JPH0716379B2 - Soy sauce fermentation equipment - Google Patents

Soy sauce fermentation equipment

Info

Publication number
JPH0716379B2
JPH0716379B2 JP62252272A JP25227287A JPH0716379B2 JP H0716379 B2 JPH0716379 B2 JP H0716379B2 JP 62252272 A JP62252272 A JP 62252272A JP 25227287 A JP25227287 A JP 25227287A JP H0716379 B2 JPH0716379 B2 JP H0716379B2
Authority
JP
Japan
Prior art keywords
fermentation
soy sauce
fermenter
immobilized
carrier
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.)
Expired - Lifetime
Application number
JP62252272A
Other languages
Japanese (ja)
Other versions
JPH0195742A (en
Inventor
紘志 若園
義明 柴田
忠彦 犬飼
宏 伊丹
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.)
Nippon Sharyo Ltd
Kirin Brewery Co Ltd
Original Assignee
Nippon Sharyo Ltd
Kirin Brewery 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 Nippon Sharyo Ltd, Kirin Brewery Co Ltd filed Critical Nippon Sharyo Ltd
Priority to JP62252272A priority Critical patent/JPH0716379B2/en
Publication of JPH0195742A publication Critical patent/JPH0195742A/en
Publication of JPH0716379B2 publication Critical patent/JPH0716379B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は醤油の製造装置に係わり、特に固定化菌体を用
いた発酵装置に関するものである。
TECHNICAL FIELD The present invention relates to a soy sauce production apparatus, and more particularly to a fermentation apparatus using immobilized bacterial cells.

〔従来の技術〕[Conventional technology]

従来、醤油の製造は、脱脂大豆を吸水させて加圧下で蒸
し、小麦を煎って割砕したものと混合し、これに種麹を
散布して麹菌を培養したものを塩水中に仕込んで諸味と
し、これを約6ケ月間発酵熟成させた後に圧搾濾過し、
この汁液を分離して火入れとオリ引きを行ない製品とし
ているが、製品とするまでに長い期間が必要であり、短
期間で製造できる方法及び装置の開発が望まれていた。
Conventionally, soy sauce is manufactured by absorbing defatted soybeans, steaming them under pressure, mixing them with roasted and crushed wheat, sprinkling seed koji and cultivating the koji mold into salt water, and adding them to various flavors. And fermented and aged for about 6 months, then press-filtered,
Although this juice is separated into a product that is fired and pulled, it takes a long period of time to obtain a product, and it has been desired to develop a method and an apparatus that can be manufactured in a short period of time.

近年醤油酵母を担体に固定化した固定化菌体を用いた発
酵装置により醤油を短期間に製造する方法が提案され、
実用化に向けて研究が進められており、本出願人は、こ
の要望に応え、先に醤油を短期間に製造する装置を開発
した(特願昭61−235157号)。
In recent years, a method of producing soy sauce in a short period of time by a fermentation apparatus using immobilized cells in which soy sauce yeast is immobilized on a carrier has been proposed,
Research is progressing toward practical application, and the applicant of the present invention has responded to this request and previously developed a device for producing soy sauce in a short period of time (Japanese Patent Application No. 61-235157).

この装置は、醤油製造用原料を酵素的に加水分解すると
ともに乳酸発酵を行なって圧搾,濾過した汁液(以下基
質という)を、アルコール発酵用酵母を担体に固定化し
た固定化菌体を用いた発酵装置と、醤油香気成分を生成
させる後熟発酵用酵母を担体に固定化した固定化菌体を
用いた発酵装置とを備えて順次連続的に発酵させるもの
である。
This device uses immobilized cells in which a juice (hereinafter referred to as a substrate) obtained by enzymatically hydrolyzing a raw material for producing soy sauce, lactic acid fermentation, pressing, and filtering (hereinafter referred to as a substrate) is immobilized on a carrier for yeast for alcohol fermentation. A fermentor and a fermentor using immobilized cells in which a yeast for post-ripening fermentation for producing a soy sauce aroma component is immobilized on a carrier are used to successively and sequentially ferment.

