WO2004099427A1 - Method of extracting crude beta glucan from phellinus linteus - Google Patents

Method of extracting crude beta glucan from phellinus linteus Download PDF

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Publication number
WO2004099427A1
WO2004099427A1 PCT/KR2003/001723 KR0301723W WO2004099427A1 WO 2004099427 A1 WO2004099427 A1 WO 2004099427A1 KR 0301723 W KR0301723 W KR 0301723W WO 2004099427 A1 WO2004099427 A1 WO 2004099427A1
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Prior art keywords
phellinus linteus
beta glucan
crude beta
phellinus
linteus
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PCT/KR2003/001723
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French (fr)
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Kwan Ho Kim
Il Keun Roh
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Kwan Ho Kim
Il Keun Roh
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Priority to AU2003256111A priority Critical patent/AU2003256111A1/en
Publication of WO2004099427A1 publication Critical patent/WO2004099427A1/en

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    • EFIXED CONSTRUCTIONS
    • E06DOORS, WINDOWS, SHUTTERS, OR ROLLER BLINDS IN GENERAL; LADDERS
    • E06BFIXED OR MOVABLE CLOSURES FOR OPENINGS IN BUILDINGS, VEHICLES, FENCES OR LIKE ENCLOSURES IN GENERAL, e.g. DOORS, WINDOWS, BLINDS, GATES
    • E06B9/00Screening or protective devices for wall or similar openings, with or without operating or securing mechanisms; Closures of similar construction
    • E06B9/24Screens or other constructions affording protection against light, especially against sunshine; Similar screens for privacy or appearance; Slat blinds
    • E06B9/26Lamellar or like blinds, e.g. venetian blinds
    • E06B9/36Lamellar or like blinds, e.g. venetian blinds with vertical lamellae ; Supporting rails therefor
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/04Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B37/00Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
    • C08B37/0006Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
    • C08B37/0024Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid beta-D-Glucans; (beta-1,3)-D-Glucans, e.g. paramylon, coriolan, sclerotan, pachyman, callose, scleroglucan, schizophyllan, laminaran, lentinan or curdlan; (beta-1,6)-D-Glucans, e.g. pustulan; (beta-1,4)-D-Glucans; (beta-1,3)(beta-1,4)-D-Glucans, e.g. lichenan; Derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P1/00Preparation of compounds or compositions, not provided for in groups C12P3/00 - C12P39/00, by using microorganisms or enzymes
    • C12P1/02Preparation of compounds or compositions, not provided for in groups C12P3/00 - C12P39/00, by using microorganisms or enzymes by using fungi
    • EFIXED CONSTRUCTIONS
    • E06DOORS, WINDOWS, SHUTTERS, OR ROLLER BLINDS IN GENERAL; LADDERS
    • E06BFIXED OR MOVABLE CLOSURES FOR OPENINGS IN BUILDINGS, VEHICLES, FENCES OR LIKE ENCLOSURES IN GENERAL, e.g. DOORS, WINDOWS, BLINDS, GATES
    • E06B9/00Screening or protective devices for wall or similar openings, with or without operating or securing mechanisms; Closures of similar construction
    • E06B9/24Screens or other constructions affording protection against light, especially against sunshine; Similar screens for privacy or appearance; Slat blinds
    • E06B9/26Lamellar or like blinds, e.g. venetian blinds
    • E06B9/38Other details
    • E06B9/386Details of lamellae

