JP3813507B2 - Continuous cooling mixing method and continuous cooling mixing apparatus for raw materials for brewing - Google Patents

Continuous cooling mixing method and continuous cooling mixing apparatus for raw materials for brewing Download PDF

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JP3813507B2
JP3813507B2 JP2001400011A JP2001400011A JP3813507B2 JP 3813507 B2 JP3813507 B2 JP 3813507B2 JP 2001400011 A JP2001400011 A JP 2001400011A JP 2001400011 A JP2001400011 A JP 2001400011A JP 3813507 B2 JP3813507 B2 JP 3813507B2
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raw material
solid
mixing
heated
continuous cooling
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JP2003189833A (en
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栄 田中
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Fujiwara Techno Art Co Ltd
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Fujiwara Techno Art Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、加熱固体原料と該加熱固体原料以外の原料を混合する醸造用原料の連続冷却混合方法及び無端帯ベルト式連続冷却混合装置に関する。
【0002】
【従来の技術】
穀物等の原料を処理する場合、製造する製品等の種類によっては、加熱処理した原料にこの加熱固体原料以外の固体原料を合わせて混合処理することがある。例えば、醤油の醸造においては、原料大豆を蒸煮加熱後、冷却装置で冷却したものに、小麦を焙煎割砕したものを加えて混合撹拌し、その後製麹装置で麹作りするのが一般的である。混合方法としては、スクリューコンベアで混合しながら運搬する方法や、ミキサーで混合してコンベア等で運搬する方法等が一般的である。
【0003】
【発明が解決しようとする課題】
近年、食品分野の品質管理における国際化に伴い、従来の衛生管理だけでは不十分で、HACCP(Hazard Analysis and Critical Control Point:危害・分析・重要管理点)に対応した装置、設備でなければならない。そのためには原料が付着して残る可能性のある個所や機械の数を減らし、できるだけ洗浄性の良いシンプルな構造のものにする必要がある。スクリューコンベアは、密閉構造であるため夾雑物の侵入が無く、用途に応じてスクリューの形状を変えて使用できるという利点はあるが、スクリューの推進力で運搬するため磨耗が大きく効率は余り良くないだけでなく、その構造上スクリューに付着する原料の洗浄が難しい。ミキサーやコンベア等を使用した場合でも、原料の付着や洗浄個所が増えることに変わりはない。また、醸造分野においても技術の進歩に伴う大量生産処理のための機械化が進み、既設の建築施設の中でいかに効率よく機械装置の設置をするかが、生産能力を大きく左右する要因にもなっている。
【0004】
本発明においては、加熱処理した原料と合わせて2種以上の原料を混合処理する場合における、加熱固体原料の冷却工程と混合工程のサニタリー化・シンプル化を図れる方法の提供を課題とするものである。
【0005】
【課題を解決するための手段】
前記の問題解決を図るため、本発明では、通気性のある無端帯状の固体原料移送ベルト上で、加熱固体原料とこの加熱固体原料以外の固体原料を混合することとした。通気性のある無端帯状の固体原料移送ベルト上で混合処理することにより、同ベルト上で混合以外の工程ができることとなり、洗浄の手間暇と機械設置のコストダウンに大きく貢献できる。ここで「原料」とは、例えば丸大豆や脱脂加工大豆あるいは圧偏大豆、割砕小麦や麹麦等の小麦、白米等の穀物のほか、酵素生産等に用いる麸や米糠あるいはビーンフラワー等や、その他食品原料等をいい、これらを加熱して用いるものが「加熱固体原料」であり、加熱しない又は加熱後冷却して用いるものが「加熱固体原料以外の固体原料」である。原料の同種、異種は問わない。
【0006】
具体的には、(1)通気性のある無端帯状の移送ベルト上で加熱固体原料を通風冷却した後、この加熱固体原料以外の固体原料を混合する、又は(2)通気性のある無端帯状の移送ベルト上へ加熱固体原料と加熱固体原料以外の固体原料とを同時に投入して混合し、併せて通風冷却することとした。冷却工程と混合工程を同一装置(移送ベルト)上で実施することにより、洗浄とコストダウンに大きく貢献できるだけでなく、乗り移りが無いため、ほこりが立たず雑菌数も下がる。
【0007】
