JPH07255409A - Production of soybean paste having fluid state - Google Patents

Production of soybean paste having fluid state

Info

Publication number
JPH07255409A
JPH07255409A JP6057473A JP5747394A JPH07255409A JP H07255409 A JPH07255409 A JP H07255409A JP 6057473 A JP6057473 A JP 6057473A JP 5747394 A JP5747394 A JP 5747394A JP H07255409 A JPH07255409 A JP H07255409A
Authority
JP
Japan
Prior art keywords
miso
fermentation
yeast
raw materials
cooled
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
JP6057473A
Other languages
Japanese (ja)
Inventor
Eiji Kusaba
英治 草場
Toshio Yoshida
利夫 吉田
Yoshimi Yamaguchi
義巳 山口
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.)
MIYAJIMA SHOYU KK
Original Assignee
MIYAJIMA SHOYU KK
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 MIYAJIMA SHOYU KK filed Critical MIYAJIMA SHOYU KK
Priority to JP6057473A priority Critical patent/JPH07255409A/en
Publication of JPH07255409A publication Critical patent/JPH07255409A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a method for producing MISO (soybean paste) in a fluid state, capable of readily industrially producing MISO in a fluid state having taste of conventional MISO and desired properties. CONSTITUTION:In charging of MISO by mixing at least soybean with charging water and koji, charging amount of water per charging weight when charging is set to 25-35% and raw materials capable of having fluidity after charging is heated to enzymatically digest the raw materials and the raw materials after enzymatically digesting are cooled and lactobacillus is added to the raw materials to carrying out lactobacillary fermentation, and the raw material after the fermentation is once heated and cooled and yeast is added thereto to carry out yeast fermentation. The fermented raw materials are cooled and, after-aging, yeast is added according to the purpose and, after post-aging fermentation is carried out, the treated raw materials are once heated and then cooled, and further, the raw materials are aged.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、工業化規模で製造する
のに適した流動態味噌の製造法に関する。
FIELD OF THE INVENTION The present invention relates to a process for producing a hydrodynamic miso suitable for production on an industrial scale.

【0002】[0002]

【従来の技術】味噌は、半固形の性状を持つ発酵調昧食
品であり、原料に大豆と麹及び麹に由来する酵素・有用
菌、または添加有用菌を利用し、食塩の持つ酵素・発酵
菌への抑制力を利用して、それらの働きを調整し、原料
を完全に酵素消化・発酵をさせず、原料の一部を残して
醸造する発酵調味食品である。
BACKGROUND OF THE INVENTION Miso is a fermented food having a semi-solid property. It uses soybeans, koji, and enzymes / useful bacteria derived from koji or added useful bacteria as raw materials, and the enzyme / fermentation of salt It is a fermented seasoning food that utilizes the inhibitory effect on bacteria to adjust their functions, does not completely enzymatically digest and ferment the raw material, and leaves a part of the raw material for brewing.

【0003】この味噌を工業化規模で製造することを考
えると、原料から製品までを一連の連続した流れの中で
処理することが望ましい。ところが、味噌は特有の性状
特性を持っているために、各製造工程において、複雑な
処理と多大な労力を必要とする等の理由により、工業化
に適さないという問題があった。すなわち、味噌は半固
形であるために、取り扱いにくい、完全に溶解させるこ
とが困難であり原料滓が残る、製品の品質を均一にする
ための醸造管理が難しい、液体食品を製造する際に使用
されている熱交換機等の高効率機器が使用できない等の
問題があった。また、原料の温度を変えることにより発
酵や消化の進行を制御しようとしても、仕込み原料全体
に対して均一に温度を制御することが困難であるため、
目的とする性状を有する味噌を製造することが困難であ
るという問題があった。
Considering the production of this miso on an industrial scale, it is desirable to process from raw material to product in a continuous stream. However, since miso has unique property characteristics, there is a problem that it is not suitable for industrialization because it requires complicated treatment and great labor in each manufacturing process. That is, since miso is a semi-solid, it is difficult to handle, it is difficult to completely dissolve it, raw material residue remains, brewing control is difficult to make the quality of the product uniform, and it is used when manufacturing liquid foods. There is a problem that high efficiency equipment such as existing heat exchangers cannot be used. Further, even if trying to control the progress of fermentation and digestion by changing the temperature of the raw material, it is difficult to uniformly control the temperature for the entire charged raw material,
There is a problem that it is difficult to produce miso having the desired properties.

