JP2009219490A - Method for producing fermented liquor - Google Patents

Method for producing fermented liquor Download PDF

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JP2009219490A
JP2009219490A JP2009059004A JP2009059004A JP2009219490A JP 2009219490 A JP2009219490 A JP 2009219490A JP 2009059004 A JP2009059004 A JP 2009059004A JP 2009059004 A JP2009059004 A JP 2009059004A JP 2009219490 A JP2009219490 A JP 2009219490A
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fermentation
fermented liquor
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fermentable sugar
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Sonkuan Yomu
ソンクァン ヨム
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12GWINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
    • C12G3/00Preparation of other alcoholic beverages
    • C12G3/02Preparation of other alcoholic beverages by fermentation
    • C12G3/021Preparation of other alcoholic beverages by fermentation of botanical family Poaceae, e.g. wheat, millet, sorghum, barley, rye, or corn
    • C12G3/022Preparation of other alcoholic beverages by fermentation of botanical family Poaceae, e.g. wheat, millet, sorghum, barley, rye, or corn of botanical genus Oryza, e.g. rice
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12GWINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
    • C12G3/00Preparation of other alcoholic beverages
    • C12G3/04Preparation of other alcoholic beverages by mixing, e.g. for preparation of liqueurs
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12HPASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
    • C12H1/00Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages
    • C12H1/02Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages combined with removal of precipitate or added materials, e.g. adsorption material

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a fermented liquor capable of maintaining carbon dioxide by a prescribed pressure in its product because of utilizing living yeasts in a seasoned liquid by adding a fermenting sugar necessary for the generation of an objective carbonic acid (carbon dioxide) pressure in a not heat-treated state and post-fermenting. <P>SOLUTION: This method for producing the fermented liquor includes a first process as a one stage preparation process, a second process as a two stage preparation process, a third process of seasoning by adding an acid material and a sweet material after filtering and diluting, a fourth process of adding the fermenting sugar to the seasoned liquid without heat-treating and a fifth process of performing post fermentation, or after adding the fermenting sugar to the seasoned liquid, injecting the liquid into a heat resistant and pressure resistant container and then capable of performing hermetical sealing with a cap and the post-fermentation. Also, it is possible to further include a sixth process of sterilizing the product completing the post fermentation while housing the liquid in the container for performing the fifth process. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、発酵酒の製造方法に関する。   The present invention relates to a method for producing fermented liquor.

発酵酒とは、穀類、さつまいも、果実汁などを糖化及び発酵して作った濁った酒、又は、これらを濾過した澄んだ酒を意味する。発酵酒は、製造形式によって、単発酵式と複発酵式とに分けられる。単発酵式は、葡萄酒のように直接糖類を原料にして酵母でアルコール発酵させる方式であり、複発酵式は、澱粉を原料にして第1工程でアミラーゼ(amylase)で糖化をし、第2工程でアルコール発酵を行う方式である。複発酵の場合、糖化とアルコール発酵とを製造工程において独立させる2工程で行なう方式を並行複発酵式という。   Fermented liquor means turbid liquor made by saccharifying and fermenting cereals, sweet potatoes, fruit juice, etc., or clear liquor obtained by filtering these. Fermented liquor is divided into a single fermentation type and a double fermentation type depending on the production format. The simple fermentation method is a method in which saccharides are directly fermented using yeast as a raw material, such as sake, while the double fermentation method is saccharified with amylase in the first step using starch as a raw material, and the second step. In this method, alcohol fermentation is performed. In the case of double fermentation, a method of performing saccharification and alcohol fermentation in two steps, which are independent in the production process, is called a parallel double fermentation method.

穀類を原料にした発酵酒の製造工程については、澱粉質自体はそのまま発酵されることはないため、澱粉糖化酵素であるジアスターゼ(diastase)を入れて澱粉を糖化させ酵母で発酵させる。このとき、二酸化炭素は遊離され、アルコール成分だけが生成され、この液が発酵酒となる。   As for the production process of fermented liquor using cereals as raw materials, the starch itself is not fermented as it is, and therefore, starch is saccharified to saccharify the starch and ferment with yeast. At this time, carbon dioxide is liberated and only the alcohol component is produced, and this liquid becomes fermented liquor.

