JPH10117725A - Continuous apparatus for pressurized steaming using water-cooled type rotary valve - Google Patents

Continuous apparatus for pressurized steaming using water-cooled type rotary valve

Info

Publication number
JPH10117725A
JPH10117725A JP8282523A JP28252396A JPH10117725A JP H10117725 A JPH10117725 A JP H10117725A JP 8282523 A JP8282523 A JP 8282523A JP 28252396 A JP28252396 A JP 28252396A JP H10117725 A JPH10117725 A JP H10117725A
Authority
JP
Japan
Prior art keywords
water
cooling water
raw material
rotary valve
steaming
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP8282523A
Other languages
Japanese (ja)
Other versions
JP3776531B2 (en
Inventor
Sakae Tanaka
栄 田中
Akio Fujiwara
章夫 藤原
Yoshinari Fujiwara
善也 藤原
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fujiwara Techno Art Co Ltd
Original Assignee
Fujiwara Techno Art Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fujiwara Techno Art Co Ltd filed Critical Fujiwara Techno Art Co Ltd
Priority to JP28252396A priority Critical patent/JP3776531B2/en
Publication of JPH10117725A publication Critical patent/JPH10117725A/en
Application granted granted Critical
Publication of JP3776531B2 publication Critical patent/JP3776531B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Beans For Foods Or Fodder (AREA)
  • Soy Sauces And Products Related Thereto (AREA)
  • Flow Control (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a continuous apparatus for pressurized steaming, using water-cooled type rotary valves and capable of carrying out the pressurized steaming treatment while continuously feeding and transferring a raw material. SOLUTION: This continuous apparatus for steaming treatment using water- cooled rotary valves is capable of sprinkling hot water over a raw material and carrying out the steaming treatment of the raw material. The apparatus is equipped with the water-cooled type rotary valves 4 and 5 arranged at a raw material charging inlet 2 or a raw material discharging outlet 3 of a pressurized steaming vessel 1 and obtained by composing a flow channel for producing the hot water with cooling water, passed through the rotary valves 4 and 5 and heated or a flow channel for converting the cooling water into the hot water after the heating. The flow channel is composed by providing a temperature measuring means or a flow measuring means 9 for obtaining measured values with time from the temperature or flow rate of cooling water after heating and a flow controlling means 10 for adjusting the flow rate of the cooling water based on the measured values.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、原料を連続的に供
給、移送しながら加圧蒸煮処理する水冷式ロータリーバ
ルブを使用する連続加圧蒸煮装置の改良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement of a continuous pressurized steaming apparatus using a water-cooled rotary valve for performing a steaming process while continuously supplying and transferring raw materials.

【0002】[0002]

【従来の技術】醤油製造における脱脂大豆に一定温度の
温水(以下、撒水用温水と呼ぶ)を撒水しながらの加圧蒸
煮、酵素製造におけるフスマに一定温度の撒水用温水を
撒水しながらの加圧蒸煮や納豆製造における加圧蒸煮等
では、生産効率を高めるため、原料を移送しながら連続
的に蒸煮可能な連続加圧蒸煮装置(以下、蒸煮装置と略
する)が使用される。この蒸煮装置は、原料を連続的に
投入、排出しながら加圧蒸煮缶内を略密閉にして加圧状
態を維持するため、加圧蒸煮缶の原料投入口及び原料排
出口それぞれにロータリーバルブが用いられるのが通例
である。このロータリーバルブは、通常ロータを冷却可
能にしている。
2. Description of the Related Art Pressurized steaming is performed while sprinkling hot water at a certain temperature (hereinafter referred to as hot water for sprinkling) on defatted soybeans in soy sauce production, and heating while sprinkling hot water at a certain temperature on bran in enzyme production. In the case of pressure steaming or pressure steaming in natto production, a continuous pressure steaming apparatus (hereinafter, abbreviated as steaming apparatus) capable of continuously steaming while transferring raw materials is used in order to increase production efficiency. In this steaming apparatus, a rotary valve is provided at each of the raw material inlet and the raw material outlet of the pressurized steaming can in order to maintain the pressurized state by substantially closing the inside of the pressurized steaming can while continuously charging and discharging the raw materials. It is usually used. This rotary valve normally allows the rotor to be cooled.

