JPS6228660B2 - - Google Patents

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Publication number
JPS6228660B2
JPS6228660B2 JP11779180A JP11779180A JPS6228660B2 JP S6228660 B2 JPS6228660 B2 JP S6228660B2 JP 11779180 A JP11779180 A JP 11779180A JP 11779180 A JP11779180 A JP 11779180A JP S6228660 B2 JPS6228660 B2 JP S6228660B2
Authority
JP
Japan
Prior art keywords
alcohol
liquefied
starch
amylase
wheat
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.)
Expired
Application number
JP11779180A
Other languages
Japanese (ja)
Other versions
JPS5743661A (en
Inventor
Yasuyoshi Odaka
Itsuo Takeuchi
Michio Harada
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.)
Kikkoman Corp
Original Assignee
Kikkoman Corp
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 Kikkoman Corp filed Critical Kikkoman Corp
Priority to JP11779180A priority Critical patent/JPS5743661A/en
Publication of JPS5743661A publication Critical patent/JPS5743661A/en
Publication of JPS6228660B2 publication Critical patent/JPS6228660B2/ja
Granted legal-status Critical Current

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  • Alcoholic Beverages (AREA)

Description

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

本発明は麦類、雑穀類を原料として従来の味淋
に非常に近く香味の良好な酒精含有甘味調味料を
製造する方法に関する。 従来、味淋は蒸した糯米に米麹と水とアルコー
ルを混和して、糯米をアルコールの存在下で麹菌
の酵素で糖化熟成して製造されるが、糯米は生産
量が粳米に比べて極めて少量であり、近年糯米の
供給が不足し、また値段も高く、生産コストが割
高なものとなる欠点を有している。 そこで、本発明者らは以上の如き事情に鑑み、
糯米以外の低兼な原料を用いて味淋と同様な酒精
含有甘味調味料を製造することが出来れば味淋業
界にとつて多大の貢献となることに着目し、種々
研究を重ねた結果、加熱変性した麦類または雑穀
類に酸またはα−アミラーゼを作用させ、該麦類
または雑穀類の澱粉の95%以上を液化し、該液化
物をそのままアルコールおよび米麹と共に仕込
み、糖化熟成することによつて、麦類や雑穀類を
原料として、従来の味淋に非常に近い酒精含有甘
味調味料が得られることを知り、この知見に基い
て本発明を完成した。 即ち本発明は麦類または雑穀類を加熱変性し、
酸またはα−アミラーゼを作用させ、該麦類また
は雑穀類の澱粉の95%以上を液化し、該液化物を
そのままアルコールおよび米麹と共に仕込み、糖
化熟成させることを特徴とする酒精含有甘味調味
料の製造法である。 以下、本発明を詳細に説明する。 本発明に用いられる麦類としては、大麦、小
麦、ライ麦、エンバクなどが、また雑穀類として
は玉蜀黍、栗、稗、黍、高梁、マイロ、蒿麦など
が挙げられる。 これらは粳性のもの、糯性のものいずれも使用
でき、通常は精穀したものをそのままで、あるい
は必要により細かく割砕して用いることができ
る。 そして、これら麦類または雑穀類の加熱変性と
は、澱粉質の糊化、蛋白質の変性、穀粒組織の緩
和、崩壊などを起こさせて、酸またはα−アミラ
ーゼの作用を受け易くする方法を意味し、例えば
蒸煮する方法、蒸〓する方法または密閉容器中で
飽和水蒸気又は過熱水蒸気により加圧加熱した後
急激に放圧し膨化破壊する方法等が挙げられる。 このようにして加熱変性した麦類または雑穀類
を液化するのに用いられる酸としては塩酸、硫
酸、蓚酸などの無機および有機の酸が挙げられ、
またα−アミラーゼとしてはα−アミラーゼを主
要酵素とする酵素剤あるいは市販のα−アミラー
ゼ剤などが挙げられる。これらは、バチルス・ズ
ブチリス、アスペルギリス・オリゼー、アスペル
ギリス・ニガーに属する菌株等、微生物の生産す
るもの、麦芽など植物の生産するもの等が挙げら
れるが、ことにバチルス・ズブチリスに属する菌
株が生産する酵素が耐熱性が高く、高温下での澱
粉の液化が出来るので好適である。上記α−アミ
ラーゼの酵素剤としては上記菌株の培養濾液、抽
出液の硫安塩析物、アルコールやアセトン等の有
機溶剤沈澱物、限外濾過濃縮物、あるいはその乾
燥物、あるいは更にこれらを精製した酵素などが
挙げられる。また市販のα−アミラーゼ剤として
は、50〜90℃に作用至適温度を有するもので、例
えばスピターゼCP(長瀬産業社製)、クライスタ
ーゼ(大和化成社製)、YA3−5、YA3−6、
YA3−7(近畿ヤクルト社製)などが挙げられ、
また70〜110℃に作用至適温度を有するもので、
例えばスピターゼHS(長瀬産業社製)、ターマミ
ル(ノボ社製)、クライスターゼTS(大和化成社
製)などが挙げられる。 次に、加熱変性した麦類または雑穀類に酸また
はα−アミラーゼを作用させて、該麦類または雑
穀類の澱粉の液化率が95%以上となるように液化
する。このような液化の条件は酸を使用する場合
とα−アミラーゼを使用する場合とで異なる。即
ち、酸の場合は上記加熱変性した麦類または雑穀
類に、生の麦類または雑穀類の40〜140重量%に
相当する、0.01〜0.3(W/V)%の塩酸、0.005
〜0.2(W/V)%の硫酸、0.02〜0.5(W/V)
%の蓚酸を加え、100〜130℃で5〜30分間保持
し、該麦類または雑穀類の澱粉の液化率が95%以
上となつた時点で急冷して反応を止め水酸化ナト
リウム、炭酸ナトリウム、炭酸水素ナトリウムお
よび炭酸カルシウム等のアルカリを加え中和す
る。 酸を使用して穀類澱粉の95%以上を液化したも
のは、次の工程の醪仕込を径て圧搾を行うとき、
圧搾が極めて容易であるが、酸液化の性質として
液化率が10%を越すと糖化が開始され、95%以上
液化されたときは大部分が糖化を受けた状態とな
る。この時は液の着色が進み、香味的には好まし
くないので、酸を使用する時は、液化率10〜15%
程度に止め一旦冷却中和後に、α−アミラーゼを
加えて酵素法に切換え液化を進めることが望まし
い。 また、α−アミラーゼ単独で液化する場合は、
上記した麦類または雑穀類に、生の麦類および雑
穀類の40〜140重量%の水と、生の麦類または雑
穀類の澱粉の1/100〜1/60000重量倍に相当する、
50〜90℃に作用至適温度を有するα−アミラーゼ
または70〜110℃に作用至適温度を有するα−ア
ミラーゼを加え、前者のα−アミラーゼを加えた
場合、50〜90℃で15時間以上、好ましくは15〜40
時間、後者のα−アミラーゼを加える場合は70〜
110℃で2時間以上、好ましくは3〜20時間、保
持して該麦類または雑穀類の澱粉の液化率が95%
以上となつた時点で常温まで放冷する。 麦類および栗、稗などは液化が容易であるの
で、上記液化は1回で充分であるが、玉蜀黍、マ
イロなどは液化が円滑に行なわれないので、上記
液化に際しては、原料に酸またはα−アミラーゼ
の前記規定量の一部を添加して液化を行ない、該
原料の澱粉の液化率が10〜20%となつた時点で前
半の液化を中止し、該液化物を達温120℃以上に
加熱し、次いで元の液化温度まで冷却し、酸また
はα−アミラーゼの残部を添加して後半の液化を
開始し、最終的に該原料の澱粉の液化率を95%以
上とする。該原料の澱粉の液化率が10〜20%とな
つた時点で前半の液化を終了するのは、該液化率
が10%未満では後半の液化が円滑に行なわれない
場合があり、また反対に20%を越えると後半の液
化は円滑に行なわれるが加熱の際に液化物が褐変
する危険性が生ずるので好ましくない。また、該
液化物を達温120℃以上の温度に加熱する手段と
しては、例えば液化物を密閉式の高圧蒸煮缶に入
れ、飽和蒸気をゲージ圧2Kg/cm2以上となるまで
導入し、加圧加熱すればよい。 なお、該麦類または雑穀類の澱粉の液化率が95
%以上となつた時点とは、液化物の透明な液汁中
の全糖量を求め、これを麦類または雑穀類の全澱
粉を全糖として表わした糖量で除した値の百分率
で求めたものであつて、この値が95%以上となつ
た場合である。即ち、日本醸友会発行の「国税庁
所定分析法」第56〜57頁記載の方法によつてデン
プン価を計算し、麦類または生雑穀類の全澱粉量
を求め、次いでこの全澱粉量を0.9で除して該麦
類または生雑穀類の全糖量を求める。次いで、該
「国税庁所定分析法」第69頁に記載の総糖分分析
法に従つて液化物内の、透明液汁中に含まれる全
糖量を求め、次式に従つて、計算した値が95%以
上となつた場合である。 液化率=透明液汁中の全糖量/生の麦類または雑穀類
の全糖量×100 また、本発明においてα−アミラーゼを使用す
ることも極めて重要であつて、s−アミラーゼ
(糖化型澱粉加水分解酵素)やプロテアーゼ等を
著量含有する酵素剤、またはこれらの酵素を著量
含有する〓麹や米麹そのものを用いると、製品が
過度に着色したり、甘酒様あるいは芋飴様の香味
が生成して、従来の味淋とは風味性状が異なつた
ものとなる欠を有する。 また、麦類または雑穀類の澱粉の95%以上好ま
しくは97%以上を液化することも極めて重要であ
つて液化物に5%以上の澱粉が液化されないまま
残存すると、この澱粉が仕込後、醪中で老化して
糊状となり、醪中に均一に分散して醪の被圧搾濾
過性を著しく低下させ、濾過助剤を添加すること
なしでは、通常の圧搾濾過機による圧搾を殆んど
不可能ならしめ、また粗い目の濾布を使用し導入
圧を高めるなど無理をして圧搾して得た濾液は糊
状白濁物質(〓)を多量に含むので、この糊状白
濁物質を沈停させ、透明な上澄液を得る(以下、
これを「〓引き」という)ことが非常に困難とな
る欠点を有する。 次に、このようにして得られた液化物はそのま
まで、即ち該液化物中の未溶解物(固形物)を少
