JPS60181579A - Method of drying cereal - Google Patents

Method of drying cereal

Info

Publication number
JPS60181579A
JPS60181579A JP3632684A JP3632684A JPS60181579A JP S60181579 A JPS60181579 A JP S60181579A JP 3632684 A JP3632684 A JP 3632684A JP 3632684 A JP3632684 A JP 3632684A JP S60181579 A JPS60181579 A JP S60181579A
Authority
JP
Japan
Prior art keywords
drying
hot air
air temperature
moisture value
moisture
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.)
Granted
Application number
JP3632684A
Other languages
Japanese (ja)
Other versions
JPH0419467B2 (en
Inventor
金子 愛次郎
渡辺 鉄四郎
加藤 尚久
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)

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、乾燥初期は乾燥開始時に設定した基準熱風温
度を保ち、次いで基準熱風温度を一定の温度幅に変化さ
せて設定した乾減率で乾燥するように制御し、乾燥終期
に再び初期の基準熱風温度に戻して乾燥する穀物乾燥方
法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention maintains the reference hot air temperature set at the start of drying in the initial stage of drying, and then controls the reference hot air temperature to vary within a certain temperature range to dry at a set drying loss rate. This invention relates to a grain drying method in which the temperature of the hot air is returned to the initial reference temperature at the end of drying.

乾燥中の被乾燥穀物の水分値を、予め設定された水分値
に近づけるように熱風温度を補正制御する、いわゆる乾
減率制御を行う穀物乾燥方法は、さきに本出願人が特願
昭57−213193号に記載されたように開発したも
のである。
A grain drying method that performs so-called drying loss rate control, in which hot air temperature is corrected and controlled so that the moisture value of the grain to be dried during drying approaches a preset moisture value, was previously proposed by the applicant in Japanese Patent Application No. 1983. It was developed as described in No.-213193.

ところで、上記の穀物乾燥方法によれば、乾燥中の被乾
燥穀物の水分値を、予め設定された好条件下の基準水分
値に沿って乾燥するので、乾燥中に外気温度がいかに変
化しても、胴割れが発生したり、乾燥不足の状′態に陥
ることがなく、常に高品質の乾燥穀物を能率的に得るこ
とができるが、乾燥終期における最終の水分測定時に、
たまたま設定水分値よりかなり離れた高い水分が測定さ
れた場合には熱風温度がかなり高い値に制御され、逆に
低い水分が測定された場合には、熱風温度がかなり低い
値に制御されるので、前者の場合は乾燥仕上げまでの時
間が早すぎ、後者の場合には時間が長過ぎて乾燥能率が
低下する虞れがある。
By the way, according to the above-mentioned grain drying method, the moisture value of the grain to be dried is dried according to a preset standard moisture value under favorable conditions, so it is not possible to change the outside temperature during drying. However, during the final moisture measurement at the end of the drying period,
If a high moisture content that is far away from the set moisture value happens to be measured, the hot air temperature will be controlled to a fairly high value, and conversely, if a low moisture content is measured, the hot air temperature will be controlled to a fairly low value. In the former case, the time required to finish drying is too fast, and in the latter case, the time is too long, which may reduce drying efficiency.

そこで本発明は、上記穀物乾燥方法を改良して、乾燥終
期における乾燥仕上げまでの時間を常に適正に維持して
、能率的に、しかも品質の低下をきたすことがなく乾燥
を終了させ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。
Therefore, the present invention improves the above-mentioned grain drying method, so that the time required to finish drying at the end of drying can be maintained at an appropriate level, and drying can be completed efficiently and without deterioration of quality. The object is to provide a grain drying method.

本発明は前記に鑑み、上記目的を達成させるため、特に
その方法を、乾燥初期は乾燥開始時に設定した基準熱f
@湯温度保って乾燥し、次いで乾燥仕上げ水分値より若
干、高い水分値まで社測定水分値と予め設定された乾燥
時間当りの基準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、再び初期の基準熱
風温度を保って仕上げ水分値まで乾燥することを特徴と
する穀物乾燥方法としたものであって、かかる方法によ
れば、乾燥終期における水分値の測定結果の如何にかか
わらず、乾燥仕上げまでの時間を適正に維持することが
でき、常に能率よく、しかも胴割れ等を生じさせること
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。
In view of the foregoing, in order to achieve the above object, the present invention particularly provides a method using a standard temperature f set at the beginning of drying.
@Dry while maintaining the hot water temperature, then heat air temperature at a preset temperature range according to the difference between the measured moisture value and the preset reference moisture value per drying time until the moisture value is slightly higher than the finished drying moisture value. After drying by controlling the drying temperature, the grain drying method is characterized in that the initial standard hot air temperature is maintained again to dry the grain to the finished moisture value, and according to this method, the moisture value at the final stage of drying is Regardless of the measurement results, the time until drying can be maintained appropriately, and high-quality dried grains can always be obtained efficiently and without causing cracks or the like.

