水-正已烷-乙醇体系的液液平衡研究

近年来,超临界合成进展迅速。钟炳等人在超临界状态下利用正己烷、环已烷等液体介质,将一氧化碳合成甲醇1],效率已达90%以上。作为基础工作,刘建国等人研究了水-正己烷-甲醇体系的液液平衡2];冯耀声等人研究了水-丙烷-乙醇体系的相平衡3];Letcher等人研究了水-正庚烷-醇体系

Research on the liguid-liquid equilibrium in system water-n-hexane-ethanol

Four isothermal sections at 298.15K,308.15K,318.15K and 328.15K in system water-n-hexane-ethanol were measured by gas chromatograph method.The innerscaling method was used to determine the concentrations of n-hexane and ethanol in this ternary system.Ethy1 acetate was chosen as the sample of inner-scaling because of its separability and fit retainning time.Acetylacetone was chosen as diluent of the oil phase andn-butyl alcohol was chosen as diluent of the water phase.The experimental data of four isothermal sections at 298.15K,308.15K,318.15K adn 328.15K in system water-n-hexane-ethanol at normal pressure were given.Four schematic figures were also given.The character of these phase diagrams was analysed.They were compared with the phase diagram of system water-n-hexane-methanol.The possible causes of experimental error were discussed.The root mean square error of measurement is 1.47%.