JPH0419467B2 - - Google Patents

Info

Publication number
JPH0419467B2
JPH0419467B2 JP59036326A JP3632684A JPH0419467B2 JP H0419467 B2 JPH0419467 B2 JP H0419467B2 JP 59036326 A JP59036326 A JP 59036326A JP 3632684 A JP3632684 A JP 3632684A JP H0419467 B2 JPH0419467 B2 JP H0419467B2
Authority
JP
Japan
Prior art keywords
drying
hot air
grain
moisture value
air temperature
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 - Lifetime
Application number
JP59036326A
Other languages
Japanese (ja)
Other versions
JPS60181579A (en
Inventor
Aijiro Kaneko
Tetsushiro Watanabe
Naohisa Kato
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.)
Kaneko Agricultural Machinery Co Ltd
Original Assignee
Kaneko Agricultural Machinery 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 Kaneko Agricultural Machinery Co Ltd filed Critical Kaneko Agricultural Machinery Co Ltd
Priority to JP3632684A priority Critical patent/JPS60181579A/en
Publication of JPS60181579A publication Critical patent/JPS60181579A/en
Publication of JPH0419467B2 publication Critical patent/JPH0419467B2/ja
Granted legal-status Critical Current

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  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】 本発明は、被乾燥穀物の水分を経時的に測定し
て、この測定水分値と予め設定された乾燥時間毎
の基準水分値との差を検出し、熱風温度を制御し
て通風乾燥する穀物乾燥方法に関する。
Detailed Description of the Invention The present invention measures the moisture content of grains to be dried over time, detects the difference between the measured moisture value and a reference moisture value for each preset drying time, and calculates the hot air temperature. This invention relates to a grain drying method that performs controlled ventilation drying.

従来、乾燥中の穀物の水分の変化に応じて熱風
の温度を補正しながら乾燥を行う穀物の乾燥制御
方法は、特開昭58−193082号公報に記載されてお
り、また、乾燥の終期に至つて、その際の穀物の
水分情報から、熱風温度を再設定して乾燥を続け
る方法は、特開昭58−72872号公報に記載されて
いる。
Conventionally, a grain drying control method in which drying is performed while correcting the temperature of hot air according to changes in the moisture content of the grain during drying is described in Japanese Patent Application Laid-Open No. 193082/1982. A method of continuing drying by resetting the hot air temperature based on the moisture information of the grain at that time is described in JP-A-58-72872.

ところで、上記特開昭58−193082号公報に記載
されているように、乾燥中の穀物の水分を検出
し、その変化に応じて熱風の温度を補正しながら
通風乾燥を行う乾燥制御方法によれば、乾燥の開
始時に設定した温度の熱風で乾燥を続ける制御手
段に比べて、穀物の水分の変化に応じた適切な乾
燥制御ができる。
By the way, as described in the above-mentioned Japanese Patent Application Laid-open No. 193082/1982, a drying control method that detects the moisture content of grains during drying and performs ventilation drying while correcting the temperature of the hot air according to the change in moisture content is used. For example, compared to a control means that continues drying with hot air at a temperature set at the start of drying, it is possible to perform appropriate drying control according to changes in grain moisture.

また、上記特開昭58−72872号公報に記載され
ているように、乾燥の終期に至つて、その際の穀
物の水分情報から、熱風温度を再設定して乾燥を
続ける方法によれば、熱風の温度を再設定する際
の穀物の水分検出が正しく行われた場合は、適切
な乾燥制御ができることになる。
In addition, as described in the above-mentioned Japanese Patent Application Laid-open No. 58-72872, according to a method in which drying is continued by resetting the hot air temperature based on the moisture information of the grain at the end of drying, If moisture in the grain is detected correctly when resetting the temperature of the hot air, appropriate drying control will be possible.

しかしながら、穀物乾燥機において、乾燥中の
穀物の水分測定は、極く少量の穀物を抽出して行
われるので、全体の平均値より水分の多い穀物が
測定試料となつたり、逆に水分の少ない穀物が測
定試料となることがあると、乾燥終期における熱
風温度が適切に再設定されず、それが原因で胴割
れや乾燥不足を起こすことが、しばしばあつたの
である。
However, in a grain dryer, the moisture content of the grain being dried is measured by extracting a very small amount of the grain, so the measurement sample may be a grain with a higher moisture content than the overall average value, or conversely a grain with a lower moisture content. When grains were used as measurement samples, the temperature of the hot air at the end of drying was not properly reset, which often caused shell cracking and insufficient drying.

