JPS6244164A - Production of viscous vinegar - Google Patents

Production of viscous vinegar

Info

Publication number
JPS6244164A
JPS6244164A JP60183130A JP18313085A JPS6244164A JP S6244164 A JPS6244164 A JP S6244164A JP 60183130 A JP60183130 A JP 60183130A JP 18313085 A JP18313085 A JP 18313085A JP S6244164 A JPS6244164 A JP S6244164A
Authority
JP
Japan
Prior art keywords
acetic acid
fermentation
viscous
vinegar
acetobacter
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP60183130A
Other languages
Japanese (ja)
Inventor
Reiichi Nukada
額田 礼一
Hiroshi Masai
正井 博司
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nakano Vinegar Co Ltd
Original Assignee
Nakano Vinegar Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nakano Vinegar Co Ltd filed Critical Nakano Vinegar Co Ltd
Priority to JP60183130A priority Critical patent/JPS6244164A/en
Publication of JPS6244164A publication Critical patent/JPS6244164A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain viscous vinegar having improved flavor and taste, by carrying out continuous two-stage fermentation by the use of acetic acid bacteria belonging to the genus Acetobacter or Gluconobacter. CONSTITUTION:Viscous vinegar is obtained by using the following continuous fermentation processes of (a) and (b). (a) The fermentation process wherein a belonging to the genus Acetobacter or Gluconobacter, capable of producing a viscous substance, is cultivated to produce the viscous substance. (b) The fermentation process wherein the culture mixture prepared by the fermentation process a is incorporated with a nutrient source necessary for acetic acid fermentation and acetic acid fermentation is carried out by acetic acid bacteria belonging to the genus Acetobacter or Gluconbacter. Any substance produced by acetic acid bacteria belonging to the genus Acetobacter or Gluconbacter can be used as the viscous substance. Acetobacter polysaccharogens MT-11-2(FERM BP-112) can be used as the acetic acid bacteria.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、粘稠な食酢の製造法に関し、更に詳しくはア
セトバクター(八ce tobac ter)属もしく
はグルコノバクタ−(Gluconobacter)属
に属する酢酸菌を使用して連続する発酵によって粘稠な
食酢を製造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for producing viscous vinegar, and more specifically, to a method for producing viscous vinegar, and more specifically, using acetic acid bacteria belonging to the genus Acetobacter or the genus Gluconobacter. The present invention relates to a method for producing viscous vinegar through continuous fermentation.

(従来の技術) 従来の粘稠な食酢を製造する方法としては、酢酸発酵終
了後に酢酸菌の生産する粘稠物質を添加する方法が知ら
れている程度である〔 特開昭60−105460号、
特開昭59−156253号、「発酵調味食品に関する
研究」 (昭和52年度技術開発研究費補助事業成果普
及講習会テキスト、中小企業庁、第35頁〜第44頁 
昭和53年〕。酢酸菌を使用して粘稠物質を生産し、更
にその後に酢酸発酵の栄養源、即ち食酢醪を添加してそ
のまま粘稠物質生産菌を培養するかあるいは別の酢酸菌
を接種して酢酸発酵を行い粘稠な食酢を製造するという
連続した発酵によって粘稠な食酢を生産する方法は知ら
れていない。
(Prior Art) As a conventional method for producing viscous vinegar, the only known method is to add a viscous substance produced by acetic acid bacteria after the completion of acetic acid fermentation [JP-A-60-105460] ,
JP-A-59-156253, "Research on Fermented Seasoned Foods" (Textbook for the FY1973 Technology Development and Research Grant Project Result Dissemination Seminar, Small and Medium Enterprise Agency, pp. 35-44
1978]. Acetic acid bacteria are used to produce a viscous substance, and then a nutrient source for acetic acid fermentation, i.e. vinegar mash, is added and the viscous substance producing bacteria are directly cultured, or another acetic acid bacteria is inoculated and acetic acid fermentation is carried out. There is no known method for producing viscous vinegar through continuous fermentation.

(発明が解決しようとする問題点) 酢酸発酵終了液、即ち生酔に粘稠な多糖類を添加溶解し
て粘稠な食酢を製造するには、該生酔に水溶性多糖類を
溶解する方法がある。しかし、市販の水溶性多糖類はす
べて粉末状で、これを食酢の様な低pHの食品に完全溶
解させる為には多くのエネルギーと時間を要し、更に該
多糖類を溶解させる間に食酢特有の芳醇な香りが劣下し
てしまう。
(Problems to be Solved by the Invention) In order to produce viscous vinegar by adding and dissolving viscous polysaccharides to the acetic acid fermentation finished liquid, that is, raw liquor, water-soluble polysaccharides are dissolved in the raw liquor. There is a way. However, commercially available water-soluble polysaccharides are all in powder form, and it takes a lot of energy and time to completely dissolve them in low-pH foods such as vinegar. The characteristic rich aroma deteriorates.

