摘要
MH-81状态方程结合两种不同的混合法则(混合法则Ⅰ和Ⅱ)关联了醇-烃体系的汽-液平衡。结果表明,混合法则Ⅱ比混合法则Ⅰ更优越。而且混合法则Ⅱ关联醇-烃体系汽液平衡的精度与Wilson活度系数模型相当。
The MH-81 equation of state has been used to correlate vapor-liquid equilibria for
1-alcohol-hydrocarbon systems.The results of bubble-point calculations by the EOS
with two different mixing rules (set Ⅰ and set Ⅱ )are compared,and the mixing rule set
Ⅱ yield results equivalent to those from Wilson activity coefficient model.
出处
《石油学报（石油加工）》
EI
CAS
CSCD
北大核心
1993年第2期79-85,共7页
Acta Petrolei Sinica(Petroleum Processing Section)
