WO2007116772A1 - Process for producing powdery soy milk and application of the same - Google Patents

Process for producing powdery soy milk and application of the same Download PDF

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Publication number
WO2007116772A1
WO2007116772A1 PCT/JP2007/056503 JP2007056503W WO2007116772A1 WO 2007116772 A1 WO2007116772 A1 WO 2007116772A1 JP 2007056503 W JP2007056503 W JP 2007056503W WO 2007116772 A1 WO2007116772 A1 WO 2007116772A1
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WO
WIPO (PCT)
Prior art keywords
suspension
soy milk
soymilk
steam
beans
Prior art date
Application number
PCT/JP2007/056503
Other languages
French (fr)
Japanese (ja)
Inventor
Masanobu Yanagisawa
Takaya Koseki
Atsushi Yura
Takashi Nishimura
Original Assignee
Fuji Oil Company, Limited
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Publication date
Application filed by Fuji Oil Company, Limited filed Critical Fuji Oil Company, Limited
Priority to JP2007545480A priority Critical patent/JP4605226B2/en
Publication of WO2007116772A1 publication Critical patent/WO2007116772A1/en

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Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23CDAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C11/00Milk substitutes, e.g. coffee whitener compositions
    • A23C11/02Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins
    • A23C11/10Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing or not lactose but no other milk components as source of fats, carbohydrates or proteins
    • A23C11/103Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing or not lactose but no other milk components as source of fats, carbohydrates or proteins containing only proteins from pulses, oilseeds or nuts, e.g. nut milk
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L11/00Pulses, i.e. fruits of leguminous plants, for production of food; Products from legumes; Preparation or treatment thereof
    • A23L11/05Mashed or comminuted pulses or legumes; Products made therefrom
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L11/00Pulses, i.e. fruits of leguminous plants, for production of food; Products from legumes; Preparation or treatment thereof
    • A23L11/30Removing undesirable substances, e.g. bitter substances
    • A23L11/31Removing undesirable substances, e.g. bitter substances by heating without chemical treatment, e.g. steam treatment, cooking
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L11/00Pulses, i.e. fruits of leguminous plants, for production of food; Products from legumes; Preparation or treatment thereof
    • A23L11/60Drinks from legumes, e.g. lupine drinks
    • A23L11/65Soy drinks

Definitions

  • the present invention relates to a method for producing soymilk from beans and its application.
  • Patent Documents To 7 describe a method of refining okara fibers by homogenizing means such as a homogenizer from a suspension obtained by adding water to soybean and grinding.
  • Patent Documents 8 to 14 describe a method of refining okara fibers by homogenizing means such as a homogenizer from a suspension obtained by adding water to soybean fine powder.
  • Patent Document 7 discloses a method of homogenizing a suspension and performing high-temperature and high-pressure treatment in a subcritical or critical state.
  • Patent Document 15 discloses a method for degrading okara fibers using a plant tissue-disrupting enzyme.
  • the okara fiber is solubilized and the water-soluble soybean polysaccharide is extracted, so that the viscosity of the soy milk becomes high and the food texture becomes heavy. Further, in Patent Document 15, there is a possibility that it takes time force S for the homogenization process in the liquid.
  • Patent Document 1 Japanese Patent Laid-Open No. 51-41459
  • Patent Document 2 Japanese Patent Publication No. 53-66466
  • Patent Document 3 JP-A 59-210861
  • Patent Document 4 Japanese Patent Application Laid-Open No. 61-119154
  • Patent Document 5 JP-A 61-192256
  • Patent Document 6 Japanese Patent Laid-Open No. 62-11068
  • Patent Document 7 Japanese Patent Laid-Open No. 2002-95433
  • Patent Document 8 Japanese Patent Laid-Open No. 48-26957
  • Patent Document 9 JP-A-60-141247
  • Patent Document 10 Japanese Unexamined Patent Publication No. 63-24868
  • Patent Document 11 JP-A-1-128759
  • Patent Document 12 Japanese Patent Application Laid-Open No. 2003_159020
  • Patent Document 13 Japanese Unexamined Patent Application Publication No. 2004-141155
  • Patent Document 14 Japanese Unexamined Patent Application Publication No. 2004-16120
  • Patent Document 15 JP-A-11-299442
  • An object of the present invention is to provide a soy milk powder that does not have a rough texture, does not increase in viscosity, and has a refreshing mouth, and its application product, despite containing okara.
  • a method for producing fermented soymilk characterized in that the soymilk obtained by the production method described in 1. is fermented by microorganisms,
  • the bean meal of beans is performed "dry", and "direct high-temperature heat treatment with steam", which was conventionally only a sterilization means for the suspension, is performed in a “specific temperature range” and There is a limit to the degree of improvement in the conventional technology due to the combination of what is done at a “specific time”. It has the unique effect of minimizing the rough texture of kala and producing soy milk powder that does not increase in viscosity and has a smooth mouth.
  • % means “% by mass” unless otherwise specified.
  • a suspension containing beans powder obtained by dry-pulverizing beans is prepared, and the heating temperature is at least for the okara content in the suspension. 120 ° C or more
  • the “soy milk powder” obtained by the production method of the present invention is distinguished from ordinary soy milk obtained by completely removing soybean power okara, and broadly means soy milk containing okara (particularly cotyledon cell walls). Is.
  • a suspension (slurry) obtained by pulverizing beans is obtained by removing okara as it is or by removing only a part of it and refining the okara content.
  • the soymilk of the present invention may be obtained by separating a part or all of okara from a suspension, refining it, and then restoring it again. Soymilk also includes soymilk and defatted soymilk that have had okara removed from soymilk, and those that have been fermented during the process.
  • the form of the soy milk can be processed into any form such as liquid, powder or granule.
  • soybean is representative, and as for the variety, yellow soybean, green soybean, black soybean and the like can be used without limitation.
  • 7S globulin-conglycinin 7S globulin-conglycinin
  • 11S globulin glycinin
  • isoflavones saponins
  • nicotianamine nicotianamine
  • lecithin oligosaccharides
  • vitamins It is also possible to use soybeans enriched with certain components in soybeans such as minerals.
  • ⁇ -conglycinin is thought to reduce blood neutral fat and visceral fat and is effective in preventing metabolic syndrome. It is effective to use beans.
  • beans such as red beans, kidney beans, bean paste, flower beans, endo, broad beans, bamboo shoots, lentils, quail beans, raisins, leopard beans, peanuts, etc. can also be used, and these are used at an appropriate ratio. It is also possible to use it in a mixture.
  • the beans may include the outer skin and the hypocotyl part, but it is also possible to use those obtained by removing them.
  • the first feature of the soy milk powder of the present invention is that the above-mentioned beans are dry-ground and used as soy flour in the production of soy milk powder.
  • the dry powder mash is a powder mash method that is pulverized by a dry pulverizer such as a jet type, tornado type, hammer type or cutter type mill without substantially adding water to the beans.
  • the average particle size of the dry-milled bean powder is suitably lOO / im or less, preferably 50 / im or less. Further, if the particle size is too large, the soybean powder may not be completely diffused and dissolved, so that the content of particles having a particle size of 100 ⁇ m or less in the soybean powder is preferably 70% or more.
  • wet mash is a method of pulverizing after adding water to beans, but when using only wet pulverization, the texture is smoother than when using dry pulverization. It is inferior, and the viscosity becomes high and the drinking mouth becomes heavy.
  • the solid content concentration in the suspension is not particularly limited, and may be set to a concentration that those skilled in the art consider optimal in terms of quality. However, if the solids concentration is too high, the viscosity increases due to direct high-temperature heat treatment with steam, and the ability to lower the mouthful of soy milk powder. 20% or less, preferably 15% or less Is appropriate. When emphasizing the richness of soy milk powder, it is appropriate to set the solid content concentration to 2% or more, preferably 4% or more.
  • the temperature of the water to be added here may be room temperature (20 ° C), but 40-60 ° C is desirable to facilitate the preparation of the suspension.
  • the soybean powder suspension can be prepared by any method, for example, for the production of a normal beverage.
  • the melting stirring blade can be rotated at a rotational speed of 40 to 60 mm, for example, using a melting tank or the like.
  • the suspension can be homogenized by a homogenizer or the like if necessary.
  • a homogenizer for example, when using a high-pressure homogenizer, a pressure of 3 to 15 MPa is appropriate.
  • Saccharides can be added to the soybean powder suspension at this stage.
  • the type of saccharide is not particularly limited, and sugar, glucose, maltose, ratatoose, trehalose, oligosaccharide, and the like can be used.
  • various food ingredients and additives added to prepared soymilk and soymilk beverages can also be added.
  • the okara content in the above-mentioned bean powder suspension is subjected to a direct high-temperature heat treatment with steam.
  • a direct high-temperature heat treatment with steam not only when the soybean powder suspension is directly subjected to high-temperature heat treatment by steam, but also when the okara content is once separated from the suspension of soybean flour and then directly subjected to high-temperature heat treatment by steam. included. It is characterized in that the okara content contained in the bean powder suspension is refined by performing such heat treatment under specific conditions.
  • Direct high-temperature heat treatment with steam is a type of UHT sterilization (ultra-high temperature sterilization).
  • UHT sterilization ultra-high temperature sterilization
  • This is a heating method in which the pressure is released to evaporate water in the treatment liquid and cool it.
  • there are a steam injection method in which high-temperature steam is injected into the pipe through which the processing liquid flows, and a steam infusion method in which the processing liquid is injected into the high-temperature steam.
  • VTIS sterilizers Alfa Laval
  • Kureha ultra-high temperature flash sterilizers Kureha Techno Engineering Co., Ltd.
  • infusion systems Iwai Kikai Kogyo Co., Ltd.
  • Etc. Similar sterilizers can also be used.
  • the object of the present invention cannot be achieved under heating conditions that are merely aimed at sterilization as in the prior art. That is, it is important that the heating temperature is at least 120 ° C or higher, more preferably 120 to 165 ° C, and still more preferably 135 to 155. C, most preferably 140. C-155. C power is appropriate.
  • the okara content can be made sufficiently fine, and soy milk can be given a refreshing texture with a low-viscosity mouthfeel without roughness.
  • a typical refinement means of the prior art is a homogenization means such as a homogenizer, but it is difficult to obtain a soy milk powder having a texture as in the present invention, no matter how much the homogenization pressure is increased.
  • the heating temperature is low, it becomes difficult to make the suspension particle size fine by direct high-temperature heat treatment with steam, and the soybean powder suspension after the heat treatment tends to have a rough feeling.
  • the temperature exceeds 165 ° C, the effect of reducing the rough feeling of the soybean powder suspension does not change, but it should be noted that the viscosity of the suspension may increase or the flavor may deteriorate.
  • the heating time be at least 10 seconds, preferably 15 to 80 seconds, more preferably 20 to 70 seconds, and further preferably 20 to 60 seconds.
  • the heating time is short, it will be difficult to make the particle size of the suspension fine by direct high-temperature heat treatment with steam, and there will tend to be a rough feel of the bean powder suspension. If it exceeds 80 seconds, the effect of reducing the rough feeling of the soybean powder suspension will not change, but the viscosity of the suspension may increase or the flavor may deteriorate. So be careful.
  • the effect of refining the okara component is that a constant shear force is applied to the okara particles by direct contact of the okara particles with the high-pressure steam, and this time exceeds 10 seconds. This is thought to be caused by continuous efforts.
  • the heat-treated soybean powder suspension can be homogenized with a homogenizer or the like.
  • a homogenizer for example, when using a high-pressure homogenizer, a pressure of 3 to 15 MPa is appropriate.
  • soybean powder suspension contains protease, peptidase, transglutaminase, dull It is possible to appropriately modify the physical properties and physiological functions of soy milk by adding various enzymes such as decanoic acid decanolase, phytase, amylase, pectinase, and hemicenolase to perform an enzyme reaction.
  • various enzymes such as decanoic acid decanolase, phytase, amylase, pectinase, and hemicenolase to perform an enzyme reaction.
  • the soy milk powder obtained by the above production method is a fine particle having an average particle size of 15 zm or less, and further 12 ⁇ m or less, and has a smooth texture that is extremely difficult to feel roughness. Furthermore, when the solid content concentration of soy milk is 9%, the viscosity at 10 ° C is less than lOOmPa's, and further has a low viscosity property of less than 50mPa's, and has a clean texture. .
