Condenser Design on Aspen-Plus Software
(Heat Exchanger design with a phase change)
Author: Jim Lang (©SDSM&T, 2000)
This is a continued look into the process of condensation and condenser design on AspenPlus. The following example will be used.
Problem statement:
Saturated steam at 1atm and 101° C needs to be condensed so that it may be used as a stripping fluid in a column downstream. Once again, Ethylene Glycol is available at 340 K and 1 atm. All of the steam needs to be condensed. The plant manager recommends using a vertical countercurrent heat exchanger with the steam in the tubes. Pressure drop is not a concern.
Condenser Design on Aspen-Plus Software.pdf
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