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Process for the removal and recovery of phenolic compounds from aqueous fluids.

机译:从水性液体中去除和回收酚类化合物的方法。

摘要

Process for removing and recovering one or more phenolic compounds undissociated in aqueous liquid, said method comprising the following steps: (a) transfer one or more phenolic compounds from the aqueous fluid (1) to an alkaline stripping solution (3) wherein the transfer of one or more undissociated phenolic compounds from the aqueous fluid (1) to the alkaline stripping solution (3) occurs across a membrane (5); wherein the membrane (5) is a nonporous permselective membrane; (B) regulating the volume used of alkaline stripping solution (3) on the treated aqueous liquid (1) volume, so that the total phenolic compound concentration in the alkaline stripping solution (4) comprising the sum of concentrations of dissociated phenolic compounds and undissociated, is greater than the solubility of the phenolic compounds in the solution acidified stripping step (d); (c) regulating the pH of the alkaline stripping solution (3) in contact with the membrane (5) to a value of at least 0, 5 pH units above the acidic dissociation constant of the phenolic compound; (D) adjusting the pH of the alkaline stripping solution (4) containing phenolic compound to lower the acid dissociation constant of the phenolic compound and value; (E) separating the resulting phase rich in phenolic compounds (11) of the solution acidified reextraction (12).
机译:去除和回收在水性液体中未离解的一种或多种酚类化合物的方法,所述方法包括以下步骤:(a)将一种或多种酚类化合物从水性流体(1)转移到碱性汽提溶液(3)中,其中从水流体(1)到碱性汽提溶液(3)的一种或多种未离解的酚类化合物跨过膜(5)发生;其中膜(5)是无孔的选择性渗透膜; (B)调节碱性汽提液(3)在处理的含水液体(1)上的体积,使碱性汽提液(4)中的总酚化合物浓度包括解离的酚化合物和未解离的酚化合物的浓度之和。大于溶液酸化汽提步骤(d)中酚类化合物的溶解度; (c)将与膜(5)接触的碱性汽提溶液(3)的pH调节至比酚类化合物的酸解离常数高至少0、5个pH单位的值; (D)调节含有酚类化合物的碱性汽提溶液(4)的pH值,以降低酚类化合物的酸离解常数和值。 (E)分离酸化的再萃取液(12)的所得的富含酚化合物的相(11)。

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