JPH0238195B2 - - Google Patents

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Publication number
JPH0238195B2
JPH0238195B2 JP57176348A JP17634882A JPH0238195B2 JP H0238195 B2 JPH0238195 B2 JP H0238195B2 JP 57176348 A JP57176348 A JP 57176348A JP 17634882 A JP17634882 A JP 17634882A JP H0238195 B2 JPH0238195 B2 JP H0238195B2
Authority
JP
Japan
Prior art keywords
rice
sake
brewing
water
refined
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 - Lifetime
Application number
JP57176348A
Other languages
Japanese (ja)
Other versions
JPS5966875A (en
Inventor
Satoshi Imayasu
Koji Suginami
Fumio Uchikoshi
Shoji Kawato
Kaoru Ooishi
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.)
Gekkeikan Sake Co Ltd
Original Assignee
Gekkeikan Sake 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 Gekkeikan Sake Co Ltd filed Critical Gekkeikan Sake Co Ltd
Priority to JP57176348A priority Critical patent/JPS5966875A/en
Publication of JPS5966875A publication Critical patent/JPS5966875A/en
Publication of JPH0238195B2 publication Critical patent/JPH0238195B2/ja
Granted legal-status Critical Current

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Description

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

〔産業上の利用分野〕 本発明は濃厚な清酒の醸造法に関し、詳しくは
原料利用率を向上させる清酒の醸造法に関する。 〔技術の背景および従来技術の説明〕 従来の清酒の醸造では、酒造用の高度に精白さ
れた精白米を米粒の状態で蒸きようして蒸米をつ
くり、これを酒造原料の麹米および掛米として使
用する。しかしながら製麹段階および発酵段階に
おいて粒状の蒸米が麹菌の培地となり、また麹菌
または酵母菌の酵素作用を受ける場合、その表面
に近いアルフアー化された米デン粉が利用される
だけであつて、その内部にあるアルフアー化され
た米デン粉は、麹菌または酵母菌に利用される以
前に老化するために、完全に利用され難い欠点が
ある。本発明者は、清酒の醸造において粒状の酒
造原料の粒径を細かくするならば、酒造原料の内
部にあるアルフアー化された米デン粉が老化する
以前に麹菌または酵母菌に利用されるであろうと
考えて、粉体状の米を使用する製麹法および清酒
の醸造法を提案した(特開昭58―43784号、特開
昭58―224679号および特開昭58―224680号)。こ
れらの方法では酒造原料が粉体状であるがゆえ
に、酒造原料の内部に存在する米デン粉も利用さ
れるので、原料利用率は大巾に向上するが、粉体
状の米をアルフアー化した場合、その加水倍率
(適当な粘度を有する溶液をつくるのに必要な水
の量)が大きいので、粉体状の米を利用する清酒
の醸造では、汲水歩合を常法よりも大きくしなけ
ればならない。しかしながら、これらの方法で
は、原料利用率が向上しているので、通常のアル
コール度を有する清酒の醸造であれば、汲水歩合
を大きくしても差支えはない。本発明者は、汲水
歩合を従来法のままにすることによつて、アルコ
ール度が高く、味の濃い貴醸酒タイプの清酒の醸
造ができると考えて、さらに研究を重ねて本発明
を完成するに到つた。 〔発明の目的および発明の要約〕 本発明の目的は、酒造原料の利用率が高く、ま
たアルコール度が高く、かつ味の濃い貴醸酒タイ
プの清酒の醸造法を提供することにある。 本発明のもう1つの目的は、工程管理が容易で
ある清酒の醸造法を提供することにある。 本発明は、清酒の醸造において、精製米の液化
液を掛米として使用することおよび汲水歩合を
120〜125%にすることを特徴とする清酒の醸造法
である。 〔発明の具体的な説明〕 本明細書における「精製米」は、玄米より酒造
原料として好ましくない成分、すなわち脂肪およ
び蛋白質を多く含む部分を除去して得られた米で
あつて、酒造用に高度に精白した従来の精白米を
アルフアー化しないように粉砕した粉末状の米の
他に、米を水の存在下において粉砕または摩砕
し、得られた乳液状のスラリーを遠心分離し、遠
心分離残渣中の米デン粉を多く含む部分を回収し
た粉状の米を含むものである。 次に本発明を具体的に説明する。 本発明では、精製米の液化液を清酒の醸造にお
ける掛米として使用する。精製米の液化液をつく
る場合、先ず最初に原料米を粉砕するが、原料米
の粉砕はなるべく細かい粒度の米粉を得ることが
好ましい。米粉の粒度を細かくすることによつて
米デン粉の液化が容易になり、また清酒の醸造に
おける粕歩合を低下させ、原料利用率を向上させ
ることができる。通常の場合、米粉の粒度は32メ
ツシユ以下、好ましくは100メツシユ以下、より
好ましくは150メツシユ以下である。原料米の粉
砕手段としては乾式および湿式のいずれの手段を
採ることができるが、湿式粉砕、すなわち原料米
を水に浸漬して充分に吸水させた後、グラインダ
ーまたはミキサーによつて粉砕するのが好まし
い、通常の場合は原料米として酒造用に高度に精
白した精白米を使用するが、米を粉砕した後に脂
肪および蛋白質を多く含む部分を除去するなら
ば、玄米または部分的に精白した白米も原料米と
して使用することができる。 玄米または部分的に精白した白米を原料米とし
て使用する場合、玄米または部分的に精白した白
米を水に浸漬し、充分に吸水させた後、グライン
ダーまたはミキサーによつて米粒を細かく粉砕し
て乳液状のスラリーをつくる。この粉砕における
粉砕度を細かくすることによつて、脂肪および蛋
白質を多く含む部分の除去を容易にすることがで
きる。乳液状のスラリーが100メツシユ篩(より
好ましくは145メツシユ篩)を通過しうる程度の
粒度に粉砕するのが好ましい。このようにして得
られた乳液状のスラリーを引続いて遠心分離す
る。これによつて乳液状のスラリーは上澄液と遠
心分離残渣に分れるが、遠心分離残渣において
は、その上層に脂肪および蛋白質を多く含む部分
が集積し、その下層に米デン粉を多く含む部分が
集積するので、この米デン粉を多く含む部分を取
り出して、本発明の精製米として使用する。 本発明において、上記の湿式手段によつて粉砕
した精製米粉または前記の湿式精製手段によつて
精製した精製米粉を用いる場合は、乾燥すること
なく、そのまま米デン粉の液化に使用するのが好
ましい。本発明の米デン粉の液化においては、充
