WO2012049737A1 - Method for manufacturing liquid malt enhanced in starch-degrading enzyme activity and dietary fiber-degrading enzyme activity - Google Patents

Method for manufacturing liquid malt enhanced in starch-degrading enzyme activity and dietary fiber-degrading enzyme activity Download PDF

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WO2012049737A1
WO2012049737A1 PCT/JP2010/067894 JP2010067894W WO2012049737A1 WO 2012049737 A1 WO2012049737 A1 WO 2012049737A1 JP 2010067894 W JP2010067894 W JP 2010067894W WO 2012049737 A1 WO2012049737 A1 WO 2012049737A1
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liquid
fiber
degrading enzyme
koji
enzyme activity
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PCT/JP2010/067894
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French (fr)
Japanese (ja)
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晋 舛田
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アサヒグループホールディングス株式会社
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    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
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    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14Hydrolases (3)
    • C12N9/24Hydrolases (3) acting on glycosyl compounds (3.2)
    • C12N9/2402Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
    • C12N9/2405Glucanases
    • C12N9/2408Glucanases acting on alpha -1,4-glucosidic bonds
    • C12N9/2411Amylases
    • C12N9/2414Alpha-amylase (3.2.1.1.)
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    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14Hydrolases (3)
    • C12N9/24Hydrolases (3) acting on glycosyl compounds (3.2)
    • C12N9/2402Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
    • C12N9/2405Glucanases
    • C12N9/2408Glucanases acting on alpha -1,4-glucosidic bonds
    • C12N9/2411Amylases
    • C12N9/2428Glucan 1,4-alpha-glucosidase (3.2.1.3), i.e. glucoamylase
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    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14Hydrolases (3)
    • C12N9/24Hydrolases (3) acting on glycosyl compounds (3.2)
    • C12N9/2402Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
    • C12N9/2405Glucanases
    • C12N9/2434Glucanases acting on beta-1,4-glucosidic bonds
    • C12N9/2437Cellulases (3.2.1.4; 3.2.1.74; 3.2.1.91; 3.2.1.150)
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    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14Hydrolases (3)
    • C12N9/24Hydrolases (3) acting on glycosyl compounds (3.2)
    • C12N9/2402Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
    • C12N9/2477Hemicellulases not provided in a preceding group
    • C12N9/248Xylanases
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    • 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
    • C12P19/14Preparation of compounds containing saccharide radicals produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase, e.g. by cellulase, hemicellulase
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    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12YENZYMES
    • C12Y302/00Hydrolases acting on glycosyl compounds, i.e. glycosylases (3.2)
    • C12Y302/01Glycosidases, i.e. enzymes hydrolysing O- and S-glycosyl compounds (3.2.1)
    • C12Y302/01001Alpha-amylase (3.2.1.1)
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    • C12YENZYMES
    • C12Y302/00Hydrolases acting on glycosyl compounds, i.e. glycosylases (3.2)
    • C12Y302/01Glycosidases, i.e. enzymes hydrolysing O- and S-glycosyl compounds (3.2.1)
    • C12Y302/01003Glucan 1,4-alpha-glucosidase (3.2.1.3), i.e. glucoamylase
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    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12YENZYMES
    • C12Y302/00Hydrolases acting on glycosyl compounds, i.e. glycosylases (3.2)
    • C12Y302/01Glycosidases, i.e. enzymes hydrolysing O- and S-glycosyl compounds (3.2.1)
    • C12Y302/01004Cellulase (3.2.1.4), i.e. endo-1,4-beta-glucanase

Definitions

  • the present invention relates to a method for producing liquid koji with enhanced enzyme activity, and more particularly, to a method for producing liquid koji with enhanced amylolytic enzyme activity and dietary fiber degrading enzyme activity.
  • the starch When producing alcoholic beverages from grains such as wheat, rice and rice bran, since the carbohydrates in the grains exist in the form of starch, the starch is first decomposed into sugar (ie, saccharified). In order to saccharify starch, an amylolytic enzyme such as amylase is required. As the enzyme supply source, straw and malt are used.
  • Non-Patent Document 1 enzyme activity is measured for various rice cakes in which wheat bran, rice bran, corn husk and the like are combined with filamentous fungi, Aspergillus niger and Aspergillus awamori as rice bran media. The measurement results show that these wrinkles mainly have amylolytic enzyme activity.
  • a solid koji that inoculates and inoculates filamentous fungal spores on the raw material after the treatment such as steaming, and a liquid medium is prepared by adding the raw materials and other nutrients to the water, to which the koji mold spores or There are liquid rice cakes that are inoculated with pre-cultured mycelia.
  • the liquid culture method is easy to control culture and quality control, and is a culture format suitable for efficiently producing koji.
  • liquid koji is actually used as an enzyme supply source for producing alcoholic beverages and the like because saccharification power cannot be sufficiently obtained.
  • Patent Document 1 culturing white koji mold or black koji mold using a liquid medium containing a nitrogen source such as cereal with all or part of the grain surface covered with husk and potassium nitrate, It is described that the amylolytic enzyme activity of liquid koji is enhanced.
  • the raw material for saccharification contains a large amount of fiber
  • a problem has been revealed that saccharification does not proceed easily with conventional liquid koji.
  • the reason why saccharification is difficult to proceed in a saccharified raw material containing a large amount of fiber is considered to be because the fiber remains as a solid content in the process of saccharifying starch. That is, in order to obtain a practical level of saccharification even for grains containing a large amount of fiber, it is necessary to enhance not only the starch degrading enzyme activity of liquid koji but also the dietary fiber degrading enzyme activity.
  • the present inventor solves the above-mentioned conventional problems, and the object is to enhance not only the starch degrading enzyme activity of liquid koji but also the dietary fiber degrading enzyme activity in liquid koji. .
  • the present invention includes a step of cultivating white koji mold or black koji mold using a liquid medium containing a carbon source containing a substrate containing cereal and fiber containing all or part of the grain surface covered with husk.
  • a method for producing a liquid koji with enhanced starch degrading enzyme activity and dietary fiber degrading enzyme activity is provided.
  • the starch degrading enzyme is at least acid-resistant ⁇ -amylase and glucoamylase, and the dietary fiber degrading enzyme is at least ⁇ -glucanase and xylanase.
  • the substrate containing the fiber is at least one selected from the group consisting of beet fiber and radish.
  • the substrate containing the fiber is beet fiber.
  • the white gonococcus is Aspergillus kawachi and the black gonococcus is Aspergillus awamori.
  • the grain in which the whole or part of the grain surface is covered with husks is brown rice, rice with all or part of rice husks, or barley or wheat having an unpolished to polished ratio of 92% or more. It is.
  • the present invention also provides a liquid bottle produced by any one of the methods described above.
  • the present invention also includes a step of causing the starch-degrading enzyme and the dietary fiber-degrading enzyme contained in the liquid koji to act on the fiber cereal or the fiber koji.
  • a method for saccharifying glycation is provided.
  • the fibrous cereals are wheat, barley, corn, straw, and the like, and the fibrous cereals are cassava, sweet potato, potato, and the like.
  • the amylolytic enzyme activity and the dietary fiber degrading enzyme activity are enhanced in the liquid koji. Therefore, even a saccharification raw material containing a large amount of fiber can be efficiently saccharified using a liquid koji. That is, the object of practical saccharification by liquid koji is expanded to cereals or koji that contain a large amount of fiber.
  • 3 is a graph showing ⁇ -glucanase activity of a liquid koji of the present invention produced using a substrate containing various fibers and Aspergillus kawachi. It is a graph which shows the xylanase activity about the liquid rice cake of this invention manufactured using the substrate and various Aspergillus kawachi containing various fiber. 3 is a graph showing ⁇ -glucanase activity of a liquid koji of the present invention produced using a substrate containing various fibers and Aspergillus awamori. It is a graph which shows the xylanase activity about the liquid rice cake of this invention manufactured using the substrate and various Aspergillus awamori containing various fiber.
  • 3 is a graph showing acid-resistant ⁇ -amylase activity of a liquid koji of the present invention produced using a substrate containing various fibers and Aspergillus kawachi. It is a graph which shows the glucoamylase activity about the liquid koji of this invention manufactured using the substrate and Aspergillus kawachi containing various fiber. 3 is a graph showing acid-resistant ⁇ -amylase activity of a liquid koji of the present invention produced using a substrate containing various fibers and Aspergillus awamori. It is a graph which shows the glucoamylase activity about the liquid rice cake of this invention manufactured using the board
  • the liquid medium used in the method of the present invention is a liquid in which nutrients necessary for growth and growth of white koji mold or black koji mold are dissolved or suspended in water.
  • nutrients include, for example, carbon sources, nitrogen sources, inorganic salts and the like.
  • Cereal is used as one of the carbon sources. Then, an amylolytic enzyme that degrades starch is produced. Examples of cereals include barley, wheat, rice, buckwheat, millet, millet, millet, cucumber, and corn. Cereal particles, or grains, need to be entirely or partially covered, preferably all, of the surface. The husk is a film covering the surface of the grain.
  • the surface of the grain is covered with husk, it takes time to saccharify the starch in the grain, the rate of sugar release to the culture system is suppressed, and the enzyme activity of the liquid koji is enhanced.
  • unpolished products such as brown rice, brown barley, and brown wheat, or refined products that have been refined to such an extent that the grain skin is left on the surface of the grain
  • the rice husk may be entirely or partially attached.
  • the milling ratio used in the method of the present invention is that the milling ratio is unmilled milling ratio (100% ) Or more than the ratio obtained by subtracting the grain percentage of the grain.
  • barley having a grain ratio of 7-8% and a milling ratio of 92-93% or more can be used.
  • Cereals have a content of 1 to 20% (w / vo1) in the liquid medium, preferably 8 to 10% (w / vol) when the grains are unmilled, and preferably 95%. Is used in an amount of 1 to 4% (w / vo1). If the cereal content is less than 1%, the koji mold does not grow or proliferate sufficiently, and the enzyme activity becomes insufficient. If it exceeds 20%, the viscosity of the culture solution becomes high, and the koji mold is aerobically cultured. The supply of necessary oxygen and air becomes insufficient, the oxygen concentration in the culture decreases, and the culture becomes difficult to proceed.
  • Starch contained in cereals may be gelatinized in advance before culturing.
  • the starch gelatinization method is not particularly limited, and may be performed according to a conventional method such as a steaming method or a roasting method.
  • a steaming method or a roasting method.
  • gelatinization of starch is simultaneously performed by this treatment.
  • a substrate containing fiber is also used in combination with cereals. Then, not only starch degrading enzymes but also dietary fiber degrading enzymes are produced.
  • the substrate containing fiber is preferably at least one selected from the group consisting of beet fiber and radish. The radish is preferably cut and dried. In order to produce a high amount of dietary fiber degrading enzyme, beet fiber is preferable.
