JPH02219976A - Dry control system for grain drier - Google Patents

Dry control system for grain drier

Info

Publication number
JPH02219976A
JPH02219976A JP4075089A JP4075089A JPH02219976A JP H02219976 A JPH02219976 A JP H02219976A JP 4075089 A JP4075089 A JP 4075089A JP 4075089 A JP4075089 A JP 4075089A JP H02219976 A JPH02219976 A JP H02219976A
Authority
JP
Japan
Prior art keywords
air temperature
hot air
exhaust air
sensor
detected
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
JP4075089A
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 JP4075089A priority Critical patent/JPH02219976A/en
Publication of JPH02219976A publication Critical patent/JPH02219976A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

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、穀粒を流下させながらバーナによる熱風を通風
させて乾燥する乾燥室と、この乾燥室を通風前の熱風温
度と通風後に機外へ排風する排風温度を検出する熱風温
度センサ、排風温度センサ及び乾燥中の穀粒水分を検出
する水分センサとを設け、該熱風温度センサが検出する
熱風温度が設定熱風温度と同じ温度になるように制御し
、又該熱風温度センサが検出する熱風温度と誠排風温度
センサが検出する排風温度とによって乾燥中の穀粒の温
度を算出し、この算出した穀粒温度が設定穀粒温度以上
に上昇しないように熱風温度を制御して乾燥制御する方
式であり、この乾燥作業中に該熱風温度センサ及び該排
風温度センサに不具合が発生して熱風温度及び排風温度
を検出しなくなると穀粒の乾燥を停止する乾燥制御方式
であった。
Conventional technology Conventionally, there was a drying chamber in which grains were dried by passing hot air through a burner while flowing down, and a hot air temperature in this drying chamber was detected to detect the temperature of the hot air before ventilation and the temperature of the exhaust air discharged outside the machine after ventilation. A temperature sensor, an exhaust air temperature sensor, and a moisture sensor for detecting grain moisture during drying are provided, and the hot air temperature detected by the hot air temperature sensor is controlled to be the same as the set hot air temperature, and the hot air temperature is The temperature of the grains being dried is calculated from the hot air temperature detected by the sensor and the exhaust air temperature detected by the Makoto exhaust air temperature sensor, and the hot air temperature is adjusted so that the calculated grain temperature does not rise above the set grain temperature. This method controls drying by controlling the temperature of the grains, and if a malfunction occurs in the hot air temperature sensor and the exhaust air temperature sensor during this drying operation and the hot air temperature and exhaust air temperature are no longer detected, drying of the grains is stopped. It was a drying control method.

発明が解決しようとする課題 穀粒は乾燥室内を繰出し流下する循環を繰返しながら、
バーナから発生する熱風がこの乾燥室を通風することに
より、この乾燥室内を流下中のこの穀粒はこの熱風に晒
されて乾燥され、水分センサが仕上目標水分と同じ穀粒
水分を検出すると穀粒の乾燥を停止する。
Problems to be solved by the invention While the grains are repeatedly circulated as they are fed out and flowed down inside the drying chamber,
The hot air generated from the burner passes through the drying chamber, and the grains flowing down the drying chamber are exposed to the hot air and dried. When the moisture sensor detects the same grain moisture as the finishing target moisture, the grains are Stop grain drying.

この乾燥のときは、熱風温度センサが検出する熱風温度
が設定熱風温度と同じ温度になるように熱風温度が制御
され、又該熱風温度センサが検出する熱風温度と排風温
度センサが検出する排風温度とによって乾燥中の穀粒の
温度を算出し、この算出した穀粒温度が設定穀粒温度以
上に上昇しないように熱風温度が制御されて穀粒を乾燥
制御するが、この乾燥中に該熱風温度センサ及び詠排風
温度センサに不具合が発生して熱風温度及び排風温度を
検出しなくなると穀粒の乾燥を停止]−シていたが、熱
風温度及び排風温度を検出しなくなっても、この検出す
る熱風温度及びこの検出する排風温度に相当する制御熱
風温度及び制御排風温度を算出させて、この算出した制
御熱風温度及び制御排風温度で穀粒の乾燥を継続制御さ
せようとするものである。
During this drying, the hot air temperature is controlled so that the hot air temperature detected by the hot air temperature sensor is the same as the set hot air temperature, and the hot air temperature detected by the hot air temperature sensor and the exhaust air temperature detected by the exhaust air temperature sensor are controlled. The temperature of the grains during drying is calculated based on the air temperature, and the hot air temperature is controlled so that the calculated grain temperature does not rise above the set grain temperature to control the drying of the grains. When a malfunction occurs in the hot air temperature sensor and exhaust air temperature sensor and the hot air temperature and exhaust air temperature are no longer detected, drying of grains is stopped. Even if the hot air temperature is detected, the control hot air temperature and control exhaust air temperature corresponding to the detected hot air temperature and the detected exhaust air temperature are calculated, and the drying of grains is continuously controlled using the calculated control hot air temperature and control exhaust air temperature. It is an attempt to do so.

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、穀粒を流下させながらバーナ(1)による
熱風を通風させて乾燥する乾燥室(2)と、この乾燥室
(2)を通風前の熱風温度を検出する熱風温度センサ(
3)、この乾燥室(2)を通風して機外へ排風する排風
温度を検出する排風温度センサ(4)、及び乾燥中の穀
粒水分を検出する水分センサ(5)とを設けた穀粒乾燥
機において、該排風温度センサ(4)で該排風温度が検
出されないときは該熱風温度センサ(3)が検出する該
熱風温度、及び該水分センサ(5)が検出する該穀粒水
分によって該排風温度に相当する制御排風温度を算出し
て乾燥制御を行うか、又は、該水分センサ(5)が検出
する該穀粒水分の他に排風の排風湿度を検出する排風湿
度センサ(6)が検出する排風湿度によって該排風温度
に相当する該制御排風温度を算出して乾燥制御すること
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 This invention provides a drying chamber (2) in which grains are dried by passing hot air from a burner (1) while flowing down, and a drying chamber (2) in which the grains are dried by ventilation. Hot air temperature sensor to detect the previous hot air temperature (
3), an exhaust air temperature sensor (4) that detects the temperature of the exhaust air ventilated through this drying room (2) and exhausted outside the machine, and a moisture sensor (5) that detects the moisture content of the grains during drying. In the provided grain dryer, when the exhaust air temperature is not detected by the exhaust air temperature sensor (4), the hot air temperature is detected by the hot air temperature sensor (3), and the moisture sensor (5) is detected. Drying control is performed by calculating a controlled exhaust air temperature corresponding to the exhaust air temperature based on the grain moisture, or the exhaust air humidity of the exhaust air is calculated in addition to the grain moisture detected by the moisture sensor (5). The drying control method is characterized in that the control exhaust air temperature corresponding to the exhaust air temperature is calculated based on the exhaust air humidity detected by the exhaust air humidity sensor (6) that detects the exhaust air humidity, and the drying control is performed.

