JPH03113281A - Dry control system for grain dryer - Google Patents

Dry control system for grain dryer

Info

Publication number
JPH03113281A
JPH03113281A JP25305189A JP25305189A JPH03113281A JP H03113281 A JPH03113281 A JP H03113281A JP 25305189 A JP25305189 A JP 25305189A JP 25305189 A JP25305189 A JP 25305189A JP H03113281 A JPH03113281 A JP H03113281A
Authority
JP
Japan
Prior art keywords
air
humidity
drying
chamber
grain
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
JP25305189A
Other languages
Japanese (ja)
Inventor
Shigeo Kobayashi
繁夫 小林
Noriki Nomaru
能丸 憲樹
Keiichi Miyazaki
啓市 宮崎
Kusuo Matsui
松井 久寿男
Masashi Yumitate
正史 弓立
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 JP25305189A priority Critical patent/JPH03113281A/en
Publication of JPH03113281A publication Critical patent/JPH03113281A/en
Pending legal-status Critical Current

Links

Landscapes

  • Drying Of Solid Materials (AREA)

Abstract

PURPOSE:To save drying energy and stabilize grain drying by detecting absolute humidity of dehumidified air before and after ventilating a dryer chamber, computing the difference between the humidity of the air, and drying the air under the control of an air capacity to be sucked and exhausted with an exhauster in order to maintain the compute differential humidity at a fixed value. CONSTITUTION:During drying operation a dehumidification humidity sensor 14 detects the absolute humidity of dehumidified air generated from a dehumidification device 2 prior to the passage through a drying chamber 1 while an exhausted air humidity sensor detects 15 in an exhaust chamber detects the absolute humidity of exhausted air which has passed the drying chamber 1. The difference between the thus detected absolute humidity is computed and the air capacity of open air to be sucked and exhausted with an exhauster 4 is sucked from an intake port 27 and converted into dehumidified air under the control to fix the differential humidity, thereby drying grains. Then, the computed differential humidity is compared with the predetermined differential humidity set and stored based on the classification of grain moisture content. When the difference is detected, the air capacity of open air is controlled so that it may be same as the predetermined differential humidity.

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、穀粒を乾燥室へ繰出し流下させながら、除湿装
置による除湿風をこの乾燥室へ通風させて排風室を経て
排風機で機外へ吸引排風され、この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乾燥制御方式であ
った。
Conventional technology In the past, while the grains were fed into the drying chamber and allowed to flow down, dehumidified air from a dehumidifier was passed through the drying chamber, passed through the ventilation chamber, and then sucked and exhausted outside the machine by an exhaust fan. This was a drying control method in which the grains flowing down were exposed to this dehumidified air and dried.

発明が解決しようとする課題 穀粒は穀粒乾燥機の乾燥室内を繰出し流下する循環が繰
返されながら、除湿装置から発生する除湿風がこの乾燥
室を通過して排風室を経て排風機で吸引排風されること
により、この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この除湿乾燥作業は、乾燥所要時間
が長時間になるが、これは乾燥中の穀粒の温度を低温度
に押さえているために穀粒の水分移行がゆるやかになる
ためであり、このような状態のときに除湿風の風量を増
加させても、穀粒の乾減率が向上することなく、除湿風
がむだになったり、又穀粒水分が低水分域になると除湿
風の風量を減少させると乾減率が低下して乾燥が進まな
くなることがあり、これらを解消して省エネルギー乾燥
を図ると共に、穀粒乾燥の安定化を図ろうとするもので
ある。
Problems to be Solved by the Invention While the grain is repeatedly circulated through the drying chamber of the grain dryer and flowing down, the dehumidified air generated from the dehumidifier passes through this drying chamber, passes through the exhaust chamber, and is discharged by the exhaust fan. The grains flowing down the drying chamber are exposed to the dehumidifying air and dried by suction and exhaust air.This dehumidifying and drying process takes a long time to dry, but this is due to the This is because the grain temperature is kept low, which slows down the moisture transfer in the grains, and even if you increase the amount of dehumidifying air under these conditions, the drying rate of the grains will decrease. If the dehumidifying air does not improve and the grain moisture reaches a low moisture range, reducing the air volume of the dehumidifying air may reduce the drying rate and prevent drying from proceeding. The aim is to achieve energy-saving drying and stabilize grain drying.

請求項1の発明について 課題を解決するための手段 この発明は、穀粒を乾燥室1へ繰出し流下させながら除
湿装置2による除湿風を該乾燥室1へ通風させて排風室
3を経て排風機4で機外へ吸引排風させて乾燥させる穀
粒乾燥機において、この乾燥室1を通風前のこの除湿風
と通風後の排風との両者の絶対湿度を検出して湿度差を
算出してこの算出湿度差を一定値に保持すべく誠排風機
4で吸引排風する該除湿風風量を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 Regarding the Invention of Claim 1 The present invention provides a system in which grains are fed into a drying chamber 1 and flowed down, while dehumidifying air from a dehumidifying device 2 is ventilated into the drying chamber 1 and exhausted through an exhaust chamber 3. In a grain dryer that sucks and exhausts air outside the machine using a fan 4 to dry the grain, the absolute humidity of both the dehumidifying air before ventilation and the exhaust air after ventilation in the drying chamber 1 is detected to calculate the humidity difference. The drying control method is characterized in that the air volume of the dehumidifying air sucked and discharged by the Makoto fan 4 is controlled in order to maintain the calculated humidity difference at a constant value.