  • the substrate containing fibrous material accounts for 1 to 40% (w / v), preferably 5 to 30% (w / v), more preferably 10 to 25% (w / v) of the carbon source in the liquid medium. ), And if it is less than 1%, there is no effect, and if it exceeds 40%, the activity decreases.
  • the nitrogen source is not particularly limited as long as it is a nitrogen supply source necessary for the growth and growth of Neisseria gonorrhoeae.
  • organic substances include yeast cells or processed products thereof (for example, yeast cell decomposition products, yeast extracts, etc.), and examples of inorganic substances include nitrates.
  • nitrate potassium nitrate, sodium nitrate or the like can be used, and potassium nitrate is particularly preferable.
  • the nitrogen source may be used alone or in combination of two or more organic substances and / or inorganic substances.
  • the amount of nitrogen source added is not particularly limited as long as it promotes the growth of Aspergillus, but it is 0.1 to 2% (w / vol), preferably 0.5 to 1.0% (w / Vol).
  • the amount of nitrate added as an inorganic substance is 0.05 to 2.0% (w / vol), preferably 0.1 to 2.0% (w / vol), most preferably 0.2 to 1.5%. % (W / vol).
  • the nitrogen source is added beyond the upper limit, it is not preferable because it inhibits the growth of Aspergillus. Moreover, when the addition amount is less than the lower limit, enzyme production is not promoted, which is also not preferable.
  • Yeasts used as a kind of nitrogen source in the present invention include beer yeasts, wine yeasts, whiskey yeasts, shochu yeasts, sake yeasts, baker's yeasts used in brewing processes and food production, genus Saccharomyces , Candida ( Candida) genus, Torulopsis (Torulopsis) genus, Han Zegna Supora (Hanseniaspora) genera, Hansenula (Hansenula) spp., Debaryomyces (Debaryomyces) genus Saccharomyces Maiko-flops cis (Saccharomycopsis) genus Saccharomyces Maiko death (Saccharomycodes) genus Pichia ( Pichia ) and yeasts such as Pachysolen can be mentioned.
  • yeasts can be used as a nitrogen source, but can also be used as a yeast cell decomposition product or yeast extract.
  • Yeast cell degradation products or yeast extracts are produced by self-digestion of yeast cells (method of solubilizing cells using the proteolytic enzyme inherent in yeast cells), enzyme decomposition methods (from microorganisms and plants) (Methods of solubilization by adding enzyme preparations, etc.), hot water extract method (method of soaking yeast cells in hot water for a certain period of time), acid or alkali decomposition method (various acids or alkalis) Additive solubilization method), physical crushing method (sonication, high-pressure homogenization method, crushing method by mixing and stirring solid materials such as glass beads), freeze-thawing method (freezing / thawing) For example, by crushing once or more).
  • liquid medium used in the present invention may contain sulfate and phosphate in addition to the carbon source or nitrogen source. Enzyme activity is enhanced by using these inorganic salts in combination.
  • magnesium sulfate heptahydrate for example, calcium sulfate, magnesium sulfate heptahydrate, iron sulfate heptahydrate, ammonium sulfate and the like can be used, and magnesium sulfate heptahydrate is particularly preferable.
  • phosphate potassium dihydrogen phosphate, ammonium phosphate or the like can be used, and potassium dihydrogen phosphate is particularly preferable.
  • These inorganic salts can be used alone or in combination of two or more.
  • the concentration of the above-mentioned inorganic salts in the liquid medium is adjusted to such a level that enzymes such as amylolytic enzymes, dietary fiber degrading enzymes, and proteolytic enzymes are selectively generated and accumulated in the koji mold culture.
  • enzymes such as amylolytic enzymes, dietary fiber degrading enzymes, and proteolytic enzymes are selectively generated and accumulated in the koji mold culture.
  • sulfate 0.01 to 0.5% (w / vo1), preferably 0.02 to 0.2% (w / vo1)
  • phosphate 0.05 to 1.0. % (W / vo1), preferably 0.1 to 0.8% (w / vol).
  • organic substances and inorganic salts other than the aforementioned nitrogen sources and inorganic salts can be added as nutrient sources as appropriate.
  • These additives are not particularly limited as long as they are generally used for culturing koji molds, but organic substances such as wheat koji, corn steep liquor, soybean koji, defatted soybeans, etc., and inorganic salts such as ammonium salt and potassium Water-soluble compounds such as salts, calcium salts and magnesium salts can be mentioned, and two or more kinds of organic substances and / or inorganic salts may be used simultaneously.
  • the amount of these additives is not particularly limited as long as it promotes the growth of Neisseria gonorrhoeae, but is about 0.1 to 5% (w / vo1) for organic substances, and 0.1 to 1% (w / vo1) for inorganic salts. It is preferable to add about vo1).
  • the liquid medium of Aspergillus obtained by mixing the above-mentioned culture raw material and nitrogen source with water may be sterilized as necessary, and the treatment method is not particularly limited.
  • a high-temperature and high-pressure sterilization method can be mentioned, which may be performed at 121 ° C. for 15 minutes.
  • Manufacture of liquid koji After cooling the sterilized liquid medium to the culture temperature, inoculate white koji mold and / or black koji mold on the liquid medium.
  • the form of the koji mold inoculated into the medium is arbitrary, and spores or hyphae can be used.
  • the amount of koji mold inoculated into the liquid medium there is no particular limitation on the amount of koji mold inoculated into the liquid medium, but about 1 ⁇ 10 4 to 1 ⁇ 10 6 spores per 1 ml of the liquid medium, and 0.1 to 10 of the preculture solution for mycelia. It is preferable to inoculate about 1%.
  • the culture temperature of Aspergillus is not particularly limited as long as it does not affect the growth, but it is preferably 25 to 45 ° C, more preferably 30 to 40 ° C. When the culture temperature is low, the growth of Aspergillus is delayed, and contamination with various bacteria is likely to occur.
  • the culture time is suitably 24 to 120 hours.
  • koji mold having an ability to produce starch-degrading enzymes such as glucoamylase, acid-resistant ⁇ -amylase and ⁇ -amylase, and dietary fiber degrading enzymes such as cellulase, ⁇ -glucosidase and xylanase are preferable.
  • starch-degrading enzymes such as glucoamylase, acid-resistant ⁇ -amylase and ⁇ -amylase
  • dietary fiber degrading enzymes such as cellulase, ⁇ -glucosidase and xylanase are preferable.
  • Aspergillus kawachii and the like are Aspergillus or aspergillus niger and Aspergillus niger and the like are Aspergillus awachi and Aspergillus niger .
  • Aspergillus oryzae Aspergillus kawachi is preferable. Aspergillus niger is preferably Aspergillus awamori. This is because by using these, starch-degrading enzymes and dietary fiber-degrading enzymes are highly produced.
  • koji molds can be used either by culturing with one type of strain or by mixed culturing with two or more types of strains of the same or different types. There is no problem with using any form of spores or hyphae obtained by preculture, but it is preferable to use hyphae because the time required for the logarithmic growth phase is shortened.
  • the culture apparatus may be any apparatus that can perform liquid culture. However, since Neisseria gonorrhoeae needs to perform aerobic culture, it needs to be performed under aerobic conditions in which oxygen and air can be supplied into the medium. Moreover, it is preferable to stir so that the raw material, oxygen, and koji mold in the medium are uniformly distributed in the apparatus during the culture.
  • the stirring conditions and the aeration amount may be any conditions as long as the culture environment can be maintained aerobically, and may be appropriately selected depending on the culture apparatus, the viscosity of the medium, and the like.
  • a liquid koji having enzyme activity such as starch-degrading enzyme that degrades starch and dietary fiber-degrading enzyme that degrades dietary fiber and hemicellulose can be obtained.
  • the liquid koji includes a liquid culture itself, a culture supernatant, a clarified liquid obtained by filtering or centrifuging the culture, a concentrate thereof, and the like. Also, dried liquid koji is equivalent to liquid koji and can be used as an enzyme source as well.
  • the liquid cake of the present invention preferably exhibits, for example, the following enzyme activity in an unconcentrated state. Each enzyme activity is measured according to the method described in the examples.
  • the acid-resistant ⁇ -amylase (ASAA) activity is 16 U / ml or more, preferably 18 U / ml or more, more preferably 20 U / ml or more, and further preferably 23 U / ml or more.
  • About glucoamylase (GA) activity it is 45 U / ml or more, Preferably it is 50 U / ml or more, More preferably, it is 60 U / ml or more, More preferably, it is 70 U / ml or more.
  • the ⁇ -glucanase (BG) activity is 0.15 U / ml or more, preferably 0.20 U / ml or more, more preferably 0.80 U / ml or more, and further preferably 1.0 U / ml or more.
  • the xylanase (XY) activity is 0.20 U / ml or more, preferably 0.28 U / ml or more, more preferably 0.30 U / ml or more, and further preferably 0.40 U / ml or more.
  • the liquid koji obtained by the production method of the present invention can be used in the same manner as solid koji as an enzyme source for producing fermented foods and drinks such as shochu, sake, soy sauce, miso, mirin and amazake.
  • liquid soot a part of the obtained liquid soot can be used as a starter in the next liquid soot production.
  • stable production is possible, and at the same time, production efficiency can be improved.
  • the liquid koji of the present invention can be used as a pharmaceutical preparation such as an enzyme preparation and a digestive agent because of its high enzyme activity.
  • the obtained koji mold culture may be concentrated and purified to a desired degree, and an appropriate excipient, thickener, sweetener and the like may be added to prepare a preparation by a conventional method.
  • Saccharification of saccharification raw material When the saccharification raw material is saccharified using the liquid koji of the present invention, the amylolytic enzyme and dietary fiber degrading enzyme contained in the liquid koji of the present invention are allowed to act on the saccharification raw material.
  • the saccharified raw material is pretreated as necessary, and then poured into water containing a sufficient amount of liquid soot for the saccharified raw material to be immersed, and statically maintained at a temperature suitable for the enzyme to act. Or shaken or agitated as necessary.
  • pretreatment of the saccharification raw material operations such as washing, pulverization, heating, and alkali treatment are generally performed.
  • the liquid koji of the present invention is rich in starch degrading enzymes and dietary fiber degrading enzymes. That is, this liquid koji is excellent in the decomposing power of starch contained in the saccharification raw material and also in the decomposing power of the fiber. Therefore, even when the saccharification raw material contains a large amount of fiber, the fiber does not remain as a solid content during the saccharification process, and the progress of saccharification is promoted.
  • the saccharification raw material rich in fiber which has been difficult to saccharify with conventional liquid koji, or has low saccharification efficiency, includes cereals rich in fiber or potatoes rich in fiber, specifically Are wheat, barley, corn, and straw as cereals, and cassava, sweet potato, and potato as potatoes.
