摘要
把汽液平衡的真实状态看成是3个虚拟状态的组合,结合Gibbs-Dubem方程,推得了等温低压汽液平衡时p-y-x之间的一个近似关系式,并把它推广应用到加压及含超临界组分体系的汽液平衡计算.
The real state of vapor liquid equilibria is considered as a combination of three fictitious states. From the relation between the real state and three fictitious states, the approximatep, y, x relationship can be obtained from these fictitious states with the help of the Gibbs-Duhem equation. This method was used to calculate isothermal high (low) pressure vapor liquid equilibria with satisfactory results, while no equations of state or equations of activity coefficients were needed.
出处
《化工学报》
EI
CAS
CSCD
北大核心
1992年第3期345-352,共8页
CIESC Journal
关键词
汽液平衡
状态方程
超临界
vapor liquid equilibria, equation of state, supercritical