JPS6167459A - Production of seasoning solution - Google Patents

Production of seasoning solution

Info

Publication number
JPS6167459A
JPS6167459A JP59188852A JP18885284A JPS6167459A JP S6167459 A JPS6167459 A JP S6167459A JP 59188852 A JP59188852 A JP 59188852A JP 18885284 A JP18885284 A JP 18885284A JP S6167459 A JPS6167459 A JP S6167459A
Authority
JP
Japan
Prior art keywords
soy sauce
yeast
carrier
liquid
raw material
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
JP59188852A
Other languages
Japanese (ja)
Inventor
Akira Okuhara
奥原 章
Shiyousuke Shigeta
重田 敞右
Isao Kimura
功 木村
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.)
Kikkoman Corp
Original Assignee
Kikkoman Corp
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 Kikkoman Corp filed Critical Kikkoman Corp
Priority to JP59188852A priority Critical patent/JPS6167459A/en
Publication of JPS6167459A publication Critical patent/JPS6167459A/en
Pending legal-status Critical Current

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  • Soy Sauces And Products Related Thereto (AREA)
  • Seasonings (AREA)

Abstract

PURPOSE:To obtain seasoning having improved color, luster, and flavor in a short period efficiently, by bringing enzymatically or chemically hydrolyzed solution of a raw material for producing soy sauce into contact with a fermentation column packed with a hydrophilic fibrous carrier to which a yeast is attached, and passing the solution through it. CONSTITUTION:A liquid medium for yeast culture of soy sauce yeast mold is inoculated with a soy sauce yeast mold such as Saccharomyces rouxii having film yeast properties, the mold is cultivated, put in the vapor-liquid separating tank 4, sent and circulated by the feed pump 3 through the fermentation tank 1 packed with a lipophilic carrier such as PP, etc. for about 6 days, the soy sauce yeast mold is sufficiently attached to the surface of the carrier, and the medium is taken out from the column 1 and the tank 4. Then, a raw material for producing soy sauce, obtained by adding a starch raw material to a protein raw material, is hydrolyzed enzymatically with an enzymatic agent such as Aspergillus oryzae, etc. or hydrolyzed chemically with 3-10wt% HCl solution to give a solution, which is added to the tank 4 instead of the medium, the temperature is controlled by the temperature control device 8, and it is repeatedly circulated through the tank 4 - the heat exchanger 2 - the column 1, and after 20 days is passed, soy sauce having improved color, luster and fragrance is obtained.

Description

【発明の詳細な説明】 本発明は、高品質の調味液を効率良く安定して製造でき
る調味液の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a seasoning liquid that can efficiently and stably produce a high-quality seasoning liquid.

従来、醤油製造用原料を無塩又は低食塩下で短期間に加
水分解し、これを順次乳酸発酵、酵母発酵を経、熟成さ
せて醤油を得る、醤油の速醸法が種々知られているが、
これらの速醸法においてはいずれも泥状諸法の発酵、熟
成方式を採用しているため、必然的に前記発酵、熟成に
要する時間が長期となるばかりでなく、諸法の品温管理
、通気攪拌等の醤油製造工程上極めて重要な操作がいず
れも均一な状態で行なわれ難く、又諸法粘度も高いため
諸法輸送及び圧搾工程に著しい障害を来している。
Conventionally, various quick brewing methods for soy sauce have been known, in which raw materials for soy sauce production are hydrolyzed in a short period of time under salt-free or low-salt conditions, and then sequentially subjected to lactic acid fermentation, yeast fermentation, and aging to obtain soy sauce. but,
Since these quick brewing methods all use muddy fermentation and maturation methods, not only do the fermentation and maturation processes inevitably take a long time, but also the product temperature control and Operations that are extremely important in the soy sauce manufacturing process, such as aeration and stirring, are difficult to perform in a uniform state, and the viscosity of soy sauce is also high, which poses significant obstacles to transportation and pressing processes.

そこで本発明者等は、このような従来技術の欠点を解消
すべく鋭意検討した結果、従来全く知られていない、親
油性繊維状担体に酵母菌を付着せしめ得られた担体を使
用し、これに醤油製造用原料を酵素的もしくは化学的に
加水分解して得られだ液を接触通過せしめると、簡単に
前記担体上に酵母菌を付着増殖せしめ、担体を詰めた発
酵塔容積当りの菌濃度を高くシ、短期間に効率良く調味
液が得られること、担体に付着増殖した醤油酵母菌は長
期間連続的に使用しても活性が安定で寿命が頗る長く、
半永久的に使用できること、特に産膜性醤油酵母菌は担
体上への付着増殖力、菌相互の凝集力が強いので担体表
面上に厚い菌膜層を形成し、非常に効率良く調味液が得
られること、醤油酵母を付着増殖せしめて得られた担体
に対しては通気が不要なので通気のための設備費、運転
費が軽減され、又調味液の通気による酸化褐変増色と風
味の劣化が抑制されるので色沢が縦置で香シの優れた調
味液が得られること、醤油製造用原料を酵素的もしくは
化学的に加水分解して得られた液は低塩分であるにも拘
らず酵母菌を付着増殖せしめた担体と接触中、贋造又は
酸敗しないこと、そして担体の表面に形成された酵母の
菌膜層は水洗滌又は洗剤洗滌等によシ簡単に取シ除くこ
とができるので担体の再生及び付着酵母菌の変更を任意
に行いうる等の知見を得、これらの知見に基づいて本発
明を完成した。
Therefore, the present inventors conducted intensive studies in order to solve these drawbacks of the conventional technology, and as a result, they used a carrier obtained by attaching yeast bacteria to a lipophilic fibrous carrier, which was completely unknown in the past. When the liquid obtained by enzymatically or chemically hydrolyzing raw materials for soy sauce production is passed through contact with the carrier, yeast bacteria easily adhere and grow on the carrier, and the concentration of bacteria per volume of the fermentation tower packed with the carrier increases. The soy sauce yeast bacteria grown on the carrier has stable activity even when used continuously for a long period of time, and has a long lifespan.
In particular, film-producing soy sauce yeast bacteria have a strong ability to adhere to the carrier and coagulate with each other, so they form a thick bacterial film layer on the carrier surface and produce a seasoning liquid very efficiently. Since the carrier obtained by adhering and growing soy sauce yeast does not require aeration, equipment costs and operating costs for aeration are reduced, and oxidative browning and color increase and flavor deterioration due to aeration of the seasoning liquid are avoided. Because the color luster is suppressed, it is possible to obtain a seasoning liquid with excellent aroma even when placed vertically, and the liquid obtained by enzymatically or chemically hydrolyzing raw materials for soy sauce production has a low salt content. During contact with the carrier on which yeast bacteria have adhered and grown, it will not be forged or become rancid, and the bacterial film layer of yeast formed on the surface of the carrier can be easily removed by washing with water or detergent. The present invention was completed based on the knowledge that the carrier can be regenerated and the yeast bacteria attached can be changed arbitrarily.

