JPH0436582A - Dry control system for grain dryer - Google Patents

Dry control system for grain dryer

Info

Publication number
JPH0436582A
JPH0436582A JP14293090A JP14293090A JPH0436582A JP H0436582 A JPH0436582 A JP H0436582A JP 14293090 A JP14293090 A JP 14293090A JP 14293090 A JP14293090 A JP 14293090A JP H0436582 A JPH0436582 A JP H0436582A
Authority
JP
Japan
Prior art keywords
dry
drying
chamber
grains
dehumidified 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.)
Pending
Application number
JP14293090A
Other languages
Japanese (ja)
Inventor
Eiji Nishino
栄治 西野
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 and Co Ltd
Iseki Agricultural Machinery Mfg Co Ltd
Original Assignee
Iseki and Co Ltd
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 and Co Ltd, Iseki Agricultural Machinery Mfg Co Ltd filed Critical Iseki and Co Ltd
Priority to JP14293090A priority Critical patent/JPH0436582A/en
Publication of JPH0436582A publication Critical patent/JPH0436582A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To make it possible to dry up grains even in a dry chamber on a lower stage to a satisfactory extent and hence improve dry performance by controlling dehumidified air which passes from a dry chamber on an upper stage to the dry chamber on the lower stage so that dry operation may be carried out at a low humidity and high temperature. CONSTITUTION:When grains which flow down from a storage section 1 in the upper art by way of several stages of dry chambers located top and bottom are dried by sucking up and discharging the dehumidified air generated from a dehumidification device 3 installed per dry chamber 2 by means of an exhaust fan 4 installed per dry chamber 2, the dehumidified air which passes from the dry chambers 2 on the upper stage to the dry chambers 2 on the lower stage is controlled so that it may be dried at a low humidity and high temperature. The grains are repeatedly circulated from a plurality of lower stages, for example, the dry chambers 2 on the second stage. During the recycled dry operation, the dehumidification device 3 on the lower stage side is more efficient than the dehumidification device 3 on the upper stage installed for each dry chamber 2 to suck up and discharge the dehumidified air which is set to low humidity and high temperature by means of the exhaust fan 4 installed per dry chamber 2. Therefore, the grains which pass through each dry chamber 2 individually, are exposed to the dehumidified air and dried.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、穀粒乾燥機の乾燥制御方式に関する。[Detailed description of the invention] Industrial applications The present invention relates to a drying control method for a grain dryer.

従来の技術 従来は、穀粒を上部の貯留室から下部の上下複数段の乾
燥室へ流下させながら、該乾燥室別に設けた除湿装置か
ら発生する除湿風を該乾燥室別に設けた排風機により、
この各乾燥室を通過して機外へ吸引排風させることによ
り、この各乾燥室を流下中の穀粒はこの除湿風に晒され
て乾燥されるが、この除湿風の温度及び湿度は上下複数
段共に同じ温度及び湿度の除湿風に制御されて、穀粒は
乾燥される乾燥制御方式であった。
Conventional technology In the past, while grains were flowing down from the storage chamber in the upper part to the drying chambers in multiple upper and lower stages in the lower part, the dehumidified air generated from the dehumidifier installed in each drying chamber was used by the exhaust fan installed in each drying chamber. ,
By passing through each drying room and sucking and exhausting the air outside the machine, the grains flowing down each drying room are exposed to this dehumidified air and dried, but the temperature and humidity of this dehumidified air vary. It was a drying control method in which grains were dried by controlling dehumidified air at the same temperature and humidity in multiple stages.

発明が解決しようとする課題 穀粒は、上部の貯留室から下部の複数段の乾燥室を繰出
し流下する循環が繰返されながら、該各乾燥室別に設け
た除湿装置から設定した温度及び湿度の除湿風が発生し
、この除湿風が該各乾煙室別に設けた排風機で個別に吸
引排風されることにより、この各乾燥室を個別に通過し
、この各乾燥室内を流下中の穀粒は、この除湿風に晒さ
れて乾燥される。
The problem to be solved by the invention is to dehumidify grains at a temperature and humidity set by a dehumidifying device installed in each drying chamber while the grain is repeatedly circulated from an upper storage chamber to a plurality of lower drying chambers and flowing down. Wind is generated, and this dehumidified air is individually sucked and exhausted by the exhaust fan installed in each drying room, so that it passes through each drying room individually, and the grains flowing down in each drying room are removed. is exposed to this dehumidified air and dried.

