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Permeate flux decline prediction in the ultrafiltration of macromolecules with empirical estimation of the gel layer concentration

机译:大分子超滤过程中渗透通量下降的预测与凝胶层浓度的经验估计

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Permeate flux decline with time was estimated by means of a model[1]that considers gel layer formation as the main fouling mechanism.Several experiments were performed with two different membranes.Both of them were monotubular ceramic membranes.One of them was made of ZrO2-TiO2 with a molecular weight cut off(MWCO)of 15 kDa(Orelis,France)and the other was made of Al2O3-TiO2 with a MWCO of 5 kDa(Tami Industries,France).The feed was an aqueous solution of polyethylene glycol with a molecular weight of 35 kDa.All the experiments were carried out at the crossflow velocity of 1 m/s,when the cake layer is more likely to form.Transmembrane pressure(TMP)was varied between 0.1 and 0.5 MPa and the feed concentration was in the range of 5-15 g/L.The experimental results and those predicted by the model were compared for the experimental conditions tested.Model predictions were better for the Orelis membrane than in the case of the Tami Industries membrane under the same experimental conditions.
机译:渗透率随时间的下降是通过模型[1]估算的,模型将凝胶层的形成作为主要的结垢机理。对两种不同的膜进行了多次实验,两种都是单管陶瓷膜,其中一种是由ZrO2制成的。 -截留分子量(MWCO)为15 kDa的TiO2(法国奥利利斯),另一种是MWCO为5 kDa的Al2O3-TiO2(Tami Industries,法国)。进料为聚乙二醇水溶液分子量为35 kDa。所有实验均在错流速度为1 m / s的条件下进行,此时更容易形成滤饼层。跨膜压力(TMP)在0.1至0.5 MPa之间变化,进料浓度在5-15 g / L的范围内。比较了实验结果和模型预测的实验条件。在相同的实验条件下,Orelis膜的模型预测要比Tami Industries膜更好条件。

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