CN101933540A - Edible wild fungus oil - Google Patents
Edible wild fungus oil Download PDFInfo
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- CN101933540A CN101933540A CN 201010284780 CN201010284780A CN101933540A CN 101933540 A CN101933540 A CN 101933540A CN 201010284780 CN201010284780 CN 201010284780 CN 201010284780 A CN201010284780 A CN 201010284780A CN 101933540 A CN101933540 A CN 101933540A
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Abstract
The invention relates to edible wild fungus oil. In the invention, supercritical carbon dioxide is used for extracting wild fungus essential oil, and then the wild fungus essential oil is mixed with sunflower seed oil to prepare the wild fungus oil; the extraction by the supercritical carbon dioxide can reserve unique fat soluble ingredients, vitamins, trace elements and active substances in the wild funguses, and the extraction process is carried out below 50 DEG C so as to effectively reduce the oxidation of conjugated unsaturated fatty acid oil; under high pressure, the carbon dioxide can permeate into the interior of wild fungus cells, thus the separation rate of effective ingredients is high; in the whole extraction process, entrainers are not used, so that the quality of the wild fungus essential oil is purer; through mix with the sunflower seed oil, the taste of the wild fungus oil is strong and mellow; and the wild fungus oil maintains the unique nutrient ingredients of the wild funguses and is convenient to transport and store.
Description
Technical field
The present invention relates to food, especially edible oil.
Background technology
The nutritive value of wild bacterium is very high, be rich in crude protein, crude fat, crude fibre and vitamin B1, B2, vitamin C, elements such as nicotinic acid, not only delicious flavour is good to eat, also has medical value, can keep fit, the benefit stomach, pain relieving, regulating qi-flowing for eliminating phlegm, unique effects such as expelling parasite and treatment diabetes, but the place of production scope of wild bacterium is smaller, moisture is big, plucking the back is difficult for preserving, thereby carry out drying usually in the place of origin, freezing, modes such as oil immersion are processed the back and are being sold to the other places, but existing processing mode has not only destroyed the flavour of wild bacterium, the also forfeiture in a large number in process of its nutritional labeling is so need the processing method of a kind of wild bacterium newly of research.
Summary of the invention
The object of the present invention is to provide a kind of edible wild bacterium bacterium oil,, flavour of wild bacterium and nutritional labeling are not suffered a loss, be convenient to storage and transport by supercritical carbon dioxide extracting.
Edible wild bacterium bacterium oil of the present invention, its feature is mixed and made into wild bacterium edible oil with sunflower oil then using the overcritical titanium dioxide pool to extract wild bacterium essential oil, and concrete processing step is as follows:
Step 1, selected wild bacterium is carried out drying, pulverize and be 70-80 order bacterium powder;
Step 2, the bacterium powder is put into extraction kettle, pressure 35-40Mpa, temperature 40-50 ℃, 40-90 minute extraction time, supercritical carbon dioxide under high pressure enters extraction kettle, infiltrates wild bacterial cell, and grease and liposoluble constituent in the wild bacterium dissolve in supercritical carbon dioxide;
Step 3, the supercritical carbon dioxide that has dissolved in wild bacterium grease and liposoluble constituent enter No. 1 separating still and separate, temperature 35-40 ℃, pressure 5 Mpa are wild bacterium essential oil and carbon dioxide separation in lower temperature and pressure, still have the wild bacterium bacterium of part oil to be dissolved in the carbon dioxide, thereby need carry out the second time and separate;
The carbon dioxide that still is dissolved with the wild bacterium essential oil of part after step 4, the first step are separated enters No. 2 separating stills and carries out the separation second time;
Step 5, collect No. 1 and No. 2 separating stills in wild bacterium essential oil, wild bacterium essential oil and sunflower oil according to weight ratio 0.3-3:100 mixing, are obtained wild bacterium bacterium oil.
Described wild bacterium is preferably matsutake.
Described wild bacterium can also be one or more in bolete, ferfas or the glossy ganoderma;
Do not use any entrainer in the extraction process of described wild bacterium essential oil.
Supercritical carbon dioxide extracting can keep liposoluble constituent, vitamin, trace element and active material unique in the wild bacterium, extraction process is carrying out below 50 ℃, effectively reduce the oxidation of conjugated polyunsaturated fatty acid lipid, under high pressure, carbon dioxide can infiltrate wild bacterial cell inside, active ingredient eduction rate height, in whole extraction process, do not use entrainer, make that the quality of wild bacterium essential oil is purer, by mixing with sunflower oil, mouthfeel is strong aromatic, and unique nutritional labeling of wild bacterium is kept, and also is convenient to transportation and preservation.
