JPS62106280A - Cereal drier - Google Patents

Cereal drier

Info

Publication number
JPS62106280A
JPS62106280A JP24292885A JP24292885A JPS62106280A JP S62106280 A JPS62106280 A JP S62106280A JP 24292885 A JP24292885 A JP 24292885A JP 24292885 A JP24292885 A JP 24292885A JP S62106280 A JPS62106280 A JP S62106280A
Authority
JP
Japan
Prior art keywords
drying
grain
drying chamber
air
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.)
Granted
Application number
JP24292885A
Other languages
Japanese (ja)
Other versions
JPH0454875B2 (en
Inventor
孝吉 花岡
為ケ井 清
関根 弘之
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.)
SEKINE KK
Original Assignee
SEKINE KK
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 SEKINE KK filed Critical SEKINE KK
Priority to JP24292885A priority Critical patent/JPS62106280A/en
Publication of JPS62106280A publication Critical patent/JPS62106280A/en
Publication of JPH0454875B2 publication Critical patent/JPH0454875B2/ja
Granted legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、一定恒温状態で穀物を減圧乾燥する穀物乾燥
装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a grain drying apparatus for drying grain under reduced pressure at a constant constant temperature.

従来の技術 従来、被乾燥物を強制乾燥させる方法として、熱風によ
る熱風伝導乾燥、赤外線や遠赤外線等による輻射伝熱乾
燥及び高周波による高周波伝熱乾燥が良く知られている
。これらはいずれも熱によって被乾燥物内の水分の気化
を促進させる熱依存の乾燥である。一方、真空乾燥やα
桔乾燥等雰囲気を真空にすることによって、水の蒸気圧
を低下させて水分除去を行なう乾燥法も知られている。
BACKGROUND ART Conventionally, hot air conduction drying using hot air, radiation heat transfer drying using infrared rays, far infrared rays, etc., and high frequency heat transfer drying using high frequency waves are well known as methods for forcibly drying objects to be dried. All of these methods are heat-dependent drying methods that use heat to promote the vaporization of moisture in the material to be dried. On the other hand, vacuum drying
Drying methods, such as box drying, are also known in which water is removed by reducing the vapor pressure of water by creating a vacuum atmosphere.

さらに、例えば特開昭57−19582号公報に記載さ
れているような、熱を出しながら排気するファンを用い
て加熱、減圧して乾燥する方法も行われている0また、
加熱、減圧して乾燥する前記方法による穀物等の乾燥装
置としては、例えば特開昭59−18344号公報に記
載されているような減圧モ衝摩擦熱発生機構を有する中
空室と顆粒物収納室とを通気可能に形成したようなもの
が提案されている。
Furthermore, there is also a method of drying by heating and reducing pressure using a fan that exhausts air while emitting heat, as described in, for example, Japanese Unexamined Patent Publication No. 57-19582.
An apparatus for drying grains, etc. by the above-mentioned method of drying by heating and reducing pressure may include a hollow chamber and a granule storage chamber having a mechanism for generating frictional heat under reduced pressure as described in JP-A No. 59-18344. It has been proposed that the structure is formed to allow ventilation.

発明が解決しようとする問題点 前記従来の熱依存の乾燥方法は、蒸発熱によって水分を
除去するので、水1g当り100℃で539.8 ca
lの気化熱を必要とし、多大な熱源を要しランニングコ
ストが高価になる欠点を有する。また熱依存の乾燥方法
は、乾燥効率ばかりでなく乾燥仕上りにも問題がある。
Problems to be Solved by the Invention The conventional heat-dependent drying method removes moisture by heat of evaporation, so the drying method uses 539.8 ca per gram of water at 100°C.
1 of vaporization heat, a large heat source is required, and the running cost is high. Further, heat-dependent drying methods have problems not only in drying efficiency but also in drying finish.

