Concentration of magnesium chloride solution in experimental equipment with a descending film
The aim of the work is determination of production temperature and salt regimes for an industrial three-vessel vacuum evaporation unit for concentrating magnesium chloride solution, included within technology for artificial carnallite preparation. A scheme is provided, and a unit developed and manuf...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Tretyakov, D. S. [verfasserIn] Kartovskii, Yu. V. [verfasserIn] Tokarev, S. M. [verfasserIn] Vasiliev, S. G. [verfasserIn] Glushko, K. V. [verfasserIn] Trufanov, V. A. [verfasserIn] Chernykh, N. G. [verfasserIn] Tolkachev, N. N. [verfasserIn] Chemezov, V. A. [verfasserIn] Emelina, N. G. [verfasserIn] Shchelkonogov, A. A. [verfasserIn] Kiselev, V. A. [verfasserIn] Potekha, A. I. [verfasserIn] Abzalov, R. Kh. [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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| Übergeordnetes Werk: |
Enthalten in: Chemical and petroleum engineering - New York, NY [u.a.] : Consultants Bureau, 1965, 47(2011), 7-8 vom: Nov., Seite 520-525 |
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| Übergeordnetes Werk: |
volume:47 ; year:2011 ; number:7-8 ; month:11 ; pages:520-525 |
| Links: |
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| DOI / URN: |
10.1007/s10556-011-9503-1 |
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| Katalog-ID: |
SPR011269367 |
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| 245 | 1 | 0 | |a Concentration of magnesium chloride solution in experimental equipment with a descending film |
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| 520 | |a The aim of the work is determination of production temperature and salt regimes for an industrial three-vessel vacuum evaporation unit for concentrating magnesium chloride solution, included within technology for artificial carnallite preparation. A scheme is provided, and a unit developed and manufactured for this purpose is described. Experimental data are provided that were obtained during magnesium chloride solution concentration within a single-tube evaporation unit with a descending film (unit) under different regimes. A distribution device is selected for provision of stable film flow over the inner surface of a heat-exchange tube. The possibility is confirmed by experiment for the first time of using equipment with a descending film for concentrating actual magnesium chloride solution. Data are obtained for the limiting salt content within the concentrated solution providing operation of the unit in a crystallization-free regime. | ||
| 650 | 4 | |a Heat Transfer Coefficient |7 (dpeaa)DE-He213 | |
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| 650 | 4 | |a Heat Exchanger Tube |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Carnallite |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Steam Condensate |7 (dpeaa)DE-He213 | |
| 700 | 1 | |a Kartovskii, Yu. V. |e verfasserin |4 aut | |
| 700 | 1 | |a Tokarev, S. M. |e verfasserin |4 aut | |
| 700 | 1 | |a Vasiliev, S. G. |e verfasserin |4 aut | |
| 700 | 1 | |a Glushko, K. V. |e verfasserin |4 aut | |
| 700 | 1 | |a Trufanov, V. A. |e verfasserin |4 aut | |
| 700 | 1 | |a Chernykh, N. G. |e verfasserin |4 aut | |
| 700 | 1 | |a Tolkachev, N. N. |e verfasserin |4 aut | |
| 700 | 1 | |a Chemezov, V. A. |e verfasserin |4 aut | |
| 700 | 1 | |a Emelina, N. G. |e verfasserin |4 aut | |
| 700 | 1 | |a Shchelkonogov, A. A. |e verfasserin |4 aut | |
| 700 | 1 | |a Kiselev, V. A. |e verfasserin |4 aut | |
| 700 | 1 | |a Potekha, A. I. |e verfasserin |4 aut | |
| 700 | 1 | |a Abzalov, R. Kh. |e verfasserin |4 aut | |
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10.1007/s10556-011-9503-1 doi (DE-627)SPR011269367 (SPR)s10556-011-9503-1-e DE-627 ger DE-627 rakwb eng 620 660 ASE 58.00 bkl 58.21 bkl Tretyakov, D. S. verfasserin aut Concentration of magnesium chloride solution in experimental equipment with a descending film 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The aim of the work is determination of production temperature and salt regimes for an industrial three-vessel vacuum evaporation unit for concentrating magnesium chloride solution, included within technology for artificial carnallite preparation. A scheme is provided, and a unit developed and manufactured for this purpose is described. Experimental data are provided that were obtained during magnesium chloride solution concentration within a single-tube evaporation unit with a descending film (unit) under different regimes. A distribution