WO2013073424A1 - Liquid fermented milk and method for producing same - Google Patents

Liquid fermented milk and method for producing same Download PDF

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Publication number
WO2013073424A1
WO2013073424A1 PCT/JP2012/078793 JP2012078793W WO2013073424A1 WO 2013073424 A1 WO2013073424 A1 WO 2013073424A1 JP 2012078793 W JP2012078793 W JP 2012078793W WO 2013073424 A1 WO2013073424 A1 WO 2013073424A1
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Prior art keywords
fermented milk
fermentation
lactic acid
liquid
milk
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PCT/JP2012/078793
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French (fr)
Japanese (ja)
Inventor
祐子 後藤
伊代 田中
滋 山田
雅弘 北島
Original Assignee
株式会社明治
オリエンタル酵母工業株式会社
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Application filed by 株式会社明治, オリエンタル酵母工業株式会社 filed Critical 株式会社明治
Priority to SG11201402248QA priority Critical patent/SG11201402248QA/en
Priority to JP2013544225A priority patent/JP6181557B2/en
Priority to CN201280045513.3A priority patent/CN103813715A/en
Publication of WO2013073424A1 publication Critical patent/WO2013073424A1/en

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    • 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
    • A23C9/00Milk preparations; Milk powder or milk powder preparations
    • A23C9/12Fermented milk preparations; Treatment using microorganisms or enzymes
    • A23C9/127Fermented milk preparations; Treatment using microorganisms or enzymes using microorganisms of the genus lactobacteriaceae and other microorganisms or enzymes, e.g. kefir, koumiss

Definitions

  • the present invention relates to liquid fermented milk and a method for producing the same.
  • Patent Document 1 discloses a step of partially degrading lactose contained in animal milk by lactose-degrading enzyme, a step of performing lactic acid fermentation with lactic acid bacteria that do not accumulate galactose in the medium, and fermented milk obtained by the lactic acid fermentation.
  • a method for producing a kefir-like dairy product is described, which comprises a step of subjecting to a lactose-fermenting yeast and subjecting the alcohol fermentation to substantially the disappearance of lactose in the medium.
  • Patent Document 2 describes Examples 5-1 to 5-3, where skim milk powder is added to deionized water, sterilized, inoculated with a lactic acid strain, fermented at 37 ° C. for 24 hours, and fermented milk is obtained. It is described that, after adding HF liquid sugar and fructose to this fermented milk, a yeast starter was inoculated, and fermentation was performed at various fermentation temperatures and fermentation times to obtain a fermented product. In addition, in Patent Document 2, when the sensory evaluation was performed on the fermented product obtained in the above-mentioned Examples, there was a milk-like flavor with reduced sweetness, and a unique aroma that matched yogurt odor and fruit odor. It is described that it was obtained.
  • Example 1 of Patent Document 3 after adding a non-fat dry milk culture solution of lactic acid bacteria starter to a whey powder solution and standing fermentation, a glucose solution and a yeast extract solution are added to the obtained lactic acid bacteria fermentation solution. Then, it is described that a culture solution of yeast starter was added thereto, and aerated and stirred culture was performed at 200 rpm, 30 ° C. for 20 hours while blowing sterile air to obtain lactic acid bacteria / yeast fermented whey.
  • liquid fermented milk In the production of liquid fermented milk, generally, after adding lactic acid bacteria to the raw material of fermented milk (for example, skim milk powder, raw milk, etc.), it is allowed to stand and form a card that is a lactic acid fermentation product, The card is finely crushed to obtain liquid fermented milk.
  • the present inventor examined the combined use of lactic acid bacteria and yeast in order to give a rich fragrance and the like when developing liquid fermented milk. However, if lactic acid bacteria and yeast are added to the raw material of fermented milk at the same time, followed by stationary fermentation, solids will float due to the carbon dioxide produced by the yeast, and subsequent processing such as homogenization and sterilization Turned out to be impossible.
  • an object of the present invention is to provide a liquid fermented milk having a rich fragrance and the like derived from fermentation by yeast using lactic acid bacteria and yeast, and having a good appearance and drinking mouth, and a method for producing the same.
  • the present inventor added lactic acid bacteria to the raw material of fermented milk, allowed to stand and ferment, then added yeast and stirred and fermented. It is found that liquid fermented milk having a good appearance and drinking mouth can be obtained without having coarse particles observed with the naked eye after completion of stirring and fermentation, without causing solid content to float, The present invention has been completed.
  • the present invention provides the following [1] to [9].
  • [1] (A) After adding lactic acid bacteria to the raw material of fermented milk, static fermentation is performed to obtain a lactic acid fermentation product by static fermentation; and (B) after adding yeast to the lactic acid fermentation product, A method for producing liquid fermented milk, comprising a step of stirring and fermenting to obtain liquid fermented milk.
  • the stationary fermentation in the step (A) is performed at a temperature of 20 to 44 ° C.
  • the stirring fermentation in the step (B) is performed at a temperature of 20 to 44 ° C. 2]
  • the manufacturing method of the liquid fermented milk in any one.
  • a beverage comprising the liquid fermented milk according to [7] or [8] above, wherein the median diameter of particles constituting the solid content of the beverage is 2.5 ⁇ m or less.
  • liquid fermented milk of the present invention stationary fermentation is carried out after the addition of lactic acid bacteria, and then stirring fermentation is carried out after the addition of yeast, so that the solid content found when only stationary fermentation is carried out.
  • the solid particles which are not floated or agitation culture, are not coarsened, and a liquid fermented milk having a uniform liquid appearance and a good drinking mouth can be obtained.
  • yeast since yeast is used in addition to lactic acid bacteria, the sourness derived from lactic acid, which is a fermentation product of lactic acid bacteria, and the richness derived from the fermentation product of yeast.
  • a liquid fermented milk having a fragrance, a savory flavor, and a slight alcohol flavor can be obtained.
  • the liquid fermented milk of this invention has an alcohol content less than 0.5 weight%, it can use for drinking as a non-alcoholic drink.
  • the liquid fermented milk of the present invention can be used for drinking alone or after being mixed with other materials such as sugar and water.
  • the processed liquid fermented milk and other materials for example, water, sugar, etc.
  • the resulting mixture is mixed.
  • By further performing the homogenization treatment it is possible to obtain a beverage having an appearance as a homogeneous liquid material, a good drinking mouth, and palatability.
  • This beverage has a high commercial value without causing a precipitate (solid content) at the bottom or the like of a container for containing the beverage.
  • the method for producing liquid fermented milk of the present invention includes (A) a stationary fermentation step in which a lactic acid bacterium is added to the raw material of fermented milk, followed by stationary fermentation to obtain a lactic acid fermentation product, and (B) step (A). After adding yeast to the lactic acid fermentation product obtained in step 1, the mixture is stirred and fermented to obtain a liquid fermented milk. Moreover, the manufacturing method of the liquid fermented milk of this invention performs the homogenization process with respect to the liquid fermented milk obtained by (C) process (B), and the homogenization process of obtaining the liquid fermented milk after the homogenization process, Can be included. Hereinafter, each step will be described in detail.
  • Step (A) is a step of obtaining a lactic acid fermentation product by adding lactic acid bacteria to the raw material of fermented milk and then allowing it to stand and ferment.
  • the raw material of the fermented milk may be any material that can obtain a liquid product having a nonfat milk solid content of 5% by weight or more, preferably 8% by weight or more at the end of the stirring fermentation in the step (B). .
  • any milk can be used without particular limitation as long as it is milk such as animal milk (milk, sheep milk, goat milk, buffalo milk, etc.) and soy milk and processed products thereof,
  • whey powder produced using whey as a raw material, whey protein concentrate, and the like can be used in addition to skim milk powder, skim milk, raw milk, milk protein concentrate, and the like.
  • the main raw material of fermented milk can use said 1 type individually or in combination of 2 or more types.
  • any known foods and food additives that do not significantly delay the fermentation time can be used without particular limitation. Examples include glucose and yeast extract used in the examples.
  • the main raw material of fermented milk means the raw material derived from milk.
  • the auxiliary raw material of fermented milk means raw materials other than milk-derived raw materials (however, excluding lactic acid bacteria and yeast).
  • the ratio of the main raw material in the whole quantity of the raw material of fermented milk is not specifically limited.
  • Water can be added to the raw material of fermented milk as needed. For example, when only skim milk powder is used as the main raw material of fermented milk, it is preferable to add 50 to 150 parts by weight of water to 10 parts by weight of skim milk powder.
  • lactic acid bacteria When adding water, lactic acid bacteria may be added to the mixture of fermented milk raw material and water, or water may be added to the mixture of fermented milk raw material and lactic acid bacteria, and fermented milk. The raw material, water and lactic acid bacteria may be mixed at the same time.
  • the lactic acid bacterium is not particularly limited as long as it contains a lactic acid bacterium that is a living bacterium, but usually a liquid product obtained by culturing lactic acid bacterium in the presence of a nutrient source is used.
  • a liquid material is, for example, a mixture containing a nutrient source such as skim milk powder, water, and lactic acid bacteria at a predetermined temperature (for example, 35 to 40 ° C.) for a predetermined time (for example, 10 to 20 hours).
  • lactic acid bacteria in the lactic acid bacteria is not particularly limited, but is, for example, 1 ⁇ 10 7 to 1 ⁇ 10 9 cfu / ml.