加熱固体原料以外の固体原料の投入位置については、固体原料の種類と特性に合わせ、様々な位置が考えられる。投入する固体原料が熱の影響を受けないものであれば、加熱固体原料と同時に投入する場合がある。冷却装置の最初から投入することにより、撹拌や熱の均一性、あるいは加熱固体原料が水分率の高い場合は水分の移行等も、速やかにできる。加熱固体原料以外の固体原料が熱の影響を受ける物である場合や加熱固体原料のみ冷却したい場合であれば、投入位置は加熱固体原料の冷却後の移送ベルト上が考えられる。ここから排出口までの間は積極的に通風冷却する必要は無く、ナイフクラッシャーやピンクラッシャー等の撹拌又は混合手段のみあればよい。また、冷却途中の移送ベルト上への投入も考えられる。冷却装置は、堆積した加熱固体原料の上方から下方へ通風してもよいが、下方から上方に向けて通風するとよい。その場合、移送ベルトの目詰まりが発生せず、送風された空気のほぼ全量が加熱固体原料中を通過するため、特に効果的である。
【0008】
加熱固体原料以外の固体原料は冷却装置上で全て投入する必要は無い。投入する固体原料の割合を制限し、後工程で投入することや、時間と共に投入量を変更することが考えられる。ここで、加熱固体原料以外の固体原料の種類は、単種類とは限らず、複数である場合も含まれる。その場合、前述したように固体原料の種類と特性に合わせ、投入位置と量をそれぞれ設定することにより、複数の投入固体原料に最適な混合ができるのである。
【0009】
固体原料の組合わせとしては、醤油醸造における原料処理の一例として、加熱固体原料が蒸煮大豆であり、この加熱固体原料以外の固体原料が小麦である組合わせを例示できる。ここでいう大豆とは丸大豆や脱脂加工大豆や圧偏大豆のことをいい、小麦とは割砕小麦や麹麦のことをいう。一般的に、加圧蒸煮装置により蒸煮された大豆は、連続冷却装置で冷却し、その後、移送ベルトコンベア上で小麦を追加投入し、ピンクラッシャー等で混合撹拌したものを、盛込コンベア等で製麹装置の中に盛り込むのである。このように、加熱固体原料が蒸煮大豆であり、蒸煮大豆以外の固体原料が小麦である本発明の連続冷却混合方法の実施により、個々の移送コンベアベルトがなくなるだけでなく、冷却装置から移送コンベアへの接続部分が減ることによるほこりの発生防止になり、サニタリー性とコストダウンが更に向上する。
【0010】
【発明の実施の形態】
以下、図を参照しながら、本発明の実施形態について説明する。図1は本発明を適用した醸造用原料の連続冷却混合装置(移送ベルト3下方から送風する方式)の概略縦断面図、図2は本発明を適用した別例の醸造用原料の連続冷却混合装置(移送ベルト3上方から送風する方式)の概略縦断面図、図3は醤油製造における原料から製麹までの従来の製造工程のフローチャート図であり、図4は醤油製造における原料から製麹までの本発明の製造工程のフローチャート図である。
【0011】
まず、図1に見られるように、冷却のために移送ベルト3下から上へと送風する装置構成の例について説明する。加熱原料(加熱固体原料)Kは、図1中左側に位置する投入口1から装置内に投入されて、ほぐし機及び均し機としてのピンクラッシャー2により略分散状態にほぐされた後、移送ベルト3上に堆積され、更にほぐし機としての横型ピンクラッシャー4により撹拌された後、図1中右側の排出口5へ移送される。本例の装置ではピンクラッシャー2の上方であって投入口1近傍にファン6が設けられており、略分散状態にほぐされた加熱原料K中を通過した空気の効率的な排気を図っている。移送ベルト3としては、通気性のあるステンレス製メッシュベルトや多数の通気用開孔を設けたステンレススチールベルトが用いられている。また、風洞7の右側にはこの加熱原料K以外の原料投入口8が配設されており、投入した追加原料(加熱固体原料以外の固体原料)Tは移送中の加熱原料K上に堆積し、原料投入口8の下方、図1中右よりの移送ベルト3上に設けた混合機としてのナイフクラッシャー9で撹拌混合される。移送ベルト3の下方に3区画に分けた風洞7が配設されており、風洞7の各々に対して、送風機10の二次側が接続されており、移送ベルト3を通して加熱原料K中を通過しながら送風できるように構成されている。各送風機10の送風能力は、移送ベルト3上に堆積される加熱原料K中を通過可能な送風圧力と送風量を備えるものである。
【0012】
各送風機10の二次側には送風量調節のためのダンパー11が配設され、外気の取り入れ口になっている一次側には、除菌フィルター12及び除塵フィルター13が配設されている。また風洞7の数は、加熱原料Kの冷却に伴う物性に合わせた送風ができるよう複数個あることが望ましいが、単数でも十分にその効果は発揮できる。
【0013】
図1は、追加原料(加熱固体原料以外の固体原料)Tを加熱原料(加熱固体原料)Kの冷却後又は冷却途中に投入する場合を想定しているが、図2のように追加原料Tを加熱原料Kと共に投入する場合も考えられる。加熱原料K及び追加原料Tは、図2中左側に位置する投入口1から装置内に投入されて、混合機としてのピンクラッシャー2により略分散状態にほぐされながら混合された後、移送ベルト3上に堆積され、更にほぐし機としての横型ピンクラッシャー4により撹拌された後、図2中右側の排出口5へ移送される。移送ベルト3としては、通気性のあるステンレス製メッシュベルトや多数の通気用開孔を設けたステンレススチールベルトが用いられている。移送ベルト3の下方に3区画に分けた風洞7が配設されており、風洞7の各々に対して、送風機10の一次側が接続されており、移送ベルト3を通して加熱原料K中を通過しながら吸引送風できるように構成されている。各送風機10の吸引送風能力は、移送ベルト3上に堆積される加熱原料K中を通過可能な送風圧力と吸引送風量を備えるものである。
【0014】
【実施例】
