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首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >Effect of pretreatment and membrane orientation on fluxes for concentration of whey with high foulants by using NH3/CO2 in forward osmosis
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Effect of pretreatment and membrane orientation on fluxes for concentration of whey with high foulants by using NH3/CO2 in forward osmosis

机译:使用NH3 / CO2在前渗透中使用NH3 / CO2对高污垢乳清浓度的预处理和膜取向的影响

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Usage of forward osmosis membrane in FO mode, in which active and support layers of the membrane were in contact with the feed and the draw solutions respectively, provided higher initial water flux (12 L/m(2) h) than the usage of membrane in PRO mode (6 L/m(2) h) having opposite orientation but fluxes approached to each other after 4 h during concentration of whey with NH3/CO2 as draw salt. High organic and inorganic foulants of whey was considered as reason for observed result in addition to lower solute resistivity. Initial water flux (8,5 L/m(2) h) was lower when pre-treatment was applied before forward osmosis process but final flux (4 L/m(2) h) was equal flux of non pre-treatment. Reduction of solute resistivity or absence of hydraulic pressure can be reasons for lower initial flux. Detection of organic carbon but absence of lactose in draw solution showed passage of molecules being different than lactose into draw solution. (C) 2017 Elsevier Ltd. All rights reserved.
机译:在FO模式中使用前渗透膜,其中膜的活性和支撑层分别与进料和拉伸溶液接触,提供比膜的使用更高的初始水通量(12L / m(2)H) 在Pro模式(6L / m(2)小时)具有相反的取向,但在用NH 3 / CO2浓度为3小时后彼此接近彼此,用NH 3 / CO2为拉盐。 乳清的高有机和无机污垢被认为是观察结果的原因,除了较低的溶质电阻率之外。 当在前渗透过程之前施用预处理时,初始水通量(8,5升/米(2)H)较低,但最终通量(4L / m(2)H)是相等的非预处理通量。 溶质电阻率或不存在液压的降低可以是初始通量较低的原因。 有机碳的检测,但脱脂溶液中没有乳糖显示出分子通过与乳糖不同的分子。 (c)2017 Elsevier Ltd.保留所有权利。

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