この除湿乾燥のときに、上下複数段の該各乾燥室を通過
する除湿風の温度及び湿度は同じであることにより、最
下段の該乾燥室内では穀粒は乾燥されないことがあった
が、これを解決しようとするものである。
During dehumidification and drying, the temperature and humidity of the dehumidified air passing through each of the upper and lower drying chambers are the same, so grains may not be dried in the lowest drying chamber. This is an attempt to solve the problem.

課題を解決するための手段 この発明は、上部の貯留室1かも下部の上下複数段の乾
燥室2を経て流下する穀粒を、該乾燥室2別に設けた除
湿装置3から発生する除湿風を該乾燥室2別に設けた排
風機4で吸引排風させながら乾燥する穀粒乾燥機におい
て、上段の該乾燥室2より下段の該乾燥室2を通過する
該除湿風を低湿高温度に制御して乾燥することを特徴と
する乾燥制御方式の構成とする。
Means for Solving the Problems The present invention provides a method for treating grains flowing down through an upper storage chamber 1 and a lower drying chamber 2 with multiple upper and lower stages using dehumidified air generated from a dehumidifying device 3 provided separately from the drying chamber 2. In a grain dryer that dries while sucking and exhausting air with an air exhaust fan 4 provided separately from the drying chamber 2, the dehumidified air passing through the lower drying chamber 2 from the upper drying chamber 2 is controlled to have low humidity and high temperature. The drying control system is characterized by drying.

発明の作用 穀粒は、上部の貯留室1かも下部の複数段5例えば、二
段の乾燥室2を繰出し流下する循環が繰返されながら、
該各乾燥室2別に設けた上段側の除湿装置3より下段側
の除湿装置3の方が低湿高温度に設定された除湿風が発
生し、この除湿風が該各乾燥室2別に設けた排風14で
個別に吸引排風されることにより、この各乾燥室2を個
別に通過し、この各乾燥室2内を流下中の穀粒は、この
除湿風に晒されて乾燥される。
The working grains of the invention are repeatedly circulated through the upper storage chamber 1 and the lower multiple stages 5, for example, the two-stage drying chamber 2.
The lower dehumidifier 3, which is installed separately in each drying room 2, generates dehumidifying air with lower humidity and higher temperature than the upper dehumidifier 3, and this dehumidified air flows through the exhaust air installed in each drying room 2. By being individually sucked and discharged by the wind 14, the grains passing through each drying chamber 2 individually and flowing down within each drying chamber 2 are exposed to this dehumidified wind and dried.

発明の効果 この発明により、上段側の乾燥室2を通過する除湿装置
3より発生する除湿風の温度及び湿度より、下段側の乾
燥室2を通過する除湿装置3より発生する除湿風の温度
は高温度に、又温度は低湿度に設定されて制御されるこ
とにより、下段の該乾燥室内でも穀粒は十分乾燥される
こととなり、このため穀粒の乾燥性能は向上するし、又
乾燥は安定した。
Effects of the Invention According to this invention, the temperature and humidity of the dehumidified air generated from the dehumidifying device 3 passing through the drying chamber 2 on the lower side are lower than the temperature and humidity of the dehumidifying air generated from the dehumidifying device 3 passing through the drying chamber 2 on the lower side. By controlling the temperature at a high temperature and at a low humidity, the grains can be sufficiently dried in the drying chamber at the lower stage, which improves the drying performance of the grains. Stable.

実施例 以下、本発明の一実施例を図面に基づいて説明する。Example Hereinafter, one embodiment of the present invention will be described based on the drawings.

区制は、除湿装!3.3を、穀粒を乾燥する循環型の穀
粒乾燥機5に装着した状態を示すものである。
The ward system is dehumidifying! 3.3 is shown attached to a circulation type grain dryer 5 for drying grains.

