Dynamic Model of Basic Oxygen Steelmaking Process Based on Multizone Reaction Kinetics: Modeling of Decarburization
In a previous study by the authors (Rout et al . in Metall Mater Trans B 49:537–557, 2018 ), a dynamic model for the BOF, employing the concept of multizone kinetics was developed. In the current study, the kinetics of decarburization reaction is investigated. The jet impact and slag–metal emulsion...
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creator | Rout, Bapin Kumar Brooks, Geoffrey Akbar Rhamdhani, M. Li, Zushu Schrama, Frank N. H. Overbosch, Aart |
description | In a previous study by the authors (Rout
et al
. in Metall Mater Trans B 49:537–557,
2018
), a dynamic model for the BOF, employing the concept of multizone kinetics was developed. In the current study, the kinetics of decarburization reaction is investigated. The jet impact and slag–metal emulsion zones were identified to be primary zones for carbon oxidation. The dynamic parameters in the rate equation of decarburization such as residence time of metal drops in the emulsion, interfacial area evolution, initial size, and the effects of surface-active oxides have been included in the kinetic rate equation of the metal droplet. A modified mass-transfer coefficient based on the ideal Langmuir adsorption equilibrium has been proposed to take into account the surface blockage effects of SiO
2
and P
2
O
5
in slag on the decarburization kinetics of a metal droplet in the emulsion. Further, a size distribution function has been included in the rate equation to evaluate the effect of droplet size on reaction kinetics. The mathematical simulation indicates that decarburization of the droplet in the emulsion is a strong function of the initial size and residence time. A modified droplet generation rate proposed previously by the authors has been used to estimate the total decarburization rate by slag–metal emulsion. The model’s prediction shows that about 76 pct of total carbon is removed by reactions in the emulsion, and the remaining is removed by reactions at the jet impact zone. The predicted bath carbon by the model has been found to be in good agreement with the industrially measured data. |
doi_str_mv | 10.1007/s11663-018-1244-5 |
format | Article |
fullrecord | <record><control><sourceid>proquest_osti_</sourceid><recordid>TN_cdi_osti_scitechconnect_22857933</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>2015879028</sourcerecordid><originalsourceid>FETCH-LOGICAL-c447t-f6aa9612a2ab000edbf4da7c044a66d203c86a1d95ea2601823c3ddce2503183</originalsourceid><addsrcrecordid>eNp1kUtPwzAQhCMEEqXwA7hF4hzwI3YSbtDyEq2KoHfLdTbFpbWL7Ui0vx5HQeqJ03qtmU-zmiS5xOgaI1TceIw5pxnCZYZJnmfsKBlgltMMV5gfxzcqaMY4ZqfJmfcrhBCvKjpI_Hhn5EardGprWKe2Se-lj-vsZ7cEk34EgPVGfmmzTN-cVeB9J4A6tSadtuug99ZA-g5SBR2_XrWBoJW_7XmdLSLHoKRbtE7vZac6T04aufZw8TeHyfzxYT56ziazp5fR3SRTeV6ErOFSVhwTSeQi5oV60eS1LBTKc8l5TRBVJZe4rhhIwuPlhCpa1woIQxSXdJhc9VjrgxZe6QDqU1ljQAVBSMmKitKDauvsdws-iJVtnYm5BEGYlUWFSMfCvUo5672DRmyd3ki3ExiJrgDRFyBiDNEVIFj0kN7jo9YswR3I_5t-AbV4iIA</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2015879028</pqid></control><display><type>article</type><title>Dynamic Model of Basic Oxygen Steelmaking Process Based on Multizone Reaction Kinetics: Modeling of Decarburization</title><source>Springer Nature - Complete Springer Journals</source><creator>Rout, Bapin Kumar ; Brooks, Geoffrey ; Akbar Rhamdhani, M. ; Li, Zushu ; Schrama, Frank N. H. ; Overbosch, Aart</creator><creatorcontrib>Rout, Bapin Kumar ; Brooks, Geoffrey ; Akbar Rhamdhani, M. ; Li, Zushu ; Schrama, Frank N. H. ; Overbosch, Aart</creatorcontrib><description>In a previous study by the authors (Rout
et al
. in Metall Mater Trans B 49:537–557,
2018
