恒通量和恒跨膜压力条件下横流反渗透过程中矿物垢的形成

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Mostafa Nassr, Sarah M. Dischinger, Ji Yeon Lee, Kristofer L. Gleason, Sergi Molins, Nicolas Spycher, Pedram Bigdelou, Jacob Johnston, Nathaniel A. Lynd, Nils Tilton, William T. Stringfellow, Benny D. Freeman, Daniel J. Miller
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引用次数: 0

摘要

膜表面矿物垢的形成是反渗透净水技术面临的一个重大挑战。实验室的污染实验通常是这样进行的:跨膜压力(TMP)是固定的,渗透通量随着时间的推移随着膜表面的鳞片积累而减少。然而,这种通量的变化意味着膜表面的水动力条件是不断变化的,这可能会影响结晶和污垢沉积过程。相比之下,在恒定渗透通量条件下操作是有利的,因为它使流体动力条件相对一致,从而可以比较膜特性(例如表面化学)如何影响污垢倾向。工业反渗透操作并不严格按照恒定TMP或恒定通量模式运行;虽然它们可能以恒定的TMP启动,但进料压力可能会定期调整,以保持渗透水产量在指定范围内。文献中报道的恒渗透通量反渗透结垢实验的缺乏,阻碍了对恒TMP和恒通量条件下膜污染过程的比较。首次比较了恒定TMP和恒定通量反渗透过滤过程中污染层阻力随膜面积累积渗透体积的变化规律。用接近饱和硫酸钙(石膏)的模型饲料溶液挑战商用反渗透膜进行结垢实验。在低通量下,两种运行模式下污垢层阻力的增加在数量上相似。在高通量条件下,恒通量过滤比恒TMP过滤的污染层阻力增大得更快。恒定TMP和恒定通量下的结垢机制分别为自限和自强化机制。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Mineral Scale Formation during Crossflow Reverse Osmosis at Constant Flux and Constant Transmembrane Pressure Conditions

Mineral Scale Formation during Crossflow Reverse Osmosis at Constant Flux and Constant Transmembrane Pressure Conditions
Mineral scale formation on membrane surfaces is a significant challenge in reverse osmosis water purification. Laboratory fouling experiments are typically run such that the transmembrane pressure (TMP) is fixed, and the permeate flux decreases over time as scales accumulate on the membrane surface. However, this change in flux means that the hydrodynamic conditions at the membrane surface are continuously changing, which could affect crystallization and foulant deposition processes. Operating under constant permeate flux conditions, in contrast, is advantageous because it keeps the hydrodynamic conditions relatively consistent, making it possible to compare how membrane properties (e.g., surface chemistry) affect fouling propensity. Industrial reverse osmosis operations are not run strictly in either constant TMP or constant flux mode; while they may start at a constant TMP, feed pressure may be periodically adjusted to maintain permeate water production within a specified range. The scarcity of constant permeate flux reverse osmosis scaling experiments reported in the literature frustrates efforts to compare membrane fouling processes under constant TMP and constant flux conditions. For the first time, the evolution of the fouling layer resistance was compared as a function of cumulative permeate volume per membrane area during constant TMP and constant flux reverse osmosis filtrations. Scaling experiments were conducted by challenging commercial reverse osmosis membranes with a model feed solution nearly saturated with calcium sulfate dihydrate (gypsum). At low fluxes, the increase in fouling layer resistance was quantitatively similar for the two operational modes. In contrast, at high fluxes, the fouling layer resistance increased more rapidly in constant flux filtration than in constant TMP filtration. The mechanism of scale formation in constant TMP and constant flux operation was self-limiting and self-reinforcing, respectively.
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来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.
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