  • the manufacturing method of the food / beverage products of this invention mix
  • Soymilk can be used as a raw material for the production of various soymilk products, in the same way as soymilk that does not contain okara obtained by a normal production method. Since it has excellent physical properties as described above, it can be easily handled in the same manner as ordinary soy milk without okara, and it has excellent convenience.
  • the food and drink of the present invention can be produced by mixing the soymilk and normal soymilk in a desired ratio.
  • beverages such as prepared soy milk, soy milk beverages and soft drinks, tofu, pudding, bavaria, jelly, whipped cream, fillings and other fresh confectionery, yogurt, cheese and lactic acid fermented soy milk Fermented foods (see below), Japanese sweets such as dumplings and supper, puffed snacks such as snacks, bakery products such as biscuits, cookies, breads and cakes, seasonings such as chocolate, margarine, spreads and mayonnaise, sauces , Soups, fried foods, seafood paste products, birds and fish products.
  • beverages such as prepared soy milk, soy milk beverages and soft drinks, tofu, pudding, bavaria, jelly, whipped cream, fillings and other fresh confectionery, yogurt, cheese and lactic acid fermented soy milk Fermented foods (see below), Japanese sweets such as dumplings and supper, puffed snacks such as snacks, bakery products such as biscuits, cookies, breads and cakes, seasonings such as chocolate, margarine, spreads and mayonnaise, sauces
  • soymilk for the production of various soymilk products, necessary food ingredients (fruit juice, pulp, vegetables, sugars, fats and oils, dairy products, flours, starches, cacao mass, avian fish products, etc.) and food additives (Minerals, vitamins, emulsifiers, thickening stabilizers, acidulants, flavors, etc.) can be used as appropriate.
  • necessary food ingredients fruit juice, pulp, vegetables, sugars, fats and oils, dairy products, flours, starches, cacao mass, avian fish products, etc.
  • food additives Minerals, vitamins, emulsifiers, thickening stabilizers, acidulants, flavors, etc.
  • non-food products such as chemicals such as stone shampoo and cosmetics such as lotions.
  • One of the methods for producing fermented soymilk of the present invention is a method of fermenting the soymilk obtained by the above method with microorganisms.
  • the other is the method for producing soymilk according to claim 1, further comprising a fermentation step with microorganisms. That is, the fermentation of microorganisms may be carried out as a raw material for fermentation after the soybean milk of the present invention is obtained by being produced by itself or purchased from the outside, or at any stage in the production process of soybean milk. You can do it.
  • the stage of the fermentation process is not particularly limited.
  • the stage is prepared by adding water to soy flour and preparing a suspension of bean flour.
  • the subsequent stage is a stage after the soybean powder suspension is separated into soy milk and okara (in this case, both soy milk and okara can be used as fermentation raw materials).
  • an assimilating saccharide as a nutrient source of microorganisms to the fermentation raw material.
  • glucose, sucrose, maltose, galactose, latatose, roughinose, trehalose, soybean oligosaccharide, furato oligosaccharide and the like can be used.
  • These sugar raw materials may be used alone or in combination of two or more.
  • the microorganism used in the fermentation of the present invention is not particularly limited as long as it is a microorganism generally used in the production of fermented foods.
  • lactic acid bacteria, bifidobacteria, yeast, koji mold, natto Bacteria and tempeh bacteria can be used alone or in appropriate combination
  • lactic acid bacteria are not particularly limited as long as they use bacterial species used in normal yogurt.
  • Lactobacillus casei Lactobacillus plantarum, Ratatobacillus, Helveticas, Lactobacillus bulgaricus, Lactobacillus 'Gasselli, Lactobacillus acidophilus, Lactobacillus' Lattice, Lactobacillus 'Sarivarius' Salinorius, Lact Bacillus 'Galinaram, Lactobacillus' Amyroboras, Lactobacillus 'Brevis' Brevis, Lactobacillus, Fermentum, Lactobacillus.
  • Lactobacillus.Italica Lactobacillus.Raikimani, Ratatobacillus.Power Lubatas, Lactobacillus' Hilgardi, Lactobacillus' Noreteri, Lactobacillus' Pastorianus, Lactobacillus 'Bukneri, Lactobacillus' Cerobiosus, Rata Lactobacillus spp.
  • Lactic acid bacteria of the genus Leuconostoc such as Leuconostoc genus, Leuconostoc mesenteroides Talemorris, Leuconostoc Lactis, etc. can be used without particular limitation.
  • Bifidobacteria include Bifido Batterium 'Bifidum', Bifido Batterium 'Longham', Bifido Batterium 'Infantasies', Bifido Batterium' Breve ', Bifido Bacterium' Addresses, Bif Id Batterium 'Angular Tam, Bifid Batterium' Cate ⁇ uratum Tam, Bifid Batterium 'SyudoCatenyuratum, Bifid Batterium' Dentium, Bifid Batterium 'Globos, Bifid Batterium 'Syudulongum, Bifido Batterium' Kuniki Yuri, Bifido Batterium 'Coelinum, Bifido Batterium, Animalice, Bifido Batterium, Thermophilum, Bifido Batterium, Baum, Bifid Batterium,
  • yeast used for bread fermentation, for example, sourdough used as bread seeds (San Francisco sour seed, laisa spear, panettone, etc.), Hops seed, beer seed Yeasts derived from liquor, fruit (grape fruit, apple fruit, etc.) can be used.
  • Rhizopus Aspergillus' force, Aspergillus genus Aspergillus genus, Monascus' Anca, Monascus perpareus, etc., Monascus genus, Neurospora genus, Rhizopus. You can use the genus without limitation. [0035] As Tempe bacteria, Rhizopus genus such as Rhizopus. Oligosporus, Rhizopus.
  • fermented soymilk fermented with lactic acid bacteria or bifidobacteria is plant-like and exhibits a refreshing sour taste like yogurt, and thus is particularly suitable as a food or drink.
  • the pH decreases due to the production of organic acids such as lactic acid and acetic acid. A feeling. Therefore, in the case of soy milk containing okara, if it is not sufficiently refined to have a high viscosity, a heavy and rough texture will stand out.
  • fermented soymilk fermented with soymilk containing ordinary okara and fermented soymilk with almost no change in physical properties can be produced.
  • a Balta starter can be prepared and added, or it can be added directly to the fermentation raw material with freeze-concentrated bacteria or freeze-dried concentrated bacteria.
  • the amount of microorganism added can be adjusted according to the fermentation temperature and fermentation time.
  • the fermentation temperature is 20 to 50 ° C., 3 to 48 hours, preferably 25 to 45 ° C., and 4 to 24 hours is appropriate because it varies depending on the type of microorganism.
  • the pH of the obtained fermented soy milk powder is not particularly limited because it depends on the type of microorganism, but when fermented with lactobacilli or bifidobacteria, ⁇ 3 ⁇ 5 to 5 ⁇ 5 is preferred. Preferably, ⁇ 4 to 5, more preferably ⁇ 4.2 to 4.7. If the pH immediately after fermentation is less than the desired pH, it can be further adjusted with an organic acid such as lactic acid, citrate, or malic acid, or phosphoric acid.
  • an organic acid such as lactic acid, citrate, or malic acid, or phosphoric acid.
  • the obtained fermented soymilk is solid or already in liquid form, it is not essential, but when it is a liquid type product, it is homogenized by a homogenizer or the like. It is preferable to make it completely liquid. For example, when using a high-pressure homogenizer, a pressure of 3 to 15 MPa is appropriate.
  • the fermented soymilk obtained as described above can be commercialized as a live bacteria type as it is, or the fermentation is stopped by heat sterilization, the biological activity of microorganisms is inactivated, and the sterilization fermentation is performed. It can also be commercialized as soy milk powder. As for the sterilization conditions when it is strong, it is sufficient to treat at the temperature and time to kill the used microorganisms.
  • Soy flour made by dry milling of dehulled and hypocotyled soybean (made by Pelican Co., Ltd., average particle size 15 ⁇ m, content of particles with particle size of 100 ⁇ m or less 92%) is 10.5% thicker
  • a suspension was prepared by dispersing in 60 ° C water while stirring with a homomixer.
  • the suspension was supplied to a steam injection type direct high-temperature heating device (TANAKA FOOD MA CHINERY), and the heating temperature was 145 ° C and the heating time was 36 seconds. .
  • Example 2 The same dry-milled soybean flour as in Example 1 had a concentration of 10.5% and granulated sugar had a concentration of 5.0%.
  • a suspension was prepared by dispersing in water at 60 ° C. while stirring with a homomixer.
  • the suspension was supplied to a homogenizer (manufactured by APV) and homogenized at 150 kg / fcm 2 .
  • the homogenized suspension is supplied to a steam injection type direct high-temperature heating device (TANAKA FOOD MACHINER Y), and the heating temperature is set to 110 ° C, 130 ° C, 145 ° C or 160 ° C, and the heating time is set.
  • Soy milk was produced by ik contact heat treatment with steam for each fixed at 36 seconds. Using the unheated suspension as a control, the average particle size and viscosity were measured at 12.2% solids for each soymilk after the heat treatment, and the roughness of the mouth was evaluated (see Table 1).
  • the average particle size of soy milk powder was decreased as the heating temperature was increased up to 160 ° C, and there was a tendency that roughness was eliminated. It was good at 160 ° C with no roughness, but conversely the viscosity increased and the mouth became heavier, and the mouth was not evaluated as well as 145 ° C.
  • Example 2 had excellent quality. Compared with the same heating condition # (145 ° C, 36 seconds), Example 2 However, there was a tendency that the average particle size and its standard deviation were slightly smaller than that of fine particles. That is, it is considered that Example 2 was subjected to stronger and shearing forces on the okara particles. As for the viscosity, Example 2 had a lower viscosity.
  • Example 2 In the same manner as in Example 2, the heating temperature was fixed at 145 ° C, and the heating time was set to 16 seconds, 36 seconds, 49 seconds, and 73 seconds, and direct high temperature heat treatment with steam was performed to produce soymilk. Using the unheated suspension as a control, each soy milk powder after the heat treatment was evaluated in the same manner as in Example 1 (see Table 2).
  • Standard deviation is a value related to the average particle size.
  • a suspension was prepared by dispersing the same soybean powder (produced by Pelican Co., Ltd.) as in Example 1 in 60 DC water while stirring with a homomixer so as to be 9.2%.
  • the suspension was supplied to a homogenizer (APV) and homogenized at 800 kg / fcm 2 to produce soy milk powder.
  • the roughness and flavor of the obtained soymilk were evaluated and compared with the soymilk obtained in Example 1 (see Table 3).
  • Commit Roll (URSCHEL Co., Ltd.): 4 parts of water is added to 1 part of demolted and hypocotyled soybean, and 6 parts of hot water (90 ° C) is added to 1 part of moulted and dehulled soybean that has sufficiently absorbed water. ) To obtain a soybean suspension having a particle size of 30 to 70 microns.
  • the soybean suspension was directly subjected to high-temperature heat treatment with steam in the same manner as in Example 1 to produce soy milk powder.
  • the heating conditions at this time were 36 seconds at 145 ° C.
  • the obtained soymilk was evaluated in the same manner as in Example 1 (see Table 4).
  • Standard deviation is a value related to the average particle size.
  • Soymilk was produced in the same manner as in Example 1 except that the direct high temperature heating device using steam in Example 1 was replaced with the plate-type U HT sterilizer (made by International Co., Ltd.) which is an indirect high temperature heating device. .
  • the heating conditions at this time were 36 seconds at 145 ° C.
  • the obtained soymilk was evaluated in the same manner as in Example 1 (see Table 5).
  • the standard deviation is a value related to the average particle diameter.
  • Example 4 Production of Fermented Soymilk
  • Example 3 direct high temperature treatment with steam was performed under the heating conditions of heating temperature 145 ° C, heating time 16 seconds and 36 seconds, and fermentation was performed with lactic acid bacteria using the produced soymilk. Lactic acid bacteria starter was added to soy milk powder with stirring to 0.016%, and the fermentation was performed at 42 ° C for 6 hours and up to ⁇ 4.6. After fermentation, 50% lactic acid was added to the fermented product to adjust the pH of the fermented product to 4.3, and homogenized with lOMPa using a homogenizer (APV).