この乾燥4115は、前後方向に長い長方形状で櫟壁6
上部には、移送螺旋を回転自在に内装した移送樋7及び
天井板8を設け、この天井板8下側には穀粒を貯留する
貯留室1を形成している。
This dryer 4115 has a rectangular shape long in the front and back direction and has a vertical wall 6.
A transfer gutter 7 in which a transfer spiral is rotatably installed and a ceiling plate 8 are provided at the upper part, and a storage chamber 1 for storing grains is formed below the ceiling plate 8.

この貯留室1下側において、左右両側の排風室9.9と
中央部の送風室10との間に左右の乾燥室2.2を設け
、これら排風室9,9.送風室10及び乾燥室2.2は
上下二段に設けられた構成であり、こtら下段の乾燥室
2.2下部には穀粒を繰出し流下させる繰出バルブ11
.11を回転自在に軸支している。
On the lower side of the storage chamber 1, left and right drying chambers 2.2 are provided between the left and right ventilation chambers 9.9 and the central ventilation chamber 10, and these ventilation chambers 9,9. The ventilation chamber 10 and the drying chamber 2.2 are arranged in two stages, upper and lower. At the bottom of the lower drying chamber 2.2, there is a feed-out valve 11 that feeds out the grains and allows them to flow down.
.. 11 is rotatably supported.

これら下段の乾燥室2.2下側には移送螺旋を回転自在
に内装した集穀樋12を連通させた構成としている。
A grain collection gutter 12 rotatably equipped with a transfer spiral is connected to the lower side of these lower drying chambers 2.2.

前記機構6正面側において、前記送風室10゜10人口
側に対応すべく前記除湿装置3.3を着脱自在に前後に
配設すると共に、該機構6外側面には、この除湿装置3
,3と前記乾燥機5とを張込、乾燥及び排出の各作業別
に始動及び停止操作する操作装置13を着脱自在に装着
して設けである。
On the front side of the mechanism 6, the dehumidifier 3.3 is removably installed in the front and back to correspond to the ventilation chamber 10° and the population side.
, 3 and the dryer 5 are removably attached to the operating device 13 for starting and stopping operations for loading, drying, and discharging operations.

又前記機構6の背面側には上下段の左右の前記排風室9
.9に連通しうる排風路室14.14を上下に形成し、
この排風路室14.14中央後部側排風胴15.15に
は排風機4,4及びこの排風機4,4を変速回転駆動す
る変速用の排風機モータ16,16を設けている。
Further, on the back side of the mechanism 6, there are the left and right ventilation chambers 9 in the upper and lower stages.
.. Forming upper and lower exhaust duct chambers 14 and 14 that can communicate with 9,
The exhaust cylinder 15.15 on the rear side of the center of the exhaust passage chamber 14.14 is provided with exhaust fans 4, 4 and variable speed exhaust fan motors 16, 16 for rotating and driving the exhaust fans 4, 4 at variable speeds.

17はバルブモータで前記繰出バルブ11.11を減速
機構18を介して回転駆動する構成である。
Reference numeral 17 designates a structure in which a valve motor rotationally drives the delivery valve 11.11 via a speed reduction mechanism 18.

前記移送樋7底板の前後方向中央部には移送穀粒を前記
貯留室1内へ供給する供給口を設け、二の供給口の下側
には穀粒をこの貯留室1内へ均等に拡散還元する拡散盤
19を設けている。
A supply port for supplying transferred grains into the storage chamber 1 is provided at the center in the longitudinal direction of the bottom plate of the transfer gutter 7, and a supply port for distributing the grains evenly into the storage chamber 1 is provided below the second supply port. A diffusion board 19 is provided for reduction.

昇穀[20は、前記櫟壁6萌外部に設けられ、内部には
パケットコンベア21付ベルトを張設してなり、上端部
は、前記移送樋7始端部との間において投出筒22を設
けて連通させ、下端部は、前記集穀樋12終端部との間
において供給樋23を設けて連通させた構成としている
Grain raising [20] is provided on the outside of the vertical wall 6, and a belt with a packet conveyor 21 is stretched inside. A supply gutter 23 is provided between the lower end and the terminal end of the grain collecting gutter 12 to communicate with each other.

