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High temperature gas desulfurization with elemental sulfur production
Preliminary results on the use of cerium oxide as a high-temperature desulfurization sorbent are presented. The primary advantage of cerium over current zinc-based sorbents is the potential to produce elemental sulfur during the regeneration phase of the process. Although CeO 2 is less effective for...
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Published in: | Chemical engineering science 1999, Vol.54 (15), p.3007-3017 |
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creator | Zeng, Y. Zhang, S. Groves, F.R. Harrison, D.P. |
description | Preliminary results on the use of cerium oxide as a high-temperature desulfurization sorbent are presented. The primary advantage of cerium over current zinc-based sorbents is the potential to produce elemental sulfur during the regeneration phase of the process. Although CeO
2 is less effective for H
2S removal during sulfidation, the sulfided product, Ce
2O
2S, will react with SO
2 to produce elemental sulfur directly. Rapid and complete regeneration is possible over the range of 500 to 700°C, and only elemental sulfur is formed. Elemental sulfur concentrations (considered as S
2) as large as 20
mol% have been produced in the regeneration product. The sorbent has been subjected to ten sulfidation–regeneration cycles using a laboratory-scale fixed-bed reactor with negligible activity loss. Effectively complete conversion of CeO
2 to Ce
2O
2S during sulfidation and subsequent regeneration to CeO
2 was achieved in each cycle. A two-stage desulfurization process using CeO
2 for bulk H
2S removal followed by a zinc sorbent polishing step has been proposed to meet specifications of the integrated gasification combined cycle (IGCC) process. Economic comparison with a single-stage desulfurization process using zinc sorbent followed by elemental sulfur recovery using the direct sulfur recovery process (DSRP) shows that the two-stage cerium process may be less costly if the cerium sorbent is sufficiently durable. |
doi_str_mv | 10.1016/S0009-2509(98)00427-8 |
format | article |
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2 is less effective for H
2S removal during sulfidation, the sulfided product, Ce
2O
2S, will react with SO
2 to produce elemental sulfur directly. Rapid and complete regeneration is possible over the range of 500 to 700°C, and only elemental sulfur is formed. Elemental sulfur concentrations (considered as S
2) as large as 20
mol% have been produced in the regeneration product. The sorbent has been subjected to ten sulfidation–regeneration cycles using a laboratory-scale fixed-bed reactor with negligible activity loss. Effectively complete conversion of CeO
2 to Ce
2O
2S during sulfidation and subsequent regeneration to CeO
2 was achieved in each cycle. A two-stage desulfurization process using CeO
2 for bulk H
2S removal followed by a zinc sorbent polishing step has been proposed to meet specifications of the integrated gasification combined cycle (IGCC) process. Economic comparison with a single-stage desulfurization process using zinc sorbent followed by elemental sulfur recovery using the direct sulfur recovery process (DSRP) shows that the two-stage cerium process may be less costly if the cerium sorbent is sufficiently durable.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/S0009-2509(98)00427-8</identifier><identifier>CODEN: CESCAC</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Air pollution caused by fuel industries ; Applied sciences ; Atmospheric pollution ; Cerium oxide ; Combustion and energy production ; Elemental sulfur ; Energy ; Energy. Thermal use of fuels ; Exact sciences and technology ; Gas desulfurization ; Pollution ; Pollution reduction ; Prevention and purification methods ; Stack gas and industrial effluent processing</subject><ispartof>Chemical engineering science, 1999, Vol.54 (15), p.3007-3017</ispartof><rights>1999 Elsevier Science Ltd</rights><rights>1999 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c405t-67a7ee204cba8ef6ed9724f0ccd4bf2959120c3f9ab1a1e298475a4c060a77563</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>309,310,314,780,784,789,790,4024,4050,4051,23930,23931,25140,27923,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=1849961$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Zeng, Y.</creatorcontrib><creatorcontrib>Zhang, S.</creatorcontrib><creatorcontrib>Groves, F.R.</creatorcontrib><creatorcontrib>Harrison, D.P.</creatorcontrib><title>High temperature gas desulfurization with elemental sulfur production</title><title>Chemical engineering science</title><description>Preliminary results on the use of cerium oxide as a high-temperature desulfurization sorbent are presented. The primary advantage of cerium over current zinc-based sorbents is the potential to produce elemental sulfur during the regeneration phase of the process. Although CeO
2 is less effective for H
2S removal during sulfidation, the sulfided product, Ce
2O
2S, will react with SO
2 to produce elemental sulfur directly. Rapid and complete regeneration is possible over the range of 500 to 700°C, and only elemental sulfur is formed. Elemental sulfur concentrations (considered as S
2) as large as 20
mol% have been produced in the regeneration product. The sorbent has been subjected to ten sulfidation–regeneration cycles using a laboratory-scale fixed-bed reactor with negligible activity loss. Effectively complete conversion of CeO
2 to Ce
2O
