JP5564719B2 - Storage method of acetic acid bacteria, manufacturing method of vinegar - Google Patents
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本発明は、深部発酵法にて発酵中の食酢発酵液から採取した酢酸菌を、後日別の機会に酢酸発酵を行う際の種酢(発酵の種となる「種菌」を含む発酵液)として使用するために、菌の活性を維持した状態で保管しておく酢酸菌の保管方法、食酢の製造方法に関するものである。 As the seed vinegar (fermented liquid containing “inoculum” that becomes the seed of fermentation), acetic acid bacteria collected from the vinegar fermented liquid being fermented by the deep fermentation method are subjected to acetic acid fermentation at a later date. for use, the method storage acetic acid bacteria to be stored while keeping the activity of the bacteria, those concerning the manufacturing process of vinegar.
食酢の深部醗酵法では、発酵を開始する際に仕込み液に種酢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み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 fermentation method of vinegar, it is necessary to add seed vinegar 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 a seed vinegar is quickly and directly added to the next charged liquid. 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み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)。 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 the preparation solution as seed vinegar when starting fermentation has been conventionally proposed (for example, patents). Reference 1).
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。 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. .
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。そして、このような保管技術の一例として、深部発酵法にて発酵中の食酢の発酵液を、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時間以上保管する食酢発酵液の保管方法が提案されている(特許文献2参照)。 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. And as an example of such storage technology, the vinegar fermented liquor being fermented by the deep fermentation method is diluted so that the acetic acid concentration becomes 2 wt / vol% to 5 wt / vol% by adding a diluent solvent And the storage method of the vinegar fermented liquid which cools so that liquid temperature may be 0 degreeC or more and 15 degrees C or less, and stores for 24 hours or more is proposed (refer patent document 2).
しかしながら、特許文献2に記載の保管方法は、1週間程度か、長くても数ヶ月程度という短期間の保管にしか適用できないため、それ以上の期間保管したいような場合には適さない。また、特許文献2に記載の保管方法で保管した食酢発酵液を種酢として用いた場合、食酢発酵が立ち上がるまでの時間(ラグタイム)にばらつきが大きくなり、生産計画を正確に立てることができないという不具合が想定される。さらに、特許文献2に記載の方法によって例えば3ヶ月以上保管をすると、当該保管した食酢発酵液を種酢として用いて食酢発酵を行った場合に発酵の立ち上がりまでの時間(ラグタイム)が長くかかってしまうか、あるいは発酵が立ち上がらないという不具合が想定される。 However, since the storage method described in Patent Document 2 can be applied only to short-term storage of about one week or several months at the longest, it is not suitable for a case where it is desired to store for a longer period. Moreover, when the vinegar fermentation liquid stored by the storage method of patent document 2 is used as seed vinegar, dispersion | variation becomes large in the time (lag time) until vinegar fermentation starts, and a production plan cannot be made correctly. The malfunction is assumed. Furthermore, when it is stored for 3 months or more by the method described in Patent Document 2, for example, when the vinegar fermentation is performed using the stored vinegar fermented liquid as seed vinegar, it takes a long time to start fermentation (lag time). It is assumed that there is a problem that fermentation does not start.
また、特許文献2に記載の保管方法の場合、保管される発酵液には、酢酸菌の他、それぞれの食酢の種類に必要な原料の成分(例えばリンゴ酢ならリンゴ成分、米酢なら米の成分)が含まれている。そのため、保管された発酵液を使用できる範囲(使用できる食酢の種類)が極めて限定されたものとなる。 In the case of the storage method described in Patent Document 2, the fermented liquid to be stored includes acetic acid bacteria and other ingredients of the raw materials necessary for each vinegar type (for example, apple ingredients for apple vinegar and rice ingredients for rice vinegar). Component). Therefore, the range (kind of vinegar that can be used) in which the stored fermentation broth can be used is extremely limited.
ここで、従来における他の菌保管方法として、次のような方法もある。即ち、発酵中の発酵液を採取後、希釈せずに遠心分離を行い、分離された沈殿物にグリセロールや糖化液などの菌凍結保存剤を添加する。そして、菌凍結保存剤が添加された菌沈殿物を凍結して、−80℃程度の極低温で保管する、という方法である。この方法のメリットは、長期間(例えば3ヶ月〜半年)の保存が可能なことである。 Here, as another conventional bacteria storage method, there is also the following method. That is, after collecting the fermentation broth during fermentation, it is centrifuged without dilution, and a microbe preservative such as glycerol or saccharified solution is added to the separated precipitate. And it is the method of freezing the microbe deposit to which the microbe preservative was added, and storing it at an extremely low temperature of about −80 ° C. The merit of this method is that it can be stored for a long time (for example, 3 months to 6 months).
しかしながら、極低温で保管する上記従来方法は、食酢の実生産工程に用いる種酢としての発酵液を保管するのには不向きである。なぜなら、実生産において発酵をすぐに立ち上げるだけの酢酸菌数を含む発酵液を−80℃で保管するためには、大掛かりな設備と多くのコストがかかってしまい、現実的ではないからである。また、菌凍結保存剤を添加した酢酸菌発酵液は、食酢の発酵工程の種酢として用いると、本来の食酢原料以外の原料が混入することとにもなり得るため、好ましくないからである。勿論、食酢製造工程から抜き出した糖化液を菌凍結保存剤として用いるような場合は問題ないが、少なくとも使用できる品種が限定されることになり、やはり好ましくない。 However, the above conventional method of storing at an extremely low temperature is unsuitable for storing a fermented liquid as a seed vinegar used in the actual production process of vinegar. This is because it takes a large amount of equipment and a lot of costs to store a fermentation broth containing the number of acetic acid bacteria that can quickly start fermentation in actual production at −80 ° C., which is not practical. . Moreover, it is because the acetic acid bacteria fermented liquid which added the microbe preservation | save agent is not preferable when using it as a seed vinegar of the vinegar fermentation process, since raw materials other than the original vinegar raw material may be mixed. Of course, there is no problem when the saccharified solution extracted from the vinegar production process is used as a microbe preservative, but at least the varieties that can be used are limited, which is also not preferable.
本発明は、上記の課題に鑑みてなされたものであり、その目的は、例えば半年〜1年程度の長期間の保管に耐え、ラグタイムが安定していることから正確なスケジュールで生産可能であり、かつあらゆる食酢製造に利用できる汎用性の高い酢酸菌の保管方法を提供することにある。 The present invention has been made in view of the above problems, and its purpose is to withstand long-term storage of, for example, about six months to one year, and because the lag time is stable, it can be produced on an accurate schedule. It is another object of the present invention to provide a highly versatile storage method for acetic acid bacteria that can be used for vinegar production.
上記の課題を解決すべく、本願発明者が鋭意検討を行ったところ、深部発酵中の酢酸発酵液から採取した発酵液をあらかじめ希釈してから遠心分離及び希釈を行うことで所定の酢酸濃度以下とし、これを凍結することで、格段に長期の保管が可能となることを新規に見出した。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検討を行い、下記の課題解決手段[1]〜[5]を完成させた。 In order to solve the above-mentioned problems, the inventors of the present application have made extensive studies, and by diluting the fermentation liquid collected from the acetic acid fermentation liquid during the deep fermentation in advance and then performing centrifugation and dilution, the concentration is below a predetermined acetic acid concentration. And it was newly found that it can be stored for a long time by freezing it. Then, the inventor of the present application has made further studies based on this new knowledge, and completed the following problem solving means [1] to [ 5 ].
