Computation of turbulence and dispersion of cork in the NETL riser
The knowledge of dispersion coefficients is essential for reliable design of gasifiers. However, a literature review had shown that dispersion coefficients in fluidized beds differ by more than five orders of magnitude. This study presents a comparison of the computed axial solids dispersion coeffic...
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| Veröffentlicht in: | Chemical engineering science 2008-04, Vol.63 (8), p.2135-2148 |
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| creator | Jiradilok, Veeraya Gidaspow, Dimitri Breault, Ronald W. Shadle, Lawrence J. Guenther, Chris Shi, Shaoping |
| description | The knowledge of dispersion coefficients is essential for reliable design of gasifiers. However, a literature review had shown that dispersion coefficients in fluidized beds differ by more than five orders of magnitude. This study presents a comparison of the computed axial solids dispersion coefficients for cork particles to the NETL riser cork data. The turbulence properties, the Reynolds stresses, the granular temperature spectra and the radial and axial gas and solids dispersion coefficients are computed.
The standard kinetic theory model described in Gidaspow's 1994 book, Multiphase Flow and Fluidization, Academic Press and the IIT and Fluent codes were used to compute the measured axial solids volume fraction profiles for flow of cork particles in the NETL riser. The Johnson–Jackson boundary conditions were used. Standard drag correlations were used. This study shows that the computed solids volume fractions for the low flux flow are within the experimental error of those measured, using a two-dimensional model. At higher solids fluxes the simulated solids volume fractions are close to the experimental measurements, but deviate significantly at the top of the riser. This disagreement is due to use of simplified geometry in the two-dimensional simulation. There is a good agreement between the experiment and the three-dimensional simulation for a high flux condition.
This study concludes that the axial and radial gas and solids dispersion coefficients in risers operating in the turbulent flow regime can be computed using a multiphase computational fluid dynamics model. |
| doi_str_mv | 10.1016/j.ces.2008.01.019 |
| format | Article |
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The standard kinetic theory model described in Gidaspow's 1994 book, Multiphase Flow and Fluidization, Academic Press and the IIT and Fluent codes were used to compute the measured axial solids volume fraction profiles for flow of cork particles in the NETL riser. The Johnson–Jackson boundary conditions were used. Standard drag correlations were used. This study shows that the computed solids volume fractions for the low flux flow are within the experimental error of those measured, using a two-dimensional model. At higher solids fluxes the simulated solids volume fractions are close to the experimental measurements, but deviate significantly at the top of the riser. This disagreement is due to use of simplified geometry in the two-dimensional simulation. There is a good agreement between the experiment and the three-dimensional simulation for a high flux condition.
This study concludes that the axial and radial gas and solids dispersion coefficients in risers operating in the turbulent flow regime can be computed using a multiphase computational fluid dynamics model.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/j.ces.2008.01.019</identifier><identifier>CODEN: CESCAC</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Applied sciences ; Chemical engineering ; Computational fluid dynamics ; CORK ; DESIGN ; DISPERSIONS ; DRAG ; ENGINEERING ; Exact sciences and technology ; FLOW MODELS ; Fluidization ; FLUIDIZED BEDS ; GAS GENERATORS ; Gas-particle flow ; Hydrodynamics of contact apparatus ; Reynolds stress ; TURBULENCE ; TWO-PHASE FLOW</subject><ispartof>Chemical engineering science, 2008-04, Vol.63 (8), p.2135-2148</ispartof><rights>2008</rights><rights>2008 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c450t-5e76e3ff9af694498c0cc19a7ebf62a06452db386d23fb5370e746dcd41ecf723</citedby><cites>FETCH-LOGICAL-c450t-5e76e3ff9af694498c0cc19a7ebf62a06452db386d23fb5370e746dcd41ecf723</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0009250908000249$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>230,314,776,780,881,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=20241941$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.osti.gov/biblio/934997$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Jiradilok, Veeraya</creatorcontrib><creatorcontrib>Gidaspow, Dimitri</creatorcontrib><creatorcontrib>Breault, Ronald W.</creatorcontrib><creatorcontrib>Shadle, Lawrence J.</creatorcontrib><creatorcontrib>Guenther, Chris</creatorcontrib><creatorcontrib>Shi, Shaoping</creatorcontrib><creatorcontrib>National Energy Technology Laboratory (NETL), Pittsburgh, PA, Morgantown, WV, and Albany, OR</creatorcontrib><title>Computation of turbulence and dispersion of cork in the NETL riser</title><title>Chemical engineering science</title><description>The knowledge of dispersion coefficients is essential for reliable design of gasifiers. However, a literature review had shown that dispersion coefficients in fluidized beds differ by more than five orders of magnitude. This study presents a comparison of the computed axial solids dispersion coefficients for cork particles to the NETL riser cork data. The turbulence properties, the Reynolds stresses, the granular temperature spectra and the radial and axial gas and solids dispersion coefficients are computed.
