JP7023627B2 - Rice gel manufacturing system and rice gel manufacturing method - Google Patents

Rice gel manufacturing system and rice gel manufacturing method Download PDF

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JP7023627B2
JP7023627B2 JP2017128660A JP2017128660A JP7023627B2 JP 7023627 B2 JP7023627 B2 JP 7023627B2 JP 2017128660 A JP2017128660 A JP 2017128660A JP 2017128660 A JP2017128660 A JP 2017128660A JP 7023627 B2 JP7023627 B2 JP 7023627B2
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JP2019010044A (en
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邦保 土屋
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Yanmar Co Ltd
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Priority to EP17869287.7A priority patent/EP3539392B1/en
Priority to EP21167163.1A priority patent/EP3939438A1/en
Priority to US16/348,430 priority patent/US11583127B2/en
Priority to PCT/JP2017/036662 priority patent/WO2018088092A1/en
Priority to CN201780053151.5A priority patent/CN109890218A/en
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Description

本発明は、ゲル状の米ゲルを製造する米ゲル製造システム及び米ゲル製造方法に関する。 The present invention relates to a rice gel production system for producing a gel-like rice gel and a rice gel production method.

近年、白米を製粉装置で挽いて製造される米粉は、米粉パン等の材料として広く利用されている(例えば、特許文献1を参照。)。しかしながら、このような米粉は、澱粉のβ化(老化)が早く、その食味を長く維持できないという問題があった。
そこで、米粉の代替食品として、食味を比較的長期で維持でき、取り扱い性が良好な米ゲルが注目されている。そして、このような米ゲルの製造方法としては、従来、白米や米粉に水を加えて加熱することで糊状の糊化物とし、その糊化物を機械的に撹拌することで米ゲルとする方法が知られている(例えば、特許文献2を参照。)。
In recent years, rice flour produced by grinding white rice with a flour milling apparatus has been widely used as a material for rice flour bread and the like (see, for example, Patent Document 1). However, such rice flour has a problem that the betaization (aging) of starch is rapid and the taste cannot be maintained for a long time.
Therefore, as a substitute food for rice flour, rice gel, which can maintain its taste for a relatively long period of time and has good handleability, is attracting attention. As a method for producing such a rice gel, conventionally, water is added to white rice or rice flour and heated to form a paste-like paste, and the paste is mechanically stirred to form a rice gel. Is known (see, for example, Patent Document 2).

特開2006-136255号公報Japanese Unexamined Patent Publication No. 2006-136255 国際公開2014/199961号公報International Publication 2014/199961

従来技術では、米から米ゲルを製造する技術は開示されているが、1日あたり10kg程度のテーブル試作レベルの少量生産の一例が示されているに過ぎない。例えば加工食品の材料として大量に使用されることを前提にすると、大量生産技術が不可欠である。
さらに、米ゲルは、アイスクリームやホワイトソース等の材料等としての使用用途を考慮すると白色であることが望まれるが、製造過程において熱が加わることで変色してしまい、品質が低下する虞がある。また、滑らかで嗜好性が高い米ゲルを製造するためには、米ゲルに残存する微細米粒の数に対応する粒感を減らすことが望まれる。
In the prior art, a technique for producing rice gel from rice is disclosed, but only an example of small-quantity production at a table prototype level of about 10 kg per day is shown. For example, assuming that it is used in large quantities as a material for processed foods, mass production technology is indispensable.
Furthermore, rice gel is desirable to be white in consideration of its intended use as a material for ice cream, white sauce, etc., but there is a risk that the quality will deteriorate due to discoloration due to heat applied during the manufacturing process. be. Further, in order to produce a smooth and highly palatable rice gel, it is desired to reduce the graininess corresponding to the number of fine rice grains remaining in the rice gel.

この実情に鑑み、本発明の主たる課題は、品質及び嗜好性の高い米ゲルを大量生産可能な米ゲル製造システム及び米ゲル製造方法を提供する点にある。 In view of this situation, a main object of the present invention is to provide a rice gel production system and a rice gel production method capable of mass-producing rice gel having high quality and taste.

本発明の第1特徴構成は、ゲル状の米ゲルを製造する米ゲル製造システムであって、
原料米を炊飯又は蒸煮して炊飯米を得る炊飯部と、
前記炊飯米を搬送する炊飯米搬送部と、
前記炊飯米搬送部から受け継いだ前記炊飯米を粉砕して前記米ゲルを得る粉砕部と、を備え、
前記粉砕部として、
前記炊飯米を粉砕して第1粉砕米を得る第1粉砕部と、
前記第1粉砕部から排出された第1粉砕米を前記第1粉砕部よりも細かく粉砕して前記米ゲルを得る第2粉砕部と、を備える点にある。
The first characteristic configuration of the present invention is a rice gel production system for producing a gel-like rice gel.
A rice cooker that cooks or steams raw rice to obtain cooked rice,
The cooked rice transport unit that transports the cooked rice,
A crushing section for crushing the cooked rice inherited from the cooked rice transport section to obtain the rice gel is provided.
As the crushing part,
The first crushing section for crushing the cooked rice to obtain the first crushed rice,
The point is that the first crushed rice discharged from the first crushed portion is crushed more finely than the first crushed portion to obtain the rice gel, and the second crushed portion is provided.

本構成によれば、原料米を炊飯又は蒸煮して炊飯米を得る炊飯部と、前記炊飯米を搬送する炊飯米搬送部と、前記炊飯米搬送部から受け継いだ前記炊飯米を粉砕して米ゲルを得る粉砕部を備えるようにしたので、炊飯米搬送部により炊飯米を炊飯部から粉砕部へ自動で搬送して、粉砕部で米ゲルを順次生産できるので、米ゲルの大量生産が可能になる。 According to this configuration, a rice-cooking section for obtaining rice-cooked rice by cooking or steaming raw rice, a rice-cooking rice transport section for transporting the rice-cooked rice, and the rice-cooked rice inherited from the rice-cooked rice transport section are crushed into rice. Since it is equipped with a crushing section to obtain gel, the rice-cooking rice transport section automatically transports the cooked rice from the rice-cooking section to the crushing section, and the crushing section can sequentially produce rice gel, enabling mass production of rice gel. become.

さらに、第1粉砕部と第2粉砕部とを直列に配置した2段式の粉砕部を備え、炊飯米を第1粉砕部で比較的粗く粉砕した後に当該粉砕後の第1粉砕米を第2粉砕部でより細かく粉砕して米ゲルを製造するので、夫々の粉砕部での粉砕負荷が軽減される。このことで、当該夫々の粉砕部での処理量を増加させる形態で、米ゲルの生産量を一層増加することができる。また、夫々の粉砕部での粉砕負荷が軽減されるので、第2粉砕部において粒感が少なくなるよう米ゲルを十分に粉砕しながら、夫々の粉砕部での粉砕時に粉砕対象物である炊飯米又は第1粉砕米に対して加えられる摩擦熱を軽減して、当該摩擦熱による米ゲルの変色を抑制し、品質及び嗜好性の高い米ゲルを製造することができる。 Further, it is provided with a two-stage crushing section in which a first crushing section and a second crushing section are arranged in series, and after the cooked rice is crushed relatively coarsely by the first crushing section, the first crushed rice after the crushing is first. 2 Since the rice gel is produced by crushing it more finely in the crushing section, the crushing load in each crushing section is reduced. As a result, the production amount of rice gel can be further increased in the form of increasing the processing amount in each of the crushed portions. In addition, since the crushing load in each crushing section is reduced, the rice gel is sufficiently crushed so that the graininess is reduced in the second crushing section, and the rice is cooked as an object to be crushed during crushing in each crushing section. It is possible to reduce the frictional heat applied to the rice or the first pulverized rice, suppress the discoloration of the rice gel due to the frictional heat, and produce a rice gel having high quality and palatability.

本発明の第2特徴構成は、前記第1粉砕部から排出された第1粉砕米を前記第2粉砕部に搬送する第1粉砕米搬送部を備える点にある。 The second characteristic configuration of the present invention is to include a first crushed rice transport section for transporting the first crushed rice discharged from the first crushed section to the second crushed section.

本構成によれば、第1粉砕米搬送部を備えることで、第1粉砕部から排出された第1粉砕米を自動で第2粉砕部に搬送して、夫々の粉砕部で米ゲルを順次生産できるので、米ゲルの一層の大量生産が可能になる。 According to this configuration, by providing the first crushed rice transport section, the first crushed rice discharged from the first crushed section is automatically transported to the second crushed section, and the rice gel is sequentially transferred in each crushed section. Since it can be produced, further mass production of rice gel becomes possible.

本発明の第3特徴構成は、前記第2粉砕部が、相対回転する上臼部と下臼部との隙間に粉砕対象物を通過させる形態で、前記第1粉砕米を粉砕する石臼式の磨砕装置で構成されている点にある。 The third characteristic configuration of the present invention is a stone mill type that crushes the first crushed rice in a form in which the second crushed portion allows the crushed object to pass through the gap between the upper and lower mortar portions that rotate relative to each other. The point is that it is composed of a grinding device.

本構成によれば、第1粉砕米をより細かく粉砕して米ゲルを得る第2粉砕部を、上記のような石臼式の磨砕装置で好適に構成することができる。即ち、この第2粉砕部として構成される石臼式の磨砕装置では、相対回転する上臼部と下臼部との隙間に第1粉砕米を通過させる形態で、当該通過の際に発生するせん断力により第1粉砕米を微細に磨砕して、より滑らかな高品質の米ゲルを得ることができる。また、この第2粉砕部では、予め第1粉砕部で比較的粗く粉砕された第1粉砕米が粉砕対象物として供給されるので、粒感が少なくなるよう第1粉砕米を微細に磨砕した場合であっても、粉砕負荷が低く抑えられて第1粉砕米の摩擦熱による変色を抑制することができる。 According to this configuration, the second crushed portion for obtaining rice gel by crushing the first crushed rice more finely can be suitably configured by the above-mentioned stone mill type grinding device. That is, in the stone mill type grinding device configured as the second crushing portion, the first crushed rice is passed through the gap between the upper mill portion and the lower mill portion that rotate relative to each other, and is generated at the time of the passage. The first crushed rice can be finely crushed by the shearing force to obtain a smoother and higher quality rice gel. Further, in this second crushed portion, the first crushed rice that has been relatively coarsely crushed in the first crushed portion is supplied as a crushing object, so that the first crushed rice is finely crushed so as to reduce the graininess. Even in this case, the crushing load is suppressed to a low level, and discoloration due to the frictional heat of the first crushed rice can be suppressed.

本発明の第4特徴構成は、上記第3特徴構成に加えて、前記第1粉砕部が、相対回転する上臼部と下臼部との隙間に粉砕対象物を通過させる形態で、前記炊飯米を粉砕する石臼式の磨砕装置で構成されており、
前記第2粉砕部での上臼部と下臼部との隙間の幅であるギャップ幅が、前記第1粉砕部でのギャップ幅よりも小さく設定されている点にある。
In the fourth characteristic configuration of the present invention, in addition to the third characteristic configuration, the first crushing portion allows the crushed object to pass through the gap between the upper mill portion and the lower mill portion that rotate relative to each other, and the rice is cooked. It consists of a stone mill type grinder that grinds rice.
The gap width, which is the width of the gap between the upper mill portion and the lower mill portion in the second crushing portion, is set to be smaller than the gap width in the first crushing portion.

本構成によれば、第1粉砕部及び第2粉砕部の両方を石臼式の磨砕装置として構成した場合において、第2粉砕部でのギャップ幅が第1粉砕部でのギャップ幅よりも小さく設定されているので、第1粉砕部では、比較的粒径が大きい炊飯米を比較的広い上下臼部の隙間に通過させて、できるだけ大量の炊飯米を比較的粗く粉砕することができる。一方、第2粉砕部では、比較的粒径が小さい第1粉砕米を比較的狭い上下臼部の隙間に通過させて、当該第1粉砕米をできるだけ微細に磨砕して、より滑らかな高品質の米ゲルを得ることができる。 According to this configuration, when both the first crushing section and the second crushing section are configured as a stone mill type grinding device, the gap width in the second crushing section is smaller than the gap width in the first crushing section. Since it is set, in the first crushing portion, rice cooked rice having a relatively large particle size can be passed through a relatively wide gap between the upper and lower millstones, and as much rice cooked rice as possible can be crushed relatively coarsely. On the other hand, in the second crushed portion, the first crushed rice having a relatively small particle size is passed through a relatively narrow gap between the upper and lower mills, and the first crushed rice is ground as finely as possible to make the height smoother. You can get quality rice gel.

本発明の第5特徴構成は、ゲル状の米ゲルを製造する米ゲル製造方法であって、
原料米を炊飯又は蒸煮して得た炊飯米を粉砕してゲル状の米ゲルを得る粉砕工程を備え、
前記粉砕工程として、
前記炊飯米を粉砕して第1粉砕米を得る第1粉砕工程と、
前記第1粉砕工程で得た第1粉砕米を前記第1粉砕工程よりも細かく粉砕して前記米ゲルを得る第2粉砕工程と、を備える点にある。
The fifth characteristic configuration of the present invention is a method for producing a rice gel for producing a gel-like rice gel.
It is equipped with a crushing process to obtain a gel-like rice gel by crushing cooked rice obtained by cooking or steaming raw rice.
As the crushing step,
In the first crushing step of crushing the cooked rice to obtain the first crushed rice,
The point is that the first crushed rice obtained in the first crushing step is pulverized more finely than the first crushing step to obtain the rice gel, and the second crushing step is provided.

本構成によれば、炊飯米を第1粉砕工程で比較的粗く粉砕した後に当該粉砕後の第1粉砕米を第2粉砕部でより細かく粉砕して米ゲルを製造するので、夫々の粉砕工程での粉砕負荷が軽減される。このことで、当該夫々の粉砕工程での処理量を増加させる形態で、米ゲルの生産量を一層増加することができる。また、夫々の粉砕工程での粉砕負荷が軽減されるので、第2粉砕工程において粒感が少なくなるよう米ゲルを十分に粉砕しながら、夫々の粉砕工程での粉砕時に粉砕対象物である炊飯米又は第1粉砕米に対して加えられる摩擦熱を軽減して、当該摩擦熱による米ゲルの変色を抑制し、品質及び嗜好性の高い米ゲルを製造することができる。 According to this configuration, after the cooked rice is crushed relatively coarsely in the first crushing step, the crushed first crushed rice is crushed more finely in the second crushing section to produce a rice gel. The crushing load in the rice is reduced. As a result, the production amount of rice gel can be further increased in the form of increasing the processing amount in each of the crushing steps. In addition, since the crushing load in each crushing step is reduced, the rice gel is sufficiently crushed so that the graininess is reduced in the second crushing step, and the rice is cooked as a crushed object at the time of crushing in each crushing step. It is possible to reduce the frictional heat applied to the rice or the first ground rice, suppress the discoloration of the rice gel due to the frictional heat, and produce a rice gel having high quality and palatability.

ところで、原料米の澱粉成分が糊化(アルファ(α)化とも称される)した炊飯米において、炊飯米の温度が低下すると老化(ベータ(β)化とも称される)が進み、炊飯米の硬さが増し、粉砕機で炊飯米を粉砕する際の粉砕負荷が大きくなって、粉砕機の故障や寿命低下を招く。そこで、本発明の米ゲル製造システムにおいて、前記炊飯米は、老化する温度よりも高い温度で粉砕機に供給されるようにしてもよい。これにより、炊飯米の老化に起因する粉砕機の粉砕負荷増大を防止でき、ひいては粉砕機の故障や寿命低下を防止できる。これにより、粉砕部の維持管理コストを低減できると共に、粉砕機の修理頻度や交換頻度を低減して安定した米ゲル生産を実現できる。 By the way, in cooked rice in which the starch component of the raw rice is gelatinized (also referred to as alpha (α) conversion), when the temperature of the cooked rice decreases, aging (also referred to as beta (β) formation) progresses, and the cooked rice The hardness of the rice increases, and the crushing load when crushing the cooked rice with the crusher increases, leading to the failure of the crusher and the shortening of the life of the rice. Therefore, in the rice gel production system of the present invention, the cooked rice may be supplied to the crusher at a temperature higher than the aging temperature. As a result, it is possible to prevent an increase in the crushing load of the crusher due to the aging of the cooked rice, and eventually it is possible to prevent the crusher from malfunctioning or shortening its life. As a result, the maintenance cost of the crushed portion can be reduced, and the frequency of repair and replacement of the crusher can be reduced to realize stable rice gel production.

また、本発明の米ゲル製造システムにおいて、前記粉砕部は複数の前記粉砕機を備え、前記炊飯米搬送部は、前記炊飯部から受け継いだ前記炊飯米を複数の前記粉砕機に振り分けて供給するようにしてもよい。
このようにすれば、炊飯部からの炊飯米を複数の粉砕機で並行して粉砕して米ゲルを生産できるので、より高い炊飯米生産能力を有する炊飯部の導入が可能になり、米ゲル生産能力をより向上できる。
Further, in the rice gel production system of the present invention, the crushing unit includes a plurality of the crushers, and the rice-cooking rice transporting unit distributes and supplies the cooked rice inherited from the rice-cooking unit to the plurality of crushers. You may do so.
By doing so, the rice cooked from the rice cooker can be crushed in parallel by multiple crushers to produce rice gel, so that it becomes possible to introduce a rice cooker with a higher rice cooker production capacity, and the rice gel. The production capacity can be further improved.

さらに、前記炊飯米搬送部は、前記炊飯部に連結される主コンベヤと、前記主コンベヤに連結されると共に直列連結される複数の投入用コンベヤを備え、前記主コンベヤの搬送下流端の下方に1段目の前記投入用コンベヤの中途部が配置され、前記投入用コンベヤの両端の下方に、前記粉砕機又は後段側の前記投入用コンベヤの中途部が配置され、前記投入用コンベヤの搬送方向を切り替えることで、前記炊飯米を前記粉砕機に供給し、又は後段側の前記投入用コンベヤに供給して、前記炊飯米を複数の前記粉砕機に振り分けて供給するようにしてもよい。
このようにすれば、簡単な構成で炊飯米を複数の粉砕機へ振り分けて供給できる。
Further, the rice-cooking rice transport section includes a main conveyor connected to the rice-cooking section and a plurality of feeding conveyors connected to the main conveyor and connected in series, and below the transport downstream end of the main conveyor. The middle part of the loading conveyor of the first stage is arranged, and the middle part of the charging conveyor on the crusher or the rear stage side is arranged below both ends of the charging conveyor, and the transport direction of the charging conveyor. By switching between, the rice cooked rice may be supplied to the crusher, or may be supplied to the loading conveyor on the subsequent stage side, and the rice cooked rice may be distributed and supplied to the plurality of crushers.
In this way, cooked rice can be distributed and supplied to a plurality of crushers with a simple configuration.