即ち本発明は、親油性繊維状担体を通液可能な発酵塔内
に詰め、該担体に酵母菌を付着せしめ、これに醤油製造
用原料を酵素的もしくは化学的に加水分解して得られた
液を接触通過せしめることを特徴とする調味液の製造法
である。
That is, the present invention provides a lipophilic fibrous carrier packed in a fermentation tower through which liquid can pass, yeast bacteria attached to the carrier, and a raw material for soy sauce production enzymatically or chemically hydrolyzed onto the carrier. This is a method for producing a seasoning liquid, which is characterized by passing the liquid through contact.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

本発明に用いる親油性繊維状担体としては、親油性が高
い、即ち油に対して馴染み易い合成樹脂を繊維状にし、
表面積を大きくした集積体で、布状、綿状、スポンジ状
又は不織布構造のもの等があシ、これらは一般に油吸着
材として用いられているものである。また、これらは必
要により適轟な大きさにカットした不定形状又は定形状
(例えばチップ状)のものとして使用してもよい。
The lipophilic fibrous carrier used in the present invention is made of a synthetic resin that has high lipophilicity, that is, is easily compatible with oil, and is made into a fibrous form.
These are aggregates with a large surface area, such as cloth-like, cotton-like, sponge-like, or non-woven structures, which are generally used as oil adsorbents. Further, these may be used in the form of an irregular shape or a fixed shape (for example, a chip shape) cut into an appropriate size if necessary.

上記担体の素材としては、例えばアタクティク・ポリプ
ロピレン、アイツタクチイック・ポリプロピレン、グロ
ビレンーエチレンブロック共重合体、プロピレン−エチ
レンランダム共重合体などのプロピレン系ポリマー、高
圧ポリエチレン、中低圧ポリエチレンなどのポリエチレ
ン類、エチレン−酸ピコポリマー、ポリスチレン系ポリ
マー、ポリエステル系ポリマー及びポリウレタンフォー
ム等が挙げられる。そして、これらは単用又は併用する
ことができる。
Examples of materials for the carrier include propylene polymers such as atactic polypropylene, tactical polypropylene, globylene-ethylene block copolymer, propylene-ethylene random copolymer, and polyethylenes such as high-pressure polyethylene and medium-low pressure polyethylene. , ethylene-acid picopolymers, polystyrene polymers, polyester polymers, and polyurethane foams. These can be used alone or in combination.

また、親油性繊維状担体の具体例としては、「レオマッ
ト」(住友化学社製)、「ウオセツプ」(東し社製)、
「オイリーバ」(大和紡績社製)、「ハイセパーレ」(
チッソ社製)、「タフネル」、「タフネル・オイルプロ
ッター」(三井石油化学社製)、「ペトレル」(三菱レ
イヨン社製)、「オイルソーベント」(住友スリーエム
社製)及び「オルソーブ」(奇人社製)等が挙げられる
Specific examples of lipophilic fibrous carriers include "Rheomat" (manufactured by Sumitomo Chemical Co., Ltd.), "Uosep" (manufactured by Toshisha Co., Ltd.),
“Oi Lever” (manufactured by Daiwabo Co., Ltd.), “Hi Separe” (
(Manufactured by Chisso Corporation), "Tuffnel", "Tuffnel Oil Plotter" (manufactured by Mitsui Petrochemicals), "Petrel" (manufactured by Mitsubishi Rayon), "Oil Sorvent" (manufactured by Sumitomo 3M), and "Orsorb" (Kijin) company), etc.

本発明において、親油性繊維状担体を用いることは極め
て重要である。
In the present invention, it is extremely important to use a lipophilic fibrous carrier.

即ち、親水性繊維状担体を用いるときは、その担体を詰
めた発酵塔内での通液抵抗が犬となって運転できなくな
る。繊維状担体の外径を大きくすれば通液抵抗の問題は
解決′するが、表面積が小さくなって発酵塔容積当シの
菌濃度が低下し、短期間に効率良く調味液が得られない
欠点を有する。
That is, when a hydrophilic fibrous carrier is used, the resistance to passage of liquid inside the fermentation tower packed with the carrier increases, making operation impossible. Increasing the outer diameter of the fibrous carrier solves the problem of liquid flow resistance, but this reduces the surface area and reduces the bacterial concentration per fermentation tower volume, making it impossible to efficiently obtain a seasoning liquid in a short period of time. has.

これに対して親油性繊維状担体ははつ水性が良好である
ため発酵塔内での通液抵抗は非常に少なく、繊維の外径
を非常に細くすることができるので、そこに酵母菌が付
着増殖し得る表面積が犬となって発酵塔容積当りの菌濃
度を増大し、短期間に効率良く調味液が得られる。
On the other hand, lipophilic fibrous carriers have good water repellency, so there is very little resistance to liquid passage inside the fermentation tower, and the outer diameter of the fibers can be made very thin, so yeast bacteria can The surface area for adhesion and growth increases the bacterial concentration per volume of the fermentation tower, and a seasoning liquid can be obtained efficiently in a short period of time.

