JPH08178529A - Burner combustion controller of grain drier - Google Patents

Burner combustion controller of grain drier

Info

Publication number
JPH08178529A
JPH08178529A JP31958194A JP31958194A JPH08178529A JP H08178529 A JPH08178529 A JP H08178529A JP 31958194 A JP31958194 A JP 31958194A JP 31958194 A JP31958194 A JP 31958194A JP H08178529 A JPH08178529 A JP H08178529A
Authority
JP
Japan
Prior art keywords
burner
time
flow rate
amount
rate
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
JP31958194A
Other languages
Japanese (ja)
Inventor
Takashi Nagai
永井  隆
Shinji Ninomiya
伸治 二宮
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 JP31958194A priority Critical patent/JPH08178529A/en
Publication of JPH08178529A publication Critical patent/JPH08178529A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE: To prevent the hunting from occurring in ON time of a burner in a big flow-rate for a set heating-amount by making difference in the amount of change in the ON time of the burner between the big flow-rate and the middle flow-rate of fuel for a solenoid pump. CONSTITUTION: In a grain drying machine, drying by burning a burner intermittently by the ON/OFF control of the supply of fuel in a given period and whose flow-rate of fuel supplied for the burner is controlled in at least two stages of a big flow-rate and a middle flow-rate, the amount of one change in ON time of the burner for the big flow rate and the middle flow rate is set so that the amount may be small for the big flow-rate, and big for the middle flow-rate.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、穀物乾燥機のバ−ナ
燃焼制御装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a burner combustion control device for a grain dryer.

【0002】[0002]

【従来技術及び発明が解決しようとする課題】従来、バ
−ナを間歇的に燃焼させて乾燥する形態の穀物乾燥機に
おいて、一定周期内の平均加温量が設定加温量となるよ
うバ−ナのON時間を変更制御するようにしている。そ
して、このときの変更量は、電磁ポンプの大流量.中流
量により区別していないため、設定加温量に対する大流
量時のバ−ナON時間の増え過ぎ、減り過ぎなどによる
ハンチングを招いていた。
2. Description of the Related Art Conventionally, in a grain dryer in which a burner is intermittently burned and dried, an average heating amount within a certain cycle is set to a preset heating amount. -The ON time of the switch is controlled to be changed. The change amount at this time is the large flow rate of the electromagnetic pump. Since no distinction was made according to the medium flow rate, hunting was caused due to excessive increase or decrease of the burner ON time at a large flow rate with respect to the set heating amount.

【0003】本発明は、かかる問題点を解消することを
目的とする。この目的達成のため、次のような技術的手
段を講じた。
An object of the present invention is to eliminate such problems. To achieve this purpose, the following technical measures were taken.

【0004】[0004]

【課題を解決するための手段】すなわち、この発明にか
かる技術的手段は、一定周期内で燃料の供給ON,OF
F制御によりバ−ナを間歇的に燃焼させて乾燥する穀物
乾燥機であって、バ−ナへの燃料供給を少なくとも大流
量と中流量の2段階にて流量制御するものにおいて、大
流量時と中流量時におけるバ−ナON時間の1回あたり
の変更量を、大流量時は小さく中流量時は大きくするよ
う区別して設定してあることを特徴とする。
That is, the technical means according to the present invention is to turn on and off the fuel supply within a fixed cycle.
A grain dryer for intermittently burning and drying a burner by F control, in which the fuel supply to the burner is controlled in at least two stages of a large flow rate and a medium flow rate, at a large flow rate. And the amount of change of the burner ON time per medium flow rate is set so as to be small at a large flow rate and large at a medium flow rate.