24は昇穀機モータで、該パケットコンベア21付ベル
ト、前記移送樋7内の前記移送螺旋及び前記拡散盤19
等を回転駆動する構成とし、又前記集穀樋12内の前言
己移送螺旋を該パケットコンベア21付ベルトを介して
回転駆動する構成としている。
Reference numeral 24 denotes a grain raising machine motor, which includes a belt attached to the packet conveyor 21, the transfer spiral in the transfer gutter 7, and the spreading plate 19.
etc., and the grain transfer spiral in the grain collecting trough 12 is driven to rotate via the belt attached to the packet conveyor 21.

前記昇穀機20の上下方向はぼ中央部には穀粒υ! 水分を検出する水分センサ25を設けている。この水分
センサ25は前記操作装置13からの電気的測定信号の
発信により、水分モータ26が回転してこの水分センサ
25の各部が回転駆動されて前記パケットコンベア21
で上部へ搬送中に落下する穀粒を受け、この穀粒を挟圧
粉砕すると同時に、この粉砕穀粒の水分を検出する構成
である。
In the vertical direction of the grain raising machine 20, grains υ! A moisture sensor 25 is provided to detect moisture. This moisture sensor 25 is operated by transmitting an electrical measurement signal from the operating device 13 to cause a moisture motor 26 to rotate and each part of this moisture sensor 25 to be rotationally driven.
The structure is such that the grains that fall during transportation to the upper part are received, the grains are crushed under pressure, and at the same time, the water content of the crushed grains is detected.

底板にキャスタを設けて移動自在に構成する前記除湿装
置3,3は、圧縮機27、凝縮器28、膨張弁29及び
蒸発器30をそれぞれに備えたもので、前側のこの除湿
装置3は、外気吸入通路31を経て吸入された外気風と
、この除湿装置3内へ吸入された外気風が除湿風に変換
されたこの除湿風とが混合され、この混合乾燥風が上段
の鶴記送風室lO内へ吸入される構成としている。
The dehumidifiers 3, 3, which are movable by providing casters on the bottom plate, are each equipped with a compressor 27, a condenser 28, an expansion valve 29, and an evaporator 30. The outside air sucked in through the outside air suction passage 31 and this dehumidified air, which is the outside air sucked into the dehumidifier 3 and converted into dehumidified air, are mixed, and this mixed dry air is sent to the upper Tsurugi ventilation chamber. It is configured to be inhaled into IO.

後側の前記除湿装置3は、この除湿装置3内へ吸入され
た外気風が除湿風に変換され、この除湿風が下段の前記
送風室10内へ吸入される構成としている。
The dehumidifying device 3 on the rear side is configured so that the outside air sucked into the dehumidifying device 3 is converted into dehumidified air, and this dehumidified air is sucked into the ventilation chamber 10 on the lower stage.

前記除湿装置3.3は、前部の外気吸入口32からこの
除湿装置3.3内へ供給される外気風を低湿度の除湿風
に変換するために、冷媒である低温低圧ガスは該圧縮機
27にて断熱圧縮されつつ高温高圧ガスに変換され、こ
れが該凝縮器28を通過する際に熱を奪われて高温高圧
液体へ変化し、その後該膨張弁29を通過の際に圧力降
下を伴ない低温低圧液体へ変化し、さらに該蒸発器30
を通過する際に熱を吸収して低温低圧ガスへと変化する
もので、順次このサイクルを繰返す。尚、33は該圧縮
機27駆動用モータである。
The dehumidifying device 3.3 converts the outside air supplied into the dehumidifying device 3.3 from the outside air inlet 32 at the front into dehumidified air with low humidity. The gas is adiabatically compressed and converted into a high-temperature, high-pressure gas in the machine 27, and when it passes through the condenser 28, heat is removed and it changes into a high-temperature, high-pressure liquid, and then the pressure decreases as it passes through the expansion valve 29. The evaporator 30
As it passes through the gas, it absorbs heat and turns into low-temperature, low-pressure gas, and this cycle is repeated one after another. Note that 33 is a motor for driving the compressor 27.