Definitions

  • Phellinus Linteus with high yield rate Phellinus Linteus with high yield rate, and crude beta glucan extracted by the method.
  • Phellinus Linteus is a kind of perennial mushroom growing on mulberry trees and broad- leaved trees in an alpine region, which is classified to scores of species.
  • Phellinus Linteus The typical species of the mushroom Phellinus are Phellinus Linteus and Phellinus Baumi, which grow on the stalks of the mulberry trees and the broad-leaved trees.
  • Phellinus Linteus has been generally used as a medical material, but is also used as a food material recently.
  • Phellinus Linteus contains beautiful nutrition beneficial to a human body such as potassium, calcium, magnesium, vitamin B2, B3 and C, fibroid material, amino acids, etc., and also contains beta glucan that is a kind of polysaccharide.
  • beta glucan is especially beneficial to a human body in a medical point of view, and the immunity enhancement and cancer resistance effects of the beta glucan have been mentioned on a variety of classical medical books in the Orient.
  • Phellinus Linteus has the immunity improvement effect by suppressing virus, bacteria, mildew, and vermin, cancer resistance effect resisting the cancer with the level of 96.7%, and anti-oxidation effect influencing on noxious oxygen and radical.
  • Beta glucan in Phellinus Linteus exists as proteins cohesive on the cell walls, and surrounded by plenty of non-water-soluble fibroid materials. Furthermore, the fruit body of Phellinus Linteus is hardened thickly with a great amount of cell layers.
  • Korean Patent Laid-Open Publication No. 2003-30636 dated April 18, 2003. discloses the method for obtaining the protein polysaccharide by adding inorganic compound and organic nutrition to the fruit body of a mushroom to manufacture ferment compound, fermenting after inoculating Basidiomycota hypha or yeast to the ferment compound, and performing hydrothermal process, dialysis, centrifugal separation, and freeze drying.- ""
  • the yield rate of the protein polysaccharide increases as the tissues of the fruit body is softened by the fermenting process to make the extracting process of the protein polysaccharide easy, however, such a method has a shortcoming in that the original ingredients of the mushroom are generated together with other ferment metabolic products, so the functional substance in a natural mushroom cannot be extracted as it is.
  • the robust fruit body of Phellinus Linteus is, even when it is crushed into powder, too voluminous to be a substrate of enzyme generated during the fermentation by the Basidiomycota hypha and yeast, and it also shows limited solubility, so it is inappropriate to be used in extracting the beta glucan in large quantities. Moreover, many kinds of foreign substances other than beta glucan are included.
  • the Korean Patent No. 308392 dated August 28, 2001 discloses a method for obtaining an extract from natural Phellinus Linteus, in which method Phellinus Linteus undergoes the " extraction process wherein the crushed Phellinus is mixed with extraction solvent and then is warmed up in a double boiler with being decompressed, and in such a situation, ultrasonic wave is applied for about 24 hours to increase the extraction efficiency.
  • beta glucan that is beneficial in the medical point of view exists on the hardened cell layers, and it is a bulky molecule of which molecular weight is more than a million Dalton. As the quantity measurement of such a bulky beta glucan has not been set yet, mere hydrothermal extraction has to be reconsidered.
  • Another object of the present invention is to provide a method of extracting a beneficial ingredient, including crude beta glucan, from Phellinus Linteus with high yield rate. Another object of the invention is to provide crude beta glucan extracted from
  • a method of extracting beneficial ingredients inclusive of crude beta glucan from Phellinus Linteus comprising the steps of: (a) mixing crushed powder of Phellinus Linteus with distilled water of which weight is 20 through 50 times greater than the weight of Phellinus Linteus; (b) applying ultrasonic wave to the mixture obtained at said step (a); (c) subjecting the ultrasonically treated material to a hydrothermal process; (d) filtering the hydrothermally treated material; (e) causing the filtered material to be fermented with cellulase and alcalase; and (f) subjecting the fermented material to ultra-filtration to thereby obtain crude beta glucan.