なくとも一部残存した状態で、通常の味淋の製造
法と同様にして熟成醪液汁のアルコール濃度が13
〜15%になるような量のアルコールおよび生の麦
類または雑穀類の10〜30重量%の米麹と混和し、
さらに必要によりブドウ糖、水飴等を混和して仕
込み、20〜30℃で10〜20日間時々撹拌しながら糖
化熟成を行ない、常法により圧搾濾過、〓引き、
火入をした後、精製してアルコール分13〜15%、
エキス分45〜50%の酒精含有甘味調味料を得るこ
とができる。 なお、上記において、液化物をそのまま仕込に
用いることも極めて重要であつて、該液化物を濾
過精製して、該液化物中の未溶解物(固形物)を
完全に取り除いた透明な液化物に仕込に用いると
きは、長時間糖化熟成しても、最終製品に良好な
味淋様風味が醸成されず、従つて味淋様風味に乏
しい酒精含有甘味調味料しか得られないが、液化
物をそのまま、またはこれを目の粗い濾布等によ
つて簡単に濾過し、濾液中に未溶解物がまだ懸濁
して残つている液化物を用いるときは、香りと味
が融和して従来の蒸した糯米を用いて得た味淋に
非常に近き、極めて香味良好と判断される酒精含
有甘味調味料を得ることがきる。 従来、味淋は調理食品を得る場合、味淋独特の
香りと味とが相乗的に作用して、調理効果を発揮
するものであり、香りと味は切り離すことの出来
ない重要な要素となつている。従つて、味ばかり
でなく香り、その他についても従来の味淋に非常
に近い酒精含有甘味調味料を得ることは極めて大
きな意義を有する。 以下、本発明の効果について実験例を挙げて説
明する。 実験例 1 下記第1表「注」の区分A〜Fに示す如き方法
に従つて、それぞれA〜Fの6種類の酒精含有甘
味調味料を製造した。これらについて圧搾濾過性
試験、〓引き試験および10名の識別能力を有する
訓練されたパネルにより官能試験を行なつたとこ
ろ、第1表に示す如き結果が得られた。なお圧搾
濾過性試験は糖化熟成醪をハンドプレスで圧搾し
た場合における圧搾の難易の程度を経験的な尺度
で示し、また〓引き試験は圧搾して得た液汁100
mlを100ml容メスシリンダーに入れ、60時間静置
したときの透明な液量で示し、この液量が多い
程、〓引きが容易であることを示し、さらにまた
官能試験は評点法によつて行ない、B〜F区分の
醪液汁をそれぞれA区分(対照法)の味淋と比較
し、A区分の味淋を標準0とし、下記規準で採点
をし、その平均値をもつて示した。
The present invention relates to a method for producing an alcohol-containing sweet seasoning having a flavor very close to that of conventional gourd, using wheat and cereals as raw materials. Traditionally, Ajirin is produced by mixing steamed glutinous rice with rice malt, water, and alcohol, and then saccharifying and aging the glutinous rice with enzymes from koji mold in the presence of alcohol, but the production volume of glutinous rice is extremely low compared to glutinous rice. It has the disadvantage that it is produced in small quantities, the supply of glutinous rice has been insufficient in recent years, and the price is high, making the production cost relatively high. Therefore, in view of the above circumstances, the present inventors
We focused on the fact that it would be a great contribution to the ajirin industry if we could produce a sweet seasoning containing alcoholic spirit similar to ajirin using low-grade raw materials other than glutinous rice, and after conducting various research, we found that Applying acid or α-amylase to heat-denatured barley or millet to liquefy 95% or more of the starch of the barley or millet, and then adding the liquefied product as is with alcohol and rice malt for saccharification and ripening. As a result, it was discovered that an alcohol-containing sweet seasoning very similar to conventional goo could be obtained using barley and cereals as raw materials, and based on this knowledge, the present invention was completed. That is, the present invention heat-denatures wheat or cereals,
An alcohol-containing sweet seasoning characterized by liquefying 95% or more of the starch of the barley or millet by the action of acid or α-amylase, and adding the liquefied product as it is with alcohol and rice malt to saccharify and ripen it. This is the manufacturing method. The present invention will be explained in detail below. Examples of barley used in the present invention include barley, wheat, rye, oat, etc., and examples of cereals include onion, chestnut, millet, millet, takahashi, milo, and konjac. Both starchy and sticky grains can be used, and usually the milled grains can be used as they are, or if necessary, they can be crushed finely. Heat denaturation of wheat or cereals is a method of causing gelatinization of starch, denaturation of proteins, relaxation and disintegration of grain structure, and making it more susceptible to the action of acids or α-amylase. This means, for example, a method of steaming, a method of steaming, a method of heating under pressure with saturated steam or superheated steam in a closed container, and then rapidly releasing the pressure to cause swelling and destruction. Acids used to liquefy wheat or cereals heat-denatured in this way include inorganic and organic acids such as hydrochloric acid, sulfuric acid, and oxalic acid.
Examples of α-amylase include enzyme preparations containing α-amylase as a main enzyme and commercially available α-amylase preparations. These include those produced by microorganisms such as strains belonging to Bacillus subtilis, Aspergillus oryzae, and Aspergillus niger, and those produced by plants such as malt, but especially those produced by strains belonging to Bacillus subtilis. This enzyme is suitable because it has high heat resistance and can liquefy starch at high temperatures. The enzyme agent for α-amylase may be culture filtrate of the above bacterial strain, ammonium sulfate salt precipitate of extract, organic solvent precipitate such as alcohol or acetone, ultrafiltration concentrate, or dried product thereof, or further purified product thereof. Examples include enzymes. Commercially available α-amylase agents have an optimal temperature of action between 50 and 90°C, such as Spitase CP (manufactured by Nagase Sangyo Co., Ltd.), Klystase (manufactured by Daiwa Kasei Co., Ltd.), YA3-5, YA3-6. ,
