JPS6265678A - Production of liquor - Google Patents
Production of liquorInfo
- Publication number
- JPS6265678A JPS6265678A JP60202534A JP20253485A JPS6265678A JP S6265678 A JPS6265678 A JP S6265678A JP 60202534 A JP60202534 A JP 60202534A JP 20253485 A JP20253485 A JP 20253485A JP S6265678 A JPS6265678 A JP S6265678A
- Authority
- JP
- Japan
- Prior art keywords
- starch
- granular
- raw material
- rice
- superheated steam
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Alcoholic Beverages (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、粒状α化澱粉を用いて製麹操作、仕込操作及
び醪管理を容易に行い、高品質の酒類を得る方法に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for obtaining high-quality alcoholic beverages by using granular pregelatinized starch to easily perform koji production, preparation, and mash management.
従来、清酒は米を主原料として製造されるためその価格
に占める原料米の割合が高いが、近年この原料米の価格
が高騰し、安価な清酒等の製造が次第に困難になりつつ
ある。Traditionally, sake is produced using rice as the main ingredient, so rice accounts for a high proportion of its price, but in recent years the price of this rice has soared, making it increasingly difficult to produce cheap sake.
そこで本発明者らは、価格が米より常に紙庫な澱粉を用
いて、従来の清酒等と同様な品質の酒類を製造すること
ができれば、酒造業界にとっ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、澱粉を加湿、造粒して
粒状澱粉となし、これを過熱水蒸気の存在下で加圧加熱
し、得られた粒状α化澱粉を酒造原料として使用すると
きは、製麹し易く、仕込時に作業場に飛散せず粉塵公害
が少なく、取扱いが容易で、また仕込に際し、醪中で原
料の分散が早く均一に行われ、溶は方が従来の蒸米と同
様に徐々に、しかも均一に行われ、酵母の増殖、発酵が
旺盛に行なわれ、醪管理を容易に行うことができ、風味
がスッキリとして、非常に嗜好性の高い酒類が得られる
ことを発見し。Therefore, the present inventors focused on the fact that it would be a great contribution to the sake brewing industry if it were possible to produce alcoholic beverages of the same quality as conventional sake, etc., using starch, which is always cheaper than rice. As a result of various studies, we have found that when starch is humidified and granulated into granular starch, which is heated under pressure in the presence of superheated steam, and the resulting granular pregelatinized starch is used as a raw material for sake brewing, It is easy to make koji, it does not scatter in the workplace during preparation, there is little dust pollution, and it is easy to handle.Also, during preparation, the ingredients are dispersed quickly and uniformly in the moromi, and the melting process is gradual, similar to traditional steamed rice. Moreover, they discovered that the fermentation process was uniform, the yeast multiplication and fermentation were active, the mash could be easily controlled, and a highly palatable alcoholic beverage with a clean flavor could be obtained.
この知見に基いて本発明を完成した。The present invention was completed based on this knowledge.
即ち、本発明は、澱粉を加湿、造粒して粒状澱粉となし
、これを過熱水蒸気の存在下で加圧加熱し、得られた粒
状α化澱粉を原料として使用することを特徴とする酒類
の製造法である。That is, the present invention provides an alcoholic beverage characterized by humidifying and granulating starch to obtain granular starch, pressurizing and heating this in the presence of superheated steam, and using the obtained granular pregelatinized starch as a raw material. This is the manufacturing method.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
先ず、本発明において用いられる澱粉としては、大麦、
小麦、エンバク等の麦類から分離した澱粉、コーン(ト
ウモロコシ)、粟、稗、黍、高梁、マイロ等の雑穀類か
ら分離した澱粉、及び馬鈴薯、せ薯、キャラサバ等、芋
類から分離した澱粉等が挙げられる。そして、これらは
単用或いは併用しても良い。本発明は、分離した澱粉を
用いることを必須要件としているが、麦類、雑穀類、及
び芋類を割砕又は粉砕(粉末化も含む)しただけのもの
は、これを原料として製造した生成酒のアミノ酸度が高
く、雑味の多い酒質となり、また着色度が大となり、活
性炭等の精製剤を多址使用しなければ、淡麗な酒類が得
にくく、商品価値の低下はまぬがれない。First, the starches used in the present invention include barley,
Starch separated from barley such as wheat and oats; starch separated from cereals such as corn, millet, millet, millet, takaliang, and milo; and starch separated from potatoes such as potatoes, horse mackerel, and mackerel. etc. These may be used alone or in combination. Although the present invention requires the use of separated starch, products made by simply crushing or pulverizing (including powdering) wheat, cereals, and potatoes are not suitable for products manufactured using this as a raw material. The high amino acid content of alcoholic beverages results in alcoholic beverages with a lot of off-flavors and a high degree of coloring, making it difficult to obtain clear-tasting alcoholic beverages without frequent use of refining agents such as activated carbon, which inevitably leads to a decline in product value. .
