2018
DOI: 10.1016/j.ijhydene.2018.02.194
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Hydrogen production by water-gas shift reaction over Co-promoted MoS2/Al2O3 catalyst: The intrinsic activities of Co-promoted and unprompted sites

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Cited by 12 publications
(6 citation statements)
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“…Recently, Alamolhoda et al worked on understanding the synergetic effect between nickel and cerium as catalysts in WGS reaction, and reported the use of low percentage loading (0-3 wt%) of cerium and nickel as dispersed phases on MFI framework [102]. According to the results, the cerium only catalysts had shown no sign of reaction, whereas the single metal Ni-MFI series catalysts successfully activated the CO.…”
Section: Transition Metal Catalystsmentioning
confidence: 99%
See 1 more Smart Citation
“…Recently, Alamolhoda et al worked on understanding the synergetic effect between nickel and cerium as catalysts in WGS reaction, and reported the use of low percentage loading (0-3 wt%) of cerium and nickel as dispersed phases on MFI framework [102]. According to the results, the cerium only catalysts had shown no sign of reaction, whereas the single metal Ni-MFI series catalysts successfully activated the CO.…”
Section: Transition Metal Catalystsmentioning
confidence: 99%
“…The prepared Ni-Ce-MFI succession had together speeded up the WGSR even at a low temperature of 503 K, and in some cases, the equilibrium conversion was achieved at temperatures less than 548 K. The presence of ceria is believed to provide the oxygen required for promoting nickel activity, which was clear from the TPR profile requiring lower temperature for nickel reduction in Ni-Ce-MFI catalysts. The lowest reduction temperature was observed when Ni and Ce were present in equal weight percentages [102]. Iriarte-Velasco et al used calcined pork bone, composed mainly of hydroxyapatite (HAp), as support for transition metals for WGSR [103].…”
Section: Transition Metal Catalystsmentioning
confidence: 99%
“…For instance, MoS 2 shows a WGS conversion rate of 3 × 10 17 molecules per cm 2 per s at 733 K in the presence of 2500 ppm H 2 S, which compares most favorably with the rates obtained with chromia-alumina and iron oxidechromia catalysts. 17 The performance of MoS 2 catalysts can be further enhanced by doping 3d transition metals in highly sulfided feeds at 575-675 K. 18 MoS 2 edges are generally believed to be the active sites for a number of catalytic reactions, while the (001) basal plane with the largest site density is generally inert. [6][7][8][9][10][11][12][13][14][15] To capitalize on the site abundance, numerous studies have been devoted to modify the basal plane by creating S vacancies or doping specific transition metals (M).…”
Section: Introductionmentioning
confidence: 99%
“…For instance, MoS 2 shows a WGS conversion rate of 3 × 10 17 molecules per cm 2 per s at 733 K in the presence of 2500 ppm H 2 S, which compares most favorably with the rates obtained with chromia–alumina and iron oxide–chromia catalysts. 17 The performance of MoS 2 catalysts can be further enhanced by doping 3d transition metals in highly sulfided feeds at 575–675 K. 18…”
Section: Introductionmentioning
confidence: 99%
“…Since the intrinsic activities of the active sites can be tuned by modulating the electronic structure, it is highly desirable for designing efficient catalysts for WGSR by introducing transition metals into MoS 2 to replace Mo without sacrificing the sulfur sites. However, to our knowledge, there are only a few reports about using doped MoS 2 for WGSR, let alone the systemic study of electronic modulating in MoS 2 for WGSR …”
mentioning
confidence: 99%