Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting

Abstract This paper is concerned with the double diffusive convection due to the melting of an ice plate into a calcium chloride aqueous solution inside a rectangular cavity. It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood...
Ausführliche Beschreibung

Gespeichert in:

Autor*in:	Sugawara, M. [verfasserIn] Ishikura, T. Beer, H.

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2004

Schlagwörter:	Nusselt Number Sherwood Number Melting Rate Stagnant Region Double Diffusive Convection

Systematik:	ELIB31 ELIB41

Anmerkung:	© Springer-Verlag 2004

Übergeordnetes Werk:	Enthalten in: Heat and mass transfer - Springer-Verlag, 1968, 41(2004), 5 vom: 17. Nov., Seite 432-441
Übergeordnetes Werk:	volume:41 ; year:2004 ; number:5 ; day:17 ; month:11 ; pages:432-441

Links:	Volltext

DOI / URN:	10.1007/s00231-004-0557-x

Katalog-ID:	OLC209067623X

Internformat


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520			\|a Abstract This paper is concerned with the double diffusive convection due to the melting of an ice plate into a calcium chloride aqueous solution inside a rectangular cavity. It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood-numbers, experimentally as well as numerically. The ice plate melts spontaneously with decreasing temperature at the melting front even if initially there does not exist a temperature difference between the ice and the liquid. The concentration- and temperature-gradients near the melting front induce double diffusive convection in the liquid, which will affect the melting rate. Experiments reveal that the mean melting mass increases monotonically with increasing cavity inclination. The numerical analysis based on the laminar assumption predicts well the melting mass in the range of θ=0–90°, however, under-predicts the melting mass in the range of θ=90–180° as compared with the experimental results.
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matchkey_str	article:14321181:2004----::fetfaiynlntooaeprtradocnrtocnrleduldfui
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bklnumber	58.13$jThermische Verfahrenstechnik 50.38$jTechnische Thermodynamik
publishDate	2004
allfields	10.1007/s00231-004-0557-x doi (DE-627)OLC209067623X (DE-He213)s00231-004-0557-x-e DE-627 ger DE-627 rakwb eng 530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Sugawara, M. verfasserin aut Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting 2004 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer-Verlag 2004 Abstract This paper is concerned with the double diffusive convection due to the melting of an ice plate into a calcium chloride aqueous solution inside a rectangular cavity. It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood-numbers, experimentally as well as numerically. The ice plate melts spontaneously with decreasing temperature at the melting front even if initially there does not exist a temperature difference between the ice and the liquid. The concentration- and temperature-gradients near the melting front induce double diffusive convection in the liquid, which will affect the melting rate. Experiments reveal that the mean melting mass increases monotonically with increasing cavity inclination. The numerical analysis based on the laminar assumption predicts well the melting mass in the range of θ=0–90°, however, under-predicts the melting mass in the range of θ=90–180° as compared with the experimental results. Nusselt Number Sherwood Number Melting Rate Stagnant Region Double Diffusive Convection Ishikura, T. aut Beer, H. aut Enthalten in Heat and mass transfer Springer-Verlag, 1968 41(2004), 5 vom: 17. Nov., Seite 432-441 Online-Ressource (DE-627)27012635X (DE-600)1476367-9 (DE-576)078128927 1432-1181 nnns volume:41 year:2004 number:5 day:17 month:11 pages:432-441 https://dx.doi.org/10.1007/s00231-004-0557-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_267 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4012 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 ELIB31 ELIB41 58.13$jThermische Verfahrenstechnik VZ 181570548 (DE-625)181570548 50.38$jTechnische Thermodynamik VZ 106420534 (DE-625)106420534 AR 41 2004 5 17 11 432-441