[1]深部培養法にて酢酸発酵中の酢酸菌濃度が10 7 個/mL以上の発酵液を採取し、その酢酸菌発酵液よりも液温の低い希釈溶媒を添加することにより、酢酸濃度が0.5重量/容量%以上4重量/容量%以下となるように酢酸菌発酵液を低温化しつつ希釈する一次希釈工程と、前記一次希釈工程で低温化かつ希釈された酢酸菌発酵液を遠心分離しかつ希釈溶媒を添加することにより、酢酸濃度が0.001重量/容量%以上0.1重量/容量%以下かつ酢酸菌濃度が10 7 個/mL以上となるように希釈する遠心分離及び二次希釈工程と、前記遠心分離及び二次希釈工程を経て上記酢酸濃度かつ上記酢酸菌濃度となった酢酸菌を含有する酢酸菌含有液を凍結する凍結工程と、前記凍結工程を経て凍結された酢酸菌含有液を−5℃以下で保管する保管工程とを有し、前記酢酸発酵中の発酵液を採取してから前記酢酸菌含有液を凍結するまでの作業を72時間以内に行うことを特徴とする酢酸菌の保管方法。 [1] By collecting a fermentation broth having an acetic acid bacteria concentration of 10 7 cells / mL or more during acetic acid fermentation by a submerged culture method and adding a diluting solvent having a lower liquid temperature than that of the acetic acid bacteria fermentation solution , the acetic acid concentration A primary dilution step of diluting the acetic acid bacteria fermentation solution while reducing the temperature so that the concentration of the acetic acid bacteria fermentation solution is lower than 0.5 wt / vol% to 4 wt / vol%, and an acetic acid bacteria fermented solution reduced in temperature and diluted in the primary dilution step by adding centrifuged and diluted solvent, centrifugation acetate concentration is diluted to 0.001 wt / vol% 0.1 wt / vol% or less and acetic acid bacteria concentration of 10 7 cells / mL or more And the secondary dilution step, the freezing step of freezing the acetic acid bacteria-containing solution containing the acetic acid bacteria having the acetic acid concentration and the acetic acid bacteria concentration through the centrifugation and secondary dilution steps, and the freezing through the freezing step The acetic acid bacteria-containing solution is -5 ° C or less And a storing storage step, storage method of the acetic acid bacterium and performing work within 72 hours before freezing the acetic acid bacterium-containing liquid fermentation liquor after collection in the acetic acid fermentation.
[2]前記遠心分離及び二次希釈工程において、遠心分離の際に希釈溶媒を注ぎ入れることにより遠心分離と希釈とを同時に行うことを特徴とする上記手段1に記載の酢酸菌の保管方法。 [ 2 ] The method for storing acetic acid bacteria according to the above means 1 , wherein in the centrifugation and secondary dilution step, centrifugation and dilution are simultaneously performed by pouring a dilution solvent during centrifugation.
[3]前記凍結工程にて凍結される酢酸菌含有液には、菌凍結保存剤が添加されていないことを特徴とする上記手段1または2に記載の酢酸菌の保管方法。 [ 3 ] The method for storing acetic acid bacteria according to the above means 1 or 2 , wherein the bacteria cryopreservative is not added to the acetic acid bacteria-containing solution frozen in the freezing step.
[4]前記保管工程において、30日以上の期間保管することを特徴とする上記手段1乃至3のいずれか1項に記載の酢酸菌の保管方法。 [ 4 ] The method for storing acetic acid bacteria according to any one of the above means 1 to 3 , wherein in the storage step, the storage is performed for a period of 30 days or more.
[5]深部培養法にて酢酸発酵中の酢酸菌濃度が10 7 個/mL以上の発酵液を採取し、その酢酸菌発酵液よりも液温の低い希釈溶媒を添加することにより、酢酸濃度が0.5重量/容量%以上4重量/容量%以下となるように酢酸菌発酵液を低温化しつつ希釈する一次希釈工程と、前記一次希釈工程で低温化かつ希釈された酢酸菌発酵液を遠心分離しかつ希釈溶媒を添加することにより、酢酸濃度が0.001重量/容量%以上0.1重量/容量%以下かつ酢酸菌濃度が10 7 個/mL以上となるように希釈する遠心分離及び二次希釈工程と、前記遠心分離及び二次希釈工程を経て上記酢酸濃度かつ上記酢酸菌濃度となった酢酸菌を含有する酢酸菌含有液を凍結する凍結工程と、前記凍結工程を経て凍結された酢酸菌含有液を−5℃以下で保管する保管工程と、前記保管工程を経て保管された前記酢酸菌を種菌として用いて酢酸発酵を行う酢酸発酵工程とを有し、前記酢酸発酵中の発酵液を採取してから前記酢酸菌含有液を凍結するまでの作業を72時間以内に行うことを特徴とする食酢の製造方法。 [5] By collecting a fermentation broth having an acetic acid bacteria concentration of 10 7 cells / mL or more during acetic acid fermentation by a submerged culture method and adding a diluting solvent having a lower liquid temperature than that of the acetic acid bacteria fermentation solution, the acetic acid concentration A primary dilution step of diluting the acetic acid bacteria fermentation solution while reducing the temperature so that the concentration of the acetic acid bacteria fermentation solution is lower than 0.5 wt / vol% to 4 wt / vol%, and an acetic acid bacteria fermented solution reduced in temperature and diluted in the primary dilution step by adding centrifuged and diluted solvent, centrifugation acetate concentration is diluted to 0.001 wt / vol% 0.1 wt / vol% or less and acetic acid bacteria concentration of 10 7 cells / mL or more And the secondary dilution step, the freezing step of freezing the acetic acid bacteria-containing solution containing the acetic acid bacteria having the acetic acid concentration and the acetic acid bacteria concentration through the centrifugation and secondary dilution steps, and the freezing through the freezing step The acetic acid bacteria-containing solution is -5 ° C or less A storage step of storing, and an acetic acid fermentation step of performing acetic acid fermentation using the acetic acid bacteria stored through the storage step as an inoculum, and collecting the fermentation liquor during the acetic acid fermentation and then containing the acetic acid bacteria A method for producing vinegar, characterized in that the operation until the liquid is frozen is performed within 72 hours .
従って、請求項1〜4に記載の発明によると、例えば半年〜1年程度の長期間の保管に耐え、ラグタイムが安定していることから正確なスケジュールで生産可能であり、かつあらゆる食酢製造に利用できる汎用性の高い酢酸菌の保管方法を提供することができる。また、請求項5に記載の製造方法によれば、効率のよい酢酸発酵が可能となり、目的とする食酢を確実に製造することができる。 Therefore, according to the invention described in claims 1 to 4 , for example, it can withstand long-term storage of about six months to one year, and the lag time is stable, so that it can be produced on an accurate schedule, and any vinegar production A highly versatile storage method for acetic acid bacteria can be provided. Moreover, according to the manufacturing method of Claim 5 , efficient acetic acid fermentation is attained and the target vinegar can be manufactured reliably.
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. Specific examples of suitable 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).
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される(一次希釈)。 And the vinegar fermented liquor during fermentation obtained by said deep culture method is diluted as follows (primary dilution).
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。)のものを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。 As the vinegar fermented liquor, it is necessary to collect a fermented liquid (that is, acetic acid produced), and more preferably a period excluding an initial stage and an end stage of fermentation (referred to as a medium stage for convenience). It is good to do. 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106個/mL以上であることが好ましく、特には107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.
本発明における一次希釈は、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。また、発酵装置から分岐している食酢発酵液の配管と、希釈溶媒が供給される配管とが合流することにより、連続的に混合されるような形態であってもよい。 The primary dilution in the present invention is carried out by mixing the collected vinegar fermented vinegar and a diluting 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. Moreover, the form which is continuously mixed may be sufficient as the piping of the vinegar fermentation liquid branched from the fermenter and the piping to which the dilution solvent is supplied merge.
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い。水以外の成分を含んだ希釈溶媒を用いると、保管された菌を使用できる食酢の品種が限定されてしまう(例えば、純米酢は、米と水のみを原料として製造するため、他からアルコール分や糖分を混入できない)ため、特には水を使用することが望ましい。もちろん、純水だけに限らす若干のミネラル分等が含まれている水(水道水など)を用いてもよい。もちろん、遠心分離及び二次希釈工程において用いる希釈溶媒も上記と同様であり、水が好ましい。 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 scheduled to be used later as seed vinegar for vinegar fermentation, a liquid containing only components that are acceptable as vinegar components (for example, water, raw sugar solution, alcohol, etc.) is used. It is desirable. If a diluent solvent containing components other than water is used, the varieties of vinegar that can use the stored fungi are limited (for example, pure rice vinegar is produced using only rice and water as raw materials. In particular, it is desirable to use water. Of course, water (such as tap water) containing a slight amount of minerals that is limited to pure water may be used. Of course, the dilution solvent used in the centrifugation and secondary dilution steps is the same as described above, and water is preferable.
