JPS6142181B2 - - Google Patents
Info
- Publication number
- JPS6142181B2 JPS6142181B2 JP54163934A JP16393479A JPS6142181B2 JP S6142181 B2 JPS6142181 B2 JP S6142181B2 JP 54163934 A JP54163934 A JP 54163934A JP 16393479 A JP16393479 A JP 16393479A JP S6142181 B2 JPS6142181 B2 JP S6142181B2
- Authority
- JP
- Japan
- Prior art keywords
- drying
- grains
- air
- moisture content
- chamber
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/52—Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
Landscapes
- Drying Of Solid Materials (AREA)
Description
【発明の詳細な説明】
本発明は乾燥室内へ相当厚さに亘り静置状態の
もとに上積み収容した穀物に循環乾燥風を浴びせ
て乾燥せしめた場合にあつても、乾燥風の送風側
と排風側との間に生じる乾燥差を無くして収容し
た総ての穀物を均一な仕上含水率に乾燥すること
ができる穀物均一乾燥方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for drying grains stored in a drying chamber over a considerable thickness in a stationary state by blowing circulating drying air on them. The present invention relates to a method for uniformly drying grains, which can dry all stored grains to a uniform finished moisture content by eliminating the drying difference between the side and the exhaust side.
一般に乾燥室内へ静置状態のもとに或る堆積高
さをもつて収容した穀物に乾燥熱風を一方通風状
態のもとに浴びせて乾燥作業を継続すると、乾燥
熱風の送風側に面した穀物は速かに水分を蒸発し
て乾燥が進行される反面、排風側に面した穀物は
送風側において蒸発した水分を吸湿した湿潤性空
気を浴びることで仲々乾燥が進行せず、その結
果、送風側と排風側とでは穀物の乾燥度に差が生
じ、総ての穀物を均一に乾燥させることができな
い。そして上記の現象は穀物の堆積高さに比例し
て大きくなるものである。 In general, if the drying process is continued by blowing dry hot air on grains stored at a certain stacking height in a drying room under a static state, the grains facing the side where the dry hot air is blown will be On the other hand, grains facing the ventilation side are exposed to humid air that has absorbed the evaporated moisture on the ventilation side, and drying does not proceed as quickly as possible. There is a difference in the degree of dryness of the grains between the ventilation side and the ventilation side, and it is not possible to dry all the grains uniformly. The above phenomenon increases in proportion to the height of the grain pile.
従つて静置状態のもとで穀物の乾燥作業を行う
場合は乾燥差を生じさせない程度の堆積層に規制
する必要がある。 Therefore, when drying grains under a stationary condition, it is necessary to control the accumulated layer to such an extent that no difference in drying occurs.
然かし乍ら上述のような堆積層に規制すると大
量の穀物を均一に乾燥させるためには多くの乾燥
施設や労力が必要となり、実際面において不可能
である。 However, if the grains are restricted to the above-mentioned sedimentary layer, a large amount of drying facilities and labor will be required to uniformly dry a large amount of grain, which is practically impossible.
そこで本発明者は静置乾燥作業時に、
穀物が乾燥風をを浴びると穀物中の水分が蒸
発されて穀物層より排出される乾燥風は吸湿し
て湿潤性空気となること。 Therefore, the inventor of the present invention discovered that during stationary drying work, when grains are exposed to drying air, the moisture in the grains is evaporated, and the drying air discharged from the grain layer absorbs moisture and becomes humid air.
或る程度乾燥された穀物に湿潤性空気を浴び
せると乾燥された穀物は吸湿反応現象により湿
潤性空気中の水分を逆に吸湿して穀物自体の水
分が増量されるということ。 When moist air is applied to grains that have been dried to a certain extent, the dried grains absorb moisture from the humid air through a hygroscopic reaction phenomenon, increasing the moisture content of the grains themselves.
を応用すれば、静置状態のもとで相当高さに亘り
堆積された穀物といえども総て均一の仕上含水率
に乾燥させることができると考えたものである。It was thought that if this method was applied, it would be possible to dry all the grains, even if they were piled up over a considerable height under static conditions, to a uniform finished moisture content.
