JPS6211061A - Gelatinized starch granule for brewing and production thereof - Google Patents
Gelatinized starch granule for brewing and production thereofInfo
- Publication number
- JPS6211061A JPS6211061A JP60149230A JP14923085A JPS6211061A JP S6211061 A JPS6211061 A JP S6211061A JP 60149230 A JP60149230 A JP 60149230A JP 14923085 A JP14923085 A JP 14923085A JP S6211061 A JPS6211061 A JP S6211061A
- Authority
- JP
- Japan
- Prior art keywords
- pregelatinized
- production
- brewing
- granule
- flour
- 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.)
- Granted
Links
Landscapes
- Alcoholic Beverages (AREA)
- Cereal-Derived Products (AREA)
- Grain Derivatives (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は清酒、焼酎等の酒類及び味噌の醸造を行う際に
、f11酵原料として使用されるアルファ化穀粉又はア
ルファ化澱粉質原料に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to pregelatinized grain flour or pregelatinized starch material used as a raw material for F11 fermentation when brewing alcoholic beverages such as sake and shochu, and miso.
従来の技術
酒類を製造する際、酒母、麹、水、蒸米及び蒸した穀類
等を混合調整して醪としているが、蒸米を蒸す工程を省
略するためにアルファ化した穀粉またはアルファ化した
澱粉質原料を使用する方法が考えられている。Conventional technology When producing alcoholic beverages, sake mother, koji, water, steamed rice, steamed grains, etc. are mixed and adjusted to make moromi, but in order to omit the step of steaming steamed rice, pregelatinized grain flour or pregelatinized starch is used. A method using raw materials is being considered.
このようなアルファ化物粉末を醪に添加すると、アルフ
ァ化物の溶解性が大きいために一度に醪中に溶は込み、
醪の粘度を増大させる。醪の粘度が増大すると、醪中の
対流が阻害されるので均一な醗酵が起りにくくなる。こ
のような欠点を改良するために、アルファ化した造粒物
を利用する方法が特開昭48−99397号公報、同5
5−111784号公報および同60−62976号公
報に示されている。これらの文献に記載されている方法
によれば、造粒物の製法は澱粉質原料を加圧蒸煮するこ
とによりアルファ化した後、常圧下に放出することによ
ってアルファ化と同時に乾燥を行なうものであって、ア
ルファ化された粒子が膨化して多孔質になるため、見掛
比重が小さくて嵩が大きくなる。このような見掛比重が
小さいアルファ化された粒子を醪に添加すると、アルフ
ァ化された粒子が浮遊して層をなし、醪の中で対流が起
りにくくなる。When such a pregelatin powder is added to the moromi, the solubility of the pregelatide is high, so it dissolves into the moromi all at once.
Increase the viscosity of the moromi. When the viscosity of the moromi increases, convection within the mortar is inhibited, making it difficult for uniform fermentation to occur. In order to improve these drawbacks, a method using pregelatinized granules is disclosed in Japanese Patent Application Laid-open Nos. 48-99397 and 5.
It is shown in 5-111784 and 60-62976. According to the methods described in these documents, the method for producing granules involves pregelatinizing starchy raw materials by pressure steaming and then drying them at the same time by releasing them under normal pressure. As a result, the alpha-ized particles expand and become porous, resulting in a small apparent specific gravity and a large bulk. When such pregelatinized particles with a small apparent specific gravity are added to the moromi, the pregelatinized particles float and form a layer, making it difficult for convection to occur in the moromi.
また、アルファ化され、膨化した粒子は溶解性が大きい
ため、糖化とアルコール醗酵のバランスが崩れ、極端な
場合には醪がベタつくという難点がある。さらに、アル
ファ化された粒子を味噌醸造用の原料として使用する場
合にも、このような膨化アルファ化粒子の吸水速度が過
大であるため、製麹の際に水分調整が困難となり、かつ
、麹がベタつく等の難点がある。In addition, because the particles that have been pregelatinized and expanded have a high solubility, the balance between saccharification and alcohol fermentation is disrupted, and in extreme cases, the mortar becomes sticky. Furthermore, when using pregelatinized particles as a raw material for miso brewing, the water absorption rate of such swollen pregelatinized particles is excessive, making it difficult to adjust the moisture content during koji making. There are disadvantages such as stickiness.
