Hydrodynamic Flow Regimes, Gas Holdup, and Liquid Circulation in Airlift Reactors
This study reports an experimental investigation into the hydrodynamic behavior of an external-loop airlift reactor (ALR) for the air−water system. Three distinct flow regimes are identifiednamely homogeneous, transition, and heterogeneous regimes. The transition between homogeneous and heterogeneo...
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Veröffentlicht in: | Industrial & engineering chemistry research 1998-04, Vol.37 (4), p.1251-1259 |
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creator | Abashar, Mohamed E Narsingh, Udi Rouillard, Andre E Judd, Robin |
description | This study reports an experimental investigation into the hydrodynamic behavior of an external-loop airlift reactor (ALR) for the air−water system. Three distinct flow regimes are identifiednamely homogeneous, transition, and heterogeneous regimes. The transition between homogeneous and heterogeneous flow is observed to occur over a wide range rather than being merely a single point as has been previously reported in the literature. A gas holdup correlation is developed for each flow regime. The correlations fit the experimental gas holdup data with very good accuracy (within ±5%). It would appear, therefore, that a deterministic equation to describe each flow regime is likely to exist in ALRs. This equation is a function of the reactor geometry and the system's physical properties. New data concerning the axial variation of gas holdup is reported in which a minimum value is observed. This phenomenon is discussed and an explanation offered. Discrimination between two sound theoretical modelsnamely model I (Chisti et al., 1988) and model II (Garcia Calvo, 1989)shows that model I predicts satisfactorily the liquid circulation velocity with an error of less than ±10%. The good predictive features of model I may be due to the fact that it allows for a significant energy dissipation by wakes behind bubbles. Model I is now further improved by the new gas holdup correlations which are derived for the three different flow regimes. |
doi_str_mv | 10.1021/ie9704612 |
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Three distinct flow regimes are identifiednamely homogeneous, transition, and heterogeneous regimes. The transition between homogeneous and heterogeneous flow is observed to occur over a wide range rather than being merely a single point as has been previously reported in the literature. A gas holdup correlation is developed for each flow regime. The correlations fit the experimental gas holdup data with very good accuracy (within ±5%). It would appear, therefore, that a deterministic equation to describe each flow regime is likely to exist in ALRs. This equation is a function of the reactor geometry and the system's physical properties. New data concerning the axial variation of gas holdup is reported in which a minimum value is observed. This phenomenon is discussed and an explanation offered. Discrimination between two sound theoretical modelsnamely model I (Chisti et al., 1988) and model II (Garcia Calvo, 1989)shows that model I predicts satisfactorily the liquid circulation velocity with an error of less than ±10%. The good predictive features of model I may be due to the fact that it allows for a significant energy dissipation by wakes behind bubbles. 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Eng. Chem. Res</addtitle><description>This study reports an experimental investigation into the hydrodynamic behavior of an external-loop airlift reactor (ALR) for the air−water system. Three distinct flow regimes are identifiednamely homogeneous, transition, and heterogeneous regimes. The transition between homogeneous and heterogeneous flow is observed to occur over a wide range rather than being merely a single point as has been previously reported in the literature. A gas holdup correlation is developed for each flow regime. The correlations fit the experimental gas holdup data with very good accuracy (within ±5%). It would appear, therefore, that a deterministic equation to describe each flow regime is likely to exist in ALRs. This equation is a function of the reactor geometry and the system's physical properties. New data concerning the axial variation of gas holdup is reported in which a minimum value is observed. This phenomenon is discussed and an explanation offered. Discrimination between two sound theoretical modelsnamely model I (Chisti et al., 1988) and model II (Garcia Calvo, 1989)shows that model I predicts satisfactorily the liquid circulation velocity with an error of less than ±10%. The good predictive features of model I may be due to the fact that it allows for a significant energy dissipation by wakes behind bubbles. Model I is now further improved by the new gas holdup correlations which are derived for the three different flow regimes.