JP2010136636A - Method for producing milk-fermented product - Google Patents
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本発明は、乳発酵物の製造方法に関し、より詳しくは強い粘性を有する後発酵タイプの乳発酵物の製造方法に関する。 The present invention relates to a method for producing a fermented milk product, and more particularly to a method for producing a post-fermentation type fermented milk product having a strong viscosity.
近年、コーカサス地方に由来し、強い粘性及び曳糸性を有することを特徴とする、いわゆる「カスピ海ヨーグルト」という名称の乳発酵物が注目されている。 In recent years, a fermented milk named “Caspian Sea Yogurt”, which is derived from the Caucasus region and has strong viscosity and spinnability, has attracted attention.
この乳発酵物からは、粘性多糖類を産生する乳酸菌の一種であるラクトコッカス・ラクティス・サブスピーシズ・クレモリス(Lactococcus lactis subsp. cremoris、以下「クレモリス菌」と称する)が分離及び同定されている(非特許文献1)。この粘性多糖類(菌体外多糖類)は、単に官能的な特徴を乳発酵物に付与するだけでなく、種々の生理作用を有することが報告されている(非特許文献2) From this fermented milk product, Lactococcus lactis subsp. Cremoris (hereinafter referred to as “Cremolis”), which is a kind of lactic acid bacterium producing viscous polysaccharides, has been isolated and identified (non-Cremoris bacterium). Patent Document 1). It has been reported that this viscous polysaccharide (extracellular polysaccharide) has various physiological functions as well as simply imparting sensory characteristics to the fermented milk (Non-patent Document 2).
また、その共存菌として酢酸菌の一種であるアセトバクター・オリエンタリス(Acetobacter orientalis)も分離及び同定されており、発酵中に酢酸菌がクレモリス菌の産生する乳酸の一部を消費することが知られている。また、発酵物の表面付近に増殖して内部を嫌気的状態にすることによって、クレモリス菌の菌数減少を抑制することや、発酵物の粘性を維持することが推測されている(非特許文献3)。 In addition, Acetobacter orientalis, a kind of acetic acid bacteria, has been isolated and identified as its coexisting bacteria, and it is known that acetic acid bacteria consume part of lactic acid produced by Cremoris during fermentation. ing. In addition, it has been speculated that by suppressing the decrease in the number of bacteria of Cremoris and maintaining the viscosity of the fermented product by growing near the surface of the fermented product and making the inside anaerobic (non-patent document) 3).
なお、後発酵型の乳発酵物に関する先行技術としては、特許文献1及び2に開示されているようなものが知られている。
いわゆる「カスピ海ヨーグルト」の粘性及び曳糸性を増大させるために、通常形態の紙又はプラスチック製容器に牛乳を主体とする培地を分注し、クレモリス菌を植菌し、後発酵させる従来技術の乳発酵物の製造方法によっては、乳発酵物中の溶存酸素濃度を低く抑えることができないため、クレモリス菌が産生する粘性多糖類を増加させ、乳発酵物の粘性を増加させることには限度がある。 In order to increase the viscosity and spinnability of the so-called “Caspian Sea Yogurt”, a conventional technique in which a medium mainly composed of milk is dispensed into a normal paper or plastic container, inoculated with Cremoris bacteria, and post-fermented. Depending on the milk fermented product manufacturing method, the concentration of dissolved oxygen in the milk fermented product cannot be kept low, so there is a limit to increasing the viscosity of the milk fermented product by increasing the viscous polysaccharides produced by Cremoris bacteria. There is.
また、アセトバクター・オリエンタリス等の酢酸菌を同時に植菌して後発酵させても、発酵後の乳発酵物の性状の安定化(乳発酵物の粘性及び曳糸性の維持)に若干の効果が期待できるものの、クレモリス菌が産生する粘性多糖類を増加させ、乳発酵物の粘性を増加させることは困難である。 In addition, even if acetic acid bacteria such as Acetobacter orientalis are inoculated at the same time and post-fermented, there is a slight effect on stabilizing the properties of the fermented milk product (maintaining the viscosity and spinnability of the fermented milk product). However, it is difficult to increase the viscosity of the milk fermented product by increasing the viscous polysaccharides produced by Cremoris bacteria.
