JPS6188846A - Method and apparatus for heat-treatment of cereal - Google Patents

Method and apparatus for heat-treatment of cereal

Info

Publication number
JPS6188846A
JPS6188846A JP59210287A JP21028784A JPS6188846A JP S6188846 A JPS6188846 A JP S6188846A JP 59210287 A JP59210287 A JP 59210287A JP 21028784 A JP21028784 A JP 21028784A JP S6188846 A JPS6188846 A JP S6188846A
Authority
JP
Japan
Prior art keywords
pressure
grains
pressurized
continuous
container
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP59210287A
Other languages
Japanese (ja)
Inventor
Yoshihiko Nishizawa
西澤 嘉彦
Satoru Abe
悟 阿部
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.)
Kikkoman Corp
Original Assignee
Kikkoman Corp
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 Kikkoman Corp filed Critical Kikkoman Corp
Priority to JP59210287A priority Critical patent/JPS6188846A/en
Publication of JPS6188846A publication Critical patent/JPS6188846A/en
Pending legal-status Critical Current

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  • Beans For Foods Or Fodder (AREA)
  • Cereal-Derived Products (AREA)
  • General Preparation And Processing Of Foods (AREA)
  • Commercial Cooking Devices (AREA)

Abstract

PURPOSE:To enable the heat-treatment of cereals, eliminating the restriction of the raw material, and preventing the deformation or breakage of the material, by heating cereals in a closed pressure vessel under pressure, transferring to another closed vessel maintained to the pressure and taken out of the vessel after cooling. CONSTITUTION:The cereals supplied by the feeder 4 are transferred with a screw conveyor 1 through a closed pressure vessel 3, heated in the vessel 3 with high-pressure steam under pressure, and delivered with the delivery device 5 to another closed pressure vessel 6. The cereals in the closed pressure vessel 6 are cooled by supplying a coolant such as chilled air from the refrigerator 7, and discharged continuously from the system by the discharging device 8.

Description

【発明の詳細な説明】 〔発明の産業上の利用分野〕 本発明は、穀類の原形を損なうことの少ない、穀類の加
熱処理法及び装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application of the Invention] The present invention relates to a method and apparatus for heat treatment of grains, which does not significantly damage the original shape of grains.

〔従来の技術及び発明が解決しようとする問題点〕近年
、米及び大豆等の穀類(原料)の加熱処理にあたっては
、芸多温度を高くして短時間処理することが、米の截粉
利用率又は大豆の窒素利用率を向上させる上で重要であ
ると認識されており、これに伴って蒸煮圧力を高くする
凹向にある。
[Problems to be solved by the prior art and the invention] In recent years, when heating grains (raw materials) such as rice and soybeans, it has become possible to heat the grains (raw materials) such as rice and soybeans by increasing the heating temperature and processing them for a short time. It is recognized that it is important to improve the nitrogen utilization rate of soybeans, and there is a trend to increase the steaming pressure accordingly.

しかし、Hg圧力を高くすると、g9.類は一般Gこ柔
らかく蒸煮されるので、これを原形状態を保持して排出
することは非常に困難であり、その殆とが膨化したり崩
れたりして原形を損なうことが多かった。加熱処理後の
穀類は、このように原形が損なわれていると、使用に際
して、均一に、吸水、他の原料と混和、乾燥、又は冷却
する操f乍が困汁となり作業性をニルくし、又物性上食
感が劣る等の欠点を有する。
However, when the Hg pressure is increased, g9. Generally, G-type products are steamed to a soft state, so it is very difficult to discharge them while maintaining their original shape, and most of them often swell or crumble and lose their original shape. If the original shape of the grains after heat treatment is damaged in this way, it will be difficult to uniformly absorb water, mix with other raw materials, dry, or cool the grains during use, which will impede workability. It also has disadvantages such as poor texture due to its physical properties.

このようなことから、穀類の原形をt員なうことの少な
い加熱処理法の開発が強く望まれており、そのための方
法及び装置が従来いくつか提案されたが、何れも未だ充
分とはいい難い。
For this reason, there is a strong desire to develop a heat treatment method that minimizes the loss of the original shape of grains, and although several methods and devices for this purpose have been proposed, none of them are yet satisfactory. hard.

卯ち、穀類をオートクレーブ等の密閉可能な容器に収容
し、回分的に茎気を用いて加圧加熱した後、減圧操作を
緩慢に行って取り出す方法が提案されているが、この方
法は穀類を連続的に加熱処理を行えないので能率的でな
い。
A method has been proposed in which grains are stored in a sealable container such as an autoclave, heated under pressure using stalk air in batches, and then taken out by slowly depressurizing the grains. It is not efficient because it cannot be heated continuously.

また、互いに連通ずる范炙缶を上下2段に設け、原料導
入ロータリーバルブから原料を上段の范煮缶に導入して
1.4 kg / clで蒸煮し、これを中間のロータ
リーバルブにより下段の朶煮缶に移行させてここで史に
約0.7 kz / ctMで荒者し、しかる後排出ロ
ータリーバルブで排出する等、上下の范煮缶の圧力差を
Q、7kg/cal程度にして蔑煮穀類の崩れを幾分少
なくする装置(特開昭50−58294号公報参照)が
提案されているが、この装置では、上下の蔑煮缶の圧力
をそれぞれ選択された特定圧力としなければならず、上
記以外の蓬六圧力、その他温度条件を採用することがで
きない。更に、この装置では、39を2つの蔑煮缶で2
回に分けて行わなければならない等、原料のS:煮過多
、イイミげ、又は過変性等の品質低下を招来し易い。
In addition, there are two upper and lower levels of boiling cans that communicate with each other, and raw materials are introduced into the upper boiling can through the raw material introduction rotary valve and steamed at 1.4 kg/cl. Transfer to boiling can, boiling at about 0.7 kHz / ctM, and then draining with a discharge rotary valve, etc. to make the pressure difference between the upper and lower boiling cans Q, about 7 kg/cal. A device has been proposed to somewhat reduce the crumbling of lightly boiled grains (see Japanese Patent Application Laid-open No. 58294/1983), but this device requires that the pressure in the upper and lower cans be set to specific pressures selected respectively. Therefore, pressures and other temperature conditions other than those listed above cannot be used. Furthermore, with this device, 39 can be made into two cans.
If the process has to be carried out in several batches, the quality of the raw material may deteriorate, such as overcooking, overcooking, or excessive denaturation.

