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JPH0391474A - Wine making - Google Patents

Wine making

Info

Publication number
JPH0391474A
JPH0391474A JP1224678A JP22467889A JPH0391474A JP H0391474 A JPH0391474 A JP H0391474A JP 1224678 A JP1224678 A JP 1224678A JP 22467889 A JP22467889 A JP 22467889A JP H0391474 A JPH0391474 A JP H0391474A
Authority
JP
Japan
Prior art keywords
reaction
rice
wine
alcohol
fermentation
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
JP1224678A
Other languages
Japanese (ja)
Inventor
Tadashi Numata
忠 沼田
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.)
Shibaura Mechatronics Corp
Original Assignee
Shibaura Engineering Works 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 Shibaura Engineering Works Co Ltd filed Critical Shibaura Engineering Works Co Ltd
Priority to JP1224678A priority Critical patent/JPH0391474A/en
Publication of JPH0391474A publication Critical patent/JPH0391474A/en
Pending legal-status Critical Current

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  • Alcoholic Beverages (AREA)

Abstract

PURPOSE:To efficiently make a wine in a state capable of readily controlling the concentration of alcohol by subjecting a mixture of beans and rice mainly comprising soybean as a raw material to two step reactions comprising digestion and alcohol fermentation. CONSTITUTION:A mixture of beans and rice containing soybean and the rice in a low water content state is finely ground, subjected to a digestion reaction and subsequently subjected to the removal of undigested components from the reaction solution. The filtrate is subjected to an alcohol fermentation using a yeast such as Zygosaccharomyces.rouxii or Candida.versatillis.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、大豆をベースとしたワインの製造方法に関す
るちのである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a method for producing soybean-based wine.

(発明の背景) 近年、食生活のトレンドに適合した種々の食品の創出が
試みられている。ワインの分野においても、従来のブド
ウを原料とするものだけでなく、リンゴ、カポチャ、メ
ロンなどの種々の原料を用いその原料の特性を生かした
ワインの製造が試みられている。しかし大豆は植物性タ
ンパク質、不飽和脂肪酸などの有用な栄養素を多く含む
にもかかわらず、この大豆をベースとしたワインは未だ
生産された例が無いのが現状である。そこでこの点に着
目して、大豆をベースとし、米などの穀類を用いてワイ
ンを作ることが考えられる。しかしこれら豆穀類による
ワインの製造は製造に要する時間、日数が長くなり能率
が悪いという問題があった。
(Background of the Invention) In recent years, attempts have been made to create various foods that suit dietary trends. In the field of wine as well, attempts are being made to produce wine not only from conventional grapes but also from various other materials such as apples, capochas, and melons, taking advantage of the characteristics of these materials. However, despite the fact that soybeans contain many useful nutrients such as vegetable protein and unsaturated fatty acids, there is currently no example of soybean-based wine being produced. Taking this into account, it is conceivable to make wine using soybeans as a base and grains such as rice. However, the production of wine using these legumes has a problem in that it takes a long time and days for production and is inefficient.

またアルコール濃度は消化反応における糖化の程度の影
響を受けるものであるが、例えば清酒などの従来の製造
方法では消化反応とアルコール発酵とが同時に平行して
進行(平行複発酵)するため、その作業は長年の経験と
カンによる部分が多く、特にアルコール濃度の管理が困
難であった。
Alcohol concentration is also affected by the degree of saccharification in the digestive reaction, but in conventional production methods such as sake, the digestive reaction and alcohol fermentation proceed in parallel at the same time (parallel multiple fermentation). Much of this was based on years of experience and intuition, and it was particularly difficult to control alcohol concentration.

一方平行複発酵においては、スラッジ状態でいわゆるも
ろみ発酵を行うが、発酵後に清澄ろ過の前行程として圧
搾ろ過装置などによる未消化物の除去を行う。しかし、
ここに反応液には身消化物が混在しているため清澄行程
におけるろ過装置の負担が大きくなり、ろ過膜の目詰ま
りが起り易いという問題ちあった。
On the other hand, in parallel multiple fermentation, so-called mash fermentation is performed in a sludge state, and after fermentation, undigested materials are removed using a squeeze filter or the like as a step before clarifying filtration. but,
However, since the reaction solution contains digested meat, the burden on the filtration equipment during the clarification process becomes heavy, and the filtration membrane is likely to become clogged.

