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Binary ion exchange equilibria in systems containing NO_3~-, Cl~- and SO_4~(2-) on fibrous anion exchangers with tetraalkylammomium groups

机译:具有四烷基铵基团的纤维阴离子交换剂上含NO_3〜-,Cl〜-和SO_4〜(2-)的系统中的二元离子交换平衡

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Ion exchange equilibria Cl~-- NO_3~-, Cl~- -SO_4~(2-) , NO~_3~- -SO_4~(2-) on fibrous strong base anion exchangers on the basis of graft copolymer of styrene and divinylbenzene to polypropylene fibers with groups of benzyl trimethyl- (TMA), triethyl- (TEA), and tributyl- (TBA) ammonium have been studied and characterized by values of the equilibrium coefficients and separation factors. They were compared with the same equilibria on ion exchange resins Dowexl with different cross-linkage. An equation allowing calculating the separation factor for different ionic concentrations and ratios of the ions in solutions of uni-and divalent ions from the equilibrium coefficient invariant to the concentration has been derived. The selectivity of nitrate and chloride sorption increases with increasing size of alkyl radicals in the functional group and with increasing percent of divinylbenzene in the resins. A quantity characterizing selectivity of ion exchanger to bivalent ion against the univalent ion named concentration of zeroth selectivity (CZS) has been suggested to describe the efficiency of ion exchangers in processes of water purification from univalent ions, specifically nitrates in waters containing sulfates. At concentrations above the CZS the univalent ion is absorbed selectively compared to the bivalent one; the "dumping effect" in frontal chromatograms of mixtures of such ions is not possible above the CZS point and this criterion can be used for choosing the ion exchanger for selective removal of univalent ions from mixtures with polyvalent ones. The CZS values for conventional strong base ion exchangers in ion exchange NO_3~- SO_4~(2-) is higher than typical total ionic concentrations in drinking waters (1-3 × 10~(-3) eq/L). For Dowex 1 × 10 it was found equal 1.3 × 10~(-2) eq/L. For the fibrous ion exchanger with benzyltribu-tylammonium groups CZS = 3.3 × 1~(-6) eq/L. This ion exchanger is suitable for selective removal of nitrates from the solutions with concentrations higher than this value and has exceedingly high selectivity to nitrates which makes the process of its regeneration difficult. The most suitable fibrous ion exchangers for application in drinking waters purification from nitrates with guarantied absence of the nitrate dumping appeared FIBAN A-1 TEA having the CZS values 4.3 × 10~(-4) eq/L.
机译:基于苯乙烯和二乙烯基苯接枝共聚物的纤维强碱阴离子交换剂上的离子交换平衡Cl〜-NO_3〜-,Cl〜--SO_4〜(2-),NO〜_3〜--SO_4〜(2-)对具有苄基三甲基(TMA),三乙基(TEA)和三丁基(TBA)铵基团的聚丙烯纤维进行了研究,并通过平衡系数和分离因子的值对其进行了表征。将它们与具有不同交联键的离子交换树脂Dowexl的相同平衡进行比较。得出了一个方程,该方程可以根据浓度不变的平衡系数计算出不同离子浓度和一价和二价离子溶液中离子比例的分离系数。硝酸盐和氯化物吸附的选择性随官能团中烷基自由基大小的增加以及树脂中二乙烯基苯百分比的增加而增加。已经提出了表征离子交换剂对二价离子相对于单价离子的选择性的特征,称为零选择性浓度(CZS),以描述离子交换剂在从单价离子(特别是含硫酸盐的水中)中纯化水的过程中的效率。在高于CZS的浓度下,与二价离子相比,单价离子被选择性吸收。在CZS点以上,此类离子混合物的正面色谱图中的“倾倒效应”是不可能的,并且该标准可用于选择离子交换剂,以从多价离子混合物中选择性去除单价离子。离子交换NO_3〜-SO_4〜(2-)中常规强碱离子交换剂的CZS值高于饮用水中典型的总离子浓度(1-3×10〜(-3)eq / L)。对于Dowex 1×10,发现等于1.3×10〜(-2)eq / L。对于具有苄基-丁基铵基团的纤维离子交换剂,CZS = 3.3×1〜(-6)eq / L。该离子交换剂适于从浓度高于该值的溶液中选择性除去硝酸盐,并且对硝酸盐具有极高的选择性,这使其再生过程变得困难。在保证没有硝酸盐倾泻的情况下,最适合用于从硝酸盐净化饮用水中的纤维离子交换剂出现了FIBAN A-1 TEA,其CZS值为4.3×10〜(-4)eq / L。

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