そして一次希釈工程においては、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4重量/容量%以下となるように希釈される。仮に、希釈を行わないか、または酢酸濃度を4重量/容量%を超える程度に希釈した場合には、遠心分離工程を経ることで酢酸菌にダメージを与えてしまう。 And in a primary dilution process, the vinegar fermented liquor during fermentation is diluted so that an acetic acid concentration may be 4 weight / volume% or less by addition of such a dilution solvent. If dilution is not performed or the concentration of acetic acid is diluted to an extent exceeding 4% by weight / volume, acetic acid bacteria are damaged through the centrifugation step.
この段階では、必要以上に希釈をすることは、以下の理由により好ましくない場合がある。即ち、初期の酢酸濃度や希釈する量などにもよるが、この段階で必要以上に希釈をすると、遠心分離にかける酢酸菌発酵液の量が多くなってしまうため、遠心分離工程に時間を要してしまう。その結果、酢酸発酵中の発酵液を採取してから酢酸菌含有液を凍結するまでの時間が必要以上にかかってしまい、菌にダメージを与えやすくなるため好ましくない。よって、一次希釈工程においては酢酸濃度が0.5重量/容量%以上となるように留めておく方が好ましい。 At this stage, diluting more than necessary may not be preferable for the following reasons. That is, depending on the initial concentration of acetic acid and the amount to be diluted, if it is diluted more than necessary at this stage, the amount of acetic acid fermentation broth to be centrifuged increases, so the centrifugation step takes time. Resulting in. As a result, it is not preferable because it takes more time than necessary from collecting the fermentation broth during acetic acid fermentation until the acetic acid bacteria-containing liquid is frozen, and easily damages the bacteria. Therefore, it is preferable to keep the acetic acid concentration at 0.5 wt / vol% or more in the primary dilution step.
一次希釈工程では、液温を下げることは必須ではないが、低温とする方が菌へのダメージを抑えやすく好ましい。好ましくは20℃以下、更に好ましくは10℃以下、とすれば十分である。希釈時の温度は低い方が好ましい。なお、液温を下げるための手法としては、例えば冷却装置を用いながら一次希釈を行ってもよいほか、冷却装置を用いず希釈溶媒として冷水や氷水を使用して一次希釈を行ってもよい。 In the primary dilution step, it is not essential to lower the liquid temperature, but a lower temperature is preferable because it is easy to suppress damage to bacteria. It is sufficient that the temperature is preferably 20 ° C. or lower, more preferably 10 ° C. or lower. The temperature at the time of dilution is preferably lower. As a method for lowering the liquid temperature, for example, primary dilution may be performed using a cooling device, or primary dilution may be performed using cold water or ice water as a dilution solvent without using a cooling device.
一次希釈工程で希釈された酢酸菌発酵液は、遠心分離機によって遠心分離を行う。使用する遠心分離機は、連続式でも回分式でも構わない。連続式の遠心分離機とは、連続的に分離用液を供給しながら、上清と沈降物とを分離していく形式であって、例えば斉藤遠心機工業製の遠心分離機(ADS-1001CS)などが利用できる。また、回分式の遠心分離機とは、分離液の供給、遠心分離の操作が分かれているものであって、例えば久保田商事株式会社のKUBOTA3700などが利用できる。処理量が多い場合には、沈降物を短時間で採取できる連続式が適している。処理量が少ない場合には、処理条件の微調整がいらない回分式が簡易であり適している。 The acetic acid bacteria fermentation liquor diluted in the primary dilution step is centrifuged by a centrifuge. The centrifuge used may be a continuous type or a batch type. A continuous centrifuge is a type that separates supernatant and sediment while continuously supplying a separation solution. For example, a centrifuge manufactured by Saito Centrifuge (ADS-1001CS) ) Etc. are available. In addition, the batch-type centrifuge is one in which the supply of the separation liquid and the operation of centrifugation are separated, and for example, KUBOTA 3700 from Kubota Corporation can be used. When the amount of treatment is large, a continuous type capable of collecting sediment in a short time is suitable. When the amount of processing is small, a batch system that does not require fine adjustment of processing conditions is simple and suitable.
本発明では凍結前に酢酸濃度を0.1重量/容量%以下となるように希釈する必要があるが(二次希釈)、その方法としては例えば以下のようなものが採用できる。 In the present invention, it is necessary to dilute the acetic acid concentration to 0.1 wt / vol% or less before freezing (secondary dilution). As the method, for example, the following can be employed.
一次希釈された酢酸菌発酵液を連続式の遠心分離機に流入させながら遠心分離を行い、前記酢酸菌発酵液を全て流入させた後、続いて希釈溶媒を連続的に遠心分離機に流入させて所定時間遠心分離を行うことによって主に上清部分を希釈して、その結果遠心分離機内の酢酸濃度を下げる。そして、最終的に遠心分離機に蓄積された沈殿層を取り出し、凍結前の酢酸菌含有液とする。 Centrifugation while allowing the primary diluted acetic acid fermentation broth to flow into a continuous centrifuge, after all the acetic acid fermentation broth has flowed in, the diluted solvent is then allowed to flow continuously into the centrifuge. The supernatant portion is mainly diluted by centrifuging for a predetermined time, and as a result, the acetic acid concentration in the centrifuge is lowered. And finally, the sediment layer accumulated in the centrifuge is taken out and used as a solution containing acetic acid bacteria before freezing.
あるいは、一次希釈された酢酸菌発酵液を回分式の遠心分離機に流入させて所定時間遠心分離を行い、沈殿物だけを採取して希釈溶媒と混合する。その後さらに回分式の遠心分離機に流入させて遠心分離を行い、最終的に遠心分離機に蓄積された沈殿層を取り出し、凍結前の酢酸菌含有液とする。 Alternatively, the primary diluted acetic acid bacteria fermentation broth is allowed to flow into a batch centrifuge and centrifuged for a predetermined time, and only the precipitate is collected and mixed with the diluting solvent. Thereafter, the mixture is further introduced into a batch-type centrifuge and centrifuged, and finally the sediment layer accumulated in the centrifuge is taken out to obtain a solution containing acetic acid bacteria before freezing.
連続式の遠心分離機を用いた場合、作業性が向上するため好ましい。それだけでなく、一次希釈工程から遠心分離までの時間が短くて済むようになり、結果として酢酸存在下での酢酸菌へのダメージを与え難くなる(活性のある菌数が多くなる)ため、好ましい。 Use of a continuous centrifuge is preferable because workability is improved. In addition, the time from the primary dilution step to centrifugation can be shortened, and as a result, it is difficult to damage acetic acid bacteria in the presence of acetic acid (the number of active bacteria increases), which is preferable. .
なお、遠心分離機の容量、回転数、動力は、遠心分離の処理をしたい量などに合わせて適宜選択すればよい。 Note that the capacity, rotation speed, and power of the centrifuge may be appropriately selected according to the amount to be centrifuged.
遠心分離及び二次希釈工程においては、酢酸菌含有液の酢酸濃度が0.1重量/容量%以下となるまで希釈される。仮に、酢酸濃度が0.1重量/容量%を超える程度にしか希釈をしなかった場合、凍結保存中に酢酸菌がダメージを受けてしまい、活性のある酢酸菌数が減少してしまう。この結果、所定期間(例えば半年)保管した後に食酢発酵の種菌として用いた場合に、発酵立ち上がりまでのラグタイムが長く(例えば96時間以上)かかってしまい、好ましくない。 In the centrifugation and secondary dilution steps, the acetic acid bacteria-containing liquid is diluted until the acetic acid concentration is 0.1 wt / vol% or less. If the acetic acid concentration is diluted only to the extent that it exceeds 0.1% by weight / volume, the acetic acid bacteria are damaged during cryopreservation, and the number of active acetic acid bacteria decreases. As a result, when used as an inoculum for vinegar fermentation after storage for a predetermined period (for example, half a year), the lag time until the start of fermentation takes a long time (for example, 96 hours or more), which is not preferable.
