1.
Cost accounting and comparison on three types of double-effect distillation configurations
双效精馏结构的运行成本核算与比较
2.
Dynamic Behavior of a Novel Double-effect Distillation Process for Methanol Purification;
新型甲醇精制双效精馏流程的动态行为研究
3.
Simulation and optimization of pressure swing distillation of methanol with countercurrent heat integration process
甲醇变压逆流双效精馏系统工艺模拟与优化
4.
Researches on Modeling, Dynamical Behavior and Controllability Analysis of a Novel Double-effect Distillation Process for Methanol Purification;
一种新型甲醇双效精馏系统建模、动态行为与控制的若干问题研究
5.
Simulation of Separating Toluene-Butanol by Double Effect Pressure Swing Distillation
采用双效变压精馏工艺分离甲苯-正丁醇的模拟
6.
Study on separation of H_2/HD by cryogenic distillation with two interlinking columns
双柱级联低温精馏分离H_2/HD过程研究
7.
Study on Dual-still Batch Extractive Distillation with Two Solvent Inlets;
双溶剂口的双釜间歇萃取精馏过程研究
8.
Analyzes the Crack Failure of the Aldehyde Rectifying Tower Stainless Steel 00Cr17Ni14Mo3joint Pipe;
00Cr17Ni14MO3钢乙醛精馏塔底接管失效研究
9.
Adaptability and Thermodynamic Efficiency of Thermally Coupled Distillation;
热耦合精馏的适应性及其热力学效率
10.
Effects of the feed composition on the energy-saving efficiency of the thermally coupled distillation
进料组成对热偶精馏节能效果的影响
11.
Study on Dual Temeprature Control of Batch Distillation;
循环全回流间歇精馏双温控制方式研究
12.
The Study of Multi-effect Distillation Energy-saving Technology Based on Genetic Algorithm;
基于遗传算法的多效精馏节能技术研究
13.
Research on Exergy Analysis and Energy Saving of Diabatic Column
透热精馏有效能分析和节能方法的研究
14.
OPERATION EXPERIENCE AND EFFECT OF OPTIMIZATING PRIMARY FRACTIONATOR DURING CRUDE BENZOL REFINING PRODUCTION
粗苯精制生产中优化初馏塔操作实践及效果
15.
Synthesizing and Analyzing the Dual-Point Temperature Control System of an Ideal Heat-Integrated Distillation Column
理想内部热耦合精馏塔双温度控制系统的综合与分析
16.
Study on the Cascaded Process of Dynamic-Accumulation in Batch Distillation with Exchange of Liquid Phase
间歇精馏双塔动态累积液相交换串联过程的研究
17.
After reforming, the top cyclohexene in separating column decreased from6.5% to4.0%, the top cyclohexene of recovery column decreased from3.5%～4.8% to2.5%, the purity of cyclohexene increased from95% to97%.
本次改造提供了一种萃取精馏塔扩能改造的新思路———更改部分工艺,提高提馏段效率。
18.
The rectification of errors, alcohol
错误的改正、酒精的精馏