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JP4413860B2 - Production method of vinegar, seed vinegar solution for acetic acid fermentation - Google Patents
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JP4413860B2 - Production method of vinegar, seed vinegar solution for acetic acid fermentation - Google Patents

Production method of vinegar, seed vinegar solution for acetic acid fermentation Download PDF

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JP4413860B2
JP4413860B2 JP2005365636A JP2005365636A JP4413860B2 JP 4413860 B2 JP4413860 B2 JP 4413860B2 JP 2005365636 A JP2005365636 A JP 2005365636A JP 2005365636 A JP2005365636 A JP 2005365636A JP 4413860 B2 JP4413860 B2 JP 4413860B2
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vinegar
fermentation
acetic acid
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fermented
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JP2007166928A (en
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洋樹 縣
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Mizkan Group Corp
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Description

本発明は、深部培養法にて発酵中の食酢発酵液を例えば次回仕込時の種酢として使用する食酢の製造方法、酢酸発酵用種酢溶液に関するものである。 The present invention relates to a manufacturing method, for acetic ferment vinegar solution VINEGAR that use vinegar fermentation liquid, for example, as a seed vinegar for the next charge in the fermentation by submerged culture method.

食酢の深部培養法では、発酵を開始する際に仕込液に種菌を添加する必要がある。そして、従来においては、発酵中の食酢発酵液の一部を採取して残しておき、これを種酢として次の仕込液に速やかに直接添加する方法が、通常よく実施されている。しかしながら、この方法では種酢となるべき食酢の発酵を常に維持しておく必要があり、無駄な食酢ができるという問題点があった。   In the deep culture method of vinegar, it is necessary to add an inoculum to the preparation liquid when starting fermentation. And conventionally, a method of collecting a part of the fermented vinegar fermented liquid during fermentation and leaving it as seed vinegar and adding it directly to the next charged liquid is usually well practiced. However, this method has a problem that it is necessary to always maintain fermentation of vinegar to be used as seed vinegar, and wasteful vinegar can be produced.

また、食酢製造用酢酸菌用培地にて前培養された前培養液をあらかじめ用意し、発酵を開始する際にこれを種酢として仕込液に添加する方法も従来提案されている(例えば、特許文献1参照)。
特開2004−33111号公報
In addition, a method in which a preculture solution pre-cultured in a medium for acetic acid bacteria for producing vinegar is prepared in advance and added to a preparation solution as seed vinegar when starting fermentation has been proposed (for example, patents). Reference 1).
JP 2004-33111 A

しかしながら、特許文献1に記載の従来方法の場合、本発酵用の発酵装置とは別に小スケールの前培養用発酵装置を稼動させなければならず、二度手間で作業効率が悪いという問題がある。それゆえ、食酢発酵液を採取及び保管しておき、生産計画に合わせて後日これを種酢として利用する技術が従来強く望まれている。   However, in the case of the conventional method described in Patent Document 1, a small-scale pre-culture fermentation apparatus must be operated separately from the fermentation apparatus for main fermentation, and there is a problem that work efficiency is poor twice. . Therefore, a technique for collecting and storing a vinegar fermented liquid and using it as a seed vine at a later date according to the production plan has been strongly desired.

そしてこのような採取・保管技術の一例としては、食酢発酵液を遠心分離して酢酸等の液体成分と酢酸菌とを分離し、その分離した酢酸菌を0℃未満の温度で凍結保存するという保管方法が提案されている。しかしながら、この方法を実施するには遠心分離機や冷凍庫が必要となるため、イニシャルコスト及びランニングコストがかかりすぎるという問題がある。従って、この方法は実験室レベルでは有効であるといえるが、規模を拡大して工業的に実施しようとした場合には多くの困難を伴うと予想される。   And as an example of such collection and storage technology, the vinegar fermented liquid is centrifuged to separate liquid components such as acetic acid and acetic acid bacteria, and the separated acetic acid bacteria are stored frozen at a temperature below 0 ° C. A storage method has been proposed. However, since this method requires a centrifuge and a freezer, there is a problem that the initial cost and running cost are excessive. Therefore, it can be said that this method is effective at the laboratory level, but it is expected to be accompanied by many difficulties when it is attempted to carry out the industrial scale expansion.

そこで本願出願人は、採取した食酢発酵液の保管時に菌体の活性を維持する方法を模索した結果、例えば酢酸濃度を低くすればよいと考え、具体的には食酢発酵液に何らかの添加物(例えば中和反応によって酢酸濃度を低下させるアルカリなどの中和剤)を添加すればよいと考えた。ところが、この種の添加物は必ずしも食酢成分として許容できるものとは限らず、仮に許容できるものであったとしても、その添加によって食酢の風味、品質、純度等を低下させる可能性がある。従って、中和剤等のような添加物の使用は極力避けたいという事情がある。   Therefore, the applicant of the present application sought to maintain the activity of the bacterial cells during storage of the collected vinegar fermented liquid. As a result, for example, the acetic acid concentration should be lowered. For example, it was thought that a neutralizing agent such as an alkali that lowers the acetic acid concentration by a neutralization reaction may be added. However, this type of additive is not always acceptable as a vinegar component, and even if it is acceptable, there is a possibility that the flavor, quality, purity, etc. of vinegar may be reduced by the addition. Therefore, there is a situation where it is desired to avoid the use of additives such as neutralizing agents as much as possible.

本発明は上記の課題に鑑みてなされたものであり、その第1の目的は、簡便でコスト性に優れるにもかかわらず、食酢発酵液の菌体活性を維持した状態で保管可能な食酢発酵液の保管方法を提供することにある。   This invention is made | formed in view of said subject, The 1st objective is the vinegar fermentation which can be stored in the state which maintained the microbial cell activity of the vinegar fermentation liquid in spite of being simple and excellent in cost property. It is to provide a method for storing liquid.

本発明の第2の目的は、速やかに発酵を開始できるため生産性向上に好都合な食酢の製造方法を提供することにある。   The second object of the present invention is to provide a method for producing vinegar that is convenient for improving productivity because fermentation can be started quickly.

本発明の第3の目的は、菌体活性が維持されているため速やかに発酵を開始できる酢酸発酵用種酢溶液を提供することにある。   The third object of the present invention is to provide a seed vinegar solution for acetic acid fermentation that can quickly start fermentation because the cell activity is maintained.

上記の課題を解決しうる手段を模索すべく、本願発明者が鋭意研究を行ったところ、発酵中の食酢発酵液を希釈しかつ凍結しない程度の低温にすれば、中和剤に代表される添加物等を使用しなくても菌体活性を維持しつつ保管できることを新規に知見した。そして本願発明者は、この新規な知見に基づいてさらに鋭意研究を行うことで、最終的に下記の発明を完成させるに至ったのである。   The present inventor has conducted extensive research to find a means that can solve the above-described problems. If the vinegar fermentation liquid during fermentation is diluted to a temperature that does not freeze, it is represented by a neutralizing agent. It was newly found that it can be stored while maintaining the cell activity without using additives. And this inventor finally came to complete the following invention by conducting earnest research based on this novel knowledge.

即ち、上記課題を解決する第1の手段(請求項1に記載の発明)は、深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により酢酸濃度が2重量/容量%以上5重量/容量%以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、24時間以上60日間以下保管された食酢発酵液を、別の酢酸発酵を行う際に種酢として使用することで酢酸発酵を行うことを特徴とする食酢の製造方法をその要旨とする。また、上記課題を解決する第2の手段(請求項2に記載の発明)は、深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により酢酸濃度が2重量/容量%以上5重量/容量%以下の範囲となることを条件として希釈倍率が1.5倍以上4.0倍以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、24時間以上60日間以下保管された食酢発酵液を、別の酢酸発酵を行う際に種酢として使用することで酢酸発酵を行うことを特徴とする食酢の製造方法をその要旨とする。 That is, the first means for solving the above problems (the invention according to claim 1) is that a vinegar fermented liquid being fermented by a submerged culture method is used, and an acetic acid concentration of 2 wt / vol% or more by adding a diluent solvent is 5 or more. A vinegar fermented liquid diluted to a weight / volume% or lower and cooled to a liquid temperature of 0 ° C. or higher and 15 ° C. or lower and stored for 24 hours or longer and 60 days or less is subjected to another acetic acid fermentation. The gist is a method for producing vinegar characterized by performing acetic acid fermentation by using as seed vinegar when performing . A second means for solving the above problem (the invention according to claim 2) is that a vinegar fermentation liquid being fermented by a submerged culture method is used, and an acetic acid concentration of 2 wt / vol% or more is 5 by adding a diluting solvent. Dilute so that the dilution ratio is 1.5 times or more and 4.0 times or less under the condition that the weight / volume% or less range , and cool the liquid temperature to be 0 ° C or more and 15 ° C or less The vinegar fermentation solution stored for 24 hours or more and 60 days or less is used as seed vinegar when another acetic acid fermentation is performed .

