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JPS5826516B2 - Circulating grain dryer - Google Patents
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JPS5826516B2 - Circulating grain dryer - Google Patents

Circulating grain dryer

Info

Publication number
JPS5826516B2
JPS5826516B2 JP53096819A JP9681978A JPS5826516B2 JP S5826516 B2 JPS5826516 B2 JP S5826516B2 JP 53096819 A JP53096819 A JP 53096819A JP 9681978 A JP9681978 A JP 9681978A JP S5826516 B2 JPS5826516 B2 JP S5826516B2
Authority
JP
Japan
Prior art keywords
grain
drying
temperature
tank
hot 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
JP53096819A
Other languages
Japanese (ja)
Other versions
JPS5523877A (en
Inventor
祐治 金藤
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.)
Iseki Agricultural Machinery Mfg Co Ltd
Original Assignee
Iseki Agricultural Machinery Mfg Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Iseki Agricultural Machinery Mfg Co Ltd filed Critical Iseki Agricultural Machinery Mfg Co Ltd
Priority to JP53096819A priority Critical patent/JPS5826516B2/en
Publication of JPS5523877A publication Critical patent/JPS5523877A/en
Publication of JPS5826516B2 publication Critical patent/JPS5826516B2/en
Expired legal-status Critical Current

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  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】 本発明は、穀物乾燥装置に係るものである。[Detailed description of the invention] The present invention relates to a grain drying device.

循環式穀物乾燥装置にも2種類ある。There are two types of circulating grain dryers.

一つは熱風温度を35℃以下とした循環式乾燥装置であ
り、循環させることにより攪拌効果を期待し、数10回
も循環させて乾燥を終了する。
One is a circulation type drying device in which the temperature of the hot air is set to 35° C. or lower, and the circulation is expected to produce an agitation effect, and the drying is completed by circulating the air several dozen times.

以前は、全べて上記の構成であるが、最近は殆んど製作
されていない。
In the past, all of them had the above configuration, but recently they are hardly manufactured.

他の一つは、流下式調湿タンクの下部に、該タンクと連
通している流下式乾燥室を設け、側方位置には、乾燥室
から調湿タンクに至る循環用昇降機を設けたものであり
、熱風温度は略50’Cと高く、乾燥室内で表皮部分を
主力的に乾燥させ、これを調湿タンク内に上積み還元し
、調湿タンク内を1〜2時間位かけてゆっくり流下させ
、その間に、乾燥した表皮部分により、内部の水分を吸
湿させ、これを5回程反覆(5回循環させる)させるこ
とにより乾燥を終了するものであり(特公昭50−19
426号公報)、現在は、殆んど、この種の循環式穀物
乾燥機が製造販売されている。
The other type is a type in which a flow-down type drying chamber is provided at the bottom of the flow-down type humidity control tank and is connected to the tank, and a circulation elevator is installed at a side position to reach the humidity control tank from the drying room. The hot air temperature is as high as approximately 50'C, and the epidermis is mainly dried in the drying room, which is then piled up and returned to the humidity control tank, where it slowly flows down for about 1 to 2 hours. During this period, the dried epidermis absorbs the internal moisture, and this process is repeated five times (circulated five times) to complete the drying process.
No. 426), and currently most of this type of circulating grain dryer is manufactured and sold.

本発明も後者の乾燥装置を改良したものである。The present invention is also an improvement on the latter drying device.

後者の乾燥装置は、略50℃と高い熱風を使用するが、
それは、穀物の表皮をすばやく乾燥させたいためである
The latter drying equipment uses hot air as high as approximately 50°C,
This is because we want to quickly dry the outer skin of the grain.

50℃というように高い温度の熱風だと、たちまち乾燥
させうる。
Hot air at temperatures as high as 50 degrees Celsius can quickly dry things out.

しかし、上記の温度の熱風を、常に用いることは良策で
ない。
However, it is not a good idea to always use hot air at the above temperature.

すなわち、その日の外気温度が相当に高い日の米穀温度
は最初から相当に上昇しているから、これに高温熱風を
与えると乾燥が進みすぎて胴割れを起す心配がある。
In other words, on days when the outside air temperature is quite high, the temperature of the rice has already risen considerably from the beginning, so if high-temperature hot air is applied to it, there is a risk that it will dry out too much and cause cracking.