分に吸水し、乳液状になつた米粉のスラリーに耐
熱性のα―アミラーゼ製剤を加え、α―アミラー
ゼの至適温度に加温して精製米の液化液を得る。 本発明では、このようにして得られた精製米の
液化液を清酒の醸造における掛米として使用する
ことによつて、粕歩合を低下し、それによつて米
デン粉の利用率を向上させる。清酒の醸造は一
段、二段、または三段あるいは四段仕込みのいず
れによることもできるが、工程の省力化の点で一
段仕込みを採るのが好ましい。清酒の醸造におけ
る汲水歩合は、常法通りの汲水歩合、すなわち、
120〜125%とし、それによつて濃厚な貫醸酒タイ
プの清酒をつくることができる。 すなわち、本発明による清酒の醸造の特徴は、
粕歩合が低下し、原料利用率が向上すること、お
よび汲水歩合を調整することによつて貫醸酒タイ
プの清酒を所望に応じてつくることができること
にある。 次に本発明において使用する湿式手段によつて
精製した精製米粉の製造の一例を参考例に示すと
ともに、実施の一例を実施例に示すが、本発明
は、これらの具体例に限定されるものではない。 参考例:(湿式法による精製米の製造) 玄米(日本晴)を精米によつて胚芽だけを除去
した白米(精白歩合:90%)1Kgに水1.2Kgを加
えて、一夜浸漬した後、ミキサー〔三菱電機(株)製
JM―362形〕で5分間粉砕して乳液状のスラリー
を得た。このスラリーを145メツシユの篩で篩別
した後、篩下のスラリーを遠心分離機に入れて、
5000r.p.m.において10分間遠心分離した。遠心分
離によつてスラリーは上澄液と遠心分離残渣に分
離したが、遠心分離残渣はさらに2層に分れ、上
に脂肪および蛋白質を多く含む部分が集積し、下
に米デン粉を多く含む部分(精製米部分)が集積
していた。この2層を別々に取り出して、50〜55
℃の温度で16時間乾燥した。精製米部分および脂
肪および蛋白質の多い部分の分析値を原料米の精
白歩合90%の白米および従来法の精白歩合73%の
白米の分析値と比較した結果を表1に示し、玄米
100gからの精製米の収量を従来法の精白歩合73
%の白米の収量と比較した場合の結果を表2に示
し、さらに原料米1000Kgを処理した場合に生ずる
廃水の汚染度を従来法の精白歩合73%の白米を洗
米した場合に生ずる廃水の汚染度を比較した結果
を表3に示す。なお分析はすべて国税庁所定の分
析法注解によつて行なつた。
[Industrial Field of Application] The present invention relates to a method for brewing rich sake, and more particularly to a method for brewing sake that improves the utilization rate of raw materials. [Technical background and explanation of conventional technology] In conventional sake brewing, highly polished rice for sake brewing is steamed in the form of rice grains to create steamed rice, which is then mixed with koji rice and kakekake, which are raw materials for sake brewing. Use as rice. However, in the koji production and fermentation stages, when granular steamed rice becomes a medium for koji mold and is subjected to the enzymatic action of koji mold or yeast, only the alpha-ized rice starch near the surface is used. The alpha-formed rice starch inside the rice starch deteriorates before it can be utilized by Aspergillus or yeast, so it has the disadvantage that it is difficult to be fully utilized. The present inventor believes that if the particle size of granular sake brewing raw materials is made finer in sake brewing, the alpha-formed rice starch inside the sake brewing raw materials will be utilized by Aspergillus or yeast before aging. With this in mind, he proposed a method for making koji and brewing sake using powdered rice (Japanese Patent Application Laid-Open No. 58-43784, JP-A No. 58-224679, and JP-A No. 58-224680). In these methods, since the raw material for sake brewing is in the form of powder, the rice starch present inside the raw material for sake brewing is also used, which greatly improves the raw material utilization rate, but it is difficult to turn the powdered rice into alpha. In this case, the water ratio (the amount of water required to make a solution with an appropriate viscosity) is large, so when brewing sake using powdered rice, the water pumping ratio must be larger than in the conventional method. There must be. However, these methods improve the raw material utilization rate, so if sake is brewed with a normal alcohol content, there is no problem even if the water pumping ratio is increased. The inventor of the present invention believed that by keeping the water pumping ratio the same as the conventional method, it was possible to brew Kijoshu-type sake with a high alcohol content and strong taste, and after further research, he completed the present