発明の作用 穀粒は乾燥室(2)内を繰出し流下する循環を繰返しな
がら、バーナ(1)から発生する熱風がこの乾燥室(2
)を通風することにより、この乾燥室(2)内を流下中
のこの穀粒はこの熱風に晒されて乾燥され、水分センサ
(5)が仕上目標水分と同じ穀粒水分を検出すると穀粒
の乾燥を停止する。
Effect of the invention While the grains are repeatedly circulated in the drying chamber (2) and flowing down, the hot air generated from the burner (1) flows into the drying chamber (2).
), the grains flowing down in the drying chamber (2) are exposed to this hot air and dried, and when the moisture sensor (5) detects the same grain moisture as the finishing target moisture, the grains are stop drying.

この乾燥のときは、該バーナ(1)から発生して該乾燥
室(2)を通風前の熱風温度は熱風温度センサ(3)で
検出され、該乾燥室(2)を通風して機外へ排風する排
風温度は排風温度センサ(4)で検出され、又排風湿度
は排風湿度センサ(6)で検出され、これら検出された
熱風温度と排風温度とによって乾燥中の穀粒の温度が算
出され、この算出された穀粒温度と設定した穀粒温度と
が比較され、設定穀粒温度以上に算出穀粒温度が上昇し
ないように熱風温度が制御されなから穀粒は乾燥される
が、この乾燥中に排風温度が該排風温度センサ(4)で
検出されなくなると、検出した熱風温度と検出した穀粒
水分とによって、この排風温度に相当する制御排風温度
が算出され、この算出の制御排風温度と検出された熱風
温度とによって、上記の如く穀粒温度が算出され、この
算出穀粒温度と設定穀粒温度とによって、熱風温度が制
御されながら穀粒は乾燥されるか、又は検出した排風湿
度と検出した穀粒水分とによって、この排風温度に相当
する制御排風温度が算出され、この算出の制御排風温度
と検出された熱風温度とによって、上記の如く穀粒温度
が算出され、この算出穀粒温度と設定穀粒温度とによっ
て、熱風温度が制御されながら穀粒は乾燥される。
During this drying, the temperature of the hot air generated from the burner (1) before being ventilated into the drying chamber (2) is detected by the hot air temperature sensor (3), and the temperature of the hot air generated from the burner (1) is detected by the hot air temperature sensor (3). The temperature of the exhaust air discharged to the air is detected by the exhaust air temperature sensor (4), and the exhaust air humidity is detected by the exhaust air humidity sensor (6). The temperature of the grain is calculated, the calculated grain temperature is compared with the set grain temperature, and the hot air temperature is controlled so that the calculated grain temperature does not rise above the set grain temperature. is dried, but if the exhaust air temperature is no longer detected by the exhaust air temperature sensor (4) during this drying, the detected hot air temperature and the detected grain moisture will cause the controlled exhaust air to correspond to this exhaust air temperature. The wind temperature is calculated, and the grain temperature is calculated as described above using the calculated control exhaust air temperature and the detected hot air temperature, and the hot air temperature is controlled based on the calculated grain temperature and the set grain temperature. The grains are dried while the grains are being dried, or a controlled exhaust air temperature corresponding to this exhaust air temperature is calculated based on the detected exhaust air humidity and the detected grain moisture, and the calculated controlled exhaust air temperature is detected. The grain temperature is calculated as described above based on the hot air temperature, and the grains are dried while the hot air temperature is controlled based on the calculated grain temperature and the set grain temperature.

発明の効果 この発明により、乾燥作業中に排風温度を検出する排風
温度センサ(4)に不具合が発生して、排風温度を検出
しなくなったときでも、熱風温度センサ(3)が検出す
る熱風温度、水分センサ(5)が検出する穀粒水分及び
排風湿度センサ(6)が検出する排風湿度等によって、
この排風温度に相当する制御排風温度が算出され、この
算出された制御排風温度によって穀粒の乾燥制御が行わ
れることにより、所定の時間内に乾燥を終了させること
ができるし、又所定の穀粒温度が確保できることにより
穀粒に銅剤が発生することもない。
Effects of the Invention With this invention, even when a malfunction occurs in the exhaust air temperature sensor (4) that detects the exhaust air temperature during drying work and the exhaust air temperature is no longer detected, the hot air temperature sensor (3) can still detect the exhaust air temperature. Depending on the hot air temperature, the grain moisture detected by the moisture sensor (5), the exhaust air humidity detected by the exhaust air humidity sensor (6), etc.
A controlled exhaust air temperature corresponding to this exhaust air temperature is calculated, and grain drying control is performed based on this calculated controlled exhaust air temperature, so that drying can be completed within a predetermined time. Since a predetermined grain temperature can be ensured, no copper agent is generated in the grains.

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、穀粒を流下させながらバーナ(1)による
熱風を通風させて乾燥する乾燥室(2)と、この乾燥室
(2)を通風前の熱風温度を検出する熱風温度センサ(
3)、この乾燥室(2)を通風後に機外へ排風する排風
温度を検出する排風温度センサ(4)、及び乾燥中の穀
粒水分を検出する水分センサ(5)とを設けた穀粒乾燥
機において、該熱風温度センサ(3)で該熱風温度が検
出されないときは該排風温度センサ(4)が検出する該
排風温度、及び該水分センサ(5)が検出する該穀粒水
分によって誠熱風温度に相当する制御熱風温度を算出し
て乾燥制御を行うか、又は、該水分センサ(5)が検出
する該穀粒水分の他に排風の排風湿度を検出する排風湿
度センサ(6)が検出する排風湿度によって該熱風温度
に相当する該制御熱風温度を算出して乾燥制御すること
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 This invention provides a drying chamber (2) in which grains are dried by passing hot air from a burner (1) while flowing down, and a drying chamber (2) in which the grains are dried by ventilation. Hot air temperature sensor to detect the previous hot air temperature (
3) This drying room (2) is equipped with an exhaust air temperature sensor (4) that detects the temperature of the exhaust air discharged outside the machine after ventilation, and a moisture sensor (5) that detects the moisture content of the grains during drying. In the grain dryer, when the hot air temperature sensor (3) does not detect the hot air temperature, the exhaust air temperature detected by the exhaust air temperature sensor (4) and the temperature detected by the moisture sensor (5) are Drying control is performed by calculating a controlled hot air temperature corresponding to the true hot air temperature based on the grain moisture, or the humidity of the exhaust air is detected in addition to the grain moisture detected by the moisture sensor (5). The drying control method is characterized in that drying control is performed by calculating the control hot air temperature corresponding to the hot air temperature based on the exhaust air humidity detected by the exhaust air humidity sensor (6).

