A new generalized algorithm for design calculation of various kinds of complex distillation columns(with multiple feeds
vapor and liquid phase side withdrawals and intermediate heat exchangers) has been developed. Based on specified independent variables: conditions of feeds
yields of light and heavy key components
yield and concentration of specified component in side-cut product
etc.
a set of optimum design variables (reflux ratio
number of equilibrium stages required
feeds and sidewithdrawals locations
etc. )were determined by optimization technique. This new algorithm as coupled with the SHBWR or PR model for vapor-liquid equilibrium and enthalpy calculations
has been tested on five-light hydrocarbon complex distillation columns(including three field operating columns)