invention. I came to the point. [Objective of the Invention and Summary of the Invention] An object of the present invention is to provide a method for brewing Kijoshu type sake that has a high utilization rate of sake brewing raw materials, a high alcohol content, and a strong taste. Another object of the present invention is to provide a method for brewing sake that is easy to control. The present invention uses the liquefied liquid of refined rice as kakemai and improves the water pumping ratio in the brewing of sake.
This is a method of brewing sake that is characterized by the sake being 120-125%. [Specific Description of the Invention] In this specification, "refined rice" refers to rice obtained by removing components undesirable as raw materials for sake brewing from brown rice, that is, parts containing a large amount of fat and protein. In addition to powdered rice, which is made by grinding highly polished conventional polished rice to prevent it from becoming alpha, rice is ground or ground in the presence of water, and the resulting milky slurry is centrifuged. It contains powdered rice obtained from the separated residue containing a large amount of rice starch. Next, the present invention will be specifically explained. In the present invention, a liquefied liquid of refined rice is used as rice for sake brewing. When producing a liquefied liquid of refined rice, the raw rice is first ground, and it is preferable to grind the raw rice to obtain rice flour with as fine a particle size as possible. By reducing the particle size of rice flour, it becomes easier to liquefy rice starch, and the lees ratio in sake brewing can be lowered to improve raw material utilization. Usually, the particle size of the rice flour is 32 mesh or less, preferably 100 mesh or less, more preferably 150 mesh or less. Both dry and wet methods can be used to crush raw rice, but wet crushing, that is, immersing raw rice in water to absorb enough water, and then crushing it with a grinder or mixer is preferable. Preferably, highly polished polished rice for sake brewing is used as raw material rice, but if the fat and protein-rich parts are removed after the rice is ground, brown rice or partially polished white rice may also be used. It can be used as raw rice. When using brown rice or partially milled white rice as raw material, soak the brown rice or partially milled white rice in water, absorb enough water, and then finely grind the rice grains with a grinder or mixer to make an emulsion. Make a slurry. By increasing the degree of pulverization in this pulverization, it is possible to easily remove portions containing a large amount of fat and protein. It is preferable to grind the emulsion-like slurry to a particle size that allows it to pass through a 100 mesh sieve (more preferably a 145 mesh sieve). The emulsion-like slurry thus obtained is subsequently centrifuged. As a result, the emulsion-like slurry is separated into a supernatant liquid and a centrifugation residue, but in the centrifugation residue, the upper layer contains a portion rich in fat and protein, and the lower layer contains a large amount of rice starch. Since the portions accumulate, the portions containing a large amount of rice starch are taken out and used as the refined rice of the present invention. In the present invention, when using refined rice flour pulverized