また、外気温が異常に低い日は、通常の高温熱風でもな
かなか乾燥しない。
Also, on days when the outside temperature is abnormally low, even normal high-temperature hot air will not dry the skin.

また、穀物の収容量も軽視することはできない。Also, the grain capacity cannot be underestimated.

たとえば、所定量を収容しうる調湿タンクは、その所定
量を充満したとき予定の略2時間で循環するように形成
されているのであるから、これに半分しか充填しないと
したら1時間で循環することになり、穀温か充分下降し
ないうちに次の熱風を受けて、次第に乾燥が多くなり過
ぎることになる。
For example, a humidity control tank that can hold a certain amount of water is designed so that when it is filled with the specified amount, it will circulate in about two hours, so if it is only half filled, it will circulate in one hour. As a result, the grain will be exposed to the next round of hot air before the grain temperature has sufficiently decreased, resulting in excessive drying.

したがって、外気温と穀物の収容量の変化に基づいてそ
の熱風温度を変えた力がよいのであり、本発明は、流下
式穀物調湿用タンクの下部に前記タンクと連通している
流下式穀物乾燥室を形成し、側方位置には前記乾燥室よ
り排出された穀物を上部の前記調湿用タンク内に上積み
還元させる昇降機を設けた循環式穀物乾燥装置において
、該乾燥装置には外気温度検知器と前記調湿用タンクお
よび前記乾燥室に収容された総収容量を検知する検動量
を設け、前記両横動量を前記乾燥室の熱風発生装置に関
連的に結合した循環式穀物乾燥装置の構成としたもので
ある。
Therefore, it is preferable to change the temperature of the hot air based on changes in the outside temperature and the amount of grain stored, and the present invention provides a method for controlling the humidity of grains that is connected to the lower part of the tank for controlling the moisture content of grains. A circulating grain drying device that forms a drying chamber and is provided with an elevator at a side position that stacks and returns the grain discharged from the drying chamber into the humidity control tank at the top, the drying device has an outside air temperature. A circulating grain drying device, which is provided with a detector and a detection amount for detecting the total capacity accommodated in the humidity control tank and the drying chamber, and in which both the lateral movement amounts are connected to a hot air generator in the drying chamber. The structure is as follows.

図により説明すると、1は流下式穀物調湿タンクで、四
角状の空胴の大きなタンクであり、大量の穀物を収容し
うる(5石〜40石位)大きさに形成される。
To explain with a diagram, reference numeral 1 denotes a flowing-down type grain humidity control tank, which is a large tank with a rectangular cavity, and is formed in a size that can accommodate a large amount of grain (approximately 5 to 40 grains).

流下式穀物調湿タンク1の下部には、該タンク1と連通
している流下式乾燥室2を形成する。
A downstream drying chamber 2 communicating with the tank 1 is formed in the lower part of the downstream grain humidity control tank 1.

該流下式乾燥室2は垂直に流下する穀物に対して、水平
横方向に熱風を与えて穀物表皮を乾燥させるもので、送
風装置3(または吸風装置)を備えた火炉4を有する熱
風発生装置5を取付ける。
The down-flow drying chamber 2 applies hot air horizontally and laterally to the vertically flowing grain to dry the grain skin, and has a hot air generating furnace 4 equipped with an air blower 3 (or air suction device). Install device 5.

前記乾燥室2より排出した穀物は、側力に設けた循環用
昇降機6により上昇して調湿タンク1内に上積み還元さ
れる。
The grains discharged from the drying chamber 2 are lifted up by a circulation elevator 6 provided on the side, and then piled up in the humidity control tank 1 and returned.

しかして、前記火炉4は、主燃料制御バルブMVおよび
燃料ポンプSP等を介して燃料タンク7に連結し、前記
主燃料制御バルブMVは、外気温検知器8により制御さ
れるように形成する。
The furnace 4 is connected to the fuel tank 7 via a main fuel control valve MV and a fuel pump SP, and the main fuel control valve MV is controlled by an outside temperature detector 8.