図1に示した醸造用原料の連続冷却混合装置を用いて、加熱原料Kとして醤油の原料となる脱脂加工大豆を冷却し、追加原料Tとして割砕小麦を混合した。脱脂加工大豆は、連続的に散水率130%で散水し、100℃まで予熱処理した後、連続加圧蒸煮装置で0.2MPaの飽和水蒸気で3分間蒸煮処理した物を用いた。脱脂加工大豆の冷却処理量は2,000kg/hとし投入口より順次冷却装置内に投入した。投入直後の温度は約80℃であった。600rpmで回転させてあるピンクラッシャーにより略分散状態になった脱脂加工大豆は、移送ベルト上に約10cm堆積される。脱脂加工大豆は移送ベルトとともに移動しながら送風機の移送ベルト下方よりの送風によって冷却され、追加原料の投入口直下位置にくる。このときの品温は40℃まで降下している。送風機の風量は約110m3/分である。追加原料である割砕小麦の投入量は2,000kg/hであり、投入口より順次連続して投入される。割砕小麦の投入後ピンクラッシャーにより脱脂加工大豆と混合された原料は、移送ベルト上に約13cm堆積され、排出口より排出される。このときの品温は35℃になっていた。混合された原料は、その後製麹装置へと移されるのである。実施例では、割砕小麦と共に種麹を270g/hの割合で投入した。通風が移送ベルト下より送風したが、種麹が軽い粉状であるにもかかわらず、飛散することなく混合撹拌され、製麹装置に投入後40時間の培養工程の後、酵素力価等の品質が均一な麹となった。
【0015】
実施例で、製麹後の雑菌数を測定した。出麹後の麹を100gとり、そのなかから、1.5gを3サンプルとり、防黴培地で雑菌数を測定した。その結果、平均雑菌数が3.2×103個であった。従前の出麹後の麹における平均雑菌数は2.0×104個であったから、サニタリー性は大きく改善されたといえる。
【0016】
【発明の効果】
本発明により、加熱処理した原料と合わせて2種以上の原料を混合処理する場合における、加熱固体原料の冷却工程と混合工程のサニタリー化・シンプル化を図ることができる方法と、前記方法に基づく装置とを提供できるようになる。具体的には、本発明によれば雑菌が混入する機会が少なくなるので、必然的に原料中の雑菌数が下がるほか、コンタミがなくなる利点がある。また、本発明に基づく醸造用原料の連続冷却混合装置は、洗浄が容易であり、処理中にほこりが立たないほか、省スペースを図ることができる効果がある。
【図面の簡単な説明】
【図1】本発明を適用した加熱固体原料の連続冷却装置の概略縦断面図である。
【図2】追加原料を加熱固体原料と共に投入する連続冷却装置の概略縦断面図である。
【図3】醤油製造における原料から製麹までの従来の製造工程のフローチャート図である。
【図4】醤油製造における原料から製麹までの本発明の製造工程のフローチャート図である。
【符号の説明】
1 投入口
2 ピンクラッシャー
3 移送ベルト
4 横型ピンクラッシャー
5 排出口
6 ファン
7 風洞
8 加熱固体原料K以外の原料投入口
9 ナイフクラッシャー
10 送風機
11 ダンパー
12 除菌フィルター
13 除塵フィルター
K 加熱原料(加熱固体原料)
追加原料(加熱固体原料以外の固体原料)
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a continuous cooling mixing method and an endless belt type continuous cooling mixing apparatus for a brewing raw material in which a heated solid raw material and raw materials other than the heated solid raw material are mixed.
[0002]
[Prior art]
When processing raw materials such as cereals, depending on the type of product to be manufactured, solid processing other than the heated solid raw material may be mixed with the heat-treated raw material. For example, in brewing soy sauce, it is common to cook raw soybeans that have been cooked and then cooled with a cooling device, add wheat roasted and cracked, mix and stir, and then make koji with a koji making device. It is. As a mixing method, a method of conveying while mixing with a screw conveyor, a method of mixing with a mixer and conveying with a conveyor or the like are common.
[0003]
[Problems to be solved by the invention]