発明の作用 穀粒は乾燥室(2)内を繰出し流下する循環を繰返しな
がら、バーナ(1)から発生する熱風がこの乾燥室(2
)を通風することにより、この乾燥室(2)内を滴下中
のこの穀粒はこの熱風に晒されて乾燥され、水分センサ
く5)が仕上目標水分と同じ穀粒水分を検出すると穀粒
の乾燥を停止する。
Effect of the invention While the grains are repeatedly circulated in the drying chamber (2) and flowing down, the hot air generated from the burner (1) flows into the drying chamber (2).
), the grains dripping in the drying chamber (2) are exposed to this hot air and dried, and when the moisture sensor 5) detects grain moisture equal to the finishing target moisture, the grains are stop drying.

この乾燥のときは、該バーナ(1)から発生して該乾燥
室(2)を通風前の熱風温度は熱風温度センサ(3)で
検出され、該乾燥室(2)を通風して機外へ排風する排
風温度は排風温度センサ(4)で検出され、又排風湿度
は排風湿度センサ(6)で検出され、この検出された熱
風温度と設定された熱風温度とが比較され、相違してい
ると設定熱風温度と同じ温度になるように制御されなが
ら穀粒は乾燥されるが、この乾燥中に熱風温度が該熱風
温度センサ(3)で検出されなくなると、検出した排風
温度と検出した穀粒水分とによって、この熱風温度に相
当する制御熱風温度が算出され、この算出の制御熱風温
度と設定熱風温度とが上記の如く比較され、相違してい
る設定熱風温度と同じ温度になるように制御されなから
穀粒は乾燥されるか、又は検出した排風湿度と検出した
穀粒水分とによって、この熱風温度に相当する制御熱風
温度が算出され、この算出の制御熱風温度と設定熱風温
度とが上記の如く比較され、相違している設定熱風温度
と同じ温度になるように制御されながら穀粒は乾燥され
る。
During this drying, the temperature of the hot air generated from the burner (1) before being ventilated into the drying chamber (2) is detected by the hot air temperature sensor (3), and the temperature of the hot air generated from the burner (1) is detected by the hot air temperature sensor (3). The temperature of the exhaust air discharged to the air is detected by the exhaust air temperature sensor (4), and the humidity of the exhaust air is detected by the exhaust air humidity sensor (6), and the detected hot air temperature and the set hot air temperature are compared. If the hot air temperature is different, the grains are dried while being controlled so that the temperature is the same as the set hot air temperature, but if the hot air temperature is no longer detected by the hot air temperature sensor (3) during this drying, it is detected. A control hot air temperature corresponding to this hot air temperature is calculated based on the exhaust air temperature and the detected grain moisture, and the calculated control hot air temperature and the set hot air temperature are compared as described above to determine which set hot air temperature is different. Either the grains are dried without being controlled to the same temperature as the temperature, or the controlled hot air temperature corresponding to this hot air temperature is calculated from the detected exhaust air humidity and the detected grain moisture. The controlled hot air temperature and the set hot air temperature are compared as described above, and the grains are dried while being controlled to have the same temperature as the different set hot air temperature.

発明の効果 この発明により、乾燥作業中に熱風温度を検出する熱風
温度センサ(3)に不具合が発生して、熱風温度を検出
しなくなったときでも、排風温度センサ(4)が検出す
る排風温度、水分センサ(5)が検出する穀粒水分及び
排風湿度センサ(6)が検出する排風湿度等によって、
この熱風温度に相半する制御熱風温度が算出され、この
算出された制御熱風温度によって穀粒の乾燥制御が行わ
れることにより、所定の時間内に乾燥を終了させること
ができるし、又所定の熱風温度が確保できることにより
安定した穀粒の乾燥ができる。
Effects of the Invention According to the present invention, even when a malfunction occurs in the hot air temperature sensor (3) that detects the hot air temperature during drying work and the hot air temperature is no longer detected, the exhaust air temperature sensor (4) detects the hot air temperature. Depending on the wind temperature, grain moisture detected by the moisture sensor (5), exhaust air humidity detected by the exhaust air humidity sensor (6), etc.
A control hot air temperature that is half of this hot air temperature is calculated, and grain drying control is performed based on this calculated control hot air temperature, so that drying can be completed within a predetermined time, and the drying can be completed within a predetermined time. By ensuring the hot air temperature, stable grain drying is possible.

実施例 なお、園側において、(7)は穀粒乾燥機であり、この
乾燥機(7)の機壁(8)は前後方向に長い長方形状で
、前後壁板及び左右壁板よりなり、この前壁板にはこの
乾燥機(7)を始動及び停止操作する操作装置(9)及
びバーナ(1)を内装したバーナケース(lO)を設け
、このバーナケース(10)下板外側には燃料バルブを
有する燃料ポンプ(11)を設け、この燃料バルブの開
閉によりこの燃料ポンプ(11)で燃料タンク(12)
内の燃料を吸入して該バーナ(1)へ供給する構成であ
り、上板外側には送風機(13)及び変速モータ(14
)を設け、この変速モータ(14)の回転により該送風
機(13)を回転駆動して供給燃料量に見合った燃焼用
空気を該バーナ(1)へ供給する構成であり、該後壁板
には排風機(15)及びモータ(16)を設けた構成で
ある。
Embodiment On the farm side, (7) is a grain dryer, and the machine wall (8) of this dryer (7) has a rectangular shape long in the front and back direction, and consists of front and rear wall plates and left and right wall plates. A burner case (lO) containing an operating device (9) for starting and stopping the dryer (7) and a burner (1) is installed on this front wall plate, and the outside of the lower plate of this burner case (10) is A fuel pump (11) having a fuel valve is provided, and the fuel tank (12) is opened and closed by the fuel pump (11) by opening and closing the fuel valve.
The structure is such that fuel is sucked in and supplied to the burner (1), and a blower (13) and a variable speed motor (14) are installed on the outside of the upper plate.
), and the blower (13) is rotationally driven by the rotation of the variable speed motor (14) to supply combustion air commensurate with the amount of fuel to be supplied to the burner (1). The configuration includes an exhaust fan (15) and a motor (16).

