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Radiative slab heating analysis for various fuel gas compositions in an axial-fired reheating furnace
A transient radiative slab heating analysis was performed to investigate the effect of various fuel mixtures on the performance of an axial-fired reheating furnace. The various fuel mixtures tested were assumed to be attained by mixing COG (coke oven gas) and BFG (blast furnace gas), which are the t...
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Published in: | International journal of heat and mass transfer 2012-07, Vol.55 (15-16), p.4029-4036 |
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cites | cdi_FETCH-LOGICAL-c405t-fdf0b803222116fc5e6d6d3e2b4bd11461137c6a906d91ee7b5e1d18aca95d7a3 |
container_end_page | 4036 |
container_issue | 15-16 |
container_start_page | 4029 |
container_title | International journal of heat and mass transfer |
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creator | Han, Sang Heon Chang, Daejun |
description | A transient radiative slab heating analysis was performed to investigate the effect of various fuel mixtures on the performance of an axial-fired reheating furnace. The various fuel mixtures tested were assumed to be attained by mixing COG (coke oven gas) and BFG (blast furnace gas), which are the two main byproduct gases found in the integrated steel mill industry. The numerical prediction of radiative heat transfer was calculated using an FVM radiation solving method, which is a well-known and efficient method for curvilinear coordinates. The WSGGM (weighted sum of gray gas model) was also adopted to calculate the radiative heat transfer in composition dependent media. The entire furnace was divided into fourteen sub-zones to calculate the radiative thermal characteristics of the furnace without flow field calculations. Each sub-zone was assumed to have homogeneous media and wall temperatures. All of the medium and wall temperatures were computed by calculating the overall heat balance using some relevant assumptions. The overall heat balance was satisfied when the net heat input equaled the three sources of heat loss in each sub-zone, wall loss, skid loss, and slab heating loss. |
doi_str_mv | 10.1016/j.ijheatmasstransfer.2012.03.041 |
format | article |
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The various fuel mixtures tested were assumed to be attained by mixing COG (coke oven gas) and BFG (blast furnace gas), which are the two main byproduct gases found in the integrated steel mill industry. The numerical prediction of radiative heat transfer was calculated using an FVM radiation solving method, which is a well-known and efficient method for curvilinear coordinates. The WSGGM (weighted sum of gray gas model) was also adopted to calculate the radiative heat transfer in composition dependent media. The entire furnace was divided into fourteen sub-zones to calculate the radiative thermal characteristics of the furnace without flow field calculations. Each sub-zone was assumed to have homogeneous media and wall temperatures. All of the medium and wall temperatures were computed by calculating the overall heat balance using some relevant assumptions. The overall heat balance was satisfied when the net heat input equaled the three sources of heat loss in each sub-zone, wall loss, skid loss, and slab heating loss.</description><identifier>ISSN: 0017-9310</identifier><identifier>EISSN: 1879-2189</identifier><identifier>DOI: 10.1016/j.ijheatmasstransfer.2012.03.041</identifier><identifier>CODEN: IJHMAK</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Air pollution caused by fuel industries ; Applied sciences ; Combustion of gaseous fuels ; Combustion. Flame ; Devices using thermal energy ; Energy ; Energy. Thermal use of fuels ; Exact sciences and technology ; Fuel mixture composition ; Furnaces ; Pollution reduction ; Radiative slab heating ; Reheating furnace ; Stack gas and industrial effluent processing ; Theoretical studies. Data and constants. Metering ; WSGGM</subject><ispartof>International journal of heat and mass transfer, 2012-07, Vol.55 (15-16), p.4029-4036</ispartof><rights>2012 Elsevier Ltd</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c405t-fdf0b803222116fc5e6d6d3e2b4bd11461137c6a906d91ee7b5e1d18aca95d7a3</citedby><cites>FETCH-LOGICAL-c405t-fdf0b803222116fc5e6d6d3e2b4bd11461137c6a906d91ee7b5e1d18aca95d7a3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=25955238$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Han, Sang Heon</creatorcontrib><creatorcontrib>Chang, Daejun</creatorcontrib><title>Radiative slab heating analysis for various fuel gas compositions in an axial-fired reheating furnace</title><title>International journal of heat and mass transfer</title><description>A transient radiative slab heating analysis was performed to investigate the effect of various fuel mixtures on the performance of an axial-fired reheating furnace. The various fuel mixtures tested were assumed to be attained by mixing COG (coke oven gas) and BFG (blast furnace gas), which are the two main byproduct gases found in the integrated steel mill industry. The numerical prediction of radiative heat transfer was calculated using an FVM radiation solving method, which is a well-known and efficient method for curvilinear coordinates. The WSGGM (weighted sum of gray gas model) was also adopted to calculate the radiative heat transfer in composition dependent media. The entire furnace was divided into fourteen sub-zones to calculate the radiative thermal characteristics of the furnace without flow field calculations. Each sub-zone was assumed to have homogeneous media and wall temperatures. All of the medium and wall temperatures were computed by calculating the overall heat balance using some relevant assumptions. The overall heat balance was satisfied when the net heat input equaled the three sources of heat loss in each sub-zone, wall loss, skid loss, and slab heating loss.