Abstract
The concentration vs time, or breakthrough, curves for a number of binary systems containing hydrogen have been measured on both charcoal [1] and a synthetic zeolite [2]. The equations proposed by Eagleton and Bliss [3] were applied to these breakthrough curves in order to evaluate a gas phase mass transfer coefficient k s and an adsorbed phase mass transfer coefficient k s .
Tabular values for all of the curves are available from the Cyogenie Data Center, NBS Institute for Basic Stadards, Bouder, Colo. 80302.
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Kidnay, A.J., Hiza, M.J., Dickson, P.F. (1995). Adsorption Kinetics in a Ternary System Containing Hydrogen. In: Timmerhaus, K.D. (eds) Advances in Cryogenic Engineering. Advances in Cryogenic Engineering, vol 15. Springer, Boston, MA. https://doi.org/10.1007/978-1-4757-0513-3_7
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DOI: https://doi.org/10.1007/978-1-4757-0513-3_7
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