by the above-mentioned wet method or refined rice flour refined by the above-mentioned wet refining method, it is preferable to use it as it is for liquefying rice starch flour without drying it. . In the liquefaction of rice starch flour of the present invention, a heat-resistant α-amylase preparation is added to the rice flour slurry that has sufficiently absorbed water and has become a milky liquid, and the mixture is heated to the optimum temperature for α-amylase to produce refined rice. Obtain liquefied liquid. In the present invention, the liquefied refined rice obtained in this way is used as rice for sake brewing, thereby reducing the lees ratio and thereby improving the utilization rate of rice starch. Sake brewing can be done in one, two, three, or four stages, but it is preferable to use one stage to save labor in the process. The water extraction rate in sake brewing is the conventional extraction rate, that is,
By setting it at 120-125%, it is possible to make a rich kanjoshu type of sake. In other words, the characteristics of sake brewing according to the present invention are as follows:
The lees ratio is lowered, the raw material utilization rate is improved, and by adjusting the pumping water ratio, it is possible to make kanjoshu-type sake as desired. Next, an example of the production of refined rice flour refined by wet means used in the present invention will be shown in Reference Examples, and an example of implementation will be shown in Examples, but the present invention is not limited to these specific examples. isn't it. Reference example: (Production of refined rice by wet method) Brown rice (Nipponbare) is polished to remove only the germ (polishing ratio: 90%). 1 kg of water is added to 1.2 kg of water, and after soaking overnight, it is mixed with a mixer. Manufactured by Mitsubishi Electric Corporation
JM-362 type] for 5 minutes to obtain a milky slurry. After sieving this slurry with a 145 mesh sieve, the slurry under the sieve was put into a centrifuge.
Centrifuged at 5000 rpm for 10 minutes. Through centrifugation, the slurry was separated into a supernatant liquid and a centrifugation residue, but the centrifugation residue was further divided into two layers, with the upper layer containing a lot of fat and protein, and the bottom layer containing a lot of rice starch. The containing portion (refined rice portion) was concentrated. Take out these two layers separately and add 50 to 55
Dry for 16 hours at a temperature of °C. Table 1 shows the results of comparing the analytical values of the refined rice portion and the fat and protein-rich portion with the analytical values of white rice with a milling ratio of 90% as raw material and white rice with a polishing ratio of 73% using the conventional method.
The yield of refined rice from 100g is determined by the polishing ratio of 73 using the conventional method.
The results are shown in Table 2 when compared with the yield of 73% white rice, and the contamination level of wastewater generated when 1000 kg of raw rice is processed is compared to the pollution level of wastewater generated when white rice with a polishing ratio of 73% is washed using the conventional method. Table 3 shows the results of comparing the degrees. All analyzes were conducted in accordance with the analysis method commentary prescribed by the National Tax Agency.

