首页 | 本学科首页   官方微博 | 高级检索  
     

乙烯-甲苯等温汽液平衡数据的测定
引用本文:何伟,郑丹星,武向红,朱彩凤,荆树宏.乙烯-甲苯等温汽液平衡数据的测定[J].石油化工,2007,36(4):362-365.
作者姓名:何伟  郑丹星  武向红  朱彩凤  荆树宏
作者单位:北京化工大学,化学工程学院,北京,100029
摘    要:自行设计了高压汽液平衡数据的测定装置,实现汽液两相在线气相色谱分析。在压力0.305~2.036MPa、温度303.15,333.15,363.15K的条件下,测定了乙烯-甲苯二组分物系的汽液平衡数据。汽液平衡数据满足热力学一致性检验。由实验数据对乙烯-甲苯二组分物系的汽相采用Peng-Robinson方程、液相采用NRTL方程进行关联,得到NRTL方程的二元交互作用参数。乙烯-甲苯二组分物系的汽液平衡数据的计算值与实验值的平均偏差为3.14%,最大偏差为10.68%。

关 键 词:乙烯-甲苯二组分物系  汽液平衡  状态方程
文章编号:1000-8144(2007)04-0362-04
修稿时间:2006年12月1日

Isothermal Vapor-Liquid Equilibrium Data of Ethylene-Toluene Binary System
He Wei,Zheng Danxing,Wu Xianghong,Zhu Caifeng,Jing Shuhong.Isothermal Vapor-Liquid Equilibrium Data of Ethylene-Toluene Binary System[J].Petrochemical Technology,2007,36(4):362-365.
Authors:He Wei  Zheng Danxing  Wu Xianghong  Zhu Caifeng  Jing Shuhong
Abstract:Isothermal vapor-liquid equilibrium(VLE) data of ethylene-toluene binary system under high-pressure were measured by a self-made apparatus.The vapor and liquid samples could be analyzed online by means of gas chromatography.The VLE data of the binary system were determined under 0.305-2.036 MPa at 303.15,333.15 and 363.15 K.The VLE data can meet demand of thermodynamic consistency test. Correlation of experimental data was carried out by means of Peng-Robinson(PR) equation for gas phase and NRTL equation for liquid phase.The average deviation between experimental data and correlated results is 3.14% and the maximum deviation is 10.68%.The VLE data of ethylene-toluene binary system can be calculated by PR-NRTL equation.
Keywords:ethylene-toluene binary system  vapor-liquid equilibrium  state equation
本文献已被 CNKI 万方数据 等数据库收录!
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号