In recent years, with the internationalization of quality control in the food field, conventional hygiene management alone is not sufficient, and it must be a device and equipment compatible with HACCP (Hazard Analysis and Critical Control Point). . For that purpose, it is necessary to reduce the number of places and machines where the raw material may remain and to have a simple structure with as good a cleanability as possible. The screw conveyor has a hermetic structure, so there is no intrusion of foreign substances and there is an advantage that it can be used by changing the screw shape according to the application, but because it is transported by the propulsive force of the screw, the wear is large and the efficiency is not so good In addition, it is difficult to clean the material adhering to the screw due to its structure. Even when a mixer, a conveyor, or the like is used, there is no change in the adhesion of raw materials and the number of cleaning points. Also, in the brewing field, mechanization for mass production processing has progressed along with technological advances, and how efficiently the installation of machinery in existing building facilities has become a factor that greatly affects production capacity. ing.
[0004]
In the present invention, it is an object to provide a method capable of sanitizing and simplifying the cooling step and the mixing step of the heated solid raw material when two or more raw materials are mixed with the heat-treated raw material. is there.
[0005]
[Means for Solving the Problems]
In order to solve the above problem, in the present invention, a heated solid material and a solid material other than the heated solid material are mixed on a breathable endless solid material transfer belt. By performing the mixing treatment on the breathable endless belt-shaped solid material transfer belt, steps other than mixing can be performed on the belt, which can greatly contribute to the labor of washing and the cost reduction of the machine installation. The “raw material” as used herein refers to, for example, whole soybeans, defatted soybeans or pressure-biased soybeans, wheat such as cracked wheat and buckwheat, grains such as white rice, rice bran, rice bran or bean flour used for enzyme production, etc. In addition, it refers to other food raw materials and the like, and those that are heated and used are “heated solid raw materials ”, and those that are not heated or cooled after heating are “ solid raw materials other than the heated solid raw materials ”. It does not matter whether the raw material is the same or different.