たとえば、市販の米酢500mj!に市販のザンタンガ
ム1%(W/V)を溶解させようとすると、該米酢にザ
ンタンガムを添加した時点でザンタンガムが塊になり、
6時間攪拌しても完全には溶解しない。
For example, 500 mj of commercially available rice vinegar! When trying to dissolve commercially available xanthan gum 1% (W/V) in rice vinegar, the xanthan gum became lumps when added to the rice vinegar.
Even after stirring for 6 hours, it is not completely dissolved.

また、発酵によって生産された粘稠物質、即ち粘性物質
を含有する発酵終了液もしくは該発酵終了液を精製、殺
菌した粘稠物質含有液を酢酸発酵終了液たる食酢に添加
混合する方法では、該粘稠物質生産の為の発酵工程及び
精製、殺菌工程の為に各種の設備を必要とするほかそれ
に伴う労力と管理が不可欠であり、実用上問題が多い。
In addition, in the method of adding and mixing a viscous substance produced by fermentation, that is, a fermentation-finished liquid containing a viscous substance, or a viscous substance-containing liquid obtained by purifying and sterilizing the fermentation-finished liquid, to vinegar, which is an acetic acid fermentation-finished liquid, Various types of equipment are required for the fermentation process, purification, and sterilization process for producing a viscous substance, and the associated labor and management are indispensable, which poses many practical problems.

しかも、このような粘稠な物質を食酢に添加する方法で
は、食酢特有の芳香の他に異臭が含まれることが避けら
れず、改善の余地が多く残されていた。
Moreover, the method of adding such a viscous substance to vinegar inevitably contains an off-flavor in addition to the aroma peculiar to vinegar, leaving much room for improvement.

(問題点を解決するための手段) そこで発明物らは、香味の良い粘稠食酢を効率よく生産
する方法を鋭意研究した結果、アセトバクター属もしく
はグルコノバクタ−属に属する酢酸菌が、水溶性の粘稠
物質である多糖類(特開昭58−78596号、特開昭
5”9−203498号の明細書参照)を生産し、更に
酢酸発酵を行なう能力を有していることに着目し、まず
該酢酸菌により粘稠物質を生産する発酵工程を行い、次
いで酢酸発酵を行う発酵工程を連続して行ったところ、
香味の良い粘稠な食酢を製造することができた。
(Means for Solving the Problem) As a result of intensive research into a method for efficiently producing viscous vinegar with good flavor, the inventors discovered that acetic acid bacteria belonging to the genus Acetobacter or Gluconobacter are water-soluble. Noting that it has the ability to produce polysaccharides, which are viscous substances (see the specifications of JP-A-58-78596 and JP-A-5''9-203498), and further perform acetic acid fermentation, First, a fermentation process was performed to produce a viscous substance using the acetic acid bacteria, and then a fermentation process was performed in which acetic acid fermentation was performed.
We were able to produce viscous vinegar with good flavor.

一方、粘稠物質の有する生理効果として、例えば抗腫瘍
効果、降コレステロール効果、耐糖能改善効果等が知れ
ている。さらに、食酢は古来から酸性調味量としての利
用に加えて近年は高血−圧予防や疲労回復等の生理効果
を有することが見出されつつある。したがって、上記の
方法で得られる粘稠な食酢はこれら両者の生理効果を併
せ持つ健康食品としても価値あるものである。加えて、
従来の食酢にない粘稠性を付与した新しい食品であるこ
とから、例えばギョウザのタレに使用すればギョウザへ
の調味料の乗りが良いし、ドレッシング用の食酢として
は油と食塩やスパイス類を添加し、軽く振るだけで乳化
i安定性のすぐれたドレッシングができるという利点も
ある。
On the other hand, the physiological effects of viscous substances include, for example, antitumor effects, cholesterol-lowering effects, and glucose tolerance-improving effects. Furthermore, vinegar has been used as an acidic seasoning since ancient times, and in recent years it has been discovered that it has physiological effects such as preventing high blood pressure and relieving fatigue. Therefore, the viscous vinegar obtained by the above method is valuable as a health food that has both of these physiological effects. In addition,
Because it is a new food that has a consistency that conventional vinegar does not have, it can be used in sauces for dumplings, for example, to add seasonings to the dumplings, and vinegar for dressings can be used with oil, salt, and spices. Another advantage is that a dressing with excellent emulsification stability can be made by simply adding and shaking lightly.