また、本発明の米ゲル製造システムにおいて、前記炊飯部は、前記原料米及び炊飯水を収容する複数の炊飯釜を搬送しながら加熱して前記炊飯米を得る連続式炊飯機により構成され、前記炊飯米搬送部は、前記炊飯釜を反転させて前記炊飯米を前記炊飯釜から取り出して前記粉砕部に供給するようにしてもよい。
このようにすれば、炊飯米を大量生産できると共に、その炊飯米を炊飯米搬送部により炊飯釜から取り出して粉砕部へ自動で供給して、米ゲルの大量生産が可能になる。
Further, in the rice gel production system of the present invention, the rice cooking unit is configured by a continuous rice cooker for obtaining the cooked rice by heating while transporting a plurality of rice cookers accommodating the raw rice and the cooked water. The rice cooker transport unit may invert the rice cooker to take out the rice cooker from the rice cooker and supply it to the crushed unit.
By doing so, the rice cooked rice can be mass-produced, and the cooked rice is taken out from the rice cooker by the rice cooked rice transport section and automatically supplied to the crushing section, so that the rice gel can be mass-produced.

また、本発明の米ゲル製造システムにおいて、前記炊飯部は、前記原料米をコンベヤで搬送しながら蒸煮する連続炊飯装置により構成されるようにしてもよい。
このようにすれば、例えばコンベヤで搬送される複数の炊飯釜で炊飯する炊飯装置に比べて、炊飯米の生産能力を向上でき、ひいては米ゲル生産能力をより向上できる。
Further, in the rice gel production system of the present invention, the rice cooking unit may be configured by a continuous rice cooking device that steams the raw rice while transporting it by a conveyor.
By doing so, the production capacity of cooked rice can be improved, and the rice gel production capacity can be further improved, as compared with a rice cooker that cooks rice in a plurality of rice cookers transported by a conveyor, for example.

また、本発明の米ゲル製造システムにおいて、前記粉砕部で得られる前記米ゲルを移送する米ゲル移送部と、前記米ゲル移送部から受け継いだ前記米ゲルを小分け収容するゲル収容部を備えるようにしてもよい。
このようにすれば、ゲル収容部で米ゲルを小分け収容して出荷しやすい状態にできる。
Further, in the rice gel production system of the present invention, a rice gel transfer unit for transferring the rice gel obtained in the crushing unit and a gel storage unit for subdividedly accommodating the rice gel inherited from the rice gel transfer unit are provided. You may do it.
In this way, the rice gel can be subdivided and stored in the gel storage section so that it can be easily shipped.

さらに、前記米ゲル移送部は、一軸偏心ねじポンプにより前記米ゲルを移送するようにしてもよい。
このようにすれば、一軸偏心ねじポンプは高粘性流体を移送可能なので、粉砕部で得られる米ゲルの粘度が高い場合であっても米ゲルを包装部へ移送できる。
Further, the rice gel transfer unit may transfer the rice gel by a uniaxial eccentric screw pump.
By doing so, since the uniaxial eccentric screw pump can transfer the highly viscous fluid, the rice gel can be transferred to the packaging portion even when the viscosity of the rice gel obtained in the pulverized portion is high.

米ゲル製造システムの一実施形態の概略平面図である。It is a schematic plan view of one Embodiment of a rice gel production system. 同実施形態の概略構成図である。It is a schematic block diagram of the same embodiment. 粉砕部として設けられた粉砕設備の概略構成を示す立断面図である。It is a vertical sectional view which shows the schematic structure of the crushing equipment provided as a crushing part. 米ゲル製造システムの他の実施形態の概略構成図である。It is a schematic block diagram of another embodiment of a rice gel production system. 米ゲル製造システムのさらに他の実施形態の概略平面図である。FIG. 3 is a schematic plan view of still another embodiment of the rice gel production system. 同実施形態の概略構成図である。It is a schematic block diagram of the same embodiment. 同実施形態の炊飯米搬送部周辺の概略構成図である。It is a schematic block diagram around the rice cooked rice transport part of the same embodiment. 同炊飯米搬送部の制御系を示す概略構成図である。It is a schematic block diagram which shows the control system of the cooked rice transport part. 同炊飯米搬送部の動作の一例を説明するための図である。It is a figure for demonstrating an example of the operation of the cooked rice transport part. 同炊飯米搬送部の動作の他の例を説明するための図である。It is a figure for demonstrating another example of the operation of the cooked rice transport part. 米ゲル製造システムのさらに他の実施形態における炊飯米搬送部周辺を示す概略平面図である。It is a schematic plan view which shows the periphery of the cooked rice transport part in still another embodiment of a rice gel production system. 同実施形態における炊飯米搬送部周辺の概略構成図である。It is a schematic block diagram around the cooked rice transport part in the same embodiment. 米ゲル製造システムのさらに他の実施形態における炊飯米搬送部周辺を示す概略平面図である。It is a schematic plan view which shows the periphery of the cooked rice transport part in still another embodiment of a rice gel production system. 米ゲル製造システムのさらに他の実施形態の概略平面図である。FIG. 3 is a schematic plan view of still another embodiment of the rice gel production system. 同実施形態における炊飯米搬送部周辺を拡大して示す概略平面図である。It is a schematic plan view which shows the area around the cooked rice transport part in the same embodiment in an enlarged manner.

以下に、図面を参照しながら本願発明を具体化した実施形態を説明する。なお、本願特許請求の範囲及び本願明細書等において、炊飯米とは、原料米が加水及び加熱されて原料米の澱粉成分が糊化した状態の糊化物を意味し、例えば、炊飯米にはいわゆる蒸米も含まれる。 Hereinafter, embodiments embodying the present invention will be described with reference to the drawings. In the scope of the claims of the present application and the specification of the present application, the cooked rice means a gelatinized product in which the starch component of the raw rice is gelatinized by adding water and heating the raw rice. So-called steamed rice is also included.

図1は、米ゲル製造システムの一実施形態の概略平面図である。図2は、同実施形態の概略構成図である。米ゲル製造システム1は、大まかな構成として、原料米を貯留する貯米部2、原料米を水洗いする洗米部3、洗米を浸漬する浸漬部4、浸漬米を炊飯する炊飯部5、炊飯米を搬送する炊飯米搬送部6、炊飯米を粉砕して米ゲルを得る粉砕部7、米ゲルを移送する米ゲル移送部8、米ゲルを小分け収容するゲル収容部9、米ゲル収容物を検査する検査部10、米ゲル袋を出荷する出荷部11を備える。 FIG. 1 is a schematic plan view of an embodiment of a rice gel production system. FIG. 2 is a schematic configuration diagram of the same embodiment. The rice gel production system 1 has a rough structure of a rice storage unit 2 for storing raw rice, a rice washing unit 3 for washing raw rice, a dipping unit 4 for immersing the washed rice, a rice cooking unit 5 for cooking the soaked rice, and rice cooking rice. Rice-cooking rice transport section 6 for transporting rice, crushing section 7 for crushing rice-cooked rice to obtain rice gel, rice gel transfer section 8 for transferring rice gel, gel storage section 9 for subdividing rice gel, and rice gel container. It includes an inspection unit 10 for inspection and a shipping unit 11 for shipping rice gel bags.

例えば玄米や精白米などの原料米は、貯米部2で納米ホッパー12に投入され、納米昇降機13により上昇されて、納米庫14の上部から納米庫14に収容される。納米庫14は、納米庫14の下部から排出する原料米を計量する計量装置を備え、所定量の原料米を排出する。納米庫14から排出された原料米は、昇降機等を有する原料米搬送機15にて洗米部3の洗米機16に送られる。洗米機16で原料米を水洗いして得られる洗米は、洗米移送管17を介して浸漬部4の浸漬タンク18に送られ、浸漬タンク18内で例えば1.5時間程度、浸漬される。 For example, raw rice such as brown rice and polished rice is put into the rice hopper 12 by the rice storage unit 2, raised by the rice elevator 13, and stored in the rice storage 14 from the upper part of the rice storage 14. The rice storage 14 is provided with a weighing device for measuring the raw rice discharged from the lower part of the rice storage 14, and discharges a predetermined amount of raw rice. The raw rice discharged from the rice storage 14 is sent to the rice washing machine 16 of the rice washing unit 3 by the raw rice transporting machine 15 having an elevator or the like. The rice washing obtained by washing the raw rice with water in the rice washing machine 16 is sent to the dipping tank 18 of the dipping section 4 via the rice washing transfer pipe 17 and is immersed in the dipping tank 18 for, for example, about 1.5 hours.

浸漬タンク18内の浸漬米は、計量及び水切りされて所定量ずつ炊飯釜Aに供給される。米ゲル製造システム1は、複数の炊飯釜Aと、炊飯釜Aを炊飯部5へ搬送するコンベヤ19を備える。コンベヤ19の搬送上流側に配置された空の炊飯釜Aに、浸漬タンク18から所定量の浸漬米が供給される。また、炊飯釜Aには、加水機20から所定量の炊飯水が供給される。浸漬米(原料米)及び炊飯水を収容する炊飯釜Aは、コンベヤ19により炊飯部5側へ搬送され、搬送途中で蓋配置部(図示省略)により蓋がされた後、炊飯部5の連続式炊飯機21へ送られる。 The soaked rice in the soaking tank 18 is weighed and drained, and is supplied to the rice cooker A in predetermined amounts. The rice gel manufacturing system 1 includes a plurality of rice cookers A and a conveyor 19 that conveys the rice cookers A to the rice cooker 5. A predetermined amount of soaked rice is supplied from the soaking tank 18 to the empty rice cooker A arranged on the transport upstream side of the conveyor 19. Further, a predetermined amount of rice cooking water is supplied to the rice cooking pot A from the water addition machine 20. The rice cooker A for accommodating soaked rice (raw rice) and rice cooking water is conveyed to the rice cooking section 5 side by the conveyor 19, and is covered by the lid arrangement section (not shown) during the transfer, and then the rice cooking section 5 is continuous. It is sent to the rice cooker 21.

連続式炊飯機21は、内部に設けたコンベヤ及び熱源(図示省略)により炊飯釜Aを搬送しながら加熱し、炊飯釜A内の浸漬米を炊飯する。連続式炊飯機21には、浸漬米及び炊飯水を収容する炊飯釜Aがコンベヤ19から順次供給される。連続式炊飯機21は、コンベヤ19から受け継いだ複数の炊飯釜A内の浸漬米を連続的に炊飯する。なお、連続式炊飯機21の熱源は、いかなるものであってもよく、例えばガス式であってもよいし、IH(Induction Heating)式であってもよい。 The continuous rice cooker 21 heats the rice cooker A while conveying it by a conveyor and a heat source (not shown) provided inside, and cooks the soaked rice in the rice cooker A. A rice cooker A for accommodating soaked rice and rice cooking water is sequentially supplied from the conveyor 19 to the continuous rice cooker 21. The continuous rice cooker 21 continuously cooks the soaked rice in the plurality of rice cookers A inherited from the conveyor 19. The heat source of the continuous rice cooker 21 may be any type, for example, a gas type or an IH (Induction Heating) type.

連続式炊飯機21で炊飯された炊飯米を収容する炊飯釜Aは、炊飯米搬送部6の搬送コンベヤ22に受け継がれる。炊飯米搬送部6は、搬送コンベヤ22と自動反転機23とほぐし機24を備え、連続式炊飯機21から受け継いだ炊飯釜A内の炊飯米を搬送コンベヤ22上で蒸らしながら、炊飯釜Aを自動反転機23へ搬送する。搬送コンベヤ22の搬送下流端側で炊飯釜A上の蓋が蓋取外し機(図示省略)により取り外された後、炊飯釜Aが自動反転機23により持ち上げられて反転され、炊飯釜A内の炊飯米が取り出されてほぐし機24に供給される。 The rice cooker A for accommodating the cooked rice cooked by the continuous rice cooker 21 is inherited by the conveyor 22 of the cooked rice transport unit 6. The rice cooker transfer unit 6 is provided with a transfer conveyor 22, an automatic reversing machine 23, and a loosening machine 24, and while steaming the rice cooked rice in the rice cooker A inherited from the continuous rice cooker 21 on the transfer conveyor 22, the rice cooker A is moved. It is conveyed to the automatic reversing machine 23. After the lid on the rice cooker A is removed by the lid remover (not shown) at the downstream end side of the transfer of the transfer conveyor 22, the rice cooker A is lifted and inverted by the automatic reversing machine 23 to cook rice in the rice cooker A. The rice is taken out and supplied to the loosening machine 24.

ほぐし機24は、炊飯米を攪拌してほぐす。ほぐされた炊飯米は、粉砕部7を構成する粉砕設備25へ供給される。粉砕設備25へ供給されるときの炊飯米の温度は、老化する温度よりも高い温度であり、この実施形態では85度程度である。なお、搬送コンベヤ22上で蒸らし搬送されるときの炊飯米の温度は90度程度である。粉砕設備25は、例えば石臼形式の摩砕装置(融砕機とも呼ばれる)で構成され、炊飯米を粉砕して米ゲルを得る。なお、粉砕設備25は、炊飯米を粉砕して米ゲルを得ることができる構成であれば、粉砕方式は特に限定されない。 The loosening machine 24 stirs and loosens the cooked rice. The loosened cooked rice is supplied to the crushing equipment 25 constituting the crushing unit 7. The temperature of the cooked rice when it is supplied to the crushing equipment 25 is higher than the temperature at which it ages, and is about 85 degrees in this embodiment. The temperature of the cooked rice when it is steamed and transported on the conveyor 22 is about 90 degrees. The crushing equipment 25 is composed of, for example, a stone mill type grinding device (also called a crusher), and crushes cooked rice to obtain rice gel. The crushing equipment 25 is not particularly limited in the crushing method as long as the rice gel can be obtained by crushing the cooked rice.

粉砕設備25で得られる米ゲルは、米ゲル移送部8の移送ポンプ26に供給される。移送ポンプ26は、例えばモーノポンプと呼ばれる一軸偏心ねじポンプで構成され、米ゲル移送配管27を介して米ゲルをゲル収容部9の包装機28へ移送する。米ゲル移送配管27は例えばステンレス鋼製である。 The rice gel obtained in the crushing equipment 25 is supplied to the transfer pump 26 of the rice gel transfer unit 8. The transfer pump 26 is composed of, for example, a uniaxial eccentric screw pump called a mono pump, and transfers rice gel to the packaging machine 28 of the gel accommodating portion 9 via the rice gel transfer pipe 27. The rice gel transfer pipe 27 is made of, for example, stainless steel.

ゲル収容部9は米ゲルを小分け収容する。ゲル収容部9の包装機28は、樹脂フィルムを製袋すると共に、袋状樹脂フィルムに米ゲルを充填して所定量(例えば5キログラム)ずつに封止し、一袋ずつに切断して米ゲル収容物Pを順次得る。 The gel storage unit 9 stores rice gel in small portions. The packaging machine 28 of the gel accommodating portion 9 makes a bag of the resin film, fills the bag-shaped resin film with rice gel, seals it in a predetermined amount (for example, 5 kilograms), cuts it into bags, and cuts the rice into bags. The gel inclusions P are sequentially obtained.

ゲル収容部9で得られる米ゲル収容物Pは、コンベヤ30により検査部10へ搬送される。検査部10では、米ゲル収容物P内の異物の有無が異物検出機31で検査され、米ゲル収容物Pの重さが所定重さ範囲内であることが重さ検査機32で検査される。検査完了後の米ゲル収容物Pは、出荷部11の移動台33へ順次載せられる。出荷部11では、複数の米ゲル収容物Pが移動台33ごと搬送され、殺菌機34で加熱殺菌及び冷却されて、除水機35で順次除水された後、箱詰めされて出荷可能な状態にされる。 The rice gel container P obtained in the gel container 9 is conveyed to the inspection unit 10 by the conveyor 30. In the inspection unit 10, the presence or absence of foreign matter in the rice gel container P is inspected by the foreign substance detector 31, and the weight of the rice gel container P is inspected by the weight inspection machine 32 within a predetermined weight range. To. After the inspection is completed, the rice gel container P is sequentially placed on the moving table 33 of the shipping unit 11. In the shipping unit 11, a plurality of rice gel containers P are transported together with the moving table 33, sterilized by heating and cooled by the sterilizer 34, water is sequentially removed by the water remover 35, and then packed in a box and shipped. Be made.

なお、炊飯米搬送部6において、自動反転機23により炊飯米が取り出されて搬送コンベヤ22に戻された空の炊飯釜Aは、例えば手作業で釜洗浄機36へ搬送されて洗浄された後、コンベヤ19の搬送上流端側の浸漬米供給位置に配置される。ここで、図1において破線矢印で示すように、搬送コンベヤ22に戻された空の炊飯釜Aが、別のコンベヤ等により搬送コンベヤ22から自動で釜洗浄機36へ移動され、釜洗浄機36にて自動で洗浄されて、さらに別のコンベヤ等により、コンベヤ19の浸漬米供給位置に自動で配置されるようにしてもよい。これにより、コンベヤ19、連続式炊飯機21、搬送コンベヤ22、自動反転機23及び釜洗浄機36の移動経路を炊飯釜Aが自動で循環移動するので、作業者の負担が軽減される。 In the rice-cooking rice transport unit 6, the empty rice-cooking kettle A from which the cooked rice is taken out by the automatic reversing machine 23 and returned to the transport conveyor 22 is, for example, manually transported to the kettle washing machine 36 for cleaning. , Is arranged at the soaked rice supply position on the upstream end side of the conveyor 19. Here, as shown by the broken line arrow in FIG. 1, the empty rice cooker A returned to the transfer conveyor 22 is automatically moved from the transfer conveyor 22 to the kettle cleaning machine 36 by another conveyor or the like, and the kettle cleaning machine 36 is used. It may be automatically washed by the conveyor 19 and automatically arranged at the soaked rice supply position of the conveyor 19 by another conveyor or the like. As a result, the rice cooker A automatically circulates and moves along the moving paths of the conveyor 19, the continuous rice cooker 21, the conveyor 22, the automatic reversing machine 23, and the pot washing machine 36, so that the burden on the operator is reduced.