  • FIGS, la through le show the change of structure of the fruit body of Phellinus Linteus observed with an optical microscope of 1250 magnifications, each of the fruit body obtained in Example 1 and Comparative Examples 1 and 2, in which, FIG. la sEows Phellinus Linteus as it is;
  • FIG. lb depicts powdery Phellinus Linteus
  • FIG. 1 c shows Phellinus Linteus crushed by ultrasonic wave
  • FIG. 1 d illustrates Phellinus Linteus after going through a high pressure hydrothermal process
  • FIG. le shows Phellinus Linteus after subjected to fermentation.
  • the hardened cells of Phellinus Linteus are disrupted through an ultrasonic wave process and a hydrothermal process, thus enabling protein decomposing enzyme and cellulose decomposing enzyme to act in such a manner that beta glucan and other beneficial ingredients are extracted with high yield rate. Furthermore, the content of soluble ingredients is confirmed by a drying method to measure the total extraction efficiency, while the extraction efficiency of crude beta glucan is analyzed quantitatively by virtue of an ultra-filtration method which takes advantage of the molecular size of beta glucan.
  • Comparative Example 1 Hydrothermal Extraction and Ultra-filtration of a Sample.
  • the remaining 10 ml of the concentrated material is ultra-filtrated by use of a membrane filter with one hundred thousand pore-size, and 10 ml of phosphoric acid buffering solution with pH 5.8 is added to the ultra-filtrated material.
  • 10 ml of phosphoric acid buffering solution with pH 5.8 is added to the ultra-filtrated material.
  • 1.2 ml of cellulase(Fluka 22180 0.3U/mg) is added to the resultant material, which material is then cultured for one day.
  • the acidity of the resultant material is changed into 9.0 with potassium phosphate, and an enzyme reaction is performed with cellulase.
  • the resultant material is added with 1 ml of alcalase and cultured at 60 °C for one day.
  • the resultant material is ultra-filtrated with the membrane filter of one hundred thousand pore-size to obtain 1 ml of concentrated supernatant liquid, and then the concentrated liquid is ultra-filtrated once again with the use of 20 ml of distilled water, the resultant material of which is allowed to dry under a vacuum condition to obtain dark brown-colored crude beta glucan. Then, the weight of the crude beta glucan is multiplied by one and a half, and the calculated result is shown in Table 1 in terms of extraction efficiency of crude beta glucan.
  • Comparative Example 2 High Pressure Hydrothermal Extraction and Ultra- filtration of a Sample.
  • Example 1 Ultrasonic Hydrothermal Extraction under High Pressure and Ultra- filtration of a Sample
  • the maximum yield of the total dried extract reaches as high as 34.6% and the maximum yield of crude beta glucan reaches up to 5.2% according to Example 1 wherein the fruit body of Phellinus Linteus is decomposed through the ultrasonic wave process and extracted with the high pressure hydrothermal process, which result is better than the result in Comparative Examples 1 and 2.
  • Such a result means that the total yield of the dried extract in the present invention is five times greater than, and the yield of the cancer-resistant crude beta glucan is twelve times greater than the yield according to the hydrothermal extract method.
  • the content of crude beta glucan in the dried extract obtained in Example 1 is confirmed in accordance with the methods proposed by Mannors. D. J. et. al. (1973, The structure of a ⁇ -(l,6)-D-glucan from yeast cell walls, Biochem. J. 135, 19-30), and Catley, B. J. et. al. (1988. Isolation and analysis of cell walls yeast (A practical approach), IRL press, pp. 163-183).
  • the content of crude beta glucan in the total dried extract is measured by calculating the quantity of glucose in glucan fractions obtained through the chemical process with NaOH solution.
  • the inventive extraction method makes it possible to extract beneficial components, including crude beta glucan, in a cost-effective and highly quantitative manner and therefore can be broadly used in manufacturing medicines, cosmetics and foodstuffs.