【0003】ロータリーバルブのロータを冷却するの
は、次の理由による。蒸煮処理を施す原料は、予め加水
されていたり、また撒水用温水が撒水されることから、
加圧蒸煮缶からの熱気で加温されたロータリーバルブの
ロータに付着しやすくなっている。原料がロータに付着
すると、原料投入口や原料排出口を詰まらせたり、ロー
タに長時間付着し続けて変色、焦げつきを起こし、蒸煮
後の原料品質を低下させるという問題を惹き起こす。特
に、タンパク質を含む脱脂大豆では、タンパク質がゲル
化し、粘性を増してロータに付着しやすく、問題は深刻
化する。そこで、ロータリーバルブのロータ内部を冷却
してロータ表面に水蒸気を結露させ、ロータを覆う薄い
水の膜により原料のロータへの付着を抑制し、付着した
場合でも容易に剥離できるようにしている。前記ロータ
内部の冷却手段としては空冷も考えられるが、ロータを
効率よく冷却するには水冷式が好ましく、現在では水冷
式ロータリーバルブが一般的になっている。従来は、ロ
ータリーバルブの冷却水の流路と装置内で原料に撒水す
る撒水用温水の流路とは、その役割の違いから当然に別
系統とされていた。
[0003] The rotor of the rotary valve is cooled for the following reasons. The raw material to be steamed is pre-watered, or because hot water for sprinkling is sprinkled,
It easily adheres to the rotor of a rotary valve heated by hot air from a pressurized steaming can. When the raw material adheres to the rotor, it causes clogging of the raw material input port and the raw material discharge port, and causes a problem that the raw material continues to adhere to the rotor for a long time, causing discoloration and burning, thereby deteriorating the raw material quality after steaming. Particularly, in the case of defatted soybeans containing protein, the protein gels, increases in viscosity and easily adheres to the rotor, and the problem becomes serious. Therefore, the inside of the rotor of the rotary valve is cooled to condense water vapor on the rotor surface, and a thin film of water covering the rotor suppresses the adhesion of the raw material to the rotor, so that even if it adheres, the raw material can be easily separated. Air cooling may be considered as a cooling means inside the rotor, but a water-cooled type is preferable for efficiently cooling the rotor, and a water-cooled rotary valve is generally used at present. Conventionally, the flow path of the cooling water of the rotary valve and the flow path of the hot water for sprinkling water to the raw material in the apparatus have been naturally separated from each other due to the difference in their roles.

【0004】[0004]

【発明が解決しようとする課題】従来の蒸煮装置では、
原料に撒水する撒水用温水を、貯水した撒水タンクに蒸
気パイプを潜らせて蒸気により加熱したり、気水混合
(蒸気と水との混合、以下同じ)した温水を撒水タンクへ
送り込んで生成している。上述のとおり、原料に撒水す
る撒水用温水とロータリーバルブの冷却水とは別系統の
流路を構成しており、一方ではロータ冷却後の加温され
た冷却水(以下、加温後冷却水と呼ぶ)は棄てられ、他方
では撒水用温水を新たに生成していたのである。
SUMMARY OF THE INVENTION In a conventional steaming apparatus,
Hot water for sprinkling water into the raw material is heated by steam through a steam pipe in a sprinkling tank where water is stored, or steam-water mixing
Hot water (mixing of steam and water, the same applies hereinafter) is sent to a sprinkling tank to generate water. As described above, the hot water for sprinkling water on the raw material and the cooling water for the rotary valve constitute a separate flow path.On the other hand, heated cooling water after cooling the rotor (hereinafter, cooling water after heating) is used. Was abandoned, while on the other hand it produced fresh hot water for sprinkling.

【0005】上記冷却水と撒水用温水との関係は、エネ
ルギーの使用の観点から非常に無駄の多いシステムとい
うことができるが、冷却水と撒水用温水とを同列に扱う
ことはできない。なぜなら、冷却水は、ロータリーバル
ブのロータを冷却することを主眼としているために流量
が一定ではなく、加温後冷却水の温度も変動するが、撒
水用温水は定量、定温である必要があるからである。こ
のため、従来は両者を分離せざるを得ず、加温後冷却水
のエネルギーを利用することはなかった。
The relationship between the cooling water and the hot water for sprinkling can be said to be a very wasteful system from the viewpoint of energy use, but the cooling water and the hot water for watering cannot be treated in the same line. Because the main purpose of cooling water is to cool the rotor of the rotary valve, the flow rate is not constant, and the temperature of the cooling water fluctuates after heating, but the hot water for sprinkling needs to be constant and constant temperature Because. For this reason, conventionally, both had to be separated, and the energy of the cooling water after heating was not used.

【0006】そこで、蒸煮装置全体としてのエネルギー
利用を効率化し、省エネルギー化を図ることを目的と
し、設備的、運用的にコストの削減が可能な蒸煮装置の
開発を試みた。
[0006] In view of the above, for the purpose of improving the energy utilization of the entire steaming apparatus and saving energy, an attempt has been made to develop a steaming apparatus capable of reducing costs in terms of equipment and operation.