この実施形態の米ゲル製造システム1は、原料米を炊飯又は蒸煮して炊飯米を得る炊飯部5と、炊飯米を搬送する炊飯米搬送部6と、炊飯米搬送部6から受け継いだ炊飯米を粉砕設備25で粉砕して米ゲルを得る粉砕部7を備えるので、炊飯米搬送部6により炊飯米を炊飯部5から粉砕部7へ自動で搬送して、粉砕部7で米ゲルを順次生産でき、米ゲルの大量生産が可能になる。 The rice gel production system 1 of this embodiment has a rice cooking unit 5 that cooks or steams raw rice to obtain rice cooked rice, a rice cooked rice transport unit 6 that transports rice cooked rice, and rice cooked rice inherited from the rice cooked rice transport unit 6. Is provided with a crushing section 7 for obtaining rice gel by crushing the rice in the crushing facility 25. Therefore, the rice cooking section 6 automatically transports the cooked rice from the rice cooking section 5 to the crushing section 7, and the crushing section 7 sequentially transfers the rice gel. It can be produced, and mass production of rice gel becomes possible.

また、米ゲル製造システム1は、老化する温度よりも高い温度(例えば85度程度)の炊飯米を粉砕設備25に供給するので、炊飯米の老化に起因する粉砕設備25の粉砕による負荷増大を防止でき、ひいては粉砕設備25の故障や寿命低下を防止できる。これにより、粉砕部7の維持管理コストを低減できると共に、粉砕設備25の修理頻度や交換頻度を低減して安定した米ゲル生産を実現できる。なお、加水及び加熱によって米の澱粉成分が糊化する温度は概ね60度程度であり、80~90度程度で急速に糊化する。また、澱粉成分が糊化した炊飯米は、温度が概ね20度未満になると老化が促進される。そこで、粉砕設備25に供給される炊飯米の温度は、炊飯米が老化する温度よりも高い温度であることが好ましく、例えば20度以上、より好ましくは30度以上、さらに好ましくは60度以上である。 Further, since the rice gel production system 1 supplies the rice cooked rice having a temperature higher than the aging temperature (for example, about 85 degrees) to the crushing equipment 25, the load increase due to the crushing of the crushing equipment 25 due to the aging of the cooked rice is increased. This can be prevented, and by extension, the failure of the crushing equipment 25 and the shortening of its life can be prevented. As a result, the maintenance cost of the crushing unit 7 can be reduced, and the repair frequency and the replacement frequency of the crushing equipment 25 can be reduced to realize stable rice gel production. The temperature at which the starch component of rice is gelatinized by watering and heating is about 60 degrees, and the starch is rapidly gelatinized at about 80 to 90 degrees. Further, the cooked rice in which the starch component is gelatinized is accelerated to age when the temperature is less than about 20 ° C. Therefore, the temperature of the cooked rice supplied to the crushing equipment 25 is preferably a temperature higher than the temperature at which the cooked rice ages, for example, 20 degrees or higher, more preferably 30 degrees or higher, still more preferably 60 degrees or higher. be.

また、米ゲル製造システム1において、炊飯部5は、原料米(浸漬米)及び炊飯水を収容する複数の炊飯釜Aを搬送しながら加熱して炊飯米を得る連続式炊飯機21により構成され、炊飯米搬送部6は、炊飯釜Aを反転させて炊飯米を炊飯釜Aから取り出して粉砕部7に供給する。これにより、炊飯米を大量生産できると共に、その炊飯米を炊飯米搬送部6により炊飯釜Aから取り出して粉砕部7へ自動で供給して、米ゲルの大量生産が可能になる。 Further, in the rice gel production system 1, the rice cooking unit 5 is composed of a continuous rice cooker 21 for obtaining rice cooked rice by heating while transporting a plurality of rice cookers A accommodating raw rice (immersed rice) and rice cooking water. The rice cooker transport unit 6 inverts the rice cooker A, takes out the rice cooked rice from the rice cooker A, and supplies the rice cooked rice to the crushing unit 7. As a result, the rice cooked rice can be mass-produced, and the cooked rice is taken out from the rice cooker A by the rice cooked rice transport unit 6 and automatically supplied to the crushing unit 7, enabling mass production of rice gel.

また、米ゲル製造システム1は、粉砕部7で得られる米ゲルを移送する米ゲル移送部8と、米ゲル移送部8から受け継いだ米ゲルを小分け収容するゲル収容部9を備えるので、ゲル収容部9で米ゲルを例えば米ゲル収容物Pに小分け収容して出荷しやすい状態にできる。なお、ゲル収容部9における米ゲルの小分け収容方式は、特に限定されず、米ゲルを小分け収容できる構成であればどのような収容方式であってもよい。例えば、ゲル収容部9は、タンク等の複数の容器に米ゲルを順次小分け収容する構成であってもよい。 Further, the rice gel production system 1 includes a rice gel transfer unit 8 for transferring the rice gel obtained in the crushing unit 7, and a gel storage unit 9 for subdividing the rice gel inherited from the rice gel transfer unit 8. The rice gel can be subdivided and stored in, for example, the rice gel container P in the storage unit 9 to make it easy to ship. The method for subdividing the rice gel in the gel accommodating portion 9 is not particularly limited, and any accommodating method may be used as long as the rice gel can be subdivided and accommodated. For example, the gel storage unit 9 may be configured to sequentially store rice gel in a plurality of containers such as tanks.

さらに、米ゲル移送部8は、高粘性流体を移送可能な一軸偏心ねじポンプで構成される移送ポンプ26で米ゲルを移送するので、粉砕部7で得られる米ゲルの粘度が高い場合であっても、米ゲルをゲル収容部9へ移送できる。 Further, since the rice gel transfer unit 8 transfers the rice gel by a transfer pump 26 composed of a uniaxial eccentric screw pump capable of transferring a highly viscous fluid, the rice gel obtained in the crushing unit 7 has a high viscosity. However, the rice gel can be transferred to the gel container 9.

以下に、米ゲル製造システム1において粉砕部7として設けられた粉砕設備25の詳細構成について、図3に基づいて説明を加える。 The detailed configuration of the crushing equipment 25 provided as the crushing unit 7 in the rice gel manufacturing system 1 will be described below with reference to FIG.

図3は、粉砕設備25の概略構成を示す立断面図である。
粉砕設備25は、ほぐし機24(図1及び図2参照)から供給された炊飯米Rを粉砕してゲル状の米ゲルRGを得る粉砕工程を実行するものとして構成されている。
FIG. 3 is a vertical cross-sectional view showing a schematic configuration of the crushing equipment 25.
The crushing equipment 25 is configured to execute a crushing step of crushing the cooked rice R supplied from the loosening machine 24 (see FIGS. 1 and 2) to obtain a gel-like rice gel RG.

この粉砕設備25は、前段の第1粉砕部100Aと後段の第2粉砕部100Bとを直列に配置した2段式の粉砕部7として構成されている。
第1粉砕部100Aは、ほぐし機24(図1及び図2参照)からホッパー110に供給された炊飯米Rを比較的粗く粉砕して第1粉砕米Raを得る第1粉砕工程を実行するものとして構成されている。
一方、第2粉砕部100Bは、第1粉砕部100Aから排出された第1粉砕米Raを第1粉砕部100Aよりも細かく粉砕して米ゲルRGを得る第2粉砕工程を実行するものとして構成されている。そして、この第2粉砕部100Bで得られた米ゲルRGは、ゲル収容部9(図1及び図2参照)に移送される。
The crushing equipment 25 is configured as a two-stage crushing unit 7 in which a first crushing unit 100A in the front stage and a second crushing unit 100B in the rear stage are arranged in series.
The first crushing unit 100A executes a first crushing step of relatively coarsely crushing the cooked rice R supplied to the hopper 110 from the loosening machine 24 (see FIGS. 1 and 2) to obtain the first crushed rice Ra. It is configured as.
On the other hand, the second crushing unit 100B is configured to execute a second crushing step of crushing the first crushed rice Ra discharged from the first crushing unit 100A into smaller pieces than the first crushing unit 100A to obtain rice gel RG. Has been done. Then, the rice gel RG obtained in the second crushing section 100B is transferred to the gel containing section 9 (see FIGS. 1 and 2).

このように炊飯米Rを二段式の粉砕設備25で粉砕することで、夫々の粉砕部100A,100Bでの粉砕負荷が軽減される。
よって、一段式の粉砕設備で粉砕する場合と比較して、処理量が増加されている。さらには、第2粉砕部100Bにおいて粒感が少なくなるよう米ゲルRGを十分に粉砕しながら、夫々の粉砕部100A,100Bでの粉砕時に粉砕対象物である炊飯米R又は第1粉砕米Raに対して加えられる摩擦熱が軽減する。このことで、当該摩擦熱による米ゲルRGの変色が抑制され、品質及び嗜好性の高い米ゲルRGが製造される。
By crushing the cooked rice R in the two-stage crushing equipment 25 in this way, the crushing load in the crushing portions 100A and 100B, respectively, is reduced.
Therefore, the amount of processing is increased as compared with the case of crushing with a one-stage crushing facility. Further, while sufficiently crushing the rice gel RG in the second crushed portion 100B so as to reduce the graininess, the cooked rice R or the first crushed rice Ra, which are the objects to be crushed at the time of crushing in the respective crushed portions 100A and 100B, respectively. The frictional heat applied to the rice is reduced. As a result, discoloration of the rice gel RG due to the frictional heat is suppressed, and the rice gel RG having high quality and palatability is produced.

夫々の粉砕部100A,100Bは、公知の石臼式の磨砕装置として構成されている。
即ち、粉砕部100A,100Bは、上下に配置された円盤状の上臼部107と下臼部108とを相対回転させた状態で、これら上臼部107の下面と下臼部108の上面との間に形成された隙間103に粉砕対象物R,Raを通過させることで、当該粉砕対象物R,Raを粉砕するように構成されている。詳しくは、下臼部108の中心部には、モータ(図示省略)により回転駆動される回転駆動軸109が固定されており、この回転駆動軸109が回転駆動することで、静止状態に固定された上臼部107に対して下臼部108が相対回転する。
Each of the crushing portions 100A and 100B is configured as a known millstone type crushing device.
That is, in the crushing portions 100A and 100B, the lower surface of the upper mill portion 107 and the upper surface of the lower mill portion 108 are in a state where the disc-shaped upper mill portion 107 and the lower mill portion 108 arranged above and below are rotated relative to each other. By passing the crushed object R, Ra through the gap 103 formed between the crushed objects R, Ra, the crushed object R, Ra is configured to be crushed. Specifically, a rotary drive shaft 109 rotationally driven by a motor (not shown) is fixed to the central portion of the lower die portion 108, and the rotary drive shaft 109 is rotationally driven to be fixed in a stationary state. The lower mill portion 108 rotates relative to the upper mill portion 107.

そして、処理前の粉砕対象物R,Raが、上臼部107の中心部に形成された投入口101を介して、隙間103の中心側に形成された投入空間102に投入される。この投入空間102に投入された粉砕対象物R,Raは、下臼部108の回転駆動により外方に押し込まれて隙間103を通過する。すると、隙間103を通過する粉砕対象物R,Raは、上臼部107に対する下臼部108の相対回転によりせん断力が加えられることで粉砕されて隙間103の外方から落下し、排出口105を通じて外部に払い出される。 Then, the pulverized objects R and Ra before the treatment are charged into the charging space 102 formed on the center side of the gap 103 through the charging port 101 formed in the central portion of the upper mill portion 107. The crushing objects R and Ra charged into the charging space 102 are pushed outward by the rotational drive of the lower sulcus portion 108 and pass through the gap 103. Then, the crushed objects R and Ra passing through the gap 103 are crushed by applying a shearing force due to the relative rotation of the lower mortar portion 108 with respect to the upper mortar portion 107, and fall from the outside of the gap 103, and are discharged from the discharge port 105. It is paid out to the outside through.

粉砕設備25には、夫々の粉砕部100A,100Bで米ゲルRGを順次生産するために、第1粉砕部100Aの排出口105から排出された第1粉砕米Raを自動で第2粉砕部100Bの投入口101に搬送する第1粉砕米搬送部111が設けられている。第1粉砕米搬送部111は、例えばモーノポンプと呼ばれる一軸偏心ねじポンプで構成されている。 In the crushing equipment 25, in order to sequentially produce rice gel RG in the respective crushing units 100A and 100B, the first crushed rice Ra discharged from the discharge port 105 of the first crushing unit 100A is automatically used in the second crushing unit 100B. A first crushed rice transport section 111 is provided for transporting the rice to the charging port 101. The first crushed rice transport unit 111 is composed of, for example, a uniaxial eccentric screw pump called a mono pump.

これら粉砕部100A,100Bを構成する磨砕装置は、上臼部107の下面と下臼部108の上面との間に形成された隙間103の幅であるギャップ幅が、粉砕対象物R,Raに対する粉砕の細かさを決定するパラメータとして変更可能に構成されている。そして、第2粉砕部100Bのギャップ幅が、第1粉砕部100Aでのギャップ幅よりも小さく設定されている。よって、第1粉砕部100Aでは、比較的粒径が大きい炊飯米Rを比較的広い上臼部107と下臼部108との隙間103に通過させて、できるだけ大量の炊飯米Rを比較的粗く粉砕することができる。一方、第2粉砕部100Bでは、比較的粒径が小さい第1粉砕米Raを比較的狭い上臼部107と下臼部108との隙間103に通過させて、当該第1粉砕米Raをできるだけ微細に磨砕して、より滑らかな高品質の米ゲルRGを得ることができる。 In the grinding apparatus constituting these crushing portions 100A and 100B, the gap width, which is the width of the gap 103 formed between the lower surface of the upper mill portion 107 and the upper surface of the lower mill portion 108, is the width of the crushing object R, Ra. It is configured to be changeable as a parameter that determines the fineness of crushing. The gap width of the second crushing unit 100B is set to be smaller than the gap width of the first crushing unit 100A. Therefore, in the first crushed portion 100A, the cooked rice R having a relatively large particle size is passed through the gap 103 between the upper mill portion 107 and the lower mill portion 108 having a relatively wide particle size, and as much rice cooked rice R as possible is made relatively coarse. Can be crushed. On the other hand, in the second crushed portion 100B, the first crushed rice Ra having a relatively small particle size is passed through the gap 103 between the relatively narrow upper mill portion 107 and the lower mill portion 108, and the first crushed rice Ra is passed as much as possible. Finely ground to obtain a smoother, higher quality rice gel RG.

米ゲルの生産性と品質の評価を、本発明による実施例と、別の発明による比較例とについて実施した。以下に、その内容を説明する。 The productivity and quality of rice gel were evaluated for the examples according to the present invention and the comparative examples according to another invention. The contents will be described below.

(実施例1)
実施例1では、2台の磨砕装置(増幸産業株式会社製のマスコロイダー)を直列に設置した粉砕設備を準備し、炊飯米を2段の磨砕装置で順次粉砕する形態で粉砕実験を実施して、米ゲルを得るものとした。なお、この実施例1では、前段の磨砕装置で粉砕された第1粉砕米は、直ぐに後段の磨砕装置に処理対象物として投入するようにした。
また、この実施例1では、第1粉砕部としての前段の磨砕装置のギャップ幅Hを260μmに設定し、第2粉砕部としての後段の磨砕装置のギャップ幅Hを210μmに設定した。
なお、以下に示す表において、S2-1及びS2-2は、本実施例1で用いた2段の粉砕設備に関する評価であり、S2-1は、本実施例1で用いた前段の磨砕装置に関する評価であり、S2-2は、本実施例1の用いた後段の磨砕装置に関する評価である。
(Example 1)
In Example 1, a crushing facility in which two grinders (mass colloider manufactured by Masuko Sangyo Co., Ltd.) are installed in series is prepared, and a crushing experiment is conducted in a form in which cooked rice is sequentially crushed by a two-stage grinder. It was decided to carry out to obtain a rice gel. In Example 1, the first crushed rice crushed by the crushing device in the first stage was immediately put into the crushing device in the latter stage as an object to be processed.
Further, in the first embodiment, the gap width H of the front-stage grinding device as the first crushing unit is set to 260 μm, and the gap width H of the rear-stage grinding device as the second crushing unit is set to 210 μm.
In the table shown below, S2-1 and S2-2 are evaluations relating to the two-stage crushing equipment used in Example 1, and S2-1 is the evaluation of the previous stage pulverization used in Example 1. It is an evaluation about an apparatus, and S2-2 is an evaluation about a post-stage grinding apparatus used in Example 1.

(比較例1)
比較例1では、上記実施例1と同様の磨砕装置を準備し、炊飯米を1段の磨砕装置で粉砕する形態で粉砕実験を実施して、米ゲルを得るものとした。
また、この比較例1では、磨砕装置のギャップ幅Hを220μmに設定した。
なお、以下に示す表において、S1は、本比較例1で用いた磨砕装置に関する評価である。
(Comparative Example 1)
In Comparative Example 1, a crushing device similar to that in Example 1 was prepared, and a crushing experiment was carried out in a form of crushing cooked rice with a one-stage crushing device to obtain a rice gel.
Further, in Comparative Example 1, the gap width H of the grinding device was set to 220 μm.
In the table shown below, S1 is an evaluation of the grinding apparatus used in Comparative Example 1.

〔評価内容及び結果〕
実施例1及び比較例1について実施した評価の内容及び結果を、以下に説明する。
[Evaluation details and results]
The contents and results of the evaluations carried out for Example 1 and Comparative Example 1 will be described below.

(生産性評価)
実施例1と比較例1の夫々について、所定重量(11.25kg)の炊飯米を粉砕する粉砕実験を2回実施した。また、1回目の粉砕実験と2回目の粉砕実験との間には、磨砕装置を冷却するための冷却時間を設けた。
この実験結果を、下記の表1に示す。
(Productivity evaluation)
For each of Example 1 and Comparative Example 1, a crushing experiment of crushing a predetermined weight (11.25 kg) of cooked rice was carried out twice. Further, a cooling time for cooling the grinding device was provided between the first crushing experiment and the second crushing experiment.
The results of this experiment are shown in Table 1 below.

