Deodorizing system modification for heat recovery and steam refining of palm oil
Abstract With continuous deodorizers of the double shell type most of the steam normally used to preheat the feedstock in the deaerating section can be saved by a modification-the essential feature of which is the addition of a heat recovery section location between the final deodorizing section and...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Gavin, Arnold M. [verfasserIn] |
|---|
| Format: |
Artikel |
|---|---|
| Sprache: |
Englisch |
| Erschienen: |
1973 |
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| Schlagwörter: |
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| Anmerkung: |
© The American Oil Chemists' Society 1973 |
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| Übergeordnetes Werk: |
Enthalten in: Journal of the American Oil Chemists Society - Springer-Verlag, 1947, 50(1973), 11 vom: Nov., Seite 466A-472A |
|---|---|
| Übergeordnetes Werk: |
volume:50 ; year:1973 ; number:11 ; month:11 ; pages:466A-472A |
| Links: |
|---|
| DOI / URN: |
10.1007/BF02639859 |
|---|
| Katalog-ID: |
OLC2068048582 |
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| 520 | |a Abstract With continuous deodorizers of the double shell type most of the steam normally used to preheat the feedstock in the deaerating section can be saved by a modification-the essential feature of which is the addition of a heat recovery section location between the final deodorizing section and the cooling section, by means of which heat is transferred from the hot deodorized oil to the feedstock. Consistent with the principles of the original design, no pumping or piping of hot oil outside the deodorizer is required. Continuous deodorizers of the stripping tray type can be modified for “steam refining” or “stripping” of high free fatty acid palm oil to reduce the free fatty acid palm oil to reduce the free fatty acids to 0.03% max. This is accomplished by means of additional trays in the stripping sections of the deodorizer. The capacity, sparge steam temperature, vacuum and retention time remain the same as with normal deodorization. | ||
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10.1007/BF02639859 doi (DE-627)OLC2068048582 (DE-He213)BF02639859-p DE-627 ger DE-627 rakwb eng 660 VZ Gavin, Arnold M. verfasserin aut Deodorizing system modification for heat recovery and steam refining of palm oil 1973 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © The American Oil Chemists' Society 1973 Abstract With continuous deodorizers of the double shell type most of the steam normally used to preheat the feedstock in the deaerating section can be saved by a modification-the essential feature of which is the addition of a heat recovery section location between the final deodorizing section and the cooling section, by means of which heat is transferred from the hot deodorized oil to the feedstock. Consistent with the principles of the original design, no pumping or piping of hot oil outside the deodorizer is required. Continuous deodorizers of the stripping tray type can be modified for “steam refining” or “stripping” of high free fatty acid palm oil to reduce the free fatty acid palm oil to reduce the free fatty acids to 0.03% max. This is accomplished by means of additional trays in the stripping sections of the deodorizer. The capacity, sparge steam temperature, vacuum and retention time remain the same as with normal deodorization. Steam Free Fatty Acid Heat Recovery Free Fatty Acid Concentration High Free Fatty Acid Berger, Ralph W. aut Enthalten in Journal of the American Oil Chemists Society Springer-Verlag, 1947 50(1973), 11 vom: Nov., Seite 466A-472A (DE-627)129595691 (DE-600)240684-6 (DE-576)015088715 0003-021X nnns volume:50 year:1973 number:11 month:11 pages:466A-472A https://doi.org/10.1007/BF02639859 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_26 GBV_ILN_40 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2360 GBV_ILN_4012 GBV_ILN_4036 GBV_ILN_4046 GBV_ILN_4125 GBV_ILN_4219 GBV_ILN_4306 GBV_ILN_4315 AR 50 1973 11 11 466A-472A |
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10.1007/BF02639859 doi (DE-627)OLC2068048582 (DE-He213)BF02639859-p DE-627 ger DE-627 rakwb eng 660 VZ Gavin, Arnold M. verfasserin aut Deodorizing system modification for heat recovery and steam refining of palm oil 1973 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © The American Oil Chemists' Society 1973 Abstract With continuous deodorizers of the double shell type most of the steam normally used to preheat the feedstock in the deaerating section can be saved by a modification-the essential feature of which is the addition of a heat recovery section location between the final deodorizing section and the cooling section, by means of which heat is transferred from the hot deodorized oil to the feedstock. Consistent with the principles of the original design, no pumping or piping of hot oil outside the deodorizer is required. Continuous deodorizers of the stripping tray type can be modified for “steam refining” or “stripping” of high free fatty acid palm oil to reduce the free fatty acid palm oil to reduce the free fatty acids to 0.03% max. This is accomplished by means of additional trays in the stripping sections of the deodorizer. The capacity, sparge steam temperature, vacuum and retention time remain the same as with normal deodorization. Steam Free Fatty Acid Heat Recovery Free Fatty Acid Concentration High Free Fatty Acid Berger, Ralph W. aut Enthalten in Journal of the American Oil Chemists Society Springer-Verlag, 1947 50(1973), 11 vom: Nov., Seite 466A-472A (DE-627)129595691 (DE-600)240684-6 (DE-576)015088715 0003-021X nnns volume:50 year:1973 number:11 month:11 pages:466A-472A https://doi.org/10.1007/BF02639859 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_26 GBV_ILN_40 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2360 GBV_ILN_4012 GBV_ILN_4036 GBV_ILN_4046 GBV_ILN_4125 GBV_ILN_4219 GBV_ILN_4306 GBV_ILN_4315 AR 50 1973 11 11 466A-472A |
