A new sol‐gel route alumina for selective oxidation of H2S to sulphur
In this study, a new synthesis method was developed for the production of modified sol‐gel alumina (SG‐M) for the selective oxidation of H2S to elemental sulphur. The catalytic activity of this modified alumina without any active metal incorporation was then compared with the activity of commercial...
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Veröffentlicht in: | Canadian journal of chemical engineering 2019-12, Vol.97 (12), p.3125-3137 |
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creator | Tasdemir, H. Mehmet Yagizatli, Yavuz Yasyerli, Sena Yasyerli, Nail Dogu, Gulsen |
description | In this study, a new synthesis method was developed for the production of modified sol‐gel alumina (SG‐M) for the selective oxidation of H2S to elemental sulphur. The catalytic activity of this modified alumina without any active metal incorporation was then compared with the activity of commercial alumina (alumina‐com) for H2S selective oxidation. The N2 adsorption‐desorption isotherm showed that the SG‐M alumina synthesized in this work has a mesoporous structure with well‐defined hysteresis loops. Both alumina materials showed a γ‐Al2O3 crystalline phase with an amorphous structure in their crystal structure. The surface acidity of the alumina materials was determined using pyridine‐adsorbed FTIR analyses, and both alumina showed Lewis acid sites on their surfaces. The catalytic activity tests were performed at 250°C using a feed ratio of O2/H2S:0.5. The complete conversion of H2S over SG‐M was achieved during 400 minutes of reaction time. However, the commercial alumina lost its activity at earlier reaction times. Lewis acid sites and surface hydroxyl groups caused the alumina to be active in H2S selective catalytic oxidation, and the formation of Al‐S bonds, observed when the H2S conversion fell, caused a decrease in the catalytic activity of the alumina materials. A high sulphur yield (≥95%) was obtained over SG‐M, even though there was no active metal incorporation and even in the presence of excess oxygen. Considering the catalytic activities, the new sol‐gel alumina synthesized in this work is superior to commercial alumina. It was concluded that, as a catalyst without any active metal, SG‐M is a promising catalyst in H2S selective oxidation to sulphur.
Activity comparison of synthesized alumina (SG‐M) and commercial alumina (alumina‐com) for H2S selective oxidation. |
doi_str_mv | 10.1002/cjce.23609 |
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Activity comparison of synthesized alumina (SG‐M) and commercial alumina (alumina‐com) for H2S selective oxidation.</description><identifier>ISSN: 0008-4034</identifier><identifier>EISSN: 1939-019X</identifier><identifier>DOI: 10.1002/cjce.23609</identifier><language>eng</language><publisher>Hoboken, USA: John Wiley & Sons, Inc</publisher><subject>Alumina ; Aluminum oxide ; Amorphous materials ; Catalysts ; Catalytic activity ; Catalytic converters ; Catalytic oxidation ; Conversion ; Crystal structure ; FTIR ; H2S selective oxidation ; Hydrogen sulfide ; Hydroxyl groups ; Hysteresis loops ; Lewis acid ; Oxidation ; Reaction time ; Route selection ; Sol-gel processes ; sol‐gel ; Sulfur</subject><ispartof>Canadian journal of chemical engineering, 2019-12, Vol.97 (12), p.3125-3137</ispartof><rights>2019 Canadian Society for Chemical Engineering</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fcjce.23609$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fcjce.23609$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>315,781,785,1418,27929,27930,45579,45580</link.rule.ids></links><search><creatorcontrib>Tasdemir, H. Mehmet</creatorcontrib><creatorcontrib>Yagizatli, Yavuz</creatorcontrib><creatorcontrib>Yasyerli, Sena</creatorcontrib><creatorcontrib>Yasyerli, Nail</creatorcontrib><creatorcontrib>Dogu, Gulsen</creatorcontrib><title>A new sol‐gel route alumina for selective oxidation of H2S to sulphur</title><title>Canadian journal of chemical engineering</title><description>In this study, a new synthesis method was developed for the production of modified sol‐gel alumina (SG‐M) for the selective oxidation of H2S to elemental sulphur. The catalytic activity of this modified alumina without any active metal incorporation was then compared with the activity of commercial alumina (alumina‐com) for H2S selective oxidation. The N2 adsorption‐desorption isotherm showed that the SG‐M alumina synthesized in this work has a mesoporous structure with well‐defined hysteresis loops. Both alumina materials showed a γ‐Al2O3 crystalline phase with an amorphous structure in their crystal structure. The surface acidity of the alumina materials was determined using pyridine‐adsorbed FTIR analyses, and both alumina showed Lewis acid sites on their surfaces. The catalytic activity tests were performed at 250°C using a feed ratio of O2/H2S:0.5. The complete conversion of H2S over SG‐M was achieved during 400 minutes of reaction time. However, the commercial alumina lost its activity at earlier reaction times. Lewis acid sites and surface hydroxyl groups caused the alumina to be active in H2S selective catalytic oxidation, and the formation of Al‐S bonds, observed when the H2S conversion fell, caused a decrease in the catalytic activity of the alumina materials. A high sulphur yield (≥95%) was obtained over SG‐M, even though there was no active metal incorporation and even in the presence of excess oxygen. Considering the catalytic activities, the new sol‐gel alumina synthesized in this work is superior to commercial alumina. It was concluded that, as a catalyst without any active metal, SG‐M is a promising catalyst in H2S selective oxidation to sulphur.
