JPS5828971A - Automatic controller for cereal drier - Google Patents

Automatic controller for cereal drier

Info

Publication number
JPS5828971A
JPS5828971A JP12691481A JP12691481A JPS5828971A JP S5828971 A JPS5828971 A JP S5828971A JP 12691481 A JP12691481 A JP 12691481A JP 12691481 A JP12691481 A JP 12691481A JP S5828971 A JPS5828971 A JP S5828971A
Authority
JP
Japan
Prior art keywords
grain
section
drying
moisture
hot air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP12691481A
Other languages
Japanese (ja)
Inventor
佐竹 利彦
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.)
Satake Engineering Co Ltd
Original Assignee
Satake Engineering 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 Satake Engineering Co Ltd filed Critical Satake Engineering Co Ltd
Priority to JP12691481A priority Critical patent/JPS5828971A/en
Publication of JPS5828971A publication Critical patent/JPS5828971A/en
Pending legal-status Critical Current

Links

Landscapes

  • Drying Of Solid Materials (AREA)

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】 本発明は穀物乾燥機の自動制御装置に関する。[Detailed description of the invention] The present invention relates to an automatic control device for a grain dryer.

穀物の機械的乾燥は一定条件を設定することにより乾燥
能率を上げることができるが、一旦適正な熱風の温度お
よび風量の調節を怠ると、胴割粒、熱損傷粒などの被害
粒を生じ、また食味の低下を来たしてその品質面の影響
は多大である。
Mechanical drying of grains can improve the drying efficiency by setting certain conditions, but if the temperature and air volume of the hot air are not properly adjusted, damaged grains such as split grains and heat-damaged grains may occur. In addition, the taste deteriorates, which has a great impact on quality.

従来、穀物乾燥機に配設した自動水分計により測定した
穀粒水分値によりて前記熱風の温度および風量を連続的
に制御する方法があるが、一般に、抵抗式の自動水分計
では、穀温や穀粒密度等の変化により水分測定値に2−
〜3ts程度の誤差を生ずるので、%に熱感受性の激し
い穀粒水分16%〜21−区域の熱風の温度および風量
を水分針によ抄連続的に自動制御すると、かえって危険
で事故を誘発するおそれがある。
Conventionally, there is a method of continuously controlling the temperature and air volume of the hot air based on the grain moisture value measured by an automatic moisture meter installed in a grain dryer. Moisture measurements may vary by 2-2 due to changes in grain density, grain density, etc.
Continuously automatically controlling the temperature and air volume of the hot air in the 16% to 21-area with grain moisture, which is extremely heat sensitive, using a moisture needle, would be dangerous and cause accidents. There is a risk.

本発明は上記の諸問題を解決するため、循環式の穀物乾
燥機において、その穀物循環行程に水分測定器を設け、
また、火熱発生装置に温度調節部を設けると共に、通風
装置に変速部のある電動機を設け、前記穀量検出部を前
記水分測定器とを制御装置を介して前記温度調節部と前
妃通風装置の変速部に関連的に1かつ電気的に連結する
ことによ抄、前記乾燥機に供給した原料穀粒(11米)
の初期水分値とその穀量をそれぞれ正確K11l定して
制御装置に入力し1前記穀粒(高水分数)に対する初期
の乾燥用熱風を任意所定の温贋(60℃前後)と大風*
(’Id/sec、を以上)に設定すると共に、以後の
前記熱風の風量を制御装置に設けた計時器の信号によっ
て段階的に、または漸減的に低下するようにし、以って
前述の熱感受性の激しい穀粒水分16−〜21チ区域の
乾燥作用を標準乾減率(0,8〜1.011/時)K対
応する熱風の適正風t(4g’ / s・c、t ) 
IIc自動的に調節して胴割粒などの被害粒の発生を完
全に防止し、常に被害粒のない良質の乾燥穀物を能率的
に量産する自動化装置を開発して提供せんとするもので
ある。
In order to solve the above-mentioned problems, the present invention provides a circulation type grain dryer with a moisture measuring device in the grain circulation process.
In addition, the fire heat generating device is provided with a temperature control section, and the ventilation device is provided with an electric motor having a speed change section, and the grain amount detection section is connected to the moisture measuring device through the control device to the temperature control section and the front ventilation device. The raw material grains (11 rice) were fed to the dryer by being electrically connected to the transmission section of the dryer.
Accurately determine the initial moisture value and the amount of grain and input them into the control device, and then set the initial hot air for drying the grains (high moisture content) to an arbitrary predetermined temperature (around 60°C) and large wind *
('Id/sec, or more), and the subsequent flow rate of the hot air is decreased stepwise or gradually by a signal from a timer provided in the control device. The drying effect of the highly sensitive grain moisture zone 16-21 is determined by the standard drying loss rate (0.8-1.011/hour)K.
IIc The objective is to develop and provide an automated device that automatically adjusts to completely prevent the occurrence of damaged grains such as split grains, and efficiently mass-produces high-quality dried grains without damaged grains at all times. .