本発明は、このような従来の穀物乾燥制御方法
における問題点を解消するものであり、乾燥終期
には、乾燥中の穀物の水分測定値にかかわらず、
再び初期の基準熱風温度を保つて仕上げ水分値ま
で乾燥することにより、胴割れを起こしたり乾燥
不足となることなく、高品質の乾燥穀物を得るこ
とができる穀物乾燥方法を提供することを目的と
するものである。
The present invention solves these problems in conventional grain drying control methods, and at the end of drying, regardless of the moisture content of the grain during drying,
The purpose of the present invention is to provide a grain drying method that can obtain high-quality dried grain without causing shell cracking or insufficient drying by drying to the finished moisture value while maintaining the initial standard hot air temperature again. It is something to do.

次に本発明の一実施例を図面に示した装置の一
例を参照して説明する。
Next, an embodiment of the present invention will be described with reference to an example of an apparatus shown in the drawings.

第1図において、1は熱風温度検出器、2は基
準熱風温度設定回路、3は温度比較回路であり、
また、4は水分測定器、5は基準水分値設定回
路、6は水分比較回路であつて、水分比較回路6
の出力は制御パターン切換回路7に入力し、かつ
温度比較回路3に送られ、熱風温度の設置値を補
正するように構成されている。8は熱風温度制御
回路、9は燃料供給ポンプであつて、熱風温度制
御回路8は、温度比較回路3からの補正された制
御信号を受け、燃料供給ポンプ9を制御するもの
である。
In FIG. 1, 1 is a hot air temperature detector, 2 is a reference hot air temperature setting circuit, and 3 is a temperature comparison circuit.
Further, 4 is a moisture measuring device, 5 is a reference moisture value setting circuit, and 6 is a moisture comparison circuit.
The output is input to the control pattern switching circuit 7 and sent to the temperature comparison circuit 3, so as to correct the set value of the hot air temperature. 8 is a hot air temperature control circuit, and 9 is a fuel supply pump. The hot air temperature control circuit 8 receives the corrected control signal from the temperature comparison circuit 3 and controls the fuel supply pump 9.

上記基準熱風温度設定回路2は、乾燥初期の基
準熱風温度を設定するものであり、基準水分値設
定回路5は基準水分値を予め設定しておくもので
ある。また制御パターン切換回路7は乾燥開始時
から一定の乾燥時間が経過するまではその入力を
温度比較回路3に送らず、その後測定水分値が乾
燥仕上げ水分値に近づく乾燥終期の一定値(例え
ば16%)に至るまではその入力を温度比較回路3
に、さらに、その後、仕上げ水分値(例えば15
%)に至るまでは再びその入力を温度比較回路3
に送らないように動作するものである。
The reference hot air temperature setting circuit 2 is for setting a reference hot air temperature at the initial stage of drying, and the reference moisture value setting circuit 5 is for setting a reference moisture value in advance. Furthermore, the control pattern switching circuit 7 does not send its input to the temperature comparison circuit 3 until a certain drying time has elapsed from the start of drying, and after that, the measured moisture value approaches a certain value at the end of drying (for example, 16 %), the input is sent to temperature comparison circuit 3.
In addition, then the finish moisture value (e.g. 15
%), the input is again sent to temperature comparison circuit 3.
It operates in such a way that it is not sent to

以上のように構成された装置においては、乾燥
開始に際し、張込穀量および外気温度等により、
基準熱風温度を決定し、その熱風温度を保つて乾
燥が行われる。そして、制御パターン切換回路7
の動作により、乾燥仕上げ水分値より若干高い水
分値までは、測定水分値と予め設定された水分値
との差に応じて予め設定した温度幅で熱風温度が
制御されて乾燥が続けられ、乾燥終期に至ると、
再び初期の基準熱風温度を保つて仕上げ水分値ま
で乾燥される。このため、乾燥中の穀物の水分測
定値にかかわらず、胴割れを起こしたり乾燥不足
となることなく乾燥することができる。
In the apparatus configured as described above, at the start of drying, depending on the amount of grain loaded, the outside temperature, etc.
A reference hot air temperature is determined, and drying is performed while maintaining that hot air temperature. And the control pattern switching circuit 7
By this operation, the hot air temperature is controlled in a preset temperature range according to the difference between the measured moisture value and the preset moisture value until the moisture value is slightly higher than the finished drying moisture value, and drying continues. When reaching the final stage,
The initial standard hot air temperature is maintained again to dry to the final moisture value. Therefore, regardless of the measured moisture value of the grain during drying, it is possible to dry the grain without causing shell cracking or insufficient drying.