Examples include YA3-7 (manufactured by Kinki Yakult Co., Ltd.),
It also has an optimum temperature of 70 to 110℃.
Examples include Spitase HS (manufactured by Nagase Sangyo Co., Ltd.), Termamil (manufactured by Novo Corporation), and Klystase TS (manufactured by Daiwa Kasei Co., Ltd.). Next, the heat-denatured barley or millet is treated with acid or α-amylase to liquefy the barley or millet so that the starch liquefaction rate is 95% or more. The conditions for such liquefaction differ depending on whether an acid is used or α-amylase is used. That is, in the case of acid, 0.01 to 0.3 (W/V)% hydrochloric acid, which corresponds to 40 to 140% by weight of raw wheat or millet, and 0.005% to the heat-denatured wheat or millet are added.
~0.2(W/V)% sulfuric acid, 0.02-0.5(W/V)
% of oxalic acid and held at 100 to 130°C for 5 to 30 minutes, and when the liquefaction rate of the starch of the barley or millet reaches 95% or more, the reaction is stopped by rapid cooling and sodium hydroxide and sodium carbonate are added. , add an alkali such as sodium bicarbonate and calcium carbonate to neutralize. Grain starch that has liquefied more than 95% of its starch using acid must be pressed during the next process of mashing.
Although it is extremely easy to squeeze, the nature of acid liquefaction is that when the liquefaction rate exceeds 10%, saccharification begins, and when 95% or more is liquefied, most of the saccharification occurs. At this time, the color of the liquid will progress and the flavor will be undesirable, so when using acid, the liquefaction rate should be 10 to 15%.
It is desirable to limit the amount to a certain level and once cool and neutralize, add α-amylase and switch to an enzymatic method to proceed with liquefaction. In addition, when liquefying with α-amylase alone,
To the above-mentioned barley or millet, water equivalent to 40 to 140% by weight of raw barley or millet and 1/100 to 1/60000 times the weight of starch of raw barley or millet,
If α-amylase whose optimal temperature for action is between 50 and 90°C or α-amylase whose optimal temperature for action is between 70 and 110°C is added, and the former α-amylase is added, it is heated at 50 to 90°C for 15 hours or more. , preferably 15-40
time, if adding the latter α-amylase, 70~
Hold at 110°C for 2 hours or more, preferably 3 to 20 hours, until the liquefaction rate of the starch of the wheat or millet is 95%.
When the temperature reaches this point, let it cool to room temperature. Wheat, chestnuts, millet, etc. are easily liquefied, so it is sufficient to liquefy them once. However, since the liquefaction of corn, corn, etc. is not smooth, it is necessary to add acid or α to the raw materials when liquefying them. - Liquefaction is carried out by adding a portion of the specified amount of amylase, and when the liquefaction rate of the raw starch reaches 10 to 20%, the first half of the liquefaction is stopped, and the liquefied product is heated to a temperature of 120°C or higher. The starch is then cooled to the original liquefaction temperature, and the remainder of the acid or α-amylase is added to initiate the second half of liquefaction, ultimately achieving a liquefaction rate of starch of the raw material of 95% or more. The reason for finishing the first half of the liquefaction when the liquefaction rate of starch as the raw material reaches 10 to 20% is because if the liquefaction rate is less than 10%, the second half of the liquefaction may not be carried out smoothly. If it exceeds 20%, the latter half of the liquefaction will be carried out smoothly, but there is a risk that the liquefied product will turn brown during heating, which is not preferable. In addition, as a means of heating the liquefied material to a temperature of 120°C or higher, for example, the liquefied material is placed in a closed high-pressure steamer, saturated steam is introduced until the gauge pressure reaches 2 kg/cm 2 or higher, and then the liquefied material is heated. It can be heated under pressure. In addition, the starch liquefaction rate of the wheat or cereals is 95
