Analysis of transient combustion of a multicomponent liquid fuel droplet
The transient combustion of a multicomponent liquid fuel droplet has been studied. The unsteady effects caused by the liquid- and gas-phase processes are considered. The numerical results demonstrate that due to the process of fuel vapor accumulation within the inner region to the flame and to the h...
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Veröffentlicht in: | Combustion and flame 1991-03, Vol.84 (1), p.197-209 |
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description | The transient combustion of a multicomponent liquid fuel droplet has been studied. The unsteady effects caused by the liquid- and gas-phase processes are considered. The numerical results demonstrate that due to the process of fuel vapor accumulation within the inner region to the flame and to the high liquid-phase mass diffusional resistance, a situation is reached where the concentration of fuel vapor in the inner zone of the flame or in the immediate vicinity of the droplet surface exceeds that at the droplet surface for certain values of the liquid-phase Lewis number. This results in a suppression of the mass vaporization rate (i.e., negative vaporization rate) without any indication of flame extinction. The results also indicate that with the increase in the volatility differentials between the mixture constituents vaporization is suppressed earlier in the droplet lifetime. However, by decreasing the liquid Lewis number, this phenomenon can be eliminated and the complete droplet lifetime can be computed. For example, the numerical results show that for a 50-50 by mass heptane-decane droplet, a liquid-phase Lewis number larger than three results in suppression of vaporization. |
doi_str_mv | 10.1016/0010-2180(91)90048-G |
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The unsteady effects caused by the liquid- and gas-phase processes are considered. The numerical results demonstrate that due to the process of fuel vapor accumulation within the inner region to the flame and to the high liquid-phase mass diffusional resistance, a situation is reached where the concentration of fuel vapor in the inner zone of the flame or in the immediate vicinity of the droplet surface exceeds that at the droplet surface for certain values of the liquid-phase Lewis number. This results in a suppression of the mass vaporization rate (i.e., negative vaporization rate) without any indication of flame extinction. The results also indicate that with the increase in the volatility differentials between the mixture constituents vaporization is suppressed earlier in the droplet lifetime. However, by decreasing the liquid Lewis number, this phenomenon can be eliminated and the complete droplet lifetime can be computed. For example, the numerical results show that for a 50-50 by mass heptane-decane droplet, a liquid-phase Lewis number larger than three results in suppression of vaporization.</description><identifier>ISSN: 0010-2180</identifier><identifier>EISSN: 1556-2921</identifier><identifier>DOI: 10.1016/0010-2180(91)90048-G</identifier><identifier>CODEN: CBFMAO</identifier><language>eng</language><publisher>New York, NY: Elsevier Inc</publisher><subject>02 PETROLEUM ; 025000 - Petroleum- Combustion ; ALKANES ; Applied sciences ; CHEMICAL REACTION KINETICS ; COMBUSTION KINETICS ; Combustion of liquid fuels ; Combustion. Flame ; DECANE ; Energy ; Energy. Thermal use of fuels ; EVAPORATION ; Exact sciences and technology ; FLUIDS ; FUELS ; GASES ; HEPTANE ; HYDROCARBONS ; KINETICS ; LIQUID FUELS ; ORGANIC COMPOUNDS ; PHASE TRANSFORMATIONS ; REACTION KINETICS ; Theoretical studies. Data and constants. Metering ; VAPORS ; VOLATILITY</subject><ispartof>Combustion and flame, 1991-03, Vol.84 (1), p.197-209</ispartof><rights>1991</rights><rights>1991 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c392t-7362369975f148b7b2a881a14b87aedcd0e338adb9bb139afc5c3013a0ddb5653</citedby><cites>FETCH-LOGICAL-c392t-7362369975f148b7b2a881a14b87aedcd0e338adb9bb139afc5c3013a0ddb5653</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/0010-2180(91)90048-G$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>230,314,777,781,882,3537,27905,27906,45976</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=19579299$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.osti.gov/biblio/5647545$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Mawid, M.</creatorcontrib><creatorcontrib>Aggarwal, S.K.</creatorcontrib><title>Analysis of transient combustion of a multicomponent liquid fuel droplet</title><title>Combustion and flame</title><description>The transient combustion of a multicomponent liquid fuel droplet has been studied. The unsteady effects caused by the liquid- and gas-phase processes are considered. The numerical results demonstrate that due to the process of fuel vapor accumulation within the inner region to the flame and to the high liquid-phase mass diffusional resistance, a situation is reached where the concentration of fuel vapor in the inner zone of the flame or in the immediate vicinity of the droplet surface exceeds that at the droplet surface for certain values of the liquid-phase Lewis number. This results in a suppression of the mass vaporization rate (i.e., negative vaporization rate) without any indication of flame extinction. The results also indicate that with the increase in the volatility differentials between the mixture constituents vaporization is suppressed earlier in the droplet lifetime. However, by decreasing the liquid Lewis number, this phenomenon can be eliminated and the complete droplet lifetime can be computed. For example, the numerical results show that for a 50-50 by mass heptane-decane droplet, a liquid-phase Lewis number larger than three results in suppression of vaporization.