この段階では、必要以上に希釈をすることは、以下の理由により好ましくない場合がある。即ち、遠心分離及び二次希釈を行う酢酸菌発酵液の量などにもよるが、この段階で必要以上に希釈をしようとすると、遠心分離にかける量が多くなってしまい、その結果凍結までの時間が長くかかってしまうことになる。あるいは、時間をかけないために遠心分離を十分に行わなければ、凍結保存する酢酸菌含有液の量が多くなってしまうため、保管設備費用や維持費用などが多くかかってしまい好ましくない。よって、遠心分離及び二次希釈工程においては酢酸濃度が0.001重量/容量%以上となるように留めておく方が好ましい。 At this stage, diluting more than necessary may not be preferable for the following reasons. In other words, depending on the amount of the fermentation solution of acetic acid bacteria that undergoes centrifugation and secondary dilution, if you try to dilute more than necessary at this stage, the amount of centrifugation will increase, resulting in the amount of time until freezing. It will take a long time. Alternatively, if sufficient centrifugation is not performed so as not to spend time, the amount of the acetic acid bacteria-containing solution to be cryopreserved increases, which increases the storage facility costs and maintenance costs, which is not preferable. Therefore, it is preferable to keep the acetic acid concentration at 0.001 wt / vol% or more in the centrifugation and secondary dilution steps.
遠心分離及び二次希釈工程を経た段階(凍結直前)の酢酸菌含有液中には、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107個/mL以上、特には108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 the acetic acid bacterium-containing liquid at the stage after the centrifugation and secondary dilution process (immediately before freezing) contains as many acetic acid bacteria as possible, specifically 10 7 / mL or more, in particular It is preferable to contain 10 8 pieces / 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.
本発明において酢酸菌含有液を凍結する方法としては、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、酢酸菌含有液を凍結保管用のネジ式キャップチューブに入れ、それを−20〜80℃の冷凍庫に静置する方法などがある。 In the present invention, any conventionally known method can be employed as a method for freezing the acetic acid bacteria-containing solution. When the suitable example is given, there exists a method etc. which put an acetic acid bacteria containing liquid in the screw-type cap tube for frozen storage, and leave it still in a freezer of -20-80 degreeC.
ここで、凍結を行うときのスピードは特に限定されないが、酢酸発酵中の発酵液を採取してから酢酸菌含有液を凍結するまでの作業時間をできるだけ短く(72時間以内)することが必要であるため、できるだけ急速に凍結することが好ましい。当該作業時間を72時間以内とするのは、菌体の活性をできるだけ維持した状態で凍結休眠状態に移行させるためである。好ましくは48時間以内であり、さらに好ましくは24時間以内であり、短いほどよい。 Here, the speed when freezing is not particularly limited, but it is necessary to shorten the working time from collecting the fermentation broth during acetic acid fermentation to freezing the liquid containing acetic acid bacteria as much as possible (within 72 hours). Because of this, it is preferable to freeze as quickly as possible. The reason for setting the working time within 72 hours is to shift to a frozen and dormant state while maintaining the activity of the cells as much as possible. The time is preferably within 48 hours, more preferably within 24 hours, and the shorter the better.
酢酸菌含有液は、酢酸菌の休眠状態を維持するため、凍結後に−5℃以下で保管される。この場合、さらに低温で保管した方が保管中の酢酸菌の活性を完全に抑えることができ、種菌として使用する際の活性のある酢酸菌数が多い状態で保管することができる。好ましくは−20℃以下、より好ましくは−30℃以下で保管することがよい。ただし、これ以上低温で保管しても、保管後の活性のある酢酸菌数は大きく変化せず、種菌として使用する際のラグタイムも変化しない。よって、設備コストや電力コストを考慮すると、−20〜−30℃が好ましい。 The acetic acid bacteria-containing liquid is stored at −5 ° C. or lower after freezing in order to maintain the dormant state of the acetic acid bacteria. In this case, the storage at a lower temperature can completely suppress the activity of the acetic acid bacteria being stored, and can be stored in a state where the number of active acetic acid bacteria is large when used as a seed fungus. It is preferable to store at −20 ° C. or lower, more preferably −30 ° C. or lower. However, even if stored at a lower temperature than this, the number of active acetic acid bacteria after storage does not change significantly, and the lag time when used as an inoculum does not change. Therefore, considering the equipment cost and the power cost, -20 to -30 ° C is preferable.
通常、研究所等において菌体を凍結保存するような場合には、グリセロールや糖化液などの菌凍結保存剤を15〜50%程度添加する。しかしながら、本発明の方法を用いれば、そのような菌凍結保存剤を使用しなくても、酢酸菌の活性が高い状態で長期保存を達成することが可能となる。保管する酢酸菌にグリセロールや糖化液を添加してしまうと、食酢の品種によっては、食酢の原料以外の成分が混入することになる。つまり、種菌として活用できる食酢の品種を限定してしまうこととなる。 Usually, in the case where microbial cells are cryopreserved in a laboratory or the like, about 15 to 50% of a microbe preservative such as glycerol or a saccharified solution is added. However, if the method of the present invention is used, long-term storage can be achieved in a state where the activity of acetic acid bacteria is high, without using such a microbe preservative. If glycerol or a saccharified solution is added to acetic acid bacteria to be stored, components other than the vinegar raw material may be mixed depending on the varieties of vinegar. That is, the varieties of vinegar that can be used as inoculum are limited.
菌凍結保存剤の例としては、グリセロールや糖化液の他に、例えばDMSOやスキムミルクなどがある。 Examples of the microbe preservative include DMSO and skim milk, in addition to glycerol and saccharified solution.
そして、上述のように希釈及び冷却された食酢発酵液は、凍結した状態で長期間保管される。短期保管(例えば29日以内)の場合には、本発明の方法を適用しなくとも特許文献2の方法などが利用可能である。ゆえに、本発明の方法は、30日間以上、特には半年〜1年以上保管する場合に好適である。例えば本発明の保管方法によれば、年間数回しか生産されない小ロット品に対し、その食酢の品種に最適な能力を持った酢酸菌を保管することができる。 And the vinegar fermented liquid diluted and cooled as mentioned above is stored for a long time in the frozen state. In the case of short-term storage (for example, within 29 days), the method of Patent Document 2 can be used without applying the method of the present invention. Therefore, the method of the present invention is suitable for storing for 30 days or more, particularly for half a year to one year or more. For example, according to the storage method of the present invention, acetic acid bacteria having the optimum ability for the vinegar variety can be stored for small lot products that are produced only several times a year.
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、好適な菌体活性を維持する。従って、これを別の酢酸発酵を行う際に種酢として使用して酢酸発酵を行えば、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菌凍結保存剤やその他の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 maintains a suitable fungal activity even if stored for a long time. Therefore, if acetic acid fermentation is performed using this as another 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. Moreover, according to the present invention, since the stored vinegar fermented liquid does not contain any fungicide cryopreservatives or other additives, the flavor, quality of vinegar, even if this is used as seed vinegar, It does not lead to a decrease in purity or the like.
以下に本発明をより具体化した実施例を記載するが、本発明は実施例に限定されるものではない。 Examples that further embody the present invention will be described below, but the present invention is not limited to the examples.
[実施例1]保管用酢酸菌の作製(試験例1)
(1)本発明の方法による保管用酢酸菌の作製
[Example 1] Preparation of acetic acid bacteria for storage (Test Example 1)
(1) Preparation of acetic acid bacteria for storage by the method of the present invention
(a)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1Lの食酢発酵液を用意した。この食酢発酵液は米を原材料とする仕込液とアセトバクター・アセチを用いて培養されたものであって、酢酸濃度が8.0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107個/mLとなっている。 (A) 1 L of vinegar fermented liquor was prepared in advance using a fermentation tank capable of deep fermentation (5 L capacity: manufactured by Mitsuwa Richemical Co., Ltd.). This vinegar fermented broth was cultivated using Acetobacter aceti prepared from a feed solution made from rice, and the acetic acid concentration was 8.0 wt / vol%, the alcohol concentration was 0.3 vol / vol%, The liquid temperature is about 30 ° C. to 35 ° C., and the acetic acid bacteria concentration is about 10 7 cells / mL.