ここで、本願出願人は極低温や高濃度酢酸等が酢酸菌活性の阻害要因であると考えているが、第1及び第2の手段にかかる発明では発酵中の食酢発酵液を原液のままではなく、ある程度希釈して酢酸濃度を下げた状態で保管するようにしているため、休眠している酢酸菌が酢酸によるダメージを受けにくくなる。また、上記発明では0℃以上15℃以下の液温、即ち凍結しない程度の低温で食酢発酵液を保管するようにしているため、休眠している酢酸菌が低温によるダメージを受けにくくなる。以上の結果、菌体活性を維持した状態で食酢発酵液を保管することができ、それゆえその保管しておいた食酢発酵液を後日、生産計画に合わせて種酢として利用すること等が可能となる。   Here, although the present applicant thinks that cryogenic temperature, high concentration acetic acid, etc. are the inhibition factors of acetic acid bacteria activity, in the invention concerning the 1st and 2nd means, the vinegar fermented liquor under fermentation remains with a stock solution. Instead, it is stored in a state where the acetic acid concentration is lowered by diluting to some extent, so that the dormant acetic acid bacteria are not easily damaged by acetic acid. Moreover, in the said invention, since the vinegar fermentation liquid is stored at the liquid temperature of 0 degreeC or more and 15 degrees C or less, ie, the low temperature which is not frozen, the dormant acetic acid bacteria become difficult to receive the damage by low temperature. As a result, it is possible to store vinegar fermented liquid while maintaining the cell activity. Therefore, it is possible to use the stored vinegar fermented liquid as seed vinegar at a later date according to the production plan. It becomes.

さらに、上記発明の方法を実施する場合であっても、小スケールの前培養用発酵装置、遠心分離機、冷凍庫などといった装置を必須とするわけではない。それゆえ、上記発明の方法は、従来方法と比較して簡便であってコスト性にも優れていると言うことができる。 Furthermore, even when carrying out the way of the invention, the culture fermentor previous small-scale centrifuge, not as essential such devices such as a freezer. Therefore, how the invention is a simple as compared with the conventional method can be said to be excellent in cost properties.

上記発明の方法においては、発酵中の食酢発酵液と、前記発酵中の食酢発酵液よりも低温に設定された希釈溶媒とを混合することにより、前記発酵中の食酢発酵液の希釈及び冷却を行うことが好ましい(請求項3)。本発明によると、希釈溶媒が冷媒としての役割も果たすため、混合によって希釈及び冷却を同時にかつ速やかに行うことが可能となる。従って、希釈及び冷却を別々に行うような場合に比べて、簡便性及び作業性が確実に向上する。 In how the above invention, a vinegar fermentation liquid in the fermentation, by mixing the diluting solvent is set to a temperature lower than vinegar fermentation liquid in the fermentation, dilution and cooling of the vinegar fermentation liquid in the fermentation (Claim 3). According to the present invention, since the dilution solvent also serves as a refrigerant, dilution and cooling can be performed simultaneously and rapidly by mixing. Therefore, compared with the case where dilution and cooling are performed separately, simplicity and workability are reliably improved.

さらに、上記発明の方法においては、深部発酵用発酵装置から採取された発酵中の食酢発酵液と、前記発酵中の食酢発酵液よりも低温に設定された希釈溶媒とを、耐酸性を有する保管容器内にて混合することにより、前記発酵中の食酢発酵液の希釈及び冷却を同時に行った後、前記保管容器内にて保管を行うことが好ましい(請求項4)。即ち本発明によると、食酢発酵液の希釈及び冷却を深部発酵用発酵装置とは別の場所(つまり保存容器内)に移して行うようにしているため、深部発酵用発酵装置内の環境に大きな影響を及すこともなく、当該槽内での発酵を継続、維持することができる。また、この保管容器は耐酸性を有しているため、長期にわたり保管を行ったとしても酢酸による腐食を起こさず、食酢発酵液を確実に保管することができる。 Furthermore, in the way of the invention, a vinegar fermentation solution during the fermentation was collected from submerged fermentation fermentor, and a diluting solvent is set to a temperature lower than vinegar fermentation liquid in the fermentation, acid-resistant It is preferable to store in the storage container after simultaneously diluting and cooling the vinegar fermentation liquid during the fermentation by mixing in the storage container (Claim 4). That is, according to the present invention, the dilution and cooling of the vinegar fermented liquid is performed by moving it to a place different from the fermentation apparatus for deep fermentation (that is, in the storage container), so that the environment in the fermentation apparatus for deep fermentation is large. The fermentation in the tank can be continued and maintained without affecting. Moreover, since this storage container has acid resistance, even if it is stored for a long period of time, it does not cause corrosion due to acetic acid and can reliably store the vinegar fermented liquid.

なお、耐酸性を有する保管容器は例えば蓋付きであることがよく、保管の際にはその蓋を閉じておくことが好ましい。その理由は、雑菌や埃の侵入を防ぐことができるため、食酢発酵液の腐敗を防止でき、かつ酢酸菌の活性を維持することができるからである。   The storage container having acid resistance is preferably provided with a lid, for example, and the lid is preferably closed during storage. The reason for this is that it is possible to prevent invasion of various germs and dust, so that the vinegar fermented liquid can be prevented from decaying and the activity of the acetic acid bacteria can be maintained.

そして、上記課題を解決する第の手段(請求項に記載の発明)は、深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により酢酸濃度が2重量/容量%以上5重量/容量%以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、24時間以上60日間以下保存してなることを特徴とする酢酸発酵用種溶液をその要旨とする。また、上記課題を解決する第の手段(請求項に記載の発明)は、深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により希釈倍率が酢酸濃度が2重量/容量%以上5重量/容量%以下の範囲となることを条件として1.5倍以上4.0倍以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、24時間以上60日間以下保存してなることを特徴とする酢酸発酵用種溶液をその要旨とする。従って、第3及び第4の手段にかかる発明の酢酸発酵用種溶液では菌体活性が維持されているため、この溶液を仕込液に添加することにより、速やかに発酵を開始することができる。 And the 3rd means (invention of Claim 5 ) which solves the said subject is the acetic acid density | concentration of 2 weight / volume% or more 5 by adding the dilution solvent to the vinegar fermented liquid currently fermented by the submerged culture method. A seed for acetic acid fermentation characterized by being diluted to weight / volume% or less, cooled to a liquid temperature of 0 ° C. or more and 15 ° C. or less, and stored for 24 hours or more and 60 days or less The vinegar solution is the gist. Moreover, the 4th means (invention of Claim 6 ) which solves the said subject is a vinegar fermentation liquid currently fermented by the submerged culture method, and the dilution rate is an acetic acid density | concentration 2 weight / volume by addition of a dilution solvent. The solution is diluted so that it is 1.5 times or more and 4.0 times or less under the condition that it is in the range of not less than 5% and not more than 5% weight / volume% , and cooled so that the liquid temperature becomes not less than 0 ° C and not more than 15 ° C. A ginseng solution for acetic acid fermentation, which is stored for 24 hours or more and 60 days or less . Therefore, since the bacterial cell activity is maintained in the seed vinegar solution for acetic acid fermentation of the invention according to the third and fourth means, the fermentation can be started quickly by adding this solution to the charged solution. .

以上詳述したように、請求項1〜4に記載の発明によると、食酢発酵液の菌体活性を維持した状態で保管されていた食酢発酵液を種酢として利用することで速やかに発酵を開始できるため、生産性向上に好都合な食酢の製造方法を提供することができる。請求項5,6に記載の発明によると、菌体活性が維持されているため速やかに発酵を開始できる酢酸発酵用種酢溶液を提供することができる。 As described in detail above, according to the inventions described in claims 1 to 4, fermentation can be performed quickly by using the vinegar fermented liquid stored in the state of maintaining the bacterial activity of the vinegar fermented liquid as seed vinegar. Since it can start, the manufacturing method of the vinegar which is convenient for productivity improvement can be provided. According to invention of Claim 5 , 6 , since the microbial cell activity is maintained, the seed vinegar solution for acetic acid fermentation which can start fermentation rapidly can be provided.

以下、本発明を具体化した一実施の形態を詳細に説明する。   Hereinafter, an embodiment of the present invention will be described in detail.