  • the lactic acid bacteria one or two or more kinds of lactic acid bacteria selected from general lactic acid bacteria used for producing fermented milk can be used.
  • Examples of lactic acid bacteria include lactic acid bacteria belonging to the genus Lactobacillus and lactic acid bacteria belonging to the genus Streptococcus.
  • Examples of lactic acid bacteria belonging to the genus Lactobacillus include Lactobacillus helveticus, Lactobacillus delbruekii subsp. Bulgaricus, Lactobacillus acidophilus (Lactobacillus acidophilus), and the like. Can be mentioned.
  • Lactobacillus helveticus is preferable from the viewpoint of preventing the growth of contaminating microorganisms even in fermented milk that requires fermentation for a long time because the acidity increases more than other lactic acid bacteria.
  • Lactobacillus helveticus can obtain a commercial item easily.
  • Examples of Streptococcus lactic acid bacteria include Streptococcus thermophilus.
  • stationary fermentation means fermenting in the state which left still, without stirring.
  • the time for stationary fermentation is preferably 3 to 45 hours, more preferably 5 to 45 hours, still more preferably 8 to 45 hours, still more preferably 10 to 40 hours, still more preferably 15 to 35 hours, and particularly preferably 20 hours. ⁇ 30 hours.
  • the temperature of the stationary fermentation is preferably 25 to 50 ° C, more preferably 30 to 45 ° C, still more preferably 32 to 43 ° C, and particularly preferably 35 to 40 ° C.
  • curd which is a fermentation product is obtained by stationary fermentation. This card is finely crushed in the step (B) to become a liquid material.
  • Step (B) is a step of adding liquid yeast to the lactic acid fermentation product obtained in step (A), followed by stirring and fermentation to obtain liquid fermented milk.
  • the yeast is not particularly limited as long as it contains yeast that is a living bacterium, and examples thereof include dry yeast (dry yeast). Dry yeast is yeast that is dormant due to drying. Dry yeast can be used in the state of the liquid substance formed, for example by mixing with water. Examples of the yeast include Saccharomyces cerevisiae, Saccharomyces pastrianus, Saccharomyces paradoxus, and Saccharomyces bayanus.
  • Saccharomyces cerevisiae is preferred from the viewpoint of versatility because it is a commercially available product and can be easily obtained.
  • Examples of commercially available products of Saccharomyces cerevisiae include Saff Instant Dry Yeast Red (manufactured by Lesaffre), Oriental Dry Yeast (manufactured by Oriental Yeast Co., Ltd.), and the like.
  • Yeast can be used individually by 1 type or in combination of 2 or more types. Since the lactic acid fermentation product obtained in the step (A) is obtained by stationary fermentation, it is not liquid but has a solid card form.
  • the curd may be finely crushed and then yeast may be added. Alternatively, after adding yeast to the curd, the curd may be finely broken by stirring.
  • the speed of stirring is not particularly limited, but is preferably 10 to 150 rpm, more preferably from the viewpoint of crushing the curd formed by the action of lactic acid bacteria by shearing, removing carbon dioxide produced by yeast, and suppressing the floating of the solid matter. Is 30 to 100 rpm.
  • the stirring may be either continuous stirring or intermittent stirring, but continuous stirring is preferable from the viewpoint of removal of carbon dioxide gas produced by yeast and suppression of solid floating.
  • the stirring fermentation time is preferably 20 to 50 hours, more preferably 25 to 45 hours, still more preferably 30 to 40 hours, and particularly preferably 35 to 40 hours.
  • the temperature of the stirring fermentation is preferably 20 to 44 ° C, more preferably 25 to 42 ° C, still more preferably 30 to 40 ° C, and particularly preferably 35 to 38 ° C.
  • the total of the stationary fermentation time in the step (A) and the stirring fermentation time in the step (B) is preferably 40 to 85 hours, more preferably 45 to 45 hours from the viewpoint of the flavor and practicality of the liquid fermented milk. 80 hours, more preferably 50 to 75 hours, further preferably 55 to 70 hours, particularly preferably 60 to 70 hours.
  • finish of stirring fermentation lactic acid etc. can be added and the lactic acid acidity of liquid fermented milk can be adjusted.
  • the lactic acid acidity of the liquid fermented milk is preferably 2.1 to 2.7% from the viewpoint of giving an appropriate acidity.
  • Step (C) is a step of homogenizing the liquid fermented milk obtained in step (B).
  • the homogenization is not limited to the homogenization process using a homogenizer (homogenizer), but also includes known shearing processes such as stirring, a homomixer, and an extruder.
  • a homogenizer homogenizer
  • the homogenization treatment is performed at a pressure of 7 to 13 MPa as the first-stage homogenization treatment, and then at a pressure of 4 to 6 MPa as the second-stage homogenization treatment. This is done by applying pressure.
  • the homogenization process combining the first stage and the second stage may be performed only once, or the homogenization process combining the first stage and the second stage may be performed twice or more. Good.
  • heat sterilization and cooling may be performed, and then the homogenization process combining the first stage and the second stage may be further performed.
  • the median diameter of the particles constituting the solid content contained in the treated liquid fermented milk obtained in the step (C) is preferably 30 ⁇ m or less, more preferably 25 ⁇ m or less, further preferably 20 ⁇ m or less, particularly preferably 15 ⁇ m. It is as follows.
  • the liquid fermented milk obtained in the step (C) may be used alone for drinking, or may be mixed with other components for drinking.
  • examples of other components mixed with the liquid fermented milk include sweeteners such as sugar for imparting sweetness, acidity adjusting agents such as lactic acid, salt, fragrance, and fruit juice.
  • a homogenization process can also be performed with respect to the mixture of liquid fermented milk and another component.
  • the homogenization process in this case may be only one stage or a plurality of stages (for example, combined use of the first and second stages).
  • the total pressure of the homogenization treatment is preferably 10 to 20 MPa.
  • the median diameter of the particles constituting the solid content contained in the homogenized beverage is preferably 2.5 ⁇ m or less, more preferably 2. It is 0 ⁇ m or less, more preferably 1.5 ⁇ m or less, and particularly preferably 1.0 ⁇ m or less.
  • Example 1 (1) Preparation of lactic acid bacteria starter Nonfat dry milk (manufactured by Meiji Co., Ltd.), powdered yeast extract (trade name: yeast extract T-154, manufactured by Oriental Yeast Co., Ltd.), lactic acid bacteria (Lactobacillus helveticus, “FLAV 54 LYO 5D” manufactured by Danisco Co., Ltd.) ) And water were used to prepare lactic acid bacteria starters.
  • This lactic acid bacteria starter contained skim milk powder 10% by weight, water 90% by weight, yeast extract 0.002% by weight, and lactic acid bacteria 3 ⁇ 10 8 cfu / ml.
  • the lactic acid acidity of this lactic acid bacteria starter was 1.6%.
  • (2) Preparation of yeast starter Dry yeast (trade name: Saff Instant Dry Yeast Red, manufactured by Lesaffre) was added to 40 ° C sterilized water, and the mixture was allowed to stand for 20 minutes. Used in the preparation of fermented milk.
  • the stirrer is started and the curd is crushed.
  • the yeast starter is converted to the weight of the dry yeast to be 0.01 parts by weight (total 100 parts by weight above).
  • Stirring was continuously performed at 60 rpm.
  • the lactic acid acidity of the obtained liquid fermented milk was confirmed to be 2.4%. Therefore, lactic acid was added to adjust the acidity to 2.5%.
  • the liquid fermented milk was subjected to a homogenization treatment of 10 MPa as the first stage and 5 MPa as the second stage. The liquid fermented milk after the treatment was sterilized at 75 ° C. for 30 minutes and then cooled to 10 ° C.
  • liquid fermented milk In the obtained liquid fermented milk, the total solid content is 11.6% by weight, the non-fat milk solid content is 10.4% by weight, the lactic acid acidity is 2.5%, and the pH is 3. 3.
  • liquid fermented milk is a homogeneous, milky white liquid that does not contain floating solids and coarse particles, and has a sourness derived from lactic acid fermentation and a flavor derived from yeast fermentation (such as mellowness and fruit). Fragrance) and a slight alcohol fragrance. In the liquid fermented milk, no off-flavor, off-flavor, or foreign matter was observed.
  • aqueous solution 10.112 parts by weight of sugar, 0.063 parts by weight of lactic acid (trade name: 50% lactic acid, manufactured by Daiichi Fine Chemical Co., Ltd.), 0.004 parts by weight of sodium chloride, and a liquid that has been treated with the above homomixer 7.6 parts by weight of fermented milk (a total of 100 parts by weight above) was added to obtain a mixed solution. After heating this mixed liquid to 60 degreeC, it homogenized by the pressure of a total of 15 MPa with a homogenizer, and then cooled to 10 degrees C or less. The mixed liquid after cooling was heated at 110 ° C. for 1 minute using an autoclave to obtain a beverage. With respect to this beverage, the median diameter of the particles constituting the solid content was measured and found to be 1.0 ⁇ m. In addition, the simulated beverage was milky white and homogeneous liquid without any solid surface floating or abnormal appearance due to coarse particles.
  • Example 2 The experiment was conducted in the same manner as in Example 1 except that the time for stationary fermentation was set at 24 hours and the time for stirring fermentation was set at 40 hours.
  • the liquid fermented milk before the homogenization treatment like Example 1, is a homogeneous, milky white liquid that does not contain floating solids and coarse particles, and has a sourness derived from lactic acid fermentation. I had it.