(b)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160mL採取して、これを、希釈溶媒である15℃の水20mLをあらかじめ入れておいた8本の50mL遠心分離用チューブ(耐酸性を有する保管容器)に20mLずつ速やかに添加し、両液を混合し40mLとした。希釈後の酢酸濃度は4.0重量/容量%であった。 (B) 160 mL of such a vinegar fermented liquid is collected at the middle stage of fermentation, that is, at a stage where the activity of the fungus body is high and fermentation is actively taking place, and 20 mL of 15 ° C. water as a dilution solvent is preliminarily added thereto. 20 mL each was quickly added to the eight 50 mL centrifuge tubes (acid-resistant storage containers), and both solutions were mixed to make 40 mL. The acetic acid concentration after dilution was 4.0% w / v.
(c)次に、希釈された食酢発酵液を回分式遠心分離機(KUBOTA3700 久保田商事株式会社製)で、8000rpmで遠心分離を5分間行った。遠心分離後、上清を全て廃棄し、27℃の水を40mL加えて沈澱を懸濁し、再度8000rpmで遠心分離を5分間行った。遠心分離後、上清をすべて廃棄し、27℃の水1mLで沈澱を懸濁した。懸濁後の酢酸濃度は0.1重量/容量%であった。 (C) Next, the diluted vinegar fermented liquid was centrifuged at 8000 rpm for 5 minutes with a batch centrifuge (KUBOTA 3700, manufactured by Kubota Corporation). After centrifugation, all the supernatant was discarded, 40 mL of 27 ° C. water was added to suspend the precipitate, and centrifugation was again performed at 8000 rpm for 5 minutes. After centrifugation, all the supernatant was discarded, and the precipitate was suspended in 1 mL of water at 27 ° C. The acetic acid concentration after suspension was 0.1% by weight / volume.
(d)懸濁した沈澱液は密閉性の高い1.5mL容量ポリプロピレン容器に入れ、冷凍庫に保管し2時間のうちに−30℃に冷却した。このようにして保管菌サンプル1を作製した。なお、酢酸発酵中の発酵液を採取してから酢酸菌含有液を凍結するまでの作業時間は3時間であった。
さらに、基本的には上記方法と同じであるが、酢酸発酵中の発酵液を採取してから酢酸菌含有液を凍結するまでの作業時間を24時間としたものを作製し、保管菌サンプル5とした。また、基本的には上記方法と同じであるが、酢酸発酵中の発酵液を採取してから酢酸菌含有液を凍結するまでの作業時間を72時間としたものを作製し、保管菌サンプル6とした。
(D) The suspended precipitation liquid was put into a 1.5 mL capacity polypropylene container having high airtightness, stored in a freezer, and cooled to −30 ° C. within 2 hours. In this way, the stored bacteria sample 1 was produced. The working time from collecting the fermentation broth during acetic acid fermentation to freezing the acetic acid bacteria-containing solution was 3 hours.
Furthermore, although it is basically the same as the above method, a sample in which the working time from collecting the fermentation broth during acetic acid fermentation to freezing the acetic acid bacteria-containing solution is 24 hours is prepared, and the stored bacteria sample 5 It was. Moreover, although it is the same as the said method fundamentally, what made the working time from collecting the fermented liquor during acetic acid fermentation until freezing the acetic acid bacteria containing liquid was produced, and the storage microbe sample 6 It was.
(2)希釈をせずに遠心分離と凍結とをした保管用酢酸菌の作製 (2) Preparation of acetic acid bacteria for storage that was centrifuged and frozen without dilution
(a)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1Lの食酢発酵液を用意した。この食酢発酵液は米を原材料とする仕込液とアセトバクター・アセチを用いて培養されたものであって、酢酸濃度が8.0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107個/mLとなっている。 (A) 1 L of vinegar fermented liquor was prepared in advance using a fermentation tank capable of deep fermentation (5 L capacity: manufactured by Mitsuwa Richemical Co., Ltd.). This vinegar fermented broth was cultivated using Acetobacter aceti prepared from a feed solution made from rice, and the acetic acid concentration was 8.0 wt / vol%, the alcohol concentration was 0.3 vol / vol%, The liquid temperature is about 30 ° C. to 35 ° C., and the acetic acid bacteria concentration is about 10 7 cells / mL.
(b)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320mL採取して、一次希釈を行うことなく8本の50mL遠心分離用チューブ(耐酸性を有する保管容器)に速やかに40mLずつ投入した。 (B) 320 mL of such a vinegar fermented broth is collected at the middle stage of fermentation, that is, at a stage where the activity of the fungus body is high and fermentation is actively occurring, and eight 50 mL centrifuge tubes are used without performing primary dilution. Immediately 40 mL was put into (acid-resistant storage container).
(c)次に、投入した食酢発酵液を回分式遠心分離機(KUBOTA3700 久保田商事株式会社製)で、8000rpmで遠心分離を5分間行った。遠心分離後、上清を全て廃棄した。沈澱液の酢酸濃度は8.0重量/容量%であった。 (C) Next, the charged vinegar fermented liquid was centrifuged at 8000 rpm for 5 minutes with a batch centrifuge (KUBOTA 3700, manufactured by Kubota Corporation). After centrifugation, all the supernatant was discarded. The acetic acid concentration of the precipitation liquid was 8.0% w / v.
(d)そして、二次希釈を行うことなく、沈澱を回収した容器をそのまま冷凍庫に保管し、2時間のうちに−30℃に冷却した。このようにして保管菌サンプル2を作製した。なお、酢酸発酵中の発酵液を採取してから酢酸菌含有液を凍結するまでの作業時間は3時間であった。 (D) And the container which collect | recovered precipitation was stored in a freezer as it was, without performing secondary dilution, and it cooled to -30 degreeC within 2 hours. In this way, the stored bacteria sample 2 was prepared. The working time from collecting the fermentation broth during acetic acid fermentation to freezing the acetic acid bacteria-containing solution was 3 hours.
(3)一次希釈をせずに遠心分離をかけ、その後は本発明の方法のようにした保管用酢酸菌の作製 (3) Centrifugation without primary dilution, and then storage acetic acid bacteria for storage as in the method of the present invention
(a)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1Lの食酢発酵液を用意した。この食酢発酵液は米を原材料とする仕込液とアセトバクター・アセチを用いて培養されたものであって、酢酸濃度が8.0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107個/mLとなっている。 (A) 1 L of vinegar fermented liquor was prepared in advance using a fermentation tank capable of deep fermentation (5 L capacity: manufactured by Mitsuwa Richemical Co., Ltd.). This vinegar fermented broth was cultivated using Acetobacter aceti prepared from a feed solution made from rice, and the acetic acid concentration was 8.0 wt / vol%, the alcohol concentration was 0.3 vol / vol%, The liquid temperature is about 30 ° C. to 35 ° C., and the acetic acid bacteria concentration is about 10 7 cells / mL.
(b)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320mL採取して、これを8本の50mL遠心分離用チューブ(耐酸性を有する保管容器)に速やかに40mLずつ投入した。 (B) 320 mL of such vinegar fermented liquor is collected at the middle stage of fermentation, that is, at the stage where the activity of the bacterial cells is high and the fermentation is actively occurring, and this is collected into eight 50 mL centrifuge tubes (acid resistance is reduced). 40 mL each was quickly charged into the storage container).
(c)次に、この食酢発酵液を回分式遠心分離機(KUBOTA3700 久保田商事株式会社製)で、8000rpmで遠心分離を5分間行った。遠心分離後、上清を全て廃棄し、27℃の水を40mL加えて沈澱を懸濁し、再度8000rpm程度で遠心分離を5分間行った。遠心分離後、上清をすべて廃棄し、27℃の水1mLで沈澱を懸濁した。沈澱液の酢酸濃度は0.1重量/容量%であった。 (C) Next, this vinegar fermented liquid was centrifuged at 8000 rpm for 5 minutes with a batch centrifuge (KUBOTA 3700, manufactured by Kubota Corporation). After centrifugation, all the supernatant was discarded, 40 mL of 27 ° C. water was added to suspend the precipitate, and centrifugation was again performed at about 8000 rpm for 5 minutes. After centrifugation, all the supernatant was discarded, and the precipitate was suspended in 1 mL of water at 27 ° C. The acetic acid concentration of the precipitation solution was 0.1% w / v.
