Reboiler Steam Flow Control
All the reboilers I have worked with have had the flow control valve in
the steam line feeding the reboiler, and a steam trap in the condensate
exit line.
However, I recently saw a P&ID which showed the
flow control valve in the condensate line, but with the flow element
still in the steam line. I suppose this has the advantage of making the
valve smaller and saving a steam trapping station, but I would be
interested to know if this works without blowing steam into the
condensate line?Screw pumps
This is a situation of expecting many things to be done without enough
measured or manipulated variables. You are correct that there is no
mechanism to prevent steam from blowing through to the condensate
line.Self-priming pumps I suggest an external liquid leg with steam trap be placed on the
condensate outlet or a level instrument to measure the liquid level as
TDK2 suggested. Even if the control valve fails open, the steam trap
will prevent blow through. You may also want to relocate the control
valve, albeit larger, back to the reboiler inlet. This method hase some
weaknesses, but nothing as bad as what you'd get with this scheme.
This
scheme has a potential failure built into it that could be very
aggravating. The tower will respond to a change by increasing the heat
input and steam flow rate. The condensate drain valve will open and
reboiler could lose the liquid leg and get steam blowing through. At
this point the steam is providing sensible and no latent heat to the
tower. The controls will ask for more steam flow and increase the
amount of blow through.Chemical pumps
Also maintaining a water level in the
reboiler promotes corrosion and after a while you'll get a leak in the
reboiler and something is going where it's not wanted.Pneumatic and electric diaphragm pumps
By not regulating the steam supply one provides the reboiler with the
maximum pressure (and saturation temperature) available. So instead of
changing the delta T, one changes the surface. Changes in HE surface
would be "linear" if the the reboiler is a vertical cylinder.
A
demand for the "highest" and "constant" steam temperature for the
particular duty could serve to explain the reboiler's controlling
procedure.Sweage pumps &Sludge pumps
Besides, by not regulating down the steam pressure,
one may obviate the need of using a special pump/trap for the removal of
condensate.
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