JPH04210575A - Production of soy sauce - Google Patents

Production of soy sauce

Info

Publication number
JPH04210575A
JPH04210575A JP2401079A JP40107990A JPH04210575A JP H04210575 A JPH04210575 A JP H04210575A JP 2401079 A JP2401079 A JP 2401079A JP 40107990 A JP40107990 A JP 40107990A JP H04210575 A JPH04210575 A JP H04210575A
Authority
JP
Japan
Prior art keywords
soy sauce
membrane
stock solution
dissolved oxygen
ppm
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
JP2401079A
Other languages
Japanese (ja)
Inventor
Kazuya Kuriyama
和也 栗山
Toshio Kanbe
利夫 神戸
Masayoshi Takatake
正義 高武
Hitoshi Kato
均 加藤
Yasushi Tomita
康司 富田
Kazumi Oi
和美 大井
Nobumasa Tan
伸巨 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.)
DIC Corp
Original Assignee
Dainippon Ink and Chemicals 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 Dainippon Ink and Chemicals Co Ltd filed Critical Dainippon Ink and Chemicals Co Ltd
Priority to JP2401079A priority Critical patent/JPH04210575A/en
Publication of JPH04210575A publication Critical patent/JPH04210575A/en
Pending legal-status Critical Current

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  • Soy Sauces And Products Related Thereto (AREA)

Abstract

PURPOSE:To obtain soy sauce prevented from discoloration without impairing the flavor inherent therein by deaerating, using a membrane type deaerator, a soy sauce stock liquor obtained by squeezing. CONSTITUTION:A soy sauce stock liquor obtained by squeezing is brought into contact with a deaerating membrane and deaerated to 2 or less ppm (pref. 0.5 or less ppm) in the dissolved oxygen level using a membrane type deaerator to make a vacuum deaeration through said deaerating membrane, and a glass or plastic container is then filled with the resulting soy sauce and closed.

Description

【発明の詳細な説明】[Detailed description of the invention]

【産業上の利用分野]本発明は醤油の製造法に関するも
のである。 [0002] 【従来の技術】従来、醤油の製造方法としては、脱脂加
工大豆を蒸煮、種付、製麹、熟成したのち圧搾しガラス
、プラスチック等の容器に充填、密閉されていた。 然しながら、醤油は径時的に着色する性質があり、特に
色の薄い醤油においては着色する事はその商品価値を低
下させるためその対策が強く求められている。醤油の着
色防止法として窒素ガスを長時間吹き込む方法があるが
、かかる方法は醤油特有の風味を損ね好ましくない。 [0003]
[Industrial Field of Application] The present invention relates to a method for producing soy sauce. [0002] Conventionally, soy sauce has been produced by steaming defatted soybeans, seeding them, making koji, aging them, pressing them, filling them into containers made of glass, plastic, etc., and sealing them. However, soy sauce has the property of becoming colored over time, and coloring, especially in pale soy sauce, reduces its commercial value, so there is a strong need for countermeasures against this problem. One way to prevent soy sauce from discoloring is to blow nitrogen gas into it for a long period of time, but such a method is undesirable because it impairs the unique flavor of soy sauce. [0003]

【発明が解決しようとする課題】本発明はかかる現状に
かんがみ醤油の風味を損ねずに着色を防止せんとするも
のである。 [0004]
SUMMARY OF THE INVENTION In view of the current situation, the present invention aims to prevent discoloration of soy sauce without impairing its flavor. [0004]

【課題を解決するための手段】 本発明は、醤油を製造
するに際して、圧搾した醤油の原液を脱気膜に接触せし
め該脱気膜を介して真空脱気する膜式脱気装置を用いて
溶存酸素濃度2pprn以下迄脱気せしめてガラス、プ
ラスチックス等の容器に充填密閉する事により問題を解
決せんとするものである。 [0005]
[Means for Solving the Problems] When producing soy sauce, the present invention uses a membrane-type deaerator that brings the compressed soy sauce undiluted solution into contact with a deaeration membrane and vacuum deairs it through the deaeration membrane. This is an attempt to solve the problem by deaerating the solution to a dissolved oxygen concentration of 2 pprn or less and filling it into a glass, plastic, etc. container and sealing it. [0005]