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Abstract

Disclosed is a method of extracting beneficial ingredients inclusive of crude beta glucan from Phellinus Linteus. The fruit body of Phellinus Linteus is decomposed by ultrasonic wave, the cell walls of the fruit body are disrupted by hydrothermal process, and then enzyme fermentation is performed, whereby crude beta glucan can be extracted from Phellinus Linteus with increased yield rate.

Description

METHOD OF EXTRACTING CRUDE BETA GLUCAN FROM PHELLINUS
LINTEUS
TECHNICAL FIELD The present invention is directed to a method of extracting crude beta glucan from
Phellinus Linteus with high yield rate, and crude beta glucan extracted by the method.
BACKGROUND ART
Phellinus Linteus is a kind of perennial mushroom growing on mulberry trees and broad- leaved trees in an alpine region, which is classified to scores of species.
The typical species of the mushroom Phellinus are Phellinus Linteus and Phellinus Baumi, which grow on the stalks of the mulberry trees and the broad-leaved trees. Phellinus Linteus has been generally used as a medical material, but is also used as a food material recently. Phellinus Linteus contains magnificent nutrition beneficial to a human body such as potassium, calcium, magnesium, vitamin B2, B3 and C, fibroid material, amino acids, etc., and also contains beta glucan that is a kind of polysaccharide. Among such ingredients, beta glucan is especially beneficial to a human body in a medical point of view, and the immunity enhancement and cancer resistance effects of the beta glucan have been mentioned on a variety of classical medical books in the Orient.
Furthermore, the recent research results show that Phellinus Linteus has the immunity improvement effect by suppressing virus, bacteria, mildew, and vermin, cancer resistance effect resisting the cancer with the level of 96.7%, and anti-oxidation effect influencing on noxious oxygen and radical. Beta glucan in Phellinus Linteus exists as proteins cohesive on the cell walls, and surrounded by plenty of non-water-soluble fibroid materials. Furthermore, the fruit body of Phellinus Linteus is hardened thickly with a great amount of cell layers.
Korean Patent Laid-Open Publication No. 2003-30636 dated April 18, 2003., discloses the method for obtaining the protein polysaccharide by adding inorganic compound and organic nutrition to the fruit body of a mushroom to manufacture ferment compound, fermenting after inoculating Basidiomycota hypha or yeast to the ferment compound, and performing hydrothermal process, dialysis, centrifugal separation, and freeze drying.-""
According to this method, the yield rate of the protein polysaccharide increases as the tissues of the fruit body is softened by the fermenting process to make the extracting process of the protein polysaccharide easy, however, such a method has a shortcoming in that the original ingredients of the mushroom are generated together with other ferment metabolic products, so the functional substance in a natural mushroom cannot be extracted as it is.
Furthermore, the robust fruit body of Phellinus Linteus is, even when it is crushed into powder, too voluminous to be a substrate of enzyme generated during the fermentation by the Basidiomycota hypha and yeast, and it also shows limited solubility, so it is inappropriate to be used in extracting the beta glucan in large quantities. Moreover, many kinds of foreign substances other than beta glucan are included.
The Korean Patent No. 308392 dated August 28, 2001 discloses a method for obtaining an extract from natural Phellinus Linteus, in which method Phellinus Linteus undergoes the "extraction process wherein the crushed Phellinus is mixed with extraction solvent and then is warmed up in a double boiler with being decompressed, and in such a situation, ultrasonic wave is applied for about 24 hours to increase the extraction efficiency. However, such a method is time-consuming, and the organic solvent such as 1,3- butylenechloride, propyleneglicol, or isopropanol has to be used besides water as the extraction solvent, so such a method is not preferable for use in the extraction of the beta glucan of high polarity included in the cell wall in a large quantities, and in the extraction of the original ingredient as it is.