device is selected for provision of stable film flow over the inner surface of a heat-exchange tube. The possibility is confirmed by experiment for the first time of using equipment with a descending film for concentrating actual magnesium chloride solution. Data are obtained for the limiting salt content within the concentrated solution providing operation of the unit in a crystallization-free regime. Heat Transfer Coefficient (dpeaa)DE-He213 Steel 12Kh18N10T (dpeaa)DE-He213 Heat Exchanger Tube (dpeaa)DE-He213 Carnallite (dpeaa)DE-He213 Steam Condensate (dpeaa)DE-He213 Kartovskii, Yu. V. verfasserin aut Tokarev, S. M. verfasserin aut Vasiliev, S. G. verfasserin aut Glushko, K. V. verfasserin aut Trufanov, V. A. verfasserin aut Chernykh, N. G. verfasserin aut Tolkachev, N. N. verfasserin aut Chemezov, V. A. verfasserin aut Emelina, N. G. verfasserin aut Shchelkonogov, A. A. verfasserin aut Kiselev, V. A. verfasserin aut Potekha, A. I. verfasserin aut Abzalov, R. Kh. verfasserin aut Enthalten in Chemical and petroleum engineering New York, NY [u.a.] : Consultants Bureau, 1965 47(2011), 7-8 vom: Nov., Seite 520-525 (DE-627)325568421 (DE-600)2037114-7 1573-8329 nnns volume:47 year:2011 number:7-8 month:11 pages:520-525 https://dx.doi.org/10.1007/s10556-011-9503-1 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 47 2011 7-8 11 520-525 |
| spelling |
10.1007/s10556-011-9503-1 doi (DE-627)SPR011269367 (SPR)s10556-011-9503-1-e DE-627 ger DE-627 rakwb eng 620 660 ASE 58.00 bkl 58.21 bkl Tretyakov, D. S. verfasserin aut Concentration of magnesium chloride solution in experimental equipment with a descending film 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The aim of the work is determination of production temperature and salt regimes for an industrial three-vessel vacuum evaporation unit for concentrating magnesium chloride solution, included within technology for artificial carnallite preparation. A scheme is provided, and a unit developed and manufactured for this purpose is described. Experimental data are provided that were obtained during magnesium chloride solution concentration within a single-tube evaporation unit with a descending film (unit) under different regimes. A distribution device is selected for provision of stable film flow over the inner surface of a heat-exchange tube. The possibility is confirmed by experiment for the first time of using equipment with a descending film for concentrating actual magnesium chloride solution. Data are obtained for the limiting salt content within the concentrated solution providing operation of the unit in a crystallization-free regime. Heat Transfer Coefficient (dpeaa)DE-He213 Steel 12Kh18N10T (dpeaa)DE-He213 Heat Exchanger Tube (dpeaa)DE-He213 Carnallite (dpeaa)DE-He213 Steam Condensate (dpeaa)DE-He213 Kartovskii, Yu. V. verfasserin aut Tokarev, S. M. verfasserin aut Vasiliev, S. G. verfasserin aut Glushko, K. V. verfasserin aut Trufanov, V. A. verfasserin aut Chernykh, N. G. verfasserin aut Tolkachev, N. N. verfasserin aut Chemezov, V. A. verfasserin aut Emelina, N. G. verfasserin aut Shchelkonogov, A. A. verfasserin aut Kiselev, V. A. verfasserin aut Potekha, A. I. verfasserin aut Abzalov, R. Kh. verfasserin aut Enthalten in Chemical and petroleum engineering New York, NY [u.a.] : Consultants Bureau, 1965 47(2011), 7-8 vom: Nov., Seite 520-525 (DE-627)325568421 (DE-600)2037114-7 1573-8329 nnns volume:47 year:2011 number:7-8 month:11 pages:520-525 https://dx.doi.org/10.1007/s10556-011-9503-1 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 47 2011 7-8 11 520-525 |
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10.1007/s10556-011-9503-1 doi (DE-627)SPR011269367 (SPR)s10556-011-9503-1-e DE-627 ger DE-627 rakwb eng 620 660 ASE 58.00 bkl 58.21 bkl Tretyakov, D. S. verfasserin aut Concentration of magnesium chloride solution in experimental equipment with a descending film 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The aim of the work is determination of production temperature and salt regimes for an industrial three-vessel vacuum evaporation unit for concentrating magnesium chloride solution, included within technology for artificial carnallite preparation. A scheme is provided, and a unit developed and manufactured for this purpose is described. Experimental data are provided that were obtained during magnesium chloride solution concentration within a single-tube evaporation unit with a descending film (unit) under different regimes. A distribution device is selected for provision of stable film flow over the inner surface of a heat-exchange tube. The possibility is