摘要
测制了正丁醇-邻、间、对二甲苯二元系固液平衡相图。3个体系均属简单低共熔混合物类。计算了它们在298.15K的摩尔过量Gibbs自由能GEm。结果表明,3个体系对理想溶液均产生较大的正偏差。3个体系GEm的最大值分别为985、1023和1258Jmol-1。
Melting temperatures have been measured and the solidliquid phase diagrams were constructed for nbutanol+oxylene,nbutanol+mxylene and nbutanol+pxylene.They are simple eutectic systems.Excess mole Gibbs free energies were calculated at 29815K,showing large positive deviations from idealsolution behavior.The largest values of GEm are 985,1023 and 1258 J·mol-1 for oC6H4(CH3)2+C4H9OH,mC6H4(CH3)2+C4H9OH and pC6H4(CH3)2+C4H9OH,respectively.
出处
《石油学报(石油加工)》
EI
CAS
CSCD
北大核心
1998年第1期73-76,共4页
Acta Petrolei Sinica(Petroleum Processing Section)
基金
国家自然科学基金
关键词
固液平衡
Gibbs自由能
二甲苯
正丁醇
蒸馏
原油
phase diagram,solidliquid equilibrium,excess Gibbs free energy,xylene,1butanol