spelling	10.1007/s00231-004-0557-x doi (DE-627)OLC209067623X (DE-He213)s00231-004-0557-x-e DE-627 ger DE-627 rakwb eng 530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Sugawara, M. verfasserin aut Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting 2004 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer-Verlag 2004 Abstract This paper is concerned with the double diffusive convection due to the melting of an ice plate into a calcium chloride aqueous solution inside a rectangular cavity. It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood-numbers, experimentally as well as numerically. The ice plate melts spontaneously with decreasing temperature at the melting front even if initially there does not exist a temperature difference between the ice and the liquid. The concentration- and temperature-gradients near the melting front induce double diffusive convection in the liquid, which will affect the melting rate. Experiments reveal that the mean melting mass increases monotonically with increasing cavity inclination. The numerical analysis based on the laminar assumption predicts well the melting mass in the range of θ=0–90°, however, under-predicts the melting mass in the range of θ=90–180° as compared with the experimental results. Nusselt Number Sherwood Number Melting Rate Stagnant Region Double Diffusive Convection Ishikura, T. aut Beer, H. aut Enthalten in Heat and mass transfer Springer-Verlag, 1968 41(2004), 5 vom: 17. Nov., Seite 432-441 Online-Ressource (DE-627)27012635X (DE-600)1476367-9 (DE-576)078128927 1432-1181 nnns volume:41 year:2004 number:5 day:17 month:11 pages:432-441 https://dx.doi.org/10.1007/s00231-004-0557-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_267 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4012 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 ELIB31 ELIB41 58.13$jThermische Verfahrenstechnik VZ 181570548 (DE-625)181570548 50.38$jTechnische Thermodynamik VZ 106420534 (DE-625)106420534 AR 41 2004 5 17 11 432-441
allfields_unstemmed	10.1007/s00231-004-0557-x doi (DE-627)OLC209067623X (DE-He213)s00231-004-0557-x-e DE-627 ger DE-627 rakwb eng 530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Sugawara, M. verfasserin aut Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting 2004 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer-Verlag 2004 Abstract This paper is concerned with the double diffusive convection due to the melting of an ice plate into a calcium chloride aqueous solution inside a rectangular cavity. It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood-numbers, experimentally as well as numerically. The ice plate melts spontaneously with decreasing temperature at the melting front even if initially there does not exist a temperature difference between the ice and the liquid. The concentration- and temperature-gradients near the melting front induce double diffusive convection in the liquid, which will affect the melting rate. Experiments reveal that the mean melting mass increases monotonically with increasing cavity inclination. The numerical analysis based on the laminar assumption predicts well the melting mass in the range of θ=0–90°, however, under-predicts the melting mass in the range of θ=90–180° as compared with the experimental results. Nusselt Number Sherwood Number Melting Rate Stagnant Region Double Diffusive Convection Ishikura, T. aut Beer, H. aut Enthalten in Heat and mass transfer Springer-Verlag, 1968 41(2004), 5 vom: 17. Nov., Seite 432-441 Online-Ressource (DE-627)27012635X (DE-600)1476367-9 (DE-576)078128927 1432-1181 nnns volume:41 year:2004 number:5 day:17 month:11 pages:432-441 https://dx.doi.org/10.1007/s00231-004-0557-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_267 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4012 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 ELIB31 ELIB41 58.13$jThermische Verfahrenstechnik VZ 181570548 (DE-625)181570548 50.38$jTechnische Thermodynamik VZ 106420534 (DE-625)106420534 AR 41 2004 5 17 11 432-441
allfieldsGer	10.1007/s00231-004-0557-x doi (DE-627)OLC209067623X (DE-He213)s00231-004-0557-x-e DE-627 ger DE-627 rakwb eng 530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Sugawara, M. verfasserin aut Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting 2004 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer-Verlag 2004 Abstract This paper is concerned with the double diffusive convection due to the melting of an ice plate into a calcium chloride aqueous solution inside a rectangular cavity. It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood-numbers, experimentally as well as numerically. The ice plate melts spontaneously with decreasing temperature at the melting front even if initially there does not exist a temperature difference between the ice and the liquid. The concentration- and temperature-gradients near the melting front induce double diffusive convection in the liquid, which will affect the melting rate. Experiments reveal that the mean melting mass increases monotonically with increasing cavity inclination. The numerical analysis based on the laminar assumption predicts well the melting mass in the range of θ=0–90°, however, under-predicts the melting mass in the range of θ=90–180° as compared with the experimental results. Nusselt Number Sherwood Number Melting Rate Stagnant Region Double Diffusive Convection Ishikura, T. aut Beer, H. aut Enthalten in Heat and mass transfer Springer-Verlag, 1968 41(2004), 5 vom: 17. Nov., Seite 432-441 Online-Ressource (DE-627)27012635X (DE-600)1476367-9 (DE-576)078128927 1432-1181 nnns volume:41 year:2004 number:5 day:17 month:11 pages:432-441 https://dx.doi.org/10.1007/s00231-004-0557-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_267 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4012 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 ELIB31 ELIB41 58.13$jThermische Verfahrenstechnik VZ 181570548 (DE-625)181570548 50.38$jTechnische Thermodynamik VZ 106420534 (DE-625)106420534 AR 41 2004 5 17 11 432-441
