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Influence of spacer thickness on permeate flux in spiral-wound seawater reverse osmosis systems

机译:间隔厚度对螺旋缠绕海水逆转渗透系统渗透通量的影响

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A primary reason for flux decline during the initial period of a membrane separation process is concentration polarization of the solute at the membrane surface. The objective of the present study was to analyze and model concentration polarization in spiral-wound seawater membrane elements. In particular, the influence of spacer thickness in the membrane units on permeate flow and its salinity was evaluated. Membrane parameters were also estimated using an analytical osmotic pressure model for high salinity applications. The effects of spacer thickness on permeate flux suggest that the observed flux decreases by up to 50% in going from a spacer thickness of 0.1168 to 0.0508 cm. The different geometry/configuration of the spacer may influence turbulence at the membrane surface that in turn affected concentration polarization. This suggests less turbulence with the smaller spacer thickness. The membrane module with an intermediate spacer thickness of 0.0711 cm was found to be the best economically since it gave the highest water production rate (L/h).
机译:在膜分离过程的初始时段期间的助焊剂下降的主要原因是膜表面上溶质的浓度极化。本研究的目的是分析螺旋伤口海水膜元件中的浓度极化。特别地,评价膜单元中的间隔物厚度对渗透物流的影响及其盐度。还使用用于高盐度应用的分析渗透压模型来估算膜参数。间隔物厚度对渗透剂的影响表明,从间隔厚度为0.1168至0.0508cm至0.0508厘米,观察到的磁通量降低了50%。间隔物的不同几何/配置可以影响膜表面的湍流,又影响受影响的浓度极化。这表明较小的间隔物厚度较小。中间间隔物厚度为0.0711cm的膜组件是最经济上的,因为它给出了最高的水生产率(L / H)。

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