即ち、被乾燥物品の内部と表面を均一に乾燥させること
が困難であり、表面過乾燥や加熱による組織的変化を来
たし、表面が硬化してしまうことがある。
That is, it is difficult to uniformly dry the inside and surface of the article to be dried, and the surface may become over-dried or undergo structural changes due to heating, and the surface may become hardened.

さらに、真空乾燥や凍結乾燥方法は、乾燥効率は比較的
高いが、装置が高師でありコスト高になるので、特殊品
の乾燥にしか利用されていないのが現状である。また熱
全出しながら排気するファンを用いて加熱、減圧して乾
燥する従来の装置は、夏季に行う乾燥では減圧を維持す
ると40℃以上に加熱してしまい、温度を下げようとす
ると減圧度が下がってしまい温度と減圧度を同時に制御
することが不可能であり、比較的低温で乾燥させること
が要求される穀物の乾燥には満足に適用させることがで
きなかつたつさらに、穀物等の顆粒状被乾燥物品は、乾
燥室内に静止させた状態で乾燥させる従来の乾燥装置で
は粒間に充分な通気が行われず、満足に乾燥させること
ができなかった。
Further, although vacuum drying and freeze drying methods have relatively high drying efficiency, they require expensive equipment and are expensive, so they are currently only used for drying special products. In addition, conventional equipment that heats and depressurizes and dries using a fan that exhausts heat while emitting all of it heats up to over 40°C if the vacuum is maintained during drying in the summer, and if you try to lower the temperature, the degree of depressurization will increase. It is impossible to control the temperature and the degree of vacuum at the same time, and it cannot be satisfactorily applied to drying grains that require drying at relatively low temperatures. In conventional drying apparatuses in which the articles to be dried are dried in a stationary state in a drying chamber, sufficient ventilation is not provided between the particles, and the articles cannot be dried satisfactorily.

而して本発明は、上記従来技術の欠点に鑑み創案された
ものであって、乾燥効率及び乾燥仕上すが良く、しかも
ランニングコスト及び装置が安価で簡便に操作出来る穀
物乾燥装置を提供することを目的とするものである。
SUMMARY OF THE INVENTION The present invention has been devised in view of the above-mentioned drawbacks of the prior art, and it is an object of the present invention to provide a grain drying device that has good drying efficiency and drying finish, is inexpensive in running cost, and is easy to operate. The purpose is to

問題点を解決するための手段 上記問題点を解決するための技術的手段を、実施例に対
応する図面に基づいて説明する。
Means for Solving the Problems Technical means for solving the above problems will be explained based on drawings corresponding to embodiments.

本発明は一1断熱材及び耐圧材によって構成された乾燥
室1において熱源と排気を2系統とする手段を採用した
。即ち、熱源は冷暖装置9を用い、排気は排気装e3に
よって行ない、且つ一定の綾圧匿を保持するために一定
量の外気を導入口より導入する。さらに乾燥室1内に網
状材等の通気材から成る回転可能な穀物容器12と送風
機11とを設置して、乾燥室内金一定恒温状態かつ一定
減圧状態にして、穀物全回動する穀物容器内で移動させ
ながら減圧乾燥させるようにし念。
The present invention employs a method of providing two systems for the heat source and exhaust in the drying chamber 1, which is constructed of heat insulating material and pressure-resistant material. That is, the heat source is the cooling/heating device 9, the exhaust is performed by the exhaust system e3, and a certain amount of outside air is introduced from the inlet in order to maintain a certain amount of air pressure. Furthermore, a rotatable grain container 12 made of ventilation material such as a mesh material and a blower 11 are installed in the drying chamber 1 to keep the interior of the drying chamber in a constant constant temperature state and a constant depressurized state. Make sure to dry it under reduced pressure while moving it around.