上記の事情のもとに、適度の溶解性と吸水性を有し、し
かも密度の大きなな顆粒状のアルファ化澱粉質原料が望
まれている。ところが、ひとたびアルファ化した澱粉質
原料を再加工する場合に、これに加湿すると澱粉の裁化
現象により、アルファ化度が低下し、酵素消化性が悪化
する。また、従来のホットローラー等によりアルファ化
したものを軽度に粉砕することにより、このような顆粒
状アルファ化澱粉質原料を得る方法もあるが、その方法
によると粒の大きさが不揃いになるため、ふるい分けに
よって整粒するのであるが。Under the above circumstances, a granular pregelatinized starchy raw material with appropriate solubility and water absorption and high density is desired. However, when a starchy raw material that has been pregelatinized is reprocessed, if it is humidified, the degree of pregelatinization decreases due to starch cleavage, and enzymatic digestibility deteriorates. There is also a method of obtaining such a granular pregelatinized starchy material by lightly crushing the pregelatinized material using a conventional hot roller, etc., but this method results in irregular grain sizes. The particles are sorted by sieving.
その方法では生産歩留が悪化するという欠点を避けられ
ない。This method cannot avoid the disadvantage that the production yield deteriorates.
発明が解決しようとする問題点
本発明の目的は、上記の諸欠点を解消し、酒類製造時に
おいては醪中で浮遊することなく、しかも醗酵を阻害す
ることがなく、また、味噌用麹を製造するために用いた
場合にも水分の量が容易に調整でき、しかも作業性が良
好で、さらに従来のアルファ化粒状物と同等もしくはそ
れ以上のアルファ化度を有するアルファ化穀粉もしくは
アルファ化澱粉質原料を提供することにある。Problems to be Solved by the Invention The purpose of the present invention is to eliminate the above-mentioned drawbacks, and to provide a method for producing koji for miso that does not float in the mortar during the production of alcoholic beverages and does not inhibit fermentation. Pregelatinized flour or pregelatinized starch whose moisture content can be easily adjusted when used for production, has good workability, and has a degree of pregelatinization equal to or higher than that of conventional pregelatinized granules. Our goal is to provide quality raw materials.
問題点を解決するための手段
発明者らは、見掛比重が0.5以上でアルファ化度が5
0%以上の範囲にあるアルファ化穀粉もしくはアルファ
化澱粉質原料の粒状物が本発明の目的に適合することを
知り、本発明に到達した。Means to Solve the Problem The inventors proposed that the apparent specific gravity be 0.5 or more and the degree of alphaning be 5.
The present invention was achieved based on the finding that granules of pregelatinized flour or pregelatinized starchy raw materials in a range of 0% or more are suitable for the purpose of the present invention.
上記の条件を満たすアルファ化穀粉もしくはアルファ化
澱粉質原料の粒状物は、前述の技術的問題点をすべて解
消すると同時に、醸造用醗酵原料として効率よく利用さ
れるものである。Granules of pregelatinized flour or pregelatinized starchy raw materials that meet the above conditions can solve all of the above-mentioned technical problems and at the same time can be used efficiently as fermentation raw materials for brewing.
本発明を構成する諸要素について、以下に詳説する。The various elements constituting the present invention will be explained in detail below.
(アルファ化穀粉)
本発明においてアルファ化穀粉とは、米、小麦、大麦等
の穀類の粉末をアルファ化した物のほか、粟、マイロ、
蕎麦等の雑穀類のアルファ化物や、トウモロコシのグリ
ッツやフラワーのアルファ化物をも包含する。(Pregelatinized grain flour) In the present invention, pregelatinized grain flour refers to pregelatinized powders of grains such as rice, wheat, and barley, as well as millet, milo,
It also includes pregelatinized products of cereals such as buckwheat noodles, and pregelatinized products of corn grits and flour.