(d)懸濁した沈澱液は、密閉性の高い1.5mL容量ポリプロピレン容器に入れて冷凍庫に保管し、2時間のうちに−30℃に冷却した。このようにして保管菌サンプル3を作製した。なお、酢酸発酵中の発酵液を採取してから酢酸菌含有液を凍結するまでの作業時間は3時間であった。 (D) The suspended precipitation liquid was put into a 1.5 mL capacity polypropylene container having high airtightness, stored in a freezer, and cooled to −30 ° C. within 2 hours. In this way, the stored bacteria sample 3 was prepared. The working time from collecting the fermentation broth during acetic acid fermentation to freezing the acetic acid bacteria-containing solution was 3 hours.
(4)一次希釈の後、遠心分離及び二次希釈工程を行うが0.2%までしか希釈をしない保管用酢酸菌の作製 (4) Preparation of acetic acid bacteria for storage that undergoes centrifugation and secondary dilution steps after primary dilution but dilutes only to 0.2%
(a)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1Lの食酢発酵液を用意した。この食酢発酵液は米を原材料とする仕込液とアセトバクター・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107個/mLとなっている。 (A) 1 L of vinegar fermented liquor was prepared in advance using a fermentation tank capable of deep fermentation (5 L capacity: manufactured by Mitsuwa Richemical Co., Ltd.). This vinegar fermented broth was cultivated using a feed solution made from rice and Acetobacter aceti, with an acetic acid concentration of 7.0 wt / vol%, an alcohol concentration of 0.3 vol / vol%, The liquid temperature is about 30 ° C. to 35 ° C., and the acetic acid bacteria concentration is about 10 7 cells / mL.
(b)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160mL採取して、これを、希釈溶媒である15℃の水をあらかじめ入れておいた8本の50mL遠心分離用チューブ(耐酸性を有する保管容器)に速やかに20mLずつ添加し、両液を混合し40mLとした。希釈後の酢酸濃度は4.0重量/容量%であった。 (B) 160 mL of such vinegar fermented broth is collected at the middle stage of fermentation, that is, at the stage where the activity of the bacterial cells is high and the fermentation is actively occurring, and this is preliminarily charged with 15 ° C. water as a diluent solvent. 20 mL each was quickly added to the eight 50 mL centrifuge tubes (acid-resistant storage container), and both solutions were mixed to make 40 mL. The acetic acid concentration after dilution was 4.0% w / v.
(c)次に、この食酢発酵液を回分式遠心分離機(KUBOTA3700 久保田商事株式会社製)で、8000rpmで遠心分離を5分間行った。遠心分離後、上清を1mL残して廃棄し、27℃の水16.5mLで沈澱を懸濁した。懸濁後の酢酸濃度は0.2重量/容量%であった。 (C) Next, this vinegar fermented liquid was centrifuged at 8000 rpm for 5 minutes with a batch centrifuge (KUBOTA 3700, manufactured by Kubota Corporation). After centrifugation, 1 mL of the supernatant was left and discarded, and the precipitate was suspended in 16.5 mL of 27 ° C. water. The acetic acid concentration after suspension was 0.2% w / v.
(d)懸濁した沈澱液は密閉性の高い1.5mL容量ポリプロピレン容器に入れ、冷凍庫に保管し2時間のうちに−30℃に冷却した。このようにして保管菌サンプル4を作製した。なお、酢酸発酵中の発酵液を採取してから酢酸菌含有液を凍結するまでの作業時間は3時間であった。 (D) The suspended precipitation liquid was put into a 1.5 mL capacity polypropylene container having high airtightness, stored in a freezer, and cooled to −30 ° C. within 2 hours. In this way, the stored bacteria sample 4 was produced. The working time from collecting the fermentation broth during acetic acid fermentation to freezing the acetic acid bacteria-containing solution was 3 hours.
[実施例2]保管した酢酸菌を用いての発酵試験(試験例2)
試験例1で作製した保管菌サンプル1〜6を半年保管したものを食酢発酵に用いて比較した。米を原材料とする仕込み液をあらかじめ3L入れておいた深部発酵用の発酵タンク(5L容量:ミツワ理化学工業社製)内に各々の保管菌サンプルを投入した。なお、投入した保管菌サンプルの量は、それぞれの保管菌サンプルを作製する段階において、同量の発酵液(発酵液量で15mL)から作製された保管菌サンプル量として初発の菌数を統一した。
[Example 2] Fermentation test using stored acetic acid bacteria (Test Example 2)
What stored the storage microbe samples 1-6 produced in Test Example 1 for half a year was used for vinegar fermentation and compared. Each stored bacteria sample was put into a fermentation tank for deep fermentation (5 L capacity: manufactured by Mitsuwa Riken Co., Ltd.) in which 3 L of a feed solution made from rice was put in advance. In addition, the amount of the stored bacteria sample input was unified with the initial number of bacteria as the amount of the stored bacteria sample prepared from the same amount of fermentation broth (15 mL of fermentation liquid) at the stage of preparing each stored bacteria sample. .
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発酵を所定時間継続的に行い、玄米酢を製造した。仕込み液には、酒、種酢(菌体除去したもの)を混合したものを用いた。 Thereafter, the submerged fermentation of acetic acid bacteria was continuously performed for a predetermined time in accordance with a conventional method while aeration stirring was performed to produce brown rice vinegar. As the preparation liquid, a mixture of sake and seed vinegar (those from which the cells were removed) was used.
ここで、培養を開始してから酢酸濃度が0.1%上昇し始めるまでの時間(つまり、発酵開始までのラグタイム)を保管菌サンプル1〜6についてそれぞれ計測した。これらの結果を表1に示す。 Here, the time until the acetic acid concentration starts to rise by 0.1% after starting the culture (that is, the lag time until the start of fermentation) was measured for each of the stored bacteria samples 1-6. These results are shown in Table 1.
(試験結果)
表1によると、保管菌サンプル2〜4では、発酵開始までのラグタイムが72時間以上となってしまうことがわかった。ここで、実用上好ましいラグタイムの程度が72時間以内、好ましくは48時間以内であると定義した場合、保管菌サンプル2〜4の方法では、長期にわたる保管ができないことが明らかとなった。
(Test results)
According to Table 1, it was found that in the stored bacteria samples 2 to 4, the lag time until the start of fermentation was 72 hours or more. Here, when it was defined that the practically preferred lag time was within 72 hours, preferably within 48 hours, it became clear that the method of the stored bacteria samples 2 to 4 could not be stored for a long time.
これに対し、保管菌サンプル1,5,6については発酵開始までのラグタイム40時間程度であることから、明らかに上記の好適範囲内であり、48時間以内に収まっていた。従って、保管菌サンプル1,5,6の手順を踏めば、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になった。なお、保管菌サンプル1,5,6について、さらに酢酸濃度が1.5%上昇し始めるまでの時間を調査したところ、保管菌サンプル1,5では殆ど差がなかったが、保管菌サンプル6では時間が長くなる傾向が見られた。 On the other hand, the stored bacteria samples 1, 5, and 6 have a lag time of about 40 hours until the start of fermentation, and thus clearly fall within the above-mentioned preferred range and were within 48 hours. Therefore, it has been clarified that if the procedure of the stored bacteria samples 1, 5, 6 is followed, the storage is possible for a considerably long period. In addition, when the time until the acetic acid concentration started to increase by 1.5% was further investigated for the stored bacteria samples 1, 5 and 6, there was almost no difference in the stored bacteria samples 1 and 5, but in the stored bacteria sample 6 There was a tendency to increase the time.
