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A CFD modeling of the gas-solid two-phase flow in an FCC riser under the electrostatic conditions
ABSTRACT Electrostatics is an inevitable phenomenon in fluidization processes and granular flow, where collisions between particulates and walls with different materials occur. In this work, a two‐dimensional computational fluid dynamics model based on the Eulerian–Eulerian approach was applied and...
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Published in: | Asia-Pacific journal of chemical engineering 2014-09, Vol.9 (5), p.645-655 |
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container_end_page | 655 |
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container_title | Asia-Pacific journal of chemical engineering |
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creator | Jiang, Li Fang-Zhi, Xiao Zheng-Hong, Luo |
description | ABSTRACT
Electrostatics is an inevitable phenomenon in fluidization processes and granular flow, where collisions between particulates and walls with different materials occur. In this work, a two‐dimensional computational fluid dynamics model based on the Eulerian–Eulerian approach was applied and coupled with a first‐principles electrostatic model to describe the gas–solid two‐phase flow behavior in a fluid catalytic cracking (FCC) riser reactor under the electrostatic conditions. The coupled model was used to predict the main gas–solid flow distribution parameters in the FCC riser, such as electric potential, particle volume fraction, gas‐phase temperature, and gas‐phase component fractions. The simulation results showed that the electrostatic had a significant influence on the particle distribution in the bottom dense region of the FCC riser, whereas it had a weak influence in the upper dilute region at the cold‐flow conditions. The simulation results also showed that the electrostatic had a weak influence on the particle concentration, gas‐phase temperature, and lump concentration distributions when the cracking reaction was considered. © 2014 Curtin University of Technology and John Wiley & Sons, Ltd. |
doi_str_mv | 10.1002/apj.1793 |
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Electrostatics is an inevitable phenomenon in fluidization processes and granular flow, where collisions between particulates and walls with different materials occur. In this work, a two‐dimensional computational fluid dynamics model based on the Eulerian–Eulerian approach was applied and coupled with a first‐principles electrostatic model to describe the gas–solid two‐phase flow behavior in a fluid catalytic cracking (FCC) riser reactor under the electrostatic conditions. The coupled model was used to predict the main gas–solid flow distribution parameters in the FCC riser, such as electric potential, particle volume fraction, gas‐phase temperature, and gas‐phase component fractions. The simulation results showed that the electrostatic had a significant influence on the particle distribution in the bottom dense region of the FCC riser, whereas it had a weak influence in the upper dilute region at the cold‐flow conditions. The simulation results also showed that the electrostatic had a weak influence on the particle concentration, gas‐phase temperature, and lump concentration distributions when the cracking reaction was considered. © 2014 Curtin University of Technology and John Wiley & Sons, Ltd.</description><identifier>ISSN: 1932-2135</identifier><identifier>EISSN: 1932-2143</identifier><identifier>DOI: 10.1002/apj.1793</identifier><language>eng</language><publisher>Blackwell Publishing Ltd</publisher><subject>CFD simulation ; Computational fluid dynamics ; Computer simulation ; electrostatic modeling ; Electrostatics ; Euler-Euler approach ; FCC riser ; Flow distribution ; Joining ; Mathematical models ; Particulates ; Risers</subject><ispartof>Asia-Pacific journal of chemical engineering, 2014-09, Vol.9 (5), p.645-655</ispartof><rights>2014 Curtin University of Technology and John Wiley & Sons, Ltd.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c4063-ddd7ec2b44bc5401f4bff2f0fa0900aab6ecba683e2fdc4d3c34fbdf908c597c3</citedby><cites>FETCH-LOGICAL-c4063-ddd7ec2b44bc5401f4bff2f0fa0900aab6ecba683e2fdc4d3c34fbdf908c597c3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Jiang, Li</creatorcontrib><creatorcontrib>Fang-Zhi, Xiao</creatorcontrib><creatorcontrib>Zheng-Hong, Luo</creatorcontrib><title>A CFD modeling of the gas-solid two-phase flow in an FCC riser under the electrostatic conditions</title><title>Asia-Pacific journal of chemical engineering</title><addtitle>Asia-Pac. J. Chem. Eng</addtitle><description>ABSTRACT
