PREPARATION OF ACTIVATED CARBON FROM ION EXCHANGE RESIN WASTE AND ITS APPLICATION FOR MANGANESE REMOVAL FROM GROUNDWATER

A. Swelam, Y. Gedamy, A. El.shahed
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Abstract

The present study aims to synthesize an activated carbon adsorbent (S-AC, P-AC and OH-AC) from polystyrene divinyl benzene waste under different carbonization temperature (450oC and 900 oC and activation conditions (H2SO4, H3PO4 or NaOH). It being characterized and applied as an adsorbent for manganese removal from groundwater. FTIR results indicate that the changes in the peak intensities clear that the binding process was occurring on the surface of the adsorbent. Different factors such as solution pH, adsorbent dosage, contact time, temperature and Mn(II) initial concentration were investigated. The results showed that manganese adsorption capacity decreases with the increase of the carbonization temperature (900oC) and of activating agent H2SO4 > H3PO4 >NaOH. Kinetically, it was shown that the activation temperature of 450oC is the best temperature for activating the adsorbent carbons. The pseudo-first-order model is appropriate for predicting the adsorption process of Mn(II) onto the P-AC 450oC, P-AC 900oC and OH-AC 900oC, while the pseudo-second-order model is appropriate for predicting the adsorption process of Mn(II) onto the both S-AC 450oC, S-AC 900oC, OH-AC 450oCand OH-AC 900oC. Thermodynamic calculations affirmed that Mn(II) adsorption onto S-AC and P-AC was an endothermic process while onto OH-AC was exothermic process. Finally, the results suggested that the prepared S-AC has high adsorption capacities for Mn(II) compared with other adsorbents, such as P-AC and OH-AC. Therefore, S-AC 450oCcan be used in the groundwater treatment unit.
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离子交换树脂废渣制备活性炭及其在地下水除锰中的应用
本研究以聚苯乙烯二乙烯苯废料为原料,在不同的炭化温度(450℃和900℃)和活化条件(H2SO4、H3PO4或NaOH)下合成活性炭吸附剂(S-AC、P-AC和OH-AC)。对其进行了表征,并将其作为一种吸附剂用于去除地下水中的锰。FTIR结果表明,峰强度的变化清楚地表明结合过程发生在吸附剂表面。考察了溶液pH、吸附剂投加量、接触时间、温度和Mn(II)初始浓度等因素的影响。结果表明:随着炭化温度(900℃)和活化剂H2SO4 > H3PO4 >NaOH的升高,锰的吸附量减小;动力学结果表明,450℃的活化温度是吸附炭活化的最佳温度。拟一阶模型适用于预测Mn(II)在P-AC 450oC、P-AC 900oC和OH-AC 900oC上的吸附过程,拟二阶模型适用于预测Mn(II)在S-AC 450oC、S-AC 900oC、OH-AC 450oC和OH-AC 900oC上的吸附过程。热力学计算证实了Mn(II)在S-AC和P-AC上的吸附是吸热过程,而在OH-AC上的吸附是放热过程。结果表明,与P-AC和OH-AC等吸附剂相比,制备的S-AC对Mn(II)具有较高的吸附能力。因此,S-AC 450oc可用于地下水处理机组。
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