発明の作用 穀粒は穀粒乾燥機の乾燥室1内を繰出し流下する循環が
繰返されながら、除湿装置2から発生する除湿風がこの
乾燥室1を通過して排風室3を経て排風機4で吸引排風
されることにより、この乾燥室1内を流下中の穀粒は、
この除湿風に晒されて乾燥される。
Effect of the Invention While the grain is repeatedly circulated in the drying chamber 1 of the grain dryer and flowing down, the dehumidified air generated from the dehumidifier 2 passes through the drying chamber 1, passes through the exhaust chamber 3, and is sent to the exhaust fan. 4, the grains flowing down in the drying chamber 1 are
It is exposed to this dehumidified air and dried.

この除湿乾燥作業中は、該乾燥室1を通過する以前の除
湿風の絶対湿度が検出され、又この乾燥室1を通過した
以後の排風されるこの排風の絶対湿度が検出され、これ
ら検出された両者の絶対湿度が比較されて湿度差が算出
され、この算出された湿度差が常に一定値になるように
、該排風機4で吸引排風される除湿風の風量が制御され
なから穀粒は乾燥される。
During this dehumidifying and drying work, the absolute humidity of the dehumidified air before it passes through the drying chamber 1 is detected, and the absolute humidity of the exhausted air after it passes through the drying chamber 1 is also detected. The detected absolute humidity between the two is compared to calculate the humidity difference, and the volume of dehumidified air sucked and exhausted by the exhaust fan 4 is controlled so that the calculated humidity difference is always a constant value. The grains are then dried.

発明の効果 この発明により、乾燥室1を通過する通過前の除湿風の
絶対湿度と通過後の排風の絶対湿度とが検出され、この
両者によって湿度差が算出され、この算出された湿度差
が一定値になるように、排風機4で吸引排風する除湿風
の風量が制御されて、穀粒の除水量が一定値になるよう
に制御されることにより、除湿風の風量を必要以上に増
加制御されることがなくなり、又穀粒水分が低水分域に
なって水分が抜けにくくなると風量が減少制御されるこ
とにより、むだなエネルギーの消費がなくなって省エネ
ルギーができたと同時に、穀粒乾燥の安定化ができた。
Effects of the Invention According to this invention, the absolute humidity of the dehumidified air before passing through the drying chamber 1 and the absolute humidity of the exhaust air after passing through are detected, the humidity difference is calculated from both, and the calculated humidity difference The volume of dehumidified air sucked and discharged by the exhaust fan 4 is controlled so that the amount of water removed from the grains is maintained at a constant value. In addition, when the grain moisture reaches a low moisture range and becomes difficult to remove, the air flow is controlled to decrease, which eliminates wasted energy consumption and saves energy. Drying has been stabilized.

請求項2の発明について 課題を解決するための手段 この発明は、穀粒を乾燥室lへ繰出し流下させながら除
湿装置2による除湿風を該乾燥室1へ通風させて排風室
3を経て排風機4で機外へ吸引排風させて乾燥させる穀
粒乾燥機において、この乾燥室1を通風前のこの除湿風
と通風後の排風との両者の絶対湿度を検出して湿度差を
算出してこの算出湿度差を穀粒水分にもとづいてあらか
じめ設定して記憶させた設定湿度差と同じにすべく該排
風機4で吸引排風する該除湿風風量を制御して乾燥する
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 Regarding the Invention of Claim 2 The present invention provides a system in which dehumidified air from a dehumidifying device 2 is ventilated into the drying chamber 1 and exhausted through the exhaust chamber 3 while the grains are fed into the drying chamber 1 and flowed down. In a grain dryer that sucks and exhausts air outside the machine using a fan 4 to dry the grain, the absolute humidity of both the dehumidifying air before ventilation and the exhaust air after ventilation in the drying chamber 1 is detected to calculate the humidity difference. Drying is performed by controlling the volume of the dehumidifying air sucked and discharged by the exhaust fan 4 so that this calculated humidity difference is the same as a preset humidity difference that has been set and stored in advance based on the grain moisture content. The drying control method is configured as follows.

発明の作用 穀粒は穀粒乾燥機の乾燥室1内を繰出し流下する循環が
繰返されながら、除湿装置2から発生する除湿風がこの
乾燥室lを通過して排風室3を経て排風機4で吸引排風
されることにより、この乾燥室1内を流下中の穀粒は、
この除湿風に晒されて乾燥される。
Effect of the Invention While the grain is repeatedly circulated through the drying chamber 1 of the grain dryer and flowing down, the dehumidified air generated from the dehumidifier 2 passes through the drying chamber 1, passes through the exhaust chamber 3, and is sent to the exhaust fan. 4, the grains flowing down in the drying chamber 1 are
It is exposed to this dehumidified air and dried.