% or more is calculated as the percentage of the total sugar content in the clear liquid juice of the liquefied product, divided by the sugar content expressed as total sugar from the total starch of wheat or cereals. and this value is 95% or more. That is, calculate the starch value using the method described on pages 56-57 of the National Tax Agency Specified Analysis Method published by the Japan Joyukai, determine the total starch content of wheat or raw cereals, and then calculate the total starch content. Divide by 0.9 to determine the total sugar content of the wheat or raw cereals. Next, the total amount of sugar contained in the clear juice in the liquefied product was determined according to the total sugar content analysis method described on page 69 of the National Tax Agency Specified Analysis Method, and the value calculated according to the following formula was 95 % or more. Liquefaction rate = total amount of sugar in clear liquid juice / total amount of sugar in raw barley or cereals x 100 In addition, it is extremely important to use α-amylase in the present invention, If you use enzyme preparations that contain significant amounts of hydrolytic enzymes (hydrolytic enzymes) or proteases, or koji or rice malt itself that contains significant amounts of these enzymes, the product may become excessively colored or have a sweet sake-like or potato candy-like flavor. It has a defect that the taste is different from that of conventional ajirin. It is also extremely important to liquefy at least 95% or more, preferably at least 97%, of the starch of barley or cereals. If more than 5% of starch remains in the liquefied product without being liquefied, this starch will be added to the mash after brewing. It ages inside the mortar and becomes pasty, and is uniformly dispersed in the moromi, significantly reducing the press-filterability of the moromi, making it almost impossible to press with a normal press filter without adding a filter aid. The filtrate obtained by squeezing by force, such as using a coarse filter cloth and increasing the introduction pressure, contains a large amount of a pasty cloudy substance (〓). to obtain a clear supernatant (hereinafter,
This has the disadvantage that it is extremely difficult to do so. Next, the liquefied product obtained in this way is aged as is, that is, with at least a portion of the undissolved matter (solid matter) remaining in the liquefied product, in the same manner as in the normal production method of Ajirin. Alcohol concentration of moromi juice is 13
~15% of alcohol and raw barley or millet mixed with 10-30% by weight of rice malt,
Furthermore, if necessary, glucose, starch syrup, etc. are mixed and prepared, and saccharified and aged at 20 to 30℃ for 10 to 20 days with occasional stirring.
After pasteurization, it is purified to an alcohol content of 13-15%,
A sweet seasoning containing alcohol with an extract content of 45-50% can be obtained. In addition, in the above, it is extremely important to use the liquefied product as it is for preparation, and the liquefied product is purified by filtration to completely remove undissolved matter (solid matter) in the liquefied product to obtain a transparent liquefied product. When used for preparation, even if saccharified and aged for a long period of time, the final product will not have a good melon-like flavor, resulting in only an alcohol-containing sweet seasoning that lacks the melon-like flavor. When using the liquefied product as it is or simply filtering it through a coarse filter cloth, etc., and the undissolved matter is still suspended in the filtrate, the aroma and taste are harmonized and it becomes different from the conventional method. It is possible to obtain an alcohol-containing sweet seasoning that is judged to have an extremely good flavor and flavor that is very close to the taste of gourd obtained using steamed glutinous rice. Conventionally, when preparing cooked foods from Ajirin, the unique aroma and taste of Ajirin work synergistically to produce a cooking effect, and the aroma and taste are important elements that cannot be separated. ing. Therefore, it is of great significance to obtain an alcohol-containing sweet seasoning that is very close to the conventional ajirin not only in taste but also in aroma and other aspects. Hereinafter, the effects of the present invention will be explained using experimental examples. Experimental Example 1 Six types of alcohol-containing sweet seasonings A to F were produced in accordance with the methods shown in Sections A to F of the Notes in Table 1 below, respectively. When these were subjected to a squeeze filtration test, a pull test, and a sensory test using a panel of 10 people trained in discrimination ability, the results shown in Table 1 were obtained. The squeeze filterability test uses an empirical scale to show the degree of difficulty in squeezing when saccharified aged mash is squeezed using a hand press, and the filterability test uses 100% of the juice obtained by squeezing.
ml into a 100 ml graduated cylinder and left to stand for 60 hours.The larger the amount of liquid, the easier it is to draw.Furthermore, the sensory test was conducted using a scoring system. The mortar soups in categories B to F were each compared with Ajirin in Category A (control method), and the Ajirin in Category A was set as standard 0, and scores were given using the following criteria, and the average value is shown.