The standard kinetic theory model described in Gidaspow's 1994 book, Multiphase Flow and Fluidization, Academic Press and the IIT and Fluent codes were used to compute the measured axial solids volume fraction profiles for flow of cork particles in the NETL riser. The Johnson–Jackson boundary conditions were used. Standard drag correlations were used. This study shows that the computed solids volume fractions for the low flux flow are within the experimental error of those measured, using a two-dimensional model. At higher solids fluxes the simulated solids volume fractions are close to the experimental measurements, but deviate significantly at the top of the riser. This disagreement is due to use of simplified geometry in the two-dimensional simulation. There is a good agreement between the experiment and the three-dimensional simulation for a high flux condition.
This study concludes that the axial and radial gas and solids dispersion coefficients in risers operating in the turbulent flow regime can be computed using a multiphase computational fluid dynamics model.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Computational fluid dynamics</subject><subject>CORK</subject><subject>DESIGN</subject><subject>DISPERSIONS</subject><subject>DRAG</subject><subject>ENGINEERING</subject><subject>Exact sciences and technology</subject><subject>FLOW MODELS</subject><subject>Fluidization</subject><subject>FLUIDIZED BEDS</subject><subject>GAS GENERATORS</subject><subject>Gas-particle flow</subject><subject>Hydrodynamics of contact apparatus</subject><subject>Reynolds stress</subject><subject>TURBULENCE</subject><subject>TWO-PHASE FLOW</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2008</creationdate><recordtype>article</recordtype><recordid>eNp9kE1rGzEQQEVpoG7SH9Db5pDe1hlptSuLnFqTJgGTXNKzkGdHRO565UjaQP59tdjkWBgYhnnzwWPsO4clB95d75ZIaSkAVkvgJfQntuAr1dRSQvuZLQBA16IF_YV9TWlXSqU4LNivddgfpmyzD2MVXJWnuJ0GGpEqO_ZV79OBYjo1McS_lR-r_ELV4-3zpoo-UbxgZ84Oib6d8jn78_v2eX1fb57uHtY_NzXKFnLdkuqocU5b12kp9QoBkWuraOs6YaGTrei3zarrReO2baOAlOx67CUndEo05-zyuDek7E1CnwlfMIwjYTa6kVqrwvw4MocYXidK2ex9QhoGO1KYkmmEUroVsoD8CGIMKUVy5hD93sZ3w8HMRs3OFKNmNmqAl9Bl5uq03Ca0g4t2RJ8-BgUIybXkhbs5clRsvHmK87Oz0t7H-dc--P9c-QeyBIpV</recordid><startdate>20080401</startdate><enddate>20080401</enddate><creator>Jiradilok, Veeraya</creator><creator>Gidaspow, Dimitri</creator><creator>Breault, Ronald W.</creator><creator>Shadle, Lawrence J.</creator><creator>Guenther, Chris</creator><creator>Shi, Shaoping</creator><general>Elsevier Ltd</general><general>Elsevier</general><general>Elsevier, Ltd</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7U5</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>L7M</scope><scope>OTOTI</scope></search><sort><creationdate>20080401</creationdate><title>Computation of turbulence and dispersion of cork in the NETL riser</title><author>Jiradilok, Veeraya ; Gidaspow, Dimitri ; Breault, Ronald W. ; Shadle, Lawrence J. ; Guenther, Chris ; Shi, Shaoping</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c450t-5e76e3ff9af694498c0cc19a7ebf62a06452db386d23fb5370e746dcd41ecf723</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2008</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Computational fluid dynamics</topic><topic>CORK</topic><topic>DESIGN</topic><topic>DISPERSIONS</topic><topic>DRAG</topic><topic>ENGINEERING</topic><topic>Exact sciences and technology</topic><topic>FLOW MODELS</topic><topic>Fluidization</topic><topic>FLUIDIZED BEDS</topic><topic>GAS GENERATORS</topic><topic>Gas-particle flow</topic><topic>Hydrodynamics of contact apparatus</topic><topic>Reynolds stress</topic><topic>TURBULENCE</topic><topic>TWO-PHASE FLOW</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Jiradilok, Veeraya</creatorcontrib><creatorcontrib>Gidaspow, Dimitri</creatorcontrib><creatorcontrib>Breault, Ronald W.