また、親油性繊維状担体は有用な酵母菌、特に醤油酵母
菌は付着し、増殖し易く、反対に有害な細菌は付着、増
殖し難いという調味液の製造に極めて好都合な性質を有
しておシ、該担体に一旦付着した酵母菌は旺盛に増殖し
、生育し続けることができるが、木綿などの親水性繊維
状担体は有用な酵母菌の付着、増殖力が弱いので効率良
く安定して製造できない。
In addition, the lipophilic fibrous carrier has properties that are extremely convenient for the production of seasoning liquids, such that useful yeast bacteria, especially soy sauce yeast, easily attach and proliferate, while harmful bacteria have difficulty adhering and proliferating. However, on hydrophilic fibrous carriers such as cotton, yeast bacteria that have attached to the carrier can proliferate vigorously and continue to grow, but since the ability of useful yeast bacteria to attach and multiply is weak, it cannot be efficiently stabilized. cannot be manufactured.

また従来知られているゲル包括法で得られる担体、塊状
、板状、薄片状等の非繊維状担体は繊維状担体に比べて
酵母菌の担体表面上への付着力が弱く、一旦担体上に付
着した酵母菌も時間の経過と共に次第に減少し、効率良
く、安定して調味液を製造できない。
In addition, carriers obtained by the conventionally known gel entrapment method, non-fibrous carriers in the form of lumps, plates, flakes, etc., have a weaker adhesion force for yeast bacteria on the carrier surface than fibrous carriers. The number of yeast bacteria attached to the container gradually decreases over time, making it impossible to efficiently and stably produce a seasoning liquid.

次に担体を詰める発酵塔としては、カラム状、塔状など
の通液可能な形式があるが、前記担体を詰め、通液可能
なものであれば形状、大きさは限定されない。そして、
これらは複数個直列又は並列に接続して用いることもで
きる。
Next, the fermentation tower into which the carriers are packed may be of a type such as a column or tower that allows liquid to flow therethrough, but the shape and size are not limited as long as the carriers can be packed therein and liquids can flow through the fermentation tower. and,
A plurality of these may be connected in series or in parallel.

次に、この担体に付着せしめる酵母菌としては、醤油、
味噌、清酒、アルコール等の製造に使用される酵母菌等
特に限定されないが、これらのうち食塩存在下で酵母に
よるアルコール発酵を行って調味液を作ることを考慮す
れば、食塩濃度10%以上の酵母培養液体培地に生育可
能でアルコール生産能を有する酵母菌、特に醤油諸法か
ら分離されるアルコール生産能の強い菌が好ましい。そ
の具体例としては、サツカロミセス・ルキシー1335
6、同14679、同14680、トルロプシス・ノダ
エンンスATCC20189、トルロプシス・マグノリ
アATCC13782、トルロプシス・エチニルシーA
TCC20190、トルロプシス・スフエリ力ATCC
13193、トルロプシス・プエルfチ’) 、(A 
T CC2Q191゜チゴサッカロミセス・ルキシー、
ハンセヌラ・アノマラ、ピヒヤ・ハリタケ、トルロプシ
ス・ハロフィルス、トルロプシス・アノツマATCC2
0222等が挙げられる。そして、これらのうちチゴサ
ッカロミセス・ルキシー、ハンセヌラ・アノマラ、ピ、
ヒヤ・ハリタケに属し産膜性を有する醤油酵母菌が特に
好ましい。
Next, the yeast bacteria to be attached to this carrier include soy sauce,
Yeasts used in the production of miso, sake, alcohol, etc. are not particularly limited, but considering that alcoholic fermentation with yeast is performed in the presence of salt to produce seasoning liquid, yeasts with a salt concentration of 10% or more are used. Yeast bacteria that can grow in a yeast culture liquid medium and have alcohol-producing ability, particularly bacteria with strong alcohol-producing ability isolated from soy sauce methods, are preferred. A specific example is Satsucharomyces luxii 1335.
6, Torulopsis 14679, Torulopsis 14680, Torulopsis nodaens ATCC 20189, Torulopsis magnolia ATCC 13782, Torulopsis ethinisii A
TCC20190, Torulopsis spheeri ATCC
13193, Torulopsis puerfchi'), (A
T CC2Q191゜Chigosaccharomyces luxii,
Hansenula anomara, Pihya haritake, Torulopsis halophilus, Torulopsis anotsuma ATCC2
0222 and the like. And among these, Chigosaccharomyces ruxii, Hansenula anomala, Pi,
Particularly preferred is a soy sauce yeast that belongs to the Hiya Haritake family and has film-producing properties.

次に、上記担体に酵母菌を付着、増殖せしめる方法は極
めて簡単で、担体を詰めた発酵塔の一端より予め別に培
養して得られた酵母菌培養液、発酵旺盛な醤油諸法液汁
等、酵母菌含有液を少量塔内に注入し、引続き麹汁等の
酵母増殖用借地又は、醤油製造用原料を酵素的もしくは
化学的に加水分解し濾過して得られたものを、そのまま
或いは酵母の栄養源を加え、本発明では特に必要としな
いが空気(酸素含有気体)と共に送入しつつ、20〜3
5℃、特に27〜33℃の発酵適温に保ち、発酵塔の他
端から流出してくる発酵液は必要により成分の規格を調
製した後再び発酵塔の一端から流入し、以下上記操作を
継続して行う方法が挙げられる。
Next, the method of attaching and multiplying yeast bacteria to the carrier is extremely simple, and yeast culture broth obtained by culturing separately from one end of a fermentation tower packed with carriers, actively fermented soy sauce broth, etc. A small amount of the yeast-containing solution is injected into the tower, and then the yeast-propagating soil such as koji soup or the raw material for soy sauce production is enzymatically or chemically hydrolyzed and filtered, and the resultant product is either used directly or as a yeast-containing solution. While adding a nutrient source and feeding it together with air (oxygen-containing gas), which is not particularly required in the present invention,
The fermentation liquid flowing out from the other end of the fermentation tower is kept at 5°C, especially 27 to 33°C, which is suitable for fermentation, and after adjusting the specifications of the ingredients as necessary, it flows back into the fermentation tower from one end, and the above operations are continued. An example of this method is to do so.