2S during sulfidation and subsequent regeneration to CeO
2 was achieved in each cycle. A two-stage desulfurization process using CeO
2 for bulk H
2S removal followed by a zinc sorbent polishing step has been proposed to meet specifications of the integrated gasification combined cycle (IGCC) process. Economic comparison with a single-stage desulfurization process using zinc sorbent followed by elemental sulfur recovery using the direct sulfur recovery process (DSRP) shows that the two-stage cerium process may be less costly if the cerium sorbent is sufficiently durable.</description><subject>Air pollution caused by fuel industries</subject><subject>Applied sciences</subject><subject>Atmospheric pollution</subject><subject>Cerium oxide</subject><subject>Combustion and energy production</subject><subject>Elemental sulfur</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Exact sciences and technology</subject><subject>Gas desulfurization</subject><subject>Pollution</subject><subject>Pollution reduction</subject><subject>Prevention and purification methods</subject><subject>Stack gas and industrial effluent processing</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1999</creationdate><recordtype>article</recordtype><recordid>eNqFkEFPwzAMhSMEEmPwE5B6QAgOhaRNm-SE0DQY0iQOwDnyUmcL6tqRpCD49XQrgiMny_L3_OxHyCmjV4yy8vqJUqrSrKDqQslLSnkmUrlHRkyKPOWcFvtk9IsckqMQXvtWCEZHZDpzy1UScb1BD7HzmCwhJBWGrradd18QXdskHy6uEqxxjU2EOhmGyca3VWe2wDE5sFAHPPmpY_JyN32ezNL54_3D5Haemv6KmJYCBGJGuVmARFtipUTGLTWm4gubqUKxjJrcKlgwYJgpyUUB3NCSghBFmY_J-bC3t37rMES9dsFgXUODbRc04wXL80z1YDGAxrcheLR6490a_KdmVG9D07vQ9DYRraTehaZlrzv7MYBgoLYeGuPCn1hypUrWYzcDhv2z7w69DsZhY7ByHk3UVev-MfoG2X-Bmg</recordid><startdate>1999</startdate><enddate>1999</enddate><creator>Zeng, Y.</creator><creator>Zhang, S.</creator><creator>Groves, F.R.</creator><creator>Harrison, D.P.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope></search><sort><creationdate>1999</creationdate><title>High temperature gas desulfurization with elemental sulfur production</title><author>Zeng, Y. ; Zhang, S. ; Groves, F.R. ; Harrison, D.P.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c405t-67a7ee204cba8ef6ed9724f0ccd4bf2959120c3f9ab1a1e298475a4c060a77563</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1999</creationdate><topic>Air pollution caused by fuel industries</topic><topic>Applied sciences</topic><topic>Atmospheric pollution</topic><topic>Cerium oxide</topic><topic>Combustion and energy production</topic><topic>Elemental sulfur</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>Exact sciences and technology</topic><topic>Gas desulfurization</topic><topic>Pollution</topic><topic>Pollution reduction</topic><topic>Prevention and purification methods</topic><topic>Stack gas and industrial effluent processing</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Zeng, Y.</creatorcontrib><creatorcontrib>Zhang, S.</creatorcontrib><creatorcontrib>Groves, F.R.</creatorcontrib><creatorcontrib>Harrison, D.P.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Zeng, Y.</au><au>Zhang, S.</au><au>Groves, F.R.</au><au>Harrison, D.P.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>High temperature gas desulfurization with elemental sulfur production</atitle><jtitle>Chemical engineering science</jtitle><date>1999</date><risdate>1999</risdate><volume>54</volume><issue>15</issue><spage>3007</spage><epage>3017</epage><pages>3007-3017</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>Preliminary results on the use of cerium oxide as a high-temperature desulfurization sorbent are presented. The primary advantage of cerium over current zinc-based sorbents is the potential to produce elemental sulfur during the regeneration phase of the process. Although CeO
2 is less effective for H
2S removal during sulfidation, the sulfided product, Ce
2O
2S, will react with SO
2 to produce elemental sulfur directly. Rapid and complete regeneration is possible over the range of 500 to 700°C, and only elemental sulfur is formed. Elemental sulfur concentrations (considered as S
2) as large as 20
mol% have been produced in the regeneration product. The sorbent has been subjected to ten sulfidation–regeneration cycles using a laboratory-scale fixed-bed reactor with negligible activity loss. Effectively complete conversion of CeO
2 to Ce
2O
2S during sulfidation and subsequent regeneration to CeO
2 was achieved in each cycle. A two-stage desulfurization process using CeO
2 for bulk H
2S removal followed by a zinc sorbent polishing step has been proposed to meet specifications of the integrated gasification combined cycle (IGCC) process. Economic comparison with a single-stage desulfurization process using zinc sorbent followed by elemental sulfur recovery using the direct sulfur recovery process (DSRP) shows that the two-stage cerium process may be less costly if the cerium sorbent is sufficiently durable.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/S0009-2509(98)00427-8</doi><tpages>11</tpages></addata></record> |
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source | ScienceDirect Journals |
subjects | Air pollution caused by fuel industries Applied sciences Atmospheric pollution Cerium oxide Combustion and energy production Elemental sulfur Energy Energy. Thermal use of fuels Exact sciences and technology Gas desulfurization Pollution Pollution reduction Prevention and purification methods Stack gas and industrial effluent processing |
title | High temperature gas desulfurization with elemental sulfur production |
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