  • the median diameter of the particles constituting the solid content of the liquid fermented milk after the homogenization treatment was 10 ⁇ m.
  • grains of the obtained drink was 0.8 micrometer.
  • this beverage was milky white and homogeneous liquid with no precipitation at the bottom of the container containing the simulated beverage.
  • Example 3 The experiment was conducted in the same manner as in Example 1 except that the time for stationary fermentation was set to 5 hours and the time for stirring fermentation was set to 59 hours.
  • the particle size of the particles is slightly large, and although sedimentation of coarse particles was seen when left for a long time, it did not contain any floating solids, and was a milky white liquid, It had a sour taste derived from lactic acid fermentation.
  • no off-flavor, off-flavor, or foreign matter was observed.
  • grains of the obtained simulation drink was 2.1 micrometers. A slight amount of precipitate was observed at the bottom of the container containing the beverage.
  • Example 1 Experiments were carried out in the same manner as in Example 1 except that a lactic acid bacteria starter and a yeast starter were added simultaneously, the time of stationary fermentation was set to 64 hours, and stirring fermentation was not performed. As a result, in liquid fermented milk, the solid content floated on the liquid surface at the end of fermentation, dried and hardened, and the appearance was poor. For this reason, the solid content was pulverized manually and then homogenized. Moreover, the median diameter of the particle
  • Example 2 Experiments were conducted in the same manner as in Example 1 except that a lactic acid bacteria starter and a yeast starter were added simultaneously, the time for stirring fermentation was set to 64 hours, and stationary fermentation was not performed. As a result, at the end of the fermentation of the liquid fermented milk, although the solid content did not rise to the liquid surface, an abnormality in the appearance due to the sedimentation of the coarse particles was observed. The subsequent treatment of the liquid fermented milk was carried out including the coarse particles that settled. Moreover, the median diameter of the particle
  • Example 3 Experiments were carried out in the same manner as in Example 1 except that the lactic acid bacteria starter and the yeast starter were added simultaneously, the time for stationary fermentation was set at 24 hours, and the time for stirring fermentation was set at 40 hours.
  • the liquid fermented milk had a solid content that floated on the liquid surface, dried and hardened at the end of fermentation, and had a poor appearance. For this reason, the solid content was pulverized manually and then homogenized.
  • grains of the obtained simulation drink was 2.0 micrometers. Some precipitates were observed at the bottom of the container for containing the beverage. The results are shown in Table 1. In Table 1, regarding the comprehensive evaluation, “ ⁇ ” represents “very good”, “ ⁇ ” represents “good”, and “x” represents “bad”.

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Abstract

Provided is a method for producing a liquid fermented milk having favorable flavor and appearance, having no occurrence of solid content floating up, having no contained large particles observed with the naked eye after completion of stirring fermentation, and having a rich aroma and the like deriving from fermentation by yeast. The method for producing a liquid fermented milk contains: (A) a static fermentation step that, after adding a lactobacillus to the starting material for fermented milk, causes static fermentation to obtain a lactic acid fermentation product; (B) a stirring fermentation step that, after adding yeast to the lactic acid fermentation product obtained in step (A), causes stirring fermentation to obtain a liquid fermented milk; and (C) a homogenization step for subjecting the liquid fermented milk obtained in step (B) to homogenization processing.

Description

液状発酵乳及びその製造方法Liquid fermented milk and method for producing the same
 本発明は、液状発酵乳及びその製造方法に関する。 The present invention relates to liquid fermented milk and a method for producing the same.
 発酵乳の製造に際して、酵母による独特の風味の付与等を目的として、乳酸菌及び酵母を併用する技術が知られている。
 例えば、特許文献1に、乳糖分解酵素により獣乳中に含まれる乳糖を部分的に分解する工程、ガラクトースを培地中に蓄積しない乳酸菌による乳酸発酵を行う工程および当該乳酸発酵により得られた発酵乳を乳糖発酵性酵母によりアルコール発酵する工程を含み、上記アルコール発酵を培地中の乳糖が実質的に消失するまで行うことを特徴とするケフィア様乳製品の製造法が記載されている。
 また、特許文献2に、実施例5-1~5-3として、脱イオン水に脱脂粉乳を添加し、殺菌後、乳酸菌株を接種し、37℃、24時間の発酵を行い、発酵乳を得たこと、及び、この発酵乳にHF液糖及び果糖を添加後、酵母スターターを接種し、様々な発酵温度及び発酵時間で発酵を行ない、発酵物を得たことが記載されている。また、特許文献2には、前記の実施例で得られた発酵物について官能評価を行ったところ、甘さを抑えた乳酒様の風味、及びヨーグルト臭と果実臭のマッチした独特の香りが得られたことが記載されている。
In the production of fermented milk, a technique is known in which lactic acid bacteria and yeast are used in combination for the purpose of imparting a unique flavor by yeast.
For example, Patent Document 1 discloses a step of partially degrading lactose contained in animal milk by lactose-degrading enzyme, a step of performing lactic acid fermentation with lactic acid bacteria that do not accumulate galactose in the medium, and fermented milk obtained by the lactic acid fermentation. A method for producing a kefir-like dairy product is described, which comprises a step of subjecting to a lactose-fermenting yeast and subjecting the alcohol fermentation to substantially the disappearance of lactose in the medium.
Patent Document 2 describes Examples 5-1 to 5-3, where skim milk powder is added to deionized water, sterilized, inoculated with a lactic acid strain, fermented at 37 ° C. for 24 hours, and fermented milk is obtained. It is described that, after adding HF liquid sugar and fructose to this fermented milk, a yeast starter was inoculated, and fermentation was performed at various fermentation temperatures and fermentation times to obtain a fermented product. In addition, in Patent Document 2, when the sensory evaluation was performed on the fermented product obtained in the above-mentioned Examples, there was a milk-like flavor with reduced sweetness, and a unique aroma that matched yogurt odor and fruit odor. It is described that it was obtained.
 一方、発酵方法として、静置発酵と撹拌発酵を組み合わせた方法が知られている。
 例えば、特許文献3の実施例1に、ホエーパウダー溶液に、乳酸菌スターターの脱脂粉乳培養液を加えて、静置発酵した後、得られた乳酸菌発酵液に、グルコース溶液および酵母エキス溶液を添加し、次いで、これに酵母スターターの培養液を加え、無菌エアーを吹き込みながら、200rpm、30℃、20時間の通気攪拌培養を行い、乳酸菌・酵母発酵乳清液を得たことが記載されている。
On the other hand, as a fermentation method, a method combining stationary fermentation and stirring fermentation is known.
For example, in Example 1 of Patent Document 3, after adding a non-fat dry milk culture solution of lactic acid bacteria starter to a whey powder solution and standing fermentation, a glucose solution and a yeast extract solution are added to the obtained lactic acid bacteria fermentation solution. Then, it is described that a culture solution of yeast starter was added thereto, and aerated and stirred culture was performed at 200 rpm, 30 ° C. for 20 hours while blowing sterile air to obtain lactic acid bacteria / yeast fermented whey.
特開平10-56961号公報Japanese Patent Laid-Open No. 10-56961 特許第3929630号公報Japanese Patent No. 3929630 特開平7-75521号公報JP-A-7-75521
 液状発酵乳の製造に際しては、一般に、発酵乳の原料(例えば、脱脂粉乳、生乳等)に乳酸菌を添加した後に、静置発酵させて、乳酸発酵生成物であるカードを形成させ、次いで、このカードを細かく砕いて、液状発酵乳を得ている。
 本発明者は、液状発酵乳の開発に際し、芳醇な香り等を与えるために、乳酸菌と酵母を併用することを検討した。
 しかし、発酵乳の原料に、乳酸菌及び酵母を同時に添加し、その後、静置発酵させると、酵母の産生する二酸化炭素によって固形物が浮上してしまい、その後の均質化処理、殺菌処理などの処理が不可能になることが判明した。
 また、発酵乳の原料に乳酸菌を添加し、静置発酵させて、カードを形成させた後、このカードを細かく砕いて得られた液状物と、酵母を混合し、その後、静置発酵させた場合には、酵母の産生する二酸化炭素によって固形物が浮上してしまい、その後の均質化処理、殺菌処理などの処理が不可能になることが判明した。
 そこで、本発明は、乳酸菌及び酵母を用いて、酵母による発酵に由来する芳醇な香り等を有するとともに、外観及び飲み口が良好な液状発酵乳及びその製造方法を提供することを目的とする。
In the production of liquid fermented milk, generally, after adding lactic acid bacteria to the raw material of fermented milk (for example, skim milk powder, raw milk, etc.), it is allowed to stand and form a card that is a lactic acid fermentation product, The card is finely crushed to obtain liquid fermented milk.
The present inventor examined the combined use of lactic acid bacteria and yeast in order to give a rich fragrance and the like when developing liquid fermented milk.
However, if lactic acid bacteria and yeast are added to the raw material of fermented milk at the same time, followed by stationary fermentation, solids will float due to the carbon dioxide produced by the yeast, and subsequent processing such as homogenization and sterilization Turned out to be impossible.
Moreover, after adding lactic acid bacteria to the raw material of fermented milk and making it leave and ferment and forming a card | curd, the liquid obtained by crushing this card | curd finely and yeast were mixed, and it was made to leave still fermentation after that. In some cases, it was found that the solid matter floated by the carbon dioxide produced by the yeast, making it impossible to perform subsequent homogenization and sterilization treatments.