(発明の目的) 本発明は、このような事情に鑑みなされたものであり、
大豆をベースとする豆穀類を用いてワインを能率良く製
造することができ、またアルコール濃度の管理がし易く
、ろ過装置の負担も少なくすることが可能なワインの製
造方法を提供することを目的とする。
(Object of the invention) The present invention has been made in view of the above circumstances,
The purpose of the present invention is to provide a method for producing wine that can efficiently produce wine using legumes based on soybeans, and that also allows for easy control of alcohol concentration and reduces the burden on filtration equipment. shall be.

(発明の構成) 本発明によればこの目的は、低含水率状態で大豆および
米を含む豆穀類を微粉細化して消化反応させた後、この
反応液から未消化成分を除き、アルコール発酵させるこ
とを特徴とする大豆をベースとしたワインの製造方法に
より達成される。
(Structure of the Invention) According to the present invention, this purpose is to pulverize legumes including soybeans and rice in a low water content state and subject them to a digestion reaction, and then remove undigested components from this reaction solution and carry out alcohol fermentation. This is achieved by a soybean-based wine production method characterized by:

(実施例) 第1図は本発明の一実施例の工程図である。(Example) FIG. 1 is a process diagram of an embodiment of the present invention.

まず丸大豆や米などの豆穀類を適当量配合した後(第1
図、ステップ100)、これを70〜110°C(好ま
しくは105°C)に加熱し乾燥しつつ、高速ミキサー
により微粉細化する(ステップ102)。この微粉細化
した原料に適量の水とコウジ菌を添加し、35〜70°
C(好ましくは55’ C)に保って2〜10日間(好
ましくは4日)高温消化反応を行う(ステップ104)
。ここに原料は微粉細化され、かつ高温に保たれている
ので、消化反応は迅速に進行し、コウジ菌中のアミラー
ゼやプロテアーゼなどの酵素反応が速やかに進み、後記
アルコール発酵の基質となるグルコースや各種アミノ酸
が得られる。
First, after adding an appropriate amount of legumes such as whole soybeans and rice (first step)
Figure 1, step 100), while heating and drying this at 70 to 110°C (preferably 105°C), it is pulverized using a high-speed mixer (step 102). Add an appropriate amount of water and Aspergillus to this finely powdered raw material, and
C (preferably 55' C) and perform a high temperature digestion reaction for 2 to 10 days (preferably 4 days) (step 104)
. Since the raw materials are finely divided and kept at a high temperature, the digestive reaction proceeds quickly, and enzymatic reactions such as amylase and protease in Aspergillus aspergillus proceed rapidly, resulting in the production of glucose, which becomes the substrate for alcoholic fermentation as described below. and various amino acids can be obtained.

また後記のアルコール発酵におけるアルコール濃度は、
この消化反応によって進行する糖化の程度による影響を
大きく受けるので、このステップ104における消化反
応の度合を反応日数あるいは原料の配合割合、温度等に
より管理することができ、これにより生成アルコール濃
度の管理が可能になる。
In addition, the alcohol concentration in the alcoholic fermentation described below is
Since it is greatly influenced by the degree of saccharification that progresses through this digestive reaction, the degree of the digestive reaction in step 104 can be controlled by the number of reaction days, the blending ratio of raw materials, temperature, etc., and thereby the concentration of alcohol produced can be controlled. It becomes possible.

次に、前記の消化反応の後、ろ過装置によって未消化物
を除去する(ステップ106)。このろ過装置は高分子
膜、セラミック膜等の精密ろ過膜や、高分子限外ろ過膜
などの膜を用いて固液分離を行うものであり、ここで得
られるる液を用いて行う後記アルコール発酵後の清澄ろ
過行程(ステップ112)においては、未消化物が除去
されているから、ろ過装置の負担の軽減につながる。
Next, after the above-mentioned digestion reaction, undigested substances are removed by a filtration device (step 106). This filtration device performs solid-liquid separation using microfiltration membranes such as polymer membranes and ceramic membranes, and membranes such as polymer ultrafiltration membranes. In the clarification filtration step (step 112) after fermentation, undigested substances are removed, which leads to a reduction in the burden on the filtration device.

さらにここで分離された未消化物は再び高温消化反応の
工程(ステップ104)に戻して再利用してもよい(ス
テップ108)。
Furthermore, the undigested material separated here may be returned to the high temperature digestion reaction step (step 104) and reused (step 108).

