Removal of Double Oxide Film Defects by Ceramic Foam Filters
Abstract In this study, Weibull statistical and statistical image analyses of porosity were employed to determine the efficiency of ceramic foam filters for the removal of double oxide film (bifilm) defects from a pure Al melt. Using these efficiencies and the branch filter model, the average size o...
Ausführliche Beschreibung
Autor*in: |
Ardekhani, Arash [verfasserIn] |
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Format: |
E-Artikel |
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Sprache: |
Englisch |
Erschienen: |
2011 |
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Schlagwörter: |
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Anmerkung: |
© ASM International 2011 |
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Übergeordnetes Werk: |
Enthalten in: Journal of materials engineering and performance - New York, NY : Springer, 1992, 21(2011), 7 vom: 02. Juli, Seite 1352-1362 |
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Übergeordnetes Werk: |
volume:21 ; year:2011 ; number:7 ; day:02 ; month:07 ; pages:1352-1362 |
Links: |
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DOI / URN: |
10.1007/s11665-011-9991-3 |
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Katalog-ID: |
SPR021588309 |
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520 | |a Abstract In this study, Weibull statistical and statistical image analyses of porosity were employed to determine the efficiency of ceramic foam filters for the removal of double oxide film (bifilm) defects from a pure Al melt. Using these efficiencies and the branch filter model, the average size of the inclusions present in the liquid was estimated, and assuming that most of the inclusions in the melt are in the form of double oxide films, the possible dimensions for these defects were calculated. The results showed that the foam filters can remove oxide defects from the melt and that the efficiency of this filtration depends on the pore size of the filter. The average dimension of the oxide film defects was calculated to be 13.8 × 13.8 μm with a maximum thickness of 1 μm, if they remained non-convoluted in the metal flow. If they became convoluted because of the turbulence of the liquid flow, then the dimensions of the flat defect before it became curled up in the flow were calculated to be between 37 × 37 × 1 and 370 × 370 × 0.01 μm. | ||
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700 | 1 | |a Raiszadeh, Ramin |4 aut | |
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10.1007/s11665-011-9991-3 doi (DE-627)SPR021588309 (SPR)s11665-011-9991-3-e DE-627 ger DE-627 rakwb eng Ardekhani, Arash verfasserin aut Removal of Double Oxide Film Defects by Ceramic Foam Filters 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © ASM International 2011 Abstract In this study, Weibull statistical and statistical image analyses of porosity were employed to determine the efficiency of ceramic foam filters for the removal of double oxide film (bifilm) defects from a pure Al melt. Using these efficiencies and the branch filter model, the average size of the inclusions present in the liquid was estimated, and assuming that most of the inclusions in the melt are in the form of double oxide films, the possible dimensions for these defects were calculated. The results showed that the foam filters can remove oxide defects from the melt and that the efficiency of this filtration depends on the pore size of the filter. The average dimension of the oxide film defects was calculated to be 13.8 × 13.8 μm with a maximum thickness of 1 μm, if they remained non-convoluted in the metal flow. If they became convoluted because of the turbulence of the liquid flow, then the dimensions of the flat defect before it became curled up in the flow were calculated to be between 37 × 37 × 1 and 370 × 370 × 0.01 μm. bifilm (dpeaa)DE-He213 double oxide film defect (dpeaa)DE-He213 foam filter (dpeaa)DE-He213 melt quality (dpeaa)DE-He213 Raiszadeh, Ramin aut Enthalten in Journal of materials engineering and performance New York, NY : Springer, 1992 21(2011), 7 vom: 02. Juli, Seite 1352-1362 (DE-627)329975447 (DE-600)2048384-3 1544-1024 nnns volume:21 year:2011 number:7 day:02 month:07 pages:1352-1362 https://dx.doi.org/10.1007/s11665-011-9991-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_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_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 21 2011 7 02 07 1352-1362 |