Therefore, an object of the present invention is to provide a liquid fermented milk having a rich fragrance and the like derived from fermentation by yeast using lactic acid bacteria and yeast, and having a good appearance and drinking mouth, and a method for producing the same.
 本発明者は、上記課題を解決するために鋭意検討した結果、発酵乳の原料に乳酸菌を添加し、静置発酵させた後、酵母を添加し、撹拌発酵させれば、酵母による発酵に由来する芳醇な香り等を有するとともに、攪拌発酵終了後に肉眼で観察される粗大粒子を含まず、固形分の浮上も生じない、外観及び飲み口が良好な液状発酵乳を得ることができることを見出し、本発明を完成した。 As a result of intensive studies to solve the above-mentioned problems, the present inventor added lactic acid bacteria to the raw material of fermented milk, allowed to stand and ferment, then added yeast and stirred and fermented. It is found that liquid fermented milk having a good appearance and drinking mouth can be obtained without having coarse particles observed with the naked eye after completion of stirring and fermentation, without causing solid content to float, The present invention has been completed.
 すなわち、本発明は、以下の[1]~[9]を提供するものである。
[1] (A)発酵乳の原料に乳酸菌を添加した後、静置発酵させて、乳酸発酵生成物を得る静置発酵工程と、(B)上記乳酸発酵生成物に酵母を添加した後、撹拌発酵させて、液状発酵乳を得る撹拌発酵工程、を含む液状発酵乳の製造方法。
[2] 工程(A)における静置発酵を、3~45時間で行ない、かつ、工程(B)における撹拌発酵を、20~65時間で行なう、上記[1]に記載の液状発酵乳の製造方法。
[3] 工程(A)における静置発酵を、20~44℃の温度下で行ない、かつ、工程(B)における撹拌発酵を、20~44℃の温度下で行なう、上記[1]又は[2]に記載の液状発酵乳の製造方法。
[4] 工程(A)における上記静置発酵の開始時から、工程(B)における上記撹拌発酵の終了時までの間、酵母スターター以外のものを添加しない、上記[1]~[3]のいずれかに記載の液状発酵乳の製造方法。
[5] 上記発酵乳の原料が、脱脂粉乳、脱脂乳、生乳、及び乳タンパク質濃縮物からなる群より選ばれる一種以上を含む、上記[1]~[4]のいずれかに記載の液状発酵乳の製造方法。
[6] 工程(B)の後に、(C)上記発酵乳に対して均質化処理を行なう均質化工程、を含む、上記[1]~[5]のいずれかに記載の液状発酵乳の製造方法。
[7] 上記[6]に記載の液状発酵乳の製造方法によって得られた液状発酵乳。
[8] 上記液状発酵乳の固形分を構成する粒子のメディアン径が、30μm以下である上記[7]に記載の液状発酵乳。
[9] 上記[7]又は[8]に記載の液状発酵乳を含む飲料であって、該飲料の固形分を構成する粒子のメディアン径が、2.5μm以下である飲料。
That is, the present invention provides the following [1] to [9].
[1] (A) After adding lactic acid bacteria to the raw material of fermented milk, static fermentation is performed to obtain a lactic acid fermentation product by static fermentation; and (B) after adding yeast to the lactic acid fermentation product, A method for producing liquid fermented milk, comprising a step of stirring and fermenting to obtain liquid fermented milk.
[2] Production of liquid fermented milk according to the above [1], wherein the stationary fermentation in the step (A) is performed in 3 to 45 hours, and the stirring fermentation in the step (B) is performed in 20 to 65 hours. Method.
[3] The stationary fermentation in the step (A) is performed at a temperature of 20 to 44 ° C., and the stirring fermentation in the step (B) is performed at a temperature of 20 to 44 ° C. 2] The manufacturing method of liquid fermented milk of description.
[4] From the start of the stationary fermentation in the step (A) to the end of the stirred fermentation in the step (B), no other than the yeast starter is added. The manufacturing method of the liquid fermented milk in any one.
[5] The liquid fermentation according to any one of [1] to [4] above, wherein the raw material of the fermented milk contains one or more selected from the group consisting of skim milk powder, skim milk, raw milk, and milk protein concentrate. Milk production method.
[6] Production of liquid fermented milk according to any one of [1] to [5], further comprising (C) a homogenization step of performing homogenization treatment on the fermented milk after step (B) Method.
[7] Liquid fermented milk obtained by the method for producing liquid fermented milk according to [6] above.
[8] The liquid fermented milk according to the above [7], wherein the median diameter of the particles constituting the solid content of the liquid fermented milk is 30 μm or less.
[9] A beverage comprising the liquid fermented milk according to [7] or [8] above, wherein the median diameter of particles constituting the solid content of the beverage is 2.5 μm or less.
 本発明の液状発酵乳の製造方法によれば、乳酸菌の添加後に静置発酵させ、次いで、酵母の添加後に、撹拌発酵させているので、静置発酵のみを行なった場合に見られる固形分の浮上や、撹拌培養のみを行なった場合に見られる固形分の粒子の粗大化が生じず、均質な液状物としての外観、及び、良好な飲み口を有する液状発酵乳を得ることができる。
 また、本発明の液状発酵乳の製造方法によれば、乳酸菌に加えて酵母を用いているので、乳酸菌による発酵生成物である乳酸に由来する酸味とともに、酵母による発酵生成物に由来する芳醇な香り、後引きのある風味、及び若干のアルコール香を有する液状発酵乳を得ることができる。なお、本発明の液状発酵乳は、アルコール含量が0.5重量%を下回るため、ノンアルコール飲料として飲用に供することができる。
 本発明の液状発酵乳は、そのまま単独で、または、砂糖、水等の他の材料と混合した後に、飲用に供することができる。
 例えば、本発明で得られる液状発酵乳に対して均質化処理を行った後に、この処理済みの液状発酵乳と他の材料(例えば、水、砂糖等)を混合し、得られた混合物に対して、さらに均質化処理を行うことによって、均質な液状物としての外観と、良好な飲み口と、嗜好性を兼ね備えた飲料を得ることができる。この飲料は、当該飲料を収容する容器の底部等に沈殿物(固形分)を生じさせることがなく、商品価値が高い。
According to the method for producing liquid fermented milk of the present invention, stationary fermentation is carried out after the addition of lactic acid bacteria, and then stirring fermentation is carried out after the addition of yeast, so that the solid content found when only stationary fermentation is carried out. As a result, the solid particles, which are not floated or agitation culture, are not coarsened, and a liquid fermented milk having a uniform liquid appearance and a good drinking mouth can be obtained.
In addition, according to the method for producing liquid fermented milk of the present invention, since yeast is used in addition to lactic acid bacteria, the sourness derived from lactic acid, which is a fermentation product of lactic acid bacteria, and the richness derived from the fermentation product of yeast. A liquid fermented milk having a fragrance, a savory flavor, and a slight alcohol flavor can be obtained. In addition, since the liquid fermented milk of this invention has an alcohol content less than 0.5 weight%, it can use for drinking as a non-alcoholic drink.
The liquid fermented milk of the present invention can be used for drinking alone or after being mixed with other materials such as sugar and water.
For example, after homogenizing the liquid fermented milk obtained in the present invention, the processed liquid fermented milk and other materials (for example, water, sugar, etc.) are mixed, and the resulting mixture is mixed. By further performing the homogenization treatment, it is possible to obtain a beverage having an appearance as a homogeneous liquid material, a good drinking mouth, and palatability. This beverage has a high commercial value without causing a precipitate (solid content) at the bottom or the like of a container for containing the beverage.
 本発明の液状発酵乳の製造方法は、(A)発酵乳の原料に乳酸菌を添加した後、静置発酵させて、乳酸発酵生成物を得る静置発酵工程と、(B)工程(A)で得られた乳酸発酵生成物に酵母を添加した後、撹拌発酵させて、液状発酵乳を得る撹拌発酵工程、を含む。
 また、本発明の液状発酵乳の製造方法は、(C)工程(B)で得られた液状発酵乳に対して均質化処理を行ない、均質化処理済みの液状発酵乳を得る均質化工程、を含むことができる。
 以下、各工程について詳しく説明する。
The method for producing liquid fermented milk of the present invention includes (A) a stationary fermentation step in which a lactic acid bacterium is added to the raw material of fermented milk, followed by stationary fermentation to obtain a lactic acid fermentation product, and (B) step (A). After adding yeast to the lactic acid fermentation product obtained in step 1, the mixture is stirred and fermented to obtain a liquid fermented milk.
Moreover, the manufacturing method of the liquid fermented milk of this invention performs the homogenization process with respect to the liquid fermented milk obtained by (C) process (B), and the homogenization process of obtaining the liquid fermented milk after the homogenization process, Can be included.
Hereinafter, each step will be described in detail.
