Alcohols and bio-alcohols steam and autothermal reforming in a membrane reactor
Ver/Abrir
llibre (5,714Mb) (Acceso restringido)
Solicitud de copia al autor
Què és aquest botó?
Aquest botó permet demanar una còpia d'un document restringit a l'autor. Es mostra quan:
- Disposem del correu electrònic de l'autor
- El document té una mida inferior a 20 Mb
- Es tracta d'un document d'accés restringit per decisió de l'autor o d'un document d'accés restringit per política de l'editorial
Tipo de documentoCapítulo de libro
Fecha de publicación2014-11-28
Condiciones de accesoAcceso restringido por política de la editorial
Salvo que se indique lo contrario, los contenidos
de esta obra estan sujetos a la licencia de Creative Commons
:
Reconocimiento-NoComercial-SinObraDerivada 3.0 España
Resumen
Considerable work has been reported concerning catalytic steam reforming, partial oxidation and oxidative steam reforming (autothermal reforming) aimed at hydrogen generation from alcohol-water mixtures. They include methanol, ethanol, glycerol, and the exploitiation of renewable bio-alcohols. The use of catalytic membrane reactors, with simultaneous generation and separation of hydrogen, appears as an attractive approach to optimize downstream separation and to substantially simplify on-site/on-demand alcohol reformers. Catalytic membrane reactors reduce capital costs by combining the reforming process and hydrogen separation in one system, allow an enhancement of the alcohol conversion of the equilibrium-limited reforming processes, and are able to directly produce a high purity hydrogen stream for feeding fuel cells if dense Pd-based membranes are used. Considerable work has been reported concerning catalytic steam reforming, partial oxidation and oxidative steam reforming (autothermal reforming) aimed at hydrogen generation from alcohol-water mixtures. They include methanol, ethanol, glycerol, and the exploitiation of renewable bio-alcohols. The use of catalytic membrane reactors, with simultaneous generation and separation of hydrogen, appears as an attractive approach to optimize downstream separation and to substantially simplify on-site/on-demand alcohol reformers. Catalytic membrane reactors reduce capital costs by combining the reforming process and hydrogen separation in one system, allow an enhancement of the alcohol conversion of the equilibrium-limited reforming processes, and are able to directly produce a high purity hydrogen stream for feeding fuel cells if dense Pd-based membranes are used.
CitaciónLlorca, J., Hedayati, A. Alcohols and bio-alcohols steam and autothermal reforming in a membrane reactor. A: "Alcohols and bioalcohols". 2014, p. 181-204.
ISBN978-1-63321-934-2
Ficheros | Descripción | Tamaño | Formato | Ver |
---|---|---|---|---|
Book Jordi_Ali.pdf![]() | llibre | 5,714Mb | Acceso restringido |