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Hydrogen production from a victorian brown coal with in situ CO2 capture in a 1 kWth dual fluidized-bed gasification r / Hui An in Industrial & engineering chemistry research, Vol. 51 N° 40 (Octobre 2012) 

Public ISBD [article]  in Industrial & engineering chemistry research > Vol. 51 N° 40 (Octobre 2012) . - pp. 13046–13053 Titre : Hydrogen production from a victorian brown coal with in situ CO2 capture in a 1 kWth dual fluidized-bed gasification r Type de document : texte imprimé Auteurs : Hui An, Auteur ; Tao Song, Auteur ; Laihong Shen, Auteur Année de publication : 2012 Article en page(s) : pp. 13046–13053 Note générale : Industrial chemistry Langues : Anglais (eng) Mots-clés : Hydrogen  Gasification Résumé : The removal of CO2 during coal gasification will improve H2 yield by promoting coal gasification reactions toward the production of H2. In this work, coal gasification with in situ CO2 capture has been investigated in a 1 kWth dual fluidized-bed gasification reactor. A Victorian brown coal was used as the feed stock. Coal gasification tests at 700 °C were performed with silica sands as the heat carrier and synthetic CaO sorbent for comparison. It was found that the addition of the sorbent improved H2 concentration in the outlet of the fuel reactor by nearly 53%. Carbon conversion rate was also increased and a maximum of 33% was reported. Calcium aluminate cement was used as a binder for the fabrication of the synthetic CaO sorbent, in an attempt to enhance its mechanical strength and improve its chemical properties. ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie300747m [article] Hydrogen production from a victorian brown coal with in situ CO2 capture in a 1 kWth dual fluidized-bed gasification r [texte imprimé] / Hui An, Auteur ; Tao Song, Auteur ; Laihong Shen, Auteur . - 2012 . - pp. 13046–13053. Industrial chemistry Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 51 N° 40 (Octobre 2012) . - pp. 13046–13053 Mots-clés : Hydrogen  Gasification Résumé : The removal of CO2 during coal gasification will improve H2 yield by promoting coal gasification reactions toward the production of H2. In this work, coal gasification with in situ CO2 capture has been investigated in a 1 kWth dual fluidized-bed gasification reactor. A Victorian brown coal was used as the feed stock. Coal gasification tests at 700 °C were performed with silica sands as the heat carrier and synthetic CaO sorbent for comparison. It was found that the addition of the sorbent improved H2 concentration in the outlet of the fuel reactor by nearly 53%. Carbon conversion rate was also increased and a maximum of 33% was reported. Calcium aluminate cement was used as a binder for the fabrication of the synthetic CaO sorbent, in an attempt to enhance its mechanical strength and improve its chemical properties. ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie300747m