[実施例3]本発明の保管方法により得た保管菌の多品種食酢への応用実験
試験例1の保管菌サンプル1を、米、玄米、ブドウ、リンゴ、をそれぞれ原料とする仕込み液3Lをあらかじめ入れておいた深部発酵用の発酵タンク(5L容量:ミツワ理化学工業社製)内に投入し、通気攪拌を行いながら、常法に従って酢酸菌の深部発酵を所定時間継続的に行い、米酢、黒酢、ブドウ酢、リンゴ酢を製造した。仕込み液には、米酢は米で作った酒と米酢の種酢(菌体除去したもの)とを混合したもの、黒酢は玄米で作った酒と黒酢の種酢(菌体除去したもの)とを混合したもの、ブドウ酢はブドウで作った酒とブドウ酢の種酢(菌体除去したもの)とを混合したもの、リンゴ酢はリンゴで作った酒とリンゴ酢の種酢(菌体除去したもの)とを混合したもの、を用いた。なお、投入した保管菌サンプルの量は、それぞれの保管菌サンプルを作製する段階において、同量の発酵液(発酵液量で15mL)から作製された保管菌サンプル量として初発の菌数を統一した。
[Example 3] Application experiment of stored bacteria obtained by the storage method of the present invention to multi-variety vinegar vinegar Sample 1 of storage bacteria of Test Example 1 was prepared using 3 L of feed liquid made from rice, brown rice, grapes and apples, respectively. It is put in a fermentation tank for deep fermentation (5 L capacity: manufactured by Mitsuwa Riken Kogyo Co., Ltd.) that has been put in advance, and the submerged fermentation of acetic acid bacteria is continuously carried out for a predetermined time according to a conventional method while stirring with aeration. , Black vinegar, grape vinegar, and apple cider vinegar. In the preparation liquid, rice vinegar is a mixture of sake made from rice and rice vinegar seed vinegar (those from which the cells have been removed), black vinegar is made from brown rice and black vinegar seed vinegar (from which the cells are removed) , Grape vinegar is a mixture of sake made from grapes and grape vinegar seed vinegar (with the cells removed), apple cider vinegar is made from apple and apple vinegar seed vinegar What mixed (thing which removed the microbial cell) was used. In addition, the amount of the stored bacteria sample input was unified with the initial number of bacteria as the amount of the stored bacteria sample prepared from the same amount of fermentation broth (15 mL of fermentation liquid) at the stage of preparing each stored bacteria sample. .
それぞれ保管菌サンプル投入から発酵開始までのラグタイムは、米酢は60時間、黒酢は40時間、ブドウ酢は60時間、リンゴ酢は40時間であり、全て72時間以内となり、実生産で使用するにあたって良好な結果となった。また、余分な成分の有無を分析したところ、保管菌サンプル1を作製した食酢発酵液(玄米酢)由来の成分(アミノ酸、有機酸、糖など)は1/100000(10万分の1)以下の濃度であり、玄米としては0.0645ppm以下の含有量ということになり、本発明による保管菌を異品種の食酢製造に用いても問題がないレベルであることがわかった。 The lag time from the storage of the stored bacteria sample to the start of fermentation is 60 hours for rice vinegar, 40 hours for black vinegar, 60 hours for grape vinegar and 40 hours for apple vinegar, all within 72 hours. It was a good result. Moreover, when the presence or absence of an excess component was analyzed, the components (amino acid, organic acid, sugar, etc.) derived from the vinegar fermented liquid (brown rice vinegar) which produced the storage microbe sample 1 were 1/100000 (1 / 100,000) or less. It is a concentration, and the content of brown rice is 0.0645 ppm or less, and it has been found that there is no problem even if the storage bacteria according to the present invention is used for producing varieties of vinegar.
[実施例4]保管用酢酸菌の作製(遠心分離処理量大量)
(1)試験例1よりも大量の発酵液を遠心分離処理して保管菌を作製した。手順を以下に記載する。
[Example 4] Preparation of acetic acid bacteria for storage (a large amount of centrifugal separation treatment)
(1) A larger amount of fermentation broth than in Test Example 1 was subjected to a centrifugal separation treatment to produce stored bacteria. The procedure is described below.
(a)工場の大型発酵タンク5kLで深部発酵している食酢発酵液を用意した。この食酢発酵液は米を原材料とする仕込液とアセトバクター・アセチを用いて培養されたものであって、酢酸濃度が8.0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107個/mLとなっている。 (A) A vinegar fermented liquid deeply fermented in a large-scale fermentation tank of 5 kL was prepared. This vinegar fermented broth was cultivated using Acetobacter aceti prepared from a feed solution made from rice, and the acetic acid concentration was 8.0 wt / vol%, the alcohol concentration was 0.3 vol / vol%, The liquid temperature is about 30 ° C. to 35 ° C., and the acetic acid bacteria concentration is about 10 7 cells / mL.
(b)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20L採取して、これを、希釈溶媒である15℃の水をあらかじめ180L入れておいたSUS製タンク(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。混合液の酢酸濃度は0.8重量/容量%であった。 (B) 20 L of such vinegar fermented liquor is collected at the middle stage of fermentation, that is, at the stage where the activity of the fungus body is high and the fermentation is actively occurring, and 180 L of water at 15 ° C. as a dilution solvent is collected in advance. The mixture was quickly added to the SUS tank (acid-resistant storage container), and both solutions were mixed. The acetic acid concentration of the mixed solution was 0.8% by weight / volume.
(c)次に、希釈された食酢発酵液をタンクから連続式遠心分離機(ADS-1001CS 斉藤遠心機工業製)へ200L/hで送液し、8000rpmで遠心分離を行った。この時、上清は自動的に遠心機の外へ排出され、沈澱は遠心機内に溜まっていく。希釈された食酢発酵液を全て遠心分離後、15℃の水100Lを続けて同遠心機へ200L/hで送液し、遠心機内の液体酢酸濃度を低下させた。水100Lを全て遠心機へ投入した後、遠心機内に溜まっていた沈澱液を一気に排出し、回収した。回収液は約3Lであり、酢酸濃度は0.1重量/容量%であった。この沈澱液は500mL容量ポリプロピレン容器(冷凍保管に耐えうる容器)に入れ、冷凍庫に保管し4時間のうちに−30℃に冷却した。このようにして保管菌サンプル7を作製した。なお、酢酸発酵中の発酵液を採取してから酢酸菌含有液を凍結するまでの作業時間は7時間であった。 (C) Next, the diluted vinegar fermented liquid was fed from the tank to a continuous centrifuge (ADS-1001CS, manufactured by Saito Centrifuge Co., Ltd.) at 200 L / h and centrifuged at 8000 rpm. At this time, the supernatant is automatically discharged out of the centrifuge, and the precipitate accumulates in the centrifuge. After all of the diluted vinegar fermented broth was centrifuged, 100 L of water at 15 ° C. was continuously fed to the centrifuge at 200 L / h to reduce the liquid acetic acid concentration in the centrifuge. After all 100 L of water had been put into the centrifuge, the precipitate accumulated in the centrifuge was discharged at once and recovered. The recovered liquid was about 3 L, and the acetic acid concentration was 0.1 wt / vol%. This precipitation solution was put into a 500 mL capacity polypropylene container (a container that can withstand freezing storage), stored in a freezer, and cooled to −30 ° C. within 4 hours. In this way, the stored bacteria sample 7 was prepared. The working time from collecting the fermentation broth during acetic acid fermentation to freezing the liquid containing acetic acid bacteria was 7 hours.
(2)作製した保管菌サンプル7を半年保管したものを実生産食酢発酵に用いた。即ち、米を原材料とする仕込み液をあらかじめ深部発酵用の大型発酵タンクに2kL入れておき、そこにこの保管菌を投入した。投入した保管菌の量は、発酵液20L分から回収した菌体量(回収液3L全量)とした。 (2) The produced storage bacteria sample 7 which was stored for half a year was used for the actual production vinegar fermentation. That is, 2 kL of a stock solution using rice as a raw material was previously placed in a large-scale fermentation tank for deep fermentation, and the stored bacteria were put therein. The amount of the stored bacteria introduced was the amount of cells recovered from 20 L of the fermentation broth (total amount of 3 L of recovered solution).
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発酵を所定時間継続的に行い、玄米酢を製造した。仕込み液には、米で作った酒と玄米酢の種酢(菌体除去したもの)とを混合したものを用いた。 Thereafter, the submerged fermentation of acetic acid bacteria was continuously performed for a predetermined time in accordance with a conventional method while aeration stirring was performed to produce brown rice vinegar. As the preparation liquid, a mixture of sake made from rice and seed vinegar of brown rice vinegar (those from which cells were removed) was used.
