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Noncatalytic gas-solid reactions in a vertical pneumatic transport reactor
A heterogeneous model is developed to account for noncatalytic gas‐solid reactions in a vertical pneumatic transport reactor. The model takes into consideration both the positive and negative variations of the solid porosity and the variation of the gas diffusivity with the reaction. The method of l...
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Published in: | AIChE journal 1984-01, Vol.30 (1), p.21-29 |
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cites | cdi_FETCH-LOGICAL-c4135-1fbd57a82436a50881b04bdd7f9eec43794cab8f62c213a7acd6e6f76ac7454a3 |
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container_title | AIChE journal |
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creator | Fan, Liang-Shih Satija, Sunil Kim, B. C. Nack, H. |
description | A heterogeneous model is developed to account for noncatalytic gas‐solid reactions in a vertical pneumatic transport reactor. The model takes into consideration both the positive and negative variations of the solid porosity and the variation of the gas diffusivity with the reaction. The method of lines utilizing the second order centered finite difference scheme for the spatial discretization is employed to obtain the model solution.
Experiments utilizing a vertical pneumatic transport reactor of a laboratory scale are performed to study the reaction between limestone and sulfur dioxide generated from coal combustion. The reactor is of 16.2 cm ID and 610 cm in length. The experimental data for sulfur retention are reported for various superficial gas velocities and calcium‐sulfur molar ratios. Verification of the model with experimental data is conducted. The agreement between the model prediction and experimental data is satisfactory. |
doi_str_mv | 10.1002/aic.690300105 |
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Experiments utilizing a vertical pneumatic transport reactor of a laboratory scale are performed to study the reaction between limestone and sulfur dioxide generated from coal combustion. The reactor is of 16.2 cm ID and 610 cm in length. The experimental data for sulfur retention are reported for various superficial gas velocities and calcium‐sulfur molar ratios. Verification of the model with experimental data is conducted. The agreement between the model prediction and experimental data is satisfactory.</description><identifier>ISSN: 0001-1541</identifier><identifier>EISSN: 1547-5905</identifier><identifier>DOI: 10.1002/aic.690300105</identifier><identifier>CODEN: AICEAC</identifier><language>eng</language><publisher>New York: American Institute of Chemical Engineers</publisher><subject>Applied sciences ; Combustion of solid fuels ; Combustion. Flame ; Energy ; Energy. Thermal use of fuels ; Exact sciences and technology ; Theoretical studies. Data and constants. Metering</subject><ispartof>AIChE journal, 1984-01, Vol.30 (1), p.21-29</ispartof><rights>Copyright © 1984 American Institute of Chemical Engineers</rights><rights>1984 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c4135-1fbd57a82436a50881b04bdd7f9eec43794cab8f62c213a7acd6e6f76ac7454a3</citedby><cites>FETCH-LOGICAL-c4135-1fbd57a82436a50881b04bdd7f9eec43794cab8f62c213a7acd6e6f76ac7454a3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Faic.690300105$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Faic.690300105$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,776,780,1410,4010,27900,27901,27902,46024,46448</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=9464555$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Fan, Liang-Shih</creatorcontrib><creatorcontrib>Satija, Sunil</creatorcontrib><creatorcontrib>Kim, B. C.</creatorcontrib><creatorcontrib>Nack, H.</creatorcontrib><title>Noncatalytic gas-solid reactions in a vertical pneumatic transport reactor</title><title>AIChE journal</title><addtitle>AIChE J</addtitle><description>A heterogeneous model is developed to account for noncatalytic gas‐solid reactions in a vertical pneumatic transport reactor. The model takes into consideration both the positive and negative variations of the solid porosity and the variation of the gas diffusivity with the reaction. The method of lines utilizing the second order centered finite difference scheme for the spatial discretization is employed to obtain the model solution.