本発明は次の連続する(イ)および(ロ)の発酵工程か
らなることを特徴とする粘稠な食酢の製造法を提供する
ものである。
The present invention provides a method for producing viscous vinegar characterized by comprising the following consecutive fermentation steps (a) and (b).

(イ)アセトバクター属もしくはグルコノバクタ−属に
属する粘稠物質生産菌を培養し、粘稠物質を生産する発
酵工程、 (ロ)上記発酵工程(イ)で得られた培養物に酢酸発酵
に必要な栄養源を添加してアセトバクター属もしくはグ
ルコノバクタ−属に属する酢酸菌により酢酸発酵を行う
発酵工程、 本発明において粘稠物質としてはアセトバクター属もし
くはグルコノバクター属に属する酢酸菌が生産するもの
ならばいずれも利用することができ、特に水溶性多糖類
からなる粘稠物質が安全性や生産性からみて好適に利用
できる。具体的には特開昭58−78596号及び特開
昭59−203498号の明細書に記載の水溶性多糖類
が好適な粘稠物質として利用することができる。
(a) A fermentation process in which viscous substance-producing bacteria belonging to the genus Acetobacter or Gluconobacter are cultivated to produce a viscous substance; (b) The culture obtained in the above fermentation process (a) is used for acetic acid fermentation. A fermentation process in which acetic acid fermentation is carried out by acetic acid bacteria belonging to the genus Acetobacter or Gluconobacter by adding a nutrient source, and in the present invention, the viscous substance is produced by acetic acid bacteria belonging to the genus Acetobacter or Gluconobacter. If so, any of them can be used, and in particular, a viscous substance made of water-soluble polysaccharide is preferably used from the viewpoint of safety and productivity. Specifically, water-soluble polysaccharides described in the specifications of JP-A-58-78596 and JP-A-59-203498 can be used as suitable viscous substances.

かかる粘稠物質の生産菌としては、アセトバクター属も
しくはグルコノバクタ−属に属し、粘稠物質を生産しう
る酢酸菌ならばいずれも使用できる。この発酵工程で使
用する酢酸菌は単−菌でも良いし、複数の菌でもよく、
後者の場合は異なる粘稠物質の混合体を目的として発酵
させることができる。具体的にはアセトバクター・ポリ
サン力ロゲネス(Acetobaeter  olys
accharogenes) M T−11−2(FE
RM  BP−112)、アセトバクター・ポリサソカ
ロゲネス(Ace tobac terpot sac
charogenes)MF −8(F ERM  B
 P −113)、アセトバクター(^cetobac
ter) M、H1597(FERM  BP−280
)などが利用できる。更に、粘稠物質を含有する酢酸発
酵培養液、即ち食酢醪を酢酸発酵するために用いる酢酸
菌としては、酢酸発酵の活性を有する酢酸菌であればよ
く、通常は食酢として良好な香味を有し、かつ生産性の
高い食酢を醸造する菌として使用されている酢酸菌が好
適である。このような酢酸菌として、たとえば微工研1
号菌、微工研2号菌などがある。粘稠物質生産活性を有
し、かつ食酢醸造菌としての活性を保有している酢酸菌
が最も効率的に利用できるが、異なる発酵工程を2種以
上の酢酸菌を用いて発酵を行い粘稠な食酢を製造するこ
とも可能である。即ち、それぞれの発酵工程に適した酢
酸菌を選択し、これらを組合せて使用することができる
As the bacteria producing the viscous substance, any acetic acid bacteria belonging to the genus Acetobacter or the genus Gluconobacter and capable of producing a viscous substance can be used. The acetic acid bacteria used in this fermentation process may be a single bacteria or multiple bacteria.
In the latter case, mixtures of different viscous substances can be fermented. Specifically, Acetobacter olis
accharogenes) M T-11-2 (FE
RM BP-112), Ace tobacter terpot sac
charogenes) MF-8 (FERM B
P-113), Acetobacter
ter) M, H1597 (FERM BP-280
) etc. can be used. Furthermore, the acetic acid bacteria used for acetic acid fermentation of the acetic acid fermentation culture solution containing a viscous substance, that is, vinegar mash, may be any acetic acid bacteria that has acetic acid fermentation activity, and usually has a good flavor as vinegar. Acetobacter bacteria, which is used as a bacterium for brewing vinegar and has high productivity, is suitable. As such acetic acid bacteria, for example,
There are Bacterium No. 2 and Bacterium No. 2 of the Microtech Institute. The most efficient method is to use acetic acid bacteria, which have viscous substance production activity and also have the activity as a vinegar-brewing bacterium. It is also possible to produce vinegar. That is, acetic acid bacteria suitable for each fermentation process can be selected and used in combination.