【表】【table】

【表】 表1によると、湿式法による精製米は従来法の
酒造米よりも粗脂肪および粗蛋白質含量が低い。
すなわち精製度の高いことがわかる。
[Table] According to Table 1, rice refined by the wet method has a lower crude fat and crude protein content than rice produced by the conventional method.
In other words, it can be seen that the degree of purification is high.

【表】 た場合の比率である。
表2によると、湿式法による精製米は従来法の
酒造米よりも収量が大きく、特にデン粉の収量が
さらに大きくなつている。
[Table] This is the ratio when
According to Table 2, rice refined by the wet method has a higher yield than rice produced by the conventional method, and in particular, the yield of starch is even higher.

【表】 表3によると、湿式法による精製米の製造から
生ずる廃水を浄化するのに必要な負荷は、従来法
の清酒の醸造から生ずる廃水のそれよりも大巾に
軽減されている。 実施例 精白歩合73%に精白した精白米(昭和56年産
米、日本晴)1Kgに水1.2Kgを加え、一夜水に浸
漬して充分に吸水させ、コクゲン〔耐熱性α―ア
ミラーゼ製剤、大和化成(株)の商品名〕0.5gを加
え、ミキサー〔三菱電機(株)JM―362形〕で3分間
粉砕して乳液状のスラリーを得た。このスラリー
を湯浴中で60〜90℃に10分間加温して米デン粉の
液化液2.2Kgを得た。 清酒の醸造における掛米として、この液化液
400g(白米換算)を用い、麹歩合20%および汲
水歩合123%、135%において総米500gで15℃定
温の1段仕込みを行なつた。仕込配合は表4に示
す通りである。 一方、対照として同じ精白米を常法によつて蒸
きようし、掛米として用い表5に示す仕込配合で
15℃定温の2段仕込みを行なつた。
[Table] According to Table 3, the load required to purify the wastewater generated from the production of refined rice using the wet process is significantly reduced compared to that of the wastewater generated from the conventional sake brewing process. Example: Add 1.2 kg of water to 1 kg of polished rice (produced in 1980, Nipponbare) polished to a polishing ratio of 73%, soak it in water overnight to absorb enough water, and prepare Kokugen [heat-resistant α-amylase preparation, Daiwa Kasei ( Co., Ltd. (trade name)] was added and ground for 3 minutes using a mixer (Mitsubishi Electric Co., Ltd. JM-362 model) to obtain a milky slurry. This slurry was heated in a water bath at 60 to 90°C for 10 minutes to obtain 2.2 kg of a liquefied rice starch liquid. This liquefied liquid is used as rice for sake brewing.
Using 400g (in terms of polished rice), one-stage preparation was carried out at a constant temperature of 15°C with 500g of total rice at a koji ratio of 20% and a water ratio of 123% and 135%. The preparation composition is as shown in Table 4. On the other hand, as a control, the same polished rice was steamed in a conventional manner and used as kakemai with the mixing ratio shown in Table 5.
Two stages of preparation were carried out at a constant temperature of 15°C.