また、牛乳を主体とする培地にクレモリス菌を植菌し、乳発酵物中の溶存酸素濃度を低く抑えた状態で前発酵させる製造方法では、一連の工程を常時嫌気的な状態に維持する必要があり、商業ベースで実施するには無理がある。また、前発酵させたヨーグルトのカードを崩さずに容器に充填するのは困難である。 In addition, in the production method in which Cremoris is inoculated in a milk-based medium and pre-fermented with a low concentration of dissolved oxygen in the fermented milk, the series of steps must be maintained in an anaerobic state at all times. It is impossible to implement on a commercial basis. Moreover, it is difficult to fill the container without breaking the pre-fermented yogurt card.
本発明は、上記事情に鑑みなされたものであり、特別な添加物を加えることなく、従来よりも粘性の高い乳発酵物を安定的かつ効率的に製造する、乳発酵物の製造方法の提供を目的とする。 The present invention has been made in view of the above circumstances, and provides a method for producing a fermented milk product that stably and efficiently produces a fermented milk product having higher viscosity than before without adding a special additive. With the goal.
本発明者等は、鋭意検討した結果、酸素透過性が小さい材質からなる密封容器内で後発酵させる場合、初期溶存酸素を10ppm以下に調整すれば従来よりも粘性の高い乳発酵物を、安定的かつ効率的に製造しうることを見出し、本発明を完成させるに至った。 As a result of diligent study, the inventors of the present invention, when post-fermenting in a sealed container made of a material having low oxygen permeability, by adjusting the initial dissolved oxygen to 10 ppm or less, stable milk fermented product with higher viscosity than before The present invention has been completed by finding that it can be manufactured efficiently and efficiently.
具体的に、本発明は、
酸素透過度が50 fmol/m2・s・Pa以下である材質から構成される密封容器内に、
殺菌した乳又は乳製品を主成分とした原料とクレモリス菌とを封入し、
初期溶存酸素を10ppm以下に調整して後発酵させることを特徴とする乳発酵物の製造方法に関する。
Specifically, the present invention
In a sealed container made of a material having an oxygen permeability of 50 fmol / m 2 · s · Pa or less,
Enclose the raw material and the Cremoris bacteria which are mainly composed of sterilized milk or dairy products,
The present invention relates to a method for producing a fermented milk product, characterized in that initial dissolved oxygen is adjusted to 10 ppm or less and post-fermented.
密封容器内で、殺菌乳をクレモリス菌によって後発酵させる場合、培養開始時に殺菌した原料乳中の溶存酸素濃度を10ppm以下に調整すれば、発酵物がクレモリス菌の増殖に適した嫌気的条件となる。その結果、粘性多糖類の産生量が増加し、乳発酵物の粘性が増大する。 When post-fermentation of pasteurized milk with Cremolis bacteria in a sealed container, if the dissolved oxygen concentration in the raw milk sterilized at the start of culture is adjusted to 10 ppm or less, the fermented product has anaerobic conditions suitable for the growth of Cremoris bacteria. Become. As a result, the production amount of the viscous polysaccharide is increased and the viscosity of the fermented milk product is increased.
密封容器は、酸素透過性が低い材質でなければ、大気中の酸素が乳発酵物へと溶解し、乳発酵物をクレモリス菌に適した嫌気的状態に維持することができない。このため、殺菌した原料乳中の溶存酸素濃度を10ppm以下に調整するだけでなく、酸素透過度が50fmol/m2・s・Pa以下である材質から密封容器が構成されている必要がある。 If the sealed container is not made of a material having low oxygen permeability, oxygen in the atmosphere is dissolved in the fermented milk product, and the fermented milk product cannot be maintained in an anaerobic state suitable for the Cremoris bacteria. For this reason, it is necessary not only to adjust the dissolved oxygen concentration in the sterilized raw milk to 10 ppm or less, but also to form a sealed container from a material having an oxygen permeability of 50 fmol / m 2 · s · Pa or less.