Furthermore, the overall extraction rate just reaches to 5% to 12%, and the remaining after the extraction is not used again. Considering the fact that the price of Phellinus Linteus is as high as hundreds to thousands of dollars per kilogram, the above hydrothermal extraction cannot be said economical.
Moreover, the beta glucan that is beneficial in the medical point of view exists on the hardened cell layers, and it is a bulky molecule of which molecular weight is more than a million Dalton. As the quantity measurement of such a bulky beta glucan has not been set yet, mere hydrothermal extraction has to be reconsidered.
Therefore, the research to extract the beneficial ingredients including the beta glucan from Phellinus Linteus will make it possible that such a superior material is supplied to the patients with low cost, and the clinical results can be brought about scientifically.
DISCLOSURE OF THE INVENTION
With the above-noted problems in mind, it is an object of the present invention to provide a method of extracting a beneficial ingredient, including crude beta glucan, from Phellinus Linteus with high yield rate. Another object of the invention is to provide crude beta glucan extracted from
Phellinus Linteus by the method set forth just above.
In accordance with one aspect of the invention, there is provided a method of extracting beneficial ingredients inclusive of crude beta glucan from Phellinus Linteus, comprising the steps of: (a) mixing crushed powder of Phellinus Linteus with distilled water of which weight is 20 through 50 times greater than the weight of Phellinus Linteus; (b) applying ultrasonic wave to the mixture obtained at said step (a); (c) subjecting the ultrasonically treated material to a hydrothermal process; (d) filtering the hydrothermally treated material; (e) causing the filtered material to be fermented with cellulase and alcalase; and (f) subjecting the fermented material to ultra-filtration to thereby obtain crude beta glucan.
In accordance with another aspect of the invention, there is provided crude beta glucan extracted from Phellinus Linteus by means of the above-referenced method BRIEF DESCRIPTION OF THE DRAWINGS
FIGS, la through le show the change of structure of the fruit body of Phellinus Linteus observed with an optical microscope of 1250 magnifications, each of the fruit body obtained in Example 1 and Comparative Examples 1 and 2, in which, FIG. la sEows Phellinus Linteus as it is;
FIG. lb depicts powdery Phellinus Linteus; FIG. 1 c shows Phellinus Linteus crushed by ultrasonic wave;
FIG. 1 d illustrates Phellinus Linteus after going through a high pressure hydrothermal process; and FIG. le shows Phellinus Linteus after subjected to fermentation.
BEST MODE FOR CARRYING OUT THE INVENTION
According to the present invention, the hardened cells of Phellinus Linteus are disrupted through an ultrasonic wave process and a hydrothermal process, thus enabling protein decomposing enzyme and cellulose decomposing enzyme to act in such a manner that beta glucan and other beneficial ingredients are extracted with high yield rate. Furthermore, the content of soluble ingredients is confirmed by a drying method to measure the total extraction efficiency, while the extraction efficiency of crude beta glucan is analyzed quantitatively by virtue of an ultra-filtration method which takes advantage of the molecular size of beta glucan.
The present invention will no be described in greater detail. It should be apreciated that the following explanation is not to limit the scope of the invention but to show a preferred example of the invention.
Comparative Example 1: Hydrothermal Extraction and Ultra-filtration of a Sample.
