Influence of Cs Loading on Pt/m-ZrO2 Water–Gas Shift Catalysts

dc.contributor.authorRajabi, Zahra
dc.contributor.authorMartinelli, Michela
dc.contributor.authorWatson, Caleb D.
dc.contributor.authorCronauer, Donald C.
dc.contributor.authorKropf, A. Jeremy
dc.contributor.authorJacobs, Gary
dc.date.accessioned2021-06-10T13:47:00Z
dc.date.available2021-06-10T13:47:00Z
dc.date.issued2021-04-29
dc.date.updated2021-06-10T13:47:02Z
dc.description.abstractCertain alkali metals (Na, K) at targeted loadings have been shown in recent decades to significantly promote the LT-WGS reaction. This occurs at alkali doping levels where a redshift in the C-H band of formate occurs, indicating electronic weakening of the bond. The C-H bond breaking of formate is the proposed rate-limiting step of the formate associative mechanism, lending support to the occurrence of this mechanism in H2-rich environments of the LT-WGS stage of fuel processors. Continuing in this vein of research, 2%Pt/m-ZrO2 was promoted with various levels of Cs in order to explore its influence on the rate of formate intermediate decomposition, as well as that of LT-WGS in a fixed bed reactor. In situ DRIFTS experiments revealed that Cs promoter loadings of 3.87% to 7.22% resulted in significant acceleration of the forward formate decomposition in steam at 130 °C. Of all of the alkali metals tested to date, the redshift in the formate ν(CH) band with the incorporation of Cs was the greatest. XANES difference experiments at the Pt L2 and L3 edges indicated that the electronic effect was not likely due to an enrichment of electronic density on Pt. CO2 TPD experiments revealed that, unlike Na and K promoters, Cs behaves more like Rb in that the decomposition of the second intermediate in LT-WGS, carbonate species, is hindered due to (1) increased basicity of Cs, (2) the tendency of Cs to cover Pt sites that facilitate CO2 decomposition, and (3) the tendency of Cs to increase Pt particle size as shown by EXAFS results, resulting in fewer Pt sites that facilitate CO2 decomposition. As such, the LT-WGS rate was hindered overall and the rate-limiting step shifted to carbonate decomposition (CO2 removal). Like its Rb counterpart, low levels of added Cs (e.g., 0.72%Cs) were found to improve the stability of the catalyst relative to the unpromoted catalyst; the stability comparison was made at similar CO conversion level as well as similar space velocity.
dc.description.departmentBiomedical Engineering and Chemical Engineering
dc.description.departmentMechanical Engineering
dc.identifierdoi: 10.3390/catal11050570
dc.identifier.citationCatalysts 11 (5): 570 (2021)
dc.identifier.urihttps://hdl.handle.net/20.500.12588/617
dc.rightsAttribution 4.0 United States
dc.rights.urihttps://creativecommons.org/licenses/by/4.0/
dc.subjectcesium (Cs)
dc.subjectplatinum (Pt)
dc.subjectzirconia (ZrO2)
dc.subjectlow-temperature water–gas shift (LT-WGS)
dc.subjectalkali promotion
dc.subjectelectronic effect
dc.subjectformate
dc.subjectassociative mechanism
dc.subjecthydrogen
dc.titleInfluence of Cs Loading on Pt/m-ZrO2 Water–Gas Shift Catalysts
dc.typeArticle

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