[0006]
Specifically, (1) the heated solid material is blown and cooled on the breathable endless belt-shaped transfer belt, and then the solid material other than the heated solid material is mixed, or (2) the breathable endless belt The heated solid raw material and the solid raw material other than the heated solid raw material were simultaneously charged and mixed on the transfer belt, and were cooled by ventilation. By performing the cooling process and the mixing process on the same apparatus (transfer belt), not only can the cleaning and cost reduction be greatly contributed, but there is no transfer, so dust does not stand up and the number of germs decreases.
[0007]
Various positions can be considered for the input positions of solid raw materials other than the heated solid raw material in accordance with the types and characteristics of the solid raw materials . If the solid raw material to be charged is not affected by heat, it may be charged simultaneously with the heated solid raw material . By introducing from the beginning of the cooling device, stirring and heat uniformity, or when the heated solid raw material has a high moisture content, moisture can be quickly transferred. If the solid raw material other than the heated solid raw material is affected by heat, or if it is desired to cool only the heated solid raw material , the charging position may be on the transfer belt after cooling of the heated solid raw material . There is no need to actively cool and cool between here and the outlet, and only stirring or mixing means such as a knife crusher or pink lasher may be used. Also, it is possible to put it on a transfer belt in the middle of cooling. The cooling device may ventilate the deposited heated solid material from above to below, but may ventilate from below to above. In this case, the transfer belt is not clogged, and almost all of the blown air passes through the heated solid material , which is particularly effective.
[0008]
Solid materials other than heating the solid starting material need not be all on a cooling device is turned on. It is conceivable to limit the ratio of the solid raw material to be charged and to charge it in a later process, or to change the input amount with time. Here, the type of solid materials other than heating the solid material is a single type and not limited, but also the case where they are plural. In that case, according to the type and properties of the solid material as described above, by setting-up position and amount, respectively, but they can optimal mixing a plurality of input solid material.
[0009]
As a combination of the solid raw materials , as an example of the raw material processing in soy sauce brewing, a combination in which the heated solid raw material is steamed soybean and the solid raw material other than the heated solid raw material is wheat can be exemplified. Soy here refers to whole soybean, defatted soybean and pressure-biased soybean, and wheat means cracked wheat and buckwheat. In general, soybeans cooked in a pressure steaming device are cooled with a continuous cooling device, then wheat is added on a transfer belt conveyor, mixed and stirred with a pink lasher, etc. It is included in the iron making equipment. Thus, by carrying out the continuous cooling and mixing method of the present invention in which the heated solid raw material is steamed soybean and the solid raw material other than the steamed soybean is wheat , not only the individual transfer conveyor belt is eliminated, but also the transfer conveyor from the cooling device. Dust generation due to the reduced number of connected parts is prevented, and sanitary and cost reductions are further improved.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a schematic longitudinal sectional view of a continuous cooling and mixing apparatus for brewing raw materials to which the present invention is applied (a method of blowing air from below the transfer belt 3), and FIG. 2 is a continuous cooling and mixing of another example of brewing raw materials to which the present invention is applied. FIG. 3 is a flow chart of a conventional manufacturing process from raw materials in soy sauce production to koji making, and FIG. 4 is from raw materials in soy sauce production to koji making. It is a flowchart figure of the manufacturing process of this invention.
