二甲基甲酰胺法萃取精馏生产1,3-丁二烯的模拟计算(英文)

被引：19

作者：

杨小健 ^{[1
]}

殷绚 ^{[1
]}

欧阳平凯 ^{[2
]}

机构：

[1] Controlling Engineering Center,Nanjing University of Technology,Nanjing ,China

[2] College of Life Science and Pharmaceutical Engineering,Nanjing University of Technology,Nanjing,China

来源：

ChineseJournalofChemicalEngineering | 2009年 / 17卷 / 01期

关键词：

D O I：

暂无

中图分类号：

TQ221.223 [];

学科分类号：

摘要：

Nowadays,extractive distillation is the main technique to produce 1,3-butadiene.This study simulated the 1,3-butadiene production process with DMF extractive distillation by Aspen Plus.The solvent ratio is the most important parameter to the extractive distillation process.The article has given out the proper solvent ratios,reflux ratios,distillate ratios,and bottom product ratios of the columns.It also discusses the thermal loads of several columns.The results of simulation are consequently compared with the plant data,which shows good accordance with each other.

引用

页码：27 / 35

页数：9

共 4 条

[1]

Simulation of circulating fluidized bed reactors using ASPEN PLUS [J].

Sotudeh-Gharebaagh, R ;

Legros, R ;

Chaouki, J ;

Paris, J .

FUEL, 1998, 77 (04) :327-337

[2]

影响丁二烯装置长周期运行的原因分析 [J].

周彤 ;

巩家志 ;

赵德智 .

辽宁化工, 2004, (12) :711-713+737

[3]

国内外丁二烯发展态势 [J].

赵玉中 ;

张兰波 ;

王进 .

弹性体, 2004, (01) :57-61

[4]

Process for producing1;3-butadiene Arakawa;M;Yoshioka;H;Nakazawa;K; US Pat.4504692 1985,

← 1 →