発酵とは、酵母菌(Yeast)が分泌する酵素を触媒として作用させて、糖類が加水分解されアルコールと炭酸ガスに置換されることをいう。
発酵酒中の香味成分は、発酵原料、微生物の種類、発酵条件、濾過方法、熟成期間によって異なるため、品質管理には高度の技術を要する。
Fermentation means that an enzyme secreted by yeast (Yeast) is allowed to act as a catalyst to hydrolyze sugars and replace them with alcohol and carbon dioxide.
Since flavor components in fermented liquor vary depending on fermentation raw materials, types of microorganisms, fermentation conditions, filtration methods, and ripening periods, advanced techniques are required for quality control.

既存の方法では、発酵が完了した発酵液を篩を利用して濾過しボトルに入れた後、人為的に炭酸を注入してからキャップで密封し、発酵が進行中の発酵液をボトルに入れられている。しかし、この時発生する二酸化炭素が特殊製作されたキャップを通過して連続的に外部に排出されるので、時間が経過するにつれて、発生する二酸化炭素に比べ排出される二酸化炭素の量が多くなって容器内のガス圧が低くなる等、品質の劣化が起こるという問題があった。   In the existing method, the fermented liquor that has been fermented is filtered using a sieve and put into a bottle, and then artificially injected with carbonic acid and sealed with a cap, and the fermented liquor undergoing fermentation is put into the bottle. It has been. However, since the carbon dioxide generated at this time passes through a specially manufactured cap and is continuously discharged to the outside, the amount of carbon dioxide discharged increases as time passes. As a result, the gas pressure in the container is lowered, resulting in a problem of quality deterioration.

本発明による発酵酒の製造方法によれば、調味が完了した液に生存している酵母をそのまま利用するために、熱処理していない状態で、要求される炭酸圧の発生に必要な適当量の発酵性糖を添加して、キャップで密封した状態で後発酵を施すため、製品を出荷した後も二酸化炭素がボトルの外部に流出するのを防止し、品質の維持を図ることができ、消費者が常に清涼感を感じられる製品を供給することができる。   According to the method for producing fermented liquor according to the present invention, in order to use the yeast that is alive in the liquid whose seasoning has been completed as it is, an appropriate amount necessary for generating the required carbonic acid pressure without being heat-treated. Since fermentable sugar is added and post-fermentation is performed in a state sealed with a cap, carbon dioxide can be prevented from flowing out of the bottle even after the product is shipped, and quality can be maintained. Can always supply products with a refreshing feeling.

特許文献1には、もち米と米麹と醸造用酵素剤を水と混合して酵母を加え培養して酒母をつくり、この酒母にもち米と米麹と水と醸造用酵素剤とを複数回加えて、活性の酵母が豊富に存在する白濁状で炭酸ガスの溶存する発酵酒を製造する製造方法が開示されている。   In Patent Document 1, glutinous rice, rice bran and brewing enzyme are mixed with water, yeast is added and cultured to produce a liquor mother. In addition, a production method is disclosed for producing a fermented liquor in which the active yeast is abundant and is cloudy and in which carbon dioxide is dissolved.

特開昭58−5182号公報Japanese Patent Laid-Open No. 58-5182

本発明の目的は、調味した液中の生きている酵母をそのまま利用するために、熱処理していない状態で、目的とする炭酸圧の発生に必要な発酵性糖を添加して後発酵することにより、製品内に一定圧の炭酸ガスを維持できる発酵酒の製造方法を提供することにある。   The purpose of the present invention is to post-ferment by adding fermentable sugar necessary for generating the target carbonic acid pressure without heat treatment in order to use live yeast in the seasoned liquid as it is. Therefore, it is providing the manufacturing method of fermented liquor which can maintain the carbon dioxide gas of a fixed pressure in a product.