【0004】これらの問題点を解決するために、半固形
の味噌を調理加工してペースト状にして使用するなどの
方法が取られてきていたが、加工すればするほど、味噌
本来の風味を薄める結果になるきらいがあった。
In order to solve these problems, a method of cooking and processing semi-solid miso and using it as a paste has been used. However, the more it is processed, the more the original flavor of miso becomes. There was a tendency to dilute.

【0005】また、特開昭58−98054号公報に
は、高食塩分濃度での高水分仕込みを行い、麹由来の発
酵菌または、タンパク分解酵素酵母を添加し、これらが
混在した中で醸造中の攪拌機によるミキシングを頻繁に
行うことにより味噌を液化する液状味噌の製造法が記載
されている。
Further, in Japanese Patent Laid-Open No. 98054/1983, a high water content is charged at a high salt concentration, a fermenting bacterium derived from koji or a proteolytic enzyme yeast is added, and brewing is performed in a mixture of these. A method for producing a liquid miso by liquefying the miso by frequently performing mixing with an agitator is described.

【0006】しかしながら、上記特開昭58−9805
4号公報に記載の製造方法においては、高食塩分の下で
味噌を醸造し、菌の働きを抑制するので、熟成味噌の利
用範囲が狭くなり、また、複雑に存在する麹に由来する
菌をそのまま利用するため、味噌の品質が麹の出来不出
来に左右されるという問題があった。なお、上記特開昭
58−98054号公報に記載の製造方法においては、
仕込み味噌の水分は、47.5〜44.5%、仕込み水
量は15.5〜18.7%となっている。
However, the above-mentioned JP-A-58-9805 is used.
In the production method described in Japanese Patent Publication No. 4, the miso is brewed under a high salt content and the action of the fungus is suppressed, so that the range of use of the aged miso is narrowed, and the fungus derived from koji existing in a complicated manner. However, there is a problem that the quality of miso depends on the quality of koji. Incidentally, in the manufacturing method described in the above-mentioned JP-A-58-98054,
The water content of the charged miso is 47.5 to 44.5%, and the water content is 15.5 to 18.7%.

【0007】また、特開平2−23846号公報には、
味噌原料を酵素により加水分解して液化物を得、この液
化物を乳酸発酵槽へ装入し、乳酸発酵を行って乳酸発酵
物を得、この乳酸発酵物を酵母発酵槽へ装入し、酵母に
より酵母発酵を行って液体状味噌風調味料を得る液体状
味噌風調味料の製造法が記載されている。
Further, Japanese Patent Application Laid-Open No. 2-23846 discloses that
The miso raw material is hydrolyzed with an enzyme to obtain a liquefaction, the liquefaction is charged into a lactic acid fermentation tank, lactic acid fermentation is performed to obtain a lactic acid fermentation product, and the lactic acid fermentation product is charged into a yeast fermentation tank, A method for producing a liquid miso-flavored seasoning is described, which comprises performing yeast fermentation with yeast to obtain a liquid miso-flavored seasoning.

【0008】しかしながら、上記特開平2−23846
号公報に記載の製法においては、仕込み水分を65〜8
5%と高くして、仕込み時に原料を全てミキサーで微粒
子して液化しており、仕込み水分の割合が非常に高いの
で、対水食塩濃度が低く、菌に対する抑制力が低下して
おり、また、乳酸菌醗酵後及び酵母菌醗酵後の菌の抑制
や静菌化工程がなく、複雑に混在する菌の醗酵を調整し
にくいという問題があった。
However, the above-mentioned Japanese Laid-Open Patent Publication No. 2-23846.
In the manufacturing method described in Japanese Patent Publication No.
It is set to 5% and the raw material is all liquefied by fine particles with a mixer at the time of charging, and since the ratio of the charged water is very high, the salt concentration against water is low, and the inhibitory effect on bacteria is reduced. However, there is a problem that it is difficult to control the fermentation of bacteria that are mixed in a complicated manner, because there is no step of bacteriostatic control or bacteriostatic process after fermentation of lactic acid bacteria and yeast fermentation.

