Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium
Results are presented for a computational analysis performed to determine the most favorable diameters of the high-temperature section of the flue pipe in crude heaters with an intermediate heat-transfer medium. It is demonstrated that economically suitable diameters for the flue pipe are limited by...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Pechenegov, Yu. Ya. [verfasserIn] Denisenko, I. P. [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2012 |
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| Schlagwörter: |
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| Übergeordnetes Werk: |
Enthalten in: Chemical and petroleum engineering - New York, NY [u.a.] : Consultants Bureau, 1965, 48(2012), 1-2 vom: Mai, Seite 87-92 |
|---|---|
| Übergeordnetes Werk: |
volume:48 ; year:2012 ; number:1-2 ; month:05 ; pages:87-92 |
| Links: |
|---|
| DOI / URN: |
10.1007/s10556-012-9579-2 |
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| Katalog-ID: |
SPR011270128 |
|---|
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| 100 | 1 | |a Pechenegov, Yu. Ya. |e verfasserin |4 aut | |
| 245 | 1 | 0 | |a Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium |
| 264 | 1 | |c 2012 | |
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| 520 | |a Results are presented for a computational analysis performed to determine the most favorable diameters of the high-temperature section of the flue pipe in crude heaters with an intermediate heat-transfer medium. It is demonstrated that economically suitable diameters for the flue pipe are limited by the minimum value for which the working expression was obtained in the study. It is also indicated that ring-vortex generators placed in the high-temperature section of the flue pipe for intensification of convective heat exchange are technically and economically expedient. | ||
| 650 | 4 | |a crude heater |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a diameter of flue pipe |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a convective heat exchange |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a radiant heat exchange |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a annual reduced costs |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a optimization |7 (dpeaa)DE-He213 | |
| 700 | 1 | |a Denisenko, I. P. |e verfasserin |4 aut | |
| 773 | 0 | 8 | |i Enthalten in |t Chemical and petroleum engineering |d New York, NY [u.a.] : Consultants Bureau, 1965 |g 48(2012), 1-2 vom: Mai, Seite 87-92 |w (DE-627)325568421 |w (DE-600)2037114-7 |x 1573-8329 |7 nnns |
| 773 | 1 | 8 | |g volume:48 |g year:2012 |g number:1-2 |g month:05 |g pages:87-92 |
| 856 | 4 | 0 | |u https://dx.doi.org/10.1007/s10556-012-9579-2 |z lizenzpflichtig |3 Volltext |
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2012 |
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58.00 58.21 |
| publishDate |
2012 |
| allfields |
10.1007/s10556-012-9579-2 doi (DE-627)SPR011270128 (SPR)s10556-012-9579-2-e DE-627 ger DE-627 rakwb eng 620 660 ASE 58.00 bkl 58.21 bkl Pechenegov, Yu. Ya. verfasserin aut Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium 2012 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Results are presented for a computational analysis performed to determine the most favorable diameters of the high-temperature section of the flue pipe in crude heaters with an intermediate heat-transfer medium. It is demonstrated that economically suitable diameters for the flue pipe are limited by the minimum value for which the working expression was obtained in the study. It is also indicated that ring-vortex generators placed in the high-temperature section of the flue pipe for intensification of convective heat exchange are technically and economically expedient. crude heater (dpeaa)DE-He213 diameter of flue pipe (dpeaa)DE-He213 convective heat exchange (dpeaa)DE-He213 radiant heat exchange (dpeaa)DE-He213 annual reduced costs (dpeaa)DE-He213 optimization (dpeaa)DE-He213 Denisenko, I. P. verfasserin aut Enthalten in Chemical and petroleum engineering New York, NY [u.a.] : Consultants Bureau, 1965 48(2012), 1-2 vom: Mai, Seite 87-92 (DE-627)325568421 (DE-600)2037114-7 1573-8329 nnns volume:48 year:2012 number:1-2 month:05 pages:87-92 https://dx.doi.org/10.1007/s10556-012-9579-2 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_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_206 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_381 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_2056 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 58.00 ASE 58.21 ASE AR 48 2012 1-2 05 87-92 |
| spelling |
10.1007/s10556-012-9579-2 doi (DE-627)SPR011270128 (SPR)s10556-012-9579-2-e DE-627 ger DE-627 rakwb eng 620 660 ASE 58.00 bkl 58.21 bkl Pechenegov, Yu. Ya. verfasserin aut Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium 2012 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Results are presented for a computational analysis performed to determine the most favorable diameters of the high-temperature section of the flue pipe in crude heaters with an intermediate heat-transfer medium. It is demonstrated that economically suitable diameters for the flue pipe are limited by the minimum value for which the working expression was obtained in the study. It is also indicated that ring-vortex generators placed in the high-temperature section of the flue pipe for intensification of convective heat exchange are technically and economically expedient. crude heater (dpeaa)DE-He213 diameter of flue pipe (dpeaa)DE-He213 convective heat exchange (dpeaa)DE-He213 radiant heat exchange (dpeaa)DE-He213 annual reduced costs (dpeaa)DE-He213 optimization (dpeaa)DE-He213 Denisenko, I. P. verfasserin aut Enthalten in Chemical and petroleum engineering New York, NY [u.a.] : Consultants Bureau, 1965 48(2012), 1-2 vom: Mai, Seite 87-92 (DE-627)325568421 (DE-600)2037114-7 1573-8329 nnns volume:48 year:2012 number:1-2 month:05 pages:87-92 https://dx.doi.org/10.1007/s10556-012-9579-2 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_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_206 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_381 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_2056 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 58.00 ASE 58.21 ASE AR 48 2012 1-2 05 87-92 |