なお、前記除湿装置3.3内へ吸入される外気風の状態
は、前記蒸発器30部を通過する際に冷却されて空気中
の水分が結露し、絶対湿度が低下した低温低湿風となり
、その後前記凝縮器28部を通過する際に熱を吸収して
常温より若干高い温度の低除湿風を得る構成としている
The condition of the outside air sucked into the dehumidifying device 3.3 is that it is cooled while passing through the evaporator 30, moisture in the air condenses, and the absolute humidity becomes low-temperature, low-humidity wind. Thereafter, when passing through the condenser 28 section, heat is absorbed to obtain low dehumidified air at a temperature slightly higher than room temperature.

前記操作装置13は、箱形状でこの箱体の表面板には、
前記乾燥機5及び前記除湿装置3,3等を張込、乾燥及
び排出の各作業別に始動操作する始動スイッチ34.停
止操作する停止スイッチ35、穀粒の仕上目標水分を操
作位置によって設定する水分設定猟み36.除湿風の温
度及び湿度を操作位置によって設定する穀物種類設定猟
み37及び張込量設定猟み38、検出穀粒水分、検出乾
燥温度及び乾燥残時間等を交互に表示するデジタル表示
部39及びモニター表示を設け、底板外側には外気温度
を検出する外気温度センサ46及び外気湿度を検出する
外気温度センサ47を設けている。
The operating device 13 has a box shape, and the surface plate of the box has a
A start switch 34 for starting the dryer 5 and the dehumidifiers 3, 3, etc. for each operation of loading, drying, and discharging. A stop switch 35 for stopping operation, a moisture setting switch 36 for setting the finishing target moisture content of grains according to the operation position. Grain type setting setting 37 and loading amount setting 38 for setting the temperature and humidity of the dehumidifying air depending on the operating position; a digital display section 39 for alternately displaying detected grain moisture, detected drying temperature, remaining drying time, etc.; A monitor display is provided, and an outside air temperature sensor 46 for detecting outside air temperature and an outside air temperature sensor 47 for sensing outside air humidity are provided on the outside of the bottom plate.

又内部には検出値をA−D変換するA−D変換器40.
このA−D変換器40で変換された変換値が入力される
入力回路41、各種検出値が入力される入力回路42、
これら入力値を算術論理演算及び比較演算等を行なうC
PO43、このCPU43から指令される各種指令を受
けて出力する出力回路44等よりなる乾燥制御装置45
を内蔵する構成である。尚、該各設定猟み36,37゜
38はロータリースイッチ方式とし、操作位置によって
所定の数値及び種類等が設定される構成としている。
Also, there is an A-D converter 40 inside that converts the detected value from A to D.
An input circuit 41 to which the converted value converted by this A-D converter 40 is input, an input circuit 42 to which various detected values are input,
C that performs arithmetic and logical operations, comparison operations, etc. on these input values.
A drying control device 45 comprising a PO 43, an output circuit 44 that receives various commands from the CPU 43, and outputs them.
It has a built-in configuration. The settings 36, 37, and 38 are of rotary switch type, and are configured to set predetermined values, types, etc. depending on the operating position.

該乾燥制御装置45による穀粒の乾燥制御は下記の如く
行なわれる構成である。即ち、前記水分設定猟み36の
操作内容が該CPU43へ入力され、この入力によって
穀粒の仕上目標水分が設定される。一方前記水分センサ
25が検出する穀粒水分も該CPU43へ入力され、こ
れら入力された検出穀粒水分と設定仕上目標水分とが比
較され、検出穀粒水分が仕上目標水分に達したと検出さ
れると、前記乾燥機5運転各部を自動停止して穀粒の乾
燥が終了する構成としている。
Drying control of grains by the drying control device 45 is performed as follows. That is, the operation details of the moisture setting setting 36 are input to the CPU 43, and the finishing target moisture of the grain is set by this input. On the other hand, the grain moisture detected by the moisture sensor 25 is also input to the CPU 43, the input detected grain moisture is compared with the set finishing target moisture, and it is detected that the detected grain moisture has reached the finishing target moisture. Then, each operating part of the dryer 5 is automatically stopped to finish drying the grains.