【表】 劣 劣 る い 良 良
る る い い
[Table] Inferior Inferior Good Good Good Good

【表】 (注) 区分A:糯白米2Kgを常法により洗滌、浸漬、
水切りし、蒸〓して得た蒸糯米2.4Kgを得、これ
を米麹400gおよび40%アルコール1434mlと共に
仕込み、25℃で60日間糖化熟成し、次いで圧搾、
〓引きをして対照の味淋を得た。 区分B:精白した粳性の玉蜀黍(コーングリツ
ツ、50〜60メツシユ)2Kgを常法により洗滌、浸
漬、水切りし、蒸〓して蒸玉蜀黍2.3Kgを得、こ
れに0.1(W/V)%蓚酸880mlを加え、100℃で
20分間液化(加水分解)したのち30℃に冷却し、
炭酸カルシウムを加えて中和した。次にでα−ア
ミラーゼ剤(YA3−6)1gを加え70℃で40時間
保持して玉蜀黍の澱粉を100%液化した。次い
で、この液化物を米麹400gおよび99%アルコー
ル560mlと共に仕込み、25℃で10日間糖化熟成を
行ない、次いで圧搾、〓引きをして本発明の酒精
含有甘味調味料を得た。 区分C:精白した玉蜀黍(コーングリツツ、50
〜60メツシユ)2Kgを常法により洗滌、浸漬、水
切りし、蒸〓して蒸玉蜀黍2.3Kgを得、これを水
880mlおよび2gのα−アミラーゼ剤(YA3−
6、近畿ヤクルト社製)を混和し、70℃で6時間
液化を行い、次いで得られた液化物を加圧蒸煮缶
に移してゲージ圧2Kg/cm2まで加熱したのち、70
℃まで冷却し、これに前記α−アミラーゼ剤1g
を添加して70℃で40時間保持し、玉蜀黍の澱粉を
100%液化(加水分解)した。次いで、この液化
物を米麹400gおよび99%アルコール560mlと共に
仕込み、25℃で10日間糖化熟成させ、次いで圧
搾、〓引きして、本発明の酒精含有甘味調味料を
得た。 区分D:上記酒精含有甘味調味料C区分の製造
法において玉蜀黍の澱粉の100%液化物を用いる
代わりに、該液化物をハンドプレスで圧搾し、得
られた濾液にセライトを加え、ザルトリウス式濾
過機を用いザイツ製厚型濾紙により濾過して得た
透明な濾液を前記液化物と等量用いる以外は全く
同様にして酒精含有甘味調味料を得た。 区分E:上記酒精含有甘味調味料C区分の製造
法においてα−アミラーゼ剤を用いる代わりに著
量の、s−アミラーゼおよびプロテアーゼを含有
する市販の酵素剤(タカジアスターゼ、三共製薬
社製)を用い温度を55℃にする以外は全く同様に
して酒精含有甘味調味料を得た。 区分F:精白した玉蜀黍(コーングリツツ、50
〜60メツシユ)2Kgを常法により洗滌、浸漬、水
切りし、蒸〓して蒸玉蜀黍2.3Kgを得、これを水
880mlおよび250gの米麹を混和し、55Kgで6時間
液化を行い、次いで得られた液化物を加圧蒸煮缶
に移してケージ圧2Kg/cm2まで加熱したのち、55
℃まで冷却し、これに前記米麹150gを混和し、
55℃で40時間保持し、玉蜀黍の澱粉を100%液化
(加水分解)した。次いでこの液化物を米麹400g
および99%アルコール560mlと共に仕込み、25℃
で10日間糖化熟成させ、次いで圧搾、〓引きし
て、酒精含有甘味調味料を得た。 第1表の結果から著量のs−アミラーゼおよび
著量のプロテアーゼを含有する酵素剤を使用する
区分Eは圧搾が困難であり、〓引きが殆んど不可
能であるばかりか、製品は色がかなり劣り、強い
芋臭を有し、更に麦芽水飴様に呈すことから、対
照の味淋と比べ風味、性状がかなり劣るものであ
ることが判る。 また米麹を使用する区分Fは圧搾が非常に困難
であり、〓引きが不可能であるばかりか、製品は
色が非常に劣り区分Eと同様な香りと味を有し、
これもまた対照の味淋と比べ風味がかなり劣るも
のであることが判る。 また、玉蜀黍の澱粉の液化物を濾過して得た、
液中に未溶解物を全く含まない透明な濾液を使用
するD区分は対称の味淋と比べ、香り、味ともに
貧弱で味淋様風味に乏しく劣つていることが判
る。 これに対し、蒸した玉蜀黍を酸またはα−アミ
ラーゼで液化し得られたものを使用する本発明の
B区分、C区分は圧搾、〓引きとも非常に容易で
あり、しかも色、香り、味も対照の味淋に近い、
あるいは非常に近い、極めて良好な品質のもので
あることが判る。 なお、小麦、大麦、栗、稗などの原料を用い、
該原料の澱粉を100%液化したものを、そのまま
アルコールおよび米麹と共に仕込み糖化熟成させ
得られた醪について圧搾濾過性試験を行い、また
醪液汁の〓引き試験および得られた製品の官能試
験を行つた結果、前記実験例とほぼ同様の結果が
得られた。 実験例 精白した粳性の玉蜀黍(コーングリツツ、50〜
60メツシユ)20Kgを常法により洗滌、浸漬、水切
りし、蒸〓して蒸玉蜀黍24Kgを得た。これを6区
分用意し、それぞれ8.8の水および20gのα−
アミラーゼ剤(YA3−6、近畿ヤクルト社製)を
混和し、70℃にて6時間液化し、該液化物を加圧
蒸煮缶に移し、飽和蒸気を用いてゲージ圧2Kg/
cm2になるまで加熱したあと70℃に冷却し、次いで
前記α−アミラーゼ剤を10g加え、再び70℃にて
適当な時間保持し、玉蜀黍の澱粉を、第1区分は
100%、第2区分は99%、第3区分は97%、第4
区分は95%、第5区分は90%そして第6区分は80
%それぞれ液化し、6種類の液化物を得た。次い
でこの液化物を30℃に冷却後それぞれ4Kgの米麹
および5.6の99%アルコールと共に仕込み、25
℃で10日間糖化熟成させ、得られた醪を薮田式圧
搾試験機(薮田産業社製)で圧搾濾過する場合の
20時間後の搾汁液総量を調べた結果、第2表に示
す如き結果が得られた。
[Table] (Note) Category A: 2 kg of glutinous white rice was washed, soaked, and
2.4 kg of steamed glutinous rice was obtained by draining and steaming, which was then mixed with 400 g of rice malt and 1434 ml of 40% alcohol, saccharified and aged at 25°C for 60 days, and then pressed.
〓I subtracted it and got a contrast taste. Category B: 2 kg of refined corn grits (50-60 mesh) was washed, soaked, drained, and steamed using a conventional method to obtain 2.3 kg of steamed corn grits, and 0.1 (W/V)% oxalic acid was added to this. Add 880ml and heat at 100℃
After liquefying (hydrolyzing) for 20 minutes, it was cooled to 30℃.
Calcium carbonate was added to neutralize. Next, 1 g of α-amylase agent (YA3-6) was added and kept at 70°C for 40 hours to liquefy 100% of the starch of the onion. Next, this liquefied product was charged with 400 g of rice malt and 560 ml of 99% alcohol, and subjected to saccharification and ripening at 25° C. for 10 days, followed by compression and filtration to obtain the alcohol-containing sweet seasoning of the present invention. Category C: Refined corn grits, 50
~60 mesh) 2 kg was washed, soaked, drained, and steamed using the usual method to obtain 2.3 kg of steamed scallions, which was then washed with water.
880 ml and 2 g of α-amylase agent (YA3-
6, manufactured by Kinki Yakult Co., Ltd.) and liquefied at 70℃ for 6 hours, then transferred the obtained liquefied product to a pressure steamer and heated to a gauge pressure of 2Kg/ cm2 , and then
Cool to ℃ and add 1 g of the α-amylase agent to this.
was added and held at 70℃ for 40 hours to extract the starch from the onion.
