MX168698B - A CONCENTRATE OF REFINED FISH OIL AND PROCEDURE FOR THE PRODUCTION OF THE SAME - Google Patents
A CONCENTRATE OF REFINED FISH OIL AND PROCEDURE FOR THE PRODUCTION OF THE SAMEInfo
- Publication number
- MX168698B MX168698B MX004578A MX457886A MX168698B MX 168698 B MX168698 B MX 168698B MX 004578 A MX004578 A MX 004578A MX 457886 A MX457886 A MX 457886A MX 168698 B MX168698 B MX 168698B
- Authority
- MX
- Mexico
- Prior art keywords
- fatty acid
- fish oil
- esters
- concentrate
- production
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/001—Refining fats or fatty oils by a combination of two or more of the means hereafter
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
Abstract
La presente invención se refiere a procedimiento para la producción de un concentrado de aceite de pescado refinado, caracterizado porque la fracción de grasa/ácido graso del producto de aceite de pescado se esterifica y/o se trans-esterifica a temeratura ambiente con un alcohol inferior, en un ambiente alcalino, y porque el éster alquílico resltante se somete posteriormente a una precipitación fraccionaria por medio de un exceso de urea en un alcanol, y porque esta precipitación tiene lugar enfriando la mezcla a 0ºC despues de haber sido calentada a 55-90ºC mediante un metodo conocido, después de lo cual el aducto de éster alquílico de urea ácido graso precipitado se separa, y porque el resto que ahora contiene principalmente los ésteres de ácido graso w3 esenciales y la porción no saponificable se extrae después mediante un metodo conocido con un solvente para los ésteres al quílicos de ácido graso w3 y la porción insaponificable, después de lo cual el solvente, después de una limpieza preparatoria del extracto con un ácido diluído soluble en agua se separa de manera que el concentrado resultante, junto con sus ésteres al quílicos de ácido graso w3 y la porción no saponificable, son enfriados para la cristalización del colesterol y otros compuestos insaponificables no definidos.The present invention relates to a process for the production of a refined fish oil concentrate, characterized in that the fat / fatty acid fraction of the fish oil product is esterified and / or transesterified at room temperature with a lower alcohol , in an alkaline environment, and because the resulting alkyl ester is subsequently subjected to a fractional precipitation by means of an excess of urea in an alkanol, and because this precipitation takes place by cooling the mixture to 0ºC after having been heated to 55-90ºC by a known method, after which the precipitated fatty acid urea alkyl ester adduct is separated, and because the moiety now containing mainly the essential w3 fatty acid esters and the non-saponifiable portion is then removed by a known method with a solvent for the w3 fatty acid chyl esters and the unsaponifiable portion, after which the solv After a preparatory cleaning of the extract with a dilute acid soluble in water, it is separated so that the resulting concentrate, together with its fatty acid chyl esters w3 and the non-saponifiable portion, are cooled for the crystallization of cholesterol and others. undefined unsaponifiable compounds.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NO855147A NO157302C (en) | 1985-12-19 | 1985-12-19 | PROCEDURE FOR THE PREPARATION OF A FISH OIL CONCENTRATE. |
Publications (1)
Publication Number | Publication Date |
---|---|
MX168698B true MX168698B (en) | 1993-06-04 |
Family
ID=19888637
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX004578A MX168698B (en) | 1985-12-19 | 1986-12-08 | A CONCENTRATE OF REFINED FISH OIL AND PROCEDURE FOR THE PRODUCTION OF THE SAME |
Country Status (15)
Country | Link |
---|---|
EP (1) | EP0255824B1 (en) |
AR (1) | AR242111A1 (en) |
AU (1) | AU6621186A (en) |
CA (1) | CA1303416C (en) |
DD (1) | DD261805A1 (en) |