該機壁(8)内下部の中央部には前後方向に亘り移送螺
旋を内装した集穀樋(17)を設け、この集穀1 (1
7)上側には通気網間に形成した乾燥室(2)を並設し
て連通させ、この乾燥室(2)下部には穀粒を繰出し流
下させる繰出バルブ(20)を軸装した構成であり、こ
の各乾燥室(2)内側間には熱風室(18)を形成して
該バーナ(1)と連通させ、この熱風室(工8)にはこ
の熱風室(18)内を通過する熱風の熱風温度を検出す
る熱風温度センサ(3)を設けた構成であり、該各乾燥
室(2)外側には排風室(19)を形成してこの各排風
室(19)と該排風機(15)とを連通させ、この各排
風室(19)内にはこの排風室(19)内を通過する排
風の排風温度を検出する排風温度センサ(4)及び排風
湿度を検出する排風湿度センサ(6)を設けた構成であ
り、該モータ(16)で該移送螺旋、該各繰出バルブ(
20)及び該排風機(15)等を回転駆動する構成であ
る。
A grain collection gutter (17) equipped with a transfer spiral in the front and back direction is provided in the center of the lower part of the machine wall (8), and this grain collection 1 (1
7) On the upper side, drying chambers (2) formed between ventilation networks are arranged in parallel and communicated with each other, and at the bottom of this drying chamber (2), a feeding valve (20) for feeding and flowing grains is installed. A hot air chamber (18) is formed between the inner sides of each of the drying chambers (2) and communicates with the burner (1). The configuration includes a hot air temperature sensor (3) that detects the temperature of hot air, and an exhaust chamber (19) is formed outside each drying chamber (2), and a The exhaust fan (15) is connected to the exhaust fan (15), and each exhaust chamber (19) includes an exhaust air temperature sensor (4) that detects the temperature of the exhaust air passing through the exhaust chamber (19). The configuration includes an exhaust air humidity sensor (6) that detects wind humidity, and the motor (16) operates the transfer spiral and each delivery valve (
20) and the exhaust fan (15).

該各乾燥室(2)上側には貯留室(21)を形成して連
通させ、この貯留室(21)上側には天井板(23)及
び移送螺旋を内装した移送樋(24)を設け、この移送
@ (24)中央部には移送穀粒をこの貯留室(21)
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(21)内へ穀粒を均等に拡散還元する拡散盤(2
5)を設けた構成である。
A storage chamber (21) is formed above each of the drying chambers (2) and communicated with each other, and a ceiling plate (23) and a transfer gutter (24) equipped with a transfer spiral are provided above the storage chamber (21). This transfer @ (24) In the central part, the transferred grain is stored in this storage chamber (21)
A diffusion plate (2) is provided below the supply port to uniformly diffuse and return grains into the storage chamber (21).
5).

昇穀機(26)は、前記前壁板的方部に設け、内部には
パケットコンベア(27)ベルトを上下プーリ間に張設
し、上端部と誤移送樋(24)始端部との間には投出筒
(28)を設けて連通させ、下端部と前記集穀@ (1
7)終端部との間には供給@(29)を設けて連通させ
た構成であり、この昇穀機(26)上部にはモータ(3
0)を設け、このモータ(30)で該パケットコンベア
(27)ベルト、該移送樋(24)内の該移送螺旋及び
該拡散盤(25)等を回転駆動する構成であり、又上下
方向はぼ中央部には該パケットコンベア(27)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水分センサ
(5)を設け、この水分センサ(5)には二の水分セン
サ(5)の各部を回転駆動するモータ(31)を内装し
た構成である。
The grain elevating machine (26) is installed on the side of the front wall plate, and inside thereof, a packet conveyor (27) belt is stretched between the upper and lower pulleys, and between the upper end and the starting end of the mistransfer gutter (24). is provided with a discharging tube (28) to communicate with the lower end and the grain collecting @ (1
7) A supply @ (29) is provided between the terminal end and the motor (3) is connected, and a motor (3
0), and this motor (30) rotates the packet conveyor (27) belt, the transfer spiral in the transfer gutter (24), the diffusion plate (25), etc., and the vertical direction is A moisture sensor (5) is installed in the center of the machine to receive grains that fall while being conveyed to the upper part of the packet conveyor (27), crush the grains under pressure, and simultaneously detect moisture in the crushed grains. This moisture sensor (5) has a built-in motor (31) that rotationally drives each part of the second moisture sensor (5).

前記操作装置(9)は、箱形状でこの箱体の表面板には
、前記乾燥機(7)を張込、乾燥及び排出の各作業別に
始動操作する各始動スイッチ(32)、停止操作する停
止スイッチ(33) 、前記バーナ(1)から発生する
熱風温度が操作位置によって設定される各温度設定風み
(34) 、仕−ヒ目標水分が操作位置によって設定さ
れる水分設定風み(35)、該水分センサ(5)が検出
する穀粒水分、前記熱風温度センサ(3)が検出する熱
風温度、乾燥残時間等を交互に表示する表示窓(36)
及びモニター表示等を設けた構成であり、内部には乾燥
制御装置(37)及び燃焼制御装置(38)を設けた構
成であり、該各設定猟み(34)、(35)はロータリ
スイッチ方式であり、操作位置によって所定の数値が設
定される構成である。
The operating device (9) is box-shaped, and on the surface plate of the box body are installed start switches (32) for starting and stopping the dryer (7) for each of drying and discharging operations. A stop switch (33), each temperature setting airflow (34) in which the temperature of the hot air generated from the burner (1) is set depending on the operating position, and a moisture setting airflow (35) in which the service target moisture content is set depending on the operating position. ), a display window (36) that alternately displays grain moisture detected by the moisture sensor (5), hot air temperature detected by the hot air temperature sensor (3), remaining drying time, etc.
The structure includes a drying control device (37) and a combustion control device (38), and each setting (34) and (35) is controlled by a rotary switch. The configuration is such that a predetermined numerical value is set depending on the operating position.