【0007】[0007]

【課題を解決するための手段】検討の結果、開発したも
のが、原料に撒水用温水を撒水し、この原料を蒸煮処理
する装置であって、加圧蒸煮缶の原料投入口又は原料排
出口に水冷式ロータリーバルブを配しており、このロー
タリーバルブを通過した加温後冷却水を用いて撒水用温
水を生成する流路又はこの加温後冷却水を前記撒水用温
水とする流路を構成した水冷式ロータリーバルブを使用
する蒸煮装置である。撒水用温水は、熱交換器を用いて
加温後冷却水により間接的に水を昇温させて生成するこ
ともできるが、水質的に問題がなければ、加温後冷却水
を撒水用温水そのものとして利用する方が効率的であ
る。
As a result of the examination, what has been developed is an apparatus for sprinkling warm water for sprinkling water on a raw material and steaming the raw material. A water-cooled rotary valve is arranged in the flow path for generating hot water for sprinkling by using the cooling water after heating passed through the rotary valve or a flow path for using the cooling water after the heating as the hot water for spraying. It is a steaming apparatus using the water-cooled rotary valve thus configured. The hot water for sprinkling can be generated by heating the water using a heat exchanger and then indirectly raising the temperature of the water using cooling water. It is more efficient to use it as it is.

【0008】上記装置においては、加温後冷却水の流量
又は温度を制御することで、エネルギーの利用率を上
げ、撒水用温水の温度を安定して一定に保つことができ
る。具体的には、水冷式ロータリーバルブに対し、(a)
ロータリーバルブを通過した加温後冷却水の温度から経
時的な計測値を取得する温度計測手段と、前記計測値に
基づいて冷却水の流量を加減する流量制御手段とを備え
た流路を構成する、(b)ロータリーバルブを通過する冷
却水の流量から経時的な計測値を取得する流量計測手段
と、前記計測値に基づいて冷却水の流量を加減する流量
制御手段とを備えた流路を構成した水冷式ロータリーバ
ルブを使用する蒸煮装置である。流量を計測する冷却水
は、ロータリーバルブの通過前後を問わない。
In the above apparatus, by controlling the flow rate or the temperature of the cooling water after the heating, the energy utilization rate can be increased, and the temperature of the hot water for sprinkling can be stably kept constant. Specifically, for a water-cooled rotary valve, (a)
A flow path comprising a temperature measuring means for acquiring a measured value over time from the temperature of the cooling water after heating passed through the rotary valve, and a flow control means for adjusting the flow rate of the cooling water based on the measured value (B) a flow path including flow rate measuring means for acquiring a measured value over time from the flow rate of cooling water passing through the rotary valve, and flow rate controlling means for adjusting the flow rate of cooling water based on the measured value Is a steaming apparatus using a water-cooled rotary valve. The cooling water for measuring the flow rate does not matter before or after passing through the rotary valve.

【0009】流量制御手段は、計測値に基づいて流量を
決定する計算部(例えばコンピュータや調節計等、現時
点での流量をフィードバックする流量計等を含む)と、
この計算部により駆動、制御される流量調節部(例えば
各種開閉バルブや回転数の増減可能なポンプ等)とから
なる。計算部と流量調節部とは一体であってもよい。
The flow control means includes a calculation unit (for example, a computer, a controller, etc., including a flow meter for feeding back the current flow rate, etc.) for determining the flow rate based on the measured value;
It comprises a flow control unit (for example, various open / close valves, a pump capable of increasing or decreasing the number of revolutions) driven and controlled by the calculation unit. The calculation unit and the flow rate adjustment unit may be integrated.

【0010】温度計測手段又は流量計測手段が取得する
計測値は、経時的に連続する値であれば、アナログ値、
ディジタル値を問わない。例えば、ロータリーバルブか
ら撒水タンクへ向かう配管途中に電磁流量計(流量計測
手段)を配し、この電磁流量計の出力、すなわち計測値
(アナログ値)を、ロータリーバルブへ冷却水を送り込む
配管の開閉弁を操作する調節計(流量制御手段:計算部)
に入力し、調節計に開閉弁(流量制御手段:流量調節部)
の開度を操作させてもよいし、電磁流量計の出力をサン
プリングして得た値を計測値(ディジタル値)としてコン
ピュータ等(流量制御手段)に入力し、コンピュータに開
閉弁の開度を操作するモータ等を制御させてもよい。
The measured value obtained by the temperature measuring means or the flow rate measuring means may be an analog value,
Regardless of digital value. For example, an electromagnetic flow meter (flow rate measuring means) is arranged in the middle of the pipe from the rotary valve to the watering tank, and the output of the electromagnetic flow meter, that is, the measured value
(Analog value) is a controller that operates an open / close valve of a pipe that sends cooling water to a rotary valve (flow control means: calculation unit)
Input to the controller and open / close valve on the controller
May be operated, or a value obtained by sampling the output of the electromagnetic flowmeter may be input as a measured value (digital value) to a computer or the like (flow control means), and the computer may control the opening of the on-off valve. The operating motor or the like may be controlled.

