首页> 外文期刊>Fluid Phase Equilibria >Vapor-liquid equilibrium for model Fischer-Tropsch waxes (hexadecane, 1-hexadecene, and 1-hexadecanol) in supercritical hexane
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Vapor-liquid equilibrium for model Fischer-Tropsch waxes (hexadecane, 1-hexadecene, and 1-hexadecanol) in supercritical hexane

机译:费-托模型蜡(十六烷,1-十六烯和1-十六醇)在超临界己烷中的汽液平衡

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摘要

Vapor and liquid equilibrium compositions have been measured for the hexane + 1-hexadecene system at 472.1, 524.7, and 572.5 K and at pressures ranging from 7.9 to 40.1 bar. A continuous-flow apparatus was used both to minimize 1-hexadecene polymerization and to measure the low 1-hexadecene concentrations in the vapor phase. Mixture critical pressures and compositions were measured for the two temperatures above the critical point of hexane. Results with 1-hexadecene are compared with those recently obtained for binary mixtures of hexane with hexadecane and 1-hexadecanol, respectively. The data for these three binary systems have been correlated with the Peng-Robinson equation of state.
机译:已在472.1、524.7和572.5 K以及7.9至40.1 bar的压力下测量了己烷+ 1-十六碳烯体系的蒸汽和液体平衡组成。使用连续流动装置以最小化1-十六碳烯聚合并测量气相中低的1-十六碳烯浓度。在高于己烷的临界点的两个温度下测量混合物的临界压力和组成。将1-十六碳烯的结果与最近分别获得的己烷,十六烷和1-十六醇的二元混合物的结果进行了比较。这三个二进制系统的数据已与状态的Peng-Robinson方程相关联。

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