本発明において前段の粘稠物質の生産に使用する培地と
しては通常使用されているもので良く、例えば炭素源と
してはグルコース、キシロース。
In the present invention, the culture medium used in the production of the viscous substance in the first stage may be one that is commonly used. For example, the carbon source may be glucose or xylose.

ソルビトール、ソルボース、マンニトール、フラクトー
ス、アラビノース、シュークロース、グルコン酸、酢酸
、グリセロール、W蜜、澱粉質含有穀類の糖化液等を1
種もしくは2種以上混合して使用することができる。培
地中の炭素源の濃度については0.5〜8%(w/w)
、好ましくは1〜5%(w/w)である。また、後段の
酢酸発酵で使用する培地としては食酢醪と言われる原料
で良いが、米酢、穀物節、リンゴ酢、ブドウ酢等の各種
食酢にはそれぞれ特有の原料があり、これらの製造用原
料として通常に使用されているものを用い、通常に実施
されている方法で利用できる。
Sorbitol, sorbose, mannitol, fructose, arabinose, sucrose, gluconic acid, acetic acid, glycerol, double honey, saccharified liquid of starchy grains, etc.
A species or a mixture of two or more kinds can be used. For the concentration of carbon source in the medium 0.5-8% (w/w)
, preferably 1 to 5% (w/w). In addition, the medium used in the subsequent acetic acid fermentation may be a raw material called vinegar moromi, but each type of vinegar, such as rice vinegar, cereal vinegar, apple vinegar, and grape vinegar, has its own unique raw materials. It can be used using commonly used raw materials and by commonly used methods.

次に、発酵工程について述べると、(イ)粘稠な物質を
生産する発酵工程では上記培地に粘稠な物質の生産菌で
ある酢酸菌を植菌する。培養は好気的に行い、通気攪拌
培養装置を稼動させ、発酵温度は20〜35℃、好まし
くは25〜30℃とし、更に培地のpHを3〜8、好ま
しくは5〜7に制御して培養を行うことにより目的とす
る粘稠な多糖を生成させることができる。この時の通気
量は0. I VVM以上ならば目的物質の生産が可能
であるが、粘稠物質の生産効率の立場からすると、0.
4〜0.6 VVMが好適である。次に、(ロ)食酢を
生産する酢酸発酵工程では、一般的な酢酸発酵の条件、
例えば通気攪拌培養装置を使用して発酵温度約30℃、
通気盟約0. I VVMの条件で培養することにより
最終酢酸濃度4〜10%(w/w)の通常の食酢を生産
することができる。また、発酵時間はいずれの場合も目
的の物質が十分に生産されるまでとすればよい。
Next, regarding the fermentation process, (a) In the fermentation process for producing a viscous substance, the above medium is inoculated with acetic acid bacteria, which are viscous substance producing bacteria. Cultivation is carried out aerobically, operating an aerated agitation culture device, fermentation temperature is 20 to 35 °C, preferably 25 to 30 °C, and the pH of the medium is controlled to 3 to 8, preferably 5 to 7. By culturing, the desired viscous polysaccharide can be produced. The ventilation amount at this time is 0. It is possible to produce the target substance if it is above I VVM, but from the standpoint of production efficiency of viscous substances, 0.
4 to 0.6 VVM is preferred. Next, (b) In the acetic acid fermentation process to produce vinegar, the conditions for general acetic acid fermentation,
For example, using an aerated stirring culture device, the fermentation temperature is approximately 30°C.
Ventilation agreement 0. By culturing under IVVM conditions, normal table vinegar with a final acetic acid concentration of 4 to 10% (w/w) can be produced. Further, in either case, the fermentation time may be set until the desired substance is sufficiently produced.