【0011】加温後冷却水を撒水用温水の生成に利用し
ようとした場合、加温後冷却水を適切な流量に設定して
いても経時的な変動が生じ(流路を開閉するバルブを流
路一定に固定していても水源からの水圧が一定しないの
で、結果として流量が変動する場合等)、撒水用温水の
温度を変動させる。また、必要により外部の水源から水
を補給し、別途加温源を用意して加温後冷却水と補充し
た水とを混合して加温しなければならないが、補充した
水の量が多ければ、撒水用温水の温度が一時的に急激に
下がるという問題を生ずる。上記流量制御は、経時的に
変動する加温後冷却水の温度又は冷却水の流量を安定さ
せ、加温後冷却水による温度一定の撒水用温水の生成を
実現するのである。
When the cooling water after heating is used to generate hot water for sprinkling, even if the cooling water after heating is set to an appropriate flow rate, there is a variation with time (a valve for opening and closing the flow path is used). Even if the flow path is fixed, the water pressure from the water source is not constant, so that the flow rate fluctuates as a result, for example). Also, if necessary, replenish water from an external water source, prepare a separate heating source, mix the cooling water with the replenished water after heating, and heat it.However, if the amount of replenished water is large, For example, there arises a problem that the temperature of the hot water for sprinkling drops temporarily. The flow rate control stabilizes the temperature of the cooling water after heating or the flow rate of the cooling water that fluctuates with time, and realizes the generation of hot water for sprinkling at a constant temperature by the cooling water after heating.

【0012】加温後冷却水の温度を計測して冷却水の流
量を制御する装置では、例えば、冷却水の流量を増減し
てロータからの熱量に対する水量を加減することによ
り、加温後冷却水の温度を撒水用温水の温度に等しくし
てやれば、通常必要な撒水用温水に足りない水量だけ撒
水用温水に等しい温度の温水を加温後冷却水に加えてや
るだけで、安定した一定温度の撒水用温水の確保を可能
にする。
In a device for controlling the flow rate of the cooling water by measuring the temperature of the cooling water after the heating, for example, by increasing or decreasing the flow rate of the cooling water to adjust the amount of water with respect to the heat amount from the rotor, the cooling after the heating is performed. If the temperature of the water is made equal to the temperature of the hot water for sprinkling, a stable constant temperature can be achieved by simply adding the amount of water that is not enough for the required hot water for sprinkling and then adding it to the cooling water after heating. It is possible to secure hot water for watering.

【0013】冷却水の流量を計測して冷却水の流量を制
御する装置では、例えば、加温後冷却水の水量を必要な
撒水用温水の水量に維持してやれば、撒水用温水の温度
が低下した場合に蒸気等により撒水用温水を昇温するだ
けで、安定した一定温度の撒水用温水の確保を可能にす
る。このように、本発明は加温後冷却水の流量又は温度
のいずれかを定量にすることで、温度変化の小さい撒水
用温水の効率的な生成を可能にしている。
In a device for controlling the flow rate of cooling water by measuring the flow rate of cooling water, for example, if the amount of cooling water is maintained at a required level after the heating, the temperature of the hot water for spraying decreases. In this case, it is possible to secure a stable and constant temperature of the sprinkling water simply by raising the temperature of the sprinkling water with steam or the like. As described above, the present invention enables efficient generation of hot water for sprinkling with a small temperature change by quantifying either the flow rate or the temperature of the cooling water after heating.

【0014】上述の加温後冷却水の温度又は冷却水の流
量の計測値に基づく冷却水の流量制御は、加圧蒸煮圧
力、加圧蒸煮温度、熱膨張を考慮したロータリーバルブ
のロータとケーシングとの隙間の大きさ、あるいはロー
タの表面への原料の付着程度等に応じて実施することに
より、例えば過剰なエネルギーの使用を抑えた省エネル
ギーを実現したり、蒸煮装置としての性能面での向上が
図れるなど、多面的効用を有している。
The above-mentioned cooling water flow rate control based on the measured value of the temperature of the cooling water or the flow rate of the cooling water after heating is performed by taking into account the pressurized steaming pressure, the pressurized steaming temperature, and the thermal expansion in consideration of the rotor and casing of the rotary valve. The amount of raw material on the surface of the rotor, etc. to achieve energy saving, for example, by suppressing the use of excessive energy, or to improve the performance of a steaming device It has a multifaceted effect such as being able to achieve.