上記本発明の目的を達成するために、本発明は、蒸煮器(市販されている米蒸し用蒸し器)を利用して白米で強飯を作って、水と混合し、麹を入れた後、酒母を接種し、水を添加した後、25乃至30℃で24時間培養する1段仕込み工程としての第1工程、蒸煮器を利用して白米で強飯を作って、麹と共に、前記1段仕込み工程で培養された発酵液に添加してから、水を添加した後、25乃至30℃で5乃至7日間発酵する2段仕込み工程としての第2工程、篩を利用して濾過してから、最終アルコール濃度が3〜14%(v/v)になるように希釈した後、発酵性糖成分のない酸味料及び甘味料を添加して調味する第3工程、調味が完了した液に如何なる熱処理も無しに発酵性糖を添加する第4工程、及び7乃至38℃で1乃至48時間に亘って後発酵を実施する第5工程からなる発酵酒の製造方法を提供する。   In order to achieve the above object of the present invention, the present invention uses a steamer (commercially available steamer for rice steaming) to make boiled rice with white rice, mix with water, put rice cake, First step as a one-stage preparation process in which water is added and then cultured at 25 to 30 ° C. for 24 hours, making boiled rice with white rice using a steamer, and the first-stage preparation process with rice cake After adding to the fermentation broth cultivated in step 2, after adding water, the second step as a two-stage charging step of fermenting at 25-30 ° C. for 5-7 days, filtering using a sieve, and finally The third step of diluting the alcohol concentration to 3 to 14% (v / v) and then seasoning it with the addition of acidulant and sweetener without fermentable sugar components, any heat treatment to the seasoned liquid 4th step of adding fermentable sugar without, and 1 to 48 hours at 7 to 38 ° C Over to provide a method for manufacturing a fermented liquor made of the fifth step of performing a post-fermentation.

前記第3工程で発酵が完了すれば、発酵液中の発酵酵母と固形物質が沈殿して澄んだ上澄液ができる。この時、発酵液を適当な大きさ(メッシュ)の篩を利用して濾過してから、濾液のアルコール濃度、酵母数、糖濃度、酸度などを分析し、最終アルコール濃度が3〜14%(v/v)になるように希釈する。その後、発酵性糖成分のない酸味料と甘味料を添加して調味する。   When fermentation is completed in the third step, a fermented yeast and solid substances in the fermented liquid precipitate and a clear supernatant is obtained. At this time, the fermented liquor is filtered using a sieve of an appropriate size (mesh), and then the alcohol concentration, yeast number, sugar concentration, acidity, etc. of the filtrate are analyzed, and the final alcohol concentration is 3 to 14% ( Dilute to v / v). Thereafter, seasoning is performed by adding a sour agent and a sweetener free of fermentable sugar components.

前記第4工程で調味が完了した液に如何なる熱処理も施さない理由は、調味液中に生存している酵母を後発酵にそのまま利用するためである。また、前記第4工程で添加する発酵性糖の濃度は、最終製品に要求される炭酸圧によって決定すればよい。前記炭酸圧は0.02〜6Volであり、目的とする炭酸圧により決定されて添加される発酵性糖(直接還元糖)の濃度は0.01〜2.4%である。しかし、炭酸圧及び発酵性糖の濃度はこれに限られるものではなく、目的によって多様な条件で実施できる。   The reason why no heat treatment is applied to the liquid that has been seasoned in the fourth step is to use yeast that is alive in the seasoning liquid as it is for post-fermentation. Moreover, what is necessary is just to determine the density | concentration of the fermentable sugar added at the said 4th process with the carbonic acid pressure requested | required of a final product. The carbonic acid pressure is 0.02 to 6 Vol, and the concentration of fermentable sugar (direct reducing sugar) determined by the target carbonic acid pressure and added is 0.01 to 2.4%. However, the carbonic acid pressure and the fermentable sugar concentration are not limited to these, and can be carried out under various conditions depending on the purpose.

本発明において、前記第4工程は、調味が完了した液に熱処理無しに発酵性糖を添加した後、耐熱耐圧容器に注入してからキャップで密封することを特徴とすることができる。上記容器としては、ペットボトルを使用できる。
また、前記第5工程の後発酵の条件は望ましい実施のための一例であって、より多様な条件で実施できる。
In the present invention, the fourth step may be characterized in that after the fermentable sugar is added to the liquid that has been seasoned without heat treatment, it is poured into a heat and pressure resistant container and then sealed with a cap. A plastic bottle can be used as the container.
In addition, the post-fermentation conditions of the fifth step are examples for desirable implementation, and can be implemented under more various conditions.