Activity comparison of synthesized alumina (SG‐M) and commercial alumina (alumina‐com) for H2S selective oxidation.</description><subject>Alumina</subject><subject>Aluminum oxide</subject><subject>Amorphous materials</subject><subject>Catalysts</subject><subject>Catalytic activity</subject><subject>Catalytic converters</subject><subject>Catalytic oxidation</subject><subject>Conversion</subject><subject>Crystal structure</subject><subject>FTIR</subject><subject>H2S selective oxidation</subject><subject>Hydrogen sulfide</subject><subject>Hydroxyl groups</subject><subject>Hysteresis loops</subject><subject>Lewis acid</subject><subject>Oxidation</subject><subject>Reaction time</subject><subject>Route selection</subject><subject>Sol-gel processes</subject><subject>sol‐gel</subject><subject>Sulfur</subject><issn>0008-4034</issn><issn>1939-019X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNotkE1OwzAUhC0EEqWw4QSWWKe8Z7tJvKyi0oIqsQAkdlaaPJdUblychLY7jsAZOQn9YTUz0mhG-hi7RRgggLgvlgUNhIxBn7EeaqkjQP1-znoAkEYKpLpkV02z3EcBCntsMuI1bXjj3e_3z4IcD75rieeuW1V1zq0PvCFHRVt9EffbqszbytfcWz4VL7z1vOnc-qML1-zC5q6hm3_ts7eH8Ws2jWbPk8dsNIsWIhY6KjUWaSmThHQ8RJgPbSmsKjGVBEoTCVS5VAnh3Ao7J8REWKHJqiLVSmIs--zutLsO_rOjpjVL34V6f2mERIUJJCnuW3hqbSpHO7MO1SoPO4NgDpTMgZI5UjLZUzY-OvkHOM1cXA</recordid><startdate>201912</startdate><enddate>201912</enddate><creator>Tasdemir, H. 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Mehmet ; Yagizatli, Yavuz ; Yasyerli, Sena ; Yasyerli, Nail ; Dogu, Gulsen</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-g2629-d91c8d377e96510b5fd2f4d183e049ee214a347e1bf2fbe1172f29ef4c8943163</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2019</creationdate><topic>Alumina</topic><topic>Aluminum oxide</topic><topic>Amorphous materials</topic><topic>Catalysts</topic><topic>Catalytic activity</topic><topic>Catalytic converters</topic><topic>Catalytic oxidation</topic><topic>Conversion</topic><topic>Crystal structure</topic><topic>FTIR</topic><topic>H2S selective oxidation</topic><topic>Hydrogen sulfide</topic><topic>Hydroxyl groups</topic><topic>Hysteresis loops</topic><topic>Lewis acid</topic><topic>Oxidation</topic><topic>Reaction time</topic><topic>Route selection</topic><topic>Sol-gel processes</topic><topic>sol‐gel</topic><topic>Sulfur</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Tasdemir, H. Mehmet</creatorcontrib><creatorcontrib>Yagizatli, Yavuz</creatorcontrib><creatorcontrib>Yasyerli, Sena</creatorcontrib><creatorcontrib>Yasyerli, Nail</creatorcontrib><creatorcontrib>Dogu, Gulsen</creatorcontrib><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>Canadian journal of chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Tasdemir, H. Mehmet</au><au>Yagizatli, Yavuz</au><au>Yasyerli, Sena</au><au>Yasyerli, Nail</au><au>Dogu, Gulsen</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A new sol‐gel route alumina for selective oxidation of H2S to sulphur</atitle><jtitle>Canadian journal of chemical engineering</jtitle><date>2019-12</date><risdate>2019</risdate><volume>97</volume><issue>12</issue><spage>3125</spage><epage>3137</epage><pages>3125-3137</pages><issn>0008-4034</issn><eissn>1939-019X</eissn><abstract>In this study, a new synthesis method was developed for the production of modified sol‐gel alumina (SG‐M) for the selective oxidation of H2S to elemental sulphur. The catalytic activity of this modified alumina without any active metal incorporation was then compared with the activity of commercial alumina (alumina‐com) for H2S selective oxidation. The N2 adsorption‐desorption isotherm showed that the SG‐M alumina synthesized in this work has a mesoporous structure with well‐defined hysteresis loops. Both alumina materials showed a γ‐Al2O3 crystalline phase with an amorphous structure in their crystal structure. The surface acidity of the alumina materials was determined using pyridine‐adsorbed FTIR analyses, and both alumina showed Lewis acid sites on their surfaces. The catalytic activity tests were performed at 250°C using a feed ratio of O2/H2S:0.5. The complete conversion of H2S over SG‐M was achieved during 400 minutes of reaction time. However, the commercial alumina lost its activity at earlier reaction times. Lewis acid sites and surface hydroxyl groups caused the alumina to be active in H2S selective catalytic oxidation, and the formation of Al‐S bonds, observed when the H2S conversion fell, caused a decrease in the catalytic activity of the alumina materials. A high sulphur yield (≥95%) was obtained over SG‐M, even though there was no active metal incorporation and even in the presence of excess oxygen. Considering the catalytic activities, the new sol‐gel alumina synthesized in this work is superior to commercial alumina. It was concluded that, as a catalyst without any active metal, SG‐M is a promising catalyst in H2S selective oxidation to sulphur.
Activity comparison of synthesized alumina (SG‐M) and commercial alumina (alumina‐com) for H2S selective oxidation.</abstract><cop>Hoboken, USA</cop><pub>John Wiley & Sons, Inc</pub><doi>10.1002/cjce.23609</doi><tpages>13</tpages></addata></record> |
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subjects | Alumina Aluminum oxide Amorphous materials Catalysts Catalytic activity Catalytic converters Catalytic oxidation Conversion Crystal structure FTIR H2S selective oxidation Hydrogen sulfide Hydroxyl groups Hysteresis loops Lewis acid Oxidation Reaction time Route selection Sol-gel processes sol‐gel Sulfur |
title | A new sol‐gel route alumina for selective oxidation of H2S to sulphur |
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