基于Aspen Plus对副产氯化氢精馏模拟与分析  

Simulation And Analysis of By-Product Hydrogen Chloride Distillation Based on Aspen Plus

作　　者：董涛[1] 姜涛[1] 范正林[1] 任少科[1] 娄玥辉[1] 李丽[1] 岳文岩 

机构地区：[1]中昊光明化工研究设计院有限公司,辽宁大连116031

出　　处：《低温与特气》2014年第1期18-21,共4页Low Temperature and Specialty Gases

摘　　要：通过Aspen Plus灵敏度分析工具对氯化氢精馏塔的塔板数、进料位置及回流比对产品纯度及热负荷的影响进行了分析和优化,最后通过使用设计规定工具使优化后的精馏塔满足氯化氢的分离要求,并得到了塔内温度以及气液相组成的变化规律。By using Aspen Plus sensitivity analysis tool, the impact of stage numbers, feeding position and reflux ratio on product purity and heat duty of column was analyzed and optimized. Finally, by using design specifications tool, hydrogen chloride separation requirements of the optimized column was meet and the variation law of the temperature and the compo- sition of gas and liquid phase in column were also obtained.

关 键 词：ASPEN PLUS 副产 氯化氢 精馏 模拟 

分 类 号：TQ124.42[化学工程—无机化工]