本発明は、前記のように、乾燥初期は乾燥開始
時に設定した基準熱風温度を保つて乾燥し、次い
で乾燥仕上げ水分値より若干高い水分値までは測
定水分値と予め設定された水分値との差に応じて
予め設定した温度幅で熱風温度を制御して乾燥し
た後、乾燥終期に至つて再び初期の基準熱風温度
を保つて仕上げ水分値まで乾燥する方法であるか
ら、乾燥終期には、乾燥中の穀物の水分測定値に
かかわらず、再び初期の基準熱風温度を保つて仕
上げ水分値まで乾燥することにより、胴割れを起
こしたり乾燥不足となることなく、高品質の乾燥
穀物を得ることができる効果を奏する。
As described above, the present invention maintains the standard hot air temperature set at the beginning of drying in the initial stage of drying, and then maintains the measured moisture value and the preset moisture value until the moisture value is slightly higher than the finished drying moisture value. After drying by controlling the hot air temperature in a preset temperature range according to the difference, the initial reference hot air temperature is maintained again at the end of the drying period to dry to the finished moisture value. Regardless of the measured moisture value of the grain during drying, by maintaining the initial standard hot air temperature again and drying to the finished moisture value, high quality dried grain can be obtained without causing shell cracking or insufficient drying. It produces the effect that can be achieved.

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

図面は本発明に係る穀物乾燥方法を実施するた
めの装置の一実施例を示すものであつて、第1図
は構成の要部を示すブロツク図、第2図はその作
用説明図である。 1……熱風温度検出器、2……基準熱風温度設
定回路、3……温度比較回路、4……水分測定
器、5……基準水分値設定回路、6……水分比較
回路、7……制御パターン切換回路、8……熱風
温度制御回路、9……燃料供給ポンプ。
The drawings show an embodiment of the apparatus for carrying out the grain drying method according to the present invention, in which FIG. 1 is a block diagram showing the main parts of the structure, and FIG. 2 is an explanatory diagram of its operation. 1...Hot air temperature detector, 2...Reference hot air temperature setting circuit, 3...Temperature comparison circuit, 4...Moisture measuring device, 5...Reference moisture value setting circuit, 6...Moisture content comparison circuit, 7... Control pattern switching circuit, 8... hot air temperature control circuit, 9... fuel supply pump.

Claims (1)

【特許請求の範囲】[Claims] 1 乾燥初期は乾燥開始時に設定した基準熱風温
度を保つて乾燥し、次いで乾燥仕上げ水分値より
若干高い水分値までは測定水分値と予め設定され
た水分値との差に応じて予め設定した温度幅で熱
風温度を制御して乾燥した後、乾燥終期に至つて
再び初期の基準熱風温度を保つて仕上げ水分値ま
で乾燥することを特徴とする穀物乾燥方法。
1. In the initial stage of drying, drying is carried out by maintaining the reference hot air temperature set at the start of drying, and then, until the moisture value is slightly higher than the dry finish moisture value, the temperature is set in advance according to the difference between the measured moisture value and the preset moisture value. This grain drying method is characterized in that after drying by controlling the hot air temperature according to the grain width, the initial standard hot air temperature is maintained again at the end of the drying period to dry the grain to a finishing moisture value.
JP3632684A 1984-02-29 1984-02-29 Method of drying cereal Granted JPS60181579A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3632684A JPS60181579A (en) 1984-02-29 1984-02-29 Method of drying cereal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3632684A JPS60181579A (en) 1984-02-29 1984-02-29 Method of drying cereal

Publications (2)

Publication Number Publication Date
JPS60181579A JPS60181579A (en) 1985-09-17
JPH0419467B2 true JPH0419467B2 (en) 1992-03-30

Family

ID=12466711

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3632684A Granted JPS60181579A (en) 1984-02-29 1984-02-29 Method of drying cereal

Country Status (1)

Country Link
JP (1) JPS60181579A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58193082A (en) * 1982-05-06 1983-11-10 辰本 韶弘 Method of controlling hot air in cereal drier

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58193082A (en) * 1982-05-06 1983-11-10 辰本 韶弘 Method of controlling hot air in cereal drier

Also Published As

Publication number Publication date
JPS60181579A (en) 1985-09-17

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