以下に本発明に係る穀物乾燥方法を、その実施のための
装置について説明する。
The grain drying method according to the present invention and the apparatus for carrying out the method will be explained below.

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、5it基準水分値設定回路、6は水分比較回路で
あって、水分比較回路6の出力は制御パターン切換回路
7に入力されこれが温度比較回路に送られ、熱風温度の
設定値を補正する。8は熱風温度制御回路、9は燃料供
給ポンプであって、熱風温度制御回路8は温度比較回路
3から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, 3 is a temperature comparison circuit, 4 is a moisture measuring device, 5 is a reference moisture value setting circuit, and 6 is a moisture comparison circuit. The output of the moisture comparison circuit 6 is input to the control pattern switching circuit 7 and sent to the temperature comparison circuit 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は乾燥開始時から乾減率制御開始時まではそ
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. In addition, the control pattern switching circuit 7 does not send its input to the temperature comparison circuit 3 from the start of drying to the start of drying loss rate control, and after that, the measured moisture value approaches a constant value (for example, 16%) that approaches the dry finish moisture value.
The input is not sent to the temperature comparison circuit 3 until reaching the final moisture value (for example, 15%), and the input is not sent to the temperature comparison circuit 3 again until the finished moisture value (for example, 15%) is reached.

次にその作用について説明する。Next, its effect will be explained.

今、乾燥機に被乾燥穀物を張込み、乾燥作業な開始する
に際し、張込穀量および外気温度による補正その他によ
り基準熱風温度を決定し、その基準熱風温度を基準熱風
温度設定回路2に設定する。
Now, when loading the grain to be dried in the dryer and starting the drying work, determine the standard hot air temperature by correcting the amount of grain to be loaded and the outside temperature, etc., and set the standard hot air temperature in the standard hot air temperature setting circuit 2. do.

そして乾燥作業i開始する。さすれば乾燥中の熱am度
は熱風温度検出器1で検出され、乾燥中の熱風温度は温
度比較回路3に入力し、その出力を受けて基準熱風温度
を保つように熱風温度制御回路8が燃料供給ポンプ9を
制御する。この間、制御パターン回路7から温度比較回
路3への入力は遮断されている。そして、被乾燥穀物の
水分が水分ムラの発生が少なくなった水分値(例えば2
2%)となると、制御パターン切換回路7と温度比較回
路3が接続され切換るので、乾燥中の一定時間(例えば
1時間)ごとに水分測定器4で測定される水分値が水分
比較回路6において基準水分値と比較され、それを基準
水分値に近づけるため、熱風温度が予め設定された温度
幅で補正されるように熱風温度制御回路8によって燃料
供給ポンプ9が制御される。
Then, the drying operation starts. Then, the heat am degree during drying is detected by the hot air temperature detector 1, the hot air temperature during drying is input to the temperature comparison circuit 3, and based on the output, the hot air temperature control circuit 8 is operated to maintain the reference hot air temperature. controls the fuel supply pump 9. During this time, the input from the control pattern circuit 7 to the temperature comparison circuit 3 is cut off. Then, the moisture content of the grain to be dried is determined at a moisture value (for example, 2
2%), the control pattern switching circuit 7 and the temperature comparison circuit 3 are connected and switched, so that the moisture value measured by the moisture measuring device 4 at fixed time intervals (for example, 1 hour) during drying is transferred to the moisture comparison circuit 6. The fuel supply pump 9 is controlled by the hot air temperature control circuit 8 so that the hot air temperature is corrected within a preset temperature range in order to bring it closer to the reference moisture value.

例えば基準水分値に対して測定水分値が±0.1%〜±
0.5%の範囲でti ±5 a(、±0.5%〜:i
=1.oO%の範囲では±10°Cの温度補正をする。
For example, the measured moisture value is ±0.1% to ±± of the standard moisture value.
ti ±5 a(, ±0.5% ~: i
=1. Temperature correction of ±10°C is performed in the oO% range.