  • a saccharified solution obtained by saccharifying a saccharified raw material containing a large amount of fiber is used to produce alcoholic beverages such as shochu or bioethanol by, for example, fermenting alcohol using yeast and, if necessary, distilling it. Is done.
  • Example 1 Manufacture of liquid cake Aspergillus oryzae strains, Aspergillus kawachi (NBRC4308 strain), which is a standard strain related to white mold, and Aspergillus awamori (NBRC4388 strain), which is a standard strain related to Aspergillus niger, were prepared.
  • Preculture method 100 ml of a preculture medium having a composition of 65% refined barley 8% (w / v), KNO 3 0.2% (w / v), KH 2 PO 4 0.3% (w / v), It put into the conical flask with a capacity
  • Substrate containing fiber As a substrate containing fiber, beet fiber (derived from sugar beet: manufactured by Nippon Sugar Sugar Co., Ltd.) and Japanese radish (cut dried radish) were prepared. The radish was pulverized before use.
  • starch soluble starch
  • Enzyme activity was measured using a culture supernatant obtained by centrifugation from the culture medium in which main culture was performed, as a liquid sputum sample.
  • the measuring method is as follows.
  • Acid-resistant ⁇ -amylase (ASAA) activity After 9 ml of 100 mM acetate buffer (pH 3) was added to 1 ml of the culture supernatant and acid treatment was performed at 37 ° C. for 1 hour, the measurement was performed using an ⁇ -amylase measurement kit (manufactured by Kikkoman).
  • Glucoamylase (GA) activity Measured according to the National Tax Agency prescribed analysis method. Specifically, 0.2 ml of 0.2 M acetate buffer was added to 1 ml of starch solution and preheated at 40 ° C. for 5 minutes. To this, 0.1 ml of the culture supernatant was added and reacted at 40 ° C. for 20 minutes, and 0.1 ml of 1N sodium hydroxide solution was added to stop the reaction. Thereafter, the mixture was allowed to stand for 30 minutes and neutralized by adding 0.1 ml of 1N hydrochloric acid solution. As a control, add 0.2 ml of 0.2 M acetate buffer to 1 ml of starch solution, preheat at 40 ° C.
  • the glucoamylase activity was expressed with 1 unit of activity to produce 1 mg of glucose from soluble starch at 40 ° C. for 60 minutes.
  • ⁇ -glucanase activity was determined by measuring the absorbance of a stained fragment produced by enzymatic degradation using ⁇ -glucan labeled with a dye, using a ⁇ -glucanase measurement kit manufactured by Megazyme. Specifically, 0.5 ml of the culture supernatant was added to 0.5 ml of the azo barley glucan substrate solution, and the enzyme reaction was carried out at 40 ° C. for exactly 10 minutes, and then the stop solution [4% sodium acetate, 0% .4% zinc acetate and 80% methyl cellosolve (pH 5)] 3.0 ml was added and left for 5 minutes to stop the reaction. Subsequently, after centrifugation, the absorbance of the supernatant was measured at 590 nm.
  • 1 unit of ⁇ -glucanase activity was expressed as the amount of enzyme that produces reducing sugar corresponding to 1 ⁇ mol of glucose per minute under the reaction conditions of 40 ° C. and 10 minutes.
  • Xylanase (XY) activity The xylanase activity was determined by measuring the absorbance of a stained fragment produced by enzymatic degradation using azo-xylan as a substrate, using a xylanase measurement kit manufactured by Megazyme. More specifically, 0.5 ml of the culture supernatant was added to 0.5 ml of 1% azo-xylan substrate solution (manufactured by Megazyme), and the enzyme reaction was performed at 40 ° C. for exactly 10 minutes. [Ethanol (95% v / v)] 2.5 ml was added and mixed well to stop the reaction. Subsequently, after centrifugation, the absorbance of the supernatant was measured at 590 nm.
  • 1 unit of xylanase activity was expressed as the amount of enzyme that produces reducing sugar corresponding to 1 ⁇ mol of glucose per minute under the reaction conditions of 40 ° C. and 10 minutes.
  • FIG. 1 and FIG. 2 show BG activity (U / ml) and XY activity (U / ml) for a liquid sputum sample using Aspergillus kawachi.
  • FIG. 3 and FIG. 4 show the BG activity (U / ml) and XY activity (U / ml) of the liquid sputum sample using Aspergillus awamori.
  • BG activity and XY activity which are dietary fiber degrading enzyme activities, were increased in both liquid aspergillus samples using Aspergillus kawachi and Aspergillus awamori.
  • ASAA activity (U / ml) and GA activity (U / ml) for the liquid sputum sample using Aspergillus kawachi are shown in FIG. 5 and FIG.
  • ASAA activity (U / ml) and GA activity (U / ml) about the liquid sputum sample using Aspergillus awamori are shown in FIG. 7 and FIG.
  • ASAA activity and GA activity which are amylolytic enzyme activities, were increased in both liquid aspergillus samples using Aspergillus kawachi and Aspergillus awamori.
  • FIG. 9 shows the results for a liquid koji sample using Aspergillus kawachi as a saccharification ratio, and the results for a liquid koji sample using Aspergillus awamori. As shown in FIG.
  • FIG. 11 shows the results for the liquid koji sample using Aspergillus kawachi as the saccharification rate, and the results for the liquid koji sample using Aspergillus awamori as the saccharification rate with respect to the total starch amount in 1.0 g of cassava. As shown in FIG.

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Abstract

The present invention addresses the problem of enhancing not only the starch-degrading enzyme activity but also the dietary fiber-degrading enzyme activity of a liquid malt. The means for solving the problem is a method for manufacturing a liquid malt that has enhanced starch-degrading enzyme activity and dietary fiber-degrading enzyme activity, the method including a step for culturing a white malt or a black malt in a liquid culture medium that contains carbon sources containing grains the surfaces of which are wholly or partially covered with grain hulls and containing substrates containing fibers.

Description

デンプン分解酵素活性及び食物繊維分解酵素活性が増強された液体麹の製造方法Method for producing liquid koji with enhanced starch degrading enzyme activity and dietary fiber degrading enzyme activity
 本発明は、酵素活性が増強された液体麹の製造方法に関し、特に、デンプン分解酵素活性及び食物繊維分解酵素活性が増強された液体麹の製造方法に関する。 The present invention relates to a method for producing liquid koji with enhanced enzyme activity, and more particularly, to a method for producing liquid koji with enhanced amylolytic enzyme activity and dietary fiber degrading enzyme activity.
 麦、米、芋などの穀物類から酒類を製造する場合、穀物類の中の炭水化物はデンプンの形で存在しているため、先ず、デンプンが糖に分解(即ち糖化)される。デンプンを糖化するためにはアミラーゼ等のデンプン分解酵素が必要である。酵素の供給源としては麹及び麦芽等が用いられる。 When producing alcoholic beverages from grains such as wheat, rice and rice bran, since the carbohydrates in the grains exist in the form of starch, the starch is first decomposed into sugar (ie, saccharified). In order to saccharify starch, an amylolytic enzyme such as amylase is required. As the enzyme supply source, straw and malt are used.
 例えば、非特許文献1には、麹媒体として小麦ふすま、米ぬか、トウモロコシの皮などを、糸状菌であるアスペルギルス・ニガー及びアスペルギルス・アワモリと組み合わせた各種麹について、酵素活性が測定されている。測定結果において、これらの麹は主としてデンプン分解酵素活性を有することが示されている。 For example, in Non-Patent Document 1, enzyme activity is measured for various rice cakes in which wheat bran, rice bran, corn husk and the like are combined with filamentous fungi, Aspergillus niger and Aspergillus awamori as rice bran media. The measurement results show that these wrinkles mainly have amylolytic enzyme activity.
 麹には、蒸煮等の処理後の原料に糸状菌の胞子を接種して培養する固体麹と、水に原料及びその他の栄養源を添加して液体培地を調製し、これに麹菌の胞子又は前培養した菌糸等を接種して培養する液体麹がある。 For the koji, a solid koji that inoculates and inoculates filamentous fungal spores on the raw material after the treatment such as steaming, and a liquid medium is prepared by adding the raw materials and other nutrients to the water, to which the koji mold spores or There are liquid rice cakes that are inoculated with pre-cultured mycelia.
 液体培養法は培養制御や品質管理が容易であり、麹を効率的に生産するのに適した培養形態である。しかし、糖化力が十分に得られない等の理由から、酒類等を製造するために、実際に液体麹を酵素の供給源として用いた例は少ない。 The liquid culture method is easy to control culture and quality control, and is a culture format suitable for efficiently producing koji. However, there are few examples in which liquid koji is actually used as an enzyme supply source for producing alcoholic beverages and the like because saccharification power cannot be sufficiently obtained.
 液体麹の糖化力を向上させるために、本発明者らは、これまでも液体培養法の改良を試みてきた。例えば、特許文献1には、穀粒表面の全部又は一部が穀皮で覆われた穀類、及び硝酸カリウム等の窒素源を含有する液体培地を用いて白麹菌又は黒麹菌を培養することで、液体麹のデンプン分解酵素活性が増強されることが記載されている。 In order to improve the saccharification power of liquid koji, the present inventors have tried to improve the liquid culture method so far. For example, in Patent Document 1, culturing white koji mold or black koji mold using a liquid medium containing a nitrogen source such as cereal with all or part of the grain surface covered with husk and potassium nitrate, It is described that the amylolytic enzyme activity of liquid koji is enhanced.
 しかし、糖化の原料が繊維質を多く含む場合、例えば、繊維質を多く含む穀類又は芋類である場合、従来の液体麹では糖化が進行し難くなる問題が明らかになった。繊維質を多く含む糖化原料において糖化が進行し難い理由は、デンプンを糖化する過程で繊維質が固形分として残存するためと考えられる。即ち、繊維質を多く含む穀物類に対しても実用レベルの糖化力を得るには、液体麹のデンプン分解酵素活性だけでなく、食物繊維分解酵素活性をも増強する必要がある。 However, when the raw material for saccharification contains a large amount of fiber, for example, when it is a cereal or cocoon containing a large amount of fiber, a problem has been revealed that saccharification does not proceed easily with conventional liquid koji. The reason why saccharification is difficult to proceed in a saccharified raw material containing a large amount of fiber is considered to be because the fiber remains as a solid content in the process of saccharifying starch. That is, in order to obtain a practical level of saccharification even for grains containing a large amount of fiber, it is necessary to enhance not only the starch degrading enzyme activity of liquid koji but also the dietary fiber degrading enzyme activity.
特許4083194Patent 4083194
 本発明者は、上記従来の問題を解決するものであり、その目的とするところは、液体麹において、液体麹のデンプン分解酵素活性だけでなく、食物繊維分解酵素活性をも増強することにある。 The present inventor solves the above-mentioned conventional problems, and the object is to enhance not only the starch degrading enzyme activity of liquid koji but also the dietary fiber degrading enzyme activity in liquid koji. .
