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BETTER ECONOMICS OF DESALINATION THROUGH HYBRID SEAWATER – BRACKISH RO DESALINATION SYSTEMS

机译:通过混合海水进行海水淡化的更好的经济方法-咸淡的RO海水淡化系统

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Seawater desalination is projected to be the major source of additional potable water in thefuture. The leading desalination technology for seawater desalination is reverse osmosis (RO).Although among seawater desalination methods the RO process has the lowest powerrequirement it is still quite high, in the range of 11 – 15 kwhr/kgallon (3 – 4 kwhr/m3). At theprevailing operating parameters of commercial seawater RO desalination systems, powerrequirement is mainly function of feed water salinity. The seawater salinity ranges from 3% -3.5% for Atlantic and Pacific Oceans, 3.8% - 4.2% for Mediterranean and 4% - 4.7% for theArabian Gulf area. By comparison, the salinity of brackish concentrate streams that aredischarged as waste from brackish RO desalination plants has salinity usually below 2%. Theconcentrate from brackish RO systems is saturated with sparingly soluble salts, conditionsdetermining the maximum recovery rate. However, if brackish RO concentrate is blended withhigher salinity seawater, the solubility of sparingly soluble salts increases due to increase of ionicstrength, allowing subsequent RO processing. At locations, where brackish RO and seawater ROplants are located adjacent to each other this phenomena opens possibility of utilizing thebrackish water concentrate stream to reduce salinity of seawater feed by blending feed toseawater RO with concentrate from brackish RO system. This approach will result in lowerpower requirement of seawater RO process, due to lower salinity of feed water and may alsosimplify discharge of brackish concentrate.The paper will evaluate the approach to optimizing RO seawater systems design through theutilization of a hybrid brackish – seawater process configuration. Projected process parametersand economic results for a number of selected sites will be presented. The rationale behind theselection of design parameters, economics benefits and the technical challenges associated withthe above hybrid configuration will be discussed.
机译:海水淡化预计将成为该地区额外饮用水的主要来源。 未来。海水淡化的主要淡化技术是反渗透(RO)。 尽管在海水淡化方法中,RO工艺的能耗最低 要求仍然很高,范围为11 – 15千瓦时/公斤(3 – 4千瓦时/立方米)。在 商业海水反渗透淡化系统的主要运行参数,功率 需求量主要是给水盐度的函数。海水盐度范围为3%- 大西洋和太平洋为3.5%,地中海为3.8%-4.2%,大西洋为4%-4.7% 阿拉伯海湾地区。相比之下,咸淡精矿流的盐度为 从微咸的反渗透淡化厂中作为废物排放的盐度通常低于2%。这 来自微咸型反渗透系统的精矿被微溶盐饱和,条件 确定最大恢复率。但是,如果将微咸的反渗透浓缩液与 较高盐度的海水,由于离子的增加,难溶盐的溶解度增加 强度,可以进行后续的RO处理。在含RO和海水微咸的地方 植物位于彼此相邻,这种现象打开了利用 通过将盐水混合到 海水反渗透,含苦咸反渗透系统的浓缩液。这种方法将导致降低 海水反渗透过程的功率需求,因为给水的盐度较低,并且可能 简化微咸精矿的排放。 本文将通过以下方法评估优化反渗透海水系统设计的方法: 混合淡咸水的利用-海水工艺配置。预计的工艺参数 以及一些选定站点的经济结果。背后的理由 选择设计参数,经济效益以及与之相关的技术挑战 将讨论以上混合配置。

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