(イ)粘稠物質を生産する発酵工程から(ロ)酢酸発酵
工程に移る工程では、発酵装置の稼動を停止または連続
的に稼動しながら発酵槽に酢酸発酵に必要な栄養源を全
量添加して(ロ)の工程の酢酸発酵を回分法にて行って
も良いし、連続して発酵装置を稼動させながら酢酸発酵
を流加培養法で、即ち酢酸濃度4〜10%(in/+4
)に相当するエタノールを徐々に流加して発酵を行うこ
ともできる。
In the process of moving from (a) the fermentation process that produces a viscous substance to (b) the acetic acid fermentation process, the entire amount of nutrients necessary for acetic acid fermentation is added to the fermenter while the operation of the fermentation equipment is stopped or continuously operated. The acetic acid fermentation in step (b) may be carried out batchwise, or the acetic acid fermentation may be carried out in a fed-batch culture method while continuously operating the fermentation equipment, i.e., at an acetic acid concentration of 4 to 10% (in/+4).
) Fermentation can also be carried out by gradually adding ethanol corresponding to

発酵効率上から云えば、後者の方が望ましいが、適宜に
回分法、流加法のいずれかを選択できる。
From the viewpoint of fermentation efficiency, the latter method is preferable, but either the batch method or the fed-batch method can be selected as appropriate.

酢酸発酵工程において前段の粘稠物質生産発酵に使用し
た酢酸菌と異なる酢酸菌を使用する場合は、栄養源を加
える時点で酢酸菌を植菌すればよい。
When using acetic acid bacteria different from those used in the previous viscous substance production fermentation in the acetic acid fermentation process, the acetic acid bacteria may be inoculated at the time of adding the nutrient source.

次に、実験例を掲げて本発明の方法を詳しく説明する。Next, the method of the present invention will be explained in detail using experimental examples.

発酵容1ffi!M!のジャーファーメンタ−に11の
水道水あたりリン酸1カリウム0.1g、  リン酸2
カリウム0.1g、硫酸マグネシウム・7水塩0.3g
、塩化第2鉄0.005g、酵母エキス2gおよびシュ
ークロース15gを溶解し、pH6に調整した粘稠物質
生産発酵用の培地31を入れ、これに同様組成の培地で
振とう培養にて前培養したアセトバクター・ポリサン力
ロゲネスMT−11−2(FERM  BP−112)
を接種し、培養温度30℃1通気量0.6 VVMで4
8時間培養した。なお、2N−NaOH溶液と15%酢
酸水溶液で培養中のpHをpH5,5〜6.0に制御し
た。
Fermentation capacity 1ffi! M! 1 Potassium phosphate 0.1g, 2 phosphoric acid per 11 tap water in Jar Fermenter
Potassium 0.1g, Magnesium sulfate heptahydrate 0.3g
, 0.005 g of ferric chloride, 2 g of yeast extract, and 15 g of sucrose were dissolved, and medium 31 for viscous substance production fermentation, adjusted to pH 6, was added, and precultured with a medium of the same composition by shaking culture. Acetobacter polysanirogenes MT-11-2 (FERM BP-112)
inoculated and cultured at 30°C, 1 aeration volume, 0.6 VVM, and 4
Cultured for 8 hours. In addition, the pH during the culture was controlled to pH 5.5 to 6.0 using a 2N-NaOH solution and a 15% acetic acid aqueous solution.

また、培養中の粘度はB型粘度計で測定した。続いて粘
稠物質が生産されたこのジャーファメンターに米糖化酢
液とエタノール60%(v/v)を含む培地を添加して
エタノール濃度が5%(v/v)になるまで調整し、発
酵温度30℃2通気量0. I VVllで更に通気攪
拌培養を継続する。この時にジャーファメンターは通気
攪拌を停止せず栄養源を一度に添加しても良いし、ある
いは栄養源を流加培養法で徐々に加えて酢酸発酵を行っ
′ても良い。
In addition, the viscosity during culture was measured using a B-type viscometer. Next, a medium containing rice saccharified vinegar solution and 60% (v/v) ethanol was added to this jar fermenter in which a viscous substance was produced, and the ethanol concentration was adjusted to 5% (v/v). Fermentation temperature 30℃ 2 Aeration rate 0. Continue aeration and agitation culture at IVVll. At this time, the nutrient source may be added to the jar fermenter all at once without stopping the aeration and agitation, or the nutrient source may be gradually added using a fed-batch culture method to carry out acetic acid fermentation.