  • AAV homogenizer
  • the fermented liquor is again supplied to the steam injection type direct high-temperature heating device (Iwai Kikai Kogyo Co., Ltd.) and subjected to heat treatment at 144 ° C for 4 seconds. Biological activity was stopped and fermented soymilk was obtained.
  • the steam injection type direct high-temperature heating device Iwai Kikai Kogyo Co., Ltd.
  • the obtained fermented soymilk was measured for viscosity, average particle size, and acidity, respectively, and evaluated for texture.
  • Example 3 direct heating was performed with steam at a heating temperature of 149 ° C. and a heating time of 30 seconds, and fermentation was performed with lactic acid bacteria using the produced soymilk.
  • the other conditions were the same as in Example 4 to produce fermented soymilk.
  • a homogenized soy flour suspension obtained in the same manner as in Example 2 was used as a steam injector. Supplied to a Chillon-type direct high-temperature heating device (Iwai Kikai Kogyo Co., Ltd.), sterilized at 145 ° C for 4 seconds, and then this heat-sterilized suspension was cooled to 42 ° C.
  • a Chillon-type direct high-temperature heating device Iwai Kikai Kogyo Co., Ltd.
  • lactic acid bacteria were fermented, and the fermented liquid was supplied to a steam-incubation-type direct high-temperature heating device (TANAKA FOOD MACHINERY) and subjected to heat treatment at 149 ° C for 30 seconds. Fermented soymilk was obtained. '
  • Example 6 has a tendency to increase the viscosity and average particle size compared to Example 5, but Example 6 has a difference in roughness between Examples 5 and 6. The degree of stickiness was somewhat felt as the viscosity increased.

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Abstract

It is intended to provide a powdery soy milk which has non-coarse texture, a low viscosity and a refreshing feel in drinking even though containing okara (bean curd refuse) and a product obtained by applying the same. In the process of producing a powdery soy milk by milling beans, the beans are milled by the dry milling method and water is added to the milled beans to give a suspension. To cutting the suspension containing the bean powder, the direct high temperature heating treatment using steam, which has been employed exclusively for sterilization hitherto, is used and the heating conditions in the direct high temperature heating treatment using steam are set to a certain level or higher. Thus, it is found out that a powdery soy milk which has non-coarse texture, a low viscosity and a refreshing feel in drinking can be obtained, thereby solving the problem as described above.

Description

明 細 書  Specification
豆粉乳の製造方法とその応用  Production method of soybean milk and its application
技術分野  Technical field
[0001] 本発明は豆類から豆粉乳を製造する方法とその応用に関するものである。  [0001] The present invention relates to a method for producing soymilk from beans and its application.
背景技術  Background art
[0002] 従来、豆乳の製造過程において、副産物として大量のオカラが排出される。このォ カラの廃棄処分が環境へ与える影響を考慮し、オカラを排出しなレ、豆粉乳やオカラ 乳の提供が望まれている。  Conventionally, a large amount of okara is discharged as a by-product in the production process of soymilk. In consideration of the environmental impact of this okara disposal, it is desirable to provide soy milk and okara milk that do not discharge okara.
し力 豆粉乳に含まれるオカラの粒度が大きいとざらつきのある舌触りの悪い飲み にくい食感となることが問題である。この傾向は豆粉乳を乳酸発酵した場合も同じで あり、独特の青臭みと相俟ってさらに飲みにくくなる傾向にある。  Strength The problem is that if the particle size of the okara contained in the soy milk powder is large, the texture becomes rough and the texture is difficult to drink. This tendency is the same when soy milk is fermented with lactic acid, and it tends to be more difficult to drink in combination with the unique blue odor.
そこで力かる問題解決のため、以下のような技術が開示されている。  In order to solve this problem, the following techniques are disclosed.
[0003] 特許文献:!〜 7では、大豆に水を加えて磨砕した懸濁液をホモゲナイザーなどの均 質化手段によってオカラの繊維を微細化する方法が記載されている。  [0003] Patent Documents:! To 7 describe a method of refining okara fibers by homogenizing means such as a homogenizer from a suspension obtained by adding water to soybean and grinding.
これらの方法は、大豆を水の存在下で粉砕するレ、わゆる湿式粉砕と均質化手段と の組み合わせによってざらつきのない豆粉乳を製造する技術である。  These methods are techniques for producing a soy milk powder that is not rough by a combination of pulverization of soybeans in the presence of water, so-called wet pulverization and homogenization means.
[0004] 特許文献 8〜: 14では、大豆微粉末に水をカ卩えて得た懸濁液をホモゲナイザーなど の均質化手段によってオカラの繊維を微細化する方法が記載されている。  [0004] Patent Documents 8 to 14 describe a method of refining okara fibers by homogenizing means such as a homogenizer from a suspension obtained by adding water to soybean fine powder.
これらの方法は、大豆に水を加える前に粉砕するいわゆる乾式粉砕と均質化手段 との組み合わせによってざらつきのない豆粉乳を製造する技術である。  These methods are techniques for producing soy-free soymilk by combining so-called dry pulverization, which is performed before adding water to soybeans, and a homogenizing means.
[0005] これら特許文献 1〜: 14などの技術によりオカラが微細化され、ざらつき感がある程 度改善されるに至ったものの、通常のオカラを含有しない豆乳に比べると依然として ざらつき感が気になる。このざらつき感は乳酸発酵を行うとさらにその傾向が強くなる 傾向にある。そしてこのざらつき感は均質化の圧力をいくら高くしても改善することが 困難であった。  [0005] Although techniques such as Patent Documents 1 to 14: Okara has been refined and has been improved to some extent with a feeling of roughness, the feeling of roughness is still a concern compared to soy milk that does not contain normal okara. Become. This feeling of roughness tends to become stronger with lactic acid fermentation. This roughness was difficult to improve no matter how high the homogenization pressure was.
[0006] また、上記問題を改善するための付加的ないし別の方法として、特許文献 7では懸 濁液を均質化すると共に、亜臨界又は臨界状態に高温高圧処理をする方法が開示 されており、特許文献 15では植物組織崩壊酵素によりオカラ繊維を分解する方法が 開示されている。 [0006] Further, as an additional or another method for improving the above problem, Patent Document 7 discloses a method of homogenizing a suspension and performing high-temperature and high-pressure treatment in a subcritical or critical state. Patent Document 15 discloses a method for degrading okara fibers using a plant tissue-disrupting enzyme.
しかし、これらの方法ではオカラ繊維が可溶化して水溶性大豆多糖類が抽出される ためか、豆粉乳の粘度が高くなり、重たい食感になってしまう。また特許文献 15では 、液中における均質化処理に時間力 Sかかる可能性がある。  However, in these methods, the okara fiber is solubilized and the water-soluble soybean polysaccharide is extracted, so that the viscosity of the soy milk becomes high and the food texture becomes heavy. Further, in Patent Document 15, there is a possibility that it takes time force S for the homogenization process in the liquid.
[0007] (参考文献) [0007] (References)
特許文献 1:特開昭 51— 41459号公報  Patent Document 1: Japanese Patent Laid-Open No. 51-41459
特許文献 2:特開昭 53— 66466号公幸  Patent Document 2: Japanese Patent Publication No. 53-66466
特許文献 3 :特開昭 59— 210861号公報  Patent Document 3: JP-A 59-210861
特許文献 4 :特開昭 61— 119154号公報  Patent Document 4: Japanese Patent Application Laid-Open No. 61-119154
特許文献 5 :特開昭 61— 192256号公報  Patent Document 5: JP-A 61-192256
特許文献 6:特開昭 62— 11068号公報  Patent Document 6: Japanese Patent Laid-Open No. 62-11068
特許文献 7:特開 2002— 95433号公報  Patent Document 7: Japanese Patent Laid-Open No. 2002-95433
特許文献 8 :特開昭 48— 26957号公報  Patent Document 8: Japanese Patent Laid-Open No. 48-26957
特許文献 9 :特開昭 60— 141247号公報  Patent Document 9: JP-A-60-141247
特許文献 10:特開昭 63— 24868号公報  Patent Document 10: Japanese Unexamined Patent Publication No. 63-24868
特許文献 11 :特開平 1—128759号公報  Patent Document 11: JP-A-1-128759
特許文献 12:特開 2003 _ 159020号公報  Patent Document 12: Japanese Patent Application Laid-Open No. 2003_159020
特許文献 13:特開 2004— 141155号公報  Patent Document 13: Japanese Unexamined Patent Application Publication No. 2004-141155
特許文献 14 :特開 2004— 16120号公報  Patent Document 14: Japanese Unexamined Patent Application Publication No. 2004-16120
特許文献 15:特開平 11 - 299442号公報  Patent Document 15: JP-A-11-299442
発明の開示  Disclosure of the invention
発明が解決しょうとする課題  Problems to be solved by the invention
[0008] 本発明は、オカラ分を含有するにもかかわらず、ざらつきがなぐかつ粘度があまり 上昇せずに飲み口もスッキリとした豆粉乳とその応用製品を提供することを課題とす る。 [0008] An object of the present invention is to provide a soy milk powder that does not have a rough texture, does not increase in viscosity, and has a refreshing mouth, and its application product, despite containing okara.
課題を解決するための手段  Means for solving the problem
[0009] 本発明者らは、豆類を粉砕して豆粉乳を製造する工程において、豆類の粉碎方式 を乾式粉砕とし、これに水をカ卩えて懸濁液とすること、そして、豆粉を含む懸濁液の 微細化手段として、従来は殺菌目的にしか用いられていなかった蒸気による直接高 温加熱処理を利用すること、さらに、蒸気による直接高温加熱処理の加熱条件を特 定の程度以上に設定することとした。これによりざらつきがなぐかつ粘度が低く飲み 口のすっきりとした豆粉乳を得られるという知見を得ることができ、上記課題を解決す るに至った。 [0009] In the process of pulverizing beans to produce a soy milk powder, the present inventors have used As a means of refining the suspension containing soybean flour, direct high temperature with steam, which was conventionally used only for sterilization purposes, It was decided to use heat treatment and to set the heating conditions for direct high-temperature heat treatment with steam to a specific level or higher. As a result, it was possible to obtain the knowledge that a soy milk powder having a smooth texture and a low viscosity can be obtained, and the above-mentioned problems have been solved.
[0010] 即ち、本発明は、 [0010] That is, the present invention provides
1.豆類を乾式粉碎した豆粉を含む懸濁液を調製すること、及び少なくとも該懸濁液 中のオカラ分に対して、加熱温度が 120°C以上、加熱時間が 10秒を超える蒸気によ る直接高温加熱処理を施すことを特徴とする豆粉乳の製造方法、  1. Prepare a suspension containing beans powder that has been dry-milled with beans, and at least for the okara content in the suspension, the heating temperature should be 120 ° C or more and the heating time should be more than 10 seconds. A method for producing soy milk powder, characterized by direct high-temperature heat treatment,
2.前記豆類が大豆である前記 1.記載の豆粉乳の製造方法、  2. The method for producing soy milk powder according to 1. above, wherein the beans are soybeans,
3.加熱温度が 120〜165°Cである前記 1.記載の豆粉乳の製造方法、  3. The method for producing soymilk according to 1. above, wherein the heating temperature is 120 to 165 ° C.
4.加熱時間が 15〜80秒である前記 1.記載の豆粉乳の製造方法、  4. The method for producing soy milk powder according to 1. above, wherein the heating time is 15 to 80 seconds,
5.前記 1.記載の豆粉乳を配合することを特徴とする飲食品の製造方法、  5. A method for producing a food or drink comprising the soy milk powder according to 1. above,
6.前記 1.記載の製造方法により得られた豆粉乳を微生物で発酵させることを特徴と する発酵豆粉乳の製造方法、  6. A method for producing fermented soymilk, characterized in that the soymilk obtained by the production method described in 1. is fermented by microorganisms,
7.前記 1.記載の豆粉乳の製造法において、さらに微生物による発酵工程を有する ことを特徴とする発酵豆粉乳の製造方法、  7. The method for producing fermented soymilk according to 1. above, further comprising a fermentation step with microorganisms,
8.豆粉の懸濁液を調製した後、蒸気による直接高温加熱処理を施す前に、微生物 による発酵を行う前記 7.記載の発酵豆粉乳の製造方法、  8. The method for producing fermented soymilk according to 7. above, wherein after the suspension of the soybean powder is prepared and before the direct high-temperature heat treatment with steam, the fermentation with microorganisms is performed,
9.豆類を乾式粉砕した豆粉を含む懸濁液を調製すること、及び少なくとも該懸濁液 中のオカラ分に対して、加熱温度が 120°C以上、加熱時間が 10秒を超える蒸気によ る直接高温加熱処理を施すことを特徴とする豆粉の微細化方法、  9. Prepare a suspension containing beans powder obtained by dry-pulverizing beans, and at least with the okara content in the suspension, the heating temperature is 120 ° C or more and the heating time is more than 10 seconds. A method for refinement of bean flour, characterized by direct high-temperature heat treatment,
を提供するものである。  Is to provide.