confirmed by experiment for the first time of using equipment with a descending film for concentrating actual magnesium chloride solution. Data are obtained for the limiting salt content within the concentrated solution providing operation of the unit in a crystallization-free regime. Heat Transfer Coefficient (dpeaa)DE-He213 Steel 12Kh18N10T (dpeaa)DE-He213 Heat Exchanger Tube (dpeaa)DE-He213 Carnallite (dpeaa)DE-He213 Steam Condensate (dpeaa)DE-He213 Kartovskii, Yu. V. verfasserin aut Tokarev, S. M. verfasserin aut Vasiliev, S. G. verfasserin aut Glushko, K. V. verfasserin aut Trufanov, V. A. verfasserin aut Chernykh, N. G. verfasserin aut Tolkachev, N. N. verfasserin aut Chemezov, V. A. verfasserin aut Emelina, N. G. verfasserin aut Shchelkonogov, A. A. verfasserin aut Kiselev, V. A. verfasserin aut Potekha, A. I. verfasserin aut Abzalov, R. Kh. verfasserin aut Enthalten in Chemical and petroleum engineering New York, NY [u.a.] : Consultants Bureau, 1965 47(2011), 7-8 vom: Nov., Seite 520-525 (DE-627)325568421 (DE-600)2037114-7 1573-8329 nnns volume:47 year:2011 number:7-8 month:11 pages:520-525 https://dx.doi.org/10.1007/s10556-011-9503-1 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 47 2011 7-8 11 520-525 |
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10.1007/s10556-011-9503-1 doi (DE-627)SPR011269367 (SPR)s10556-011-9503-1-e DE-627 ger DE-627 rakwb eng 620 660 ASE 58.00 bkl 58.21 bkl Tretyakov, D. S. verfasserin aut Concentration of magnesium chloride solution in experimental equipment with a descending film 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The aim of the work is determination of production temperature and salt regimes for an industrial three-vessel vacuum evaporation unit for concentrating magnesium chloride solution, included within technology for artificial carnallite preparation. A scheme is provided, and a unit developed and manufactured for this purpose is described. Experimental data are provided that were obtained during magnesium chloride solution concentration within a single-tube evaporation unit with a descending film (unit) under different regimes. A distribution device is selected for provision of stable film flow over the inner surface of a heat-exchange tube. The possibility is confirmed by experiment for the first time of using equipment with a descending film for concentrating actual magnesium chloride solution. Data are obtained for the limiting salt content within the concentrated solution providing operation of the unit in a crystallization-free regime. Heat Transfer Coefficient (dpeaa)DE-He213 Steel 12Kh18N10T (dpeaa)DE-He213 Heat Exchanger Tube (dpeaa)DE-He213 Carnallite (dpeaa)DE-He213 Steam Condensate (dpeaa)DE-He213 Kartovskii, Yu. V. verfasserin aut Tokarev, S. M. verfasserin aut Vasiliev, S. G. verfasserin aut Glushko, K. V. verfasserin aut Trufanov, V. A. verfasserin aut Chernykh, N. G. verfasserin aut Tolkachev, N. N. verfasserin aut Chemezov, V. A. verfasserin aut Emelina, N. G. verfasserin aut Shchelkonogov, A. A. verfasserin aut Kiselev, V. A. verfasserin aut Potekha, A. I. verfasserin aut Abzalov, R. Kh. verfasserin aut Enthalten in Chemical and petroleum engineering New York, NY [u.a.] : Consultants Bureau, 1965 47(2011), 7-8 vom: Nov., Seite 520-525 (DE-627)325568421 (DE-600)2037114-7 1573-8329 nnns volume:47 year:2011 number:7-8 month:11 pages:520-525 https://dx.doi.org/10.1007/s10556-011-9503-1 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 47 2011 7-8 11 520-525 |
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10.1007/s10556-011-9503-1 doi (DE-627)SPR011269367 (SPR)s10556-011-9503-1-e DE-627 ger DE-627 rakwb eng 620 660 ASE 58.00 bkl 58.21 bkl Tretyakov, D. S. verfasserin aut Concentration of magnesium chloride solution in experimental equipment with a descending film 2011 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The aim of the work is determination of production temperature and salt regimes for an industrial three-vessel vacuum evaporation unit for concentrating magnesium chloride solution, included within technology for artificial carnallite preparation. A scheme is provided, and a unit developed and manufactured for this purpose is described. Experimental data are provided that were obtained during magnesium chloride solution concentration within a single-tube evaporation unit with a descending film (unit) under different regimes. A distribution device is selected for provision of stable film flow over the inner surface of a heat-exchange tube. The possibility is confirmed by experiment for the first time of using equipment with a