更に、原料を連続的に蕉煮処理する蒸欣缶の排出ロータ
リーバルブにおけるローグーの各隔室の周壁に、蔑気の
みを排出する脱気孔を設け、ローターの回転中に、圧力
范気のみを外部に排出し、蒸煮原料の崩れを防止する方
法(特開昭50−58294号公報及び同49−749
6号公報参照)が提案されているが、この方法は、長時
間連続運転する場合、脱気孔の目詰りを起こして作業途
中から脱気が不充分となり易く、このような場合は原料
が高圧に保持された状態から瞬間的に外部に放出される
ため、原料の損傷が生じ易い。
Furthermore, in the exhaust rotary valve of a steam can that continuously boils raw materials, a deaeration hole is provided in the peripheral wall of each chamber of the steam can to discharge only the air, so that only the pressure air can be discharged while the rotor is rotating. Method for preventing crumbling of steamed raw materials by discharging them to the outside (Japanese Patent Laid-Open Nos. 50-58294 and 49-749)
However, if this method is operated continuously for a long period of time, the deaeration holes tend to become clogged and the deaeration becomes insufficient midway through the work. Since the raw material is momentarily released from the state where it is held, the raw material is likely to be damaged.

更にまた、加圧蒸煮の完了した大豆をそのまま水封され
た水中に投入した後、外気中に取り出す方法(特開昭5
2−79091号公報参!lりが提案されているが、こ
の方法は、水封された水が芸名缶内の茎気と直接接触し
て高温に熱せられるため、水中から搬出された大豆を冷
却、更に乾燥しなければならず、又、水との接触を避け
たい穀類を(史用できない等の欠点を有する。
Furthermore, there is a method in which the soybeans that have been pressure-cooked are directly put into sealed water and then taken out into the open air (Japanese Patent Laid-Open No. 5
See Publication No. 2-79091! However, in this method, the sealed water comes into direct contact with the stalks inside the can and is heated to a high temperature, so the soybeans taken out of the water must be cooled and then dried. It also has the disadvantage that it cannot be used for grains that should avoid contact with water.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らは、使用原料に制約がなく、加圧加熱条件を
任息に設定でき、高温高圧で加熱処理した場合も能率が
良く、原料の原形がtSなわれるのを確実に防止するこ
とのできる穀類の加熱処理法の開発を目的として種々研
究を重ねた結果、59.類を高圧密閉容器内に導入して
加圧下に水茎気又はその他の気体により加熱処理した後
、この加熱処理時の圧力と同圧又は圧力差の少ない加圧
密閉容器内に加熱処理された穀類を導入し、ここで強制
的に冷却を行えば、膨化の原因となる穀類中の高温の水
分が冷却され、系外に排出された時に断る水分が気化す
ることがなく、従って穀類の膨化を抑制又は調節し、穀
類の形、大きさ等の原形が保たれたg、 = ’t9.
 類がijiられることを知見し、この知見に基づき本
発明を完成した。
The present inventors have developed a technology that has no restrictions on the raw materials to be used, allows pressure and heating conditions to be set arbitrarily, is efficient even when heat-treated at high temperature and pressure, and reliably prevents the original shape of the raw materials from being distorted. As a result of various research aimed at developing a heat treatment method for grains that can produce 59. grains that are introduced into a high-pressure sealed container and heat-treated with water stalks or other gas under pressure, and then heat-treated in a pressurized sealed container with the same pressure or a small pressure difference as the pressure during this heat treatment. By introducing a system and forcibly cooling the grains, the high-temperature moisture in the grains that causes puffing will be cooled, and the moisture will not evaporate when it is discharged outside the system, thus preventing the grains from puffing. g that suppresses or adjusts and maintains the original shape, size, etc. of grains = 't9.
The present invention was completed based on this knowledge.

部ち、本発明は、穀類を高圧密閉容器を具備した連続式
加圧加熱装置の該高圧密閉容器内に導入して加圧下に加
熱処理した後、加圧下に維持された別の加圧密閉容器内
に導入して冷却し、しかる後系外に排出することを特徴
とする穀類の加熱処理法を提供するものである。
Particularly, the present invention provides a method for introducing grains into a high-pressure hermetic container of a continuous pressurizing and heating apparatus equipped with a high-pressure hermetic container and heat-treating the same under pressure. The present invention provides a heat treatment method for grains, which is characterized by introducing grains into a container, cooling them, and then discharging them outside the system.

また、本発明は、上記加Fg処理法の実施に用いる装置
として、連続式加圧加熱装置と連続式加圧冷却装置とか
らなり、上記連続式加圧加熱装置は、高圧密閉容器と、
該高圧密閉容器内に穀類を連続的に導入する導入装置と
、上記高圧密閉容器内の穀類を連続的に送出する送出装
置とを具備しており、また、上記連続式加圧冷却装置は
、加圧下に維持され且つ上記送出装置から送出される穀
類が導入される加PE密閉容器と、該加圧密閉容器内の
穀類を強制的に冷却する冷却装置と、上記加圧密閉容器
内の99. Mを系外に連続的に排出する排出装置とを
具備していることを特徴とするi9. LAの110熱
処理装置を提供するものである。
Moreover, the present invention includes a continuous pressurizing and heating device and a continuous pressurizing and cooling device as an apparatus used for carrying out the above-mentioned Fg treatment method, and the continuous pressurizing and heating device includes a high-pressure closed container,
The continuous pressurized cooling device includes an introduction device that continuously introduces grains into the high-pressure hermetic container, and a delivery device that continuously delivers the grains from the high-pressure hermetic container, and the continuous pressurized cooling device includes: a pressurized PE airtight container maintained under pressure and into which the grains delivered from the delivery device are introduced; a cooling device for forcibly cooling the grains in the pressurized airtight container; .. i9., characterized in that it is equipped with a discharge device that continuously discharges M out of the system; LA's 110 heat treatment equipment is provided.