【0005】[0005]

【発明の作用、及び効果】穀物乾燥機の貯留タンク内へ
収容された穀粒は、このタンクから乾燥室内へ繰り出し
流下されて循環される。貯留タンク内へ張込みされた張
込穀粒量、穀物種類及び外気温度センサ39で測定され
た外気温度等によってバ−ナ5から発生する乾燥風温度
が設定され、乾燥機が始動して穀粒の乾燥が開始される
と、該バ−ナ5ヘ燃焼用燃料を供給する電磁ポンプ20
等が所定時間間隔でON−OFF制御され、バ−ナはO
N時間の間は燃焼して熱風が発生し、OFF時間の間は
燃焼休止して熱風は発生しない。このようにしてバ−ナ
は間歇燃焼制御される。
The operation and effect of the invention The grains contained in the storage tank of the grain dryer are fed out from this tank into the drying chamber and circulated. The drying air temperature generated from the burner 5 is set according to the amount of grain infused into the storage tank, the type of grain, the outside air temperature measured by the outside air temperature sensor 39, etc., and the dryer starts and the grains are started. When the drying of the grains is started, the electromagnetic pump 20 which supplies the burning fuel to the burner 5
ON / OFF control is performed at predetermined time intervals, and the burner is turned off.
During the N hours, combustion is performed to generate hot air, and during the OFF time, combustion is stopped and hot air is not generated. In this way, the burner is controlled for intermittent combustion.

【0006】この乾燥作業中は、前回燃焼時の平均加温
量Ksと設定加温量Kとが比較され、その差が一定値と
等しいか、又は一定値より小なる時はON時間は変更せ
ず、今回燃焼時のON時間が決定される。前記の比較差
が一定値より大なる時には、バ−ナへの燃料供給が大流
量か、中流量かを判別し、この燃料供給が大流量の場合
にはON時間の一回あたりの変更量を小さくして制御さ
れ、中流量の場合にはON時間の一回あたりの変更量を
大きくして制御される。このようにして一定周期内の平
均加温量Ksが設定加温量Kとなるように、バ−ナのO
N時間変更制御が行われる。
During this drying operation, the average heating amount Ks at the previous combustion is compared with the set heating amount K, and when the difference is equal to or less than the constant value, the ON time is changed. Without this, the ON time at the time of this combustion is determined. When the comparison difference is larger than a certain value, it is determined whether the fuel supply to the burner is a large flow rate or a medium flow rate, and when this fuel supply is a large flow rate, the change amount per ON time is changed. Is controlled to be small, and in the case of a medium flow rate, the amount of change per ON time is controlled to be large. In this way, the burner O is adjusted so that the average heating amount Ks within the constant period becomes the set heating amount K.
N time change control is performed.

【0007】要するに、本発明によれば、大流量時の一
回あたりの変更量を小さく、中流量時の一回あたりの変
更量を大きくすることにより、1回あたりの変更量に対
する加温量変化をほぼ等しくして、設定加温量に対する
大流量時のバ−ナON時間のハンチングをなくすことが
できる。
In short, according to the present invention, the amount of change per change at the time of a large flow rate is small and the amount of change per time at the time of a medium flow rate is large, so that the heating amount with respect to the amount of change per time is increased. By making the changes almost equal, it is possible to eliminate hunting of the burner ON time at a large flow rate with respect to the set heating amount.

【0008】[0008]

【実施例】この発明の一実施例を図面に基づいて説明す
る。1は乾燥機であって、上部から貯留タンク2、乾燥
室3、集穀室4を縦設し、このうち乾燥室3は、バ−ナ
5を有する熱風室6と吸引フアン7を有する排風室8と
の間に穀物流下通路9,9を形成してなり、各流下通路
9,9の下部に設ける繰出バルブ10,10の一定回転
により所定量毎に流下する穀物に熱風を浴びせて乾燥す
るよう構成している。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to the drawings. A dryer 1 has a storage tank 2, a drying chamber 3 and a grain collecting chamber 4 which are vertically installed from the upper part. Of these, the drying chamber 3 has a hot air chamber 6 having a burner 5 and an exhaust fan 7 having a suction fan 7. Grain downflow passages 9 and 9 are formed between the airflow chambers 8 and hot air is blown onto the grains flowing down by a predetermined amount by the constant rotation of the feeding valves 10 and 10 provided at the lower portions of the downflow passages 9 and 9. It is configured to dry.