この方法によれば75〜20時間で充分な量の酵母菌を
該担体の表面上に付着増殖することがで糖濃度の減少か
らも知ることができる。
According to this method, a sufficient amount of yeast bacteria can adhere and proliferate on the surface of the carrier in 75 to 20 hours, which can be seen from the decrease in sugar concentration.

こうして、酵母菌の付着増殖した担体の発酵効率は極め
て高く、発酵塔に詰めた担体の単位体積当りの発酵効率
は従来のゲル包括法によって酵母菌を固定化した場合に
比べて2倍以上に達する。
In this way, the fermentation efficiency of the carrier on which yeast bacteria have adhered and grown is extremely high, and the fermentation efficiency per unit volume of the carrier packed in the fermentation tower is more than twice that of the case where yeast bacteria are immobilized using the conventional gel entrapment method. reach

従って、小型の発酵塔を用いて調味液を一定時間内に大
量に生産することができる。
Therefore, a large amount of seasoning liquid can be produced within a certain period of time using a small fermentation tower.

次に、本発明においては原料として醤油製造用原料、を
酵素的もしくは化学的に加水分解し濾過して得られたも
のを使用する。
Next, in the present invention, a material obtained by enzymatically or chemically hydrolyzing and filtering a raw material for soy sauce production is used as a raw material.

上記醤油製造用原料としては、醤油製造に通常用いられ
るもの、即ち蛋白質原料に澱粉質原料を加えたものが用
いられ、蛋白質原料としては例えば脱脂大豆、夫大豆、
小麦グルテン、コーングルテン、大豆精製蛋白、今箒セ
分離蛋白等が、澱粉質原料としては例えば小麦、大麦、
トウモロコシ等が好適なものとして挙げられる。
The above-mentioned raw materials for soy sauce production include those commonly used in soy sauce production, that is, protein raw materials with starchy raw materials added to them. Examples of protein raw materials include defatted soybeans, soybeans,
Wheat gluten, corn gluten, soybean purified protein, Imahose isolated protein, etc. Starchy raw materials include wheat, barley,
Suitable examples include corn and the like.

そして、これらの原料に対しては常法による原料処理、
即ち原料組織の軟化、蛋白質の変性、澱粉のα化、殺菌
等が行なわれる。
Then, these raw materials are processed by conventional methods,
That is, the raw material tissue is softened, proteins are denatured, starch is gelatinized, sterilized, etc.

次に醤油製造用原料の酵素による加水分解は、酵素剤に
よる方法、醤油製造用原料を醤油麹として加水分解する
方法等の何れでもよい。
Next, the hydrolysis of the raw material for soy sauce production with an enzyme may be performed by any method using an enzyme agent, a method in which the raw material for soy sauce production is hydrolyzed as soy sauce malt, or the like.

上記酵素剤としては、例えば醤油用麹菌であるアスペル
ギルス−オリーゼ、アスペルギルス・ンーヤ等の黄麹菌
、クモノスカビ等を適当な培地に培養し、培養物より例
えば水等によシ抽出して得た粗酵素液、さらにはこれよ
シ常法例えば有機溶媒による沈澱法等分用いて得た粗酵
素剤等が特に好適であるが、その池一般に市販されてい
る各種酵素製剤も有効に用いられる。これらの酵素製剤
としては、酵素剤による醤油醸造法において通常用いら
れるものが有効に使用されるが、例えばα−アミラーゼ
製剤、β−アミラーゼ製剤、アルカリプロテアーゼ製剤
、中性プロテアーゼ製剤、酸性プロテアーゼ製剤等が一
例として挙げられる。
The above-mentioned enzyme agent may be a crude enzyme obtained by culturing Aspergillus oryzae, which is a koji mold for soy sauce, Aspergillus yellow mold such as Aspergillus nya, or Arachnidium sp., in an appropriate medium and extracting the culture with water or the like. Particularly suitable are liquid enzyme preparations, and crude enzyme preparations obtained by a conventional method such as precipitation using an organic solvent, but various commercially available enzyme preparations can also be effectively used. As these enzyme preparations, those commonly used in the soy sauce brewing method using enzyme preparations can be effectively used, such as α-amylase preparations, β-amylase preparations, alkaline protease preparations, neutral protease preparations, acidic protease preparations, etc. is given as an example.

酵素剤による加水分解は、通常原料処理した醤油製造用
原料に必要に応じて水を加え、水および酵素の存在下で
基質が沈降しない程度の攪拌を行いつつ30〜乙O℃程
度で加水分解するというようにして実施する。この加水
分解工程における食塩濃度は0〜20%(、W/V )
が好ましく、無菌的に加水分解するか、比較的高温(I
AO−1j’c )で加水分解するのがよい。そして酵
素剤による醤油製造用原料の加水分解は糖及びアミノ酸
の溶出が殆んど終了するのに充分な時間、例えば10時
間〜約/ケ月間行うのが好ましい。
Hydrolysis using an enzyme agent is usually carried out by adding water as necessary to the raw material for soy sauce production that has been treated as a raw material, and hydrolyzing at 30 to 20°C while stirring to the extent that the substrate does not settle in the presence of water and enzymes. Implement it as follows. The salt concentration in this hydrolysis step is 0 to 20% (, W/V)
is preferably hydrolyzed aseptically or at a relatively high temperature (I
It is preferable to hydrolyze with AO-1j'c). The hydrolysis of the raw material for soy sauce production using an enzyme agent is preferably carried out for a sufficient period of time, for example, from 10 hours to about a month, until the elution of sugars and amino acids is almost completed.