), a dynamic model for the BOF, employing the concept of multizone kinetics was developed. In the current study, the kinetics of decarburization reaction is investigated. The jet impact and slag–metal emulsion zones were identified to be primary zones for carbon oxidation. The dynamic parameters in the rate equation of decarburization such as residence time of metal drops in the emulsion, interfacial area evolution, initial size, and the effects of surface-active oxides have been included in the kinetic rate equation of the metal droplet. A modified mass-transfer coefficient based on the ideal Langmuir adsorption equilibrium has been proposed to take into account the surface blockage effects of SiO
2
and P
2
O
5
in slag on the decarburization kinetics of a metal droplet in the emulsion. Further, a size distribution function has been included in the rate equation to evaluate the effect of droplet size on reaction kinetics. The mathematical simulation indicates that decarburization of the droplet in the emulsion is a strong function of the initial size and residence time. A modified droplet generation rate proposed previously by the authors has been used to estimate the total decarburization rate by slag–metal emulsion. The model’s prediction shows that about 76 pct of total carbon is removed by reactions in the emulsion, and the remaining is removed by reactions at the jet impact zone. The predicted bath carbon by the model has been found to be in good agreement with the industrially measured data.</description><identifier>ISSN: 1073-5615</identifier><identifier>EISSN: 1543-1916</identifier><identifier>DOI: 10.1007/s11663-018-1244-5</identifier><language>eng</language><publisher>New York: Springer US</publisher><subject>ADSORPTION ; CARBON ; Characterization and Evaluation of Materials ; Chemistry and Materials Science ; Computer simulation ; DECARBURIZATION ; Decarburizing ; DISTRIBUTION FUNCTIONS ; EMULSIONS ; Impact prediction ; Kinetics ; MASS TRANSFER ; MATERIALS SCIENCE ; Mathematical models ; Metallic Materials ; Metallurgy ; METALS ; Nanotechnology ; OXIDATION ; OXYGEN ; Oxygen steel making ; Parameter identification ; PHOSPHORUS OXIDES ; Phosphorus pentoxide ; REACTION KINETICS ; Silicon dioxide ; SILICON OXIDES ; SIMULATION ; Size distribution ; SLAGS ; Structural Materials ; SURFACES ; Surfaces and Interfaces ; Thin Films</subject><ispartof>Metallurgical and materials transactions. B, Process metallurgy and materials processing science, 2018-06, Vol.49 (3), p.1022-1033</ispartof><rights>The Minerals, Metals & Materials Society and ASM International 2018</rights><rights>Metallurgical and Materials Transactions B is a copyright of Springer, (2018). All Rights Reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c447t-f6aa9612a2ab000edbf4da7c044a66d203c86a1d95ea2601823c3ddce2503183</citedby><cites>FETCH-LOGICAL-c447t-f6aa9612a2ab000edbf4da7c044a66d203c86a1d95ea2601823c3ddce2503183</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s11663-018-1244-5$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s11663-018-1244-5$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>230,314,776,780,881,27901,27902,41464,42533,51294</link.rule.ids><backlink>$$Uhttps://www.osti.gov/biblio/22857933$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Rout, Bapin Kumar</creatorcontrib><creatorcontrib>Brooks, Geoffrey</creatorcontrib><creatorcontrib>Akbar Rhamdhani, M.</creatorcontrib><creatorcontrib>Li, Zushu</creatorcontrib><creatorcontrib>Schrama, Frank N. H.</creatorcontrib><creatorcontrib>Overbosch, Aart</creatorcontrib><title>Dynamic Model of Basic Oxygen Steelmaking Process Based on Multizone Reaction Kinetics: Modeling of Decarburization</title><title>Metallurgical and materials transactions. B, Process metallurgy and materials processing science</title><addtitle>Metall Mater Trans B</addtitle><description>In a previous study by the authors (Rout
et al