【0009】昇穀機11は、内部にバケットコンベア1
2を張設してあり、集穀室4の下部に横設する集穀移送
螺旋13により一側に移送された乾燥穀物を掬い上げて
上部に揚上搬送できる構成としている。この昇穀機11
の上部から投出される穀物は、投出樋14を介して移送
螺旋15を架設する移送樋16の始端部に案内落下され
る。移送螺旋15により移送される穀物は貯留タンク2
の中央上部に配設した拡散盤17に案内され、貯留タン
ク2内に拡散落下されるように構成している。
The grain elevator 11 has a bucket conveyor 1 inside.
2 is stretched so that the dry grain transferred to one side can be picked up and lifted and conveyed to the upper part by the grain collecting transfer spiral 13 provided laterally at the lower part of the grain collecting chamber 4. This sublimation machine 11
Grains thrown out from the upper part of the above are guided and dropped through a throwing gutter 14 to a starting end portion of a transfer gutter 16 which is provided with a transfer spiral 15. The grain transferred by the transfer spiral 15 is stored in the storage tank 2.
It is configured so that it is guided by a diffusion plate 17 disposed in the upper center part of and is dropped into the storage tank 2.

【0010】水分センサ18は、昇穀機11の中間部に
設け、操作装置からの電気的測定信号の発信により、水
分モ−タ19が回転してこの水分センサ−の各部が回転
駆動され、バケットコンベア12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しながら、この粉
砕穀粒の水分を検出するようにしている。バ−ナ5は、
電磁ポンプ20の駆動によって燃料タンク21内の灯油
が供給され、イグナイタ22の通電による点火で着火燃
焼される構成である。電磁ポンプ20による燃料供給量
は予め設定する設定温度との関係で、大流量(大供給、
即ち高燃焼)と中流量(小供給、即ち低燃焼)の2段に
切替できる構成である。送風フアン23は、送風モ−タ
24で変速回転駆動され、供給燃料に見合った燃焼用空
気をバ−ナ5へ送風している。
The moisture sensor 18 is provided at an intermediate portion of the grain raising machine 11, and the moisture motor 19 is rotated by the transmission of an electric measurement signal from the operating device, whereby each portion of the moisture sensor is rotationally driven. The bucket conveyor 12 receives the grains that are falling during conveyance to the upper portion, and while crushing the grains under pressure, the moisture content of the crushed grains is detected. Burner 5
Kerosene in the fuel tank 21 is supplied by driving the electromagnetic pump 20 and is ignited and burned by ignition by energization of the igniter 22. The fuel supply amount by the electromagnetic pump 20 has a large flow rate (large supply,
That is, it is a configuration that can be switched between two stages of high combustion) and medium flow rate (small supply, that is, low combustion). The blower fan 23 is rotationally driven at a variable speed by the blower motor 24 to blow the combustion air commensurate with the supplied fuel to the burner 5.