Initially, 300 ml of distilled water is mixed with lOg of powder of Phellinus Linteus, and then the mixture is heated at 100°C for one hour, two hours, three hours, and for hours, respectively. Then, the centrifugal -separation is performed against the resultant material, and then the supernatant obtained through the centrifugal separation is concentrated with heat into the quantity of 15 ml. Subsequently, 5 ml of the concentrated material is allowed to dry and then the weight of the dried material is multiplied by 3 and recorded in Table 1 as the data for the total dried extract. The remaining 10 ml of the concentrated material is ultra-filtrated by use of a membrane filter with one hundred thousand pore-size, and 10 ml of phosphoric acid buffering solution with pH 5.8 is added to the ultra-filtrated material. Then, 1.2 ml of cellulase(Fluka 22180 0.3U/mg) is added to the resultant material, which material is then cultured for one day. The acidity of the resultant material is changed into 9.0 with potassium phosphate, and an enzyme reaction is performed with cellulase. The resultant material is added with 1 ml of alcalase and cultured at 60 °C for one day. Then, the resultant material is ultra-filtrated with the membrane filter of one hundred thousand pore-size to obtain 1 ml of concentrated supernatant liquid, and then the concentrated liquid is ultra-filtrated once again with the use of 20 ml of distilled water, the resultant material of which is allowed to dry under a vacuum condition to obtain dark brown-colored crude beta glucan. Then, the weight of the crude beta glucan is multiplied by one and a half, and the calculated result is shown in Table 1 in terms of extraction efficiency of crude beta glucan.
TABLE 1
Figure imgf000006_0001
Comparative Example 2: High Pressure Hydrothermal Extraction and Ultra- filtration of a Sample.
300 ml of distilled water is mixed with lOg of Phellinus Linteus powder, and then the mixture is heated at 120°C for one hour, two hours, three hours, and four hours, respectively, under 2 atm.. Then, the same steps as in Comparative Example"l is carried out, the result of which is recorded in Table 2.
TABLE 2
Figure imgf000007_0001
Example 1: Ultrasonic Hydrothermal Extraction under High Pressure and Ultra- filtration of a Sample
300 ml of distilled water is mixed with lOg of Phellinus Linteus powder, and then the ultrasonic wave (Power 6, Sonifier Cell Disrupter 350, Branson Sonic Power Co., Ltd.) is applied to the mixture for 10 minutes, 20 minutes, 30 minutes, and 60 minutes, respectively. The ultrasonically treated mixture is then subjected to a hydrothermal extraction process at 120°C under 2 atm. for three hours. Subsequently, the same steps as in Comparative Example 1 is carried out, the result of which is indicated in Table 3. TABLE 3
Figure imgf000008_0001
As is apparent from the above table, the maximum yield of the total dried extract reaches as high as 34.6% and the maximum yield of crude beta glucan reaches up to 5.2% according to Example 1 wherein the fruit body of Phellinus Linteus is decomposed through the ultrasonic wave process and extracted with the high pressure hydrothermal process, which result is better than the result in Comparative Examples 1 and 2.
Such a result means that the total yield of the dried extract in the present invention is five times greater than, and the yield of the cancer-resistant crude beta glucan is twelve times greater than the yield according to the hydrothermal extract method.
Experiment for Confirming the Content of Crude Beta Glucan in the Dried Extract Obtained in Example 1.
The content of crude beta glucan in the dried extract obtained in Example 1 is confirmed in accordance with the methods proposed by Mannors. D. J. et. al. (1973, The structure of a β -(l,6)-D-glucan from yeast cell walls, Biochem. J. 135, 19-30), and Catley, B. J. et. al. (1988. Isolation and analysis of cell walls yeast (A practical approach), IRL press, pp. 163-183). The content of crude beta glucan in the total dried extract is measured by calculating the quantity of glucose in glucan fractions obtained through the chemical process with NaOH solution.
Further, the structural change of Phellinus Linteus at the respective process steps is shown in FIGS.- la through le, respectively. Referring to the figures, it can be appreciated that the fruit body of Phellinus Linteus becomes loose, thus assuring easier extraction.
INDUSTRIAL APPLICABILITY
As set forth hereinabove, the inventive extraction method makes it possible to extract beneficial components, including crude beta glucan, in a cost-effective and highly quantitative manner and therefore can be broadly used in manufacturing medicines, cosmetics and foodstuffs.

