Hydrogen production over Co-promoted Mo-S water gas shift catalysts supported on ZrO2

[Display omitted] •Co addition enhanced the WGS activity of Mo-S/ZrO2 catalysts.•The formation of CoMo-S species increased with Co content up to Co/Mo = 0.3.•CO conversion was stable during 4 weeks of WGS reaction in 7000 ppm H2S containing feed at 35,000 h−1 GHSV and 350 °C.•The optimal atomic Co/M...

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Veröffentlicht in:Applied catalysis. A, General General, 2020-01, Vol.590, p.117361, Article 117361
Hauptverfasser: Yun, SeongUk, Guliants, Vadim
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description [Display omitted] •Co addition enhanced the WGS activity of Mo-S/ZrO2 catalysts.•The formation of CoMo-S species increased with Co content up to Co/Mo = 0.3.•CO conversion was stable during 4 weeks of WGS reaction in 7000 ppm H2S containing feed at 35,000 h−1 GHSV and 350 °C.•The optimal atomic Co/Mo ratio at monolayer coverage on ZrO2 resulted in enhanced WGS activity.•The active metal loading in the best CoMo-S catalyst was lower than in pure Mo-S/ZrO2 and commercial catalysts. A series of CoMo-S/ZrO2 catalysts were prepared by modifying Co and Mo content using incipient wetness impregnation method, investigated in the water gas shift (WGS) reaction in the presence of H2S and characterized by TEM, XRD, Raman, TPR, and XPS. The supported CoMo-S catalyst corresponding to the CoMo-O monolayer coverage displayed the presence of highly dispersed CoMo-S species that were characterized by the highest extent of sulfidation. The presence of cobalt facilitated the formation of active CoMo-S species that were more H2S-dependent as compared to Mo-S entities. The Co/Mo = 0.3 catalyst at monolayer CoMo-O coverage was the most active and thermally stable, as well as the least H2S-dependent during 4 weeks of WGS reaction among all catalysts investigated.
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A series of CoMo-S/ZrO2 catalysts were prepared by modifying Co and Mo content using incipient wetness impregnation method, investigated in the water gas shift (WGS) reaction in the presence of H2S and characterized by TEM, XRD, Raman, TPR, and XPS. The supported CoMo-S catalyst corresponding to the CoMo-O monolayer coverage displayed the presence of highly dispersed CoMo-S species that were characterized by the highest extent of sulfidation. The presence of cobalt facilitated the formation of active CoMo-S species that were more H2S-dependent as compared to Mo-S entities. 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A, General</title><description>[Display omitted] •Co addition enhanced the WGS activity of Mo-S/ZrO2 catalysts.•The formation of CoMo-S species increased with Co content up to Co/Mo = 0.3.•CO conversion was stable during 4 weeks of WGS reaction in 7000 ppm H2S containing feed at 35,000 h−1 GHSV and 350 °C.•The optimal atomic Co/Mo ratio at monolayer coverage on ZrO2 resulted in enhanced WGS activity.•The active metal loading in the best CoMo-S catalyst was lower than in pure Mo-S/ZrO2 and commercial catalysts. A series of CoMo-S/ZrO2 catalysts were prepared by modifying Co and Mo content using incipient wetness impregnation method, investigated in the water gas shift (WGS) reaction in the presence of H2S and characterized by TEM, XRD, Raman, TPR, and XPS. The supported CoMo-S catalyst corresponding to the CoMo-O monolayer coverage displayed the presence of highly dispersed CoMo-S species that were characterized by the highest extent of sulfidation. The presence of cobalt facilitated the formation of active CoMo-S species that were more H2S-dependent as compared to Mo-S entities. The Co/Mo = 0.3 catalyst at monolayer CoMo-O coverage was the most active and thermally stable, as well as the least H2S-dependent during 4 weeks of WGS reaction among all catalysts investigated.