表1に発酵プロセスの態様と発酵結果をまとめたが、(
A)の発酵プロセスは栄養源を一度に添加する方法で行
ったものであり、(B)の方法は粘稠物質生産のための
栄養源と酢酸発酵に必要な栄養源の両方をジャーファメ
ンターに入れ発酵濃度30℃1通気3i0. I VV
Mで上記発酵プロセス(A)で使用の酢酸菌を接種して
行ったものである。また、(C)の方法は酢酸発酵工程
を先に行うという上記発酵プロセス(A)と逆の工程で
行ったものである。表から明らかな如く、発酵プロセス
(A)のみが目的とする粘稠な食酢−を生産しうる方法
である。なお、この実験より、pHを制御すると香味の
良い粘稠な食酢が得られることも明らかとなった。次に
、発酵プロセス(A)の経過を表2に示す。
Table 1 summarizes the fermentation process aspects and fermentation results.
The fermentation process in A) was carried out by adding the nutrient source at once, and in the method in B), both the nutrient source for viscous production and the nutrient source necessary for acetic acid fermentation were added to the jar fermenter. Fermentation concentration 30℃ 1 ventilation 3i0. I VV
M was inoculated with the acetic acid bacteria used in the fermentation process (A) above. In addition, method (C) was carried out using the reverse process of the above fermentation process (A), in which the acetic acid fermentation process was performed first. As is clear from the table, fermentation process (A) is the only method capable of producing the desired viscous vinegar. This experiment also revealed that viscous vinegar with good flavor can be obtained by controlling the pH. Next, the progress of the fermentation process (A) is shown in Table 2.

表2 発酵プロセス(A)の経過 * 酢酸発酵用の栄養源を添加した。Table 2 Progress of fermentation process (A) *A nutrient source for acetic acid fermentation was added.

本発明における粘稠な食酢は発酵終了液そのものである
が、発酵終了液には酢酸菌体や夾雑物等を含有している
ので、各種の醸造用振下げ剤、さらには清澄剤、例えば
柿渋、卵白、ヘントナイト等を添加したり、あるいは遠
心分離等の物理的処理を行うことにより酢酸菌体や夾雑
物を除くことによって清澄窓のある香味の一層すぐれた
粘稠な食酢を得ることができる。
The viscous vinegar used in the present invention is the fermentation-finished liquid itself, but since the fermentation-finished liquid contains acetic acid bacteria and impurities, it can be used with various brewing shaking agents, as well as with clarifying agents, such as persimmon juice. By removing acetic acid bacteria and impurities by adding , egg white, hentonite, etc., or by performing physical treatment such as centrifugation, it is possible to obtain viscous vinegar with a clear window and even better flavor. .

(実施例) 実施例を以下に挙げて本発明を具体的に説明する。(Example) The present invention will be specifically explained with reference to Examples below.

実施例1 リン酸1カリウム0.1g、  リン酸2カリウム0.
1g、硫酸マグネシウム・7水塩0.25g、塩化第2
鉄0.005g、酵母エキス2gおよびグルコース15
gを11の水道水に溶解して培地とした。
Example 1 Monopotassium phosphate 0.1g, dipotassium phosphate 0.
1g, magnesium sulfate heptahydrate 0.25g, dichloride
0.005g iron, 2g yeast extract and 15g glucose
g was dissolved in 11 tap water to prepare a culture medium.

この培地37!をp H7,0に調整した後、51容ジ
ャーファーメンタ−に入れ、上記と同様な培地を用いて
アセトバクター・ポリサソカロゲネスMF−8(FE’
RM  BP−113)を前培養したものを種菌として
前記培地の入ったジャーファーメンタ−に接種し、発酵
温度30°C1通気量0.5 VVMで48時間培養し
た。培養中、2N−NaOH溶液と15%酢酸溶液を使
用して培養液のpHを5.5〜6.0に制御した。培養
48時間後、培養液の粘度は830cpであった。引続
き、この粘稠物。
This medium is 37! After adjusting the pH to 7.0, the culture medium was placed in a 51-volume jar fermenter, and Acetobacter polysasocalogenes MF-8 (FE'
A preculture of RM BP-113) was inoculated as a seed into a jar fermenter containing the above medium, and cultured for 48 hours at a fermentation temperature of 30° C. and an aeration volume of 0.5 VVM. During the culture, the pH of the culture solution was controlled at 5.5 to 6.0 using a 2N-NaOH solution and a 15% acetic acid solution. After 48 hours of culture, the viscosity of the culture solution was 830 cp. Continuing with this viscous substance.

質が生産された培養液に米糖化液とエタノール60%(
v/v)を含有する培養液を酢酸濃度5%(W/W)に
相当するエタノールシン農度が5%(ν/ν)になるま
で発酵温度30℃1通気ff1o、 I VVM、 5
00 rpm(7)攪拌条件で流加培養する。この時に
は培養液のpH制御は必要はない。このようにして48
時間培養を行うことにより粘度700cp、酢酸濃度4
.5%の粘稠な食酢ができた。
Rice saccharification solution and 60% ethanol (
v/v) was fermented at a fermentation temperature of 30° C. with 1 aeration of 5% (v/v) until the ethanol concentration was 5% (v/v), which corresponds to an acetic acid concentration of 5% (w/w).
00 rpm (7) agitation condition. At this time, there is no need to control the pH of the culture solution. In this way 48
By culturing for hours, the viscosity was 700 cp and the acetic acid concentration was 4.
.. A 5% viscous vinegar was made.