作用 乾燥室内に被乾燥物である穀物を前記容器12に入れて
セットし、電源入れて作動させると排気装置3によって
乾燥室内が減圧されるが一定の減圧度になると外気導入
口よりの空気とモ衝になってその状態で維持される。ま
た前記室内は冷暖装置9によって一定温度に保持される
Operation When the grain to be dried is placed in the container 12 and set in the drying chamber, the power is turned on and the drying chamber is operated, the pressure inside the drying chamber is reduced by the exhaust device 3, but when the pressure reaches a certain degree, the air from the outside air inlet is removed. It becomes a state of conflict and is maintained in that state. Further, the interior of the room is maintained at a constant temperature by a cooling/heating device 9.

穀物容器12内の穀物は、該容器内を移動しながら減圧
によってその水分が表面に移動し送風機11によって表
面の水被膜が前記室内雰囲気中に飛散させられる。前記
排気装置は、前記室内を除湿し、常に前記室内の湿度全
低減させる方向に作用するので、連続的に効率良くしか
も均一に乾燥が行われる。
As the grains in the grain container 12 move within the container, moisture is moved to the surface by reduced pressure, and the water film on the surface is scattered by the blower 11 into the indoor atmosphere. The exhaust device dehumidifies the room and always works to reduce the total humidity in the room, so that drying is carried out continuously, efficiently and uniformly.

実施例 以下、本発明の実施例全図面に基づいて説明する。Example Embodiments of the present invention will be described below with reference to all the drawings.

第1図は本発明【係る穀物乾燥装置の一実施例を示す概
略側断面図であジ、第2図はその穀物容器の側面図であ
る。
FIG. 1 is a schematic side sectional view showing an embodiment of a grain drying apparatus according to the present invention, and FIG. 2 is a side view of a grain container thereof.

図に於いて、1は乾燥室であシ、内部に断熱材を充填し
た減圧に耐えられる耐圧材で形成しfc筐体2で構成さ
れている。3は筐体2に形成された内部排気口4に面し
て筐体2外部に設けられた排気装置である排気用ファン
であり、該排気用ファンからの排気は熱交換器8内を通
過して、外部排気口5より外気に排出される。なお、排
気装置は真空ポンプ全採用しても良い、一方7は、外部
吸気口であり、該外部吸気口より吸気された外気は図示
のように熱交換器8内を通過して内部吸気口6よυ乾燥
室1内に吸気される。従って、乾燥室内の吸排気はその
@度差に応じ互に熱交換器内で熱交換されるから、エネ
ルギーの損失が少なく外気は乾燥室内の温度に近い状態
で乾燥室内に吸気される。
In the figure, reference numeral 1 denotes a drying chamber, which is composed of an FC housing 2 made of a pressure-resistant material that can withstand reduced pressure and filled with a heat insulating material inside. Reference numeral 3 denotes an exhaust fan which is an exhaust device provided outside the housing 2 facing the internal exhaust port 4 formed in the housing 2, and the exhaust from the exhaust fan passes through the heat exchanger 8. Then, it is discharged to the outside air from the external exhaust port 5. Incidentally, the exhaust device may entirely employ a vacuum pump. On the other hand, 7 is an external intake port, and the outside air taken in from the external intake port passes through the inside of the heat exchanger 8 as shown in the figure, and then enters the internal intake port. 6. Air is taken into the drying chamber 1. Therefore, the air taken in and exhausted from the drying chamber is heat exchanged with each other in the heat exchanger according to the temperature difference, so that there is little loss of energy and the outside air is drawn into the drying chamber at a temperature close to the temperature inside the drying chamber.