発明の効果  The invention's effect
[0011] 本発明は、豆類の粉碎を「乾式」で行うことと、その懸濁液に対して従来は殺菌手段 に過ぎなかった「蒸気による直接高温加熱処理」を「特定の温度範囲」かつ「特定の 時間」で行うことの組み合わせによって、従来技術では改善の程度に限界があったォ カラのざらつき感を極小化することができ、さらに粘度があまり上昇せずに飲み口もす つきりとした豆粉乳を製造できるという特異な効果を奏する。 [0011] In the present invention, the bean meal of beans is performed "dry", and "direct high-temperature heat treatment with steam", which was conventionally only a sterilization means for the suspension, is performed in a "specific temperature range" and There is a limit to the degree of improvement in the conventional technology due to the combination of what is done at a “specific time”. It has the unique effect of minimizing the rough texture of kala and producing soy milk powder that does not increase in viscosity and has a smooth mouth.
発明を実施するための最良の形態  BEST MODE FOR CARRYING OUT THE INVENTION
[0012] 以下、本発明の具体的構成について説明する。以下の説明において「%」は特に 断らない限り「質量%」を意味する。  Hereinafter, a specific configuration of the present invention will be described. In the following description, “%” means “% by mass” unless otherwise specified.
[0013] まず、本発明の豆粉乳の製造方法は、豆類を乾式粉砕した豆粉を含む懸濁液を調 製すること、及び少なくとも該懸濁液中のオカラ分に対して、加熱温度が 120°C以上[0013] First, in the method for producing soymilk of the present invention, a suspension containing beans powder obtained by dry-pulverizing beans is prepared, and the heating temperature is at least for the okara content in the suspension. 120 ° C or more
、加熱時間が 10秒を超える蒸気による直接高温加熱処理を施すことを特徴とするも のである。 It is characterized by direct high-temperature heat treatment with steam with a heating time exceeding 10 seconds.
[0014] (豆粉乳) [0014] (Soy milk powder)
本発明の製造方法により得られる「豆粉乳」は、大豆力 オカラを完全に除去して得 られる通常の豆乳とは区別され、広義にはオカラ分(特に子葉の細胞壁)を含む豆乳 を意味するものである。  The “soy milk powder” obtained by the production method of the present invention is distinguished from ordinary soy milk obtained by completely removing soybean power okara, and broadly means soy milk containing okara (particularly cotyledon cell walls). Is.
典型的には豆類を粉砕して得た懸濁液 (スラリー)をそのままオカラを全く除去する ことなく、又は一部のみを除去し、オカラ分を微細化して得られるものである。また、例 えばオカラの一部又は全部を一旦懸濁液から分離し、微細化を行ってから再び元に 戻して得られるものも本発明の豆粉乳の範疇である。豆粉乳はまた、豆粉乳に対して オカラを除去した豆乳や脱脂豆乳を加えたもの、さらには工程中に発酵を施したもの を包含する。  Typically, a suspension (slurry) obtained by pulverizing beans is obtained by removing okara as it is or by removing only a part of it and refining the okara content. In addition, for example, the soymilk of the present invention may be obtained by separating a part or all of okara from a suspension, refining it, and then restoring it again. Soymilk also includes soymilk and defatted soymilk that have had okara removed from soymilk, and those that have been fermented during the process.
豆粉乳の形態は液状、粉末状、顆粒状など、何れの形態へも加工され得る。  The form of the soy milk can be processed into any form such as liquid, powder or granule.
[0015] (豆類) [0015] (Beans)
本発明に用いる豆類としては、大豆が代表的であり、その品種は黄大豆、青大豆、 黒大豆などを限定なく使用することができる。また大豆に含まれる成分の栄養機能を 考慮して、育種、遺伝子操作や発芽処理等により 7Sグロブリン —コングリシニン) 、 11Sグロブリン(グリシニン)、イソフラボン、サポニン、ニコチアナミン、レシチン、オリ ゴ糖、ビタミン類、ミネラル類などの大豆中の特定の成分が富化された大豆を使用す ることも可能である。特に、 β コングリシニンは血中中性脂肪や内臓脂肪を低減し 、メタボリックシンドロームの予防に効果があると考えられており、これが富化された大 豆を使用することは有効である。また、大豆以外にも小豆、インゲン豆、ささげ、花豆 、エンドゥ、ソラマメ、たけあずき、レンズ豆、うずら豆、らい豆、ヒョコ豆、落花生等の 豆類も使用可能であり、これらを適当な割合で混合して使用することも可能である。 上記豆類は、外皮及び胚軸部分を含むものでもよいが、これらを除去したものを使 用することも可能である。 As the beans used in the present invention, soybean is representative, and as for the variety, yellow soybean, green soybean, black soybean and the like can be used without limitation. In consideration of the nutritional functions of the components contained in soybeans, 7S globulin-conglycinin), 11S globulin (glycinin), isoflavones, saponins, nicotianamine, lecithin, oligosaccharides, vitamins, It is also possible to use soybeans enriched with certain components in soybeans such as minerals. In particular, β-conglycinin is thought to reduce blood neutral fat and visceral fat and is effective in preventing metabolic syndrome. It is effective to use beans. In addition to soybeans, beans such as red beans, kidney beans, bean paste, flower beans, endo, broad beans, bamboo shoots, lentils, quail beans, raisins, leopard beans, peanuts, etc. can also be used, and these are used at an appropriate ratio. It is also possible to use it in a mixture. The beans may include the outer skin and the hypocotyl part, but it is also possible to use those obtained by removing them.
[0016] (乾式粉砕した豆粉) [0016] (Dry-milled soy flour)
本発明の豆粉乳は、上記の豆類を乾式粉砕し、豆粉として豆粉乳の製造に使用す ることが第一の特徴である。  The first feature of the soy milk powder of the present invention is that the above-mentioned beans are dry-ground and used as soy flour in the production of soy milk powder.
乾式粉碎は実質的に豆類に水を加水せずにジェット式、トルネード式、ハンマー式 、カッター式のミルなどの乾式粉砕機で粉砕される粉碎方式である。  The dry powder mash is a powder mash method that is pulverized by a dry pulverizer such as a jet type, tornado type, hammer type or cutter type mill without substantially adding water to the beans.
乾式粉碎された豆粉の平均粒子径は、 lOO /i m以下、好ましくは 50 /i m以下である ことが適当である。また、粒子径が大きすぎると大豆粉が完全に拡散'溶解できなくな る可能性があることから豆粉の粒子径 100 μ m以下の粒子の含有量が 70%以上で あるものが好ましい。  The average particle size of the dry-milled bean powder is suitably lOO / im or less, preferably 50 / im or less. Further, if the particle size is too large, the soybean powder may not be completely diffused and dissolved, so that the content of particles having a particle size of 100 μm or less in the soybean powder is preferably 70% or more.
なお、本発明は豆類に加水してから粉砕する方式である湿式粉碎を併用することを 除外するものではないが、湿式粉砕のみを用いる場合、乾式粉砕を用いる場合に比 ベ、食感の滑らかさに劣り、また粘度が高く飲み口が重たくなつてしまう。  Note that the present invention does not exclude the use of wet mash, which is a method of pulverizing after adding water to beans, but when using only wet pulverization, the texture is smoother than when using dry pulverization. It is inferior, and the viscosity becomes high and the drinking mouth becomes heavy.
[0017] (豆粉を含む懸濁液) [0017] (suspension containing soy flour)
次に、乾式粉砕された豆粉に加水し、攪拌装置や均質化装置などにより懸濁液 (ス ラリー)とする。このとき、懸濁液中の固形分濃度は特に限定されず、当業者が品質 上最適と考える濃度に設定すればよい。ただし過度に固形分濃度が高すぎると蒸気 による直接高温加熱処理により粘性が増し、豆粉乳の飲み口が低下する可能性があ ること力 、 20%以下、好ましくは 15%以下にしておくのが適当である。また、豆粉乳 の濃厚感を重視する場合には、固形分濃度を 2%以上、好ましくは 4%以上としてお くのが適当である。  Next, water is added to the dry pulverized bean powder to form a suspension (slurry) using a stirrer or homogenizer. At this time, the solid content concentration in the suspension is not particularly limited, and may be set to a concentration that those skilled in the art consider optimal in terms of quality. However, if the solids concentration is too high, the viscosity increases due to direct high-temperature heat treatment with steam, and the ability to lower the mouthful of soy milk powder. 20% or less, preferably 15% or less Is appropriate. When emphasizing the richness of soy milk powder, it is appropriate to set the solid content concentration to 2% or more, preferably 4% or more.
ここで加水する水の温度は、常温 (20°C)でも良いが懸濁液の調製を容易にするた めに 40〜60°C程度が望ましレ、。  The temperature of the water to be added here may be room temperature (20 ° C), but 40-60 ° C is desirable to facilitate the preparation of the suspension.
[0018] 上記の豆粉懸濁液の調製は、いかなる方法でも良ぐ例えば通常の飲料の製造に 用いられてレ、る溶解タンクなどを使用して、溶解攪拌翼を例えば 40〜60卬 mの回転速 度で回転させるなどして行うことができる。 [0018] The soybean powder suspension can be prepared by any method, for example, for the production of a normal beverage. The melting stirring blade can be rotated at a rotational speed of 40 to 60 mm, for example, using a melting tank or the like.
また必須な工程ではないが、要すれば懸濁液をホモゲナイザーなどによって均質 化することができる。例えば高圧ホモゲナイザーを用いる場合は圧力 3〜: 15MPaが 適当である。  Although not an essential step, the suspension can be homogenized by a homogenizer or the like if necessary. For example, when using a high-pressure homogenizer, a pressure of 3 to 15 MPa is appropriate.
[0019] (糖類添加) [0019] (Sugar added)
上記の豆粉懸濁液には、この段階で糖類を添加しておくことができる。糖類の種類 は特に限定されず、砂糖、グルコース、マルトース、ラタトース、トレハロース、オリゴ糖 などを用いることができる。その他、調製豆乳や豆乳飲料などに添加されている種々 の食品原料や添加剤を添加しておくこともできる。  Saccharides can be added to the soybean powder suspension at this stage. The type of saccharide is not particularly limited, and sugar, glucose, maltose, ratatoose, trehalose, oligosaccharide, and the like can be used. In addition, various food ingredients and additives added to prepared soymilk and soymilk beverages can also be added.
[0020] (蒸気による直接高温加熱処理) [0020] (Direct high temperature heat treatment with steam)
次に、本発明は、少なくとも上記の豆粉の懸濁液中のオカラ分に対して、蒸気によ る直接高温加熱処理を施すことが重要である。すなわち、豆粉の懸濁液に対して蒸 気による直接高温加熱処理を施す場合はもちろん、一旦豆粉の懸濁液からオカラ分 を分離し、これに蒸気による直接高温加熱処理を施す場合も含まれる。かかる加熱 処理を特定条件で行うことにより豆粉懸濁液に含まれるオカラ分を微細化することが 特徴である。  Next, in the present invention, it is important that at least the okara content in the above-mentioned bean powder suspension is subjected to a direct high-temperature heat treatment with steam. In other words, not only when the soybean powder suspension is directly subjected to high-temperature heat treatment by steam, but also when the okara content is once separated from the suspension of soybean flour and then directly subjected to high-temperature heat treatment by steam. included. It is characterized in that the okara content contained in the bean powder suspension is refined by performing such heat treatment under specific conditions.
