JPH0454875B2 - - Google Patents

Info

Publication number
JPH0454875B2
JPH0454875B2 JP24292885A JP24292885A JPH0454875B2 JP H0454875 B2 JPH0454875 B2 JP H0454875B2 JP 24292885 A JP24292885 A JP 24292885A JP 24292885 A JP24292885 A JP 24292885A JP H0454875 B2 JPH0454875 B2 JP H0454875B2
Authority
JP
Japan
Prior art keywords
drying
grain
drying chamber
container
air
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.)
Expired
Application number
JP24292885A
Other languages
Japanese (ja)
Other versions
JPS62106280A (en
Inventor
Kokichi Hanaoka
Kyoshi Tamegai
Hiroyuki Sekine
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

Links

Landscapes

  • Drying Of Solid Materials (AREA)

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 Industrial Application The present invention relates to a grain drying apparatus for drying grain under reduced pressure in a constant constant temperature state.

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
つ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、真空乾燥や凍結乾燥等雰囲
気を真空にすることによつて、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。
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アン
を用いて加熱、減圧して乾燥する方法も行われて
いる。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平衝
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。
Conventional technology Conventionally, as a method for forced drying of materials to be dried,
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. All of these methods are heat-dependent drying methods that use heat to promote the vaporization of moisture within the material to be dried. On the other hand, drying methods such as vacuum drying and freeze drying are also known in which water is removed by reducing the vapor pressure of water by creating a vacuum atmosphere.
Furthermore, there is also a method of drying by heating and reducing pressure using a fan that exhausts air while generating heat, as described in, for example, Japanese Patent Laid-Open No. 57-19582. Further, as a drying apparatus for grains, etc. by the above-mentioned method of drying by heating and reducing pressure, for example, JP-A-59
A device has been proposed in which a hollow chamber having a decompression frictional heat generating mechanism and a granule storage chamber are formed so as to be ventilated, as described in Japanese Patent No. 18344.

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、蒸発熱によつ
て水分を除去するので、水1g当り100℃で
539.8cal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。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。
Problems to be Solved by the Invention The conventional heat-dependent drying method described above removes moisture by heat of evaporation, so it
It requires 539.8 cal of heat of vaporization, requires a large heat source, and has the disadvantage of high running costs. Further, heat-dependent drying methods have problems not only in drying efficiency but also in drying finish. That is, it is difficult to uniformly dry the inside and surface of the article to be dried;
Overdrying of the surface or heating may cause structural changes and the surface may harden.

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、装置が高価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。また熱を出しながら排気するフア
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
圧度が下がつてしまい温度と減圧度を同雑に制御
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。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つ
た。
Furthermore, although vacuum drying and freeze drying methods have relatively high drying efficiency, they are currently only used for drying special products because the equipment is expensive and the cost is high. In addition, conventional equipment that uses a fan to heat and reduce pressure to dry while emitting heat will heat 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 vacuum will increase. This method cannot be satisfactorily applied to the drying of grains, which requires drying at a relatively low temperature. Furthermore, with conventional drying apparatuses in which granular articles such as grains are dried in a stationary state within a drying chamber, sufficient ventilation is not provided between the grains, making it impossible to dry them satisfactorily.

而して本発明は、上記従来技術の欠点に鑑み創
案されたものであつて、乾燥効率及び乾燥仕上り
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。
The present invention was 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. This is the purpose.

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、断熱材及び耐圧材によつて構成され
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、
排気は排気装置3によつて行ない、且つ一定の減
圧度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、乾燥室内を一定恒温状態かつ一定減
圧状態にして、穀物を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た。
The present invention employs a method of providing two systems for 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 uses the cooling and heating device 9,
Exhaust is performed by the exhaust device 3, and a certain amount of outside air is introduced from the inlet in order to maintain a constant degree of pressure reduction. 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 inside of the drying chamber in a constant constant temperature state and a constant reduced pressure state, and to rotate the grain inside the grain container. I dried 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
に入れてセツトし、電源入れて作動させると排気
装置3によつ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平衝になつ
てその状態で維持される。また前記室内は冷暖装
置9によつて一定温度に保持される。穀物容器1
2内の穀物は、該容器内を移動しながら減圧によ
つてその水分が表面に移動し送風機11によつて
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
記室内の湿度を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。
Effect: Grain to be dried is placed in the container 12 in the drying chamber.
When the drying chamber is set up and the power is turned on, the pressure inside the drying chamber is reduced by the exhaust device 3, but once the pressure reaches a certain degree, it is maintained in that state as it balances out with the air from the outside air inlet. Further, the interior of the room is maintained at a constant temperature by a cooling/heating device 9. Grain container 1
As the grains in the container move inside the container, water is moved to the surface by the 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 acts to reduce the humidity in the room.
Drying is carried out continuously, efficiently and uniformly.