なお、本発明でいう「乳又は乳製品を主成分とした原料」とは、牛乳等の動物乳又は牛乳等の動物乳から製造される乳製品であって、ヨーグルトの原料として利用できることが知られているものを意味する。 In the present invention, the “raw material mainly composed of milk or dairy product” is a dairy product produced from animal milk such as milk or animal milk such as cow milk, and is known to be usable as a raw material for yogurt. Means what is being done.
前記酸素透過度が50 fmol/m2・s・Pa以下である材質は、アルミニウム箔、アルミニウム蒸着フィルム、シリカ蒸着フィルム又はアルミナ蒸着フィルムの積層体を含む材質であることが好ましい。 The material having an oxygen permeability of 50 fmol / m 2 · s · Pa or less is preferably a material including a laminate of an aluminum foil, an aluminum deposited film, a silica deposited film, or an alumina deposited film.
前記密封容器は、開閉可能な注入部材を有するパウチ容器であることが好ましい。従来よりも粘性の高い乳発酵物を取り出す際に便利であり、かつ食べきれずに残した乳発酵物を保存する際に酸素の侵入が少ないからである。なお、この開閉可能な注入部材は、酸素透過度が50 fmol/m2・s・Pa以下であれば、その材質又は厚みは限定されない。 The sealed container is preferably a pouch container having an injection member that can be opened and closed. This is because it is convenient when taking out a fermented milk product having a higher viscosity than conventional ones, and has less oxygen intrusion when storing the left fermented milk product. In addition, the material or thickness of the injection member that can be opened and closed is not limited as long as the oxygen permeability is 50 fmol / m 2 · s · Pa or less.
前記密封容器内に封入するラクトコッカス・ラクティス・サブスピーシズ・クレモリス菌スターターの生菌数は1.0×106cfu/g以上1.0×109cfu/g以下の範囲内であり、その植菌量は殺菌した原料乳に対して0.3重量%以上20重量%以下とすることが好ましい。また、ラクトコッカス・ラクティス・サブスピーシズ・クレモリス菌スターターの生菌数は1.0×107cfu/g以上5.0×108cfu/g以下の範囲内であり、その植菌量は殺菌した原料乳に対して0.5%以上10%以下であることがより好ましい。 The viable count of Lactococcus lactis subspices cremollis starter sealed in the sealed container is in the range of 1.0 × 10 6 cfu / g or more and 1.0 × 10 9 cfu / g or less, and the amount of inoculation is sterilized. It is preferable to be 0.3 wt% or more and 20 wt% or less with respect to the raw material milk. In addition, the viable count of Lactococcus lactis subspices cremolith starter is in the range of 1.0 x 10 7 cfu / g to 5.0 x 10 8 cfu / g And more preferably 0.5% or more and 10% or less.
なお、アセトバクター・オリエンタリスも同時に植菌する場合、スターターの生菌数が1.0×102cfu/g以上1.0×109cfu/g以下の範囲内であり、その植菌量が殺菌した原料乳に対して0.3%以上20%以下であることが好ましい。 In addition, when Acetobacter orientalis is inoculated at the same time, the starter's viable count is 1.0 × 10 2 cfu / g or more and 1.0 × 10 9 cfu / g or less, and the amount of inoculated raw milk Is preferably 0.3% or more and 20% or less.
後発酵温度は、クレモリス菌の至適温度が25℃〜30℃であることから、23℃以上33℃以下であり、後発酵時間は5時間24以上時間以下であることが好ましい。 The post-fermentation temperature is preferably 23 ° C. or higher and 33 ° C. or lower because the optimal temperature of Cremoris bacteria is 25 ° C. to 30 ° C., and the post-fermentation time is preferably 5 hours or longer and 24 hours or shorter.