このようにして乾燥が進み、乾燥終期(例えば被乾燥穀
物の水分16%)K至って水分測定器4で乾燥仕上げ値
より若干高い水分値が測定されると、制御パターン切換
回路1と温度比較回路3が遮断され、仕上げ水分値(例
えば15%)が測定されるまで乾燥初期の基準熱風温度
を保って乾燥される。
In this way, the drying progresses, and when the moisture value reaches the final stage of drying (for example, the moisture content of the grain to be dried is 16%) and the moisture value is measured by the moisture measuring device 4, which is slightly higher than the dry finish value, the control pattern switching circuit 1 and the temperature comparison circuit 3 is shut off, and the drying is carried out while maintaining the reference hot air temperature at the initial stage of drying until the finished moisture value (for example, 15%) is measured.

そして仕上げ水分値(例えば15%)になると乾燥が自
動的に終了する(以上第2図参照)。
Then, when the finished moisture value (for example, 15%) is reached, drying is automatically terminated (see FIG. 2 above).

上記のように、乾燥終期においては、水分測定器4によ
る測定水分値の如何にかかわらず、乾燥初期に設定され
た基準熱風温度を保って仕上げ水分値まで乾燥されるの
で、乾燥終了に至るまでの時間が長過ぎたり、逆に短か
過ぎる制御がなされ ゛ることがなく、常に能率よく、
しかも胴割れ等が生ぜず高品質の乾燥穀物を得ることが
できる。
As mentioned above, at the end of drying, regardless of the moisture content measured by the moisture meter 4, the standard hot air temperature set at the beginning of drying is maintained and the drying reaches the finished moisture value, so until the end of drying. The control time is never too long or too short, and the process is always efficient.
Furthermore, high-quality dried grains can be obtained without cracking or the like.

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

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
のブロック図、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 特許出願人 金子農機株式会社 第1図 第2図 イれ −31カー4(り1イ遺L% O測り木ケ償% +−++ N丸壕し@C 手続補正書 (方式) %式% 1、事件の表示 特願昭59−36326号 2、発明の名称 穀物乾燥方法 3、補正をする者 事件との関係 特許出願人 埼玉県羽生市西2丁目21番10号 (146) 金子農機株式会社 代表者 金 子 愛次部 4、代理人 〒201 6、補正の対象 明細書中の「図面の簡単な説明の欄」 7、補正の内容 (11明細書第6頁第19行記載の「図面は」とあるを
「第1図は」と補正します。
The drawing is a block diagram of an apparatus for implementing the grain drying method according to the present invention, and FIG. 2 is an explanatory diagram of its operation. DESCRIPTION OF SYMBOLS 1... Hot air temperature detector, 2... Reference hot air temperature setting circuit, 3... Temperature comparison circuit, 4... Moisture measuring device, 5...
・・Reference moisture setting circuit, 6−・・Moisture comparison circuit, 7・・
・Control pattern switching circuit, 8...Hot air temperature control circuit,
9...Fuel supply pump patent applicant Kaneko Agricultural Machinery Co., Ltd. Figure 1 Figure 2 -31 Car 4 (R1 I L% O measurement tree compensation % +-++ N round trench @C Procedure amendment (Method) % formula % 1. Indication of the case Japanese Patent Application No. 59-36326 2. Name of the invention Grain drying method 3. Person making the amendment Relationship to the case Patent applicant 2-21-10 Nishi, Hanyu City, Saitama Prefecture No. (146) Kaneko Agricultural Machinery Co., Ltd. Representative Aiji Kaneko 4, Agent 〒201 6. "Brief description of drawings column" in the specification subject to amendment 7. Contents of amendment (11 Specification No. 6 In line 19 of the page, the phrase ``The drawing is'' has been corrected to ``Figure 1 is''.

Claims (1)

【特許請求の範囲】[Claims] 乾燥初期は乾燥開始時に設定した基準熱風温度を保って
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、
再び初期の基準熱風温度を保っ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。
In the initial stage of drying, the standard hot air temperature set at the start of drying is maintained, and then until the moisture value is slightly higher than the finished drying moisture value, the temperature range is set in advance according to the difference between the measured moisture value and the preset moisture value. After drying by controlling the hot air temperature,
A grain drying method characterized by drying to a finishing moisture value while maintaining the initial standard hot air temperature again.
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 true JPS60181579A (en) 1985-09-17
JPH0419467B2 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
JPH0419467B2 (en) 1992-03-30

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