AN ANALYSIS OF THE INDUSTRIAL USE OF A PHASE-EQUILIBRIA PREDICTION MODEL BASED ON THERMODYNAMIC PERTURBATION-THEORY

被引：15

作者：

MOSER, B

KISTENMACHER, H

机构：

[1] LINDE AG, Hoellriegelskreuth, West Ger, LINDE AG, Hoellriegelskreuth, West Ger

来源：

FLUID PHASE EQUILIBRIA | 1987年 / 34卷 / 2-3期

关键词：

EQUATIONS OF STATE;

D O I：

10.1016/0378-3812(87)80031-6

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

An extended Gubbins-Gray perturbation theory is analysed and compared with the results from a common equation of state. Industrially important phase equilibria are studied for systems relevant to natural gas and 'syngas' processing. Systematic test systems are developed. At present the success of the theory is limited and unsystematic, indicating that its predictive power is very small.

引用

页码：189 / 201

页数：13

共 12 条

[1]

[Anonymous], MONATSH CHEM

[2] VAPOR-LIQUID EQUILIBRIUM OF CH4-AR, CH4-CO, AND AR-CO SYSTEMS AT ELEVATED PRESSURES [J].