この除湿乾燥作業中は、該乾燥室lを通過する以前の除
湿風の絶対湿度が検出され、又この乾燥室1を通過した
以後の排風されるこの排風の絶対湿度が検出され、これ
ら検出された両者の絶対湿度が比較されて湿度差が算出
され、この算出された湿度差と穀粒水分にもとづいて設
定して記憶させた湿度差が比較され、相違していると設
定湿度差と同じになるように、該排風機4で吸引排風さ
れる除湿風の風量が制御されなから穀粒は乾燥される。
During this dehumidifying and drying work, the absolute humidity of the dehumidified air before it passes through the drying chamber 1 is detected, and the absolute humidity of the exhausted air after it passes through the drying chamber 1 is detected. The detected absolute humidity of the two is compared to calculate the humidity difference, and this calculated humidity difference is compared with the humidity difference set and stored based on the grain moisture. If there is a difference, the set humidity difference is calculated. The grains are dried because the volume of the dehumidified air sucked and exhausted by the blower 4 is not controlled so that the drying temperature is the same.

発明の効果 この発明により、乾燥室1を通過する通過前の除湿風の
絶対湿度と通過後の排風の絶対湿度とが検出され、この
両者によって湿度差が算出され、この算出された湿度差
と穀粒水分によって設定して記憶させた設定湿度差とが
比較され、設定湿度差と同じになるように、排風機4で
吸引排風される除湿風の風量が制御されて、穀粒の除水
量が一定値になるように制御されることにより、穀粒水
分が低水分域になって除水量が減少する減少域になると
、風量を減少させるとますます除水量が減少して乾燥が
進まなくなるが、除水量が一定値になるように風量が制
御されることにより、穀粒乾燥の安定化ができた。
Effects of the Invention According to this invention, the absolute humidity of the dehumidified air before passing through the drying chamber 1 and the absolute humidity of the exhaust air after passing through are detected, the humidity difference is calculated from both, and the calculated humidity difference The set humidity difference set and stored according to the grain moisture is compared, and the volume of dehumidified air sucked and discharged by the exhaust fan 4 is controlled so that it becomes the same as the set humidity difference. By controlling the amount of water removed to a constant value, when the grain moisture reaches a low moisture range and the amount of water removed decreases, reducing the air volume will further reduce the amount of water removed and drying will occur. Although the process slowed, grain drying was stabilized by controlling the air volume so that the amount of water removed remained constant.

実施例 なお、回倒において、穀粒乾燥機5の機構6は、前後壁
板及び左右壁板よりなる前後方向に長い長方形状で、こ
の前壁板には除湿装置2及びこの乾燥機5とこの除湿装
置2とを始動操作及び停止操作する操作装置7を設け、
該後壁板には排風機4、この排風機4を変速回転駆動す
る変速用の排風機モータ8及び間欠回転するバルブモー
タ9等を設けた構成である。
Embodiment When the grain dryer 5 is rotated, the mechanism 6 of the grain dryer 5 has a rectangular shape that is long in the front and back direction and is made up of front and rear wall plates and left and right wall plates, and the dehumidifier 2 and the dryer 5 are installed on this front wall plate. An operating device 7 for starting and stopping the dehumidifying device 2 is provided,
The rear wall plate is provided with an exhaust fan 4, a variable speed exhaust fan motor 8 for rotating and driving the exhaust fan 4 at variable speeds, a valve motor 9 that rotates intermittently, and the like.

該機構6内下部の中央部には、前後方向に亘り移送螺旋
を回転自在に軸支した集穀@10を設け、この集穀樋1
0上側には通気網板間に形成した乾燥室1を並設して連
通させ、この各乾燥室1下部には穀粒を繰出し流下させ
る繰出バルブ11を回転自在に軸支し、該乾燥室1内側
間には送風室12を形成して該除湿装置2と連通させ、
該各乾燥室1外側には排風室3を形成して該排風機4と
連通させた構成であり、該バルブモータ9で変速機構1
3を介して該繰出バルブ11を間欠回転駆動する構成で
あり、該送風室12内にはこの送風室12内へ該除湿装
置2から送風される除湿風の絶対湿度を検出する除湿湿
度センサ14を設け、又該排風室3内には該乾燥室1を
除湿風が通過して排風される排風の絶対湿度を検出する
排風湿度センサ15を設けた構成である。
At the center of the lower part of the mechanism 6, there is provided a grain collection @10 in which a transfer spiral is rotatably supported in the front and back direction, and this grain collection gutter 1
0 upper side, drying chambers 1 formed between ventilation mesh plates are arranged in parallel and communicated with each other, and at the bottom of each drying chamber 1, a feeding valve 11 for feeding and flowing grains is rotatably supported. 1, a ventilation chamber 12 is formed between the inner sides thereof and communicated with the dehumidification device 2,
A ventilation chamber 3 is formed outside each drying chamber 1 and communicated with the ventilation fan 4, and the valve motor 9 is connected to the speed change mechanism 1.
A dehumidifying humidity sensor 14 is installed in the ventilation chamber 12 to detect the absolute humidity of the dehumidified air blown into the ventilation chamber 12 from the dehumidifying device 2. In addition, an exhaust air humidity sensor 15 is provided in the air exhaust chamber 3 to detect the absolute humidity of the exhaust air that is discharged after the dehumidified air passes through the drying chamber 1.

該各乾燥室1上側には貯留室16を形成して連通させ、
この貯留室16上側には天井板17及び移送螺旋を回転
自在に軸支した移送樋18を設けこの移送樋18中央部
には移送穀粒をこの貯留室16内へ供給する供給口を設
け、この供給口の下側には該貯留室16内へ穀粒を均等
に拡散還元する拡散盤19を設けた構成である。
A storage chamber 16 is formed above each drying chamber 1 and communicated with the storage chamber 16,
A transfer gutter 18 in which a ceiling plate 17 and a transfer spiral are rotatably supported is provided on the upper side of the storage chamber 16, and a supply port for supplying transferred grains into the storage chamber 16 is provided in the center of the transfer gutter 18. A diffusion plate 19 is provided below the supply port to uniformly diffuse and return the grains into the storage chamber 16.