以下、本発明の穀類の加熱処理法を、図面に示す本発明
の穀類の加熱処理装置の一実施例とともに、1#述する
Hereinafter, the grain heat treatment method of the present invention will be described with reference to an embodiment of the grain heat treatment apparatus of the present invention shown in the drawings.

本発明においては、先ず、穀類を高圧密閉容器を具備し
た連続式加圧加熱装置の該高圧密閉容器内に導入して加
圧下に加熱媒体により加熱処理する。
In the present invention, first, grains are introduced into a high-pressure hermetic container of a continuous pressurizing and heating apparatus equipped with a high-pressure hermetic container, and are heat-treated with a heating medium under pressure.

上記穀類としては、屑米、砕米、小粒硬質米、未熟米、
死米、被害米、米粉(白糠)、古米等の低品位米、正當
米、玄米等の米類、大麦、小麦、ライ麦、燕麦、ハト麦
等の麦類、栗、稗、高梁、黍等の雑穀類、大豆等の豆類
、玉蜀黍、及びこれらの割砕物、粉砕物等が挙げられる
が、本発明はこれらの穀類の原形を殆ど損なうことなく
澱粉のα化又は蛋白質の変性を行うことができる。
The above grains include scrap rice, broken rice, small grain hard rice, immature rice,
Dead rice, damaged rice, rice flour (white bran), old rice and other low-grade rice, regular rice, brown rice and other rice, barley, wheat, rye, oat, pigeon barley and other wheat, chestnut, millet, high beam, millet, etc. Examples include millet grains, legumes such as soybeans, onion corn, and crushed and crushed products thereof, but the present invention allows gelatinization of starch or denaturation of protein without substantially damaging the original form of these grains. can.

また、上記加熱媒体としては、飽和水蒸気、過熱水茎気
等の水范気、加熱された炭酸ガス、窒素ガス、アルコー
ル茎気等のその他のガス等が挙げられるが、tM竜を目
的とする加熱処理の場合、飽和水蒸気、過熱水茎気が特
に好ましい。
In addition, examples of the heating medium include saturated steam, water vapor such as superheated water vapor, and other gases such as heated carbon dioxide gas, nitrogen gas, alcohol vapor, etc., but heating for the purpose of tM dragon For treatment, saturated steam and superheated steam are particularly preferred.

また、上記加熱媒体による上記高圧密閉容器内での上記
穀類1の加圧加Pハ条件は、穀ipの種類、粒度(大き
さ)や加熱の目的、即ら′4ご粉のα化、蛋白質の変性
、殺菌等に応して適宜選択すれば良い。
In addition, the conditions for pressurizing the grain 1 in the high-pressure airtight container using the heating medium include the type of grain ip, the particle size (size) and the purpose of heating, i.e. '4 gelatinization of flour, It may be selected appropriately depending on protein denaturation, sterilization, etc.

例えば、α化米とする場合には、通常、加圧圧力を、ゲ
ージ圧でl = I OKg/ cAとし、又加熱l温
度を120〜260℃とし、又加熱処理時間を2秒〜2
0分とするのが好ましい。又、上記加熱温度と上記加熱
処理時間とは反比例関係にあり、加ダハ温度が高い時は
加熱処理時間を短くし、反対に加熱温度が低い時は加熱
処理時間を長くするのが好ましく、例えば、飽和水范気
を用いて米をα化する場合は、2にg/cII+で20
分、4Kg/CII+で5分、6Kg/cnlで2分と
することが好適である。
For example, in the case of pregelatinized rice, the pressurization pressure is usually set to l=I OKg/cA in gauge pressure, the heating l temperature is set to 120 to 260°C, and the heat treatment time is set to 2 to 2 seconds.
It is preferable to set it to 0 minutes. Further, the heating temperature and the heat treatment time are in an inversely proportional relationship, and it is preferable to shorten the heat treatment time when the roofing temperature is high, and to lengthen the heat treatment time when the heating temperature is low, for example. , when gelatinizing rice using saturated water, add 20 g/cII+ to 2.
It is preferable to set the time to 5 minutes at 4Kg/CII+ and 2 minutes at 6Kg/cnl.

また、上記連続式加圧加熱装置としては、例えば、第1
図に示す如き連続式加圧加熱装置八を使用することがで
きる。第1図に示す連続式加圧加熱装置Aは、内部にス
クリューコンベアlを装備し且つ范気連通管2.2を介
し内部に茄気を流通するようにした中空の高圧密閉容器
3と、該高圧密閉容器3内に穀類を連続的に導入するロ
ータリーバルブよりなる導入装置4と、上記高圧密閉容
器3内の穀類を連続的に送出するロータリーバルブより
なる送出装置5とから構成されており、導入装置4から
導入された穀類を、高圧密閉容器3内においてスクリュ
ーコンベア1により搬送しつつ高圧水茎気により加圧加
熱し、加圧加熱された穀類を送出装置5から後述する連
続式加圧冷却装置Bの加圧密閉容器6内に送出するよう
になっている。
Further, as the above-mentioned continuous pressure heating device, for example, the first
A continuous pressure and heating device 8 as shown in the figure can be used. The continuous pressurization and heating apparatus A shown in FIG. 1 includes a hollow high-pressure airtight container 3 equipped with a screw conveyor l inside and through which air is circulated through an air communication pipe 2.2. It is composed of an introduction device 4 consisting of a rotary valve that continuously introduces grains into the high-pressure hermetic container 3, and a delivery device 5 consisting of a rotary valve that continuously delivers the grains from the high-pressure hermetic container 3. The grains introduced from the introduction device 4 are conveyed in the high-pressure sealed container 3 by the screw conveyor 1 while being pressurized and heated by high-pressure water stalks, and the pressurized and heated grains are transferred from the delivery device 5 to a continuous pressurization system described later. It is designed to be delivered into a pressurized sealed container 6 of cooling device B.