蒸気による直接高温加熱処理は、 UHT殺菌(超高温殺菌)の一種であり、処理液( 本発明では懸濁液)を直接的に高温蒸気に接触させて、一定時間保持する加熱を 行った後、圧力解除して処理液中の水分を蒸発させて冷却する加熱方式である。よ り具体的には、処理液が流れる配管中に高温蒸気を噴射するスチームインジヱクショ ン方式と、高温蒸気の中に処理液を噴射するスチームインフュージョン方式などがあ り、いずれを採用してもよレ、。例えば、スチームインジェクション方式には VTIS殺菌 装置 (アルファラバル社製)、クレハ超高温瞬間滅菌装置 (呉羽テクノエンジ (株))など があり、スチームインフュージョン方式にはインフュージョンシステム(岩井機械工業( 株))などがあり、これに類した殺菌装置も使用可能である。  Direct high-temperature heat treatment with steam is a type of UHT sterilization (ultra-high temperature sterilization). After the treatment liquid (suspension in the present invention) is directly brought into contact with high-temperature steam and heated for a certain period of time. This is a heating method in which the pressure is released to evaporate water in the treatment liquid and cool it. More specifically, there are a steam injection method in which high-temperature steam is injected into the pipe through which the processing liquid flows, and a steam infusion method in which the processing liquid is injected into the high-temperature steam. Anyway. For example, there are VTIS sterilizers (Alfa Laval) and Kureha ultra-high temperature flash sterilizers (Kureha Techno Engineering Co., Ltd.) for the steam injection method, and infusion systems (Iwai Kikai Kogyo Co., Ltd.) for the steam infusion method. )) Etc., and similar sterilizers can also be used.
一方、プレート式殺菌機などの間接高温加熱方式を採用した場合、豆粉懸濁液の ザラツキを軽減させることは困難である。 [0021] (加熱処理条件) On the other hand, when an indirect high-temperature heating method such as a plate sterilizer is adopted, it is difficult to reduce the roughness of the bean powder suspension. [0021] (Heat treatment conditions)
ただし、蒸気による直接高温加熱処理を使用した場合であっても、従来のように単 に滅菌を目的とする程度の加熱条件では本発明の目的を達成することはできない。 すなわち、加熱温度は少なくとも 120°C以上で行うことが重要であり、より好ましくは 120〜165°C、さらに好ましくは 135〜155。C、最も好ましくは 140。C〜155。C力適 当である。  However, even when direct high-temperature heat treatment using steam is used, the object of the present invention cannot be achieved under heating conditions that are merely aimed at sterilization as in the prior art. That is, it is important that the heating temperature is at least 120 ° C or higher, more preferably 120 to 165 ° C, and still more preferably 135 to 155. C, most preferably 140. C-155. C power is appropriate.
力かる条件にて蒸気による直接高温加熱処理を行うことにより、オカラ分は十分に 微細化されると共に、豆粉乳にざらつきがなく低粘度の飲み口のスッキリとした食感を 付与することができる。従来技術の代表的な微細化手段はホモゲナイザーなどの均 質化手段であるが、均質化の圧力をいくら高めても本発明のような食感の豆粉乳を 得ることが困難である。  By direct high-temperature heat treatment with steam under powerful conditions, the okara content can be made sufficiently fine, and soy milk can be given a refreshing texture with a low-viscosity mouthfeel without roughness. . A typical refinement means of the prior art is a homogenization means such as a homogenizer, but it is difficult to obtain a soy milk powder having a texture as in the present invention, no matter how much the homogenization pressure is increased.
加熱温度が低いと、蒸気による直接高温加熱処理による懸濁液の粒子径の微粒子 化が困難となり、加熱処理後の豆粉懸濁液はざらつき感が残る傾向となる。一方 165 °Cを超えても豆粉懸濁液のざらつき感が軽減される効果は変わらないが、懸濁液の 粘度の上昇が生じたり、風味の劣化等が生じる場合があるので留意する。  When the heating temperature is low, it becomes difficult to make the suspension particle size fine by direct high-temperature heat treatment with steam, and the soybean powder suspension after the heat treatment tends to have a rough feeling. On the other hand, even if the temperature exceeds 165 ° C, the effect of reducing the rough feeling of the soybean powder suspension does not change, but it should be noted that the viscosity of the suspension may increase or the flavor may deteriorate.
[0022] さらに、加熱時間は少なくとも 10秒超で行うことが重要であり、好ましくは 15〜80秒 、より好ましくは 20〜70秒、さらに好ましくは 20〜60秒が適当である。  [0022] Further, it is important that the heating time be at least 10 seconds, preferably 15 to 80 seconds, more preferably 20 to 70 seconds, and further preferably 20 to 60 seconds.
加熱時間が短いと蒸気による直接高温加熱処理による懸濁液の粒子径の微粒子 化が困難となり、豆粉懸濁液のざらつき感が感じられる傾向にある。また 80秒を超え ると豆粉懸濁液のざらつき感が軽減される効果は変わらなレ、が、懸濁液の粘度の上 昇が生じたり、風味の劣化等が生じたりする場合があるので留意する。  If the heating time is short, it will be difficult to make the particle size of the suspension fine by direct high-temperature heat treatment with steam, and there will tend to be a rough feel of the bean powder suspension. If it exceeds 80 seconds, the effect of reducing the rough feeling of the soybean powder suspension will not change, but the viscosity of the suspension may increase or the flavor may deteriorate. So be careful.
[0023] 以上のようにオカラ分を微細化する作用は、オカラ粒子に高圧蒸気が直接接触す ることによって、オカラ粒子に対して一定のせん断力がかかり、この力が 10秒を超え る時間継続して力かることによって生じるものと考えられる。  [0023] As described above, the effect of refining the okara component is that a constant shear force is applied to the okara particles by direct contact of the okara particles with the high-pressure steam, and this time exceeds 10 seconds. This is thought to be caused by continuous efforts.
[0024] 豆粉懸濁液に蒸気による直接高温加熱処理を施した後、必ずしも必須ではないが 、加熱処理された豆粉懸濁液をホモゲナイザー等により均質化することができる。例 えば高圧ホモゲナイザーを用レ、る場合は圧力 3〜 15MPaが適当である。  [0024] After the soybean powder suspension is directly subjected to high-temperature heat treatment with steam, it is not always necessary, but the heat-treated soybean powder suspension can be homogenized with a homogenizer or the like. For example, when using a high-pressure homogenizer, a pressure of 3 to 15 MPa is appropriate.
[0025] また、豆粉懸濁液にはプロテアーゼ、ぺプチダーゼ、トランスグルタミナーゼ、ダル タミン酸デカノレボキシラーゼ、フイターゼ、アミラーゼ、ぺクチナーゼ、へミセノレラーゼ 等の各種酵素を加えて酵素反応を行うことにより、豆粉乳の物性や生理機能を適宜 改質することが可能である。 [0025] In addition, the soybean powder suspension contains protease, peptidase, transglutaminase, dull It is possible to appropriately modify the physical properties and physiological functions of soy milk by adding various enzymes such as decanoic acid decanolase, phytase, amylase, pectinase, and hemicenolase to perform an enzyme reaction.
[0026] 以上の製造方法により得られる豆粉乳は、平均粒子径が 15 z m以下、さらには 12 μ m以下の微粒子であり、ざらつき感が極めて感じにくく滑らかな食感を有するもの である。さらに、豆粉乳の固形分濃度が 9%のときの 10°Cにおける粘度は lOOmPa' s 以下、さらには 50mPa' s以下の低粘度の物性を有し、すっきりとした食感を有するも のである。  [0026] The soy milk powder obtained by the above production method is a fine particle having an average particle size of 15 zm or less, and further 12 µm or less, and has a smooth texture that is extremely difficult to feel roughness. Furthermore, when the solid content concentration of soy milk is 9%, the viscosity at 10 ° C is less than lOOmPa's, and further has a low viscosity property of less than 50mPa's, and has a clean texture. .
[0027] (飲食品)  [0027] (Food and drink)
本発明の飲食品の製造方法は、前記本発明の豆粉乳を配合することを特徴とする 。豆粉乳は通常の製造方法で得たオカラ分を含まない豆乳と同様に、各種豆乳製品 の製造原料として利用することができる。そして、上記の通り優れた物性を有するた め、通常のオカラを含まない豆乳と同様に扱うことが容易であり、利便性に優れたも のである。また本発明の飲食品は前記豆粉乳と通常の豆乳を好みの比率で混合して 製造することも可能である。  The manufacturing method of the food / beverage products of this invention mix | blends the said soy milk powder of this invention. Soymilk can be used as a raw material for the production of various soymilk products, in the same way as soymilk that does not contain okara obtained by a normal production method. Since it has excellent physical properties as described above, it can be easily handled in the same manner as ordinary soy milk without okara, and it has excellent convenience. In addition, the food and drink of the present invention can be produced by mixing the soymilk and normal soymilk in a desired ratio.
上記の飲食品の種類は特に限定されず、例えば、調製豆乳、豆乳飲料及び清涼 飲料等の飲料、豆腐、プリン、ババロア、ゼリー、ホイップクリーム及びフィリング等の 生菓、ヨーグルト、チーズ及び乳酸発酵豆乳 (後述参照)等の発酵食品、団子や優 頭等の和菓子、スナック等の膨化菓子、ビスケット、クッキー、パン類及びケーキ等の ベーカリー製品、チョコレート、マーガリン、スプレッドやマヨネーズ等の調味料、ソー ス、スープ、フライ食品、水産練製品、鳥獣魚肉製品等に使用できる。  The types of the above-mentioned foods and drinks are not particularly limited. For example, beverages such as prepared soy milk, soy milk beverages and soft drinks, tofu, pudding, bavaria, jelly, whipped cream, fillings and other fresh confectionery, yogurt, cheese and lactic acid fermented soy milk Fermented foods (see below), Japanese sweets such as dumplings and supper, puffed snacks such as snacks, bakery products such as biscuits, cookies, breads and cakes, seasonings such as chocolate, margarine, spreads and mayonnaise, sauces , Soups, fried foods, seafood paste products, birds and fish products.
[0028] 各種豆乳製品の製造に際しては豆粉乳の他に必要な食品原料 (果汁、果肉、野菜 、糖類、油脂、乳製品、穀粉類、澱粉類、カカオマス、鳥獣魚肉製品等)や食品添加 物 (ミネラル、ビタミン、乳化剤、増粘安定剤、酸味料、香料等)を適宜使用することが できる。 [0028] In addition to soymilk for the production of various soymilk products, necessary food ingredients (fruit juice, pulp, vegetables, sugars, fats and oils, dairy products, flours, starches, cacao mass, avian fish products, etc.) and food additives (Minerals, vitamins, emulsifiers, thickening stabilizers, acidulants, flavors, etc.) can be used as appropriate.
また、上記食品以外にも、石鹼ゃシャンプー等の化成品、ローション等の化粧品など の非食品の原料としても使用できる。  In addition to the above foods, it can also be used as a raw material for non-food products such as chemicals such as stone shampoo and cosmetics such as lotions.
[0029] (発酵豆粉乳) 本発明の発酵豆粉乳の製造方法の一つは、前記の方法により得られた豆粉乳を 微生物で発酵させる方法である。また、他の一つは、請求項 1記載の豆粉乳の製造 法において、さらに微生物による発酵工程を有することを特徴とする方法である。 すなわち、微生物の発酵は、 自ら製造するか外部から購入することにより本発明の 豆粉乳を得た後にこれを発酵原料として行うものでも良いし、あるいは豆粉乳の製造 工程中の何れかの段階において行うものでも良い。 [0029] (Fermented soy milk powder) One of the methods for producing fermented soymilk of the present invention is a method of fermenting the soymilk obtained by the above method with microorganisms. The other is the method for producing soymilk according to claim 1, further comprising a fermentation step with microorganisms. That is, the fermentation of microorganisms may be carried out as a raw material for fermentation after the soybean milk of the present invention is obtained by being produced by itself or purchased from the outside, or at any stage in the production process of soybean milk. You can do it.
後者の場合、発酵工程の段階は特に限定されることはなぐ豆粉に加水して豆粉の 懸濁液を調製した段階、豆粉の懸濁液に蒸気による直接高温加熱処理を施す前や その後の段階、豆粉の懸濁液を豆乳とオカラ分に分離した後の段階 (この場合、豆 乳とオカラ分のいずれも発酵原料とし得る。)などである。  In the latter case, the stage of the fermentation process is not particularly limited. The stage is prepared by adding water to soy flour and preparing a suspension of bean flour. The subsequent stage is a stage after the soybean powder suspension is separated into soy milk and okara (in this case, both soy milk and okara can be used as fermentation raw materials).