</description><subject>02 PETROLEUM</subject><subject>025000 - Petroleum- Combustion</subject><subject>ALKANES</subject><subject>Applied sciences</subject><subject>CHEMICAL REACTION KINETICS</subject><subject>COMBUSTION KINETICS</subject><subject>Combustion of liquid fuels</subject><subject>Combustion. Flame</subject><subject>DECANE</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>EVAPORATION</subject><subject>Exact sciences and technology</subject><subject>FLUIDS</subject><subject>FUELS</subject><subject>GASES</subject><subject>HEPTANE</subject><subject>HYDROCARBONS</subject><subject>KINETICS</subject><subject>LIQUID FUELS</subject><subject>ORGANIC COMPOUNDS</subject><subject>PHASE TRANSFORMATIONS</subject><subject>REACTION KINETICS</subject><subject>Theoretical studies. Data and constants. Metering</subject><subject>VAPORS</subject><subject>VOLATILITY</subject><issn>0010-2180</issn><issn>1556-2921</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1991</creationdate><recordtype>article</recordtype><recordid>eNp9kE1LxDAQhoMouH78Aw9FUPRQzSRN21wEWXQVBC96DmmSYiSb7CapsP_e1l305mlg5pmZlwehM8A3gKG-xRhwSaDFVxyuOcZVWy720AwYq0vCCeyj2S9yiI5S-sQYNxWlM_R076XbJJuK0Bc5Sp-s8blQYdkNKdvgp74sloPLdmyugp_Gzq4Hq4t-MK7QMaycySfooJcumdNdPUbvjw9v86fy5XXxPL9_KRXlJJcNrQmtOW9YD1XbNR2RbQsSqq5tpNFKY0NpK3XHuw4ol71iimKgEmvdsZrRY3S-vRvGeCIpm436UMF7o7JgddWwaoIut9AqhvVgUhZLm5RxTnoThiQIo0A4wAhWW1DFkFI0vVhFu5RxIwCLya2YxIlJnOAgftyKxbh2sbsvk5KuH70pm_52OWs44Xzk7racGY18WROnwMYro22c8upg_3_0DZD1jTE</recordid><startdate>19910301</startdate><enddate>19910301</enddate><creator>Mawid, M.</creator><creator>Aggarwal, S.K.</creator><general>Elsevier Inc</general><general>Elsevier Science</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>8FD</scope><scope>H8D</scope><scope>L7M</scope><scope>OTOTI</scope></search><sort><creationdate>19910301</creationdate><title>Analysis of transient combustion of a multicomponent liquid fuel droplet</title><author>Mawid, M. ; Aggarwal, S.K.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c392t-7362369975f148b7b2a881a14b87aedcd0e338adb9bb139afc5c3013a0ddb5653</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1991</creationdate><topic>02 PETROLEUM</topic><topic>025000 - Petroleum- Combustion</topic><topic>ALKANES</topic><topic>Applied sciences</topic><topic>CHEMICAL REACTION KINETICS</topic><topic>COMBUSTION KINETICS</topic><topic>Combustion of liquid fuels</topic><topic>Combustion. Flame</topic><topic>DECANE</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>EVAPORATION</topic><topic>Exact sciences and technology</topic><topic>FLUIDS</topic><topic>FUELS</topic><topic>GASES</topic><topic>HEPTANE</topic><topic>HYDROCARBONS</topic><topic>KINETICS</topic><topic>LIQUID FUELS</topic><topic>ORGANIC COMPOUNDS</topic><topic>PHASE TRANSFORMATIONS</topic><topic>REACTION KINETICS</topic><topic>Theoretical studies. Data and constants. Metering</topic><topic>VAPORS</topic><topic>VOLATILITY</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mawid, M.</creatorcontrib><creatorcontrib>Aggarwal, S.K.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Technology Research Database</collection><collection>Aerospace Database</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>OSTI.GOV</collection><jtitle>Combustion and flame</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mawid, M.</au><au>Aggarwal, S.K.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Analysis of transient combustion of a multicomponent liquid fuel droplet</atitle><jtitle>Combustion and flame</jtitle><date>1991-03-01</date><risdate>1991</risdate><volume>84</volume><issue>1</issue><spage>197</spage><epage>209</epage><pages>197-209</pages><issn>0010-2180</issn><eissn>1556-2921</eissn><coden>CBFMAO</coden><abstract>The transient combustion of a multicomponent liquid fuel droplet has been studied. The unsteady effects caused by the liquid- and gas-phase processes are considered. The numerical results demonstrate that due to the process of fuel vapor accumulation within the inner region to the flame and to the high liquid-phase mass diffusional resistance, a situation is reached where the concentration of fuel vapor in the inner zone of the flame or in the immediate vicinity of the droplet surface exceeds that at the droplet surface for certain values of the liquid-phase Lewis number. This results in a suppression of the mass vaporization rate (i.e., negative vaporization rate) without any indication of flame extinction. The results also indicate that with the increase in the volatility differentials between the mixture constituents vaporization is suppressed earlier in the droplet lifetime. However, by decreasing the liquid Lewis number, this phenomenon can be eliminated and the complete droplet lifetime can be computed. For example, the numerical results show that for a 50-50 by mass heptane-decane droplet, a liquid-phase Lewis number larger than three results in suppression of vaporization.</abstract><cop>New York, NY</cop><pub>Elsevier Inc</pub><doi>10.1016/0010-2180(91)90048-G</doi><tpages>13</tpages></addata></record> |
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subjects | 02 PETROLEUM 025000 - Petroleum- Combustion ALKANES Applied sciences CHEMICAL REACTION KINETICS COMBUSTION KINETICS Combustion of liquid fuels Combustion. Flame DECANE Energy Energy. Thermal use of fuels EVAPORATION Exact sciences and technology FLUIDS FUELS GASES HEPTANE HYDROCARBONS KINETICS LIQUID FUELS ORGANIC COMPOUNDS PHASE TRANSFORMATIONS REACTION KINETICS Theoretical studies. Data and constants. Metering VAPORS VOLATILITY |
title | Analysis of transient combustion of a multicomponent liquid fuel droplet |
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