 本発明は、穀粒表面の全部又は一部が穀皮で覆われた穀類及び繊維質を含む基質を含有する炭素源を含有する液体培地を用いて、白麹菌又は黒麹菌を培養する工程を包含する、デンプン分解酵素活性及び食物繊維分解酵素活性が増強された液体麹の製造方法を提供する。 The present invention includes a step of cultivating white koji mold or black koji mold using a liquid medium containing a carbon source containing a substrate containing cereal and fiber containing all or part of the grain surface covered with husk. A method for producing a liquid koji with enhanced starch degrading enzyme activity and dietary fiber degrading enzyme activity is provided.
 ある一形態においては、前記デンプン分解酵素が少なくとも耐酸性α-アミラーゼ及びグルコアミラーゼであり、前記食物繊維分解酵素が少なくともβ-グルカナーゼ及びキシラナーゼである。 In one embodiment, the starch degrading enzyme is at least acid-resistant α-amylase and glucoamylase, and the dietary fiber degrading enzyme is at least β-glucanase and xylanase.
 ある一形態においては、前記繊維質を含む基質がビートファイバー及び大根からなる群から選択される少なくとも一種である。 In one embodiment, the substrate containing the fiber is at least one selected from the group consisting of beet fiber and radish.
 ある一形態においては、前記繊維質を含む基質がビートファイバーである。 In one embodiment, the substrate containing the fiber is beet fiber.
 ある一形態においては、前記白麹菌がアスペルギルス・カワチであり、前記黒麹菌がアスペルギルス・アワモリである。 In one embodiment, the white gonococcus is Aspergillus kawachi and the black gonococcus is Aspergillus awamori.
 ある一形態においては、前記穀粒表面の全部又は一部が穀皮で覆われた穀類が、玄米、籾殻が全部又は一部付いている米又は未精白から精白歩合92%以上の大麦若しくは小麦である。 In one certain form, the grain in which the whole or part of the grain surface is covered with husks is brown rice, rice with all or part of rice husks, or barley or wheat having an unpolished to polished ratio of 92% or more. It is.
 また、本発明は、上記のいずれかに記載の方法により製造された液体麹を提供する。 The present invention also provides a liquid bottle produced by any one of the methods described above.
 また、本発明は、繊維質の穀類又は繊維質の芋類に対し、前記液体麹に含まれるデンプン分解酵素及び食物繊維分解酵素を作用させる工程を包含する、繊維質の穀類又は繊維質の芋類の糖化方法を提供する。 The present invention also includes a step of causing the starch-degrading enzyme and the dietary fiber-degrading enzyme contained in the liquid koji to act on the fiber cereal or the fiber koji. A method for saccharifying glycation is provided.
 ある一形態においては、前記繊維質の穀類が小麦、大麦、トウモロコシ、稗などであり、前記繊維質の芋類がキャッサバ、サツマイモ、ジャガイモなどである。 In one embodiment, the fibrous cereals are wheat, barley, corn, straw, and the like, and the fibrous cereals are cassava, sweet potato, potato, and the like.
 本発明の方法によれば、液体麹において、デンプン分解酵素活性及び食物繊維分解酵素活性が増強される。そのため、繊維質を多く含む糖化原料であっても液体麹を用いて効率よく糖化することが可能となる。つまり、液体麹による実用的な糖化の対象が、繊維質を多く含む穀類又は芋類にまで拡大される。 According to the method of the present invention, the amylolytic enzyme activity and the dietary fiber degrading enzyme activity are enhanced in the liquid koji. Therefore, even a saccharification raw material containing a large amount of fiber can be efficiently saccharified using a liquid koji. That is, the object of practical saccharification by liquid koji is expanded to cereals or koji that contain a large amount of fiber.
各種の繊維質を含む基質及びアスペルギルス・カワチを用いて製造された本発明の液体麹についてのβ-グルカナーゼ活性を示すグラフである。3 is a graph showing β-glucanase activity of a liquid koji of the present invention produced using a substrate containing various fibers and Aspergillus kawachi. 各種の繊維質を含む基質及びアスペルギルス・カワチを用いて製造された本発明の液体麹についてのキシラナーゼ活性を示すグラフである。It is a graph which shows the xylanase activity about the liquid rice cake of this invention manufactured using the substrate and various Aspergillus kawachi containing various fiber. 各種の繊維質を含む基質及びアスペルギルス・アワモリを用いて製造された本発明の液体麹についてのβ-グルカナーゼ活性を示すグラフである。3 is a graph showing β-glucanase activity of a liquid koji of the present invention produced using a substrate containing various fibers and Aspergillus awamori. 各種の繊維質を含む基質及びアスペルギルス・アワモリを用いて製造された本発明の液体麹についてのキシラナーゼ活性を示すグラフである。It is a graph which shows the xylanase activity about the liquid rice cake of this invention manufactured using the substrate and various Aspergillus awamori containing various fiber. 各種の繊維質を含む基質及びアスペルギルス・カワチを用いて製造された本発明の液体麹についての耐酸性α-アミラーゼ活性を示すグラフである。3 is a graph showing acid-resistant α-amylase activity of a liquid koji of the present invention produced using a substrate containing various fibers and Aspergillus kawachi. 各種の繊維質を含む基質及びアスペルギルス・カワチを用いて製造された本発明の液体麹についてのグルコアミラーゼ活性を示すグラフである。It is a graph which shows the glucoamylase activity about the liquid koji of this invention manufactured using the substrate and Aspergillus kawachi containing various fiber. 各種の繊維質を含む基質及びアスペルギルス・アワモリを用いて製造された本発明の液体麹についての耐酸性α-アミラーゼ活性を示すグラフである。3 is a graph showing acid-resistant α-amylase activity of a liquid koji of the present invention produced using a substrate containing various fibers and Aspergillus awamori. 各種の繊維質を含む基質及びアスペルギルス・アワモリを用いて製造された本発明の液体麹についてのグルコアミラーゼ活性を示すグラフである。It is a graph which shows the glucoamylase activity about the liquid rice cake of this invention manufactured using the board | substrate and various Aspergillus awamoris containing various fiber. 各種の繊維質を含む基質及びアスペルギルス・カワチを用いて製造された本発明の液体麹で小麦を糖化して得られた糖化率を示すグラフである。It is a graph which shows the saccharification rate obtained by saccharifying wheat with the liquid rice bran of this invention manufactured using the substrate and various Aspergillus kawachi containing various fibers. 各種の繊維質を含む基質及びアスペルギルス・アワモリを用いて製造された本発明の液体麹で小麦を糖化して得られた糖化率を示すグラフである。It is a graph which shows the saccharification rate obtained by saccharifying wheat with the liquid rice bran of this invention manufactured using the substrate containing various fibrous materials, and Aspergillus awamori. 各種の繊維質を含む基質及びアスペルギルス・カワチを用いて製造された本発明の液体麹でキャッサバを糖化して得られた糖化率を示すグラフである。It is a graph which shows the saccharification rate obtained by saccharifying cassava with the liquid rice bran of this invention manufactured using the substrate containing various fibrous materials, and Aspergillus kawachi. 各種の繊維質を含む基質及びアスペルギルス・アワモリを用いて製造された本発明の液体麹でキャッサバを糖化して得られた糖化率を示すグラフである。It is a graph which shows the saccharification rate obtained by saccharifying cassava with the liquid rice bran of this invention manufactured using the substrate containing various fibrous materials, and Aspergillus awamori.
 液体培地
 本発明の方法で用いる液体培地は、白麹菌又は黒麹菌が生育及び増殖するのに必要な栄養を水中に溶解又は懸濁させた液体である。かかる栄養には、例えば、炭素源、窒素源、無機塩類などが含まれる。
Liquid medium The liquid medium used in the method of the present invention is a liquid in which nutrients necessary for growth and growth of white koji mold or black koji mold are dissolved or suspended in water. Such nutrients include, for example, carbon sources, nitrogen sources, inorganic salts and the like.
 炭素源の一つとしては、穀類を用いる。そうすると、デンプンを分解するデンプン分解酵素が生産される。穀類としては、例えば、大麦、小麦、米、そば、ヒエ、アワ、キビ、コウリャン、トウモロコシ等を挙げることができる。穀類の粒子、即ち穀粒は、表面の全部又は一部、好ましくは全部が穀皮で覆われていることが必要である。穀皮とは穀粒の表面を覆っている皮膜を言う。 Cereal is used as one of the carbon sources. Then, an amylolytic enzyme that degrades starch is produced. Examples of cereals include barley, wheat, rice, buckwheat, millet, millet, millet, cucumber, and corn. Cereal particles, or grains, need to be entirely or partially covered, preferably all, of the surface. The husk is a film covering the surface of the grain.
 穀粒の表面が穀皮で覆われていると、当該穀粒中のでん粉の糖化に時間がかかり、培養系への糖の放出速度が抑制され、液体麹の酵素活性が増強される。 If the surface of the grain is covered with husk, it takes time to saccharify the starch in the grain, the rate of sugar release to the culture system is suppressed, and the enzyme activity of the liquid koji is enhanced.
 穀類は、例えば、玄米、玄大麦、玄小麦などの未精白物、又は穀皮が穀粒の表面に残されている程度までに精白された精白物を用いることができる。また、米の場合には、籾殻が全部又は一部付いているものでもよい。 As the cereals, for example, unpolished products such as brown rice, brown barley, and brown wheat, or refined products that have been refined to such an extent that the grain skin is left on the surface of the grain can be used. In the case of rice, the rice husk may be entirely or partially attached.
 未精白の穀粒の重量を100として、精白後にも残存する穀粒の重量の割合を精白歩合とすると、本発明の方法で用いる精白物は、精白歩合が、未精白の精白歩合(100%)から穀粒の穀皮歩合を差し引いた割合以上である。 Assuming that the weight of unmilled grain is 100 and the ratio of the weight of grain remaining after milling is the milling ratio, the milling ratio used in the method of the present invention is that the milling ratio is unmilled milling ratio (100% ) Or more than the ratio obtained by subtracting the grain percentage of the grain.
 例えば、大麦は穀皮歩合が7~8%であり、精白歩合が92~93%以上のものを用いることができる。 For example, barley having a grain ratio of 7-8% and a milling ratio of 92-93% or more can be used.
 穀類は、液体培地中の含有量が1~20%(w/vo1)であり、穀類が未精白の場合は好ましくは8~10%(w/vol)であり、95%精白の場合は好ましくは1~4%(w/vo1)となる量で用いられる。穀類の含有量が1%未満であると麹菌は十分に育成又は増殖せず、酵素活性が不十分となり、20%を超えると、培養液の粘性が高くなり、麹菌を好気培養するために必要な酸素や空気の供給が不十分となり、培養物中の酸素濃度が低下して、培養が進み難くなる。 Cereals have a content of 1 to 20% (w / vo1) in the liquid medium, preferably 8 to 10% (w / vol) when the grains are unmilled, and preferably 95%. Is used in an amount of 1 to 4% (w / vo1). If the cereal content is less than 1%, the koji mold does not grow or proliferate sufficiently, and the enzyme activity becomes insufficient. If it exceeds 20%, the viscosity of the culture solution becomes high, and the koji mold is aerobically cultured. The supply of necessary oxygen and air becomes insufficient, the oxygen concentration in the culture decreases, and the culture becomes difficult to proceed.