Figure 0007023627000001
Figure 0007023627000001

上記表1に示す量記号の意味は、以下のとおりである。
θ:粉砕時の粉砕対象物の芯温(℃)
:1回目の粉砕実験において粉砕対象物を投入してから米ゲルの排出が完了するまでの処理時間(sec)
:2回目の粉砕実験において粉砕対象物を投入してから米ゲルの排出が完了するまでの処理時間(sec)
ave:1回目と2回目の夫々の粉砕実験における処理時間の平均値(sec)
:1回目の粉砕実験と2回目の粉砕実験との間に設けた磨砕装置を冷却するための冷却時間(sec)
:処理時間の平均値Taveと冷却時間Tの合計である合計処理時間(sec)
AT:比較例1の処理能力(合計処理時間Tの逆数)を1とした場合の処理能力の割合
The meanings of the quantity symbols shown in Table 1 above are as follows.
θ: Core temperature (° C) of the object to be crushed during crushing
T 1 : Processing time (sec) from the addition of the object to be crushed to the completion of discharge of rice gel in the first crushing experiment.
T 2 : Processing time (sec) from the addition of the object to be crushed to the completion of discharge of rice gel in the second crushing experiment.
T ave : Mean value of processing time (sec) in each of the first and second crushing experiments
TC : Cooling time (sec) for cooling the grinding device provided between the first crushing experiment and the second crushing experiment.
TA : Total processing time (sec), which is the sum of the average processing time Tave and the cooling time TC .
AT: Ratio of processing capacity when the processing capacity of Comparative Example 1 (the reciprocal of the total processing time TA ) is 1.

上記表1から判るように、炊飯米を1段の磨砕装置で粉砕する比較例1(S1)では、1回目と2回目の処理時間の平均値Taveが77sec、それに冷却時間Tを加えた合計処理時間Tが180secとなった。
一方、炊飯米を2段の磨砕装置で粉砕する実施例1では、例えば前段の磨砕装置(S2-1)の処理時間の平均値Taveが44.6sec、後段の磨砕装置(S2-2)の処理時間の平均値Taveが55.4secとなって、前段及び後段の夫々の磨砕装置での処理時間が上記比較例1(S1)よりも減少していることが判る。また、前段及び後段の磨砕装置での粉砕時の粉砕対象物の芯温θが、メイラード反応により変色を引き起こす限界温度(例えば110℃)未満に抑えられていることが判る。よって、前段及び後段の夫々の磨砕装置の冷却時間Tを15sec及び10secとすると、前段の磨砕装置(S2-1)での合計処理時間Tが59.6sec、後段の磨砕装置(S2-2)での合計処理時間Tが65.4secとなる。そして、後段の磨砕装置(S2-2)での合計処理時間Tが律速(ボトルネック)となって、その処理時間T毎に処理対象物を投入可能となることから、実施例1の合計処理時間Tは、65.4secとなる。
よって、実施例1は、比較例1の合計処理時間Tが180secであるのに対して、実施例1の合計処理時間Tが65.4secとなることから、実施例1の処理能力ATは比較例1の2.75倍であると言える。
As can be seen from Table 1 above, in Comparative Example 1 (S1) in which cooked rice is crushed by a one - stage grinder, the average value Table of the first and second processing times is 77 sec, and the cooling time TC is set to 77 sec. The total processing time TA added was 180 sec.
On the other hand, in Example 1 in which the cooked rice is crushed by a two-stage grinder, for example, the average processing time Tave of the pre-stage grinder (S2-1) is 44.6 sec, and the post-stage grinder (S2). The average value Tave of the processing time in -2) is 55.4 sec, and it can be seen that the processing time in each of the pre-stage and the post-stage grinders is shorter than that in Comparative Example 1 (S1). Further, it can be seen that the core temperature θ of the object to be crushed during pulverization by the pulverizers in the first and second stages is suppressed to less than the limit temperature (for example, 110 ° C.) that causes discoloration due to the Maillard reaction. Therefore, assuming that the cooling times TC of the front-stage and rear-stage grinders are 15 sec and 10 sec, the total processing time TA of the pre-stage grinder (S2-1) is 59.6 sec, and the post-stage grind device. The total processing time TA in (S2-2) is 65.4 sec. Then, the total processing time TA in the subsequent grinding device (S2-2) becomes a rate - determining (bottleneck), and the object to be processed can be charged for each processing time TA . Therefore, Example 1 The total processing time TA of is 65.4 sec.
Therefore, in Example 1, the total processing time TA of Comparative Example 1 is 180 sec, whereas the total processing time TA of Example 1 is 65.4 sec. Therefore, the processing capacity AT of Example 1 Can be said to be 2.75 times that of Comparative Example 1.

また、今般の実施例1において、後段の磨砕装置のギャップ幅Hを200μmに変更して粉砕実験を実施すると、粉砕時の粉砕対象物の芯温がメイラード反応により変色を引き起こす限界温度近傍まで上昇した。このことにより、実施例1における後段の磨砕装置のギャップ幅Hの下限界値は200μm程度であると考えられ、後段の磨砕装置のギャップ幅Hの最適値は上述の210μm程度であると判断できる。
一方、今般の実施例1において、前段の磨砕装置のギャップ幅を260μmに設定したが、そのギャップ幅については240μm程度まで小さくして、前段の磨砕装置において炊飯米を細かめに粉砕して、後段の磨砕装置の粉砕負荷を軽減させることもできる。
Further, in Example 1 of this time, when the crushing experiment is carried out by changing the gap width H of the grinding device in the subsequent stage to 200 μm, the core temperature of the crushed object at the time of crushing reaches near the limit temperature which causes discoloration due to the Maillard reaction. Rose. From this, it is considered that the lower limit value of the gap width H of the subsequent grinding device in Example 1 is about 200 μm, and the optimum value of the gap width H of the subsequent grinding device is about 210 μm. I can judge.
On the other hand, in Example 1 of this time, the gap width of the grinding device in the previous stage was set to 260 μm, but the gap width was reduced to about 240 μm, and the cooked rice was finely crushed in the grinding device in the previous stage. Therefore, the crushing load of the subsequent crushing device can be reduced.

また、今般の実験では、1回の炊飯米の投入重量を11.25kgとしたが、上記実施例1では、粉砕時の芯温に余裕があることから、この投入重量を例えば15kg程度に増加させることができると考えられる。 Further, in this experiment, the input weight of the cooked rice at one time was set to 11.25 kg, but in the above-mentioned Example 1, since there is a margin in the core temperature at the time of crushing, this input weight is increased to, for example, about 15 kg. It is thought that it can be made to.

(粘度評価)
実施例1と比較例1の夫々について、上述の2回の粉砕実験で得られた米ゲルの粘度について評価した。この評価結果を、下記の表2に示す。
(Viscosity evaluation)
The viscosity of the rice gel obtained in the above-mentioned two crushing experiments was evaluated for each of Example 1 and Comparative Example 1. The evaluation results are shown in Table 2 below.

Figure 0007023627000002
Figure 0007023627000002

上記表2に示す量記号の意味は、以下のとおりである。
μ:1回目の粉砕実験で得られた米ゲルの粘度(Pa・s)
μ:2回目の粉砕実験で得られた米ゲルの粘度(Pa・s)
μave:1回目と2回目の夫々の粉砕実験で得られた米ゲルの粘度の平均値(Pa・s)
:粘度μ1を測定した米ゲルの温度(℃)
:粘度μ2を測定した米ゲルの温度(℃)
ave:米ゲルの温度T1と温度T2の平均値(℃)
The meanings of the quantity symbols shown in Table 2 above are as follows.
μ 1 : Viscosity of rice gel obtained in the first crushing experiment (Pa · s)
μ 2 : Viscosity (Pa · s) of rice gel obtained in the second crushing experiment
μ ave : Mean value of viscosity of rice gel obtained in each of the first and second crushing experiments (Pa · s)
t 1 : The temperature (° C.) of the rice gel whose viscosity μ1 was measured.
t 2 : Temperature (° C) of rice gel with viscosity μ2 measured
t ave : Mean value (° C.) of temperature T1 and temperature T2 of rice gel

上記表2から判るように、比較例1で得られた米ゲルの粘度の平均値μaveは179.5Pa・sであった。それに対し、実施例1の後段の磨砕装置(S2-2)で得られた米ゲルの粘度の平均値μaveは175.5Pa・sであり、比較例1とほぼ同等の粘度であった。
このことから、粘度に関する米ゲルの品質に関しては、実施例1は、比較例1と略同等のレベルを達成できると言える。
As can be seen from Table 2 above, the average value μ- ave of the viscosity of the rice gel obtained in Comparative Example 1 was 179.5 Pa · s. On the other hand, the average value μ ave of the viscosity of the rice gel obtained by the grinding apparatus (S2-2) in the latter stage of Example 1 was 175.5 Pa · s, which was almost the same viscosity as that of Comparative Example 1. ..
From this, it can be said that Example 1 can achieve a level substantially equivalent to that of Comparative Example 1 in terms of the quality of the rice gel in terms of viscosity.

(含水率評価)
実施例1と比較例1の夫々について、上述の2回の粉砕実験で得られた米ゲルの含水率について評価した。この評価結果を、下記の表3に示す。
(Evaluation of water content)
The water content of the rice gel obtained in the above-mentioned two crushing experiments was evaluated for each of Example 1 and Comparative Example 1. The evaluation results are shown in Table 3 below.

Figure 0007023627000003
Figure 0007023627000003

上記表3に示す量記号の意味は、以下のとおりである。
u:粉砕実験で得られた米ゲルの含水率(%)
The meanings of the quantity symbols shown in Table 3 above are as follows.
u: Moisture content (%) of rice gel obtained in the crushing experiment

上記表3から判るように、比較例1で得られた米ゲルの含水率uは71.30%であった。それに対し、実施例1の後段の磨砕装置(S2-2)で得られた米ゲルの含水率uは66.3%であり、比較例1とほぼ同等の含水率であった。
このことから、含水率に関する米ゲルの品質に関しては、実施例1は、比較例1と略同等のレベルを達成できると言える。
As can be seen from Table 3 above, the water content u of the rice gel obtained in Comparative Example 1 was 71.30%. On the other hand, the water content u of the rice gel obtained by the grinding apparatus (S2-2) in the latter stage of Example 1 was 66.3%, which was almost the same as that of Comparative Example 1.
From this, it can be said that Example 1 can achieve a level substantially equivalent to that of Comparative Example 1 in terms of the quality of the rice gel with respect to the water content.

(官能性評価)
実施例1と比較例1の夫々について、上述の2回の粉砕実験で得られた米ゲルの外観、色沢、香味、食感等の官能性について、複数の評価者により実際に食して評価した。
その評価の結果、実施例1で得られた米ゲルと比較例1で得られた米ゲルとは、外観、色沢、香味については、略差がないとの結果が得られた。一方、食感に関しては、実施例1で得られた米ゲルは、比較例1よりも明らかに滑らかであるとの結果が得られた。
(Evaluation of sensuality)
For each of Example 1 and Comparative Example 1, the appearance, color, flavor, texture, and other sensualities of the rice gel obtained in the above-mentioned two crushing experiments were actually eaten and evaluated by a plurality of evaluators. did.
As a result of the evaluation, it was obtained that there was almost no difference in appearance, color and flavor between the rice gel obtained in Example 1 and the rice gel obtained in Comparative Example 1. On the other hand, regarding the texture, the rice gel obtained in Example 1 was clearly smoother than that of Comparative Example 1.

(粒感評価)
実施例1と比較例1の夫々について、上述の2回の粉砕実験で得られた米ゲルの粒感について評価した。この評価結果を、下記の表3に示す。
(Grade feeling evaluation)
For each of Example 1 and Comparative Example 1, the graininess of the rice gel obtained in the above-mentioned two crushing experiments was evaluated. The evaluation results are shown in Table 3 below.

Figure 0007023627000004
Figure 0007023627000004

上記表4に示す量記号の意味は、以下のとおりである。
:ラミネート粒感観察により測定した米ゲルに残留する微細米粒の数(個/ラミネート)
g:ラミネート粒感観察で用いた米ゲルの重量(g)
10:米ゲル10gに残留する微細米粒の数(個/10g)
なお、上記ラミネート粒感観察とは、粉砕実験で得られた米ゲルを所定の大きさのラミネート上に薄く広げた状態で残留米粒の数をカウントする粒感観察の方法である。
The meanings of the quantity symbols shown in Table 4 above are as follows.
n L : Number of fine rice grains remaining in the rice gel measured by observing the feeling of laminated grains (pieces / laminate)
g: Weight of rice gel used for observing the feeling of laminated grain (g)
n 10 : Number of fine rice grains remaining in 10 g of rice gel (pieces / 10 g)
The laminated grain texture observation is a method of grain texture observation in which the number of residual rice grains is counted in a state where the rice gel obtained in the crushing experiment is thinly spread on a laminate of a predetermined size.

上記表4から判るように、比較例1で得られた米ゲル10gに残留する微細米粒の数n10は、13.55個/10gであった。それに対し、実施例1の後段の磨砕装置(S2-2)で得られた米ゲルに残留する微細米粒の数n10は、2.90個/10gと、比較例1よりも大幅に削減されていた。
このことから、粒感に関する米ゲルの品質に関しては、実施例1は、比較例1よりも大幅に滑らかな米ゲルを得ることができると言える。
As can be seen from Table 4 above, the number n 10 of fine rice grains remaining in 10 g of the rice gel obtained in Comparative Example 1 was 13.55 / 10 g. On the other hand, the number n 10 of fine rice grains remaining in the rice gel obtained by the grinding apparatus (S2-2) in the latter stage of Example 1 was 2.90 / 10 g, which was significantly reduced as compared with Comparative Example 1. It had been.
From this, it can be said that Example 1 can obtain a rice gel that is significantly smoother than Comparative Example 1 in terms of the quality of the rice gel in terms of graininess.

〔他の実施形態〕
図4は、米ゲル製造システムの他の実施形態の概略構成図である。この実施形態の米ゲル製造システム1は、原料米に傷をつける原料米加工部38を備えている。この実施形態では、原料米加工部38は、貯米部2と洗米部3の間に設けられる。原料米加工部38は、原料米の米粒表面に傷をつけたり米粒を割ったりする損傷加工を行う粉砕装置37を備える。貯米部2から所定量の原料米が原料米加工部38に移送され、原料米加工部38で損傷加工された原料米が洗米部3の洗米機16を介して、浸漬部4の浸漬タンク18に移送される。浸漬処理前に、原料米に損傷加工を施すことにより、浸漬水と接する原料米の表面積が増えるので、浸漬時間を短くできる。なお、原料米加工部38の配置位置は、原料米を浸漬処理する前に損傷加工できる位置であればよく、例えば、貯米部2の納米ホッパー12と納米庫14の間であってもよい。
[Other embodiments]
FIG. 4 is a schematic configuration diagram of another embodiment of the rice gel production system. The rice gel production system 1 of this embodiment includes a raw rice processing unit 38 that damages the raw rice. In this embodiment, the raw rice processing section 38 is provided between the rice storage section 2 and the rice washing section 3. The raw rice processing unit 38 includes a crushing device 37 that performs damage processing such as scratching or cracking the surface of rice grains of raw rice. A predetermined amount of raw rice is transferred from the rice storage section 2 to the raw rice processing section 38, and the raw rice damaged by the raw rice processing section 38 is passed through the rice washing machine 16 of the rice washing section 3 to the immersion tank of the dipping section 4. Transferred to 18. By damaging the raw rice before the dipping treatment, the surface area of the raw rice in contact with the soaking water is increased, so that the dipping time can be shortened. The position of the raw rice processing section 38 may be any position as long as it can be damaged before the raw rice is immersed, and may be, for example, between the rice delivery hopper 12 and the rice storage 14 of the rice storage section 2. ..

図1及び図2に示した実施形態と、図4に示した実施形態は、原料米の水洗い処理を洗米部3で行うと共に、浸漬処理を浸漬部4の浸漬タンク18内で行っているが、水洗い処理及び浸漬処理は炊飯釜A内で行われてもよい。また、原料米の水洗い処理を洗米部3で行った後、洗米と浸漬水を炊飯釜A内に収容して、炊飯釜A内で浸漬処理を行う構成であってもよい。 In the embodiments shown in FIGS. 1 and 2 and the embodiment shown in FIG. 4, the raw rice is washed with water in the rice washing section 3 and the dipping process is performed in the dipping tank 18 of the dipping section 4. , The washing treatment and the dipping treatment may be performed in the rice cooker A. Further, the rice washing unit 3 may wash the raw material rice with water, and then the rice washing and the soaking water may be stored in the rice cooking pot A and the soaking treatment may be performed in the rice cooking pot A.

次に、図5から図10を参照しながら、米ゲル製造システムのさらに他の実施形態を説明する。この実施形態の米ゲル製造システム1は、炊飯部5に蒸気式の連続炊飯装置43を備え、炊飯米搬送部6に主コンベヤ46及び複数の投入用コンベヤ47a,47b,47c,47dを備え、粉砕部7は、並列状態で配置された複数の粉砕設備25として粉砕設備25a,25b,25c,25d,25eを備える。 Next, still another embodiment of the rice gel production system will be described with reference to FIGS. 5 to 10. In the rice gel production system 1 of this embodiment, the rice cooking unit 5 is provided with a steam-type continuous rice cooking device 43, and the rice cooking rice transport unit 6 is provided with a main conveyor 46 and a plurality of feeding conveyors 47a, 47b, 47c, 47d. The crushing unit 7 includes crushing equipment 25a, 25b, 25c, 25d, 25e as a plurality of crushing equipment 25 arranged in a parallel state.

原料米は、貯米部2で納米ホッパー12に投入され、納米昇降機13により搬送されて納米庫14に収容される。納米庫14から排出される所定量の原料米は、原料米搬送機15にて洗米部3の洗米機16に送られる。洗米機16で得られる洗米は、送米機41及び洗米移送管17を介して浸漬部4の浸漬タンク18に送られ、浸漬タンク18内で浸漬される。 The raw rice is put into the rice delivery hopper 12 by the rice storage unit 2, transported by the rice delivery elevator 13, and stored in the rice delivery storage 14. A predetermined amount of raw rice discharged from the rice storage 14 is sent to the rice washing machine 16 of the rice washing unit 3 by the raw rice carrier 15. The rice washing obtained by the rice washing machine 16 is sent to the immersion tank 18 of the immersion unit 4 via the rice feeder 41 and the rice washing transfer pipe 17, and is immersed in the immersion tank 18.