【0015】[0015]

【発明の実施の形態】以下、図を参照しながら本発明の
実施形態について説明する。図1は、醤油製造用の脱脂
大豆を蒸煮処理する蒸煮装置の構成図であり、加圧蒸煮
缶1の原料投入口2と原料排出口3とに配したロータリ
ーバルブ4,5には共に流量計測による流量制御の流路
を構成している。両流路を共に温度計測による流量制御
にしてもよい(図2参照)。本例では、撒水タンク6の貯
水に対し加温後冷却水を加えると共に、温度調整用に蒸
気、水量補充用に水を加える。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a block diagram of a steaming apparatus for steaming defatted soybeans for producing soy sauce. The rotary valves 4 and 5 arranged at a raw material input port 2 and a raw material discharge port 3 of a pressurized steaming can 1 have flow rates. This constitutes a flow path for flow control by measurement. Both of the flow paths may be subjected to flow rate control by temperature measurement (see FIG. 2). In the present embodiment, cooling water is added to the water stored in the watering tank 6 after heating, and steam is added for temperature adjustment, and water is added for replenishing the amount of water.

【0016】脱脂大豆は、2t/hの割合で撒水スクリュ
ー7内へ送り込まれて70℃の撒水用温水を2.6t/hの割合
で撒水され、予熱スクリュー8を経て加圧蒸煮缶1へ送
り出される。加圧蒸煮缶1の原料投入口2及び原料排出
口3にはそれぞれロータリーバルブ4,5が配されてお
り、加圧蒸煮缶1内の略密閉状態を実現し、投入された
原料を2kg/cm2Gで蒸煮する。
The defatted soybeans are fed into the sprinkling screw 7 at a rate of 2 t / h, sprinkled with hot water at 70 ° C. for sprinkling at a rate of 2.6 t / h, and sent to the pressurized steaming can 1 via the preheating screw 8. It is. Rotary valves 4 and 5 are provided at the raw material input port 2 and the raw material discharge port 3 of the pressurized steaming can 1, respectively, to realize a substantially sealed state in the pressurized steaming can 1, and to supply 2 kg / kg of the charged raw material. Steam at cm 2 G.

【0017】本例では、ロータリーバルブ4,5から撒
水タンク6へ戻される加温後冷却水の水量それぞれを1.
2t/hに保つことにした。すなわち、撒水タンク6へ計2.
4t/hの加温後冷却水が戻される。これにより、各ロータ
リーバルブ4,5から戻される加温後冷却水の温度はそ
れぞれ65〜70℃の範囲で変動することになるが、生成す
る撒水用温水に対する加温後冷却水の割合(撒水用温水
の生成にはこのほか温度調整用の蒸気、水量補充用の水
を用いている)が一定するため、加える蒸気の加減のみ
で簡単に撒水用温水の温度調整ができるようになる。む
しろ、加温後冷却水の流量を、常に必要な撒水用温水の
水量以下に抑えることができ、無駄の少ない加温後冷却
水の利用が可能になるという利点がある。
In this embodiment, the amount of the heated cooling water returned from the rotary valves 4 and 5 to the sprinkling tank 6 is 1.
We decided to keep it at 2t / h. That is, a total of 2.
After heating at 4t / h, the cooling water is returned. As a result, the temperature of the heated cooling water returned from each of the rotary valves 4 and 5 varies in the range of 65 to 70 ° C., but the ratio of the heated cooling water to the generated hot water for spraying (water spraying) In addition, steam for temperature adjustment and water for replenishing the amount of water are used for the generation of hot water, so that the temperature of the hot water for sprinkling can be easily adjusted only by adjusting the amount of steam to be added. Rather, the flow rate of the post-warming cooling water can be kept below the required amount of hot water for sprinkling.

【0018】流量制御は、ロータリーバルブ4(5)を通
過してきた加温後冷却水の流量を電磁流量計9が計測
し、その計測値を計算部である調節計(図中FIC)10に出
力することで、調節計10内において計測値と設定値(予
め決定し、調節計に入力しておいた目標値)とを比較し
た上、その差分に従って調節計10が流量調節部であるロ
ータリーバルブ4(5)へ冷却水を送る配管の開閉バルブ
11を開閉操作することで実現する。
In the flow rate control, the electromagnetic flow meter 9 measures the flow rate of the heated cooling water passing through the rotary valve 4 (5), and the measured value is sent to a controller (FIC in the figure) 10 which is a calculation unit. By outputting, the measured value is compared with a set value (a target value which is determined in advance and input to the controller) in the controller 10, and according to the difference, the controller 10 Opening / closing valve for piping that sends cooling water to valve 4 (5)
This is realized by opening and closing 11.

