ATE229T1 - PROCESS FOR RECOVERING AND/OR REFINING ANIMAL FAT. - Google Patents
PROCESS FOR RECOVERING AND/OR REFINING ANIMAL FAT.Info
- Publication number
- ATE229T1 ATE229T1 AT80810035T AT80810035T ATE229T1 AT E229 T1 ATE229 T1 AT E229T1 AT 80810035 T AT80810035 T AT 80810035T AT 80810035 T AT80810035 T AT 80810035T AT E229 T1 ATE229 T1 AT E229T1
- Authority
- AT
- Austria
- Prior art keywords
- extraction
- gas
- fats
- starting material
- recovering
- Prior art date
Links
- 235000019737 Animal fat Nutrition 0.000 title 1
- 238000000034 method Methods 0.000 title 1
- 238000007670 refining Methods 0.000 title 1
- 238000000605 extraction Methods 0.000 abstract 4
- 239000003925 fat Substances 0.000 abstract 3
- 239000007858 starting material Substances 0.000 abstract 2
- 238000007385 chemical modification Methods 0.000 abstract 1
- 210000001596 intra-abdominal fat Anatomy 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 235000013372 meat Nutrition 0.000 abstract 1
- 239000002904 solvent Substances 0.000 abstract 1
- 230000003068 static effect Effects 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
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
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
- C11B1/104—Production of fats or fatty oils from raw materials by extracting using super critical gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
- B01D11/0203—Solvent extraction of solids with a supercritical fluid
-
- 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
- C11B3/006—Refining fats or fatty oils by extraction
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Microbiology (AREA)
- Fats And Perfumes (AREA)
- Extraction Or Liquid Replacement (AREA)
- Seasonings (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
- Meat, Egg Or Seafood Products (AREA)
Abstract
Fatty animal starting material is subjected to extraction using a gas at supercritical conditions. The extraction operation takes place in a static column without circulation. The gas used as a solvent in the extraction operation may be subsequently regenerated and re-used. Any innocuous gas may be used provided its critical constants fall within the pressure and temperature ranges dictated by the extraction material. The fats are completely extracted without chemical modification of either the extract or the residue, both of which retain their natural composition. The water content of the extracted fats is less than 0.2% by weight. Scrap fat from meat and offal, such as visceral fat, may be used as starting material.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH100079 | 1979-02-01 | ||
| EP80810035A EP0014685B1 (en) | 1979-02-01 | 1980-01-31 | Process for the extraction and/or refining of animal fats |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ATE229T1 true ATE229T1 (en) | 1981-10-15 |
Family
ID=4200110
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT80810035T ATE229T1 (en) | 1979-02-01 | 1980-01-31 | PROCESS FOR RECOVERING AND/OR REFINING ANIMAL FAT. |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US4280961A (en) |
| EP (1) | EP0014685B1 (en) |
| AT (1) | ATE229T1 (en) |
| DE (1) | DE3060020D1 (en) |
| DK (1) | DK153409C (en) |
| ES (1) | ES8102183A1 (en) |
| ZA (1) | ZA80582B (en) |
Families Citing this family (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ATE12249T1 (en) * | 1980-11-06 | 1985-04-15 | Ernst Haussener | PROCESS FOR DEFATTING A CONSISTENT MASS CONTAINING FINE MEAT AND WATER. |
| US4504503A (en) * | 1981-09-09 | 1985-03-12 | Lever Brothers Company | Fractionation of butterfat using a liquefied gas or a gas in the supercritical state |
| JPS58141762A (en) * | 1982-02-18 | 1983-08-23 | Nichirei:Kk | Processing method to suppress fat oxidation in highly harvested red fish |
| DE3207914A1 (en) * | 1982-03-04 | 1983-09-15 | Skw Trostberg Ag, 8223 Trostberg | METHOD FOR EXTRACTIVELY OBTAINING HIGH QUALITY NATURAL WAXES |
| US4466923A (en) * | 1982-04-01 | 1984-08-21 | The United States Of America As Represented By The Secretary Of Agriculture | Supercritical CO2 extraction of lipids from lipid-containing materials |
