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Adsorption of Zinc(II) and Chromium(III) Ions by Modified Zeolites

机译:通过改性沸石吸附锌(II)和铬(III)离子

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The results of a study of the adsorption of zinc(II) and chromium(III) ions by zeolites modified by HCl are presented. According to the data of elemental analysis and electron spectroscopy, the zeolites contain at least 75% heulandite in their composition. The removal of aluminum ions from the tetrahedral framework of the sorbent formed by AlO4 and SiO4 occurs upon modifying the zeolites by HCl. This leads to the destruction of the main component, heulandite, and compaction of the silicate layer. The time of establishment of adsorption equilibrium in the zeolite-aqueous solution system is 90 min. The isotherms of adsorption of zinc(II) ions are obtained in a temperature range 298-318 K at pH 5.6-5.8. It is shown that the adsorption of zinc(II) ions increases with growing temperature. The isotherms of adsorption of chromium(III) ions are obtained in a temperature range 298-318 K at pH 7.6-7.9. It is found that the adsorption of chromium(III) ions decreases with increasing temperature. The differential heats of adsorption are calculated based on the isosteres of adsorption. The increase in the adsorption of chromium(III) ions is accompanied by a decrease in the differential heat of adsorption from 36.9 to 26.8 kJ/mol. This may be associated with the nonuniformity of the surface of the adsorbent, due to what the metal ions are adsorbed on less active regions of the surface as far as the growth in the saturation of more active sites. The change in the differential heat of adsorption of zinc(II) ions with the growth in the degree of filling of the surface has a nonmonotone character. In the region of low degrees of filling of the surface, the differential heat of adsorption decreases, and then increases, which is probably determined by polymolecular adsorption presuming the presence of an adsorbate-adsorbate interaction. The efficiency of treatment of industrial wastewaters of the electroplating industry in the case of the use of the modified zeolites is over 97%.
机译:本文介绍了用盐酸改性沸石吸附锌(II)和铬(III)离子的研究结果。根据元素分析和电子光谱数据,这些沸石的成分中至少含有75%的黑硅石。在用HCl改性沸石后,铝离子从AlO4和SiO4形成的吸附剂四面体框架中去除。这会导致主要成分黑硅石的破坏,以及硅酸盐层的压实。在沸石水溶液体系中建立吸附平衡的时间为90分钟。在pH 5.6-5.8的温度范围298-318 K内获得了锌(II)离子的吸附等温线。结果表明,随着温度的升高,锌离子的吸附量增加。在298-318K的温度范围内,pH值为7.6-7.9,获得了铬(III)离子的吸附等温线。研究发现,随着温度的升高,铬离子的吸附量降低。根据吸附等温线计算了不同的吸附热。铬(III)离子吸附量的增加伴随着吸附热差的降低,从36.9 kJ/mol降至26.8 kJ/mol。这可能与吸附剂表面的不均匀性有关,因为金属离子吸附在表面活性较低的区域,直至活性较高的部位的饱和增长。锌(II)离子的微分吸附热随表面填充度的增加而变化,具有非单调性。在表面填充度较低的区域,吸附差热先减小,然后增大,这可能是由假定存在吸附质-吸附质相互作用的多分子吸附决定的。在使用改性沸石的情况下,电镀工业废水的处理效率超过97%。

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