昇穀機20は、前記前壁板前方部に設け、内部にはパケ
ットコンベア21ベルトを上下プーリ間に張設し、上端
部と該移送樋18始端部との間には投出筒22を設けて
連通させ、下端部と前記集穀樋10終端部との間には供
給樋23を設けて連通させた構成である。
The grain raising machine 20 is installed in the front part of the front wall plate, and inside thereof, a packet conveyor 21 belt is stretched between upper and lower pulleys, and a discharging cylinder 22 is provided between the upper end and the starting end of the transfer gutter 18. A supply gutter 23 is provided between the lower end and the terminal end of the grain collection gutter 10 to communicate with each other.

この昇穀機20上部に設けた昇穀機モータ24で該パケ
ットコンベア21ベルト、該移送樋18内の該移送螺旋
、該拡散盤19及び該パケットコンベア21ベルトを介
して該集穀樋10内の前記移送螺旋等を回転駆動する構
成である。
The grain raising machine motor 24 installed on the upper part of the grain raising machine 20 moves the packet conveyor 21 belt, the transfer spiral in the transfer gutter 18, the spreading plate 19, and the packet conveyor 21 belt into the grain collection gutter 10. This configuration rotates the transfer spiral and the like.

父上下方向はぼ中央部に設けた水分センサ25で該パケ
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り、この水分センサ25の各部は
、前記操作装置7からの電気的測定信号の発信により、
内部に設けた水分モータ26が回転し、この水分モータ
26の回転により回転駆動される構成である。
A moisture sensor 25 installed approximately in the center in the vertical direction receives grains falling while being conveyed to the upper part of the packet conveyor 21, crushes the grains under pressure, and at the same time detects the moisture content of the crushed grains. Each part of the moisture sensor 25 can be controlled by transmitting an electrical measurement signal from the operating device 7.
The moisture motor 26 provided inside rotates, and is rotationally driven by the rotation of this moisture motor 26.

前記除湿装置2は、箱形状でこの箱体の前壁板には外気
を吸入する吸入口27を設け、後壁板にはこの除湿装置
2内で外気風が除湿風に変換されたこの除湿風を前記送
風室12へ送風する送風口28を設けた構成であり、該
除湿装置2内へ吸入された外気風を、この外気風より若
干高い温度の除湿風に変換するために、冷媒である低温
低圧ガスは圧縮機29にて高温高圧ガスへ断熱圧縮され
て凝縮器30を通過する際に熱を奪われ高温高圧液体へ
変化し、その後膨張弁31にて低温低圧液体へと圧力降
下され、さらに蒸発器32を通過する際に熱を吸引し低
温低圧ガスへと変化し、順次冷媒がこのサイクルを繰返
すことにより、該除湿装置2内を通過する外気風を除湿
する。
The dehumidifying device 2 has a box shape, and the front wall plate of the box body is provided with an inlet 27 for sucking outside air, and the rear wall plate is provided with an inlet 27 for inhaling outside air. The structure is provided with an air outlet 28 for blowing air into the air blowing chamber 12, and a refrigerant is used to convert the outside air sucked into the dehumidifier 2 into dehumidified air at a slightly higher temperature than the outside air. A certain low-temperature, low-pressure gas is adiabatically compressed into high-temperature, high-pressure gas in the compressor 29, and when it passes through the condenser 30, it loses heat and changes into a high-temperature, high-pressure liquid.Then, the pressure is reduced to a low-temperature, low-pressure liquid in the expansion valve 31. The refrigerant then absorbs heat when passing through the evaporator 32 and changes into low-temperature, low-pressure gas, and by sequentially repeating this cycle, the outside air passing through the dehumidifier 2 is dehumidified.

なお、前記除湿装置2内へ吸入された外気の状態は、該
蒸発器32を通過する際に冷却され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、その後肢凝縮
器30部を通過する際に熱を吸引して常温より若干高い
温度の低除湿風の除湿風を得る構成であり、なお該圧縮
機29は圧縮機モータ33で回転駆動される構成である
The state of the outside air sucked into the dehumidifier 2 is such that it is cooled when passing through the evaporator 32, and moisture in the air condenses to form low-temperature, low-humidity air with reduced absolute humidity. The compressor 29 is configured to suck heat when passing through the air to obtain low dehumidified air having a temperature slightly higher than room temperature, and the compressor 29 is rotationally driven by a compressor motor 33.