該燃焼制御装置(38)は、前記熱風温度センサ(3)
、前記排風温度センサ(4)及び前記排風湿度センサ(
6)が検出する検出値をA−D変換するA−D変換器(
39) 、このA−D変換器(39)で変換された変換
値が入力される入力回路(40)、該各スイッチ(32
)、 (33)及び該温度設定猟み(34)の操作が入
力される入力回路(41)、これら各入力回路(40)
、 (41)から入力される各種入力値を算出論理演算
及び比較演算等を行うCPU (42) 、このCPU
(42)から指令される各種指令を受けて出力する出力
rg回路り43)を設けた構成である。
The combustion control device (38) includes the hot air temperature sensor (3).
, the exhaust air temperature sensor (4) and the exhaust air humidity sensor (
6) A-D converter (
39), an input circuit (40) into which the converted value converted by this A-D converter (39) is input, and each switch (32).
), (33) and an input circuit (41) into which the temperature setting operation (34) is input, and each of these input circuits (40)
, (41) A CPU that calculates various input values, performs logical operations, comparison operations, etc. (42), this CPU
The configuration includes an output rg circuit 43) that receives various commands from (42) and outputs them.

前記乾燥制御袋R(37)は、前記水分センサ(5)が
検出する検出値をA−D変換するA−D変換器、このA
−D変換器で変換された変換値が入力される入力回路、
前記水分設定蝋み(35)の操作が入力される入力回路
、これら各入力回路から入力される各種入ノ1値を算出
論理演算及び比較演算等を行う該CPU (42) 、
このCPU(42)から指令される各種指令を受けて出
力する出力回路を設けた構成である。
The drying control bag R (37) is equipped with an A-D converter that converts the detection value detected by the moisture sensor (5) from A to D.
- an input circuit into which the converted value converted by the D converter is input;
an input circuit into which the operation of the moisture setting wax (35) is input; the CPU (42) which performs calculations, logical operations, comparison operations, etc. on various input values input from each of these input circuits;
The configuration includes an output circuit that receives various commands from the CPU (42) and outputs them.

前記燃焼制御袋Wt(38)による燃焼制御は、前記熱
風温度センサ(3)が検出する熱風温度(TB)と前記
排風温度センサ(4)が検出する排m温度(TC)とが
前記CPU(42)へ入力され、この検出した熱風温度
(TB)と排風温度(TC)とによって乾燥中の穀粒温
度が、このCPU(42)で検出される構成であり、こ
の算出された穀粒温度が該CPU(42)へ設定して記
憶させた穀粒温度と比較され、相違していると設定穀粒
温度と同じ温度になるように、前記燃料バルブの開閉回
数が制御され、前記燃料ポンプ(11)で吸入する燃料
量がこの燃焼制御装置(38)で制御される構成であり
、又該熱風温度センサ(3)が検出する熱風温度(TB
)と前記温度設定扼み(34)を操作して設定した熱風
温度(TB ’ )とが比較され、相違しているとこの
設定熱風温度(TB ’ )と同じ温度になるように、
該燃料バルブの開閉回数が制御され、該燃料ポンプ(1
1)で吸入する燃料量がこの燃焼制御装置(38)で制
御される構成である。
The combustion control by the combustion control bag Wt (38) is such that the hot air temperature (TB) detected by the hot air temperature sensor (3) and the exhaust air temperature (TC) detected by the exhaust air temperature sensor (4) are controlled by the CPU. (42), and the kernel temperature during drying is detected by this CPU (42) based on the detected hot air temperature (TB) and exhaust air temperature (TC). The grain temperature is compared with the grain temperature set and stored in the CPU (42), and if there is a difference, the number of times the fuel valve is opened and closed is controlled so that the temperature becomes the same as the set grain temperature. The amount of fuel taken in by the fuel pump (11) is controlled by this combustion control device (38), and the hot air temperature (TB) detected by the hot air temperature sensor (3) is controlled by the combustion control device (38).
) and the hot air temperature (TB') set by operating the temperature setting controller (34) are compared, and if there is a difference, the temperature is set to be the same as this set hot air temperature (TB').
The number of times the fuel valve opens and closes is controlled, and the fuel pump (1
In this configuration, the amount of fuel taken in in step 1) is controlled by this combustion control device (38).