descending film for concentrating actual magnesium chloride solution. Data are obtained for the limiting salt content within the concentrated solution providing operation of the unit in a crystallization-free regime. Heat Transfer Coefficient (dpeaa)DE-He213 Steel 12Kh18N10T (dpeaa)DE-He213 Heat Exchanger Tube (dpeaa)DE-He213 Carnallite (dpeaa)DE-He213 Steam Condensate (dpeaa)DE-He213 Kartovskii, Yu. V. verfasserin aut Tokarev, S. M. verfasserin aut Vasiliev, S. G. verfasserin aut Glushko, K. V. verfasserin aut Trufanov, V. A. verfasserin aut Chernykh, N. G. verfasserin aut Tolkachev, N. N. verfasserin aut Chemezov, V. A. verfasserin aut Emelina, N. G. verfasserin aut Shchelkonogov, A. A. verfasserin aut Kiselev, V. A. verfasserin aut Potekha, A. I. verfasserin aut Abzalov, R. Kh. verfasserin aut Enthalten in Chemical and petroleum engineering New York, NY [u.a.] : Consultants Bureau, 1965 47(2011), 7-8 vom: Nov., Seite 520-525 (DE-627)325568421 (DE-600)2037114-7 1573-8329 nnns volume:47 year:2011 number:7-8 month:11 pages:520-525 https://dx.doi.org/10.1007/s10556-011-9503-1 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 47 2011 7-8 11 520-525 |
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Enthalten in Chemical and petroleum engineering 47(2011), 7-8 vom: Nov., Seite 520-525 volume:47 year:2011 number:7-8 month:11 pages:520-525 |
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Enthalten in Chemical and petroleum engineering 47(2011), 7-8 vom: Nov., Seite 520-525 volume:47 year:2011 number:7-8 month:11 pages:520-525 |
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Tretyakov, D. S. @@aut@@ Kartovskii, Yu. V. @@aut@@ Tokarev, S. M. @@aut@@ Vasiliev, S. G. @@aut@@ Glushko, K. V. @@aut@@ Trufanov, V. A. @@aut@@ Chernykh, N. G. @@aut@@ Tolkachev, N. N. @@aut@@ Chemezov, V. A. @@aut@@ Emelina, N. G. @@aut@@ Shchelkonogov, A. A. @@aut@@ Kiselev, V. A. @@aut@@ Potekha, A. I. @@aut@@ Abzalov, R. Kh. @@aut@@ |
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A scheme is provided, and a unit developed and manufactured for this purpose is described. Experimental data are provided that were obtained during magnesium chloride solution concentration within a single-tube evaporation unit with a descending film (unit) under different regimes. A distribution device is selected for provision of stable film flow over the inner surface of a heat-exchange tube. The possibility is confirmed by experiment for the first time of using equipment with a descending film for concentrating actual magnesium chloride solution. 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|
| author |
Tretyakov, D. S. |
| spellingShingle |
Tretyakov, D. S. ddc 620 bkl 58.00 bkl 58.21 misc Heat Transfer Coefficient misc Steel 12Kh18N10T misc Heat Exchanger Tube misc Carnallite misc Steam Condensate Concentration of magnesium chloride solution in experimental equipment with a descending film |
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Tretyakov, D. S. |
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electronic Article |
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620 - Engineering & allied operations 660 - Chemical engineering |
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keep |
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springer |
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true |
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Not Illustrated |
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1573-8329 |
| topic_title |
620 660 ASE 58.00 bkl 58.21 bkl Concentration of magnesium chloride solution in experimental equipment with a descending film Heat Transfer Coefficient (dpeaa)DE-He213 Steel 12Kh18N10T (dpeaa)DE-He213 Heat Exchanger Tube (dpeaa)DE-He213 Carnallite (dpeaa)DE-He213 Steam Condensate (dpeaa)DE-He213 |
| topic |
ddc 620 bkl 58.00 bkl 58.21 misc Heat Transfer Coefficient misc Steel 12Kh18N10T misc Heat Exchanger Tube misc Carnallite misc Steam Condensate |
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ddc 620 bkl 58.00 bkl 58.21 misc Heat Transfer Coefficient misc Steel 12Kh18N10T misc Heat Exchanger Tube misc Carnallite misc Steam Condensate |
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ddc 620 bkl 58.00 bkl 58.21 misc Heat Transfer Coefficient misc Steel 12Kh18N10T misc Heat Exchanger Tube misc Carnallite misc Steam Condensate |
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Elektronische Aufsätze Aufsätze Elektronische Ressource |
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Chemical and petroleum engineering |