【0009】[0009]

【発明が解決しようとする課題】そこで本発明は、従来
の味噌の風味を持ち、所望の性状を有する流動態味噌を
工業的に容易に製造することができる流動態味噌の製造
法を提供することを目的とする。
Therefore, the present invention provides a method for producing a hydrodynamic miso having the conventional flavor of miso and capable of industrially easily producing a hydrodynamic miso having desired properties. The purpose is to

【0010】[0010]

【課題を解決するための手段】本発明は、菌抑制力要因
のーつである温度に着目し、目的の味噌に合わせて、ま
た、醸造の各工程にタイミングを合わせて温度管理を短
時間に正確に行うことにより、正常な状態で目的の流動
態味噌を製造するものである。
[Means for Solving the Problems] The present invention focuses on temperature, which is one of the factors that suppress bacteria, and controls temperature in a short time according to the desired miso and at each brewing process. By precisely performing the above, the desired flow dynamic miso can be produced in a normal state.

【0011】本発明の流動態味噌は、以下に示す工程に
より製造される。図1は、本発明の流動態味噌の製造法
を示す工程図である。
The flow-rate miso of the present invention is produced by the following steps. FIG. 1 is a process diagram showing a method for producing a flow-type miso of the present invention.

【0012】〔工程1〕蒸し大豆をミンチ処理し、仕込
み水と混合し、コロイドミルなどで微粒子化し、麹と、
食塩と、仕込み重量に対して25%〜35%の仕込み水
量を加え、目的により調昧料を加えて良く混合したもの
を、熱交換機を通して50°C〜55°Cに加熱し、保
温タンク(発酵タンク)にいれて目的により2〜3日置
き、麹由来の酵素消化を行うと共に、麹寄生菌を抑制若
しくは不活性化する。
[Step 1] Steamed soybeans are minced, mixed with charged water, finely divided by a colloid mill or the like, and then koji,
A mixture of salt and 25% to 35% of the amount of water to be charged, which was mixed well with a refining agent depending on the purpose, was heated to 50 ° C to 55 ° C through a heat exchanger and kept in a heat-retaining tank ( It is placed in a fermentation tank) and left for 2 to 3 days depending on the purpose to digest the enzyme derived from koji and suppress or inactivate koji parasites.

【0013】上記仕込み水量とは、仕込み原料である蒸
煮大豆、麹、食塩、水の合計重量中の水の重量割合を意
味する。なお、蒸煮大豆水分は65〜66%、麹水分は
25〜28%、食塩水分は1%程度である。
The amount of water charged means the weight ratio of water to the total weight of steamed soybeans, koji, salt and water which are the starting materials. The steamed soybean water content is 65 to 66%, the koji water content is 25 to 28%, and the salt water content is about 1%.

【0014】〔工程2〕消化後の原料を熱交換機によ
り、後続工程で添加される乳酸菌の種類に応じて25°
C〜30°Cに冷却し、目的の乳酸菌を添加し、保温タ
ンク(乳酸菌発酵タンク)に入れ、乳酸菌の種類に応じ
て25°C〜30°Cで5日〜7日乳酸菌発酵させる。
[Step 2] The digested raw material is heated by a heat exchanger at 25 ° depending on the kind of lactic acid bacteria added in the subsequent step.
The mixture is cooled to C to 30 ° C, the target lactic acid bacterium is added, and the lactic acid bacterium is put in a heat-retaining tank (lactic acid bacterium fermentation tank) and fermented with lactic acid bacterium at 25 ° C to 30 ° C for 5 to 7 days depending on the type of lactic acid bacterium.