尚、本発明の穀類の加熱処理法に用いる連続式加圧加熱
装置は、上述のものに制躍されず、例えば、特公昭45
−26695号公報に記載されている膨化食品の製造装
置、特公昭49−1549号公報に記載されている食品
原料の連続式蒸煮、膨化装置、及び特公昭46−347
47号公報に記載されている気流加熱方式に依る膨化食
品の製造装置等を使用することもできる。
Incidentally, the continuous pressure heating apparatus used in the grain heat treatment method of the present invention is not limited to the above-mentioned one, and is, for example, the
- A device for manufacturing puffed foods described in Japanese Patent Publication No. 26695, a continuous steaming and puffing device for food raw materials described in Japanese Patent Publication No. 1549-1983, and a device for producing puffed foods described in Japanese Patent Publication No. 49-1549.
It is also possible to use an apparatus for producing a puffed food based on an air current heating method described in Japanese Patent No. 47.

本発明においては、次いで、上述の如くして加熱処理し
たnEを、加圧下に維持された別の加圧密閉容器を具備
する連続式加圧冷却装置の該加圧密閉容器内に導入して
冷却する。
In the present invention, the nE heat-treated as described above is then introduced into a pressurized sealed container of a continuous pressurized cooling device equipped with another pressurized sealed container maintained under pressure. Cooling.

上記加圧密閉容器内での上記冷却は、空気、窒素ガス、
炭酸ガス、水等の冷媒を目的に応じて上記加圧密閉容器
内に流i1!+又は投射することにより行い、好ましく
は加熱処理された穀類の品温か105℃以下、特に10
0℃以下となる迄行う。この際の冷媒の温度は、穀類の
品温、種類、量や冷媒の種類等によって異なるが、−1
5〜50“Cとするのが好ましい。
The above cooling in the pressurized sealed container is performed using air, nitrogen gas,
Flow a refrigerant such as carbon dioxide or water into the pressurized sealed container according to the purpose i1! + or by projecting, preferably the temperature of the heat-treated grain is 105°C or less, especially 10
Continue until the temperature is below 0°C. The temperature of the refrigerant at this time varies depending on the grain temperature, type, amount, type of refrigerant, etc., but -1
It is preferable to set it as 5-50"C.

このように穀類の品温を加圧密閉容器において下げるこ
とにより、上記加圧密閉容器から糸外(常圧下)への穀
類の排出時に、膨化の原因となる高温の水分が瞬間的に
気化するのを1rll制又は調節して穀類の膨化を抑制
又は調節することができる。
By lowering the temperature of the grains in the pressurized sealed container in this way, the high-temperature moisture that causes puffiness instantly vaporizes when the grains are discharged from the pressurized sealed container to the outside (under normal pressure). The swelling of grains can be suppressed or regulated by controlling or regulating the above.

また、上記加圧密閉容器内の圧力は、前記連続式加圧加
熱装置で芸者等により加熱処理された柔軟で非常に膨化
又は敵1fiL易い穀類が、上記加圧密閉容器内に導入
された時、膨化又は破壊せずに、その原形が殆どInな
われない高圧、即ら前記連げC氏加圧加熱装置との圧力
差が1Kg/cIII以内の高圧、詩に同圧とするのが
好ましい。そして、上記圧力を、常圧よりも高く且つ前
記連続式加圧加熱装;Rの圧力よりも低い範囲において
種々設定すれば、上記加圧密閉容器内におけるf1順の
膨化度を任息に調節することができる。
Moreover, the pressure in the pressurized airtight container is such that when the soft and highly swollen grains, which have been heat-treated by a geisha etc. in the continuous pressurization heating device, are introduced into the pressurized airtight container. , a high pressure that does not swell or break and hardly retains its original shape, i.e., a high pressure where the pressure difference with the above-mentioned Mr. C pressurizing and heating device is within 1 kg/cIII, preferably the same pressure. . By setting the pressure in various ways in a range higher than normal pressure and lower than the pressure of the continuous pressure heating device R, the degree of expansion in the order of f1 in the pressurized sealed container can be adjusted as desired. can do.

また、上記連続式加圧冷却装置としては、例えば、第1
図に示す如き連続式加圧冷却装置Bを使用することがで
きる。第1図に示す連続式加圧冷却装置Bは、加圧下に
維持され且つ前記連続式加圧加熱装置への前記送出装置
5から送出される穀灯零が導入される加圧密閉容器6と
、該加圧密閉容器6内の穀類を冷却空気等の冷媒により
強制的に冷却する冷却袋rj1.7と、上記加圧書間容
器内の穀類を糸外に連続的に排出する排出装置8とを主
体として構成されている。
Further, as the continuous pressurized cooling device, for example, the first
A continuous pressurized cooling device B as shown in the figure can be used. The continuous pressurized cooling device B shown in FIG. , a cooling bag rj1.7 that forcibly cools the grains in the pressurized airtight container 6 with a refrigerant such as cooling air, and a discharge device 8 that continuously discharges the grains in the pressurized container to the outside. It is mainly composed of.

上記連続式加圧冷却装置Bについて詳述すると、上記加
圧密閉容器6は、内部中空で、その上部が前記連続式加
圧加熱装置Aの前記送出装W5に連通しており、その下
部にロータリーバルブからなる上記排出装置8が設けら
れている。そして、この加圧密閉容器6の周壁には、加
圧密閉容器6内の穀類容量を検知するレベル計9が設け
られており、このレベル計9の検知信号により排出′A
置(ロータリーバルブ) 8の排出量(回転速度)を制
御して加圧密閉容器6内のi2類のホールド量を調節し
、前記連続式加圧加熱装置Aで加熱処理されたf51類
が加圧密閉容器6内において冷媒(冷却空気)と充分接
触できるようになっている。そして又、加圧密閉容器6
には、この他、加圧密閉容器6内の穀類の品温のδす温
体10及び加圧密閉容器6内の上部空間温度の測温体1
1が設けられている。
To explain the continuous pressurized cooling device B in detail, the pressurized sealed container 6 is hollow inside, and its upper part communicates with the delivery device W5 of the continuous pressurized heating device A, and its lower part communicates with the delivery device W5 of the continuous pressurized heating device A. The above-mentioned discharge device 8 consisting of a rotary valve is provided. A level meter 9 is provided on the peripheral wall of the pressurized hermetic container 6 to detect the grain capacity in the pressurized hermetic container 6.
The discharge amount (rotational speed) of the rotary valve 8 is controlled to adjust the hold amount of the i2 class in the pressurized sealed container 6, and the f51 class heated in the continuous pressurization and heating device A is heated. In the pressure-tight container 6, sufficient contact can be made with the refrigerant (cooling air). And also, pressurized airtight container 6
In addition, there is also a thermometer 10 for measuring the temperature of grains in the pressurized airtight container 6 and a thermometer 1 for measuring the upper space temperature in the pressurized airtight container 6.
1 is provided.