この燃焼制御中に前記排風温度センサ(4)が断線等の
不具合が発生して排風温度(TC)を検出しなくなると
、この排風温度(TC)に相当する制御排風温度(TC
A)を下記式(イ)により算出する構成であり、 制御排風温度(TCA)=熱風温度(TB) X変動係
数(A)・・・(イ) 例えば、前記水分センサ(5)が検出した穀粒水分が2
0%であり、前記熱風温度センサ(3)が検出した熱風
温度(TB)が50℃であり、前記排風湿度センサ(6
)が検出した排風湿度が70%であると、第5図の如く
、前記CPU(42)へ設定して記憶させた変動係数(
A)がこのCPU(42)により、熱風温度(TB) 
50℃と穀粒水分20%とより0.68と選定され、上
記式(イ)へ代入して下記の如く算出する構成であり 制御排風温度(TCA) =50 Xo、68=34℃
この算出した制御排風温度(TCA)34℃と検出した
熱風温度(TB) 50℃とによって乾燥中の穀粒の温
度を算出する構成であるか、又は下記式(ロ)と上記式
(イ)とによって制御排風温度(TCA)を算出する構
成であり、 排風湿度(TV) =熱風温度(TB) X変動係数(
B)・・・(ロ) 検出した穀粒水分20%と検出した排風湿度(TV)7
0%ととより、第6図の如く、該CPU(42)へ設定
して記憶させた変動係数(B)を排風湿度70%と穀粒
水分20%とより1.3と選定され、上記式(イ)、 
(ロ)へ代入して下記の如く算出する構成であり、 制御排風温度(TCA)/変動係数(A)=排風湿度(
TV) /変動係数(B) 制御排風温度(TCA)=排風湿度(TV) /変動係
数(B)X変動係数(A) 制御排風温度(TCA)士70/1.3 Xo、68=
36.6℃この(イ)、(ロ)式で算出した制御排風温
度(TCA)34℃と36.6℃とを該CPU(42)
へ設定して記憶させた重み(W)を付けた下記式へ代入
して算出する構成であり、 制御排風温度(TCA)= (W) x (イ)式算出
による制御排風温度(TCA)+(1−(W) ) X
(ロ)式算出による1!制御排風温度(TCA)制御排
風温度(TCA) =0.7 X34+(1−0,7)
X36.6士35℃ この算出した制御排風温度(T(J35℃と検出した熱
風温度(TB) 50℃とによって乾燥中の穀粒の温度
を算出する構成である。
If the exhaust air temperature sensor (4) fails to detect the exhaust air temperature (TC) due to a malfunction such as wire breakage during this combustion control, the controlled exhaust air temperature (TC) corresponding to this exhaust air temperature (TC)
A) is calculated by the following formula (A), where: Control exhaust air temperature (TCA) = Hot air temperature (TB) X coefficient of variation (A)... (A) For example, the moisture sensor (5) detects The grain moisture content is 2
0%, the hot air temperature (TB) detected by the hot air temperature sensor (3) is 50°C, and the exhaust air humidity sensor (6)
) is 70%, as shown in Figure 5, the variation coefficient (
A) is controlled by this CPU (42) to determine the hot air temperature (TB)
The configuration is such that 0.68 is selected from 50°C and 20% grain moisture, and is calculated as follows by substituting it into the above formula (a). Control exhaust air temperature (TCA) = 50 Xo, 68 = 34°C
Either the temperature of the grains being dried is calculated based on the calculated controlled exhaust air temperature (TCA) of 34°C and the detected hot air temperature (TB) of 50°C, or the following formula (b) and the above formula (i) are used. ) is configured to calculate the controlled exhaust air temperature (TCA), where exhaust air humidity (TV) = hot air temperature (TB) X coefficient of variation (
B)...(B) Detected grain moisture 20% and detected exhaust air humidity (TV) 7
0%, as shown in FIG. 6, the coefficient of variation (B) set and stored in the CPU (42) is selected to be 1.3 based on the exhaust air humidity of 70% and the grain moisture of 20%, The above formula (a),
(B) is calculated as follows, Controlled exhaust air temperature (TCA) / Coefficient of variation (A) = Exhaust air humidity (
TV) / Coefficient of variation (B) Controlled exhaust air temperature (TCA) = Exhaust air humidity (TV) / Coefficient of variation (B) X Coefficient of variation (A) Controlled exhaust air temperature (TCA) 70/1.3 Xo, 68 =
36.6°C The control exhaust air temperature (TCA) 34°C and 36.6°C calculated using formulas (a) and (b) are calculated by the CPU (42).
The configuration is such that the control exhaust air temperature (TCA) is calculated by substituting it into the following formula with the weight (W) set and stored in )+(1-(W))X
(b) 1 by formula calculation! Controlled exhaust air temperature (TCA) Controlled exhaust air temperature (TCA) =0.7 X34+(1-0,7)
X36.6 -35°C The temperature of the grains being dried is calculated based on the calculated controlled exhaust air temperature (T(J35°C) and the detected hot air temperature (TB) 50°C.

又この燃焼制御中に前記熱風温度センサ(3)が断線等
の不具合が発生して熱風温度(TB)を検出しなくなる
と、この熱風温度(TB)に相当する制御熱風温度(T
BA)を下記式(ハ)により算出する構成であり、 制御熱風温度(TBA) =排風温度(TC,) /変
動係数(C)・・・(ハ) 例えば、前記水分センサ(5)が検出した穀粒水分20
%であり、前記排風温度センサ(4)が検出した排風温
度が32℃であり、前記排風湿度センサ(6)が検出し
た排風湿度75%であると、第7図の如く、前記CPU
(42)へ設定して記憶させた変動係数(C)がこのC
PU(42)により、排風温度(TO) 32℃と穀粒
水分20%とより0.62と選定され、上記(ハ)式へ
代入されて下記の如く算出する構成であり、 制御熱風温度(TDA) =3210.62=51.6
℃この算出した制御熱風温度(TBA)5:L。6℃と
設定した熱風温度(TB ”)とが比較され、この51
.6℃が設定熱風温度(TB ’ )と同じ温度になる
ように制御される構成であるか、又は下記式(ニ)によ
って制御熱風温度(TBA)を算出する構成であり、制
御熱風温度(TBA) =排風湿度(T’/) /変動
係数(D)・・・(ニ) 検出した穀粒水分20%検出した排風湿度(TV)75
%とより、第8図の如く、該CPU(42)へ設定して
記憶させた変動係数1.44と選定され、上記式(ニ)
へ代入されて下記の如く算出する構成であり、 制御熱風温度(TBA)=75/1.44=52℃この
(ハ)、(ニ)式で算出した制御熱風温度(TBA)5
1.6℃と52℃とを該にPU(42)へ設定して記憶
させた重みを付けた下記式へ代入して算出する構成であ
り、 制御熱風温度(TBA)= (w) x (ハ)式算出
による制御熱風温度(TBA)+ (1−(W) ) 
Xに)式算出による制御熱風温度(TBA)制御熱風温
度(TBA)=0.7 X51゜6+(1−0,7)X
52=51.72℃ この算出した5N、72℃と設定熱風温度(TB ’ 
)とが比較され、この51゜72℃が設定熱風温度(T
B ’)と同じ温度になるように制御される構成である
Also, if the hot air temperature sensor (3) fails to detect the hot air temperature (TB) due to a problem such as disconnection during this combustion control, the control hot air temperature (T) corresponding to this hot air temperature (TB)
BA) is calculated by the following formula (c), where: Control hot air temperature (TBA) = Exhaust air temperature (TC,) / Coefficient of variation (C) (c) For example, if the moisture sensor (5) Detected grain moisture 20
%, the exhaust air temperature detected by the exhaust air temperature sensor (4) is 32°C, and the exhaust air humidity detected by the exhaust air humidity sensor (6) is 75%, as shown in FIG. Said CPU
The coefficient of variation (C) set and stored in (42) is this C
According to PU (42), 0.62 is selected from the exhaust air temperature (TO) of 32°C and grain moisture of 20%, and is substituted into the above equation (c) to calculate as follows. Control hot air temperature (TDA) =3210.62=51.6
℃ This calculated control hot air temperature (TBA) 5:L. 6℃ and the set hot air temperature (TB”) are compared, and this 51
.. 6℃ is the same as the set hot air temperature (TB'), or the controlled hot air temperature (TBA) is calculated by the following formula (d), and the controlled hot air temperature (TBA) is the same as the set hot air temperature (TB'). ) = Exhaust air humidity (T'/) / Coefficient of variation (D)... (d) Detected grain moisture 20% Detected exhaust air humidity (TV) 75
%, the variation coefficient set and stored in the CPU (42) is selected as 1.44 as shown in FIG. 8, and the above formula (d)
Control hot air temperature (TBA) = 75/1.44 = 52°C Control hot air temperature (TBA) 5 calculated using formulas (c) and (d)
It is configured to calculate by substituting 1.6°C and 52°C into the following formula with weights set and stored in the PU (42), Control hot air temperature (TBA) = (w) x ( C) Control hot air temperature (TBA) + (1-(W)) calculated by formula
Controlled hot air temperature (TBA) by formula calculation Controlled hot air temperature (TBA) = 0.7
52=51.72℃ This calculated 5N, 72℃ and the set hot air temperature (TB'
) is compared, and this 51°72°C is the set hot air temperature (T
This is a configuration in which the temperature is controlled to be the same as that of B').

