碳三催化精馏加氢模拟计算  

Modeling computation of C3 catalytic distillation hydrogenation

作　　者：赵秀红[1] 季江宁[1] 刘昆元[1] 

机构地区：[1]北京化工大学化学工程学院,北京100029

出　　处：《化学工程》2004年第1期56-59,74,共5页Chemical Engineering(China)

摘　　要：在对碳三系统进行动力学研究的基础上,完成了碳三催化精馏塔模型的建立,并应用三对角矩阵法对其求解。对燕山石化乙烯二次扩产高压脱丙烷催化精馏塔进行MAPD(丙炔、丙二烯)催化精馏加氢计算,将计算结果与Lummus公司的设计数据进行比较,吻合良好。On the basis of the kinetic research of C3, the model of C3 catalytic distillation hydrogenation tower was set up, which was resolved by the method of triple diagonal matrix, and the modeling computation was carried out on the basis of the design data of high pressure depropanizer in Yanshan Petrochemical Factory which was given by Lummus company.The result of modeling agrees well with the design data.

关 键 词：碳三 催化精馏 加氢 模拟计算 三对角矩阵法 

分 类 号：TQ05[化学工程]