因此，本模型可用于含醋酸物系的相平衡和精馏计算。
Therefore, this model is applicable to the phase equilibrium and distillation calculation of systems containing acetic acid.
实验结果表明催化精馏技术应用于醋酸甲酯的水解反应是可行的。
The experimental results show that the catalytic rectification technique can be successfully used in the hydrolysis of methyl acetate.
计算表明，本算法可以快速准确地求解大规模复杂精馏系统优化综合问题。
The calculation results demonstrated that IGP could solve the problems of optimization synthesis for large-scale complex distillation system rapidly.
精馏是分离互溶液体混合物最常用的方法，也是化学工业中最大的能耗单元操作之一。
Distillation is the most common method to separate liquid mixtures, while it is also one of the biggest energy consuming unit operation in process industries.
催化精馏技术应用于酯化反应体系，提高了反应的转化率、原材料利用率和产品收率。
The conversion, the utilization rate of raw materials and the product yield of esterification reactions are raised by applying the catalytic rectification process.
控制精馏塔回流比，保持流量稳定。
相反，连续精馏塔处理连续进料。
In contrast, continuous columns process a continuous feed stream.
他用精馏酒精清洗瓶子。
得到了催化精馏塔内的温度及液相组成分布。
The axial profile of temperature and concentration in the column is calculated.
采用反应精馏新工艺由环氧丙烷水合制丙二醇。
A new process of Hydration of propylene oxide to glycols was introduced.
本文介绍缔合物系精馏过程模拟计算的松弛法。
The relaxation method in analog computation for rectification process of associate systems is introduced.
据此，离线求得了该精馏过程的静态最优工作点。
Thus, the optimal operating points of this distillation process are solved off line.
介绍了严格的平衡级精馏模拟操作型算法的研究进展。
The prospect of strict equilibrium-stage distillation operating algorithm is introduced in this article.
本发明大幅降低生产成本和能耗，精馏节能40%左右。
The invention greatly reduces the production cost and energy consumption, and saved energy by about 40% in rectification.
采用催化反应精馏技术，研究了合成乙酸异戊酯的新工艺。
The new process of synthesis iso-amyl acetate by catalytic reaction rectification was studied.
反应产物经精馏分离后得到的产品纯度在99.8%以上。
The purity of the product after rectifying process could reach to 99.8%.
本文对反应精馏技术在工艺和模拟方面的研究进展作了概述。
Both the technology and simulation research development of reactive distillation were introduced briefly in this article.
提出一种面向复杂过程的混合建模策略并应用于精馏塔的建模。
A hybrid modeling strategy for complex process is presented and applied to simulate a distillation.
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.
本文围绕着间歇精馏塔对其动态数学模型及其控制方法进行了研究。
The dynamic model and its control method of batch distillation column are studied in this paper.
采用演化算法求解具有组合爆炸特征的精馏分离序列优化综合问题。
Evolutionary algorithm is applied to solve distillation separation sequence optimization synthesis problems that are characteristic of combination explosion.
总结了磷化氢的精制方法，主要有吸附法、低温精馏法和膜分离法等。
The purification methods of phosphine include adsorption method, low temperature distillation method and membrane separation method etc.
以一个理想二元精馏塔为对象，讨论基于塔板温度的产品组分估计问题。
To estimate the product composition for an ideal binary distillation tower based on tray temperatures is discussed.
在精馏设计过程中，简捷法是对所提供的方案进行快速估算的先决条件。
Short-cut methods are prerequisite for the fast evaluation of alternative design methods in rectification process.
试验结果表明，苯甲酸精馏装置的实际运转结果与模拟计算的情况基本吻合。
Industrial experiments were carried out and the practical operation results were conformed to the simulation.
试验结果表明，苯甲酸精馏装置的实际运转结果与模拟计算的情况基本吻合。
Industrial experiments were carried out and the practical operation results were conformed to the simulation.
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