原料乳にグルコース又はサッカロースを0.1重量%以上5重量%以下の範囲で添加することが好ましい。グルコース又はサッカロースを添加することにより、乳発酵物の粘度をさらに増大することが可能となるためである。 It is preferable to add glucose or saccharose to the raw material milk in the range of 0.1 wt% to 5 wt%. This is because the viscosity of the fermented milk product can be further increased by adding glucose or saccharose.
前記密封容器内に、さらにアセトバクター・オリエンタリスを封入することが好ましい。アセトバクター・オリエンタリスが発酵中に酸素を消費するため、より嫌気的な状態で乳発酵物を製造することが可能になるためである。 It is preferable to further enclose Acetobacter orientalis in the sealed container. This is because Acetobacter orientalis consumes oxygen during fermentation, and thus it is possible to produce a fermented milk product in a more anaerobic state.
本発明の乳発酵物の製造方法によれば、従来よりも粘性の高いクレモリス菌由来乳発酵物を製造することが可能となる。 According to the method for producing a fermented milk product of the present invention, it is possible to produce a fermented milk product of Cremoris having a higher viscosity than before.
以下、本発明の実施の形態について、適宜図面を参酌しながら説明する。なお、本発明は、以下に限定されない。 Hereinafter, embodiments of the present invention will be described with reference to the drawings as appropriate. The present invention is not limited to the following.
(培地A)
牛乳65、脱脂粉乳3.5、生クリーム0.5、及び31(数字は重量%)で混合した。混合後、85℃で15分間加熱し、殺菌処理を行った。さらにホモジナイザー(APV社製、WU-DA100LR-C)用いて150kgf/cm2に加圧し、均質化させた。この状態の培地を、「培地A」とした。
(Medium A)
Mixed with milk 65, skim milk powder 3.5, fresh cream 0.5 and 31 (numbers are% by weight). After mixing, the mixture was heated at 85 ° C. for 15 minutes for sterilization. Further, the mixture was pressurized to 150 kgf / cm 2 using a homogenizer (APU, WU-DA100LR-C) and homogenized. The medium in this state was designated as “medium A”.
(培地B)
牛乳を85℃で15分間加熱し、殺菌処理を行った。さらにホモジナイザー(APV社製、WU-DA100LR-C)用いて150kgf/cm2に加圧し、均質化させた。この状態の培地を、「培地B」とした。
(Medium B)
Milk was heated at 85 ° C. for 15 minutes for sterilization. Further, the mixture was pressurized to 150 kgf / cm 2 using a homogenizer (APU, WU-DA100LR-C) and homogenized. The medium in this state was designated as “medium B”.
[実施例1]
培地Aにクレモリス菌FC株スターターを3.5重量%植菌した。(なお、スターターの生菌数は1.0×108cfu/g程度である。)その後、図1に示す形態の無菌アルミパウチ容器1に400mL充填した。このアルミパウチ容器の本体2の材質は、ポリエチレンテレフタレート(厚み12μm)/アルミ箔(厚み9μm)/延伸ナイロン(厚み15μm)/無延伸ポリプロピレン(厚み80μm)を順に積層した積層体であった。この積層体の酸素透過度は、5 fmol/m2・s・Pa以下(酸素透過度1級相当)であった。
[Example 1]
Medium A was inoculated with 3.5% by weight of Cremoris FC strain starter. (The number of viable bacteria in the starter is about 1.0 × 10 8 cfu / g.) Thereafter, 400 mL of a sterile
本体2の上部には、ポリプロピレン製の注入部材3が設けられており、ふた4は開閉式となっている。注入部材3は中空の円柱状であり、ふた4を開けると本体2内部は外部と連通する。なお、アルミパウチ容器1の内容積は、400mLである。
An injection member 3 made of polypropylene is provided on the upper portion of the
培地A及びクレモリス菌充填後のアルミパウチ容器1を25℃で6.5時間〜8時間保温し、培地Aをアルミパウチ容器1内で後発酵させた。得られた乳発酵物を実施例1の乳発酵物とした。
The
[比較例1]
培地Aにクレモリス菌(FC株)スターターを3.5重量%植菌した後、酸素透過度500fmol/m2・s・Pa超える紙製容器(酸素透過度5級相当)に400mL充填し、ナイロン/ポリエチレン材質のフィルムを上部にかぶせて、カップシール機(シンワ社製、SN-1)を用いて160℃で熱圧着させるという方法で密封した以外、すべて実施例1と同様の操作を行った。得られた乳発酵物を比較例1の乳発酵物とした。
[Comparative Example 1]
After inoculating 3.5% by weight of Cremoris bacteria (FC strain) starter into medium A, 400mL is filled into a paper container (corresponding to oxygen permeability grade 5) with an oxygen permeability of 500fmol / m 2 · s · Pa, nylon / polyethylene The same operation as in Example 1 was performed except that the material film was placed on top and sealed by a method of thermocompression bonding at 160 ° C. using a cup seal machine (Shinwa Co., Ltd., SN-1). The obtained milk fermented product was used as the milk fermented product of Comparative Example 1.