本発明における深部培養法にて用いられる酢酸菌としては特に限定されないが、例えばアセトバクター(Acetobacter)属の酢酸菌が用いられる。アセトバクター属酢酸菌の好適な具体例としては、アセトバクター・アセチIFO3281(Acetobacter aceti IFO3281)株、アセトバクター・アセチIFO3283(Acetobacter aceti IFO3283)株などがある。これらの酢酸菌は10.0重量/容量%以下の酢酸濃度で食酢の発酵生産に用いられる酢酸菌であるが、高酸度食酢用の酢酸菌を用いることも可能である。その具体例としては、アセトバクター・ヨーロペウス(Acetobacter europaeus)、アセトバクター・アルトアセチゲネスMH−24(FERM BP−491)などがある。   Although it does not specifically limit as an acetic acid bacterium used by the deep culture method in this invention, For example, the acetic acid bacterium of the acetobacter genus is used. Preferable specific examples of Acetobacter acetic acid bacteria include Acetobacter aceti IFO 3281 (Acetobacter acetic IFO 3281) strain, Acetobacter aceti IFO 3283 (Acetobacter acetic IFO 3283) strain and the like. These acetic acid bacteria are acetic acid bacteria used for fermenting production of vinegar at an acetic acid concentration of 10.0% by weight or less, but acetic acid bacteria for high acidity vinegar can also be used. Specific examples thereof include Acetobacter europaeus and Acetobacter altoacetigenes MH-24 (FERM BP-491).

なお、本発明において酢酸濃度とは、以下のようにして測定し、計算した結果得られる酢酸換算濃度(重量/容量%)のことを意味する。即ち、測定用試料として食酢(発酵液)5mLをビーカーにとり、1N水酸化ナトリウムを用い、フェノールフタレインを指示薬として中和滴定し、得られた滴定量(mL)を1.2倍して酢酸濃度換算した値を酸度とし、%であらわした。   In the present invention, the acetic acid concentration means an acetic acid equivalent concentration (weight / volume%) obtained as a result of measurement and calculation as follows. That is, 5 mL of vinegar (fermented liquid) as a measurement sample was placed in a beaker, neutralized with 1N sodium hydroxide and neutralized with phenolphthalein as an indicator, and the titration (mL) obtained was multiplied by 1.2 to acetic acid. The concentration converted value was defined as acidity and expressed in%.

本発明において食酢発酵液を得るための深部培養法とは、培養装置内の発酵液に対する積極的な通気・攪拌を行うことにより、発酵液全体に酸素を供給し、液表面のみならずその深部についてまでも酢酸菌を生育させて発酵を行わせる培養法のことを指し、通常は表面発酵法と対比される。   In the present invention, the submerged culture method for obtaining a vinegar fermented liquid is to supply oxygen to the whole fermented liquid by actively aeration and agitation with respect to the fermented liquid in the culture apparatus. Refers to a culture method in which acetic acid bacteria are grown and fermentation is performed, and is usually compared with the surface fermentation method.

深部培養を行うための装置としては特に限定されず、一般的な通気攪拌型の深部発酵装置を用いることができる。攪拌については従来公知の手段を採用することができ、例えばプロペラやロータ等の攪拌機を使用することが好適である。また、通気についても同様に従来公知の手段を採用することができ、その具体例としては、空気や酸素等の気体を通気管を通じて供給する方法などが挙げられる。通気量については発酵状況に応じて適宜設定すればよい。例えば、0.02〜1vvm(通気容量/発酵液量/分)の通気量にして、気体を発酵液の下部に供給し、これを攪拌機で微細化・拡散させ、発酵液中の溶存酸素が0.2〜8ppm程度で維持されるように制御すればよい。   The apparatus for performing the deep culture is not particularly limited, and a general aeration and stirring type deep fermentation apparatus can be used. A conventionally well-known means can be employ | adopted about stirring, for example, it is suitable to use stirring machines, such as a propeller and a rotor. Similarly, conventionally known means can be used for ventilation, and specific examples thereof include a method of supplying a gas such as air or oxygen through a ventilation pipe. About aeration, what is necessary is just to set suitably according to a fermentation condition. For example, the aeration rate of 0.02 to 1 vvm (aeration capacity / amount of fermentation broth / min) is supplied to the lower part of the fermentation broth, the gas is refined and diffused with a stirrer, and the dissolved oxygen in the fermentation broth is What is necessary is just to control so that it may be maintained at about 0.2-8 ppm.

また、発酵形式についても、回分発酵法、半連続発酵法、二段発酵法など、従来から実施されてきた各種の方式を採用することができる。   Moreover, about the fermentation format, the various methods conventionally implemented, such as a batch fermentation method, a semi-continuous fermentation method, and a two-stage fermentation method, are employable.

そして上記の深部培養法により得られた発酵中の食酢発酵液は、以下のようにして希釈及び冷却される。   And the vinegar fermented liquor during fermentation obtained by said deep culture method is diluted and cooled as follows.

食酢発酵液としては発酵中のもの(即ち酢酸生成中のもの)を採取する必要があり、より好ましくは発酵の初期段階及び終期段階を除く期間(便宜上、中期段階と呼ぶ。)にて採取することがよい。この期間の食酢発酵液には、活性の高い酢酸菌が多く含まれているため、保管をする対象として適当だからである。これに対し、発酵の初期段階では発酵がまだ十分に開始していないため菌体の数が少なく、発酵の終期段階ではもはや菌体の活性が高いとはいえないため、いずれも長期にわたる保管をするのに適していないからである。   The vinegar fermented liquor must be collected during fermentation (that is, during production of acetic acid), and more preferably during the period excluding the initial and final stages of fermentation (referred to as the intermediate stage for convenience). That is good. This is because the vinegar fermented liquid during this period contains a large amount of highly active acetic acid bacteria and is therefore suitable for storage. On the other hand, since the fermentation has not yet started sufficiently at the initial stage of fermentation, the number of cells is small, and at the final stage of fermentation, the activity of the cells is no longer high. Because it is not suitable to do.

発酵中の食酢発酵液の採取時における酢酸菌の濃度は特に限定されず、使用する酢酸菌の種類によっても異なるが、例えば10個/mL以上であることが好ましく、特には10個/mL以上であることが好ましい。長期にわたり保管を行った場合、活性を有する酢酸菌数の減少はある程度避けられないが、あらかじめ高濃度の酢酸菌を採取しておけば、必要とする酢酸菌数を確保しやすくなるからである。 The concentration of acetic acid bacteria at the time of collecting the vinegar fermented liquor during fermentation is not particularly limited and varies depending on the type of acetic acid bacteria to be used. For example, it is preferably 10 6 / mL or more, particularly 10 7 / It is preferable that it is mL or more. When stored for a long period of time, the number of acetic acid bacteria having activity is inevitably reduced, but if a high concentration of acetic acid bacteria is collected in advance, it becomes easier to secure the required number of acetic acid bacteria. .

発酵中の食酢発酵液の液温はいわゆる常温であり、より詳しくいうと20℃以上40℃以下である。また、発酵中の食酢発酵液における酢酸濃度は、使用する酢酸菌の種類により異なるが、概して5重量/容量%以上である。また、発酵中の食酢発酵液においてアルコール(主としてエチルアルコール)は、通常0.1〜3.0重量/容量%程度含まれている。   The liquid temperature of the vinegar fermented liquid during fermentation is so-called room temperature, and more specifically, 20 ° C. or higher and 40 ° C. or lower. Moreover, although the acetic acid concentration in the vinegar fermented liquor during fermentation changes with kinds of acetic acid bacteria to be used, it is generally 5 weight / volume% or more. In addition, alcohol (mainly ethyl alcohol) is usually contained in the vinegar fermented liquid during fermentation in an amount of about 0.1 to 3.0% by weight / volume.

酢酸発酵工程におけるアルコール濃度の測定の際には、精度の高いアルコール測定装置であるガスクロマトグラフィーや、ガスセンサーなどを利用するのが好ましい。例えば、島津製作所製ガスクロマトグラフィー(GC−17A)で、GLサイエンス製カラム(TC−WAX:0.53mm×30m)を用い、ディテクション220℃、カラム温度40℃で5分間保持し、4℃/分の条件で220℃まで昇温させて220℃で10分保持する測定条件で、試料を1μL用いる方法などが例示される。   In measuring the alcohol concentration in the acetic acid fermentation process, it is preferable to use gas chromatography, a gas sensor, or the like, which is a highly accurate alcohol measuring device. For example, with a gas chromatography (GC-17A) manufactured by Shimadzu Corporation, a column made by GL Science (TC-WAX: 0.53 mm × 30 m) is used and kept at a detection temperature of 220 ° C. and a column temperature of 40 ° C. for 5 minutes, and 4 ° C. Examples include a method of using 1 μL of a sample under measurement conditions in which the temperature is raised to 220 ° C. under the conditions of / min and held at 220 ° C. for 10 minutes.

