首页> 外文会议>Advanced membrane technology VII >DESALINATING SEAWATER AND RECOVERING WASTE WATER USING HYBRID FORWARD AND REVERSE OSMOSIS AT THE PILOT LEVEL
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DESALINATING SEAWATER AND RECOVERING WASTE WATER USING HYBRID FORWARD AND REVERSE OSMOSIS AT THE PILOT LEVEL

机译:在试点处使用混合正向和反向渗透力对海水进行脱盐并回收废水

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With the advantage of having low fouling propensity and requiring low hydraulic pressure to operate, forward osmosis (FO) has captured attention as an alternative technology which is capable of treating and desalinating highly fouling and saline water sources respectably. Established technologies such as reverse osmosis (RO) is capable of performing the aforementioned tasks at high efficiency. However, RO often requires extensive pretreatment to reduce membrane fouling which increases cost. In this work, a pilot scale FO-RO system was built using commercially available membrane modules. A combined hybrid FO-RO system where FO acts as a pre-treatment system to downstream RO system and RO acts as a recovery step for FO draw solution offers a multitude of benefits. Reduction in fouling, and fast and low cost cleanability is achievable. In addition, having similar membrane selectivity, both FO and RO provides a dual barrier protection to trace contaminants such as boron, low molecular weight organics, and metals. The pilot system includes a PLC-HMI based data acquisition system with process control and monitoring capability of flowrates, pressures, temperatures, and electricity usage. Initially, using Dl water as a benchmark for evaluating the fundamental operating parameters that are critical to FORO, the system was optimized. Using a Dow SW30-4040 spiral wound module and Porifera FOMEM plate and frame module, the system was operated at 40%-45% recovery. During this recovery, the feed concentration in the RO changed from 4000 TDS to 12000 TDS with a rejection of 93%-97% at a pH of 6.5. For a 0.25M NaCI draw solution in FO, a 10-12 Lm~(-2)hr~(-1) water flux was observed with a reverse salt flux of 11-13 gm-~2hr~1. The total peak current used was found to be 4.0-4.5 amps at a maximum feed and draw flowrate of 1.25 GPM. We anticipate an automated process control through mass transport between the FO and RO module in closed loop. Our future work include investigation of different types of feed sources to observe and record the operating parameters as well as to investigate the double barrier concept and the automated process control feature of the FO-RO hybrid system.
机译:由于具有低结垢倾向和需要低液压压力的优点,正渗透(FO)作为一种替代技术引起了人们的关注,该技术能够适当地处理和脱盐高度结垢的盐水。诸如反渗透(RO)之类的既定技术能够高效执行上述任务。然而,RO通常需要大量的预处理以减少膜结垢,这增加了成本。在这项工作中,使用市售的膜组件构建了中试规模的FO-RO系统。组合式FO-RO混合系统(其中FO充当下游RO系统的预处理系统,而RO充当FO抽取解决方案的恢复步骤)提供了很多好处。可以减少结垢,并实现快速,低成本的清洁性。此外,FO和RO具有相似的膜选择性,可提供双重屏障保护,以痕量污染物,例如硼,低分子量有机物和金属。该试验系统包括一个基于PLC-HMI的数据采集系统,该系统具有流量,压力,温度和用电量的过程控制和监视功能。最初,以去离子水作为评估对FORO至关重要的基本操作参数的基准,对该系统进行了优化。使用陶氏SW30-4040螺旋缠绕模块和Porifera FOMEM板框模块,系统的回收率为40%-45%。在此回收过程中,RO的进料浓度从4000 TDS变为12000 TDS,在pH值为6.5时的排斥率为93%-97%。对于FO中的0.25M NaCl汲取溶液,观察到10-12 Lm〜(-2)hr〜(-1)的水通量,反盐通量为11-13 gm ~~ 2hr〜1。发现在最大进料和1.25 GPM的牵引流量下,使用的总峰值电流为4.0-4.5安培。我们期望通过闭环FO和RO模块之间的大量运输实现自动过程控制。我们未来的工作包括研究不同类型的进料源,以观察和记录操作参数,以及研究FO-RO混合系统的双重屏障概念和自动化过程控制功能。

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