Experiments utilizing a vertical pneumatic transport reactor of a laboratory scale are performed to study the reaction between limestone and sulfur dioxide generated from coal combustion. The reactor is of 16.2 cm ID and 610 cm in length. The experimental data for sulfur retention are reported for various superficial gas velocities and calcium‐sulfur molar ratios. Verification of the model with experimental data is conducted. The agreement between the model prediction and experimental data is satisfactory.</description><subject>Applied sciences</subject><subject>Combustion of solid fuels</subject><subject>Combustion. Flame</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Exact sciences and technology</subject><subject>Theoretical studies. Data and constants. Metering</subject><issn>0001-1541</issn><issn>1547-5905</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1984</creationdate><recordtype>article</recordtype><recordid>eNp9kE1PwzAMhiMEEmNw5N4D10LSfLXHMcE2NA0QII6RmyYo0LVVUj7278nUaeLEybL92H79InRO8CXBOLsCpy9FgSnGBPMDNCKcyZQXmB-iEY7FNBbIMToJ4T1mmcyzEbpbtY2GHupN73TyBiENbe2qxBvQvWubkLgmgeTL-NiHOuka87mGLdt7aELX-n5gW3-KjizUwZzt4hi93N48T-fp8n62mE6WqWaE8pTYsuIS8oxRARznOSkxK6tK2sIYzagsmIYytyLTGaEgQVfCCCsFaMk4AzpG6bBX-zYEb6zqvFuD3yiC1dYIFY1QeyMifzHwHYT4go26tQv7oYIJxvkWkwP27Wqz-X-nmiymfw_sBLnQm5_9JPgPJSSVXL2uZkrOH64z_iTUI_0F_YF94Q</recordid><startdate>198401</startdate><enddate>198401</enddate><creator>Fan, Liang-Shih</creator><creator>Satija, Sunil</creator><creator>Kim, B. C.</creator><creator>Nack, H.</creator><general>American Institute of Chemical Engineers</general><general>Wiley Subscription Services</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>198401</creationdate><title>Noncatalytic gas-solid reactions in a vertical pneumatic transport reactor</title><author>Fan, Liang-Shih ; Satija, Sunil ; Kim, B. C. ; Nack, H.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c4135-1fbd57a82436a50881b04bdd7f9eec43794cab8f62c213a7acd6e6f76ac7454a3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1984</creationdate><topic>Applied sciences</topic><topic>Combustion of solid fuels</topic><topic>Combustion. Flame</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>Exact sciences and technology</topic><topic>Theoretical studies. Data and constants. Metering</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Fan, Liang-Shih</creatorcontrib><creatorcontrib>Satija, Sunil</creatorcontrib><creatorcontrib>Kim, B. C.</creatorcontrib><creatorcontrib>Nack, H.</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><jtitle>AIChE journal</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Fan, Liang-Shih</au><au>Satija, Sunil</au><au>Kim, B. C.</au><au>Nack, H.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Noncatalytic gas-solid reactions in a vertical pneumatic transport reactor</atitle><jtitle>AIChE journal</jtitle><addtitle>AIChE J</addtitle><date>1984-01</date><risdate>1984</risdate><volume>30</volume><issue>1</issue><spage>21</spage><epage>29</epage><pages>21-29</pages><issn>0001-1541</issn><eissn>1547-5905</eissn><coden>AICEAC</coden><abstract>A heterogeneous model is developed to account for noncatalytic gas‐solid reactions in a vertical pneumatic transport reactor. The model takes into consideration both the positive and negative variations of the solid porosity and the variation of the gas diffusivity with the reaction. The method of lines utilizing the second order centered finite difference scheme for the spatial discretization is employed to obtain the model solution.
Experiments utilizing a vertical pneumatic transport reactor of a laboratory scale are performed to study the reaction between limestone and sulfur dioxide generated from coal combustion. The reactor is of 16.2 cm ID and 610 cm in length. The experimental data for sulfur retention are reported for various superficial gas velocities and calcium‐sulfur molar ratios. Verification of the model with experimental data is conducted. The agreement between the model prediction and experimental data is satisfactory.</abstract><cop>New York</cop><pub>American Institute of Chemical Engineers</pub><doi>10.1002/aic.690300105</doi><tpages>9</tpages></addata></record> |
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subjects | Applied sciences Combustion of solid fuels Combustion. Flame Energy Energy. Thermal use of fuels Exact sciences and technology Theoretical studies. Data and constants. Metering |
title | Noncatalytic gas-solid reactions in a vertical pneumatic transport reactor |
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