JP2000228972A - Production of alcoholic beverage hardly having adverse effect on human liver - Google Patents

Production of alcoholic beverage hardly having adverse effect on human liver

Info

Publication number
JP2000228972A
JP2000228972A JP3296699A JP3296699A JP2000228972A JP 2000228972 A JP2000228972 A JP 2000228972A JP 3296699 A JP3296699 A JP 3296699A JP 3296699 A JP3296699 A JP 3296699A JP 2000228972 A JP2000228972 A JP 2000228972A
Authority
JP
Japan
Prior art keywords
water
reactor
viscosity
human liver
alcoholic beverage
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.)
Withdrawn
Application number
JP3296699A
Other languages
Japanese (ja)
Inventor
Hee Jung Kim
ヒ ジョン キム
Myoung Soo Shin
ミョン ス シン
Sang Chul Park
サン チョル バク
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP3296699A priority Critical patent/JP2000228972A/en
Publication of JP2000228972A publication Critical patent/JP2000228972A/en
Withdrawn legal-status Critical Current

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  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Alcoholic Beverages (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for producing alcohol beverage hardly having adverse effect on human liver. SOLUTION: This method for producing alcoholic beverage comprises multistage process obtaining low-viscosity water used for production of alcoholic beverage hardly having adverse effect on human liver. The process is constituted of plural individual batch type processes and a product having viscosity lower than a product obtained by process in previous stage is obtained in each subsequent process. The first process is carried out by passing electric current through water free from electrolyte and water having low viscosity is obtained thereby. As a result, the discharged water is put into a serial type batch type energy-feeding reactor. In this time, water is continuously irradiated with far- infrared rays for a definite retention time in each reactor. A housing vessel is provided in each batch type reactor and a proper amount of water can be discharged from the reactor.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明はアルコール飲料の製
造方法、特にアルコール飲料の製造時に照射処理及び電
気分解された水を用いる方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing alcoholic beverages, and more particularly to a method for producing alcoholic beverages by using irradiation-treated and electrolyzed water.

【0002】[0002]

【従来の技術】通常、アルコール飲料は人体の肝臓に蓄
積する脂肪含量に与えるアルコールの影響により副作用
があると知られている。この分野の公知技術で、前記の
問題を解決するための具体的な方法が発表された。アル
コール含有量は微々たるものであるが、アルコールの味
が出る無アルコール飲料が公知技術で開示された。この
解決方法は、飲酒者が身体又は精神的に得られるアルコ
ールの他の効果を選択するため、常に満足できる方法で
はない。さらに、アルコール含量がないため飲料の味が
美味しいだろうとの確信がない。
2. Description of the Related Art Generally, alcoholic beverages are known to have side effects due to the effect of alcohol on the fat content accumulated in the liver of the human body. Specific methods for solving the above problems have been disclosed in the art known in the art. Although the alcohol content is insignificant, non-alcoholic beverages with a taste of alcohol have been disclosed in the prior art. This solution is not always satisfactory because the drinker chooses other effects of the alcohol that can be obtained physically or mentally. Furthermore, there is no certainty that the taste of the beverage will be delicious due to the lack of alcohol content.

【0003】水(H2 O)は直線でない折曲状の構造で
なる極性分子である。普通の液体状で水の極性のため分
子間に水素結合が生じるとき、水の分子群(塊)が形成
される。この群は水の流れを妨害して水の粘度を増加さ
せる。水の粘度を低めるため水の分子群を分解すれば、
この群の実際の大きさが縮小されるはずである。その結
果、分解された水の分子群はそれまでの凝集した水の分
子群より一段と極性が大きくなり、従って、血管を通過
する脂肪粒子等に対し高い親和力を示す。この分野の公
知技術では、本願発明で開示したものと類似の方法が発
表されたことがない。よって、この方法は今まで明かに
されたことのない新規のものである。
[0003] Water (H 2 O) is a polar molecule having a bent structure that is not linear. When hydrogen bonds occur between molecules due to the polarity of water in an ordinary liquid state, water molecules (lumps) are formed. This group obstructs the flow of water and increases the viscosity of the water. If you break down the water molecules to lower the viscosity of the water,
The actual size of this group should be reduced. As a result, the molecules of the decomposed water have a greater polarity than the molecules of the water that have been aggregated, and thus have a higher affinity for fat particles and the like passing through the blood vessels. In the prior art in this field, a method similar to that disclosed in the present invention has not been published. Thus, this method is a new one that has never been revealed.

