Biorefining of high acid rice bran oil
Abstract Rice bran oil with a high free fatty acid content (FFA) after degumming and dewaxing can be converted into edible quality oil of satisfactory refining characteristics by first adopting the biorefining process to reduce the major portion of the FFA by converting them into neutral glycerides...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Bhattacharyya, S. [verfasserIn] |
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| Format: |
Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
1989 |
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| Schlagwörter: |
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| Anmerkung: |
© American Oil Chemists’ Society 1989 |
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| Übergeordnetes Werk: |
Enthalten in: Journal of the American Oil Chemists’ Society - Springer-Verlag, 1947, 66(1989), 12 vom: Dez., Seite 1809-1811 |
|---|---|
| Übergeordnetes Werk: |
volume:66 ; year:1989 ; number:12 ; month:12 ; pages:1809-1811 |
| Links: |
|---|
| DOI / URN: |
10.1007/BF02660752 |
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| 520 | |a Abstract Rice bran oil with a high free fatty acid content (FFA) after degumming and dewaxing can be converted into edible quality oil of satisfactory refining characteristics by first adopting the biorefining process to reduce the major portion of the FFA by converting them into neutral glycerides with the aid of 1,3-specific lipase under optimum conditions and later deacidifying the residual FFA of the biorefined oil by alkali neutralization. | ||
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10.1007/BF02660752 doi (DE-627)OLC2068111322 (DE-He213)BF02660752-p DE-627 ger DE-627 rakwb eng 660 VZ Bhattacharyya, S. verfasserin aut Biorefining of high acid rice bran oil 1989 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © American Oil Chemists’ Society 1989 Abstract Rice bran oil with a high free fatty acid content (FFA) after degumming and dewaxing can be converted into edible quality oil of satisfactory refining characteristics by first adopting the biorefining process to reduce the major portion of the FFA by converting them into neutral glycerides with the aid of 1,3-specific lipase under optimum conditions and later deacidifying the residual FFA of the biorefined oil by alkali neutralization. Free Fatty Acid Free Fatty Acid Level Alkali Refining High Free Fatty Acid Content Free Fatty Acid Percentage Bhattacharyya, D. K. aut Enthalten in Journal of the American Oil Chemists’ Society Springer-Verlag, 1947 66(1989), 12 vom: Dez., Seite 1809-1811 (DE-627)129595691 (DE-600)240684-6 (DE-576)015088715 0003-021X nnns volume:66 year:1989 number:12 month:12 pages:1809-1811 https://doi.org/10.1007/BF02660752 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_23 GBV_ILN_26 GBV_ILN_70 GBV_ILN_95 GBV_ILN_252 GBV_ILN_4012 GBV_ILN_4046 GBV_ILN_4219 GBV_ILN_4306 GBV_ILN_4315 AR 66 1989 12 12 1809-1811 |
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10.1007/BF02660752 doi (DE-627)OLC2068111322 (DE-He213)BF02660752-p DE-627 ger DE-627 rakwb eng 660 VZ Bhattacharyya, S. verfasserin aut Biorefining of high acid rice bran oil 1989 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © American Oil Chemists’ Society 1989 Abstract Rice bran oil with a high free fatty acid content (FFA) after degumming and dewaxing can be converted into edible quality oil of satisfactory refining characteristics by first adopting the biorefining process to reduce the major portion of the FFA by converting them into neutral glycerides with the aid of 1,3-specific lipase under optimum conditions and later deacidifying the residual FFA of the biorefined oil by alkali neutralization. Free Fatty Acid Free Fatty Acid Level Alkali Refining High Free Fatty Acid Content Free Fatty Acid Percentage Bhattacharyya, D. K. aut Enthalten in Journal of the American Oil Chemists’ Society Springer-Verlag, 1947 66(1989), 12 vom: Dez., Seite 1809-1811 (DE-627)129595691 (DE-600)240684-6 (DE-576)015088715 0003-021X nnns volume:66 year:1989 number:12 month:12 pages:1809-1811 https://doi.org/10.1007/BF02660752 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_23 GBV_ILN_26 GBV_ILN_70 GBV_ILN_95 GBV_ILN_252 GBV_ILN_4012 GBV_ILN_4046 GBV_ILN_4219 GBV_ILN_4306 GBV_ILN_4315 AR 66 1989 12 12 1809-1811 |
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10.1007/BF02660752 doi (DE-627)OLC2068111322 (DE-He213)BF02660752-p DE-627 ger DE-627 rakwb eng 660 VZ Bhattacharyya, S. verfasserin aut Biorefining of high acid rice bran oil 1989 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © American Oil Chemists’ Society 1989 Abstract Rice bran oil with a high free fatty acid content (FFA) after degumming and dewaxing can be converted into edible quality oil of satisfactory refining characteristics by first adopting the biorefining process to reduce the major portion of the FFA by converting them into neutral glycerides with the aid of 1,3-specific lipase under optimum conditions and later deacidifying the residual FFA of the biorefined oil by alkali neutralization. Free Fatty Acid Free Fatty Acid Level Alkali Refining High Free Fatty Acid Content Free Fatty Acid Percentage Bhattacharyya, D. K. aut Enthalten in Journal of the American Oil Chemists’ Society Springer-Verlag, 1947 66(1989), 12 vom: Dez., Seite 1809-1811 (DE-627)129595691 (DE-600)240684-6 (DE-576)015088715 0003-021X nnns volume:66 year:1989 number:12 month:12 pages:1809-1811 https://doi.org/10.1007/BF02660752 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_23 GBV_ILN_26 GBV_ILN_70 GBV_ILN_95 GBV_ILN_252 GBV_ILN_4012 GBV_ILN_4046 GBV_ILN_4219 GBV_ILN_4306 GBV_ILN_4315 AR 66 1989 12 12 1809-1811 |