次に、この澱粉を加湿、造粒して粒状澱粉とする方法と
しては、該澱粉に水分を均一に加えて、水分が15〜5
0%、好ましくは20〜40%の湿潤塊状体(又は湿潤
混線体)となし、これを通常の造粒手段により、外径1
〜15m111、好ましくは3−8mmの粒状澱粉を得
る。上記加湿及び造粒は順次行っても良いが、一工程で
一気に行っても良い。Next, as a method of humidifying and granulating this starch to make granular starch, water is added uniformly to the starch, and the water content is 15 to 5.
0%, preferably 20 to 40%, into a wet mass (or wet mixed mass), which is then processed by ordinary granulation means to an outer diameter of 1
A granular starch of ~15 m111, preferably 3-8 mm is obtained. The humidification and granulation may be performed sequentially, or may be performed all at once in one step.
上記造粒手段としては、転動造粒法、流動層造粒法、攪
拌造粒法、解砕造粒法、圧縮成形法、及び押出し成形法
等が挙げられる。また、I−記加湿及び/又は造粒に際
し、該澱粉にバインダー(例えば澱粉に水又は温湯を加
え攪拌しながら加熱して得られる糊)を加えると、粒状
澱粉がこオ)れにくくなるので好ましい。この場合、糊
は澱粉に対して10〜100重鼠%、特に30〜80%
添加することが好ましい。Examples of the granulation means include rolling granulation, fluidized bed granulation, stirring granulation, crushing granulation, compression molding, and extrusion molding. In addition, when humidifying and/or granulating the starch described in Section I, adding a binder (for example, a glue obtained by adding water or hot water to starch and heating it while stirring), the granular starch becomes difficult to break. preferable. In this case, the glue is 10-100% starch, especially 30-80%
It is preferable to add.
また、このようにして得られた粒状澱粉は、そのままで
も良いが、水分が多い場合法の過熱水蒸気工程で、相互
に付着結合し易いので、水分が5〜25%、好ましくは
10〜20%となるように乾燥することが好ましい。乾
燥方法としては、通風乾燥、熱風乾燥、真空乾燥等、任
意の手段が挙げられる。The granular starch obtained in this way may be used as it is, but in the superheated steam step of the method when the water content is high, the water content is 5 to 25%, preferably 10 to 20%, since it tends to adhere and bond to each other. It is preferable to dry it so that it becomes . Examples of the drying method include any means such as ventilation drying, hot air drying, and vacuum drying.
そして、表面のみ乾燥させて得られる粒状澱粉は、過熱
水蒸気が当っても、相互に付着結合しにくいので、処理
が容易であるばかりでなく、内部に保有される水分が多
いため膨化処理(加圧加熱後急激に解圧処理)した場合
に、好適な粒状α化澱粉となるので好ましい。Granular starch obtained by drying only the surface is not only easy to process because it is difficult to adhere and bond to each other even when exposed to superheated steam, but it also has a large amount of water retained inside, so it is not only easy to process, but also has a large amount of moisture inside. It is preferable to perform a rapid depressurization treatment after pressure heating, as this will result in a suitable granular pregelatinized starch.
次に、上記粒状澱粉を過熱水蒸気の存在下で加圧加熱し
、粒状α化澱粉を得る。Next, the granular starch is heated under pressure in the presence of superheated steam to obtain granular pregelatinized starch.
本発明において、粒状澱粉の加熱媒体として過熱水蒸気
を用いることは極めて重要であって、他の加熱媒体、例
えば加熱空気や飽和水蒸気は本発明の目的を達成するこ
とができないので好ましくない。In the present invention, it is extremely important to use superheated steam as a heating medium for granular starch, and other heating media, such as heated air or saturated steam, are not preferred because they cannot achieve the purpose of the present invention.