第5図は、制御機構の一例である。FIG. 5 is an example of a control mechanism.

第5図に示されたものは、外気温検知器8の外、前記昇
降機6によって調湿タンク1内に収容される穀物の収容
量を検知しうる検知器9も備えており、前記検知器9の
作動によって前記主燃料制御バルブMVは制御されるよ
うに構成されている。
In addition to the outside temperature detector 8, the one shown in FIG. The main fuel control valve MV is controlled by the operation of 9.

前記第5図について説明すると、T1は燃料停止からモ
ーター停止迄のタイマー、Mはモーター用リレー、Aは
モータータイマーTMより前記タイマーT1への連動リ
レー、Hvは点火燃料用バルブ、T2は点火燃料供給時
間制御用タイマー、Hは点火ヒーター用すL/−1Pは
燃料ポンプSP用のリレー、■Rは流量設定用ボリュー
ムである。
To explain FIG. 5, T1 is a timer from fuel stop to motor stop, M is a motor relay, A is an interlocking relay from the motor timer TM to the timer T1, Hv is a valve for ignition fuel, and T2 is an ignition fuel. A timer for controlling the supply time, H is for the ignition heater, L/-1P is a relay for the fuel pump SP, and R is a volume for setting the flow rate.

本発明は上述の構成からなるものであるから、昇降機6
により穀物を調湿タンク1内に収容すると、その収容量
は検知器9により検知され、また、その時の気温を外気
温検知器8により検知し、自動制御回路により制御して
主燃料制御バルブMVを自動的に制御する。
Since the present invention has the above-described configuration, the elevator 6
When the grain is stored in the humidity control tank 1, the amount of grain stored is detected by the detector 9, and the temperature at that time is detected by the outside temperature detector 8, and the main fuel control valve MV is controlled by the automatic control circuit. control automatically.

したがって、調湿タンク1内への張込量(収容量)が十
分に多いときは、検知器9により前記主燃料制御バルブ
MVに油量を多く送るように信号を送って相当に高温の
熱風を作成し、熱風発生装置5より高温熱風を穀物に与
える。
Therefore, when the amount filled (accommodated amount) in the humidity control tank 1 is sufficiently large, the detector 9 sends a signal to the main fuel control valve MV to send a large amount of oil, and the hot air at a considerably high temperature is sent. A hot air generator 5 provides high-temperature hot air to the grains.

しかるときは、穀物の表皮は十分に乾燥するが昇降機6
により調湿タンク1内に上積みされると、その収容量が
十分に多いので長時間髪して流下し、再度乾燥室2に流
入するときは、乾燥前の状態に戻るので円滑に乾燥でき
る。
When this happens, the outer skin of the grain will be sufficiently dry, but the elevator 6
When the hair is piled up in the humidity control tank 1, the storage capacity is sufficiently large, so that the hair flows down for a long time, and when it flows into the drying chamber 2 again, it returns to the state before drying, so it can be dried smoothly.

また、調湿タンク1への収容量が少ないときは、調湿タ
ンク1内の流下時間は短かくなるので、前記検知器9に
より主燃料制御バルブMVに少ない油量を送るように信
号を出して、これる調節するものである。
Furthermore, when the amount of oil stored in the humidity control tank 1 is small, the time for the oil to flow in the humidity control tank 1 is shortened, so the detector 9 sends a signal to the main fuel control valve MV to send a small amount of oil. This is something that you can adjust accordingly.

また外気温が高い場合は、穀温それ自体も相当に高くな
っているから、低い温度の熱風を当てても穀温上昇は充
分に行なわれる。
Furthermore, when the outside temperature is high, the grain temperature itself is also considerably high, so even if low-temperature hot air is applied, the grain temperature will be sufficiently raised.

したがって、検知器8により検知した外気温により、外
気温が高いときは高いなりに油量を少なくシ、外気温が
低いなりに熱風温度を高くして、もって、外気温の状態
により過剰乾燥されたり、乾燥不足になることを防止す
るものである。
Therefore, depending on the outside temperature detected by the detector 8, when the outside temperature is high, the amount of oil is decreased as the outside temperature increases, and when the outside temperature is low, the hot air temperature is increased. This prevents drying or insufficient drying.