本発明における希釈は、採取した発酵中の食酢発酵液と希釈溶媒とを混合することにより行われる。かかる混合が行われる場所は、深部発酵用発酵装置の中であってもよいが、それとは別に用意された保管容器の中であってもよい。ここで希釈溶媒としては、少なくとも採取した発酵中の食酢発酵液よりも酢酸濃度が低い溶液であれば任意の液体を使用することができる。ただし、後に食酢発酵のための種酢として使用する予定があるような場合の希釈溶媒としては、食酢成分として許容される成分(例えば水、原料糖液、アルコールなど)のみを含む液体を使用することが望ましく、特には水を使用することが望ましい。なお、希釈溶媒にエタノール等のアルコールが多く含まれていると、菌体がダメージを受ける可能性があるので、その濃度を可能な限り低くしておくことが好ましい。勿論、従来技術にて述べた中和剤に相当するような添加物は、本発明における希釈溶媒に含まれないことが望ましい。   Dilution in this invention is performed by mixing the extract | collected vinegar fermented liquor in fermentation and a dilution solvent. The place where such mixing is performed may be in the fermentation apparatus for deep fermentation, or may be in a storage container prepared separately. Here, as the diluting solvent, any liquid can be used as long as it is a solution having a lower acetic acid concentration than the collected vinegar fermented liquid during fermentation. However, as a diluting solvent when it is planned to be used as seed vinegar for vinegar fermentation later, a liquid containing only components that are acceptable as vinegar components (for example, water, raw sugar solution, alcohol, etc.) is used. It is desirable to use water in particular. It should be noted that if the diluent solvent contains a large amount of alcohol such as ethanol, the cells may be damaged, so it is preferable to keep the concentration as low as possible. Of course, it is desirable that an additive corresponding to the neutralizing agent described in the prior art is not included in the diluting solvent in the present invention.

そしてこのような希釈溶媒の添加によって、発酵中の食酢発酵液は、酢酸濃度が2重量/容量%以上5重量/容量%以下となるように希釈される。仮に、酢酸濃度を5重量/容量%を超える程度に希釈したとしても、依然として多くの酢酸が存在しているため、保管時に酢酸菌に与えるダメージを十分に軽減することができない。逆に、酢酸濃度を2重量/容量%未満となるように希釈した場合、高濃度酢酸の存在による酢酸菌のダメージ軽減が達成される反面、酢酸菌の持つ殺菌作用まで損なわれてしまい、腐敗菌が増殖しやすい環境になってしまう。従って、食酢発酵液の長期にわたる保管が困難になるおそれがある。   And by addition of such a dilution solvent, the vinegar fermented liquor during fermentation is diluted so that an acetic acid density | concentration will be 2 weight / volume% or more and 5 weight / volume% or less. Even if the acetic acid concentration is diluted to a level exceeding 5% by weight / volume, there is still a large amount of acetic acid, so that damage to acetic acid bacteria during storage cannot be sufficiently reduced. Conversely, when the acetic acid concentration is diluted to less than 2% by weight / volume, the damage of the acetic acid bacteria is reduced due to the presence of the high concentration acetic acid, but the bactericidal action of the acetic acid bacteria is impaired and spoilage occurs. It will be an environment where bacteria are easy to grow. Therefore, it may be difficult to store the vinegar fermented liquid for a long time.

また、発酵中の食酢発酵液は、希釈開始時における酢酸濃度の高低にも依存するが、希釈溶媒の添加により希釈倍率が1.5倍以上4.0倍以下となるように希釈される。仮に、希釈倍率が1.5倍未満であると、希釈溶媒の添加量が少なすぎることから、酢酸濃度を5重量/容量%以下にできないケースが生じうる。よってこの場合には、食酢発酵液中に依然として多くの酢酸が存在しているため、保管時に酢酸菌に与えるダメージを十分に軽減することができない。逆に、希釈倍率が4.0倍を超えると、希釈溶媒の添加量が多すぎることから、酢酸濃度を2重量/容量%以上にできないケースが生じうる。よってこの場合には高濃度酢酸の存在による酢酸菌のダメージ軽減が達成される反面、酢酸菌の持つ殺菌作用まで損なわれてしまい、腐敗菌が増殖しやすい環境になってしまう。従って、食酢発酵液の長期にわたる保管が困難になるおそれがある。   Further, the fermented vinegar fermented liquid during fermentation depends on the level of acetic acid at the start of dilution, but is diluted so that the dilution ratio becomes 1.5 times or more and 4.0 times or less by the addition of a dilution solvent. If the dilution ratio is less than 1.5 times, there may be a case where the acetic acid concentration cannot be reduced to 5% by weight or less because the addition amount of the dilution solvent is too small. Therefore, in this case, since much acetic acid is still present in the vinegar fermented liquid, damage to acetic acid bacteria during storage cannot be sufficiently reduced. On the other hand, when the dilution ratio exceeds 4.0 times, there may be a case where the acetic acid concentration cannot be increased to 2% by weight or more because the amount of the diluted solvent added is too large. Therefore, in this case, although the damage reduction of acetic acid bacteria due to the presence of high-concentration acetic acid is achieved, the bactericidal action of acetic acid bacteria is impaired and an environment in which spoilage bacteria are likely to grow is obtained. Therefore, it may be difficult to store the vinegar fermented liquid for a long time.

希釈された食酢発酵液中にはできるだけ多くの酢酸菌が含まれていることが好ましく、具体的には10個/mL以上、特には10個/mL以上含まれていることがよい。酢酸菌の濃度が高ければ、保管期間が長期にわたった場合でも、種酢等としての利用が可能になるからである。 It is preferable that as many acetic acid bacteria as possible are contained in the diluted vinegar fermented broth, specifically 10 5 / mL or more, particularly 10 6 / mL or more. This is because if the concentration of acetic acid bacteria is high, it can be used as seed vinegar even when the storage period is long.

また、本発明における冷却は、発酵中の食酢発酵液の液温を0℃以上15℃以下に下げることを行う。仮に液温を15℃まで下げないような不完全な冷却であると、食酢発酵液中の酢酸菌が十分に休眠せず、酢酸菌の菌数低下が生じる。さらに、野生酢酸菌など食酢製造には好ましくない菌が繁殖するなどの弊害が生じるおそれもあるため、15℃以下で保管することが必要となる。逆に、液温を0℃よりも低くする過冷却であると、食酢発酵液が凍結してしまい、かえって酢酸菌にダメージを与えてしまう結果、やはり酢酸菌の活性低下が避けられなくなる。   Moreover, the cooling in this invention reduces the liquid temperature of the vinegar fermented liquor during fermentation to 0 degreeC or more and 15 degrees C or less. If the cooling is incomplete so as not to lower the liquid temperature to 15 ° C., the acetic acid bacteria in the vinegar fermented liquid do not sufficiently sleep, and the number of acetic acid bacteria decreases. Furthermore, since there is a possibility that harmful bacteria such as wild acetic acid bacteria propagate in vinegar production, it is necessary to store at 15 ° C. or lower. On the other hand, if the liquid temperature is lower than 0 ° C., the vinegar fermented broth freezes, causing damage to the acetic acid bacteria, resulting in an inevitable decrease in the activity of the acetic acid bacteria.

本発明において食酢発酵液を冷却する場合、液温を0℃以上15℃以下に下げることができるのであれば、従来公知の任意の方法を採用することができる。その好適な例を挙げると、例えば、発酵中の食酢発酵液に冷媒を直接接触させずに熱交換器を介して間接的に接触させて熱を奪い取る間接冷却法がある。この方法の利点は、発酵中の食酢発酵液に冷媒が直接接触せず両者が互いに混ざり合うことがないため、冷媒の選択の自由度が大きいことである。なお、冷媒は液体であってもよく気体であってもよい。   In the present invention, when the vinegar fermented liquid is cooled, any conventionally known method can be adopted as long as the liquid temperature can be lowered to 0 ° C. or higher and 15 ° C. or lower. As a suitable example, for example, there is an indirect cooling method in which the refrigerant is indirectly contacted via a heat exchanger without directly contacting the fermented vinegar fermentation liquid, and the heat is taken away. The advantage of this method is that the refrigerant is not in direct contact with the fermented vinegar fermentation liquid and the two do not mix with each other, so that the degree of freedom in selecting the refrigerant is great. The refrigerant may be a liquid or a gas.

また、上記のような間接冷却法ではなく、発酵中の食酢発酵液に冷媒を直接接触させて熱を奪い取る直接冷却法を採用することも可能である。この方法によると冷媒の選択の自由度が小さくなる一方で、冷媒と希釈溶媒とを共通化することが可能となる。   Further, instead of the indirect cooling method as described above, it is also possible to employ a direct cooling method in which a refrigerant is brought into direct contact with the fermented vinegar fermentation liquid and heat is taken away. According to this method, the degree of freedom in selecting the refrigerant is reduced, while the refrigerant and the diluting solvent can be shared.