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10.1007/s11665-011-9991-3 doi (DE-627)SPR021588309 (SPR)s11665-011-9991-3-e DE-627 ger DE-627 rakwb eng Ardekhani, Arash verfasserin aut Removal of Double Oxide Film Defects by Ceramic Foam Filters 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © ASM International 2011 Abstract In this study, Weibull statistical and statistical image analyses of porosity were employed to determine the efficiency of ceramic foam filters for the removal of double oxide film (bifilm) defects from a pure Al melt. Using these efficiencies and the branch filter model, the average size of the inclusions present in the liquid was estimated, and assuming that most of the inclusions in the melt are in the form of double oxide films, the possible dimensions for these defects were calculated. The results showed that the foam filters can remove oxide defects from the melt and that the efficiency of this filtration depends on the pore size of the filter. The average dimension of the oxide film defects was calculated to be 13.8 × 13.8 μm with a maximum thickness of 1 μm, if they remained non-convoluted in the metal flow. If they became convoluted because of the turbulence of the liquid flow, then the dimensions of the flat defect before it became curled up in the flow were calculated to be between 37 × 37 × 1 and 370 × 370 × 0.01 μm. bifilm (dpeaa)DE-He213 double oxide film defect (dpeaa)DE-He213 foam filter (dpeaa)DE-He213 melt quality (dpeaa)DE-He213 Raiszadeh, Ramin aut Enthalten in Journal of materials engineering and performance New York, NY : Springer, 1992 21(2011), 7 vom: 02. Juli, Seite 1352-1362 (DE-627)329975447 (DE-600)2048384-3 1544-1024 nnns volume:21 year:2011 number:7 day:02 month:07 pages:1352-1362 https://dx.doi.org/10.1007/s11665-011-9991-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_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_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 21 2011 7 02 07 1352-1362 |
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10.1007/s11665-011-9991-3 doi (DE-627)SPR021588309 (SPR)s11665-011-9991-3-e DE-627 ger DE-627 rakwb eng Ardekhani, Arash verfasserin aut Removal of Double Oxide Film Defects by Ceramic Foam Filters 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © ASM International 2011 Abstract In this study, Weibull statistical and statistical image analyses of porosity were employed to determine the efficiency of ceramic foam filters for the removal of double oxide film (bifilm) defects from a pure Al melt. Using these efficiencies and the branch filter model, the average size of the inclusions present in the liquid was estimated, and assuming that most of the inclusions in the melt are in the form of double oxide films, the possible dimensions for these defects were calculated. The results showed that the foam filters can remove oxide defects from the melt and that the efficiency of this filtration depends on the pore size of the filter. The average dimension of the oxide film defects was calculated to be 13.8 × 13.8 μm with a maximum thickness of 1 μm, if they remained non-convoluted in the metal flow. If they became convoluted because of the turbulence of the liquid flow, then the dimensions of the flat defect before it became curled up in the flow were calculated to be between 37 × 37 × 1 and 370 × 370 × 0.01 μm. bifilm (dpeaa)DE-He213 double oxide film defect (dpeaa)DE-He213 foam filter (dpeaa)DE-He213 melt quality (dpeaa)DE-He213 Raiszadeh, Ramin aut Enthalten in Journal of materials engineering and performance New York, NY : Springer, 1992 21(2011), 7 vom: 02. Juli, Seite 1352-1362 (DE-627)329975447 (DE-600)2048384-3 1544-1024 nnns volume:21 year:2011 number:7 day:02 month:07 pages:1352-1362 https://dx.doi.org/10.1007/s11665-011-9991-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_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_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 21 2011 7 02 07 1352-1362 |
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10.1007/s11665-011-9991-3 doi (DE-627)SPR021588309 (SPR)s11665-011-9991-3-e DE-627 ger DE-627 rakwb eng Ardekhani, Arash verfasserin aut Removal of Double Oxide Film Defects by Ceramic Foam Filters 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © ASM International 2011 Abstract In this study, Weibull statistical and statistical image analyses of porosity were employed to determine the efficiency of ceramic foam filters for the removal of double oxide film (bifilm) defects from a pure Al melt. Using these efficiencies and the branch filter model, the average size of the inclusions present in the liquid was estimated, and assuming that most of the inclusions in the melt are in the form of double oxide films, the possible dimensions for these defects were calculated. The results showed that the foam filters can remove oxide defects from the melt and that the efficiency of this filtration depends on the pore size of the filter. The average dimension of the oxide film defects was calculated to be 13.8 × 13.8 μm with a