ろ過されて未消化物が除去されたろ液は特定の酵母によ
りアルコール発酵される(ステップ110)。この反応
は20〜356C(好ましくは25°C)の温度の下で
、2〜10日間(好ましくは3日間)、嫌気雰囲気の下
で行われる。また−層まろやかな熟成を行う場合には、
温度を5〜20’C(好ましくは10’C)で長期間(
lか月〜2か月)発酵させるとよい。
The filtrate from which undigested substances have been removed is subjected to alcohol fermentation by specific yeast (step 110). This reaction is carried out under an anaerobic atmosphere at a temperature of 20-356C (preferably 25C) for 2-10 days (preferably 3 days). In addition, when performing layer-mellow aging,
Keep the temperature at 5-20'C (preferably 10'C) for a long period of time (
It is best to ferment for 1 month to 2 months).

ここに用いる酵母は、大豆を主体とする原料に対して優
れたワイン香を生成する酵母であって、スクリーニング
の結果、例えば味噌や醤油関連の酵母が好適であること
が解った。すなわち、チゴサッ力ロマイセス ルーキシ
− (Z  osaccharom ces rouxii
 )、キャンデイグ ベルサティリス (C,Versatilis) 等である。
The yeast used here is a yeast that produces an excellent wine aroma for raw materials mainly composed of soybeans, and as a result of screening, it was found that yeasts related to miso and soy sauce, for example, are suitable. That is, Z osaccharom ces rouxii
), Candaig Versatilis (C, Versatilis), etc.

また酸味の添加についてはアルコール発酵に加えて、例
えば乳酸菌 ベディオコシウス ハロフィヒス (Pediococius Iセ止恒工鋤1を使っても
よい。
For addition of sourness, in addition to alcoholic fermentation, for example, lactic acid bacterium Pediococius I may be used.

(発明の効果) 本発明は以上のように、大豆を含む豆穀類を低含水率状
態で微粉細化して消化反応を行い、その反応液から未消
化成分を除去した後アルコール発酵を行わせるものであ
り、消化反応とアルコール発酵とを2段階に分けて反応
させるものである。
(Effects of the Invention) As described above, the present invention involves pulverizing legumes including soybeans in a low moisture content state, performing a digestive reaction, removing undigested components from the reaction liquid, and then performing alcoholic fermentation. The reaction is carried out in two stages: digestive reaction and alcoholic fermentation.

従ってそれぞれの反応に好ましい反応条件下で能率よく
反応させることができ、ワインの生産能率が向上する。
Therefore, each reaction can be efficiently carried out under favorable reaction conditions, and wine production efficiency is improved.

また消化反応における糖化の程度を管理することにより
、アルコール度の管理が可能である。
Furthermore, the alcohol content can be controlled by controlling the degree of saccharification in the digestive reaction.

さらに未消化物は消化反応終了時点でろ過分離4゜ するから、アルコール発酵の段階では不要な未消化物が
含まれずアルコール発酵が十分かつ能率よく行われると
共に、アルコール発酵後のろ過装置の負担が軽くなり、
トータルな視点からみてコスト低減に適する。
Furthermore, since undigested substances are filtered and separated by 4 degrees at the end of the digestion reaction, unnecessary undigested substances are not included during the alcohol fermentation stage, and alcohol fermentation is carried out sufficiently and efficiently, and the burden on the filtration equipment after alcohol fermentation is reduced. become lighter,
Suitable for cost reduction from a total perspective.

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

第1図は本発明の一実施例の工程図である。 FIG. 1 is a process diagram of an embodiment of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 低含水率状態で大豆および米を含む豆穀類を微粉細化し
て消化反応させた後、この反応液から未消化成分を除き
、アルコール発酵させることを特徴とする大豆をベース
としたワインの製造方法。
A method for producing soybean-based wine, which comprises pulverizing legumes including soybeans and rice in a low water content state and subjecting them to a digestive reaction, removing undigested components from the reaction solution, and carrying out alcohol fermentation. .
JP1224678A 1989-09-01 1989-09-01 Wine making Pending JPH0391474A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1224678A JPH0391474A (en) 1989-09-01 1989-09-01 Wine making

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1224678A JPH0391474A (en) 1989-09-01 1989-09-01 Wine making

Publications (1)

Publication Number Publication Date
JPH0391474A true JPH0391474A (en) 1991-04-17

Family

ID=16817509

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1224678A Pending JPH0391474A (en) 1989-09-01 1989-09-01 Wine making

Country Status (1)

Country Link
JP (1) JPH0391474A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102899223A (en) * 2012-11-16 2013-01-30 崔承禄 Nutritive and health-care natto essence wine and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102899223A (en) * 2012-11-16 2013-01-30 崔承禄 Nutritive and health-care natto essence wine and preparation method thereof

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