摘要
采用Aspen Plus模拟软件对二异丙苯精馏分离工艺进行模拟计算。设计出精馏工艺流程,用DSTWU简捷法精馏设计模型和NRTL-RK模型,得到回流比、塔板数和进料位置等工艺参数,为该工艺的开发提供依据。
Using Aspen Plus simulation software, the simulation of diisopropylbenzene rectification process was carried out. The separation route was designed. The operation parameters such as reflux ratio, number of plates, and feed position were obtained with DSTWU and NRTL - RK module. The simulation results could provide the basis for the development on the rectification process.
出处
《精细石油化工进展》
CAS
2010年第6期23-25,共3页
Advances in Fine Petrochemicals