maximum thickness of 1 μm, if they remained non-convoluted in the metal flow. If they became convoluted because of the turbulence of the liquid flow, then the dimensions of the flat defect before it became curled up in the flow were calculated to be between 37 × 37 × 1 and 370 × 370 × 0.01 μm. bifilm (dpeaa)DE-He213 double oxide film defect (dpeaa)DE-He213 foam filter (dpeaa)DE-He213 melt quality (dpeaa)DE-He213 Raiszadeh, Ramin aut Enthalten in Journal of materials engineering and performance New York, NY : Springer, 1992 21(2011), 7 vom: 02. Juli, Seite 1352-1362 (DE-627)329975447 (DE-600)2048384-3 1544-1024 nnns volume:21 year:2011 number:7 day:02 month:07 pages:1352-1362 https://dx.doi.org/10.1007/s11665-011-9991-3 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_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_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 21 2011 7 02 07 1352-1362 |
language |
English |
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Enthalten in Journal of materials engineering and performance 21(2011), 7 vom: 02. Juli, Seite 1352-1362 volume:21 year:2011 number:7 day:02 month:07 pages:1352-1362 |
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Enthalten in Journal of materials engineering and performance 21(2011), 7 vom: 02. Juli, Seite 1352-1362 volume:21 year:2011 number:7 day:02 month:07 pages:1352-1362 |
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Ardekhani, Arash @@aut@@ Raiszadeh, Ramin @@aut@@ |
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Ardekhani, Arash |
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Ardekhani, Arash misc bifilm misc double oxide film defect misc foam filter misc melt quality Removal of Double Oxide Film Defects by Ceramic Foam Filters |
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Removal of Double Oxide Film Defects by Ceramic Foam Filters bifilm (dpeaa)DE-He213 double oxide film defect (dpeaa)DE-He213 foam filter (dpeaa)DE-He213 melt quality (dpeaa)DE-He213 |
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Removal of Double Oxide Film Defects by Ceramic Foam Filters |
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Removal of Double Oxide Film Defects by Ceramic Foam Filters |
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Ardekhani, Arash Raiszadeh, Ramin |
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removal of double oxide film defects by ceramic foam filters |
title_auth |
Removal of Double Oxide Film Defects by Ceramic Foam Filters |
abstract |
Abstract In this study, Weibull statistical and statistical image analyses of porosity were employed to determine the efficiency of ceramic foam filters for the removal of double oxide film (bifilm) defects from a pure Al melt. Using these efficiencies and the branch filter model, the average size of the inclusions present in the liquid was estimated, and assuming that most of the inclusions in the melt are in the form of double oxide films, the possible dimensions for these defects were calculated. The results showed that the foam filters can remove oxide defects from the melt and that the efficiency of this filtration depends on the pore size of the filter. The average dimension of the oxide film defects was calculated to be 13.8 × 13.8 μm with a maximum thickness of 1 μm, if they remained non-convoluted in the metal flow. If they became convoluted because of the turbulence of the liquid flow, then the dimensions of the flat defect before it became curled up in the flow were calculated to be between 37 × 37 × 1 and 370 × 370 × 0.01 μm. © ASM International 2011 |
abstractGer |
Abstract In this study, Weibull statistical and statistical image analyses of porosity were employed to determine the efficiency of ceramic foam filters for the removal of double oxide film (bifilm) defects from a pure Al melt. Using these efficiencies and the branch filter model, the average size of the inclusions present in the liquid was estimated, and assuming that most of the inclusions in the melt are in the form of double oxide films, the possible dimensions for these defects were calculated. The results showed that the foam filters can remove oxide defects from the melt and that the efficiency of this filtration depends on the pore size of the filter. The average dimension of the oxide film defects was calculated to be 13.8 × 13.8 μm with a maximum thickness of 1 μm, if they remained non-convoluted in the metal flow. If they became convoluted because of the turbulence of the liquid flow, then the dimensions of the flat defect before it became curled up in the flow were calculated to be between 37 × 37 × 1 and 370 × 370 × 0.01 μm. © ASM International 2011 |
abstract_unstemmed |