【0004】[0004]

【発明が解決しようとする課題】従って、本願発明の主
な目的は人体の肝臓に対する副作用の少ないアルコール
飲料を製造する方法を提供することである。さらに、高
価の装備が必要なく水の粘度を低下させる方法を提供す
ることも、本発明のさらに他の目的である。
SUMMARY OF THE INVENTION Accordingly, it is a primary object of the present invention to provide a method for producing an alcoholic beverage having less side effects on the human liver. It is yet another object of the present invention to provide a method for reducing the viscosity of water without the need for expensive equipment.

【0005】[0005]

【課題を解決するための手段】本発明は、人体の肝臓に
対し副作用の少ないアルコール飲料を得る方法に関す
る。この方法は通常醗酵工程で用いる一般的な蒸留濾過
水の代りに、特殊製造された水を用いてアルコール飲料
を従前通り製造する方法である。
SUMMARY OF THE INVENTION The present invention relates to a method for obtaining an alcoholic beverage having less side effects on the liver of the human body. This method is a method for producing an alcoholic beverage by using specially produced water instead of general distilled and filtered water used in the fermentation process.

【0006】特殊な水の製造方法は、低粘度の水を得る
多段階工程を含む。この工程は複数の個別バッチ式プロ
セスで構成され、この時、後続のプロセスでは前段階の
プロセスで得られた生成物より低い粘度の生成物が得ら
れる。一回目のプロセスは、電解質が存在しない水に電
流を通過させ低粘度の水を得ることである。これは、水
素結合により形成された水の分子群の大きさを減少させ
ると達成することができる。水の分子群の大きさの縮小
は水を電気分解すれば達成できる。水を電気分解すれ
ば、水の分子間の水素結合が破壊されて水の分子群を分
解することができ、従って水の粘度が減少する。この結
果、得られた水を再び直列のバッチ式エネルギー供給反
応器に供給し、これにより、水は各バッチ式反応器で一
定の滞留時間の間遠赤外線で連続照射処理され、その結
果、各反応器で低粘度の生成物が得られる。
[0006] Special water production processes include a multi-step process to obtain low viscosity water. This step consists of a plurality of individual batch processes, where the subsequent process results in a lower viscosity product than the product obtained in the previous process. The first process is to pass an electric current through the electrolyte-free water to obtain a low viscosity water. This can be achieved by reducing the size of the water molecules formed by hydrogen bonding. Reduction of the size of the water molecules can be achieved by electrolysis of water. When water is electrolyzed, the hydrogen bonds between the water molecules are broken and the water molecules can be decomposed, thus reducing the viscosity of the water. As a result, the obtained water is fed again to the batch-type batch energy supply reactor, whereby the water is continuously irradiated with far infrared rays in each batch-type reactor for a certain residence time, and as a result, A low viscosity product is obtained in the reactor.

【0007】最終収容器から出た流出物は、従来の醸造
工程の順序図に従い供給され、この結果物として飲酒の
際、人体の肝臓に対する副作用の少ない生成物を得るこ
とができる。
[0007] The effluent discharged from the final container is supplied in accordance with the flow chart of the conventional brewing process, and as a result, it is possible to obtain a product having less side effects on the human liver during drinking.