【構成】原液を脱気した醤油の溶存酸素濃度としては2
ppm以下、好ましくは0.5ppm以下であり、2p
pm以上では十分な着色防止効果が得られない。液体の
溶存酸素濃度を下げる他の方法として還元脱酸素剤(例
えばヒドラジン等)を用いる方法が有るが、この方法は
毒性の点で好ましくない。又、煮沸する方法や、前述の
窒素ガス吹き込み方法では醤油の風味を損なうと共に溶
存酸素濃度を2 p pm以下、好ましくは0.2pp
m以下に下げるのは困難である。 [0006]本発明に於ける膜式脱気装置としては、原
液を脱気膜に接触させ、この脱気膜を介して、真空、減
圧にする事により生ずる脱気膜を介した分圧差により原
液中から、真空、減圧側へ溶存酸素を効率よく除去する
ことが、可能なものであり、薬剤等の混入しない、安全
で醤油の風味を損なうことなく脱酸素醤油を得る事が出
来るものである。 [0007]かかる膜式脱気装置の一例を図−1に示す
。この脱気装置は概略膜モジュール1と真空ポンプ2か
ら構成されるものである。膿モジコニル1は脱気膜3を
エレメント化してなるものである。この脱気膜3は原液
と接触させることにより、酸素を透過して脱気するもの
であれば特に限定されるものではなく、複合膜、不均質
膜、疎水性多孔質膜、均質膜など任意のものを使用でき
る。又、この脱気膜3の形状についても中空糸状、管状
、平膜状など任意の形状のものを使用できる。しかしこ
れらのなかでも膜が疎水性のポリマ〜からなり、膜壁を
空気(酸素)が選択的に透過できるように、膜壁に空気
(酸素)連通孔が形成された特殊スポンジ構造を有する
中空糸膜く不均質膜)が好適である。 [0008]膜モジユール】には、原液供給管4と、フ
ロースイッチ5が接続された脱酸素液排出管10とがそ
れぞれ接続されている。原液供給管4は、減圧弁8を介
して図示しない原液供給源に接続されているとともに、
膜モジュール1の直前で分岐されている。原液供給管4
から分岐された分岐管9は、膜モジュ一ル1に原液を定
流儀で供給できるように設けられたものであって、定流
量弁Oと電磁弁6を介して真空ポンプ2に接続されてい
る。この真空ポンプ2はまた、電磁弁6を介して膜モジ
ュール1に接続されており、真空ライン7を形成してい
る。そしてこの真空ライン7によって、モジュール1内
に供給された原液を真空脱気できるようになっている。 なお、このような脱気装置としては、具体的には、特開
昭63−258605号に記載されたポリ(4−メチル
ペンテン−1)を素材とした大日本インキ化学工業(株
)製セパレ〜ルや三浦工業(株)製DORシリーズ等を
挙げることができる。 [0009]このような脱気装置において原液から酸素
を脱気するには、まず、脱気装置内に原液を流入させる
。するとフロースイッチ5が作動して真空ポンプ2が稼
働する。ついで2つの電磁弁6はそれぞれ開状態となる
。すると膿モジュール1内の脱気膜3が原液と接触せし
められるとともに、脱気膜3を介して真空脱気される。 ここでたとえば脱気膜3として中空糸膜を用いた場合に
は、この中空糸外側の膜モジユール1内が真空となり、
この中空糸内側を流れる原液は、その真空度により原液
中の溶存酸素が隔膜真空脱気されて脱酸素液(醤油)と
され、脱酸素液排出管10へと流出される。なお脱気膜
3が他の形状である場合にも、上記と全く同様にして、
脱気膜3によって真空部分と原液部分とに区画されたモ
ジュール1内、即ち脱気膜3の外側部分を真空引きする
ことにより、脱気膜3内を流動する原液を隔膜真空脱気
して脱酸素液とすることができる。 [00101この脱気装置により得られる脱酸素液は、
通常、残留溶存酸素濃度が2ppm以下となるような条
件で使用されるが、必要によってはさらに低濃度のもの
、たとえば、0.5ppm以下とすることができる。 なお脱酸素液中の溶存酸素濃度は真空ポンプ2によって
得られる真空度及び原液の流速に依存しており、この真
空ポンプ2の稼働条件によって所望の酸素濃度の脱酸素
液を得ることができる。 [0011]このように、本発明において膜式脱気装置
を用い醤油の溶存酸素を2ppm以下、好ましくない容
器に充填・密閉することにより着色のしない容器入り醤
油を製造することができる。 [0012]
[Composition] The dissolved oxygen concentration of soy sauce after deaerating the stock solution is 2
ppm or less, preferably 0.5 ppm or less, and 2p
If it exceeds pm, a sufficient coloring prevention effect cannot be obtained. Another method for lowering the dissolved oxygen concentration in a liquid is to use a reducing oxygen scavenger (eg, hydrazine, etc.), but this method is unfavorable in terms of toxicity. In addition, the boiling method and the nitrogen gas blowing method described above impair the flavor of the soy sauce and reduce the dissolved oxygen concentration to 2 ppm or less, preferably 0.2 ppm.
It is difficult to lower it below m. [0006] The membrane type deaerator according to the present invention allows the raw solution to come into contact with a deaeration membrane, and is made to have a vacuum or reduced pressure through the deaeration membrane. It is possible to efficiently remove dissolved oxygen from the stock solution to the vacuum or reduced pressure side, and it is possible to obtain deoxygenated soy sauce without mixing chemicals, etc., and without impairing the flavor of the soy sauce. be. [0007] An example of such a membrane deaerator is shown in FIG. This deaerator is generally composed of a membrane module 1 and a vacuum pump 2. Pusmodiconil 1 is made by converting the degassing membrane 3 into an element. This degassing membrane 3 is not particularly limited as long as it can degas through oxygen when brought into contact with the stock solution, and can be any membrane such as a composite membrane, a heterogeneous membrane, a hydrophobic porous membrane, a homogeneous membrane, etc. You can use the following. Further, the shape of the degassing membrane 3 can be any