« lessĪ solution strategy for retrofit problems requires a two phase procedure. In this first part of the series, we present the mathematical model for a general MFMP column, derive constraints for feasible separation and minimum reflux condition, discuss their geometric interpretations, and present an illustrative example to demonstrate the effectiveness of our approach. Compared with existing techniques, this method does not involve any rigorous tray‐by‐tray calculation, more » nor does it require guessing of key components. The classic McCabe‐Thiele or Underwood method is a special case of this general approach. In this series, we present the first accurate shortcut based algorithmic method to determine the minimum reflux condition for any general multi‐feed, multi‐product (MFMP) distillation column separating any ideal multicomponent mixture. Thus, it is a key parameter for distillation systems design, operation, and comparison. The minimum reflux ratio of a distillation column is directly related to its energy consumption and capital cost. = ,Ībstract Multi‐feed, multi‐product distillation columns are ubiquitous in multicomponent distillation systems.
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