【0011】電磁ポンプ20、電磁ポンプの燃料バルブ
及び送風モ−タ24等の燃焼系は設定記憶させた所定時
間間隔でON−OFF制御され、このON−OFF制御
により、バ−ナ5は燃焼及び燃焼休止して、このバ−ナ
5から熱風が発生したり、又休止したりする構成であ
る。また、バ−ナ5はこのような間歇燃焼形態とする
が、熱風温度センサ−25から検出される間歇燃焼周期
期間の平均熱風温度と当該設定温度とを比較しその差に
より電磁ポンプ20のON時間を変更制御し、熱風温度
が設定温度の所定範囲内になるよう制御される。なお、
図5の間歇燃焼タイムチャ−トにおいて、T:初期燃焼
時間、t:間歇燃焼周期、ton:間歇燃焼ON時間、
toff:間歇燃焼OFF時間を示し、初期燃焼時間T
は一定時間を連続燃焼とし、上記間歇燃焼の周期は一定
t(例えばt=150秒)とし、ON時間を変更できる
構成である。更に電磁ポンプ20ヘの大流量又は中流量
供給指令信号は送風モ−タ24にも出力され、予め設定
した大小2段の回転数を選択すべく出力される。すなわ
ち、予め設定された設定温度と外気温度との関係で、必
要加温度が決定されるが、この加温量が大きいときは燃
料供給を大流量にし、逆に小さいときは燃料供給を中流
量とすべく電磁ポンプ20に指令出力される。更に、微
妙な温度調節は各燃料供給状態下での燃焼周期tに対す
るON時間の長短に委ねられる。
The combustion system, such as the electromagnetic pump 20, the fuel valve of the electromagnetic pump, and the blower motor 24, is ON / OFF controlled at predetermined time intervals stored and stored, and the burner 5 burns by this ON / OFF control. The burner 5 is stopped and hot air is generated from the burner 5 or stopped. Although the burner 5 has such an intermittent combustion mode, the average hot air temperature during the intermittent combustion cycle period detected by the hot air temperature sensor 25 is compared with the set temperature, and the electromagnetic pump 20 is turned on by the difference. The time is changed and controlled so that the hot air temperature is within a predetermined range of the set temperature. In addition,
In the intermittent combustion time chart of FIG. 5, T: initial combustion time, t: intermittent combustion cycle, ton: intermittent combustion ON time,
toff: Intermittent combustion OFF time, initial combustion time T
Is a continuous combustion for a fixed time, the cycle of the intermittent combustion is constant t (for example, t = 150 seconds), and the ON time can be changed. Further, a high flow rate or medium flow rate supply command signal to the electromagnetic pump 20 is also output to the blower motor 24, and is output to select a preset number of rotations of large and small stages. That is, the required heating temperature is determined by the relationship between the preset temperature and the outside air temperature. When the heating amount is large, the fuel supply is set to a large flow rate, and conversely, when the heating amount is small, the fuel supply is set to the medium flow rate. Therefore, a command is output to the electromagnetic pump 20. Further, delicate temperature control depends on the length of the ON time with respect to the combustion cycle t under each fuel supply state.

【0012】図3は制御ブロック図であり、機体内に設
けるコントロ−ラ26の制御部(CPU)27には、コ
ントロ−ラパネル28に配設した張込.乾燥.排出.停
止の各モ−ドスイッチ29,30,31,32、穀物種
類,張込量,仕上水分の各設定スイッチ33,34,3
5、乾燥時間設定のための増・減スイッチ36,37等
の入力信号のほか、前記水分センサ−18,フレ−ムロ
ッド38,熱風温度センサ−25,外気温度センサ39
等の各種検出信号を入力する。
FIG. 3 is a control block diagram, in which a controller (CPU) 27 of a controller 26 provided inside the body is provided with a stake-in device provided on a controller panel 28. Dry. Discharge. Stop mode switches 29, 30, 31, 32, setting switches 33, 34, 3 for grain type, amount of swelling, and finished moisture
5. In addition to the input signals of the increase / decrease switches 36 and 37 for setting the drying time, the moisture sensor-18, the frame rod 38, the hot air temperature sensor-25, and the outside air temperature sensor 39
Input various detection signals such as.

【0013】一方出力信号としては前記昇穀機を駆動す
る昇穀機モ−タ40,繰出バルブ用モ−タ41等の循環
系駆動モ−タ駆動信号、バ−ナ5駆動信号等がある。な
お、バ−ナ駆動信号は、電磁ポンプ20のON−OFF
信号、及び燃料大小供給信号、バ−ナ送風モ−タ24の
回転数指令信号、イグナイタ22通電信号等がある。上
記の制御部は、予め設定記憶される設定温度と熱風温度
センサ25で検出される平均熱風温度とを比較し、その
差を小にすべく周期的にONされる電磁ポンプ20のO
N時間を長短に変更制御する。
On the other hand, as the output signals, there are a drive signal for driving the circulating system such as the motor 40 for driving the grain raising machine and the motor 41 for the feeding valve, a driving signal for the burner 5 and the like. . The burner drive signal is ON-OFF of the electromagnetic pump 20.
There are a signal, a fuel amount supply signal, a rotation speed command signal of the burner blower motor 24, an igniter 22 energization signal, and the like. The above control unit compares the set temperature stored in advance with the average hot air temperature detected by the hot air temperature sensor 25, and periodically turns on the O of the electromagnetic pump 20 to reduce the difference.
The N time is controlled to be changed to long or short.