100% liquefied (hydrolyzed). Next, this liquefied product was charged with 400 g of rice malt and 560 ml of 99% alcohol, and the mixture was saccharified and aged at 25° C. for 10 days, and then compressed and filtered to obtain the alcohol-containing sweet seasoning of the present invention. Category D: Instead of using a 100% liquefied product of corn starch in the manufacturing method of the above alcohol-containing sweet seasoning Category C, the liquefied product is squeezed with a hand press, Celite is added to the resulting filtrate, and Sartorius filtration is performed. An alcohol-containing sweet seasoning was obtained in exactly the same manner except that the same amount of the liquefied product was used as the transparent filtrate obtained by filtration using a thick filter paper made by Seitz. Category E: Instead of using an α-amylase agent in the manufacturing method of the alcohol-containing sweet seasoning Category C, a commercially available enzyme agent (Takadiastase, manufactured by Sankyo Pharmaceutical Co., Ltd.) containing a significant amount of s-amylase and protease is used. An alcoholic sweet seasoning was obtained in exactly the same manner except that the temperature was changed to 55°C. Category F: Refined corn grits (50
~60 mesh) 2 kg was washed, soaked, drained, and steamed using the usual method to obtain 2.3 kg of steamed scallions, which was then washed with water.
880 ml and 250 g of rice malt were mixed, liquefied at 55 kg for 6 hours, then the resulting liquefied product was transferred to a pressure steamer and heated to a cage pressure of 2 kg/cm 2 , and then liquefied at 55 kg.
Cool to ℃, mix 150g of the rice malt,
It was held at 55°C for 40 hours to liquefy (hydrolyze) 100% of the corn starch. Next, add 400g of rice malt to this liquefied product.
and 560ml of 99% alcohol at 25°C.
The mixture was saccharified and aged for 10 days, then compressed and distilled to obtain a sweet seasoning containing alcohol. From the results in Table 1, it is difficult to compress Category E, which uses enzyme preparations containing a significant amount of s-amylase and a significant amount of protease. It has a strong sweet potato odor and a malt starch syrup-like appearance, indicating that it is considerably inferior in flavor and properties compared to the control Ajirin. In addition, Category F, which uses rice malt, is very difficult to press and cannot be compressed, and the product is very poor in color and has the same aroma and taste as Category E.
It can also be seen that the flavor is considerably inferior to that of the control Ajirin. Also, obtained by filtering the liquefied product of corn starch,
It can be seen that the D category, which uses a transparent filtrate containing no undissolved matter in the liquid, is inferior to the symmetrical Aji Gono, as it has poor aroma and taste, and lacks a gooey-like flavor. On the other hand, the B and C categories of the present invention, which use products obtained by liquefying steamed corn with acid or α-amylase, are very easy to press and pull, and they also have a good color, aroma, and taste. The contrast taste is similar to gourd,
Or it can be seen that the quality is very close to that of extremely good quality. In addition, using raw materials such as wheat, barley, chestnuts, and millet,
100% liquefied starch is used as it is, mixed with alcohol and rice malt, and then saccharified and aged. The resulting moromi is subjected to a compression filterability test, as well as a filtration test of the moromi liquid and a sensory test of the resulting product. As a result, almost the same results as in the above experimental example were obtained. Experimental example: Refined corn grits (50~
60 mesh) 20Kg was washed, soaked, drained, and steamed using a conventional method to obtain 24Kg of steamed corn. Prepare 6 sections of this, each containing 8.8 g of water and 20 g of α-
Mix amylase agent (YA3-6, manufactured by Kinki Yakult Co., Ltd.) and liquefy at 70℃ for 6 hours, transfer the liquefied product to a pressure steamer, and use saturated steam at a gauge pressure of 2 kg/
cm 2 and then cooled to 70°C, then added 10g of the α-amylase agent and kept at 70°C again for an appropriate period of time.
100%, 99% for the second category, 97% for the third category, 4th category
Category is 95%, 5th category is 90% and 6th category is 80%
%, respectively, and six types of liquefied products were obtained. Next, this liquefied product was cooled to 30°C and mixed with 4 kg of rice malt and 5.6 liters of 99% alcohol.
When saccharifying and maturing the moromi for 10 days at
As a result of examining the total amount of squeezed liquid after 20 hours, the results shown in Table 2 were obtained.

