Simulation of Hydrogen and Propylene Coproduction in Catalytic Membrane Reactor Full article
| Journal |
International Journal of Hydrogen Energy
ISSN: 0360-3199 , E-ISSN: 1879-3487 |
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| Output data | Year: 2015, Volume: 40, Number: 8, Pages: 3592-3598 Pages count : 7 DOI: 10.1016/j.ijhydene.2014.09.004 | ||||
| Tags | Alkane dehydrogenation, Hydrogen production, Membrane reactor, Pore size distribution, Porous ceramic membrane | ||||
| Authors |
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Abstract:
A two-dimensional non isothermal mathematical model has been developed to simulate the propane dehydrogenation in a catalytic membrane reactor with tube-and-shell configuration. The permeable inner tube consists of an inert large-pore support and thin microporous membrane layer. The membrane removes hydrogen from reaction zone shifting the reaction equilibrium towards products. Both pores diameter and membrane thickness were varied to obtain the optimal membrane characteristics in terms of hydrogen and propylene productivity, and hydrogen purity. The model correctly predicted the improved process parameters when the membrane thickness was 4 μm and the pore diameter was 0.4 nm.
Cite:
Shelepova E.V.
, Vedyagin A.A.
, Mishakov I.V.
, Noskov A.S.
Simulation of Hydrogen and Propylene Coproduction in Catalytic Membrane Reactor
International Journal of Hydrogen Energy. 2015. V.40. N8. P.3592-3598. DOI: 10.1016/j.ijhydene.2014.09.004 WOS Scopus РИНЦ OpenAlex ANCAN
Simulation of Hydrogen and Propylene Coproduction in Catalytic Membrane Reactor
International Journal of Hydrogen Energy. 2015. V.40. N8. P.3592-3598. DOI: 10.1016/j.ijhydene.2014.09.004 WOS Scopus РИНЦ OpenAlex ANCAN
Dates:
| Submitted: | Jun 6, 2014 |
| Accepted: | Sep 2, 2014 |
| Published online: | Sep 26, 2014 |
| Published print: | Mar 1, 2015 |
Identifiers:
| ≡ Web of science: | WOS:000350939600049 |
| ≡ Scopus: | 2-s2.0-84922876546 |
| ≡ Elibrary: | 24008321 |
| ≡ OpenAlex: | W2002516653 |
| ≡ Chemical Abstracts: | 2014:1601574 |
| ≡ Chemical Abstracts (print): | 162:258801 |