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Continuous vapor-gas separation with a porous membrane permeation system.

机译:使用多孔膜渗透系统进行连续的蒸气-气体分离。

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In contrast to adsorption processes in which the adsorbent must be regenerated periodically, a thin porous membrane can be used to separate gaseous mixtures in an efficient and continuous manner. It is believed that adsorbed flow and capillary condensation within a porous membrane can greatly increase the vapor permeability and membrane selectivity for a vapor-gas separation.; A Continuous Porous Membrane Permeator (CPMP) was constructed that allowed the condensible vapor in the feed stream to permeate preferentially through the membrane under the driving force of a pressure difference across the membrane. A porous Vycor glass membrane was used to recover acetone and ethanol vapors from nitrogen mixtures. The separation performance, in terms of the apparent solvent permeability, separation factor, and solvent recovery, were evaluated systematically in a parametric study. Operating conditions and system parameters examined in this study were the temperature of the membrane system, total feed pressure, downstream flow rate, flow pattern, and membrane geometry.; A six-mode flow model was applied to correlate the condensible solvent permeability as a function of vapor pressures on both sides of the membrane column. A mathematical model has been developed to describe and predict the CPMP performance under various design and operating conditions. The validity of the model simulation was verified by comparing the model prediction with the experimental results.; Demonstrated by both experimental and theoretical investigations, a large solvent permeability and a high separation factor were obtained simultaneously when the feed solvent vapor pressure approached the capillary condensation vapor pressure. A semipermeable membrane system is also realized when the entire length of the membrane column is saturated with the solvent condensate. The results indicate that the CPMP is a potentially high performance membrane system for industrial application of solvent recovery from waste air emission and Volatile Organic Compounds (VOC) pollution controls.
机译:与必须定期再生吸附剂的吸附过程相反,可以使用薄多孔膜以有效和连续的方式分离气态混合物。据信多孔膜内的吸附流和毛细管冷凝可大大增加蒸气渗透性和膜选择性以进行蒸气-气体分离。构造了连续多孔膜渗透器(CPMP),其允许进料流中的可冷凝蒸气在跨膜的压力差的驱动力下优先渗透通过膜。使用多孔Vycor玻璃膜从氮气混合物中回收丙酮和乙醇蒸气。在参数研究中,系统评估了表观溶剂渗透率,分离因子和溶剂回收率方面的分离性能。在这项研究中检查的操作条件和系统参数是膜系统的温度,总进料压力,下游流速,流型和膜的几何形状。应用六模式流动模型将可冷凝溶剂的渗透性与膜塔两侧的蒸气压相关联。已经开发出数学模型来描述和预测各种设计和操作条件下的CPMP性能。通过将模型预测与实验结果进行比较,验证了模型仿真的有效性。通过实验和理论研究表明,当进料溶剂蒸气压接近毛细管冷凝蒸气压时,同时获得了较大的溶剂渗透性和较高的分离系数。当膜柱的整个长度被溶剂冷凝液饱和时,也可以实现半渗透膜系统。结果表明,对于从废气排放和挥发性​​有机化合物(VOC)污染控制中回收溶剂的工业应用而言,CPMP是一种潜在的高性能膜系统。

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