<絶対粘度>
実施例1及び比較例1の乳発酵物の絶対粘度(10℃)を、B型粘度計(ブルックスフィールド社製、スピンドルNo.4)を用いて測定した。その結果を、図2に示す。なお、ここに示す絶対粘度は、酸度0.75付近における絶対粘度である。
<Absolute viscosity>
The absolute viscosity (10 ° C.) of the fermented milk of Example 1 and Comparative Example 1 was measured using a B-type viscometer (Brooksfield, spindle No. 4). The result is shown in FIG. In addition, the absolute viscosity shown here is an absolute viscosity in the vicinity of acidity of 0.75.
図2より、実施例1の乳発酵物は、同じ発酵時間である比較例1の乳発酵物よりも13%〜31%絶対粘度が高く、発酵時間が短い場合ほど、絶対粘度の差が大きかった。 From FIG. 2, the fermented milk product of Example 1 has a higher absolute viscosity of 13% to 31% than the fermented milk product of Comparative Example 1 having the same fermentation time, and the difference in absolute viscosity is larger as the fermentation time is shorter. It was.
<動粘度>
実施例1及び比較例1の乳発酵物について、発酵中、ザーンカップ測定法によって経時的に動粘度を測定した。具体的には、離合社製No.7のザーンカップに、乳発酵物43mLを汲み入れ、全量が流出する時間(流出秒)を測定した(10℃)。その結果を、図3に示す。
<Kinematic viscosity>
About the milk fermented product of Example 1 and Comparative Example 1, kinematic viscosity was measured with time by the Zahn cup measurement method during fermentation. Specifically, 43 mL of milk fermented product was poured into a No. 7 Zaan cup made by Kogaisha Co., Ltd., and the time (outflow seconds) for the entire amount to flow out was measured (10 ° C.). The result is shown in FIG.
いずれの発酵時間においても、実施例1の乳発酵物は、比較例1の乳発酵物よりも流出秒の値が大きく、動粘度が高いことが閉められた。 In any fermentation time, it was closed that the milk fermented product of Example 1 had a larger outflow second value and a higher kinematic viscosity than the milk fermented product of Comparative Example 1.
[実施例2]
培地Aにクレモリス菌(FC株)スターターを3.5重量%、乳酸球菌であるストレプトコッカス・サーモフィラス菌(Streptococcus thermophilus)スターターを3.5重量%添加し、実施例1と同様の操作を行った。6時間発酵させた時点で酸度0.75となったので、その時点で発酵終了とし、10℃の暗所で保存を開始した。
[Example 2]
The same procedure as in Example 1 was carried out by adding 3.5% by weight of a starter of Cremoris (FC strain) and 3.5% by weight of a starter of Streptococcus thermophilus (Streptococcus thermophilus). Since the acidity reached 0.75 when fermented for 6 hours, the fermentation was terminated at that point and storage was started in the dark at 10 ° C.