9は乾燥室内全一定恒温にするための冷暖装置でちゃ、
ヒートポンプ型冷暖装置又はヒーターと冷凍装置の組合
せ等放熱と吸熱作用を行なうものであれば良い。10は
前記暖熱装置の放熱又は吸熱口を示す。11は乾燥室内
に設置された送風機であり、室内の空気全拡散して後述
する穀物容器に一定に量金与えて被乾燥物表面に移動し
た流体境膜である水の被膜全飛散させる。
9 is a heating and cooling device to maintain a constant temperature throughout the drying room.
Any device that can radiate and absorb heat may be used, such as a heat pump type cooling/heating device or a combination of a heater and a refrigeration device. 10 indicates a heat radiation or heat absorption port of the heating device. Reference numeral 11 denotes a blower installed in the drying chamber, which completely diffuses the air in the room and applies a constant amount of water to the grain container, which will be described later, to completely scatter the water film, which is a fluid film, that has moved to the surface of the object to be dried.

12は穀物乾燥容器であり該穀物乾燥容器は取付脚14
を介して間欠回転可能に乾燥室内に設置されている。穀
物乾燥容器には、第2図に示すようにホッパー16&と
ホッパー16b及び該両ホッパーを連結連通する移動路
17とを一体に形成した容器導体を複数個並設して構成
されている。そして該穀物乾燥容器のホッパー開口部は
、該容器内への穀物の出入ができるように開閉自在な蓋
体18.19によって被われている。
12 is a grain drying container, and the grain drying container has mounting legs 14.
It is installed in the drying chamber so that it can be rotated intermittently through the As shown in FIG. 2, the grain drying container is constructed by arranging a plurality of container conductors in which a hopper 16&, a hopper 16b, and a moving path 17 connecting and communicating the two hoppers are integrally formed. The hopper opening of the grain drying container is covered by a lid 18, 19 that can be opened and closed to allow grain to be taken in and out of the container.

また該容器のホッパー及び通路部は網状材や通気性多孔
材で構成され、容器内の穀物に送風機12よりの風が直
接当るようになっている。なお、19は移動路17間に
設けられた通風用空間部であり、13は前記穀物乾燥容
器の回転軸であり、15は、その回転用モータであり、
図示しない制御装置によって間欠的に回転する。
Further, the hopper and passage section of the container are made of a net-like material or a breathable porous material, so that the air from the blower 12 directly hits the grains in the container. In addition, 19 is a ventilation space provided between the moving paths 17, 13 is a rotating shaft of the grain drying container, 15 is a motor for rotation thereof,
It rotates intermittently by a control device (not shown).

以上のように構成されているので、穀物乾燥容器12の
一方のホッパー16aに穀物を入れると、穀物は自然落
下により移動路17を通って下方のホッパー1&bに移
動する。移動が終了すると適宜の制御装置が作用して回
転駆動用モータ15が作動して、穀物乾燥容器12全反
転させ、以後前記した動作を燥9返す。一方、乾燥室1
内は、排気ファン3の作動に一定の減圧状態になり、し
かも冷暖装置によって一定恒温状態に保たれているので
、減圧作用で穀物内の水分が穀物表酊に移動する。穀物
表面に移動した水分は、前記移動中に送風機11からの
送風が前記通風用空間部19′に通過することによって
前記網状材から侵入しで飛散させて、穀物全均一に乾燥
する。
With the above structure, when grains are put into one hopper 16a of the grain drying container 12, the grains naturally fall through the movement path 17 and move to the lower hoppers 1&b. When the movement is completed, an appropriate control device operates to operate the rotational drive motor 15, completely inverting the grain drying container 12, and thereafter repeating the above-described operation 9. On the other hand, drying room 1
The inside of the grain is under a certain reduced pressure due to the operation of the exhaust fan 3, and is maintained at a constant temperature by the cooling/heating device, so the water inside the grain moves to the surface of the grain due to the reduced pressure. The moisture that has moved to the surface of the grain is dispersed through the mesh material by the air from the blower 11 passing through the ventilation space 19' during the movement, thereby uniformly drying the entire grain.