上記発酵装置は、通常第5図に示す如きもので、発酵槽
1内にドラフトチューブ2を配設し、発酵槽1底部の通
気口3から少量の空気を供給し、固定化菌体4をエアリ
フト効果によってドラフトチューブ2の内側から上昇さ
せ、これをまたドラフトチューブ3の下端から流入する
ように循環させ、基質5と十分に接触させて発酵させる
ようにしている。尚、6は蓋7に設けた基質5の供給
口、8は発酵液の取出口である。
The above-mentioned fermentation apparatus is usually one as shown in FIG. 5, in which the draft tube 2 is arranged in the fermenter 1 and a small amount of air is supplied from the vent 3 at the bottom of the fermenter 1 to remove the immobilized bacterial cells 4. The air is lifted from the inside of the draft tube 2 by the airlift effect, and this is circulated so as to flow from the lower end of the draft tube 3 as well so that it is sufficiently contacted with the substrate 5 to ferment it. In addition, 6 is a supply port of the substrate 5 provided in the lid 7, and 8 is an outlet for the fermentation liquid.

このような装置に用いられる固定化菌体の担体として
は、基質内に適度に分散するように基質と同程度の比重
であって、かつ菌体の固定化が容易なものが求められて
おり、アルギン酸やカッパカラギナン等の天然物,光硬
化性樹脂等の合成高分子,活性炭等種々のものが検討さ
れている。
As a carrier for immobilized cells used in such a device, a carrier having a specific gravity similar to that of the substrate so as to be appropriately dispersed in the substrate and capable of easily immobilizing the cells is required. Various substances such as natural products such as alginic acid and kappa carrageenan, synthetic polymers such as photocurable resins, and activated carbon have been investigated.

また菌体の担体への固定化は、包括法等により発酵槽外
で行なっていた。
Further, the immobilization of the cells on the carrier has been carried out outside the fermenter by the inclusion method or the like.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかしながら、担体は、発酵中に発酵槽内を流動するた
め、流動中に担体同士または発酵槽側壁との接触や衝突
により摩耗したり破損することがあり、担体の寿命が短
いという欠点がある。
However, since the carrier flows in the fermenter during fermentation, it may be worn or damaged due to contact or collision between the carriers or the side wall of the fermentor during the flow, which has a drawback that the life of the carrier is short.

また包括法によって菌体を担体に固定化するものでは、
固定化する作業が煩雑であり、しかも発酵槽の外部で行
なうため、雑菌の浸入を完全に防止することが困難であ
った。
In addition, in the method of immobilizing bacterial cells on a carrier by the inclusion method,
It is difficult to completely prevent invasion of miscellaneous bacteria because the immobilization work is complicated and is performed outside the fermenter.

そこで本発明は、雑菌を浸入させることなく簡便に菌体
を担体に固定化でき、しかも固定化菌体の摩耗や破損が
なく、長期間連続的に安定した効率のよい発酵ができる
醤油の発酵装置を提供することを目的としている。
Therefore, the present invention is a fermentation of soy sauce that can easily immobilize the bacterial cells on the carrier without invading miscellaneous bacteria, and does not cause wear or damage of the immobilized bacterial cells, and can perform stable fermentation efficiently for a long period of time. The purpose is to provide a device.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、上記の目的を達成するために、発酵処理後の
発酵液を取出す流出口を上部に設けた発酵槽内に、高多
孔性粒状泡ガラスの担体に醤油酵母を固定化させた固定
化菌体を充填するとともに、発酵槽の下部に醤油発酵原
液を供給する供給口と、発酵中に生成する生成気体を排
気するため、0.01乃至0.04vvm(vvmは、1分間当たりの
発酵槽容積()に対する空気量()の空気を送通す
る空気供給口を設けたことを特徴とする。
The present invention, in order to achieve the above object, in a fermenter provided with an outlet at the top for taking out the fermented liquid after the fermentation treatment, the soy sauce yeast is immobilized on a carrier of highly porous granular glass, which is fixed. 0.01 to 0.04 vvm (vvm is the volume of the fermenter per minute, because the soy sauce fermentation stock solution is supplied to the bottom of the fermenter and the generated gas generated during fermentation is exhausted while filling the microbial cells. It is characterized in that an air supply port is provided through which the air of the amount () for () is communicated.