allfieldsSound	10.1007/s00231-004-0557-x doi (DE-627)OLC209067623X (DE-He213)s00231-004-0557-x-e DE-627 ger DE-627 rakwb eng 530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Sugawara, M. verfasserin aut Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting 2004 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer-Verlag 2004 Abstract This paper is concerned with the double diffusive convection due to the melting of an ice plate into a calcium chloride aqueous solution inside a rectangular cavity. It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood-numbers, experimentally as well as numerically. The ice plate melts spontaneously with decreasing temperature at the melting front even if initially there does not exist a temperature difference between the ice and the liquid. The concentration- and temperature-gradients near the melting front induce double diffusive convection in the liquid, which will affect the melting rate. Experiments reveal that the mean melting mass increases monotonically with increasing cavity inclination. The numerical analysis based on the laminar assumption predicts well the melting mass in the range of θ=0–90°, however, under-predicts the melting mass in the range of θ=90–180° as compared with the experimental results. Nusselt Number Sherwood Number Melting Rate Stagnant Region Double Diffusive Convection Ishikura, T. aut Beer, H. aut Enthalten in Heat and mass transfer Springer-Verlag, 1968 41(2004), 5 vom: 17. Nov., Seite 432-441 Online-Ressource (DE-627)27012635X (DE-600)1476367-9 (DE-576)078128927 1432-1181 nnns volume:41 year:2004 number:5 day:17 month:11 pages:432-441 https://dx.doi.org/10.1007/s00231-004-0557-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_267 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4012 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 ELIB31 ELIB41 58.13$jThermische Verfahrenstechnik VZ 181570548 (DE-625)181570548 50.38$jTechnische Thermodynamik VZ 106420534 (DE-625)106420534 AR 41 2004 5 17 11 432-441
language	English
source	Enthalten in Heat and mass transfer 41(2004), 5 vom: 17. Nov., Seite 432-441 volume:41 year:2004 number:5 day:17 month:11 pages:432-441
sourceStr	Enthalten in Heat and mass transfer 41(2004), 5 vom: 17. Nov., Seite 432-441 volume:41 year:2004 number:5 day:17 month:11 pages:432-441
format_phy_str_mv	Article
institution	findex.gbv.de
topic_facet	Nusselt Number Sherwood Number Melting Rate Stagnant Region Double Diffusive Convection
dewey-raw	530
isfreeaccess_bool	false
container_title	Heat and mass transfer
authorswithroles_txt_mv	Sugawara, M. @@aut@@ Ishikura, T. @@aut@@ Beer, H. @@aut@@
publishDateDaySort_date	2004-11-17T00:00:00Z
hierarchy_top_id	27012635X
dewey-sort	3530
id	OLC209067623X
language_de	englisch
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author	Sugawara, M.
spellingShingle	Sugawara, M. ddc 530 rvk ELIB31 rvk ELIB41 bkl 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik misc Nusselt Number misc Sherwood Number misc Melting Rate misc Stagnant Region misc Double Diffusive Convection Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting
authorStr	Sugawara, M.
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topic_title	530 620 VZ ELIB31 VZ rvk ELIB41 VZ rvk 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik bkl Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting Nusselt Number Sherwood Number Melting Rate Stagnant Region Double Diffusive Convection
topic	ddc 530 rvk ELIB31 rvk ELIB41 bkl 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik misc Nusselt Number misc Sherwood Number misc Melting Rate misc Stagnant Region misc Double Diffusive Convection
topic_unstemmed	ddc 530 rvk ELIB31 rvk ELIB41 bkl 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik misc Nusselt Number misc Sherwood Number misc Melting Rate misc Stagnant Region misc Double Diffusive Convection
topic_browse	ddc 530 rvk ELIB31 rvk ELIB41 bkl 58.13$jThermische Verfahrenstechnik bkl 50.38$jTechnische Thermodynamik misc Nusselt Number misc Sherwood Number misc Melting Rate misc Stagnant Region misc Double Diffusive Convection
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title	Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting
