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Exploring the Operation Factors that Influence Performance of a Spiral-Wound Forward Osmosis Membrane Process for Scale-up Design

机译:探索影响螺旋伤口正渗透膜工艺规模化设计性能的因素

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Forward osmosis (FO) technology has increasingly attracted attention owing to its low operational energy and low fouling propensity. Despite extensive investigations on FO, very few module-scale FO studies on the operation and design of the FO process have been conducted. In this paper, a simple and practical FO process design parameter called normalized membrane area is suggested based on a performance analysis of spiral-wound FO elements. The influence of operation factors on operating pressures and water recovery was investigated using 8-inch spiral wound elements in the continuous operation mode. The membrane area was adjusted by series connection of FO elements to a maximum value of 46 m (three elements). The feed and draw flow rates were varied between 5 and 15 LPM under various feed (10, 20, and 30 g/L) and draw (58.4 and 233.8 g/L) concentration combinations. The analysis of flow rates (feed, draw, and permeate flow rates) indicated not only high flow channel resistance on the draw side but also high permeate flow rates can induce higher operating pressures owing to strong mutual interaction of the feed and the draw streams. Feed water recovery was focused on as a key performance index, and the experimental recovery ( ) and theoretical maximum recovery ( ) values were compared. The results revealed the significance of the feed flow rate and the membrane area in terms of enhancing the water recovery performance. In addition, a clear relationship was observed between the membrane area normalized by the initial feed flow rates and the water recovery ratio ( / ), even though the applied operation conditions were different. Finally, an empirical equation to estimate the required membrane area of spiral-wound FO was proposed for the FO process design. The equation can be used to predict water recovery of FO systems as well, for example, if an FO system is operated at 0.08 m L h of the normalized membrane area, the system is expected to offer 78% of the value.
机译:正向渗透(FO)技术由于其较低的运行能量和较低的结垢倾向而越来越受到关注。尽管对FO进行了大量研究,但很少进行关于FO工艺的操作和设计的模块级FO研究。在本文中,基于螺旋缠绕式FO元件的性能分析,提出了一种简单实用的FO工艺设计参数,称为标准化膜面积。在连续操作模式下,使用8英寸螺旋缠绕元件研究了操作因素对操作压力和水回收率的影响。通过将FO元件串联连接将膜面积调整为最大值46 m(三个元件)。在各种进料(10、20和30 g / L)和抽取(58.4和233.8 g / L)浓度组合下,进料和抽取流速在5至15 LPM之间变化。对流量(进料,汲取和渗透流量)的分析表明,由于进料和汲取流之间的强烈相互作用,不仅汲取侧的流道阻力高,而且高渗透率也会引起较高的工作压力。以给水回收率作为关键性能指标,并比较了实验回收率()和理论最大回收率()。结果揭示了进料流速和膜面积对于提高水回收性能的重要性。另外,即使所应用的操作条件不同,在通过初始进料流速归一化的膜面积与水回收率(/)之间也观察到清晰的关系。最后,提出了一个经验方程式,用于估计螺旋缠绕的FO所需的膜面积,用于FO工艺设计。该公式还可用于预测FO系统的水回收率,例如,如果FO系统在归一化膜面积的0.08 m L h下运行,则该系统有望提供该值的78%。

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