(澱粉質原料)
本発明において澱粉質原料とは、精、製した地上澱粉た
とえばコーンスターチ、サゴスターチ等、及び精製した
地下澱粉たとえば馬鈴薯澱粉、甘藷澱粉、タピオカスタ
ーチ等を指す。(Starchy raw materials) In the present invention, starchy raw materials refer to refined above-ground starches such as corn starch, sago starch, etc., and refined underground starches such as potato starch, sweet potato starch, tapioca starch, etc.
これらの穀粉または澱粉質原料は、1種類だけを使用す
ることに限られず、このうち数種類を混合して使用して
もよい。These grain flours or starchy raw materials are not limited to the use of only one type, and several types thereof may be used in combination.
(製造方法)
発明者らは、前述の性状を有する密度の大きなアルファ
化造粒物を効率良く得る方法を検討してきた。(Manufacturing method) The inventors have studied a method for efficiently obtaining a high-density pregelatinized granule having the above-mentioned properties.
一般には醸造用アルファ化造粒物を製造するに際しては
、前出の特許公開公報に見られるように、押出型加圧蒸
煮機を使用する方法が経済的にも適している。Generally, when producing pregelatinized granules for brewing, it is economically suitable to use an extrusion-type pressure steamer, as shown in the above-mentioned patent publication.
しかしながら前述の性状を有する密度の大きなアルファ
化造粒物を得るには、100℃以上、好ましくは110
−150°Cの温度を有する高温部と、95℃以下、好
ましくは70〜90℃の温度の低温部を有する押出型加
圧蒸煮機が必要である。そこで発明者らは、その特性上
、バレル内で加熱および冷却のフントロールが可能であ
る二軸エクストルーダーに注目して試験を重ねた結果、
前記の温度条件でアルファ化及び冷却をした後、押出し
カッティング成型することにより、目的とする密度の大
きなアルファ化造粒物を得るに至った。However, in order to obtain a pregelatinized granule with a large density and the above-mentioned properties, the temperature must be 100°C or higher, preferably 110°C.
An extrusion type pressure steamer is required which has a high temperature section with a temperature of -150°C and a low temperature section with a temperature below 95°C, preferably between 70 and 90°C. Therefore, the inventors focused on the twin-screw extruder, which is capable of heating and cooling within the barrel due to its characteristics, and conducted repeated tests.
After pregelatinization and cooling under the above-mentioned temperature conditions, extrusion cutting molding was carried out to obtain a pregelatinized granule with a high target density.
また、必要があればバレル先端にて水分を吸引除去する
ことによって、押出し後の水分を適度に低下させてカッ
ティングを可悌にすると同時に。In addition, if necessary, by suctioning and removing moisture at the tip of the barrel, the moisture content after extrusion is appropriately reduced, making cutting more flexible.
見掛は比重を大きくすることもできる。The apparent weight can also be increased.
実 施 例
本発明をいっそう理解しやすくするために、以下に実施
例および対照例を示すが、本発明は下記の実施例によっ
て制限されるものではない。EXAMPLES In order to make the present invention easier to understand, examples and comparative examples are shown below, but the present invention is not limited to the following examples.
対照例1
原料水分 20 %バレル長
0.5mバレル温度 供給側
30℃(ホッパ一部)
グイ部 110℃
製品圧力 50 k g / c r
n’ダイ径 2mmφの条件で
、コーンスターチを二輪エクストルーダーにて処理し、
lll状状アルファ化コーンスターチ得た。Control example 1 Raw material moisture 20% Barrel length
0.5m barrel temperature supply side
30℃ (part of hopper) Gui part 110℃ Product pressure 50kg/cr
Cornstarch was processed with a two-wheeled extruder under the condition of n' die diameter 2mmφ,
ll-shaped pregelatinized corn starch was obtained.
実施例1
[料水分 30 %バレル長
0.5mバレル温度 供給側
(ホッパ一部)30℃中央部(供給側) 100℃
グイ部 80℃
製品圧力 50kg/crn’°
ダイ径 2 m mφ
の条件で、コーンフラワーを二軸エクストルーダーにて
処理し、密度の大きな顆粒状アルファ化コーンフラワー
を得た。Example 1 [Feed water 30% Barrel length
0.5m barrel temperature Supply side (hopper part) 30℃ Center part (supply side) 100℃ Gui part 80℃ Product pressure 50kg/crn'°
Die diameter 2mm mφ
Corn flour was processed with a twin-screw extruder under the following conditions to obtain granular pregelatinized corn flour with a large density.
