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水-三甘醇-一氯甲烷三元体系气液相平衡的测定
引用本文:徐新,罗国华,杨春育.水-三甘醇-一氯甲烷三元体系气液相平衡的测定[J].石油化工,2004,33(5):447-450.
作者姓名:徐新  罗国华  杨春育
作者单位:北京石油化工学院,化工系,北京,102617
摘    要:采用加压的气液相平衡釜,在0.4 MPa(绝压)、20-40℃的条件下测定含微量水的三甘醇-一氯甲烷体系的气液相平衡数据,用逸度最小方差的方法回归实验数据,以Peng-Robinson状态方程计算组分的逸度,并用单纯形优化法得到方程中的二元相互作用参数。预测了含微量水的一氯甲烷气体在三甘醇中的溶解度,将计算结果与实测值进行比较,平均相对偏差为4.96%。

关 键 词:气液相平衡  三甘醇  一氯甲烷  溶解度
文章编号:1000-8144(2004)05-0447-04
修稿时间:2003年10月8日

Determination of Gas-Liquid Equilibrium Data of Water-Triethylene Glycol-Methyl Chloride Ternary System
Xu Xin,Luo Guohua,Yang Chunyu.Determination of Gas-Liquid Equilibrium Data of Water-Triethylene Glycol-Methyl Chloride Ternary System[J].Petrochemical Technology,2004,33(5):447-450.
Authors:Xu Xin  Luo Guohua  Yang Chunyu
Abstract:Gas-liquid equilibrium data for water - triethylene glycol - methyl chloride ternary system were measured in an equilibrium cell at 0.4 MPa and 20-40 ℃. Resulted experimental data were regressed by fugacity least square method. The fugacity of the components were calculated by Peng - Robinson equation. Binary parameters were obtained by using simplex optimization method. The calculated and experimental solubility of CH3C1 with trace water in triethylene glycol were compared. Average relative deviation was 4.96%
Keywords:gas-liquid equilibrium  triethylene glycol  methyl chloride  solubility
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