The specific embodiment
Embodiment 1: selected dried matsutake 100kg, pulverizing is 70 purpose bacterium powder, the bacterium powder is put into the extraction kettle extraction, to the extraction kettle pressurization of heating, temperature is controlled at 40-45 ℃, pressure 35 Mpa, after treating pressure stability, feed supercritical carbon dioxide, supercritical carbon dioxide infiltrates wild bacterial cell, intracellular grease and liposoluble constituent ooze out, and dissolve in supercritical carbon dioxide, enter into No. 1 lower separating still of temperature and pressure and carry out first separation, temperature is controlled at 35-40 ℃, pressure 5 Mpa, the grease and the liposoluble constituent that dissolve in supercritical carbon dioxide are separated, and the supercritical carbon dioxide that still has a part of grease and liposoluble constituent enters No. two lower separating stills of temperature, remaining grease and liposoluble constituent are separated, carbon dioxide then comes back to supercriticality in high-pressure pump, recycle, and extracts time 40-90 minute.
The matsutake essential oil 1.5kg that separates and sunflower seeds 100kg mix and obtain the matsutake edible oil, and smell is aromatic, and mouthfeel is mellow, can be with giving me a little soup, botargo, and unique flavor, nutritious.
Embodiment 2, selected dried bolete 100kg, pulverizing is 75 purpose bacterium powder, the bacterium powder is put into extraction kettle, give the pressurization of heating in the extraction kettle, temperature is controlled at 40-45 ℃, pressure 35 Mpa, after treating pressure stability, feed supercritical carbon dioxide, supercritical carbon dioxide infiltrates wild bacterial cell, intracellular grease and liposoluble constituent ooze out, dissolve in supercritical carbon dioxide, enter into No. 1 lower separating still of temperature and pressure and carry out first separation, temperature is controlled at 35-40 ℃, pressure 5 Mpa, the grease and the liposoluble constituent that dissolve in supercritical carbon dioxide are separated, and the supercritical carbon dioxide that still has a part of grease and liposoluble constituent enters No. two lower separating stills of temperature, and remaining grease and liposoluble constituent are separated, carbon dioxide then comes back to supercriticality in high-pressure pump, recycle.
The Porcini essential oil 3kg that separates and sunflower seeds 100kg mix and obtain the bolete edible oil, and smell is aromatic, and mouthfeel is mellow, can be with giving me a little soup, botargo, and unique flavor, nutritious.
Embodiment 3, selected dried glossy ganoderma 100kg, pulverizing is 80 purpose bacterium powder, the bacterium powder is put into extraction kettle, give the pressurization of heating in the extraction kettle, temperature is controlled at 40-45 ℃, pressure 35 Mpa, after treating pressure stability, feed supercritical carbon dioxide, supercritical carbon dioxide infiltrates wild bacterial cell, intracellular grease and liposoluble constituent ooze out, dissolve in supercritical carbon dioxide, enter into No. 1 lower separating still of temperature and pressure and carry out first separation, temperature is controlled at 35-40 ℃, pressure 5 Mpa, the grease and the liposoluble constituent that dissolve in supercritical carbon dioxide are separated, and the supercritical carbon dioxide that still has a part of grease and liposoluble constituent enters No. two lower separating stills of temperature, and remaining grease and liposoluble constituent are separated, carbon dioxide then comes back to supercriticality in high-pressure pump, recycle.
The glossy ganoderma essential oil 1kg that separates and sunflower seeds 100kg mix and obtain the glossy ganoderma edible oil, can be with giving me a little soup, botargo, and unique flavor, nutritious.
Claims (4)
1. one kind eats wild bacterium bacterium oil, and its feature is mixed and made into wild bacterium edible oil with sunflower oil then using the overcritical titanium dioxide pool to extract wild bacterium essential oil, and concrete processing step is as follows:
Step 1, selected wild bacterium is carried out drying, pulverize and be 70-80 order bacterium powder;
Step 2, the bacterium powder is put into extraction kettle, pressure 35-40Mpa, temperature 40-50 ℃, 40-90 minute extraction time, supercritical carbon dioxide under high pressure enters extraction kettle, infiltrates wild bacterial cell, and grease and liposoluble constituent in the wild bacterium dissolve in supercritical carbon dioxide;
Step 3, the supercritical carbon dioxide that has dissolved in wild bacterium grease and liposoluble constituent enter No. 1 separating still and separate, temperature 35-40 ℃, pressure 5 Mpa are wild bacterium essential oil and carbon dioxide separation in lower temperature and pressure, still have the wild bacterium bacterium of part oil to be dissolved in the carbon dioxide, thereby need carry out the second time and separate;
The carbon dioxide that still is dissolved with the wild bacterium essential oil of part after step 4, the first step are separated enters No. 2 separating stills and carries out the separation second time;
Step 5, collect No. 1 and No. 2 separating stills in wild bacterium essential oil, wild bacterium essential oil and sunflower oil according to weight ratio 0.3-3:100 mixing, are obtained wild bacterium bacterium oil.
2. edible wild bacterium bacterium oil as claimed in claim is characterized in that said wild bacterium is preferably matsutake.
3. edible wild bacterium bacterium oil as claimed in claim is characterized in that said wild bacterium can also be one or more in bolete, ferfas or the glossy ganoderma.