【0015】〔工程3〕目的の乳酸菌発酵をさせた後、
熱交換機を通して50〜55℃に加熱し1時間保持し乳
酸菌を抑制若しくは不活性化した後、保温タンクを挟ん
で設けられた冷却用熱交換機を通し30℃〜32°Cに
冷却し、主発酵酵母菌を添加し保温タンクに入れる。そ
して、30℃〜32℃で目的により5日〜14日時々攪
拌しながら主酵母発酵させる。
[Step 3] After fermentation of the desired lactic acid bacterium,
After heating to 50 to 55 ° C through a heat exchanger and holding for 1 hour to suppress or inactivate lactic acid bacteria, cool it to 30 ° C to 32 ° C through a heat exchanger for cooling provided with a heat-retaining tank, and perform main fermentation Add yeast and put in a heat insulation tank. Then, main yeast fermentation is carried out at 30 ° C to 32 ° C for 5 to 14 days depending on the purpose with occasional stirring.

【0016】〔工程4〕目的の発酵を終了した後、熱交
換機を通し50〜55℃に加熱しl時間50〜55℃を
保持して主発酵酵母菌を不活性化し、冷却用熱交換機を
通し28゛C〜30’Cに冷却して、後熟酵母菌を目的
により添加し、後熟酵母発酵を目的の風味になるまで発
酵させる。なお、この後熟酵母菌添加醗酵の工程は、目
的の味噌により省略することもある。
[Step 4] After the desired fermentation is completed, it is heated to 50 to 55 ° C. through a heat exchanger and kept at 50 to 55 ° C. for 1 hour to inactivate the main fermenting yeast, and a heat exchanger for cooling is used. After cooling to 28 "C to 30'C, post-ripening yeast is added depending on the purpose, and the post-ripening yeast fermentation is fermented until the desired flavor is obtained. The step of fermentation after the addition of the matured yeast may be omitted depending on the intended miso.

【0017】〔工程5〕この後、熱交換機を通し50〜
55°Cに加熱しl時間置き、後熟酵母菌を不活性化さ
せる。次に、熱交換機を通し、25°C以下に冷却し保
温タンクにいれて目的の味噌の風味まで熟成させる。
[Step 5] After this, the heat exchanger is passed through 50-
Heat at 55 ° C and leave for 1 hour to inactivate post-ripening yeast. Next, it is passed through a heat exchanger, cooled to 25 ° C. or lower, put in a heat-retaining tank, and aged to the desired flavor of miso.

【0018】〔工程6〕熟成を完了した味噌は、コロイ
ドミル等の微粒化処理材により微粒子化し目的の流動性
を持ち、溶けやすく、残滓が少なく、通常の味噌と遜色
ない、加工適性を有した流動態味噌となる。なお、コロ
イドミル等により微粒子化しなければ、浮き麹味噌とし
て使用することができる。
[Step 6] Miso that has been aged is made into fine particles by an atomization treatment material such as a colloid mill, has the desired fluidity, is easily melted, has a small amount of residue, and is compatible with ordinary miso and has a processability. It becomes a kinetic miso. If it is not made into fine particles by a colloid mill or the like, it can be used as floating koji miso.

【0019】[0019]

【作用】本発明は、菌抑制力要因のーつである温度に着
目し、目的の味噌に合わせて、時を得た温度管理を短時
間に正確に行うことにより、正常な状態で目的の味噌を
醸造できることが判った。
The present invention focuses on the temperature, which is one of the factors that suppress bacteria, and controls the temperature accurately in a short time in accordance with the desired miso so that the target can be obtained in a normal state. It turns out that miso can be brewed.

【0020】更に、流動性を持つ味噌は、液体製品を製
造する場合と同様の熱交換機等の高能率機器を使用でき
るために、温度調節の為の熱交換機と保温発酵タンクの
利用で正確に温度管理ができ、有用菌の制御が工業的に
できる事が判った。また、仕込み時の水分として、仕込
み重量に対して25〜35%の仕込み水量を用いて、本
発明の製造法をとり醸造することにより、通常の味噌と
遜色ない風味を持ち、固液分離がしにくい流動性を持つ
味噌ができる事が判った。そして、通常の味噌と同様に
目的の味噌に応じた有用菌の選択添加が行え、菌の種類
に応じて温度経過を変えることで所望の流動態味噌が製
造できた。
Further, since the miso having a fluidity can use a high efficiency device such as a heat exchanger as in the case of producing a liquid product, it is possible to accurately use a heat exchanger for temperature control and a heat-retaining fermentation tank. It was found that the temperature can be controlled and useful bacteria can be controlled industrially. Further, as the water content at the time of preparation, by using the preparation water amount of 25 to 35% with respect to the preparation weight and brewing the production method of the present invention, it has a flavor comparable to that of normal miso and solid-liquid separation It was found that a miso with a fluidity that is difficult to do can be made. Then, similar to usual miso, useful bacteria can be selectively added according to the desired miso, and the desired hemodynamic miso can be produced by changing the temperature course according to the type of bacteria.