本発明を実施例図について説明する。図中符号(1)は
乾燥部機体で、該機体(1)の内部に熱風室(匂、穀物
乾燥室(8)、排風室(4)を並立すると共に、その壁
部に火熱発生装置(5)1通風装置(6)をそれぞれ装
着し、また前記機体(1)の上部に穀量検出部ff)の
ある穀槽(8)を搭載すると共に1その機体(1)の−
側に昇降機(9)を立設して穀物循環行程(lO)を一
体的に形成した穀物乾燥機である。そして前記穀物微積
行程(10)の穀槽(8)壁部に水分測定器(11)を
設置、前記火熱発生装置(5) rc温度調節部(12
)を設置ると共に、前記通風装置(6)に変速部(18
)のある電動機(14)を設け、前記穀量検出部(ηと
前記水分測定器(11)とを制御装置(15)を介して
前妃温度調節部(12)と前記通風装置(6)の変一部
(18)に関連的に連結しである。
The present invention will be explained with reference to embodiment figures. The symbol (1) in the figure is the drying section body, and inside the body (1) there are a hot air chamber (grain drying chamber (8)) and an exhaust chamber (4) in parallel, as well as a fire heat generating device on the wall. (5) 1 ventilation device (6) is installed respectively, and a grain tank (8) with a grain amount detection part ff) is mounted on the upper part of the machine body (1), and 1 - of the machine body (1).
This is a grain dryer with an elevator (9) installed on the side to integrally form a grain circulation process (lO). Then, a moisture measuring device (11) is installed on the wall of the grain tank (8) of the grain calculus step (10), and the rc temperature control unit (12) is installed on the wall of the grain tank (8).
) is installed, and a transmission section (18) is installed in the ventilation device (6).
) is provided, and the grain amount detection section (η) and the moisture measuring device (11) are connected to the front temperature control section (12) and the ventilation device (6) via a control device (15). It is connected to the variable part (18) in a relational manner.