ここで、冷却を行うときのスピードは特に限定されないが、例えば、通気を止めた後に冷却を行うような場合には、菌体の活性をできるだけ維持するために急冷を行う(例えば3時間以内で冷却を完了させる)ことが望ましい。即ち、通気を止めてしまうと、酢酸菌の活性が低下し始めるため、その前にできるだけ早期のうちに酢酸菌を休眠に移行させることが望ましいからである。   Here, the speed at which cooling is performed is not particularly limited. For example, when cooling is performed after aeration is stopped, rapid cooling is performed in order to maintain the activity of the cells as much as possible (for example, within 3 hours). It is desirable to complete the cooling). That is, if the aeration is stopped, the activity of the acetic acid bacteria starts to decrease, so that it is desirable to shift the acetic acid bacteria to dormancy as soon as possible before that.

ところで、本発明では冷却後に希釈を行ってもよく、希釈後に冷却を行ってもよいが、好ましくは希釈及び冷却を同時に行うことが工程上都合がよい。この場合においては希釈溶媒が直接接触法における冷媒としての役割も果たすことになる。よって、発酵中の食酢発酵液の希釈及び冷却を同時にかつ速やかに行うことが可能となる。   By the way, in the present invention, dilution may be performed after cooling, or cooling may be performed after dilution, but it is preferable in the process that dilution and cooling are preferably performed simultaneously. In this case, the diluted solvent also serves as a refrigerant in the direct contact method. Therefore, it becomes possible to perform dilution and cooling of the vinegar fermentation liquid during fermentation simultaneously and rapidly.

この場合、冷媒を兼ねる希釈溶媒は、発酵中の食酢発酵液の液温(通常20℃以上)よりも低温に設定された液体であることがよく、具体的には15℃以下の冷水または氷水であることが好ましい。即ち、水は食酢成分として問題なく許容されるものであるため、添加しても酢酸菌の活性等に悪影響を与えないからである。なお、急冷を行いたい場合には、5℃以下の冷水または氷水を用いることが好ましい。   In this case, the dilution solvent that also serves as the refrigerant is preferably a liquid set at a temperature lower than the liquid temperature of the vinegar fermented liquid during fermentation (usually 20 ° C. or higher), specifically, cold water or ice water of 15 ° C. or lower. It is preferable that That is, because water is acceptable as a vinegar component without any problem, even if added, it does not adversely affect the activity of acetic acid bacteria. In addition, when performing rapid cooling, it is preferable to use cold water or ice water of 5 degrees C or less.

発酵中の食酢発酵液の希釈及び冷却は、深部発酵用発酵装置内にて行うことができるが、深部発酵用発酵装置外にて行うことも可能である。具体的には、深部発酵用発酵装置から採取された発酵中の食酢発酵液と、冷媒を兼ねる希釈溶媒とを、深部発酵用発酵装置とは別に用意された保管容器内にて混合する。このような保管容器としては特に限定されず、従来公知の任意のものが使用可能であるが、酢酸に耐えうる程度の耐酸性を有する材料からなるものが好ましい。このような保管容器であれば、長期にわたり保管を行ったとしても酢酸による腐食を起こさず、食酢発酵液を確実に保管することができる。保管容器に使用される材料は、耐酸性を有するものであれば、金属、ガラス、合成樹脂等の中から任意に選択することが可能であるが、とりわけステンレス等に代表される金属材料を選択することが好適である。従って、市販のステンレス容器などを使用してもよい。また、保管容器の容量に制限はないため、必要に応じて大きいものを使用してもよい。例えば、食品工業用途の場合には容量が1kL以上の保管容器を使用してもよい。   Dilution and cooling of the vinegar fermented liquid during fermentation can be performed in the fermentation apparatus for deep fermentation, but can also be performed outside the fermentation apparatus for deep fermentation. Specifically, the fermented vinegar fermentation liquid collected from the fermentation apparatus for deep fermentation and the diluent solvent that also serves as a refrigerant are mixed in a storage container prepared separately from the fermentation apparatus for deep fermentation. Such a storage container is not particularly limited, and any conventionally known one can be used, but one made of a material having acid resistance enough to withstand acetic acid is preferable. If it is such a storage container, even if it stores for a long period of time, it will not corrode by acetic acid and can store vinegar fermented liquid reliably. The material used for the storage container can be arbitrarily selected from metals, glass, synthetic resins, etc., as long as it has acid resistance, but especially metal materials represented by stainless steel etc. are selected. It is preferable to do. Therefore, a commercially available stainless steel container or the like may be used. Moreover, since there is no restriction | limiting in the capacity | capacitance of a storage container, you may use a large thing as needed. For example, in the case of food industry use, a storage container having a capacity of 1 kL or more may be used.

なお、耐酸性を有する保管容器は例えば蓋付きであることがよく、保管の際にはその蓋を閉じておくことが好ましい。その理由は、雑菌や埃の侵入を防ぐことができるため、食酢発酵液の腐敗を防止でき、かつ酢酸菌の活性を維持することができるからである。蓋の構造は任意であるが、特に密閉性が要求されるわけではない。   The storage container having acid resistance is preferably provided with a lid, for example, and the lid is preferably closed during storage. The reason for this is that it is possible to prevent invasion of various germs and dust, so that the vinegar fermented liquid can be prevented from decaying and the activity of the acetic acid bacteria can be maintained. The structure of the lid is arbitrary, but the sealing property is not particularly required.

そして上述のように希釈及び冷却された食酢発酵液は、その液温の範囲を維持した状態で24時間以上保管される。保管時に食酢発酵液の通気や攪拌を行うことも許容されるが、そのためには保管容器に通気手段や攪拌手段が必要になり、コスト上のデメリットが大きくなる。従って、特に通気手段や攪拌手段を持たない単純な構造の保管容器を用いて保管することが、コスト的にも有利であり、簡便な方法となる。また、保管容器の温度を低く維持するためには、例えば、保管容器ごと冷蔵庫に入れておくようにすればよい。なお、本発明では冷凍庫を用いる必要はなく冷蔵庫で十分であるため、電気代がそれほどかからずランニングコストの高騰を回避することができる。   And the vinegar fermentation liquid diluted and cooled as mentioned above is stored for 24 hours or more in the state which maintained the range of the liquid temperature. Aeration and agitation of the vinegar fermented liquor during storage are permitted, but this requires a ventilation means and agitation means in the storage container, which increases cost demerits. Therefore, it is advantageous in terms of cost and a simple method to store using a storage container having a simple structure that does not have a ventilation means or a stirring means. In order to keep the temperature of the storage container low, for example, the storage container may be placed in the refrigerator. In the present invention, since it is not necessary to use a freezer and a refrigerator is sufficient, the cost of electricity is not so high and an increase in running cost can be avoided.

以上示した方法で保管しておいた食酢発酵液は、たとえ保管が長期にわたっていたとしても、菌体活性が好適に維持される。従って、これを別の酢酸発酵を行う際に種酢として使用することで酢酸発酵を行えば、酢酸発酵を速やかに開始することができる。よって、前回の深部培養法と同様に深部培養法を行うことにより、所望の食酢を効率よく製造することができる。また本発明によれば、保管しておいた食酢発酵液中には添加剤が何ら含まれていないため、これを種酢として用いたとしても食酢の風味、品質、純度等を低下させることにはつながらない。   The vinegar fermented liquid stored by the method described above is suitably maintained in cell activity even if stored for a long time. Therefore, if acetic acid fermentation is performed by using this as seed vinegar when performing another acetic acid fermentation, acetic acid fermentation can be started rapidly. Therefore, a desired vinegar can be efficiently manufactured by performing a deep culture method similarly to the last deep culture method. In addition, according to the present invention, since the stored vinegar fermented liquid does not contain any additives, even if this is used as seed vinegar, the flavor, quality, purity, etc. of vinegar are reduced. Not connected.

以下、本発明の実施形態をより具体化した実施例を説明する。   Hereinafter, examples in which the embodiment of the present invention is more specific will be described.

