http://www.cnr.it/ontology/cnr/individuo/prodotto/ID55521
Catalytic Decomposition of Natural Gas for COx-Free Hydrogen Production in a Structured Multilayer Reactor (Articolo in rivista)
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- Catalytic Decomposition of Natural Gas for COx-Free Hydrogen Production in a Structured Multilayer Reactor (Articolo in rivista) (literal)
- Anno
- 2009-01-01T00:00:00+01:00 (literal)
- Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#doi
- 10.1016/j.apcata.2009.01.004 (literal)
- Alternative label
Italiano G. ; Espro C. ; Arena F. ; Frusteri F. ; Parmaliana A. (2009)
Catalytic Decomposition of Natural Gas for COx-Free Hydrogen Production in a Structured Multilayer Reactor
in Applied catalysis. A, General (Print); ELSEVIER SCIENCE BV, PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS, AMSTERDAM (Paesi Bassi)
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- Italiano G. ; Espro C. ; Arena F. ; Frusteri F. ; Parmaliana A. (literal)
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- CNR-ITAE, Messina Italy ; Dipartimento di Chimica Industriale e Ingegneria dei Materiali, Universita` degli Studi di Messina (literal)
- Titolo
- Catalytic Decomposition of Natural Gas for COx-Free Hydrogen Production in a Structured Multilayer Reactor (literal)
- Abstract
- Using a new structured multilayer reactor (MLR) that houses Ni based thin layer catalysts, catalytic decomposition of natural gas (CDNG) for making ''COx-free'' hydrogen in a TR range of 773-873 K was investigated. The influence of Ni loading (5-50 wt%), Ni particle size, TR, and GHSV (h?1) on the reaction pattern was evaluated. A volcano shape relationship between H2 space time yield ðSTYH2 ; st p dm3 H2=kgNi=hÞ andNi loadingwith a maximumrange of 20-25 wt% was found.H2 productivity and catalyst lifetime are controlled by the nature of the coke formed on Ni active species. As such, TR and GHSV significantly affect both the kinetics and the mechanism of coking. At TR < 873 K and low GHSV (<2000 h?1), the prevailing formation of filamentous carbon (whisker-like) prolongs the catalyst lifetime, while at TR = 873 KandhighGHSV(>2000 h?1) incapsulatingcarbonis formed,causing a suddendecline in catalytic activity.Apreliminary attempt to findoptimal operating conditions ensuring the highest values of H2 productivity is presented. The features of theMLRthat allowedCDNGreaction under a quasi-isothermal regime without any pressure drop, irrespective of operating conditions and the extent of carbon formation, are discussed. (literal)
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