また醤油製造用原料を醤油麹として加水分解する場合に
は、常法にしたがって醤油製造用原料を醤油麹とし、こ
れに水或いは食塩水を加え、上記酵素剤による方法にお
ける加水分解条件と同様な条件で加水分解を行う。
In addition, when the raw material for soy sauce production is hydrolyzed as soy sauce koji, the raw material for soy sauce production is converted into soy sauce koji according to a conventional method, water or brine is added thereto, and the hydrolysis conditions are the same as in the method using the enzyme agent described above. Hydrolysis is carried out under the following conditions.

一方、醤油製造用原料を化学的に加水分解する方法とし
ては、醤油製造用原料に常法により3〜10チ程度の塩
酸溶液を加え、約70℃以上に加熱、加水分解した後、
アルカリを加え核酸分解物を中和する方法が好適な例と
して挙げられる。
On the other hand, as a method for chemically hydrolyzing raw materials for soy sauce production, a hydrochloric acid solution of about 3 to 10 chlorides is added to the raw materials for soy sauce production in a conventional manner, and after being heated to about 70°C or higher and hydrolyzed,
A preferred example is a method in which alkali is added to neutralize the nucleic acid decomposition product.

次に上記醤油製造用原料を酵素的もしくは化学的に加水
分解したものは、そのままで、又は微生物の栄養源を加
えこれを乳酸発酵させるか、もしくは酸を加えてpH3
,0−701好ましくはpHlA3〜乙、Oに調製する
。乳酸発酵は、前記加水分解物のpHを必要によりよ夕
〜70に調整した後、これにペディオコッカス・ンーエ
エAM1673(ATCC13621)、同工AM15
81(ATCC13622)、ペディオコッカス・ノ・
ロフイルスエAM1693、同FERM−P煮1414
、テトラコツカス・ソーエFIRM−P扁1401.ス
トレプトコッカス・ファエカリス又はその培養液を添加
し、時々または連続して機械的に攪拌を行いながら嫌気
的条件下で2j〜3よ℃に保持して乳酸発酵させる。
Next, the raw materials for soy sauce production that have been enzymatically or chemically hydrolyzed can be used as they are, or by adding nutrients for microorganisms and carrying out lactic acid fermentation, or by adding acid to pH 3.
, 0-701, preferably adjusted to pH 1A3-O. In the lactic acid fermentation, after adjusting the pH of the hydrolyzate to 70 to 70 as necessary, this is mixed with Pediococcus neuea AM1673 (ATCC 13621) and Pediococcus AM15.
81 (ATCC 13622), Pediococcus no.
Rofilsue AM1693, same FERM-P boiled 1414
, Tetracoccus soae FIRM-Pbian 1401. Streptococcus faecalis or its culture solution is added and kept under anaerobic conditions at 2j to 3°C with occasional or continuous mechanical stirring to carry out lactic acid fermentation.

又前記乳酸発酵の代りに、醤油製造用原料を加水分解し
たものに乳酸、酢酸等の有機酸もしくは塩酸、硫酸等の
無機酸を加えてもよい。
Instead of the lactic acid fermentation, an organic acid such as lactic acid or acetic acid or an inorganic acid such as hydrochloric acid or sulfuric acid may be added to the hydrolyzed raw material for soy sauce production.

そして上記加水分解したものが分解残渣(固形分)を殆
んど、もしくは全く含まない液体の状態である場合はそ
のまま使用し、又、固形物を含有する場合には、該加水
分解物の調製の過程で或いは調製後に常法の圧搾、濾過
、遠心分離等の操作によシ固液分離して液汁基質を得る
If the above hydrolyzed product is in a liquid state containing little or no decomposition residue (solid content), use it as is, or if it contains solids, prepare the hydrolyzate. During or after preparation, solid-liquid separation is performed by conventional operations such as compression, filtration, and centrifugation to obtain a liquid substrate.

次に、発酵塔の担体に醤油製造用原料を酵素的もしくは
化学的に加水分解して得られた液を強制的に接触通過せ
しめる方法としては、先ず原料(液汁基質)の流入口及
び流出口を有し通液可能な発酵塔(例えばカラム)に担
体を詰め、該流入口を蓋体等で密閉し、この蓋体と流入
口とで形成される空間に醤油製造用原料を酵素的もしく
は化学的に加水分解して得られた液をポンプ等を用いて
醪が塔内で滞溜することなく速やかに浸透できるよう強
制的に送入し、塔内で加水分解液と担体とを醤油酵母菌
の発酵適温例えば20〜3J℃、特に27〜33℃に保
ち順次充分な接触を行わせ、次いで塔の流出口から排出
する。
Next, as a method of forcing the liquid obtained by enzymatically or chemically hydrolyzing the raw material for soy sauce production to pass through the carrier of the fermentation tower, first, the inlet and outlet of the raw material (sap substrate) are A fermentation tower (for example, a column) that has a structure and is capable of passing liquid is packed with carriers, the inlet is sealed with a lid, etc., and raw materials for soy sauce production are enzymatically or The liquid obtained by chemical hydrolysis is forcibly fed into the tower using a pump or the like so that the moromi quickly penetrates the tower without stagnation, and the hydrolyzed liquid and carrier are mixed into soy sauce in the tower. The yeast is maintained at an appropriate temperature for fermentation, for example, 20 to 3 J.degree. C., particularly 27 to 33.degree. C., for sufficient contact, and then discharged from the outlet of the tower.