即ち、加熱空気の場合には熱伝導性が悪いので=4−
粒状澱粉の内部まで品温を上昇させるのに長時間を要し
、また局部的に高温となって粒状澱粉の全体に亘って均
一に昇温しにくく、焦げを生じ易く、更に粒状澱粉が短
時間に酸化による褐変を招来し易い等の問題点を有し、
また得られる酒類が好ましくない味、焦臭を有し、色沢
も褐色味を帯びる。In other words, in the case of heated air, the thermal conductivity is poor, so it takes a long time to raise the temperature to the inside of the granular starch, and the temperature locally becomes high and the temperature rises throughout the granular starch. It has problems such as it is difficult to raise the temperature uniformly, it tends to burn, and granular starch tends to brown due to oxidation in a short period of time.
In addition, the alcoholic beverages obtained have an unpleasant taste, a burnt odor, and a brownish color.
また、飽和水蒸気の場合には、粒状澱粉が飽和水蒸気と
接触すると、該水蒸気が凝縮して粒状澱粉の表面に付着
し、表面の澱粉が糊化するので、粒状澱粉が相互に付着
結合し、大きな塊りになったり、装置の内壁面に付着し
たり、或いは局部的に水分が増加したりして、均一にα
化した粒状澱粉(本発明では、これを粒状α化澱粉とい
う)を得にくくなる。In addition, in the case of saturated steam, when granular starch comes into contact with saturated steam, the steam condenses and adheres to the surface of the granular starch, and the starch on the surface gelatinizes, so that the granular starch adheres and bonds with each other. If it becomes a large lump, adheres to the inner wall surface of the device, or increases moisture locally, α
This makes it difficult to obtain granular pregelatinized starch (in the present invention, this is referred to as granular pregelatinized starch).
これに対して、過熱水蒸気を用いる場合には、粒状澱粉
の酸化による褐変、焦げ、澱粉の部分的水分過多、糊化
、粒状澱粉の塊状化、α化ムラ等、品質劣化を防止しつ
つ短時間に粒状澱粉の品温を上昇させ、酒類の製造に際
し、麹原料及び/又は掛原料として非常に好ましい粒状
α化澱粉を得ることができる。On the other hand, when using superheated steam, it is possible to prevent quality deterioration such as browning and scorching due to oxidation of granular starch, partial excess moisture in starch, gelatinization, clumping of granular starch, uneven gelatinization, etc., while preventing quality deterioration. By increasing the temperature of granular starch over time, it is possible to obtain granular pregelatinized starch, which is highly preferable as a koji raw material and/or a kake raw material in the production of alcoholic beverages.
次に、粒状澱粉の加圧加熱条件は、粒径の大小、粒の内
部と外表面での水分差、希望する膨化の程度によっても
異なるが、通常はケージ圧0.5〜15kg/cm2、
特に2〜9 kg/cm”が好ましく、温度115℃〜
350℃、特に150〜260℃が好ましい。また時間
は2秒〜5分、特に5秒〜2分が好ましい。そして上記
加圧加熱条件の温度と時間の関係は反比例関係にあり、
温度が高いときは時間を短くし、温度が低いときは時間
を長くすることが好ましい。Next, the pressure and heating conditions for granular starch vary depending on the particle size, the moisture difference between the inside and outside of the grain, and the desired degree of swelling, but usually the cage pressure is 0.5 to 15 kg/cm2,
In particular, 2 to 9 kg/cm" is preferable, and the temperature is 115°C to
350°C, especially 150-260°C is preferred. Moreover, the time is preferably 2 seconds to 5 minutes, particularly 5 seconds to 2 minutes. The relationship between temperature and time under the above pressure and heating conditions is inversely proportional.
It is preferable to shorten the time when the temperature is high and to lengthen the time when the temperature is low.
本発明で用いる過熱水蒸気の加熱条件は前述の通りであ
るが、該条件がゲージ圧15kg/Cl11”、温度3
50℃を越える場合は、澱粉に焦臭が付着し、また着色
(褐変)及び焦げが著しくなるので好ましくない。また
反対に、ゲージ圧が0.5kg/cm”、温度が115
℃未満であると、粒状澱粉のα化が充分に行えず、目的
とする粒状α化澱粉を得ることが困難となるので好まし
くない。The heating conditions for the superheated steam used in the present invention are as described above.
If the temperature exceeds 50°C, it is not preferable because a burnt odor will adhere to the starch and the coloring (browning) and scorching will become significant. On the other hand, the gauge pressure is 0.5 kg/cm" and the temperature is 115
If it is less than 0.degree. C., the granular starch cannot be sufficiently gelatinized, making it difficult to obtain the desired granular gelatinized starch, which is not preferable.