【0019】撒水タンク6では、加温後冷却水に蒸気と
水とが加えられ、一定温度(本例では70℃)に保たれた撒
水用温水が生成される。蒸気は、撒水タンク6内の撒水
用温水の温度を温度センサ12で計測し、調節計(図中TI
C)13が供給バルブ14を開閉して、温度が低い場合に必要
量を供給する。また、水はフロート弁17を用いた自動給
水設備等により、撒水タンク6内の撒水用温水の水量が
足りなくなったときに補充される。撒水用温水は供給ポ
ンプ15により撒水タンク6から引き出され、撒水スクリ
ュー7内の撒水パイプ16から原料に向けて撒水される。
In the watering tank 6, after heating, steam and water are added to the cooling water to generate hot water for watering maintained at a constant temperature (70 ° C. in this example). Steam measures the temperature of the hot water for watering in the watering tank 6 with the temperature sensor 12, and the controller (TI in the figure)
C) 13 opens and closes the supply valve 14 to supply the required amount when the temperature is low. Water is replenished by an automatic water supply system using the float valve 17 when the amount of hot water for watering in the watering tank 6 becomes insufficient. The hot water for watering is drawn from the watering tank 6 by the supply pump 15 and is watered from the watering pipe 16 in the watering screw 7 toward the raw material.

【0020】図2は、酵素製造として、フスマを蒸煮処
理する本発明の蒸煮装置の構成図であり、加圧蒸煮缶1
の原料投入口2又は原料排出口3に配したロータリーバ
ルブ4,5には共に温度計測による流量制御の流路を構
成している。本例では、撒水タンク6の貯水に対し加温
後冷却水を加えると共に、水量補充用に65℃の気水混合
による温水を加えることにしている。
FIG. 2 is a block diagram of a steaming apparatus of the present invention for steaming bran for the production of an enzyme.
The rotary valves 4 and 5 arranged at the raw material inlet 2 or the raw material discharge port 3 together constitute a flow path for flow control by temperature measurement. In the present embodiment, cooling water is added to the water stored in the watering tank 6 after heating, and hot water obtained by mixing air and water at 65 ° C. is added for replenishing the amount of water.

【0021】フスマは、1t/hの割合で撒水スクリュー
7内へ送り込まれて65℃の撒水用温水を1.4t/hの割合で
撒水され、予熱スクリュー8を経て加圧蒸煮缶1へ送り
出される。加圧蒸煮缶1の原料投入口2及び原料排出口
3にはそれぞれロータリーバルブ4,5が配されてお
り、加圧蒸煮缶1内の略密閉状態を実現し、投入された
原料を1.8kg/cm2Gで蒸煮する。
The bran is fed into the sprinkling screw 7 at a rate of 1 t / h, sprinkled with hot water for sprinkling at 65 ° C. at a rate of 1.4 t / h, and sent out to the pressurized steaming can 1 via the preheating screw 8. . Rotary valves 4 and 5 are provided at the raw material inlet 2 and the raw material outlet 3 of the pressurized steaming can 1, respectively, to realize a substantially closed state in the pressurized steaming can 1, and the charged raw material is 1.8 kg. Steam at / cm 2 G.

【0022】本例では、ロータリーバルブ4,5から撒
水タンク6へ戻される加温後冷却水の温度それぞれを65
℃に保つことにした。これにより、各ロータリーバルブ
4,5から戻される加温後冷却水の水量はそれぞれ0.50
〜0.65t/hの範囲で変動することになるが、撒水タンク
6に戻される加温後冷却水の温度が撒水用温水の温度で
ある65℃に等しいため、温度調整のほとんど必要ない利
点がある。加温後冷却水の水量を必要な撒水用温水の水
量以下にしておけば、加温後冷却水を無駄に棄てること
がなくなるし、水量が不足する場合には、例えば撒水タ
ンク6内の水面高さを監視するレベルセンサ20により電
磁弁21の開閉を制御して、気水混合により撒水用温水と
同じ65℃に加温された温水を補充してやればよい。
In this embodiment, the temperature of the heated cooling water returned from the rotary valves 4 and 5 to the
° C. As a result, the amount of cooling water after heating returned from the rotary valves 4 and 5 is 0.50 each.
However, since the temperature of the cooling water returned to the watering tank 6 after heating is equal to 65 ° C., which is the temperature of the water for sprinkling, there is an advantage that temperature adjustment is almost unnecessary. is there. If the amount of the cooling water after the heating is set to be equal to or less than the required amount of the hot water for sprinkling, the cooling water after the heating will not be discarded unnecessarily. The opening and closing of the electromagnetic valve 21 may be controlled by the level sensor 20 for monitoring the height, and hot water heated to 65 ° C., which is the same as the hot water for sprinkling, may be replenished by mixing air and water.