| US4568495A (en) * | 1983-05-16 | 1986-02-04 | Union Camp Corporation | Fractionation of polymerized fatty acids |
| JPS6055096A (en) * | 1983-09-06 | 1985-03-29 | 岩谷産業株式会社 | Manufacture of neutral lipid from fishes and shells |
| US4584140A (en) * | 1984-12-17 | 1986-04-22 | National Distillers And Chemical Corporation | Process for separating fatty materials from supported nickel catalysts |
| JPS6259697A (en) * | 1985-09-10 | 1987-03-16 | 昭和炭酸株式会社 | Method of extracting, purifying and separating oily components from plant seed |
| US4749522A (en) * | 1985-10-31 | 1988-06-07 | Angio-Medical Corporation | Supercritical fluid extraction of animal derived materials |
| CA1327907C (en) * | 1987-08-19 | 1994-03-22 | Owen John Catchpole | Removal of sterols and/or lipid components from foodstuffs |
| US5092964A (en) * | 1989-02-03 | 1992-03-03 | Campbell Soup Company | Production of low cholesterol butter oil by vapor sparging |
| US4997668A (en) * | 1989-05-02 | 1991-03-05 | Campbell Soup Company | Production of low-cholesterol milk fat by solvent extraction |
| WO1991001367A1 (en) * | 1989-07-20 | 1991-02-07 | Bioeng, Inc. | Supercritical fluid disruption of and extraction from microbial cells |
| DE4002161A1 (en) * | 1990-01-25 | 1991-08-01 | Walter Rau Neusser Oel Und Fet | Extracting oils and fats - from exhausted adsorbent with supercritical carbon di:oxide |
| WO1992003064A1 (en) * | 1990-08-23 | 1992-03-05 | Liquid Carbonic Corporation | Method of making reduced oil content fried chip products and product thereof |
| US5356847A (en) * | 1992-11-10 | 1994-10-18 | Engelhard Corporation | Nickel catalyst |
| US7815741B2 (en) | 2006-11-03 | 2010-10-19 | Olson David A | Reactor pump for catalyzed hydrolytic splitting of cellulose |
| US7815876B2 (en) | 2006-11-03 | 2010-10-19 | Olson David A | Reactor pump for catalyzed hydrolytic splitting of cellulose |
| EP2499093B1 (en) * | 2009-11-11 | 2017-05-31 | Dynasep Inc. | Energy efficient acetone drying method |
| CN114085709B (en) * | 2021-12-29 | 2023-09-22 | 东北农业大学 | Animal fat classification device and method |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2118454A (en) * | 1935-03-30 | 1938-05-24 | Shell Dev | Process for separating high molecular mixtures of the ester type |
| US2166160A (en) * | 1935-04-10 | 1939-07-18 | Atlantic Refining Co | Treatment of hydrocarbon oils |
| GB1058076A (en) * | 1964-06-29 | 1967-02-08 | Corn Products Co | Process for extraction of oil from oil-bearing vegetable material |
| DE2127596A1 (en) | 1971-06-03 | 1972-12-21 | Hag Ag, 2800 Bremen | Process for the production of vegetable fats and oils. |
| DE2255667C3 (en) * | 1972-11-14 | 1982-05-06 | Studiengesellschaft Kohle mbH, 4330 Mülheim | Process for producing a fat-free, storage-stable starch |
| AT331374B (en) * | 1972-12-22 | 1976-08-25 | Studiengesellschaft Kohle Mbh | PROCESS FOR THE PRODUCTION OF FATS AND OILS FROM VEGETABLE AND ANIMAL PRODUCTS |
| US3923847A (en) * | 1973-05-23 | 1975-12-02 | Studiengesellschaft Kohle Mbh | Methods of producing cocoa butter |
-
1980
- 1980-01-31 DE DE8080810035T patent/DE3060020D1/en not_active Expired
- 1980-01-31 US US06/117,227 patent/US4280961A/en not_active Expired - Lifetime
- 1980-01-31 DK DK042780A patent/DK153409C/en not_active IP Right Cessation
- 1980-01-31 ZA ZA00800582A patent/ZA80582B/en unknown
- 1980-01-31 EP EP80810035A patent/EP0014685B1/en not_active Expired
- 1980-01-31 ES ES488155A patent/ES8102183A1/en not_active Expired
- 1980-01-31 AT AT80810035T patent/ATE229T1/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| ES488155A0 (en) | 1980-12-16 |
| DE3060020D1 (en) | 1981-12-03 |
| DK42780A (en) | 1980-08-02 |
| ES8102183A1 (en) | 1980-12-16 |
| DK153409C (en) | 1988-12-12 |
| EP0014685B1 (en) | 1981-09-16 |
| DK153409B (en) | 1988-07-11 |
| US4280961A (en) | 1981-07-28 |
| ZA80582B (en) | 1981-01-28 |
| EP0014685A1 (en) | 1980-08-20 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| REN | Ceased due to non-payment of the annual fee |