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Development of a simulation program for the forward osmosis and reverse osmosis process

机译:开发用于正向渗透和反向渗透过程的仿真程序

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摘要

Forward osmosis (FO) is an osmotic process that uses a semi-permeable membrane to effect separation of water from dissolved solutes by an osmotic pressure gradient. Unlike RO, FO does not require high pressure for separation, allowing low energy consumption to produce water. Therefore FO, a potential alternative to conventional membrane process, has been considered a novel technology for seawater desalination. There is no forward osmosis (FO) process simulation program yet, though. Therefore, the main objective of this paper is to develop such computer program based on the solution-diffusion model modified with the film theory for simulating and optimizing the FO, RO, and FO-RO hybrid process. The effect of concentration polarization on FO and RO process efficiency was also considered in the model. AMATLAB-based graphical user interface (GUI) program was used to develop the simulation program. Using the program, the effects of various factors, including the draw solution concentration, feed concentration, and feed pressure and temperature, on the FO and RO process performance were examined. The simulation results showed that the FO-RO hybrid process has higher recovery (66.8%) with reasonable flux (13.1 L/m~2-h) and permeate concentration (382 mg/L) than the FO and RO process. Thus, the advantages of the FO-RO hybrid process over the FO and RO process are its low permeate concentration and high recovery, which are difficult to attain in the FO and RO process, respectively.
机译:正向渗透(FO)是一种渗透过程,该过程使用半渗透膜通过渗透压梯度实现水与溶解溶质的分离。 FO与RO不同,FO不需要高压进行分离,从而降低了能耗来生产水。因此,作为传统膜法的潜在替代品的FO被认为是用于海水淡化的新技术。但是,还没有正向渗透(FO)过程仿真程序。因此,本文的主要目的是开发基于膜理论修正的溶液扩散模型的计算机程序,以模拟和优化FO,RO和FO-RO混合过程。模型中还考虑了浓度极化对FO和RO工艺效率的影响。基于AMATLAB的图形用户界面(GUI)程序用于开发仿真程序。使用该程序,检查了各种因素(包括汲取溶液浓度,进料浓度以及进料压力和温度)对FO和RO工艺性能的影响。模拟结果表明,FO-RO混合工艺比FO和RO工艺具有更高的回收率(66.8%),通量(13.1 L / m〜2-h)和渗透浓度(382 mg / L)。因此,FO-RO混合工艺相对于FO和RO工艺的优势在于其渗透物浓度低和回收率高,这分别在FO和RO工艺中难以实现。

著录项

  • 来源
    《Desalination and water treatment》 |2011年第3期|p.273-282|共10页
  • 作者单位

    University of Science & Technology, 113 Gwahangno, Uuseong-Gu, Daejeon 305-333, Korea;

    Korea Institute of Construction Technology, 2311 Daehwa-Dong, Ilsan-Gu, Goyang-Si, Gyeonggi-Do 411-712, Korea,Koohnin university, Jeongneung-gil 77, 861-1 Jeongneung-Dong, Senobuk-Gu, Seoul. 136-702 Korea;

    Koohnin university, Jeongneung-gil 77, 861-1 Jeongneung-Dong, Senobuk-Gu, Seoul. 136-702 Korea;

    Koohnin university, Jeongneung-gil 77, 861-1 Jeongneung-Dong, Senobuk-Gu, Seoul. 136-702 Korea;

    Koohnin university, Jeongneung-gil 77, 861-1 Jeongneung-Dong, Senobuk-Gu, Seoul. 136-702 Korea;

    Department of Civil & Environmental Engineering, College of Engineering, Yonsei University, Seoul 120-749, Korea;

    Department of Civil & Environmental Engineering, College of Engineering, Yonsei University, Seoul 120-749, Korea;

    Department of Civil & Environmental Engineering, College of Engineering, Yonsei University, Seoul 120-749, Korea;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    forward osmosis; program; model; hybrid process; simulation;

    机译:正向渗透程序;模型;混合过程模拟;

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