本発明は前記に鑑み、乾燥室内へ静止状態のも
とに上積み収容した穀物に対し略20℃〜30℃の循
環乾燥風を浴びせて乾燥し、次いで前記循環乾燥
風による乾燥作用で送風側に面した穀物が最終の
仕上含水率に近づいたら循環乾燥風の代りに湿潤
常温風を循環させながら連続状に穀物に浴びせて
堆積高さに関係なく総ての穀物を均一な仕上含水
率となるように乾燥させることができる穀物均一
乾燥方法を提供したものであつて、以下に本発明
方法を使用した装置の構成を添附図面に示された
好適な一実施例について説明する。 In view of the above, the present invention has been developed by drying the grains stacked in a drying chamber in a stationary state by blowing circulating drying air at approximately 20°C to 30°C, and then drying the grains by the drying action of the circulating drying air. When the facing grain approaches the final finished moisture content, instead of the circulating drying wind, humid room temperature air is circulated and continuously showered on the grain, so that all the grains have a uniform finished moisture content regardless of the pile height. The present invention provides a method for uniformly drying grains that can be dried in a manner similar to that of the present invention, and the construction of an apparatus using the method of the present invention will be described below with reference to a preferred embodiment shown in the accompanying drawings.
図面において、1は周囲を壁板2で囲つて形成
した乾燥庫であつて、該乾燥庫1の内部には乾燥
室3と循環室4とが併設されており、該循環室4
の上部は乾燥室3の上方に、又下部は乾燥室3の
底部に敷設された通気平床板6を介して配設した
通風室5にそれぞれ接続してある。上記循環室4
内には循環用の送風機7が配置されると共に、該
送風機7の下段には乾燥熱風又は湿潤常温風を起
成させるためのヒートポンプ8が設置されてい
る。該ヒートポンプ8は圧縮機9と凝縮器10と
受液槽11と膨脹弁12および蒸発器13とから
成り立つており、凝縮器10と蒸発器13とは循
環室4内に上下に亘り間隔をおいてそれぞれ設置
されている。そして圧縮機9と凝縮器10とは高
圧ガス管14を介して接続され、凝縮器10と受
液槽11とは接続管15により接続され、又受液
槽11は膨脹弁12を備えた液体管16を介して
蒸発器13に、更に蒸発器13は吸収管17を介
して圧縮機9にそれぞれ接続して一定の循環経路
を形成せしめてある。18は乾燥室3内に静置状
態の下に上積み収容された上層部の穀物の含水率
を測定するための含水率検知器であつて、該含水
率検知器18は制御器19を経て圧縮機9に接続
されている。なお、該含水率検知器18は中層部
に設けてもよいものとする。20は循環室4の底
部に装着された脱水管である。 In the drawing, reference numeral 1 denotes a drying chamber surrounded by wall plates 2, and inside the drying chamber 1, a drying chamber 3 and a circulation chamber 4 are installed.
The upper part of the drying chamber 3 is connected to the upper part of the drying chamber 3, and the lower part of the drying chamber 3 is connected to a ventilation chamber 5 provided through a ventilation flat plate 6 installed at the bottom of the drying chamber 3. The above circulation chamber 4
An air blower 7 for circulation is disposed inside, and a heat pump 8 for generating dry hot air or humid normal temperature air is installed below the air blower 7. The heat pump 8 is composed of a compressor 9, a condenser 10, a liquid receiving tank 11, an expansion valve 12, and an evaporator 13. They are installed separately. The compressor 9 and the condenser 10 are connected via a high-pressure gas pipe 14, the condenser 10 and the liquid receiving tank 11 are connected by a connecting pipe 15, and the liquid receiving tank 11 is equipped with an expansion valve 12. The evaporator 13 is connected via a pipe 16 to the compressor 9 via an absorption pipe 17, thereby forming a constant circulation path. Reference numeral 18 denotes a moisture content detector for measuring the moisture content of the upper layer of grain stored in the drying chamber 3 in a static state. It is connected to machine 9. Note that the moisture content detector 18 may be provided in the middle layer. 20 is a dehydration pipe attached to the bottom of the circulation chamber 4.
上述の乾燥庫1には図面に示されていないが乾
燥室3内に穀物を搬入させたり或は搬出するため
の搬入、搬出装置が設けられていることは勿論で
ある。 Although not shown in the drawings, the drying chamber 1 described above is of course provided with a loading and unloading device for loading and unloading grains into and out of the drying chamber 3.
次に本発明の方法について説明する。 Next, the method of the present invention will be explained.