【0021】仕込み時の水分を、仕込み重量に対して2
5〜35%の仕込み水量とするのは、25%よりも少な
い場合には、味噌の性状が高粘度となり、流動性がなく
なるため、均一な温度管理が困難となり、醗酵菌の管理
に異常が出やすいという不都合があり、35%より多い
場合には、固液分離を生じやすく、また、大豆、麹の固
形分が少なくなり、固形分を含めて味噌の香味を形成し
ている味噌の特性からして、香味が不足して本来の香味
から離れてくるという不都合があるからである。
Water content at the time of preparation is 2 with respect to the weight of preparation.
When the amount of water to be charged is 5 to 35%, if the amount is less than 25%, the miso properties become highly viscous and the fluidity disappears, making uniform temperature control difficult and abnormal fermentation control. There is a problem that it is easy to come out, and if it is more than 35%, solid-liquid separation is likely to occur, and the solid content of soybeans and koji becomes small, and the characteristics of miso forming the flavor of miso including solid content. This is because there is a disadvantage that the flavor is insufficient and the flavor is separated from the original flavor.

【0022】[0022]

【実施例】【Example】

〔実施例1〕表1に示す配合割合で発酵試験を行った。 [Example 1] Fermentation tests were conducted at the blending ratios shown in Table 1.

【0023】[0023]

【表1】 上記配合に基づく発酵試験を以下の手順で行った。[Table 1] A fermentation test based on the above formulation was performed according to the following procedure.

【0024】酵素消化(50°C2日)→25°C冷却
→乳酸菌添加→乳酸菌醗酵(25°C5日間)→加熱
(55°C1時間)→冷却(30°C)→酵母菌添加→
酵母菌醗酵(30°C7日間)→加熱(50°C1時
間)→冷却(30°C)→後熟酵母菌添加→後熟酵母菌
醗酵(35°C5日間)→加熱(50°C1時間)→冷
却(25°C)→熟成(25°C15日間) 試験結果を表2に示す。
Enzyme digestion (2 days at 50 ° C) → cooling at 25 ° C → addition of lactic acid bacteria → fermentation of lactic acid bacteria (5 days at 25 ° C) → heating (1 hour at 55 ° C) → cooling (30 ° C) → addition of yeast →
Yeast fermentation (30 ° C for 7 days) → heating (50 ° C 1 hour) → cooling (30 ° C) → post-ripening yeast addition → post-ripening yeast fermentation (35 ° C 5 days) → heating (50 ° C 1 hour) → Cooling (25 ° C) → Aging (25 ° C for 15 days) The test results are shown in Table 2.

【0025】[0025]

【表2】 各醗酵工程後の加熱による、醗酵菌の抑制効果につい
て、各工程でこの仕込み流動態味噌の一部を取り、試験
を行ったところ、加熱温度50〜55°Cで1時間加熱
することにより、抑制,静菌効果があることが判明し
た。加熱試験の結果を以下に示す。
[Table 2] Regarding the inhibitory effect of the fermentation bacterium by heating after each fermentation step, a part of the prepared flow dynamic miso was taken in each step, and a test was conducted, by heating at a heating temperature of 50 to 55 ° C for 1 hour, It was proved to have a suppressive and bacteriostatic effect. The results of the heating test are shown below.

【0026】表3は、酵素消化後の加熱試験の結果を示
す。
Table 3 shows the results of the heating test after enzymatic digestion.

【0027】[0027]

【表3】 表4は、乳酸菌醗酵後の加熱試験の結果を示す。[Table 3] Table 4 shows the result of the heating test after fermentation of lactic acid bacteria.

【0028】[0028]

【表4】 表5は、主酵母菌醗酵後の加熱試験の結果を示す。[Table 4] Table 5 shows the result of the heating test after fermentation of the main yeast.