上記実へ例の装置全便用して、減圧するための排気ファ
ンk 1.51cw出力で作動させて、800 vx 
Aq  の減8Eばに保ち、乾燥室内?20℃の恒温状
態で、米50Kgを10時間で乾燥しtoその結果、香
り、色、及び味とも優れた高品質の米を得ることができ
た。
Using the entire device in the example above, the exhaust fan k for pressure reduction was operated at an output of 1.51 cw, and the output was 800 vx.
Reduce Aq by 8E and keep it in a drying room? 50 kg of rice was dried in 10 hours at a constant temperature of 20° C. As a result, high quality rice with excellent aroma, color, and taste could be obtained.

なお、上記実施例の装置では、冷暖装置9を筐体2の上
部に設けて直接乾燥室内に放熱又は吸熱するようにした
が、該冷暖装置は熱交換器8の外部吸気ロアに設置して
も良い。また、本装置は、必ずしも穀物の乾燥に限らず
顆粒状物品の乾燥に好適であることは言うまでもない。
In the apparatus of the above embodiment, the cooling/heating device 9 is installed at the top of the housing 2 to directly radiate or absorb heat into the drying chamber, but the cooling/heating device is installed at the external intake lower of the heat exchanger 8. Also good. Furthermore, it goes without saying that this apparatus is suitable not only for drying grains but also for drying granular articles.

効果 本発明は以上のように構成されているので、次のような
顕著な効果を奏するものである。
Effects Since the present invention is configured as described above, it has the following remarkable effects.

げ)減圧乾燥であるので多大な熱源全必要とせず、しか
も冷暖装置によって乾燥室内を被乾燥物の乾燥適温に任
へに設定できるので、乾燥効率が卓越し、ランニングコ
ストの大幅な低減と、肋に類を見ない高品質の穀物の乾
燥物を作ることが出来る。
(G) Since it is vacuum drying, it does not require a large heat source, and the temperature inside the drying chamber can be set at will to suit the drying of the material to be dried, so drying efficiency is outstanding, and running costs are significantly reduced. It can produce dried grains of unparalleled quality.

(ロ)通気材からなる回転可能な穀物容器に穀物を入れ
、穀物が各器内を移動しながら乾燥されるので、穀物を
均一にかつ効率良ぐ乾燥させることができる。
(b) Grain is placed in a rotatable grain container made of ventilation material, and the grain is dried while moving within each container, so that the grain can be dried uniformly and efficiently.

fW  送風機により殺′吻表面に移動した水の被膜を
効率的に飛散させ、且つ排気装置によって連続的に除湿
されるので、連続的に均一な乾燥が行われる。
fW Since the film of water that has moved to the sterilized proboscis surface is efficiently scattered by the blower and continuously dehumidified by the exhaust device, uniform drying is performed continuously.

に) 装置が簡はであり、かつ簡梗に操作でき、また、
多大な熱源全必要としないから安全である。
) The device is simple and easy to operate, and
It is safe because it does not require a large heat source.

(ホ)熱交換器を設けることによって、排気と吸気が熱
交換されてエネルギーロスが少なく、省エネルギー効果
を一没と高めることができる。
(e) By providing a heat exchanger, heat is exchanged between exhaust air and intake air, resulting in less energy loss, and the energy saving effect can be instantly enhanced.

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

π1図は、本発明に係る穀物乾燥容器の一実施例の側断
面図、第2図はその穀物容器の側面図である。 1:乾燥室 2:渣体 3:排気装置 4:内部、排気口 5:外部排気口 6:内部吸気口 
7:外部吸気口 8:熱交1奥器 9:冷暖装置 ]1
:送風機 】2:穀物乾燥容器16a、16b:ホッパ
ー 17=移動器特許出願人  昧弐会仕  セ  キ
  ネ巣1図
FIG. π1 is a side sectional view of one embodiment of the grain drying container according to the present invention, and FIG. 2 is a side view of the grain container. 1: Drying room 2: Residue 3: Exhaust device 4: Internal, exhaust port 5: External exhaust port 6: Internal intake port
7: External intake port 8: Heat exchanger 1 inner unit 9: Cooling/heating device] 1
:Blower]2:Grain drying container 16a, 16b:Hopper 17=Movers patent applicant