shape such as a hollow fiber shape, a tubular shape, or a flat membrane shape. However, among these, hollow membranes are made of hydrophobic polymers and have a special sponge structure with air (oxygen) communication holes formed in the membrane walls so that air (oxygen) can selectively permeate through the membrane walls. Thread membranes (heterogeneous membranes) are preferred. [0008] A stock solution supply pipe 4 and a deoxidized liquid discharge pipe 10 to which a flow switch 5 is connected are respectively connected to the membrane module. The stock solution supply pipe 4 is connected to a stock solution supply source (not shown) via a pressure reducing valve 8, and
It branches just before the membrane module 1. Stock solution supply pipe 4
A branch pipe 9 branched from the membrane module 1 is provided to supply the stock solution to the membrane module 1 in a constant flow manner, and is connected to the vacuum pump 2 via a constant flow valve O and a solenoid valve 6. There is. This vacuum pump 2 is also connected to the membrane module 1 via a solenoid valve 6 and forms a vacuum line 7. The vacuum line 7 allows the stock solution supplied into the module 1 to be vacuum degassed. In addition, a specific example of such a deaerator is the Separator manufactured by Dainippon Ink and Chemicals Co., Ltd., which is made of poly(4-methylpentene-1) and is described in JP-A No. 63-258605. Examples include the DOR series manufactured by Miura Kogyo Co., Ltd. [0009] In order to degas oxygen from the stock solution in such a deaerator, first, the stock solution is caused to flow into the deaerator. Then, the flow switch 5 is activated and the vacuum pump 2 is activated. Then, the two solenoid valves 6 are each opened. Then, the degassing membrane 3 in the pus module 1 is brought into contact with the stock solution, and vacuum degassing is performed via the degassing membrane 3. For example, if a hollow fiber membrane is used as the degassing membrane 3, the inside of the membrane module 1 outside the hollow fiber becomes a vacuum,
Due to the degree of vacuum, dissolved oxygen in the stock solution flowing inside the hollow fiber is degassed through a diaphragm vacuum to form a deoxygenated liquid (soy sauce), which is then discharged to the deoxygenated liquid discharge pipe 10. Note that even when the degassing membrane 3 has a different shape, the same procedure as above is performed,
By evacuating the inside of the module 1, which is divided by the degassing membrane 3 into a vacuum part and a stock solution part, that is, the outside part of the degassing membrane 3, the stock solution flowing inside the degassing membrane 3 is degassed using a diaphragm vacuum. It can be a deoxidizing liquid. [00101 The deoxidized liquid obtained by this deaerator is
Usually, it is used under conditions such that the residual dissolved oxygen concentration is 2 ppm or less, but if necessary, it can be lowered to a lower concentration, for example, 0.5 ppm or less. The dissolved oxygen concentration in the deoxidized liquid depends on the degree of vacuum obtained by the vacuum pump 2 and the flow rate of the stock solution, and depending on the operating conditions of the vacuum pump 2, a deoxidized liquid with a desired oxygen concentration can be obtained. [0011] As described above, in the present invention, by using a membrane deaerator to reduce dissolved oxygen in soy sauce to 2 ppm or less, and filling and sealing an undesirable container, it is possible to produce containerized soy sauce without coloring. [0012]