次に、前記制御装置(16)を第2図について説明する
。前記水分測定器(11)の水分セン!−(16)と穀
量検出部(7)の各出力倒れアナログ選択回路(17)
、VDコンバータ(18)ヲ介シテCPU(lシリ回路
に連結され、該CPU (19)回路の出力側は前記通
風装置(6)に設けた電動機(14)の変速部(13)
に連結しである。したがって、前記水分測定器(11)
の水分センサー(16)と穀量検出部(7)の各検出信
号はアナレグ選択回路(17)にそれぞれ入力されると
共に、  CPU (19)側からの命令信号によりて
選択されて水分センサー(16)のアナログ信号から順
次K 4/Dコンバータ(18)によりてデジタル値に
変換されてそれぞれ適宜なCPU (19)の記憶装置
に記憶される。そして該水分センサー(16)の測定値
と前記穀量検出部(7)の測定値とによつて前記穀粒(
高水分数)の初期の50℃前後の熱風温f(例えば55
℃)と風量(7m’/eec−t)をそれぞれ算定する
と共に、任意所定の乾燥速fK応じた乾燥行程における
穀粒水分16−〜21−の区域で、標準乾減率(例えば
0.9−7時)の乾燥作用を実施しながら任意の仕上砂
水分値(例えば14.61G)K達するまでの各時間毎
(1時間、2時間・・・・・・I時間)の風量をそれぞ
れ算案してCPU^の記憶装置に格納される。そして前
記各時間毎に計算され九デジタル値は、別の命令により
て出力信号となりて前記通風装置(6)の変速部(18
)に入力されると共に、その都度前記電動機(14)を
適宜に減速回転して風量を漸減的に低下する。なお、前
記乾燥用風量は、水分21−で5 wl / sec、
t 、水分16Isで8 #// sec、tのように
段階的に低下する場合もち抄、また乾燥温度を風量調節
と併行して適宜に低減する場合がある。また、乾燥終了
の直前には、前記水分測定器によってその仕上水分値を
確認することになる。
Next, the control device (16) will be explained with reference to FIG. Moisture sensor of the moisture measuring device (11)! - (16) and each output collapse analog selection circuit (17) of the grain amount detection section (7)
, the VD converter (18) is connected to the CPU (l series circuit), and the output side of the CPU (19) circuit is connected to the transmission section (13) of the electric motor (14) provided in the ventilation device (6).
It is connected to. Therefore, the moisture measuring device (11)
The detection signals from the moisture sensor (16) and the grain detection section (7) are respectively input to the analog selection circuit (17), and are selected by a command signal from the CPU (19) side and sent to the moisture sensor (16). ) are sequentially converted into digital values by a K4/D converter (18) and stored in a storage device of an appropriate CPU (19). Then, the grain (
The initial hot air temperature f around 50℃ (high moisture content) (for example, 55
℃) and air volume (7 m'/eec-t), and calculate the standard drying loss rate (for example, 0.9 Calculate the air volume for each hour (1 hour, 2 hours, etc.) until the desired finished sand moisture value (for example, 14.61G) is reached while performing the drying action (7 o'clock). The data is stored in the CPU's storage device. Then, the nine digital values calculated for each time are converted into output signals by another command, and are converted into output signals by the speed change section (18) of the ventilation device (6).
), and each time the electric motor (14) is rotated at an appropriate deceleration speed, the air volume is gradually reduced. Note that the drying air volume is 5 wl/sec at a moisture content of 21-
In some cases, the drying temperature is reduced stepwise, such as 8 #// sec at a moisture content of 16 Is, or the drying temperature is appropriately reduced in parallel with the air volume adjustment. Further, just before the end of drying, the finished moisture value is checked using the moisture measuring device.

このように本発明の穀物乾燥機の自動制御装置轄、乾燥
機への穀物の張込作業が終了すると、前記水分測定器の
水分センサーと穀量検出部とによつて、穀粒水分とその
穀量を測定して初期の熱風温度と風量を高温度で大風量
に設定すると共に、乾燥作業中は制御装置に設は九計時
器の信号によりて前記風量を適宜に規正して段階的に、
または漸減的に低下するので、極めて乾燥能率がよく、
かつ胴割粒、熱損傷粒1発芽障害粒などのない良質の乾
燥穀物を確実に、かつ円滑迅速に量産できる等の効果が
ある。
In this way, when the grain dryer automatic control device of the present invention finishes loading the grain into the dryer, the moisture sensor and the grain amount detection section of the moisture measuring device measure the moisture content of the grains. The amount of grain is measured and the initial hot air temperature and air volume are set to high temperature and large air volume, and during drying work, the air volume is adjusted in stages according to the signal from the clock set in the control device. ,
or gradually decreases, resulting in extremely high drying efficiency.
In addition, it is possible to reliably, smoothly and quickly mass-produce high-quality dried grains without split grains, heat-damaged grains, germination-impaired grains, etc.

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

図面は本発明の実施例図である。第1図は本装置の儒断
面図、第2図はその制御装置の電気回路図である。 1・・・乾燥部機体    2・・・熱風室8・・・穀
物乾燥室    4・・・排風室5・・・火熱発生装置
   6・・・通風装置7・・・穀量検出部    8
・・・穀 槽9・・・昇降機      1G−・・穀
物循環行程11・・・水分測定器    12・・・温
度調節部13・・・変速部      14・・・電動
機15・・・制御装置     16・・・水分センサ
ー17・・・アナログ選択回路  18・・・A/Dコ
ンバータ19・・・CPU 第 1 4Al 第20
The drawings are illustrations of embodiments of the present invention. FIG. 1 is a sectional view of this device, and FIG. 2 is an electric circuit diagram of its control device. 1...Drying section body 2...Hot air chamber 8...Grain drying room 4...Exhaust air chamber 5...Fire heat generating device 6...Ventilator 7...Grain amount detection section 8
...Grain tank 9...Elevator 1G-...Grain circulation stroke 11...Moisture measuring device 12...Temperature adjustment section 13...Transmission section 14...Electric motor 15...Control device 16. ...Moisture sensor 17...Analog selection circuit 18...A/D converter 19...CPU 1st 4Al 20th

