2005
DOI: 10.1016/j.apcata.2005.02.020
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Catalytic activities and coking resistance of Ni/perovskites in steam reforming of methane

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Cited by 176 publications
(78 citation statements)
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“…In addition, the obtained BTOSiO 2 catalyst was applied to methane steam reforming. 5) Results show that the methane conversion ratio of this material was approximately three times as large as that of the reported BTO catalyst, 4) even at a lower processing temperature. However, the temperature limit of this material was 600°C because of the generation of Ba 2 (TiO)Si 2 O 7 phase during steam reforming, which is attributable to the diffusion of Ba component to SiO 2 core particles during the process.…”
Section: )2)mentioning
confidence: 89%
See 1 more Smart Citation
“…In addition, the obtained BTOSiO 2 catalyst was applied to methane steam reforming. 5) Results show that the methane conversion ratio of this material was approximately three times as large as that of the reported BTO catalyst, 4) even at a lower processing temperature. However, the temperature limit of this material was 600°C because of the generation of Ba 2 (TiO)Si 2 O 7 phase during steam reforming, which is attributable to the diffusion of Ba component to SiO 2 core particles during the process.…”
Section: )2)mentioning
confidence: 89%
“…Lately, Ni on perovskite material (Ni/Perovskite) has received much attention as a catalyst for methane steam reforming and partial oxidation of CH 4 .…”
Section: )2)mentioning
confidence: 99%
“…50,87 A presença desses compostos deve-se à ocorrência do craqueamento da carga em altas temperaturas, podendo levar à formação de produtos primários (>C5), hidrocarbonetos secundários (C1-C4), além de coque. 46 52,89 Adicionalmente, os estudos mostraram que a adição de 10 %m/m de naftaleno em solução de tolueno causou uma redução acentuada na conversão do tolueno, pois o naftaleno se adsorve mais fortemente que o tolueno, prejudicando a conversão deste último. 90 A Figura 4 ilustra o tipo de coque formado na reação de reforma a vapor de naftaleno/tolueno a 800 °C, com razão V/C = 1,5.…”
Section: Catalisadores Metálicosunclassified
“…One approach to solve these problems is to highly disperse the active species, which improves apparent catalytic activity and enhances the reactivity of possible intermediate carbonaceous species in the reforming reactions. Supported base metal catalysts with high dispersion have been prepared using uniform mixed oxide materials such as hexaaluminates, hydrotalcites, and perovskites Urasaki et al, 2005;Li et al, 2009). In this study, nickel-containing spinel-type oxide catalysts were developed for methane and propane steam reforming, and nitrous oxide titration was used for the first time for the characterization of nickel surface area of the spinel-based catalysts.…”
Section: Introductionmentioning
confidence: 99%