本発明において、前記第5工程後、容器で後発酵が完了した製品を殺菌する第6工程をさらに含むことができる。殺菌条件は65℃で30分間とすることができるが、これは一例に過ぎず、当業界に公知となった多様な条件で実施できる。   The present invention may further include a sixth step of sterilizing the product that has been post-fermented in the container after the fifth step. The sterilization conditions can be 30 minutes at 65 ° C., but this is only an example and can be performed under various conditions known in the art.

本発明によれば、調味が完了した液中の生酵母をそのまま利用するために、熱処理を行わず、要求される炭酸圧の発生に必要な適当量の発酵性糖を添加してからキャップで密封した状態で後発酵を実施するため、製品を出荷した後も二酸化炭素がボトルの外部に流出せず消費者が常に清涼感を感じられる製品を供給できる。また、製品中の二酸化炭素の圧力は、添加する発酵性糖を調節することにより必要に応じていくらでも調節でき、耐熱耐圧容器(例えば、ペットボトル)の中で後発酵を実施してから殺菌するため、殺菌製品でも一定圧の二酸化炭素を維持できる。容器内に一定圧の二酸化炭素を維持できるため、生製品(非殺菌の製品)の製品寿命も延長できる。   According to the present invention, in order to use the live yeast in the liquid that has been seasoned as it is, the cap is added after adding an appropriate amount of fermentable sugar necessary for generating the required carbonic acid pressure without performing heat treatment. Since post-fermentation is performed in a sealed state, carbon dioxide does not flow out of the bottle even after the product is shipped, and a product that allows consumers to always feel a refreshing feeling can be supplied. In addition, the pressure of carbon dioxide in the product can be adjusted as much as necessary by adjusting the fermentable sugar to be added, and sterilized after post-fermentation in a heat and pressure resistant container (for example, a PET bottle). Therefore, a constant pressure of carbon dioxide can be maintained even in sterilized products. Since a constant pressure of carbon dioxide can be maintained in the container, the product life of raw products (non-sterile products) can be extended.

以下、非制限的な実施例によって本発明の技術的特徴をより詳しく説明する。これら実施例は、本発明を例示するためのものであって、本発明の範囲がこれら実施例により制限されると解釈されないことは、当業界について通常の知識を有する者にとって自明のことである。   Hereinafter, the technical features of the present invention will be described in more detail by way of non-limiting examples. These examples are intended to illustrate the present invention, and it is obvious to those skilled in the art that the scope of the present invention should not be construed as being limited by these examples. .

第1工程:1段仕込み工程
蒸煮器(市販されている米蒸し用蒸し器)を利用して白米780gで強飯を作って、水約3.5Lと混合し、麹(自社製造)265gを入れた。次に、ここに別途培養した酒母を接種し、最終体積が5Lになるように水を添加した後、25〜30℃で24時間培養した。酒母は、酵母(Saccharomyces cerevisiae)(自社保管)を大量に増殖培養したものを言う。
First step: One-stage preparation step Using a steamer (commercially available steamer for rice steaming), cooked rice with 780 g of white rice, mixed with about 3.5 L of water, and put 265 g of koji (manufactured in-house) . Next, separately cultivated liquor mothers were inoculated here, water was added so that the final volume was 5 L, and then cultured at 25 to 30 ° C. for 24 hours. A liquor is a product obtained by growing and cultivating yeast (Saccharomyces cerevisiae) (stored in-house) in large quantities.

第2工程:2段仕込み工程及び本発酵
白米1.82kgを称量して1段仕込みの時と同様に強飯を作って、麹0.66kgと共に、1段仕込みによって培養された発酵液に添加してから、最終体積が15Lになるように水を添加した。25〜30℃で5〜7日間発酵した。
Second step: Two-step charging step and main fermentation 1.82 kg of white rice is used to make strong rice in the same manner as in the first step, and added to the fermentation broth cultured by one-step charging together with 0.66 kg of rice cake Then, water was added so that the final volume was 15L. Fermented at 25-30 ° C for 5-7 days.