 穀類に含まれるデンプンは、培養前に予め糊化しておいてもよい。デンプンの糊化方法については特に限定はなく、蒸きょう法、焙焼法等常法に従って行なえばよい。後述する液体培地の殺菌工程において、高温高圧滅菌等によりデンプンの糊化温度以上に加熱する場合は、この処理によりデンプンの糊化も同時に行なわれる。 Starch contained in cereals may be gelatinized in advance before culturing. The starch gelatinization method is not particularly limited, and may be performed according to a conventional method such as a steaming method or a roasting method. In the sterilization step of the liquid medium described later, when heating is performed at a temperature higher than the gelatinization temperature of starch by high-temperature high-pressure sterilization or the like, gelatinization of starch is simultaneously performed by this treatment.
 また、液体培地の炭素源としては、穀類と組み合わせて、繊維質を含む基質も用いる。そうすると、デンプン分解酵素ばかりでなく、食物繊維分解酵素も生産される。繊維質を含む基質としてはビートファイバー及び大根からなる群から選択される少なくとも一種であることが好ましい。大根は、好ましくは切断し乾燥する。食物繊維分解酵素を高生産させるために、好ましくはビートファイバーである。 Also, as a carbon source for the liquid medium, a substrate containing fiber is also used in combination with cereals. Then, not only starch degrading enzymes but also dietary fiber degrading enzymes are produced. The substrate containing fiber is preferably at least one selected from the group consisting of beet fiber and radish. The radish is preferably cut and dried. In order to produce a high amount of dietary fiber degrading enzyme, beet fiber is preferable.
 繊維質を含む基質は、液体培地中の炭素源に占める割合が1~40%(w/v)、好ましくは5~30%(w/v)、より好ましくは10~25%(w/v)となる割合で用いられ、1%未満であると効果がなく、40%を超えると活性が低下する。 The substrate containing fibrous material accounts for 1 to 40% (w / v), preferably 5 to 30% (w / v), more preferably 10 to 25% (w / v) of the carbon source in the liquid medium. ), And if it is less than 1%, there is no effect, and if it exceeds 40%, the activity decreases.
 窒素源としては、麹菌が育成及び増殖するのに必要な窒素供給源であれば特に限定はない。有機物としては、例えば、酵母菌体又はその処理物(例えば、酵母菌体分解物、酵母エキスなど)等が挙げられ、無機物としては、例えば、硝酸塩が挙げられる。 The nitrogen source is not particularly limited as long as it is a nitrogen supply source necessary for the growth and growth of Neisseria gonorrhoeae. Examples of organic substances include yeast cells or processed products thereof (for example, yeast cell decomposition products, yeast extracts, etc.), and examples of inorganic substances include nitrates.
 硝酸塩としては硝酸カリウム、硝酸ナトリウムなどを用いることができ、特に硝酸カリウムが好ましい。窒素源は、単独で用いる他、2種類以上の有機物及び/又は無機物を組み合せて使用してもよい。 As the nitrate, potassium nitrate, sodium nitrate or the like can be used, and potassium nitrate is particularly preferable. The nitrogen source may be used alone or in combination of two or more organic substances and / or inorganic substances.
 窒素源の添加量は、麹菌の増殖を促進する程度であれば特に限定はないが、有機物としては0.1~2%(w/vol)、好ましくは0.5~1.0%(w/vol)である。また、無機物としての硝酸塩の添加量は0.05~2.0%(w/vol)、好ましくは0.1~2.0%(w/vol)、もっとも好ましくは0.2~1.5%(w/vol)である。 The amount of nitrogen source added is not particularly limited as long as it promotes the growth of Aspergillus, but it is 0.1 to 2% (w / vol), preferably 0.5 to 1.0% (w / Vol). The amount of nitrate added as an inorganic substance is 0.05 to 2.0% (w / vol), preferably 0.1 to 2.0% (w / vol), most preferably 0.2 to 1.5%. % (W / vol).
 上限値を超えて窒素源を添加した場合は、麹菌の増殖を阻害するため好ましくない。また、添加量が下限値未満である場合は、酵素生産が促されないため、やはり好ましくない。 If the nitrogen source is added beyond the upper limit, it is not preferable because it inhibits the growth of Aspergillus. Moreover, when the addition amount is less than the lower limit, enzyme production is not promoted, which is also not preferable.
 本発明で窒素源の一種として用いられる酵母は、醸造工程や食品製造で用いられるビール酵母、ワイン酵母、ウイスキー酵母、焼酎酵母、清酒酵母、パン酵母のほかにサッカロマイセス(Saccharomyces)属、キャンディダ(Candida)属、トルロプシス(Torulopsis)属、ハンゼニアスポラ(Hanseniaspora)属、ハンゼヌラ(Hansenula)属、デバリオマイセス(Debaryomyces)属、サッカロマイコプシス(Saccharomycopsis)属、サッカロマイコデス(Saccharomycodes)属、ピヒア(Pichia)属、パキィソレン(Pachysolen)属等の酵母菌体を挙げることができる。 Yeasts used as a kind of nitrogen source in the present invention include beer yeasts, wine yeasts, whiskey yeasts, shochu yeasts, sake yeasts, baker's yeasts used in brewing processes and food production, genus Saccharomyces , Candida ( Candida) genus, Torulopsis (Torulopsis) genus, Han Zegna Supora (Hanseniaspora) genera, Hansenula (Hansenula) spp., Debaryomyces (Debaryomyces) genus Saccharomyces Maiko-flops cis (Saccharomycopsis) genus Saccharomyces Maiko death (Saccharomycodes) genus Pichia ( Pichia ) and yeasts such as Pachysolen can be mentioned.
 これらの酵母は、菌体そのものを窒素源として用いることもできるが、酵母菌体分解物や酵母エキスとして用いることもできる。酵母菌体分解物あるいは酵母エキスは、酵母菌体を自己消化法(酵母菌体内に本来あるタンパク質分解酵素を利用して菌体を可溶化する方法)、酵素分解法(微生物由来や植物由来の酵素製剤等を添加して可溶化する方法)、熱水抽出物法(熱水中に酵母菌体を一定時間浸漬して可溶化する方法)、酸あるいはアルカリ分解法(種々の酸あるいはアルカリを添加して可溶化する方法)、物理的破砕法(超音波処理や高圧ホモジナイズ法、ガラスビーズ等の固形物を混合して混合・攪拌することにより破砕する方法)、凍結融解法(凍結・融解を1回以上行なうことにより破砕する方法)等により処理することで得られる。 These yeasts can be used as a nitrogen source, but can also be used as a yeast cell decomposition product or yeast extract. Yeast cell degradation products or yeast extracts are produced by self-digestion of yeast cells (method of solubilizing cells using the proteolytic enzyme inherent in yeast cells), enzyme decomposition methods (from microorganisms and plants) (Methods of solubilization by adding enzyme preparations, etc.), hot water extract method (method of soaking yeast cells in hot water for a certain period of time), acid or alkali decomposition method (various acids or alkalis) Additive solubilization method), physical crushing method (sonication, high-pressure homogenization method, crushing method by mixing and stirring solid materials such as glass beads), freeze-thawing method (freezing / thawing) For example, by crushing once or more).
 その他の栄養
 本発明に用いる液体培地には、炭素源又は窒素源の他に、硫酸塩及びリン酸塩を添加し含有させることができる。これらの無機塩類を併用することにより、酵素活性が増強される。
Other Nutrition The liquid medium used in the present invention may contain sulfate and phosphate in addition to the carbon source or nitrogen source. Enzyme activity is enhanced by using these inorganic salts in combination.
 例えば、硫酸塩としては硫酸カルシウム、硫酸マグネシウム7水和物、硫酸鉄7水和物、硫酸アンモニウムなどを用いることができ、特に硫酸マグネシウム7水和物が好ましい。リン酸塩としてはリン酸2水素カリウム、リン酸アンモニウムなどを用いることができ、特にリン酸2水素カリウムが好ましい。これらの無機塩類は、単独で用いることもでき、2種以上を組み合わせて用いることもできる。 For example, as the sulfate, calcium sulfate, magnesium sulfate heptahydrate, iron sulfate heptahydrate, ammonium sulfate and the like can be used, and magnesium sulfate heptahydrate is particularly preferable. As the phosphate, potassium dihydrogen phosphate, ammonium phosphate or the like can be used, and potassium dihydrogen phosphate is particularly preferable. These inorganic salts can be used alone or in combination of two or more.
 また、液体培地における上記の無機塩類の濃度は、麹菌培養物中にデンプン分解酵素や食物繊維分解酵素、タンパク分解酵素などの酵素が選択的に生成、蓄積される程度のものに調整される。例えば、硫酸塩の場合は0.01~0.5%(w/vo1)、好ましくは0.02~0.2%(w/vo1)、リン酸塩の場合は0.05~1.0%(w/vo1)、好ましくは0.1~0.8%(w/vol)とする。 Also, the concentration of the above-mentioned inorganic salts in the liquid medium is adjusted to such a level that enzymes such as amylolytic enzymes, dietary fiber degrading enzymes, and proteolytic enzymes are selectively generated and accumulated in the koji mold culture. For example, in the case of sulfate, 0.01 to 0.5% (w / vo1), preferably 0.02 to 0.2% (w / vo1), and in the case of phosphate, 0.05 to 1.0. % (W / vo1), preferably 0.1 to 0.8% (w / vol).
 液体培地には、前述の窒素源や無機塩類以外の有機物や無機塩類等も、栄養源として適宜添加することができる。これらの添加物は麹菌の培養に一般に使用されているものであれば特に限定はないが、有機物としては小麦麩、コーンスティープリカー、大豆粕、脱脂大豆等を、無機塩類としてはアンモニウム塩、カリウム塩、カルシウム塩、マグネシウム塩等の水溶性の化合物を挙げることができ、2種類以上の有機物及び/又は無機塩類を同時に使用してもよい。 In the liquid medium, organic substances and inorganic salts other than the aforementioned nitrogen sources and inorganic salts can be added as nutrient sources as appropriate. These additives are not particularly limited as long as they are generally used for culturing koji molds, but organic substances such as wheat koji, corn steep liquor, soybean koji, defatted soybeans, etc., and inorganic salts such as ammonium salt and potassium Water-soluble compounds such as salts, calcium salts and magnesium salts can be mentioned, and two or more kinds of organic substances and / or inorganic salts may be used simultaneously.