今、適宜の搬入装置(図示せず)を用いて高含
水率例えば略26%の穀物を所定の堆積層が形成さ
れるよう静置状態の下に乾燥室3内へ上積み収容
する。次いで循環用の送風機7を始動すると同時
にヒートポンプ8を運転させる。さすれば圧縮機
9で圧縮された高圧ガスが凝縮器10に送られ、
ここで冷されて凝縮熱を放熱し、この熱エネルギ
ーによつて循環室4内を流通する空気を加温して
乾燥風を起成させる。そして凝縮器10のガスは
凝縮熱を奪われて液体となり、受液槽11に還元
された後、更に膨脹弁12を通つて減圧され、こ
こで蒸発して熱を吸収し循環室4内に通風室5を
介して吸入される空気を冷却して露点以下にし脱
湿する。 Now, using a suitable loading device (not shown), grains with a high moisture content, for example, about 26%, are stacked and stored in the drying chamber 3 under a static condition so that a predetermined piled layer is formed. Next, the circulation blower 7 is started and the heat pump 8 is operated at the same time. Then, the high pressure gas compressed by the compressor 9 is sent to the condenser 10,
Here, the air is cooled and condensed heat is radiated, and this thermal energy warms the air flowing in the circulation chamber 4 to generate dry air. Then, the gas in the condenser 10 is deprived of condensation heat and becomes a liquid, and after being returned to the liquid receiving tank 11, the pressure is further reduced through the expansion valve 12, where it evaporates, absorbs heat, and flows into the circulation chamber 4. The air taken in through the ventilation chamber 5 is cooled to below the dew point and dehumidified.
従つて、加温された乾燥風を循環室4上方より
実線矢印方向に乾燥室3内を流通させて穀物に浴
びせ乾燥を行えば、乾燥風は穀物自体から蒸発さ
れる水分を吸収して吸湿乾燥風となつて通風室5
内に排風された後、循環室4内に吸引され、蒸発
器13に噴き当り氷結することなく脱水されて乾
燥空気となり再び凝縮器10で加温され乾燥室3
に送り込まれる循環作用を反復する。この乾燥風
の反復循環作用では穀物は次第に除湿乾燥され
る。そして送風側に面した穀物層即ち本実施例に
あつては乾燥室3上部の穀物が最終の仕上含水率
例えば略14%に近づいたことを含水率検知器18
が検知すると制御器19を介して圧縮機9の運転
を停止し、ヒートポンプ8の作動を停止させる。
さすれば送風機7により乾燥室3と循環室4内を
循環流通されていた乾燥風はヒートポンプによる
除湿作用を受けない乾燥風となつて、穀物層中を
通過して通風室5内に排出され脱湿されないこと
で水分を吸湿した湿潤性空気となる。従つてこの
湿潤性の常温乾燥風を送風機7により前述と同様
の流通方向に向け乾燥室3内へ流通して静置状態
の穀物層に浴びせると、最終の仕上含水率近くま
で乾燥された上層の穀物層は流通する湿潤性常温
乾燥風中に含まれた水分を吸湿反応現象により逆
に吸湿して穀物自体の含水率が高まり、乾燥風の
湿度が下がる。そしてこのようになつた低湿乾燥
風が次第に上層より下層に亘り穀物層を通過する
ので下層に位置された穀物層の水分は乾燥風中に
吸湿され、乾燥が進行するものである。そして吸
湿し完全な湿潤性常温乾燥風は循環室4を通り再
び上層の穀物に浴びせられ前述作用を反復する。 Therefore, if heated drying air is passed through the drying chamber 3 from above the circulation chamber 4 in the direction of the solid line arrow and is applied to the grains for drying, the drying air absorbs the moisture evaporated from the grains themselves and absorbs moisture. Ventilation room 5 as dry wind
After being exhausted into the air, it is sucked into the circulation chamber 4, hits the evaporator 13, dehydrates it without freezing, becomes dry air, and is heated again in the condenser 10 to form the drying chamber 3.
Repeat the cyclical action that is sent to the This repeated circulation of drying air gradually dehumidifies and dries the grain. The moisture content detector 18 detects when the grain layer facing the ventilation side, that is, the upper part of the drying chamber 3 in this embodiment, approaches the final finished moisture content, for example, about 14%.
When detected, the operation of the compressor 9 is stopped via the controller 19, and the operation of the heat pump 8 is also stopped.
Then, the drying air that was being circulated through the drying chamber 3 and the circulation chamber 4 by the blower 7 becomes drying air that is not affected by the dehumidification effect of the heat pump, passes through the grain layer, and is discharged into the ventilation chamber 5. Since the air is not dehumidified, it becomes humid air that has absorbed moisture. Therefore, when this humid room-temperature drying air is directed into the drying chamber 3 by the blower 7 in the same direction as described above and is applied to the grain layer in a stationary state, the upper layer is dried to a moisture content close to the final finishing moisture content. The grain layer reversely absorbs moisture contained in the circulating humid room-temperature dry air through a hygroscopic reaction phenomenon, increasing the moisture content of the grain itself and lowering the humidity of the dry air. As the low-humidity drying wind gradually passes through the grain layer from the upper layer to the lower layer, the moisture in the lower grain layer is absorbed by the drying wind, and drying progresses. The moisture-absorbing, completely humid room-temperature drying air passes through the circulation chamber 4 and is again applied to the grains in the upper layer, repeating the above-mentioned process.
