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Long-Running Comparison of Feed-Water Scaling in Membrane Distillation

机译:膜蒸馏中饲料水垢的长期比较

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摘要

Membrane distillation (MD) has shown promise for concentrating a wide variety of brines, but the knowledge is limited on how different brines impact salt scaling, flux decline, and subsequent wetting. Furthermore, past studies have lacked critical details and analysis to enable a physical understanding, including the length of experiments, the inclusion of salt kinetics, impact of antiscalants, and variability between feed-water types. To address this gap, we examined the system performance, water recovery, scale formation, and saturation index of a lab-scale vacuum membrane distillation (VMD) in long-running test runs approaching 200 h. The tests provided a comparison of a variety of relevant feed solutions, including a synthetic seawater reverse osmosis brine with a salinity of 8.0 g/L, tap water, and NaCl, and included an antiscalant. Saturation modeling indicated that calcite and aragonite were the main foulants contributing to permeate flux reduction. The longer operation times than typical studies revealed several insights. First, scaling could reduce permeate flux dramatically, seen here as 49% for the synthetic brine, when reaching a high recovery ratio of 91%. Second, salt crystallization on the membrane surface could have a long-delayed but subsequently significant impact, as the permeate flux experienced a precipitous decline only after 72 h of continuous operation. Several scaling-resistant impacts were observed as well. Although use of an antiscalant did not reduce the decrease in flux, it extended membrane operational time before surface foulants caused membrane wetting. Additionally, numerous calcium, magnesium, and carbonate salts, as well as silica, reached very high saturation indices (>1). Despite this, scaling without wetting was often observed, and scaling was consistently reversible and easily washed. Under heavy scaling conditions, many areas lacked deposits, which enabled continued operation; existing MD performance models lack this effect by assuming uniform layers. This work implies that longer times are needed for MD fouling experiments, and provides further scaling-resistant evidence for MD.
机译:膜蒸馏(MD)已经显示出浓缩各种盐水的希望,但知识有限于不同的盐水冲击盐缩放,助焊剂下降和随后的润湿。此外,过去的研究缺乏关键的细节和分析,以便能够理解,包括实验的长度,包含盐动力学,抗央气剂的影响,以及饲料水类型之间的可变性。为了解决这一差距,我们检查了200小时的长跑试验中的实验室规模真空膜蒸馏(VMD)的系统性能,水回收,规模形成和饱和度指数。该试验提供了各种相关进料溶液的比较,包括合成海水反渗透盐水,盐度为8.0g / L,自来水和NaCl,包括抗粘性剂。饱和型造型表明,方解石和金属石是有助于渗透助焊剂的主要污垢。操作时间越长,典型的研究揭示了几个见解。首先,缩放可以显着降低渗透物助焊剂,在这里看到合成盐水的49%,当达到高回收率为91%时。其次,膜表面上的盐结晶可具有长延迟但随后的显着影响,因为渗透磁通量仅在连续操作的72小时后逐渐下降。也观察到几种耐缩放的影响。虽然使用防垢剂没有降低磁通量的降低,但它在表面污垢引起的膜润湿之前延长膜操作时间。另外,许多钙,镁和碳酸盐,以及二氧化硅达到非常高的饱和索引(> 1)。尽管如此,经常观察到不润湿的缩放,并且缩放始终是可逆的并且容易洗涤。在繁重的缩放条件下,许多领域缺乏存款,使能持续运作;通过假设均匀层,现有的MD性能模型缺乏这种效果。这项工作意味着MD结垢实验需要更长的时间,并为MD提供进一步的抗缩放证据。

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