発酵に際しては、発酵原料に、微生物の栄養源として資化性糖類を添加することが 好ましい。例えばグルコース、ショ糖、マルトース、ガラクトース、ラタトース、ラフイノー ス、トレハロース、大豆オリゴ糖、フラタトオリゴ糖等を用いることができる。これら糖原 料は単独や 2種類以上の組み合わせてもよい。  At the time of fermentation, it is preferable to add an assimilating saccharide as a nutrient source of microorganisms to the fermentation raw material. For example, glucose, sucrose, maltose, galactose, latatose, roughinose, trehalose, soybean oligosaccharide, furato oligosaccharide and the like can be used. These sugar raw materials may be used alone or in combination of two or more.
[0030] 本発明の発酵に使用する微生物としては、一般的に発酵食品の製造に利用されて レ、る微生物であれば特に限定されることはなぐ例えば乳酸菌、ビフィズス菌、酵母、 麹菌、納豆菌、テンペ菌などを単独あるいは適宜組み合わせて使用することができる [0030] The microorganism used in the fermentation of the present invention is not particularly limited as long as it is a microorganism generally used in the production of fermented foods. For example, lactic acid bacteria, bifidobacteria, yeast, koji mold, natto Bacteria and tempeh bacteria can be used alone or in appropriate combination
[0031] 例えば乳酸菌としては、通常のヨーグルトに使用されている菌種を用いればよく特 に限定されない。例えばラクトバチルス 'カゼィ、ラクトバチルス 'プランタラム、ラタトバ チルス.ヘルべティカス、ラクトバチルス.ブルガリカス、ラクトバチルス'ガッセリ、ラクト バチルス ·ァシドフィルス、ラクトバチルス'ラタチス、ラクトバチルス'サリバリウス'サリ ノ リウス、ラクトバチルス 'ガリナラム、ラクトバチルス 'アミロボラス、ラクトバチルス'ブレ ビス'ブレビス、ラクトバチルス.フアーメンタム、ラクトバチルス.マリ、ラクトバチルス.デ ノレブルツキィ、ラクトバチルス ·サンフランシスェンシス、ラクトバチルス 'バネックス、ラ タトバチルス.コモェンシス、ラクトバチルス.イタリカス、ラクトバチルス.ライキマ二、ラ タトバチルス.力ルバタス、ラクトバチルス 'ヒルガルディ、ラクトバチルス 'ノレテリ、ラクト バチルス 'パストリアヌス、ラクトバチルス'ブクネリ、ラクトバチルス'セロビォサス、ラタ トバチルス ·フルクティボランス等のラクトバチルス属、ストレプトコッカス ·サーモフィノレ ス、ストレプトコッカス 'ラタチス、ストレプトコッカス'ジァセチルラクチス等のストレプトコ ッカス属、ラタトコッカス 'ラクチス'ラクチス、ラタトコッカス 'ラクチス'タレモリス等のラタ トコッカス属、ロイコノストック.メセンテロイデス.タレモリス、ロイコノストック.ラクチス等 のロイコノストック属等の乳酸菌を特に限定なく用いることができる。 [0031] For example, lactic acid bacteria are not particularly limited as long as they use bacterial species used in normal yogurt. For example, Lactobacillus casei, Lactobacillus plantarum, Ratatobacillus, Helveticas, Lactobacillus bulgaricus, Lactobacillus 'Gasselli, Lactobacillus acidophilus, Lactobacillus' Lattice, Lactobacillus 'Sarivarius' Salinorius, Lact Bacillus 'Galinaram, Lactobacillus' Amyroboras, Lactobacillus 'Brevis' Brevis, Lactobacillus, Fermentum, Lactobacillus. .Comomensis, Lactobacillus.Italica, Lactobacillus.Raikimani, Ratatobacillus.Power Lubatas, Lactobacillus' Hilgardi, Lactobacillus' Noreteri, Lactobacillus' Pastorianus, Lactobacillus 'Bukneri, Lactobacillus' Cerobiosus, Rata Lactobacillus spp. Lactic acid bacteria of the genus Leuconostoc, such as Leuconostoc genus, Leuconostoc mesenteroides Talemorris, Leuconostoc Lactis, etc. can be used without particular limitation.
[0032] ビフィズス菌としては、ビフイドバタテリゥム'ビフィダム、ビフイドバタテリゥム'ロンガム 、ビフイドバタテリゥム 'インファンテイス、ビフイドバタテリゥム 'ブレーべ、ビフイドバクテ リウム 'アドレセンテイス、ビフイドバタテリゥム 'アンギュラータム、ビフイドバタテリゥム' カテニユラ一タム、ビフイドバタテリゥム 'シユードカテニユラ一タム、ビフイドバタテリゥム 'デンティゥム、ビフイドバタテリゥム'グロボズム、ビフイドバタテリゥム 'シユードロンガ ム、ビフイドバタテリゥム'クニキユリ、ビフイドバタテリゥム 'コエリナム、ビフイドバタテリ ゥム.アニマリス、ビフイドバタテリゥム.サーモフィラム、ビフイドバタテリゥム.ボウム、ビ フイドバタテリゥム 'マグナム、ビフイドバタテリゥム'ァステロイデス、ビフイドバクテリウ ム 'インディカム、ビフイドバタテリゥム'ガリカム、ビフイドバタテリゥム 'ラタチス、ビフィ ドバクテリゥム ·イノピナ一タム、ビフイドバタテリゥム.デンティコレンス、ビフイドバタテリ ゥム 'プロ一ラム、ビフイドバタテリゥム 'スイス、ビフイドバタテリゥム 'ガリナーラム、ビフ イドバタテリゥム'ルミナンティゥム、ビフイドバタテリゥム'メリシカム、ビフイドバクテリウ ム.サーキユラーレ、ビフイドバタテリゥム.ミニマム、ビフイドバタテリゥム.サブチル、ビ フイドバタテリゥム 'コリネフオルメ等を限定なく用いることができる。  [0032] Bifidobacteria include Bifido Batterium 'Bifidum', Bifido Batterium 'Longham', Bifido Batterium 'Infantasies', Bifido Batterium' Breve ', Bifido Bacterium' Addresses, Bif Id Batterium 'Angular Tam, Bifid Batterium' Cateñuratum Tam, Bifid Batterium 'SyudoCatenyuratum, Bifid Batterium' Dentium, Bifid Batterium 'Globos, Bifid Batterium 'Syudulongum, Bifido Batterium' Kuniki Yuri, Bifido Batterium 'Coelinum, Bifido Batterium, Animalice, Bifido Batterium, Thermophilum, Bifido Batterium, Baum, Bifid Batterium 'Magnum, Bifido Batterium' Astereuides , Bifidobacteria 'Indicam, Bifid Batterium' Gallicum, Bifido Batterium 'Ratatis, Bifidobacterium Inopinatum, Bifido Batterium. Dentikorens, Bifido Batterium' Prolam , Bifido Batterium 'Switzerland, Bifido Batterium' Galinaram, Bifido Batterium 'Luminantium, Bifido Batterium' Mericicam, Bifido Bacteria. Mu-sabutyl, bifido butterium 'corynefolm, etc. can be used without limitation.
[0033] 酵母としては、パンの発酵などに使用されるイースト菌(サッカロミセス'セレビジェ) の他、例えばパン種として使用されるサワー種(サンフランシスコサワー種、ライサヮ 一種、パネトーネ種など)、ホップス種、ビール種、酒種、果実種(ブドウ果実種、リン ゴ果実種など)由来の酵母を使用することができる。 [0033] Examples of yeast include yeast (Saccharomyces cerevisiae) used for bread fermentation, for example, sourdough used as bread seeds (San Francisco sour seed, laisa spear, panettone, etc.), Hops seed, beer seed Yeasts derived from liquor, fruit (grape fruit, apple fruit, etc.) can be used.
[0034] 麹菌としては、ァスペルギルス'オリゼー、ァスペルギルス'二ガー、ァスペルギルス [0034] As for Aspergillus, Aspergillus 'Orissee, Aspergillus' Niger, Aspergillus
'ソーャ、ァスペルギルス'力ヮチ、ァスペルギルス'ァヮモリ等のァスペルギルス属、 モナスカス'アンカ、モナスカス'パーパレウス等のモナスカス属、ノィロスポア属、リゾ プス.ジャパ二カス等のリゾプス属、ムコール'ノレキシ一等のムコール属等を限定なく 用レ、ることができる。 [0035] テンペ菌としては、リゾプス.オリゴスポラス、リゾプス.ォリゼ一等のリゾプス属を用い ること力 Sできる。 'Soya, Aspergillus' force, Aspergillus genus Aspergillus genus, Monascus' Anca, Monascus perpareus, etc., Monascus genus, Neurospora genus, Rhizopus. You can use the genus without limitation. [0035] As Tempe bacteria, Rhizopus genus such as Rhizopus. Oligosporus, Rhizopus.
[0036] 上記の微生物のうち、乳酸菌やビフィズス菌で発酵させた発酵豆粉乳は、植物性 であってヨーグルト様の爽やかな酸味を呈するので、特に飲食品として適当である。 乳酸菌やビフィズス菌で発酵させた場合、乳酸や酢酸などの有機酸の生成により pH が低下するため、オカラを含まなレ、豆乳を用いたとしても豆腐のように一旦凝固して しまい、重たい食感となる。そのためオカラ分を含む豆粉乳の場合は粘度が高ぐ十 分に微細化されていないと、重たくざらついた食感が際立ったものとなってしまう。し かし、本発明の豆粉乳で発酵すると通常のオカラを含む豆乳を発酵させた発酵豆乳 と殆ど物性の変わらない発酵豆粉乳を製造することができる。  [0036] Among the above microorganisms, fermented soymilk fermented with lactic acid bacteria or bifidobacteria is plant-like and exhibits a refreshing sour taste like yogurt, and thus is particularly suitable as a food or drink. When fermented with lactic acid bacteria or bifidobacteria, the pH decreases due to the production of organic acids such as lactic acid and acetic acid. A feeling. Therefore, in the case of soy milk containing okara, if it is not sufficiently refined to have a high viscosity, a heavy and rough texture will stand out. However, when fermented with the soymilk of the present invention, fermented soymilk fermented with soymilk containing ordinary okara and fermented soymilk with almost no change in physical properties can be produced.
[0037] 発酵方法については、バルタスターターを作って添加することも、凍結濃縮菌ゃ凍 結乾燥濃縮菌で直接、発酵原料に添加することもできる。微生物の添加量は、発酵 温度、発酵時間に応じて調整することができる。微生物の種類によっても異なるため 限定されないが、発酵温度は 20〜50°Cで、 3〜48時間、好ましくは 25〜45°Cで、 4 〜24時間が適当である。  [0037] Regarding the fermentation method, a Balta starter can be prepared and added, or it can be added directly to the fermentation raw material with freeze-concentrated bacteria or freeze-dried concentrated bacteria. The amount of microorganism added can be adjusted according to the fermentation temperature and fermentation time. The fermentation temperature is 20 to 50 ° C., 3 to 48 hours, preferably 25 to 45 ° C., and 4 to 24 hours is appropriate because it varies depending on the type of microorganism.
[0038] 得られた発酵豆粉乳の pHは微生物の種類にも寄るため特に限定されないが、乳 酸菌ゃビフィズス菌で発酵させた場合には、 ρΗ3· 5〜5· 5が好ましぐより好ましく は ρΗ4〜5、さらに好ましくは ρΗ4. 2〜4. 7が適当である。発酵直後の pHが所望の pHに満たない場合には、さらに乳酸、クェン酸、リンゴ酸のような有機酸やリン酸など によって調整することができる。  [0038] The pH of the obtained fermented soy milk powder is not particularly limited because it depends on the type of microorganism, but when fermented with lactobacilli or bifidobacteria, ρΗ3 · 5 to 5 · 5 is preferred. Preferably, ρΗ4 to 5, more preferably ρΗ4.2 to 4.7. If the pH immediately after fermentation is less than the desired pH, it can be further adjusted with an organic acid such as lactic acid, citrate, or malic acid, or phosphoric acid.