第3工程:発酵液の濾過、成分分析及び調味
発酵が完了すれば、発酵液中の発酵酵母と固形物質が沈殿して澄んだ上澄液ができる。この時、発酵液を適当な大きさ(メッシュ)の篩を利用して濾過してから、濾液のアルコール濃度、酵母数、糖濃度、酸度などを分析し、最終アルコール濃度が6%(v/v)になるように希釈した後、酸味料と甘味料(発酵性糖成分のないもの)を添加して調味した。
Third Step: Filtration of Fermentation Solution, Component Analysis and Seasoning When fermentation is completed, a fermented yeast and a solid substance in the fermentation solution are precipitated to form a clear supernatant. At this time, the fermentation broth is filtered using a sieve of an appropriate size (mesh), and then the alcohol concentration, yeast number, sugar concentration, acidity, etc. of the filtrate are analyzed, and the final alcohol concentration is 6% (v / After diluting to v), acidulant and sweetener (without fermentable sugar component) was added and seasoned.

アルコール濃度は、発酵液を蒸留して、比重計の原理を利用した酒精計(Hydrometer)によって測定した。酵母数は、ヘモサイトメーター(Hemacytometer)を利用して測定した。糖濃度は、ソモギー変法を利用して分析した。酸度は、0.1N NaOHで滴定(titration)して消費されたmlで表示した。上記調味液を分析した結果は、次の表の通りである。   The alcohol concentration was measured by a spirit meter (Hydrometer) using the principle of a hydrometer after distilling the fermentation broth. The number of yeasts was measured using a hemocytometer. The sugar concentration was analyzed using a modified somogy method. Acidity was expressed in ml consumed titrated with 0.1 N NaOH. The results of analyzing the seasoning liquid are as shown in the following table.

第4工程:発酵性糖の添加
調味が完了した液に生きている酵母をそのまま利用するために、熱処理無しに発酵性糖を0.6%又は1.0%添加して、添加後に糖濃度が0.81%又は1.21%になるようにした後、耐熱耐圧ペットボトル(商品名:斗山TechPack)に注入してからキャップで密封した。この時添加する糖の濃度は、最終製品に要求される炭酸圧によって、次の反応式から算出することができる。
12----→2COH+2CO
Fourth step: Addition of fermentable sugar In order to use live yeast as it is in the liquid whose seasoning has been completed, 0.6% or 1.0% of fermentable sugar is added without heat treatment, and the sugar concentration after addition After being adjusted to 0.81% or 1.21%, it was poured into a heat-resistant and pressure-resistant PET bottle (trade name: Doosan TechPack) and sealed with a cap. The concentration of the sugar added at this time can be calculated from the following reaction formula according to the carbonic acid pressure required for the final product.
C 6 H 12 O 6 ---- → 2C 2 H 5 OH + 2CO 2

葡萄糖1分子(180g)は、酵母により2分子のアルコールと2分子の二酸化炭素(理想気体の下で2×22.4Lの体積に該当)が発生する。1L容器を例に挙げて説明すれば、1Volに該当する二酸化炭素1Lを発生するためには、1/44.8分子の葡萄糖(180g×1/44.8=4.02g)が必要になる。即ち、約0.4%(W/V)の葡萄糖を添加すればよい。但し、実施例の表2から分かるように、添加した糖に該当する理論的な二酸化炭素の発生量よりも若干多い量の二酸化炭素が発生したのは、並行複発酵であるため、外観上は発酵が完了したように見えても、実際は発酵液中の澱粉の一部がアミラーゼにより葡萄糖に転換されたためであると判断される。炭酸圧は、当業界において通常、体積(Vol)で測定されるため、BSTECH社(韓国)のCO2測定装置を利用して測定した。   One molecule of sucrose (180 g) generates two molecules of alcohol and two molecules of carbon dioxide (corresponding to a volume of 2 × 22.4 L under an ideal gas) by yeast. Taking a 1 L container as an example, in order to generate 1 L of carbon dioxide corresponding to 1 Vol, 1 / 44.8 molecule of sucrose (180 g × 1 / 44.8 = 4.02 g) is required. . That is, about 0.4% (W / V) sucrose may be added. However, as can be seen from Table 2 of the examples, the amount of carbon dioxide generated slightly larger than the theoretical amount of carbon dioxide corresponding to the added sugar was generated due to parallel double fermentation. Even if the fermentation seems to be completed, it is actually judged that a part of the starch in the fermentation broth has been converted to sucrose by amylase. Since carbonic acid pressure is usually measured in volume (Vol) in the industry, it was measured using a CO2 measuring device manufactured by BSTECH (Korea).