 これらの添加量は麹菌の増殖を促進する程度であれば特に限定はないが、有機物としては0.1~5%(w/vo1)程度、無機塩類としては0.1~1%(w/vo1)程度添加するのが好ましい。 The amount of these additives is not particularly limited as long as it promotes the growth of Neisseria gonorrhoeae, but is about 0.1 to 5% (w / vo1) for organic substances, and 0.1 to 1% (w / vo1) for inorganic salts. It is preferable to add about vo1).
 上限値を超えてこれらの栄養源を添加した場合は、麹菌の増殖を阻害するため好ましくない。また、添加量が下限値未満である場合は、酵素生産が促されないため、やはり好ましくない。 If these nutrient sources are added in excess of the upper limit, the growth of koji mold is inhibited, which is not preferable. Moreover, when the addition amount is less than the lower limit, enzyme production is not promoted, which is also not preferable.
 上記の培養原料及び窒素源を水と混合することにより得られる麹菌の液体培地は、必要に応じて滅菌処理を行なってもよく、処理方法には特に限定はない。例としては、高温高圧滅菌法を挙げることができ、121℃で15分間行なえばよい。 The liquid medium of Aspergillus obtained by mixing the above-mentioned culture raw material and nitrogen source with water may be sterilized as necessary, and the treatment method is not particularly limited. As an example, a high-temperature and high-pressure sterilization method can be mentioned, which may be performed at 121 ° C. for 15 minutes.
 液体麹の製造
 滅菌した液体培地を培養温度まで冷却後、白麹菌及び/又は黒麹菌を液体培地に接種する。培地に接種する麹菌の形態は任意であり、胞子又は菌糸を用いることができる。
Manufacture of liquid koji After cooling the sterilized liquid medium to the culture temperature, inoculate white koji mold and / or black koji mold on the liquid medium. The form of the koji mold inoculated into the medium is arbitrary, and spores or hyphae can be used.
 麹菌の液体培地への接種量には特に制限はないが、液体培地1ml当り、胞子であれば1×10~1×10個程度、菌糸であれば前培養液を0.1~10%程度接種することが好ましい。 There is no particular limitation on the amount of koji mold inoculated into the liquid medium, but about 1 × 10 4 to 1 × 10 6 spores per 1 ml of the liquid medium, and 0.1 to 10 of the preculture solution for mycelia. It is preferable to inoculate about 1%.
 麹菌の培養温度は、生育に影響を及ぼさない限りであれば特に限定はないが、好ましくは25~45℃、より好ましくは30~40℃で行なうのがよい。培養温度が低いと、麹菌の増殖が遅くなるため雑菌による汚染が起きやすくなる。培養時間は24~120時間が適当である。 The culture temperature of Aspergillus is not particularly limited as long as it does not affect the growth, but it is preferably 25 to 45 ° C, more preferably 30 to 40 ° C. When the culture temperature is low, the growth of Aspergillus is delayed, and contamination with various bacteria is likely to occur. The culture time is suitably 24 to 120 hours.
 本発明で用いる麹菌としては、グルコアミラーゼ、耐酸性α-アミラーゼ、α-アミラーゼなどのデンプン分解酵素、セルラーゼ、β-グルコシダーゼ、キシラナーゼなどの食物繊維分解酵素等の生産能を有する麹菌が好ましい。具体的には、白麹菌としてはアスペルギルス・カワチ(Aspergillus kawachii)等、黒麹菌としてはアスペルギルス・アワモリ(Aperigillus awamori)又はアスペルギルス・ニガー(Aspergillus niger)等が挙げられる。 As the koji mold used in the present invention, koji mold having an ability to produce starch-degrading enzymes such as glucoamylase, acid-resistant α-amylase and α-amylase, and dietary fiber degrading enzymes such as cellulase, β-glucosidase and xylanase are preferable. Specifically, Aspergillus kawachii and the like are Aspergillus or aspergillus niger and Aspergillus niger and the like are Aspergillus awachi and Aspergillus niger .
 白麹菌としてはアスペルギルス・カワチが好ましい。黒麹菌としてはアスペルギルス・アワモリが好ましい。これらを用いることにより、デンプン分解酵素及び食物繊維分解酵素が高生産されるからである。 As Aspergillus oryzae, Aspergillus kawachi is preferable. Aspergillus niger is preferably Aspergillus awamori. This is because by using these, starch-degrading enzymes and dietary fiber-degrading enzymes are highly produced.
 これらの麹菌は1種類の菌株による培養、又は同種若しくは異種の2種類以上の菌株による混合培養のどちらでも用いることができる。これらは胞子又は前培養により得られる菌糸のいずれの形態のものを用いても問題はないが、菌糸を用いる方が対数増殖期に要する時間が短くなるので好ましい。 These koji molds can be used either by culturing with one type of strain or by mixed culturing with two or more types of strains of the same or different types. There is no problem with using any form of spores or hyphae obtained by preculture, but it is preferable to use hyphae because the time required for the logarithmic growth phase is shortened.
 培養装置は、液体培養を行なうことができるものであればよいが、麹菌は好気培養を行なう必要があるので、酸素や空気を培地中に供給できる好気的条件下で行なう必要がある。また、培養中は培地中の原料、酸素、及び麹菌が装置内に均一に分布するように撹拌をするのが好ましい。撹拌条件や通気量については、培養環境を好気的に保つことができる条件であればいかなる条件でもよく、培養装置、培地の粘度等により適宜選択すればよい。 The culture apparatus may be any apparatus that can perform liquid culture. However, since Neisseria gonorrhoeae needs to perform aerobic culture, it needs to be performed under aerobic conditions in which oxygen and air can be supplied into the medium. Moreover, it is preferable to stir so that the raw material, oxygen, and koji mold in the medium are uniformly distributed in the apparatus during the culture. The stirring conditions and the aeration amount may be any conditions as long as the culture environment can be maintained aerobically, and may be appropriately selected depending on the culture apparatus, the viscosity of the medium, and the like.
 上記の培養法で培養することにより、デンプンを分解するデンプン分解酵素及び食物繊維及びヘミセルロースを分解する食物繊維分解酵素などの酵素活性を有する液体麹が得られる。 By culturing by the above culture method, a liquid koji having enzyme activity such as starch-degrading enzyme that degrades starch and dietary fiber-degrading enzyme that degrades dietary fiber and hemicellulose can be obtained.
 ここでいう液体麹には、液体培養した培養物そのもの、培養物の上清液、培養物を濾過又は遠心分離等することにより得られる清澄液、それらの濃縮物等が含まれる。又、液体麹の乾燥物等も液体麹の同等物であり、酵素源として同様に使用することができる。 Here, the liquid koji includes a liquid culture itself, a culture supernatant, a clarified liquid obtained by filtering or centrifuging the culture, a concentrate thereof, and the like. Also, dried liquid koji is equivalent to liquid koji and can be used as an enzyme source as well.
 本発明の液体麹は、未濃縮の状態で、例えば、次に示す酵素活性を示すことが好ましい。各酵素活性の測定は実施例に説明する方法に準じて行なわれる。 The liquid cake of the present invention preferably exhibits, for example, the following enzyme activity in an unconcentrated state. Each enzyme activity is measured according to the method described in the examples.
 耐酸性α-アミラーゼ(ASAA)活性については、16U/ml以上、好ましくは18U/ml以上、より好ましくは20U/ml以上、更に好ましくは23U/ml以上。
 グルコアミラーゼ(GA)活性については、45U/ml以上、好ましくは50U/ml以上、より好ましくは60U/ml以上、更に好ましくは70U/ml以上。
 β-グルカナーゼ(BG)活性については、0.15U/ml以上、好ましくは0.20U/ml以上、より好ましくは0.80U/ml以上、更に好ましくは1.0U/ml以上。
 キシラナーゼ(XY)活性については、0.20U/ml以上、好ましくは0.28U/ml以上、より好ましくは0.30U/ml以上、更に好ましくは0.40U/ml以上。
The acid-resistant α-amylase (ASAA) activity is 16 U / ml or more, preferably 18 U / ml or more, more preferably 20 U / ml or more, and further preferably 23 U / ml or more.
About glucoamylase (GA) activity, it is 45 U / ml or more, Preferably it is 50 U / ml or more, More preferably, it is 60 U / ml or more, More preferably, it is 70 U / ml or more.
The β-glucanase (BG) activity is 0.15 U / ml or more, preferably 0.20 U / ml or more, more preferably 0.80 U / ml or more, and further preferably 1.0 U / ml or more.
The xylanase (XY) activity is 0.20 U / ml or more, preferably 0.28 U / ml or more, more preferably 0.30 U / ml or more, and further preferably 0.40 U / ml or more.
 本発明の製造方法で得られた液体麹は、焼酎、清酒、しょうゆ、味噌、みりん及び甘酒等の発酵飲食品を製造するための酵素源として固体麹と同様に用いることができる。 The liquid koji obtained by the production method of the present invention can be used in the same manner as solid koji as an enzyme source for producing fermented foods and drinks such as shochu, sake, soy sauce, miso, mirin and amazake.
 また、得られた液体麹の一部を次の液体麹製造におけるスターターとして用いることもできる。このように液体麹を連続的に製造することにより、安定的な生産が可能になると同時に、生産効率の向上も図ることができる。 Also, a part of the obtained liquid soot can be used as a starter in the next liquid soot production. Thus, by continuously producing the liquid soot, stable production is possible, and at the same time, production efficiency can be improved.
 また、本発明の液体麹は、その高い酵素活性から、酵素製剤、並びに消化剤などの医薬品などとしての利用も可能である。この場合、得られた麹菌培養物を所望の程度に濃縮・精製し、適当な賦形剤、増粘剤、甘味料などを添加して常法により製剤化すればよい。 Moreover, the liquid koji of the present invention can be used as a pharmaceutical preparation such as an enzyme preparation and a digestive agent because of its high enzyme activity. In this case, the obtained koji mold culture may be concentrated and purified to a desired degree, and an appropriate excipient, thickener, sweetener and the like may be added to prepare a preparation by a conventional method.
 糖化原料の糖化
 本発明の液体麹を用いて糖化原料を糖化する際には、糖化原料に対し本発明の液体麹に含まれるデンプン分解酵素及び食物繊維分解酵素を作用させる。例えば、糖化原料は、必要に応じて前処理を行った後に、糖化原料が浸漬するのに十分な量の液体麹を含む水の中に投入され、酵素が作用するのに適当な温度で静置又は必要に応じて振盪あるいは攪拌される。糖化原料の前処理としては、一般に洗浄、粉砕、加熱、アルカリ処理などの操作が行われる。
Saccharification of saccharification raw material When the saccharification raw material is saccharified using the liquid koji of the present invention, the amylolytic enzyme and dietary fiber degrading enzyme contained in the liquid koji of the present invention are allowed to act on the saccharification raw material. For example, the saccharified raw material is pretreated as necessary, and then poured into water containing a sufficient amount of liquid soot for the saccharified raw material to be immersed, and statically maintained at a temperature suitable for the enzyme to act. Or shaken or agitated as necessary. As pretreatment of the saccharification raw material, operations such as washing, pulverization, heating, and alkali treatment are generally performed.