これに対し、加熱条件がゲージ圧0.5−15kg/c
I++2、温度115〜350℃であるときは、上記不
都合のない好適な粒状α化澱粉が得られる。On the other hand, the heating conditions are gauge pressure 0.5-15 kg/c.
When the temperature is I++2 and the temperature is 115 to 350°C, suitable granular pregelatinized starch without the above-mentioned disadvantages can be obtained.
このようにして加圧加熱された粒状澱粉は、除徐に、又
は、好ましくは瞬間的に、より低圧下、例えば大気圧下
に放出し、粒状α化澱粉を得る。The granular starch thus heated under pressure is gradually or preferably instantaneously released under lower pressure, for example atmospheric pressure, to obtain granular pregelatinized starch.
−に記過熱水蒸気処理を実施するための装置としては、
例えば特公昭46−34747 r気流加熱方式による
膨化食品製造方法及び装置」、特公昭55−33622
「連続式蒸煮加熱装置」、特開昭56−26180 r
粉粒物の加熱殺菌法」に記載された装置、特開昭57−
82686 r粉粒物質の加熱処理方法及び装置」等が
挙げられる。- The equipment for carrying out the superheated steam treatment described in
For example, Japanese Patent Publication No. 46-34747 r "Method and Apparatus for Producing Puffed Foods by Air Stream Heating Method", Japanese Patent Publication No. 55-33622
"Continuous steaming and heating device", JP-A-56-26180r
Apparatus described in "Heat sterilization method for powder and granular materials", JP-A-57-
82686r "Method and Apparatus for Heat Treatment of Particle Substances".
次に、こうして得られた粒状α化澱粉は、清酒及び焼酎
等の酒類の製造法における麹原料及び/又は掛原料の、
一部又は全部として使用することができる。Next, the granular pregelatinized starch thus obtained is used as a koji raw material and/or a kake raw material in the manufacturing method of alcoholic beverages such as sake and shochu.
It can be used in part or in whole.
即ち、麹原料として用いるときは、従来の米麹の製造法
の蒸米と同様に、この粒状α化澱粉に水分を添加して湿
潤体となし、これにアスペルギルス・オリゼー等の種麹
菌を接種し、盛込したのち、品温30〜40℃で、適宜
攪拌をして、2〜4日で麹を得ることができる。この麹
は従来の清酒や焼酎の米麹と同様に使用することができ
る。That is, when used as a raw material for koji, water is added to this granular pregelatinized starch to form a wet mass, and a seed koji mold such as Aspergillus oryzae is inoculated into this in the same way as steamed rice in the conventional rice koji manufacturing method. After adding the ingredients, koji can be obtained in 2 to 4 days by stirring appropriately at a temperature of 30 to 40°C. This koji can be used in the same way as conventional rice koji for sake and shochu.
また掛原料として使用するときは、後述の実施例1に示
す如く、蒸米(揚米)、麹米、汲水、酸(例えば乳酸)
及び酵母を混合して醪として発酵させる従来の清酒の製
造法、の該蒸米の一部又は全部として使用するか、或い
は後述の実施例2に示す如く、麹米、蒸米(揚米)、汲
水及び酵母を混合して醪として発酵、熟成させ、蒸留(
例えば減圧蒸留)する従来の焼酎の製造法、の該蒸米の
一部又は全部として使用する。In addition, when used as a raw material, steamed rice (ageed rice), koji rice, pumped water, acid (for example, lactic acid), as shown in Example 1 below, are used.
It can be used as part or all of the steamed rice in the conventional sake production method, in which yeast is mixed and fermented as moromi, or as shown in Example 2 below, it can be used as koji rice, steamed rice (ageed rice), or kumimai. Water and yeast are mixed to make moromi, fermented, aged, and distilled (
For example, it is used as part or all of the steamed rice in the conventional shochu production method (e.g., vacuum distillation).
本発明の利点を挙げると次の通りである。The advantages of the present invention are as follows.
従来の粉体状のα化澱粉は、溶けが早過ぎるため、醪の
粘度が急激に高くなるので、酵母の増殖が遅れ、発酵が
緩慢となり、従って歩留りも悪くなる傾向を有するが、
本発明の粒状α化澱粉は、少しづつ、徐々に溶けるので
、酵母の増殖及び発酵も旺盛となり、従来の蒸米を揚米
とする醪と殆ど同じ醪経過をたどり、歩留りも向上する
。Conventional powdered pregelatinized starch dissolves too quickly and the viscosity of the moromi increases rapidly, which delays the growth of yeast and slows down fermentation, which tends to lower the yield.
