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乙烯-甲苯等温汽液平衡数据的测定

Isothermal Vapor-Liquid Equilibrium Data of Ethylene-Toluene Binary System

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【作者】 何伟郑丹星武向红朱彩凤荆树宏

【Author】 He Wei,Zheng Danxing,Wu Xianghong,Zhu Caifeng,Jing Shuhong(Chemical Engineering School,Beijing University of Chemical Technology,Beijing 100029,China)

【机构】 北京化工大学化学工程学院北京化工大学化学工程学院 北京100029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%。

【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.

【基金】 国家自然科学基金项目(90210032;50576001)
  • 【文献出处】 石油化工 ,Petrochemical Technology , 编辑部邮箱 ,2007年04期
  • 【分类号】TQ013.1
  • 【被引频次】4
  • 【下载频次】268
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