[工程(A);静置発酵工程]
 工程(A)は、発酵乳の原料に乳酸菌を添加した後、静置発酵させて、乳酸発酵生成物を得る工程である。
 発酵乳の原料としては、工程(B)の撹拌発酵の終了時点で、無脂乳固形分の含有率が5重量%以上、好ましくは8重量%以上の液状物が得られるものであればよい。
 発酵乳の主原料としては、獣乳(牛乳、羊乳、ヤギ乳、水牛乳等)や豆乳等の乳及びその加工品であれば、特に制限されずに任意のものを使用可能であり、例えば、脱脂粉乳、脱脂乳、生乳、乳タンパク質濃縮物等の他、ホエイを原料として製造されるホエイパウダーや、ホエイタンパク濃縮物等も使用可能である。発酵乳の主原料は、前記の一種を単独でまたは二種以上を組み合わせて用いることができる。
 発酵乳の副原料としては、公知の食品及び食品添加物であって、発酵時間を大幅に遅延させるものでなければ、特に制限されずに任意のものを使用可能であり、例えば、後述の実施例で用いられているぶどう糖、酵母エキス等が挙げられる。
 なお、本明細書中、発酵乳の主原料とは、乳由来の原料をいう。発酵乳の副原料とは、乳由来の原料以外の原料(ただし、乳酸菌及び酵母を除く。)をいう。
 発酵乳の原料の全量中の主原料の割合は、特に限定されない。
 発酵乳の原料には、必要に応じて、水を加えることができる。例えば、発酵乳の主原料として、脱脂粉乳のみを用いる場合、脱脂粉乳10重量部に対して、50~150重量部の水を加えることが好ましい。
 水を加える場合、発酵乳の原料と水との混合物に対して、乳酸菌を添加してもよいし、発酵乳の原料と乳酸菌との混合物に対して、水を加えてもよいし、発酵乳の原料と水と乳酸菌を同時に混合してもよい。
[Step (A); stationary fermentation step]
Step (A) is a step of obtaining a lactic acid fermentation product by adding lactic acid bacteria to the raw material of fermented milk and then allowing it to stand and ferment.
The raw material of the fermented milk may be any material that can obtain a liquid product having a nonfat milk solid content of 5% by weight or more, preferably 8% by weight or more at the end of the stirring fermentation in the step (B). .
As the main raw material of fermented milk, any milk can be used without particular limitation as long as it is milk such as animal milk (milk, sheep milk, goat milk, buffalo milk, etc.) and soy milk and processed products thereof, For example, whey powder produced using whey as a raw material, whey protein concentrate, and the like can be used in addition to skim milk powder, skim milk, raw milk, milk protein concentrate, and the like. The main raw material of fermented milk can use said 1 type individually or in combination of 2 or more types.
As a secondary ingredient of fermented milk, any known foods and food additives that do not significantly delay the fermentation time can be used without particular limitation. Examples include glucose and yeast extract used in the examples.
In addition, in this specification, the main raw material of fermented milk means the raw material derived from milk. The auxiliary raw material of fermented milk means raw materials other than milk-derived raw materials (however, excluding lactic acid bacteria and yeast).
The ratio of the main raw material in the whole quantity of the raw material of fermented milk is not specifically limited.
Water can be added to the raw material of fermented milk as needed. For example, when only skim milk powder is used as the main raw material of fermented milk, it is preferable to add 50 to 150 parts by weight of water to 10 parts by weight of skim milk powder.
When adding water, lactic acid bacteria may be added to the mixture of fermented milk raw material and water, or water may be added to the mixture of fermented milk raw material and lactic acid bacteria, and fermented milk. The raw material, water and lactic acid bacteria may be mixed at the same time.
 乳酸菌としては、生菌である乳酸菌を含むものであればよく、特に限定されないが、通常、栄養源の存在下に、乳酸菌を培養してなる液状物が用いられる。
 このような液状物は、例えば、脱脂粉乳等の栄養源、水、及び乳酸菌を含む混合液を、所定の温度(例えば、35~40℃)下で、所定の時間(例えば、10~20時間)、培養して、マザースターターを得た後、このマザースターターと、水と、脱脂粉乳等の栄養源を混合し、得られた混合液を、所定の温度(例えば、35~40℃)下で、所定の時間(例えば、10~20時間)、さらに培養することによって、得ることができる。
 乳酸菌中の乳酸菌の数は、特に限定されないが、例えば、1×107~1×109cfu/mlである。
 乳酸菌としては、発酵乳の製造に用いられる一般的な乳酸菌の中から選択される一種又は二種以上の乳酸菌を用いることができる。乳酸菌の例としては、例えば、ラクトバチルス属の乳酸菌、ストレプトコッカス属の乳酸菌等が挙げられる。
 ラクトバチルス属の乳酸菌としては、例えば、ラクトバチルス・ヘルベチカス(Lactobacillus helveticus)、ラクトバチルス・デルブリュッキー・サブスピーシーズ・ブルガリカス(Lactobacillus delbruekii subsp. bulgaricus)、ラクトバチルス・アシドフィラス(Lactobacillus acidophilus)等が挙げられる。
 本発明において、ラクトバチルス・ヘルベチカスは、他の乳酸菌よりも酸度の上昇が進むため、長時間の発酵が必要な発酵乳においても、汚染微生物の増殖を防止することができるという観点から好ましい。なお、ラクトバチルス・ヘルベチカスは、市販品を容易に入手することができる。
 ストレプトコッカス属の乳酸菌としては、例えば、ストレプトコッカス・サーモフィルス(Streptococcus thermophilus)等が挙げられる。
The lactic acid bacterium is not particularly limited as long as it contains a lactic acid bacterium that is a living bacterium, but usually a liquid product obtained by culturing lactic acid bacterium in the presence of a nutrient source is used.
Such a liquid material is, for example, a mixture containing a nutrient source such as skim milk powder, water, and lactic acid bacteria at a predetermined temperature (for example, 35 to 40 ° C.) for a predetermined time (for example, 10 to 20 hours). ) After culturing to obtain a mother starter, this mother starter, water, and a nutrient source such as skim milk powder are mixed, and the resulting mixed solution is subjected to a predetermined temperature (for example, 35 to 40 ° C.). Then, it can be obtained by further culturing for a predetermined time (for example, 10 to 20 hours).
The number of lactic acid bacteria in the lactic acid bacteria is not particularly limited, but is, for example, 1 × 10 7 to 1 × 10 9 cfu / ml.
As the lactic acid bacteria, one or two or more kinds of lactic acid bacteria selected from general lactic acid bacteria used for producing fermented milk can be used. Examples of lactic acid bacteria include lactic acid bacteria belonging to the genus Lactobacillus and lactic acid bacteria belonging to the genus Streptococcus.
Examples of lactic acid bacteria belonging to the genus Lactobacillus include Lactobacillus helveticus, Lactobacillus delbruekii subsp. Bulgaricus, Lactobacillus acidophilus (Lactobacillus acidophilus), and the like. Can be mentioned.
In the present invention, Lactobacillus helveticus is preferable from the viewpoint of preventing the growth of contaminating microorganisms even in fermented milk that requires fermentation for a long time because the acidity increases more than other lactic acid bacteria. In addition, Lactobacillus helveticus can obtain a commercial item easily.
Examples of Streptococcus lactic acid bacteria include Streptococcus thermophilus.
 本明細書中、静置発酵とは、撹拌せずに静置した状態で発酵させることをいう。
 静置発酵の時間は、好ましくは3~45時間、より好ましくは5~45時間、さらに好ましくは8~45時間、さらに好ましくは10~40時間、さらに好ましくは15~35時間、特に好ましくは20~30時間である。
 静置発酵の温度は、好ましくは25~50℃、より好ましくは30~45℃、さらに好ましくは32~43℃、特に好ましくは35~40℃である。
 静置発酵によって、発酵生成物であるカードが得られる。このカードは、工程(B)で細かく砕かれて、液状物となる。
In this specification, stationary fermentation means fermenting in the state which left still, without stirring.
The time for stationary fermentation is preferably 3 to 45 hours, more preferably 5 to 45 hours, still more preferably 8 to 45 hours, still more preferably 10 to 40 hours, still more preferably 15 to 35 hours, and particularly preferably 20 hours. ~ 30 hours.
The temperature of the stationary fermentation is preferably 25 to 50 ° C, more preferably 30 to 45 ° C, still more preferably 32 to 43 ° C, and particularly preferably 35 to 40 ° C.
The card | curd which is a fermentation product is obtained by stationary fermentation. This card is finely crushed in the step (B) to become a liquid material.
[工程(B);撹拌発酵工程]
 工程(B)は、工程(A)で得られた乳酸発酵生成物に酵母を添加した後、撹拌発酵させて、液状発酵乳を得る工程である。
 酵母としては、生菌である酵母を含むものであればよく、特に限定されないが、一例として、乾燥酵母(ドライイースト)が挙げられる。
 乾燥酵母は、乾燥によって休眠状態にある酵母である。乾燥酵母は、例えば、水と混合してなる液状物の状態で用いることができる。
 酵母としては、例えば、サッカロマイセス・セレビシエ(saccharomyces cerevisiae)、サッカロマイセス・パストリアヌス(Saccharomyces pastrianus)、サッカロマイセス・パラドキサス(Saccharomyces paradoxus)、サッカロマイセス・バヤヌス(Saccharomyces bayanus)等が挙げられる。
 本発明において、サッカロマイセス・セレビシエは、市販品で容易に入手できるため、汎用性の観点から好ましい。サッカロマイセス・セレビシエの市販品としては、サフ インスタントドライイースト 赤(Lesaffre社製)、オリエンタルドライイースト(オリエンタル酵母工業社製)等が挙げられる。
 酵母は、一種を単独でまたは二種以上を組み合わせて用いることができる。
 工程(A)で得られた乳酸発酵生成物は、静置発酵によって得られたものであるため、液状ではなく、固形状のカードの形態を有する。工程(B)において、このカードを細かく砕いた後に、酵母を添加してもよいし、あるいは、このカードに酵母を添加した後、撹拌によって、カードを細かく砕いてもよい。
[Step (B): Stirring fermentation step]
Step (B) is a step of adding liquid yeast to the lactic acid fermentation product obtained in step (A), followed by stirring and fermentation to obtain liquid fermented milk.