【0029】[0029]

【表5】 表6は、実施例1の各工程での加熱処理後の菌抑制効果
を示す。
[Table 5] Table 6 shows the bacterial suppression effect after the heat treatment in each step of Example 1.

【0030】[0030]

【表6】 流動性を持つ本発明の流動態味噌は、均一に加熱を行う
ことができ、菌の抑制を目的通りに行うことができ、高
水分に伴う異常醗酵を防止することができる。
[Table 6] The flowable miso of the present invention, which has fluidity, can be uniformly heated, can suppress bacteria as desired, and can prevent abnormal fermentation due to high water content.

【0031】熟成を終わった流動態味噌を10人のパネ
ルにより、従来の味噌と比較官能試験を行い、大差ない
香味を有する結果を得た。比較は5点法により行い、組
成は現象を表記した。
The aged kinetic miso was subjected to a comparative sensory test with a conventional miso using a panel of 10 people, and a result having a flavor not so different was obtained. The comparison was carried out by the 5-point method, and the composition was expressed as a phenomenon.

【0032】表7は、合わせ味噌における、本発明によ
る流動態味噌と通常味噌との比較を示す。
Table 7 shows a comparison between the hydrodynamic miso according to the present invention and the normal miso in the combined miso.

【0033】[0033]

【表7】 実施例1によれば、乳酸菌醗酵の後、55°Cで1時間
加熱し、また、酵母菌発酵の後、一定温度にまで加熱
(50°C1時間)し、酵母菌の活性を抑制した後、後
熟酵母を加えたことにより、pHの低下(乳酸菌の発
酵)、アルコールの生成、コクのある香りの付加が十分
に行われた。また、麦味噌は、食塩分を9%まで低下さ
せて仕込んだが、各発酵を温度と時間で制御することに
より酸敗等の異常発酵は生じなかった。
[Table 7] According to Example 1, after fermentation of lactic acid bacteria, heating at 55 ° C for 1 hour, and after yeast fermentation, heating to a constant temperature (1 hour at 50 ° C) to suppress yeast activity. The addition of post-ripening yeast sufficiently reduced the pH (fermentation of lactic acid bacteria), produced alcohol, and added a rich scent. Further, barley miso was prepared by reducing the salt content to 9%, but abnormal fermentation such as rancidity did not occur by controlling each fermentation with temperature and time.

【0034】〔実施例2〕表8に示す配合割合で流動態
味噌の仕込み試験を行った。
[Example 2] A flow rate miso preparation test was conducted at the blending ratios shown in Table 8.

【0035】[0035]

【表8】 これを実施例1と同様に醗酵熟成を行い、表9に示すよ
うな結果を得た。
[Table 8] This was fermented and aged in the same manner as in Example 1, and the results shown in Table 9 were obtained.

【0036】[0036]

【表9】 通常味噌に比べて流動態味噌は、粘性も低く、ロータリ
ーポンプ等による輸送も充分に可能な性状を示した。
[Table 9] Compared with normal miso, the flow-type miso had a low viscosity and showed a property capable of being sufficiently transported by a rotary pump or the like.

【0037】また、仕込み水/仕込み量を25〜35%
にすることにより、固液分離も充分に許容できるもので
あった。
Further, the charged water / charged amount is 25 to 35%
By the above, solid-liquid separation was sufficiently acceptable.

【0038】[0038]

【発明の効果】以上に述べたように、本発明において
は、流動態味噌を製造するに際し、仕込み時の仕込み量
に対する仕込み水量を25%〜35%とすることによ
り、味噌に十分な流動性を与えることができる。これに
より、熱交換機等の大量生産に適した装置を使用して味
噌を製造することができると共に、この熱交換機により
原料の温度を、目的とする味噌の種類に合わせて正確に
しかも迅速に制御することができる。したがって、味噌
の対水食塩濃度が低くなった場合でも、異常な酵素消費
や発酵を生じることなく、従来の味噌と遜色ない流動態
味噌を工業的規模で製造することができる。
As described above, in the present invention, in the production of a hydrodynamic miso, the amount of water to be charged relative to the amount charged at the time of preparation is 25% to 35%, so that sufficient fluidity for miso can be obtained. Can be given. As a result, miso can be produced using a device suitable for mass production such as a heat exchanger, and the temperature of the raw material can be accurately and quickly controlled by this heat exchanger according to the type of miso to be produced. can do. Therefore, even if the salt concentration of miso to water becomes low, a hemodynamic miso comparable to the conventional miso can be produced on an industrial scale without causing abnormal enzyme consumption or fermentation.