Abstract In this study, Weibull statistical and statistical image analyses of porosity were employed to determine the efficiency of ceramic foam filters for the removal of double oxide film (bifilm) defects from a pure Al melt. Using these efficiencies and the branch filter model, the average size of the inclusions present in the liquid was estimated, and assuming that most of the inclusions in the melt are in the form of double oxide films, the possible dimensions for these defects were calculated. The results showed that the foam filters can remove oxide defects from the melt and that the efficiency of this filtration depends on the pore size of the filter. The average dimension of the oxide film defects was calculated to be 13.8 × 13.8 μm with a maximum thickness of 1 μm, if they remained non-convoluted in the metal flow. If they became convoluted because of the turbulence of the liquid flow, then the dimensions of the flat defect before it became curled up in the flow were calculated to be between 37 × 37 × 1 and 370 × 370 × 0.01 μm. © ASM International 2011 |
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Removal of Double Oxide Film Defects by Ceramic Foam Filters |
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<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">SPR021588309</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230520005524.0</controlfield><controlfield tag="007">cr uuu---uuuuu</controlfield><controlfield tag="008">201006s2011 xx |||||o 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1007/s11665-011-9991-3</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)SPR021588309</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(SPR)s11665-011-9991-3-e</subfield></datafield><datafield tag="040" ind1=" " ind2=" "><subfield code="a">DE-627</subfield><subfield code="b">ger</subfield><subfield code="c">DE-627</subfield><subfield code="e">rakwb</subfield></datafield><datafield tag="041" ind1=" " ind2=" "><subfield code="a">eng</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Ardekhani, Arash</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Removal of Double Oxide Film Defects by Ceramic Foam Filters</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2011</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="500" ind1=" " ind2=" "><subfield code="a">© ASM International 2011</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract In this study, Weibull statistical and statistical image analyses of porosity were employed to determine the efficiency of ceramic foam filters for the removal of double oxide film (bifilm) defects from a pure Al melt. Using these efficiencies and the branch filter model, the average size of the inclusions present in the liquid was estimated, and assuming that most of the inclusions in the melt are in the form of double oxide films, the possible dimensions for these defects were calculated. The results showed that the foam filters can remove oxide defects from the melt and that the efficiency of this filtration depends on the pore size of the filter. The average dimension of the oxide film defects was calculated to be 13.8 × 13.8 μm with a maximum thickness of 1 μm, if they remained non-convoluted in the metal flow. If they became convoluted because of the turbulence of the liquid flow, then the dimensions of the flat defect before it became curled up in the flow were calculated to be between 37 × 37 × 1 and 370 × 370 × 0.01 μm.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">bifilm</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">double oxide film defect</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">foam filter</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">melt quality</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Raiszadeh, Ramin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Journal of materials engineering and performance</subfield><subfield code="d">New York, NY : Springer, 1992</subfield><subfield code="g">21(2011), 7 vom: 02. Juli, Seite 1352-1362</subfield><subfield code="w">(DE-627)329975447</subfield><subfield code="w">(DE-600)2048384-3</subfield><subfield code="x">1544-1024</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:21</subfield><subfield code="g">year:2011</subfield><subfield code="g">number:7</subfield><subfield code="g">day:02</subfield><subfield code="g">month:07</subfield><subfield code="g">pages:1352-1362</subfield></datafield><datafield tag="856" ind1="4" ind2="0"><subfield code="u">https://dx.doi.org/10.1007/s11665-011-9991-3</subfield><subfield code="z">lizenzpflichtig</subfield><subfield code="3">Volltext</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_USEFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SYSFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_SPRINGER</subfield></datafield><datafield 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