[比較例2]
培地Aにクレモリス菌(FC株)スターターを3.5重量%、乳酸球菌であるストレプトコッカス・サーモフィラス菌スターターを1.5重量%、比較例1と同様の操作を行った。7.5時間発酵させた時点で酸度0.75となったので、その時点で発酵終了とし、10℃の暗所で保存を開始した。
[Comparative Example 2]
The same operation as in Comparative Example 1 was performed on medium A with a Cremollis starter (FC strain) starter of 3.5% by weight and a Streptococcus thermophilus starter that is a lactic acid bacterium. Since the acidity reached 0.75 at the time of fermentation for 7.5 hours, the fermentation was terminated at that point and storage was started in a dark place at 10 ° C.
実施例2及び比較例2の乳発酵物について、10℃保存の開始時及び28日経過後の2回、ザーンカップ測定法によって、動粘度を測定した。その結果を、図4に示す。 About the milk fermented product of Example 2 and Comparative Example 2, kinematic viscosity was measured by the Zahn cup measurement method at the time of the start of 10 degreeC preservation | save and twice after 28-day progress. The result is shown in FIG.
実施例2では、28日間保存した後の動粘度は、0日目と比較して約13%しか減少していなかった。一方、比較例2では、0日目と比較して約49%も減少しており、いわゆる「カスピ海ヨーグルト」としての食感が損なわれていることが確認された。 In Example 2, the kinematic viscosity after 28 days of storage was reduced by only about 13% compared to the 0th day. On the other hand, in Comparative Example 2, it decreased by about 49% compared with the 0th day, and it was confirmed that the texture as what is called "Caspian Sea yogurt" is impaired.
[実施例3]
培地Bにクレモリス菌(FC株)スターターを3.5重量%添加し、実施例1と同様の操作を行い、酸度0.75となった時点で得られた乳発酵物を、実施例3の乳発酵物とした。
[Example 3]
A starter of Cremoris (FC strain) was added to medium B at 3.5% by weight, and the same operation as in Example 1 was performed. The fermented milk product obtained when the acidity reached 0.75 was designated as the fermented milk product of Example 3. did.
[実施例4]
培地Bにグルコースを1重量%添加した上で、クレモリス菌(FC株)スターターを3.5重量%添加し、さらに実施例1と同様の操作を行い、酸度0.75となった時点で得られた乳発酵物を、実施例4の乳発酵物とした。
[Example 4]
After adding 1% by weight of glucose to medium B, adding 3.5% by weight of Cremoris starter (FC strain) starter, and performing the same operation as in Example 1 to obtain the milk fermentation obtained when the acidity reached 0.75 The product was the fermented milk product of Example 4.
[実施例5]
培地Bにスクロースを1重量%添加した上でクレモリス菌(FC株)スターターを3.5重量%添加し、さらに実施例1と同様の操作を行い、酸度0.75となった時点で得られた乳発酵物を、実施例5の乳発酵物とした。
[Example 5]
After adding 1% by weight of sucrose to medium B and adding 3.5% by weight of Cremoris (FC strain) starter, the same procedure as in Example 1 was performed, and the fermented milk product obtained when the acidity reached 0.75 Was the fermented milk product of Example 5.
[比較例3]
培地Bにクレモリス菌(FC株)スターターを3.5重量%添加し、比較例1と同様の操作を行い、酸度0.75となった時点で得られた乳発酵物を、比較例3の乳発酵物とした。
[Comparative Example 3]
The starter of Cremoris (FC strain) 3.5% by weight was added to medium B, the same operation as in Comparative Example 1 was performed, and the fermented milk obtained when the acidity reached 0.75 was compared with the fermented milk of Comparative Example 3. did.
[比較例4]
培地Bにグルコースを1重量%添加した上でクレモリス菌(FC株)スターターを3.5重量%添加し、比較例1と同様の操作を行い、酸度0.75となった時点で得られた乳発酵物を、比較例4の乳発酵物とした。
[Comparative Example 4]
After adding 1% by weight of glucose to medium B, adding 3.5% by weight of Cremoris (FC strain) starter, the same operation as in Comparative Example 1 was performed, and the fermented milk obtained when the acidity reached 0.75 was obtained. The fermented milk product of Comparative Example 4 was obtained.
