Macroporous alumina- and titania-based catalyst for carbonyl sulfide hydrolysis at ambient temperature
[Display omitted] •Alumina/titania-based catalysts with 3DOM structure were synthesized successfully.•The hydrolysis activity of the catalyst was enhanced remarkably by the 3DOM structure.•The addition of P123 and SiO2 could further increase the hydrolysis activity.•The most oxygenated hydrolysis pr...
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creator | He, Enyun Huang, Guan Fan, Huiling Yang, Chao Wang, Hui Tian, Zhen Wang, Longjiang Zhao, Yingrui |
description | [Display omitted]
•Alumina/titania-based catalysts with 3DOM structure were synthesized successfully.•The hydrolysis activity of the catalyst was enhanced remarkably by the 3DOM structure.•The addition of P123 and SiO2 could further increase the hydrolysis activity.•The most oxygenated hydrolysis product for the titania-based catalysts was sulfur.
In this study prepared alumina and titania carbonyl sulfide hydrolysis catalysts with three dimensional ordered macroporous (3DOM) structure were prepared by colloidal crystal template method. The fresh and used catalysts were characterized by X-ray diffraction, scanning electron microscopy, nitrogen adsorption studies, CO2 temperature programmed desorption (CO2-TPD) and Fourier transform infrared spectroscopy. The hydrolysis performance of the catalysts and their resistances to oxygen poisoning were evaluated in a fixed bed reactor at room temperature.
It was found that the hydrolysis activity of the catalysts was remarkably enhanced by introduction of 3DOM structure because the effective pulling out of the hydrolysis product H2S from the porous structure significantly inhibited the deposition of sulfur on the surface of the catalysts. Adding surfactant P123 during the preparation of the 3DOM alumina-based catalyst increased the hydrolysis activity by increasing the surface area of the catalysts. Compositing SiO2 with the 3DOM titania-based catalysts could increase the surface area as well as benefit the formation of 3DOM structure. The optimum content of SiO2 was 33 wt%, at which both catalyst performance and the amount of basic sites as measured by CO2-TPD were highest. The hydrolysis activity of the catalysts in the presence of oxygen showed that the oxygen toxicity resistance of the 3DOM titania-based catalysts were better than the 3DOM alumina-based catalysts. The most abundant sulfur specie deposited on the surface of the titania-based catalysts was elemental sulfur for the alumina-based catalysts it was sulfate species. Sulfate not only blocked the pores of the catalysts but also deactivated the catalysts seriously for its acidity. |
doi_str_mv | 10.1016/j.fuel.2019.02.097 |
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•Alumina/titania-based catalysts with 3DOM structure were synthesized successfully.•The hydrolysis activity of the catalyst was enhanced remarkably by the 3DOM structure.•The addition of P123 and SiO2 could further increase the hydrolysis activity.•The most oxygenated hydrolysis product for the titania-based catalysts was sulfur.
In this study prepared alumina and titania carbonyl sulfide hydrolysis catalysts with three dimensional ordered macroporous (3DOM) structure were prepared by colloidal crystal template method. The fresh and used catalysts were characterized by X-ray diffraction, scanning electron microscopy, nitrogen adsorption studies, CO2 temperature programmed desorption (CO2-TPD) and Fourier transform infrared spectroscopy. The hydrolysis performance of the catalysts and their resistances to oxygen poisoning were evaluated in a fixed bed reactor at room temperature.
