本文给出了一种求算二元精馏理论塔板数的简化逐板计算法。
A simplified Lewis-Mathson method for seeking the number of theoretical plates in binary rectification column is presented.
针对苯—甲苯精馏过程，采用逐板计算的方法进行动态机理建模；
A mechanism model of benzene-toluene separation process is obtained through rigorous plate-by-plate calculation.
提出了简捷优化法与逐板严格计算优化相结合的方法，克服了以往优化设计计算中仅求得局部最优解的弊端。
Simple optimization method and rigorous calculation method are integrated in process optimization. It may overcome the defect of part optimal result.
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