. in Metall Mater Trans B 49:537–557,
2018
), a dynamic model for the BOF, employing the concept of multizone kinetics was developed. In the current study, the kinetics of decarburization reaction is investigated. The jet impact and slag–metal emulsion zones were identified to be primary zones for carbon oxidation. The dynamic parameters in the rate equation of decarburization such as residence time of metal drops in the emulsion, interfacial area evolution, initial size, and the effects of surface-active oxides have been included in the kinetic rate equation of the metal droplet. A modified mass-transfer coefficient based on the ideal Langmuir adsorption equilibrium has been proposed to take into account the surface blockage effects of SiO
2
and P
2
O
5
in slag on the decarburization kinetics of a metal droplet in the emulsion. Further, a size distribution function has been included in the rate equation to evaluate the effect of droplet size on reaction kinetics. The mathematical simulation indicates that decarburization of the droplet in the emulsion is a strong function of the initial size and residence time. A modified droplet generation rate proposed previously by the authors has been used to estimate the total decarburization rate by slag–metal emulsion. The model’s prediction shows that about 76 pct of total carbon is removed by reactions in the emulsion, and the remaining is removed by reactions at the jet impact zone. The predicted bath carbon by the model has been found to be in good agreement with the industrially measured data.</description><subject>ADSORPTION</subject><subject>CARBON</subject><subject>Characterization and Evaluation of Materials</subject><subject>Chemistry and Materials Science</subject><subject>Computer simulation</subject><subject>DECARBURIZATION</subject><subject>Decarburizing</subject><subject>DISTRIBUTION FUNCTIONS</subject><subject>EMULSIONS</subject><subject>Impact prediction</subject><subject>Kinetics</subject><subject>MASS TRANSFER</subject><subject>MATERIALS SCIENCE</subject><subject>Mathematical models</subject><subject>Metallic Materials</subject><subject>Metallurgy</subject><subject>METALS</subject><subject>Nanotechnology</subject><subject>OXIDATION</subject><subject>OXYGEN</subject><subject>Oxygen steel making</subject><subject>Parameter identification</subject><subject>PHOSPHORUS OXIDES</subject><subject>Phosphorus pentoxide</subject><subject>REACTION KINETICS</subject><subject>Silicon dioxide</subject><subject>SILICON OXIDES</subject><subject>SIMULATION</subject><subject>Size distribution</subject><subject>SLAGS</subject><subject>Structural Materials</subject><subject>SURFACES</subject><subject>Surfaces and Interfaces</subject><subject>Thin Films</subject><issn>1073-5615</issn><issn>1543-1916</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><sourceid>BENPR</sourceid><recordid>eNp1kUtPwzAQhCMEEqXwA7hF4hzwI3YSbtDyEq2KoHfLdTbFpbWL7Ui0vx5HQeqJ03qtmU-zmiS5xOgaI1TceIw5pxnCZYZJnmfsKBlgltMMV5gfxzcqaMY4ZqfJmfcrhBCvKjpI_Hhn5EardGprWKe2Se-lj-vsZ7cEk34EgPVGfmmzTN-cVeB9J4A6tSadtuug99ZA-g5SBR2_XrWBoJW_7XmdLSLHoKRbtE7vZac6T04aufZw8TeHyfzxYT56ziazp5fR3SRTeV6ErOFSVhwTSeQi5oV60eS1LBTKc8l5TRBVJZe4rhhIwuPlhCpa1woIQxSXdJhc9VjrgxZe6QDqU1ljQAVBSMmKitKDauvsdws-iJVtnYm5BEGYlUWFSMfCvUo5672DRmyd3ki3ExiJrgDRFyBiDNEVIFj0kN7jo9YswR3I_5t-AbV4iIA</recordid><startdate>20180601</startdate><enddate>20180601</enddate><creator>Rout, Bapin Kumar</creator><creator>Brooks, Geoffrey</creator><creator>Akbar Rhamdhani, M.</creator><creator>Li, Zushu</creator><creator>Schrama, Frank N. H.</creator><creator>Overbosch, Aart</creator><general>Springer US</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope><scope>3V.