[比較例5]
培地Bにスクロースを1重量%添加した上でクレモリス菌(FC株)スターターを3.5重量%添加し、比較例1と同様の操作を行い、酸度0.75となった時点で得られた乳発酵物を、比較例5の乳発酵物とした。
[Comparative Example 5]
After adding 1% by weight of sucrose to medium B and adding 3.5% by weight of Cremoris (FC strain) starter, the same operation as in Comparative Example 1 was performed, and the fermented milk obtained when the acidity reached 0.75 was obtained. The fermented milk product of Comparative Example 5 was obtained.
実施例3〜5及び比較例3〜5の乳発酵物について、ザーンカップ測定法によって動粘度を測定した。その結果を、図5及び図6に示す。 About the milk fermented products of Examples 3-5 and Comparative Examples 3-5, kinematic viscosity was measured by the Zahn cup measuring method. The results are shown in FIGS.
グルコースを添加した実施例4は、糖を添加しなかった実施例3と比較して76.6%乳発酵物の動粘度が上昇し、いわゆる「カスピ海ヨーグルト」としての食感(なめらか感)が増強されていた。同様に、スクロースを添加した実施例5も、糖を添加しなかった実施例3と比較して54.5%乳発酵物の動粘度が上昇し、いわゆる「カスピ海ヨーグルト」としての食感(なめらか感)が増強されていた。 In Example 4 to which glucose was added, the kinematic viscosity of 76.6% fermented milk increased compared to Example 3 to which no sugar was added, and the texture (smooth feeling) as so-called “Caspian Sea yogurt” was enhanced. It had been. Similarly, also in Example 5 to which sucrose was added, the kinematic viscosity of the fermented 54.5% milk increased compared to Example 3 to which no sugar was added, and the texture (smooth feeling) as a so-called “Caspian Sea yogurt” ) Was enhanced.
なお、培地Bに添加するグルコース又はスクロースの添加量を0.1重量%以上5重量%以下の範囲で増減させた場合、添加しない場合と比較して動粘度が有意に増大することが確認された。また、0.1重量未満では動粘度の増大効果が認められず、5重量%を超えると動粘度は増加しても甘みが強くなりすぎて、乳発酵物としての味覚が損なわれることも確認された。 In addition, when the addition amount of glucose or sucrose added to the culture medium B was increased or decreased within the range of 0.1 wt% or more and 5 wt% or less, it was confirmed that the kinematic viscosity significantly increased as compared with the case where it was not added. In addition, the effect of increasing the kinematic viscosity was not observed when the amount was less than 0.1%, and when the amount exceeded 5% by weight, the sweetness became too strong even if the kinematic viscosity increased, and the taste as a fermented milk product was also impaired. .
一方、グルコースを添加した比較例4と、スクロースを添加した比較例5も、糖を添加しなかった比較例3と比較して乳発酵物の動粘度が上昇していた。しかし、同じ割合で糖を添加しても、動粘度は実施例4及び5の乳発酵物よりも低い数値であった。 On the other hand, Comparative Example 4 to which glucose was added and Comparative Example 5 to which sucrose was added also showed an increase in the kinematic viscosity of the fermented milk compared to Comparative Example 3 to which no sugar was added. However, even when sugar was added at the same ratio, the kinematic viscosity was lower than that of the fermented milk of Examples 4 and 5.
本発明は、従来にない強い粘性及び曳糸性を有し、なめらかな食感もつ乳発酵物の製造方法として、食品分野において有用である。 INDUSTRIAL APPLICABILITY The present invention is useful in the food field as a method for producing a fermented milk product having an unprecedented strong viscosity and spinnability and a smooth texture.