</creatorcontrib><creatorcontrib>Shadle, Lawrence J.</creatorcontrib><creatorcontrib>Guenther, Chris</creatorcontrib><creatorcontrib>Shi, Shaoping</creatorcontrib><creatorcontrib>National Energy Technology Laboratory (NETL), Pittsburgh, PA, Morgantown, WV, and Albany, OR</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>OSTI.GOV</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Jiradilok, Veeraya</au><au>Gidaspow, Dimitri</au><au>Breault, Ronald W.</au><au>Shadle, Lawrence J.</au><au>Guenther, Chris</au><au>Shi, Shaoping</au><aucorp>National Energy Technology Laboratory (NETL), Pittsburgh, PA, Morgantown, WV, and Albany, OR</aucorp><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Computation of turbulence and dispersion of cork in the NETL riser</atitle><jtitle>Chemical engineering science</jtitle><date>2008-04-01</date><risdate>2008</risdate><volume>63</volume><issue>8</issue><spage>2135</spage><epage>2148</epage><pages>2135-2148</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>The knowledge of dispersion coefficients is essential for reliable design of gasifiers. However, a literature review had shown that dispersion coefficients in fluidized beds differ by more than five orders of magnitude. This study presents a comparison of the computed axial solids dispersion coefficients for cork particles to the NETL riser cork data. The turbulence properties, the Reynolds stresses, the granular temperature spectra and the radial and axial gas and solids dispersion coefficients are computed.
The standard kinetic theory model described in Gidaspow's 1994 book, Multiphase Flow and Fluidization, Academic Press and the IIT and Fluent codes were used to compute the measured axial solids volume fraction profiles for flow of cork particles in the NETL riser. The Johnson–Jackson boundary conditions were used. Standard drag correlations were used. This study shows that the computed solids volume fractions for the low flux flow are within the experimental error of those measured, using a two-dimensional model. At higher solids fluxes the simulated solids volume fractions are close to the experimental measurements, but deviate significantly at the top of the riser. This disagreement is due to use of simplified geometry in the two-dimensional simulation. There is a good agreement between the experiment and the three-dimensional simulation for a high flux condition.
This study concludes that the axial and radial gas and solids dispersion coefficients in risers operating in the turbulent flow regime can be computed using a multiphase computational fluid dynamics model.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ces.2008.01.019</doi><tpages>14</tpages></addata></record> |
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| subjects | Applied sciences Chemical engineering Computational fluid dynamics CORK DESIGN DISPERSIONS DRAG ENGINEERING Exact sciences and technology FLOW MODELS Fluidization FLUIDIZED BEDS GAS GENERATORS Gas-particle flow Hydrodynamics of contact apparatus Reynolds stress TURBULENCE TWO-PHASE FLOW |
| title | Computation of turbulence and dispersion of cork in the NETL riser |
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