</description><subject>Catalysts</subject><subject>CoMo sulfide</subject><subject>H2S dependence</subject><subject>Hydrogen production</subject><subject>Hydrogen sulfide</subject><subject>Monolayers</subject><subject>Sulfidation</subject><subject>Surface coverage</subject><subject>Thermal stability</subject><subject>Water gas</subject><subject>Water gas shift reaction</subject><subject>X ray photoelectron spectroscopy</subject><subject>Zirconium dioxide</subject><subject>ZrO2</subject><issn>0926-860X</issn><issn>1873-3875</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNp9UMtKAzEUDaJgrf6BiwHXM-YmmddGkKJWqHShBXET0jzqDHUyJplK_94M49rV5V7O456D0DXgDDAUt20meimCyAiGOgMoaQEnaAZVSVNalfkpmuGaFGlV4PdzdOF9izEmrM5naLM8Kmd3ukt6Z9UgQ2O7xB60SxY2jacvG7RKXmz6mvyIEM874RP_2ZiQjI77ow9xH_reuhEYyR9uTS7RmRF7r6_-5hxtHh_eFst0tX56XtyvUklLCKncGlqWUhUVrhTWbMsIgASqGNQKasFETkpcbSFCFDNMlbmgJmfGUGIqYegc3Uy68dPvQfvAWzu4LlpyQvOYuSa4iCg2oaSz3jtteO-aL-GOHDAfC-QtnwrkY4F8KjDS7iaajgkOjXbcy0Z3UqvGaRm4ss3_Ar_8_ntI</recordid><startdate>20200125</startdate><enddate>20200125</enddate><creator>Yun, SeongUk</creator><creator>Guliants, Vadim</creator><general>Elsevier B.V</general><general>Elsevier Science SA</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope><scope>L7M</scope><orcidid>https://orcid.org/0000-0002-9631-2054</orcidid></search><sort><creationdate>20200125</creationdate><title>Hydrogen production over Co-promoted Mo-S water gas shift catalysts supported on ZrO2</title><author>Yun, SeongUk ; Guliants, Vadim</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c371t-cbf377cd6808d0e4b4211c13d419d19a4a52708b1cd6d4f4d75a3f54ff32f8af3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Catalysts</topic><topic>CoMo sulfide</topic><topic>H2S dependence</topic><topic>Hydrogen production</topic><topic>Hydrogen sulfide</topic><topic>Monolayers</topic><topic>Sulfidation</topic><topic>Surface coverage</topic><topic>Thermal stability</topic><topic>Water gas</topic><topic>Water gas shift reaction</topic><topic>X ray photoelectron spectroscopy</topic><topic>Zirconium dioxide</topic><topic>ZrO2</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Yun, SeongUk</creatorcontrib><creatorcontrib>Guliants, Vadim</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Applied catalysis. A, General</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Yun, SeongUk</au><au>Guliants, Vadim</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Hydrogen production over Co-promoted Mo-S water gas shift catalysts supported on ZrO2</atitle><jtitle>Applied catalysis. A, General</jtitle><date>2020-01-25</date><risdate>2020</risdate><volume>590</volume><spage>117361</spage><pages>117361-</pages><artnum>117361</artnum><issn>0926-860X</issn><eissn>1873-3875</eissn><abstract>[Display omitted] •Co addition enhanced the WGS activity of Mo-S/ZrO2 catalysts.•The formation of CoMo-S species increased with Co content up to Co/Mo = 0.3.•CO conversion was stable during 4 weeks of WGS reaction in 7000 ppm H2S containing feed at 35,000 h−1 GHSV and 350 °C.•The optimal atomic Co/Mo ratio at monolayer coverage on ZrO2 resulted in enhanced WGS activity.•The active metal loading in the best CoMo-S catalyst was lower than in pure Mo-S/ZrO2 and commercial catalysts. A series of CoMo-S/ZrO2 catalysts were prepared by modifying Co and Mo content using incipient wetness impregnation method, investigated in the water gas shift (WGS) reaction in the presence of H2S and characterized by TEM, XRD, Raman, TPR, and XPS. The supported CoMo-S catalyst corresponding to the CoMo-O monolayer coverage displayed the presence of highly dispersed CoMo-S species that were characterized by the highest extent of sulfidation. The presence of cobalt facilitated the formation of active CoMo-S species that were more H2S-dependent as compared to Mo-S entities. The Co/Mo = 0.3 catalyst at monolayer CoMo-O coverage was the most active and thermally stable, as well as the least H2S-dependent during 4 weeks of WGS reaction among all catalysts investigated.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.apcata.2019.117361</doi><orcidid>https://orcid.org/0000-0002-9631-2054</orcidid></addata></record>
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subjects Catalysts
CoMo sulfide
H2S dependence
Hydrogen production
Hydrogen sulfide
Monolayers
Sulfidation
Surface coverage
Thermal stability
Water gas
Water gas shift reaction
X ray photoelectron spectroscopy
Zirconium dioxide
ZrO2
title Hydrogen production over Co-promoted Mo-S water gas shift catalysts supported on ZrO2
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