保管菌サンプル投入から発酵開始までのラグタイムは40時間となり、実生産で使用するにあたって良好な結果となった。従って、保管菌サンプル7の手順を踏めば、かなりの長期にわたって保管が可能であり、実生産の発酵で立上げ菌として使用可能であることが明らかになった。 The lag time from the storage of the stored bacteria sample to the start of fermentation was 40 hours, which was a favorable result when used in actual production. Therefore, it has been clarified that if the procedure of the stored bacteria sample 7 is followed, it can be stored for a considerably long period of time and can be used as a starter in actual production fermentation.
(全体としての結論)
従って、上述した本発明によれば以下の効果を得ることができる。即ち、本発明にかかる酢酸菌の発酵方法によれば、あらゆる食酢製造に利用できる汎用性の高い酢酸菌の種菌を、低コストで長期間(例えば半年〜1年程度)保管することができる。保管する酢酸菌も食酢の品種ごとに用意する必要がなく極めて効率的である。また、当該保管した種菌を用いて食酢発酵を行えば、短期間(例えば48時間以内)のラグタイムで発酵が立ち上がるため、あらゆる食酢の多品種少ロット生産の要請にも柔軟に対応することができる。しかも、ラグタイム自体が安定しており、生産計画に忠実な発酵を実施することが可能である。
(Conclusion as a whole)
Therefore, according to the present invention described above, the following effects can be obtained. That is, according to the method for fermenting acetic acid bacteria according to the present invention, a highly versatile inoculum of acetic acid bacteria that can be used for any vinegar production can be stored at a low cost for a long period (for example, about six months to one year). The acetic acid bacteria to be stored need not be prepared for each variety of vinegar and is extremely efficient. In addition, if vinegar fermentation is performed using the stored inoculum, the fermentation will start with a short lag time (for example, within 48 hours), so it is possible to respond flexibly to requests for production of various varieties and small lots of vinegar. it can. Moreover, the lag time itself is stable, and it is possible to carry out fermentation faithful to the production plan.
以下、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。
(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。
(2)請求項1乃至7のいずれか1項において、前記希釈溶媒が水であること。
(3)請求項1乃至7のいずれか1項において、前記希釈溶媒が冷水または氷水であること。
(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。
(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。
(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107個/mL以上であるものを用いること。
(7)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)請求項1乃至7のいずれか1項において、前記一次希釈工程では、前記酢酸濃度が4重量/容量%以下0.5重量/容量%以上となるように希釈すること。
(9)請求項1乃至7のいずれか1項において、前記遠心分離及び二次希釈工程では、前記酢酸濃度が0.1重量/容量%以下0.001重量/容量%以上となるように希釈すること。
(10)請求項1乃至7のいずれか1項において、前記保管工程では、前記酢酸菌含有液を−30℃以上−20℃以下で保管すること。
The technical ideas grasped by the above-described embodiment will be listed below.
(1) In any one of claims 1 to 7, the dilution solvent is a liquid containing only components allowed as vinegar components.
(2) In any one of claims 1 to 7, the dilution solvent is water.
(3) In any one of claims 1 to 7, the dilution solvent is cold water or ice water.
(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) 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) 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 cells / mL or more.
(7) In any one of claims 1 to 7, the alcohol concentration is diluted to 0.2% by weight or less by addition of a dilution solvent.
(8) In any one of claims 1 to 7, in the primary dilution step, the acetic acid concentration is diluted to 4 wt / vol% or less and 0.5 wt / vol% or more.
(9) In any one of claims 1 to 7, in the centrifugation and secondary dilution step, the acetic acid concentration is diluted to 0.1 wt / vol% or less and 0.001 wt / vol% or more. To do.
(10) In any one of claims 1 to 7, in the storage step, the acetic acid bacteria-containing liquid is stored at -30 ° C or higher and -20 ° C or lower.
Claims (5)
前記一次希釈工程で低温化かつ希釈された酢酸菌発酵液を遠心分離しかつ希釈溶媒を添加することにより、酢酸濃度が0.001重量/容量%以上0.1重量/容量%以下かつ酢酸菌濃度が10 7 個/mL以上となるように希釈する遠心分離及び二次希釈工程と、
前記遠心分離及び二次希釈工程を経て上記酢酸濃度かつ上記酢酸菌濃度となった酢酸菌を含有する酢酸菌含有液を凍結する凍結工程と、
前記凍結工程を経て凍結された酢酸菌含有液を−5℃以下で保管する保管工程と
を有し、前記酢酸発酵中の発酵液を採取してから前記酢酸菌含有液を凍結するまでの作業を72時間以内に行う
ことを特徴とする酢酸菌の保管方法。 By collecting a fermentation broth having an acetic acid bacteria concentration of 10 7 cells / mL or more during the acetic acid fermentation by the submerged culture method, and adding a diluting solvent having a lower temperature than that of the acetic acid bacteria fermentation broth , the acetic acid concentration becomes 0. A primary dilution step of diluting the fermentation solution of acetic acid bacteria at a low temperature so as to be 5% by weight or more and 4 % by weight or less;
By centrifuging the acetic acid bacterium fermentation solution that has been cooled and diluted in the primary dilution step and adding a diluting solvent, the acetic acid concentration is 0.001 wt / vol% or more and 0.1 wt / vol% or less and the acetic acid bacterium is added. Centrifuge and secondary dilution steps to dilute to a concentration of 10 7 / mL or more ;
A freezing step of freezing the acetic acid bacteria-containing liquid containing the acetic acid bacteria having the acetic acid concentration and the acetic acid bacteria concentration through the centrifugation and secondary dilution steps;
A storage step of storing the acetic acid bacteria-containing solution frozen through the freezing step at −5 ° C. or lower;
A method for storing acetic acid bacteria, wherein the operation from collecting the fermentation broth during acetic acid fermentation to freezing the acetic acid bacteria-containing liquid is performed within 72 hours .
前記一次希釈工程で低温化かつ希釈された酢酸菌発酵液を遠心分離しかつ希釈溶媒を添加することにより、酢酸濃度が0.001重量/容量%以上0.1重量/容量%以下かつ酢酸菌濃度が10 7 個/mL以上となるように希釈する遠心分離及び二次希釈工程と、
前記遠心分離及び二次希釈工程を経て上記酢酸濃度かつ上記酢酸菌濃度となった酢酸菌を含有する酢酸菌含有液を凍結する凍結工程と、
前記凍結工程を経て凍結された酢酸菌含有液を−5℃以下で保管する保管工程と、
前記保管工程を経て保管された前記酢酸菌を種菌として用いて酢酸発酵を行う酢酸発酵工程と
を有し、前記酢酸発酵中の発酵液を採取してから前記酢酸菌含有液を凍結するまでの作業を72時間以内に行う
ことを特徴とする食酢の製造方法。 By collecting a fermentation broth having an acetic acid bacteria concentration of 10 7 cells / mL or more during the acetic acid fermentation by the submerged culture method, and adding a diluting solvent having a lower temperature than that of the acetic acid bacteria fermentation broth, the acetic acid concentration becomes 0. A primary dilution step of diluting the fermentation solution of acetic acid bacteria at a low temperature so as to be 5% by weight or more and 4% by weight or less;
By centrifuging the acetic acid bacterium fermentation solution that has been cooled and diluted in the primary dilution step and adding a diluting solvent, the acetic acid concentration is 0.001 wt / vol% or more and 0.1 wt / vol% or less and the acetic acid bacterium is added. Centrifuge and secondary dilution steps to dilute to a concentration of 10 7 / mL or more;
A freezing step of freezing the acetic acid bacteria-containing liquid containing the acetic acid bacteria having the acetic acid concentration and the acetic acid bacteria concentration through the centrifugation and secondary dilution steps;
A storage step of storing the acetic acid bacteria-containing solution frozen through the freezing step at −5 ° C. or lower;
An acetic acid fermentation process in which acetic acid fermentation is performed using the acetic acid bacteria stored through the storage process as an inoculum; and
A method for producing vinegar, characterized in that the operation from collecting the fermentation broth during acetic acid fermentation to freezing the liquid containing acetic acid bacteria is performed within 72 hours .
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