The system shown in the sketch achieves a suction pressure of 1 mbar.
The temperature of the available cooling water determines the pressure
which can be reached in the first surface condenser. In this example, two
ejector stages have been series-connected to achieve a suction pressure
of 1 mbar with the lowest possible use of motive flow.
Two further ejector stages compress the non-condensable components
of the suction flow from the first condenser up to atmospheric pressure.
The interconnected surface condenser condenses the motive steam
of the preceding ejector.
Advantage:
- Separation of the process- and cooling water flows
Disadvantage:
- Possibility of polution on the process- and cooling water side
Option:
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