4. edible wild bacterium bacterium oil as claimed in claim is characterized in that not using any entrainer in the extraction process of said wild bacterium essential oil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010284780 CN101933540A (en) | 2010-09-17 | 2010-09-17 | Edible wild fungus oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010284780 CN101933540A (en) | 2010-09-17 | 2010-09-17 | Edible wild fungus oil |
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| CN101933540A true CN101933540A (en) | 2011-01-05 |
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| CN 201010284780 Pending CN101933540A (en) | 2010-09-17 | 2010-09-17 | Edible wild fungus oil |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102224853A (en) * | 2011-06-08 | 2011-10-26 | 郭景龙 | Edible oil with raw material containing truffle oil |
| CN102640809A (en) * | 2012-05-18 | 2012-08-22 | 山东三星玉米产业科技有限公司 | Edible blend oil with health care function |
| CN103461543A (en) * | 2013-10-06 | 2013-12-25 | 吉林农业大学 | Edible mushroom flavor seasoning oil and production method thereof |
| CN106306118A (en) * | 2015-06-15 | 2017-01-11 | 财团法人食品工业发展研究所 | Preparation method of blend oil containing fat-soluble functional component |
| CN107216948A (en) * | 2017-07-25 | 2017-09-29 | 云南农业大学 | A kind of extracting method of Albatrellus dispansus (Lloyd) Canf. ＆ Gilb essential oil and its application |
| CN107384592A (en) * | 2017-07-24 | 2017-11-24 | 易门县康源菌业有限公司 | A kind of extraction process of wild mushroom composite essential oil |
| CN111423933A (en) * | 2020-03-16 | 2020-07-17 | 西南林业大学 | Supercritical extraction method of truffle oil |
Citations (4)
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| CN1445346A (en) * | 2002-12-09 | 2003-10-01 | 陈宝义 | Method for preparing oil of ganoderma lucidum spores by supercritical Co2 extraction |
| CN101077989A (en) * | 2007-06-19 | 2007-11-28 | 西北农林科技大学 | Supercritical extraction method of tuber indicum oil |
| CN101269095A (en) * | 2008-04-17 | 2008-09-24 | 吴晓闻 | Supercritical combined processing method of ganoderma lucidum and ganoderma lucidum spore |
| CN101664422A (en) * | 2009-09-18 | 2010-03-10 | 长沙湘蕈生物科技有限公司 | Supercritical fluid extract technology of ganoderma volatile oil, ganodenic acid and ganoderma polysaccharide |
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2010
- 2010-09-17 CN CN 201010284780 patent/CN101933540A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN1445346A (en) * | 2002-12-09 | 2003-10-01 | 陈宝义 | Method for preparing oil of ganoderma lucidum spores by supercritical Co2 extraction |
| CN101077989A (en) * | 2007-06-19 | 2007-11-28 | 西北农林科技大学 | Supercritical extraction method of tuber indicum oil |
| CN101269095A (en) * | 2008-04-17 | 2008-09-24 | 吴晓闻 | Supercritical combined processing method of ganoderma lucidum and ganoderma lucidum spore |
| CN101664422A (en) * | 2009-09-18 | 2010-03-10 | 长沙湘蕈生物科技有限公司 | Supercritical fluid extract technology of ganoderma volatile oil, ganodenic acid and ganoderma polysaccharide |
Non-Patent Citations (3)
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| 《广州食品工业科技》 20001231 莫文敏等 超临界流体萃取技术在提取功能性油脂中的应用 第16卷, 第4期 2 * |
| 《食品科技》 19970331 彭洪光等 食用菌风味油的加工 , 第6期 2 * |
| 《食用菌深加工新技术》 19920430 刘培田 食用菌菌油加工 , 1 * |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102224853A (en) * | 2011-06-08 | 2011-10-26 | 郭景龙 | Edible oil with raw material containing truffle oil |
| CN102640809A (en) * | 2012-05-18 | 2012-08-22 | 山东三星玉米产业科技有限公司 | Edible blend oil with health care function |
| CN103461543A (en) * | 2013-10-06 | 2013-12-25 | 吉林农业大学 | Edible mushroom flavor seasoning oil and production method thereof |
| CN103461543B (en) * | 2013-10-06 | 2014-12-10 | 吉林农业大学 | Edible mushroom flavor seasoning oil and production method thereof |
| CN106306118A (en) * | 2015-06-15 | 2017-01-11 | 财团法人食品工业发展研究所 | Preparation method of blend oil containing fat-soluble functional component |
| CN107384592A (en) * | 2017-07-24 | 2017-11-24 | 易门县康源菌业有限公司 | A kind of extraction process of wild mushroom composite essential oil |
| CN107216948A (en) * | 2017-07-25 | 2017-09-29 | 云南农业大学 | A kind of extracting method of Albatrellus dispansus (Lloyd) Canf. ＆ Gilb essential oil and its application |
| CN111423933A (en) * | 2020-03-16 | 2020-07-17 | 西南林业大学 | Supercritical extraction method of truffle oil |
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Application publication date: 20110105 |