Comparison of packed bed and fluidized bed membrane reactors for methane
reforming

F. Gallucci; M. van Sint Annaland; J.A.M. Kuipers

Comparison of packed bed and fluidized bed membrane reactors for methane reforming

F. Gallucci, M. van Sint Annaland, J.A.M. Kuipers

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Abstract

In this work the performance of different membrane reactor concepts, both fluidized bed and packed bed membrane reactors, have been compared for the reforming of methane for the production of ultra-pure hydrogen. Using detailed theoretical models, the required membrane area to reach a given conversion and the prevailing temperature profiles have been compared. The extent of mass and heat transfer limitations in the different reactors have been evaluated, and strategies to decrease (or avoid) these limitations have been proposed.

Original language	English
Number of pages	6
Publication status	Published - 2009
Event	6th International Symposium on Multiphase Flow, Heat Mass Transfer and Energy Conversion, ISMF 2009: Proceedings of the International Symposium of Multiphase Flows - Xi'an, China, China Duration: 11 Jul 2009 → 15 Jul 2009 Conference number: 6

Conference

Conference	6th International Symposium on Multiphase Flow, Heat Mass Transfer and Energy Conversion, ISMF 2009
Abbreviated title	ISMF
Country/Territory	China
City	Xi'an, China
Period	11/07/09 → 15/07/09

Keywords

IR-67394

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comparison

Cite this

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abstract = "In this work the performance of different membrane reactor concepts, both fluidized bed and packed bed membrane reactors, have been compared for the reforming of methane for the production of ultra-pure hydrogen. Using detailed theoretical models, the required membrane area to reach a given conversion and the prevailing temperature profiles have been compared. The extent of mass and heat transfer limitations in the different reactors have been evaluated, and strategies to decrease (or avoid) these limitations have been proposed.",

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AU - van Sint Annaland, M.

AU - Kuipers, J.A.M.

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AB - In this work the performance of different membrane reactor concepts, both fluidized bed and packed bed membrane reactors, have been compared for the reforming of methane for the production of ultra-pure hydrogen. Using detailed theoretical models, the required membrane area to reach a given conversion and the prevailing temperature profiles have been compared. The extent of mass and heat transfer limitations in the different reactors have been evaluated, and strategies to decrease (or avoid) these limitations have been proposed.

KW - IR-67394

M3 - Paper

T2 - 6th International Symposium on Multiphase Flow, Heat Mass Transfer and Energy Conversion, ISMF 2009

Y2 - 11 July 2009 through 15 July 2009

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