また、上記連続式加圧冷却装置Bにおける上記冷却装置
7は、空気圧縮機12から順次、アフター・クーラー1
3、エアー・タンク14、脱臭フィルター15、減圧弁
16を経て上記加圧密閉容器6の下部周壁に至る冷却空
気供給径路17と、上記加圧密閉容器6の上部周壁に設
けた排気路1Gとを主体とし、且つ上記脱臭フィルター
15と上記減圧弁16との間の上記冷却空気供給径路1
7中に流量計19を、又上記排気路18中に調圧バルブ
20を設けて構成されており、加圧密閉容器6内の穀類
を次の如く冷却するようになっている。
In addition, the cooling device 7 in the continuous pressurized cooling device B includes the aftercooler 1 in order from the air compressor 12.
3. A cooling air supply path 17 that passes through the air tank 14, a deodorizing filter 15, and a pressure reducing valve 16 to the lower circumferential wall of the pressurized sealed container 6, and an exhaust path 1G provided on the upper circumferential wall of the pressurized sealed container 6. and the cooling air supply path 1 between the deodorizing filter 15 and the pressure reducing valve 16;
7 and a pressure regulating valve 20 in the exhaust passage 18, the grains in the pressurized airtight container 6 are cooled as follows.

即ち、上記冷却装置7においては、穀類冷却用の空気が
空気圧縮機I2で加圧された(麦、アフター・クーラー
13で熱交換により例えば常温迄冷却されてそのFW 
k t+1水が除去され、次いでエアー・タンク14を
経て脱臭フィルター15で臭気が除去された後、減圧弁
16で断PI5膨張されて低温且つ加圧された冷却空気
として加圧密閉容器6の底部近傍に送入され、加圧密閉
容器6内の穀類と前述の如く充分に接触して断る穀類の
品温を低下させる。この際、加圧密閉容器6内のfj、
頚の品温の?y節は、n1j述の如く送入される冷却空
気の温度及び量によって調節されるが、冷却空気の温度
はアフター・クーラー13によりi円節することができ
、又その9は流量計19で確認して調圧バルブ20によ
りRI!l1ilqiすることができる。そして、加圧
密閉容器6内の穀類と接触した冷却空気の一部は、排出
装置8により穀類とともに、又その残りは、前記連続式
加圧加熱装置Aから漏れて来る寒気を同伴して調圧バル
ブ20を通して、それぞれ系外に排出される。
That is, in the cooling device 7, the air for cooling the grains is pressurized by the air compressor I2 (the wheat is cooled to room temperature, for example, by heat exchange in the aftercooler 13, and the air is
After k t+1 water is removed, the odor is removed through the air tank 14 and the deodorizing filter 15, the pressure is cut off by the pressure reducing valve 16, and the PI5 is expanded and cooled and pressurized as cooling air at the bottom of the pressurized closed container 6. It is fed into the vicinity and comes into sufficient contact with the grains in the pressurized airtight container 6, as described above, to lower the temperature of the grains to be rejected. At this time, fj in the pressurized airtight container 6,
What about the neck temperature? The y node is adjusted by the temperature and amount of the cooling air sent in as described in n1j, but the temperature of the cooling air can be adjusted by the aftercooler 13, and the 9th node is adjusted by the flow meter 19 Confirm and press RI with pressure regulating valve 20! You can l1ilqi. Then, a part of the cooling air that has come into contact with the grains in the pressurized airtight container 6 is removed together with the grains by the exhaust device 8, and the rest is regulated by entraining the cold air leaking from the continuous pressurizing and heating device A. Each of them is discharged to the outside of the system through a pressure valve 20.

尚、本発明で用いる上記連続式加圧冷却装置は、上記の
ものに制限されず、例えば、図示の連続式加圧冷却装置
Bの上記空気圧縮機12に代えて、窒素ガス等の不凝縮
ガス供給源を用いれば、不凝縮ガスによる穀類の冷却を
jテうことができる。又、上記排気路18に使用済の高
温の空気を除湿する凝縮機及び上記排出装置8から漏洩
する使用済の空気を補充する副空気圧縮機をそれぞれ介
装し、上記排気路18と上記冷却空気供給径路17とを
接続して循環路を形成すれば、使用済の空気を系外に排
出せずに再使用することを可能とし、−上記空気圧縮機
12の負荷を軽減する、二とができる。
The continuous pressurized cooling device used in the present invention is not limited to the one described above, and for example, in place of the air compressor 12 of the illustrated continuous pressurized cooling device B, non-condensable gas such as nitrogen gas may be used. A gas source can be used to cool the grain with non-condensable gas. In addition, a condenser for dehumidifying used high-temperature air and an auxiliary air compressor for replenishing used air leaking from the exhaust device 8 are installed in the exhaust passage 18, respectively, so that the exhaust passage 18 and the cooling By connecting the air supply path 17 to form a circulation path, the used air can be reused without being discharged outside the system, and the load on the air compressor 12 can be reduced. I can do it.

更に、上記アフター・クーラー13に代えて冷凍機のチ
ラー水により空気を一5〜5℃に冷却することもできる
Further, instead of the after-cooler 13, the air can be cooled to -5 to 5°C using chiller water from a refrigerator.

本発明においては、最後に、上述の如くし適温迄冷却さ
れた穀類を、系外に排出する。
In the present invention, finally, the grains that have been cooled to an appropriate temperature as described above are discharged from the system.