ここで、上記加水分解液を強制的に送入することは重要
である。即ち本発明で用いる担体は水と非常に馴染み難
く、はつ水性が強くて該加水分解液に対して浸透抵抗を
有するため、強制的に送入しなければ該加水分解液を担
体内で望ましい速度で通過させることが困難である。ま
た酵母菌の担体への付着増殖には極く微量の酸素を必要
とするが、−五組体上に酵母菌を付着増殖せしめた後の
加水分解液と担体との接触には、酸素含有ガスの供給は
無くとも酵母菌は死滅することはない。従って、酸素含
有ガスの供給装置は設けなくともよい。加水分解液は発
酵塔内において適当な時間滞溜し、担体に付着した醤油
酵母菌と充分に接触して、アルコール発酵が行なわれ、
発酵塔の流出口から炭酸ガスの気泡が混入した加水分解
液が排出される。
Here, it is important to forcibly feed the hydrolyzate. That is, the carrier used in the present invention is very difficult to mix with water, has strong water repellency, and has penetration resistance to the hydrolyzed liquid, so it is desirable that the hydrolyzed liquid is not forced into the carrier unless it is forcibly introduced. Difficult to pass at speed. In addition, a very small amount of oxygen is required for yeast to adhere and grow on the carrier; Yeast bacteria will not die even if there is no gas supply. Therefore, there is no need to provide an oxygen-containing gas supply device. The hydrolyzed solution stays in the fermentation tower for an appropriate period of time, comes into sufficient contact with the soy sauce yeast bacteria attached to the carrier, and alcohol fermentation takes place.
Hydrolyzed liquid mixed with carbon dioxide gas bubbles is discharged from the outlet of the fermentation tower.

流出する加水分解液のうちアルコール発酵が適度に連子
しているものについては発酵塔から取シ出し、そのまま
或いは濾過した後調味液として用いてもよいが、必要に
応じさらに熟成させるか、適当に加工した後、通常の濾
過、成分の規格調製、火入殺菌及び重列等を行って香味
の優れた調味液製品とすることもできる。そして、発酵
塔へ、取出した分に相当する新たな加水分解液を流入す
る。
Of the hydrolyzed liquid that flows out, the one that has undergone alcoholic fermentation can be taken out of the fermentation tower and used as it is or after filtering and used as a seasoning liquid, but if necessary, it may be further aged or After processing, conventional filtration, standard preparation of ingredients, sterilization by fire, layering, etc. can be carried out to produce a seasoning liquid product with excellent flavor. Then, a new hydrolyzate corresponding to the amount taken out flows into the fermentation tower.

記と同様の処理を行って製品とする。The product is processed in the same manner as described above.

以上説明したことから明らかなように、本発明は従来全
く知られていない親油性繊維状担体に酵母菌を付着せし
め得られた担体を使用じ、これに醤油製造用原料を酵素
的もしくは化学的に加水分解し濾過して得られたものを
接触せしめるものであるから、極めて簡単に担体表面上
に酵母菌を付着増殖せしめ厚い菌膜層を形成して該担体
を詰めた発酵塔容積当りの菌濃度を高クシ、短期間に効
率良く調味液が得られる。また特に産膜性の酵母菌は親
油性繊維状担体に対して付着力が強く、また菌相互の凝
集力も強いので、更に効率良く調味液が得られる。また
担体に付着増殖した酵母菌は長期間連続的に使用しても
活性が安定で寿命が長い。また酵母菌を付着増殖せしめ
て得られた担体に対しては通気が不要なので通気のだめ
の設備費、運転費が軽減され、調味液の酸化褐変増殖と
風味の劣化が抑制されるので高品質の調味液が得られる
。また発酵液は比較的低塩分であるにも拘らず贋造しな
い。そして親油性繊維状担体の表面に形成された醤油酵
母菌の菌膜は水洗滌にょ如簡単に取り除くことができる
ので、担体の再生及び醤油酵母菌の種類を途中から任意
に変更することができる等産業上極めて有用な効果を奏
する。
As is clear from the above explanation, the present invention uses a carrier obtained by adhering yeast bacteria to a previously unknown lipophilic fibrous carrier, and then enzymatically or chemically enzymatically or chemically injects raw materials for soy sauce production onto this carrier. Since the product obtained by hydrolysis and filtration is brought into contact with the carrier, it is extremely easy to allow yeast to adhere and grow on the surface of the carrier, forming a thick bacterial film layer, and reducing the amount per volume of the fermentation tower packed with the carrier. With high bacteria concentration, seasoning liquid can be obtained efficiently in a short period of time. In addition, film-producing yeast bacteria in particular have a strong adhesive force to the lipophilic fibrous carrier, and also have a strong cohesive force between bacteria, so that a seasoning liquid can be obtained more efficiently. In addition, yeast bacteria that adhere to and proliferate on the carrier have stable activity and a long lifespan even when used continuously for a long period of time. In addition, since the carrier obtained by adhering and multiplying yeast bacteria does not require aeration, equipment costs and operating costs for aeration tanks are reduced, and oxidative browning and proliferation of seasoning liquids and flavor deterioration are suppressed, resulting in high quality. A seasoning liquid is obtained. Furthermore, although the fermented liquid has a relatively low salt content, it cannot be counterfeited. Since the soy sauce yeast bacterial film formed on the surface of the lipophilic fibrous carrier can be easily removed by washing with water, the carrier can be regenerated and the type of soy sauce yeast can be changed at any time. It has extremely useful effects in industry.

以下、実施例を示して本発明を更に詳細に説明する。Hereinafter, the present invention will be explained in more detail by showing examples.

実施例1 第1図において通液可能な発酵塔1を内径よcm。Example 1 In Fig. 1, the inner diameter of the fermentation tower 1 through which liquid can be passed is cm.

