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JPS6235032B2 - - Google Patents
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JPS6235032B2 - - Google Patents

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Publication number
JPS6235032B2
JPS6235032B2 JP54144151A JP14415179A JPS6235032B2 JP S6235032 B2 JPS6235032 B2 JP S6235032B2 JP 54144151 A JP54144151 A JP 54144151A JP 14415179 A JP14415179 A JP 14415179A JP S6235032 B2 JPS6235032 B2 JP S6235032B2
Authority
JP
Japan
Prior art keywords
flow rate
limit value
humidity
fuel flow
burner
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.)
Expired
Application number
JP54144151A
Other languages
Japanese (ja)
Other versions
JPS5668782A (en
Inventor
Juji Kanefuji
Sadakazu Fujioka
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 Agricultural Machinery Mfg Co Ltd
Original Assignee
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 Agricultural Machinery Mfg Co Ltd filed Critical Iseki Agricultural Machinery Mfg Co Ltd
Priority to JP14415179A priority Critical patent/JPS5668782A/en
Publication of JPS5668782A publication Critical patent/JPS5668782A/en
Publication of JPS6235032B2 publication Critical patent/JPS6235032B2/ja
Granted legal-status Critical Current

Links

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  • Regulation And Control Of Combustion (AREA)
  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は籾や麦などの穀粒を乾燥する場合にお
いて乾燥熱風を供給するバーナの燃焼制御方法に
関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a combustion control method for a burner that supplies drying hot air when drying grains such as paddy and wheat.

(従来の技術と発明が解決しようとする問題点) バーナの熱風で穀粒を乾燥する場合、熱風の温
度は同じでも大気の湿度が低く乾いているほうが
湿つているときよりも乾燥時間が早い。しかし乾
燥時間が早すぎると穀粒に胴割れを生じ、逆に遅
すぎると乾燥機の処理能力が低下することにな
る。
(Problems to be solved by the prior art and the invention) When drying grains using hot air from a burner, the drying time is faster when the air is low in humidity and dry than when it is humid, even though the temperature of the hot air is the same. . However, if the drying time is too fast, the grains will crack, and if the drying time is too slow, the throughput of the dryer will be reduced.

ところが従来は大気の湿度に関係なくバーナの
燃焼制御をするから、適切な乾燥ができない欠点
があつた。
However, in the past, the combustion of the burner was controlled regardless of the humidity of the atmosphere, which resulted in the drawback that proper drying could not be achieved.

本発明は大気の湿度に応じてバーナの熱風温度
を制御し、いつも同じ最適な速さで乾燥すること
を目的とする。
The object of the present invention is to control the temperature of the hot air from the burner according to the humidity of the atmosphere, and to always dry at the same optimum speed.

(問題点を解決するための手段) この目的を達成するため、本発明は、穀粒乾燥
機のバーナに備える燃料流量調節手段を計算機の
出力側に、またその入力側には湿度センサをそれ
ぞれ接続し、大気の湿度が上限値と下限値の中間
の場合には前記燃料流量調節手段の流量を標準値
に設定し、湿度が上限値を上回る場合には前記燃
料流量調節手段の流量を標準値よりも増量し、下
限値を下回る場合には前記燃料流量調節手段の流
量を標準値よりも減量することを特徴とする。
(Means for Solving the Problems) In order to achieve this object, the present invention provides a fuel flow rate regulating means for the burner of a grain dryer on the output side of the computer, and a humidity sensor on the input side of the computer. When the atmospheric humidity is between the upper limit value and the lower limit value, the flow rate of the fuel flow rate adjusting means is set to the standard value, and when the humidity exceeds the upper limit value, the flow rate of the fuel flow rate adjusting means is set to the standard value. The fuel flow rate adjustment means is characterized in that the flow rate of the fuel flow rate adjusting means is decreased from the standard value when the fuel flow rate is increased from the standard value and is below the lower limit value.

