2021
DOI: 10.1016/j.apcata.2020.117891
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Effect of Lanthanum Doping on the reactivity of unsupported CoMoS2 catalysts

Abstract: Highlights:  A triphasic La-Co-Mo sulfide HDS catalyst was successfully synthesized using solvothermal synthesis  LaCoMoS2 showed enhanced activity over CoMoS2 catalysts.  The LaCoMoS2 activity as improved with increasing La doping  LaCoMoS2 showed less carbon than CoMoS2 after once catalytic cycle.  The La doping of the CMoS2 catalyst led to improvement in the direct desulfurization pathway.

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Cited by 5 publications
(3 citation statements)
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“…The vapor pressure of water becomes a limiting factor and alterative solvents are to be explored for high temperature syntheses. In addition, the solvothermal process allows for the control of the phase, particle size, and morphology [124][125][126][127][128][129][130][131][132][133][134][135].…”
Section: Solvothermal Processesmentioning
confidence: 99%
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“…The vapor pressure of water becomes a limiting factor and alterative solvents are to be explored for high temperature syntheses. In addition, the solvothermal process allows for the control of the phase, particle size, and morphology [124][125][126][127][128][129][130][131][132][133][134][135].…”
Section: Solvothermal Processesmentioning
confidence: 99%
“…The authors successfully synthesized CdS nanowires at 180 • C, with diameters of 25 nm and lengths into the µm ranges, which showed controlled synthesis of CdS nanomaterials. Valdes et al on the other hand, synthesized nanosized CoMoS 2 doped with La ions for the desulfurization of fuels [135]. The authors prepared a CoMoS 4 precursor which was doped with different amounts of La ions to replace Co atoms from 5 to 25%.…”
Section: Solvothermal Processesmentioning
confidence: 99%
“…Hydrodesulfurization (HDS) is one of the most important catalytic processes in the petroleum industry to remove sulfur from organosulfur molecules such as dibenzothiophene (DBT), 2,8-dimethyldibenzothiophene (2,8-DMDBT), and 4,6-dimethyldibenzothiophene (4,6-DMDBT) from crude feed. , The most widely used catalysts in the HDS process are Al 2 O 3 -supported MoS 2 catalysts with Co or Ni as a promoter. Ni or Co promoters are preferred (1) because they lower sulfur vacancy formation energy in MoS 2 due to weaker bond energies of Ni–S/Co–S compared to Mo–S bond and (2) because of easier dissociation of molecular hydrogen. , The activities of promoted catalysts are influenced by many factors such as type of support, , pore size, poisoning of catalyst by undesirable atoms during synthesis, metal loading, and synergistic effect of dopants . Though most of the above influencing factors have been explored in detail, the effect of Na incorporation in Ni-promoted MoS 2 has not been investigated sufficiently despite the presence of a few reports. , In this regard, we would like to mention that the effects of other group IA (e.g., Li, K) and IIA (e.g.,Mg) metal dopants have been documented in the literature. …”
Section: Introductionmentioning
confidence: 99%