【実施例】以下に実施例をあげて本発明を詳述する。な
お、実施例における部数は重量部を表す。 (実施例1) 圧搾して得られた醤油原液100部に水400部を加え
均一に混合し、ガードナー法カラーメーターで着色度を
測定、カラー13であった。次に醤油原液を膜式脱気装
置を用いて、溶存酸素2ppm迄脱気した醤油100部
に水400部を加えカラーを測定し、同じくカラー13
であった。 [00131次に脱気した醤油原液を醤油瓶に入れ上部
空間を窒素ガスで置換後、密閉室温にて3力月放置後開
封、醤油100部に水400部を加えカラーを測定し、
カラー14であった。 (実施例2) 脱気した醤油原液の溶存酸素濃度が0.4ppmである
以外は実施例1とまったく同様に、室温放置、着色試験
を行った。3力月後のカラーは13であった。 (0014]  (比較例1) 実施例1に於て醤油原液を脱気せずに用いる以外はまっ
たく同様に、室温放置着色試験を行い、3力月後のカラ
は16であった。 (実施例3) 圧搾して得られた薄口醤油用原液100部に水100部
を加えカラーをガードナー法カラーメーターで測定し、
カラーは183であった。薄日醤油用原液を膜式脱気装
置にて溶存酸素濃度0.5ppm迄脱気、脱気した醤油
原液のカラーは同じく13であった。 Co 015]次に脱気した醤油原液を醤油瓶にいれ、
上部空間を窒素ガスで置換後、密閉室温にて3力月放置
後開封カラーを測定し、カラーは同じく13であった。 (比較例2) 実施例3に於て、薄口醤油原液を脱気しない以外はまっ
たく同様にして室温放置、着色試験を行った結果、カラ
16であった。 [0016]
[Examples] The present invention will be explained in detail with reference to Examples below. In addition, the number of parts in the examples represents parts by weight. (Example 1) 400 parts of water was added to 100 parts of the soy sauce stock solution obtained by pressing and mixed uniformly, and the degree of coloring was measured using a Gardner method color meter, and the color was 13. Next, 400 parts of water was added to 100 parts of soy sauce that had been deaerated to 2 ppm of dissolved oxygen using a membrane deaerator, and the color was measured.
Met. [00131] Next, put the degassed soy sauce stock solution into a soy sauce bottle, replace the upper space with nitrogen gas, leave it sealed at room temperature for 3 months, then open the bottle, add 400 parts of water to 100 parts of soy sauce, and measure the color.
It was color 14. (Example 2) A coloring test was carried out in the same manner as in Example 1, except that the dissolved oxygen concentration of the deaerated soy sauce stock solution was 0.4 ppm. The color after 3 months was 13. (Comparative Example 1) A room temperature coloring test was conducted in exactly the same manner as in Example 1 except that the soy sauce stock solution was used without degassing, and the color after 3 months was 16. Example 3) Add 100 parts of water to 100 parts of the stock solution for light soy sauce obtained by pressing, and measure the color with a Gardner method color meter.
The color was 183. The color of the soy sauce stock solution obtained by deaerating the Usunichi soy sauce stock solution using a membrane deaerator to a dissolved oxygen concentration of 0.5 ppm was the same as 13. Co 015] Next, put the degassed soy sauce stock solution into a soy sauce bottle,
After replacing the upper space with nitrogen gas, the product was left sealed at room temperature for 3 months, and then the unsealed color was measured, and the color was also 13. (Comparative Example 2) A coloring test was carried out in exactly the same manner as in Example 3, except that the light soy sauce stock solution was not degassed, and the result was that the color was 16. [0016]