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

【図1】 本発明の流動態味噌の製造法を示す工程図で
ある。
FIG. 1 is a process drawing showing a method for producing a hydrodynamic miso of the present invention.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】少なくとも大豆と仕込み水と麹とを混合す
る味噌の仕込みにおいて、仕込み時の仕込み重量に対す
る仕込み水量を25%〜35%としたことを特徴とする
流動態味噌の製造法。
1. A method for producing a hydrodynamic miso, characterized in that, in the preparation of miso in which at least soybeans, preparation water and koji are mixed, the amount of preparation water relative to the preparation weight at the preparation is 25% to 35%.
【請求項2】仕込み後の流動性を有する原料を加熱し麹
に由来する菌を抑制または静菌化して酵素消化させ、 酵素消化後の原料を冷却して乳酸菌を添加して乳酸菌醗
酵させ、 乳酸菌醗酵後の原料を一旦加熱したのち冷却して酵母菌
を添加して酵母菌醗酵させ、 酵母菌醗酵後の原料を一旦加熱したのち冷却して熟成さ
せることを特徴とする請求項1記載の流動態味噌の製造
法。
2. A raw material having fluidity after being charged is heated to suppress or bacteriolyze bacteria derived from koji and enzymatically digested, and the raw material after enzymatic digestion is cooled and lactic acid bacteria are added to ferment lactic acid bacteria, The raw material after fermentation of lactic acid bacteria is once heated and then cooled and yeast is added to ferment the yeast, and the raw material after fermentation of yeast is heated once and then cooled and aged. A method for producing kinetic miso.
【請求項3】上記流動態味噌を熟成後、湿式微細粒化処
理して残滓が少ない流動態味噌を得る請求項2記載の流
動態味噌の製造法。
3. The method for producing a hydrodynamic miso according to claim 2, wherein the hydrodynamic miso is aged after the ripening of the hydrodynamic miso to obtain a hydrodynamic miso having a small amount of residue.
JP6057473A 1994-03-28 1994-03-28 Production of soybean paste having fluid state Pending JPH07255409A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6057473A JPH07255409A (en) 1994-03-28 1994-03-28 Production of soybean paste having fluid state

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6057473A JPH07255409A (en) 1994-03-28 1994-03-28 Production of soybean paste having fluid state

Publications (1)

Publication Number Publication Date
JPH07255409A true JPH07255409A (en) 1995-10-09

Family

ID=13056679

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6057473A Pending JPH07255409A (en) 1994-03-28 1994-03-28 Production of soybean paste having fluid state

Country Status (1)

Country Link
JP (1) JPH07255409A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998043498A1 (en) * 1997-04-01 1998-10-08 Nichimo Co., Ltd. Product comprising health-promotive ingredient and process for producing the same
JP2017029068A (en) * 2015-07-31 2017-02-09 株式会社浅利佐助商店 Method for producing reduced-salt miso
CN112772897A (en) * 2020-12-24 2021-05-11 四川省食品发酵工业研究设计院 Method for preparing sweet fermented flour paste by using sweet petal fermentation liquor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6303161B1 (en) 1996-04-01 2001-10-16 Nichimo Co., Ltd. Product containing healthful component and process for preparing the same
WO1998043498A1 (en) * 1997-04-01 1998-10-08 Nichimo Co., Ltd. Product comprising health-promotive ingredient and process for producing the same
JP2017029068A (en) * 2015-07-31 2017-02-09 株式会社浅利佐助商店 Method for producing reduced-salt miso
CN112772897A (en) * 2020-12-24 2021-05-11 四川省食品发酵工业研究设计院 Method for preparing sweet fermented flour paste by using sweet petal fermentation liquor

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