【表】 第2表の結果から、玉蜀黍の澱粉の液化率が95
%よりも低い値、即ち80〜90%では圧搾濾過性が
極めて悪いが、95%以上、特に97%以上となると
圧搾濾過性が著しく向上することが判る。 本発明は以上の如き構成を有するものであるか
ら以下に示す如き利点を有する。 (1) 糯米を全く使用することがなく、麦類、玉蜀
黍、栗、稗などの雑穀類を主原料として従来の
味淋に非常に近く、香味の良好な酒精含有甘味
調味料を製造することができる。 (2) 主原料を安価で入手容易な麦類または雑穀類
に求めているため、将来糯米の入手が困難また
は糯米の価格が現在より更に高騰し、味淋の製
造が困難になつた場合においても、味淋に代る
ものとして消費者に低兼に安定して供給するこ
とができる。 (3) 本発明の酒精含有甘味調味料は製造に要する
期間が10〜20日間であつて、これを従来の味淋
の製造に要するそれの40〜60日間と比べると判
るように、極めて短期間に製造することが出来
る利点を有する。 以下、実施例を示して本発明をさらに詳細に説
明する。 実施例 1 精白した玉蜀黍(コーングリツツ、50〜60メツ
シユ)2Kgをよく洗滌し、17時間浸漬し、1時間
水切した後、オートクレーブで無圧で60分間蒸〓
し、30℃に冷却して蒸した玉蜀黍を得た。 次いで、この蒸した玉蜀黍に0.01gのα−アミ
ラーゼ剤(スピターゼHS、長瀬産業社製)を溶
解した水880mlを加え、100℃で1時間液化し、次
いで該液化物をオートクレーブに移し、飽和蒸気
を用いてゲージ圧2Kg/cm2(達圧)まで加熱した
あと100℃まで冷却し、次いで0.005gの前記α−
アミラーゼ剤を加え更に100℃で6時間液化し玉
蜀黍の完全液化物を得た。次いで、液化物を400
gの米麹および555mlの99%アルコールと共に混
和して仕込み、25℃で10日間糖化、熟成した。 次いで得られた熟成醪をハンドプレスで圧搾
し、得られた濾液を2日間常温に静置して〓を沈
停(〓引き)させ、清澄な上澄液を分離して、本
発明の酒精含有甘味調味料を得た。 なお対照方法として、糯白米2Kgをよく洗滌
し、15時間浸漬し、30分水切りした後、オートク
レーブで無圧で30分間蒸〓し、冷却して蒸した糯
米2.4Kgを得た。次いでこの蒸した糯米を400gの
米麹、555mlの99%アルコールおよび880mlの水と
共に混和して仕込み、25℃で60日間糖化熟成し、
以下上記本発明方法と同様に圧搾、〓引きして味
淋を得た。 このようにして得られた酒精含有甘味調味料と
味淋とを比較対照すると、第3表の如くであつ
て、本発明の製品は従来の味淋と比べて色、香
り、味、総合および成分分析値について殆んど遜
色のない、高品質の酒精含有甘味調味料を、高価
な糯米を全く使用することなしで、安価な玉蜀黍
を主原料として、極めて短期間に製造することが
出来ることが判る。
[Table] From the results in Table 2, the liquefaction rate of starch in corn is 95.
%, that is, 80 to 90%, the squeeze filtration property is extremely poor, but when the value is 95% or more, especially 97% or more, the squeeze filtration property is significantly improved. Since the present invention has the above configuration, it has the following advantages. (1) To produce an alcohol-containing sweet seasoning that does not use glutinous rice at all, but uses grains such as barley, onion corn, chestnuts, and millet as main ingredients, and has a flavor that is very close to that of conventional gourd and has a good flavor. Can be done. (2) Because the main raw materials are barley or grains that are cheap and easily available, if it becomes difficult to obtain glutinous rice in the future or the price of glutinous rice increases even more than it currently does, making it difficult to produce Ajirin. It can also be stably supplied to consumers as a low-cost alternative to ajirin. (3) The alcohol-containing sweet seasoning of the present invention requires 10 to 20 days to manufacture, which is extremely short compared to the 40 to 60 days required to manufacture conventional Ajirin. It has the advantage that it can be manufactured in between. Hereinafter, the present invention will be explained in more detail by showing examples. Example 1 2 kg of polished corn grits (50 to 60 pieces) was thoroughly washed, soaked for 17 hours, drained for 1 hour, and then steamed in an autoclave without pressure for 60 minutes.
Then, the maize was cooled to 30°C and steamed. Next, 880 ml of water in which 0.01 g of α-amylase agent (Spitase HS, manufactured by Nagase Sangyo Co., Ltd.) was dissolved was added to the steamed onion, and the mixture was liquefied at 100°C for 1 hour.Then, the liquefied product was transferred to an autoclave and heated with saturated steam. was heated to a gauge pressure of 2 kg/cm 2 (final pressure) using
An amylase agent was added and the mixture was further liquefied at 100°C for 6 hours to obtain a completely liquefied product of corn. Then, add 400% of the liquefied material.
g of rice malt and 555 ml of 99% alcohol were mixed and prepared, and the mixture was saccharified and aged at 25°C for 10 days. Next, the obtained aged mash is squeezed with a hand press, the obtained filtrate is allowed to stand at room temperature for 2 days to settle (remove) the filtrate, and the clear supernatant liquid is separated to produce the alcoholic spirit of the present invention. A sweet seasoning was obtained. As a control method, 2 kg of glutinous white rice was thoroughly washed, soaked for 15 hours, drained for 30 minutes, steamed in an autoclave for 30 minutes without pressure, and cooled to obtain 2.4 kg of steamed glutinous rice. Next, this steamed glutinous rice was mixed with 400g of rice malt, 555ml of 99% alcohol, and 880ml of water, and saccharified and aged at 25℃ for 60 days.
Thereafter, the mixture was squeezed and strained in the same manner as in the method of the present invention described above to obtain ajirin. Comparing and contrasting the alcohol-containing sweet seasoning obtained in this manner with Ajirin, it is shown in Table 3 that the product of the present invention has better color, aroma, taste, general and It is possible to produce a high-quality sweet seasoning containing alcohol with almost comparable component analysis values in an extremely short period of time, using inexpensive onion corn as the main raw material, without using any expensive glutinous rice. I understand.