[0011]
First, as shown in FIG. 1, an example of a device configuration for blowing air from below the transfer belt 3 for cooling will be described. Heated raw material (heated solid raw material) K is introduced into the apparatus from the inlet 1 located on the left side in FIG. 1 and is transferred to a substantially dispersed state by a pink lasher 2 as a loosening machine and a leveling machine. After being deposited on the belt 3 and further stirred by a horizontal pink lasher 4 as a loosening machine, it is transferred to the discharge port 5 on the right side in FIG. In the apparatus of the present example, a fan 6 is provided above the pink lasher 2 and in the vicinity of the inlet 1 so as to efficiently exhaust the air that has passed through the heated raw material K that has been loosened into a substantially dispersed state. . As the transfer belt 3, a stainless steel mesh belt having air permeability and a stainless steel belt provided with a large number of ventilation holes are used. Further, a raw material charging port 8 other than the heating raw material K is disposed on the right side of the wind tunnel 7, and the added additional raw material ( solid raw material other than the heating solid raw material) T is deposited on the heating raw material K being transferred. The mixture is stirred and mixed by a knife crusher 9 as a mixer provided on the transfer belt 3 below the raw material inlet 8 and on the right in FIG. A wind tunnel 7 divided into three sections is disposed below the transfer belt 3, and the secondary side of the blower 10 is connected to each of the wind tunnels 7, and passes through the heating raw material K through the transfer belt 3. It is comprised so that it can blow. The blowing capacity of each blower 10 is provided with a blowing pressure and a blowing amount capable of passing through the heating raw material K deposited on the transfer belt 3.
[0012]
A damper 11 for adjusting the air flow rate is disposed on the secondary side of each blower 10, and a sterilization filter 12 and a dust removal filter 13 are disposed on the primary side serving as an outside air intake. The number of the wind tunnels 7 is preferably plural so that air can be blown in accordance with the physical properties associated with the cooling of the heating raw material K, but even a single one can sufficiently exhibit the effect.
[0013]
FIG. 1 assumes that an additional raw material ( solid raw material other than the heated solid raw material ) T is added after heating raw material (heated solid raw material) K or during cooling, but the additional raw material T as shown in FIG. It is also conceivable that the is added together with the heating raw material K. The heated raw material K and the additional raw material T are introduced into the apparatus from the inlet 1 located on the left side in FIG. 2 and mixed while being loosened to a substantially dispersed state by a pink lasher 2 as a mixer, and then transferred to the transfer belt 3. After being deposited on top and further stirred by a horizontal pink lasher 4 as a loosening machine, it is transferred to the discharge port 5 on the right side in FIG. As the transfer belt 3, a stainless steel mesh belt having air permeability and a stainless steel belt provided with a large number of ventilation holes are used. A wind tunnel 7 divided into three sections is disposed below the transfer belt 3, and the primary side of the blower 10 is connected to each of the wind tunnels 7 while passing through the heating raw material K through the transfer belt 3. It is comprised so that suction ventilation can be performed. The suction blowing capacity of each blower 10 is provided with a blowing pressure and a suction blowing amount that can pass through the heating raw material K deposited on the transfer belt 3.
[0014]
【Example】
Using the continuous cooling and mixing apparatus for the raw material for brewing shown in FIG. 1, defatted soybeans as a raw material for soy sauce were cooled as the heated raw material K, and cracked wheat was mixed as the additional raw material T. The defatted soybeans used were water sprinkled continuously at a watering rate of 130%, preheated to 100 ° C., and then steamed with 0.2 MPa saturated steam for 3 minutes in a continuous pressure steaming apparatus. The cooling rate of defatted soybeans was set at 2,000 kg / h, and was sequentially fed into the cooling device from the inlet. The temperature immediately after charging was about 80 ° C. The defatted soybeans, which are substantially dispersed by the pink lasher rotated at 600 rpm, are deposited on the transfer belt by about 10 cm. The defatted soybean is moved with the transfer belt, is cooled by the air blown from below the transfer belt of the blower, and comes to a position immediately below the inlet of the additional raw material. The product temperature at this time has dropped to 40 ° C. The air volume of the blower is about 110m 3 / min. The amount of additional wheat, which is an additional raw material, is 2,000 kg / h, and it is introduced sequentially from the inlet. The raw material mixed with the defatted soybeans by the pink lasher after the split wheat is charged is deposited about 13 cm on the transfer belt and discharged from the outlet. The product temperature at this time was 35 ° C. The mixed raw material is then transferred to the iron making apparatus. In the examples, seed meal was added at a rate of 270 g / h together with the cracked wheat. Ventilation was blown from under the transfer belt, but the seed koji was lightly powdered and mixed and stirred without scattering, after 40 hours of cultivation after being put into the koji making apparatus, enzyme titer etc. The quality became uniform.