Since the granular pregelatinized starch of the present invention dissolves little by little, the growth and fermentation of yeast will be active, and the process of moromi will be almost the same as that of conventional moromi using steamed rice as fried rice, and the yield will also improve.
また1本発明で用いる粒状α化澱粉は、粉体ではなく粒
状で、全体的に多花性(ポーラス)であるが比較的緻密
で固いため、取扱いが容易で、粒内部への麹菌のハゼ込
みが良好で麹原料として好適に用いることができる。In addition, the granular pregelatinized starch used in the present invention is not a powder but a granule, and although it is porous as a whole, it is relatively dense and hard, so it is easy to handle, and it is easy to handle the granular pregelatinized starch. It has good incorporation and can be suitably used as a raw material for koji.
また仕込操作のとき、作業場に飛散しないため粉塵公害
が少なく、取扱いが容易である。In addition, during the preparation operation, there is less dust pollution because it does not scatter in the workplace, and it is easy to handle.
また、粉末状のα化澱粉は清酒醪や焼耐醪の如く、汲水
の割合が比較的少ない醪に混入されると部分的に粘着結
合して、醪中に小さな塊状物が出来易く、この部分の溶
けが遅延し、糖化の速度も不均一となり、醪管理が比較
的むずかしいが、本発明の粒状α化澱粉は、粒状である
ため、部分的に小さな塊状物とはならず、醪に対して均
一に、しかも速やかに分散し、醪管理が容易である。In addition, when powdered pregelatinized starch is mixed into a moromi with a comparatively low proportion of water, such as sake mash or roasted mash, it tends to partially adhesively bond and form small lumps in the mash. The dissolution of this part is delayed, the rate of saccharification becomes uneven, and it is relatively difficult to manage the moromi. However, since the granular pregelatinized starch of the present invention is granular, it does not form small lumps locally, and the mortar The mash is dispersed evenly and quickly, making it easy to manage the mash.
更に、本発明は澱粉を原料として使用するため淡麗で、
風味がスッキリとしており、非常に嗜好性の高い酒類が
得られる。Furthermore, since the present invention uses starch as a raw material, it is light and
The resulting alcoholic beverage has a refreshing flavor and is highly palatable.
以下、実験例及び実施例を示して本発明の効果を具体的
に説明する。Hereinafter, the effects of the present invention will be specifically explained with reference to experimental examples and examples.
実験例1
原料として、コーンスターチ(水分10%) 10kg
を用い、これに馬鈴薯澱粉10重量%水溶液を攪拌しな
がら加熱して得られる澱粉糊6kgを混ぜ、混練して、
湿潤混線物を得、これを(株)岩魚製作所、単式製粒機
のバスケット(孔径5mmの多孔板)上に入れ、押出に
より造粒し、80”Cの熱風通風乾燥機にかけ、粒体の
平均水分15.0%の粒状澱粉を得た。Experimental example 1 10 kg of cornstarch (moisture 10%) as raw material
was mixed with 6 kg of starch paste obtained by heating a 10% by weight potato starch aqueous solution with stirring, and kneaded.
A wet mixed material was obtained, which was placed in a basket (perforated plate with a hole diameter of 5 mm) of a single-type granulator made by Iwao Seisakusho Co., Ltd., and granulated by extrusion. Granular starch with an average moisture content of 15.0% was obtained.
次に、この粒状澱粉を気流加熱方式による連続式加圧加
熱装置(特公昭46−34747号公報に記載の装置)
に連続的に導入し、下記第1表記載の各加圧加熱条件に
て、加熱処理し、それぞれ第1表記載の如き外観及び特
徴を有する粒状α化コーンスターチが得られた。Next, this granular starch is heated using a continuous pressure heating device using an air current heating method (device described in Japanese Patent Publication No. 46-34747).
, and heat-treated under the pressure and heating conditions listed in Table 1 below to obtain granular pregelatinized cornstarch having the appearance and characteristics listed in Table 1.
それらの酵素剤による消化性(酒米研究会「酒米統一分
析法」による)、及びα化度〔貝沼圭二等著、「澱粉化
学」Z旦、 235 (1981)による〕は第1表に
示す通りである。The digestibility of these enzymes (according to the Sake Rice Research Group's "Unified Analysis Method for Sake Rice") and degree of gelatinization (according to Keiji Kainuma et al., "Starch Chemistry," Zdan, 235 (1981)) are shown in Table 1. As shown.