前記操作装置7は、箱形状でこの箱体の表面板には、前
記乾燥機5と前記除湿装置2とを張込、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扼み36、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表示窓37
及びモニター表示等を設け、底板外側には外気湿度を検
出する外気温度センサ38及び外気湿度を検出する外気
湿度センサ39を設けた構成であり、内部には乾燥制御
装置4o及び温度制御装置41等を設けた構成であり、
該水分設定猟み36はロータリースイッチ方式であり、
操作装置によって所定の数値が設定される構成である。
The operating device 7 is box-shaped, and has a start switch 34 on the surface plate of the box for installing the dryer 5 and the dehumidifying device 2, and a start switch 34 for starting the drying and discharging operations, and a stop switch 34 for stopping the dryer 5 and the dehumidifying device 2. A switch 35, a moisture setting strainer 36 for setting the grain finishing target moisture depending on the operating position, and a display window 37 for alternately displaying detected grain moisture, detected drying temperature, remaining drying time, etc.
and a monitor display, etc., and an outside air temperature sensor 38 for detecting outside air humidity and an outside air humidity sensor 39 for sensing outside air humidity are installed on the outside of the bottom plate, and a drying control device 4o, a temperature control device 41, etc. are installed inside. It has a configuration with
The moisture setting switch 36 is a rotary switch type,
This configuration is such that a predetermined numerical value is set by an operating device.

該乾燥制御装置40は、前記除湿湿度センサ14、前記
排風湿度センサ15、前記水分センサ25、該外気温度
センサ38及び該外気温度センサ39が検出する検出値
をA−D変換するA−D変換器42、このA−D変換器
42で変換された変換値が入力される入力回路43、該
各スイッチ34.35及び該水分設定猟み36の操作が
入力される入力回路44、これら各入力回路43.44
から入力される各種入力値を算術論理演算及び比較演算
等を行うCPU45、このCPU45から指令される各
種指令を受けて出力する出力回路46を設けた構成であ
る。
The drying control device 40 converts the detected values detected by the dehumidifying humidity sensor 14, the exhaust air humidity sensor 15, the moisture sensor 25, the outside air temperature sensor 38, and the outside air temperature sensor 39 from AD to AD. A converter 42, an input circuit 43 to which the converted value converted by the A-D converter 42 is input, an input circuit 44 to which the operations of the switches 34, 35 and the moisture setting control 36 are input, and each of these Input circuit 43.44
The configuration includes a CPU 45 that performs arithmetic and logical operations, comparison operations, etc. on various input values input from the CPU 45, and an output circuit 46 that receives and outputs various commands issued from the CPU 45.

前記温度制御装置41は、前記除湿装置2から発生する
除湿風の温度を温度センサ47で検出する検出値をA−
D変換するA−D変換器、このA−り変換器で変換され
た変換値が人力される入力回路、この入力回路から入力
される入力値を算術論理演算及び比較演算等を行う該C
PU45、このCPU45から指令される各種指令を受
けて出力する該出力回路46を設けた構成である。
The temperature control device 41 detects the temperature of the dehumidified air generated from the dehumidifying device 2 using a temperature sensor 47, and converts the detected value to A-.
An A-D converter that performs D conversion, an input circuit into which the converted value converted by this A-to-D converter is input manually, and a C that performs arithmetic and logical operations, comparison operations, etc. on the input values input from this input circuit.
The configuration includes a PU 45 and an output circuit 46 that receives various commands from the CPU 45 and outputs them.

前記乾燥制御装置40による乾燥制御は下記の如く行わ
れる構成であり、前記水分設定猟み36を操作するとこ
の操作位置が前記CPU45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、前記水分センサ2
5が検出する穀粒水分が該CPU45へ入力され、これ
ら入力された検出穀粒水分と設定された仕上目標水分と
が比較され、検出穀粒水分が設定仕上目標水分と同じに
なると、この乾燥制御装置40で自動制御して前記乾燥
機5を自動停止する構成である。
The drying control by the drying control device 40 is performed as follows. When the moisture setting knob 36 is operated, this operating position is input to the CPU 45, and the finishing target moisture of the grain is set by this input. The moisture sensor 2
The grain moisture detected by 5 is input to the CPU 45, and the input detected grain moisture and the set finishing target moisture are compared, and when the detected grain moisture becomes the same as the set finishing target moisture, this drying The dryer 5 is automatically controlled by a control device 40 to automatically stop the dryer 5.

前記除湿湿度センサ14で前記送風室12内の除湿風の
絶対湿度が検出されて該CPU45へ入力され、又前記
排風湿度センサ15で前記排風室3内の排風の絶対湿度
が検出されて該CPU45へ入力されると、これら入力
された両者の絶対湿度の湿度差がこのCPU45で算出
され、この算出された算出湿度差と該CPU45へ設定
して記憶させた一定値の設定湿度差とが比較され、相違
していると設定の一定値の湿度差と同じになるように、
前記排風機モータ8の回転数が制御されこの排風機モー
タ8で回転駆動する前記排風機4の回転数が制御され、
この排風機4で吸引排風する前記吸入口27より吸入す
る外気風の風量が増減制御される構成であり、又この算
出された算出湿度差と穀粒水分側によって該CPU45
へ設定して記憶させた設定湿度差とが比較され、相違し
ていると設定湿度差と同じになるように、上記と同じよ
うに、該排風機4の回転数が制御され、この排風機4で
吸引排風する該吸入口27より吸入する外気風の風量が
増減制御される構成である。
The dehumidifying humidity sensor 14 detects the absolute humidity of the dehumidified air in the ventilation chamber 12 and inputs it to the CPU 45, and the exhaust air humidity sensor 15 detects the absolute humidity of the exhaust air in the ventilation chamber 3. When the humidity is inputted to the CPU 45, the CPU 45 calculates the difference in absolute humidity between the two inputs, and the calculated humidity difference and the set humidity difference of the constant value set and stored in the CPU 45. are compared, and if there is a difference, it will be the same as the humidity difference of the set constant value,
The rotation speed of the exhaust fan motor 8 is controlled, and the rotation speed of the exhaust fan 4 rotationally driven by the exhaust fan motor 8 is controlled,
The exhaust fan 4 is configured to increase or decrease the amount of outside air sucked in through the suction port 27, and the CPU 45 controls the calculated humidity difference and grain moisture side.
The set humidity difference set and stored is compared, and if there is a difference, the rotation speed of the exhaust fan 4 is controlled in the same way as above so that the humidity difference is the same as the set humidity difference, and this exhaust fan 4, the amount of outside air sucked in through the suction port 27 is controlled to increase or decrease.