実施例2 麹で糖化した米糖化液および米酢を混合して還元糖とし
て2%輛/−)、酢酸濃度0.3%(iv/iy)にな
るように水道水で希釈した培地71を調製した。次に、
この培地を実施例1で使用したNaOHにてpHを6.
0に調整し、301容ジャーファーメンタ−に仕込んだ
。一方、同一組成の培地を使用して坂ロフラスコにて振
とう前培養したアセトバクター・MH−1597(FE
RMBP−280)を種菌として前記培地の入ったジャ
ーファメンターに接種し、培養温度30℃9通気量0.
5 VVMで40時間培養した。培養中、2N−NaO
H溶液と15%酢酸溶液を用いて培養液のpHを5〜7
に制御した。40時間培養後の培養液の粘度はB型粘度
計で550cpであった。続いて、この培養液に麹で糖
化した15%(鰹い還元糖濃度の糖化液およびエタノー
ル濃度8.1%(v/ν)である培養液13I!を添加
するとともにpH制御は停止し、培養温度30℃2通気
量0.IVVMで通気攪拌培養を行い、粘度140cp
、酢酸濃度4.48%(w/w)の粘稠な食酢201を
得た。
Example 2 Culture medium 71 was prepared by mixing rice saccharification solution saccharified with koji and rice vinegar to give a reducing sugar of 2% (iv/iy) and acetic acid concentration of 0.3% (iv/iy) with tap water. Prepared. next,
This medium was adjusted to pH 6.0 with NaOH used in Example 1.
The mixture was adjusted to 0 and placed in a 301 volume jar fermenter. On the other hand, Acetobacter MH-1597 (FE
RMBP-280) was inoculated into a jar fermenter containing the above medium as a seed, and the culture temperature was 30°C and the aeration rate was 0.
The cells were cultured for 40 hours at 5 VVM. During culture, 2N-NaO
Adjust the pH of the culture solution to 5-7 using H solution and 15% acetic acid solution.
was controlled. The viscosity of the culture solution after 40 hours of culture was 550 cp using a B-type viscometer. Next, culture solution 13I!, which was saccharified with koji and had a 15% saccharified reducing sugar concentration and an ethanol concentration of 8.1% (v/ν), was added to this culture solution, and the pH control was stopped. Aerated agitation culture was performed at a culture temperature of 30°C and aeration volume of 0.IVVM, and the viscosity was 140 cp.
, viscous vinegar 201 with an acetic acid concentration of 4.48% (w/w) was obtained.

更に、このようにして得た粘稠な食酢の1部を800 
Or、p、m、、  30分間遠心分離して酢酸菌体等
を沈澱させることにより、上澄液としてODI、6゜に
よる濁度が0.106という透明性にすぐれた粘度13
8cpの本発明の食酢が得られた。
Furthermore, one part of the viscous vinegar obtained in this way was added to 800 yen.
Or, p, m,, By centrifuging for 30 minutes to precipitate the acetic acid bacteria, the supernatant has a viscosity of 13 with excellent transparency and a turbidity of 0.106 at ODI 6°.
8 cp of vinegar of the present invention was obtained.

この粘稠な食酢100mAに食塩6g、 こしょう0.
2gおよびグルタミン酸ソーダ0.5gを加えて溶解し
、激しく振とうしながらサラダオイル300m/を少し
づつ加え(サラダドレッシングを作成した。一方、対照
として前述の粘稠な食酢の代りに市販の米酢(酢酸酸度
4.5%(w/w) )100mlに市販のキサンタン
ガム0.2gを溶解し、これに上記の食塩、こしょう、
グルタミン酸ソーダを前記と同量加え、以下同様にして
サラダドレッシングを作成した。これらサラダドレッシ
ングについて官能評価を行ったところ、嗜好性。
Add 6 g of salt and 0.0 g of pepper to 100 mA of this viscous vinegar.
2g and 0.5g of sodium glutamate were added and dissolved, and 300ml of salad oil was added little by little while shaking vigorously (salad dressing was made.On the other hand, as a control, commercially available rice vinegar was used instead of the viscous vinegar mentioned above). Dissolve 0.2 g of commercially available xanthan gum in 100 ml (acetic acid acidity 4.5% (w/w)), add the above salt, pepper,
A salad dressing was prepared in the same manner by adding the same amount of sodium glutamate as above. A sensory evaluation of these salad dressings revealed that they were palatable.