【0008】従来の醸造工程は、麦芽(水飴)処理され
た麦及びそれ以外の穀物を製粉機で粉砕する方法を含
む。“醸造用水飴(grist)”で知られている麦芽
をマッシュ(mash)型酒樽で熱い水と混合すれば、
麦芽内の酵素が澱粉を醗酵性及び非醗酵性糖に転換させ
ることができる。その結果出た甘い液体を“麦芽汁”と
いい、これが煮沸釜内に供給される。この液体が、釜の
中に入る供給段階で時間間隔を置いてホップを添加す
る。選別されたホップのオイル液がエール(ale)と
ラガー液の味と香り及び濃度に影響を及ぼす。ホップ処
理された麦芽汁を冷却して醗酵タンクにポンプ注入し、
この時イーストを添加すれば醗酵反応が開始される。イ
ーストは醗酵性糖をアルコールと二酸化炭素に転換さ
せ、その反面、非醗酵性糖は液体状に残り飲料の味付け
に寄与する。3〜5日が経過すると活性醗酵工程が終了
し、その後タンクを密封して液体を自然炭素化反応(熟
成)させる。活性醗酵工程での反応終結は、タンク内の
液体の比重を測定すれば決定することができる。このよ
うな主要製造段階以外にも特殊な醸造法や、望む生成物
の種類に従いさらに他の濾過及び処理用タンクを用いる
こともできる。本発明の用いられるアルコール飲料は、
特に限定されず、ビール、ワイン、日本酒、泡盛、焼
酎、ウイスキー、ウォッカ、ブランデー、ラム、ジン、
カオリャンチュー、パイカル、リキュール、各種カクテ
ル等を含む。
[0008] The conventional brewing process includes a method in which malt (sugar syrup) -treated barley and other grains are pulverized by a mill. If malt known as "grist for brewing (grist)" is mixed with hot water in a mash type keg,
Enzymes in the malt can convert starch into fermentable and non-fermentable sugars. The resulting sweet liquid is called "wort", which is fed into a boiling pot. Hops are added at time intervals during the feed phase where the liquid enters the kettle. The selected hop oil solution affects the taste, aroma and concentration of the ale and lager solution. Cool the hop-treated wort and pump it into the fermentation tank,
At this time, if yeast is added, the fermentation reaction is started. Yeast converts fermentable sugars to alcohol and carbon dioxide, while non-fermentable sugars remain liquid and contribute to the flavoring of beverages. After 3 to 5 days, the active fermentation process is completed, and then the tank is sealed and the liquid is allowed to undergo a natural carbonization reaction (aging). The end of the reaction in the active fermentation step can be determined by measuring the specific gravity of the liquid in the tank. Apart from these main production steps, special brewing methods and further filtration and processing tanks can be used depending on the type of product desired. The alcoholic beverage used in the present invention,
Not particularly limited, beer, wine, sake, awamori, shochu, whiskey, vodka, brandy, rum, gin,
Includes Kaoliangchu, pikal, liqueur, various cocktails, etc.

【0009】これ以外の他の目的とともに、前記内容を
添付の特許請求の範囲でさらに具体的に説明する。本発
明をさらによく理解するため、本発明を利用して達成し
た操作上の長所と特別な目的等は、添付の図面と具体的
な実施例を参照してさらに詳しく説明する。本発明の原
理と特性は、次の添付図面と詳しい説明を参照すれば一
層よく理解できる。
[0009] The above content, together with other objects, will be more specifically described in the appended claims. For a better understanding of the present invention, operational advantages and special objects achieved by using the present invention will be described in more detail with reference to the accompanying drawings and specific embodiments. The principles and characteristics of the present invention may be better understood with reference to the following drawings and detailed description.

