反应精馏

给出了一种能有效求解反应精馏微分代数方程组模型的数值算法。

An efficient numerical algorithm for a differential-algebraic system model of reactive distillation is given .

反应精馏（ReactiveDistillation，简称RD）是化工过程强化的重要方法之一，其数学模型一般为一具有强非线性的微分代数方程组，用传统方法进行数值模拟较为困难。

Reactive distillation is one of the important methods of process strengthening in chemical engineering .

连续反应精馏合成C（16～18）混酸甲酯的研究

Synthesis of Fatty Acid Methyl Esters by Continuous Reaction Rectification

反应精馏法合成N，N-二甲基乙酰胺

Synthesis Technology on N , N-Dimethylacetamide With Reaction Rectification Method

ASPENPLUS模拟与分析酯化反应精馏过程

The Simulation and Analysis of Esterification Reactive Distillation Using ASPEN PLUS

以Visualc++为编程工具，开发了一个新的反应精馏模拟软件SRD。

A new software SRD of simulating reactive distillation processes was developed by use of Visual C + + . The software has a good user interface .

MTBE反应精馏过程动态模拟和控制系统分析

Dynamic Simulation and Control Strategy Evaluation for MTBE Reactive Distillation Process

PbO均相催化反应精馏合成碳酸二苯酯的研究

Study on the synthesis of diphenyl carbonate in homogeneous catalysis by PbO

研究了将反应精馏法用于聚对苯二甲酸乙二醇酯（PET聚酯）生产的直接酯化反应和酯交换反应，并采用过程模拟软件aspenplus模拟了整个反应精馏过程。

The reaction distillation was used for synthesis of polymer monomer BHET . The process was simulated by using ASPEN PLUS .

MTBE装置反应精馏塔工艺操作条件的探讨及优化

Discussion on the Operating Conditions and Optimization of MTBE Reactive Distillation Column

板式反应精馏塔的模拟计算&修正的Newton-Raphson法

Simulation of Distillation with Simultaneous Chemical Reaction & Modified Newton-Raphson Method

对反应精馏塔顶馏出物的分离进行了aspenplus模拟，EA的总回收率可达98.95%。

The separation of overhead product was simulated by ASPEN PLUS . The yield of EA can reach 98.95 % .

UNIFAC方法在醚化反应精馏中的应用分析

The Analysis of Application or UNIFAC Method in Etherification Reaction Distillation

采用化学交换反应精馏法，针对三氟化硼-苯甲醚分离体系，研究了硼同位素分离生产过程的特点，建立了交换精馏塔的稳态数学模型，并利用matlab程序进行模型求解。

By chemical exchange reaction and distillation between BF3 and the complex anisole · BF3 the separation character of boron-10 isotopes was studied . A mathematical model , proposed in this paper , was solved by a Matlab program .

首先对反应精馏装置进行试验研究，并利用aspenplus对其进行模拟，模拟结果与试验结果较吻合。

Based on the results of the Aspen Plus simulation and experiment of the reactive distillation column , the process simulation and experiment were carried out and the feasible process scheme was proposed .

提出了以偏氯乙烯为原料生产1-氯-1,1-二氟乙烷的反应精馏新工艺，并运用aspenplus软件对实现该工艺的反应精馏塔的定态行为进行了数值模拟研究。

A novel process for producing 1-chloro-1,1-difluoroethane from vinylidene chloride by reactive distillation technique was proposed and a numerical simulation study on the steady behavior of the reactive distillation column was carried out with Aspen Plus software .

利用国产固体酸催化剂，以低浓度乙醇及丙烯氧化副产品叔丁醇为原料，用反应精馏与膜分离相耦合的高新技术，直接制取高效无污染汽油添加剂乙基叔丁基醚（ETBE）。

Ethyl tert butyl ether was prepared from ethanol and tert butyl alcohol on strong acid cation exchange resin via reactive distillation coupled with pervaporation .

采用内径φ125/φ140的新型CTST反应精馏复合塔进行了反应精馏合成醋酸甲酯的中试试验，获得了较为满意的试验数据。

The reactive distillation synthesis middle experiment was carried out in the pilot plant with novel composite CTST reactive distillation column , φ 125 / φ 140 in diameter .

研究了混合碳四和乙醇合成乙基叔丁基醚（ETBE）的反应精馏过程。

Reactive distillation of synthesizing ethyl tertiary-butyl ether ( ETBE ) from C4 cuts and ethanol was investigated , in which the structured packing coated with β zeolite was used as catalyst .

初步完成了年产2万吨醋酸甲酯工艺包的设计工作。反应精馏塔高度为42.7米，78块CTST塔板，直径为Φ1200/Φ1600。

A reactive / distillation column which is 20000t / year in production has been designed and the column is 42.7 meters high with 78 CTST trays , Φ 1200 / Φ 1600 in diameter .

本文对环氧乙烷（EO）和正丁醇（n-Butanol）合成乙二醇单丁醚（EGMBE）反应精馏塔的控制方案设计进行了研究，旨在为装置的稳态运行和操作控制奠定理论基础。

In this paper , the reactive distillation column control structure of ethylene glycol monobutyl ether synthesized by ethylene oxide and n-butyl alcohol are designed , aiming at providing some theoretical foundation for dynamic operation and operation control .

介绍连续反应精馏过程设计的两种研究方法：静态分析法和有限元正交搭配OCFE法。

Tow researching methods of design of continuous reactive distillation processes are addressed in this paper Analysis of statics and orthogonal collocation on finite elements ( OCFE ) .

内部热耦合反应精馏塔（简称IHIRDC）是将原来反应塔的反应段塔板数平均分为高压塔段和低压塔段进行热传递。

In the internal heat-integrated reactive distillation column ( IHIRDC ), the reaction zone is divided into a high pressure section and a low pressure section to achieve the heat transfer .

反应精馏过程图解法设计策略研究

Studies on the Strategy of Graphical Design for Reactive Distillation System

加盐萃取精馏法制无水异丙醇过程模拟催化氧化-反应精馏法处理炼油废水的研究

Study on treatment of refinery wastewater by catalytic oxidation-reactive distillation method

反应精馏法合成乙酸乙酯工艺条件的选择

Technological Conditions Selection of Synthesizing Ethyl Acetate by Reactive Distillation Method

连续催化反应精馏生产醋酸丁酯新工艺

Butyl Acetate Production New Process by Continuous Catalytic Reaction and Distillation

反应精馏相关技术研究进展（Ⅱ）&过程优化与控制技术

Advances in Reactive Distillation Research (ⅱ) & Process Control and Optimization

乳酸提纯反应精馏新工艺非平衡级稳态模拟

Non-equilibrium stage static simulation of lactic acid purification reactive distillation process

有机氯化物的反应精馏合成研究

Study on Synthesis of Organic Chloride by the Reaction Rectification Technique