海水给水反渗透预热评价第1部分:先导元件性能

A. Karameldin, M. Saadawy
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引用次数: 3

摘要

以海水反渗透预热过程为研究对象,对该过程进行了参数化研究。给出了描述先导元素的基本输运方程,并对其进行了评价。对控制整个系统性能的主导因素进行了研究和分析。研究了不同进料盐浓度下的进料压力和温度。此外,还研究了不同进料流量对渗透通量、渗透器排盐率和渗透器回收率的影响。采用一种知名数据的海水膜,例如FT30SW380HR,来进行研究。确定了膜的透水系数Kw,并进行了相关分析。此外,给出并讨论了制造商系统分析程序(ROSA)中的膜盐渗透系数k。输运控制方程以一种有利于实现实际参数研究的方式进行编程。结果表明,随着进料压力的增大,渗透通量显著增大。随着进料盐浓度的降低,以及进料温度和压力的升高,它也显著增加。同时,随着进料压力的增加,渗透器排盐量显著增加,随着进料温度的升高,渗透器排盐量显著降低。对阵列先导元件的研究表明,必须考虑最大膜通量、最大施加进料压力、最大进料流量和最大进料温度等约束条件。因此,为了获得最大的膜通量,必须在进料温度升高的同时降低施加的进料压力。当进料温度从18°C提高到45°C时,根据进料盐浓度和进料流量的不同,可实现7%至26%的压力节约。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Seawater feed reverse osmosis preheating appraisal, Part I: leading element performance
This paper is concerned with the seawater reverse osmosis preheating process, and presents a parametric study of the process. The basic transport equations describing the leading element are exhibited and appraised. The leading element, which governs the whole system performance, is studied and analysed. The incorporated and investigated operating parameters are the feed pressure and the temperature for different feed salt concentrations. In addition, different feed flow rates, effects on permeate flux and permeator salt rejection, together with the permeator recovery, are studied. A seawater membrane of a well-known data, for instance FT30SW380HR, is used to perform the study. The membrane water permeability coefficient Kw is determined and correlated. Furthermore, the membrane salt permeability coefficient Ks from the manufacturer system analysis program (ROSA) is given and discussed. The transport governing equations are programmed in a way that facilitates the achievement of a realistic parametric study. The results showed that the permeate flux increases significantly as the feed pressure increases. Also, it increases significantly as the feed salt concentration decreases, and also as the feed temperature and pressure increase. Meanwhile, the permeator salt rejection increases significantly as the feed pressure increases, and decreases significantly as the feed temperature increases. The study of the leading element of the array showed that there are constraints that must be considered, such as maximum membrane flux, maximum applied feed pressure, maximum feed flow rate and maximum feed temperature. Therefore, to attain the maximum membrane flux, the applied feed pressure must be lowered when the feed temperature is increased. In the case where the feed temperature is increased from 18°C to 45°C, a pressure saving of between 7% and 26% is achieved, according to the feed salt concentration and feed flow rate.
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