It was found that the hydrolysis activity of the catalysts was remarkably enhanced by introduction of 3DOM structure because the effective pulling out of the hydrolysis product H2S from the porous structure significantly inhibited the deposition of sulfur on the surface of the catalysts. Adding surfactant P123 during the preparation of the 3DOM alumina-based catalyst increased the hydrolysis activity by increasing the surface area of the catalysts. Compositing SiO2 with the 3DOM titania-based catalysts could increase the surface area as well as benefit the formation of 3DOM structure. The optimum content of SiO2 was 33 wt%, at which both catalyst performance and the amount of basic sites as measured by CO2-TPD were highest. The hydrolysis activity of the catalysts in the presence of oxygen showed that the oxygen toxicity resistance of the 3DOM titania-based catalysts were better than the 3DOM alumina-based catalysts. The most abundant sulfur specie deposited on the surface of the titania-based catalysts was elemental sulfur for the alumina-based catalysts it was sulfate species. Sulfate not only blocked the pores of the catalysts but also deactivated the catalysts seriously for its acidity.</description><identifier>ISSN: 0016-2361</identifier><identifier>EISSN: 1873-7153</identifier><identifier>DOI: 10.1016/j.fuel.2019.02.097</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>3DOM ; Acidity ; Alumina ; Aluminum oxide ; Ambient temperature ; Carbon dioxide ; Carbonyl sulfide ; Carbonyls ; Catalysis ; Catalysts ; Crystal pulling ; Crystal structure ; Deactivation ; Fixed bed reactors ; Fixed beds ; Fourier transforms ; Hydrogen sulfide ; Hydrolysis ; Hyperoxia ; Infrared spectroscopy ; Oxygen ; Scanning electron microscopy ; Silicon dioxide ; Sulfates ; Sulfur ; Surface area ; Temperature effects ; Titania ; Titanium dioxide ; Toxicity ; X-ray diffraction</subject><ispartof>Fuel (Guildford), 2019-06, Vol.246, p.277-284</ispartof><rights>2019 Elsevier Ltd</rights><rights>Copyright Elsevier BV Jun 15, 2019</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c431t-f9828fcc0a448fcb2135b21a150ab6c19acc17757bce434cb7e79fc467c721d33</citedby><cites>FETCH-LOGICAL-c431t-f9828fcc0a448fcb2135b21a150ab6c19acc17757bce434cb7e79fc467c721d33</cites><orcidid>0000-0003-0945-1871</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.fuel.2019.02.097$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids></links><search><creatorcontrib>He, Enyun</creatorcontrib><creatorcontrib>Huang, Guan</creatorcontrib><creatorcontrib>Fan, Huiling</creatorcontrib><creatorcontrib>Yang, Chao</creatorcontrib><creatorcontrib>Wang, Hui</creatorcontrib><creatorcontrib>Tian, Zhen</creatorcontrib><creatorcontrib>Wang, Longjiang</creatorcontrib><creatorcontrib>Zhao, Yingrui</creatorcontrib><title>Macroporous alumina- and titania-based catalyst for carbonyl sulfide hydrolysis at ambient temperature</title><title>Fuel (Guildford)</title><description>[Display omitted]
•Alumina/titania-based catalysts with 3DOM structure were synthesized successfully.•The hydrolysis activity of the catalyst was enhanced remarkably by the 3DOM structure.•The addition of P123 and SiO2 could further increase the hydrolysis activity.•The most oxygenated hydrolysis product for the titania-based catalysts was sulfur.
In this study prepared alumina and titania carbonyl sulfide hydrolysis catalysts with three dimensional ordered macroporous (3DOM) structure were prepared by colloidal crystal template method. The fresh and used catalysts were characterized by X-ray diffraction, scanning electron microscopy, nitrogen adsorption studies, CO2 temperature programmed desorption (CO2-TPD) and Fourier transform infrared spectroscopy. The hydrolysis performance of the catalysts and their resistances to oxygen poisoning were evaluated in a fixed bed reactor at room temperature.