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>CHEMICAL REACTORS</subject><subject>EFFICIENCY</subject><subject>ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION</subject><subject>Exact sciences and technology</subject><subject>FLOW MODELS</subject><subject>GASES</subject><subject>HYDRODYNAMICS</subject><subject>LIQUIDS</subject><subject>MASS TRANSFER</subject><subject>Reactors</subject><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1998</creationdate><recordtype>article</recordtype><recordid>eNpt0E1P4zAQBmALsRKlu4f9B0aCAxIBf8bOEZWPIlXapWUve7EG2wFDGhc7FfTfkyqoJ04jzTwzI70I_abknBJGL4KvFBElZXtoRCUjhSRC7qMR0VoXUmt5gA5zfiGESCnECN1PNy5Ft2lhGSy-aeI7nvunsPT5DN9CxtPYuPXqDEPr8Cy8rYPDk5DsuoEuxBaHFl-G1IS669fAdjHln-hHDU32v77qGP27uX6YTIvZn9u7yeWsAK5VV0j56GTtCChRC2JLbmtgjFRlrZyufCVUWRHQlbNeWM7Bc8ahdFRxXsK2M0ZHw92Yu2CyDZ23zza2rbedKZngPR2j08HYFHNOvjarFJaQNoYSs83L7PLq7fFgV5AtNHWC1oa8W2CMU623rBhYyJ3_2I0hvZpScSXNw9-FUTM6_3-1uDK69yeDB5vNS1yntg_lm_efQz-Dow</recordid><startdate>19980401</startdate><enddate>19980401</enddate><creator>Abashar, Mohamed E</creator><creator>Narsingh, Udi</creator><creator>Rouillard, Andre E</creator><creator>Judd, Robin</creator><general>American Chemical Society</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>OTOTI</scope></search><sort><creationdate>19980401</creationdate><title>Hydrodynamic Flow Regimes, Gas Holdup, and Liquid Circulation in Airlift Reactors</title><author>Abashar, Mohamed E ; Narsingh, Udi ; Rouillard, Andre E ; Judd, Robin</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a387t-55bd5fd0a74f40c63cfa22096f7d89e947690a89dce4c33ae323a6d17336a4c33</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1998</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>CHEMICAL REACTORS</topic><topic>EFFICIENCY</topic><topic>ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION</topic><topic>Exact sciences and technology</topic><topic>FLOW MODELS</topic><topic>GASES</topic><topic>HYDRODYNAMICS</topic><topic>LIQUIDS</topic><topic>MASS TRANSFER</topic><topic>Reactors</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Abashar, Mohamed E</creatorcontrib><creatorcontrib>Narsingh, Udi</creatorcontrib><creatorcontrib>Rouillard, Andre E</creatorcontrib><creatorcontrib>Judd, Robin</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>Abashar, Mohamed E</au><au>Narsingh, Udi</au><au>Rouillard, Andre E</au><au>Judd, Robin</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Hydrodynamic Flow Regimes, Gas Holdup, and Liquid Circulation in Airlift Reactors</atitle><jtitle>Industrial & engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>1998-04-01</date><risdate>1998</risdate><volume>37</volume><issue>4</issue><spage>1251</spage><epage>1259</epage><pages>1251-1259</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><coden>IECRED</coden><abstract>This study reports an experimental investigation into the hydrodynamic behavior of an external-loop airlift reactor (ALR) for the air−water system. Three distinct flow regimes are identifiednamely homogeneous, transition, and heterogeneous regimes. The transition between homogeneous and heterogeneous flow is observed to occur over a wide range rather than being merely a single point as has been previously reported in the literature. A gas holdup correlation is developed for each flow regime. The correlations fit the experimental gas holdup data with very good accuracy (within ±5%). It would appear, therefore, that a deterministic equation to describe each flow regime is likely to exist in ALRs. This equation is a function of the reactor geometry and the system's physical properties. New data concerning the axial variation of gas holdup is reported in which a minimum value is observed. This phenomenon is discussed and an explanation offered. Discrimination between two sound theoretical modelsnamely model I (Chisti et al., 1988) and model II (Garcia Calvo, 1989)shows that model I predicts satisfactorily the liquid circulation velocity with an error of less than ±10%. The good predictive features of model I may be due to the fact that it allows for a significant energy dissipation by wakes behind bubbles. Model I is now further improved by the new gas holdup correlations which are derived for the three different flow regimes.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ie9704612</doi><tpages>9</tpages></addata></record> |
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subjects | Applied sciences Chemical engineering CHEMICAL REACTORS EFFICIENCY ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION Exact sciences and technology FLOW MODELS GASES HYDRODYNAMICS LIQUIDS MASS TRANSFER Reactors |
title | Hydrodynamic Flow Regimes, Gas Holdup, and Liquid Circulation in Airlift Reactors |
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