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死端超滤中蛋白质 - 多糖混合物导致的膜污染;渗透通量对抗污染性能的影响

Membrane Fouling Due to Protein-Polysaccharide Mixtures in Dead-End Ultrafiltration; the Effect of Permeation Flux on Fouling Resistance.

作者信息

Sioutopoulos Dimitrios, Karabelas Anastasios, Mappas Vasileios

机构信息

Chemical Process and Energy Resources Institute, Centre for Research and Technology-Hellas, 6th km Charilaou-Thermi Road, 57001 Thermi-Thessaloniki, Greece.

Department of Chemical Engineering, Aristotle University of Thessaloniki, 54623 Thessaloniki, Greece.

出版信息

Membranes (Basel). 2019 Feb 1;9(2):21. doi: 10.3390/membranes9020021.

DOI:10.3390/membranes9020021
PMID:30717080
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC6409950/
Abstract

Significant gaps exist in our knowledge of ultrafiltration (UF) membrane fouling, due to mixtures of poly-saccharides and proteins, despite a fair amount of related research. To get new insights into fouling layer characteristics, experiments were performed under constant-flux, within the range of practical interest (15⁻90 L/m²h), with typical polysaccharides (sodium alginate, SA), proteins (bovine serum albumin, BSA) as well as their mixtures in various proportions (1:3, 1:1, 3:1), and total organic matter concentration of 30 mg/L. The feed-water salinity and calcium ion concentration were 2000 mg/L NaCl and 2 mM, respectively. The temporal evolution of such fouling layers on flat-sheet membranes was monitored by recording the trans-membrane pressure variation. The results show that the specific fouling resistance α is strongly affected by flux, and the fouling propensity of polysaccharide-protein mixtures is significantly enhanced compared to single foulants, i.e., when BSA and SA are alone. The fouling layers are compressible and their resistance α tends to increase with the mass ratio of alginate in the mixture, particularly at high fluxes. To quantify these effects, correlations are presented of the initial fouling resistance α with permeate flux J and of the evolution of α. R&D priorities are suggested on this topic of mixed foulants.

摘要

尽管已有大量相关研究,但由于多糖和蛋白质的混合物,我们对超滤(UF)膜污染的认识仍存在重大差距。为了深入了解污染层特性,在实际感兴趣的通量范围(15⁻90 L/m²h)内进行了恒通量实验,使用典型的多糖(海藻酸钠,SA)、蛋白质(牛血清白蛋白,BSA)以及它们不同比例(1:3、1:1、3:1)的混合物,总有机物质浓度为30 mg/L。进水盐度和钙离子浓度分别为2000 mg/L NaCl和2 mM。通过记录跨膜压力变化来监测平板膜上此类污染层的时间演变。结果表明,比污染阻力α受通量的强烈影响,与单一污染物(即单独的BSA和SA)相比,多糖 - 蛋白质混合物的污染倾向显著增强。污染层是可压缩的,其阻力α往往随着混合物中海藻酸盐的质量比增加而增加,特别是在高通量时。为了量化这些影响,给出了初始污染阻力α与渗透通量J以及α演变的相关性。针对混合污染物这一主题提出了研发重点。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/c9163f6c7f79/membranes-09-00021-g013.jpg
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https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/127b5595a3e2/membranes-09-00021-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/f2bafe5dabcc/membranes-09-00021-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/76a93a6ee492/membranes-09-00021-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/549fcb58a9d2/membranes-09-00021-g010.jpg
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https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/c9163f6c7f79/membranes-09-00021-g013.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/9d77dfab3436/membranes-09-00021-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/047145e99810/membranes-09-00021-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/d0eeff041def/membranes-09-00021-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/49c11165aa11/membranes-09-00021-g004a.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/d76a6e7b50e2/membranes-09-00021-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/bb252cb2315c/membranes-09-00021-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/127b5595a3e2/membranes-09-00021-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/f2bafe5dabcc/membranes-09-00021-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/76a93a6ee492/membranes-09-00021-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/549fcb58a9d2/membranes-09-00021-g010.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/2c02673a0d3e/membranes-09-00021-g011.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/e277395a69d5/membranes-09-00021-g012.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/afe5/6409950/c9163f6c7f79/membranes-09-00021-g013.jpg

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