第1表の結果から、飽和水蒸気を用いる区分2は全体的
にベトベトして部分的な塊りとなり、α化度も低く、直
接還元糖、ボーメもやや低く、消化性がやや低い難点を
有し、また加熱空気を用いる区分3は全体的に淡褐色と
なり、かなりの焦臭を有するが、過熱水蒸気を用いる区
分1は、得られた粒状α化コーンスターチが全体的にサ
ラサラとした顆粒状で、塊状物はなく、白色で、異臭も
なく、またα化度が非常に高い値を示し、更にまた消化
性についてもボーメ、直接還元糖が高く、良好な結果が
得られることが判る。From the results in Table 1, it can be seen that Category 2, which uses saturated steam, is sticky overall and forms partial lumps, has a low degree of gelatinization, has a slightly low level of direct reducing sugar and Baumé, and has the disadvantages of slightly low digestibility. In addition, in Category 3, which uses heated air, the overall color becomes light brown and has a considerable burnt odor, but in Category 1, which uses superheated steam, the obtained granular pregelatinized cornstarch is entirely smooth and granular. It is clear that there are no lumps, the color is white, there is no off-odor, the degree of gelatinization is very high, and the digestibility is high in Baume and direct reducing sugars, indicating that good results can be obtained.
=11−
実験例2
上記実験例1の粒状αコーンスターチの製造法において
、製粒機のバスケットの孔径を、第2表に示す如き孔径
とする以外は、全く同様にして各種粒径の異なる粒状α
化コーンスターチを得た。=11- Experimental Example 2 In the method for producing granular α cornstarch in Experimental Example 1 above, granules with different particle sizes were prepared in exactly the same manner except that the pore diameter of the basket of the granulator was set to the pore diameter as shown in Table 2. α
Corn starch was obtained.
そして、粒状澱粉の粒径と、該粒状澱粉を過熱水蒸気で
加熱処理して得られる粒状α化澱粉の特徴(結着塊生成
)との関係について調べたところ、第2表に示す如き結
果が得られた。When we investigated the relationship between the particle size of granular starch and the characteristics of granular pregelatinized starch (formation of cohesive lumps) obtained by heat-treating the granular starch with superheated steam, we found the results shown in Table 2. Obtained.
第2表の結果から、粒状澱粉の粒径がト■であるときは
、結着塊が多いが、2ml11となると少なくなり、3
mm以上となると散見されなくなることが判る。即ち粒
状澱粉の粒径は2m+a以上であると、非常に好ましい
粒状α化澱粉が得られることが判る。From the results in Table 2, it can be seen that when the particle size of the granular starch is T, there are many bound lumps, but when the particle size is 2ml11, there are fewer and 3
It can be seen that when the diameter is larger than mm, they are no longer seen. That is, it can be seen that a very preferable granular pregelatinized starch can be obtained when the particle size of the granular starch is 2 m+a or more.
第2表
(注)十二多い
±:散見される
m:なし
実施例1
(各種澱粉を原料とする清酒の製造法)上記実験例1の
粒状α化コーンスターチの製造法において、原料として
下記第3表に示す如き澱粉を用いる以外は、」−記実験
例1と全く同様にして、各種の粒状α化澱粉を得た。Table 2 (Note) 12 more ±: Occasionally found m: None Example 1 (Method for producing sake using various starches as raw materials) In the method for producing granular pregelatinized cornstarch in Experiment Example 1 above, the following raw materials are used: Various granular pregelatinized starches were obtained in exactly the same manner as in Experimental Example 1 except that the starches shown in Table 3 were used.
次にこうして得た粒状α化澱粉を用い、通常の清酒の製
造法に準じ、次のような仕込配合で、清酒仕込を行った
。Next, using the granular pregelatinized starch thus obtained, sake was brewed according to the usual sake manufacturing method using the following brewing composition.
仕込配合
蒸 米(揚米) 100g粒状α化澱粉(
揚米)60g
麹米 40g
汲水 260g
なお、麹米は精米歩合75%の白米を常法通り製麹した
もので、乳酸(7,5%)を1 、2mQ加え、あらか
じめ培養した清酒酵母「に−701号(協会701号)
」な汲水1+oQ当り1×107細胞となるように接種
し、仕込時から醪品温を15℃に保ち、通常の醪管理を
行った。Mixed steamed rice (fried rice) 100g granular pregelatinized starch (
60g of fried rice 40g of koji rice 260g of water 260g of kojimai The kojimai is made by koji-making the white rice with a polishing ratio of 75% using the conventional method, adding 1.2 mQ of lactic acid (7.5%), and pre-cultured sake yeast. Ni-701 (Association No. 701)
The mash was inoculated at 1 x 107 cells per 1+oQ of water, and the temperature of the mash was maintained at 15°C from the time of preparation, and the mash was managed as usual.
