VAPOR-LIQUID-EQUILIBRIA OF THE SYSTEM ETHANE + 2-AMINOPROPANE

被引：4
|
作者：
DELOOS, TW
TIJSSELING, HR
ARONS, JD
机构：
[1] Delft Univ of Technology, Delft, Neth, Delft Univ of Technology, Delft, Neth
来源：
JOURNAL OF CHEMICAL AND ENGINEERING DATA | 1987年 / 32卷 / 03期
关键词：
HYDROCARBONS - Phase Equilibria - SODIUM CHLORIDE - Production;
D O I：
10.1021/je00049a027
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
Bubble and dew point pressures have been measured as a function of temperature for 19 mixtures of the binary system ethane plus 2-aminopropane in the temperature range 278. 15-368. 15 K. It is shown that the data can be represented by using the Peng-Robinson equation of state. The Peng-Robinson equation of state (1) has proved to be well suited for the description and prediction of high-pressure vapor-liquid equilibria in hydrocarbon systems. Here the equation is applied for the representation of vapor-liquid equilibria in a system consisting of a hydrocarbon and a powder hydrogen-bonding compound.
引用
收藏
页码：374 / 377
页数：4
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