上記排出は、前記連続式加圧冷却装置Bの前記排出装置
8により前述の如くして所定9づつ行うことができ、斯
くして排出される穀類からは殆ど水分が気化することが
ないため、本発明によれば、殆ど原形が損なわれていな
い、或いは原形がtiなねれることが適度に関節された
、穀類の加熱処理物が得られる。
The above-mentioned discharge can be carried out by the discharge device 8 of the continuous pressurized cooling device B in a predetermined number of nine times as described above, and since almost no moisture evaporates from the grains thus discharged, According to the present invention, it is possible to obtain a heat-treated grain product in which the original shape is almost intact, or the original shape is properly rounded.

尚、排出装置8から排出される穀類の落下通路内に、該
通路を塞ぐようにしてスポンジ等の衝撃吸収材を斜め上
方に設けるとともに該衝撃吸収材の周囲をゴム製ノート
等で囲った緩衝装置を設けることができる。
In addition, a shock absorbing material such as a sponge is installed diagonally upward in the falling passage of the grains discharged from the discharging device 8 so as to block the passage, and a cushioning material such as a rubber notebook is placed around the shock absorbing material. A device may be provided.

〔実施例〕〔Example〕

以下、実施例により本発明の穀類の加熱処理法を更に具
体的に説明する。
Hereinafter, the method for heat treatment of grains of the present invention will be explained in more detail with reference to Examples.

実施例1 精白米を、導入装置(導入ロータリーバルブ)4を介し
て、毎時100に+rの割合で高圧密閉容器3に連続的
に導入し、飽和水朶気を用いて圧力6Kg/cd・G、
温度164°Cで2.5分間加圧加本した後、送出装置
5を介して、圧縮空気により圧力6にg/−・Gに維持
された加圧密閉容器6中に連続的に送出し、ここで圧縮
空気と充分接触させて品温を98°C迄冷却し、しかる
後加圧密閉容器らの底部から排出装置(排出ロータリー
バルブ)8を用いて系外に連続的に排出しα化米(本発
明品)を得た。
Example 1 Polished rice was continuously introduced into the high-pressure sealed container 3 at a rate of 100 +r per hour via the introduction device (introduction rotary valve) 4, and the pressure was increased to 6Kg/cd・G using saturated water vapor. ,
After being pressurized for 2.5 minutes at a temperature of 164°C, it is continuously delivered via a delivery device 5 into a pressurized sealed container 6 maintained at a pressure of 6 g/-.G with compressed air. Here, the product is brought into sufficient contact with compressed air to cool down to 98°C, and then continuously discharged from the bottom of the pressurized sealed container using a discharge device (discharge rotary valve) 8 outside the system. A converted rice (product of the present invention) was obtained.

尚、上記圧縮空気のt’AMは、空気を、空気圧縮機1
2でl OKg/e+J −Gに圧縮した後、アフター
クーラー13で20℃迄冷却し、しかる後減圧弁16で
5Kg/cd−Gまで断熱膨張を行って−lO℃迄冷却
することにより行った。又、圧縮空気の加圧密閉容器6
への供給量は、該加圧密閉容器6から外部に排出する空
気量を、排気路18の途中に具備させた調圧バルブ20
を関節して加減し、毎時5ONn?に調節した。
In addition, t'AM of the compressed air is the air compressor 1.
After compressing to 1 OKg/e+J -G at 2, it was cooled to 20°C with an aftercooler 13, and then adiabatically expanded to 5Kg/cd-G with a pressure reducing valve 16, and cooled to -10°C. . In addition, a pressurized airtight container 6 for compressed air
The amount of air supplied to the pressurized airtight container 6 is determined by a pressure regulating valve 20 provided in the middle of the exhaust path 18.
Joint and adjust, 5 ONn every hour? It was adjusted to

一方、比較例として、上記の精白米と同し精白米を高圧
密閉容器に導入し、上記と同じ加圧加熱条件下で加圧加
熱した後、瞬間的に排出ロータリーバルブを介し糸外に
排出してα化米(対照界)を得た。
On the other hand, as a comparative example, the same polished rice as the above-mentioned polished rice was introduced into a high-pressure airtight container, heated under the same pressure and heating conditions as above, and then instantly discharged to the outside of the yarn through a discharge rotary valve. Pregelatinized rice (control field) was obtained.

このようにして得られた2種類のα化米について、膨化
度(精白米の容積に対するα化米のそれの割合)を(り
定した。その結果を第1表に示す。
The swelling degree (the ratio of the gelatinized rice to the volume of the polished rice) was determined for the two types of gelatinized rice thus obtained. The results are shown in Table 1.

第1表 第1表の結果から、比較例の方法では米が良く膨化して
原形がffiなわれてしまうが、本発明の方法によれば
、米の膨化が抑制され、膨化度が極めて低く原形が殆ど
tiなわれていないα化米が得られることが刈る。
Table 1 From the results in Table 1, it can be seen that with the method of the comparative example, the rice puffs up well and loses its original shape, but according to the method of the present invention, the puffing of rice is suppressed and the degree of puffing is extremely low. It is possible to obtain pregelatinized rice whose original shape is almost intact.

実施例2 実施例1において、精白米に代えて、洗強後水t3に/
120時間行った?I ’/R吸収九大豆を用い、又加
圧密閉容器6内における;に煮大豆の冷却温度を40℃
とした以外は、実施例1と全く同様にして蒸煮丸大豆(
本発明品)を得た。
Example 2 In Example 1, instead of polished rice, water t3 was used after washing.
Did you go for 120 hours? I'/R absorption nine soybeans were used, and the cooling temperature of the boiled soybeans in the pressurized sealed container 6 was set at 40°C.
Steamed whole soybeans (
A product of the present invention) was obtained.

一方、比較例として、上記の浸漬吸収丸大豆と同じ浸漬
吸収丸大豆を高圧密閉容器に導入し、上記と同じ加圧加
熱条件下で加圧加熱した後、瞬間的に排出ロータリーバ
ルブを介し系外に排出して蒸煮丸大豆(対照界)を得た
On the other hand, as a comparative example, soaked and absorbed whole soybeans, which are the same as the soaked and absorbed whole soybeans described above, were introduced into a high-pressure sealed container, heated under the same pressure and heating conditions as above, and then instantly discharged into the system via a rotary valve. Steamed whole soybeans (control field) were obtained by discharging to the outside.

