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水-正丙醇-正丁醇三元体系汽液平衡实验数据与计算 被引量:1
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作者 张建华 魏顺安 +1 位作者 李诗纯 董立春 《高校化学工程学报》 EI CAS CSCD 北大核心 2010年第5期729-734,共6页
水-正丙醇-正丁醇三元体系常见于乙炔法生产1,4-丁二醇工艺产生的废液中,对该体系汽液平衡数据进行测定是对其进行分离回收的前提,而目前文献中,仅在极窄的温度范围内有很少的相关数据。今测定了99.2kPa时,在正丙醇与正丁醇的配料体积... 水-正丙醇-正丁醇三元体系常见于乙炔法生产1,4-丁二醇工艺产生的废液中,对该体系汽液平衡数据进行测定是对其进行分离回收的前提,而目前文献中,仅在极窄的温度范围内有很少的相关数据。今测定了99.2kPa时,在正丙醇与正丁醇的配料体积比分别为1/4、3/7、2/3、1/1和3/2,水含量直至气相出现液液分层条件下水-正丙醇-正丁醇溶液的三元汽液平衡数据,从而明显扩大了该体系的实验数据及温度适用范围;研究中还用扩展型UNIQUAC方程建立了溶液组分的活度系数模型,关联该体系的汽液平衡数据,通过单纯型法回归获得三元体系组分之间的相互作用能参数。计算结果表明,建立的模型应用相同的相互作用能参数,可以很好的关联本实验测定的数据及文献数据,一方面说明本实验数据与文献数据有很好的一致性,另一方面也表明建立的UNIQUAC模型可以可靠地预测水-正丙醇-正丁醇的汽液平衡数据。 展开更多
关键词 水-正丙醇-正丁醇体系 汽液平衡 UNIQUAC模型 相互作用能参数
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Measurements of the Heat Capacity of an Azeotropic Mixture of Water and n-Butanol from 78 to 320 K
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作者 南照东 谭志诚 邢军 《Chinese Journal of Chemistry》 SCIE CAS CSCD 2005年第10期1297-1302,共6页
Molar heat capacities of n-butanol and the azeotropic mixture in the binary system [water (x=0.716) plus n-butanol (x=0.284)] were measured with an adiabatic calorimeter in a temperature range from 78 to 320 K. Th... Molar heat capacities of n-butanol and the azeotropic mixture in the binary system [water (x=0.716) plus n-butanol (x=0.284)] were measured with an adiabatic calorimeter in a temperature range from 78 to 320 K. The functions of the heat capacity with respect to thermodynamic temperature were estabhshed for the azeotropic mixture. A glass transition was observed at (111.9±1.2) K. The phase transitions took place at (179.26±0.77) and (269.69±0.14) K corresponding to the solid-hquid phase transitions of n-butanol and water, respectively. The phase-transition enthalpy and entropy of water were calculated. A thermodynamic function of excess molar heat capacity with respect to temperature was estabhshed, which took account of physical mixing, destructions of self-association and cross-association for n-butanol and water, respectively. The thermodynamic functions and the excess thermodynamic ones of the binary systems relative to 298.15 K were derived based on the relationships of the thermodynamic functions and the function of the measured heat capacity and the calculated excess heat capacity with respect to temperature. 展开更多
关键词 adiabatic calorimetry heat capacity excess heat capacity azeotropic mixture water n-butanol
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