1:アルミパウチ容器
2:本体
3:注入部材
4:注入部材のふた
1: Aluminum pouch container 2: Main body 3: Injection member 4: Lid of injection member
Claims (7)
殺菌した乳又は乳製品を主成分とした原料とラクトコッカス・ラクティス・サブスピーシズ・クレモリス菌とを封入し、
初期溶存酸素を10ppm以下に調整して後発酵させることを特徴とする乳発酵物の製造方法。 In a sealed container made of a material having an oxygen permeability of 50 fmol / m 2 · s · Pa or less,
Enclose the raw material and pasteurized lactococcus lactis subspices cremolith with the main component of sterilized milk or dairy products,
A method for producing a fermented milk product, characterized in that initial dissolved oxygen is adjusted to 10 ppm or less and post-fermented.
The method for producing a fermented milk product according to any one of claims 1 to 6, wherein Acetobacter orientalis is further enclosed in the sealed container.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101846277B1 (en) * | 2016-10-12 | 2018-04-06 | 인제대학교 산학협력단 | Sweet potato yogurt and a method of manufacturing the same |
JP2018170981A (en) * | 2017-03-31 | 2018-11-08 | 株式会社明治 | Method for producing fermented milk through low-temperature fermentation, and fermented milk produced by the method |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61115445A (en) * | 1984-11-10 | 1986-06-03 | Kyodo Nyugyo Kk | Preparation of cottage cheese preservable for long period |
JP2004261176A (en) * | 2003-02-13 | 2004-09-24 | Fujicco Co Ltd | Yogurt starter and fermented food and drink given by using the same |
JP2005176603A (en) * | 2002-12-03 | 2005-07-07 | Meiji Milk Prod Co Ltd | Method for producing fermented milk and fermented milk |
JP2005261303A (en) * | 2004-03-18 | 2005-09-29 | Meiji Milk Prod Co Ltd | Method for producing natural cheese |
JP2005328831A (en) * | 2004-09-17 | 2005-12-02 | Fujicco Co Ltd | Method for producing yoghurt and yoghurt obtained by the same |
-
2008
- 2008-12-09 JP JP2008313537A patent/JP5142966B2/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61115445A (en) * | 1984-11-10 | 1986-06-03 | Kyodo Nyugyo Kk | Preparation of cottage cheese preservable for long period |
JP2005176603A (en) * | 2002-12-03 | 2005-07-07 | Meiji Milk Prod Co Ltd | Method for producing fermented milk and fermented milk |
JP2004261176A (en) * | 2003-02-13 | 2004-09-24 | Fujicco Co Ltd | Yogurt starter and fermented food and drink given by using the same |
JP2005261303A (en) * | 2004-03-18 | 2005-09-29 | Meiji Milk Prod Co Ltd | Method for producing natural cheese |
JP2005328831A (en) * | 2004-09-17 | 2005-12-02 | Fujicco Co Ltd | Method for producing yoghurt and yoghurt obtained by the same |
Non-Patent Citations (2)
Title |
---|
DIERKSEN, K.P. ET AL.: ""Expression of ropy and mucoid phenotypes in Lactococcus lactis."", J. DAIRY SCI., vol. 80, no. 8, JPN6012021080, August 1997 (1997-08-01), pages 1528 - 1536, XP002944214, ISSN: 0002367266, DOI: 10.3168/jds.S0022-0302(97)76082-X * |
ISHIDA, T. ET AL.: ""Identification and characterization of lactococcal and Acetobacter strains isolated from traditiona", J. NUTR. SCI. VITAMINOL. (TOKYO), vol. 51, no. 3, JPN6012021078, June 2005 (2005-06-01), pages 187 - 193, ISSN: 0002367265 * |
Cited By (2)
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KR101846277B1 (en) * | 2016-10-12 | 2018-04-06 | 인제대학교 산학협력단 | Sweet potato yogurt and a method of manufacturing the same |
JP2018170981A (en) * | 2017-03-31 | 2018-11-08 | 株式会社明治 | Method for producing fermented milk through low-temperature fermentation, and fermented milk produced by the method |
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