又この制御熱風温度(TrlA)51.72℃を前記C
PU (42)へ設定して記憶させた補正係数0.9で
補正して51.75℃X0.9 =46゜5℃と算出し
、この算出した46.5℃と設定熱風温度(TB ’ 
)とが比較され、この46.5℃が設定熱風温度(TB
 ”)とが同じ温度になるように制御される構成とする
もよい。
In addition, this controlled hot air temperature (TrlA) of 51.72°C is
Corrected with the correction coefficient 0.9 set and stored in PU (42), it was calculated as 51.75°C x 0.9 = 46°5°C, and this calculated 46.5°C and the set hot air temperature (TB'
) is compared, and this 46.5℃ is the set hot air temperature (TB
”) may be controlled to have the same temperature.

前記乾燥制御装置(37)による乾燥制御は、前記水分
センサ(5)が前記水分設定扼み(35)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、この
乾燥制御袋fl (37)で自動制御して前記乾燥機(
7)を自動停止する構成である。
The drying control by the drying control device (37) is performed when the moisture sensor (5) detects the same grain moisture as the finishing target moisture set by operating the moisture setting strainer (35). (37) automatically controls the dryer (
7) is configured to automatically stop.

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(9)の各設定扼み(34)、(35)を所定
の位置へ操作し、乾燥作業を開始する始動スイッチ(3
2)を操作することにより、穀粒乾燥機(7)の各部、
バーナ(1)及び水分センサ(5)等が始動し、このバ
ーナ(1)から熱風が発生し二の熱風が熱風室(18)
から乾燥室(2)を通風し、排風室(19)を経て排風
機(15)で吸引排風されることにより、この乾燥機(
7)内に収容した穀粒は、貯留室(21)から該乾燥室
(2)内を流下中にこの熱風に晒されて乾燥され、繰出
バルブ(20)で下部へと繰出されて流下し集穀@(1
7)内へ供給され、この集穀1 (17)から供給樋(
29)を経て昇穀機(26)内へ下部の移送螺旋で移送
供給され、パケットコンベア(27)で上部へ搬送され
投出! (28)を経て移送+ii (24)内へ供給
され、この移送! (24)から拡散盤(25)上へ上
部の移送螺旋で移送供給され、この拡散盤(25)で該
貯留室(21)内へ均等に拡散還元され、循環乾燥され
て該水分センサ(5)が該水分設定扼み(35)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
、vi操作装置(9)の乾燥制御装置(37)で自動制
御して該乾燥機(7)を自動停止する。
Operate each setting knob (34), (35) of the operating device (9) to a predetermined position, and press the start switch (3) to start the drying operation.
2), each part of the grain dryer (7),
The burner (1), moisture sensor (5), etc. start, and hot air is generated from this burner (1), and the second hot air is sent to the hot air chamber (18).
This dryer (
7) The grains housed in the storage chamber (21) are exposed to this hot air and dried while flowing down in the drying chamber (2), and are fed out to the lower part by the feeding valve (20) and flowed down. Grain gathering @ (1
7) and from this collection 1 (17) to the supply gutter (
29) and into the grain hoisting machine (26) by the lower transfer spiral, and then conveyed to the upper part by the packet conveyor (27) and thrown out! (28) and is supplied into transport+ii (24), and this transport! (24) onto the diffusion plate (25) by the upper transfer spiral, and is evenly diffused and reduced into the storage chamber (21) by this diffusion plate (25), and is circulated and dried. ) detects the same grain moisture as the finishing target moisture set by operating the moisture setting strainer (35), the drying control device (37) of the vi operating device (9) automatically controls the drying machine ( 7) to automatically stop.

この乾燥作業中に排風温度を検出する排風温度センサ(
4)に不具合が発生し、この排風温度が検出されなくな
ると、二の排風温度に相当する制御排風温度が、熱風温
度センサ(3)が検出する熱風温度、該水分センサ(5
)が検出する穀粒水分及び排風湿度センサ(6)が検出
する排風湿度等によって算出され、この算出された制御
排風温度と検出熱風温度とによって乾燥中の穀粒温度が
算出され、この制御排風温度と設定穀粒温度とが比較さ
れ、該バーナ(1)から発生する温度が制御されて穀粒
は乾燥される。
Exhaust air temperature sensor (
If a problem occurs in 4) and this exhaust air temperature is no longer detected, the controlled exhaust air temperature corresponding to the second exhaust air temperature will be changed to the hot air temperature detected by the hot air temperature sensor (3) and the moisture sensor (5).
) is detected by the grain moisture and the exhaust air humidity detected by the exhaust air humidity sensor (6), and the grain temperature during drying is calculated from the calculated control exhaust air temperature and the detected hot air temperature, This controlled exhaust air temperature is compared with a set grain temperature, and the temperature generated from the burner (1) is controlled to dry the grains.

又熱風温度を検出する該熱風温度センサ(3)に不具合
が発生し、この熱風温度が検出されなくなると、この熱
風温度に相当する制御熱風温度が、該排風温度センサ(
4)が検出する排風温度、前記水分センサ(5)が検出
する穀粒水分及び該排風湿度センサ(6)が検出する排
風湿度等によって算出され、この算出された制御熱風温
度と設定熱風温度とが比較され、前記バーナ(1)から
発生する熱風温度が制御されて穀粒は乾燥される。
In addition, if a malfunction occurs in the hot air temperature sensor (3) that detects the hot air temperature and the hot air temperature is no longer detected, the control hot air temperature corresponding to this hot air temperature will be changed to the exhaust air temperature sensor (3).
4), the grain moisture detected by the moisture sensor (5), the exhaust humidity detected by the exhaust humidity sensor (6), etc., and the calculated control hot air temperature and settings. The temperature of the hot air is compared with that of the hot air, and the temperature of the hot air generated from the burner (1) is controlled to dry the grains.