ctrlnum	(DE-627)OLC209067623X (DE-He213)s00231-004-0557-x-e
title_full	Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting
author_sort	Sugawara, M.
journal	Heat and mass transfer
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author_browse	Sugawara, M. Ishikura, T. Beer, H.
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author-letter	Sugawara, M.
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title_sort	effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting
title_auth	Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting
abstract	Abstract This paper is concerned with the double diffusive convection due to the melting of an ice plate into a calcium chloride aqueous solution inside a rectangular cavity. It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood-numbers, experimentally as well as numerically. The ice plate melts spontaneously with decreasing temperature at the melting front even if initially there does not exist a temperature difference between the ice and the liquid. The concentration- and temperature-gradients near the melting front induce double diffusive convection in the liquid, which will affect the melting rate. Experiments reveal that the mean melting mass increases monotonically with increasing cavity inclination. The numerical analysis based on the laminar assumption predicts well the melting mass in the range of θ=0–90°, however, under-predicts the melting mass in the range of θ=90–180° as compared with the experimental results. © Springer-Verlag 2004
abstractGer	Abstract This paper is concerned with the double diffusive convection due to the melting of an ice plate into a calcium chloride aqueous solution inside a rectangular cavity. It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood-numbers, experimentally as well as numerically. The ice plate melts spontaneously with decreasing temperature at the melting front even if initially there does not exist a temperature difference between the ice and the liquid. The concentration- and temperature-gradients near the melting front induce double diffusive convection in the liquid, which will affect the melting rate. Experiments reveal that the mean melting mass increases monotonically with increasing cavity inclination. The numerical analysis based on the laminar assumption predicts well the melting mass in the range of θ=0–90°, however, under-predicts the melting mass in the range of θ=90–180° as compared with the experimental results. © Springer-Verlag 2004
abstract_unstemmed	Abstract This paper is concerned with the double diffusive convection due to the melting of an ice plate into a calcium chloride aqueous solution inside a rectangular cavity. It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood-numbers, experimentally as well as numerically. The ice plate melts spontaneously with decreasing temperature at the melting front even if initially there does not exist a temperature difference between the ice and the liquid. The concentration- and temperature-gradients near the melting front induce double diffusive convection in the liquid, which will affect the melting rate. Experiments reveal that the mean melting mass increases monotonically with increasing cavity inclination. The numerical analysis based on the laminar assumption predicts well the melting mass in the range of θ=0–90°, however, under-predicts the melting mass in the range of θ=90–180° as compared with the experimental results. © Springer-Verlag 2004
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container_issue	5
title_short	Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting
url	https://dx.doi.org/10.1007/s00231-004-0557-x
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author2	Ishikura, T. Beer, H.
author2Str	Ishikura, T. Beer, H.
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doi_str	10.1007/s00231-004-0557-x
up_date	2024-07-04T05:18:58.422Z
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It is mainly considered the effect of the cavity inclination θ on the melting rate and the mean melting Nusselt- and Sherwood-numbers, experimentally as well as numerically. The ice plate melts spontaneously with decreasing temperature at the melting front even if initially there does not exist a temperature difference between the ice and the liquid. The concentration- and temperature-gradients near the melting front induce double diffusive convection in the liquid, which will affect the melting rate. Experiments reveal that the mean melting mass increases monotonically with increasing cavity inclination. 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Effect of cavity inclination on a temperature and concentration controlled double diffusive convection at ice plate melting

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