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High Pressure Vapor-Liquid Equilibria for Carbon Dioxide + n-Butanol and Carbon dioxide + i-Butanol

机译:用于二氧化碳+正丁醇和二氧化碳+ I-丁醇的高压蒸汽液平衡

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摘要

A new high pressure apparatus was constructed on which vapor-liquid phase equilibria were measured for carbon dioxide + n-butanol system at temperatures 313.2K, 323.2K and 333.2K, and for carbon dioxide +i-butanol system at 298.2K, 313.2K and 328.2K. The pressures range from about 0.6 MPa up to near the system critical pressure. Experimental data were correlated by use of the PRSV2 equation of state.
机译:构建了一种新的高压装置,在313.2K,323.2K和333.2K的温度下对二氧化碳+正丁醇体系测量蒸汽相位平衡,以及298.2K,313.2K的二氧化碳+ I-丁醇系统。和328.2k。压力范围为约0.6MPa,靠近系统临界压力。通过使用PRSV2状态的实验数据是相关的。

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