併せて前記乾燥制御装置45は次の機能を有する。即ち
、萌記穀物種類設定猟み37及び前記張込量設定猟み3
8の操作内容が前記CPU43へ入力され、又前記外気
温度センサ46及び外気湿度センサ47が検出する外気
温度(TE)及び外気相対湿度(WE)も該CPU43
へ入力され、これら入力値から該CPU43へ設定して
記憶させた前記除湿袋ft3.3から発生する除湿風の
温度(T)及び湿度(W)が選定されると同時に、前記
排風114.4で吸引排風する総吸引風量(Q■)が選
定され、これら各選定値と同じになるように制御される
構成としている。
Additionally, the drying control device 45 has the following functions. That is, Moeki grain type setting setting 37 and the setting amount setting 3
8 is input to the CPU 43, and the outside air temperature (TE) and outside air relative humidity (WE) detected by the outside air temperature sensor 46 and outside air humidity sensor 47 are also input to the CPU 43.
At the same time, the temperature (T) and humidity (W) of the dehumidifying air generated from the dehumidifying bag ft3.3, which are input to the CPU 43 and stored in the CPU 43, are selected from these input values. 4, the total suction air volume (Q■) to be suctioned and discharged is selected, and the configuration is such that it is controlled to be equal to each of these selected values.

例えば、前記穀物種類設定担み37が柄位置へ操作され
、前記張込量設定扼み38が36位置へ操作され、これ
らの操作内容が前記CPU43へ入力されると同時に、
第2図の如(、前記外気温度センサ46が検出した外気
温度(TE)15℃と、前記外気温度センサ47が検出
した外気相対湿度(WE)70%とが該CPU43へ入
力されると、この入力によって上段の前記乾燥室2へ供
給される前記除湿装置3から発生する除湿風の温度(T
)は設定記憶値から18℃と選定され、又湿度(W)は
設定記憶値から50%と選定される。
For example, the grain type setting lever 37 is operated to the handle position, the loading amount setting lever 38 is operated to the 36th position, and the contents of these operations are input to the CPU 43 at the same time,
As shown in FIG. 2, when the outside air temperature (TE) of 15° C. detected by the outside air temperature sensor 46 and the outside air relative humidity (WE) of 70% detected by the outside air temperature sensor 47 are input to the CPU 43, Based on this input, the temperature (T
) is selected as 18° C. from the set memory value, and humidity (W) is selected as 50% from the set memory value.

下段の前記乾燥室2へ供給される前記除湿装置3から発
生する除湿風の温度(T)は設定記憶値から22℃と選
定され、又湿度(W)は設定記憶値から30%と選定さ
れる。これら選定された各数値と同じになるように、該
除湿装@3.3の前記圧縮機モータ33,33の回転が
制御される構成としている。
The temperature (T) of the dehumidified air generated from the dehumidifying device 3 supplied to the drying chamber 2 in the lower stage is selected to be 22° C. from the set memory value, and the humidity (W) is selected to be 30% from the set memory value. Ru. The rotation of the compressor motors 33, 33 of the dehumidifier @3.3 is controlled so as to be equal to each of these selected values.

又上段の前記乾燥室2を通過する総吸引風量(Ql)は
設定記憶値から1.off1″/secと選定され、こ
の1.0ゴ/secの内訳は、前記外気吸入口32から
吸入されて除湿風に変換された除湿風量(Q2)が設定
記憶値から0゜5m’/secと選定され、又前記外気
吸入通路31から吸入される外気風量(Q3)が設定記
憶値から0.5ゴ/secと選定される。
Also, the total suction air volume (Ql) passing through the drying chamber 2 in the upper stage is 1. off1''/sec, and the breakdown of this 1.0 go/sec is that the dehumidifying air volume (Q2) taken in from the outside air intake port 32 and converted to dehumidifying air is 0°5 m'/sec from the set memory value. The outside air flow rate (Q3) taken in from the outside air intake passage 31 is selected to be 0.5 go/sec from the set stored value.