【0023】温度制御は、ロータリーバルブ4(5)を通
過してきた加温後冷却水の温度を温度センサ18が計測
し、その計測値を計算部である調節計(図中TIC)19に出
力することで、調節計19内において計測値と設定値(予
め決定し、調節計に入力しておいた目標値)とを比較し
た上、その差分に従って調節計19が流量調節部であるロ
ータリーバルブ4(5)へ冷却水を送る配管の開閉バルブ
11を開閉操作し、撒水タンク6へ戻される加温後冷却水
の流量を制御する形で実現する。
In the temperature control, the temperature sensor 18 measures the temperature of the cooling water after heating which has passed through the rotary valve 4 (5), and outputs the measured value to a controller (TIC in the figure) 19 which is a calculation unit. By doing so, the measured value is compared with a set value (a target value that is determined in advance and input to the controller) in the controller 19, and the controller 19 is a rotary valve that is a flow rate controller according to the difference. 4 (5) Open / close valve for piping that sends cooling water
11 is opened and closed to control the flow rate of the heated cooling water returned to the watering tank 6.

【0024】撒水タンク6では、加温後冷却水に気水混
合による温水が加えられ、一定温度(本例では65℃)に保
たれた温水が生成される。気水混合による温水は、レベ
ルセンサ20により制御される電磁弁21の開閉により、撒
水タンク6内の撒水用温水の水量が足りなくなったとき
に補充される。撒水用温水は、供給ポンプ15により撒水
タンク6から引き出され、撒水スクリュー7内の撒水パ
イプ16から原料に向けて撒水される。
In the watering tank 6, warm water is added to the cooling water after heating by mixing air and water to generate warm water maintained at a constant temperature (65 ° C. in this example). Hot water resulting from the mixing of air and water is replenished when the amount of hot water for watering in the watering tank 6 becomes insufficient due to opening and closing of the electromagnetic valve 21 controlled by the level sensor 20. The hot water for watering is drawn out of the watering tank 6 by the supply pump 15 and is watered from the watering pipe 16 in the watering screw 7 toward the raw material.

【0025】[0025]

【発明の効果】本発明の蒸煮装置により、従来棄てるだ
けであったロータリーバルブを通過した加温後冷却水の
有効利用が図れるようになった。すなわち、この加温後
冷却水を撒水用温水の生成、又は撒水用温水そのものと
して利用することで運用コストを低減し、流路を簡略化
できることで設備コストを低減する。また、撒水タンク
における撒水用温水の温度調整が簡単になり、この温度
調整必要な処理がすべて自動制御で実現される点に本発
明の特徴がある。これにより、撒水用温水の温度変動が
ほとんど見られなくなり、温度的に安定した撒水が実現
できる結果、蒸煮処理した製品の品質の向上も図れるの
ようになるのである。
According to the steaming apparatus of the present invention, it is possible to effectively use the cooling water after heating which has passed through the rotary valve which has been merely discarded. That is, the operation cost is reduced by using the cooling water after the heating as the hot water for sprinkling or the hot water for sprinkling itself, and the facility cost is reduced by simplifying the flow path. Further, the present invention is characterized in that the temperature adjustment of the hot water for watering in the watering tank is simplified, and all the processes required for the temperature adjustment are realized by automatic control. As a result, the temperature fluctuation of the hot water for spraying is hardly observed, and the stable spraying of the temperature can be realized. As a result, the quality of the steamed product can be improved.

【図面の簡単な説明】[Brief description of the drawings]

【図1】醤油製造用の脱脂大豆を蒸煮処理する本発明の
蒸煮装置の構成図である。
FIG. 1 is a configuration diagram of a steaming apparatus of the present invention for steaming defatted soybeans for producing soy sauce.

【図2】酵素製造として、フスマを蒸煮処理する本発明
の蒸煮装置の構成図である。
FIG. 2 is a configuration diagram of a steaming apparatus of the present invention for steaming bran for enzyme production.