</scope><scope>4T-</scope><scope>4U-</scope><scope>7SR</scope><scope>7XB</scope><scope>88I</scope><scope>8AF</scope><scope>8AO</scope><scope>8BQ</scope><scope>8FD</scope><scope>8FE</scope><scope>8FG</scope><scope>8FK</scope><scope>ABJCF</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>BGLVJ</scope><scope>CCPQU</scope><scope>D1I</scope><scope>DWQXO</scope><scope>GNUQQ</scope><scope>HCIFZ</scope><scope>JG9</scope><scope>KB.</scope><scope>L6V</scope><scope>M2P</scope><scope>M7S</scope><scope>PDBOC</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PRINS</scope><scope>PTHSS</scope><scope>Q9U</scope><scope>S0X</scope><scope>OTOTI</scope></search><sort><creationdate>20180601</creationdate><title>Dynamic Model of Basic Oxygen Steelmaking Process Based on Multizone Reaction Kinetics: Modeling of Decarburization</title><author>Rout, Bapin Kumar ; Brooks, Geoffrey ; Akbar Rhamdhani, M. ; Li, Zushu ; Schrama, Frank N. H. ; Overbosch, Aart</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c447t-f6aa9612a2ab000edbf4da7c044a66d203c86a1d95ea2601823c3ddce2503183</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>ADSORPTION</topic><topic>CARBON</topic><topic>Characterization and Evaluation of Materials</topic><topic>Chemistry and Materials Science</topic><topic>Computer simulation</topic><topic>DECARBURIZATION</topic><topic>Decarburizing</topic><topic>DISTRIBUTION FUNCTIONS</topic><topic>EMULSIONS</topic><topic>Impact prediction</topic><topic>Kinetics</topic><topic>MASS TRANSFER</topic><topic>MATERIALS SCIENCE</topic><topic>Mathematical models</topic><topic>Metallic Materials</topic><topic>Metallurgy</topic><topic>METALS</topic><topic>Nanotechnology</topic><topic>OXIDATION</topic><topic>OXYGEN</topic><topic>Oxygen steel making</topic><topic>Parameter identification</topic><topic>PHOSPHORUS OXIDES</topic><topic>Phosphorus pentoxide</topic><topic>REACTION KINETICS</topic><topic>Silicon dioxide</topic><topic>SILICON OXIDES</topic><topic>SIMULATION</topic><topic>Size distribution</topic><topic>SLAGS</topic><topic>Structural Materials</topic><topic>SURFACES</topic><topic>Surfaces and Interfaces</topic><topic>Thin Films</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Rout, Bapin Kumar</creatorcontrib><creatorcontrib>Brooks, Geoffrey</creatorcontrib><creatorcontrib>Akbar Rhamdhani, M.</creatorcontrib><creatorcontrib>Li, Zushu</creatorcontrib><creatorcontrib>Schrama, Frank N. H.</creatorcontrib><creatorcontrib>Overbosch, Aart</creatorcontrib><collection>CrossRef</collection><collection>ProQuest Central (Corporate)</collection><collection>Docstoc</collection><collection>University Readers</collection><collection>Engineered Materials Abstracts</collection><collection>ProQuest Central (purchase pre-March 2016)</collection><collection>Science Database (Alumni Edition)</collection><collection>STEM Database</collection><collection>ProQuest Pharma Collection</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>ProQuest SciTech Collection</collection><collection>ProQuest Technology Collection</collection><collection>ProQuest Central (Alumni) (purchase pre-March 2016)</collection><collection>Materials Science & Engineering Collection</collection><collection>ProQuest Central (Alumni Edition)</collection><collection>ProQuest Central UK/Ireland</collection><collection>ProQuest Central Essentials</collection><collection>ProQuest Central</collection><collection>Technology Collection</collection><collection>ProQuest One Community College</collection><collection>ProQuest Materials Science Collection</collection><collection>ProQuest Central Korea</collection><collection>ProQuest Central Student</collection><collection>SciTech Premium Collection</collection><collection>Materials Research Database</collection><collection>Materials Science Database</collection><collection>ProQuest Engineering Collection</collection><collection>Science Database</collection><collection>Engineering Database</collection><collection>Materials Science