmitter
can work properly again.
(Draining the level transmitter that often wouldnt be necessary if you
have stainless steel tubing between the boiler drum and the level transmitter).
N.B. the feedwater flow controller has to be in manual mode
during these procedures.
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