• Reflux ratio, feed concentration and cycling time have effect on the separation.

    回流比、进料浓度、周期循环时间均对半连续热参数泵分离效果产生影响。

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  • The effects of reflux ratio and operating pressure on separation performance were also studied.

    研究了操作压力和回流比对系统分离性能的影响。

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  • Increase of the reflux ratio can improve the removal efficiency, with optimum reflux ratio is 60%-80%.

    适当提高回流比,可提高去除效率,一般最佳回流比为60% ~ 80%。

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  • The effects of separation temperature, time and reflux ratio on separation efficiency were investigated.

    考察了分离温度、时间和回流比等因素对分离效果的影响。

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  • A new train of thought for finding minimum reflux ratio in distillation has been proposed in this paper.

    本文提出寻求精馏系统最小回流比的新思路,并将它用于对二元精馏最小回流比的计算。

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  • Effect of reflux ratio, operation pressure and bottom temperature on fractionation results were discussed.

    讨论和分析了脂肪酸甲酯间歇精馏过程中回流比、操作压力、釜温对精馏效果的影响。

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  • The effects of acid-alcohol ratio, reflux ratio, feeding flux, and feeding location on the process are investigated.

    考察了酸醇比、回流比、进料流量、进料位置等因素对反应过程的影响。

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  • In this paper, the controlled object is concentration of distillate, reflux ratio is selected as the manipulated variable.

    两种控制方法以塔顶产品的液相轻组分浓度为被控变量,回流比为控制量。

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  • The distillation conditions including overhead pressure, reflux ratio for the recovery of 1,2- propylene glycol were studied.

    本文还研究了精馏的一些操作条件对1,2-丙二醇精制过程的影响(塔顶压力、回流比等)。

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  • Furthermore the effects of tower top pressure, temperatures of tower top and bottom, reflux ratio on product purity were analyzed.

    同时探讨了塔顶压强、塔顶和塔釜温度、回流比变化对产品纯度的影响,获得了试验条件下的最佳操作条件。

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  • The changing curve of temperature and concentration in top and bottom with time in fixed reflux ratio and batch distillation, were also obtained.

    获得了该塔在全回流及部分回流条件下的全塔效率,固定回流比间歇精馏下的塔顶、塔釜温度及浓度随时间的变化曲线等。

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  • The results show that the top concentration of 1-hexene increases and the reflux ratio of 1-hexene slowly decreases with the increase of the reflux rate.

    试验得出随着回流比的增加,塔顶1-己烯浓度增大,而1-己烯的收率有缓慢下降的趋势。

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  • The recovered ethanol with less than 10% methanol can be purified in a dehydration tower and a separation tower with 40 theoretical plates and a reflux ratio of 15.

    环合废液脱水后,分离塔回流比为15,理论板为40时,回收乙醇中甲醇的质量分数小于10%。

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  • The main design parameters, such as NTS, reflux ratio and feed location are analyzed in detail to get the optimized design of the ethyl acetate concentration column.

    对提浓塔的理论塔板数、回流量和进料位置等参数进行分析,得到了最优化的设计参数。

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  • In order to determine the influence on account of operating conditions, aeration time, DO, reflux ratio, water drainage ratio were studied by using small CAST test-bed.

    为了确定运行条件的影响,采用搭建CAST小试试验台对曝气时间、DO、回流比、排水比进行了研究。

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  • The effects of catalyst quantity, acetic alcohol mole ratio, acetic acid and ethyl alcohol feed site, reflux ratio and reflux composition on the process are investigated.

    对乙酸与乙醇酯化反应体系,考察了催化剂用量、酸醇比、进料位置、回流比、回流组成等因素对过程的影响。

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  • Using reflux ratio and recovery as decision variables and total cost as objective function, the computer programs were programmed and optimized calculation was carried out.

    以回流比、回收率为决策变量,总费用最小为目标函数,编制计算机程序进行优化计算。

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  • A case study of gas separation system is given to illustrate the effects of product quality, reflux ratio and tower pressure to total economic benefit through flow simulation.

    本文以某气体分馏装置为例,通过严格的流程模拟,分析了产品质量、回流比和塔压等操作参数对总经济效益的影响。

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  • In this paper, a method of optimizing reflux ratio in rectifying tower is introduced. An economical model of the rectifying tower and its solving approaches are also presented.

    本文介绍一种精馏塔中适宜回流比的优化方法。给出了精馏塔的经济模型及相应的求解方法和求解过程。

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  • By simulation, the effects of reflux ratio, the area of the preheat-cool exchanger, cool duty of still pot, heat duty of evaporator and the liquid flow recycled by pump on heat sens...

    通过模拟计算,研究了回流比、预热冷却器面积、塔釜冷却量、蒸发器加热量以及泵循环流量对热敏精馏过程的影响。

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  • By analyzing the changes of reflux ratio, the optimum feed positions within the two distillation columns in the experimental device for double-effects distillation HGL of forward feed was determined.

    根据回流比的变化,对顺流双效HGL精馏实验装置中两精馏塔的进料位置进行了优化。

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  • The catalyst quantity, alcohol-acetic mole ratio, feed rate and reflux feed site effects on the process are investigated.

    对醋酸与正丁醇酯化反应体系,考察了催化剂用量、醇酸比、进料流量、进料位置、回流位置等因素对过程的影响。

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  • The catalyst quantity, alcohol-acetic mole ratio, feed rate and reflux feed site effects on the process are investigated.

    对醋酸与正丁醇酯化反应体系,考察了催化剂用量、醇酸比、进料流量、进料位置、回流位置等因素对过程的影响。

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