実施例2
原料水分 27%バレル長
1mバレル温度 供給側(ホッ
パ一部)30℃中央部(供給側) 140℃
中央部(グイ側) 100℃
ダイ側 70℃
製品圧力 70 k g / c m
″ダイ径 2mmφの条件で、
コーンスターチを二軸エクストルーダーにて処理し、密
度の大きな顆粒状アルファ化コーンスターチを得た。Example 2 Raw material moisture 27% Barrel length
1m barrel temperature Supply side (part of hopper) 30℃ Center section (supply side) 140℃ Center section (guinea side) 100℃ Die side 70℃ Product pressure 70 kg / cm
``Under the condition of die diameter 2mmφ,
Corn starch was processed using a twin-screw extruder to obtain granular pregelatinized corn starch with a large density.
性質の測定
対照例1、実施例1および実施例2によって試作した粒
状アルファ化物を、以下の項目につき評価測定した。Measurement of Properties The granular pregelatinized products prepared as samples in Control Example 1, Example 1, and Example 2 were evaluated and measured for the following items.
見掛は比重 試料そのままでの1fL容量分の重量を
測定した。Apparent Specific Gravity The weight of a 1fL volume of the sample as it was was measured.
吸水量 試料を一定時間水中(常温)に浸漬し、
10メツシユ金網にて
水を切ったときの重量増加分で
ある。Water absorption The sample is immersed in water (at room temperature) for a certain period of time,
This is the weight increase when water is drained using a 10-mesh wire mesh.
膨潤度 試料を一定時間水中(常温)に浸漬した
ときの沈降1体積値であ
る。Swelling degree This is the sedimentation volume value when a sample is immersed in water (at room temperature) for a certain period of time.
溶出成分量 試料を一定時間水中(常温)に浸漬し、
No、131の口紙に
て濾過した濾液中の固形分量で
ある。Amount of eluted components Immerse the sample in water (at room temperature) for a certain period of time,
This is the solid content in the filtrate filtered through No. 131 paper.
アルファ化度 試料に3倍量の水を加えて60℃とし、
市販の長瀬産業酒
運用酵素スピターゼを対試料
0.06%添加し、24時間攪
拌処理したときに生じた還元糖
分の全糖分に対する割合であ
る。(重量%固形分当り)
浮遊粒 試料の水中での浮遊粒体積の全体積に対
する割合であって、浸
漬60分後の値である。Degree of alphaning Add 3 times the amount of water to the sample and bring it to 60℃.
This is the ratio of the reducing sugar to the total sugar content when 0.06% of the commercially available Nagase Sangyo sake operating enzyme spitase was added to the sample and stirred for 24 hours. (per weight % solid content) Floating particles This is the ratio of the volume of suspended particles in water to the total volume of the sample, and is the value after 60 minutes of immersion.
測定結果を以下に記す。The measurement results are described below.
(注)対照例は溶出量が多いため吸水量と膨潤度を測定
できない。(Note) Water absorption and degree of swelling cannot be measured in the control example due to the large amount of elution.
発明の効果
本発明によって得られた醸造用アルファ化粒状物は、従
来のアルファ化量と比較して同等又はそれ以上のアルフ
ァ化度であり、見掛は比重、溶解性も従来使用されてい
る蒸米に近づけることも可能となった。更に、吸水速度
も従来のフルツーγ化量に比して小さく、製麹の際に前
浸漬による水分調整が容易となった。Effects of the Invention The pregelatinized granules for brewing obtained by the present invention have a degree of pregelatinization equal to or higher than that of conventional pregelatinization, and the apparent specific gravity and solubility are also higher than those conventionally used. It has also become possible to produce rice that is close to steamed rice. Furthermore, the water absorption rate is also lower than the amount of conventional full-to-γ conversion, making it easy to adjust the water content by pre-soaking during koji making.
Claims (4)
て、見掛比重が0.5以上であって、アルファ化度が5
0%以上であることを特徴とする醸造用アルファ化造粒
物。(1) Pregelatinized granulated grain flour or starchy raw material with an apparent specific gravity of 0.5 or more and a pregelatinization degree of 5
A pregelatinized granule for brewing, characterized in that the content is 0% or more.
