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- W2022803822 abstract "Experimental concentration profiles obtained in the separation of H2 - D2 mixtures, by selective adsorption on charcoal in a moving-bed adsorber, were used to test the validity of semi-rigorous adsorber design equations based on considerations of gas film diffusion (utilizing the linear driving force concept), solid phase diffusion (utilizing Fick's law) and axial dispersion.The adsorption equilibrium data and solid phase diffusivities used in the design equations were also measured directly in separate experiments, whereas the gas film and axial diffusion values were evaluated from published data(3,0)In general, good agreement was obtained between the experimental and theoretically predicted concentration profiles, except at the lowest flow rates investigated.Les profils de concentration obtenus experimentalement dans la separation par adsorbtion selective sur un lit mobile de charbon, de melanges H2-D2, ont ete utilises pour verifier la validite d'une methode de calcul de colonnes d'adsorption. Cetto methode se fonde sur les concepts de diffusion du film gazeux (utilisant un gradient lineaire) de diffusion de la phase solide (utilisant la loi de Fick) et de dispersion axiale.Les donnees d'equilibre pour l'adsorption et les diffusivites de la phase solide utilisees dans les relations ont ete obtenues experimentalement alors que les valeurs de diffusion axiale et de diffusion du film gazeux ont ete evaluees selon la bibliographie.En general les profils de concentration experimentaux et theoriques sont en accord sauf pour les plus faibles debits utilises dans cette recherche." @default.
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- W2022803822 date "1963-12-01" @default.
- W2022803822 modified "2023-09-27" @default.
- W2022803822 title "The separation of H2 and D2 by moving-bed adsorption: Corroboration of adsorber design equations" @default.
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- W2022803822 doi "https://doi.org/10.1002/cjce.5450410609" @default.
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