浸漬タンク18内の浸漬米は、メッシュベルト等を有する水切りコンベヤ42の搬送上流端側に供給され、水切りコンベヤ42で搬送されながら水切りされて、連続炊飯装置43に供給される。連続炊飯装置43は、例えば炊飯釜A(図1等参照)を用いずに、浸漬米をコンベヤ(図示省略)で搬送しながら、蒸気及び熱湯で加熱して連続炊飯し、炊飯米R(図9及び図10参照)を炊飯米排出コンベヤ44で排出する。炊飯米排出コンベヤ44から排出される炊飯米Rの温度は95度以上である。 The soaked rice in the dipping tank 18 is supplied to the transport upstream end side of the drainer conveyor 42 having a mesh belt or the like, is drained while being transported by the drainer conveyor 42, and is supplied to the continuous rice cooking device 43. The continuous rice cooker 43 heats the cooked rice R with steam and boiling water while transporting the soaked rice with a conveyor (not shown) without using, for example, the rice cooker A (see FIG. 1 and the like). 9 and FIG. 10) are discharged by the cooked rice discharge conveyor 44. The temperature of the cooked rice R discharged from the cooked rice discharge conveyor 44 is 95 degrees or higher.

連続炊飯装置43の炊飯米排出コンベヤ44から排出される炊飯米Rは、炊飯米搬送部6のコンベヤ45、主コンベヤ46及び投入用コンベヤ47a,47b,47c,47dを介して粉砕部7に搬送される。炊飯米搬送部6は、連続炊飯装置43から受け継いだ炊飯米Rを粉砕部7の複数の粉砕設備25a,25b,25c,25d,25eに振り分けて供給する。粉砕設備25a,25b,25c,25d,25eに供給される炊飯米Rの温度は85度以上である。 The cooked rice R discharged from the cooked rice discharge conveyor 44 of the continuous rice cooker 43 is conveyed to the crushing section 7 via the conveyor 45 of the cooked rice transport section 6, the main conveyor 46, and the feeding conveyors 47a, 47b, 47c, 47d. Will be done. The cooked rice transport unit 6 distributes and supplies the cooked rice R inherited from the continuous rice cooker 43 to a plurality of crushing facilities 25a, 25b, 25c, 25d, 25e of the crushing unit 7. The temperature of the cooked rice R supplied to the crushing equipment 25a, 25b, 25c, 25d, 25e is 85 degrees or higher.

図7に示すように、炊飯米搬送部6は、連続炊飯装置43の炊飯米排出コンベヤ44にコンベヤ45を介して連結される主コンベヤ46と、主コンベヤ46に連結されると共に直列連結される複数の投入用コンベヤ47a,47b,47c,47dを備える。第1投入用コンベヤ47a、第2投入用コンベヤ47b及び第3投入用コンベヤ47cは、搬送方向が傾斜するように配置される。主コンベヤ46の搬送下流端の下方に1段目の第1投入用コンベヤ47aの中途部が配置される。第1投入用コンベヤ47aの一端(下方端)の下方に第1粉砕設備25aが配置され、他端(上方端)の下方に後段側の第2投入用コンベヤ47bの中途部が配置される。第2投入用コンベヤ47bの一端(下方端)の下方に第2粉砕設備25bが配置され、他端(上方端)の下方に後段側の第3投入用コンベヤ47cの中途部が配置される。第3投入用コンベヤ47cの一端(下方端)の下方に第3粉砕設備25cが配置され、他端(上方端)の下方に後段側の第4投入用コンベヤ47dの中途部が配置される。第4投入用コンベヤ47dは水平配置され、一端の下方に第4粉砕設備25dが配置され、他端の下方に第5粉砕設備25eが配置される。 As shown in FIG. 7, the rice-cooking rice transport unit 6 is connected to the main conveyor 46 connected to the rice-cooking rice discharge conveyor 44 of the continuous rice cooking device 43 via the conveyor 45, and is connected to the main conveyor 46 and connected in series. A plurality of loading conveyors 47a, 47b, 47c, 47d are provided. The first charging conveyor 47a, the second charging conveyor 47b, and the third charging conveyor 47c are arranged so that the transport direction is inclined. An intermediate portion of the first-stage first loading conveyor 47a is arranged below the transport downstream end of the main conveyor 46. The first crushing equipment 25a is arranged below one end (lower end) of the first loading conveyor 47a, and the middle portion of the second loading conveyor 47b on the rear stage side is arranged below the other end (upper end). The second crushing equipment 25b is arranged below one end (lower end) of the second loading conveyor 47b, and the middle portion of the third loading conveyor 47c on the rear stage side is arranged below the other end (upper end). The third crushing equipment 25c is arranged below one end (lower end) of the third loading conveyor 47c, and the middle portion of the fourth loading conveyor 47d on the rear stage side is arranged below the other end (upper end). The fourth loading conveyor 47d is horizontally arranged, the fourth crushing equipment 25d is arranged below one end, and the fifth crushing equipment 25e is arranged below the other end.

炊飯米搬送部6は、投入用コンベヤ47a,47b,47c,47dの搬送方向を切り替えることで、炊飯米Rを粉砕設備25a,25b,25c,25d,25eのいずれかに供給し、又は後段側の投入用コンベヤ47b,47c,47dに供給する。これにより、炊飯米搬送部6は、炊飯米Rを複数の粉砕設備25a,25b,25c,25d,25eに振り分けて供給する。各粉砕設備25a,25b,25c,25d,25eの粉砕処理能力は、ここでは同じである。炊飯米搬送部6の振り分け動作については後述する。 The cooked rice transport unit 6 supplies the cooked rice R to any of the crushing facilities 25a, 25b, 25c, 25d, 25e by switching the transport direction of the feeding conveyors 47a, 47b, 47c, 47d, or the rear stage side. Is supplied to the loading conveyors 47b, 47c, 47d. As a result, the cooked rice transport unit 6 distributes and supplies the cooked rice R to the plurality of crushing facilities 25a, 25b, 25c, 25d, 25e. The crushing processing capacity of each crushing facility 25a, 25b, 25c, 25d, 25e is the same here. The sorting operation of the cooked rice transport unit 6 will be described later.

粉砕部7は、粉砕設備25a,25b,25c,25d,25eで炊飯米を粉砕して米ゲルを得る。粉砕設備25a,25b,25c,25d,25eで得られる米ゲルは、米ゲル移送部8の米ゲルホッパー48を介して移送ポンプ26に供給され、1台の移送ポンプ26により米ゲル移送配管27を介してゲル収容部9の包装機28へ移送される。包装機28で米ゲルが小分け収容されて得られる米ゲル収容物Pは、コンベヤ30により検査部10へ搬送され、異物検出機31及び重さ検査機32で検査された後、出荷部11の移動台33へ順次載せられる。さらに、米ゲル収容物Pは、殺菌機34で加熱殺菌及び冷却され、除水機35で除水された後、箱詰めされて出荷可能な状態にされる。 The crushing unit 7 crushes the cooked rice with the crushing equipment 25a, 25b, 25c, 25d, 25e to obtain a rice gel. The rice gel obtained by the crushing equipment 25a, 25b, 25c, 25d, 25e is supplied to the transfer pump 26 via the rice gel hopper 48 of the rice gel transfer section 8, and the rice gel transfer pipe 27 is supplied by one transfer pump 26. It is transferred to the packaging machine 28 of the gel accommodating portion 9 via the above. The rice gel container P obtained by subdividing the rice gel in the packaging machine 28 is conveyed to the inspection unit 10 by the conveyor 30, inspected by the foreign matter detector 31 and the weight inspection machine 32, and then in the shipping unit 11. It is sequentially placed on the moving table 33. Further, the rice gel container P is sterilized by heating and cooled by the sterilizer 34, water is removed by the water remover 35, and then packed in a box so that it can be shipped.

図8に示すように、米ゲル製造システム1には、炊飯米搬送部6のコンベヤ46,47a,47b,47c,47dのコンベヤ駆動モータ56,57a,57b,57c,57dの動作を制御する制御装置58が設けられる。制御装置58は、主コンベヤ46の搬送速度や、投入用コンベヤ47a,47b,47c,47dの搬送方向及び搬送速度を制御する。 As shown in FIG. 8, the rice gel manufacturing system 1 has a control for controlling the operation of the conveyor drive motors 56, 57a, 57b, 57c, 57d of the conveyors 46, 47a, 47b, 47c, 47d of the rice cooking rice transport unit 6. The device 58 is provided. The control device 58 controls the transport speed of the main conveyor 46, the transport direction and the transport speed of the loading conveyors 47a, 47b, 47c, 47d.

図9を参照しながら、炊飯米搬送部6における炊飯米Rの振り分け動作の一例を説明する。この振り分け動作例では、工程(1)から(4)が繰り返されて、炊飯米Rが複数の粉砕設備25a,25b,25c,25d,25eに振り分けて供給される。以下に説明する工程(1)から(4)は、図9のかっこ数字(1)から(4)に対応している。連続炊飯装置43から排出される炊飯米Rは、コンベヤ45(図7参照)及び主コンベヤ46を介して、第1投入用コンベヤ47aへ搬送される。 An example of the distribution operation of the cooked rice R in the cooked rice transport unit 6 will be described with reference to FIG. 9. In this distribution operation example, the steps (1) to (4) are repeated, and the cooked rice R is distributed and supplied to a plurality of crushing facilities 25a, 25b, 25c, 25d, 25e. The steps (1) to (4) described below correspond to the parenthesized numbers (1) to (4) in FIG. The cooked rice R discharged from the continuous rice cooker 43 is conveyed to the first feeding conveyor 47a via the conveyor 45 (see FIG. 7) and the main conveyor 46.

工程(1):図9(1)に示すように、炊飯米Rを第1粉砕設備25aに供給する場合、第1投入用コンベヤ47aの搬送方向が第1粉砕設備25a側へ向くように制御し、主コンベヤ46から供給される炊飯米Rを所定量だけ第1粉砕設備25aに供給する。また、工程(1)では、後述する第5粉砕設備25eに向けて搬送する炊飯米Rが投入用コンベヤ47b,47c,47d上で搬送され、所定量の炊飯米Rが第5粉砕設備25eに供給される。 Step (1): As shown in FIG. 9 (1), when the cooked rice R is supplied to the first crushing equipment 25a, the transport direction of the first feeding conveyor 47a is controlled to face the first crushing equipment 25a side. Then, a predetermined amount of the cooked rice R supplied from the main conveyor 46 is supplied to the first crushing facility 25a. Further, in the step (1), the cooked rice R to be conveyed to the fifth crushing equipment 25e, which will be described later, is conveyed on the feeding conveyors 47b, 47c, 47d, and a predetermined amount of the cooked rice R is transferred to the fifth crushing equipment 25e. Will be supplied.

工程(2):図9(2)に示すように、炊飯米Rを第2粉砕設備25bに供給する場合、上記工程(1)での動作状態から、第1投入用コンベヤ47aの搬送方向を第2投入用コンベヤ47b側へ向くように切り替える。また、第2投入用コンベヤ47bの搬送方向が第2粉砕設備25b側へ向くように制御する。主コンベヤ46から供給される炊飯米Rを、投入用コンベヤ47a,47bを介して所定量だけ第2粉砕設備25bに供給する。 Step (2): As shown in FIG. 9 (2), when the cooked rice R is supplied to the second crushing facility 25b, the transport direction of the first feeding conveyor 47a is changed from the operating state in the above step (1). Switch so that it faces the second loading conveyor 47b side. Further, the transport direction of the second loading conveyor 47b is controlled to face the second crushing equipment 25b side. The cooked rice R supplied from the main conveyor 46 is supplied to the second crushing facility 25b by a predetermined amount via the feeding conveyors 47a and 47b.

工程(3):図9(3)に示すように、炊飯米Rを第3粉砕設備25cに供給する場合、上記工程(2)での動作状態から、第2投入用コンベヤ47bの搬送方向を第3投入用コンベヤ47c側へ向くように切り替える。また、第3投入用コンベヤ47cの搬送方向が第3粉砕設備25c側へ向くように制御する。主コンベヤ46から供給される炊飯米Rを、投入用コンベヤ47a,47b,47cを介して所定量だけ第3粉砕設備25cに供給する。 Step (3): As shown in FIG. 9 (3), when the cooked rice R is supplied to the third crushing facility 25c, the transport direction of the second feeding conveyor 47b is changed from the operating state in the above step (2). Switch so that it faces the third loading conveyor 47c side. Further, the transport direction of the third loading conveyor 47c is controlled to face the third crushing equipment 25c side. The cooked rice R supplied from the main conveyor 46 is supplied to the third crushing facility 25c in a predetermined amount via the feeding conveyors 47a, 47b, 47c.

工程(4):図9(4)に示すように、炊飯米Rを第4粉砕設備25dに供給する場合、上記工程(3)の動作状態から、第3投入用コンベヤ47cの搬送方向を第4投入用コンベヤ47d側へ向くように切り替える。また、第4投入用コンベヤ47dの搬送方向が第4粉砕設備25d側へ向くように制御する。主コンベヤ46から供給される炊飯米Rを、投入用コンベヤ47a,47b,47c,47dを介して所定量だけ第4粉砕設備25dに供給する。 Step (4): As shown in FIG. 9 (4), when the cooked rice R is supplied to the fourth crushing facility 25d, the transport direction of the third feeding conveyor 47c is changed from the operating state of the above step (3). 4 Switch so that it faces the loading conveyor 47d side. Further, the transport direction of the 4th loading conveyor 47d is controlled to face the 4th crushing equipment 25d side. The cooked rice R supplied from the main conveyor 46 is supplied to the fourth crushing facility 25d in a predetermined amount via the feeding conveyors 47a, 47b, 47c, 47d.

上記工程(4)で、第4粉砕設備25dに所定量の炊飯米Rが供給された後、第4投入用コンベヤ47dの搬送方向を逆に切り替えて、第5粉砕設備25e側へ向くように制御する。これにより、第5粉砕設備25eへの炊飯米Rの供給が開始される。第5粉砕設備25eへ投入された炊飯米Rの量と、第2から第4の投入用コンベヤ47b,47c,47d上の炊飯米Rの量の合計が所定量になると、第1投入用コンベヤ47aの搬送方向を逆に切り替えて、第1粉砕設備25aへの炊飯米Rの投入を開始する(上記工程(1)及び図9(1)参照)。第2から第4の投入用コンベヤ47b,47c,47d上の炊飯米Rは、投入用コンベヤ47b,47c,47dの駆動により、第5粉砕設備25eへ搬送される。これにより、所定量の炊飯米Rが第5粉砕設備25eへ供給される。 In the above step (4), after a predetermined amount of cooked rice R is supplied to the 4th crushing equipment 25d, the transport direction of the 4th feeding conveyor 47d is switched in the opposite direction so as to face the 5th crushing equipment 25e side. Control. As a result, the supply of cooked rice R to the fifth crushing facility 25e is started. When the sum of the amount of cooked rice R charged into the fifth crushing facility 25e and the amount of cooked rice R on the second to fourth feeding conveyors 47b, 47c, 47d reaches a predetermined amount, the first feeding conveyor The transport direction of 47a is reversed, and the rice cooked rice R is started to be charged into the first crushing facility 25a (see the above steps (1) and FIG. 9 (1)). The cooked rice R on the second to fourth charging conveyors 47b, 47c, 47d is conveyed to the fifth crushing facility 25e by driving the charging conveyors 47b, 47c, 47d. As a result, a predetermined amount of cooked rice R is supplied to the fifth crushing facility 25e.

上記工程(1)から(4)を繰り返すことで、粉砕設備25a,25b,25c,25d,25eに炊飯米Rが順次振り分けて供給される。なお、投入用コンベヤ47a,47b,47c,47dの搬送方向の切り替え時期は、例えば、各コンベヤの駆動時間を計測することで行う。また、主コンベヤ46上の所定位置を通過する炊飯米Rの量を計測する計測器を設けて、その計測器の出力に基づいて各粉砕設備25a,25b,25c,25d,25eに供給される炊飯米Rの量が所定量になるように、投入用コンベヤ47a,47b,47c,47dの搬送方向を切り替えてもよい。なお、投入用コンベヤ47a,47b,47c,47dの搬送速度は、主コンベヤ46の搬送速度と同じであるか、それよりも大きいことが好ましいが、主コンベヤ46の搬送速度よりも小さくてもよい。また、粉砕設備25a,25b,25c,25d,25eに炊飯米Rが供給される順番は、特に限定されない。 By repeating the above steps (1) to (4), the cooked rice R is sequentially distributed and supplied to the crushing equipment 25a, 25b, 25c, 25d, 25e. The time for switching the transport directions of the loading conveyors 47a, 47b, 47c, and 47d is determined by, for example, measuring the drive time of each conveyor. Further, a measuring instrument for measuring the amount of cooked rice R passing through the predetermined position on the main conveyor 46 is provided, and the rice is supplied to each crushing facility 25a, 25b, 25c, 25d, 25e based on the output of the measuring instrument. The transport directions of the feeding conveyors 47a, 47b, 47c, and 47d may be switched so that the amount of cooked rice R becomes a predetermined amount. The transfer speed of the loading conveyors 47a, 47b, 47c, 47d is preferably the same as or higher than the transfer speed of the main conveyor 46, but may be lower than the transfer speed of the main conveyor 46. .. Further, the order in which the cooked rice R is supplied to the crushing equipment 25a, 25b, 25c, 25d, 25e is not particularly limited.

次に、図10を参照しながら、炊飯米搬送部6における炊飯米Rの振り分け動作の他の例を説明する。この振り分け動作例では、工程(1)から(3)が繰り返されて、炊飯米Rが複数の粉砕設備25a,25b,25c,25d,25eに振り分けて供給される。以下に説明する工程(1)から(3)は、図10のかっこ数字(1)から(3)に対応している。 Next, another example of the distribution operation of the cooked rice R in the cooked rice transport unit 6 will be described with reference to FIG. 10. In this distribution operation example, the steps (1) to (3) are repeated, and the cooked rice R is distributed and supplied to a plurality of crushing facilities 25a, 25b, 25c, 25d, 25e. The steps (1) to (3) described below correspond to the parenthesized numbers (1) to (3) in FIG.

