使用高通量、抗污染纳滤膜解决硫酸盐去除装置的操作挑战

T. Krebs, R. Ganguli, G. Lage, P. Verbeek, V. Mehrotra, P. Florido, M. R. Akdim
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引用次数: 1

摘要

为了控制储层酸化和结垢,需要在注入前对海水进行脱硫处理。为了完成这项任务,操作人员在硫酸盐去除装置(sru)中使用纳滤(NF)膜。膜的变质趋势是一个关键的操作挑战。为了克服污垢,需要经常进行化学清洗。sru的另一个限制是处理水量不能轻易增加,因为更高的水量会导致更快的膜污染。本文介绍了一种提高脱硫膜渗透通量和抗污染性能的方法。这些增强是通过使用永久涂层修饰商用纳滤膜的活性层来实现的,该涂层增加了纳滤膜的亲水性,同时保留了纳滤膜的高表面电荷特性。我们报告了为期六个月的涂膜现场试验的结果。该试验在加利福尼亚州休内梅港的海水淡化试验设施进行,使用2.5英寸直径。膜模块。测试滑板包含两条不同的平行流线,有6根2.5英寸直径的涂层管线。膜系列,和一个未涂层的2.5“膜作为参考。结果表明,在相同的跨膜压力下,涂覆膜的渗透通量比未涂覆膜高25%。在整个测试过程中,涂覆膜和未涂覆膜的硫酸盐截留率都没有变化。涂覆膜的污染率也低于未涂覆膜。与未涂覆膜相比,涂覆膜的清洗间隔时间增加了~ 38%,并且在需要清洗之前,涂覆膜多处理了~ 63%的渗透性。初步结果还表明,在1 ppm的连续氯化作用下,涂层膜的氯耐受性至少提高了3000 ppm-h。本文将讨论涂层对SRU运行经济性的影响。本文的研究结果表明,新开发的涂层可以显着提高sru的性能和可操作性,并且可以显着降低sru的生命周期成本。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Solving the Operational Challenges of Sulfate Removal Units Using High-Flux, Fouling-Resistant Nanofiltration Membranes
Desulfation of seawater before injection is required to control reservoir souring and scale formation. For this task, operators use nanofiltration (NF) membranes in sulfate removal units (SRUs). The tendency of the membranes to foul is a key operational challenge. To overcome fouling, frequent chemical cleaning is required. An additional constraint for SRUs is that the amount of treated water cannot be increased easily as a higher water output results in an even faster fouling of membranes. In this paper, we describe a method to enhance permeate flux and fouling resistance of desulfation membranes. The enhancements are achieved by modifying the active layer of commercially available NF membranes using a permanent coating that increases hydrophilicity while retaining the high surface charge characteristic of NF membranes. We report the results of a six-month field trial with the coated membranes. The test was executed at the Seawater Desalination Test Facility in Port Hueneme, California using 2.5" dia. membrane modules. The test skid contained two different parallel flow lines with a stack of six coated 2.5" dia. membranes in series, and an uncoated 2.5" membrane for reference. The results show a 25% higher permeate flux for the coated membranes compared to the uncoated membrane at the same transmembrane pressure. Sulfate rejection was unchanged for both coated and uncoated membranes during the entire duration of the test. The coated membrane also showed a lower fouling rate than the uncoated membrane. The time between cleaning events increased by ∼ 38 % for the coated membranes as compared to the uncoated membrane, and the coated membrane processed ∼ 63 % more permeate before cleaning was required. Preliminary results also indicate an enhanced chlorine tolerance of the coated membranes of at least 3000 ppm-h under continuous chlorination at ∼ 1 ppm. The impact of the coating on the economics of SRU operations will be discussed in the paper. The results presented in this paper demonstrate that performance and operability of SRUs can be significantly enhanced by a newly-developed coating, and that a significant reduction in the lifecycle cost of SRUs can be achieved.
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