 本発明の液体麹にはデンプン分解酵素及び食物繊維分解酵素が多く含まれている。つまり、この液体麹は、糖化原料に含まれるデンプンの分解力に優れると共に繊維質の分解力にも優れている。それゆえ、糖化原料が繊維質を多く含んでいる場合でも、糖化の過程中繊維質が固形分として残存することがなく、糖化の進行が促進される。 The liquid koji of the present invention is rich in starch degrading enzymes and dietary fiber degrading enzymes. That is, this liquid koji is excellent in the decomposing power of starch contained in the saccharification raw material and also in the decomposing power of the fiber. Therefore, even when the saccharification raw material contains a large amount of fiber, the fiber does not remain as a solid content during the saccharification process, and the progress of saccharification is promoted.
 従来の液体麹では糖化が困難であった、又は糖化効率が低かった、繊維質を多く含む糖化原料には、繊維質を多く含む穀類又は繊維質を多く含む芋類が含まれ、具体的には、穀類として、小麦、大麦、トウモロコシ及び稗など、また、芋類として、キャッサバ、サツマイモ及びジャガイモなどである。 The saccharification raw material rich in fiber, which has been difficult to saccharify with conventional liquid koji, or has low saccharification efficiency, includes cereals rich in fiber or potatoes rich in fiber, specifically Are wheat, barley, corn, and straw as cereals, and cassava, sweet potato, and potato as potatoes.
 繊維質を多く含む糖化原料を糖化して得られた糖化液は、例えば、酵母を用いてアルコール発酵させ、要すれば蒸留して、焼酎のようなアルコール飲料又はバイオエタノールを製造するのに利用される。 A saccharified solution obtained by saccharifying a saccharified raw material containing a large amount of fiber is used to produce alcoholic beverages such as shochu or bioethanol by, for example, fermenting alcohol using yeast and, if necessary, distilling it. Is done.
 以下、本発明を実施例によってより具体的に説明するが、本発明はこれらの実施例に限定されるものではない。 Hereinafter, the present invention will be described more specifically by way of examples. However, the present invention is not limited to these examples.
 実施例1
 液体麹の製造
 1.麹菌
 菌株として、白麹菌に関する標準株であるアスペルギルス・カワチ(NBRC4308株)、及び黒麹菌に関する標準株であるアスペルギルス・アワモリ(NBRC4388株)を準備した。
Example 1
Manufacture of liquid cake Aspergillus oryzae strains, Aspergillus kawachi (NBRC4308 strain), which is a standard strain related to white mold, and Aspergillus awamori (NBRC4388 strain), which is a standard strain related to Aspergillus niger, were prepared.
 2.前培養方法
 65%精白大麦8%(w/v)、KNO0.2%(w/v)、KHPO0.3%(w/v)の組成を有する前培養培地100mlを、容量500mlのバッフル付三角フラスコに入れ、121℃、15分間オートクレーブ滅菌し、室温冷却後、麹菌の胞子1白金耳を接種した。その後、温度37℃、100rpmにて24時間回転振盪培養を行った。
2. Preculture method 100 ml of a preculture medium having a composition of 65% refined barley 8% (w / v), KNO 3 0.2% (w / v), KH 2 PO 4 0.3% (w / v), It put into the conical flask with a capacity | capacitance of 500 ml with a baffle, autoclaved at 121 degreeC for 15 minutes, and inoculated the spore 1 platinum ear of the koji mold after cooling at room temperature. Thereafter, rotary shaking culture was performed at a temperature of 37 ° C. and 100 rpm for 24 hours.
 3.繊維質を含む基質
 繊維質を含む基質として、ビートファイバー(甜菜由来:日本甜菜製糖社製)、ダイコン(切干大根)準備した。ダイコンについては、使用する前に粉砕処理を行った。
3. Substrate containing fiber As a substrate containing fiber, beet fiber (derived from sugar beet: manufactured by Nippon Sugar Sugar Co., Ltd.) and Japanese radish (cut dried radish) were prepared. The radish was pulverized before use.
 また、対照例として、スターチ(溶性デンプン)を準備した。 Moreover, starch (soluble starch) was prepared as a control example.
 4.本培養方法
 精白歩合が98%の大麦2.0%(w/v)、KNO0.4%(w/v)、KHPO0.6%(w/v)、繊維質を含む基質0.5%(w/v)の組成を有する本培養培地(pH無調整)100mlを、500ml容のバッフル付三角フラスコに入れ、121℃、15分間オートクレーブ滅菌し、室温冷却後、前培養液を2ml接種した。その後、37℃、100rpmにて72時間回転振盪培養を行った。
4). Main culture method 98% barley 2.0% (w / v), KNO 3 0.4% (w / v), KH 2 PO 4 0.6% (w / v), including fiber 100 ml of a main culture medium (pH unadjusted) having a composition of 0.5% (w / v) substrate is put into a 500 ml baffled Erlenmeyer flask, autoclaved at 121 ° C. for 15 minutes, cooled to room temperature, and pre-cultured 2 ml of the liquid was inoculated. Then, the rotation shaking culture was performed at 37 degreeC and 100 rpm for 72 hours.
 5.酵素活性の測定
 本培養を行った培養液から遠心分離により得た培養上清液を液体麹試料として、酵素活性を測定した。測定方法は次の通りである。
5. Measurement of enzyme activity Enzyme activity was measured using a culture supernatant obtained by centrifugation from the culture medium in which main culture was performed, as a liquid sputum sample. The measuring method is as follows.
 耐酸性α-アミラーゼ(ASAA)活性:
 培養上清液1mlに100mM酢酸緩衝液(pH3)9mlを添加して37℃で1時間酸処理を行なった後に、α-アミラーゼ測定キット(キッコーマン製)を用いて測定した。
Acid-resistant α-amylase (ASAA) activity:
After 9 ml of 100 mM acetate buffer (pH 3) was added to 1 ml of the culture supernatant and acid treatment was performed at 37 ° C. for 1 hour, the measurement was performed using an α-amylase measurement kit (manufactured by Kikkoman).
 グルコアミラーゼ(GA)活性:
 国税庁所定分析法に従い測定した。具体的には、デンプン溶液1mlに0.2M酢酸緩衝液0.2mlを加え、40℃で5分間予熱した。これに培養上清液0.1mlを加え、40℃で20分間反応させ、1N水酸化ナトリウム溶液0.1mlを添加して反応を停止させた。その後30分間放置し、1N塩酸溶液0.1mlを加えて中和した。別に対照として、デンプン溶液1mlに0.2M酢酸緩衝液0.2mlを加え、40℃で5分間予熱し、1N水酸化ナトリウム溶液0.1mlを加えた後に培養上清液0.1mlを添加し、以下上記と同様に操作した。反応液中に生成したグルコース量はグルコースCII-テストワコー(和光純薬製)を用いて測定した。
Glucoamylase (GA) activity:
Measured according to the National Tax Agency prescribed analysis method. Specifically, 0.2 ml of 0.2 M acetate buffer was added to 1 ml of starch solution and preheated at 40 ° C. for 5 minutes. To this, 0.1 ml of the culture supernatant was added and reacted at 40 ° C. for 20 minutes, and 0.1 ml of 1N sodium hydroxide solution was added to stop the reaction. Thereafter, the mixture was allowed to stand for 30 minutes and neutralized by adding 0.1 ml of 1N hydrochloric acid solution. As a control, add 0.2 ml of 0.2 M acetate buffer to 1 ml of starch solution, preheat at 40 ° C. for 5 minutes, add 0.1 ml of 1N sodium hydroxide solution, and then add 0.1 ml of culture supernatant. Thereafter, the same operation as described above was performed. The amount of glucose produced in the reaction solution was measured using Glucose CII-Test Wako (manufactured by Wako Pure Chemical Industries).
 グルコアミラーゼ活性は、可溶性デンプンから40℃で60分間に1mgのブドウ糖を生成する活性を1単位として表した。 The glucoamylase activity was expressed with 1 unit of activity to produce 1 mg of glucose from soluble starch at 40 ° C. for 60 minutes.
 β-グルカナーゼ(BG)活性:
 β-グルカナーゼ活性は、メガザイム社製のβ‐グルカナーゼ測定キットを用い、色素標識したβ-グルカンを基質とした酵素分解によって生じた染色断片を吸光度測定した。具体的には、アゾ大麦グルカン基質溶液0.5mlに培養上清液0.5mlを加えて、40℃にて正確に10分間酵素反応を行なわせた後、停止液〔4%酢酸ナトリウム、0.4%酢酸亜鉛、80%メチルセルソルブを含む(pH5)〕3.0mlを加えて5分放置し、反応を停止した。続いて遠心分離した後、上澄液を590nmの吸光度測定した。
β-glucanase (BG) activity:
The β-glucanase activity was determined by measuring the absorbance of a stained fragment produced by enzymatic degradation using β-glucan labeled with a dye, using a β-glucanase measurement kit manufactured by Megazyme. Specifically, 0.5 ml of the culture supernatant was added to 0.5 ml of the azo barley glucan substrate solution, and the enzyme reaction was carried out at 40 ° C. for exactly 10 minutes, and then the stop solution [4% sodium acetate, 0% .4% zinc acetate and 80% methyl cellosolve (pH 5)] 3.0 ml was added and left for 5 minutes to stop the reaction. Subsequently, after centrifugation, the absorbance of the supernatant was measured at 590 nm.
 1単位のβ-グルカナーゼ活性は、40℃、10分間の反応条件下で、1分間に1μmolのグルコースに相当する還元糖を生成する酵素量として表した。 1 unit of β-glucanase activity was expressed as the amount of enzyme that produces reducing sugar corresponding to 1 μmol of glucose per minute under the reaction conditions of 40 ° C. and 10 minutes.
 キシラナーゼ(XY)活性:
 キシラナーゼ活性は、メガザイム社製のキシラナーゼ測定キットを用い、アゾ-キシランを基質とした酵素分解によって生じた染色断片を吸光度測定した。より具体的には1%アゾ-キシラン基質溶液(メガザイム社製)0.5mlに培養上清液0.5mlを加えて、40℃にて正確に10分間酵素反応を行なわせた後、停止液〔エタノール(95%v/v)〕2.5mlを加えてよく混合し、反応を停止した。続いて遠心分離した後、上澄液を590nmの吸光度測定した。
Xylanase (XY) activity:
The xylanase activity was determined by measuring the absorbance of a stained fragment produced by enzymatic degradation using azo-xylan as a substrate, using a xylanase measurement kit manufactured by Megazyme. More specifically, 0.5 ml of the culture supernatant was added to 0.5 ml of 1% azo-xylan substrate solution (manufactured by Megazyme), and the enzyme reaction was performed at 40 ° C. for exactly 10 minutes. [Ethanol (95% v / v)] 2.5 ml was added and mixed well to stop the reaction. Subsequently, after centrifugation, the absorbance of the supernatant was measured at 590 nm.