Claims (1)

【特許請求の範囲】 1)断熱材及び耐圧材によつて構成された乾燥室と、該
乾燥室内の空気を排気し空気が一定圧に達するまでの時
間内に於いて空気の排気量と吸気量の差によつて減圧度
を制御する排気装置と、前記乾燥室内に設置され網状材
等の通気材から成る回転可能な穀物容器と、穀物容器内
の被乾燥物に対して一定風量を与える前記乾燥室内に設
置された送風機と、前記乾燥室内を一定恒温状態にする
冷暖装置とから成り、一定恒温状態で穀物を減圧乾燥す
ることを特徴とする穀物乾燥装置。 2)前記穀物容器が、2台のホッパーの連結体により構
成されている特許請求の範囲第1項記載の穀物乾燥装置
。 3)前記乾燥室内への吸排気が、該乾燥室外へ設置され
た熱交換装置を通して行われる特許請求の範囲第1又は
2項記載の穀物乾燥装置。 4)前記排気装置が送風ファンである特許請求の範囲第
1、2又は3項記載の穀物乾燥装置。 5)前記排気装置が真空ポンプである特許請求の範囲第
1、2又は3項記載の穀物乾燥装置。
[Claims] 1) A drying chamber configured with heat insulating materials and pressure-resistant materials, and the amount of air exhausted and intake within the time period from when the air in the drying chamber is exhausted until the air reaches a constant pressure. an exhaust device that controls the degree of decompression based on the difference in volume; a rotatable grain container installed in the drying chamber and made of a ventilation material such as a mesh material; and a constant air volume for the material to be dried in the grain container. A grain drying apparatus comprising a blower installed in the drying chamber and a cooling/heating device that maintains the inside of the drying chamber at a constant temperature, and drying grain under reduced pressure at a constant constant temperature. 2) The grain drying apparatus according to claim 1, wherein the grain container is constituted by a connected body of two hoppers. 3) The grain drying apparatus according to claim 1 or 2, wherein the air intake and exhaust into the drying chamber is performed through a heat exchange device installed outside the drying chamber. 4) The grain drying apparatus according to claim 1, 2 or 3, wherein the exhaust device is a blower fan. 5) The grain drying apparatus according to claim 1, 2 or 3, wherein the exhaust device is a vacuum pump.
JP24292885A 1985-10-31 1985-10-31 Cereal drier Granted JPS62106280A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24292885A JPS62106280A (en) 1985-10-31 1985-10-31 Cereal drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24292885A JPS62106280A (en) 1985-10-31 1985-10-31 Cereal drier

Publications (2)

Publication Number Publication Date
JPS62106280A true JPS62106280A (en) 1987-05-16
JPH0454875B2 JPH0454875B2 (en) 1992-09-01

Family

ID=17096297

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24292885A Granted JPS62106280A (en) 1985-10-31 1985-10-31 Cereal drier

Country Status (1)

Country Link
JP (1) JPS62106280A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02290488A (en) * 1989-04-28 1990-11-30 Mitsubishi Kakoki Kaisha Ltd Method and apparatus for drying granule
JPH03191288A (en) * 1989-12-19 1991-08-21 Yanmar Agricult Equip Co Ltd Grain drying apparatus

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5623237B2 (en) * 2010-10-26 2014-11-12 八尋産業株式会社 Vacuum drying system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02290488A (en) * 1989-04-28 1990-11-30 Mitsubishi Kakoki Kaisha Ltd Method and apparatus for drying granule
JPH03191288A (en) * 1989-12-19 1991-08-21 Yanmar Agricult Equip Co Ltd Grain drying apparatus

Also Published As

Publication number Publication date
JPH0454875B2 (en) 1992-09-01

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