Influence of Catalyst Weight/Biomass Flow Rate Ratio on Gas Production in the Catalytic Pyrolysis of Pine Sawdust at Low Temperatures
Pine sawdust catalytic pyrolysis has been studied in a fluidized bed at temperatures of 650 and 700 °C. The experimental work was carried out in a bench-scale plant based on Waterloo Fast Pyrolysis Process (WFPP) technology. The Ni−Al catalyst used was prepared by coprecipitation with a molar ratio...
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Veröffentlicht in: | Industrial & engineering chemistry research 1998-10, Vol.37 (10), p.3812-3819 |
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creator | Garcia, Lucia Salvador, María L Arauzo, Jesús Bilbao, Rafael |
description | Pine sawdust catalytic pyrolysis has been studied in a fluidized bed at temperatures of 650 and 700 °C. The experimental work was carried out in a bench-scale plant based on Waterloo Fast Pyrolysis Process (WFPP) technology. The Ni−Al catalyst used was prepared by coprecipitation with a molar ratio 1:2 (Ni−Al) and calcined at 750 °C for 3 h. The catalyst was not reduced prior to the biomass reaction. The influence of the catalyst weight/biomass flow rate ratio (W/mb) on the product distribution and on the quality of the gas product obtained was analyzed. An increase of the W/mb ratio increases the total gas yield and diminishes the liquid yield. When the W/mb ratio increases, H2 and CO yields increase while CO2, CH4, and C2 yields decrease. For W/mb ratios ≥ 0.4 h, no significant modifications are observed on the initial yields of different gases, and it is confirmed that under these conditions the initial gas composition is similar to that for thermodynamic equilibrium. For W/mb ratios < 0.4 h, a simple first-order kinetic equation has been suggested for H2 and CO formation. |
doi_str_mv | 10.1021/ie9801960 |
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The experimental work was carried out in a bench-scale plant based on Waterloo Fast Pyrolysis Process (WFPP) technology. The Ni−Al catalyst used was prepared by coprecipitation with a molar ratio 1:2 (Ni−Al) and calcined at 750 °C for 3 h. The catalyst was not reduced prior to the biomass reaction. The influence of the catalyst weight/biomass flow rate ratio (W/mb) on the product distribution and on the quality of the gas product obtained was analyzed. An increase of the W/mb ratio increases the total gas yield and diminishes the liquid yield. When the W/mb ratio increases, H2 and CO yields increase while CO2, CH4, and C2 yields decrease. For W/mb ratios ≥ 0.4 h, no significant modifications are observed on the initial yields of different gases, and it is confirmed that under these conditions the initial gas composition is similar to that for thermodynamic equilibrium. For W/mb ratios < 0.4 h, a simple first-order kinetic equation has been suggested for H2 and CO formation.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/ie9801960</identifier><identifier>CODEN: IECRED</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>09 BIOMASS FUELS ; Agriculture, rearing and food industries wastes ; Applied sciences ; Biomass ; CARBON DIOXIDE ; CATALYSTS ; CHEMICAL REACTION YIELD ; Energy ; Exact sciences and technology ; FLOW RATE ; KINETIC EQUATIONS ; METHANE ; Natural energy ; Pollution ; PYROLYSIS ; SYNTHESIS GAS ; Wastes ; WOOD WASTES</subject><ispartof>Industrial & engineering chemistry research, 1998-10, Vol.37 (10), p.3812-3819</ispartof><rights>Copyright © 1998 American Chemical Society</rights><rights>1998 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a387t-d1e1d05b12e2b1f606df62fb1fcbc5b0dbf700c083366c0c5c21a80e4b328fdb3</citedby><cites>FETCH-LOGICAL-a387t-d1e1d05b12e2b1f606df62fb1fcbc5b0dbf700c083366c0c5c21a80e4b328fdb3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/ie9801960$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/ie9801960$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,780,784,885,2765,27076,27924,27925,56738,56788</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=2397467$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.osti.gov/biblio/669979$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Garcia, Lucia</creatorcontrib><creatorcontrib>Salvador, María L</creatorcontrib><creatorcontrib>Arauzo, Jesús</creatorcontrib><creatorcontrib>Bilbao, Rafael</creatorcontrib><title>Influence of Catalyst Weight/Biomass Flow Rate Ratio on Gas Production in the Catalytic Pyrolysis of Pine Sawdust at Low Temperatures</title><title>Industrial & engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>Pine sawdust catalytic pyrolysis has been studied in a fluidized bed at temperatures of 650 and 700 °C. The experimental work was carried out in a bench-scale plant based on Waterloo Fast Pyrolysis Process (WFPP) technology. The Ni−Al catalyst used was prepared by coprecipitation with a molar ratio 1:2 (Ni−Al) and calcined at 750 °C for 3 h. The catalyst was not reduced prior to the biomass reaction. The influence of the catalyst weight/biomass flow rate ratio (W/mb) on the product distribution and on the quality of the gas product obtained was analyzed. An increase of the W/mb ratio increases the total gas yield and diminishes the liquid yield. When the W/mb ratio increases, H2 and CO yields increase while CO2, CH4, and C2 yields decrease. For W/mb ratios ≥ 0.4 h, no significant modifications are observed on the initial yields of different gases, and it is confirmed that under these conditions the initial gas composition is similar to that for thermodynamic equilibrium. For W/mb ratios < 0.4 h, a simple first-order kinetic equation has been suggested for H2 and CO formation.