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首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Volumetric Adsorption Measurements of N2, CO2, CH4, and a CO2 + CH4 Mixture on a Natural Chabazite from (5 to 3000) kPa
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Volumetric Adsorption Measurements of N2, CO2, CH4, and a CO2 + CH4 Mixture on a Natural Chabazite from (5 to 3000) kPa

机译:天然菱沸石上(5至3000)kPa的N2,CO2,CH4和CO2 + CH4混合物的体积吸附测量

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We report here measured adsorption capacities for a natural chabazite zeolite at pressures ranging from (5 to 3000) kPa, at temperatures of (244 and 305) K, for pure N2, CH4, and CO2, and for gas mixtures of CH4 + CO2. The pure gas data sets from this work and from the literature were in good agreement (10 %) and were regressed to Toth models over a wide range of pressure and temperature. We show that extrapolation of models that were fit only to low pressure data (below 120 kPa) can lead to a 30 % deviation in adsorption capacities predicted at high pressures. Similarly, models fit only to high pressure pure fluid data resulted in unreliable predictions for mixture adsorption capacities particularly when the component's partial pressure was low. The experimental results indicate that, while the chabazite is unlikely to be useful for N2/CH4 separation, it may have potential for removing bulk CO2 from natural gas, particularly at low temperatures. A feed gas mixture of 0.95CH4 + O.OSCO2 placed in contact with the chabazite resulted in equilibrium vapor phases with CO2mole fractions of about (0.0013 and 0.0002) at (305 and 244) K, respectively. The ideal adsorbed solution theory was used to successfully describe the observed mixture behavior, although it was found to be sensitive to the data range over which the pure fluid models were regressed.
机译:我们在这里报告了在温度(244和305)K,纯N2,CH4和CO2以及CH4 + CO2的混合气体中,天然菱沸石沸石在(5至3000)kPa压力下测得的吸附容量。来自这项工作和文献的纯气体数据集吻合良好(10%),并在很大的压力和温度范围内回归到Toth模型。我们表明,仅适用于低压数据(低于120 kPa)的模型的外推法可能会导致在高压下预测的吸附容量发生30%的偏差。同样,仅适用于高压纯流体数据的模型导致对混合物吸附能力的预测不可靠,尤其是在组件的分压较低时。实验结果表明,菱沸石虽然不太可能用于分离N2 / CH4,但可能具有从天然气中去除大量CO2的潜力,尤其是在低温下。放置在与菱沸石接触的0.95CH4 + O.OSCO2的进料气体混合物中,在(305和244)K时,CO2摩尔分数分别约为(0.0013和0.0002)的平衡气相。理想的吸附溶液理论用于成功描述观察到的混合物行为,尽管发现它对纯流体模型回归的数据范围很敏感。

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