工程(1):図10(1)に示すように、第1投入用コンベヤ47aの搬送方向が第2投入用コンベヤ47b側へ向き、第2投入用コンベヤ47bの搬送方向が第3投入用コンベヤ47c側へ向き、第3投入用コンベヤ47cの搬送方向が第4投入用コンベヤ47d側へ向き、第4投入用コンベヤ47dの搬送方向が第4粉砕設備25d側へ向くように、投入用コンベヤ47a,47b,47c,47dの駆動を制御する。投入用コンベヤ47a,47b,47cの長さはほぼ同じであり、炊飯米Rの搬送中に、各投入用コンベヤ47a,47b,47c上に存在する炊飯米Rの量は、おおよそ同量の状態になる。第4投入用コンベヤ47dの駆動により、各投入用コンベヤ47a,47b,47c上の各炊飯米Rの量とおおよそ同量の炊飯米Rが供給される。 Step (1): As shown in FIG. 10 (1), the transport direction of the first loading conveyor 47a is toward the second loading conveyor 47b, and the transport direction of the second loading conveyor 47b is the third loading conveyor. The feeding conveyor 47a faces the 47c side, the transport direction of the third loading conveyor 47c faces the fourth loading conveyor 47d side, and the transport direction of the fourth loading conveyor 47d faces the fourth crushing facility 25d side. , 47b, 47c, 47d are controlled. The lengths of the feeding conveyors 47a, 47b, 47c are almost the same, and the amount of the cooked rice R present on each of the feeding conveyors 47a, 47b, 47c during the transportation of the cooked rice R is approximately the same. become. By driving the fourth feeding conveyor 47d, approximately the same amount of cooked rice R as the amount of each cooked rice R on each of the feeding conveyors 47a, 47b, 47c is supplied.

工程(2):図10(2)に示すように、第4投入用コンベヤ47dの搬送方向が切り替えられて、第5粉砕設備25e側へ向けられ、第5粉砕設備25eへの炊飯米Rの供給が開始される。第5粉砕設備25eへ投入された炊飯米Rの量と、第4投入用コンベヤ47d上の炊飯米Rの量の合計が、各投入用コンベヤ47a,47b,47c上の各炊飯米Rの量とおおよそ同量になるまで、第5粉砕設備25eへの炊飯米Rの供給が継続される。 Step (2): As shown in FIG. 10 (2), the transport direction of the fourth feeding conveyor 47d is switched and directed to the fifth crushing equipment 25e side, and the cooked rice R to the fifth crushing equipment 25e is used. Supply will start. The total of the amount of cooked rice R charged into the fifth crushing facility 25e and the amount of cooked rice R on the fourth loading conveyor 47d is the amount of each cooked rice R on each of the feeding conveyors 47a, 47b, 47c. The supply of cooked rice R to the fifth crushing facility 25e will be continued until the amount is approximately the same as that of the fifth crushing facility 25e.

工程(3):第5粉砕設備25eへ投入された炊飯米Rの量と、第4投入用コンベヤ47d上の炊飯米Rの量の合計が、各投入用コンベヤ47a,47b,47c上の各炊飯米Rの量とおおよそ同量になると、図10(3)に示すように、投入用コンベヤ47a,47b,47cの搬送方向をそれぞれ逆に切り替えて、投入用コンベヤ47a,47b,47c上の炊飯米Rを粉砕設備25a,25b,25cへ供給する。ここで、第1投入用コンベヤ47aの搬送速度は、粉砕設備25aへの炊飯米Rの供給時に主コンベヤ46からの炊飯米Rの落下を少なくすべく、主コンベヤ46の搬送速度よりも大きいことが好ましい。これにより、工程(1)から(3)で、ほぼ同量の炊飯米Rが各粉砕設備25a,25b,25c,25d,25eに供給される。 Step (3): The total of the amount of rice cooked rice R charged into the fifth crushing facility 25e and the amount of rice cooked rice R on the fourth feeding conveyor 47d is the sum of the amounts of the rice cooked rice R on the feeding conveyors 47a, 47b, 47c, respectively. When the amount is approximately the same as the amount of rice cooked R, as shown in FIG. 10 (3), the transport directions of the charging conveyors 47a, 47b, 47c are switched in the opposite directions, and the charging conveyors 47a, 47b, 47c are placed on the charging conveyors 47a, 47b, 47c. The cooked rice R is supplied to the crushing equipment 25a, 25b, 25c. Here, the transport speed of the first feeding conveyor 47a is higher than the transport speed of the main conveyor 46 in order to reduce the drop of the cooked rice R from the main conveyor 46 when the rice cooked rice R is supplied to the crushing equipment 25a. Is preferable. As a result, in steps (1) to (3), substantially the same amount of cooked rice R is supplied to the crushing facilities 25a, 25b, 25c, 25d, 25e.

上記工程(1)から(3)を繰り返すことで、粉砕設備25a,25b,25c,25d,25eに炊飯米Rが順次振り分けて供給される。なお、投入用コンベヤ47a,47b,47c,47dの搬送方向の切り替え時期は、上記図9の実施形態で説明した構成と同様に、例えば、各コンベヤの駆動時間を計測することで行ってもよいし、主コンベヤ46上の所定位置を通過する炊飯米Rの量を計測する計測器の出力に基づいて行ってもよい。
また、上記工程(1)及び(2)での投入用コンベヤ47a,47b,47c,47dの搬送速度は、主コンベヤ46の搬送速度と同じであってもよいし、それよりも大きくてもよいし、それよりも小さくてもよい。また、上記工程(3)での投入用コンベヤ47b,47c,47dの搬送速度も同様である。
By repeating the above steps (1) to (3), the cooked rice R is sequentially distributed and supplied to the crushing equipment 25a, 25b, 25c, 25d, 25e. The time for switching the transport directions of the loading conveyors 47a, 47b, 47c, and 47d may be, for example, by measuring the drive time of each conveyor in the same manner as in the configuration described in the embodiment of FIG. Then, it may be performed based on the output of the measuring instrument that measures the amount of cooked rice R passing through the predetermined position on the main conveyor 46.
Further, the transport speeds of the loading conveyors 47a, 47b, 47c, 47d in the steps (1) and (2) may be the same as or higher than the transport speed of the main conveyor 46. However, it may be smaller than that. Further, the transfer speeds of the loading conveyors 47b, 47c, 47d in the above step (3) are also the same.

図5から図10を参照しながら説明した実施形態の米ゲル製造システム1では、粉砕部7は並列状態で配置された複数の粉砕設備25として粉砕設備25a,25b,25c,25d,25eを備え、炊飯米搬送部6は、炊飯部5から受け継いだ炊飯米Rを複数の粉砕設備25a,25b,25c,25d,25eに振り分けて供給するので、炊飯部5からの炊飯米Rを複数の粉砕設備25a,25b,25c,25d,25eで並行して粉砕して米ゲルを生産できるので、より高い炊飯米生産能力を有する蒸気式連続炊飯器43(炊飯部5)の導入が可能になり、米ゲル生産能力をより向上できる。 In the rice gel production system 1 of the embodiment described with reference to FIGS. 5 to 10, the crushing unit 7 is provided with crushing equipment 25a, 25b, 25c, 25d, 25e as a plurality of crushing equipment 25 arranged in a parallel state. , The rice cooker transport unit 6 distributes and supplies the rice cooker R inherited from the rice cooker 5 to a plurality of crushing facilities 25a, 25b, 25c, 25d, 25e, so that the rice cooker R from the rice cooker 5 is crushed into a plurality of crushers. Since rice gel can be produced by crushing in parallel with the equipment 25a, 25b, 25c, 25d, 25e, it becomes possible to introduce a steam-type continuous rice cooker 43 (rice cooker 5) having a higher rice-cooking rice production capacity. The rice gel production capacity can be further improved.

また、炊飯米搬送部6は、炊飯部5に連結される主コンベヤ46と、主コンベヤ46に連結されると共に直列連結される複数の投入用コンベヤ47a,47b,47c,47dを備える。主コンベヤ46の搬送下流端の下方に1段目の第1投入用コンベヤ47aの中途部が配置され、投入用コンベヤ47a,47b,47c,47dの両端の下方に、粉砕設備25a,25b,25c,25d,25e又は後段側の投入用コンベヤ47b,47c,47dの中途部が配置される。そして、投入用コンベヤ47a,47b,47c,47dの搬送方向を切り替えることで、炊飯米Rを粉砕設備25a,25b,25c,25d,25eに供給し、又は後段側の投入用コンベヤ47b,47c,47dに供給して、炊飯米Rを複数の粉砕設備25a,25b,25c,25d,25e又に振り分けて供給する。これにより、簡単な構成で炊飯米Rを複数の粉砕設備25a,25b,25c,25d,25eへ振り分けて供給できる。 Further, the rice-cooking rice transport unit 6 includes a main conveyor 46 connected to the rice-cooking unit 5, and a plurality of feeding conveyors 47a, 47b, 47c, 47d connected to the main conveyor 46 and connected in series. The middle part of the first loading conveyor 47a of the first stage is arranged below the transport downstream end of the main conveyor 46, and the crushing equipment 25a, 25b, 25c is located below both ends of the loading conveyors 47a, 47b, 47c, 47d. , 25d, 25e or the middle part of the loading conveyors 47b, 47c, 47d on the rear stage side is arranged. Then, by switching the transport direction of the charging conveyors 47a, 47b, 47c, 47d, the cooked rice R is supplied to the crushing equipment 25a, 25b, 25c, 25d, 25e, or the charging conveyors 47b, 47c, on the rear stage side. It is supplied to 47d, and the cooked rice R is distributed and supplied to a plurality of crushing facilities 25a, 25b, 25c, 25d, 25e. As a result, the cooked rice R can be distributed and supplied to a plurality of crushing facilities 25a, 25b, 25c, 25d, 25e with a simple configuration.

また、炊飯部5は、浸漬米(原料米)をコンベヤで搬送しながら蒸煮する連続炊飯装置43により構成されるので、例えばコンベヤで搬送される複数の炊飯釜Aで炊飯する連続式炊飯機21(図1等参照)に比べて、炊飯米Rの生産能力を向上でき、ひいては米ゲル生産能力をより向上できる。 Further, since the rice cooker 5 is composed of a continuous rice cooker 43 that steams and steams the soaked rice (raw rice) while being conveyed by the conveyor, for example, the continuous rice cooker 21 that cooks rice in a plurality of rice cookers A conveyed by the conveyor. Compared with (see FIG. 1 and the like), the production capacity of cooked rice R can be improved, and the rice gel production capacity can be further improved.

次に、図11及び図12を参照しながら、米ゲル製造システムのさらに他の実施形態を説明する。この実施形態の米ゲル製造システムは、炊飯部5に連続炊飯装置43を備え、炊飯米搬送部6に複数の投入用コンベヤ61を備え、粉砕部7は並列状態で配置された複数の粉砕設備25を備える。その他の構成は、図5等を参照して説明した上記実施形態の米ゲル製造システム1と同様である。 Next, still another embodiment of the rice gel production system will be described with reference to FIGS. 11 and 12. In the rice gel manufacturing system of this embodiment, the rice cooking unit 5 is provided with a continuous rice cooking device 43, the rice cooking rice transport unit 6 is provided with a plurality of feeding conveyors 61, and the crushing unit 7 is a plurality of crushing equipment arranged in a parallel state. 25 is provided. Other configurations are the same as those of the rice gel production system 1 of the above-described embodiment described with reference to FIG. 5 and the like.

この実施形態の米ゲル製造システムでは、並列配置される複数の投入用コンベヤ61の各搬送上流端部が、連続炊飯装置43の炊飯米排出コンベヤ44の搬送下流端の下方に配置される。この実施形態では、5本の投入用コンベヤ61が設けられる。炊飯米排出コンベヤ44の搬送下流端と、投入用コンベヤ61の搬送上流端部の間には、炊飯米排出コンベヤ44から排出される炊飯米Rを5本の投入用コンベヤ61にほぼ均等に振り分ける複数の振り分け部材62が配置される。 In the rice gel manufacturing system of this embodiment, each transport upstream end of the plurality of feeding conveyors 61 arranged in parallel is arranged below the transport downstream end of the rice cooking rice discharge conveyor 44 of the continuous rice cooking device 43. In this embodiment, five loading conveyors 61 are provided. The cooked rice R discharged from the cooked rice discharge conveyor 44 is distributed substantially evenly between the downstream end of the rice cooked rice discharge conveyor 44 and the upstream end of the rice cooked rice discharge conveyor 61. A plurality of distribution members 62 are arranged.

振り分け部材62は、炊飯米排出コンベヤ44に向けて突出する板状突起部を備え、炊飯米排出コンベヤ44の幅方向全体に存在する炊飯米Rが搬送下流端から落下する際に各投入用コンベヤ61上に載るように、炊飯米Rを分割する。各投入用コンベヤ61の搬送下流端の下方に、それぞれ粉砕設備25が配置される。この実施形態では5台の粉砕設備25が並列状態で配置される。また、各粉砕設備25の粉砕処理能力は同じである。 The sorting member 62 is provided with a plate-shaped protrusion that protrudes toward the cooked rice discharge conveyor 44, and is a conveyor for feeding rice when the cooked rice R existing in the entire width direction of the cooked rice discharge conveyor 44 falls from the downstream end of the transport. The cooked rice R is divided so as to be placed on 61. The crushing equipment 25 is arranged below the transport downstream end of each loading conveyor 61. In this embodiment, five crushing facilities 25 are arranged in parallel. Further, the crushing processing capacity of each crushing facility 25 is the same.

連続炊飯装置43で炊飯される炊飯米Rは、炊飯米排出コンベヤ44の搬送下流端から排出されて、投入用コンベヤ61へ向けて落下する。排出される炊飯米Rの温度は95度程度である。炊飯米排出コンベヤ44の搬送下流端から落下する炊飯米Rは、隣り合う投入用コンベヤ61間に配置される振り分け部材62により分割されて、各投入用コンベヤ61に振り分けて供給される。 The cooked rice R cooked by the continuous rice cooker 43 is discharged from the transport downstream end of the cooked rice discharge conveyor 44 and falls toward the input conveyor 61. The temperature of the discharged rice cooked rice R is about 95 degrees. The cooked rice R that falls from the transport downstream end of the cooked rice discharge conveyor 44 is divided by the sorting member 62 arranged between the adjacent feeding conveyors 61, and is distributed and supplied to each feeding conveyor 61.

投入用コンベヤ61に供給された炊飯米Rは、投入用コンベヤ61ごとに搬送されて、各粉砕設備25に供給される。粉砕設備25に供給される炊飯米Rの温度は、老化する温度よりも高い温度であり、ここでは85度程度である。各粉砕設備25は、炊飯米Rを粉砕して米ゲルにして、その米ゲルを米ゲルホッパー48に供給する。米ゲルホッパー48に供給される米ゲルは、移送ポンプ26により、米ゲル移送配管27を介してゲル収容部9(図5等参照)へ移送される。 The cooked rice R supplied to the charging conveyor 61 is conveyed to each charging conveyor 61 and supplied to each crushing facility 25. The temperature of the cooked rice R supplied to the crushing facility 25 is higher than the aging temperature, and is about 85 degrees here. Each crushing facility 25 crushes the cooked rice R into rice gel, and supplies the rice gel to the rice gel hopper 48. The rice gel supplied to the rice gel hopper 48 is transferred to the gel accommodating portion 9 (see FIG. 5 and the like) via the rice gel transfer pipe 27 by the transfer pump 26.

この実施形態の米ゲル製造システムでは、粉砕部7は並列状態で配置された5台(複数)の粉砕設備25を備え、炊飯米搬送部6は、炊飯部5から受け継いだ炊飯米Rを5台の粉砕設備25に振り分けて供給するので、炊飯部5からの炊飯米Rを5台の粉砕設備25で並行して粉砕して米ゲルを生産でき、より高い炊飯米生産能力を有する蒸気式連続炊飯器43(炊飯部5)の導入が可能になり、米ゲル生産能力をより向上できる。 In the rice gel production system of this embodiment, the crushing unit 7 is provided with five (plural) crushing facilities 25 arranged in parallel, and the rice cooker transport unit 6 uses the rice cooker R inherited from the rice cooker unit 5. Since the rice is distributed and supplied to the rice cooker 25, the rice cooker R from the rice cooker 5 can be crushed in parallel by the five rice cookers 25 to produce rice gel, and the steam type has a higher rice cooking capacity. The continuous rice cooker 43 (rice cooker 5) can be introduced, and the rice gel production capacity can be further improved.

また、この実施形態の米ゲル製造システムでは、炊飯米搬送部6は炊飯部5にそれぞれ連結されると共に並列配置される5本(複数)の投入用コンベヤ61を備え、粉砕部7は複数の粉砕設備25を備え、各投入用コンベヤ61の搬送下流端の下方にそれぞれ粉砕設備25が配置される。これにより、簡単な構成で炊飯米Rを複数の粉砕設備25へ振り分けて供給できると共に、複数の粉砕設備25で並列して米ゲルを生産できる。 Further, in the rice gel manufacturing system of this embodiment, the rice-cooking rice transport section 6 is provided with five (plural) loading conveyors 61 connected to the rice-cooking section 5 and arranged in parallel, and the crushing section 7 is a plurality. The crushing equipment 25 is provided, and the crushing equipment 25 is arranged below the transport downstream end of each input conveyor 61. As a result, the cooked rice R can be distributed and supplied to a plurality of crushing facilities 25 with a simple configuration, and rice gel can be produced in parallel by the plurality of crushing facilities 25.

上記実施形態では、連続炊飯装置43から排出される炊飯米Rをコンベヤにより搬送しているが、例えば、炊飯米Rを一軸偏心ねじポンプ(モーノポンプ)により移送してもよい。この場合、炊飯米Rを一軸偏心ねじポンプにより移送管を介して複数の粉砕設備25に向けて移送すると共に、該移送管の中途部に切り替えバルブ及び枝別れ移送管を設けて、該切り替えバルブの切り替えにより、炊飯米Rを複数の粉砕設備25に振り分けて供給する。ここで、移送管は、例えばステンレス鋼管で構成され、炊飯米を移送する際の炊飯米の温度低下が抑制される。これにより、老化する温度よりも高い温度(例えば85度以上)の炊飯米が各粉砕設備25に供給され、炊飯米の老化に起因する粉砕設備25の負荷増大が抑制される。 In the above embodiment, the cooked rice R discharged from the continuous rice cooker 43 is conveyed by a conveyor, but for example, the cooked rice R may be transferred by a uniaxial eccentric screw pump (mono pump). In this case, the rice cooked rice R is transferred to a plurality of crushing facilities 25 via a transfer pipe by a uniaxial eccentric screw pump, and a switching valve and a branching transfer pipe are provided in the middle of the transfer pipe to provide the switching valve. By switching between, the cooked rice R is distributed and supplied to a plurality of crushing facilities 25. Here, the transfer pipe is made of, for example, a stainless steel pipe, and the temperature drop of the cooked rice when the cooked rice is transferred is suppressed. As a result, the rice cooked rice having a temperature higher than the aging temperature (for example, 85 degrees or more) is supplied to each crushing facility 25, and the increase in the load of the crushing facility 25 due to the aging of the rice cooked rice is suppressed.