実施例 以下、本発明の実施例を図面に基づいて説明す
る。
Embodiments Hereinafter, embodiments of the present invention will be described based on the drawings.

第1図は本発明に係る穀物乾燥装置の一実施例
を示す概略側断面図であり、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は乾燥室であり、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た筐
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アンであり、該排気用フア
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
真空ポンプを採用しても良い。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より乾燥室1内に吸気される。従つて、乾燥室
内の吸排気はその温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 comprised of a casing 2 made of a pressure-resistant material that can withstand reduced pressure and is filled with a heat insulating material. 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 air from the exhaust fan passes through the heat exchanger 8. Then, it is discharged to the outside air from the external exhaust port 5. Note that a vacuum pump may be used as the exhaust device. On the other hand, 7 is an external intake port, and the outside air taken in through the external intake port passes through a heat exchanger 8 as shown in the figure, and is taken into the drying chamber 1 through the internal intake port 6. Therefore, heat is exchanged between the intake and exhaust air in the drying chamber in the heat exchanger according to the temperature difference, so there is little energy loss, and the outside air is drawn into the drying chamber at a temperature close to the temperature inside the drying chamber.

9は乾燥室内を一定恒温にするための冷暖装置
であり、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、室内の空気を拡散して後述する穀物容器
に一定風量を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を飛散させる。
Reference numeral 9 denotes a heating/cooling device for keeping the inside of the drying chamber at a constant constant temperature, and any device capable of dissipating and absorbing 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 diffuses the air in the room and applies a constant amount of air to the grain container, which will be described later, to scatter a film of water, which is a fluid film, that has moved onto 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
ようにホツパー16aとホツパー16b及び該両
ホツパーを連結連通する移動路17とを一体に形
成した容器単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ツパー開口部は、
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によつて被われている。また該
容器のホツ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つている。なお、19は移
動路17間に設けられた通風用空間部であり、1
3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
よつて間欠的に回転する。
Reference numeral 12 denotes a grain drying container, which is installed in the drying chamber via mounting legs 14 so as to be able to rotate intermittently. As shown in FIG. 2, the grain drying container is constructed by arranging a plurality of individual containers in which a hopper 16a, a hopper 16b, and a moving path 17 connecting and communicating the two hoppers are integrally formed. And the hopper opening of the grain drying container is
The container is covered with lids 18 and 19 that can be opened and closed so that grains can be taken in and out of the container. 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. Note that 19 is a ventilation space provided between the moving paths 17;
3 is a rotating shaft of the grain drying container, and 15 is
This is a rotating motor, and is intermittently rotated 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の一方のホツパー16aに穀物を入れる
と、穀物は自然落下により移動路17を通つて下
方のホツパー16b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1
5が作動して、穀物乾燥容器12を反転させ、以
後前記した動作を繰り返す。一方、乾燥室1内
は、排気フアン3の作動に一定の減圧状態にな
り、しかも冷暖装置によつ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
面に移動する。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を通過することによつて前記網状材から侵
入して飛散させて、穀物を均一に乾燥する。
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 hopper 16b. When the movement is completed, an appropriate control device acts to control the rotational drive motor 1.
5 is activated to invert the grain drying container 12 and repeat the above-described operation thereafter. On the other hand, inside the drying chamber 1, the pressure is reduced to a certain level due to the operation of the exhaust fan 3, and the temperature is maintained at a certain 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 enters through the net-like material and is scattered by the air from the blower 11 passing through the ventilation space 19 during the movement, thereby uniformly drying the grain.

上記実施例の装置を使用して、減圧するための
排気フアンを1.5kw出力で作動させて、800mmAq
の減圧度に保ち、乾燥室内を20℃の恒温状態で、
米50Kgを10時間で乾燥した。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 device of the above example, the exhaust fan for reducing pressure was operated at 1.5kw output, and 800mmAq was generated.
Maintain a reduced pressure of , and keep the drying room at a constant temperature of 20°C.
Dry 50 kg of rice in 10 hours. As a result, the scent,
It was possible to obtain high quality rice with excellent color and taste.

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
部吸気口7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 was installed at the top of the housing 2 to radiate or absorb heat directly into the drying chamber, but the cooling/heating device was installed at the external intake port 7 of the heat exchanger 8. It's okay. In addition, this device
It goes without saying that it 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.