The yeast is not particularly limited as long as it contains yeast that is a living bacterium, and examples thereof include dry yeast (dry yeast).
Dry yeast is yeast that is dormant due to drying. Dry yeast can be used in the state of the liquid substance formed, for example by mixing with water.
Examples of the yeast include Saccharomyces cerevisiae, Saccharomyces pastrianus, Saccharomyces paradoxus, and Saccharomyces bayanus.
In the present invention, Saccharomyces cerevisiae is preferred from the viewpoint of versatility because it is a commercially available product and can be easily obtained. Examples of commercially available products of Saccharomyces cerevisiae include Saff Instant Dry Yeast Red (manufactured by Lesaffre), Oriental Dry Yeast (manufactured by Oriental Yeast Co., Ltd.), and the like.
Yeast can be used individually by 1 type or in combination of 2 or more types.
Since the lactic acid fermentation product obtained in the step (A) is obtained by stationary fermentation, it is not liquid but has a solid card form. In the step (B), the curd may be finely crushed and then yeast may be added. Alternatively, after adding yeast to the curd, the curd may be finely broken by stirring.
 撹拌の速度は、特に限定されないが、乳酸菌の作用によって形成したカードの剪断による破砕、酵母が産生する炭酸ガスの除去、及び固形物の浮上の抑制の観点から、好ましくは10~150rpm、より好ましくは30~100rpmである。
 撹拌は、連続的な撹拌と断続的な撹拌のいずれでもよいが、酵母が産生する炭酸ガスの除去、及び固形物の浮上の抑制の観点から、連続的な撹拌が好ましい。
 撹拌発酵の時間は、好ましくは20~50時間、より好ましくは25~45時間、さらに好ましくは30~40時間、特に好ましくは35~40時間である。
 撹拌発酵の温度は、好ましくは20~44℃、より好ましくは25~42℃、さらに好ましくは30~40℃、特に好ましくは35~38℃である。
 工程(A)における静置発酵の時間と、工程(B)における撹拌発酵の時間の合計は、液状発酵乳の風味、実用性等の観点から、好ましくは40~85時間、より好ましくは45~80時間、さらに好ましくは50~75時間、さらに好ましくは55~70時間、特に好ましくは60~70時間である。
 なお、撹拌発酵の終了後に、乳酸等を添加して、液状発酵乳の乳酸酸度を調整することができる。液状発酵乳の乳酸酸度は、適度な酸味を与える観点から、好ましくは2.1~2.7%である。
The speed of stirring is not particularly limited, but is preferably 10 to 150 rpm, more preferably from the viewpoint of crushing the curd formed by the action of lactic acid bacteria by shearing, removing carbon dioxide produced by yeast, and suppressing the floating of the solid matter. Is 30 to 100 rpm.
The stirring may be either continuous stirring or intermittent stirring, but continuous stirring is preferable from the viewpoint of removal of carbon dioxide gas produced by yeast and suppression of solid floating.
The stirring fermentation time is preferably 20 to 50 hours, more preferably 25 to 45 hours, still more preferably 30 to 40 hours, and particularly preferably 35 to 40 hours.
The temperature of the stirring fermentation is preferably 20 to 44 ° C, more preferably 25 to 42 ° C, still more preferably 30 to 40 ° C, and particularly preferably 35 to 38 ° C.
The total of the stationary fermentation time in the step (A) and the stirring fermentation time in the step (B) is preferably 40 to 85 hours, more preferably 45 to 45 hours from the viewpoint of the flavor and practicality of the liquid fermented milk. 80 hours, more preferably 50 to 75 hours, further preferably 55 to 70 hours, particularly preferably 60 to 70 hours.
In addition, after completion | finish of stirring fermentation, lactic acid etc. can be added and the lactic acid acidity of liquid fermented milk can be adjusted. The lactic acid acidity of the liquid fermented milk is preferably 2.1 to 2.7% from the viewpoint of giving an appropriate acidity.
[工程(C);均質化工程]
 工程(C)は、工程(B)で得られた液状発酵乳に対して均質化処理を行なう工程である。ここでいう、均質化とは、均質機(ホモゲナイザー)を用いた均質化処理に限られることなく、攪拌やホモミキサー、エクストルーダーなどによる公知の剪断処理も含まれる。
 均質化処理は、例えば均質機(ホモゲナイザー)を用いる場合、1段目の均質化処理として、7~13MPaの圧力で加圧した後、2段目の均質化処理として、4~6MPaの圧力で加圧することによって行なわれる。
 工程(C)としては、1段目と2段目を組み合わせた均質化処理を1回のみ行なってもよいし、1段目と2段目を組み合わせた均質化処理を2回以上行なってもよい。例えば、1段目と2段目を組み合わせた均質化処理を行なった後、加熱殺菌及び冷却を行ない、次いで、1段目と2段目を組み合わせた均質化処理をさらに行なってもよい。
 工程(C)で得られる処理済みの液状発酵乳に含まれている固形分を構成する粒子のメディアン径は、好ましくは30μm以下、より好ましくは25μm以下、さらに好ましくは20μm以下、特に好ましくは15μm以下である。
[Step (C): Homogenization step]
Step (C) is a step of homogenizing the liquid fermented milk obtained in step (B). Here, the homogenization is not limited to the homogenization process using a homogenizer (homogenizer), but also includes known shearing processes such as stirring, a homomixer, and an extruder.
For example, when using a homogenizer (homogenizer), the homogenization treatment is performed at a pressure of 7 to 13 MPa as the first-stage homogenization treatment, and then at a pressure of 4 to 6 MPa as the second-stage homogenization treatment. This is done by applying pressure.
As the step (C), the homogenization process combining the first stage and the second stage may be performed only once, or the homogenization process combining the first stage and the second stage may be performed twice or more. Good. For example, after performing the homogenization process combining the first stage and the second stage, heat sterilization and cooling may be performed, and then the homogenization process combining the first stage and the second stage may be further performed.
The median diameter of the particles constituting the solid content contained in the treated liquid fermented milk obtained in the step (C) is preferably 30 μm or less, more preferably 25 μm or less, further preferably 20 μm or less, particularly preferably 15 μm. It is as follows.
 工程(C)で得られた液状発酵乳は、単独で飲用に供してもよいし、あるいは、他の成分と混合して、飲用に供してもよい。液状発酵乳と混合される他の成分としては、甘みを与えるための砂糖等の甘味料や、乳酸等の酸度調整剤や、食塩や、香料や、果汁等が挙げられる。
 液状発酵乳と他の成分の混合物に対して、均質化処理を行うこともできる。この場合の均質化処理は、1段のみでも、複数段(例えば、1段目と2段目の併用)でもよい。均質化処理の圧力は、合計で、好ましくは10~20MPaである。また、この場合、均質化処理後の飲料(液状発酵乳と他の成分の混合物)に含まれている固形分を構成する粒子のメディアン径は、好ましくは2.5μm以下、より好ましくは2.0μm以下、さらに好ましくは1.5μm以下、特に好ましくは1.0μm以下である。
The liquid fermented milk obtained in the step (C) may be used alone for drinking, or may be mixed with other components for drinking. Examples of other components mixed with the liquid fermented milk include sweeteners such as sugar for imparting sweetness, acidity adjusting agents such as lactic acid, salt, fragrance, and fruit juice.
A homogenization process can also be performed with respect to the mixture of liquid fermented milk and another component. The homogenization process in this case may be only one stage or a plurality of stages (for example, combined use of the first and second stages). The total pressure of the homogenization treatment is preferably 10 to 20 MPa. In this case, the median diameter of the particles constituting the solid content contained in the homogenized beverage (mixture of liquid fermented milk and other components) is preferably 2.5 μm or less, more preferably 2. It is 0 μm or less, more preferably 1.5 μm or less, and particularly preferably 1.0 μm or less.
 以下に、本発明を実施例により説明するが、本発明はこれら実施例に限定されるものではない。
[実施例1]
(1)乳酸菌スターターの調製
 脱脂粉乳(明治社製)、粉末酵母エキス(商品名:イーストエキスT-154、オリエンタル酵母工業社製)、乳酸菌(Lactobacillus helveticus、ダニスコ社製の「FLAV 54 LYO 5D」)、及び、水を用いて、乳酸菌スターターを調製した。この乳酸菌スターターは、脱脂粉乳を10重量%、水を90重量%、イーストエキスを0.002重量%、乳酸菌を3×108cfu/ml含むものであった。また、この乳酸菌スターターの乳酸酸度は、1.6%であった。
(2)酵母スターターの調製
 40℃の滅菌水に乾燥酵母(商品名:サフ インスタントドライイースト 赤、Lesaffre社製)を添加して、20分間で静置したものを、酵母スターターとして、後述の液状発酵乳の調製で用いた。
EXAMPLES The present invention will be described below with reference to examples, but the present invention is not limited to these examples.
[Example 1]
(1) Preparation of lactic acid bacteria starter Nonfat dry milk (manufactured by Meiji Co., Ltd.), powdered yeast extract (trade name: yeast extract T-154, manufactured by Oriental Yeast Co., Ltd.), lactic acid bacteria (Lactobacillus helveticus, “FLAV 54 LYO 5D” manufactured by Danisco Co., Ltd.) ) And water were used to prepare lactic acid bacteria starters. This lactic acid bacteria starter contained skim milk powder 10% by weight, water 90% by weight, yeast extract 0.002% by weight, and lactic acid bacteria 3 × 10 8 cfu / ml. The lactic acid acidity of this lactic acid bacteria starter was 1.6%.