〔作 用〕[Work]

従って、発酵槽の下部から供給された醤油発酵原液は、
充填された固定化菌体を流動させることなく、固定化菌
体と順次接触して発酵濃度を高めながら次第に上部の流
出口へ流動し、所定時間滞留すると所望の濃度の発酵液
となって流出口から取出されるので、固定化菌体の摩耗
あるいは破損を少なくすることができる。
Therefore, the soy sauce fermentation stock solution supplied from the bottom of the fermentor is
Without flowing the immobilized cells that have been filled, gradually contact the immobilized cells to increase the fermentation concentration and gradually flow to the upper outlet, and after a certain period of time, a fermentation solution of the desired concentration flows. Since it is taken out from the outlet, it is possible to reduce the abrasion or damage of the immobilized cells.

さらに、発酵槽に空気供給口から少量の空気を送通する
ことにより、発酵中に生成する生成気体を槽外へ排出で
き、かつ醤油酵母の活性を持続させることができる。
Furthermore, by sending a small amount of air to the fermentation tank from the air supply port, the product gas generated during fermentation can be discharged to the outside of the tank, and the activity of soy sauce yeast can be maintained.

〔実施例〕〔Example〕

次に本発明の一実施例を第1図を参照しながら説明す
る。
Next, an embodiment of the present invention will be described with reference to FIG.

発酵槽11の底部には、醤油発酵原液である基質12を供給
する基質管13と蒸気を送給する蒸気管14とを三方弁15を
介して配管した供給口16と、空気管17を介して空気を発
酵槽11内へ送通する空気供給口18とが設けられている。
At the bottom of the fermenter 11, a substrate pipe 13 for supplying a substrate 12 that is a soy sauce fermentation stock solution, and a supply port 16 in which a steam pipe 14 for supplying steam is piped through a three-way valve 15, and an air pipe 17. And an air supply port 18 for communicating air into the fermenter 11.

また発酵槽11の側壁上部には、発酵後の発酵液を取出す
流出口19が設けられ、発酵槽11上部の蓋20には、排気口
21が設けられている。
Further, an outlet 19 for taking out the fermented liquid after fermentation is provided at the upper part of the side wall of the fermenter 11, and an exhaust port is provided at a lid 20 on the upper part of the fermenter 11.
21 are provided.

そして発酵槽11内には、高多孔性粒状泡ガラスからなる
担体に菌体を固定化した固定化菌体22が充填されてい
る。
The fermenter 11 is filled with immobilized bacterial cells 22 in which bacterial cells are immobilized on a carrier made of highly porous granular foam glass.

上記担体として用いられる高多孔性粒状泡ガラスは、直
径2〜5mmの粒状で同径の多孔質のものであり、例えば
化学組成は酸化ケイ素(SiO2)を主成分(69.0%)と
し、これに酸化アルミニウム(Al2O3),酸化カルシウ
ム(CaO),酸化マグネシウム(MgO),酸化ナトリウム
(Na2O),その他微量成分等を含んだものであり、物性
は、見掛け比重が0.3〜0.7,細孔容積が1.0〜3.5ml/g,中
央細孔径(V)が5.0〜25.0μm,吸水率が75〜80%であ
る。
The highly porous granular foam glass used as the carrier is granular and has a diameter of 2 to 5 mm, and has the same diameter. For example, the chemical composition is silicon oxide (SiO 2 ) as a main component (69.0%). Contains aluminum oxide (Al 2 O 3 ), calcium oxide (CaO), magnesium oxide (MgO), sodium oxide (Na 2 O), and other trace components, and its physical properties have an apparent specific gravity of 0.3 to 0.7. The pore volume is 1.0 to 3.5 ml / g, the median pore diameter (V) is 5.0 to 25.0 μm, and the water absorption is 75 to 80%.