【表】 実施例 2 精白した栗2.0Kgを洗滌し、16時間浸漬し、40
分間水切りした後、オートクレーブで無圧で60分
蒸〓し、放冷して得た栗に、0.2%蓚酸880mlを加
え、100℃で15分保持して栗の澱粉を12%液化
し、次いで30℃まで急冷した後、炭酸カルシウム
を加えて中和し、次いで2gのα−アミラーゼ
(YA3−6)を加え、70℃で40時間液化し栗の完
全液化物を得た。次いでこれを400gの米麹およ
び560mlの99%アルコールと共に仕込み、25℃で
15目間糖化、熟成させ、以下実施例1と同様に圧
搾、〓引きして、香味良好な酒精含有甘味調味料
を得た。 実施例 3 精白した小麦2Kgをよく洗滌し、16時間浸漬
し、1時間水切した後、オートクレーブで無圧で
60分間蒸〓し、30℃に冷却して蒸した小麦を得
た。 次いで、この蒸した小麦に2gのα−アミラー
ゼ剤(YA3−6、近畿ヤクルト社製)を溶解した
水880mlを加え、70℃にて40時間液化し、小麦の
完全液化物を得た。次いで、この液化物を400g
の米麹および555mlの99%アルコールと共に混和
して仕込み、25℃で10日間糖化、熟成した。次い
で得られた熟成醪をハンドプレスで圧搾し、得ら
れた濾液を2日間常温で静置して〓を沈停(〓引
き)させ、清澄な上澄液を分離して、香味良好な
酒精含有甘味調味液を得た。
[Table] Example 2 2.0 kg of polished chestnuts were washed, soaked for 16 hours,
After draining for a minute, the chestnuts were steamed under no pressure in an autoclave for 60 minutes and left to cool. 880 ml of 0.2% oxalic acid was added to the chestnuts, and the chestnuts were kept at 100°C for 15 minutes to liquefy 12% of the chestnut starch. After rapidly cooling to 30°C, calcium carbonate was added for neutralization, and then 2 g of α-amylase (YA3-6) was added and liquefied at 70°C for 40 hours to obtain a completely liquefied chestnut. Next, this was prepared with 400g of rice malt and 560ml of 99% alcohol, and heated at 25℃.
The mixture was saccharified and aged for 15 days, and then compressed and strained in the same manner as in Example 1 to obtain an alcohol-containing sweet seasoning with good flavor. Example 3 2 kg of polished wheat was thoroughly washed, soaked for 16 hours, drained for 1 hour, and then autoclaved without pressure.
Steamed for 60 minutes and cooled to 30°C to obtain steamed wheat. Next, 880 ml of water in which 2 g of an α-amylase agent (YA3-6, manufactured by Kinki Yakult Co., Ltd.) was dissolved was added to the steamed wheat, and the mixture was liquefied at 70° C. for 40 hours to obtain a completely liquefied wheat product. Next, 400g of this liquefied material
of rice malt and 555 ml of 99% alcohol were mixed and prepared, and the mixture was saccharified and aged at 25°C for 10 days. Next, the obtained aged mash is squeezed with a hand press, the obtained filtrate is allowed to stand at room temperature for 2 days, the filtrate settles (pulls), and the clear supernatant liquid is separated to produce alcoholic spirit with good flavor. A sweet seasoning liquid was obtained.

Claims (1)

【特許請求の範囲】 1 麦類または雑穀類を加熱変性し、酸またはα
−アミラーゼを作用させ、該麦類または雑穀類の
澱粉の95%以上を液化し、該液化物をそのままア
ルコールおよび米麹と共に仕込み、糖化熟成させ
ることを特徴とする酒精含有甘味調味料の製造
法。 2 麦類または雑穀類が割砕されたものである特
許請求の範囲第1項記載の製造法。
[Claims] 1. Wheat or millet is heat-denatured and acid or α
- A method for producing an alcohol-containing sweet seasoning, which comprises liquefying 95% or more of the starch of the barley or cereals by applying amylase, and adding the liquefied product as it is with alcohol and rice malt to saccharify and ripen it. . 2. The manufacturing method according to claim 1, wherein wheat or cereals are crushed.
JP11779180A 1980-08-28 1980-08-28 Preparation of alcohol-containing sweet seasoning Granted JPS5743661A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11779180A JPS5743661A (en) 1980-08-28 1980-08-28 Preparation of alcohol-containing sweet seasoning

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11779180A JPS5743661A (en) 1980-08-28 1980-08-28 Preparation of alcohol-containing sweet seasoning

Publications (2)

Publication Number Publication Date
JPS5743661A JPS5743661A (en) 1982-03-11
JPS6228660B2 true JPS6228660B2 (en) 1987-06-22

Family

ID=14720379

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11779180A Granted JPS5743661A (en) 1980-08-28 1980-08-28 Preparation of alcohol-containing sweet seasoning

Country Status (1)

Country Link
JP (1) JPS5743661A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0777153A1 (en) 1995-11-30 1997-06-04 Fuji Photo Film Co., Ltd. Silver halide color photographic light-sensitive material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0777153A1 (en) 1995-11-30 1997-06-04 Fuji Photo Film Co., Ltd. Silver halide color photographic light-sensitive material

Also Published As

Publication number Publication date
JPS5743661A (en) 1982-03-11

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