We present two kinds of optimal control policy for multicomponent batch distillation.

多元间歇精馏塔最常用的操作方式是控制回流比.

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The process utility demand was related to the reflux ratio of distillation column.

最后探讨了一下蒸馏塔的回流比对过程用能方面产生的影响.

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The influence of internal recycle ratio and influent loads on biological nitrogen removal was discussed.

结果考察工艺的启动挂膜性能以及硝化液回流比和进水负荷对脱氮效果的影响.

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The effect of reflux temperature , reflux ratio and reaction pressure on the oxidation process was simulated.

用此模型考察了反应压力 、 冷凝回流温度和回流比对反应过程的影响.

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Effects of feed rate, feed fraction, reflux ratio and feed position on reaction distillation were investigated.

考察了进料流率, 进料组成, 回流比,进料位置对反应精馏的影响.

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