なお、粉砕部7が複数の粉砕設備25を備える構成において、粉砕設備25で生産される米ゲルを複数台の移送ポンプ26でゲル収容部9へ移送するようにしてもよい。また、移送部8で米ゲルを移送するための移送装置は、一軸偏心ねじポンプで構成される移送ポンプ26に限定されず、米ゲルを移送可能な移送装置であればよく、例えば渦巻ポンプ等であってもよい。また、移送部8が米ゲルを移送する方法は、ポンプを用いる移送方法に限定されず、移送部8は、米ゲルを粉砕部7からゲル収容部9へ移送可能な構成であればよい。例えば、移送部8は、コンベヤ等の搬送装置により、米ゲルを粉砕部7からゲル収容部9へ移送する構成であってもよい。 In a configuration in which the crushing unit 7 is provided with a plurality of crushing equipment 25, the rice gel produced by the crushing equipment 25 may be transferred to the gel storage unit 9 by a plurality of transfer pumps 26. Further, the transfer device for transferring the rice gel in the transfer unit 8 is not limited to the transfer pump 26 composed of the uniaxial eccentric screw pump, and may be any transfer device capable of transferring the rice gel, for example, a centrifugal pump or the like. May be. Further, the method of transferring the rice gel by the transfer unit 8 is not limited to the transfer method using a pump, and the transfer unit 8 may have a configuration in which the rice gel can be transferred from the crushing unit 7 to the gel storage unit 9. For example, the transfer unit 8 may be configured to transfer the rice gel from the crushing unit 7 to the gel storage unit 9 by a transfer device such as a conveyor.

次に、図13を参照しながら、米ゲル製造システムのさらに他の実施形態を説明する。この実施形態の米ゲル製造システムは、炊飯部5に連続炊飯装置43を備え、炊飯米搬送部6にコンベヤ45,71,72a,72b,72c,72d,72eと振り分け部材73a,73b,73c,73dと制御装置74を備え、粉砕部7に複数の粉砕設備25a,25b,25c,25d,25eを備える。その他の構成は、図5等を参照して説明した上記実施形態の米ゲル製造システム1と同様である。 Next, still another embodiment of the rice gel production system will be described with reference to FIG. In the rice gel production system of this embodiment, the rice cooking unit 5 is provided with a continuous rice cooking device 43, and the rice cooking rice transport unit 6 is provided with conveyors 45, 71, 72a, 72b, 72c, 72d, 72e and sorting members 73a, 73b, 73c, A 73d and a control device 74 are provided, and a plurality of crushing facilities 25a, 25b, 25c, 25d, 25e are provided in the crushing unit 7. Other configurations are the same as those of the rice gel production system 1 of the above-described embodiment described with reference to FIG. 5 and the like.

この実施形態の米ゲル製造システムでは、連続炊飯装置43の炊飯米排出コンベヤ44の搬送下流端の下方に、炊飯米を受け継ぐコンベヤ45が配置され、コンベヤ45の搬送下流端に主コンベヤ71の搬送上流部が連結される。主コンベヤ71の搬送中途部の側方に、第1から第4の投入用コンベヤ72a,72b,72c,72dの搬送上流端側が配置され、主コンベヤ71の搬送下流端に第5投入用コンベヤ72eの搬送上流部が連結される。各投入用コンベヤ72a,72b,72c,72d,72eの搬送下流端の下方に、粉砕部7の第1から第5の粉砕設備25a,25b,25c,25d,25eが配置される。 In the rice gel production system of this embodiment, a conveyor 45 that inherits the cooked rice is arranged below the transport downstream end of the rice-cooking rice discharge conveyor 44 of the continuous rice-cooking device 43, and the main conveyor 71 is transported at the transport downstream end of the conveyor 45. The upstream part is connected. The transport upstream ends of the first to fourth loading conveyors 72a, 72b, 72c, 72d are arranged on the side of the transport intermediate portion of the main conveyor 71, and the fifth loading conveyor 72e is arranged at the transport downstream end of the main conveyor 71. The upstream part of the conveyor is connected. Below the transport downstream ends of the loading conveyors 72a, 72b, 72c, 72d, 72e, the first to fifth crushing facilities 25a, 25b, 25c, 25d, 25e of the crushing section 7 are arranged.

炊飯米搬送部6には、主コンベヤ71上で搬送される炊飯米を第1から第4の投入用コンベヤ72a,72b,72c,72d側へ落下させる第1から第4の振り分け部材73a,73b,73c,73dが設けられる。各振り分け部材73a,73b,73c,73dは、主コンベヤ71上で炊飯米の搬送経路上に配置される遮蔽位置(二点鎖線位置)と、炊飯米の搬送経路から外れた退避位置(実線位置)の間で、それぞれ移動可能に設けられる。振り分け部材73a,73b,73c,73dは、制御装置74によって動作制御される振り分け部材移動機構(図示省略)の作動により、遮蔽位置と退避位置の間で移動される。振り分け部材73a,73b,73c,73dは、遮蔽位置では、主コンベヤ71の搬送方向に対して傾斜して配置される。 In the rice-cooking rice transport unit 6, the first to fourth sorting members 73a, 73b for dropping the cooked rice conveyed on the main conveyor 71 to the first to fourth feeding conveyors 72a, 72b, 72c, 72d side. , 73c, 73d are provided. Each of the distribution members 73a, 73b, 73c, 73d has a shielding position (two-dot chain line position) arranged on the rice-cooked rice transport path on the main conveyor 71 and a retracted position (solid line position) deviated from the rice-cooked rice transport path. ), Each is provided so as to be movable. The distribution members 73a, 73b, 73c, 73d are moved between the shielded position and the retracted position by the operation of the distribution member moving mechanism (not shown) whose operation is controlled by the control device 74. The distribution members 73a, 73b, 73c, 73d are arranged so as to be inclined with respect to the transport direction of the main conveyor 71 at the shielding position.

連続炊飯装置43で炊飯される炊飯米は、炊飯米排出コンベヤ44の搬送下流端から排出されて、炊飯米搬送部6のコンベヤ45上に落下し、コンベヤ45により主コンベヤ71の搬送上流部に搬送される。主コンベヤ71は、コンベヤ45から受け継いだ炊飯米を搬送下流側へ向けて順次搬送する。 The cooked rice cooked by the continuous rice cooking device 43 is discharged from the transport downstream end of the rice cooked rice discharge conveyor 44, falls on the conveyor 45 of the rice cooked rice transport section 6, and is moved to the transport upstream portion of the main conveyor 71 by the conveyor 45. Be transported. The main conveyor 71 sequentially conveys the cooked rice inherited from the conveyor 45 toward the downstream side of the conveyor.

炊飯米搬送部6は、主コンベヤ71で搬送される炊飯米を、投入用コンベヤ72a,72b,72c,72d,72eに振り分けて供給し、ひいては粉砕設備25a,25b,25c,25d,25eに振り分けて供給する。炊飯米を第1投入用コンベヤ72aに供給する場合、制御装置74の制御により第1振り分け部材73aが主コンベヤ71上の遮蔽位置に配置される。主コンベヤ71上を搬送される炊飯米は、搬送方向に対して傾斜配置される第1振り分け部材73aに接触し、主コンベヤ71上を搬送されながら第1振り分け部材73aに沿って第1投入用コンベヤ72a側へ移動し、第1投入用コンベヤ72aの搬送上流部の上に落下する。第1投入用コンベヤ72aに受け継がれた炊飯米は、第1投入用コンベヤ72aの作動により第1粉砕設備25aに供給される。 The cooked rice transport unit 6 distributes and supplies the cooked rice conveyed by the main conveyor 71 to the feeding conveyors 72a, 72b, 72c, 72d, 72e, and eventually distributes the rice to the crushing equipment 25a, 25b, 25c, 25d, 25e. And supply. When the cooked rice is supplied to the first feeding conveyor 72a, the first sorting member 73a is arranged at a shielding position on the main conveyor 71 under the control of the control device 74. The cooked rice transported on the main conveyor 71 comes into contact with the first distribution member 73a which is inclined with respect to the transport direction, and is conveyed on the main conveyor 71 for the first feeding along the first distribution member 73a. It moves to the conveyor 72a side and falls on the transport upstream portion of the first loading conveyor 72a. The cooked rice inherited by the first feeding conveyor 72a is supplied to the first crushing facility 25a by the operation of the first feeding conveyor 72a.

所定量の炊飯米が第1投入用コンベヤ72aに供給されると、制御装置74は、第1振り分け部材73aを退避位置へ移動させ、第2振り分け部材73bを主コンベヤ71上の遮蔽位置に配置する。主コンベヤ71の搬送によって第2振り分け部材73bに到達した炊飯米は、主コンベヤ71上を搬送されながら第2振り分け部材73bに沿って第2投入用コンベヤ72b側へ移動し、第2投入用コンベヤ72bの搬送上流部の上に落下する。第2投入用コンベヤ72bに受け継がれた炊飯米は、第2投入用コンベヤ72bの作動により第2粉砕設備25bに供給される。 When a predetermined amount of cooked rice is supplied to the first feeding conveyor 72a, the control device 74 moves the first sorting member 73a to the retracted position and arranges the second sorting member 73b at the shielding position on the main conveyor 71. do. The cooked rice that has reached the second sorting member 73b by the transport of the main conveyor 71 moves to the second feeding conveyor 72b side along the second sorting member 73b while being conveyed on the main conveyor 71, and is moved to the second feeding conveyor 72b side. It falls on the transport upstream part of 72b. The cooked rice inherited by the second feeding conveyor 72b is supplied to the second crushing facility 25b by the operation of the second feeding conveyor 72b.

所定量の炊飯米が第2投入用コンベヤ72bに供給されると、制御装置74は、第2振り分け部材73bを退避位置へ移動させ、第3振り分け部材73cを主コンベヤ71上の遮蔽位置に配置する。このとき、第1振り分け部材73aは退避位置に配置される。主コンベヤ71の搬送によって第3振り分け部材73cに到達した炊飯米は、主コンベヤ71上を搬送されながら第3振り分け部材73cに沿って第3投入用コンベヤ72c側へ移動し、第3投入用コンベヤ72cの搬送上流部の上に落下する。第3投入用コンベヤ72cに受け継がれた炊飯米は、第3投入用コンベヤ72cの作動により第3粉砕設備25cに供給される。 When a predetermined amount of cooked rice is supplied to the second feeding conveyor 72b, the control device 74 moves the second sorting member 73b to the retracted position and arranges the third sorting member 73c at the shielding position on the main conveyor 71. do. At this time, the first distribution member 73a is arranged at the retracted position. The cooked rice that has reached the third distribution member 73c by the transfer of the main conveyor 71 moves to the third input conveyor 72c side along the third distribution member 73c while being conveyed on the main conveyor 71, and moves to the third input conveyor 72c side. It falls on the upstream part of the conveyor of 72c. The cooked rice inherited by the third feeding conveyor 72c is supplied to the third crushing facility 25c by the operation of the third feeding conveyor 72c.

所定量の炊飯米が第3投入用コンベヤ72cに供給されると、制御装置74は、第3振り分け部材73cを退避位置へ移動させ、第4振り分け部材73dを主コンベヤ71上の遮蔽位置に配置する。このとき、第1及び第2の振り分け部材73a,73bは退避位置に配置される。主コンベヤ71の搬送によって第4振り分け部材73dに到達した炊飯米は、主コンベヤ71上を搬送されながら第4振り分け部材73dに沿って第4投入用コンベヤ72d側へ移動し、第4投入用コンベヤ72dの搬送上流部の上に落下する。第4投入用コンベヤ72dに受け継がれた炊飯米は、第4投入用コンベヤ72dの作動により第4粉砕設備25dに供給される。 When a predetermined amount of cooked rice is supplied to the third feeding conveyor 72c, the control device 74 moves the third sorting member 73c to the retracted position and arranges the fourth sorting member 73d at the shielding position on the main conveyor 71. do. At this time, the first and second distribution members 73a and 73b are arranged at the retracted positions. The cooked rice that has reached the 4th distribution member 73d by the transfer of the main conveyor 71 moves to the 4th input conveyor 72d side along the 4th distribution member 73d while being conveyed on the main conveyor 71, and moves to the 4th input conveyor 72d side. It falls on the upstream part of the conveyor of 72d. The cooked rice inherited by the fourth feeding conveyor 72d is supplied to the fourth crushing facility 25d by the operation of the fourth feeding conveyor 72d.

所定量の炊飯米が第4投入用コンベヤ72dに供給されると、制御装置74は、第4振り分け部材73dを退避位置へ移動させ、第1から第4の振り分け部材73a,73b,73c,73dを退避位置に配置する。主コンベヤ71で搬送される炊飯米は、主コンベヤ71の搬送下流端から第5投入用コンベヤ72eの搬送上流部の上に落下する。第5投入用コンベヤ72eに受け継がれた炊飯米は、第5投入用コンベヤ72eの作動により第5粉砕設備25eに供給される。第5投入用コンベヤ72eに供給された炊飯米の量と、第1振り分け部材73aの遮蔽位置の下流側で主コンベヤ71上に載っている炊飯米の量の合計が所定量になると、制御装置74は第1振り分け部材73aを遮蔽位置に配置して、第1投入用コンベヤ72aへの炊飯米の供給を開始する。 When a predetermined amount of cooked rice is supplied to the fourth feeding conveyor 72d, the control device 74 moves the fourth sorting member 73d to the retracted position, and the first to fourth sorting members 73a, 73b, 73c, 73d. Is placed in the retracted position. The cooked rice conveyed by the main conveyor 71 falls from the downstream end of the main conveyor 71 onto the upstream portion of the fifth feeding conveyor 72e. The cooked rice inherited by the fifth feeding conveyor 72e is supplied to the fifth crushing facility 25e by the operation of the fifth feeding conveyor 72e. When the sum of the amount of cooked rice supplied to the fifth feeding conveyor 72e and the amount of cooked rice placed on the main conveyor 71 on the downstream side of the shielding position of the first sorting member 73a reaches a predetermined amount, the control device. 74 arranges the first sorting member 73a at a shielded position, and starts supplying cooked rice to the first feeding conveyor 72a.

なお、振り分け部材73a,73b,73c,73dの移動時期は、例えば、主コンベヤ71の駆動時間を計測することで行う。また、主コンベヤ71上の搬送上流側を通過する炊飯米の量を計測する計測器を設けて、その計測器の出力に基づいて振り分け部材73a,73b,73c,73dの移動時期を制御してもよい。 The movement timing of the distribution members 73a, 73b, 73c, 73d is determined by, for example, measuring the drive time of the main conveyor 71. Further, a measuring instrument for measuring the amount of cooked rice passing through the upstream side of the transport on the main conveyor 71 is provided, and the movement timing of the distribution members 73a, 73b, 73c, 73d is controlled based on the output of the measuring instrument. May be good.

このようにして、炊飯米は、炊飯米搬送部6により、粉砕部7の粉砕設備25a,25b,25c,25d,25eに振り分けて供給される。ここで、粉砕設備25a,25b,25c,25d,25eに供給される炊飯米の温度は、老化する温度よりも高い温度であり、ここでは85度程度である。 In this way, the cooked rice is distributed and supplied by the cooked rice transport unit 6 to the crushing equipment 25a, 25b, 25c, 25d, 25e of the crushing unit 7. Here, the temperature of the cooked rice supplied to the crushing equipment 25a, 25b, 25c, 25d, 25e is higher than the aging temperature, and is about 85 degrees here.

この実施形態の米ゲル製造システムでは、炊飯米搬送部6は、主コンベヤ71と、5本(複数)の投入用コンベヤ72a,72b,72c,72d,72eと、主コンベヤ71で搬送される炊飯米を投入用コンベヤ72a,72b,72c,72d,72eに振り分ける振り分け機構(振り分け部材73a,73b,73c,73d)を備え、粉砕部7は、投入用コンベヤ72a,72b,72c,72d,72eの搬送下流端に連結される5台(複数)の粉砕設備25a,25b,25c,25d,25eを備える。これにより、簡単な構成で炊飯米を複数の粉砕設備25へ振り分けて供給できると共に、複数の粉砕設備25a,25b,25c,25d,25eで並列して米ゲルを生産でき、米ゲルの生産能力を向上できる。 In the rice gel production system of this embodiment, the rice-cooking rice transport unit 6 includes a main conveyor 71, five (plural) charging conveyors 72a, 72b, 72c, 72d, 72e, and rice-cooking rice conveyed by the main conveyor 71. A distribution mechanism (distribution members 73a, 73b, 73c, 73d) for distributing rice to the charging conveyors 72a, 72b, 72c, 72d, 72e is provided, and the crushing unit 7 is a charging conveyor 72a, 72b, 72c, 72d, 72e. It is equipped with five crushing facilities 25a, 25b, 25c, 25d, 25e connected to the downstream end of the conveyor. As a result, rice cooked rice can be distributed and supplied to a plurality of crushing facilities 25 with a simple configuration, and rice gel can be produced in parallel by a plurality of crushing facilities 25a, 25b, 25c, 25d, 25e, and the rice gel production capacity can be achieved. Can be improved.

