Alsarayreh Alanood A, Al-Obaidi Mudhar A, Ruiz-García Alejandro, Patel Raj, Mujtaba Iqbal M
Department of Chemical Engineering, Faculty of Engineering, Mutah University, Al Karak 00962, Jordan.
Department of Computer Techniques, Technical Institute of Baquba, Middle Technical University, Baquba 00964, Iraq.
Membranes (Basel). 2021 Dec 23;12(1):11. doi: 10.3390/membranes12010011.
The reverse osmosis (RO) process is one of the most popular membrane technologies for the generation of freshwater from seawater and brackish water resources. An industrial scale RO desalination consumes a considerable amount of energy due to the exergy destruction in several units of the process. To mitigate these limitations, several colleagues focused on delivering feasible options to resolve these issues. Most importantly, the intention was to specify the most units responsible for dissipating energy. However, in the literature, no research has been done on the analysis of exergy losses and thermodynamic limitations of the RO system of the Arab Potash Company (APC). Specifically, the RO system of the APC is designed as a medium-sized, multistage, multi pass spiral wound brackish water RO desalination plant with a capacity of 1200 m/day. Therefore, this paper intends to fill this gap and critically investigate the distribution of exergy destruction by incorporating both physical and chemical exergies of several units and compartments of the RO system. To carry out this study, a sub-model of exergy analysis was collected from the open literature and embedded into the original RO model developed by the authors of this study. The simulation results explored the most sections that cause the highest energy destruction. Specifically, it is confirmed that the major exergy destruction happens in the product stream with 95.8% of the total exergy input. However, the lowest exergy destruction happens in the mixing location of permeate of the first pass of RO desalination system with 62.28% of the total exergy input.
反渗透(RO)工艺是从海水和微咸水资源中制取淡水最常用的膜技术之一。由于该工艺多个单元中存在火用损失,工业规模的RO海水淡化消耗大量能源。为减轻这些限制,几位同行致力于提供可行方案来解决这些问题。最重要的是,目的是确定造成能源消耗的主要单元。然而,在文献中,尚未对阿拉伯钾肥公司(APC)的RO系统的火用损失和热力学限制进行分析。具体而言,APC的RO系统设计为中型、多级、多程螺旋卷式微咸水RO淡化厂,产能为1200立方米/天。因此,本文旨在填补这一空白,并通过纳入RO系统几个单元和隔室的物理火用和化学火用,严格研究火用破坏的分布情况。为开展这项研究,从公开文献中收集了一个火用分析子模型,并将其嵌入到本研究作者开发的原始RO模型中。模拟结果探究了造成最高能量破坏的最主要部分。具体而言,已证实主要火用破坏发生在产物流中,占总火用输入的95.8%。然而,最低火用破坏发生在RO淡化系统第一段渗透液的混合位置,占总火用输入的62.28%。