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10.1007/s10556-012-9579-2 doi (DE-627)SPR011270128 (SPR)s10556-012-9579-2-e DE-627 ger DE-627 rakwb eng 620 660 ASE 58.00 bkl 58.21 bkl Pechenegov, Yu. Ya. verfasserin aut Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium 2012 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Results are presented for a computational analysis performed to determine the most favorable diameters of the high-temperature section of the flue pipe in crude heaters with an intermediate heat-transfer medium. It is demonstrated that economically suitable diameters for the flue pipe are limited by the minimum value for which the working expression was obtained in the study. It is also indicated that ring-vortex generators placed in the high-temperature section of the flue pipe for intensification of convective heat exchange are technically and economically expedient. crude heater (dpeaa)DE-He213 diameter of flue pipe (dpeaa)DE-He213 convective heat exchange (dpeaa)DE-He213 radiant heat exchange (dpeaa)DE-He213 annual reduced costs (dpeaa)DE-He213 optimization (dpeaa)DE-He213 Denisenko, I. P. verfasserin aut Enthalten in Chemical and petroleum engineering New York, NY [u.a.] : Consultants Bureau, 1965 48(2012), 1-2 vom: Mai, Seite 87-92 (DE-627)325568421 (DE-600)2037114-7 1573-8329 nnns volume:48 year:2012 number:1-2 month:05 pages:87-92 https://dx.doi.org/10.1007/s10556-012-9579-2 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_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_206 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_381 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_2056 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 58.00 ASE 58.21 ASE AR 48 2012 1-2 05 87-92 |
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10.1007/s10556-012-9579-2 doi (DE-627)SPR011270128 (SPR)s10556-012-9579-2-e DE-627 ger DE-627 rakwb eng 620 660 ASE 58.00 bkl 58.21 bkl Pechenegov, Yu. Ya. verfasserin aut Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium 2012 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Results are presented for a computational analysis performed to determine the most favorable diameters of the high-temperature section of the flue pipe in crude heaters with an intermediate heat-transfer medium. It is demonstrated that economically suitable diameters for the flue pipe are limited by the minimum value for which the working expression was obtained in the study. It is also indicated that ring-vortex generators placed in the high-temperature section of the flue pipe for intensification of convective heat exchange are technically and economically expedient. crude heater (dpeaa)DE-He213 diameter of flue pipe (dpeaa)DE-He213 convective heat exchange (dpeaa)DE-He213 radiant heat exchange (dpeaa)DE-He213 annual reduced costs (dpeaa)DE-He213 optimization (dpeaa)DE-He213 Denisenko, I. P. verfasserin aut Enthalten in Chemical and petroleum engineering New York, NY [u.a.] : Consultants Bureau, 1965 48(2012), 1-2 vom: Mai, Seite 87-92 (DE-627)325568421 (DE-600)2037114-7 1573-8329 nnns volume:48 year:2012 number:1-2 month:05 pages:87-92 https://dx.doi.org/10.1007/s10556-012-9579-2 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_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_206 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_381 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_2056 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 58.00 ASE 58.21 ASE AR 48 2012 1-2 05 87-92 |
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10.1007/s10556-012-9579-2 doi (DE-627)SPR011270128 (SPR)s10556-012-9579-2-e DE-627 ger DE-627 rakwb eng 620 660 ASE 58.00 bkl 58.21 bkl Pechenegov, Yu. Ya. verfasserin aut Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium 2012 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Results are presented for a computational analysis performed to determine the most favorable diameters of the high-temperature section of the flue pipe in crude heaters with an intermediate heat-transfer medium. It is demonstrated that economically suitable diameters for the flue pipe are limited by the minimum value for which the working expression was obtained in the study. It is also indicated that ring-vortex generators placed in the high-temperature section of the flue pipe for intensification of convective heat exchange are technically and economically expedient. crude heater (dpeaa)DE-He213 diameter of flue pipe (dpeaa)DE-He213 convective heat exchange (dpeaa)DE-He213 radiant heat exchange (dpeaa)DE-He213 annual reduced costs (dpeaa)DE-He213 optimization (dpeaa)DE-He213 Denisenko, I. P. verfasserin aut Enthalten in Chemical and petroleum engineering New York, NY [u.a.] : Consultants Bureau, 1965 48(2012), 1-2 vom: Mai, Seite 87-92 (DE-627)325568421 (DE-600)2037114-7 1573-8329 nnns volume:48 year:2012 number:1-2 month:05 pages:87-92 https://dx.doi.org/10.1007/s10556-012-9579-2 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_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_206 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_381 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_2056 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 58.00 ASE 58.21 ASE AR 48 2012 1-2 05 87-92 |