【0010】[0010]

【発明の実施の形態】図1を参照すれば、本発明の水の
製造方法は複数のバッチ式プロセスでなる多段階工程で
あり、全工程の各段階で得られた生成物は、引続き後続
のバッチ式プロセスに供給される。一回目のバッチ式プ
ロセスは、水に電流を通過させることを含む。使用され
た水は濾過することが好ましく、塩類のように溶存汚染
物が存在する水は酸素が完全飽和され得ないため、水中
の酸素含有量を最大化するためには電解質や汚染物が水
中に含まれてはならない。電流の電圧は約50乃至10
0Vが好ましい。この方法は、電流効果を最大化するた
め複数の陰極及び陽極リード線を用いることができる。
さらに、攪拌機を用いれば全溶液に最大限露出させるこ
とができるため反応に有利である。この段階では流体の
動作を妨害し、溶液の粘度増加の原因となる水の分子群
を分解して低粘度の生成物を得ることができる。
DETAILED DESCRIPTION OF THE INVENTION Referring to FIG. 1, the method for producing water of the present invention is a multi-step process comprising a plurality of batch processes, and the products obtained at each stage of the entire process are continuously Supplied to a batch process. The first batch process involves passing an electric current through the water. The water used is preferably filtered, and water containing dissolved contaminants, such as salts, cannot be completely saturated with oxygen.In order to maximize the oxygen content in the water, electrolytes and contaminants must be removed from the water. Must not be included. The current voltage is about 50 to 10
0V is preferred. This method can use multiple cathode and anode leads to maximize the current effect.
Furthermore, the use of a stirrer is advantageous for the reaction because it can be exposed to the entire solution to the maximum. At this stage, a low-viscosity product can be obtained by decomposing water molecules that interfere with the operation of the fluid and cause an increase in the viscosity of the solution.

【0011】二回目のバッチ式プロセスは、数個の遠赤
外線電極を取付けたバッチ式プロセスタンク反応器であ
るエネルギー供給反応器を含む。この電極はタンクに沿
って位置し水に最大限露出する。一回目のバッチ式プロ
セスで得られた流出物はエネルギー供給反応器に流入
し、ここで水は電極が放出した遠赤外線、特には変化波
長の遠赤外線により照射処理される。さらに、遠赤外線
による照射処理は塊状となった水の分子等の間の水素結
合を破壊するエネルギーを供給して露出した水の粘度減
少に実質的効果を示し、さらに妨害となる水の分子群の
大きさを縮小させて水の粘度を減少することができる。
The second batch process involves an energy supply reactor which is a batch process tank reactor fitted with several far infrared electrodes. This electrode is located along the tank and has maximum exposure to water. The effluent obtained from the first batch process flows into the energy supply reactor, where the water is irradiated with far-infrared rays emitted by the electrodes, in particular far-infrared rays of varying wavelength. In addition, the irradiation treatment with far-infrared rays has a substantial effect on reducing the viscosity of exposed water by supplying energy that breaks hydrogen bonds between agglomerated water molecules, etc. Can be reduced to reduce the viscosity of the water.

【0012】エネルギー供給反応器は直列に配置し、一
反応器から出た流出物は連続の工程順に従い後続の反応
器に流入される。水の粘度変化量は遠赤外線に露出され
る滞留時間と比例する。さらに他の反応器を工程順に追
加できるが、各後続反応器での効率性が大きく減少す
る。
[0012] The energy supply reactors are arranged in series, and the effluent from one reactor flows into the subsequent reactor according to a continuous process sequence. The amount of change in viscosity of water is proportional to the residence time exposed to far infrared rays. Still other reactors can be added in process order, but the efficiency in each subsequent reactor is greatly reduced.

【0013】4回目の反応器から出た流出物は、溶液の
pHを調節するため塩基性又は酸性化合物を供給するp
H調節用ベッセルに流入させることができる。4回目の
反応器から出た流出物は、さらに活性塩電極、特には、
水に溶解しない塩電極が取付けられた反応器に供給する
こともできる。
[0013] The effluent from the fourth reactor is supplied with a basic or acidic compound to adjust the pH of the solution.
It can flow into the H adjusting vessel. The effluent from the fourth reactor is further separated by an active salt electrode, especially
It can also be fed to a reactor equipped with a water-insoluble salt electrode.