[0015]
In the examples, the number of germs after koji making was measured. 100 g of sputum after brewing was taken, from which 3 samples of 1.5 g were taken, and the number of germs was measured with an antifungal medium. As a result, the average number of miscellaneous bacteria was 3.2 × 10 3 . Since the average number of bacteria in the cocoon after the previous brewing was 2.0 × 10 4 , it can be said that the sanitary property was greatly improved.
[0016]
【The invention's effect】
According to the present invention, in the case where two or more kinds of raw materials are mixed with the heat-treated raw materials, a method for sanitizing and simplifying the cooling step and the mixing step of the heated solid raw materials , and the above method are used. Device can be provided. Specifically, according to the present invention, since the chance of contamination is reduced, the number of germs in the raw material inevitably decreases, and there is an advantage that there is no contamination. In addition, the continuous cooling and mixing apparatus for brewing raw materials based on the present invention is easy to clean, has no dust during processing, and can save space.
[Brief description of the drawings]
FIG. 1 is a schematic longitudinal sectional view of a continuous cooling device for a heated solid material to which the present invention is applied.
FIG. 2 is a schematic longitudinal cross-sectional view of a continuous cooling device for adding an additional raw material together with a heated solid raw material .
FIG. 3 is a flowchart of a conventional production process from raw materials to koji making in soy sauce production.
FIG. 4 is a flowchart of the production process of the present invention from raw materials to koji making in soy sauce production.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Input port 2 Pink lasher 3 Transfer belt 4 Horizontal type pink lasher 5 Discharge port 6 Fan 7 Wind tunnel 8 Material input ports other than the heating solid material K 9 Knife crusher
10 Blower
11 Damper
12 Sanitization filter
13 Dust removal filter K Heating material (Heating solid material)
T additional raw materials ( solid raw materials other than heated solid raw materials)

Claims (4)

通気性のある無端帯状の固体原料移送ベルト上で、加熱固体原料と該加熱固体原料以外の固体原料を混合することを特徴とする醸造用原料の連続冷却混合方法。 A continuous cooling and mixing method for a brewing raw material, comprising mixing a heated solid raw material and a solid raw material other than the heated solid raw material on a breathable endless belt-shaped solid raw material transfer belt. 空気を通して加熱固体原料を冷却した後、該加熱固体原料と該加熱固体原料以外の固体原料を混合することを特徴とする醸造用原料の連続冷却混合方法。After cooling the heated solid material through the air, the continuous cooling method for mixing brewing material, which comprises mixing a solid material other than heating the solid raw material and heating the solid source. 加熱固体原料が蒸煮大豆であり、該加熱固体原料以外の固体原料が小麦であることを特徴とする請求項1又は2記載の醸造用原料の連続冷却混合方法。 3. The continuous cooling and mixing method of a brewing raw material according to claim 1 or 2, wherein the heated solid raw material is steamed soybean, and the solid raw material other than the heated solid raw material is wheat. 通気性のある無端帯状の固体原料移送ベルトと、固体原料移送ベルトに通気する通気装置と、固体原料移送ベルト上で加熱固体原料と該加熱固体原料以外の固体原料を混合する混合装置を設けたことを特徴とする醸造用原料の連続冷却混合装置。Provided a solid material transfer belt endless belt Breathable, a ventilation device for ventilating the solid material transfer belt, a mixing device for mixing the heated solid material and heating the solid source other solid material on a solid material conveyor belts A continuous cooling and mixing apparatus for brewing raw materials .
JP2001400011A 2001-12-28 2001-12-28 Continuous cooling mixing method and continuous cooling mixing apparatus for raw materials for brewing Expired - Fee Related JP3813507B2 (en)

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