Electrostatics is an inevitable phenomenon in fluidization processes and granular flow, where collisions between particulates and walls with different materials occur. In this work, a two‐dimensional computational fluid dynamics model based on the Eulerian–Eulerian approach was applied and coupled with a first‐principles electrostatic model to describe the gas–solid two‐phase flow behavior in a fluid catalytic cracking (FCC) riser reactor under the electrostatic conditions. The coupled model was used to predict the main gas–solid flow distribution parameters in the FCC riser, such as electric potential, particle volume fraction, gas‐phase temperature, and gas‐phase component fractions. The simulation results showed that the electrostatic had a significant influence on the particle distribution in the bottom dense region of the FCC riser, whereas it had a weak influence in the upper dilute region at the cold‐flow conditions. The simulation results also showed that the electrostatic had a weak influence on the particle concentration, gas‐phase temperature, and lump concentration distributions when the cracking reaction was considered. © 2014 Curtin University of Technology and John Wiley & Sons, Ltd.</description><subject>CFD simulation</subject><subject>Computational fluid dynamics</subject><subject>Computer simulation</subject><subject>electrostatic modeling</subject><subject>Electrostatics</subject><subject>Euler-Euler approach</subject><subject>FCC riser</subject><subject>Flow distribution</subject><subject>Joining</subject><subject>Mathematical models</subject><subject>Particulates</subject><subject>Risers</subject><issn>1932-2135</issn><issn>1932-2143</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2014</creationdate><recordtype>article</recordtype><recordid>eNp10DtPwzAQB_AIgUQpSHwEjywpfiVpxiqlBVQBAw-JxXL8aF3cONiuSr89qYqKGFjubvjd6fRPkksEBwhCfM3b5QAVJTlKeqgkOMWIkuPDTLLT5CyEJYQZxTntJXwEqskYrJxU1jRz4DSICwXmPKTBWSNB3Li0XfCggLZuA0wDeAMmVQW8CcqDdSO7ultRVonoXYg8GgGEa6SJxjXhPDnR3AZ18dP7ycvk5rm6TWeP07tqNEsFhTlJpZSFErimtBYZhUjTWmusoeawhJDzOlei5vmQKKyloJIIQnUtdQmHIisLQfrJ1f5u693nWoXIViYIZS1vlFsHhnJcEgqzAv5S0f0bvNKs9WbF_ZYhyHYpsi5Ftkuxo-meboxV238dGz3d__UmRPV18Nx_sLwgRcbeHqaMDMfF6zsq2Zh8A1cggww</recordid><startdate>201409</startdate><enddate>201409</enddate><creator>Jiang, Li</creator><creator>Fang-Zhi, Xiao</creator><creator>Zheng-Hong, Luo</creator><general>Blackwell Publishing Ltd</general><scope>BSCLL</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>7U5</scope><scope>8FD</scope><scope>FR3</scope><scope>L7M</scope></search><sort><creationdate>201409</creationdate><title>A CFD modeling of the gas-solid two-phase flow in an FCC riser under the electrostatic conditions</title><author>Jiang, Li ; Fang-Zhi, Xiao ; Zheng-Hong, Luo</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c4063-ddd7ec2b44bc5401f4bff2f0fa0900aab6ecba683e2fdc4d3c34fbdf908c597c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2014</creationdate><topic>CFD simulation</topic><topic>Computational fluid dynamics</topic><topic>Computer simulation</topic><topic>electrostatic modeling</topic><topic>Electrostatics</topic><topic>Euler-Euler approach</topic><topic>FCC riser</topic><topic>Flow distribution</topic><topic>Joining</topic><topic>Mathematical models</topic><topic>Particulates</topic><topic>Risers</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Jiang, Li</creatorcontrib><creatorcontrib>Fang-Zhi, Xiao</creatorcontrib><creatorcontrib>Zheng-Hong, Luo</creatorcontrib><collection>Istex</collection><collection>CrossRef</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Asia-Pacific journal of chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Jiang, Li</au><au>Fang-Zhi, Xiao</au><au>Zheng-Hong, Luo</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A CFD modeling of the gas-solid two-phase flow in an FCC riser under the electrostatic conditions</atitle><jtitle>Asia-Pacific journal of chemical engineering</jtitle><addtitle>Asia-Pac. J. Chem. Eng</addtitle><date>2014-09</date><risdate>2014</risdate><volume>9</volume><issue>5</issue><spage>645</spage><epage>655</epage><pages>645-655</pages><issn>1932-2135</issn><eissn>1932-2143</eissn><abstract>ABSTRACT
Electrostatics is an inevitable phenomenon in fluidization processes and granular flow, where collisions between particulates and walls with different materials occur. In this work, a two‐dimensional computational fluid dynamics model based on the Eulerian–Eulerian approach was applied and coupled with a first‐principles electrostatic model to describe the gas–solid two‐phase flow behavior in a fluid catalytic cracking (FCC) riser reactor under the electrostatic conditions. The coupled model was used to predict the main gas–solid flow distribution parameters in the FCC riser, such as electric potential, particle volume fraction, gas‐phase temperature, and gas‐phase component fractions. The simulation results showed that the electrostatic had a significant influence on the particle distribution in the bottom dense region of the FCC riser, whereas it had a weak influence in the upper dilute region at the cold‐flow conditions. The simulation results also showed that the electrostatic had a weak influence on the particle concentration, gas‐phase temperature, and lump concentration distributions when the cracking reaction was considered. © 2014 Curtin University of Technology and John Wiley & Sons, Ltd.</abstract><pub>Blackwell Publishing Ltd</pub><doi>10.1002/apj.1793</doi><tpages>11</tpages></addata></record> |
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subjects | CFD simulation Computational fluid dynamics Computer simulation electrostatic modeling Electrostatics Euler-Euler approach FCC riser Flow distribution Joining Mathematical models Particulates Risers |
title | A CFD modeling of the gas-solid two-phase flow in an FCC riser under the electrostatic conditions |
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