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Adsorption of organic compounds and water vapor on activated carbon: Equilibria and fixed-bed humidity steps.

机译:活性炭对有机化合物和水蒸气的吸附:平衡和固定床湿度步骤。

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Adsorption equilibrium and fixed-bed adsorption dynamics are the two major parts investigated experimentally and theoretically in this research.; In the first part, the Virial Excess Mixing Coefficient (VEMC) model was developed to describe nonideal multicomponent adsorption equilibrium. It treats a real adsorbed solution as an ideal adsorbed solution with an excess surface mixing correction. A new model was developed to describe pure water vapor adsorption equilibrium on activated carbon with higher accuracy than other models published to date. Another new model was developed to extend a single adsorption isotherm at one specific temperature to an adsorption isotherm family at multiple temperatures with a small number of parameters. Adsorption equilibria were measured for methyl ethyl ketone (MEK), methyl isobutyl ketone (MIBK) and toluene as pure components and binary mixtures with water vapor on BPL carbon. The experimental data were analyzed using the VEMC and the Virial Mixture Coefficient (VMC) models.; In the second part, fixed-bed breakthrough behavior was measured and investigated for pure water, single organics, and binary organic mixtures under humidity steps. Pure water adsorption kinetics was studied. A new model was developed to describe the water adsorbed-phase mass transfer coefficient as a function of water loading. A new algorithm was developed to optimize the system parameters in fixed-bed simulation by combining an ODE solver with a least-squares solver. For organic fixed-bed adsorption under humidity steps, the effects of organic chemical properties (e.g., hydrophilicity and volatility), concentration and molecular interactions on breakthrough curves were examined. A general mathematical model and a computer program were developed to simulate the fixed-bed dynamics. Predicted behavior is in good agreement with the experiments in time, trend, extent, and shape of breakthrough curves. The applicability and efficiency of regenerating an adsorption bed by humidity desorption were also evaluated. Humidity increases are effective in removing light components, particularly light hydrophobic components, from a bed of activated carbon. These components are typically design-limiting for trace contaminant control systems.
机译:吸附平衡和固定床吸附动力学是实验和理论研究的两个主要部分。在第一部分中,建立了Virial过量混合系数(VEMC)模型来描述非理想的多组分吸附平衡。它将真实的吸附溶液视为理想的吸附溶液,并进行了过量的表面混合校正。开发了一个新模型来描述活性炭上纯净水蒸气的吸附平衡,其准确性要高于迄今为止发布的其他模型。开发了另一种新模型,以一个参数在一个特定温度下将单个吸附等温线扩展到多个温度下的吸附等温线族。测量了作为纯组分的甲基乙基酮(MEK),甲基异丁基酮(MIBK)和甲苯的吸附平衡,以及与水蒸气在BPL碳上的二元混合物。使用VEMC和病毒混合物系数(VMC)模型分析实验数据。在第二部分中,测量并研究了在湿度步骤下纯水,单一有机物和二元有机混合物的固定床穿透行为。研究了纯水的吸附动力学。开发了一个新模型来描述水吸附相传质系数与水负荷的关系。通过结合ODE求解器和最小二乘求解器,开发了一种新算法来优化固定床仿真中的系统参数。对于在湿度步骤下进行的有机固定床吸附,研究了有机化学性质(例如亲水性和挥发性),浓度和分子相互作用对突破曲线的影响。开发了通用数学模型和计算机程序来模拟固定床动力学。预测的行为在时间,趋势,范围和突破曲线的形状方面与实验非常吻合。还评估了通过湿度解吸再生吸附床的适用性和效率。增加湿度可有效地从活性炭床中除去轻组分,特别是轻疏水组分。这些组件通常是痕量污染物控制系统的设计限制。

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