It was found that the hydrolysis activity of the catalysts was remarkably enhanced by introduction of 3DOM structure because the effective pulling out of the hydrolysis product H2S from the porous structure significantly inhibited the deposition of sulfur on the surface of the catalysts. Adding surfactant P123 during the preparation of the 3DOM alumina-based catalyst increased the hydrolysis activity by increasing the surface area of the catalysts. Compositing SiO2 with the 3DOM titania-based catalysts could increase the surface area as well as benefit the formation of 3DOM structure. The optimum content of SiO2 was 33 wt%, at which both catalyst performance and the amount of basic sites as measured by CO2-TPD were highest. The hydrolysis activity of the catalysts in the presence of oxygen showed that the oxygen toxicity resistance of the 3DOM titania-based catalysts were better than the 3DOM alumina-based catalysts. The most abundant sulfur specie deposited on the surface of the titania-based catalysts was elemental sulfur for the alumina-based catalysts it was sulfate species. Sulfate not only blocked the pores of the catalysts but also deactivated the catalysts seriously for its acidity.</description><subject>3DOM</subject><subject>Acidity</subject><subject>Alumina</subject><subject>Aluminum oxide</subject><subject>Ambient temperature</subject><subject>Carbon dioxide</subject><subject>Carbonyl sulfide</subject><subject>Carbonyls</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Crystal pulling</subject><subject>Crystal structure</subject><subject>Deactivation</subject><subject>Fixed bed reactors</subject><subject>Fixed beds</subject><subject>Fourier transforms</subject><subject>Hydrogen sulfide</subject><subject>Hydrolysis</subject><subject>Hyperoxia</subject><subject>Infrared spectroscopy</subject><subject>Oxygen</subject><subject>Scanning electron microscopy</subject><subject>Silicon dioxide</subject><subject>Sulfates</subject><subject>Sulfur</subject><subject>Surface area</subject><subject>Temperature effects</subject><subject>Titania</subject><subject>Titanium dioxide</subject><subject>Toxicity</subject><subject>X-ray diffraction</subject><issn>0016-2361</issn><issn>1873-7153</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNp9UE1LxDAQDaLguvoHPAU8t-ajbVrwIuIXrHjRc5imE8zSbdYkFfrvzbKevcxjmPdm5j1CrjkrOePN7ba0M46lYLwrmShZp07IirdKForX8pSsWGYVQjb8nFzEuGWMqbauVsS-gQl-74OfI4Vx3rkJCgrTQJNLMDkoeog4UAMJxiUman3ITej9tIw0zqN1A9KvZQg-j13ekSjseodTogl3ewyQ5oCX5MzCGPHqD9fk8-nx4-Gl2Lw_vz7cbwpTSZ4K27WitcYwqKqMveCyzgV4zaBvDO_AGK5UrXqDlaxMr1B11lSNMkrwQco1uTnu3Qf_PWNMeuvnMOWTWgjeSi67ps0scWRl6zEGtHof3A7CojnThzz1Vh_y1Ic8NRM655lFd0cR5v9_HAYdTbZpcHABTdKDd__JfwGAc4C1</recordid><startdate>20190615</startdate><enddate>20190615</enddate><creator>He, Enyun</creator><creator>Huang, Guan</creator><creator>Fan, Huiling</creator><creator>Yang, Chao</creator><creator>Wang, Hui</creator><creator>Tian, Zhen</creator><creator>Wang, Longjiang</creator><creator>Zhao, Yingrui</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>7QO</scope><scope>7QQ</scope><scope>7SC</scope><scope>7SE</scope><scope>7SP</scope><scope>7SR</scope><scope>7T7</scope><scope>7TA</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>H8D</scope><scope>H8G</scope><scope>JG9</scope><scope>JQ2</scope><scope>KR7</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>P64</scope><orcidid>https://orcid.org/0000-0003-0945-1871</orcidid></search><sort><creationdate>20190615</creationdate><title>Macroporous alumina- and titania-based catalyst for carbonyl sulfide hydrolysis at ambient temperature</title><author>He, Enyun ; Huang, Guan ; Fan, Huiling ; Yang, Chao ; Wang, Hui ; Tian, Zhen ; Wang, Longjiang ; Zhao, Yingrui</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c431t-f9828fcc0a448fcb2135b21a150ab6c19acc17757bce434cb7e79fc467c721d33</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2019</creationdate><topic>3DOM</topic><topic>Acidity</topic><topic>Alumina</topic><topic>Aluminum oxide</topic><topic>Ambient temperature</topic><topic>Carbon dioxide</topic><topic>Carbonyl sulfide</topic><topic>Carbonyls</topic><topic>Catalysis</topic><topic>Catalysts</topic><topic>Crystal pulling</topic><topic>Crystal structure</topic><topic>Deactivation</topic><topic>Fixed bed reactors</topic><topic>Fixed beds</topic><topic>Fourier transforms</topic><topic>Hydrogen sulfide</topic><topic>Hydrolysis</topic><topic>Hyperoxia</topic><topic>Infrared spectroscopy</topic><topic>Oxygen</topic><topic>Scanning electron microscopy</topic><topic>Silicon dioxide</topic><topic>Sulfates</topic><topic>Sulfur</topic><topic>Surface area</topic><topic>Temperature effects</topic><topic>Titania</topic><topic>Titanium dioxide</topic><topic>Toxicity</topic><topic>X-ray