実施例1では、液温を一定にする一方で酢酸濃度を複数設定して保管を行う試験を行った。
(試験方法)
In Example 1, a test was performed in which the liquid temperature was kept constant while the acetic acid concentration was set in plural and stored.
(Test method)

深部発酵が可能な発酵タンク(5L容量:ミツワ理化学工業社製)を用い、あらかじめ3Lの食酢発酵液を用意した。この食酢発酵液はアセトバクター・アセチを用いて培養されたものであって、酢酸濃度が7.0重量/容量%、アルコール濃度が0.3容量/容量%、液温が30℃〜35℃程度、酢酸菌濃度が約10個/mLとなっている。このような食酢発酵液を発酵の中期段階、即ち菌体の活性が高く発酵が盛んに起こっている段階で数mL採取した。そして、採取した発酵中の食酢発酵液を、希釈溶媒である27℃の水をあらかじめ入れておいた数本の10mLガラス製試験管(耐酸性を有する保管容器)に速やかに添加し、両液を混合した。この場合、酢酸濃度を5段階(1.0、2.0、3.0、5.0、7.0重量/容量%)に設定するために、それぞれ希釈倍率を7.0倍、3.5倍、2.3倍、1.4倍、1.0倍にして希釈を行った。次に、希釈された食酢発酵液が入っている試験管を冷蔵庫に移し、数時間のうちに設定温度である5℃に冷却した。そしてこの冷却温度を維持しながら、食酢発酵液をそのまま15日間保管した。 Using a fermentation tank capable of deep fermentation (5 L capacity: manufactured by Mitsuwa Richemical Co., Ltd.), a 3 L vinegar fermentation liquid was prepared in advance. This vinegar fermented broth was cultured using Acetobacter aceti, and the acetic acid concentration was 7.0 wt / vol%, the alcohol concentration was 0.3 vol / vol%, and the liquid temperature was 30 ° C to 35 ° C. The concentration of acetic acid bacteria is about 10 8 cells / mL. Several milliliters of such a vinegar fermented liquid was collected at the middle stage of fermentation, that is, at the stage where the activity of the bacterial cells was high and fermentation was actively taking place. Then, the fermented vinegar fermented liquid during fermentation is quickly added to several 10 mL glass test tubes (acid-resistant storage containers) in which 27 ° C. water as a dilution solvent has been put in advance. Were mixed. In this case, in order to set the acetic acid concentration in 5 steps (1.0, 2.0, 3.0, 5.0, 7.0 wt / vol%), the dilution factor is diluted by 7.0, 3.5, 2.3, 1.4, 1.0, respectively. Went. Next, the test tube containing the diluted vinegar fermented liquor was transferred to a refrigerator and cooled to 5 ° C., which is the set temperature, within a few hours. And while maintaining this cooling temperature, the vinegar fermentation liquid was stored for 15 days as it was.

15日経過後、保管しておいた食酢発酵液を冷蔵庫から取り出して種酢とし、酢酸発酵用培地をあらかじめ入れておいた深部発酵用の発酵タンク内にこの種酢を投入した。この後、通気攪拌を行いながら、常法に従って酢酸菌の深部培養を所定時間継続的に行った。なお、804培地(ポリペプトン10g、酵母エキス10g、グルコース10g)に3%容量/容量となるようアルコール(エタノール)を添加したものを、深部培養用の発酵培地として用いた。   After the lapse of 15 days, the stored vinegar fermented liquid was taken out of the refrigerator to make seed vinegar, and this seed vinegar was put into a fermentation tank for deep fermentation in which a medium for acetic acid fermentation was previously placed. Thereafter, the submerged cultivation of acetic acid bacteria was continuously performed for a predetermined time in accordance with a conventional method while performing aeration and stirring. In addition, what added alcohol (ethanol) so that it might become 3% volume / volume to 804 culture medium (polypeptone 10g, yeast extract 10g, glucose 10g) was used as the fermentation medium for deep culture.

そして、培養を開始してから酢酸濃度が上昇し始めるまでの時間(つまり、発酵開始までのタイムラグ)を計測した。これらの結果を図1のグラフに示す。
(試験結果)
And the time (namely, time lag until the start of fermentation) from the start of culture until the acetic acid concentration starts to rise was measured. These results are shown in the graph of FIG.
(Test results)

図1のグラフにおいて、横軸は希釈後における食酢発酵液の酢酸濃度を示し、縦軸は発酵開始までのタイムラグを示している。このグラフによると、酢酸濃度が低くなるほどタイムラグが小さくなる傾向が認められた。また、酢酸濃度が5.0重量/容量%を超えると、急激にタイムラグが大きくなることもわかった。ここで、実用上好ましいタイムラグの程度が72時間以内であると定義した場合、そのレベルを達成するためには、食酢発酵液の酢酸濃度を1.0重量/容量%〜5.0重量/容量%にすればよいことがわかった。ただし、酢酸濃度を2.0重量/容量%以上に設定したものでは食酢発酵液の腐敗が認められなかったが、酢酸濃度を1.0重量/容量%に設定したものでは食酢発酵液の腐敗が認められた。   In the graph of FIG. 1, the horizontal axis indicates the acetic acid concentration of the vinegar fermented liquid after dilution, and the vertical axis indicates the time lag until the start of fermentation. According to this graph, it was recognized that the time lag tends to decrease as the acetic acid concentration decreases. It was also found that the time lag suddenly increased when the acetic acid concentration exceeded 5.0 wt / vol%. Here, when it is defined that the practically preferable time lag is within 72 hours, in order to achieve the level, the acetic acid concentration of the vinegar fermented liquid is 1.0 wt / vol% to 5.0 wt / vol. %. However, rot of the vinegar fermented liquid was not observed when the acetic acid concentration was set to 2.0 wt / volume% or more, but rot of the vinegar fermented liquid was not performed when the acetic acid concentration was set to 1.0 weight / volume%. Was recognized.

以上の結果を総合すると、深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により酢酸濃度が2重量/容量%以上5重量/容量%以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、24時間以上保管する、という食酢発酵液の保管方法の優秀性が実証される結果となった。ちなみに、保管温度を10℃に設定した試験も実施したが、5℃のときとほぼ同様の結果であったため、その具体的なデータは割愛する。   Summing up the above results, the vinegar fermented liquid being fermented by the submerged culture method is diluted so that the acetic acid concentration becomes 2 wt / vol% to 5 wt / vol% by adding a diluent solvent, and the liquid As a result, the superiority of the storage method of the vinegar fermented liquid in which the temperature was cooled to 0 ° C. or higher and 15 ° C. or lower and stored for 24 hours or more was demonstrated. By the way, a test was conducted in which the storage temperature was set to 10 ° C., but since the results were almost the same as those at 5 ° C., the specific data is omitted.

実施例2では、酢酸濃度を一定にする一方で液温及び保管日数を複数設定して保管を行う試験を行った。
(試験方法)
In Example 2, a test was performed in which the acetic acid concentration was kept constant while the liquid temperature and the number of storage days were set in plural.
(Test method)

実施例1にて用意したのと同じ食酢発酵液を用意し、この食酢発酵液を発酵の中期段階にて採取して、これを希釈溶媒である27℃の水をあらかじめ入れておいた数本の10mLガラス製試験管に速やかに添加し、両液を混合した。その結果、酢酸濃度が4.0%重量/容量%である食酢発酵液の希釈液を得た。次に、希釈された食酢発酵液が入っている試験管を冷蔵庫に移し、数時間のうちに設定温度である15℃に冷却した。また、一部のものについては試験管を恒温槽に移し、冷却を行うことなく比較的高い温度(30℃)に維持した。そしてこれらの液温をそれぞれ維持しながら、長期にわたって食酢発酵液を保管した。なお、保管日数については複数段階(0、7、15、35、40、60、100日)に設定した。   Prepare the same vinegar fermented liquid prepared in Example 1, collect this vinegar fermented liquid in the middle stage of fermentation, and add several water that has been preliminarily charged with 27 ° C water as a diluting solvent. Were quickly added to a 10 mL glass test tube, and both solutions were mixed. As a result, a diluted solution of vinegar fermented liquid having an acetic acid concentration of 4.0% weight / volume% was obtained. Next, the test tube containing the diluted vinegar fermented liquor was transferred to a refrigerator and cooled to 15 ° C., which is the set temperature, within a few hours. Moreover, about some things, the test tube was moved to the thermostat, and it maintained at comparatively high temperature (30 degreeC), without cooling. And the vinegar fermented liquor was stored over a long term, maintaining each of these liquid temperature. The number of storage days was set in multiple stages (0, 7, 15, 35, 40, 60, 100 days).

所定期間の経過後、保管しておいた食酢発酵液を取り出して種酢とし、酢酸発酵用培地をあらかじめ入れておいた深部発酵用の発酵タンク内にこの種酢を投入した。この後、通気攪拌を行いながら、常法に従って酢酸菌の深部培養を所定時間継続的に行った。なお、804培地(ポリペプトン10g、酵母エキス10g、グルコース10g)に3%容量/容量となるようアルコール(エタノール)を添加したものを、深部培養用の発酵培地として用いた。   After the lapse of a predetermined period, the stored vinegar fermented liquid was taken out and used as seed vinegar, and this seed vinegar was put into a fermentation tank for deep fermentation in which a medium for acetic acid fermentation was previously placed. Thereafter, the submerged cultivation of acetic acid bacteria was continuously performed for a predetermined time in accordance with a conventional method while performing aeration and stirring. In addition, what added alcohol (ethanol) so that it might become 3% volume / volume to 804 culture medium (polypeptone 10g, yeast extract 10g, glucose 10g) was used as the fermentation medium for deep culture.