【発明の効果】本発明は、実施例、比較例で明かなよう
に圧搾して得られた醤油の原液を膜式脱気装置を用いて
溶存酸素濃度を2ppm以下、好ましくは0.5ppm
以下に下げ、醤油容器に密閉、充填することにより醤油
の着色を防ぐ事ができる。
Effects of the Invention As is clear from the Examples and Comparative Examples, the present invention uses a membrane deaerator to reduce the dissolved oxygen concentration to 2 ppm or less, preferably 0.5 ppm, to the soy sauce undiluted solution obtained by squeezing.
You can prevent the soy sauce from discoloring by lowering it to below temperature, sealing it, and filling it in a soy sauce container.

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

【図1】本発明で用いることができる膜式脱気装置の模
式図である。
FIG. 1 is a schematic diagram of a membrane deaerator that can be used in the present invention.

【符号の説明】 0  電磁弁 1  膜モジュール 2  真空ポンプ 3  脱気膜 4  原液供給管 5 70−スイッチ 6  真空ライン 7  真空ライン 8  減圧弁 9  分岐管 発明者[Explanation of symbols] 0 Solenoid valve 1 Membrane module 2 Vacuum pump 3 Degassing membrane 4 Stock solution supply pipe 5 70-Switch 6 Vacuum line 7 Vacuum line 8 Pressure reducing valve 9 Branch pipe inventor

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】圧搾して得られた醤油の原液を脱気膜に接
触せしめ該脱気膜を介して真空脱気する膜式脱気装置を
用いて溶存酸素濃度2ppm以下迄脱気せしめることを
特徴とする醤油の製造法。
[Claim 1] Deaeration to a dissolved oxygen concentration of 2 ppm or less using a membrane-type deaeration device that brings the soy sauce undiluted solution obtained by squeezing into contact with a deaeration membrane and performs vacuum deaeration through the deaeration membrane. A method for producing soy sauce characterized by
【請求項2】脱気した醤油の溶存酸素濃度が0.5pp
m以下である請求項1記載の醤油の製造法。
[Claim 2] The dissolved oxygen concentration of deaerated soy sauce is 0.5 pp.
The method for producing soy sauce according to claim 1, wherein the soy sauce is less than or equal to m.
JP2401079A 1990-12-10 1990-12-10 Production of soy sauce Pending JPH04210575A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2401079A JPH04210575A (en) 1990-12-10 1990-12-10 Production of soy sauce

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2401079A JPH04210575A (en) 1990-12-10 1990-12-10 Production of soy sauce

Publications (1)

Publication Number Publication Date
JPH04210575A true JPH04210575A (en) 1992-07-31

Family

ID=18510938

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2401079A Pending JPH04210575A (en) 1990-12-10 1990-12-10 Production of soy sauce

Country Status (1)

Country Link
JP (1) JPH04210575A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007330125A (en) * 2006-06-14 2007-12-27 Kikkoman Corp Method for producing liquid seasoning

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007330125A (en) * 2006-06-14 2007-12-27 Kikkoman Corp Method for producing liquid seasoning

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