(2) Preparation of yeast starter Dry yeast (trade name: Saff Instant Dry Yeast Red, manufactured by Lesaffre) was added to 40 ° C sterilized water, and the mixture was allowed to stand for 20 minutes. Used in the preparation of fermented milk.
(3)液状発酵乳の調製
 40℃程度に加温した水86.69重量部と、脱脂粉乳(明治社製)10.76重量部と、ぶどう糖(商品名:グルファイナル、サンエイ糖化社製)0.5重量部と、粉末酵母エキス(商品名:イーストエキスT-154、オリエンタル酵母工業社製)0.04重量部を混合した後、得られた混合液を75℃、30分間で殺菌し、次いで、37℃に冷却した。冷却後の混合液に、前記の乳酸菌スターター2重量部を添加し、37℃、16時間で、静置発酵し、カードを形成させた。
 静置発酵後、撹拌装置を起動させ、カードを破砕すると同時に、前記の酵母スターターを、乾燥酵母の重量に換算して0.01重量部の配合量(以上の合計100重量部)となるように添加し、37℃、42時間で撹拌発酵した。撹拌は、60rpmで連続的に行なった。
 撹拌発酵の終了後、得られた液状発酵乳の乳酸酸度を確認したところ、2.4%であったため、乳酸を添加して、酸度を2.5%に調整した。
 次に、この液状発酵乳に対して、1段目として10MPa、2段目として5MPaの均質化処理を行なった。処理後の液状発酵乳を75℃、30分間で殺菌した後、10℃以下に冷却した。
 この、得られた液状発酵乳では、全固形分の含有率が11.6重量%、無脂乳固形分の含有率が10.4重量%、乳酸酸度が2.5%、pHが3.3であった。また、液状発酵乳では、浮上した固形物や、粗大粒子を含まず、均質で、乳白色の液状物であり、乳酸発酵に由来する酸味と、酵母発酵に由来する風味(まろやかさ、果実のような香り、後に感じる芳醇な香り)と、若干のアルコール香を有するものであった。液状発酵乳に、異味、異臭、異物は、認められなかった。
(3) Preparation of liquid fermented milk 86.69 parts by weight of water heated to about 40 ° C., 10.76 parts by weight of nonfat dry milk (manufactured by Meiji Co., Ltd.), and glucose (trade name: Glufinal, manufactured by Sanei Saku Kasei Co., Ltd.) After mixing 0.5 part by weight and 0.04 part by weight of powdered yeast extract (trade name: yeast extract T-154, manufactured by Oriental Yeast Co., Ltd.), the resulting mixture was sterilized at 75 ° C. for 30 minutes. And then cooled to 37 ° C. To the mixed solution after cooling, 2 parts by weight of the lactic acid bacteria starter was added and subjected to static fermentation at 37 ° C. for 16 hours to form a curd.
After the stationary fermentation, the stirrer is started and the curd is crushed. At the same time, the yeast starter is converted to the weight of the dry yeast to be 0.01 parts by weight (total 100 parts by weight above). And stirred and fermented at 37 ° C. for 42 hours. Stirring was continuously performed at 60 rpm.
After the stirring fermentation was completed, the lactic acid acidity of the obtained liquid fermented milk was confirmed to be 2.4%. Therefore, lactic acid was added to adjust the acidity to 2.5%.
Next, the liquid fermented milk was subjected to a homogenization treatment of 10 MPa as the first stage and 5 MPa as the second stage. The liquid fermented milk after the treatment was sterilized at 75 ° C. for 30 minutes and then cooled to 10 ° C. or lower.
In the obtained liquid fermented milk, the total solid content is 11.6% by weight, the non-fat milk solid content is 10.4% by weight, the lactic acid acidity is 2.5%, and the pH is 3. 3. In addition, liquid fermented milk is a homogeneous, milky white liquid that does not contain floating solids and coarse particles, and has a sourness derived from lactic acid fermentation and a flavor derived from yeast fermentation (such as mellowness and fruit). Fragrance) and a slight alcohol fragrance. In the liquid fermented milk, no off-flavor, off-flavor, or foreign matter was observed.
(4)飲料の調製
 前記の(3)で得られた液状発酵乳を、均質機(ホモミキサー)にて合計15MPaの圧力で均質化処理を行った後、85℃、2分間で加熱し、次いで、10℃以下に冷却した。均質化処理後の液状発酵乳の固形分を構成する粒子のメディアン径は、14.05μmであった。
 一方、40℃に加温した水82.02重量部に、大豆多糖類(商品名:SM900、三栄源エフ・エフ・アイ社製)0.2重量部を添加して、水溶液を得た後、この水溶液を10℃以下に冷却した。この水溶液に、砂糖10.112重量部、乳酸(商品名:50%乳酸、第一ファインケミカル社製)0.063重量部、食塩0.004重量部、及び、前記のホモミキサーで処理済みの液状発酵乳7.6重量部(以上の合計100重量部)を加えて、混合液を得た。この混合液を60℃に加温した後、均質機にて合計15MPaの圧力で均質化し、次いで、10℃以下に冷却した。冷却後の混合液を、オートクレーブを用いて110℃、1分間で加熱し、飲料を得た。
 この飲料について、固形分を構成する粒子のメディアン径を測定したところ、1.0μmであった。また、この模擬飲料は、固形分の浮上や粗大粒子による外観の異常が見られず、乳白色で均質な液状物であった。
(4) Preparation of beverage The liquid fermented milk obtained in (3) above was homogenized at a total pressure of 15 MPa with a homogenizer (homomixer), and then heated at 85 ° C for 2 minutes, Subsequently, it cooled to 10 degrees C or less. The median diameter of the particles constituting the solid content of the liquid fermented milk after the homogenization treatment was 14.05 μm.
On the other hand, after adding 0.2 parts by weight of soybean polysaccharide (trade name: SM900, manufactured by San-Ei Gen FFI Co., Ltd.) to 82.02 parts by weight of water heated to 40 ° C., an aqueous solution was obtained. The aqueous solution was cooled to 10 ° C. or lower. In this aqueous solution, 10.112 parts by weight of sugar, 0.063 parts by weight of lactic acid (trade name: 50% lactic acid, manufactured by Daiichi Fine Chemical Co., Ltd.), 0.004 parts by weight of sodium chloride, and a liquid that has been treated with the above homomixer 7.6 parts by weight of fermented milk (a total of 100 parts by weight above) was added to obtain a mixed solution. After heating this mixed liquid to 60 degreeC, it homogenized by the pressure of a total of 15 MPa with a homogenizer, and then cooled to 10 degrees C or less. The mixed liquid after cooling was heated at 110 ° C. for 1 minute using an autoclave to obtain a beverage.
With respect to this beverage, the median diameter of the particles constituting the solid content was measured and found to be 1.0 μm. In addition, the simulated beverage was milky white and homogeneous liquid without any solid surface floating or abnormal appearance due to coarse particles.
[実施例2]
 静置発酵の時間を24時間に定め、かつ撹拌発酵の時間を40時間に定めた以外は実施例1と同様にして実験した。
 その結果、均質化処理前の液状発酵乳では、実施例1と同様に、浮上した固形物や、粗大粒子を含まず、均質で、乳白色の液状物であり、乳酸発酵に由来する酸味等を有するものであった。液状発酵乳に、異味、異臭、異物は、認められなかった。
 均質化処理後の液状発酵乳の固形分を構成する粒子のメディアン径は、10μmであった。
 また、得られた飲料の粒子のメディアン径は、0.8μmであった。また、この飲料は、当該模擬飲料を収容する容器の底における沈殿が見られず、乳白色で均質な液状物であった。
[実施例3]
 静置発酵の時間を5時間に定め、かつ撹拌発酵の時間を59時間に定めた以外は実施例1と同様にして実験した。
 その結果、均質化処理前の液状発酵乳では、粒子の粒度は若干大きく、長時間静置すると粗大粒子の沈降がみられたものの、浮上した固形物を含まず、乳白色の液状物であり、乳酸発酵に由来する酸味等を有するものであった。液状発酵乳に、異味、異臭、異物は、認められなかった。
 また、得られた模擬飲料の粒子のメディアン径は、2.1μmであった。この飲料を収容する容器の底部等に、沈殿物が若干で認められた。
[Example 2]
The experiment was conducted in the same manner as in Example 1 except that the time for stationary fermentation was set at 24 hours and the time for stirring fermentation was set at 40 hours.
As a result, the liquid fermented milk before the homogenization treatment, like Example 1, is a homogeneous, milky white liquid that does not contain floating solids and coarse particles, and has a sourness derived from lactic acid fermentation. I had it. In the liquid fermented milk, no off-flavor, off-flavor, or foreign matter was observed.
The median diameter of the particles constituting the solid content of the liquid fermented milk after the homogenization treatment was 10 μm.
Moreover, the median diameter of the particle | grains of the obtained drink was 0.8 micrometer. Further, this beverage was milky white and homogeneous liquid with no precipitation at the bottom of the container containing the simulated beverage.
[Example 3]
The experiment was conducted in the same manner as in Example 1 except that the time for stationary fermentation was set to 5 hours and the time for stirring fermentation was set to 59 hours.
