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分层活性炭吸附柱增强对对氯苯酚的去除。

Enhanced mitigation of para-chlorophenol using stratified activated carbon adsorption columns.

机构信息

Department of Chemical and Biomolecular Engineering, The Hong Kong University of Science and Technology, Clear Water Bay, Kowloon, Hong Kong.

出版信息

Water Res. 2012 Mar 1;46(3):700-10. doi: 10.1016/j.watres.2011.11.039. Epub 2011 Nov 19.

DOI:10.1016/j.watres.2011.11.039
PMID:22154109
Abstract

The adsorptive removal of toxic para-chlorophenol using activated carbon adsorption columns is a proven effective engineering process. This paper examined the possibility to stratify an adsorbent bed into layers, in order to enhance the adsorption process performance in terms of increased column service time and adsorbent bed saturation. Four different types of fixed-bed adsorption columns are used and compared under the same operating conditions, but with the variation of column geometry and activated carbon particle size stratification. The Type 3 column - a cylindrical column with particle stratification packing, is found to be the most efficient choice, as the extent of column service time and adsorbent bed saturation are the largest. This could eventually decrease the frequency of adsorbent replacement/regeneration and hence reduce the operating cost of the fixed-bed adsorption process. The Homogeneous Surface Diffusion Model (HSDM) was applied successfully to describe the dynamic adsorption of para-chlorophenol onto Filtrasorb 400 (F400) activated carbon in different types of columns. The Redlich-Peterson isotherm model equation, an experimentally derived external mass transfer correlation and a constant surface diffusivity are used in the HSDM. The optimised surface diffusivity of para-chlorophenol is found to be 1.20E-8 cm(2)/s, which is in good agreement with other phenolics/F400 carbon diffusing systems in literature.

摘要

采用活性炭吸附柱吸附去除有毒对氯苯酚是一种经过验证的有效工程工艺。本文研究了将吸附剂床分层的可能性,以提高吸附过程的性能,延长柱的使用寿命和增加吸附剂床的饱和度。在相同的操作条件下,使用了四种不同类型的固定床吸附柱进行比较,但柱几何形状和活性炭粒径分层有所不同。结果表明,类型 3 柱——一种具有颗粒分层填充的圆柱形柱,是最有效的选择,因为柱的使用寿命和吸附剂床的饱和度最大。这最终可以减少吸附剂更换/再生的频率,从而降低固定床吸附过程的运行成本。均相表面扩散模型 (HSDM) 成功地应用于描述不同类型柱中对氯苯酚在 Filtrasorb 400(F400)活性炭上的动态吸附。在 HSDM 中使用了 Redlich-Peterson 等温模型方程、实验得出的外部传质关联和恒定的表面扩散系数。优化后的对氯苯酚表面扩散系数为 1.20E-8 cm(2)/s,与文献中其他酚类/F400 碳扩散系统吻合较好。

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