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10.1007/BF02639859 doi (DE-627)OLC2068048582 (DE-He213)BF02639859-p DE-627 ger DE-627 rakwb eng 660 VZ Gavin, Arnold M. verfasserin aut Deodorizing system modification for heat recovery and steam refining of palm oil 1973 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © The American Oil Chemists' Society 1973 Abstract With continuous deodorizers of the double shell type most of the steam normally used to preheat the feedstock in the deaerating section can be saved by a modification-the essential feature of which is the addition of a heat recovery section location between the final deodorizing section and the cooling section, by means of which heat is transferred from the hot deodorized oil to the feedstock. Consistent with the principles of the original design, no pumping or piping of hot oil outside the deodorizer is required. Continuous deodorizers of the stripping tray type can be modified for “steam refining” or “stripping” of high free fatty acid palm oil to reduce the free fatty acid palm oil to reduce the free fatty acids to 0.03% max. This is accomplished by means of additional trays in the stripping sections of the deodorizer. The capacity, sparge steam temperature, vacuum and retention time remain the same as with normal deodorization. Steam Free Fatty Acid Heat Recovery Free Fatty Acid Concentration High Free Fatty Acid Berger, Ralph W. aut Enthalten in Journal of the American Oil Chemists Society Springer-Verlag, 1947 50(1973), 11 vom: Nov., Seite 466A-472A (DE-627)129595691 (DE-600)240684-6 (DE-576)015088715 0003-021X nnns volume:50 year:1973 number:11 month:11 pages:466A-472A https://doi.org/10.1007/BF02639859 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_26 GBV_ILN_40 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2360 GBV_ILN_4012 GBV_ILN_4036 GBV_ILN_4046 GBV_ILN_4125 GBV_ILN_4219 GBV_ILN_4306 GBV_ILN_4315 AR 50 1973 11 11 466A-472A |
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10.1007/BF02639859 doi (DE-627)OLC2068048582 (DE-He213)BF02639859-p DE-627 ger DE-627 rakwb eng 660 VZ Gavin, Arnold M. verfasserin aut Deodorizing system modification for heat recovery and steam refining of palm oil 1973 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © The American Oil Chemists' Society 1973 Abstract With continuous deodorizers of the double shell type most of the steam normally used to preheat the feedstock in the deaerating section can be saved by a modification-the essential feature of which is the addition of a heat recovery section location between the final deodorizing section and the cooling section, by means of which heat is transferred from the hot deodorized oil to the feedstock. Consistent with the principles of the original design, no pumping or piping of hot oil outside the deodorizer is required. Continuous deodorizers of the stripping tray type can be modified for “steam refining” or “stripping” of high free fatty acid palm oil to reduce the free fatty acid palm oil to reduce the free fatty acids to 0.03% max. This is accomplished by means of additional trays in the stripping sections of the deodorizer. The capacity, sparge steam temperature, vacuum and retention time remain the same as with normal deodorization. Steam Free Fatty Acid Heat Recovery Free Fatty Acid Concentration High Free Fatty Acid Berger, Ralph W. aut Enthalten in Journal of the American Oil Chemists Society Springer-Verlag, 1947 50(1973), 11 vom: Nov., Seite 466A-472A (DE-627)129595691 (DE-600)240684-6 (DE-576)015088715 0003-021X nnns volume:50 year:1973 number:11 month:11 pages:466A-472A https://doi.org/10.1007/BF02639859 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_26 GBV_ILN_40 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2360 GBV_ILN_4012 GBV_ILN_4036 GBV_ILN_4046 GBV_ILN_4125 GBV_ILN_4219 GBV_ILN_4306 GBV_ILN_4315 AR 50 1973 11 11 466A-472A |
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10.1007/BF02639859 doi (DE-627)OLC2068048582 (DE-He213)BF02639859-p DE-627 ger DE-627 rakwb eng 660 VZ Gavin, Arnold M. verfasserin aut Deodorizing system modification for heat recovery and steam refining of palm oil 1973 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © The American Oil Chemists' Society 1973 Abstract With continuous deodorizers of the double shell type most of the steam normally used to preheat the feedstock in the deaerating section can be saved by a modification-the essential feature of which is the addition of a heat recovery section location between the final deodorizing section and the cooling section, by means of which heat is transferred from the hot deodorized oil to the feedstock. Consistent with the principles of the original design, no pumping or piping of hot oil outside the deodorizer is required. Continuous deodorizers of the stripping tray type can be modified for “steam refining” or “stripping” of high free fatty acid palm oil to reduce the free fatty acid palm oil to reduce the free fatty acids to 0.03% max. This is accomplished by means of additional trays in the stripping sections of the deodorizer. The capacity, sparge steam temperature, vacuum and retention time remain the same as with normal deodorization. Steam Free Fatty Acid Heat Recovery Free Fatty Acid Concentration High Free Fatty Acid Berger, Ralph W. aut Enthalten in Journal of the American Oil Chemists Society Springer-Verlag, 1947 50(1973), 11 vom: Nov., Seite 466A-472A (DE-627)129595691 (DE-600)240684-6 (DE-576)015088715 0003-021X nnns volume:50 year:1973 number:11 month:11 pages:466A-472A https://doi.org/10.1007/BF02639859 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_26 GBV_ILN_40 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2360 GBV_ILN_4012 GBV_ILN_4036 GBV_ILN_4046 GBV_ILN_4125 GBV_ILN_4219 GBV_ILN_4306 GBV_ILN_4315 AR 50 1973 11 11 466A-472A |