下段の前記乾燥室2を通過する総吸引風11(Ql)は
設定記憶値から0.5&/secと選定され、この0.
5m/secの内訳は、該外気吸入口32から吸入され
て除湿風に変換された除湿風量(Q2)が設定記憶値か
ら0.5rn”/secと選定される。これら選定され
た各数値と同じになるように、前記排風機4.4の前記
排風機モータ16,1Bの回転が制御される構成として
いる。
The total suction air 11 (Ql) passing through the drying chamber 2 in the lower stage is selected as 0.5&/sec from the set memory value, and this 0.
The breakdown of 5 m/sec is that the dehumidifying air volume (Q2) taken in from the outside air intake port 32 and converted to dehumidifying air is selected from the set memory value as 0.5 rn''/sec. The configuration is such that the rotation of the exhaust fan motors 16 and 1B of the exhaust fan 4.4 is controlled so that the exhaust fan 4.4 has the same rotation.

尚、下段の前記乾燥室2を通過する総吸引風量(Ql)
は、上段と同じように1.0!n″/secと設定して
記憶させる構成とするもよい。
In addition, the total suction air volume (Ql) passing through the lower drying chamber 2
is 1.0 as in the upper row! It may be configured to set and store n″/sec.

以下、上記実施例の作用について説明する。Hereinafter, the operation of the above embodiment will be explained.

操作装Wt13の各設定猟み36,37.38を所定位
置へ操作し、除湿乾燥を開始する始動スイッチ34を操
作することにより、穀粒乾燥Wk5の各部、除湿装置3
,3及び水分センサ25等が始動し、外気温度センサ4
6及び外気温度センサ47が検出する外気温度と外気相
対湿度が、この操作装置13へ入力されると、該除湿装
置3.3から発生する除湿風の温度及び湿度が選定され
て設定され、又排風機4.4で吸引排風する総吸引風量
が選定されて設定される。
By operating each setting switch 36, 37, 38 of the operation device Wt13 to a predetermined position and operating the start switch 34 that starts dehumidifying drying, each part of the grain drying Wk5, the dehumidifying device 3
, 3 and moisture sensor 25 etc. are started, and the outside air temperature sensor 4
When the outside air temperature and outside air relative humidity detected by the outside temperature sensor 6 and the outside air temperature sensor 47 are input to this operating device 13, the temperature and humidity of the dehumidified air generated from the dehumidifying device 3.3 are selected and set, and The total amount of suction air to be sucked and exhausted by the exhaust fan 4.4 is selected and set.

この設定された除湿風が該除湿装置3,3から発生し、
この除湿風は送風室10.10から乾燥室2.2を個別
に通過して上下の排風室9.9及び排風路室14.14
を経て該排風機4.4で個別に吸引排風されることによ
り、貯留室1内へ収容された穀粒は、この貯留室1から
上下の該乾燥室2,2内を流下中にこの除湿風に晒され
て乾燥され、繰出バルブ11.11で下部へと繰出され
て流下して集穀樋12から供給樋23を経て昇穀機20
内へ下部の移送螺旋で移送供給され、パケットコンベア
21で上部へ搬送されて投出筒22を経て移送樋7内へ
供給され、この移送樋7から拡散盤19上へ上部の移送
螺旋で移送供給され、この拡散盤19で該貯留室1内へ
均等に拡散還元され、循環乾燥されて該水分センサ25
が該水分設定猟み36を操作して設定した仕上目標水分
と同じ穀粒水分を検出すると、該操作装置13の乾燥制
御装置45で自動制御して該乾燥e15を自動停止して
穀粒の乾燥が停止される。
This set dehumidifying air is generated from the dehumidifying devices 3, 3,
This dehumidified air passes individually from the ventilation chamber 10.10 to the drying chamber 2.2, and then passes through the upper and lower ventilation chambers 9.9 and the ventilation duct chamber 14.14.
The grains accommodated in the storage chamber 1 are individually sucked and exhausted by the exhaust fan 4.4, and the grains are removed from the storage chamber 1 while flowing through the upper and lower drying chambers 2, 2. The grain is dried by being exposed to dehumidified air, and is delivered to the lower part by the delivery valve 11.11 and flows down from the collection gutter 12 through the supply gutter 23 to the grain raising machine 20.
The packets are transported to the inside by the lower transfer spiral, are transported to the upper part by the packet conveyor 21, are supplied to the transfer gutter 7 via the dispensing tube 22, and are transferred from the transfer gutter 7 onto the diffusion plate 19 by the upper transfer spiral. The moisture sensor 25 is supplied, is evenly diffused and reduced into the storage chamber 1 by the diffusion plate 19, and is circulated and dried.
When the grain moisture content is the same as the finishing target moisture set by operating the moisture setting controller 36, the drying control device 45 of the operating device 13 automatically controls the drying e15 and automatically stops the grain drying. Drying is stopped.