Collection</collection><collection>ProQuest One Academic Eastern Edition (DO NOT USE)</collection><collection>ProQuest One Academic</collection><collection>ProQuest One Academic UKI Edition</collection><collection>ProQuest Central China</collection><collection>Engineering Collection</collection><collection>ProQuest Central Basic</collection><collection>SIRS Editorial</collection><collection>OSTI.GOV</collection><jtitle>Metallurgical and materials transactions. B, Process metallurgy and materials processing science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Rout, Bapin Kumar</au><au>Brooks, Geoffrey</au><au>Akbar Rhamdhani, M.</au><au>Li, Zushu</au><au>Schrama, Frank N. H.</au><au>Overbosch, Aart</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Dynamic Model of Basic Oxygen Steelmaking Process Based on Multizone Reaction Kinetics: Modeling of Decarburization</atitle><jtitle>Metallurgical and materials transactions. B, Process metallurgy and materials processing science</jtitle><stitle>Metall Mater Trans B</stitle><date>2018-06-01</date><risdate>2018</risdate><volume>49</volume><issue>3</issue><spage>1022</spage><epage>1033</epage><pages>1022-1033</pages><issn>1073-5615</issn><eissn>1543-1916</eissn><abstract>In a previous study by the authors (Rout
et al
. in Metall Mater Trans B 49:537–557,
2018
), a dynamic model for the BOF, employing the concept of multizone kinetics was developed. In the current study, the kinetics of decarburization reaction is investigated. The jet impact and slag–metal emulsion zones were identified to be primary zones for carbon oxidation. The dynamic parameters in the rate equation of decarburization such as residence time of metal drops in the emulsion, interfacial area evolution, initial size, and the effects of surface-active oxides have been included in the kinetic rate equation of the metal droplet. A modified mass-transfer coefficient based on the ideal Langmuir adsorption equilibrium has been proposed to take into account the surface blockage effects of SiO
2
and P
2
O
5
in slag on the decarburization kinetics of a metal droplet in the emulsion. Further, a size distribution function has been included in the rate equation to evaluate the effect of droplet size on reaction kinetics. The mathematical simulation indicates that decarburization of the droplet in the emulsion is a strong function of the initial size and residence time. A modified droplet generation rate proposed previously by the authors has been used to estimate the total decarburization rate by slag–metal emulsion. The model’s prediction shows that about 76 pct of total carbon is removed by reactions in the emulsion, and the remaining is removed by reactions at the jet impact zone. The predicted bath carbon by the model has been found to be in good agreement with the industrially measured data.</abstract><cop>New York</cop><pub>Springer US</pub><doi>10.1007/s11663-018-1244-5</doi><tpages>12</tpages></addata></record> |
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source | Springer Nature - Complete Springer Journals |
subjects | ADSORPTION CARBON Characterization and Evaluation of Materials Chemistry and Materials Science Computer simulation DECARBURIZATION Decarburizing DISTRIBUTION FUNCTIONS EMULSIONS Impact prediction Kinetics MASS TRANSFER MATERIALS SCIENCE Mathematical models Metallic Materials Metallurgy METALS Nanotechnology OXIDATION OXYGEN Oxygen steel making Parameter identification PHOSPHORUS OXIDES Phosphorus pentoxide REACTION KINETICS Silicon dioxide SILICON OXIDES SIMULATION Size distribution SLAGS Structural Materials SURFACES Surfaces and Interfaces Thin Films |
title | Dynamic Model of Basic Oxygen Steelmaking Process Based on Multizone Reaction Kinetics: Modeling of Decarburization |
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