長さ23 cmの発酵塔とし、これに親油性繊維状担体
「三井・タフネル・オイルプロッター」約7゜?を詰め
、該発酵塔の試料導入口aを熱交換器2及び送液ポンプ
3を経て気液分離タンク4の液部に連通し、また発酵塔
1の試料排出口すを循環パイプ5を経て気液分離タンク
4に連通し、該気液分離タンクの頂壁に調圧弁(細長い
連通管)6を設け、更に液部に設けた測温体7を温度制
御装置8を介して前記熱交換器2と連絡し、第1図の如
くセットした。
A fermentation tower with a length of 23 cm was used, and a lipophilic fibrous carrier "Mitsui Tufnel Oil Plotter" was used at about 7°? The sample inlet a of the fermentation tower is connected to the liquid part of the gas-liquid separation tank 4 through the heat exchanger 2 and the liquid sending pump 3, and the sample outlet of the fermentation tower 1 is connected through the circulation pipe 5. It communicates with the gas-liquid separation tank 4, and a pressure regulating valve (elongated communication pipe) 6 is provided on the top wall of the gas-liquid separation tank, and a temperature measuring element 7 provided in the liquid part is connected to the temperature control device 8 for the heat exchange. Connect to device 2 and set it up as shown in Figure 1.

通常の濃口醤油の製造法に従って醤油諸法を調製し、仕
込後約/ケ月目に該諸法を圧搾し、諸法液汁(醤油製造
用原料を酵素的に加水分解して得られた液)(総窒素/
、 7 % 、食塩77%、グルコース7&%、アルコ
ール 口醤油諸法から分離して得られた産膜性の醤油酵母「サ
ツカロミセス・ルキシー」を酵母培養液体培地(グルコ
ース70%、食塩77%、酵母エキス/%)3tに接種
培養したものを第1図に示す気液分離タンク4に入れ、
送液ポンプ3にょシ2 0 rrtl 7分の流速で発
酵塔1に送液し、30℃にて担体表面に醤油酵母菌が付
着増殖するのに充分な期間2日、通液による接触を行い
、次いで前記培地を気液分離タンク及び発酵塔より抜き
取り、担体表面上に醤油酵母菌を充分に付着増殖せしめ
た。
Prepare soy sauce according to the usual method for producing dark soy sauce, squeeze the soy sauce about a month after brewing, and squeeze the soy sauce juice (liquid obtained by enzymatically hydrolyzing raw materials for soy sauce production). (total nitrogen/
, 7%, salt 77%, glucose 7&%, alcohol The film-producing soy sauce yeast "Satsucharomyces luxii" obtained by separating from various soy sauce methods was cultured in yeast culture liquid medium (glucose 70%, salt 77%, yeast Extract/%) 3t was inoculated and cultured and placed in the gas-liquid separation tank 4 shown in Figure 1.
The liquid was sent to the fermentation tower 1 at a flow rate of 7 minutes using the liquid pump 3, and contact was carried out by passing the liquid at 30°C for 2 days, which was sufficient for the soy sauce yeast to adhere to and proliferate on the surface of the carrier. Then, the medium was taken out from the gas-liquid separation tank and the fermentation tower, and soy sauce yeast was allowed to adhere and proliferate sufficiently on the surface of the carrier.

次いで、抜き取った培地の代シに、前記諸法液汁jtを
気液分離タンクに投入し、20ml1分の流速で発酵塔
へ送液し、気液分離タンク−熱交換器−発酵塔の間を繰
り返し循環させ、担体と接触させた。
Next, in place of the removed culture medium, the various method liquid juice jt was put into the gas-liquid separation tank, and the liquid was sent to the fermentation tower at a flow rate of 20 ml per minute, and the liquid was passed between the gas-liquid separation tank, the heat exchanger, and the fermentation tower. It was repeatedly circulated and contacted with the carrier.

その結果、約20日後に1色沢が縦属で香りの優れた醤
油(アルコール、2.4%、グルコース2.タチ)が得
られた。
As a result, after about 20 days, a soy sauce (alcohol, 2.4%, glucose 2.4%) with a 1 color gloss and an excellent aroma was obtained.

また比較のため、諸法液汁!tを攪拌機付タンクに入れ
30℃に加温し、実施例と同一の醤油酵母菌を70個/
 rrtlとなるように接種した後酵母菌が沈澱しない
程度にゆるやかに攪拌しつつ20日間発酵させ、成分を
分析したところ、アルコール0、 A j % 、グル
コース乙チで醤油様の香気が乏しい調味液が得られた。
Also, for comparison, various law juice! t was placed in a tank equipped with a stirrer and heated to 30°C, and 70 soy sauce yeast bacteria identical to those in the example were added.
After inoculating the yeast so that the yeast would not precipitate, it was fermented for 20 days with gentle stirring to prevent the yeast from precipitating. When the ingredients were analyzed, it was found to be a seasoning liquid with 0 alcohol, A j %, glucose ochi, and a lack of soy sauce-like aroma. was gotten.

実施例2 第1図において、発酵塔を内匝.2乙園、長さ7mの温
水通流可能なジャケット付きのカラムとし、その内部に
親油性繊維状担体「ウオセップ」(東し社製)701を
詰め、ジャケット内に30℃の温水を通流し、気液分離
タンク内は醤油酵母菌による発酵を防止するため該タン
クを70℃に冷却護持して第1図の如くセットした。
Example 2 In FIG. 1, the fermentation tower is placed in an inner container. 2 Otsuen: A 7 m long column with a jacket through which hot water can flow, the inside of which is filled with lipophilic fibrous carrier "Wosep" (manufactured by Toshisha Co., Ltd.) 701, and 30°C hot water is passed through the jacket. The inside of the gas-liquid separation tank was cooled and maintained at 70° C. to prevent fermentation by soy sauce yeast, and the tank was set as shown in FIG. 1.