そして、培養を開始してから酢酸濃度が上昇し始めるまでの時間(つまり、発酵開始までのタイムラグ)を、15℃保管の場合と30℃保管の場合の各々について計測した。これらの結果を図2のグラフに示す。
(試験結果)
And the time (namely, time lag until the start of fermentation) from the start of culture to the start of increasing acetic acid concentration was measured for each of the cases of 15 ° C. storage and 30 ° C. storage. These results are shown in the graph of FIG.
(Test results)

図2のグラフにおいて、横軸は食酢発酵液の保管日数を示し、縦軸は発酵開始までのタイムラグを示している。このグラフによると、30℃という高温で保管した場合には、保管日数が7日を超えた時点で、発酵開始までのタイムラグが72時間以上となってしまうことがわかった。従って、発酵中の食酢発酵液の液温が高いと、長期にわたる保管ができないことが明らかとなった。   In the graph of FIG. 2, the horizontal axis indicates the storage days of the vinegar fermented liquid, and the vertical axis indicates the time lag until the start of fermentation. According to this graph, when stored at a high temperature of 30 ° C., it was found that the time lag until the start of fermentation was 72 hours or more when the storage days exceeded 7 days. Therefore, it became clear that when the liquid temperature of the vinegar fermented liquid during fermentation is high, it cannot be stored for a long time.

これに対して、15℃という低温で保管した場合には、保管日数が60日を超えた時点であっても、発酵開始までのタイムラグが72時間以内に収まっていた。従って、発酵中の食酢発酵液の液温をこの程度の低さにすれば、かなりの長期にわたって保管が可能になることが明らかとなった。ちなみに、保管温度を5℃、10℃に設定した試験も実施したが、15℃のときとほぼ同様の傾向を示したため、その具体的なデータは割愛する。   On the other hand, when stored at a low temperature of 15 ° C., the time lag until the start of fermentation was within 72 hours even when the storage days exceeded 60 days. Therefore, it became clear that if the temperature of the vinegar fermented liquid during fermentation is set to such a low level, it can be stored for a considerably long period of time. Incidentally, a test was conducted in which the storage temperature was set at 5 ° C. and 10 ° C., but since the same tendency as that at 15 ° C. was shown, the specific data is omitted.

本実施例は、実施例1,2よりも規模をさらに大きくした例である。   The present embodiment is an example in which the scale is further increased as compared with the first and second embodiments.

深部発酵が可能な大型発酵タンクを用い、あらかじめ10kLの食酢発酵液を用意した。この食酢発酵液は、リンゴを原材料とする仕込液とアセトバクター・アセチとを用いて培養されたものであって、酢酸濃度が7.0重量/容量%、アルコール濃度が0.3容量/容量%、液温が30℃〜35℃程度、酢酸菌濃度が約10個/mLとなっている。この大型発酵タンクは通気手段及び攪拌手段を有しており、培養時にはこれらの手段を用いて常に通気及び攪拌を行うようにした。 Using a large-scale fermentation tank capable of deep fermentation, a 10 kL vinegar fermentation liquid was prepared in advance. This vinegar fermented broth was cultivated using a feed solution made from apples and Acetobacter aceti, with an acetic acid concentration of 7.0 wt / vol% and an alcohol concentration of 0.3 vol / vol. %, The liquid temperature is about 30 ° C. to 35 ° C., and the concentration of acetic acid bacteria is about 10 8 cells / mL. This large-scale fermentation tank has aeration means and agitation means, and these means are always used for aeration and agitation during culture.

本実施例ではこのような大型発酵タンクとは別に保管容器を用意しておく。ここで使用する保管容器は、耐酸性を有するステンレス製の箱型タンク(容量1kL)であり、その箱型タンクの上部に設けられた開口部には開閉可能な蓋が取り付けられている。なお、この保管容器内には、あらかじめ0.5kLの氷水(0℃)を入れておくようにした。氷水は、冷媒を兼ねる希釈溶媒として用いられる。   In this embodiment, a storage container is prepared separately from such a large fermentation tank. The storage container used here is an acid-resistant stainless steel box tank (capacity 1 kL), and an openable / closable lid is attached to the opening provided at the top of the box tank. In this storage container, 0.5 kL of ice water (0 ° C.) was previously placed. Ice water is used as a diluent solvent that also serves as a refrigerant.

次に、大型発酵タンクの通気手段及び攪拌手段を停止させた後、食酢発酵液を発酵の中期段階で0.5kL採取した。そして、採取した食酢発酵液をポンプ等にて速やかに保管容器内に移送し、保管容器内にて食酢発酵液と氷水とを混合することにより、液温が約5℃であって酢酸濃度が3.5重量/容量%の希釈液を作製した。つまり、本実施例では希釈倍率を2倍に設定した。   Next, after stopping the aeration means and the stirring means of the large-scale fermentation tank, 0.5 kL of vinegar fermented liquor was collected in the middle stage of fermentation. Then, the collected vinegar fermented liquid is quickly transferred into a storage container with a pump or the like, and the vinegar fermented liquid and ice water are mixed in the storage container so that the liquid temperature is about 5 ° C. and the acetic acid concentration is A 3.5 wt / vol% dilution was made. That is, in this example, the dilution factor was set to 2 times.

次に、冷却及び希釈された食酢発酵液が入っている保管容器を冷蔵庫に移し、蓋をして、5℃の冷却温度を維持しながら、食酢発酵液をそのまま15日間保管した。なお、保管容器があらかじめ冷蔵庫内に配置されているような場合には、大型発酵タンクと保管容器との間を配管で接続し、この配管を介して発酵中の食酢発酵液を圧送するようにしてもよい。   Next, the storage container containing the cooled and diluted vinegar fermented liquor was transferred to a refrigerator and covered, and the vinegar fermented broth was stored as it was for 15 days while maintaining a cooling temperature of 5 ° C. If the storage container is placed in the refrigerator in advance, connect the large-scale fermentation tank and the storage container with a pipe, and pump the vinegar fermentation liquid during fermentation through this pipe. May be.

そして60日経過後、保管しておいた食酢発酵液を保管容器から取り出して種酢とし、リンゴを原材料とする仕込液をあらかじめ入れておいた深部発酵用の大型発酵タンク内にこの種酢を投入した。この後、通気攪拌を行いながら、常法に従って酢酸菌の深部培養を継続的に行い、種酢と同じ種類の食酢(即ちリンゴ酢)を製造した。   After 60 days, the stored vinegar fermented liquid is taken out from the storage container to become seed vinegar, and this seed vinegar is put into a large-scale fermentation tank for deep fermentation in which a preparation liquid made from apples is put in advance. did. Thereafter, the submerged culture of acetic acid bacteria was continuously carried out according to a conventional method with aeration and agitation to produce the same type of vinegar (i.e., apple vinegar).

以下、特許請求の範囲に記載された技術的思想のほかに、前述した実施の形態によって把握される技術的思想を以下に列挙する。   Hereinafter, in addition to the technical ideas described in the claims, the technical ideas grasped by the above-described embodiments are listed below.

(1)請求項1乃至7のいずれか1項において、前記希釈溶媒は、食酢成分として許容される成分のみを含む液体であること。   (1) In any one of claims 1 to 7, the dilution solvent is a liquid containing only components allowed as vinegar components.

(2)請求項1乃至7のいずれか1項において、前記希釈溶媒は、15℃以下の冷水または氷水であること。   (2) In any one of claims 1 to 7, the dilution solvent is cold water or ice water of 15 ° C. or lower.

(3)請求項1乃至7のいずれか1項において、前記希釈溶媒は、1℃以上5℃以下の冷水であること。   (3) In any one of claims 1 to 7, the dilution solvent is cold water of 1 ° C or higher and 5 ° C or lower.

(4)請求項1乃至7のいずれか1項において、深部培養法にて発酵中の食酢発酵液として、発酵の初期段階及び終期段階を除く期間にて採取されたものを用いること。   (4) In any one of claims 1 to 7, the vinegar fermentation liquid being fermented by the submerged culture method should be collected in a period excluding the initial stage and the final stage of fermentation.

(5)請求項1乃至7のいずれか1項において、深部培養法にて発酵中の食酢発酵液として、酢酸菌の生育速度が安定している状態で採取されたものを用いること。   (5) In any one of Claims 1 to 7, the vinegar fermentation liquid being fermented by the submerged culture method should be collected in a state where the growth rate of the acetic acid bacteria is stable.

(6)請求項1乃至7のいずれか1項において、深部培養法にて発酵中の食酢発酵液として、酢酸菌濃度が10個/mL以上であるものを用いること。 (6) In any one of claims 1 to 7, a vinegar fermented liquid that is being fermented by a deep culture method is one having a concentration of acetic acid bacteria of 10 7 / mL or more.

(7)請求項1乃至7のいずれか1項において、希釈及び冷却された食酢発酵液を、積極的な通気を行うことなく静置状態で保管すること。   (7) The diluted and cooled vinegar fermented liquid according to any one of claims 1 to 7, wherein the vinegar fermented liquid is stored in a stationary state without positive aeration.

