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Enhanced abatement of aqueous organic compounds using stratified activated carbon adsorption columns.

机译:使用分层的活性炭吸附柱增强了水性有机化合物的减排。

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摘要

The feasibility of adsorptive removal of single component organic compounds (namely para-chlorophenol and Acid Blue 25) by Calgon Filtrasorb 400 (F400) carbon has been investigated. The Redlich-Peterson and Langmuir isotherm models were found to be the best fit models for describing the equilibrium relationship between the para-chlorophenol and Acid Blue 25 adsorption onto F400 carbon respectively.The agitated batch adsorption data proved that the smaller F400 carbons possessed faster adsorption rates compared to the larger F400 carbons. The two resistance Crank diffusion model was used to predict the batch adsorption data, and provide an estimate of the constant surface diffusivity for use in the Film Homogeneous Surface Diffusion Model implemented for the dynamic adsorption of organics onto F400 carbon in fixed-bed adsorption columns.Four adsorption columns with different column geometry and adsorbent particle stratification are used to examine the dynamic organics adsorption onto F400 carbons. The Bed Depth Service Time (BDST) model is applied and modified to analyse the performance of the columns and the effect of different operating variables. The Film Homogeneous Surface Diffusion Model (FHSDM), which incorporates the film mass transfer and surface controlled diffusion, was applied to describe the organics adsorption mass transfer process within the porous F400 carbons accurately. The FHSDM was found to correlate the breakthrough curves well for para-chlorophenol/F400 carbon and reasonably well for Acid Blue 25/F400 carbon.When combining the effects of adsorption efficiency and the associated pressure drop of each type of adsorption columns tested, the carbon stratified tapered column has been determined to be the most efficient engineering option for removing organics, in which the enhancement of the adsorbent bed in terms of longer breakthrough time and higher saturation percentage is the greatest amongst the four types of columns with reasonably small pressure drop across the fixed-bed column.
机译:已经研究了通过卡尔冈·菲尔塔吸收400(F400)碳吸附去除单组分有机化合物(即对氯苯酚和酸性蓝25)的可行性。发现Redlich-Peterson和Langmuir等温线模型是描述对氯苯酚和酸性蓝25分别吸附在F400碳上的平衡关系的最佳拟合模型。搅拌分批吸附数据表明,较小的F400碳具有更快的吸附与较大的F400碳相比。使用两个电阻的Crank扩散模型来预测批吸附数据,并提供恒定表面扩散率的估计,以用于在固定床吸附塔中将有机物动态吸附到F400碳上的膜均质表面扩散模型中。使用具有不同塔几何形状和吸附剂颗粒分层的四个吸附塔来检查动态有机物在F400碳上的吸附。应用和修改了床深服务时间(BDST)模型,以分析色谱柱的性能以及不同操作变量的影响。膜均质表面扩散模型(FHSDM)结合了膜的质量转移和表面控制的扩散,被用来准确描述多孔F400碳中有机物的吸附质量转移过程。 FHSDM被发现与对氯苯酚/ F400碳的穿透曲线有很好的相关性,与酸性蓝25 / F400碳的穿透曲线有很好的相关性。当结合吸附效率的影响和每种测试的吸附柱的相关压降时,碳分层的锥形塔被认为是去除有机物的最有效的工程选择,其中在更长的穿透时间和更高的饱和度方面,吸附床的增强在四种类型的塔中具有最大的压降。固定床色谱柱。

著录项

  • 作者

    Sze, Fan Fu.;

  • 作者单位

    Hong Kong University of Science and Technology (Hong Kong).;

  • 授予单位 Hong Kong University of Science and Technology (Hong Kong).;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 2009
  • 页码 293 p.
  • 总页数 293
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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