【符号の説明】[Explanation of symbols]

1 加圧蒸煮缶 2 原料投入口 3 原料排出口 4 原料投入口のロータリーバルブ 5 原料排出口のロータリーバルブ 6 撒水タンク 7 撒水スクリュー 8 予熱スクリュー 9 電磁流量計 10 調節計(FIC) 11 開閉バルブ 12 撒水タンク内の温度センサ 13 調節計(TIC) 14 供給バルブ 15 供給ポンプ 16 撒水パイプ 17 フロート弁 18 温度センサ 19 調節計(TIC) 20 レベルセンサ(LC) 21 電磁弁 DESCRIPTION OF SYMBOLS 1 Pressurized steaming can 2 Raw material input port 3 Raw material discharge port 4 Rotary valve of raw material input port 5 Rotary valve of raw material discharge port 6 Sprinkling tank 7 Sprinkling screw 8 Preheating screw 9 Electromagnetic flow meter 10 Controller (FIC) 11 Opening / closing valve 12 Temperature sensor in watering tank 13 Controller (TIC) 14 Supply valve 15 Supply pump 16 Watering pipe 17 Float valve 18 Temperature sensor 19 Controller (TIC) 20 Level sensor (LC) 21 Solenoid valve

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 原料に温水を撒水し、該原料を蒸煮処理
する装置であって、加圧蒸煮缶の原料投入口又は原料排
出口に水冷式ロータリーバルブを配しており、該ロータ
リーバルブを通過して加温された冷却水を用いて原料に
撒水する温水を生成する流路又は該冷却水を前記温水と
する流路を構成したことを特徴とする水冷式ロータリー
バルブを使用する連続加圧蒸煮装置。
An apparatus for steaming a raw material by spraying hot water on the raw material, wherein a water-cooled rotary valve is disposed at a raw material input port or a raw material discharge port of a pressurized steaming can. A flow path for generating hot water to be sprayed on the raw material by using the cooling water that has passed through and heated, or a flow path for using the cooling water as the hot water, is used for continuous heating using a water-cooled rotary valve. Pressure steaming equipment.
【請求項2】 水冷式ロータリーバルブに対し、ロータ
リーバルブを通過して加温された冷却水の温度から経時
的な計測値を取得する温度計測手段と、前記計測値に基
づいて該冷却水の流量を加減する流量制御手段とを備え
た流路を構成したことを特徴とする請求項1記載の水冷
式ロータリーバルブを使用する連続加圧蒸煮装置。
2. A temperature measuring means for acquiring a temporally measured value from the temperature of the cooling water heated through the rotary valve with respect to the water-cooled rotary valve, and the cooling water based on the measured value. 2. The continuous pressurized steaming apparatus using a water-cooled rotary valve according to claim 1, wherein the flow path includes a flow control means for adjusting a flow rate.
【請求項3】 水冷式ロータリーバルブに対し、ロータ
リーバルブを通過する冷却水の流量から経時的な計測値
を取得する流量計測手段と、前記計測値に基づいて該冷
却水の流量を加減する流量制御手段とを備えた流路を構
成したことを特徴とする請求項1記載の水冷式ロータリ
ーバルブを使用する連続加圧蒸煮装置。
3. A flow rate measuring means for acquiring a time-dependent measured value from a flow rate of cooling water passing through the rotary valve for a water-cooled rotary valve, and a flow rate adjusting the flow rate of the cooling water based on the measured value. The continuous pressurized steaming apparatus using a water-cooled rotary valve according to claim 1, wherein a flow path provided with a control means is configured.
JP28252396A 1996-10-24 1996-10-24 Continuous pressure steaming device using water-cooled rotary valve Expired - Lifetime JP3776531B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28252396A JP3776531B2 (en) 1996-10-24 1996-10-24 Continuous pressure steaming device using water-cooled rotary valve

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28252396A JP3776531B2 (en) 1996-10-24 1996-10-24 Continuous pressure steaming device using water-cooled rotary valve

Publications (2)

Publication Number Publication Date
JPH10117725A true JPH10117725A (en) 1998-05-12
JP3776531B2 JP3776531B2 (en) 2006-05-17

Family

ID=17653570

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28252396A Expired - Lifetime JP3776531B2 (en) 1996-10-24 1996-10-24 Continuous pressure steaming device using water-cooled rotary valve

Country Status (1)

Country Link
JP (1) JP3776531B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010099032A (en) * 2008-10-24 2010-05-06 Takano Foods Kk Method for producing steam-cooked soybean, and fermented soybean by using the same
CN105549524A (en) * 2016-01-06 2016-05-04 李锦记(新会)食品有限公司 Bean soaking operation control system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010099032A (en) * 2008-10-24 2010-05-06 Takano Foods Kk Method for producing steam-cooked soybean, and fermented soybean by using the same
CN105549524A (en) * 2016-01-06 2016-05-04 李锦记(新会)食品有限公司 Bean soaking operation control system

Also Published As

Publication number Publication date
JP3776531B2 (en) 2006-05-17

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