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Study on Vapor-Liquid Equilibria with Successive Approximation

Cai Zhiliang, Zhu Yifeng, Chen Shizhong, Yao Yunbin (Department of Chemical Engineering, Zhejiang Institute of Technology, Hanghou) Huang Qi (Tianjin Synthetic Material Industry Research Institute, Tianjin)   

  • Online:1989-06-25 Published:1989-06-25

逼近法研究汽液平衡

蔡志亮,祝一峰,陈时忠,姚允斌,黄棨   

  1. 浙江工学院化工系,浙江工学院化工系,浙江工学院化工系,浙江工学院化工系,天津合成材料工业研究所 杭州 ,杭州 ,杭州 ,杭州 ,天津

Abstract: A new approach to determining bubble point or dew point of a binary mixture has been proposed. From an equilibrium still operating steadily at a constant pressure, a portion of the equilibrium binary solution (its composition x1(0) to be evaluated) is replaced by an equal amount of solution having a known composition x1(1). If the equilibrium temperature before and after the replacement remains unchanged, i. e. T(0) - T(1)=0, then x(0)=x1(1) and the bubble point[T(1), x1(1)] is thus obtained. On the contrary, an inequality of T(0) and T(1) indicates x1(0)≠x1(1). In the latter case, pure component 1 or 2 is added in successive small increments to adjust the temperature in the still to the neighborhood of T(0), and then the replacement is repeated by a new solution of composition x1(2). The foregoing procedure is repeated until | T(n-1)-T(n)| or | x1(n-1)-x1(n)| comes up to the desired precision and the final point[T(n), x1(n)] is the bubble point of the system. In a similar way, the dew point could be obtained by replacement of the equilibuium vapor in the still.

摘要: 用已知组成为x_1~(1)的溶液对恒压下稳定运行的平衡釜中的平衡液相(其组成x_1~(0)为待求量)作等质量代换.若代换前后的相平衡温度差T~(0)-T~(1)=0,则x_1~(0)=x_1~(1),即得一泡点(T~(1),x_1~(1));否则,x_1~(0)≠x_1~(1),此时向釜中加入组分1或组分2使温度回到T~(0)附近,改用已知组成为x_1~(2)的溶液作代换.如此反复,直至|T~(n-1)-T~(n)|或|x_1~(n-1)-x_1~(n)|达到所需精度,最后的点(T~(n),x_1~(n))即为泡点.对平衡汽相作同样代换可得到露点值.