また一般に充填槽においては、菌体の生育する表面積を
大きくするために、できるだけ小径(1.0mm以下)の担
体が用いられているが、醤油の発酵においては、オリや
発酵による生成ガス等が担体の表面を覆い易く、いわゆ
るチャネリング現象を生じるため好ましくない。どの程
度の大きさにするかは、醤油原料の種類や発酵槽の大き
さ等によって定めなくてはならないが、多くの実験の結
果によれば、前述のごとく直径が2〜5mmのものが好ま
しい。
In addition, in a filling tank, generally, a carrier with a diameter as small as possible (1.0 mm or less) is used in order to increase the surface area on which cells grow. It is not preferable because it easily covers the surface and causes a so-called channeling phenomenon. The size of the soy sauce must be determined depending on the type of soy sauce raw material, the size of the fermentation tank, etc., but according to the results of many experiments, it is preferable that the diameter is 2 to 5 mm as described above. .

菌体は、チゴサッカロミセスルキシ(Zygo Saccharo my
ces rouxii)等の醤油酵母であり、また醤油香気成分を
生成させる後熟用の発酵槽の場合には、カンディダバー
サチィルス(Candida versatilus)等の酵母で、いずれ
も一般的に用いられているものを使用することができ
る。
Bacteria are Zygo Saccharo myx
ces rouxii) and so on, and in the case of a post-ripening fermenter that produces soy sauce aroma components, yeasts such as Candida versatilus are commonly used. Things can be used.

次に上記のように構成した装置の使用法を述べる。Next, a method of using the device configured as described above will be described.

まず発酵槽11内に上記高多孔性粒状泡ガラスからなる担
体を充填する。次に三方弁15を操作して蒸気管14より蒸
気を発酵槽11内へ導入し、発酵槽11内及び担体の殺菌を
行なう。そして別途培養した醤油酵母を、基質管13を利
用して供給口16から発酵槽11内へ供給する。供給された
醤油酵母は、担体の高多孔性粒状泡ガラス内に入り込み
固定化されて固定化菌体22となる。
First, the fermenter 11 is filled with the carrier made of the highly porous granular foam glass. Next, the three-way valve 15 is operated to introduce steam from the steam pipe 14 into the fermentation tank 11 to sterilize the inside of the fermentation tank 11 and the carrier. Then, the separately cultivated soy sauce yeast is supplied from the supply port 16 into the fermenter 11 using the substrate tube 13. The supplied soy sauce yeast enters the highly porous granular foam glass of the carrier and is immobilized, and becomes immobilized cells 22.

以上の作業の後、所定量の基質12を基質管13から連続的
に供給する。基質12は、供給口16から発酵槽11内へ供給
されて固定化菌体22と次々に接触して発酵し、発酵濃度
を高めながら次第に上方へ移動し、所定濃度の発酵液と
なって流出口19から溢出し、発酵液槽等(図示せず)に
貯留される。
After the above work, a predetermined amount of the substrate 12 is continuously supplied from the substrate tube 13. The substrate 12 is supplied from the supply port 16 into the fermenter 11 and sequentially fermented by contacting the immobilized bacterial cells 22, gradually moving upward while increasing the fermentation concentration, and flowing as a fermentation liquid of a predetermined concentration. It overflows from the outlet 19 and is stored in a fermented liquid tank or the like (not shown).

担体内の醤油酵母は、常に所定量が存在し、基質12から
養分を摂取して繁殖し、発酵,増殖を行なっているが、
一部は担体から離れて基質中にも浮遊し、発酵を促進さ
せて増殖しながら発酵液に混入して流出する。
The soy sauce yeast in the carrier is always present in a predetermined amount and ingests nutrients from the substrate 12 to reproduce, ferment and proliferate.
A part of it separates from the carrier and also floats in the substrate, promotes fermentation and proliferates, mixes with the fermentation liquor and flows out.

一方発酵が進むにつれ、二酸化炭素等の生成気体が発酵
槽11内に溜るために基質12が泡状になり、基質12と固定
化菌体22との接触が阻害される。これを防止するため、
空気管17を介して空気供給口18から0.01〜0.04vvm(vvm
は、1分間当たりの発酵槽容積()対する空気量
()程度の少量の空気を発酵槽11内へ送通する。この
空気は、生成気体を上方へ誘導して排気口21から排出さ
せるとともに、醤油酵母の活性を高める働きをするもの
で、空気量が少な過ぎると生成ガスの除去を効率的に行
うことができず、また多過ぎると醤油酵母の発酵を阻害
する。実験によれば0.02vvm程度で好ましい結果が得ら
れた。
On the other hand, as the fermentation progresses, the produced gas such as carbon dioxide accumulates in the fermenter 11, so that the substrate 12 becomes foamy and the contact between the substrate 12 and the immobilized microbial cells 22 is inhibited. To prevent this,
0.01 to 0.04 vvm (vvm
Sends a small amount of air (about the amount of air () to the fermenter volume () per minute) into the fermenter 11. This air serves to guide the generated gas upward to be discharged from the exhaust port 21 and to increase the activity of the soy sauce yeast, and when the amount of air is too small, the generated gas can be efficiently removed. No, and too much inhibits the fermentation of soy sauce yeast. According to the experiment, a favorable result was obtained at about 0.02 vvm.

