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基于碳的吸附剂和活性氧化铝对亚硒酸盐吸附的对比研究。

Comparative study of selenite adsorption on carbon based adsorbents and activated alumina.

作者信息

Jegadeesan G, Mondal K, Lalvani S B

机构信息

Dept. of Mechanical Engineering and Energy Process, Southern Illinois University, Mail code 6603 Carbondale, IL 62901, USA.

出版信息

Environ Technol. 2003 Aug;24(8):1049-59. doi: 10.1080/09593330309385644.

Abstract

The sorption characteristics of carbon-based adsorbents such as activated carbon and chitin for the removal of selenite, Se (IV), an anionic, hazardous contaminant, are compared with those of alpha and gamma alumina. Batch experiments were conducted to determine the influence of pH, concentration of adsorbate, adsorbent loading and temperature on the sorption characteristics of the adsorbents. Generally, low pH of the solution resulted in favorable selenium removal. With the exception of activated carbon, uptakes decreased with increase in temperature. In comparison, chitin was found to be far less effective for the removal of Se (IV) from aqueous solutions. The data also showed that gamma alumina provided higher selenium removal percentages (99%) compared to alpha alumina (94%), activated carbon (87%) and chitin (49%). The selenite removal was found to decrease with increasing initial Se (IV) concentration in the solution. Adsorption capacities of the adsorbents are reported in terms of their Langmuir adsorption isotherms. The adsorption capacity (on unit mass basis) of the adsorbents for selenite is in the order: chitin (specific area (sa) = 9.58 m2 g(-1)) < activated carbon (sa = 96.37 m2 g(-1)) < alpha alumina (sa = 6 m2 g(-1)) < gamma alumina (sa = 150 m2 g(-1)).

摘要

将活性炭和甲壳素等碳基吸附剂用于去除亚硒酸盐(Se(IV),一种阴离子型有害污染物)的吸附特性,与α-氧化铝和γ-氧化铝的吸附特性进行了比较。进行了批量实验,以确定pH值、吸附质浓度、吸附剂负载量和温度对吸附剂吸附特性的影响。一般来说,溶液的低pH值有利于硒的去除。除活性炭外,吸附量随温度升高而降低。相比之下,发现甲壳素从水溶液中去除Se(IV)的效果要差得多。数据还表明,与α-氧化铝(94%)、活性炭(87%)和甲壳素(49%)相比,γ-氧化铝的硒去除率更高(99%)。发现随着溶液中初始Se(IV)浓度的增加,亚硒酸盐的去除率降低。吸附剂的吸附容量根据其朗缪尔吸附等温线进行报告。吸附剂对亚硒酸盐的吸附容量(以单位质量计)顺序为:甲壳素(比表面积(sa)=9.58 m2 g(-1))<活性炭(sa = 96.37 m2 g(-1))<α-氧化铝(sa = 6 m2 g(-1))<γ-氧化铝(sa = 150 m2 g(-1))。

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