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

図は、この発明の一実施例を示すもので、第1図はブロ
ック図、第2図は上下段乾燥室の除湿風及び吸引風の関
係図、第3図は穀粒乾燥機の全体側面図、第4図は第3
図のA−A断面図、第5図は穀粒乾燥機の一部の背面図
、第6図は穀粒乾燥機の一部の一部破断せる拡大正面図
である。 符号の説明 1 貯留室    2 乾燥室 3 除湿装置!2  4 排風撮 代表者水田栄久 第1図 第2図 ま):9ト先l友15・oて゛外気相対進度70%の乙
ぎ。 第4図 第5図 d 1°r だ
The figures show one embodiment of the present invention. Figure 1 is a block diagram, Figure 2 is a relationship diagram of dehumidifying air and suction air in the upper and lower drying chambers, and Figure 3 is an overall side view of the grain dryer. Figure 4 is the third
FIG. 5 is a rear view of a portion of the grain dryer, and FIG. 6 is an enlarged partially cutaway front view of a portion of the grain dryer. Explanation of symbols 1 Storage chamber 2 Drying chamber 3 Dehumidifier! 2 4 Wind Exhaust Photography Representative Hidehisa Mizuta (Figure 1, Figure 2): At 9 to 15 o'clock, the relative progress of the outside air was 70%. Figure 4 Figure 5 d 1°r

Claims (1)

【特許請求の範囲】[Claims] 上部の貯留室1から下部の上下複数段の乾燥室2を経て
流下する穀粒を、該乾燥室2別に設けた除湿装置3から
発生する除湿風を該乾燥室2別に設けた排風機4で吸引
排風させながら乾燥する穀粒乾燥機において、上段の該
乾燥室2より下段の該乾燥室2を通過する該除湿風を低
湿高温度に制御して乾燥することを特徴とする乾燥制御
方式。
The grains flowing down from the storage chamber 1 in the upper part through the drying chambers 2 in multiple upper and lower stages in the lower part are removed by the dehumidifying air generated from the dehumidifying device 3 provided separately in the drying room 2 using the exhaust fan 4 provided separately in the drying room 2. In a grain dryer that dries while suctioning and exhausting air, a drying control method characterized in that the dehumidifying air passing through the lower drying chamber 2 from the upper drying chamber 2 is controlled to have low humidity and high temperature for drying. .
JP14293090A 1990-05-30 1990-05-30 Dry control system for grain dryer Pending JPH0436582A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14293090A JPH0436582A (en) 1990-05-30 1990-05-30 Dry control system for grain dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14293090A JPH0436582A (en) 1990-05-30 1990-05-30 Dry control system for grain dryer

Publications (1)

Publication Number Publication Date
JPH0436582A true JPH0436582A (en) 1992-02-06

Family

ID=15326950

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14293090A Pending JPH0436582A (en) 1990-05-30 1990-05-30 Dry control system for grain dryer

Country Status (1)

Country Link
JP (1) JPH0436582A (en)

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