前記外気温度センサ38で外気温度が検出されて前記C
PU45へ入力され、又前記外気温度センサ39で外気
湿度が検出されて該CPU45へ入力されると、これら
入力された両者の入力値がら穀粒の水分勾配が推定算出
され、このCPU45へ設定して記憶させた設定水分勾
配と比較され、この設定水分勾配と同じにするために穀
粒の循環速度がこのCPU45で算出され、この算出さ
れた循環速度から穀粒の循環間隔がこのCPU45で算
出され、この算出された循環間隔と同じになるように、
該CPU45で前記バルブモータ9の回転間隔が制御さ
れ、このバルブモータ9で回転駆動される前記各繰出バ
ルブ11の回転間隔が制御され、この繰出バルブ11は
間欠回転駆動されて穀粒は間欠循環制御され、穀粒の損
傷及び乾減率の低下を防止する構成である。
The outside air temperature is detected by the outside air temperature sensor 38 and the C
When the outside air humidity is detected by the outside air temperature sensor 39 and inputted to the CPU 45, the moisture gradient of the grain is estimated from both of these input values and set to the CPU 45. The CPU 45 calculates the grain circulation speed to make it the same as the set moisture gradient, and calculates the grain circulation interval from the calculated circulation speed. and is the same as this calculated circulation interval.
The CPU 45 controls the rotation interval of the valve motor 9, and the rotation interval of each delivery valve 11 rotationally driven by the valve motor 9 is controlled, and the delivery valve 11 is driven to rotate intermittently, so that the grains are circulated intermittently. This is a controlled configuration that prevents grain damage and reduced drying rate.

前記温度制御装置41による温度制御と湿度制御とは下
記の如く行われる構成であり、前記CPU45へ設定し
て記憶させた前記除湿装置2から発生する除湿風の温度
及び湿度と同じになるように、温度は前記温度センサ4
7で検出されて相違していると設定温度と同じになるよ
うに、吸入される外気風量が制御される構成であり、湿
度は前記除湿湿度センサ14で検出されて相違している
と設定湿度と同じになるように、前記圧縮機29を回転
駆動する前記圧縮機モータ33の回転数が制御される構
成である。
The temperature control and humidity control by the temperature control device 41 are performed as follows, and the temperature and humidity are set to be the same as the temperature and humidity of the dehumidified air generated from the dehumidifying device 2, which are set and stored in the CPU 45. , the temperature is determined by the temperature sensor 4
If the humidity is detected by the dehumidifying humidity sensor 14 and there is a difference, the amount of outside air taken in is controlled so that the temperature becomes the same as the set temperature. In this configuration, the rotation speed of the compressor motor 33 that rotationally drives the compressor 29 is controlled so that

なお、第7図と第1図の一部とは他の実施例を示す図で
、第7図の如く前記前壁板内壁部には前記貯留室16内
に貯留された乾燥中の穀粒の温度を検出する穀温センサ
48を設けた構成であり、又前記凝縮器30を吸入する
外気風が通過する通過路(イ)と熱が外部へ放熱される
通過路(ロ)との二個用に設け、これら(イ)通路、又
は(ロ)通路へ切換える各切換バルブ49を設け、この
各切換バルブ49の切換操作によって、冷媒を(イ)通
路へ通過に切換えると従来通り外気風は除湿風に変換さ
れて、この除湿風で穀粒は乾燥される構成であり、又冷
媒を(ロ)通路へ通過に切換えると外気風は冷却風に変
換されて、この冷却風で穀粒は冷却されて、穀粒温度を
低下させる構成である。
Note that FIG. 7 and a part of FIG. 1 are views showing another embodiment, and as shown in FIG. The structure is equipped with a grain temperature sensor 48 that detects the temperature of Each switching valve 49 is provided individually to switch the refrigerant to the (a) passage or (b) passage, and by switching the switching valve 49, the refrigerant is switched to pass through the (a) passage. is converted into dehumidified air, and the grains are dried with this dehumidified air.Also, when the refrigerant is changed to pass through the (b) passage, the outside air is converted into cooling air, and this cooling air is used to dry the grains. is cooled to reduce grain temperature.

前記穀温センサ48が検出する検出値は、前記A−D変
換器42で、A−D変換され、この変換値が前記入力回
路43へ入力され、更に前記CPU45へ入力される構
成であり、この入力された穀温とこのCPU45へ設定
して記憶した穀温とが比較され、検出穀温が設定穀温以
上を検出すると、このCPU45で該各切換バルブ49
の切換操作が行われ、冷媒は(ロ)通路を通過する構成
となり、穀粒を冷却する構成として穀粒の穀温上昇によ
る食味低下を防止する構成とするもよい。
The detected value detected by the grain temperature sensor 48 is A-D converted by the A-D converter 42, and this converted value is input to the input circuit 43 and further input to the CPU 45, This input grain temperature is compared with the grain temperature set and stored in this CPU 45, and when the detected grain temperature is higher than the set grain temperature, this CPU 45 controls each switching valve 49.
The switching operation may be performed and the refrigerant passes through the (b) passage, and the structure may be configured to cool the grains and to prevent a decrease in taste due to an increase in the grain temperature of the grains.

