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    周飞, 骆赞椿, 朱炳辰. 加压三相床环氧乙烷合成过程研究Ⅳ.环氧乙烷在一号液相热载体中的溶解性能[J]. 华东理工大学学报(自然科学版), 2000, (1).
    引用本文: 周飞, 骆赞椿, 朱炳辰. 加压三相床环氧乙烷合成过程研究Ⅳ.环氧乙烷在一号液相热载体中的溶解性能[J]. 华东理工大学学报(自然科学版), 2000, (1).

    加压三相床环氧乙烷合成过程研究Ⅳ.环氧乙烷在一号液相热载体中的溶解性能

    • 摘要: 使用搅拌反应釜,利用气液两相平衡技术,在333~503K,0.09~0.4MPa 的实验条件下,测定了环氧乙烷在所筛选的一号高沸点液相热载体中的平衡溶解度。运用Peng-Robinson 状态方程计算了溶剂和环氧乙烷的活度系数,并且回归出了溶解度系数与温度的关联方程。实验结果表明,环氧乙烷在该液体介质中的平衡溶解度均随着压力的升高而增加,随温度的升高而降低。

       

      Abstract: The equilibrium solubility for ethylene oxide in a high boiling point solvent was studied at 333~503K and 0.02~0.35MPa by determination of temperature T and total pressure P at equilibrium condition, and the equilibrium data for system were obtained by means of material balance and Peng Robinson equation of state. Through regressing the experimental data, the correlation equation of solubility of ethylene oxide and temperature was established. The relationship between equilibrium compositions to partial pressure of ethylene oxide and temperature were discussed respectively.The experimental results provide the basis for the determination of operating conditions of ethylene oxide synthesis in three phase bed.

       

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