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620 - Engineering 660 - Chemical engineering |
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Chemical and petroleum engineering |
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Concentration of magnesium chloride solution in experimental equipment with a descending film |
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Concentration of magnesium chloride solution in experimental equipment with a descending film |
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Tretyakov, D. S. |
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Chemical and petroleum engineering |
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Tretyakov, D. S. Kartovskii, Yu. V. Tokarev, S. M. Vasiliev, S. G. Glushko, K. V. Trufanov, V. A. Chernykh, N. G. Tolkachev, N. N. Chemezov, V. A. Emelina, N. G. Shchelkonogov, A. A. Kiselev, V. A. Potekha, A. I. Abzalov, R. Kh. |
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concentration of magnesium chloride solution in experimental equipment with a descending film |
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Concentration of magnesium chloride solution in experimental equipment with a descending film |
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The aim of the work is determination of production temperature and salt regimes for an industrial three-vessel vacuum evaporation unit for concentrating magnesium chloride solution, included within technology for artificial carnallite preparation. A scheme is provided, and a unit developed and manufactured for this purpose is described. Experimental data are provided that were obtained during magnesium chloride solution concentration within a single-tube evaporation unit with a descending film (unit) under different regimes. A distribution device is selected for provision of stable film flow over the inner surface of a heat-exchange tube. The possibility is confirmed by experiment for the first time of using equipment with a descending film for concentrating actual magnesium chloride solution. Data are obtained for the limiting salt content within the concentrated solution providing operation of the unit in a crystallization-free regime. |
| abstractGer |
The aim of the work is determination of production temperature and salt regimes for an industrial three-vessel vacuum evaporation unit for concentrating magnesium chloride solution, included within technology for artificial carnallite preparation. A scheme is provided, and a unit developed and manufactured for this purpose is described. Experimental data are provided that were obtained during magnesium chloride solution concentration within a single-tube evaporation unit with a descending film (unit) under different regimes. A distribution device is selected for provision of stable film flow over the inner surface of a heat-exchange tube. The possibility is confirmed by experiment for the first time of using equipment with a descending film for concentrating actual magnesium chloride solution. Data are obtained for the limiting salt content within the concentrated solution providing operation of the unit in a crystallization-free regime. |
| abstract_unstemmed |
The aim of the work is determination of production temperature and salt regimes for an industrial three-vessel vacuum evaporation unit for concentrating magnesium chloride solution, included within technology for artificial carnallite preparation. A scheme is provided, and a unit developed and manufactured for this purpose is described. Experimental data are provided that were obtained during magnesium chloride solution concentration within a single-tube evaporation unit with a descending film (unit) under different regimes. A distribution device is selected for provision of stable film flow over the inner surface of a heat-exchange tube. The possibility is confirmed by experiment for the first time of using equipment with a descending film for concentrating actual magnesium chloride solution. Data are obtained for the limiting salt content within the concentrated solution providing operation of the unit in a crystallization-free regime. |
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Concentration of magnesium chloride solution in experimental equipment with a descending film |
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Kartovskii, Yu. V. Tokarev, S. M. Vasiliev, S. G. Glushko, K. V. Trufanov, V. A. Chernykh, N. G. Tolkachev, N. N. Chemezov, V. A. Emelina, N. G. Shchelkonogov, A. A. Kiselev, V. A. Potekha, A. I. Abzalov, R. Kh |
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| score |
7.399971 |