【表】【table】

【表】 仕込み時のもろみ、および上層酒の分析結果を
表6、表7に示す。尚、分析は全て国脱庁所定の
分析法注解によつて行なつた。
[Table] Tables 6 and 7 show the analysis results of the moromi during preparation and of the upper layer sake. All analyzes were conducted in accordance with the analysis methods prescribed by the National Evacuation Agency.

【表】【table】

〔発明の効果〕〔Effect of the invention〕

粕歩合が低下し、原料利用率が向上する。 濃厚な清酒をつくることができる。 The lees ratio decreases and the raw material utilization rate improves. You can make rich sake.

Claims (1)

【特許請求の範囲】 1 清酒の醸造において、精製米のα―アミラー
ゼによる液化液を掛米として使用することおよび
汲水歩合を120〜125%にすることを特徴とする濃
厚な清酒の醸造法。 2 精白米を水の存在下に粉砕することによつて
得られた乳液状のスラリーを精製米として使用す
ることを特徴とする特許請求の範囲第1項に記載
の濃厚な清酒の醸造法。 3 米を水の存在下に粉砕し、得られた乳液状の
スラリーを遠心分離し、下層に集積した米デン粉
を多く含む精製米部分を精製米として使用するこ
とを特徴とする特許請求の範囲第1項に記載の濃
厚な清酒の醸造法。 4 掛米、麹米および汲水の全量を酒母に加える
ことを特徴とする特許請求の範囲第1項ないし第
3項のいずれかに記載の濃厚な清酒の醸造法。
[Scope of Claims] 1. A method for brewing rich sake, which is characterized by using a liquefied liquid produced by α-amylase from refined rice as rice for sake brewing, and setting the water ratio to 120 to 125%. . 2. The method for brewing rich sake according to claim 1, characterized in that a milky slurry obtained by pulverizing polished rice in the presence of water is used as the refined rice. 3. A patent claim characterized in that rice is ground in the presence of water, the resulting milky slurry is centrifuged, and the refined rice portion containing a large amount of rice starch accumulated in the lower layer is used as refined rice. A method for brewing rich sake as described in Scope 1. 4. The method for brewing rich sake according to any one of claims 1 to 3, characterized in that the entire amount of kakemai, kojimai, and water is added to the mash.
JP57176348A 1982-10-08 1982-10-08 Brewing of japanese sake by gelatinized liquid of rice Granted JPS5966875A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57176348A JPS5966875A (en) 1982-10-08 1982-10-08 Brewing of japanese sake by gelatinized liquid of rice

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57176348A JPS5966875A (en) 1982-10-08 1982-10-08 Brewing of japanese sake by gelatinized liquid of rice

Publications (2)

Publication Number Publication Date
JPS5966875A JPS5966875A (en) 1984-04-16
JPH0238195B2 true JPH0238195B2 (en) 1990-08-29

Family

ID=16012023

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57176348A Granted JPS5966875A (en) 1982-10-08 1982-10-08 Brewing of japanese sake by gelatinized liquid of rice

Country Status (1)

Country Link
JP (1) JPS5966875A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0525352U (en) * 1991-09-18 1993-04-02 日本特殊陶業株式会社 Lead wire lead structure in sensor
JP5851957B2 (en) * 2012-07-31 2016-02-03 月桂冠株式会社 Method for reducing sugar in sake and method for producing sake
JP2016015905A (en) * 2014-07-07 2016-02-01 サッポロビール株式会社 Sake and method of producing sake
JP6843482B2 (en) * 2017-06-30 2021-03-17 ヤンマーパワーテクノロジー株式会社 Rice gel manufacturing method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56117790A (en) * 1980-02-19 1981-09-16 Tomizo Takagi Preparation of refined sake (liquor)

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56117790A (en) * 1980-02-19 1981-09-16 Tomizo Takagi Preparation of refined sake (liquor)

Also Published As

Publication number Publication date
JPS5966875A (en) 1984-04-16

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