また本装置を長期間に亘って運転した場合には、発酵槽
11内にオリや死菌が生じて固定化菌体間に付着したり、
場合により雑菌が繁殖したりして発酵が阻害されること
がある。このような場合には、基質12を供給口16から逆
流させて槽外へ取り出した後、蒸気管14を介して発酵槽
11内へ蒸気を導入し殺菌及びオリ等の除去を行なう。
In addition, if the equipment is operated for a long period of time,
Ori and dead bacteria occur in 11 and adhere between immobilized cells,
In some cases, bacteria may be propagated and fermentation may be inhibited. In such a case, after the substrate 12 is allowed to flow backward from the supply port 16 and taken out of the tank, the fermentation tank is passed through the steam pipe 14.
Introduce steam into 11 to sterilize and remove dirt.

尚、排気口21は、発酵槽11に設けずに、発酵液を貯留す
る発酵液槽の上部等に設けることもでき、生成気体を流
出口19から発酵液とともに流出させた後に発酵液槽から
排出させてもよい。また空気供給口22は、供給口16と共
用することも可能である。
The exhaust port 21 may be provided in the upper part of the fermentation liquid tank for storing the fermentation liquid without providing it in the fermentation tank 11, and from the fermentation liquid tank after the generated gas is caused to flow out together with the fermentation liquid from the outlet 19. It may be discharged. Further, the air supply port 22 can be shared with the supply port 16.

さらに醤油発酵原液として基質を用いて説明したが、こ
れに限るものではなく、醤油製造用原料を酵素的または
化学的に加水分解したものを乳酸菌を固定化した固定化
菌体を用いて乳酸発酵処理した醤油発酵原液を用いても
よい。
Further, the substrate was used as the soy sauce fermentation stock solution, but the present invention is not limited to this, and the lactic acid fermentation is performed by using immobilized cells in which lactic acid bacteria are immobilized by enzymatically or chemically hydrolyzing the raw material for producing soy sauce. You may use the processed soy sauce fermentation stock solution.

本発明者等は本発明装置の有効性について多大な実験を
行なって確認したが、その一部を以下に示す。
The present inventors have confirmed the effectiveness of the device of the present invention through a large amount of experiments, some of which are shown below.

実験例1 上述のごとく形成され、直径/高さ比が1/3で全容量5
の発酵槽に、固定化菌体の担体として、見掛け比重0.
35,細孔容積2.2ml/g,中央細孔径(V)15.0μm,吸水率
0.80,圧縮強度2,68kg/cm2の物性を有する直径4mmの高多
孔性粒状泡ガラス(主化学組成は酸化ケイ素69.0%で、
これに酸化アルミニウム,酸化カルシウム,酸化マグネ
シウム,その他微量成分を含む)を見かけ容量で3充
填し、醤油酵母として培養したチゴサッカロミセスルキ
シを槽内に供給して固定化した。
Experimental Example 1 Formed as described above, with a diameter / height ratio of 1/3 and a total volume of 5
As a carrier for immobilized cells, the apparent specific gravity of the fermentor was 0.
35, pore volume 2.2ml / g, central pore size (V) 15.0μm, water absorption
0.80, Compressive strength 2,68 kg / cm 2 Highly porous granular foam glass with a diameter of 4 mm (main chemical composition is 69.0% silicon oxide,
Aluminum oxide, calcium oxide, magnesium oxide, and other trace components) were apparently filled in this to 3 volumes, and Tigosaccharomyces ruxii cultivated as soy sauce yeast was supplied into the tank and immobilized.