=15=
また対照として、昭和59年度産キタヒカリ白米(精米
歩合75%)の蒸米(30分間蒸し)を」−配位状α化
澱粉に代えて用い、イ1込を行い、仕込後16日目上上
槽を実施した。なお蒸し工程までに吸収した水分(白米
重量X O,4)を吸水から除いた。=15= In addition, as a control, steamed rice (30 minutes steamed) of Kitahikari white rice produced in 1982 (polishing ratio 75%) was used in place of the ``-coordination pregelatinized starch'', and A1 was added, and 16 days after preparation. A top tank was performed. Note that the water absorbed up to the steaming step (white rice weight X O, 4) was excluded from the water absorption.
粒状α化澱粉仕込の醪経過は、いずれの区分も白米(対
照)区分と比べて遅く、醪「I数は19[1と白米区分
の16日より3日遅くなるが、
製放酒の分析値及び官能上の特徴について調べたところ
第3表に示す如き結果が得られた。The fermentation time for the granular gelatinized starch preparation is slower in all categories than in the white rice (control) category, and the number of moromi is 19[1], which is 3 days later than 16 days in the white rice category. When the values and sensory characteristics were investigated, the results shown in Table 3 were obtained.
2m が閣 ! ! !>!・・V 々ゼ 硬 。 。 ゆ L 。2m ! ! ! >!・・V taze Hard. . hot water L.
88 8 旨 8
d4 ・
穎 j
$lま 宮 8 国
中 ) 二 二 、 凶
轍@ト −−
第3表の結果から過熱水蒸気で処理した粒状α化澱粉を
用いる本発明の区分1〜;3は、常法により得られた蒸
米を用いる対照区分4に比べて、成分分析値が好ましい
結果を示し、製放酒についても異味、異臭(焦臭)がな
く、軽快な風味、即ちスッキリとした風味を有し、高品
質の酒類が得られることが判る。88 8 effect 8 d4 ・ 穎$ま宮 8 国中 ) 2 2 , Crazy @ To -- From the results in Table 3, categories 1 to 3 of the present invention using granular pregelatinized starch treated with superheated steam Compared to control category 4, which uses steamed rice obtained by a conventional method, the component analysis values showed favorable results, and the produced sake had no off-taste or odor (scorched odor) and had a light flavor, that is, a refreshing taste. It can be seen that a high-quality alcoholic beverage with good flavor can be obtained.
実施例2
(各種粒状α化澱粉を原料とする焼酎の製造)下記第4
表に示す原料澱粉を用い、−に記実験例】の粒状α化コ
ーンスターチの製造法と同様に処理し、各種粒状α化澱
粉を得た。Example 2 (Production of shochu using various granular pregelatinized starches as raw materials)
Using the raw material starches shown in the table, various types of granular pregelatinized starch were obtained by processing in the same manner as in the method for producing granular pregelatinized cornstarch in Experimental Example described in -.
次に、こうして得た粒状α化澱粉を用い、通常の焼酎の
製造法に準じ、次のような仕込配合で焼酎仕込を行った
。Next, using the granular pregelatinized starch obtained in this way, shochu was prepared according to the usual method for producing shochu, using the following preparation composition.
尚、酵母はrNo、A−12J (鹿児島工業試験場
)を用いた。The yeast used was rNo, A-12J (Kagoshima Industrial Research Institute).
仕込配合
また、比較のため、対照として白米(精米歩合75%)
の蒸米(30分蒸し)を、上記粒状α化澱粉に代えて用
い、仕込を行った。尚、蒸し工程までに吸収した水分(
白米重量X0.4)を汲水から除いた。本発明の粒状α
化澱粉仕込の醪経過は、いずれの区分も二次醪日数が1
4日であって、差が見られなかった。For comparison, white rice (75% rice polishing ratio) is used as a control.
Steamed rice (steamed for 30 minutes) was used in place of the granular pregelatinized starch. In addition, the moisture absorbed during the steaming process (
White rice weight x0.4) was removed from the pumped water. Granular α of the present invention
The number of days for secondary fermentation for all categories is 1.