食感において本発明に係るものは対照品よりも優れてい
た。
In terms of texture, the products according to the present invention were superior to the control products.

〈発明の効果) このように本発明によって製造される粘稠な食酢は、香
味や食感の優れたものである上に、粘稠物質等の有する
生理効果をも有しており、健康食品としても価値が高い
<Effects of the Invention> As described above, the viscous vinegar produced by the present invention not only has excellent flavor and texture, but also has the physiological effects of a viscous substance, so it can be used as a health food. It is also of high value.

Claims (5)

【特許請求の範囲】[Claims] (1)次の連続する(イ)および(ロ)の発酵工程から
なることを特徴とする粘稠な食酢の製造法。 (イ)アセトバクター属もしくはグルコノバクター属に
属する粘稠物質生産菌を培養し、粘稠物質を生産する発
酵工程、 (ロ)上記発酵工程(イ)で得られた培養物に酢酸発酵
に必要な栄養源を添加してアセトバクター属もしくはグ
ルコノバクター属に属する酢酸菌により酢酸発酵を行う
発酵工程、
(1) A method for producing viscous vinegar characterized by comprising the following consecutive fermentation steps (a) and (b). (a) A fermentation process in which viscous substance-producing bacteria belonging to the genus Acetobacter or Gluconobacter are cultivated to produce a viscous substance; (b) The culture obtained in the above fermentation process (a) is subjected to acetic acid fermentation. A fermentation process in which acetic acid bacteria belonging to the genus Acetobacter or Gluconobacter add necessary nutrients and perform acetic acid fermentation;
(2)アセトバクター属に属する酢酸菌がアセトバクタ
ー・ポリサッカロゲネスMT−11−2(FERM B
P−112)である特許請求の範囲第1項記載の方法。
(2) Acetobacter belonging to the genus Acetobacter is Acetobacter polysaccharogenes MT-11-2 (FERM B
P-112). The method according to claim 1.
(3)アセトバクター属に属する酢酸菌がアセトバクタ
ー・ポリサッカロゲネスMF−8 (FERM BP−113)である特許請求の範囲第1
項記載の方法。
(3) Claim 1, wherein the acetic acid bacterium belonging to the genus Acetobacter is Acetobacter polysaccharogenes MF-8 (FERM BP-113)
The method described in section.
(4)アセトバクター属に属する酢酸菌がアセトバクタ
ー・MH−1597(FERM BP−280)である
特許請求の範囲第1項記載の方法。
(4) The method according to claim 1, wherein the acetic acid bacterium belonging to the genus Acetobacter is Acetobacter MH-1597 (FERM BP-280).
(5)粘稠物質が水溶性多糖類である特許請求の範囲第
1項記載の方法。
(5) The method according to claim 1, wherein the viscous substance is a water-soluble polysaccharide.
JP60183130A 1985-08-22 1985-08-22 Production of viscous vinegar Pending JPS6244164A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60183130A JPS6244164A (en) 1985-08-22 1985-08-22 Production of viscous vinegar

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60183130A JPS6244164A (en) 1985-08-22 1985-08-22 Production of viscous vinegar

Publications (1)

Publication Number Publication Date
JPS6244164A true JPS6244164A (en) 1987-02-26

Family

ID=16130320

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60183130A Pending JPS6244164A (en) 1985-08-22 1985-08-22 Production of viscous vinegar

Country Status (1)

Country Link
JP (1) JPS6244164A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5427803A (en) * 1991-12-20 1995-06-27 Nestec S.A. Trickle process for vinegar production
JP2001097869A (en) * 1999-09-28 2001-04-10 Fuso Pharmaceutical Industries Ltd New antitumor agent
WO2022163649A1 (en) * 2021-01-29 2022-08-04 株式会社Mizkan Holdings Vinegar and method of producing same

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5427803A (en) * 1991-12-20 1995-06-27 Nestec S.A. Trickle process for vinegar production
JP2001097869A (en) * 1999-09-28 2001-04-10 Fuso Pharmaceutical Industries Ltd New antitumor agent
JP4584384B2 (en) * 1999-09-28 2010-11-17 扶桑薬品工業株式会社 New antitumor agent
WO2022163649A1 (en) * 2021-01-29 2022-08-04 株式会社Mizkan Holdings Vinegar and method of producing same
JPWO2022163649A1 (en) * 2021-01-29 2022-08-04

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