基質を発酵槽の供給口から連続して供給するとともに空
気供給口から0.02vvmの空気を送通し、基質の供給量を
変化させることにより、発酵槽内での滞留時間を変化さ
せ、アルコール生成量及び流出口からの漏出菌体量等を
調べた。
The substrate is continuously supplied from the fermenter supply port and 0.02 vvm air is sent from the air supply port to change the substrate supply amount to change the residence time in the fermenter and the alcohol production amount. Also, the amount of cells leaked from the outlet was examined.

その結果、第2図に示すように、アルコールの生成量
は、滞留時間によりかなり変動するが、36日目から滞留
時間を14時間に固定したら、1.8〜1.9g/dlに安定した。
As a result, as shown in FIG. 2, the amount of alcohol produced varied considerably depending on the residence time, but when the residence time was fixed to 14 hours from the 36th day, it was stabilized at 1.8 to 1.9 g / dl.

また発酵液への漏出菌体は1×106〜1×108Cells/mlで
あり、アルコール生成量が多くなるにつれて漏出菌体も
増加する傾向にある。
The number of cells leaking into the fermentation liquor is 1 × 10 6 to 1 × 10 8 cells / ml, and the number of cells leaking out tends to increase as the amount of alcohol produced increases.

第3図は、滞留時間とアルコール生成量との関係を示す
もので、20時間以上では、略一定の生成量であり、14時
間がピークであった。
FIG. 3 shows the relationship between the residence time and the amount of alcohol produced. At 20 hours or more, the amount of alcohol produced was almost constant, with a peak of 14 hours.

実験例2 実験例1で得た所定濃度の発酵液を、クロスコンタミ防
止処理として熱交換器で65℃にて1時間加熱処理した
後、後熟発酵の発酵槽へ供給した。
Experimental Example 2 The fermentation broth having a predetermined concentration obtained in Experimental Example 1 was heat-treated at 65 ° C. for 1 hour in a heat exchanger as a cross-contamination-preventing treatment, and then fed to a fermentation tank for post-ripening fermentation.

この後熟発酵に用いた発酵槽及び固定化菌体の担体は、
前記実験例1で使用したものと同様のものを用いた。
The fermenter used for this post-ripening fermentation and the carrier of the immobilized cells are:
The same one as that used in Experimental Example 1 was used.

後熟発酵用酵母としては、カンディダバーサチィルスを
用いた。また発酵液の滞留時間は14時間とし、槽底部か
らの空気の供給量は、0.02VVMとした。
Candida versatiles was used as the yeast for post-ripening fermentation. The retention time of the fermented liquor was 14 hours, and the amount of air supplied from the bottom of the tank was 0.02 VVM.

第4図に示すように、醤油の香気成分である4EG(4−e
thylguaiacol,CH3OC6H3(C2H5)OH)及び2PE(2−phen
ylethanol,C6H5CH2CH2OH)は、60日間に亘って前者が4
〜6ppm、後者が10〜17ppmと安定して生成され、官能試
験をしたところ香りにまろやかさがあり、香味も優れて
いた。
As shown in Fig. 4, 4EG (4-e, which is the aroma component of soy sauce)
thylguaiacol, CH 3 OC 6 H 3 (C 2 H 5 ) OH) and 2PE (2-phen
ylethanol, C 6 H 5 CH 2 CH 2 OH) is the former 4 for 60 days.
〜6ppm, the latter was stably produced at 10〜17ppm, and the sensory test showed that the fragrance was mellow and the flavor was excellent.

尚、上記両実験例において発酵槽に供給する液は、供給
前に加熱殺菌したものを用い、発酵槽内も前述のとおり
菌体の固定化前に蒸気殺菌を行なったので、雑菌による
汚染は全くなかった。
Incidentally, the liquid to be supplied to the fermenter in both of the above-described experimental examples was used after being heat-sterilized before supply, and since steam sterilization was performed before immobilization of the bacterial cells in the fermenter as described above, contamination by miscellaneous bacteria was prevented. There was no.

