Extending Murphree Tray Efficiency from Mass to Heat Transfer in Distillation
In this work an extension of the well-known Murphree tray efficiency is proposed. In difference to the original model, vapor and liquid streams leaving the stage have different temperatures. In order to model the vapor temperature, the Murphree efficiency equation is used to calculate the change of...
| Main Authors: | , |
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| Format: | Article |
| Language: | English |
| Published: |
AIDIC Servizi S.r.l.
2018-10-01
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| Series: | Chemical Engineering Transactions |
| Online Access: | https://www.cetjournal.it/index.php/cet/article/view/9199 |