【0014】穀物乾燥機の貯留タンク内へ収容された穀
粒は、このタンクから乾燥室内へ繰り出し流下されて循
環される。貯留タンク内へ張込みされた張込穀粒量、穀
物種類及び外気温度センサ39で測定された外気温度等
によってバ−ナ5から発生する熱風温度が設定され、乾
燥機が始動して穀粒の乾燥が開始されると、該バ−ナ5
ヘ燃焼用燃料を供給する電磁ポンプ20等が所定時間間
隔でON−OFF制御され、バ−ナはON時間の間は燃
焼して熱風が発生し、OFF時間の間は燃焼休止して熱
風は発生しない。このようにしてバ−ナは間欠燃焼制御
される。
The grains stored in the storage tank of the grain dryer are fed out from this tank into the drying chamber and circulated. The hot air temperature generated from the burner 5 is set according to the amount of grain inflated into the storage tank, the type of grain, the outside air temperature measured by the outside air temperature sensor 39, etc., and the dryer starts and the grains are started. When the drying of the burner is started, the burner 5
(F) The electromagnetic pump 20 for supplying the fuel for combustion is ON-OFF controlled at predetermined time intervals, the burner burns during the ON time to generate hot air, and the burner pauses during the OFF time to stop the hot air. Does not occur. In this way, the burner is subjected to intermittent combustion control.

【0015】この乾燥作業中は、電磁ポンプ等のON−
OFFの所定時間内で、所定時間毎の外気温度センサ3
9及び熱風温度センサ25が測定する外気温度と乾燥風
温度とによって加温量が算出され、各加温量の平均値に
よりバ−ナON−OFFの一周期中又はN周期中の平均
加温量Ksが算出され、この算出した平均加温量Ksと
設定乾燥風温度と測定された外気温度とから算出した設
定加温量Kとが比較され、相違していると設定加温量と
同じになるように電磁ポンプ20等のON−OFF時間
が増、又は減制御されて、平均加温量Ksと設定加温量
Kとを同じにして穀物は乾燥される。
During this drying operation, the electromagnetic pump etc. is turned on.
Outside air temperature sensor 3 for every predetermined time within a predetermined time of OFF
9 and the temperature of dry air measured by the hot air temperature sensor 25 and the temperature of the dry air, the heating amount is calculated, and the average value of each heating amount is the average heating during one cycle of burner ON-OFF or during N cycles. The amount Ks is calculated, and the calculated average heating amount Ks and the set heating amount K calculated from the set drying air temperature and the measured outside air temperature are compared, and if they are different, the same as the set heating amount. The ON-OFF time of the electromagnetic pump 20 or the like is controlled to increase or decrease so that the average heating amount Ks and the set heating amount K are the same, and the grain is dried.

【0016】図3に示す構成のコントロ−ラにおいて、
図5の間歇燃焼タイムチャ−トに示すような間歇燃焼を
行い、一定周期内の平均加温量が設定加温量となるよう
にバ−ナ5のON時間を変更する。このときの1回あた
りの変更量は図6に示すフロ−チャ−トのように電磁ポ
ンプ20の大流量,中流量により区別する。つまり、図
6:フロ−チャ−トにおいて、前回燃焼時の平均加温量
Ksと設定加温量Kとが比較され、その差が一定値と等
しいか、又は一定値より小なる時はON時間は変更せ
ず、今回燃焼時のON時間が決定される。前記の比較差
が一定値より大なる時には、バ−ナへの燃料供給が大流
量か、中流量かを判別し、この燃料供給が大流量の場合
にはON時間の一回あたりの変更量を小さくして制御さ
れ、中流量の場合にはON時間の一回あたりの変更量を
大きくして制御される。このようにして一定周期内の平
均加温量Ksが設定加温量Kとなるように、バ−ナのO
N時間変更制御が行われるものである。
In the controller having the structure shown in FIG.
The intermittent combustion as shown in the intermittent combustion time chart of FIG. 5 is performed, and the ON time of the burner 5 is changed so that the average heating amount within a fixed cycle becomes the set heating amount. The change amount per time at this time is distinguished by the large flow rate and the medium flow rate of the electromagnetic pump 20 as in the flow chart shown in FIG. That is, in FIG. 6: in the flow chart, the average heating amount Ks at the previous combustion is compared with the set heating amount K, and when the difference is equal to or less than the constant value, it is turned on. The ON time at this combustion is determined without changing the time. When the comparison difference is larger than a certain value, it is determined whether the fuel supply to the burner is a large flow rate or a medium flow rate, and when this fuel supply is a large flow rate, the change amount per ON time is changed. Is controlled to be small, and in the case of a medium flow rate, the amount of change per ON time is controlled to be large. In this way, the burner O is adjusted so that the average heating amount Ks within the constant period becomes the set heating amount K.
N time change control is performed.

