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Processing of surface and ground water by hydrostatic pressure-driven membrane techniques: design and economic aspects

机译:通过静水压力驱动膜技术处理地表水和地下水:设计和经济方面

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In recent years, membrane-based ultrafiltration (UF) and reverse osmosis (RO) have become popular worldwide as possible alternative methods to conventional ion exchange and clarification processes for the production of potable water. The performance of UF and RO membranes was evaluated for treatment of surface and ground water from Prakasam District of Andhra Pradesh, India; namely, jagarlamudi well water (JWW), jagarlamudi pond water (JPW), veerannapalem old pond water (VOPW), and veerannapalem new pond water (VNPW). Pilot-scale UF and RO systems were built indigenously by incorporating commercial hollow fiber polyacrylonitrile UF and thin film composite polyamide RO modules, respectively. Operating parameters such as feed concentration, pressure, and cross-flow velocity were varied to study their effect on membrane performance. Effect of fouling on flux and rejection characteristics of the membrane was evaluated. RO membrane exhibited a rejection of 96.4% for JWW and VOPW feeds with reasonable flux of 42.5 and 48 L m~(-2) h~(-1), respectively, whereas, UF experiments with JPW and VNPW feeds revealed corresponding turbidity rejections of 95.6 and 98.2%. A mathematical model was developed for commercial RO system to simulate the process for establishing optimum operating conditions. A comparison of UF and RO processes for this application is presented along with useful details of equipment list, process flow diagram of commercial membrane plant, schematic of compact hollow fiber pilot plant, and detailed estimation of operating costs.
机译:近年来,基于膜的超滤(UF)和反渗透(RO)已作为一种可能的替代常规离子交换和净化过程的饮用水方法,在世界范围内广为流行。评价了来自印度安得拉邦Prakasam区的地表水和地下水的超滤膜和反渗透膜的性能。分别是jagarlamudi井水(JWW),jagarlamudi池水(JPW),veerannapalem旧池水(VOPW)和veerannapalem新池水(VNPW)。中试规模的超滤和反渗透系统是通过将商业中空纤维聚丙烯腈超滤和薄膜复合聚酰胺反渗透模块分别引入本机构建的。改变诸如进料浓度,压力和错流速度的操作参数以研究它们对膜性能的影响。评估了结垢对膜通量和截留特性的影响。 RO膜对JWW和VOPW进料表现出96.4%的截留率,合理通量分别为42.5和48 L m〜(-2)h〜(-1),而JPW和VNPW进料的超滤实验显示出相应的浊度截留率。 95.6和98.2%。为商业反渗透系统开发了数学模型,以模拟建立最佳运行条件的过程。介绍了该应用中超滤和反渗透工艺的比较,以及设备清单,商用膜设备的工艺流程图,紧凑型中空纤维中试设备的示意图以及运营成本的详细估算等有用的细节。

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