(実施例) 本発明の実施例を図面に示して説明すると、K
は穀粒乾燥機でその中央の熱風室k1の左右に穀
粒が流下する乾燥室k2を形成し、その外側に排
風室k3を形成する。乾燥室k2と熱風室k1お
よび排風室k3との境界は多孔板で仕切る。Bは
熱風室k1に連結したバーナで、その熱風を、排
風室k3に接続した吸引フアンFにより吸引す
る。熱風は熱風室k1から乾燥室k2を横断し穀
粒を乾燥したのち排風室から排出する。
(Example) An example of the present invention will be explained with reference to the drawings.
is a grain dryer, and a drying chamber k2 is formed on the left and right sides of a hot air chamber k1 in the center, into which the grains flow down, and an air exhaust chamber k3 is formed outside of the drying chamber k2. The boundaries between the drying chamber k2, the hot air chamber k1, and the exhaust chamber k3 are separated by a perforated plate. B is a burner connected to the hot air chamber k1, and the hot air is sucked by a suction fan F connected to the exhaust chamber k3. The hot air traverses the drying chamber k2 from the hot air chamber k1, dries the grains, and then is discharged from the exhaust chamber.

燃料タンクNに連通するポンプPを、電磁弁V
を介してバーナBに配管する。Mは吸引フアンF
や乾燥機Kのエレベータ(図示しない)などを駆
動するモータを示す。
A pump P communicating with a fuel tank N is connected to a solenoid valve V.
Connect to burner B via the pipe. M is suction fan F
The motor for driving the elevator (not shown) of the dryer K and the like is shown.

そして乾燥機Kの外壁に湿度センサHを取付
け、これを計算機Cの入力側に接続し、その出力
側には電磁弁Vを接続する。センサHには電気抵
抗式、乾湿球電気式等の公知の電気的な工業計器
を使用する。なおセンサHと弁Vの入出力機器と
計算機Cの間には図示しないA―D変換器を介在
する。
A humidity sensor H is attached to the outer wall of the dryer K, connected to the input side of the computer C, and a solenoid valve V is connected to the output side thereof. As the sensor H, a known electrical industrial instrument such as an electric resistance type or a dry/wet bulb electric type is used. Note that an AD converter (not shown) is interposed between the input/output devices of the sensor H and the valve V and the computer C.

しかして湿度センサHの出力電圧が湿度の上限
値fa(たとえば85%)に相当する電圧値を上回る
かどうかを計算機Cにより判別し、上回る場合に
は電磁弁Vに信号を送り、弁Vをあらかじめ決め
られた標準開度よりも開き燃料の送量を増し、バ
ーナBの燃焼温度を標準値より2度高くする。
Then, the computer C determines whether the output voltage of the humidity sensor H exceeds a voltage value corresponding to the upper limit value fa (for example, 85%) of humidity. It opens more than the predetermined standard opening degree, increases the amount of fuel sent, and makes the combustion temperature of burner B 2 degrees higher than the standard value.

また湿度センサHの出力が上限値fa未満の場合
には、下限値fb(たとえば60%)より大きいかど
うか同様に判別し、その結果、fbより大きければ
すなわち湿度が上限値faと下限値fbとの中間の場
合には、弁Vをあらかじめ決められた標準開度そ
のままにし、燃焼温度を標準値に設定する。
Furthermore, when the output of the humidity sensor H is less than the upper limit value fa, it is determined in the same way whether it is larger than the lower limit value fb (for example, 60%), and as a result, if it is larger than fb, that is, the humidity In the case between 2 and 3, the valve V is left at the predetermined standard opening and the combustion temperature is set to the standard value.

さらに湿度センサHの出力が下限値fbより小さ
ければ弁Vを標準開度より閉めて燃料の送量を減
らし、燃焼温度を標準値より2度低くする。
Furthermore, if the output of the humidity sensor H is smaller than the lower limit value fb, the valve V is closed from the standard opening degree to reduce the amount of fuel fed and the combustion temperature to be lowered by 2 degrees below the standard value.

なお燃焼温度を調節するのに、電磁弁Vの代り
に流量可変型のポンプを燃料流量調節手段に用い
てバーナBへの燃料流量を変更しても同効であ
る。
Incidentally, in order to adjust the combustion temperature, the same effect can be obtained by using a variable flow rate pump as the fuel flow rate adjusting means instead of the solenoid valve V to change the fuel flow rate to the burner B.

