CN1243866A - Process for extracting oyster oil - Google Patents
Process for extracting oyster oil Download PDFInfo
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- CN1243866A CN1243866A CN 99117019 CN99117019A CN1243866A CN 1243866 A CN1243866 A CN 1243866A CN 99117019 CN99117019 CN 99117019 CN 99117019 A CN99117019 A CN 99117019A CN 1243866 A CN1243866 A CN 1243866A
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- extraction
- oyster
- extracting
- oil
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- Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
- Meat, Egg Or Seafood Products (AREA)
- Fats And Perfumes (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
Abstract
A process for extracting oyster oil includes such steps as removing shell of fresh oyster, mincing, freeze-drying in vacuum, pulverizing, and supercritical fluid extracting with CO2 extractant added with alcohol as modified in a certain temp, pressure and flow speed conditions. Its advantages are simple process, easy operation, high extracting speed and output, cyclic use of extractant and low energy consumption. The extracted oyster oil is excellent raw material for extracting EPA and DHA. The dregs after extraction can be used to extract active protein, taurine and compound saccharide.
Description
The present invention is a kind of method of extracting oyster oil, belongs to halobiontic deep process technology, particularly the processing technology of oyster.
Lipid content in the Oyster is about 11.5 grams/100 gram dry powder, wherein contain abundant omega-3 unsaturated fatty acid, the DHA (docosahexaenoic acid) docosahexenoic acid (DHA) and the timnodonic acid (EPA) that particularly it has often been said account for 1/4th of fatty acid content, but also contain many saturated fatty acids, account for 1/3rd.Therefore, the oyster oil that extracts also needs reprocessing, and the content that reduces its saturated fatty acid just can meet the high request of modern grease healthcare products.Except that containing abundant omega-3 unsaturated fatty acid; also contain many chemical ingredientss in the Oyster with medical treatment and health nutrient value; as protein, taurine, compounding sugar and multivitamin etc., in the process of extracting oyster oil, should not destroy these chemical ingredientss.The available technology adopting pure carbon dioxide extracts (referring to the clear 61-78899 of Japanese Patent: カ キ meat オ イ Le manufacture method, the i.e. manufacture method of Oyster oil) as extraction agent, but extraction rate slow (about 11 hours), extraction yield low (being about 47%).
Purpose of the present invention is exactly in order to overcome the existing shortcoming that oyster oil technology extraction rate is slow, extraction yield is low of extracting, a kind of other chemical ingredients that has medical treatment and health nutrient to be worth that can extract at a lower temperature, not destroy in the Oyster of research invention, extraction rate is fast, the method for the extraction oyster oil that extraction yield is high.
The present invention realizes by following technical proposals: mashed with the meat mincer fresh oyster hinge of will shelling, vacuum lyophilization 9～12 hours, with meat mincer it is ground into dry powder again, the oyster dry powder that crushes is extracted with supercritical fluid extraction, extraction agent is the carbonic acid gas that has added the properties-correcting agent dehydrated alcohol, the weight percent content of properties-correcting agent ethanol in carbonic acid gas is 2～8%, the addition of properties-correcting agent is controlled by the properties-correcting agent compression pump, extraction temperature is 35～50 ℃, and extracting pressure is 250～400bar; When pressure rises to predetermined pressure 250～400bar, first static extracting 8～12 minutes, promptly the constant voltage static extracting is 8～12 minutes, and extraction agent was with the flow velocity dynamic extraction of 1～2ml/ (gram oyster dry powder minute) 30～120 minutes then; The preferred temperature of extraction should be 40～50 ℃, and the preferable pressure of extraction should be 300～400bar, and extraction products therefrom oyster oil sprays in the collector through the decompression throttling valve; Extract oyster oil Oyster slag afterwards and also can further process extraction as other active substances such as active protein, taurine and compounding sugars.
The present invention compared with prior art has following advantage and beneficial effect: (1) technical process of the present invention and operating process are simple, easy to operate, and rate of extraction is fast, the extraction yield height.Carbonic acid gas can be recycled, and energy consumption is low, and is pollution-free; (2) oyster oil that extracts is to extract EPA and DHA good raw material.Meat slag after the extraction can also be reprocessed extraction active protein, taurine and compounding sugar etc. wherein; (3) the present invention is suitable for the leading portion engineering of oyster comprehensive utilization deep processing.
