But why?
The reason is the reboiler must
decrease. If the reflux rate is held constant, and the concentration of the
heavy component in the overhead is held constant, then the condenser duty
(i.e., heat removal) is also constant. Thus, if I increase the heat input with the
feed, it follows that the reboiler duty must go down to maintain the tower heat
balance.
A decrease in the reboiler duty will
also decrease the vapor flow through the trays between the feed tray and the
bottom tray. As this vapor flow goes down, the stripping section trays don’t
work as hard. Or, we can say that the stripping factor is reduced. Or, perhaps,
the rate of tray deck leakage increases. Either way, the amount of the lighter
component slipping into the bottom of the distillation tower will increase.
What then are the benefits of
increased feed preheat? There must be such benefits, otherwise most of our
towers would not have feed preheaters:
- Saves Energy – The feed preheater normally uses
waste heat or low pressure steam, with little value. This saves more
valuable reboiler steam.
- Supplements Reboiler Capacity – If the tower is
not condenser limited, but limited by the capacity of the reboiler, then
more feed preheat will permit higher reflux rates, and hence better
fractionation efficiency.
- Stops Flooding in Bottom Section Trays – If the
tower is limited by flooding or entrainment in the bottom stripping trays,
then more feed preheat, which reduces the reboiler duty, will improve
fractionation. This happens because the vapor velocities will go down, as
the feed preheat goes up.
So,
depending on the hydraulic capacity of the stripping trays, feed preheat can
make fractionation better or worse.
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