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首页> 外文期刊>Chemical engineering journal >Effect of basicity of anion exchangers and number and positions of sulfonic groups of acid dyes on dyes adsorption on macroporous anion exchangers with styrenic polymer matrix
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Effect of basicity of anion exchangers and number and positions of sulfonic groups of acid dyes on dyes adsorption on macroporous anion exchangers with styrenic polymer matrix

机译:阴离子交换剂的碱性和酸性染料的磺酸基团的数量和位置对苯乙烯聚合物基大孔阴离子交换剂吸附染料的影响

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Three commercial anion exchange resins, strongly basic of type 1 (Amberlite IRA-900) and type 2 (Amberlite IRA-910) and weakly basic (Amberlyst A-21) were evaluated for the removal of anionic acid dyes, C.I. Acid Orange 7 and C.I. Acid Orange 10 from aqueous solutions. The pseudo-second order kinetic model was applied to predict the rate constant of adsorption and the equilibrium capacity as a function of initial dye concentration. Modeling of kinetic results showed that the sorption process of the dye adsorption on the anion exchangers is in the good agreement with pseudo second-order model in the entire investigated concentration domain. Also kinetic measurement showed that the process was uniform and rapid. However, CI. Acid Orange 10 demonstrated faster binding with the anion exchangers than CI. Acid Orange 7. On the basis of the Langmuir isotherm model analysis, the maximum adsorption capacity of anion exchangers and affinity of the dyes for resins were determined. For each acid dyes, the maximum adsorption capacity of Amberlite IRA-900 was higher than the maximum adsorption capacity of remaining anion exchangers. The dyes sorption did not change in whole pH range of 2-12 in accordance with a presupposed ion-exchange mechanism of the adsorption on strongly basic anion exchangers. On the other hand, the sorption of the dyes on the weakly basic anion exchanger also did not change with changing pH suggesting physical adsorption in the polymer network and hydrogen bonding as the predominant mechanism of the dyes on this ion exchange resin.
机译:评价了三种市售的阴离子交换树脂,它们分别是1型强碱性(Amberlite IRA-900)和2型强碱性(Amberlite IRA-910)和弱碱性(Amberlyst A-21)去除阴离子酸性染料C.I.酸性橙7和C.I.来自水溶液的酸性橙10。使用伪二级动力学模型来预测吸附速率常数和平衡容量与初始染料浓度的关系。动力学结果建模表明,在整个研究浓度域中,染料在阴离子交换剂上的吸附过程与拟二阶模型吻合良好。动力学测量也表明该过程是均匀且快速的。但是,CI。酸性橙10与阴离子交换剂的结合要快于CI。酸性橙7.根据Langmuir等温模型分析,确定了阴离子交换剂的最大吸附容量和染料对树脂的亲和力。对于每种酸性染料,Amberlite IRA-900的最大吸附容量高于其余阴离子交换剂的最大吸附容量。根据在强碱性阴离子交换剂上吸附的预设离子交换机理,染料的吸附在2-12的整个pH范围内均不会改变。另一方面,弱碱性阴离子交换剂上的染料吸附也没有随pH的变化而改变,这表明聚合物网络中的物理吸附和氢键是染料在该离子交换树脂上的主要机理。

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