2013
DOI: 10.1016/j.fuproc.2013.02.016
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Steam-CO2 reforming of methane on Ni/γ-Al2O3-deposited metallic foam catalyst for GTL-FPSO process

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Cited by 32 publications
(14 citation statements)
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“…There are some indications that an appropriate selection of reaction parameters is necessary to establish these promising properties. Recently, Park et al [133] applied the same synthetic procedure for a 20 wt.% Ni/γ-Al 2 O 3 foam catalyst and studied its activity for 50 h using a space velocity of 130,000 h À1 at 850°C. The initial conversions of methane and carbon dioxide were 75% and 25%, respectively.…”
Section: Effect Of Structured Catalysts (Foams Monoliths and Wires)mentioning
confidence: 99%
“…There are some indications that an appropriate selection of reaction parameters is necessary to establish these promising properties. Recently, Park et al [133] applied the same synthetic procedure for a 20 wt.% Ni/γ-Al 2 O 3 foam catalyst and studied its activity for 50 h using a space velocity of 130,000 h À1 at 850°C. The initial conversions of methane and carbon dioxide were 75% and 25%, respectively.…”
Section: Effect Of Structured Catalysts (Foams Monoliths and Wires)mentioning
confidence: 99%
“…BRM is a potential replacement for other conventional reforming processes. [6][7][8] The BRM reaction mainly consists of steam methane reforming SMR (Equation [2]), water gas shift, WGS (Equation [3]) reaction, and dry methane reforming, DMR (Equation [4]). 9 BRM:…”
Section: Introductionmentioning
confidence: 99%
“…12,13 Partial oxidation of methane is an energy-saving exothermic reaction and it has attracted much attention. [14][15][16][17][18][19][20] However, many issues such as difficult to control, easilyproduced hot spots and the associated dangers of explosion limit the large-scale application of combined reforming processes involving partial oxidation reforming. Steam-CO 2 bireforming of methane has been considered as a judicious approach for potential industrial application in synthesis gas production as the H 2 /CO ratio can be easily adjusted by controlling the H 2 O/CO 2 ratio in the feed and the catalyst has an improved coke-resistance due to the introduction of steam.…”
Section: Introductionmentioning
confidence: 99%