Claims (1)

【特許請求の範囲】[Claims] 穀物乾燥室、熱風室、排風室を並立すると共に、火熱発
生装置と通風装置を設けた転線部機体に穀量検出部のあ
る穀槽を上載して穀物循環行程を形成した乾燥装置にお
いて、前記穀物循環行程に水分測定器を設け、また前記
火熱発生装置に温度調節部を設けると共に、前記通風装
置に変速部のある電動機を設け、前記穀量検出部と前記
水分測定器とを制御装置を介して前記温度調節部と前記
通風装置の変速部に関連的に、かつ電気的に連結し、前
記制御装置に設けたタイマーなどの計時器の信号により
て前記通風装置の変速部を作動して乾燥用熱風の風量を
段階的に、また社漸減的に低下して乾燥するようにした
穀物乾燥機の自動制御装置、。
In a drying device in which a grain drying room, a hot air room, and an exhaust room are installed in parallel, and a grain tank with a grain amount detection unit is mounted on a transfer section body equipped with a heat generating device and a ventilation device to form a grain circulation process. , a moisture measuring device is provided in the grain circulation process, a temperature control section is provided in the fire heat generating device, and an electric motor with a variable speed section is provided in the ventilation device, and the grain amount detecting section and the moisture measuring device are controlled. The temperature control section and the speed change section of the ventilation device are electrically connected through a device, and the speed change section of the ventilation device is actuated by a signal from a timer such as a timer provided in the control device. An automatic control device for a grain dryer that reduces the amount of drying hot air in stages and gradually decreases the amount of drying air.
JP12691481A 1981-08-12 1981-08-12 Automatic controller for cereal drier Pending JPS5828971A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12691481A JPS5828971A (en) 1981-08-12 1981-08-12 Automatic controller for cereal drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12691481A JPS5828971A (en) 1981-08-12 1981-08-12 Automatic controller for cereal drier

Publications (1)

Publication Number Publication Date
JPS5828971A true JPS5828971A (en) 1983-02-21

Family

ID=14947010

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12691481A Pending JPS5828971A (en) 1981-08-12 1981-08-12 Automatic controller for cereal drier

Country Status (1)

Country Link
JP (1) JPS5828971A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5413064A (en) * 1977-06-30 1979-01-31 Iseki & Co Ltd Dryer
JPS55123980A (en) * 1979-03-16 1980-09-24 Satake Eng Co Ltd Automatic controller for grain drier

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5413064A (en) * 1977-06-30 1979-01-31 Iseki & Co Ltd Dryer
JPS55123980A (en) * 1979-03-16 1980-09-24 Satake Eng Co Ltd Automatic controller for grain drier

Similar Documents

Publication Publication Date Title
JPS5828971A (en) Automatic controller for cereal drier
EP0139536A2 (en) Method of and apparatus for controlling the temperature of a drying machine
JPS5826983A (en) Automatic controller for cereal drier
JPS59138880A (en) Method of drying cereal
JPS6333073B2 (en)
JPH0544593B2 (en)
JPS618590A (en) Cereal drier
JPS5872873A (en) Control system of drying of circulation type cereal drier
JPS59104074A (en) Method of drying cereal
JPS5934270B2 (en) Burner combustion control device in grain dryer
JPS636381A (en) Cereal drier controller
SU1423150A1 (en) Method of automatic control of active ventilation of grain
JPS618589A (en) Controller for temperature of hot air in circulation type cereal grain drier
JPS60228889A (en) Method and device for drying cereal
JPS58104482A (en) Automatic drying controlling system of primary product
JPH0252542B2 (en)
SU1142713A1 (en) Method of automatic control of drying process
JPS6158157B2 (en)
JPS62206375A (en) Method of controlling drying of circulation type cereal drier
JPH0633936B2 (en) Grain dryer
JPS6215190B2 (en)
JPS6122177A (en) Cereal drier
JPS62129679A (en) Automatic stop device in cereal grain drier
JPS6096887A (en) Cereal drier
JPH0472153B2 (en)