(8)請求項1乃至7のいずれか1項において、希釈溶媒の添加によりアルコール濃度が0.2重量/容量%以下となるように希釈すること。   (8) In any one of claims 1 to 7, the alcohol concentration is diluted to 0.2 wt / vol% or less by adding a diluent solvent.

(9)深部培養法を経て得られた食酢発酵液の希釈液であって、酢酸濃度が2重量/容量%以上5重量/容量%以下、かつ、液温が0℃以上15℃以下であることを特徴とする酢酸発酵用種酢溶液。   (9) A dilute solution of vinegar fermented liquor obtained through a submerged culture method, wherein the acetic acid concentration is 2 wt / vol% to 5 wt / vol% and the liquid temperature is 0 ° C. to 15 ° C. A seed vinegar solution for acetic acid fermentation.

(10)深部培養法を経て得られた食酢発酵液の希釈液であって、酢酸濃度が2重量/容量%以上5重量/容量%以下、液温が0℃以上15℃以下、かつ、酢酸菌濃度が10個/mL以上であることを特徴とする酢酸発酵用種酢溶液。 (10) A diluted vinegar fermented liquid obtained through a submerged culture method, wherein the acetic acid concentration is 2 wt / vol% to 5 wt / vol%, the liquid temperature is 0 ° C. to 15 ° C., and acetic acid for acetic ferment vinegar solution, wherein the bacteria concentration is 10 6 cells / mL or more.

(11)深部培養法を経て得られた食酢発酵液の希釈液であって、酢酸濃度が2重量/容量%以上5重量/容量%以下、アルコール濃度が0.2重量/容量%以下、液温が0℃以上15℃以下、かつ、酢酸菌濃度が10個/mL以上であることを特徴とする酢酸発酵用種酢溶液。 (11) A diluted solution of a vinegar fermented liquid obtained through a submerged culture method, wherein the acetic acid concentration is 2 wt / vol% to 5 wt / vol%, the alcohol concentration is 0.2 wt / vol% or less, and the liquid A seed vinegar solution for acetic acid fermentation, wherein the temperature is 0 ° C. or more and 15 ° C. or less, and the concentration of acetic acid bacteria is 10 6 / mL or more.

(12)深部培養法を経て得られた食酢発酵液の1.5倍以上4.0倍以下の希釈液であって、液温が0℃以上15℃以下であることを特徴とする酢酸発酵用種酢溶液。   (12) Acetic acid fermentation characterized by being a diluted solution of 1.5 times to 4.0 times the vinegar fermented liquid obtained through the submerged culture method, and having a liquid temperature of 0 ° C to 15 ° C Seed vinegar solution.

(13)深部培養法を経て得られた食酢発酵液の1.5倍以上4.0倍以下の希釈液であって、液温が0℃以上15℃以下、かつ、酢酸菌濃度が10個/mL以上であることを特徴とする酢酸発酵用種酢溶液。 (13) A diluted solution of 1.5 times or more and 4.0 times or less of the vinegar fermented liquid obtained through the deep culture method, the liquid temperature is 0 ° C. or higher and 15 ° C. or lower, and the acetic acid bacteria concentration is 10 6. A seed vinegar solution for fermentation of acetic acid, characterized in that the number is 1 / mL or more.

(14)深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により酢酸濃度が2重量/容量%以上5重量/容量%以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、耐酸性を有する蓋付きの保管容器内で24時間以上保存してなることを特徴とする容器入り酢酸発酵用種酢溶液。   (14) The vinegar fermented liquor being fermented by the submerged culture method is diluted so that the concentration of acetic acid is 2 wt / vol% to 5 wt / vol% by adding a diluent solvent, and the liquid temperature is 0 ° C. A seed vinegar solution for acetic acid fermentation, which is cooled to 15 ° C. or lower and stored in a storage container with acid resistance for 24 hours or more.

(15)深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により希釈倍率が1.5倍以上4.0倍以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、耐酸性を有する蓋付きの保管容器内で24時間以上保存してなることを特徴とする容器入り酢酸発酵用種酢溶液。   (15) The vinegar fermented liquid being fermented by the submerged culture method is diluted by adding a dilution solvent so that the dilution ratio is 1.5 times or more and 4.0 times or less, and the liquid temperature is 0 ° C. or higher and 15 ° C. or higher. A seed vinegar solution for acetic acid fermentation in a container, wherein the seed vinegar solution is stored in a storage container with a lid having acid resistance and cooled for 24 hours or longer.

実施例1の試験結果を示すグラフ。6 is a graph showing the test results of Example 1. 実施例2の試験結果を示すグラフ。6 is a graph showing the test results of Example 2.

Claims (6)

深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により酢酸濃度が2重量/容量%以上5重量/容量%以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、24時間以上60日間以下保管された食酢発酵液を、別の酢酸発酵を行う際に種酢として使用することで酢酸発酵を行うことを特徴とする食酢の製造方法。 The vinegar fermented liquid being fermented by the submerged culture method is diluted by adding a diluent solvent so that the acetic acid concentration becomes 2 wt / vol% to 5 wt / vol%, and the liquid temperature is 0 ° C. to 15 ° C. Production of vinegar characterized by performing acetic acid fermentation by using a vinegar fermented liquid that has been cooled to be as follows and stored for 24 hours or more and 60 days or less as seed vinegar when performing another acetic acid fermentation Method. 深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により酢酸濃度が2重量/容量%以上5重量/容量%以下の範囲となることを条件として希釈倍率が1.5倍以上4.0倍以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、24時間以上60日間以下保管された食酢発酵液を、別の酢酸発酵を行う際に種酢として使用することで酢酸発酵を行うことを特徴とする食酢の製造方法。 The dilution ratio of the vinegar fermented liquid being fermented by the submerged culture method is 1.5 times or more 4 on condition that the concentration of acetic acid is in the range of 2 wt / vol% to 5 wt / vol% by adding a diluent solvent. The diluted vinegar fermented liquid is cooled to a temperature of 0 ° C. to 15 ° C. and stored for 24 hours or more and 60 days or less, and another acetic acid fermentation is performed. A method of producing vinegar characterized by performing acetic acid fermentation by using as seed vinegar. 発酵中の食酢発酵液と、前記発酵中の食酢発酵液よりも低温に設定された希釈溶媒とを混合することにより、前記発酵中の食酢発酵液の希釈及び冷却を行うことを特徴とする請求項1または2に記載の食酢の製造方法。 The vinegar fermented liquid during fermentation is diluted and cooled by mixing the vinegar fermented liquid during fermentation and a dilution solvent set at a lower temperature than the vinegar fermented liquid during fermentation. Item 3. A method for producing vinegar according to Item 1 or 2 . 深部発酵用発酵装置から採取された発酵中の食酢発酵液と、前記発酵中の食酢発酵液よりも低温に設定された希釈溶媒とを、耐酸性を有する保管容器内にて混合することにより、前記発酵中の食酢発酵液の希釈及び冷却を同時に行った後、前記保管容器内にて保管を行うことを特徴とする請求項1または2に記載の食酢の製造方法。 By mixing the fermented vinegar fermented liquid collected from the fermentation apparatus for deep fermentation and the dilution solvent set at a lower temperature than the fermented vinegar fermented liquid in a storage container having acid resistance, The method for producing vinegar according to claim 1 or 2, wherein the vinegar fermentation liquid during fermentation is simultaneously diluted and cooled, and then stored in the storage container . 深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により酢酸濃度が2重量/容量%以上5重量/容量%以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、24時間以上60日間以下保存してなることを特徴とする酢酸発酵用種酢溶液。 The vinegar fermented liquid being fermented by the submerged culture method is diluted by adding a diluent solvent so that the acetic acid concentration becomes 2 wt / vol% to 5 wt / vol%, and the liquid temperature is 0 ° C. to 15 ° C. A seed vinegar solution for fermentation of acetic acid, wherein the seed vinegar solution is cooled to be as follows and stored for 24 hours to 60 days . 深部培養法にて発酵中の食酢発酵液を、希釈溶媒の添加により希釈倍率が酢酸濃度が2重量/容量%以上5重量/容量%以下の範囲となることを条件として1.5倍以上4.0倍以下となるように希釈し、かつ、液温が0℃以上15℃以下となるように冷却して、24時間以上60日間以下保存してなることを特徴とする酢酸発酵用種酢溶液。 The vinegar fermented broth being fermented by the submerged culture method is 1.5 times or more 4 on condition that the dilution ratio is within the range of 2 wt / vol% to 5 wt / vol% by adding a diluent solvent. A vinegar for acetic acid fermentation characterized by being diluted to 0.times. Or less, cooled to a temperature of 0.degree. C. to 15.degree. C. and stored for 24 hours to 60 days. solution.
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