【0017】図7に示す実施例は、一定周期にてバ−ナ
のON−OFFを行う間歇燃焼において、バ−ナON時
間の一回あたりの変更量は、設定加温量との差により算
出して変更する構成としている。即ち、図3に示す構成
のコントロ−ラにおいて、図5の間歇燃焼タイムチャ−
トに示すような間歇燃焼を行い、一定周期内の平均加温
量が設定加温量となるようにバ−ナ5のON時間を変更
する。そして、このときの1回あたりの変更量は図7に
示すフロ−チャ−トのように双方の差によって、△to
n2:大,△ton1:小と区別する。従って、設定加
温量と検出した平均加温量の差に応じてバ−ナON時間
の1回あたりの変更量を変更することにより、早く設定
加温量に到達させることができる。
In the embodiment shown in FIG. 7, in the intermittent combustion in which the burner is turned on and off in a constant cycle, the change amount of the burner ON time per change depends on the difference from the set heating amount. It is configured to calculate and change. That is, in the controller having the configuration shown in FIG. 3, the intermittent combustion timechart shown in FIG.
The intermittent combustion is performed as shown in FIG. 9C, and the ON time of the burner 5 is changed so that the average heating amount within a certain cycle becomes the set heating amount. Then, the change amount per time at this time is Δto according to the difference between the two as in the flowchart shown in FIG.
n2: large, Δton1: small. Therefore, the set heating amount can be quickly reached by changing the change amount of the burner ON time per time according to the difference between the set heating amount and the detected average heating amount.

【0018】図8に示す実施例は、一定周期にてバ−ナ
のON−OFFを行う間歇燃焼において、初期燃焼時
間:T終了後の間歇燃焼スタ−ト時のバ−ナON時間
は、設定加温量により複数のON時間に区別する構成と
している。即ち、図3に示す構成のコントロ−ラにおい
て、一定時間の初期燃焼終了後に図5のような間歇燃焼
タイムチャ−トにて間歇燃焼を行うとき、間歇燃焼1回
目(図5)のバ−ナON時間(ton)を図8のフロ
−チャ−トにて決定する構成である。従って、設定加温
量に応じたON時間とすることにより、早く設定加温量
に到達させることができ、安定した乾燥ができる。
In the embodiment shown in FIG. 8, in the intermittent combustion in which the burner is turned on and off in a constant cycle, the initial combustion time: the burner ON time at the intermittent combustion start after the end of T is A plurality of ON times are distinguished according to the set heating amount. That is, in the controller having the configuration shown in FIG. 3, when the intermittent combustion is performed in the intermittent combustion time chart as shown in FIG. 5 after the initial combustion for a certain period of time, the burner of the first intermittent combustion (FIG. 5) is performed. The ON time (ton) is determined by the flow chart in FIG. Therefore, by setting the ON time according to the set heating amount, the set heating amount can be reached quickly, and stable drying can be performed.