</description><subject>09 BIOMASS FUELS</subject><subject>Agriculture, rearing and food industries wastes</subject><subject>Applied sciences</subject><subject>Biomass</subject><subject>CARBON DIOXIDE</subject><subject>CATALYSTS</subject><subject>CHEMICAL REACTION YIELD</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>FLOW RATE</subject><subject>KINETIC EQUATIONS</subject><subject>METHANE</subject><subject>Natural energy</subject><subject>Pollution</subject><subject>PYROLYSIS</subject><subject>SYNTHESIS GAS</subject><subject>Wastes</subject><subject>WOOD WASTES</subject><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1998</creationdate><recordtype>article</recordtype><recordid>eNptkM1u1DAURi0EEkNhwRsYCRYs0l4nseMsYUR_pIEGOoDExnIcm3HJ2CPbUZkH6HvXo1Sz6ub6yt_xsfQh9JbAKYGSnFndciAtg2doQWgJBYWaPkcL4JwXlHP6Er2K8RYAKK3rBbq_cmactFMae4OXMslxHxP-re3fTTr7bP1WxojPR3-Hf8ikD8N67B2-kBF3wQ-TyhcOW4fTRj8KklW42wefVTYevJ11Gt_Iu2HKbpnwKuvWervTQaYp6PgavTByjPrN43mCfp5_WS8vi9X1xdXy06qQFW9SMRBNBqA9KXXZE8OADYaVJq-qV7SHoTcNgAJeVYwpUFSVRHLQdV-V3Ax9dYLezV4fkxVR2aTVRnnntEqCsbZt2sx8nBkVfIxBG7ELdivDXhAQh47FsePMvp_ZnYxKjiZIp2w8PiirtqlZk7FixmxM-v8xluGfyGlDxbq7Ed03Bl__fP8l1pn_MPNSRXHrp-ByKU98_wDe3Zgo</recordid><startdate>19981005</startdate><enddate>19981005</enddate><creator>Garcia, Lucia</creator><creator>Salvador, María L</creator><creator>Arauzo, Jesús</creator><creator>Bilbao, Rafael</creator><general>American Chemical Society</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>OTOTI</scope></search><sort><creationdate>19981005</creationdate><title>Influence of Catalyst Weight/Biomass Flow Rate Ratio on Gas Production in the Catalytic Pyrolysis of Pine Sawdust at Low Temperatures</title><author>Garcia, Lucia ; Salvador, María L ; Arauzo, Jesús ; Bilbao, Rafael</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a387t-d1e1d05b12e2b1f606df62fb1fcbc5b0dbf700c083366c0c5c21a80e4b328fdb3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1998</creationdate><topic>09 BIOMASS FUELS</topic><topic>Agriculture, rearing and food industries wastes</topic><topic>Applied sciences</topic><topic>Biomass</topic><topic>CARBON DIOXIDE</topic><topic>CATALYSTS</topic><topic>CHEMICAL REACTION YIELD</topic><topic>Energy</topic><topic>Exact sciences and technology</topic><topic>FLOW RATE</topic><topic>KINETIC EQUATIONS</topic><topic>METHANE</topic><topic>Natural energy</topic><topic>Pollution</topic><topic>PYROLYSIS</topic><topic>SYNTHESIS GAS</topic><topic>Wastes</topic><topic>WOOD WASTES</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Garcia, Lucia</creatorcontrib><creatorcontrib>Salvador, María L</creatorcontrib><creatorcontrib>Arauzo, Jesús</creatorcontrib><creatorcontrib>Bilbao, Rafael</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>OSTI.GOV</collection><jtitle>Industrial & engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Garcia, Lucia</au><au>Salvador, María L</au><au>Arauzo, Jesús</au><au>Bilbao, Rafael</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Influence of Catalyst Weight/Biomass Flow Rate Ratio on Gas Production in the Catalytic Pyrolysis of Pine Sawdust at Low Temperatures</atitle><jtitle>Industrial & engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>1998-10-05</date><risdate>1998</risdate><volume>37</volume><issue>10</issue><spage>3812</spage><epage>3819</epage><pages>3812-3819</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><coden>IECRED</coden><abstract>Pine sawdust catalytic pyrolysis has been studied in a fluidized bed at temperatures of 650 and 700 °C. The experimental work was carried out in a bench-scale plant based on Waterloo Fast Pyrolysis Process (WFPP) technology. The Ni−Al catalyst used was prepared by coprecipitation with a molar ratio 1:2 (Ni−Al) and calcined at 750 °C for 3 h. The catalyst was not reduced prior to the biomass reaction. The influence of the catalyst weight/biomass flow rate ratio (W/mb) on the product distribution and on the quality of the gas product obtained was analyzed. An increase of the W/mb ratio increases the total gas yield and diminishes the liquid yield. When the W/mb ratio increases, H2 and CO yields increase while CO2, CH4, and C2 yields decrease. For W/mb ratios ≥ 0.4 h, no significant modifications are observed on the initial yields of different gases, and it is confirmed that under these conditions the initial gas composition is similar to that for thermodynamic equilibrium. For W/mb ratios < 0.4 h, a simple first-order kinetic equation has been suggested for H2 and CO formation.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ie9801960</doi><tpages>8</tpages></addata></record> |
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source | ACS_美国化学学会期刊(与NSTL共建) |
subjects | 09 BIOMASS FUELS Agriculture, rearing and food industries wastes Applied sciences Biomass CARBON DIOXIDE CATALYSTS CHEMICAL REACTION YIELD Energy Exact sciences and technology FLOW RATE KINETIC EQUATIONS METHANE Natural energy Pollution PYROLYSIS SYNTHESIS GAS Wastes WOOD WASTES |
title | Influence of Catalyst Weight/Biomass Flow Rate Ratio on Gas Production in the Catalytic Pyrolysis of Pine Sawdust at Low Temperatures |
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