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

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図は一部破断せる乾燥機の全体側面図、第
3図は第2図のA、 −A断面図、第4図は乾燥機の一
部の一部破断せる拡大正面図、第5図は熱風温度、及び
穀粒水分と変動係数との関係図、第6図は排風湿度、及
び穀粒水分と変動係数との関係図、第7図は排風湿度、
及び穀粒水分と変動係数との関係図、第8図は排風湿度
、及び穀粒水分と変動係数との関係図である。 図中、符号(1)はバーナ、(2)は乾燥室、(3)は
熱風温度センサ、 (4)は排風温度センサ、(5)は
水分センサ、(6)は排風湿度センサを示す。
The figures show one embodiment of the present invention, in which Fig. 1 is a block diagram, Fig. 2 is an overall side view of the dryer that can be partially cut away, and Fig. 3 is a cross-sectional view of A and -A in Fig. 2. , Fig. 4 is an enlarged partially cutaway front view of a part of the dryer, Fig. 5 is a diagram of the relationship between hot air temperature, grain moisture, and coefficient of variation, and Fig. 6 is a diagram showing the relationship between exhaust air humidity and grain moisture. Figure 7 shows the relationship between the coefficient of variation and the exhaust air humidity.
FIG. 8 is a diagram showing the relationship between exhaust air humidity, grain moisture, and coefficient of variation. In the figure, (1) is the burner, (2) is the drying chamber, (3) is the hot air temperature sensor, (4) is the exhaust air temperature sensor, (5) is the moisture sensor, and (6) is the exhaust air humidity sensor. show.

Claims (1)

【特許請求の範囲】 1 穀粒を流下させながらバーナ(1)による熱風を通
風させて乾燥する乾燥室(2)と、この乾燥室(2)を
通風前の熱風温度を検出する熱風温度センサ(3)、こ
の乾燥室(2)を通風して機外へ排風する排風温度を検
出する排風温度センサ(4)、及び乾燥中の穀粒水分を
検出する水分センサ(5)とを設けた穀粒乾燥機におい
て、該排風温度センサ(4)で該排風温度が検出されな
いときは該熱風温度センサ(3)が検出する該熱風温度
、及び該水分センサ(5)が検出する該穀粒水分によっ
て該排風温度に相当する制御排風温度を算出して乾燥制
御を行うか、又は、該水分センサ(5)が検出する該穀
粒水分の他に排風の排風湿度を検出する排風湿度センサ
(6)が検出する排風湿度によって該排風温度に相当す
る該制御排風温度を算出して乾燥制御することを特徴と
する乾燥制御方式。 2 穀粒を流下させながらバーナ(1)による熱風を通
風させて乾燥する乾燥室(2)と、この乾燥室(2)を
通風前の熱風温度を検出する熱風温度センサ(3)、こ
の乾燥室(2)を通風後に機外へ排風する排風温度を検
出する排風温度センサ(4)、及び乾燥中の穀粒水分を
検出する水分センサ(5)とを設けた穀粒乾燥機におい
て、該熱風温度センサ(3)で該熱風温度が検出されな
いときは該排風温度センサ(4)が検出する該排風温度
、及び該水分センサ(5)が検出する該穀粒水分によっ
て該熱風温度に相当する制御熱風温度を算出して乾燥制
御を行うか、又は、該水分センサ(5)が検出する該穀
粒水分の他に排風の排風湿度を検出する排風湿度センサ
(6)が検出する排風湿度によって該熱風温度に相当す
る該制御熱風温度を算出して乾燥制御することを特徴と
する乾燥制御方式。
[Claims] 1. A drying chamber (2) in which grains are dried by blowing hot air from a burner (1) while flowing down, and a hot air temperature sensor that detects the hot air temperature before blowing through this drying chamber (2). (3), an exhaust air temperature sensor (4) that detects the temperature of the exhaust air ventilated through this drying chamber (2) and exhausted outside the machine, and a moisture sensor (5) that detects the moisture content of the grains during drying. In a grain dryer equipped with The drying control is performed by calculating the control exhaust air temperature corresponding to the exhaust air temperature based on the grain moisture, or the exhaust air temperature is calculated based on the grain moisture detected by the moisture sensor (5). A drying control method characterized by performing drying control by calculating the control exhaust air temperature corresponding to the exhaust air temperature based on the exhaust air humidity detected by an exhaust air humidity sensor (6) that detects humidity. 2. A drying chamber (2) in which the grains are dried by passing hot air through the burner (1) while flowing down, a hot air temperature sensor (3) that detects the temperature of the hot air before ventilation in this drying chamber (2), and a A grain dryer equipped with a chamber (2), an exhaust air temperature sensor (4) that detects the temperature of the exhaust air discharged outside the machine after ventilation, and a moisture sensor (5) that detects the moisture content of the grains during drying. In this case, when the hot air temperature is not detected by the hot air temperature sensor (3), the temperature is determined by the exhaust air temperature detected by the exhaust air temperature sensor (4) and the grain moisture detected by the moisture sensor (5). Drying control is performed by calculating a control hot air temperature corresponding to the hot air temperature, or an exhaust air humidity sensor (5) that detects exhaust air humidity in addition to the grain moisture detected by the moisture sensor (5) is used. 6) A drying control method characterized in that drying is controlled by calculating the controlled hot air temperature corresponding to the hot air temperature based on the exhaust air humidity detected by 6).
JP4075089A 1989-02-20 1989-02-20 Dry control system for grain drier Pending JPH02219976A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4075089A JPH02219976A (en) 1989-02-20 1989-02-20 Dry control system for grain drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4075089A JPH02219976A (en) 1989-02-20 1989-02-20 Dry control system for grain drier

Publications (1)

Publication Number Publication Date
JPH02219976A true JPH02219976A (en) 1990-09-03

Family

ID=12589309

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4075089A Pending JPH02219976A (en) 1989-02-20 1989-02-20 Dry control system for grain drier

Country Status (1)

Country Link
JP (1) JPH02219976A (en)

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