After 4 days, no difference was observed.
得られた熟成醪のpll、酸度、アルコール濃度。pll, acidity, and alcohol concentration of the obtained aged moromi.
発酵歩合、及び該熟成醪を減圧蒸留して得られた焼酎の
官能上の評価をしたところ、第4表に示す如き結果が得
られた。When the fermentation ratio and the shochu obtained by distilling the aged moromi under reduced pressure were sensory evaluated, the results shown in Table 4 were obtained.
尚、発酵歩合は次式により求めたものである。Incidentally, the fermentation ratio was determined by the following formula.
第4表の結果から、過熱水蒸気で処理した粒状α化澱粉
を使用した本発明の第1〜第3区分は、対照区分に比べ
て発酵歩合が高く、製品焼酎の官能評価も異味、異臭(
焦臭)がなく、軽快な風味を有する新しいタイプの焼酎
が得られることが判る。From the results in Table 4, the fermentation rate of the first to third categories of the present invention, which use granular pregelatinized starch treated with superheated steam, is higher than that of the control category, and the sensory evaluation of the product shochu also shows that the product shochu has an off-taste, an off-odor (
It can be seen that a new type of shochu with a light flavor and no burnt odor can be obtained.
Claims (6)
熱水蒸気の存在下で加圧加熱し、得られた粒状α化澱粉
を原料として使用することを特徴とする酒類の製造法。(1) A method for producing alcoholic beverages characterized by humidifying and granulating starch to obtain granular starch, pressurizing and heating this in the presence of superheated steam, and using the obtained granular pregelatinized starch as a raw material. .
、タピオカ、モロコシ澱粉及び粟澱粉からなる群より選
ばれる1種又は2種以上である特許請求の範囲第1項記
載の酒類の製造法。(2) The method for producing an alcoholic beverage according to claim 1, wherein the starch is one or more selected from the group consisting of corn starch, potato starch, sweet potato starch, tapioca, sorghum starch, and millet starch.
とする特許請求の範囲第1項記載の酒類の製造法。(3) The method for producing alcoholic beverages according to claim 1, characterized in that granular pregelatinized starch is used as a koji raw material.
とする特許請求の範囲第1項記載の酒類の製造法。(4) The method for producing an alcoholic beverage according to claim 1, characterized in that granular pregelatinized starch is used as a raw material.
類の製造法。(5) The method for producing an alcoholic beverage according to claim 1, wherein the alcoholic beverage is sake.
類の製造法。(6) The method for producing an alcoholic beverage according to claim 1, wherein the alcoholic beverage is shochu.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60202534A JPS6265678A (en) | 1985-09-14 | 1985-09-14 | Production of liquor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60202534A JPS6265678A (en) | 1985-09-14 | 1985-09-14 | Production of liquor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6265678A true JPS6265678A (en) | 1987-03-24 |
Family
ID=16459089
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60202534A Pending JPS6265678A (en) | 1985-09-14 | 1985-09-14 | Production of liquor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6265678A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06196912A (en) * | 1993-09-27 | 1994-07-15 | Toshiba Corp | Antenna |
JP2007236269A (en) * | 2006-03-08 | 2007-09-20 | Ensuiko Sugar Refining Co Ltd | Powdery food material and method for treating the same |
JP2008228620A (en) * | 2007-03-19 | 2008-10-02 | Kirishimashuzo | Method for producing shochu (distilled white liquor) using sweet potato |
US7538849B2 (en) | 1995-02-15 | 2009-05-26 | Semiconductor Energy Laboratory Co., Ltd. | Active matrix display and forming method thereof |
-
1985
- 1985-09-14 JP JP60202534A patent/JPS6265678A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06196912A (en) * | 1993-09-27 | 1994-07-15 | Toshiba Corp | Antenna |
US7538849B2 (en) | 1995-02-15 | 2009-05-26 | Semiconductor Energy Laboratory Co., Ltd. | Active matrix display and forming method thereof |
US7924392B2 (en) | 1995-02-15 | 2011-04-12 | Semiconductor Energy Laboratory Co., Ltd. | Active matrix display and forming method thereof |
JP2007236269A (en) * | 2006-03-08 | 2007-09-20 | Ensuiko Sugar Refining Co Ltd | Powdery food material and method for treating the same |
JP2008228620A (en) * | 2007-03-19 | 2008-10-02 | Kirishimashuzo | Method for producing shochu (distilled white liquor) using sweet potato |
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