(イ) 減圧乾燥であるので多大な熱源を必要とせ
ず、しかも冷暖装置によつて乾燥室内を被乾燥
物の乾燥適温に任意に設定できるので、乾燥効
率が卓越し、ランニングコストの大幅な低減
と、他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。
(b) Since it is drying under reduced pressure, it does not require a large heat source, and the inside of the drying chamber can be arbitrarily set to the appropriate temperature for drying the material to be dried using a cooling/heating device, resulting in outstanding drying efficiency and a significant reduction in running costs. This allows us to 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、穀物が容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く乾燥させるこ
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 the container, so that the grain can be dried evenly and efficiently.

(ハ) 送風機により穀物表面に移動した水の被膜を
効率的に飛散させ、且つ排気装置によつて連続
的に除湿されるので、連続的に均一な乾燥が行
われる。
(c) Since the film of water that has moved to the surface of the grain is efficiently scattered by the blower and continuously dehumidified by the exhaust device, uniform drying is performed continuously.

(ニ) 装置が簡単であり、かつ簡便に操作でき、ま
た、多大な熱源を必要としないから安全であ
る。
(d) 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つて、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
ネルギー効果を一段と高めることができる。
(e) By providing a heat exchanger, heat is exchanged between the exhaust air and the intake air, reducing energy loss and further increasing the energy saving effect.

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

第1図は、本発明に係る穀物乾燥装置の一実施
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:筐体、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:熱交換器、9:冷暖装置、
11:送風機、12:穀物乾燥容器、16a,1
6b:ホツパー、17:移動器。
FIG. 1 is a side sectional view of one embodiment of the grain drying apparatus according to the present invention, and FIG. 2 is a side view of the grain container thereof. 1: Drying room, 2: Housing, 3: Exhaust device, 4: Internal exhaust port, 5: External exhaust port, 6: Internal intake port,
7: External intake port, 8: Heat exchanger, 9: Cooling/heating device,
11: Blower, 12: Grain drying container, 16a, 1
6b: hopper, 17: mover.

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台のホツパーの連結体に
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ア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 material and pressure-resistant material, 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. a rotatable grain container installed in the drying chamber and made of ventilation material such as a mesh material; A grain drying device comprising a blower installed in a drying chamber and a heating and cooling 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 JPS62106280A (en) 1987-05-16
JPH0454875B2 true 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 (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012093023A (en) * 2010-10-26 2012-05-17 Yahiro Sangyo Co Ltd Vacuum drying system

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2764607B2 (en) * 1989-04-28 1998-06-11 三菱化工機株式会社 Method and apparatus for drying powders
JP2808030B2 (en) * 1989-12-19 1998-10-08 ヤンマー農機株式会社 Grain drying equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012093023A (en) * 2010-10-26 2012-05-17 Yahiro Sangyo Co Ltd Vacuum drying system

Also Published As

Publication number Publication date
JPS62106280A (en) 1987-05-16

Similar Documents

Publication Publication Date Title
CN205580098U (en) Anti -oxidation flash dryer
US3266169A (en) Vacuum freeze drying apparatus
KR101878643B1 (en) Mineral heat drying divice and mineral heat drying method
JPH04201522A (en) Vacuum drying device
WO2017101123A1 (en) Solar energy heating and drying system and drying method
JPH0454875B2 (en)
SU1657893A1 (en) Geliodrier-hothouse
KR100636892B1 (en) A drier
JPS61271032A (en) Method and apparatus for regenerating adsorbent by dehumidification
CA1210287A (en) Heating process and its apparatus in reducing air pressure within a chamber at a balanced level
PL174760B1 (en) Apapratus for drying and preserving wood and wooden products
KR200354499Y1 (en) A drier
JPH0684821B2 (en) Batch type humidity controller
RU2221974C2 (en) Microwave unit for lumber dry
JPS62106279A (en) Constant-temperature decompression drying method and device thereof
JPS6422323A (en) Dry type dehumidification apparatus
JPS59122856A (en) Pressure reduced and balanced frictional heat generating device
KR960007792B1 (en) Food dryer using the sunlight
JPS61128085A (en) Drier
JPH02208485A (en) Drying of lumber and lumber drying device
JPS62138676A (en) Rotary type decompression drier
JPH0317462B2 (en)
JPS5484654A (en) Clothes dryer
JPH01159581A (en) Thermostatic decompression drier
SU1391579A1 (en) Unit for drying tobacco