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.

操作装置7の水分設定猟み36を所定位置へ操作して、
乾燥を開始する始動スイッチ34を操作することにより
、穀粒乾燥機5の各部、除湿装置2及び水分センサ25
等が始動し、この除湿装置2から除湿風が発生し、この
除湿風が送風室12から乾燥室1を通過して排風室3を
経て排風機4で吸引排風されることにより、貯留室16
内に収容した穀粒は、この貯留室16から該乾燥室1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で下部へと繰出されて流下して集穀樋10内から供
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18内へ供給され、この移送樋18
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16内へ均等に拡散供給され、
循環乾燥されて践水分センサ25が該水分設定扼み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、誤操作装置7の乾燥制御装置40で自動制御し
て該乾燥機5を自動停止する。
Operate the moisture setting knob 36 of the operating device 7 to a predetermined position,
By operating the start switch 34 that starts drying, each part of the grain dryer 5, the dehumidifier 2 and the moisture sensor 25
etc. are started, dehumidified air is generated from this dehumidifying device 2, and this dehumidified air passes from the ventilation chamber 12 to the drying chamber 1, passes through the ventilation chamber 3, and is sucked and exhausted by the exhaust fan 4. room 16
The grains stored in the storage chamber 16 are exposed to the dehumidified air and dried while flowing down the drying chamber 1 from the storage chamber 16, and then are fed to the lower part by the feeding valve 11 and flowed down into the grain collection gutter 10. The grains are transferred from the grain through the supply gutter 23 into the grain raising machine 20 by a lower transfer spiral, are conveyed to the upper part by the packet conveyor 21, and are fed into the transfer gutter 18 via the dispensing cylinder 22, and this transfer gutter 18
From there, it is transferred and supplied onto a diffusion plate 19 by an upper transfer spiral, and uniformly diffused and supplied into the storage chamber 16 by this diffusion plate 19,
The moisture sensor 25 is circulated and dried and the moisture setting strainer 36
When the moisture content of the grains is the same as the target moisture content set by operating the dryer 5, the drying control device 40 of the erroneous operation device 7 automatically controls the dryer 5 to automatically stop the dryer 5.

この乾燥作業中は、該乾燥室1を通過する以前の該除湿
装置2から発生する除湿風の絶対湿度が該送風室12内
の除湿湿度センサ14で検出され、又この乾燥室1を通
過後の排風の絶対湿度が該排風室3内の排風湿度センサ
15で検出され、これら検出された絶対湿度の湿度差が
算出され、この算出された湿度差が一定値になるように
、該排風機4で吸引排風する吸入口27から吸入されて
除湿風に変換される外気風の風量が制御されながら穀粒
は乾燥され、又この算出された湿度差と穀粒水分側によ
って設定記憶させた設定湿度差とが比較され、相違して
いると設定湿度差と同じになるように、該排風機4で吸
引排風する吸入口27から吸入されて除湿風に変換され
る外気風の風量が制御されて穀粒は乾燥される。
During this drying work, the absolute humidity of the dehumidified air generated from the dehumidifying device 2 before passing through the drying chamber 1 is detected by the dehumidifying humidity sensor 14 in the ventilation chamber 12, and after passing through the drying chamber 1, The absolute humidity of the exhaust air of The grains are dried while controlling the volume of outside air that is sucked in from the suction port 27 and converted into dehumidified air by the exhaust fan 4, and is set based on the calculated humidity difference and the grain moisture side. The stored humidity difference is compared with the set humidity difference, and if there is a difference, the outside air is drawn in from the inlet 27 and converted into dehumidified air by the exhaust fan 4 so that the humidity becomes the same as the set humidity difference. The grains are dried by controlling the air volume.

又算出される水分勾配と設定記憶させた設定水分勾配と
が比較され、相違していると設定水分勾配と同じになる
ように、前記繰出バルブ11の間欠回転の間隔が制御さ
れて穀粒は乾燥される。
The calculated moisture gradient and the stored moisture gradient are compared, and if they are different, the intermittent rotation interval of the delivery valve 11 is controlled so that the gradient becomes the same as the set moisture gradient, and the grains are dried.

【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
ック図は、第2図フローチャート図、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正面図、第7図は他の実施例を示す
図で、第7図は穀粒乾燥機の全体側面図である。 図中、符号lは乾燥室、2は除湿装置、3は排風室、4
は排風機を示す。
The figures show one embodiment of the present invention, in which Fig. 1 is a block diagram, Fig. 2 is a flowchart, Fig. 3 is an overall side view of the grain dryer, and Fig. 4 is an A in Fig. 3. -A sectional view, 5th
The figure is a rear view of a part of the grain dryer, Figure 6 is a partially cutaway front view of a part of the grain dryer, and Figure 7 is a view showing another embodiment. It is an overall side view of a grain dryer. In the figure, symbol l is a drying room, 2 is a dehumidifier, 3 is an exhaust room, and 4 is a drying room.
indicates an exhaust fan.