その結果、上層に位置した穀物層の乾燥度と下
層に位置した穀物層の乾燥度との差が次第に減少
され、遂に乾燥度の差がなくなり、穀物の総てが
最終の仕上含水率例えば略14%となつたら送風機
7の運転を停止し、乾燥作業を終了させる。 As a result, the difference between the dryness of the grain layer located in the upper layer and the dryness of the grain layer located in the lower layer is gradually reduced, until the difference in dryness disappears, and all of the grains have a final finished moisture content, e.g. When it reaches 14%, the operation of the blower 7 is stopped and the drying work is completed.
要するに本発明は、乾燥室3内へ静置状態のも
とに上積み収容した穀物に対し循環乾燥風を浴び
せて乾燥すると共に前記循環乾燥風による乾燥作
用で送風側に面した穀物が最終の仕上含水率に近
づいたら循環乾燥熱風の代りに湿潤常温風を循環
させながら連続的に穀物に浴びせて均一の仕上含
水率に乾燥させるようにしたから、高含水率の穀
物を相当高さに亘り静置状態のもとに乾燥室3内
へ上積み収容して乾燥作業を遂行させても、乾燥
風の送風側に面した穀物の乾燥度と排風側に面し
た穀物層の乾燥度との差を無くし、総ての穀物を
希望する仕上含水率となるように均一に乾燥させ
ることができる効果を奏する。 In short, in the present invention, the grains stacked and stored in the drying chamber 3 in a stationary state are dried by blowing circulating drying air, and the drying action of the circulating drying air allows the grains facing the ventilation side to be finished in the final finish. When the moisture content approaches the grain, instead of the circulating drying hot air, humid room temperature air is circulated and continuously exposed to the grain to dry it to a uniform finished moisture content. Even if the drying work is carried out by stacking the grains in the drying chamber 3 under the drying condition, there will be a difference in the dryness between the dryness of the grain facing the drying air blowing side and the dryness of the grain layer facing the ventilation side. This has the effect that all the grains can be uniformly dried to the desired finished moisture content.
図面は本発明方法を使用した装置の一実施例で
あつて、縦断正面図を示す。
1……乾燥庫、3……乾燥室。
The drawing shows an embodiment of an apparatus using the method of the present invention, and shows a longitudinal sectional front view. 1...Drying room, 3...Drying room.
Claims (1)
穀物に対し循環乾燥風を浴びせて乾燥すると共
に、前記循環乾燥風による乾燥作用で送風側に面
した穀物が最終の仕上含水率に近づいたら循環乾
燥風の代りに湿潤常温風を循環させながら連続的
に穀物に浴びせて均一の仕上含水率に乾燥せしめ
たことを特徴とする穀物均一乾燥方法。1. Dry the grains stacked in a drying chamber under a static state by blowing circulating drying air on them, and when the grains facing the ventilation side approach the final finished moisture content due to the drying effect of the circulating drying air. A method for uniformly drying grains, which is characterized in that the grains are dried to a uniform finished moisture content by continuously blowing humid room-temperature air on the grains while circulating instead of circulating drying air.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16393479A JPS5687790A (en) | 1979-12-17 | 1979-12-17 | Method of uniformly drying cereal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16393479A JPS5687790A (en) | 1979-12-17 | 1979-12-17 | Method of uniformly drying cereal |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5687790A JPS5687790A (en) | 1981-07-16 |
| JPS6142181B2 true JPS6142181B2 (en) | 1986-09-19 |
Family
ID=15783594
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16393479A Granted JPS5687790A (en) | 1979-12-17 | 1979-12-17 | Method of uniformly drying cereal |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5687790A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0292191A (en) * | 1988-09-29 | 1990-03-30 | Shibasoku Co Ltd | Effective value measuring instrument for video noise |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0641832B2 (en) * | 1984-08-21 | 1994-06-01 | 豊国工業株式会社 | Grain drying method and apparatus |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS51126270U (en) * | 1975-12-01 | 1976-10-13 |
-
1979
- 1979-12-17 JP JP16393479A patent/JPS5687790A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0292191A (en) * | 1988-09-29 | 1990-03-30 | Shibasoku Co Ltd | Effective value measuring instrument for video noise |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5687790A (en) | 1981-07-16 |
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