第6図は、外気温検知器及び張込量検知器より、主燃料
制御バルブM■を制御する構成図であり、第6図イは標
準構成図、第6図口は等価固定回路を設けた構成図、第
6図ハは記憶回路およびブザー回路を付設した構成図で
あるが、これらの回路自体は、外気温および張込量によ
り制御するという点を除くと、コンピューター回路とし
て極く普通のものである。
Figure 6 is a configuration diagram of controlling the main fuel control valve M■ from the outside temperature detector and the filling amount detector, Figure 6 A is a standard configuration diagram, and Figure 6 Port is an equivalent fixed circuit Figure 6C is a configuration diagram with a memory circuit and a buzzer circuit attached, but these circuits themselves are very ordinary computer circuits, except that they are controlled by the outside temperature and the amount of plug-in. belongs to.

従来公知の穀類乾燥装置の乾燥温度の自動制御は、例え
ば特公昭49−46743号公報とか実開昭53−54
874号公報に示されているように、乾燥風温度と穀物
自体の温度を検出し、雨検出信号より燃料供給量を加減
するように構成しているが、この方法によるときは、乾
燥風温度は常に例えば53℃という温度が適切である基
準が正しいものという考えと、穀温も例えば50℃がよ
いという考えがあってなりたっているものである。
Automatic control of the drying temperature of conventionally known grain drying devices is disclosed, for example, in Japanese Patent Publication No. 49-46743 and Japanese Utility Model Publication No. 53-54.
As shown in Publication No. 874, the temperature of the drying wind and the temperature of the grain itself are detected, and the fuel supply amount is adjusted based on the rain detection signal. This is based on the idea that the appropriate temperature standard is always 53°C, for example, and the idea that 50°C is also the best grain temperature.

しかし、前記前提は正しいものではない。However, the above assumption is not correct.

例えば、調湿タンクと流下式乾燥室に対する張込量が少
ないときは、上積みされた穀物が再び乾燥室内に流入す
る迄のサイクル時間が比例して短かくなるので、通常の
張込量の場合に比べて相当に低温としなければ、調湿時
間が不足して移しい胴割米を生じさせてしまう。
For example, when the amount of filling into the humidity control tank and the down-flow drying chamber is small, the cycle time until the top-loaded grain flows into the drying chamber again becomes proportionally shorter, so when the amount of filling is normal, Unless the temperature is considerably lower than that of the previous year, there will be insufficient time to adjust the humidity, resulting in cracked rice.

又乾燥風温度を53℃に設定すると、外気温が異常に低
いときは、調湿時間中に、予定より冷却されてしまって
、充分の乾燥が行なわれないし、外気温が異常に高いと
きは、穀温が高いまま再度乾燥を受けることになる。
Also, if the drying air temperature is set to 53℃, if the outside temperature is abnormally low, the air will be cooled more than expected during the humidity adjustment time, and sufficient drying will not be carried out, and if the outside temperature is abnormally high, , the grain will be dried again while the temperature remains high.

しかるに、本発明は前記のように構成したので、調湿タ
ンクと乾燥室に対する収容量が非常に少なくなったとき
は、サイクル時間に見合う低温の乾燥風温度で乾燥し、
又外気温が異常に低いときは、それなりに高い乾燥風温
度で乾燥するようにしたので、前記公知例のもつ欠陥を
防止できる。
However, since the present invention is configured as described above, when the capacity of the humidity control tank and drying chamber becomes very small, drying is performed at a low drying air temperature commensurate with the cycle time.
Furthermore, when the outside temperature is abnormally low, drying is performed at a relatively high drying air temperature, so that the defects of the above-mentioned known example can be avoided.