Embodiments of the present invention can be operated by the described method and technology scheme of top specification sheets, just can implement the present invention preferably.The contriver has a lot of successful embodiment through research and the arduous test of long period, only tabulates in shown in the table 1 for 4 embodiment below.Present method technological process is simple as seen from Table 1, and is easy to operate, and rate of extraction is fast, only is about 40 minutes under preferable condition, and extraction yield is up to about 90%.Table 1
Claims (3)
1, a kind of method that comprises the extraction oyster oil of pre-treatment and extraction process, it is characterized in that: mashed with the meat mincer fresh oyster hinge of will shelling, vacuum lyophilization 9～12 hours, with meat mincer it is ground into dry powder again, the oyster dry powder that crushes is extracted with supercritical fluid extraction, extraction agent is the carbonic acid gas that has added the properties-correcting agent dehydrated alcohol, the weight percent content of properties-correcting agent ethanol in carbonic acid gas is 2～8%, the addition of properties-correcting agent is controlled by the properties-correcting agent compression pump, extraction temperature is 35～50 ℃, and extracting pressure is 250～400bar; When pressure rises to predetermined pressure 250～400bar, elder generation's static extracting 8～12 minutes, be constant voltage static extracting 8～12 minutes, extraction agent was with the flow velocity dynamic extraction of 1～2ml/ (gram oyster dry powder minute) 30～120 minutes then, and extraction products therefrom oyster oil sprays in the collector through the decompression throttling valve.
2,, it is characterized in that described extraction temperature is preferable to should be 40～50 ℃, the preferable 300～400bar that should be of extracting pressure by the described a kind of method that comprises the extraction oyster oil of pre-treatment and extraction process of claim 1.
3, by the described a kind of method that comprises the extraction oyster oil of pre-treatment and extraction process of claim 1, its feature also is to extract oyster oil Oyster slag afterwards also can further process extraction as other active substances such as active protein, taurine and compounding sugars.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99117019A CN1073621C (en) | 1999-08-03 | 1999-08-03 | Process for extracting oyster oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99117019A CN1073621C (en) | 1999-08-03 | 1999-08-03 | Process for extracting oyster oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1243866A true CN1243866A (en) | 2000-02-09 |
| CN1073621C CN1073621C (en) | 2001-10-24 |
Family
ID=5279668
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN99117019A Expired - Fee Related CN1073621C (en) | 1999-08-03 | 1999-08-03 | Process for extracting oyster oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1073621C (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100371347C (en) * | 2003-09-22 | 2008-02-27 | 于荣敏 | Active material of polypeptide proteins in bloody clam, preparation method and usage |
| US7530244B2 (en) | 2004-09-13 | 2009-05-12 | Matsushita Electric Industrial Co., Ltd. | Drum type washing machine |
| CN101530127B (en) * | 2009-04-10 | 2011-12-07 | 大连海晏堂生物有限公司 | Sea cucumber oil product and method for preparing same |
| CN103099248A (en) * | 2011-11-10 | 2013-05-15 | 深圳海王药业有限公司 | Method for preparing oyster active component |
| CN103125989A (en) * | 2012-03-31 | 2013-06-05 | 大连工业大学 | Method of extracting fish cerebrol and fish brain peptide |
| CN104673483A (en) * | 2015-01-26 | 2015-06-03 | 北海富安源生物科技有限公司 | Method for extracting polyunsaturated fatty acid from shellfish |
| CN113200889A (en) * | 2020-12-18 | 2021-08-03 | 浙江经贸职业技术学院 | Method for preparing taurine from mussels |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6178899A (en) * | 1984-09-25 | 1986-04-22 | 岩谷産業株式会社 | Manufacture of oyster meat oil |
| JPH0538271A (en) * | 1991-08-08 | 1993-02-19 | T Hasegawa Co Ltd | Smoked fish and shellfish flavor |
-
1999
- 1999-08-03 CN CN99117019A patent/CN1073621C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100371347C (en) * | 2003-09-22 | 2008-02-27 | 于荣敏 | Active material of polypeptide proteins in bloody clam, preparation method and usage |
| US7530244B2 (en) | 2004-09-13 | 2009-05-12 | Matsushita Electric Industrial Co., Ltd. | Drum type washing machine |
| CN101530127B (en) * | 2009-04-10 | 2011-12-07 | 大连海晏堂生物有限公司 | Sea cucumber oil product and method for preparing same |
| CN103099248A (en) * | 2011-11-10 | 2013-05-15 | 深圳海王药业有限公司 | Method for preparing oyster active component |
| CN103125989A (en) * | 2012-03-31 | 2013-06-05 | 大连工业大学 | Method of extracting fish cerebrol and fish brain peptide |
| CN103125989B (en) * | 2012-03-31 | 2014-08-06 | 大连工业大学 | Method of extracting fish cerebrol and fish brain peptide |
| CN104673483A (en) * | 2015-01-26 | 2015-06-03 | 北海富安源生物科技有限公司 | Method for extracting polyunsaturated fatty acid from shellfish |
| CN113200889A (en) * | 2020-12-18 | 2021-08-03 | 浙江经贸职业技术学院 | Method for preparing taurine from mussels |
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| Publication number | Publication date |
|---|---|
| CN1073621C (en) | 2001-10-24 |
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