第5工程:後発酵
ペットボトルに注入した調味液にて酵母による再発酵が起こるように25〜30℃で1〜48時間に亘って後発酵を実施した。上記後発酵の温度は一例に過ぎず、7〜38℃で実施可能で、またより多様な温度で実施できる。
上記後発酵液を分析した結果は、次の表の通りである。
5th process: Post-fermentation Post-fermentation was implemented at 25-30 degreeC over 1-48 hours so that re-fermentation by yeast might occur with the seasoning liquid inject | poured into the PET bottle. The temperature of the said post-fermentation is only an example, can be implemented at 7-38 degreeC, and can be implemented at more various temperature.
The result of analyzing the post-fermentation liquid is as shown in the following table.

表2における炭酸圧は、製品容器内に溶けている二酸化炭素の溶存量を体積で示したものである。試料1は、調味した液に発酵性糖0.6%を、試料2は、調味した液に発酵性糖1.0%を追加で添加したものである。   The carbonic acid pressure in Table 2 indicates the volume of dissolved carbon dioxide dissolved in the product container. Sample 1 is obtained by adding 0.6% fermentable sugar to the seasoned liquid, and Sample 2 is obtained by adding 1.0% fermentable sugar to the seasoned liquid.

第6工程:後発酵液の殺菌
ペットボトルにて後発酵が完了した製品を65℃で30分間殺菌した。上記殺菌条件は一例に過ぎず、当業界に公知となった多様な条件で実施できる。ペットボトルに注入して後発酵してから殺菌した製品の炭酸圧は、表2の結果と似たような炭酸圧を示した。
以上の方法により製造された発酵酒は、調味が完了した液に、要求される炭酸圧の発生に必要な適当量の発酵性糖を添加して、キャップで密封した状態で後発酵を実施するため、製品に清涼感を与えられる炭酸ガス量が含有されるようになる。
Sixth step: sterilization of post-fermentation liquid The product after post-fermentation was completed with a PET bottle at 65 ° C. for 30 minutes. The above-mentioned sterilization conditions are only examples, and can be carried out under various conditions known in the art. The carbonic acid pressure of the product sterilized after being poured into a PET bottle and sterilized was similar to that shown in Table 2.
The fermented liquor produced by the above method is subjected to post-fermentation in a state where the seasoning is completed and an appropriate amount of fermentable sugar necessary for generating the required carbonic acid pressure is added and sealed with a cap. Therefore, the amount of carbon dioxide that gives a refreshing feeling to the product is contained.

以上、本発明を特定の実施例に基づいて説明したが、当該技術分野において本発明の趣旨及び添付された特許請求の範囲内での多様な変形、変更又は修正が可能なことは勿論である。従って、前述した説明は、本発明の技術思想を限定するものではなく、本発明を例示するものとして解釈しなければならない。本発明で引用された全ての文献は、本発明の明細書に参照として取り込まれる。   Although the present invention has been described based on specific embodiments, it goes without saying that various modifications, changes or modifications within the spirit of the present invention and the scope of the appended claims are possible in the technical field. . Accordingly, the above description should not be construed as limiting the technical idea of the present invention but should be construed as illustrating the present invention. All documents cited in the present invention are incorporated by reference into the specification of the present invention.