Claims (1)

【特許請求の範囲】 1 穀粒を乾燥室1へ繰出し流下させながら除湿装置2
による除湿風を該乾燥室1へ通風させて排風室3を経て
排風機4で機外へ吸引排風させて乾燥させる穀粒乾燥機
において、この乾燥室1を通風前のこの除湿風と通風後
の排風との両者の絶対湿度を検出して湿度差を算出して
この算出湿度差を一定値に保持すべく該排風機4で吸引
排風する該除湿風風量を制御して乾燥することを特徴と
する乾燥制御方式。 2 穀粒を乾燥室1へ繰出し流下させながら除湿装置2
による除湿風を該乾燥室1へ通風させて排風室3を経て
排風機4で機外へ吸引排風させて乾燥させる穀粒乾燥機
において、この乾燥室1を通風前のこの除湿風と通風後
の排風との両者の絶対湿度を検出して湿度差を算出して
この算出湿度差を穀粒水分にもとづいてあらかじめ設定
して記憶させた設定湿度差と同じにすべく該排風機4で
吸引排風する該除湿風風量を制御して乾燥することを特
徴とする乾燥制御方式。
[Claims] 1. A dehumidifying device 2 while feeding grains into a drying chamber 1 and letting them flow down.
In a grain dryer in which dehumidified air is ventilated into the drying chamber 1, passed through an exhaust chamber 3, and sucked and exhausted outside the machine by an exhaust fan 4 for drying, this dehumidified air before being ventilated in the drying chamber 1 and The absolute humidity between the exhaust air after ventilation and the exhaust air is detected, the humidity difference is calculated, and the air volume of the dehumidifying air sucked and discharged by the exhaust fan 4 is controlled to maintain the calculated humidity difference at a constant value. A drying control method characterized by: 2 The dehumidifier 2 feeds the grains into the drying chamber 1 while letting them flow down.
In a grain dryer in which dehumidified air is ventilated into the drying chamber 1, passed through an exhaust chamber 3, and sucked and exhausted outside the machine by an exhaust fan 4 for drying, this dehumidified air before being ventilated in the drying chamber 1 and The exhaust fan detects the absolute humidity between the air and the exhaust air after ventilation, calculates the humidity difference, and makes this calculated humidity difference the same as a set humidity difference that has been set and stored in advance based on grain moisture. A drying control method characterized in that drying is carried out by controlling the volume of the dehumidifying air sucked and discharged in step 4.
JP25305189A 1989-09-27 1989-09-27 Dry control system for grain dryer Pending JPH03113281A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25305189A JPH03113281A (en) 1989-09-27 1989-09-27 Dry control system for grain dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25305189A JPH03113281A (en) 1989-09-27 1989-09-27 Dry control system for grain dryer

Publications (1)

Publication Number Publication Date
JPH03113281A true JPH03113281A (en) 1991-05-14

Family

ID=17245801

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25305189A Pending JPH03113281A (en) 1989-09-27 1989-09-27 Dry control system for grain dryer

Country Status (1)

Country Link
JP (1) JPH03113281A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002079371A1 (en) * 2001-03-29 2002-10-10 Sapporo Breweries Ltd. Method of controlling absolute humidity of air stream in kilning step and kilning apparatus
KR100967118B1 (en) * 2007-10-31 2010-07-05 이세키노우키가부시키가이샤 Drying device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002079371A1 (en) * 2001-03-29 2002-10-10 Sapporo Breweries Ltd. Method of controlling absolute humidity of air stream in kilning step and kilning apparatus
US7182268B2 (en) 2001-03-29 2007-02-27 Sapporo Breweries Ltd. Method of controlling the absolute humidity of air stream in kilning step and kilning apparatus
KR100967118B1 (en) * 2007-10-31 2010-07-05 이세키노우키가부시키가이샤 Drying device

Similar Documents

Publication Publication Date Title
JPH03113281A (en) Dry control system for grain dryer
JPH0436586A (en) Dry control system for grain dryer
JPH03181783A (en) Drying control system of grain dryer
JPH03102188A (en) Dry control system for cereals drier
JPH046387A (en) Drying control system for grain drier
JPH03102185A (en) Dry control system for cereals drier
JPH03271689A (en) Control system for drying in grain drier
JPH0436581A (en) Dehumidifier for grain dryer
JPH03247984A (en) Drying control system for grain dryer
JPH03211387A (en) Drying control method for grain dryer
JPH03181780A (en) Drying control system of grain dryer
JPH03144282A (en) Drying device for grain drying machine and the like
JPH0436585A (en) Dry control system for grain dryer
JPH03181778A (en) Drying control system for grain dryer
JPH03144283A (en) Control of drying in grain drying machine
JPH0370980A (en) Control of drying in grain drier
JPH03102187A (en) Dry control system for cereals drier
JPH046385A (en) Drying air supplying device for grain dryer
JPH03181779A (en) Drying control system for grain dryer
JPH03230083A (en) Drying control apparatus of grain dryer
JPH03233287A (en) Drying control method for grain dryer
JPH03230082A (en) Drying control apparatus of grain dryer
JPH03199884A (en) Control of drying in grain dryer
JPH03113283A (en) Dry control system for grain dryer
JPH03247985A (en) Drying control system for grain dryer