 1単位のキシラナーゼ活性は、40℃、10分間の反応条件下で、1分間に1μmolのグルコースに相当する還元糖を生成する酵素量として表した。 1 unit of xylanase activity was expressed as the amount of enzyme that produces reducing sugar corresponding to 1 μmol of glucose per minute under the reaction conditions of 40 ° C. and 10 minutes.
 6.測定結果
 アスペルギルス・カワチを用いた液体麹試料についてのBG活性(U/ml)およびXY活性(U/ml)を図1および図2に示す。また、アスペルギルス・アワモリを用いた液体麹試料についてのBG活性(U/ml)およびXY活性(U/ml)を図3および図4に示す。
6). Measurement Results FIG. 1 and FIG. 2 show BG activity (U / ml) and XY activity (U / ml) for a liquid sputum sample using Aspergillus kawachi. In addition, FIG. 3 and FIG. 4 show the BG activity (U / ml) and XY activity (U / ml) of the liquid sputum sample using Aspergillus awamori.
 これらの結果により、アスペルギルス・カワチ及びアスペルギルス・アワモリを用いた液体麹試料のいずれについても、食物繊維分解酵素活性であるBG活性及びXY活性が高まることが判明した。 From these results, it was found that BG activity and XY activity, which are dietary fiber degrading enzyme activities, were increased in both liquid aspergillus samples using Aspergillus kawachi and Aspergillus awamori.
 次に、アスペルギルス・カワチを用いた液体麹試料についてのASAA活性(U/ml)およびGA活性(U/ml)を図5および図6に示す。また、アスペルギルス・アワモリを用いた液体麹試料についてのASAA活性(U/ml)およびGA活性(U/ml)を図7および図8に示す。 Next, ASAA activity (U / ml) and GA activity (U / ml) for the liquid sputum sample using Aspergillus kawachi are shown in FIG. 5 and FIG. Moreover, the ASAA activity (U / ml) and GA activity (U / ml) about the liquid sputum sample using Aspergillus awamori are shown in FIG. 7 and FIG.
 これらの結果により、アスペルギルス・カワチ及びアスペルギルス・アワモリを用いた液体麹試料のいずれについても、デンプン分解酵素活性であるASAA活性及びGA活性が高まることが判明した。 From these results, it was found that ASAA activity and GA activity, which are amylolytic enzyme activities, were increased in both liquid aspergillus samples using Aspergillus kawachi and Aspergillus awamori.
 以上より、繊維質を含む基質を炭素源として一部添加することで、食物繊維分解酵素活性が高まり、デンプン分解酵素活性についても同時に高まることが確認された。 From the above, it was confirmed that dietary fiber-degrading enzyme activity increased and starch-degrading enzyme activity increased at the same time by partially adding a substrate containing fiber as a carbon source.
 実施例2
 小麦の糖化
 無蒸煮で粉砕した小麦1.0g、100mM酢酸緩衝液(pH4.0)45ml、液体麹試料5.0mlを100ml容三角フラスコに入れ、37℃、100rpmの往復振盪下にて糖化を行った(n=2)。4時間後、上清液のグルコース濃度をグルコース測定キット(CII-テストワコー:和光純薬社製)により測定した。
Example 2
Saccharification of wheat 1.0 g of wheat crushed without steam, 45 ml of 100 mM acetate buffer (pH 4.0) and 5.0 ml of liquid koji sample are placed in a 100 ml Erlenmeyer flask and saccharified under reciprocal shaking at 37 ° C. and 100 rpm. Performed (n = 2). After 4 hours, the glucose concentration of the supernatant was measured with a glucose measurement kit (CII-Test Wako: Wako Pure Chemical Industries, Ltd.).
 小麦1.0g中の総でんぷん量に対して生成したダルコースの割合を糖化率として、アスペルギルス・カワチを用いた液体麹試料に関する結果を図9に、アスペルギルス・アワモリを用いた液体麹試料に関する結果を図10に示す。 FIG. 9 shows the results for a liquid koji sample using Aspergillus kawachi as a saccharification ratio, and the results for a liquid koji sample using Aspergillus awamori. As shown in FIG.
 このように、アスペルギルス・カワチおよびアスペルギルス・アワモリのいずれについても、繊維質を含む基質を一部添加して培養された液体麹を用いた場合は、繊維質を多く含む穀類の糖化速度が速まることが認められた。 In this way, for both Aspergillus kawachi and Aspergillus awamori, saccharification rate of cereals rich in fiber is increased when using liquid koji cultivated with some fiber-containing substrate added. Was recognized.
 実施例3
 キャッサバの糖化
 乾燥させ無蒸煮のまま粉砕したキャッサバ1.0g、100mM酢酸緩衝液(pH4.0)45ml、液体麹試料5.0mlを100ml容三角フラスコに入れ、37℃、100rpmの往復振盪下にて糖化を行った(n=2)。4時間後、上清液のグルコース濃度をグルコース測定キット(CII-テストワコー:和光純薬社製)により測定した。
Example 3
Saccharification of cassava 1.0 g of cassava, dried and crushed without cooking, 45 ml of 100 mM acetate buffer (pH 4.0), and 5.0 ml of liquid koji sample are placed in a 100 ml Erlenmeyer flask and reciprocally shaken at 37 ° C. and 100 rpm. Then, saccharification was performed (n = 2). After 4 hours, the glucose concentration of the supernatant was measured with a glucose measurement kit (CII-Test Wako: Wako Pure Chemical Industries, Ltd.).
 キャッサバ1.0g中の総でんぷん量に対して生成したダルコースの割合を糖化率として、アスペルギルス・カワチを用いた液体麹試料に関する結果を図11に、アスペルギルス・アワモリを用いた液体麹試料に関する結果を図12に示す。 FIG. 11 shows the results for the liquid koji sample using Aspergillus kawachi as the saccharification rate, and the results for the liquid koji sample using Aspergillus awamori as the saccharification rate with respect to the total starch amount in 1.0 g of cassava. As shown in FIG.
 このように、アスペルギルス・カワチおよびアスペルギルス・アワモリのいずれについても、繊維質を含む基質を一部添加して培養された液体麹を用いた場合は、繊維質を多く含む芋類の糖化速度が速まることが認められた。 Thus, for both Aspergillus kawachi and Aspergillus awamori, saccharification rate of potatoes rich in fiber increases when using liquid cocoons cultured with a part of the substrate containing fiber added. It was recognized that
 本発明によれば、繊維質を多く含む糖化原料について、焼酎等の発酵飲食品又はバイオエタノール等の製造に利用することが促進される。 According to the present invention, use of a saccharified raw material containing a large amount of fiber for the production of fermented foods and beverages such as shochu or bioethanol is promoted.

Claims (9)

  1.  穀粒表面の全部又は一部が穀皮で覆われた穀類及び繊維質を含む基質を含有する炭素源を含有する液体培地を用いて、白麹菌又は黒麹菌を培養する工程を包含する、デンプン分解酵素活性及び食物繊維分解酵素活性が増強された液体麹の製造方法。 Starch comprising culturing white or black koji molds using a liquid medium containing a carbon source containing a substrate containing cereals and fibers, all or part of the grain surface covered with husks A method for producing liquid koji with enhanced degrading enzyme activity and dietary fiber degrading enzyme activity.
  2.  前記デンプン分解酵素が少なくとも耐酸性α-アミラーゼ及びグルコアミラーゼであり、前記食物繊維分解酵素が少なくともβ-グルカナーゼ及びキシラナーゼである請求項1に記載の液体麹の製造方法。 2. The method for producing liquid koji according to claim 1, wherein the starch degrading enzyme is at least acid-resistant α-amylase and glucoamylase, and the dietary fiber degrading enzyme is at least β-glucanase and xylanase.
  3.  前記繊維質を含む基質がビートファイバー及び大根からなる群から選択される少なくとも一種である請求項1又は2に記載の液体麹の製造方法。 The method for producing a liquid koji according to claim 1 or 2, wherein the substrate containing fiber is at least one selected from the group consisting of beet fiber and radish.
  4.  前記繊維質を含む基質がビートファイバーである請求項1又は2に記載の液体麹の製造方法。 The method for producing a liquid koji according to claim 1 or 2, wherein the substrate containing fiber is beet fiber.
  5.  前記白麹菌がアスペルギルス・カワチであり、前記黒麹菌がアスペルギルス・アワモリである請求項1~4のいずれかに記載の液体麹の製造方法。 The method for producing a liquid koji according to any one of claims 1 to 4, wherein the white koji mold is Aspergillus kawachi and the black koji mold is Aspergillus awamori.
  6.  前記穀粒表面の全部又は一部が穀皮で覆われた穀類が、玄米、籾殻が全部又は一部付いている米又は未精白から精白歩合92%以上の大麦若しくは小麦である請求項1~5のいずれかに記載の液体麹の製造方法。 The cereal in which all or part of the grain surface is covered with husk is brown rice, rice with all or part of rice husks, or barley or wheat having an unpolished to polished ratio of 92% or more. 6. A method for producing a liquid basket according to any one of 5 above.
  7.  請求項1~6のいずれかに記載の方法により製造された液体麹。 A liquid bottle produced by the method according to any one of claims 1 to 6.
  8.  繊維質の穀類又は繊維質の芋類に対し、請求項7記載の液体麹に含まれるデンプン分解酵素及び食物繊維分解酵素を作用させる工程を包含する、繊維質の穀類又は繊維質の芋類の糖化方法。 A fiber cereal or a fiber cocoon comprising a step of allowing the starch degrading enzyme and the dietary fiber degrading enzyme contained in the liquid cocoon to act on the fiber cereal or the fiber cocoon. Saccharification method.
  9.  前記繊維質の穀類が小麦、大麦、トウモロコシ又は稗であり、前記繊維質の芋類がキャッサバ、サツマイモ又はジャガイモである請求項8に記載の繊維質の穀類又は繊維質の芋類の糖化方法。 The method for saccharification of fibrous cereals or fibrous cocoons according to claim 8, wherein the fibrous cereals are wheat, barley, corn or potatoes, and the fibrous cereals are cassava, sweet potato or potato.
PCT/JP2010/067894 2010-10-12 2010-10-12 Method for manufacturing liquid malt enhanced in starch-degrading enzyme activity and dietary fiber-degrading enzyme activity WO2012049737A1 (en)

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CN103773648A (en) * 2012-10-18 2014-05-07 柳州市京阳节能科技研发有限公司 Liquid state raw material quick-acting distillation-free brewed wine

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