このようにして得られた2種類の叢μ丸大豆について、
崩れの程度を検査した。その結果を第2表に示す。
Regarding the two types of soybeans obtained in this way,
The degree of collapse was inspected. The results are shown in Table 2.

第2表 第2表の結果から、本発明の方法によれば、殆ど崩れの
ない蒸煮丸大豆が得られることが判る。
From the results shown in Table 2, it can be seen that according to the method of the present invention, steamed whole soybeans with almost no crumbling can be obtained.

実施例3 実施例1における飽和水蕩気を過熱水茄気に代え、加圧
り吋ハ条件を圧力6Kg/−・G、温度205°Cで5
分間処理とし、又圧縮空気の加圧密閉容器6への供給量
を毎時15ONr/に代えた以外は実施例1と同様な条
件下に本発明を実施してα化米(本発明品)を14だ。
Example 3 The saturated water boiling in Example 1 was replaced with superheated water boiling, and the pressurized water conditions were 5 kg/-.G at a pressure of 6 kg/-.G and a temperature of 205°C.
The present invention was carried out under the same conditions as in Example 1, except that the treatment was carried out for 1 minute, and the amount of compressed air supplied to the pressurized airtight container 6 was changed to 15 ONr/hour. It's 14.

また、比較例として、同−精白米を過熱水茎気により上
記と同一の加圧加熱条件で加圧加熱した後、瞬間的に排
出ロータリーバルブを介し系外に排出してα化米(対照
品)を得た。
In addition, as a comparative example, the same polished rice was heated under the same pressure and heating conditions as above using superheated water stalks, and then instantaneously discharged from the system via the discharge rotary valve. ) was obtained.

このようにして得られた2種類のα化米について、膨化
度(精白米の容積に対するα化米のそれの割合)を測定
した。その結果を第3表に示す。
For the two types of pregelatinized rice thus obtained, the degree of swelling (the ratio of the pregelatinized rice to the volume of polished rice) was measured. The results are shown in Table 3.

第3表 第3表の結果から、実施例1の場合と同様に、比較例の
方法では米が良(膨化して環形か1iなわれてしまうが
、本発明の方法によれば、米の膨化が抑制され、膨化度
が極めて低く環形が殆どtRなわれていないα化米が得
られることが判る。
Table 3 From the results in Table 3, it can be seen that, as in Example 1, the method of the comparative example produces rice that is not good (swelled and becomes ring-shaped), but according to the method of the present invention, the rice is It can be seen that gelatinized rice with suppressed swelling, extremely low degree of swelling, and almost no tR ring shape can be obtained.

〔発明の効果〕〔Effect of the invention〕

本発明の効果を列挙すると次の通りである。 The effects of the present invention are listed below.

(1)連続的に、高温高圧で加熱処理して得られた穀類
を、直ちに、加圧密閉容器に導入し、ここで強制的に急
激に冷却した後、系外に排出しているため、穀類の原形
が損なわれることを抑制又は1周節しつつ、蒸閘等の手
段で加熱処理した穀類を能率的に得ることができる。
(1) Grain obtained by continuous heat treatment at high temperature and high pressure is immediately introduced into a pressurized sealed container, where it is forcibly cooled rapidly, and then discharged from the system. It is possible to efficiently obtain grains that have been heat-treated by means such as a steamer, while suppressing damage to the original shape of the grains or preventing the grains from being damaged.

(2)穀類の加熱を、連続式加圧加熱装置を用いた1回
の加熱処理のみで行い得るため、HlQの種類、性質及
び加熱の目的に合わせて、苛酷な条件から緩慢な条件に
至る任意の条件を選択することができ、2つの3g缶で
2回に分けて基点を行う従来法に比べ、蒸煮等の加熱処
理条件の設定が容易で、品質の低下を招来し難い。
(2) Since grains can be heated in just one heat treatment using a continuous pressurized heating device, conditions can be varied from severe to mild depending on the type and nature of HlQ and the purpose of heating. Arbitrary conditions can be selected, and compared to the conventional method in which the starting point is divided into two batches using two 3g cans, it is easier to set the heat treatment conditions such as steaming, and quality deterioration is less likely to occur.

(3)加熱処理した穀類を、一旦別の加圧容器に保持し
、ここで品温を所定温度迄強制的に冷却しているため、
排出ロータリーバルブの回転中に圧力蒸気のみを外部に
排出することにより蒸煮穀類の崩れを防止する従来の方
法に比べ、穀類の原形保持効果が確実であり、穀類とし
て、粒径の小さいものから大きなもの迄任意のものを使
用し得る。
(3) Heat-treated grains are temporarily held in a separate pressurized container, where the product temperature is forcibly cooled to a predetermined temperature.
Compared to the conventional method of preventing steamed grains from collapsing by discharging only the pressure steam to the outside while the discharge rotary valve is rotating, the effect of preserving the original shape of grains is more reliable, and the grain size can be adjusted from small to large grain size. You can use anything up to the point.

(4)穀類の種類、加熱の目的に応じて加熱処理された
穀類の冷却に、水、空気、窒素ガス、炭酸ガス等の任意
の冷媒を選択し得るため、穀類の品質を損なうことなく
加熱処理を行うことができる。
(4) Any refrigerant such as water, air, nitrogen gas, carbon dioxide gas, etc. can be selected for cooling the heat-treated grains depending on the type of grains and the purpose of heating, so the grains can be heated without sacrificing quality. can be processed.

(5)穀類を密閉容器に入れ加圧加タハした後急激に放
圧して得られる穀類は、原料に含まれている水分が瞬間
的に蒸発して穀類の組織がスポンジ状に膨化するので、
これを各種食品の原料として使用する場合に、均一に、
吸水、他の原料と混和、乾燥、又は冷却する作業が困難
となり、作業性を悪くし、又物性上食感が劣る等の難点
を有しているが、本発明により(与られるα化穀類は、
そのような難点がなく、その利用が知られている各種の
食品、例えばパーボイルドライス、和菓子、米菓及び味
噌等の原料として好適に使用される。
(5) Grains obtained by placing grains in a sealed container, pressurizing them, and then rapidly releasing the pressure will cause the moisture contained in the raw materials to evaporate instantaneously and the grain tissue to swell into a spongy shape.
When using this as a raw material for various foods, uniformly
However, with the present invention, the pregelatinized grains provided by the present invention teeth,
It does not have such drawbacks and can be suitably used as a raw material for various foods for which its use is known, such as parboiled rice, Japanese sweets, rice crackers, and miso.