Claims

1. A method of extracting beneficial ingredients inclusive of crude beta glucan from Phellinus Linteus, comprising the steps of:
(a) mixing crushed powder of Phellinus Linteus with distilled water of which weight is 20 through 50 times greater than the weight of Phellinus Linteus;
(b) applying ultrasonic wave to the mixture obtained at said step (a);
(c) subjecting the ultrasonically treated material to a hydrothermal process;
(d) filtering the hydrothermally treated material;
(e) causing the filtered material to be fermented with cellulase and alcalase; and (f) subjecting the fermented material to ultra-filtration to thereby obtain crude beta glucan.
2. The method as recited in claim 1, wherein said step (c) is performed under the pressure of 2 through 3 atm.
3. The method as recited in claim 1, wherein said steps (d) and (f) are carried out by use of a membrane filter.
4. Crude beta glucan extracted by the method as recited in any one of claims 1, 2 and 3.
PCT/KR2003/001723 2003-05-07 2003-08-26 Method of extracting crude beta glucan from phellinus linteus WO2004099427A1 (en)

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JP2015535310A (en) * 2012-11-13 2015-12-10 コリア フード リサーチ インスティテュート β-glucan production method
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Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100825396B1 (en) * 2007-02-28 2008-04-29 주식회사 한불후치피아 Method of extracting soluble components from animal and plant organism
KR100908034B1 (en) * 2007-06-18 2009-07-20 계명대학교 산학협력단 Mushroom extract, jelly and kochujang containing it
KR100981347B1 (en) * 2007-11-23 2010-09-10 강원대학교산학협력단 The method of extracting
CN104592409B (en) * 2015-01-12 2017-07-11 陕西师范大学 A kind of method that low-pressure low-temperature extracts high activity Phellinus polysaccharide
GB201501799D0 (en) 2015-02-03 2015-03-18 Tate & Lyle Sweden Ab Methods of producing liquid compositions
KR101687985B1 (en) 2015-08-27 2016-12-23 주식회사 엔에스텍 Subcritical extraction method of -glucan derived from mushroom
KR101879506B1 (en) * 2016-10-05 2018-07-17 경북대학교 산학협력단 Extracting method of beta-glucan from Phellinus baumii
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002000229A (en) * 2000-06-23 2002-01-08 S F C:Kk Health food
JP2002262820A (en) * 2001-03-07 2002-09-17 Isao Horiuchi Method for extracting active ingredient of mushrooms
JP2003183176A (en) * 2001-10-09 2003-07-03 Wellness Movement:Kk Immunopotentiating composition

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100303886B1 (en) * 1994-11-19 2001-11-22 임곤혁 Method for extracting anticancer component from phellinus linteus
JP3093194B2 (en) * 1998-04-30 2000-10-03 韓国科学技術研究院 Immune-enhancing active polysaccharide material isolated from a novel Perinus strain and its use
JP3480926B2 (en) * 2000-12-05 2003-12-22 幸仁 秋山 Allergic reaction inhibitor
KR20030072417A (en) * 2002-03-04 2003-09-15 박홍제 Manufacture method of a functional tea and food, using extract of mushroom mycelium by new extraction technique.

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002000229A (en) * 2000-06-23 2002-01-08 S F C:Kk Health food
JP2002262820A (en) * 2001-03-07 2002-09-17 Isao Horiuchi Method for extracting active ingredient of mushrooms
JP2003183176A (en) * 2001-10-09 2003-07-03 Wellness Movement:Kk Immunopotentiating composition

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
KIM H.M. ET AL.: "Stimulation of humoral and cell mediated immunity by polysaccharide from mushroom Phellinus linteus", INTERNATIONAL JOURNAL OF IMMUNOPHARMACOLOGY, vol. 18, no. 5, 1996, pages 295 - 303, XP000877479, DOI: doi:10.1016/0192-0561(96)00028-8 *
LEE J.W. ET AL.: "Characteristics of polysaccharide isolated from the fruit body and cultured mycelia of Phellinus linteus IY001", HAN'GUK KYUNHAKHOECHI, vol. 27, no. 6, 1999, pages 424 - 429 *
LI R. ET AL.: "Study on Phellinus linteus (Berk et Curt) aoshima polysaccharide", YAOXUE XUEBAO, vol. 18, no. 6, 1983, pages 430 - 433 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015535310A (en) * 2012-11-13 2015-12-10 コリア フード リサーチ インスティテュート β-glucan production method
CN109369818A (en) * 2018-10-12 2019-02-22 齐鲁工业大学 A kind of method that ultrasonic synergistic cooking process extracts Eucalyptus xylan
CN111635916A (en) * 2020-06-28 2020-09-08 上海应用技术大学 Pretreatment method for yeast beta-glucan extraction

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