アルファ化するに当り、温度100℃以上である高温部
と温度95℃以下である低温部を持つ押出型加圧蒸煮機
を使用することを特徴とする醸造用アルファ化造粒物の
製造法。(2) When pregelatinizing grain flour or starchy raw materials using an extrusion-type pressure steamer, use an extrusion-type pressure steamer that has a high-temperature section with a temperature of 100°C or higher and a low-temperature section with a temperature of 95℃ or lower. A method for producing a pregelatinized granule for brewing, characterized by:
特許請求の範囲第2項に記載の醸造用アルファ化造粒物
の製造法。(3) The method for producing pregelatinized granules for brewing according to claim 2, wherein the extrusion type pressure steamer is a twin-screw extruder.
の温度が70〜90℃である特許請求の範囲第2項また
は第3項に記載の醸造用アルファ化造粒物の製造法。(4) The method for producing pregelatinized granules for brewing according to claim 2 or 3, wherein the temperature of the high temperature section is 110 to 150°C and the temperature of the low temperature section is 70 to 90°C. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14923085A JPH0614860B2 (en) | 1985-07-09 | 1985-07-09 | Manufacturing method of alpha granulated product for brewing |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14923085A JPH0614860B2 (en) | 1985-07-09 | 1985-07-09 | Manufacturing method of alpha granulated product for brewing |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6211061A true JPS6211061A (en) | 1987-01-20 |
JPH0614860B2 JPH0614860B2 (en) | 1994-03-02 |
Family
ID=15470712
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14923085A Expired - Lifetime JPH0614860B2 (en) | 1985-07-09 | 1985-07-09 | Manufacturing method of alpha granulated product for brewing |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0614860B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62151170A (en) * | 1985-09-19 | 1987-07-06 | Aitoo Kk | Production of gelatinized starch for brewing of sake |
JPS6471474A (en) * | 1987-09-11 | 1989-03-16 | Japan Maize Prod | Granular gelatinized starch and preparation thereof |
JPH01306598A (en) * | 1988-06-02 | 1989-12-11 | Showa Alum Corp | Production of fluororesin coated aluminum alloy sheet |
KR100391509B1 (en) * | 2000-11-06 | 2003-07-16 | 삼보종합식품 주식회사 | Method For Producing Refined Rice Wine Made From Swelled Minor Grains |
KR100885087B1 (en) | 2007-10-10 | 2009-02-25 | 주식회사 빔테크 | A preparation method of gelatinized starch using extrusion process |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS511668A (en) * | 1974-03-18 | 1976-01-08 | Harada Sangyo Kk | Komekojojinzomai no seizoho |
JPS5619988A (en) * | 1979-07-24 | 1981-02-25 | Kobe Steel Ltd | Manufacture of filter plate |
-
1985
- 1985-07-09 JP JP14923085A patent/JPH0614860B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS511668A (en) * | 1974-03-18 | 1976-01-08 | Harada Sangyo Kk | Komekojojinzomai no seizoho |
JPS5619988A (en) * | 1979-07-24 | 1981-02-25 | Kobe Steel Ltd | Manufacture of filter plate |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62151170A (en) * | 1985-09-19 | 1987-07-06 | Aitoo Kk | Production of gelatinized starch for brewing of sake |
JPS6471474A (en) * | 1987-09-11 | 1989-03-16 | Japan Maize Prod | Granular gelatinized starch and preparation thereof |
JPH01306598A (en) * | 1988-06-02 | 1989-12-11 | Showa Alum Corp | Production of fluororesin coated aluminum alloy sheet |
KR100391509B1 (en) * | 2000-11-06 | 2003-07-16 | 삼보종합식품 주식회사 | Method For Producing Refined Rice Wine Made From Swelled Minor Grains |
KR100885087B1 (en) | 2007-10-10 | 2009-02-25 | 주식회사 빔테크 | A preparation method of gelatinized starch using extrusion process |
Also Published As
Publication number | Publication date |
---|---|
JPH0614860B2 (en) | 1994-03-02 |
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