Abstract
Treatment of zeolite by the CVD method with TGA and fluidized bed reactor, it was possible to control overall the mass transfer coefficient for O2, N2, CO2 and CH4 into zeolite, that is, to control micropore entrance sizes. The control parameters were temperature, concentration, time of depositions and calcination method Possibility of mass production of modified zeolite with a fluidized bed reactor was demonstrated. The CVD method was very effective for modification of Na-A zeolite. Also, the potential energy barrier of the modified zeolite was higher than that of the original and that of O2 was lower than that of N2 in simulation. This means that the CVD modified model of zeolite 4A was simulated well.
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References
M.Niwa, S.Kato, T.Hattori and Y.Murakami, J.Chem.Soc., Faraday, Trans.l,80,pp.3135–3145(1984)
Cerius2 User’s Reference, Molecular Simulations Inc., 1994
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© 1996 Kluwer Academic Publishers
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Chihara, K., Sugizaki, K., Kato, N., Miyajima, H., Takeuchi, Y. (1996). Control of Adsorption Rate on Zeolite by Chemical Vapor Deposition. In: LeVan, M.D. (eds) Fundamentals of Adsorption. The Kluwer International Series in Engineering and Computer Science, vol 356. Springer, Boston, MA. https://doi.org/10.1007/978-1-4613-1375-5_21
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DOI: https://doi.org/10.1007/978-1-4613-1375-5_21
Publisher Name: Springer, Boston, MA
Print ISBN: 978-1-4612-8594-6
Online ISBN: 978-1-4613-1375-5
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