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Adsorption of Cr(vi) from aqueous solutions onto raw and acid-activated re?adiye and han?ili clays

机译:水溶液中Cr(vi)吸附到生酸活化的半透明和半透明粘土上

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The adsorption of Cr(VI) from aqueous solutions onto raw and acid-activated clays-namely, Re?adiye region clay (R, raw Re?adiye region clay; R-H_2SO_4, acid-activated with H_2SO_4 Re?adiye region clay; R-HCl, acid-activated with HCl Re?adiye region clay) and Han?ili.region clay (H, raw Han?ili region clay; H-H_2SO_4, acid-activated with H_2SO_4 Han?ili region clay; H-HCl, acid-activated with HCl Han?ili region clay)-was studied in a batch system. For optimization of the Cr(VI) adsorption on raw clays and acid-activated clays, the effect of pH, temperature, initial Cr(VI) concentration, time, and adsorbent dosage were investigated. X-ray diffraction analyses of raw and acid-activated clays were used to determine the effects of acid-activating on the layer structure of the clays. The surface characterizations of clays and modified clays were performed by using FT-IR spectroscopy. The Langmuir and Freundlich adsorption models were employed to describe the equilibrium isotherms, and thus the isotherm constants were determined. The data obtained from our investigations were well described by the Langmuir model. The adsorption capacity of the adsorbents Re?adiye and Han?ili clays were found to be 0.0269, 0.0144, and 0.0170 mmol/g for H, H-HCl, and H-H_2SO_4 and 0.0356, 0.0276, and 0.0422 mmol/g for R, R-HCl, and R-H_2SO_4, respectively. The results show that the adsorption was strongly dependent on pH of the medium, initial Cr(VI) concentration and temperature. The removal of Cr(VI) reached saturation in about 120 min, and the adsorption process of Cr(VI) was observed as exothermic. A maximum removal of 73% was noted at 1.0 × 10~(-4)M concentration of Cr(VI) in solution for H-HCl. Furthermore the enhancement of removal of Cr(VI) was observed from pH 3 to 4. The results are discussed to highlight the influence of acid activation on Cr(VI) adsorption characteristics of the clays.
机译:水溶液中Cr(VI)的吸附到生酸活化的粘土上,即Readidiye地区黏土(R,原始Rerefadiye地区黏土; R-H_2SO_4,用H_2SO_4 Re?adiyeye地区黏土酸活化; R-HCl,用HCl Re?adiyeye地区粘土酸活化)和Han?ili。区域粘土(H,原始Han?ili地区粘土; H-H_2SO_4,用H_2SO_4 Han?ili地区粘土酸活化; H-HCl用批处理系统研究了用HCl Han?ili地区粘土酸活化的)。为了优化Cr(VI)在原土和酸活化粘土上的吸附,研究了pH,温度,初始Cr(VI)浓度,时间和吸附剂用量的影响。对未加工的和酸活化的粘土进行X射线衍射分析,以确定酸活化对粘土层结构的影响。粘土和改性粘土的表面表征通过FT-IR光谱法进行。用Langmuir和Freundlich吸附模型描述平衡等温线,从而确定等温线常数。 Langmuir模型很好地描述了我们从调查中获得的数据。发现吸附剂Re?adiye和Han?ili粘土对H,H-HCl和H-H_2SO_4的吸附容量为0.0269、0.0144和0.0170 mmol / g,对R的吸附容量为0.0356、0.0276和0.0422 mmol / g ,R-HCl和R-H_2SO_4。结果表明,吸附强烈依赖于介质的pH,初始Cr(VI)浓度和温度。 Cr(VI)的去除在约120分钟内达到饱和,并且观察到Cr(VI)的吸附过程是放热的。在H-HCl溶液中,Cr(VI)的浓度为1.0×10〜(-4)M时,最大去除73%。此外,从pH 3到4观察到了Cr(VI)去除的增强。讨论了结果以突出酸活化对粘土对Cr(VI)吸附特性的影响。

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