また槽底部から空気を供給しない場合は、発酵運転20日
目頃から酵母の活性が徐々に低下するが、空気を送通す
れば酵母の活性が回復し、発酵を継続させることができ
る。このように空気を間欠的に発酵槽に送通してもよい
が、連続して送通した方が安定した発酵を行うことがで
きる。
When the air is not supplied from the bottom of the tank, the yeast activity gradually decreases from about the 20th day of the fermentation operation, but if the air is passed, the yeast activity is restored and the fermentation can be continued. As described above, the air may be intermittently sent to the fermenter, but if it is continuously sent, stable fermentation can be performed.

〔発明の効果〕〔The invention's effect〕

以上説明したように本発明は、発酵槽内に高多孔性粒状
泡ガラスを担体とした固定化菌体を充填したので、発酵
中に固定化菌体が接触や衝突を起こすことがなく、摩滅
や損傷することがないので長期間に亘って使用すること
ができる。また醤油酵母等の単体への固定化も発酵槽内
で簡便にしかも無菌の状態で行うことができる。さらに
発酵槽底部から少量の空気を送通するようにしたので、
発酵中の生成気体を簡便に槽外へ排出できるとともに、
醤油酵母の活性を維持でき、極めて良好かつ均質な発酵
を行なうことができる。
As described above, according to the present invention, since the immobilized bacterial cells having the highly porous granular foam glass as a carrier are filled in the fermenter, the immobilized bacterial cells do not cause contact or collision during fermentation and are worn away. Since it is not damaged, it can be used for a long period of time. Further, immobilization of soy sauce yeast or the like on a simple substance can be carried out easily and aseptically in the fermenter. Furthermore, since a small amount of air was sent from the bottom of the fermentation tank,
The generated gas during fermentation can be easily discharged out of the tank,
The activity of soy sauce yeast can be maintained, and extremely good and homogeneous fermentation can be performed.

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

第1図は本発明装置の一実施例を示す断面概観図、第2
図乃至第4図は本発明装置によって実験した結果を示す
図、第5図は従来装置の一例を示す断面概略図である。 11……発酵槽、12……基質、13……基質管、14……蒸気
管、15……三方弁、16……供給口、17……空気管、18…
…空気供給口、19……流出口、20……蓋、21……排気
口、22……固定化菌体
FIG. 1 is a schematic sectional view showing an embodiment of the device of the present invention, and FIG.
FIG. 4 to FIG. 4 are diagrams showing the results of experiments conducted by the device of the present invention, and FIG. 11 …… Fermenter, 12 …… Substrate, 13 …… Substrate tube, 14 …… Steam tube, 15 …… Three-way valve, 16 …… Supply port, 17 …… Air tube, 18…
… Air supply port, 19… Outflow port, 20… Lid, 21… Exhaust port, 22… Immobilized bacteria

───────────────────────────────────────────────────── フロントページの続き (72)発明者 若園 紘志 愛知県名古屋市熱田区三本松町1番1号 日本車輛製造株式会社内 (72)発明者 柴田 義明 愛知県宝飯郡小坂井町大字篠束字若宮53番 地 サンビシ株式会社内 (72)発明者 犬飼 忠彦 愛知県名古屋市中区錦1丁目2番7号 天 野製薬株式会社内 (72)発明者 伊丹 宏 東京都渋谷区神宮前6丁目26番1号 麒麟 麦酒株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Hiroshi Wakazono 1-1 Sanbonmatsu-cho, Atsuta-ku, Nagoya, Aichi Prefecture Japan Vehicle Manufacturing Co., Ltd. 53 In Sanbishi Co., Ltd. (72) Inventor Tadahiko Inukai 1-2-7 Nishiki, Naka-ku, Nagoya-shi, Aichi Amano Pharmaceutical Co., Ltd. (72) Hiroshi Itami 6-26-1, Jingumae, Shibuya-ku, Tokyo No. Kirin Brewery Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】発酵処理後の発酵液を取出す流出口を上部
に設けた発酵槽内に、高多孔性粒状泡ガラスの担体に醤
油酵母を固定化させた固定化菌体を充填するとともに、
発酵槽の下部に醤油発酵原液を供給する供給口と、発酵
中に生成する生成気体を排気するため、0.01乃至0.04vv
mの空気を送通する空気供給口を設けたことを特徴とす
る醤油の発酵装置。
1. A fermenter having an outlet for taking out a fermented liquid after the fermentation treatment is provided in an upper portion, and is filled with immobilized bacterial cells in which soy sauce yeast is immobilized on a carrier of highly porous granular foam glass,
To supply the soy sauce fermentation stock solution to the bottom of the fermenter and to exhaust the generated gas generated during fermentation, 0.01 to 0.04 vv
An apparatus for fermenting soy sauce, which is provided with an air supply port for transmitting m air.
【請求項2】前記多孔性粒状泡ガラスの物性は、粒径2
乃至5mm,見掛け比重0.3乃至0.7,給水率50%以上,細孔
容積1.0乃至3.5ml/g,中央細孔径(V)5.0乃至25.0μm
であることを特徴とする特許請求の範囲第1項記載の醤
油の発酵装置。
2. The physical property of the porous granular foam glass has a particle size of 2
To 5 mm, apparent specific gravity 0.3 to 0.7, water supply rate 50% or more, pore volume 1.0 to 3.5 ml / g, central pore diameter (V) 5.0 to 25.0 μm
The soy sauce fermentation apparatus according to claim 1, wherein
JP62252272A 1987-10-06 1987-10-06 Soy sauce fermentation equipment Expired - Lifetime JPH0716379B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62252272A JPH0716379B2 (en) 1987-10-06 1987-10-06 Soy sauce fermentation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62252272A JPH0716379B2 (en) 1987-10-06 1987-10-06 Soy sauce fermentation equipment