DE (1) | DE3668467D1 (en) |
IE (1) | IE59171B1 (en) |
IS (1) | IS1425B6 (en) |
MA (1) | MA20840A1 (en) |
MX (1) | MX168698B (en) |
NO (1) | NO157302C (en) |
NZ (1) | NZ218500A (en) |
PT (1) | PT83991B (en) |
WO (1) | WO1987003899A1 (en) |
ZA (1) | ZA868927B (en) |
Families Citing this family (40)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8819110D0 (en) * | 1988-08-11 | 1988-09-14 | Norsk Hydro As | Antihypertensive drug & method for production |
US5336792A (en) * | 1990-03-12 | 1994-08-09 | Einar Sola | Process for enrichment of fat with regard to polyunsaturated fatty acids and phospholipids, and application of such enriched fat |
SE9303446D0 (en) * | 1993-10-20 | 1993-10-20 | Trikonex Ab | A novel urea fractionation process |
GB9404483D0 (en) * | 1994-03-08 | 1994-04-20 | Norsk Hydro As | Refining marine oil compositions |
TW425285B (en) | 1996-06-10 | 2001-03-11 | Viva America Marketing Inc | Fish oil and garlic nutritive supplement |
EP1004303B1 (en) * | 1997-06-16 | 2004-10-13 | Nippon Suisan Kaisha, Ltd. | Composition having capability of removing risk factor during exercise |
NO309795B1 (en) * | 1998-07-01 | 2001-04-02 | Norsk Hydro As | Method for stabilizing oils and their use, method for stabilizing pigments, and method for preparing for |
IT1308613B1 (en) | 1999-02-17 | 2002-01-09 | Pharmacia & Upjohn Spa | ESSENTIAL FATTY ACIDS IN THE PREVENTION OF CARDIOVASCULAR EVENTS. |
NO311041B1 (en) * | 1999-12-22 | 2001-10-01 | Norsk Hydro As | Stabilization of pigments and polyunsaturated oils and oil concentrates |
WO2001051598A1 (en) | 2000-01-11 | 2001-07-19 | Monsanto Technology Llc | Process for making an enriched mixture of polyunsaturated fatty acid esters |
AT414205B (en) | 2000-06-20 | 2006-10-15 | Vis Vitalis Lizenz & Handels | PROCESS FOR PRODUCING UNSATURATED FATTY ACID DRY CONCENTRATE |
ITMI20010129A1 (en) | 2001-01-25 | 2002-07-25 | Pharmacia & Upjohn Spa | ESSENTIAL FATTY ACIDS IN THE THERAPY OF HEART INSUFFICIENCY AND HEART FAILURE |
EP2295529B2 (en) | 2002-07-11 | 2022-05-18 | Basf As | Use of a volatile environmental pollutants-decreasing working fluid for decreasing the amount of pollutants in a fat for alimentary or cosmetic use |
SE0202188D0 (en) | 2002-07-11 | 2002-07-11 | Pronova Biocare As | A process for decreasing environmental pollutants in an oil or a fat, a volatile fat or oil environmental pollutants decreasing working fluid, a health supplement, and an animal feed product |
ITMI20032247A1 (en) * | 2003-11-19 | 2005-05-20 | Tiberio Bruzzese | INTERACTION OF POLAR DERIVATIVES OF COMPOUNDS INSATURATED WITH INORGANIC SUBSTRATES |
PL2447356T3 (en) | 2005-06-07 | 2016-10-31 | Eukaryotic microorganisms for producing lipids and antioxidants | |
ITMI20051560A1 (en) * | 2005-08-10 | 2007-02-11 | Tiberio Bruzzese | COMPOSITION OF N-3 FATTY ACIDS WITH HIGH CONCENTRATION OF EPA AND E-O DHA AND CONTAINING N-6 FATTY ACIDS |
CN101981201A (en) | 2006-08-01 | 2011-02-23 | 加拿大海洋营养食品有限公司 | Oil producing microbes and methods of modification thereof |
PE20130491A1 (en) | 2009-12-30 | 2013-05-02 | Basf Pharma Callanish Ltd | SIMULATED PROCESS OF CHROMATOGRAPHIC SEPARATION OF MOBILE BED FOR PURIFICATION OF POLYINSATURATED FATTY ACIDS |
ITMI20102297A1 (en) | 2010-12-15 | 2012-06-16 | Prime Europ Therapeuticals | PROCEDURE FOR STABILIZING FAT POLYINSATURED ACIDS BY MEANS OF METAL HYDRATES |
JP5863833B2 (en) * | 2011-03-08 | 2016-02-17 | コグニス・アイピー・マネージメント・ゲゼルシャフト・ミット・ベシュレンクテル・ハフツングCognis IP Management GmbH | Process for distillation of fatty acid esters |
GB201111589D0 (en) | 2011-07-06 | 2011-08-24 | Equateq Ltd | New modified process |
GB201111594D0 (en) | 2011-07-06 | 2011-08-24 | Equateq Ltd | New improved process |
GB201111595D0 (en) | 2011-07-06 | 2011-08-24 | Equateq Ltd | Improved process |
GB201111591D0 (en) | 2011-07-06 | 2011-08-24 | Equateq Ltd | Further new process |