なお、この実施形態の炊飯米搬送部6において、炊飯米を投入用コンベヤ72a,72b,72c,72d,72eに振り分けて供給する順番は、特に限定されない。また、図13に示した炊飯米搬送部6における振り分け機構の構成は一例であり、振り分け部材73a,73b,73c,73dの移動方向や配置は特に限定されない。例えば、振り分け部材73a,73b,73c,73dは、上下方向に移動可能に設けられて、主コンベヤ71の上方で、遮蔽位置と退避位置の間を移動する構成であってもよいし、水平方向で回動可能に設けられて、主コンベヤ71上の遮蔽位置と主コンベヤ71上から外れた退避位置の間を移動する構成であってもよい。 In the cooked rice transport unit 6 of this embodiment, the order in which the cooked rice is distributed and supplied to the feeding conveyors 72a, 72b, 72c, 72d, 72e is not particularly limited. Further, the configuration of the distribution mechanism in the cooked rice transport unit 6 shown in FIG. 13 is an example, and the moving direction and arrangement of the distribution members 73a, 73b, 73c, 73d are not particularly limited. For example, the distribution members 73a, 73b, 73c, 73d may be provided so as to be movable in the vertical direction and may be configured to move between the shielding position and the retracting position above the main conveyor 71, or may be in the horizontal direction. It may be configured to be rotatably provided and move between a shielding position on the main conveyor 71 and a retracting position off the main conveyor 71.

また、粉砕部7が複数の粉砕設備25を備える構成において、炊飯米搬送部6が炊飯米を複数の粉砕設備25に振り分ける構成は、図7に示した構成や、図11及び図12に示した構成や、図13に示した構成に限定されず、炊飯部5から受け継いだ炊飯米を複数の粉砕設備25に振り分けて供給可能な構成であれば、どのような構成であってもよい。また、投入用コンベヤの本数や、並列状態で配置された粉砕設備の台数は、上記実施形態に限定されず、炊飯部5の炊飯米生産能力や、粉砕部7での粉砕設備25の粉砕処理能力に応じて、適宜変更可能である。 Further, in the configuration in which the crushing unit 7 includes a plurality of crushing equipment 25, the configuration in which the cooked rice transport unit 6 distributes the cooked rice to the plurality of crushing equipment 25 is shown in the configuration shown in FIG. 7 and in FIGS. 11 and 12. The configuration is not limited to the above configuration and the configuration shown in FIG. 13, and any configuration may be used as long as the cooked rice inherited from the rice cooking unit 5 can be distributed and supplied to a plurality of crushing facilities 25. Further, the number of input conveyors and the number of crushing equipment arranged in parallel are not limited to the above-described embodiment, and the rice cooking capacity of the rice cooking unit 5 and the crushing process of the crushing equipment 25 in the crushing unit 7 are performed. It can be changed as appropriate according to the ability.

また、複数の炊飯釜Aを用いて連続的に炊飯する炊飯部5を備える構成において、複数の粉砕設備25を備えると共に、炊飯釜Aから取り出す炊飯米を複数の粉砕設備25に振り分けて供給する炊飯米搬送部6を備えるようにしてもよい。例えば、炊飯釜Aから取り出した炊飯米をほぐすほぐし機24(図1及び図2参照)の下方に、粉砕設備25に替えて主コンベヤ46(図5から図10参照)を配置し、炊飯釜Aからほぐし機24を介して供給される炊飯米を複数の投入用コンベヤ47a,47b,47c,47dで複数の粉砕設備25a,25b,25c,25d,25eに振り分けて供給してもよい。ここで、炊飯釜A内の炊飯米の量に応じて、投入用コンベヤの本数及び粉砕設備の台数を減らすことも可能である。 Further, in a configuration including a rice cooking unit 5 for continuously cooking rice using a plurality of rice cooking pots A, a plurality of crushing facilities 25 are provided, and the cooked rice taken out from the rice cooking pot A is distributed and supplied to the plurality of crushing facilities 25. The cooked rice transport unit 6 may be provided. For example, a main conveyor 46 (see FIGS. 5 to 10) is placed below the rice cooker 24 (see FIGS. 1 and 2) to loosen the cooked rice taken out from the rice cooker A in place of the crushing equipment 25. The cooked rice supplied from A via the loosening machine 24 may be distributed and supplied to a plurality of crushing facilities 25a, 25b, 25c, 25d, 25e by a plurality of input conveyors 47a, 47b, 47c, 47d. Here, it is possible to reduce the number of feeding conveyors and the number of crushing facilities according to the amount of cooked rice in the rice cooker A.

次に、図14及び図15を参照しながら、米ゲル製造システムのさらに他の実施形態を説明する。この実施形態の米ゲル製造システム1は、炊飯部5に連続炊飯装置43を備え、炊飯米搬送部6にコンベヤ45と投入用コンベヤ81を備え、粉砕部7に1台の粉砕設備82を備える。その他の構成は、図5等を参照して説明した上記実施形態の米ゲル製造システム1と同様である。 Next, still another embodiment of the rice gel production system will be described with reference to FIGS. 14 and 15. In the rice gel manufacturing system 1 of this embodiment, the rice cooking unit 5 is provided with a continuous rice cooking device 43, the rice cooking rice transport unit 6 is provided with a conveyor 45 and a feeding conveyor 81, and the crushing unit 7 is provided with one crushing facility 82. .. Other configurations are the same as those of the rice gel production system 1 of the above-described embodiment described with reference to FIG. 5 and the like.

この実施形態の米ゲル製造システム1では、連続炊飯装置43の炊飯米排出コンベヤ44の搬送下流端の下方に、炊飯米を受け継ぐコンベヤ45が配置され、コンベヤ45の搬送下流端に投入用コンベヤ81の搬送上流部が連結される。炊飯米搬送部6は、炊飯部5の連続炊飯装置43から排出される炊飯米を受け継いで、コンベヤ45,81の作動により、大型の粉砕設備82へ搬送する。 In the rice gel manufacturing system 1 of this embodiment, a conveyor 45 that inherits the cooked rice is arranged below the transport downstream end of the rice cooked rice discharge conveyor 44 of the continuous rice cooker 43, and a feeding conveyor 81 is arranged at the transport downstream end of the conveyor 45. The upstream part of the conveyor is connected. The cooked rice transport unit 6 inherits the cooked rice discharged from the continuous rice cooker 43 of the rice cooker 5, and transports the cooked rice to the large crushing facility 82 by the operation of the conveyors 45 and 81.

粉砕設備82は、粉砕処理速度(粉砕能力)が大きいものであり、連続炊飯装置43から排出される炊飯米を滞留させることなく粉砕して米ゲルを生産可能な粉砕処理速度を有する。換言すれば、粉砕設備82が単位時間あたりに粉砕可能な炊飯米の量は、単位時間あたりに炊飯部5(連続炊飯装置43)から排出される炊飯米の量よりも多い。粉砕設備82で得られる米ゲルは、米ゲル移送部8の米ゲルホッパー48を介して移送ポンプ26に供給され、移送ポンプ26により米ゲル移送配管27を介してゲル収容部9へ移送される。 The crushing equipment 82 has a high crushing processing speed (crushing capacity), and has a crushing processing speed capable of producing rice gel by crushing the cooked rice discharged from the continuous rice cooking device 43 without retaining the rice. In other words, the amount of cooked rice that can be crushed by the crushing equipment 82 per unit time is larger than the amount of cooked rice discharged from the rice cooking unit 5 (continuous rice cooking device 43) per unit time. The rice gel obtained in the crushing facility 82 is supplied to the transfer pump 26 via the rice gel hopper 48 of the rice gel transfer section 8, and is transferred to the gel storage section 9 by the transfer pump 26 via the rice gel transfer pipe 27. ..

このように、この実施形態の米ゲル製造システム1では、粉砕部7は1台の粉砕設備82で炊飯米を粉砕して米ゲルを得るので、粉砕部7に複数の粉砕設備が設置される場合に比べて、炊飯米搬送部6及び粉砕部7の構成が単純になると共に、それらの設置空間を小さくできる。なお、この実施形態において、コンベヤ45の搬送下流端の下方に粉砕設備82を配置して、投入用コンベヤ81を省略すれば、炊飯米搬送部6の構成より単純にできる。 As described above, in the rice gel production system 1 of this embodiment, since the crushing unit 7 crushes the cooked rice with one crushing facility 82 to obtain the rice gel, a plurality of crushing devices are installed in the crushing unit 7. Compared with the case, the configuration of the rice cooking rice transport unit 6 and the crushing unit 7 can be simplified and the installation space for them can be reduced. In this embodiment, if the crushing equipment 82 is arranged below the downstream end of the conveyor 45 and the feeding conveyor 81 is omitted, the configuration of the rice cooking rice transport unit 6 can be simplified.

以上、実施形態を説明したが、本発明は、前述の実施形態に限らず、様々な態様に具体化できる。各部の構成は図示の実施形態に限定されるものではなく、本発明の趣旨を逸脱しない範囲で種々変更が可能である。 Although the embodiments have been described above, the present invention can be embodied in various embodiments without being limited to the above-described embodiments. The configuration of each part is not limited to the illustrated embodiment, and various changes can be made without departing from the spirit of the present invention.

例えば、上記実施形態では、炊飯部5は連続式炊飯機21又は連続炊飯装置43で構成されるが、米ゲル製造システム1において、炊飯部5は、原料米を炊飯又は蒸煮して炊飯米を得られる構成であればよく、例えば、浸漬米(原料米)をコンベヤで搬送しながら蒸煮して蒸米を得る連続式蒸米機であってもよい。 For example, in the above embodiment, the rice cooker 5 is composed of a continuous rice cooker 21 or a continuous rice cooker 43, but in the rice gel production system 1, the rice cooker 5 cooks or steams raw rice to cook rice. Any structure may be used as long as it can be obtained, and for example, a continuous rice cooker may be used in which the soaked rice (raw rice) is steamed while being conveyed by a conveyor to obtain steamed rice.

また、実施形態の米ゲル製造システムで使用する原料米は、欠け米や割れ米等のいわゆる屑米であってもよい。安価な屑米を原料米として使用すれば、米ゲルの製造コストを低減できる。なお、実施形態の米ゲル製造システムでは、原料米が炊飯されて得られる炊飯米は、そのまま出荷されるのではなく、粉砕部で粉砕されて米ゲルにされるので、原料米が屑米であっても何ら問題はない。 Further, the raw material rice used in the rice gel production system of the embodiment may be so-called scrap rice such as chipped rice or cracked rice. If inexpensive waste rice is used as the raw material rice, the production cost of rice gel can be reduced. In the rice gel production system of the embodiment, the cooked rice obtained by cooking the raw rice is not shipped as it is, but is crushed in the crushing section to make a rice gel, so that the raw rice is scrap rice. There is no problem even if there is.

上記実施形態では、粉砕設備25を、前段の第1粉砕部100Aと後段の第2粉砕部100Bとを有する2段式に構成したが、これら前後の粉砕部に対して、さらに粉砕部を直列で配置して、3段式以上に構成しても構わない。 In the above embodiment, the crushing equipment 25 is configured in a two-stage system having a first crushing section 100A in the front stage and a second crushing section 100B in the rear stage, but further crushing sections are connected in series with the crushing sections before and after these. It may be arranged in 3 or more stages.

上記実施形態では、粉砕設備25を構成する前段の第1粉砕部100A及び後段の第2粉砕部100Bの夫々を石臼式の磨砕装置で構成したが、磨砕装置以外の他の形式の粉砕装置で構成しても構わない。
さらに、前段の第1粉砕部100Aについては、粉砕対象物を収容した環状凹部を有する環状収容部を、その中心軸周りに回転させながら、当該環状凹部内で環状周方向に沿った軸周りでカッターを回転させる形態で、前記炊飯米を粉砕するサイレントカッターで構成することもできる。このように比較的安価なサイレントカッターを第1粉砕部に採用することで、設備コストを低く抑えることができる。更には、第1粉砕部に採用されたサイレントカッターにより、比較的大量の炊飯米を順次切断しながら安定して粉砕することができる。
In the above embodiment, each of the first crushing section 100A in the front stage and the second crushing section 100B in the rear stage constituting the crushing facility 25 is configured by a stone mill type crushing device, but crushing of other types other than the crushing device. It may be configured by a device.
Further, regarding the first crushing portion 100A in the previous stage, the annular accommodating portion having the annular recess accommodating the object to be crushed is rotated around the central axis thereof, and around the axis along the annular circumferential direction in the annular recess. It can also be configured by a silent cutter that crushes the cooked rice in the form of rotating the cutter. By adopting such a relatively inexpensive silent cutter for the first crushing section, the equipment cost can be kept low. Furthermore, the silent cutter adopted in the first crushing unit can stably crush a relatively large amount of cooked rice while sequentially cutting it.

1 米ゲル製造システム
4 浸漬部
5 炊飯部
6 炊飯米搬送部
7 粉砕部
8 米ゲル移送部
9 ゲル収容部
21 連続式炊飯機
25 粉砕設備(粉砕部)
25a 第1粉砕設備(粉砕部)
25b 第2粉砕設備(粉砕部)
25c 第3粉砕設備(粉砕部)
25d 第4粉砕設備(粉砕部)
25e 第5粉砕設備(粉砕部)
26 移送ポンプ(一軸偏心ねじポンプ)
38 原料米加工部
43 蒸気式連続炊飯機
46 主コンベヤ
47a 第1投入用コンベヤ
47b 第2投入用コンベヤ
47c 第3投入用コンベヤ
47d 第4投入用コンベヤ
82 粉砕設備
100A 第1粉砕部
100B 第2粉砕部
R 炊飯米
Ra 第1粉砕米
RG 米ゲル
1 Rice gel manufacturing system 4 Immersion part 5 Rice cooking part 6 Rice cooking rice transfer part 7 Crushing part 8 Rice gel transfer part 9 Gel storage part 21 Continuous rice cooker 25 Crushing equipment (crushing part)
25a 1st crushing equipment (crushing part)
25b 2nd crushing equipment (crushing part)
25c 3rd crushing equipment (crushing part)
25d 4th crushing equipment (crushing part)
25e 5th crushing equipment (crushing part)
26 Transfer pump (uniaxial eccentric screw pump)
38 Raw rice processing section 43 Steam-type continuous rice cooker 46 Main conveyor 47a 1st loading conveyor 47b 2nd loading conveyor 47c 3rd loading conveyor 47d 4th loading conveyor 82 Crushing equipment 100A 1st crushing section 100B 2nd crushing Part R Rice Cooked Rice Ra 1st Crushed Rice RG Rice Gel

Claims (5)

ゲル状の米ゲルを製造する米ゲル製造システムであって、
原料米を炊飯又は蒸煮して炊飯米を得る炊飯部と、
前記炊飯米を搬送する炊飯米搬送部と、
前記炊飯米搬送部から受け継いだ前記炊飯米を粉砕して前記米ゲルを得る粉砕部と、を備え、
前記粉砕部として、
前記炊飯米を粉砕して第1粉砕米を得る第1粉砕部と、
前記第1粉砕部から排出された第1粉砕米を前記第1粉砕部よりも細かく粉砕して前記米ゲルを得る第2粉砕部と、を備え
前記第1粉砕部と前記第2粉砕部との少なくとも一方は、相対回転する上臼部と下臼部との隙間に粉砕対象物を通過させる形態で、前記粉砕対象物を粉砕する石臼式の磨砕装置で構成されている米ゲル製造システム。
A rice gel manufacturing system that manufactures gel-like rice gel.
A rice cooker that cooks or steams raw rice to obtain cooked rice,
The cooked rice transport unit that transports the cooked rice,
A crushing section for crushing the cooked rice inherited from the cooked rice transport section to obtain the rice gel is provided.
As the crushing part,
The first crushing section for crushing the cooked rice to obtain the first crushed rice,
A second crushed portion for obtaining the rice gel by crushing the first crushed rice discharged from the first crushed portion more finely than the first crushed portion is provided .
At least one of the first crushed portion and the second crushed portion is a stone mill type that crushes the crushed object in a form in which the crushed object is passed through the gap between the upper and lower mortar portions that rotate relative to each other. A rice gel manufacturing system consisting of a crusher .
前記第1粉砕部から排出された第1粉砕米を前記第2粉砕部に搬送する第1粉砕米搬送部を備える請求項1に記載の米ゲル製造システム。 The rice gel production system according to claim 1, further comprising a first crushed rice transport section for transporting the first crushed rice discharged from the first crushed section to the second crushed section. 前記第2粉砕部が、前記粉砕対象物として前記第1粉砕米を粉砕する前記石臼式の磨砕装置で構成されている請求項1又は2に記載の米ゲル製造システム。 The rice gel production system according to claim 1 or 2, wherein the second crushing unit comprises the stone mill type crushing device for crushing the first crushed rice as the crushing object . 前記第1粉砕部が、前記粉砕対象物として前記炊飯米を粉砕する前記石臼式の磨砕装置で構成されており、
前記第2粉砕部での上臼部と下臼部との隙間の幅であるギャップ幅が、前記第1粉砕部でのギャップ幅よりも小さく設定されている請求項3に記載の米ゲル製造システム。
The first crushing unit is composed of the stone mill type crushing device that crushes the cooked rice as the crushing object .
The rice gel production according to claim 3, wherein the gap width, which is the width of the gap between the upper and lower mortar portions in the second crushing portion, is set to be smaller than the gap width in the first crushing portion. system.
ゲル状の米ゲルを製造する米ゲル製造方法であって、
原料米を炊飯又は蒸煮して得た炊飯米を粉砕してゲル状の米ゲルを得る粉砕工程を備え、
前記粉砕工程として、
前記炊飯米を粉砕して第1粉砕米を得る第1粉砕工程と、
前記第1粉砕工程で得た第1粉砕米を前記第1粉砕工程よりも細かく粉砕して前記米ゲルを得る第2粉砕工程と、を備え
前記第1粉砕部と前記第2粉砕部との少なくとも一方は、相対回転する上臼部と下臼部との隙間に粉砕対象物を通過させる形態で、前記粉砕対象物を粉砕する石臼式の磨砕装置で構成されている米ゲル製造方法。
It is a rice gel manufacturing method for producing gel-like rice gel.
It is equipped with a crushing process to obtain a gel-like rice gel by crushing cooked rice obtained by cooking or steaming raw rice.
As the crushing step,
In the first crushing step of crushing the cooked rice to obtain the first crushed rice,
A second crushing step of crushing the first crushed rice obtained in the first crushing step into smaller pieces than the first crushing step to obtain the rice gel is provided .
At least one of the first crushed portion and the second crushed portion is a stone mill type that crushes the crushed object in a form in which the crushed object is passed through the gap between the upper and lower mortar portions that rotate relative to each other. A rice gel manufacturing method consisting of a grinding device .
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JP7201641B2 (en) 2020-06-24 2023-01-10 ヤンマーパワーテクノロジー株式会社 rice gel manufacturing equipment

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