[0039] 次に、得られた発酵豆粉乳を固形状とする場合やすでに液状となっている場合は 必須ではないが、液状タイプの製品とする場合には、ホモゲナイザー等により均質化 処理を行って完全に液状とすることが好ましい。例えば高圧ホモゲナイザーを用いる 場合は圧力 3〜 15MPaが適当である。  [0039] Next, when the obtained fermented soymilk is solid or already in liquid form, it is not essential, but when it is a liquid type product, it is homogenized by a homogenizer or the like. It is preferable to make it completely liquid. For example, when using a high-pressure homogenizer, a pressure of 3 to 15 MPa is appropriate.
[0040] 以上のようにして得られた発酵粉豆乳は、そのまま生菌タイプとして製品化すること もできるし、加熱殺菌により発酵を停止させ、微生物の生物的活性を不活性化し、殺 菌発酵豆粉乳として製品化することもできる。力かる場合の殺菌条件としては、使用 した微生物を死滅させる温度と時間で処理すれば足りる。 実施例 [0040] The fermented soymilk obtained as described above can be commercialized as a live bacteria type as it is, or the fermentation is stopped by heat sterilization, the biological activity of microorganisms is inactivated, and the sterilization fermentation is performed. It can also be commercialized as soy milk powder. As for the sterilization conditions when it is strong, it is sufficient to treat at the temperature and time to kill the used microorganisms. Example
[0041] 以下、本発明の実施例を示すが、本発明がこれらによってその技術的範囲が限定 されるものではない。  [0041] Examples of the present invention are shown below, but the technical scope of the present invention is not limited by these examples.
[0042] 園実施例 1 [0042] Garden Example 1
脱皮脱胚軸された大豆を乾式粉碎した大豆粉 ((株)ペリカン社製、平均粒子径 15 μ m、粒子径 100 μ m以下の粒子の含有量 92%)が 10.5%濃 になるようにホモミキ サ一で攪拌しながら 60°Cの水に分散させて懸濁液を調製した。  Soy flour made by dry milling of dehulled and hypocotyled soybean (made by Pelican Co., Ltd., average particle size 15 μm, content of particles with particle size of 100 μm or less 92%) is 10.5% thicker A suspension was prepared by dispersing in 60 ° C water while stirring with a homomixer.
懸濁液をスチームインジヱクシヨン方式の直接高温加熱装置 (TANAKA FOOD MA CHINERY社製)に供給し、加熱温度を 145°C、加熱時間を 36秒にして蒸気による直 接加熱処理を行った。  The suspension was supplied to a steam injection type direct high-temperature heating device (TANAKA FOOD MA CHINERY), and the heating temperature was 145 ° C and the heating time was 36 seconds. .
より詳しくは、懸濁液が流れる装置の流路内に 8気圧の蒸気を注入し、蒸気を懸濁 液に直接接触させた。流路內の懸濁液を 145°Cまで一気に昇温させ^後、同温度に て 36秒間保持させた。その後、減圧弁により圧力を一気に解除し、冷却して豆粉乳を 製造した。 ' 製造した豆粉 ftの固形分は 9.2%、平均粒子径は 10.97 /i m、粒子径の標準偏差は More specifically, 8 atm of steam was injected into the flow path of the apparatus through which the suspension flows, and the steam was brought into direct contact with the suspension. The suspension in the channel was heated up to 145 ° C all at once, and then held at that temperature for 36 seconds. After that, the pressure was released at once by the pressure reducing valve, and cooled to produce soymilk. '' The solid content of the produced soy flour ft is 9.2%, the average particle size is 10.97 / im, and the standard deviation of the particle size is
 8 ©
、 6. 655 m,粘度は 54.5mPa'sであった。また、この豆粉乳はざらつき5 < X  6.655 m, viscosity was 54.5 mPa's. In addition, this soy milk powder has a roughness of 5 <X
がなくオカラ粒 ■ 子の角が取れたような、非常になめらかな食感であり、粘度が低く飲み口が軽いとい う評価であった。なお、ざらつき'飲み口の評価は下記に示す 5段階で表わした (パネ ラー 6名)。  Okara grains ■ It was evaluated that it had a very smooth texture, with a small corner, and a low viscosity and a light mouth. In addition, the evaluation of the graininess' drinking mouth was expressed in the following 5 levels (6 panelists).
[0043]  [0043]
ざらつき 飲み口 評価記号 非常にざらつきあり 非常に重い  Roughness Drinking mouth Evaluation symbol Very rough and very heavy
ざらつきあり 重い  Rough and heavy
わずかにざらつきあり ふつう  Slightly rough
なめらか 軽い  Smooth light
非常になめらか 非常に軽い 園実施例 2  Very smooth very light garden example 2
実施例 1と同じ乾式粉砕した大豆粉が 10.5%濃度、グラニュー糖が 5.0%濃度にな  The same dry-milled soybean flour as in Example 1 had a concentration of 10.5% and granulated sugar had a concentration of 5.0%.
差替え用紙 則 26) るようにホモミキサーで攪拌しながら 60°Cの水に分散させて懸濁液を調製した。懸濁 液を均質機 (APV社製)に供給し、 150kg/fcm2で均質化処理した。均質化した懸濁液 をスチームインジェクション方式の直接高温加熱装置 (TANAKA FOOD MACHINER Y社製)に供給し、加熱温度を 110°C、 130°C、 145°C 又は 160°Cとし、加熱時間を 36 秒に固定してそれぞれ蒸気による ik接加熱処理を行い、豆粉乳を製造した。未加熱 の懸濁液を対照として、加熱処理後の各々の豆粉乳について固形分 12. 2%で平均 粒子径と粘度の測定、及びざらつき'飲み口の評価を行った (表 1参照)。 Replacement paper Rule 26) A suspension was prepared by dispersing in water at 60 ° C. while stirring with a homomixer. The suspension was supplied to a homogenizer (manufactured by APV) and homogenized at 150 kg / fcm 2 . The homogenized suspension is supplied to a steam injection type direct high-temperature heating device (TANAKA FOOD MACHINER Y), and the heating temperature is set to 110 ° C, 130 ° C, 145 ° C or 160 ° C, and the heating time is set. Soy milk was produced by ik contact heat treatment with steam for each fixed at 36 seconds. Using the unheated suspension as a control, the average particle size and viscosity were measured at 12.2% solids for each soymilk after the heat treatment, and the roughness of the mouth was evaluated (see Table 1).
[表 1]  [table 1]
Figure imgf000014_0001
Figure imgf000014_0001
※標準偏差は粒子径の値である。  * Standard deviation is the particle size.
[0046] 上記結果より、 145°C、 36秒の加熱条件のもの力 S、食感が非常に滑らかで、かつ粘 度が低く、飲み口もすつきりしており、最も良好であった。また実施例 1と比較してもざ らに粘度が低粘度となって飲み口がすっきりしており、平均粒子径も小さくなつてなめ らかな食感が際立っていた。 [0046] From the above results, the strength of the heating condition at 145 ° C for 36 seconds S, the texture was very smooth, the viscosity was low, and the drinking mouth was smooth, which was the best . Compared with Example 1, the viscosity was much lower and the drinking mouth was clean, and the average particle size was smaller, and the smooth texture was outstanding.
また表 1によれば、 160°Cまでは加熱温度を髙くするほど豆粉乳の平均粒子径が 小さくなり、ざらつきがなくなる傾向にあった。 160°Cでもざらつきはない点で良好で あつたが、逆に粘度が増加して飲み口が重たくなり、 145°Cほど飲み口の評価は良く なかった。  Further, according to Table 1, the average particle size of soy milk powder was decreased as the heating temperature was increased up to 160 ° C, and there was a tendency that roughness was eliminated. It was good at 160 ° C with no roughness, but conversely the viscosity increased and the mouth became heavier, and the mouth was not evaluated as well as 145 ° C.
[0047] また、実施例 1と実施例 2の豆粉乳はいずれも優れた品質を有していた力 同一の 加熱条 # (145°C、 36秒)で敢えて比較すると、実施例 2の方が若干平均粒子径とそ の標準偏差が小さぐより微粒子化されている傾向にあった。すなわち、実施例 2の 方がオカラ粒子に対してより強レ、せん断力がかかってレ、たと考えられる。そして、粘 度については実施例 2の方が低粘度であった。  [0047] Also, the soy milk powder of Example 1 and Example 2 both had excellent quality. Compared with the same heating condition # (145 ° C, 36 seconds), Example 2 However, there was a tendency that the average particle size and its standard deviation were slightly smaller than that of fine particles. That is, it is considered that Example 2 was subjected to stronger and shearing forces on the okara particles. As for the viscosity, Example 2 had a lower viscosity.
差替え用紙(規 j2S》 [0048] 顧実施例 3 Replacement paper (Regulation j2S) [0048] Advisory Example 3
実施例 2と同様の方法で、加熱温度を 145°Cに固定し、加熱時間を 16秒、 36秒、 49 秒、 73秒として蒸気による直接高温加熱処理を行い、豆粉乳を製造した。未加熱の 懸濁液を対照として、加熱処理後の各々の豆粉乳について実施例 1と同様に評価し た (表 2参照)。  In the same manner as in Example 2, the heating temperature was fixed at 145 ° C, and the heating time was set to 16 seconds, 36 seconds, 49 seconds, and 73 seconds, and direct high temperature heat treatment with steam was performed to produce soymilk. Using the unheated suspension as a control, each soy milk powder after the heat treatment was evaluated in the same manner as in Example 1 (see Table 2).
[0049] [表 2] [0049] [Table 2]
Figure imgf000015_0001
Figure imgf000015_0001
※標準偏差は平均粒子径に関する値である。  * Standard deviation is a value related to the average particle size.
[0050] 上記結果より、加熱時間を長くするほど、平均粒子径とその標準偏差が小さくなり、 豆粉乳のざらつきはなくなる傾向にあり、一方で粘度は加熱時間を長くするほど増加 する傾向が確認された。以上の結果から、最も良好な条件は、 145°C · 36秒又は 14 5°C '49秒であった。 [0050] From the above results, it was confirmed that the longer the heating time, the smaller the average particle size and its standard deviation, and the tendency for the soy milk powder to disappear, while the viscosity increased as the heating time was increased. It was done. From the above results, the best conditions were 145 ° C · 36 seconds or 145 ° C '49 seconds.
[0051] 騸比較例 1 (均質化のみ)  [0051] 騸 Comparative Example 1 (homogenization only)
実施例 1と同じ大豆粉 ((株)ペリカン社製)を 9.2%になるようにホモミキサーで攪拌し ながら 60DCの水に分散させて懸濁液を調製した。懸濁液をホモゲナイザー (APV社 製)に供給し、 800kg/fcm2で均質化処理し、豆粉乳を製造した。得られた豆粉乳のざ らつきと風味の評価を行 ヽ、実施例 1で得られた豆粉乳と比較した (表 3参照)。 A suspension was prepared by dispersing the same soybean powder (produced by Pelican Co., Ltd.) as in Example 1 in 60 DC water while stirring with a homomixer so as to be 9.2%. The suspension was supplied to a homogenizer (APV) and homogenized at 800 kg / fcm 2 to produce soy milk powder. The roughness and flavor of the obtained soymilk were evaluated and compared with the soymilk obtained in Example 1 (see Table 3).
[0052] [表 3]  [0052] [Table 3]
Figure imgf000015_0002
Figure imgf000015_0002
※標準偏差は平均粒子径に関する値である。 [0053] 均質機のみで処理した比較例 1の豆粉乳は、蒸気による直接髙温加熱処理を施し た実施例 1の豆粉乳に比べ、ざらつきがあり、風味も良くなかった。実施例 1の豆粉乳 の食感はオカラ分を単に物理的に微粒子化したものでなぐ高圧蒸気によって強力 なせん断力がかかっているためか、粒子の角が取れたような滑らかな食感であった。 * Standard deviation is a value related to the average particle size. [0053] The soy milk powder of Comparative Example 1 treated with only a homogenizer was rough and not as good as the soy milk powder of Example 1 that had been subjected to direct soaking and heating with steam. The texture of the soy milk powder of Example 1 is a smooth texture with the corners of the particles removed, probably because of the strong shearing force applied by the high-pressure steam, which is not the physical fine particles of okara. there were.