Claims (5)

発酵酒の製造方法において、
蒸煮器を利用して白米で強飯を作って、水と混合し、麹を入れた後、酒母を接種し、水を添加した後、培養する1段仕込み工程としての第1工程と、
蒸煮器を利用して白米で強飯を作って、麹と共に、前記1段仕込み工程で培養された発酵液に添加してから、水を添加した後、発酵する2段仕込み工程としての第2工程と、
篩を利用して濾過してから、希釈した後、発酵性糖成分のない酸味料及び甘味料を添加して調味する第3工程と、
調味が完了した液に熱処理無しに発酵性糖を添加する第4工程と、
後発酵を実施する第5工程と、
を備えたことを特徴とする発酵酒の製造方法。
In the method for producing fermented liquor,
Making a strong rice with white rice using a steamer, mixing with water, putting rice cake, inoculating a liquor, adding water, and then cultivating the first step,
The second step as a two-stage preparation process in which a strong rice is made with white rice using a steamer and added to the fermentation broth cultured in the first-stage preparation process together with the koji, followed by addition of water and then fermentation. When,
A third step of adding a sour agent and a sweetener free from fermentable sugar components and then seasoning after dilution using a sieve and dilution;
A fourth step of adding fermentable sugar to the liquid that has been seasoned without heat treatment;
A fifth step of performing post-fermentation;
A method for producing fermented liquor, comprising:
前記第4工程で目的とする炭酸圧によって決定された発酵性糖を添加することを特徴とする請求項1に記載の発酵酒の製造方法。   The method for producing fermented liquor according to claim 1, wherein fermentable sugar determined by the target carbonic acid pressure in the fourth step is added. 前記炭酸圧は0.02〜6Volで、添加する発酵性糖濃度は0.01〜2.4%であることを特徴とする請求項2に記載の発酵酒の製造方法。   The method for producing fermented liquor according to claim 2, wherein the carbonic acid pressure is 0.02 to 6 Vol, and the fermentable sugar concentration to be added is 0.01 to 2.4%. 前記第4工程において、調味が完了した液に熱処理無しに発酵性糖を添加した後、耐熱耐圧容器に注入してからキャップで密封することを特徴とする請求項1〜3のうち何れか1項に記載の発酵酒の製造方法。   In said 4th process, after adding fermentable sugar to the liquid which seasoning was completed without heat processing, after inject | pouring into a heat-resistant pressure-resistant container, it seals with a cap, The any one of Claims 1-3 characterized by the above-mentioned. The manufacturing method of fermented liquor as described in a term. 前記第5工程の後に、後発酵が完了した製品を殺菌する第6工程をさらに含むことを特徴とする請求項4に記載の発酵酒の製造方法。   The method for producing fermented liquor according to claim 4, further comprising a sixth step of sterilizing the product after the post-fermentation after the fifth step.
JP2009059004A 2008-03-14 2009-03-12 Method for producing fermented liquor Pending JP2009219490A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5971678A (en) * 1982-10-14 1984-04-23 Ookura Syuzo Kk Brewing of refined sake
JPH0440883A (en) * 1990-06-08 1992-02-12 Masahisa Takeda Production of yeast-containing sake containing fermentation gas
JPH09140371A (en) * 1995-11-24 1997-06-03 Tohoku Meijiyou Kk Production of sparkling refined japanese rice wine
JP2007117063A (en) * 2005-10-31 2007-05-17 Suntory Ltd Alcoholic drink having fresh invigorating feeling

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030002041A (en) * 2001-06-30 2003-01-08 남종현 Herb medicinal rice wine and preparing method thereof
JP3798689B2 (en) * 2001-12-25 2006-07-19 株式会社喜多屋 Effervescent sake and method for producing the same

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5971678A (en) * 1982-10-14 1984-04-23 Ookura Syuzo Kk Brewing of refined sake
JPH0440883A (en) * 1990-06-08 1992-02-12 Masahisa Takeda Production of yeast-containing sake containing fermentation gas
JPH09140371A (en) * 1995-11-24 1997-06-03 Tohoku Meijiyou Kk Production of sparkling refined japanese rice wine
JP2007117063A (en) * 2005-10-31 2007-05-17 Suntory Ltd Alcoholic drink having fresh invigorating feeling

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