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Structural analysis and modeling of the commercial high performance composite flat sheet membranes for membrane distillation application

机译:用于膜蒸馏的商用高性能复合平板膜的结构分析和建模

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摘要

Direct contact membrane distillation (DCMD) module was operated with three flat sheet commercial membranes (PTFE/PP 1.0, PTFE/PP 0.45, and PTFE/PE 0.45) under various operating conditions. High flux was observed when the PTFE/PP 1.0 membrane was used and there was no membrane wetting when the feed concentration was up to 3.0 M as NaCl. In order to understand the relationship between membrane characteristics and operating conditions, the heat and mass transfer models were employed. Instrumental analyses (SEM, porosimetry and contact angle analysis) were carried out for the membrane characteristics and thermo-hydrodynamic parameters were calculated under given experimental conditions. High flux of PTFE/PP 1.0 membrane was thermody-namically possible because the flow in the feed side was not fully developed in the water channel of the module. The membrane characteristics, such as pore-size of active layer and porosity and thickness of support layer were also attributed to a high flux of PTFE/PP 1.0 membrane.
机译:直接接触膜蒸馏(DCMD)模块在不同的操作条件下与三种平板商用膜(PTFE / PP 1.0,PTFE / PP 0.45和PTFE / PE 0.45)一起运行。当使用PTFE / PP 1.0膜时,观察到高通量;当进料浓度(以NaCl计)达到3.0 M时,没有膜润湿。为了理解膜特性和操作条件之间的关系,采用了传热和传质模型。对膜特性进行了仪器分析(SEM,孔隙率法和接触角分析),并在给定的实验条件下计算了热流体动力学参数。从热力学上讲,PTFE / PP 1.0膜的通量很高,这是因为进料侧的流量在模块的水通道中并未完全展开。诸如活性层的孔径,支撑层的孔隙率和厚度之类的膜特性也归因于PTFE / PP 1.0膜的高通量。

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