Calculation of y from T, p and x Data in Vapor-Liquid Equilibrium Using Spline Function Method (Ⅱ) Ternary System
|更新时间:2025-12-16
|
Calculation of y from T, p and x Data in Vapor-Liquid Equilibrium Using Spline Function Method (Ⅱ) Ternary System
CIESC JournalIssue 4, (1991)
作者机构:
华东化工学院热力学研究室,华东化工学院热力学研究室,华东化工学院热力学研究室 ,上海,上海,上海
作者简介:
基金信息:
DOI:
CLC:
Online First:25 August 1991,
Published:25 August 1991
稿件说明:
移动端阅览
刘洪来, 英徐根, 胡英. Calculation of y from T, p and x Data in Vapor-Liquid Equilibrium Using Spline Function Method (Ⅱ) Ternary System[J]. CIESC Journal, 1991, (4).
DOI:
刘洪来, 英徐根, 胡英. Calculation of y from T, p and x Data in Vapor-Liquid Equilibrium Using Spline Function Method (Ⅱ) Ternary System[J]. CIESC Journal, 1991, (4).DOI:
Calculation of y from T, p and x Data in Vapor-Liquid Equilibrium Using Spline Function Method (Ⅱ) Ternary System
By using a spline function for curved surface used in simulating the bending of a plate to describe the ternary excess free enthalpy function Q
a new indirect method for calculating ternary vapor composition y from T
p and liquid composition x was established. Broyden-Nowton-Raphson iteration procedure was used for solving the nonlinear equations. The calculation of 30 ternary systems from nearly ideal to highly nonideal phase behavior showed that this new method was very stable and reliable. The calculated results were in good agreement with the experimental data. More-over
this method had a variety of distinguishing features such as good convergence
no special requirement for initial values and little influence caused by neglecting the excess properties during calculation.