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10.1007/BF02660752 doi (DE-627)OLC2068111322 (DE-He213)BF02660752-p DE-627 ger DE-627 rakwb eng 660 VZ Bhattacharyya, S. verfasserin aut Biorefining of high acid rice bran oil 1989 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © American Oil Chemists’ Society 1989 Abstract Rice bran oil with a high free fatty acid content (FFA) after degumming and dewaxing can be converted into edible quality oil of satisfactory refining characteristics by first adopting the biorefining process to reduce the major portion of the FFA by converting them into neutral glycerides with the aid of 1,3-specific lipase under optimum conditions and later deacidifying the residual FFA of the biorefined oil by alkali neutralization. Free Fatty Acid Free Fatty Acid Level Alkali Refining High Free Fatty Acid Content Free Fatty Acid Percentage Bhattacharyya, D. K. aut Enthalten in Journal of the American Oil Chemists’ Society Springer-Verlag, 1947 66(1989), 12 vom: Dez., Seite 1809-1811 (DE-627)129595691 (DE-600)240684-6 (DE-576)015088715 0003-021X nnns volume:66 year:1989 number:12 month:12 pages:1809-1811 https://doi.org/10.1007/BF02660752 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_23 GBV_ILN_26 GBV_ILN_70 GBV_ILN_95 GBV_ILN_252 GBV_ILN_4012 GBV_ILN_4046 GBV_ILN_4219 GBV_ILN_4306 GBV_ILN_4315 AR 66 1989 12 12 1809-1811 |
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10.1007/BF02660752 doi (DE-627)OLC2068111322 (DE-He213)BF02660752-p DE-627 ger DE-627 rakwb eng 660 VZ Bhattacharyya, S. verfasserin aut Biorefining of high acid rice bran oil 1989 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © American Oil Chemists’ Society 1989 Abstract Rice bran oil with a high free fatty acid content (FFA) after degumming and dewaxing can be converted into edible quality oil of satisfactory refining characteristics by first adopting the biorefining process to reduce the major portion of the FFA by converting them into neutral glycerides with the aid of 1,3-specific lipase under optimum conditions and later deacidifying the residual FFA of the biorefined oil by alkali neutralization. Free Fatty Acid Free Fatty Acid Level Alkali Refining High Free Fatty Acid Content Free Fatty Acid Percentage Bhattacharyya, D. K. aut Enthalten in Journal of the American Oil Chemists’ Society Springer-Verlag, 1947 66(1989), 12 vom: Dez., Seite 1809-1811 (DE-627)129595691 (DE-600)240684-6 (DE-576)015088715 0003-021X nnns volume:66 year:1989 number:12 month:12 pages:1809-1811 https://doi.org/10.1007/BF02660752 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_23 GBV_ILN_26 GBV_ILN_70 GBV_ILN_95 GBV_ILN_252 GBV_ILN_4012 GBV_ILN_4046 GBV_ILN_4219 GBV_ILN_4306 GBV_ILN_4315 AR 66 1989 12 12 1809-1811 |
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Abstract Rice bran oil with a high free fatty acid content (FFA) after degumming and dewaxing can be converted into edible quality oil of satisfactory refining characteristics by first adopting the biorefining process to reduce the major portion of the FFA by converting them into neutral glycerides with the aid of 1,3-specific lipase under optimum conditions and later deacidifying the residual FFA of the biorefined oil by alkali neutralization. © American Oil Chemists’ Society 1989 |
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Abstract Rice bran oil with a high free fatty acid content (FFA) after degumming and dewaxing can be converted into edible quality oil of satisfactory refining characteristics by first adopting the biorefining process to reduce the major portion of the FFA by converting them into neutral glycerides with the aid of 1,3-specific lipase under optimum conditions and later deacidifying the residual FFA of the biorefined oil by alkali neutralization. © American Oil Chemists’ Society 1989 |
| abstract_unstemmed |
Abstract Rice bran oil with a high free fatty acid content (FFA) after degumming and dewaxing can be converted into edible quality oil of satisfactory refining characteristics by first adopting the biorefining process to reduce the major portion of the FFA by converting them into neutral glycerides with the aid of 1,3-specific lipase under optimum conditions and later deacidifying the residual FFA of the biorefined oil by alkali neutralization. © American Oil Chemists’ Society 1989 |
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Biorefining of high acid rice bran oil |
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https://doi.org/10.1007/BF02660752 |
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false |
| author2 |
Bhattacharyya, D. K. |
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Bhattacharyya, D. K. |
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| doi_str |
10.1007/BF02660752 |
| up_date |
2024-07-03T17:37:18.505Z |
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1803580330220716032 |
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