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Examination Of Methods To Reduce Membrane Fouling During Dairy Microfiltration And Ultrafiltration

机译:减少乳制品微滤和超滤过程中膜污染的方法的检验

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摘要

Pressure-driven membrane filtration processes such as microfiltration (MF), ultrafiltration (UF), nanofiltration (NF), and reverse osmosis (RO) provide opportunities for the dairy industry to better utilize milk by separating its components based on size. However, widespread adoption of some of these processes has yet to be realized due to membrane fouling. Membrane fouling is the accumulation of soil, or foulant, on the surface or within the pores of a membrane. Fouling prolongs processing times, increases energy and cleaning costs, decreases separation efficiency, and, in severe cases, may lead to irreversible clogging of the membrane. Microfiltration can be used to remove serum proteins (SP) from skim milk. The process' SP removal efficiency directly influences the technology's financial feasibility. Our first objective was to quantify the capacity of 0.14 [MICRO SIGN]m ceramic Isoflux MF membranes to remove SP from skim milk. The Isoflux membranes' manufacturer claims that using these membranes will reduce localized membrane fouling at the inlet end of the membrane that results from using high cross-flow velocities (5 - 7 m/s) to mitigate overall membrane fouling. Contrary to theoretical cumulative SP removal percentages of 68%, 90%, and 97% after 1, 2, and 3 stages of 3X MF processing, respectively, the 3X Isoflux process removed only 39.5%, 58.4%, and 70.2% after 1, 2, and 3 stages, respectively. Several design aspects of the membrane are thought to have resulted in this inefficiency. Ultrafiltration can be used to concentrate SP and reduce the lactose content of cheese whey or MF permeate of skim milk to produce 80% whey protein concentrates (WPC80) or 80% serum protein concentrates (SPC80), respectively. The objectives of our second study were to determine if adding annatto color to milk or bleaching whey or MF permeate of skim milk with hydrogen peroxide (H2O2) or benzoyl peroxide (BPO) influenced UF flux, diafiltration flux, or membrane fouling during production of WPC80 or SPC80. Addition of annatto color to milk had no effect on flux or fouling. Bleaching with or without added color increased flux during processing. Bleaching with H2O2 produced higher flux than bleaching with BPO. While bleaching with BPO reduced membrane fouling during WPC80 production, it did not impact membrane fouling during SPC80 production. Bleaching with H2O2 led to the largest reduction in fouling for both production processes.
机译:压力驱动的膜过滤工艺(例如微滤(MF),超滤(UF),纳滤(NF)和反渗透(RO))为乳品行业提供了机会,可以通过根据大小分离其成分来更好地利用牛奶。然而,由于膜结垢,尚未实现其中一些方法的广泛采用。膜结垢是土壤或污垢在膜表面或孔中的积聚。结垢延长了处理时间,增加了能源和清洁成本,降低了分离效率,在严重的情况下,可能会导致不可逆转的膜堵塞。微滤可用于去除脱脂乳中的血清蛋白(SP)。该工艺的SP去除效率直接影响该技术的财务可行性。我们的首要目标是量化0.14 [MICRO SIGN] m陶瓷Isoflux MF膜从脱脂乳中去除SP的能力。 Isoflux膜的制造商声称,使用这些膜将减少因使用高横流速度(5-7 m / s)减轻整体膜结垢而在膜入口端造成的局部膜结垢。与3X MF处理的1、2和3阶段后的理论累积SP去除百分比分别为68%,90%和97%相​​反,3X Isoflux处理在1、1和2之后仅去除了39.5%,58.4%和70.2%。 2个阶段和3个阶段。膜的几个设计方面被认为导致这种效率低下。超滤可用于浓缩SP并降低脱脂奶中干酪乳清或MF渗透物中的乳糖含量,分别生产80%的乳清蛋白浓缩物(WPC80)或80%的血清蛋白浓缩物(SPC80)。我们第二项研究的目的是确定在过氧化氢(H2O2)或过氧化苯甲酰(BPO)的脱脂牛奶或漂白乳清或MF渗透液中添加胭脂红会影响WPC80生产过程中的UF通量,渗滤通量或膜污染或SPC80。在牛奶中添加胭脂红对通量或结垢没有影响。在有或没有添加颜色的情况下进行漂白处理都会增加通量。用H2O2漂白比用BPO漂白产生更高的通量。虽然用BPO漂白减少了WPC80生产过程中的膜污染,但并没有影响SPC80生产过程中的膜污染。使用H2O2漂白可最大程度减少两种生产工艺的结垢。

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    Adams Michael;

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  • 年度 2012
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