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Enthalten in Chemical and petroleum engineering 48(2012), 1-2 vom: Mai, Seite 87-92 volume:48 year:2012 number:1-2 month:05 pages:87-92 |
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Enthalten in Chemical and petroleum engineering 48(2012), 1-2 vom: Mai, Seite 87-92 volume:48 year:2012 number:1-2 month:05 pages:87-92 |
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Chemical and petroleum engineering |
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Pechenegov, Yu. Ya. @@aut@@ Denisenko, I. P. @@aut@@ |
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| author |
Pechenegov, Yu. Ya. |
| spellingShingle |
Pechenegov, Yu. Ya. ddc 620 bkl 58.00 bkl 58.21 misc crude heater misc diameter of flue pipe misc convective heat exchange misc radiant heat exchange misc annual reduced costs misc optimization Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium |
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Pechenegov, Yu. Ya. |
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620 - Engineering & allied operations 660 - Chemical engineering |
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620 660 ASE 58.00 bkl 58.21 bkl Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium crude heater (dpeaa)DE-He213 diameter of flue pipe (dpeaa)DE-He213 convective heat exchange (dpeaa)DE-He213 radiant heat exchange (dpeaa)DE-He213 annual reduced costs (dpeaa)DE-He213 optimization (dpeaa)DE-He213 |
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ddc 620 bkl 58.00 bkl 58.21 misc crude heater misc diameter of flue pipe misc convective heat exchange misc radiant heat exchange misc annual reduced costs misc optimization |
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ddc 620 bkl 58.00 bkl 58.21 misc crude heater misc diameter of flue pipe misc convective heat exchange misc radiant heat exchange misc annual reduced costs misc optimization |
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ddc 620 bkl 58.00 bkl 58.21 misc crude heater misc diameter of flue pipe misc convective heat exchange misc radiant heat exchange misc annual reduced costs misc optimization |
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Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium |
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| title_full |
Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium |
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Pechenegov, Yu. Ya. |
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Chemical and petroleum engineering |
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Chemical and petroleum engineering |
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2012 |
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Pechenegov, Yu. Ya. Denisenko, I. P. |
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620 660 ASE 58.00 bkl 58.21 bkl |
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Elektronische Aufsätze |
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Pechenegov, Yu. Ya. |
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10.1007/s10556-012-9579-2 |
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620 660 |
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verfasserin |
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selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium |
| title_auth |
Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium |
| abstract |
Results are presented for a computational analysis performed to determine the most favorable diameters of the high-temperature section of the flue pipe in crude heaters with an intermediate heat-transfer medium. It is demonstrated that economically suitable diameters for the flue pipe are limited by the minimum value for which the working expression was obtained in the study. It is also indicated that ring-vortex generators placed in the high-temperature section of the flue pipe for intensification of convective heat exchange are technically and economically expedient. |
| abstractGer |
Results are presented for a computational analysis performed to determine the most favorable diameters of the high-temperature section of the flue pipe in crude heaters with an intermediate heat-transfer medium. It is demonstrated that economically suitable diameters for the flue pipe are limited by the minimum value for which the working expression was obtained in the study. It is also indicated that ring-vortex generators placed in the high-temperature section of the flue pipe for intensification of convective heat exchange are technically and economically expedient. |
| abstract_unstemmed |
Results are presented for a computational analysis performed to determine the most favorable diameters of the high-temperature section of the flue pipe in crude heaters with an intermediate heat-transfer medium. It is demonstrated that economically suitable diameters for the flue pipe are limited by the minimum value for which the working expression was obtained in the study. It is also indicated that ring-vortex generators placed in the high-temperature section of the flue pipe for intensification of convective heat exchange are technically and economically expedient. |
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Selection of flue-pipe diameter for crude heaters with an intermediate liquid heat-transfer medium |
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https://dx.doi.org/10.1007/s10556-012-9579-2 |
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Denisenko, I. P. |
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10.1007/s10556-012-9579-2 |
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|
| score |
7.401043 |