【0019】図9に示す実施例は、一定周期にてバ−ナ
のON−OFFを行う間歇燃焼で、設定加温量に応じて
燃料を大流量と中流量の2段階で燃焼制御を行うとき、
中流量による初期燃焼終了後の間歇燃焼スタ−ト時は設
定加温量が一定値より大きいときは大流量側で、また、
一定値以下のときは中流量側とする構成としている。即
ち、図3に示す構成のコントロ−ラにおいて、図5のよ
うな間歇燃焼タイムチャ−トにて間歇燃焼を行うとき、
初期燃焼終了時に穀物種類設定と温度調節設定とにより
設定加温量を求め(乾燥開始時に行ってもよい)、その
設定加温量により、大流量でスタ−トするか、中流量で
スタ−トするかを決定する構成である。従って、設定加
温量に応じた流量で間歇燃焼を開始することにより、早
く設定加温量に到達させることができ、安定した乾燥が
できる。
The embodiment shown in FIG. 9 is an intermittent combustion in which the burner is turned on and off in a constant cycle, and the combustion control of the fuel is performed in two stages of a large flow rate and a medium flow rate according to the set heating amount. When
At the time of intermittent combustion start after the end of initial combustion with medium flow rate, when the set heating amount is larger than a certain value, it is on the large flow rate side,
When the value is below a certain value, it is set to the medium flow rate side. That is, in the controller having the configuration shown in FIG. 3, when performing the intermittent combustion in the intermittent combustion time chart as shown in FIG.
At the end of the initial combustion, the set heating amount is obtained from the grain type setting and the temperature adjustment setting (may be performed at the start of drying), and depending on the set heating amount, start at a large flow rate or start at a medium flow rate. This is a configuration for determining whether to execute. Therefore, by starting intermittent combustion at a flow rate according to the set heating amount, the set heating amount can be reached quickly, and stable drying can be performed.

【0020】図10に示す実施例は、一定周期にてバ−
ナのON−OFF制御を行う間歇燃焼において、初期燃
焼終了後のスタ−ト時のバ−ナON時間は、運転時に設
定された設定加温量に相当するON時間とし、1回の間
歇燃焼で設定加温量とならない場合でも、一定回数はそ
のON時間を保持する構成としている。即ち、図3に示
す構成のコントロ−ラにおいて、図5のような間歇燃焼
タイムチャ−トにて間歇燃焼を行うとき、1回目の間歇
燃焼のON時間については、図10のフロ−チャ−ト
(A)のように設定加温量Kから算出したON時間と
し、N回まではこのON時間とした後に、算出された平
均加温量Ksと設定加温量Kとの比較によりON時間を
変更する構成である。
The embodiment shown in FIG. 10 has a constant cycle of bursting.
In the intermittent combustion in which the ON / OFF control of the engine is performed, the burner ON time at the start after the completion of the initial combustion is set to the ON time corresponding to the set heating amount set during the operation, and the intermittent combustion is performed once. Even if the set heating amount is not reached, the ON time is held for a certain number of times. That is, in the controller having the configuration shown in FIG. 3, when the intermittent combustion is performed at the intermittent combustion time chart as shown in FIG. 5, the ON time of the first intermittent combustion is shown in the flowchart of FIG. The ON time calculated from the set heating amount K as shown in (A) is set to this ON time up to N times, and then the ON time is calculated by comparing the calculated average heating amount Ks with the set heating amount K. This is the configuration to be changed.

【0021】従って、設定加温量に対応するON時間で
間歇燃焼をスタ−トさせることにより、早く設定加温量
に到達させることができ、また、そのON時間を一定時
間保持することにより、間欠燃焼中の温度検出における
初期燃焼時の熱風温度による影響(初期燃焼時の熱風に
より設定加温量に対応するON時間に成らない恐れがあ
る。)を除くことができる。
Therefore, by starting the intermittent combustion at the ON time corresponding to the set heating amount, the set heating amount can be quickly reached, and by keeping the ON time for a certain period of time, It is possible to exclude the influence of the hot air temperature at the initial combustion in the temperature detection during the intermittent combustion (the ON time corresponding to the set heating amount may not be reached due to the hot air at the initial combustion).

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

【図1】穀物乾燥機の一部破断せる全体側面図[Fig.1] Side view of grain dryer

【図2】同上要部の縦断正面図FIG. 2 is a vertical sectional front view of a main part of the same.

【図3】制御ブロック図FIG. 3 is a control block diagram.