diffraction</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>He, Enyun</creatorcontrib><creatorcontrib>Huang, Guan</creatorcontrib><creatorcontrib>Fan, Huiling</creatorcontrib><creatorcontrib>Yang, Chao</creatorcontrib><creatorcontrib>Wang, Hui</creatorcontrib><creatorcontrib>Tian, Zhen</creatorcontrib><creatorcontrib>Wang, Longjiang</creatorcontrib><creatorcontrib>Zhao, Yingrui</creatorcontrib><collection>CrossRef</collection><collection>Aluminium Industry Abstracts</collection><collection>Biotechnology Research Abstracts</collection><collection>Ceramic Abstracts</collection><collection>Computer and Information Systems Abstracts</collection><collection>Corrosion Abstracts</collection><collection>Electronics & Communications Abstracts</collection><collection>Engineered Materials Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Materials Business File</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Copper Technical Reference Library</collection><collection>Materials Research Database</collection><collection>ProQuest Computer Science Collection</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Computer and Information Systems Abstracts Academic</collection><collection>Computer and Information Systems Abstracts Professional</collection><collection>Biotechnology and BioEngineering Abstracts</collection><jtitle>Fuel (Guildford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>He, Enyun</au><au>Huang, Guan</au><au>Fan, Huiling</au><au>Yang, Chao</au><au>Wang, Hui</au><au>Tian, Zhen</au><au>Wang, Longjiang</au><au>Zhao, Yingrui</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Macroporous alumina- and titania-based catalyst for carbonyl sulfide hydrolysis at ambient temperature</atitle><jtitle>Fuel (Guildford)</jtitle><date>2019-06-15</date><risdate>2019</risdate><volume>246</volume><spage>277</spage><epage>284</epage><pages>277-284</pages><issn>0016-2361</issn><eissn>1873-7153</eissn><abstract>[Display omitted]
•Alumina/titania-based catalysts with 3DOM structure were synthesized successfully.•The hydrolysis activity of the catalyst was enhanced remarkably by the 3DOM structure.•The addition of P123 and SiO2 could further increase the hydrolysis activity.•The most oxygenated hydrolysis product for the titania-based catalysts was sulfur.
In this study prepared alumina and titania carbonyl sulfide hydrolysis catalysts with three dimensional ordered macroporous (3DOM) structure were prepared by colloidal crystal template method. The fresh and used catalysts were characterized by X-ray diffraction, scanning electron microscopy, nitrogen adsorption studies, CO2 temperature programmed desorption (CO2-TPD) and Fourier transform infrared spectroscopy. The hydrolysis performance of the catalysts and their resistances to oxygen poisoning were evaluated in a fixed bed reactor at room temperature.
It was found that the hydrolysis activity of the catalysts was remarkably enhanced by introduction of 3DOM structure because the effective pulling out of the hydrolysis product H2S from the porous structure significantly inhibited the deposition of sulfur on the surface of the catalysts. Adding surfactant P123 during the preparation of the 3DOM alumina-based catalyst increased the hydrolysis activity by increasing the surface area of the catalysts. Compositing SiO2 with the 3DOM titania-based catalysts could increase the surface area as well as benefit the formation of 3DOM structure. The optimum content of SiO2 was 33 wt%, at which both catalyst performance and the amount of basic sites as measured by CO2-TPD were highest. The hydrolysis activity of the catalysts in the presence of oxygen showed that the oxygen toxicity resistance of the 3DOM titania-based catalysts were better than the 3DOM alumina-based catalysts. The most abundant sulfur specie deposited on the surface of the titania-based catalysts was elemental sulfur for the alumina-based catalysts it was sulfate species. Sulfate not only blocked the pores of the catalysts but also deactivated the catalysts seriously for its acidity.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.fuel.2019.02.097</doi><tpages>8</tpages><orcidid>https://orcid.org/0000-0003-0945-1871</orcidid></addata></record> |
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subjects | 3DOM Acidity Alumina Aluminum oxide Ambient temperature Carbon dioxide Carbonyl sulfide Carbonyls Catalysis Catalysts Crystal pulling Crystal structure Deactivation Fixed bed reactors Fixed beds Fourier transforms Hydrogen sulfide Hydrolysis Hyperoxia Infrared spectroscopy Oxygen Scanning electron microscopy Silicon dioxide Sulfates Sulfur Surface area Temperature effects Titania Titanium dioxide Toxicity X-ray diffraction |
title | Macroporous alumina- and titania-based catalyst for carbonyl sulfide hydrolysis at ambient temperature |
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