醤油麹≠Kp及び蒸煮脱脂大豆(原料脱脂大豆で3 K
y )を塩水(食塩量5soBに仕込み、攪拌しながら
ti−o−t1ts℃に50時間保ち、圧搾して醤油麹
の減塩高温消化液(総窒素、2.≠チ、食塩7弼、糖分
1〕)を得、これは濃すぎるので食塩水を加え、低塩分
の消化液(総窒素2.0%、食塩量2g%、糖分乙、!
r%)を調製した。
Soy sauce koji≠Kp and steamed defatted soybeans (3K for raw defatted soybeans)
y) was prepared with salt water (salt amount: 5 soB, kept at ti-o-t1ts℃ for 50 hours while stirring, and squeezed to obtain a low-salt, high-temperature digestive liquid of soy sauce koji (total nitrogen, 2. 1]) was too concentrated, so I added saline and added low-salt digestive fluid (total nitrogen 2.0%, salt content 2g%, sugar content B,!).
r%) was prepared.

次に、実施例1と全く同様にして親油性繊維状担体「ウ
オセツプ」に産膜性の醤油酵母菌「サツカロミセス・ル
ーキシ」を充分付着増殖せしめた。
Next, in exactly the same manner as in Example 1, a film-producing soy sauce yeast strain, ``Saccharomyces rukisi,'' was allowed to adhere and proliferate sufficiently on the lipophilic fibrous carrier ``Uosep''.

次いで、前記低塩分の消化液jtを気液分離タンクに入
れ、途中熱交換器で30℃に加温した後流速70m1/
分で発酵塔に送液し、循環させ、担体と接触させた。
Next, the low-salt digestive fluid jt was put into a gas-liquid separation tank, heated to 30°C with a heat exchanger, and then heated at a flow rate of 70ml/
The solution was pumped into the fermentation tower within minutes, circulated, and brought into contact with the carrier.

その結果、10日後に発酵は終了し、色沢が縦属で香)
の優れた醤油様調味液(グルコース2.2慢、アルコー
ル2.3チ)を得た。
As a result, fermentation was completed after 10 days, and the color was vertical and fragrant).
An excellent soy sauce-like seasoning liquid (glucose: 2.2%, alcohol: 2.3%) was obtained.

尚、比較のため、前記の醤油麹の減塩高温消化液よOl
を攪拌機付タンクに入れ、30℃に加温し、本実施例と
同一の醤油酵母菌を10個/mlとなるように接種した
後、酵母菌が沈澱しない程度にゆ“るやかに攪拌しつつ
70日間発酵熟成させたところ、得られた調味液は、醤
油様香気及びアルコールの生成がなかった。
For comparison, the above-mentioned low-salt high-temperature digestive liquid of soy sauce koji
was placed in a tank equipped with a stirrer, heated to 30°C, and inoculated with the same soy sauce yeast as in this example at a concentration of 10 cells/ml, then stirred gently to prevent the yeast from settling. When fermented and aged for 70 days, the resulting seasoning liquid had no soy sauce-like aroma and no alcohol production.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の調味液の製造法に使用する装置の/具
体例を示す概略説明図である。 1・・・発酵塔、2・・・熱交換器、4・・・気液分離
タンク
FIG. 1 is a schematic explanatory diagram showing a specific example of an apparatus used in the seasoning liquid manufacturing method of the present invention. 1... Fermentation tower, 2... Heat exchanger, 4... Gas-liquid separation tank

Claims (4)

【特許請求の範囲】[Claims] (1)親油性繊維状担体を通液可能な発酵塔内に詰め、
該担体に酵母菌を付着せしめ、これに醤油製造用原料を
酵素的もしくは化学的に加水分解して得られた液を接触
通過せしめることを特徴とする調味液の製造法。
(1) Packing the lipophilic fibrous carrier into a fermentation tower that allows liquid to flow through it,
A method for producing a seasoning liquid, which comprises attaching yeast bacteria to the carrier, and allowing a liquid obtained by enzymatically or chemically hydrolyzing a raw material for soy sauce production to pass through the carrier.
(2)酵母菌が醤油酵母菌である特許請求の範囲第1項
記載の調味液の製造法。
(2) The method for producing a seasoning liquid according to claim 1, wherein the yeast is a soy sauce yeast.
(3)酵母菌が産膜性醤油酵母菌である特許請求の範囲
第1項又は第2項記載の調味液の製造法。
(3) The method for producing a seasoning liquid according to claim 1 or 2, wherein the yeast is a film-producing soy sauce yeast.
(4)通気することなく接触通過せしめる特許請求の範
囲第1項記載の調味液の製造法。
(4) The method for producing a seasoning liquid according to claim 1, wherein the seasoning liquid is allowed to pass through contact without aeration.
JP59188852A 1984-09-11 1984-09-11 Production of seasoning solution Pending JPS6167459A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59188852A JPS6167459A (en) 1984-09-11 1984-09-11 Production of seasoning solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59188852A JPS6167459A (en) 1984-09-11 1984-09-11 Production of seasoning solution

Publications (1)

Publication Number Publication Date
JPS6167459A true JPS6167459A (en) 1986-04-07

Family

ID=16230966

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59188852A Pending JPS6167459A (en) 1984-09-11 1984-09-11 Production of seasoning solution

Country Status (1)

Country Link
JP (1) JPS6167459A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62278965A (en) * 1986-05-28 1987-12-03 Higeta Shoyu Kk Method for improving raw soy sauce having low quality
JPS633775A (en) * 1986-06-24 1988-01-08 Kikkoman Corp Preparation of seasoning
CN104256513A (en) * 2014-10-23 2015-01-07 哈尔滨派特纳生物科技开发有限公司 Method for producing soy sauce by fermenting brewer grains

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62278965A (en) * 1986-05-28 1987-12-03 Higeta Shoyu Kk Method for improving raw soy sauce having low quality
JPH0522500B2 (en) * 1986-05-28 1993-03-29 Higeta Shoyu Kk
JPS633775A (en) * 1986-06-24 1988-01-08 Kikkoman Corp Preparation of seasoning
CN104256513A (en) * 2014-10-23 2015-01-07 哈尔滨派特纳生物科技开发有限公司 Method for producing soy sauce by fermenting brewer grains

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