【0014】[0014]

【発明の効果】本願発明は、低粘度の水を得る多段階工
程を介して得た特殊な水を利用してアルコール飲料を製
造し、この時の飲料は飲酒の際人体の肝臓に対し副作用
が少ない効果を有する。
According to the present invention, an alcoholic beverage is manufactured using special water obtained through a multi-step process of obtaining low-viscosity water, and the beverage at this time has a side effect on the human liver when drinking. Has less effect.

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

【図1】 人体の肝臓に対する副作用の少ないアルコー
ル飲料の製造に用いられる水を製造する工程を示すフロ
ー図である。
FIG. 1 is a flow chart showing a process for producing water used for producing an alcoholic beverage having few side effects on a human liver.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) // A61P 1/16 A61K 31/00 601K (72)発明者 シン ミョン ス 大韓民国 136−020 ソウル ソンブック ソンブッドン 8−16 (72)発明者 バク サン チョル 大韓民国 137−044 ソウル ソチョグ バンポ 4ドン ドンクワン−ビラ 101 Fターム(参考) 4B015 AG17 BA01 CG01 LH12 MA04 NG17 4D061 DA01 DA10 DB20 EA02 EB02 ED20 FA07 FA11 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification FI FI Theme Court ゛ (Reference) // A61P 1/16 A61K 31/00 601K (72) Inventor Shin Myung-soo Korea 136-020 Seoul Songbook Songbudong 8-16 (72) Inventor Bak Sang-cheol South Korea 137-044 Seoul Seochogu Bampo 4 Dong Dongkwan-Villa 101 F-term (reference) 4B015 AG17 BA01 CG01 LH12 MA04 NG17 4D061 DA01 DA10 DB20 EA02 EB02 ED20 FA07 FA11

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】(a)水を濾過し、 (b)この水を、陰極と陽極を利用して50乃至100
V電圧の電流で電気分解し、 (c)この水を、再び遠赤外線で照射処理することを特
徴とするアルコール飲料製造に用いられる水の製造方
法。
(A) filtering water; and (b) dissolving the water by using a cathode and an anode.
(C) irradiating the water again with far infrared rays to produce water used for producing alcoholic beverages.
【請求項2】水を変化波長の遠赤外線で照射処理するこ
とを特徴とする請求項1記載のアルコール飲料製造に用
いられる水の製造方法。
2. The method for producing water used in the production of alcoholic beverages according to claim 1, wherein the water is irradiated with far-infrared rays having a variable wavelength.
【請求項3】水のpH値を調節することを特徴とする請
求項1または2に記載のアルコール飲料製造に用いられ
る水の製造方法。
3. The method according to claim 1, wherein the pH of the water is adjusted.
【請求項4】水を塩電極に供給することを特徴とする請
求項1〜3のいずれかに記載のアルコール飲料製造に用
いられる水の製造方法。
4. The method according to claim 1, wherein the water is supplied to the salt electrode.
【請求項5】水を水に溶解しない塩電極に供給すること
を特徴とする請求項4記載のアルコール飲料製造に用い
られる水の製造方法。
5. The method according to claim 4, wherein the water is supplied to a salt electrode that does not dissolve in the water.
JP3296699A 1999-02-10 1999-02-10 Production of alcoholic beverage hardly having adverse effect on human liver Withdrawn JP2000228972A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3296699A JP2000228972A (en) 1999-02-10 1999-02-10 Production of alcoholic beverage hardly having adverse effect on human liver

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3296699A JP2000228972A (en) 1999-02-10 1999-02-10 Production of alcoholic beverage hardly having adverse effect on human liver

Publications (1)

Publication Number Publication Date
JP2000228972A true JP2000228972A (en) 2000-08-22

Family

ID=12373663

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3296699A Withdrawn JP2000228972A (en) 1999-02-10 1999-02-10 Production of alcoholic beverage hardly having adverse effect on human liver

Country Status (1)

Country Link
JP (1) JP2000228972A (en)

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Legal Events

Date Code Title Description
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Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20060509