【図面の簡単な説明】 第1図は側面図、第2図は縦断正面図、第3図は乾燥室
横断面図、第4図は熱風供給装置の一部断面側面図、第
5図は制御回路図、第6図イ1口。 ハは構成図である。 符号の説明、1・・・・・・流下式穀物調湿タンク、2
・・・・・・流下式乾燥室、3・・・・・・送風装置、
4・・・・・・火炉、5・・・・・・熱風発生装置、6
・・・・・・循環用昇降機、7・・・・・・燃料タンク
、8・・・・・・外気温検知器、9・・・・・・張込量
検知器、M■・・・・・・主燃料制御バルブ、SP・・
・・・・燃料ポンプ、T1・・・・・・タイマー、T2
・・・・00点火燃料供給時間制御用タイマー、M・・
・・・・モーター用リレー、A・・・・・・連動リレー
、TM・・・・・・モーター用タイマー、H■・・・・
・・点火燃料用タイマー、H・・・・・・点火ヒーター
用リレー、P・・・・・・燃料ポンプ用リレー、VR・
・・・・・流量設定用ボリューム。
[Brief Description of the Drawings] Figure 1 is a side view, Figure 2 is a longitudinal front view, Figure 3 is a cross-sectional view of the drying chamber, Figure 4 is a partially sectional side view of the hot air supply device, and Figure 5 is a side view of the hot air supply device. Control circuit diagram, Figure 6 A. C is a configuration diagram. Explanation of symbols, 1... Downflow type grain humidity control tank, 2
...downflow drying room, 3...blower device,
4... Furnace, 5... Hot air generator, 6
...Circulation elevator, 7...Fuel tank, 8...Outside temperature detector, 9...Filling amount detector, M■... ...Main fuel control valve, SP...
...Fuel pump, T1...Timer, T2
...00 Ignition fuel supply time control timer, M...
...Relay for motor, A...Interlocking relay, TM...Timer for motor, H■...
...Timer for ignition fuel, H...Relay for ignition heater, P...Relay for fuel pump, VR...
...Volume for flow rate setting.

Claims (1)

【特許請求の範囲】[Claims] 1 流下式穀物調湿用タンクの下記に前記タンクと連通
している流下式穀物乾燥室を形成し、側力位置には前記
乾燥室より排出された穀物を上部の前記調湿用タンク内
に上積み還元させる昇降機を設けた循環式穀物乾燥装置
において、該乾燥装置には外気温度検知器と前記調湿タ
ンクおよび前記乾燥室に収容された穀物の総収容量を検
知する検知器を設け、前記両検知器とを前記乾燥室の熱
風発生装置の燃料制御バルブとを結合した循環式穀物乾
燥装置。
1. A downstream grain drying chamber is formed below the downstream grain humidity conditioning tank and communicates with the tank, and at the side force position, the grain discharged from the drying chamber is placed in the humidity conditioning tank at the top. In a circulating grain drying device equipped with an elevator for top-loading and returning, the drying device is provided with an outside temperature sensor and a detector for detecting the total amount of grain stored in the humidity control tank and the drying chamber, A circulating grain drying apparatus in which both detectors are connected to a fuel control valve of a hot air generator in the drying chamber.
JP53096819A 1978-08-09 1978-08-09 Circulating grain dryer Expired JPS5826516B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53096819A JPS5826516B2 (en) 1978-08-09 1978-08-09 Circulating grain dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53096819A JPS5826516B2 (en) 1978-08-09 1978-08-09 Circulating grain dryer

Publications (2)

Publication Number Publication Date
JPS5523877A JPS5523877A (en) 1980-02-20
JPS5826516B2 true JPS5826516B2 (en) 1983-06-03

Family

ID=14175179

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53096819A Expired JPS5826516B2 (en) 1978-08-09 1978-08-09 Circulating grain dryer

Country Status (1)

Country Link
JP (1) JPS5826516B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61137557U (en) * 1985-01-11 1986-08-26

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6096885A (en) * 1983-10-31 1985-05-30 金子農機株式会社 Method of controlling temperature of hot air in cereal drier
JPS60134183A (en) * 1983-12-22 1985-07-17 井関農機株式会社 Controller for combustion of burner in cereal grain drier

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4946743A (en) * 1972-09-08 1974-05-04
JPS5824149Y2 (en) * 1976-10-12 1983-05-23 金子農機株式会社 Automatic temperature control device in dryer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61137557U (en) * 1985-01-11 1986-08-26

Also Published As

Publication number Publication date
JPS5523877A (en) 1980-02-20

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