</description><subject>Air pollution caused by fuel industries</subject><subject>Applied sciences</subject><subject>Combustion of gaseous fuels</subject><subject>Combustion. Flame</subject><subject>Devices using thermal energy</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Exact sciences and technology</subject><subject>Fuel mixture composition</subject><subject>Furnaces</subject><subject>Pollution reduction</subject><subject>Radiative slab heating</subject><subject>Reheating furnace</subject><subject>Stack gas and industrial effluent processing</subject><subject>Theoretical studies. Data and constants. Metering</subject><subject>WSGGM</subject><issn>0017-9310</issn><issn>1879-2189</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><recordid>eNqNkE2LFDEQQIO44Ljrf8hF2Eu3qaTTHzdl0VVZEMQ9h-qksmbo6R5TPYP77zfDrF68eEoFHq-oJ8Q1qBoUtO-2ddr-JFx3yLxmnDlSrrUCXStTqwZeiA303VBp6IeXYqMUdNVgQL0Sr5m3p69q2o2g7xgSrulIkicc5UmZ5geJM06PnFjGJcsj5rQcynygST4gS7_s9gunNS0zyzQXWuLvhFMVU6YgM_3RxEOe0dOVuIg4Mb15fi_F_aePP24-V3ffbr_cfLirfKPsWsUQ1dgro7UGaKO31IY2GNJjMwaApgUwnW9xUG0YgKgbLUGAHj0ONnRoLsX12bvPy68D8ep2iT1NE85UDnCgTNND21tb0Pdn1OeFOVN0-5x2mB8L5E6F3db9W9idCjtlXClcFG-ftyF7nGJhfOK_Hm0Ha7XpC_f1zFE5_ZiKhX2i2VMotfzqwpL-f-kTv72gEQ</recordid><startdate>20120701</startdate><enddate>20120701</enddate><creator>Han, Sang Heon</creator><creator>Chang, Daejun</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope></search><sort><creationdate>20120701</creationdate><title>Radiative slab heating analysis for various fuel gas compositions in an axial-fired reheating furnace</title><author>Han, Sang Heon ; Chang, Daejun</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c405t-fdf0b803222116fc5e6d6d3e2b4bd11461137c6a906d91ee7b5e1d18aca95d7a3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2012</creationdate><topic>Air pollution caused by fuel industries</topic><topic>Applied sciences</topic><topic>Combustion of gaseous fuels</topic><topic>Combustion. Flame</topic><topic>Devices using thermal energy</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>Exact sciences and technology</topic><topic>Fuel mixture composition</topic><topic>Furnaces</topic><topic>Pollution reduction</topic><topic>Radiative slab heating</topic><topic>Reheating furnace</topic><topic>Stack gas and industrial effluent processing</topic><topic>Theoretical studies. Data and constants. Metering</topic><topic>WSGGM</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Han, Sang Heon</creatorcontrib><creatorcontrib>Chang, Daejun</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><jtitle>International journal of heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Han, Sang Heon</au><au>Chang, Daejun</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Radiative slab heating analysis for various fuel gas compositions in an axial-fired reheating furnace</atitle><jtitle>International journal of heat and mass transfer</jtitle><date>2012-07-01</date><risdate>2012</risdate><volume>55</volume><issue>15-16</issue><spage>4029</spage><epage>4036</epage><pages>4029-4036</pages><issn>0017-9310</issn><eissn>1879-2189</eissn><coden>IJHMAK</coden><abstract>A transient radiative slab heating analysis was performed to investigate the effect of various fuel mixtures on the performance of an axial-fired reheating furnace. The various fuel mixtures tested were assumed to be attained by mixing COG (coke oven gas) and BFG (blast furnace gas), which are the two main byproduct gases found in the integrated steel mill industry. The numerical prediction of radiative heat transfer was calculated using an FVM radiation solving method, which is a well-known and efficient method for curvilinear coordinates. The WSGGM (weighted sum of gray gas model) was also adopted to calculate the radiative heat transfer in composition dependent media. The entire furnace was divided into fourteen sub-zones to calculate the radiative thermal characteristics of the furnace without flow field calculations. Each sub-zone was assumed to have homogeneous media and wall temperatures. All of the medium and wall temperatures were computed by calculating the overall heat balance using some relevant assumptions. The overall heat balance was satisfied when the net heat input equaled the three sources of heat loss in each sub-zone, wall loss, skid loss, and slab heating loss.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijheatmasstransfer.2012.03.041</doi><tpages>8</tpages></addata></record> |
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language | eng |
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source | Elsevier |
subjects | Air pollution caused by fuel industries Applied sciences Combustion of gaseous fuels Combustion. Flame Devices using thermal energy Energy Energy. Thermal use of fuels Exact sciences and technology Fuel mixture composition Furnaces Pollution reduction Radiative slab heating Reheating furnace Stack gas and industrial effluent processing Theoretical studies. Data and constants. Metering WSGGM |
title | Radiative slab heating analysis for various fuel gas compositions in an axial-fired reheating furnace |
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