Publications (2)

Publication Number Publication Date
JPH0195742A JPH0195742A (en) 1989-04-13
JPH0716379B2 true JPH0716379B2 (en) 1995-03-01

Family

ID=17234932

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62252272A Expired - Lifetime JPH0716379B2 (en) 1987-10-06 1987-10-06 Soy sauce fermentation equipment

Country Status (1)

Country Link
JP (1) JPH0716379B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02257849A (en) * 1989-03-30 1990-10-18 Hiroaki Horitsu Production of seasoning solution of soy sauce
KR100421961B1 (en) * 2000-11-03 2004-03-18 학교법인 영남학원 Fermentation apparatus for refermented soy sauce
CN105402911B (en) * 2015-12-08 2018-04-06 邓州市鑫隆酱业调料有限公司 One kind sauce solar constant temperature device and constant temperature keeping method

Also Published As

Publication number Publication date
JPH0195742A (en) 1989-04-13

Similar Documents

Publication Publication Date Title
KR100910238B1 (en) Combination continuous/batch fermentation processes
Margaritis et al. Advances in ethanol production using immobilized cell systems
RU2060277C1 (en) Process of production of ethanol product
White et al. Continuous fermentation by immobilized brewers yeast
JPH0817692B2 (en) Fermentation method and fermenter
JPS6137919B2 (en)
CN107022541A (en) A kind of process for fixation of aspergillus niger
JP3594227B2 (en) Production of fermented products
CA1277620C (en) Preparation process of immobilized enzymes and apparatus for carrying out same
JPH0716379B2 (en) Soy sauce fermentation equipment
CA2133789A1 (en) Immobilized-cell carrageenan bead production and a brewing process utilizing carrageenan bead immobilized yeast cells
CN1219071C (en) Method for producing yeast extracellular trehalose by two step fermentation method
JPH0817679B2 (en) Soy sauce fermentation equipment
US2524200A (en) Continuous method of conducting microbiological processes
Unger et al. Continuous aerobic process for distiller's yeast
KR950025097A (en) Calcium alginate microorganism immobilized capsule and method for producing same
US2302079A (en) Process for producing enzymes by the cultivation of micro-organisms on nitrogen and carbohydratecontaining mashes
Aleksieva et al. Production of acid proteinases by Humicola lutea immobilized in polyacrylamide gel
US2549465A (en) Process for biochemical production of enzymes
JPS5911160A (en) Preparation of seasoning liquid
JPS6090096A (en) Preparation of deoxidized water
GB2104914A (en) Process for manufacturing alcohol by fermentation
SU975799A1 (en) Strain of fungus aspergillus niger l-4 producer of citric acid
JPH05336981A (en) Production of optically active m-hydroxy acid
JPH0363352B2 (en)