Catalytic pyrolysis-gasification of waste tire and tire elastomers for hydrogen production (Record no. 172014)

MARC details
000 -LEADER
fixed length control field 02217nab a2200205 4500
008 - CÓDIGOS DE INFORMACIÓN DE LONGITUD FIJA - INFORMACIÓN GENERAL
Campo de control de longitud fija 260224s2010 xxu
245 00 - TITULO
Título Catalytic pyrolysis-gasification of waste tire and tire elastomers for hydrogen production
260 ## - PUBLICACION, DISTRIBUCION, ETC
Lugar de publicación, distribución, etc.
Nombre de publicador, distribuidor, etc.
Fecha de publicación, distribución, etc. jul./ago. 2010
270 ## - FECHA DE CARGA
Fecha de carga 19/11/2010 ; 19/11/2010
300 ## - DESCRIPCION FISICA
Otra extensión 8 p. ; 3928-3935
520 ## - RESUMEN, ETC
Resumen Transcripción del resumen del autor. Hydrogen production from waste tires was investigated using a two-stage pyrolysis-gasification reactor and Ni-Mg-Al (1:1:1) as a catalyst. In addition, the elastomer constituents most commonly used in tires, natural rubber (NR), styrene-butadiene rubber (SBR), and butadiene rubber (BR), were also investigated. Experiments were conducted at a pyrolysis temperature of 500 °C and gasification temperature of 800 °C. The results showed that the gas and hydrogen yield were increased for the tire and elastomer constituents during pyrolysis-gasification. However, there was a dramatic increase in H2 and CO concentrations as well as a consequent decrease in CH4 and C2-C4 concentrations when the Ni-Mg-Al catalyst was applied to the pyrolysis-gasification process. For example, hydrogen production increased from 0.68 to 5.43 wt % for the catalytic steam pyrolysis-gasification of waste tire in the presence of Ni-Mg-Al catalyst. The highest hydrogen production (15.26 wt %) was obtained for the BR feedstock. Reacted catalysts were characterized using a variety of methods, including temperature-programmed oxidation (TPO) and scanning electron microscopy (SEM) with energy dispersive X-ray spectrometry (EDXS). The SEM results showed that large amounts of filamentous carbons were observed for the reacted Ni-Mg-Al catalysts derived from all the feedstocks. The total amount of coke deposition on the reacted catalyst, calculated from TPO experiments, was lowest for the BR feedstock (7.0 wt %) and was 31, 21.8, and 18.4 wt % for the waste tire, NR, and SBR samples, respectively.
581 ## - ESTADO DE COLECCIÓN
Estado de colección 4
773 0# - CORRECCIÓN
Título Energy & fuels
Partes relacionadas 24
942 ## - DESC. DE MATERIAL
Tipo de item KOHA Artículo de Revista
100 1# - RESPONSABLE PERSONAL
Apellido, Nombre Elbaba, Ibrahim F.
9 (RLIN) 43728
100 1# - RESPONSABLE PERSONAL
Apellido, Nombre Wu, Chunfei
9 (RLIN) 43729
100 1# - RESPONSABLE PERSONAL
Apellido, Nombre Williams, Paul T.
9 (RLIN) 43730
Holdings
Biblioteca propietaria Biblioteca actual Fecha de adquisición Inventario Total de préstamos Inventario Fecha de carga Tipo de item KOHA
Biblioteca Alejandro Angel Bulgheroni Biblioteca Alejandro Angel Bulgheroni 05/03/2026 200049982   200049982 05/03/2026 Artículo de Revista


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