Energy recovery by pressure retarded osmosis (PRO) in SWRO-PRO integrated processes

被引:95
|
作者
Wan, Chun Feng [1 ]
Chung, Tai-Shung [1 ,2 ]
机构
[1] Natl Univ Singapore, Dept Chem & Biomol Engn, Singapore 117585, Singapore
[2] King Abdullah Univ Sci & Technol, WDR Ctr, Thuwal 239556900, Saudi Arabia
基金
新加坡国家研究基金会;
关键词
Reverse osmosis; Pressure retarded osmosis; Osmotic energy; Energy recovery; Process integration; SUSTAINABLE POWER-GENERATION; HOLLOW-FIBER MEMBRANES; REVERSE-OSMOSIS; SEAWATER DESALINATION; CONCENTRATED BRINES; SALINITY GRADIENT; HYBRID PROCESS; RO-PRO; WATER; TECHNOLOGIES;
D O I
10.1016/j.apenergy.2015.10.067
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Pressure retarded osmosis (PRO) is a promising technology to reduce the specific energy consumption of a seawater reverse osmosis (SWRO) plant. In this study, it is projected that 25.6-40.7 million kW h/day of energy can be recovered globally, if the brines from SWRO are used as the draw solution and diluted to the seawater level in a PRO system. Detailed integrated SWRO-PRO processes are developed in this study with the option to form a closed-loop SWRO-PRO process that can substantially reduce the pretreatment cost of desalination. The governing mathematical models that describe both the transport phenomena on a module level and the energy flow on a system level are developed to evaluate the performances of the SWRO-PRO processes. The model aims to investigate the performance of the hollow fibers as dilution occurs and provides guidelines on hollow fiber module design and process operation. Determining the dilution factor and the corresponding operating pressure of PRO is the key to optimize the integrated process. The specific energy consumptions of three SWRO-involved processes; namely, (1) SWRO without a pressure exchanger, (2) SWRO with a pressure exchanger, and (3) SWRO with pressure exchangers and PRO are compared. The results show that the specific energy consumptions for the above three processes are 5.51, 1.79 and 1.08 kW h/(m(3) of desalinated water) for a 25% recovery SWRO plant; and 4.13, 2.27 and 1.14 kW h/(m(3) of desalinated water) for a 50% recovery SWRO plant, using either freshwater or wastewater as the feed solution in PRO. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:687 / 698
页数:12
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