(発明の効果) このように本発明においては、大気の湿度に応
じて燃料流量調節手段により供給燃料を調節し、
大気の湿度が上限値faと下限値fbの中間の場合に
はバーナの燃焼温度を所定の標準値にし、また上
限値faを上回る場合には標準値よりも数度高く
し、さらに下限値fbを下回る場合には数度低くす
るので、所定の含水率までに穀粒を仕上げるまで
の所要時間が大気の湿度に左右されることなくい
つもほぼ一定で、乾燥機Kの処理能力いつぱいに
効率よくしかも穀粒に胴われを生ずるおそれなく
最適の早さで乾燥できるという効果を生ずる。
(Effects of the Invention) As described above, in the present invention, the supplied fuel is adjusted by the fuel flow rate adjustment means according to the humidity of the atmosphere,
When the atmospheric humidity is between the upper limit value fa and the lower limit value fb, the combustion temperature of the burner is set to a predetermined standard value, and when it exceeds the upper limit value fa, it is set several degrees higher than the standard value, and then set to the lower limit value fb. If the moisture content is lower than 100%, the temperature is lowered by several degrees, so the time required to finish the grains to the specified moisture content remains almost constant regardless of atmospheric humidity, and the dryer K's processing capacity is maximized efficiently. Moreover, the effect is that the grains can be dried at an optimum speed without the risk of causing shelling.

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

第1図は本発明を実施した穀粒乾燥機の系統
図、第2図はそのフローチヤートである。 Kは穀粒乾燥機、Bはバーナ、Vは電磁弁、C
は計算機、Hは湿度センサ。
FIG. 1 is a system diagram of a grain dryer embodying the present invention, and FIG. 2 is a flowchart thereof. K is the grain dryer, B is the burner, V is the solenoid valve, C
is a calculator and H is a humidity sensor.

Claims (1)

【特許請求の範囲】[Claims] 1 穀粒乾燥機KのバーナBに備える燃料流量調
節手段を計算機Cの出力側に、またその入力側に
は湿度センサHをそれぞれ接続し、大気の湿度が
上限値faと下限値fbの中間の場合には前記燃料流
量調節手段の流量を標準値に設定し、湿度が上限
値faを上回る場合には前記燃料流量調節手段の流
量を標準値よりも増量し、下限値fbを下回る場合
には前記燃料流量調節手段の流量を標準値よりも
減量することを特徴とする穀粒乾燥機におけるバ
ーナの燃焼制御方法。
1. A fuel flow rate adjustment means provided in burner B of grain dryer K is connected to the output side of computer C, and a humidity sensor H is connected to its input side, so that the atmospheric humidity is between the upper limit value fa and the lower limit value fb. In this case, the flow rate of the fuel flow rate adjusting means is set to the standard value, and when the humidity exceeds the upper limit value fa, the flow rate of the fuel flow rate adjusting means is increased from the standard value, and when the humidity is below the lower limit value fb, the flow rate of the fuel flow rate adjusting means is set to the standard value. A method for controlling combustion of a burner in a grain dryer, characterized in that the flow rate of the fuel flow rate adjusting means is reduced from a standard value.
JP14415179A 1979-11-06 1979-11-06 Burner burning control method for grain dryer Granted JPS5668782A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14415179A JPS5668782A (en) 1979-11-06 1979-11-06 Burner burning control method for grain dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14415179A JPS5668782A (en) 1979-11-06 1979-11-06 Burner burning control method for grain dryer

Publications (2)

Publication Number Publication Date
JPS5668782A JPS5668782A (en) 1981-06-09
JPS6235032B2 true JPS6235032B2 (en) 1987-07-30

Family

ID=15355394

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14415179A Granted JPS5668782A (en) 1979-11-06 1979-11-06 Burner burning control method for grain dryer

Country Status (1)

Country Link
JP (1) JPS5668782A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59119173A (en) * 1982-12-26 1984-07-10 井関農機株式会社 Controller for hot air of burner in cereal grain drier

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4831781A (en) * 1971-08-25 1973-04-26
JPS5912825B2 (en) * 1976-07-19 1984-03-26 野田合板株式会社 Base plate for mortar wall construction and its manufacturing method
JPS563592Y2 (en) * 1977-06-29 1981-01-26

Also Published As

Publication number Publication date
JPS5668782A (en) 1981-06-09

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