The effect Cooling Water Temperature in Air Gap Membrane Distillation for Breaking of Butyric acid – Water Azeotrope

Rajeshwar Kholapure, Kailash Singh, S. Upadhyaya
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Abstract

– Air gap membrane distillation is a thermal membrane separation method. In this method, the vapour phase is let through a hydrophobic membrane. The vapour pressure difference is created due to the temperature gradient across the hydrophobic microporous membrane, which is the driving force. I have investigated experimentally the feasibility of Air Gap Membrane Distillation module with PTFE hydrophobic membrane for the breaking of butyric acid-water azeotrope. Because of differences in diffusivity rates in the air, separation is possible. The influence of bulk feed temperature on the diffusivity of water and butyric acid, as well as the vapour pressure of butyric acid and water, was examined in this paper. Also, the effect of cooling water temperature (5-20 0 C) on total permeate flux, selectivity of butyric acid, and the concentration of butyric acid in permeate and retentate for various air gap (3-11mm) were experimentally studied. All other parameters were held constant during the experiment, including the Bulk Feed Temperature of 80 o C, Feed Flow Rate of 2 L/min, and Cooling Water Flow Rate of 2 L/min.
气隙膜蒸馏中冷却水温度对丁酸-水共沸物裂解的影响
—气隙膜蒸馏是一种热膜分离方法。在这种方法中,气相通过疏水膜。蒸汽压差是由于疏水微孔膜上的温度梯度而产生的,这是驱动力。实验研究了用PTFE疏水膜气隙膜蒸馏模块裂解丁酸-水共沸物的可行性。由于空气中扩散率的不同,分离是可能的。本文研究了物料温度对水和丁酸扩散系数以及丁酸和水的蒸气压的影响。实验研究了不同气隙(3 ~ 11mm)下,冷却水温度(5 ~ 20℃)对渗透液总通量、丁酸选择性以及渗透液和保留液中丁酸浓度的影响。实验过程中其他参数均保持恒定,其中物料温度为80℃,进料流量为2 L/min,冷却水流量为2 L/min。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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