摘要
采用改进的Ｒｏｓｅ－Ｗｉｌｌｉａｍｓ釜测定了等压下正戊烷一叔丁醇（１．０１３×１０５、７９９７４Ｐａ）和叔丁醇-正辛烷（１．０１１０５Ｐａ）体系的汽液平衡数据。实验数据通过了热力学一致性检验，采用Ｐ－Ｔ状态方程和Ｗｉｌｓｏｎ方程关联，获得较满意的结果。
The isobaric vapor-liquid equilibrium data of n-pentane(1)-tert-butyl alcohol(2)(1.0l3 x 105Pa,79974Pa), tert-butyl alcohol(1)-n-octane(2)(1.0l3x 105Pa) were measured by usingmodified Rose-Williams still.The experimental data were tested for thermodynamic consistency andcorrelated satisfactorily with P-T equation of state and Wilson equation.
出处
《高校化学工程学报》
EI
CAS
CSCD
北大核心
1999年第3期259-263,共5页
Journal of Chemical Engineering of Chinese Universities
关键词
正戊烷
正辛烷
叔丁醇
汽液平衡
汽油
调合剂
N-pentane,n-octane, Tert-butyl alcohol, Vapor-liquid equilibrium, Thermodynamicconsistency, P-Tequation, Wilson equation