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| title_full |
Deodorizing system modification for heat recovery and steam refining of palm oil |
| author_sort |
Gavin, Arnold M. |
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Journal of the American Oil Chemists Society |
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Journal of the American Oil Chemists Society |
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eng |
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600 - Technology |
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marc |
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1973 |
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txt |
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466 |
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Gavin, Arnold M. Berger, Ralph W. |
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50 |
| class |
660 VZ |
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Aufsätze |
| author-letter |
Gavin, Arnold M. |
| doi_str_mv |
10.1007/BF02639859 |
| dewey-full |
660 |
| title_sort |
deodorizing system modification for heat recovery and steam refining of palm oil |
| title_auth |
Deodorizing system modification for heat recovery and steam refining of palm oil |
| abstract |
Abstract With continuous deodorizers of the double shell type most of the steam normally used to preheat the feedstock in the deaerating section can be saved by a modification-the essential feature of which is the addition of a heat recovery section location between the final deodorizing section and the cooling section, by means of which heat is transferred from the hot deodorized oil to the feedstock. Consistent with the principles of the original design, no pumping or piping of hot oil outside the deodorizer is required. Continuous deodorizers of the stripping tray type can be modified for “steam refining” or “stripping” of high free fatty acid palm oil to reduce the free fatty acid palm oil to reduce the free fatty acids to 0.03% max. This is accomplished by means of additional trays in the stripping sections of the deodorizer. The capacity, sparge steam temperature, vacuum and retention time remain the same as with normal deodorization. © The American Oil Chemists' Society 1973 |
| abstractGer |
Abstract With continuous deodorizers of the double shell type most of the steam normally used to preheat the feedstock in the deaerating section can be saved by a modification-the essential feature of which is the addition of a heat recovery section location between the final deodorizing section and the cooling section, by means of which heat is transferred from the hot deodorized oil to the feedstock. Consistent with the principles of the original design, no pumping or piping of hot oil outside the deodorizer is required. Continuous deodorizers of the stripping tray type can be modified for “steam refining” or “stripping” of high free fatty acid palm oil to reduce the free fatty acid palm oil to reduce the free fatty acids to 0.03% max. This is accomplished by means of additional trays in the stripping sections of the deodorizer. The capacity, sparge steam temperature, vacuum and retention time remain the same as with normal deodorization. © The American Oil Chemists' Society 1973 |
| abstract_unstemmed |
Abstract With continuous deodorizers of the double shell type most of the steam normally used to preheat the feedstock in the deaerating section can be saved by a modification-the essential feature of which is the addition of a heat recovery section location between the final deodorizing section and the cooling section, by means of which heat is transferred from the hot deodorized oil to the feedstock. Consistent with the principles of the original design, no pumping or piping of hot oil outside the deodorizer is required. Continuous deodorizers of the stripping tray type can be modified for “steam refining” or “stripping” of high free fatty acid palm oil to reduce the free fatty acid palm oil to reduce the free fatty acids to 0.03% max. This is accomplished by means of additional trays in the stripping sections of the deodorizer. The capacity, sparge steam temperature, vacuum and retention time remain the same as with normal deodorization. © The American Oil Chemists' Society 1973 |
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| container_issue |
11 |
| title_short |
Deodorizing system modification for heat recovery and steam refining of palm oil |
| url |
https://doi.org/10.1007/BF02639859 |
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| author2 |
Berger, Ralph W. |
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| up_date |
2024-07-03T17:26:06.759Z |
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