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

第1図は、本発明の穀類の加熱処理法の実施に用いる本
発明の穀類の加熱処理装置の一実施例を示す概略図であ
る。 A・・・連続式加圧加熱装置 B・・・連続式加圧冷却装置 3・・・高圧密閉容器 4・・・導入装置 5・・・送出装置 6・・・加圧密閉容器 7・・・冷却装置 8・・・排出装置 特許出願人    キッコーマン株式会社、゛工光 昭和60年 2月27日 特許庁長官  志 賀   学 殿 2、発明の名称 穀類の加熱処理法及びその装置 3、補正をする者 事件との関係 特許出願人 (447)キッコーマン株式会社 4、代理人 東京都港区赤坂九丁目6番29号 パシフィソク乃木坂601号 6、補正の対象 図   面 7、補正の内容
FIG. 1 is a schematic diagram showing an embodiment of the grain heat treatment apparatus of the present invention used to carry out the grain heat treatment method of the present invention. A... Continuous pressure heating device B... Continuous pressure cooling device 3... High pressure sealed container 4... Introducing device 5... Delivery device 6... Pressurized sealed container 7...・Cooling device 8... Discharging device Patent applicant: Kikkoman Corporation, Kokomatsu February 27, 1985 Mr. Manabu Shiga, Commissioner of the Patent Office 2, Title of invention: Grain heat treatment method and apparatus 3, Amendment. Patent applicant (447) Kikkoman Corporation 4, Agent 601-601 Nogizaka, Nogizaka, 9-29 Akasaka, Minato-ku, Tokyo 6 Drawings subject to amendment 7 Contents of amendment

Claims (3)

【特許請求の範囲】[Claims] (1)穀類を高圧密閉容器を具備した連続式加圧加熱装
置の該高圧密閉容器内に導入して加圧下に加熱処理した
後、加圧下に維持された別の加圧密閉容器内に導入して
冷却し、しかる後系外に排出することを特徴とする穀類
の加熱処理法。
(1) Grain is introduced into a high-pressure airtight container of a continuous pressurization heating device equipped with a high-pressure airtight container, heat-treated under pressure, and then introduced into another pressurized airtight container maintained under pressure. A method for heat treatment of grains, which is characterized in that the grains are heated, cooled, and then discharged from the system.
(2)加圧密閉容器内の圧力と高圧密閉容器内の圧力と
の圧力差が1kg/cm^2以内である、特許請求の範
囲第(1)項記載の穀類の加熱処理法。
(2) The method for heat-treating grains according to claim (1), wherein the pressure difference between the pressure in the pressurized sealed container and the pressure in the high-pressure sealed container is within 1 kg/cm^2.
(3)連続式加圧加熱装置と連続式加圧冷却装置とから
なり、上記連続式加圧加熱装置は、高圧密閉容器と、該
高圧密閉容器内に穀類を連続的に導入する導入装置と、
上記高圧密閉容器内の穀類を連続的に送出する送出装置
とを具備しており、また、上記連続式加圧冷却装置は、
加圧下に維持され且つ上記送出装置から送出される穀類
が導入される加圧密閉容器と、該加圧密閉容器内の穀類
を強制的に冷却する冷却装置と、上記加圧密閉容器内の
穀類を系外に連続的に排出する排出装置とを具備してい
ることを特徴とする穀類の加熱処理装置。
(3) Consisting of a continuous pressure heating device and a continuous pressure cooling device, the continuous pressure heating device includes a high pressure sealed container and an introduction device that continuously introduces grains into the high pressure sealed container. ,
A delivery device that continuously delivers the grains in the high-pressure airtight container, and the continuous pressurized cooling device includes:
A pressurized airtight container maintained under pressure and into which the grains delivered from the delivery device are introduced, a cooling device for forcibly cooling the grains in the pressurized airtight container, and the grains in the pressurized airtight container. 1. A heat treatment device for grains, comprising: a discharge device for continuously discharging grains to the outside of the system.
JP59210287A 1984-10-06 1984-10-06 Method and apparatus for heat-treatment of cereal Pending JPS6188846A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59210287A JPS6188846A (en) 1984-10-06 1984-10-06 Method and apparatus for heat-treatment of cereal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59210287A JPS6188846A (en) 1984-10-06 1984-10-06 Method and apparatus for heat-treatment of cereal

Publications (1)

Publication Number Publication Date
JPS6188846A true JPS6188846A (en) 1986-05-07

Family

ID=16586896

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59210287A Pending JPS6188846A (en) 1984-10-06 1984-10-06 Method and apparatus for heat-treatment of cereal

Country Status (1)

Country Link
JP (1) JPS6188846A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100587767B1 (en) 2005-08-22 2006-06-09 박병철 Grain heating and cooling unit
JP2015216920A (en) * 2014-05-14 2015-12-07 幸蔵 倉持 Manufacturing method of scorched brown rice
EP3971506A1 (en) * 2020-09-18 2022-03-23 LAW Iberica S.A. Method and apparatus to process grain received from a dryer
US11644237B2 (en) 2020-09-18 2023-05-09 LAW Iberica S.A. Apparatus to process grain received from a dryer

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100587767B1 (en) 2005-08-22 2006-06-09 박병철 Grain heating and cooling unit
JP2015216920A (en) * 2014-05-14 2015-12-07 幸蔵 倉持 Manufacturing method of scorched brown rice
EP3971506A1 (en) * 2020-09-18 2022-03-23 LAW Iberica S.A. Method and apparatus to process grain received from a dryer
US11304424B2 (en) 2020-09-18 2022-04-19 LAW Iberica S.A. Method and apparatus to process grain process grain received from a dryer
EP4102164A1 (en) * 2020-09-18 2022-12-14 LAW Iberica S.A. Method and apparatus to process grain received from a dryer
US11644237B2 (en) 2020-09-18 2023-05-09 LAW Iberica S.A. Apparatus to process grain received from a dryer

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