As a result, in the liquid fermented milk before homogenization treatment, the particle size of the particles is slightly large, and although sedimentation of coarse particles was seen when left for a long time, it did not contain any floating solids, and was a milky white liquid, It had a sour taste derived from lactic acid fermentation. In the liquid fermented milk, no off-flavor, off-flavor, or foreign matter was observed.
Moreover, the median diameter of the particle | grains of the obtained simulation drink was 2.1 micrometers. A slight amount of precipitate was observed at the bottom of the container containing the beverage.
[比較例1]
 乳酸菌スターターと酵母スターターを同時に添加し、かつ、静置発酵の時間を64時間に定め、撹拌発酵を行なわなかった以外は実施例1と同様にして実験した。
 その結果、液状発酵乳では、発酵終了時に、固形分が液面に浮上して乾燥し、硬化しており、外観が劣っていた。このため、手作業にて固形分を粉砕した後、均質化処理を行った。
 また、得られた飲料の粒子のメディアン径は、3.1μmであった。この飲料を収容する容器の底部等に、実施例3よりも多量の沈殿物が認められた。
[比較例2]
 乳酸菌スターターと酵母スターターを同時に添加し、かつ、撹拌発酵の時間を64時間に定め、静置発酵を行なわなかった以外は実施例1と同様にして実験した。
 その結果、液状発酵乳の発酵終了時に、固形分の液面への浮上は見られなかったものの、粗大粒子の沈降による外観の異常が認められた。以後の液状発酵乳の処理は、沈降した粗大粒子も含めて行った。
 また、得られた飲料の粒子のメディアン径は、4.6μmであった。この飲料を収容する容器の底に、比較例1よりも多量の沈殿物が認められた。
[比較例3]
 乳酸菌スターターと酵母スターターを同時に添加し、かつ、静置発酵の時間を24時間に定め、撹拌発酵の時間を40時間に定めた以外は実施例1と同様にして実験した。
 その結果、液状発酵乳は、発酵終了時に、固形分が液面に浮上して乾燥し、硬化しており、外観が劣っていた。このため、手作業にて固形分を粉砕した後、均質化処理を行った。
 また、得られた模擬飲料の粒子のメディアン径は、2.0μmであった。この飲料を収容する容器の底部等に、沈殿物が若干認められた。
 以上の結果を表1に示す。なお、表1中、総合評価に関し、「◎」は「非常に良好」、「○」は「良好」、「×」は「不良」を表す。
[Comparative Example 1]
Experiments were carried out in the same manner as in Example 1 except that a lactic acid bacteria starter and a yeast starter were added simultaneously, the time of stationary fermentation was set to 64 hours, and stirring fermentation was not performed.
As a result, in liquid fermented milk, the solid content floated on the liquid surface at the end of fermentation, dried and hardened, and the appearance was poor. For this reason, the solid content was pulverized manually and then homogenized.
Moreover, the median diameter of the particle | grains of the obtained drink was 3.1 micrometers. A larger amount of precipitate than in Example 3 was observed at the bottom of the container containing the beverage.
[Comparative Example 2]
Experiments were conducted in the same manner as in Example 1 except that a lactic acid bacteria starter and a yeast starter were added simultaneously, the time for stirring fermentation was set to 64 hours, and stationary fermentation was not performed.
As a result, at the end of the fermentation of the liquid fermented milk, although the solid content did not rise to the liquid surface, an abnormality in the appearance due to the sedimentation of the coarse particles was observed. The subsequent treatment of the liquid fermented milk was carried out including the coarse particles that settled.
Moreover, the median diameter of the particle | grains of the obtained drink was 4.6 micrometers. A larger amount of precipitate than in Comparative Example 1 was observed at the bottom of the container containing the beverage.
[Comparative Example 3]
Experiments were carried out in the same manner as in Example 1 except that the lactic acid bacteria starter and the yeast starter were added simultaneously, the time for stationary fermentation was set at 24 hours, and the time for stirring fermentation was set at 40 hours.
As a result, the liquid fermented milk had a solid content that floated on the liquid surface, dried and hardened at the end of fermentation, and had a poor appearance. For this reason, the solid content was pulverized manually and then homogenized.
Moreover, the median diameter of the particle | grains of the obtained simulation drink was 2.0 micrometers. Some precipitates were observed at the bottom of the container for containing the beverage.
The results are shown in Table 1. In Table 1, regarding the comprehensive evaluation, “◎” represents “very good”, “◯” represents “good”, and “x” represents “bad”.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
 表1から、乳酸菌スターターの添加後に静置発酵させ、次いで、酵母スターターを添加して、その後、撹拌発酵させた場合(実施例1~3)には、粗大粒子が生じず、また、固形分の浮上が生じないことがわかる。
 一方、静置発酵のみを行なった場合(比較例1)には、固形分が浮上するなどの問題があった。撹拌発酵のみを行なった場合(比較例2)には、固形分の浮上は認められなかったものの、粗大粒子の沈降による外観の異常が認められた。静置発酵と撹拌発酵を組み合わせたものの、乳酸菌スターターと酵母スターターを同時に添加した場合(比較例3)には、固形分が浮上するなどの問題があった。
From Table 1, when the lactic acid bacteria starter was added and then static fermentation was performed, and then the yeast starter was added and then stirred and fermented (Examples 1 to 3), coarse particles were not generated, and solid content It can be seen that no levitation occurs.
On the other hand, when only stationary fermentation was performed (comparative example 1), there existed problems, such as solid content rising. When only the stirring fermentation was performed (Comparative Example 2), the appearance of abnormalities due to sedimentation of coarse particles was observed, although no solid content was observed. Although stationary fermentation and stirring fermentation were combined, when the lactic acid bacterium starter and the yeast starter were added simultaneously (Comparative Example 3), there was a problem such as solid content rising.

Claims (9)

  1. (A)発酵乳の原料に乳酸菌を添加した後、静置発酵させて、乳酸発酵生成物を得る静置発酵工程と、
    (B)上記乳酸発酵生成物に酵母を添加した後、撹拌発酵させて、液状発酵乳を得る撹拌発酵工程、
    を含む液状発酵乳の製造方法。
    (A) After adding lactic acid bacteria to the raw material of fermented milk, it is subjected to stationary fermentation to obtain a lactic acid fermentation product,
    (B) After adding yeast to the lactic acid fermentation product, stirring fermentation to obtain liquid fermented milk by stirring and fermentation;
    A method for producing liquid fermented milk comprising
  2.  工程(A)における静置発酵を、3~45時間で行ない、かつ、工程(B)における撹拌発酵を、20~65時間で行なう請求項1に記載の液状発酵乳の製造方法。 The method for producing liquid fermented milk according to claim 1, wherein the stationary fermentation in the step (A) is performed in 3 to 45 hours, and the stirring fermentation in the step (B) is performed in 20 to 65 hours.
  3.  工程(A)における静置発酵を、20~44℃の温度下で行ない、かつ、工程(B)における撹拌発酵を、20~44℃の温度下で行なう請求項1又は2に記載の液状発酵乳の製造方法。 The liquid fermentation according to claim 1 or 2, wherein the stationary fermentation in the step (A) is performed at a temperature of 20 to 44 ° C, and the stirring fermentation in the step (B) is performed at a temperature of 20 to 44 ° C. Milk production method.
  4.  工程(A)における上記静置発酵の開始時から、工程(B)における上記撹拌発酵の終了時までの間、酵母以外のものを添加しない請求項1~3のいずれか1項に記載の液状発酵乳の製造方法。 The liquid according to any one of claims 1 to 3, wherein nothing other than yeast is added from the start of the stationary fermentation in the step (A) to the end of the stirred fermentation in the step (B). A method for producing fermented milk.
  5.  上記発酵乳の原料が、脱脂粉乳、脱脂乳、生乳、及び乳タンパク質濃縮物からなる群より選ばれる一種以上を含む請求項1~4のいずれか1項に記載の液状発酵乳の製造方法。 The method for producing liquid fermented milk according to any one of claims 1 to 4, wherein the raw material of the fermented milk contains one or more selected from the group consisting of skim milk powder, skim milk, raw milk, and milk protein concentrate.
  6.  工程(B)の後に、(C)上記発酵乳に対して均質化処理を行なう均質化工程、を含む請求項1~5のいずれか1項に記載の液状発酵乳の製造方法。 The method for producing liquid fermented milk according to any one of claims 1 to 5, further comprising (C) a homogenization step of performing homogenization treatment on the fermented milk after step (B).
  7.  請求項6に記載の液状発酵乳の製造方法によって得られた液状発酵乳。 Liquid fermented milk obtained by the method for producing liquid fermented milk according to claim 6.
  8.  上記液状発酵乳の固形分を構成する粒子のメディアン径が、30μm以下である請求項7に記載の液状発酵乳。 The liquid fermented milk according to claim 7, wherein the median diameter of the particles constituting the solid content of the liquid fermented milk is 30 µm or less.
  9.  請求項7又は8に記載の液状発酵乳を含む飲料であって、該飲料の固形分を構成する粒子のメディアン径が、2.5μm以下である飲料。 A beverage containing the liquid fermented milk according to claim 7 or 8, wherein the median diameter of particles constituting the solid content of the beverage is 2.5 µm or less.
PCT/JP2012/078793 2011-11-14 2012-11-07 Liquid fermented milk and method for producing same WO2013073424A1 (en)

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