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

机译:通过混合海水 - 咸罗海水淡化系统更好地脱盐经济学

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Seawater desalination is projected to be the major source of additional potable water in the future. The leading desalination-technology for seawater desalination is reverse osmosis (RO). Although among seawater desalination methods the RO process has the lowest power requirement it is still quite high, in the range of 11 - 15 kwhr/kgallon (3 - 4 kwhr/m3). At the, prevailing operating parameters of commercial seawater RO desalination systems, power requirement 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 the Arabian Gulf area. By comparison, the salinity of brackish concentrate streams that are discharged as waste from brackish RO desalination plants has salinity usually below 2%. The concentrate from brackish RO systems is saturated with sparingly soluble salts, conditions determining the maximum recovery rate. However, if brackish RO concentrate is blended with higher salinity seawater, the solubility of sparingly soluble salts increases due to increase of ionic strength, allowing subsequent RO processing. At locations, where brackish RO and seawater RO plants are located adjacent to each other this phenomena opens possibility of utilizing the brackish water concentrate stream to reduce salinity of seawater feed by blending feed to seawater RO with concentrate from brackish RO system. This approach will result in lower power requirement of seawater RO process, due to lower salinity of feed water and may also simplify discharge of brackish concentrate. The paper will evaluate the-approach to optimizing RO seawater systems design through the utilization of a hybrid brackish - seawater process configuration. Projected process parameters and economic results for a number of selected sites will be presented. The rationale behind the selection of design parameters, economics benefits and the technical challenges associated with the above hybrid configuration will be discussed.
机译:预计海水淡化将成为未来额外饮用水的主要来源。海水淡化的主要脱盐技术是反渗透(RO)。虽然在海水淡化方法中,RO工艺的功率要求最低,但在11-15 kWhr / kgallon(3-4kWhr / m3)的范围内。在商业海水RO脱盐系统的普遍经营参数,功率要求主要是饲料水盐度的作用。海水盐度为大西洋和太平洋的3%-3.5%,地中海的3.8% - 4.2%,阿拉伯海湾地区的4%-4.7%。相比之下,作为咸叶脱盐植物的废物排出的咸浓缩物流的盐度通常低于2%。来自咸罗系统的浓缩物饱和,含有微小溶于盐,条件确定最大回收率。然而,如果咸腐浓浓缩物与高盐度海水混合,则由于离子强度的增加,差异溶于盐的溶解度增加,允许随后的RO加工。在位置,其中,微咸水RO和海水RO工厂位于彼此相邻的该现象打开利用微咸水浓缩流通过混合进料至海水反渗透从微咸水RO系统的浓缩物以减少海水进料的盐度的可能性。由于饲料水的较低盐度,这种方法将导致海水RO工艺的功率要求较低,并且还可以简化淡淡的浓缩物的排放。本文将评估通过利用混合咸水处理配置来提供RO海水系统设计的方法。将提出预计的一些选定网站的过程参数和经济结果。将讨论设计参数,经济效益和与上述混合配置相关的技术挑战背后的理由。

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