[0054] 驪比較例 2 (湿式粉砕後の蒸気による直接高温加熱)  [0054] Comparative Example 2 (direct high temperature heating with steam after wet grinding)
脱皮脱胚軸した大豆 1部に水 4部を加え、十分に吸水した脱皮 ·脱胚軸大豆 1部に 対し、熱水(90°C) 6部を加えたものをコミットロール (URSCHEL社製)を用いて湿 式粉砕し、粒子径 30〜70ミクロンの大豆懸濁液を得た。  Commit Roll (URSCHEL Co., Ltd.): 4 parts of water is added to 1 part of demolted and hypocotyled soybean, and 6 parts of hot water (90 ° C) is added to 1 part of moulted and dehulled soybean that has sufficiently absorbed water. ) To obtain a soybean suspension having a particle size of 30 to 70 microns.
この大豆懸濁液に対して実施例 1と同様に蒸気による直接高温加熱処理を行レヽ、 豆粉乳を製造した。このときの加熱条件は、 145°Cで 36秒とした。  The soybean suspension was directly subjected to high-temperature heat treatment with steam in the same manner as in Example 1 to produce soy milk powder. The heating conditions at this time were 36 seconds at 145 ° C.
得られた豆粉乳について実施例 1と同様にして評価した (表 4参照)。  The obtained soymilk was evaluated in the same manner as in Example 1 (see Table 4).
[0055] [表 4] [0055] [Table 4]
Figure imgf000016_0001
Figure imgf000016_0001
※標準偏差は平均粒子径に関する値である。  * Standard deviation is a value related to the average particle size.
[0056] 湿式粉砕した比較例 2の豆粉乳は、乾式粉砕した実施例 1の豆粉乳よりも粘度が高 く飲み口が重力 た。 [0056] The soy powdered milk of Comparative Example 2 that had been wet crushed had a higher viscosity and a gravity mouth than the dry pulverized soymilk of Example 1.
[0057] 騸比較例 3 (間接加熱方式の場合) [0057] 騸 Comparative Example 3 (Indirect heating method)
実施例 1の蒸気による直接高温加熱装置を間接高温加熱装置であるプレート式 U HT殺菌装置レ^—ポイント 'インターナショナル社製)に代え、それ以外は実施例 1 と同様にして豆粉乳を製造した。このときの加熱条件は、 145°Cで 36秒とした。  Soymilk was produced in the same manner as in Example 1 except that the direct high temperature heating device using steam in Example 1 was replaced with the plate-type U HT sterilizer (made by International Co., Ltd.) which is an indirect high temperature heating device. . The heating conditions at this time were 36 seconds at 145 ° C.
得られた豆粉乳について実施例 1と同様にして評価した (表 5参照)。  The obtained soymilk was evaluated in the same manner as in Example 1 (see Table 5).
[0058] [表 5] [0058] [Table 5]
Figure imgf000016_0002
Figure imgf000016_0002
標準偏差は平均粒子径に関する値である。 [0059] プレート加熱処理した比較例 3の豆粉乳は、蒸気による直接高温加熱処理を施し た実施例 1の懸濁液に比べ、ざらつきがあり、風味も良くなかった。 The standard deviation is a value related to the average particle diameter. [0059] The soy milk powder of Comparative Example 3, which had been subjected to plate heat treatment, was rougher and less flavorful than the suspension of Example 1, which had been subjected to direct high temperature heat treatment with steam.
[0060] 颺実施例 4 (発酵豆粉乳の製造) [0060] Example 4 (Production of Fermented Soymilk)
実施例 3において、加熱条件を加熱温度 145°C、加熱時間 16秒および 36秒として蒸 気による直接高温処琏をし、製造された豆粉乳を用いて乳酸菌で発酵を行った。 乳酸菌スターターを 0.016%になるように豆粉乳に攪拌しながら添加し、 42°C、 6Η ' 間、 ρΗ4.6まで発酵を行った。発酵後、発酵物に 50%乳酸を加えて発酵物の pHを 4 . 3に調整し、均質機 (APV社製)で lOMPaで均質ィヒ処理した。  In Example 3, direct high temperature treatment with steam was performed under the heating conditions of heating temperature 145 ° C, heating time 16 seconds and 36 seconds, and fermentation was performed with lactic acid bacteria using the produced soymilk. Lactic acid bacteria starter was added to soy milk powder with stirring to 0.016%, and the fermentation was performed at 42 ° C for 6 hours and up to ρΗ4.6. After fermentation, 50% lactic acid was added to the fermented product to adjust the pH of the fermented product to 4.3, and homogenized with lOMPa using a homogenizer (APV).
均質化後、発酵液を再度スチームインジェクション方式の直接高温加熱装置 (岩井 機械工業 (株)製)に供給し、 144°C、 4秒の加熱処理を行い、発酵を止めると同時に乳 酸菌の生物的活性を止め、発酵豆粉乳を得た。  After homogenization, the fermented liquor is again supplied to the steam injection type direct high-temperature heating device (Iwai Kikai Kogyo Co., Ltd.) and subjected to heat treatment at 144 ° C for 4 seconds. Biological activity was stopped and fermented soymilk was obtained.
得られた発酵豆粉乳について、それぞれ粘度、平均粒子径、酸度を測定し、さらに 食感のざらつきについて評価した。  The obtained fermented soymilk was measured for viscosity, average particle size, and acidity, respectively, and evaluated for texture.
[0061] [表 6] ' [0061] [Table 6] '
Figure imgf000017_0001
Figure imgf000017_0001
※ 標準偏差は粒子径に関する値である。  * Standard deviation is a value related to particle size.
[0062] 豆粉乳を乳酸菌で発酵させることにより、風味が非常に良好でざらつきのない発酵 豆粉乳を調製することができた。発酵前後における豆粉乳の舌触りとざらつき'風味 の変化はほとんど現れないことから、豆粉乳のざらつきが発酵豆粉乳のざらつきにも 影響を及ぼすことが確認された。  [0062] By fermenting soymilk with lactic acid bacteria, it was possible to prepare fermented soymilk with very good flavor and no roughness. The change in the texture and taste of the soy milk before and after the fermentation showed almost no change. Thus, it was confirmed that the roughness of the soy milk has an effect on the roughness of the fermented soy milk.
[0063] 騸実施例 5 (発酵豆粉乳の製造 2)  0063 Example 5 (Production of fermented soy milk powder 2)
実施例 3において、加熱条件を加熱温度 149°C、加熱時間 30秒として蒸気による直 接高温処理をし、製造された豆粉乳を用いて乳酸菌で発酵を行った。他の条件は実 施例 4と同様にして発酵豆粉乳を製造した。  In Example 3, direct heating was performed with steam at a heating temperature of 149 ° C. and a heating time of 30 seconds, and fermentation was performed with lactic acid bacteria using the produced soymilk. The other conditions were the same as in Example 4 to produce fermented soymilk.
[0064] '騮実施例 6 (発酵豆粉乳の製造 3)  [0064] '騮 Example 6 (Production of Fermented Soymilk 3)
実施例 2と同様にして得られた均質ィ匕した大豆粉の懸濁液を、スチームインジェク シヨン方式の直接高温加熱装置 (岩井機械工業 (株)製)に供給し、 145°C、 4秒の加熱 殺菌処理を行った後に、この加熱殺菌済みの懸濁液を 42°Cまで冷却し、実施例 5と 同様にして乳酸菌発酵し、発酵液をスチームインジヱクシヨン方式の直接高温加熱 装置 (TANAKA FOOD MACHINERY社製)に供給し、 149°C、 30秒の加熱処理を行 い、発酵豆粉乳を得た。 ' A homogenized soy flour suspension obtained in the same manner as in Example 2 was used as a steam injector. Supplied to a Chillon-type direct high-temperature heating device (Iwai Kikai Kogyo Co., Ltd.), sterilized at 145 ° C for 4 seconds, and then this heat-sterilized suspension was cooled to 42 ° C. In the same manner as in Example 5, lactic acid bacteria were fermented, and the fermented liquid was supplied to a steam-incubation-type direct high-temperature heating device (TANAKA FOOD MACHINERY) and subjected to heat treatment at 149 ° C for 30 seconds. Fermented soymilk was obtained. '
[0065] 実施例 5, 6で得られた発酵豆粉乳について、実施例 1と同様にして粘度及び平均 粒子径を測定し、発酵後のざらつきについて評価した。  [0065] For the fermented soymilk obtained in Examples 5 and 6, the viscosity and average particle size were measured in the same manner as in Example 1 to evaluate the roughness after fermentation.
[0066] [表 7]  [0066] [Table 7]
Figure imgf000018_0001
Figure imgf000018_0001
標準偏差は粒子径に関する値である。 表 7に示すとおり、実施例 6は実施例 5に比べると粘度と平均粒子径が大きくなる傾 向にあつたが、実施例 5, 6の間にざらつきの差はなぐ実施例 6の方が粘度が大きく なった分多少粘りを感じる程度であった。  The standard deviation is a value related to the particle size. As shown in Table 7, Example 6 has a tendency to increase the viscosity and average particle size compared to Example 5, but Example 6 has a difference in roughness between Examples 5 and 6. The degree of stickiness was somewhat felt as the viscosity increased.
このように、乾式粉砕した大豆粉の懸濁液に対する加熱温度が 1.20°C以上、加熱 時間が 10秒を超える蒸気による直接高温加熱処理は、発酵前後のいずれで施して も、発酵豆粉乳の粒子径を細力べ滑らかにし、粉っぽさを軽減させた。  In this way, direct high-temperature heat treatment with steam for a dry-milled soy flour suspension with a heating temperature of 1.20 ° C or higher and a heating time of more than 10 seconds can be performed either before or after fermentation. The particle size was smoothed to reduce powderiness.
達替え用紙麵 26) Delivery paper 麵 26)

Claims

請求の範囲 The scope of the claims
[1] 豆類を乾式粉砕した豆粉を含む懸濁液を調製すること、及び少なくとも該懸濁液中 のオカラ分に対して、加熱温度が 120°C以上、加熱時間が 10秒を超える蒸気による 直接高温加熱処理を施すことを特徴とする豆粉乳の製造方法。  [1] Preparing a suspension containing bean powder obtained by dry-pulverizing beans, and steam with a heating temperature of 120 ° C or more and a heating time exceeding 10 seconds for at least the okara content in the suspension A method for producing soy milk powder, characterized by subjecting to direct high-temperature heat treatment.
[2] 前記豆類が大豆である請求項 1記載の豆粉乳の製造方法。 [2] The method for producing soybean milk according to claim 1, wherein the beans are soybeans.
[3] 加熱温度が 120〜165°Cである請求項 1記載の豆粉乳の製造方法。 [3] The method for producing soymilk according to claim 1, wherein the heating temperature is 120 to 165 ° C.
[4] 加熱時間が 15〜80秒である請求項 1記載の豆粉乳の製造方法。 [4] The method for producing soymilk according to claim 1, wherein the heating time is 15 to 80 seconds.
[5] 請求項 1記載の豆粉乳を配合することを特徴とする飲食品の製造方法。 [5] A method for producing a food or drink, comprising the soymilk according to claim 1.
[6] 請求項 1記載の製造方法により得られた豆粉乳を微生物で発酵させることを特徴とす る発酵豆粉乳の製造方法。 [6] A method for producing fermented soymilk, characterized in that the soymilk obtained by the production method according to [1] is fermented with microorganisms.
[7] 請求項 1記載の豆粉乳の製造法において、さらに微生物による発酵工程を有するこ とを特徴とする発酵豆粉乳の製造方法。 [7] The method for producing fermented soymilk according to claim 1, further comprising a fermentation step using microorganisms.
[8] 豆粉の懸濁液を調製し、蒸気による直接高温加熱処理を施す前に微生物による発 酵を行う請求項 7記載の発酵豆粉乳の製造方法。 [8] The method for producing fermented soymilk according to claim 7, wherein a suspension of the soy flour is prepared, and fermentation with microorganisms is performed before direct high-temperature heat treatment with steam.
[9] 豆類を乾式粉砕した豆粉を含む懸濁液を調製すること、及び少なくとも該懸濁液中 のオカラ分に対して、加熱温度が 120°C以上、加熱時間が 10秒を超える蒸気による 直接高温加熱処理を施すことを特徴とする豆粉の微細化方法。 [9] Preparing a suspension containing bean powder obtained by dry-pulverizing beans, and steam with a heating temperature of 120 ° C or more and a heating time of more than 10 seconds for at least the okara content in the suspension A method for refining soybean powder characterized by subjecting to direct high-temperature heat treatment.
PCT/JP2007/056503 2006-03-28 2007-03-27 Process for producing powdery soy milk and application of the same WO2007116772A1 (en)

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