[1]王训遒,王卉,闫炳利,等.常压下环己烷-环己酮二元体系汽液平衡研究[J].郑州大学学报(工学版),2012,33(02):48-50,54.[doi:10.3969/j.issn.1671-6833.2012.02.012]
　WANG Xunqiu,WANG Hui,YAN Bingli,et al.Study on the Vapor-Liquid Equilibrium for Cyclohexane-CyclohexanoneBinary System under Normal Atmospheric Pressure[J].Journal of Zhengzhou University (Engineering Science),2012,33(02):48-50,54.[doi:10.3969/j.issn.1671-6833.2012.02.012]
点击复制

常压下环己烷-环己酮二元体系汽液平衡研究()
分享到：

《郑州大学学报(工学版)》[ISSN:1671-6833/CN:41-1339/T]

卷:
33
期数:
2012年02期
页码:
48-50,54
栏目:
出版日期:
2012-03-10

文章信息/Info

Title:
Study on the Vapor-Liquid Equilibrium for Cyclohexane-CyclohexanoneBinary System under Normal Atmospheric Pressure
作者:
王训遒; 王卉; 闫炳利; 等.
郑州大学化工与能源学院,河南郑州,450001, 郑州大学化工与能源学院,河南郑州,450001, 郑州大学化工与能源学院,河南郑州,450001, 郑州大学化工与能源学院,河南郑州,450001
Author(s):
WANG Xunqiu; WANG Hui; YAN Bingli; etc;
School of Chemical and Energy Engineering, Zhengzhou University, Zhengzhou 450001, China
关键词:
汽液平衡;  环己烷;  环己酮;  Wilson方程;  NRTL方程
Keywords:
vapor-liquid equilibrium;  cyclohexane;  cyclohexanone;  Wilson equation;  NR’TL equation
分类号:
TQ231 0642.42
DOI:
10.3969/j.issn.1671-6833.2012.02.012
摘要:
为了计算多元体系的汽液平衡关系,采用改进的Rose汽液平衡釜测定常压(101.3kPa)下环己烷-环己酮二元体系汽液平衡数据,并对数据进行热力学一致性检验,结果表明实验数据符合热力学一致性.以汽相组成的误差平方和作为目标函数,分别用Wilson方程和NRTL方程关联实验数据,得到分子交互作用能量参数,并对汽液平衡计算值与实验值进行比较,发现二者偏差较小,可以满足工程上分离设计的需要.
Abstract:
In order to calculate the vapor-iquid equilibrium ( VLE ) data of the multicomponent system, theVLE data of cyclohexane-cyclohexanone system were determined under normal atmospheric pressure ( 101. 3kPa) by using an improved Rose vapor-liquid equilibrium still, and the thermodynamic consistencies of theobtained data were examined. ’The results show that the experimental data satisfy the examination of the ther.modynamic consistencies. Then the VlE data obtained were correlated with Wilson equation and NRTL equa.tion respectively, and the model parameters of interaction energies between the molecules were determined byusing the error sum squares of vapor phase composition as target function. The comparison of the experimentalVLE data with those calculated with Wilson equation and NRTL equation shows that the deviations are little,which indicates that the models are suitable to be used for the engineering separation design.

相似文献/References:

[1]陈卫航,陈军航,蒋元力,等.真空下1,2-丙二醇-乙二醇二元体系汽液平衡研究[J].郑州大学学报(工学版),2013,34(06):36.[doi:10.3969/j.issn.1671-6833.2013.06.009]
　CHENWeihan9,CHEN Junhan9,JIANGYuani,et al.Investigation into IsobaricVapor-Liquid Equilibrium for the Binary System 1，2-PropyleneGlycol—Ethylene GlycolUnderVacuum[J].Journal of Zhengzhou University (Engineering Science),2013,34(02):36.[doi:10.3969/j.issn.1671-6833.2013.06.009]

更新日期/Last Update: 1900-01-01