GB201111601D0 (en) | 2011-07-06 | 2011-08-24 | Equateq Ltd | New process |
GB201300354D0 (en) | 2013-01-09 | 2013-02-20 | Basf Pharma Callanish Ltd | Multi-step separation process |
CN105189740B (en) | 2013-03-13 | 2019-01-15 | 帝斯曼营养品股份公司 | Engineered microorganisms |
US9428711B2 (en) | 2013-05-07 | 2016-08-30 | Groupe Novasep | Chromatographic process for the production of highly purified polyunsaturated fatty acids |
EP2883860B1 (en) | 2013-12-11 | 2016-08-24 | Novasep Process | Chromatographic method for producing polyunsaturated fatty acids |
US10975031B2 (en) | 2014-01-07 | 2021-04-13 | Novasep Process | Method for purifying aromatic amino acids |
US9163198B2 (en) * | 2014-01-17 | 2015-10-20 | Orochem Technologies, Inc. | Process for purification of EPA (eicosapentanoic acid) ethyl ester from fish oil |
WO2016028235A1 (en) * | 2014-08-18 | 2016-02-25 | Chiang Mai University | A system and method for extracting and/or concentrating vitamin e |
AR104042A1 (en) | 2015-03-26 | 2017-06-21 | Mara Renewables Corp | HIGH-DENSITY PRODUCTION OF BIOMASS AND OIL USING GLUCEROL IN GROSS |
CN107666904B (en) | 2015-03-26 | 2022-02-01 | 提贝托·布鲁泽塞 | Purified composition of polyunsaturated fatty acids, method for preparing same and use thereof |
WO2016182452A1 (en) | 2015-05-13 | 2016-11-17 | Epax Norway As | Very long chain polyunsaturated fatty acids from natural oils |
KR102676949B1 (en) | 2015-07-13 | 2024-06-19 | 마라 리뉴어블즈 코퍼레이션 | How to enhance microalgae metabolism of xylose |
US10851395B2 (en) | 2016-06-10 | 2020-12-01 | MARA Renewables Corporation | Method of making lipids with improved cold flow properties |
CN111315855B (en) | 2017-09-14 | 2023-07-25 | 发酵生物技术有限公司 | Improved method for extracting cholesterol from fish oil waste residue |
US10196586B1 (en) * | 2018-02-14 | 2019-02-05 | Golden Omega S.A. | Feed ingredient |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1176916B (en) * | 1984-10-10 | 1987-08-18 | Elvira Pistolesi | PHARMACEUTICAL OR DIETETIC COMPOSITION WITH HIGH ANTI-THROMBOTIC AND ANTI-ARTERIOSCLEROTIC ACTIVITY |
-
1985
- 1985-12-19 NO NO855147A patent/NO157302C/en not_active IP Right Cessation
-
1986
- 1986-11-21 WO PCT/NO1986/000077 patent/WO1987003899A1/en active IP Right Grant
- 1986-11-21 AU AU66211/86A patent/AU6621186A/en not_active Withdrawn
- 1986-11-21 EP EP86906964A patent/EP0255824B1/en not_active Expired - Lifetime
- 1986-11-21 IS IS3159A patent/IS1425B6/en unknown
- 1986-11-21 DE DE8686906964T patent/DE3668467D1/en not_active Expired - Lifetime
- 1986-11-21 IE IE306486A patent/IE59171B1/en not_active IP Right Cessation
- 1986-11-25 ZA ZA868927A patent/ZA868927B/en unknown
- 1986-11-27 CA CA000523914A patent/CA1303416C/en not_active Expired - Lifetime
- 1986-12-03 NZ NZ218500A patent/NZ218500A/en unknown
- 1986-12-08 MX MX004578A patent/MX168698B/en unknown
- 1986-12-17 DD DD86297792A patent/DD261805A1/en not_active IP Right Cessation
- 1986-12-19 AR AR86306258A patent/AR242111A1/en active
- 1986-12-19 PT PT83991A patent/PT83991B/en not_active IP Right Cessation
- 1986-12-19 MA MA21072A patent/MA20840A1/en unknown
Also Published As
Publication number | Publication date |
---|---|
IE59171B1 (en) | 1994-01-12 |
DD261805A1 (en) | 1988-11-09 |
CA1303416C (en) | 1992-06-16 |
DE3668467D1 (en) | 1990-03-01 |
PT83991A (en) | 1987-01-01 |
AU6621186A (en) | 1987-07-15 |
EP0255824A1 (en) | 1988-02-17 |
PT83991B (en) | 1989-01-17 |
ZA868927B (en) | 1987-08-26 |
IS3159A7 (en) | 1987-06-20 |
IS1425B6 (en) | 1990-03-28 |
NO157302C (en) | 1988-02-24 |
AR242111A1 (en) | 1993-03-31 |
MA20840A1 (en) | 1987-07-01 |
EP0255824B1 (en) | 1990-01-24 |
NO855147L (en) | 1987-06-22 |
NZ218500A (en) | 1989-03-29 |
NO157302B (en) | 1987-11-16 |
IE863064L (en) | 1987-06-19 |
WO1987003899A1 (en) | 1987-07-02 |
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