【図4】コントロ−ラパネル[Fig. 4] Controller panel

【図5】間歇燃焼タイムチャ−ト[Fig. 5] Intermittent combustion time chart

【図6】フロ−チャ−トFIG. 6 Flow chart

【図7】フロ−チャ−ト[Fig. 7] Flow chart

【図8】フロ−チャ−トFIG. 8: Flow chart

【図9】フロ−チャ−トFIG. 9: Flow chart

【図10】フロ−チャ−トFIG. 10: Flow chart

【符号の説明】[Explanation of symbols]

1 乾燥機 2 貯留タンク 3 乾燥室 4 集穀室 5 バ−ナ 6 熱風室 7 吸引フアン 8 排風室 9 穀物流下通路 10 繰出バルブ 11 昇穀機 12 バケットコンベア 13 集穀移送螺旋 14 投出樋 15 移送螺旋 16 移送樋 17 拡散盤 18 水分センサ− 19 水分モ−タ 20 電磁ポンプ 21 燃料タンク 22 イグナイタ 23 送風フアン 24 送風モ−タ 25 熱風温度センサ 26 コントロ−ラ 27 制御部 28 コントロ−ラパネ
ル 29 張込スイッチ 30 乾燥スイッチ 31 排出スイッチ 32 停止スイッチ 33 穀物種類設定スイッチ 34 張込量設定スイッ
チ 35 停止水分設定スイッチ 36,37 増・減スイ
ッチ 38 フレ−ムロッド 39 外気温センサ 40 昇穀機モ−タ 41 繰出バルブ用モ−
DESCRIPTION OF SYMBOLS 1 Dryer 2 Storage tank 3 Drying room 4 Grain collecting room 5 Burner 6 Hot air chamber 7 Suction fan 8 Exhaust air chamber 9 Grain flow path 10 Feeding valve 11 Grain raising machine 12 Bucket conveyor 13 Grain transfer spiral 14 Throwing gutter 15 Transfer Spiral 16 Transfer Gutter 17 Diffusion Board 18 Moisture Sensor-19 Moisture Motor 20 Electromagnetic Pump 21 Fuel Tank 22 Igniter 23 Blower Fan 24 Blower Motor 25 Hot Air Temperature Sensor 26 Controller 27 Controller 28 Controller Panel 29 Suction switch 30 Drying switch 31 Discharge switch 32 Stop switch 33 Grain type setting switch 34 Strain amount setting switch 35 Stop moisture setting switch 36, 37 Increase / decrease switch 38 Frame rod 39 Outside air temperature sensor 40 Grain raising machine motor 41 Feed valve mode
Ta

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 一定周期内で燃料の供給ON,OFF制
御によりバ−ナを間歇的に燃焼させて乾燥する穀物乾燥
機であって、バ−ナへの燃料供給を少なくとも大流量と
中流量の2段階にて流量制御するものにおいて、大流量
時と中流量時におけるバ−ナON時間の1回あたりの変
更量を、大流量時は小さく中流量時は大きくするよう区
別して設定してあることを特徴とする穀物乾燥機のバ−
ナ燃焼制御装置。
1. A grain dryer for intermittently burning and drying a burner by controlling ON / OFF of fuel supply within a fixed cycle, wherein the fuel supply to the burner is at least large and medium flow rates. In the two-stage flow rate control, the change amount of the burner ON time per large flow rate and medium flow rate is set separately so that it is small at large flow rate and large at medium flow rate. Bar of grain dryer characterized by being
Combustion control device.
JP31958194A 1994-12-22 1994-12-22 Burner combustion controller of grain drier Pending JPH08178529A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31958194A JPH08178529A (en) 1994-12-22 1994-12-22 Burner combustion controller of grain drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31958194A JPH08178529A (en) 1994-12-22 1994-12-22 Burner combustion controller of grain drier

Publications (1)

Publication Number Publication Date
JPH08178529A true JPH08178529A (en) 1996-07-12

Family

ID=18111870

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31958194A Pending JPH08178529A (en) 1994-12-22 1994-12-22 Burner combustion controller of grain drier

Country Status (1)

Country Link
JP (1) JPH08178529A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015124896A (en) * 2013-12-25 2015-07-06 井関農機株式会社 Agricultural product dryer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015124896A (en) * 2013-12-25 2015-07-06 井関農機株式会社 Agricultural product dryer

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