JP2016061479A - Grain drier - Google Patents

Grain drier Download PDF

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JP2016061479A
JP2016061479A JP2014189163A JP2014189163A JP2016061479A JP 2016061479 A JP2016061479 A JP 2016061479A JP 2014189163 A JP2014189163 A JP 2014189163A JP 2014189163 A JP2014189163 A JP 2014189163A JP 2016061479 A JP2016061479 A JP 2016061479A
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moisture
drying
grain
moisture value
measured
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JP6492477B2 (en
JP2016061479A5 (en
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裕人 薬内
Yuto Yakunai
裕人 薬内
浩史 豊田
Hiroshi Toyoda
浩史 豊田
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Iseki and Co Ltd
Iseki Agricultural Machinery Mfg Co Ltd
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Iseki and Co Ltd
Iseki Agricultural Machinery Mfg Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To perform a positive retention of returning of water content value of grain after finishing of drying reached to a dryness target water content value at a grain drier.SOLUTION: This invention relates to a grain drier comprising drying work finishing control means for measuring a water content value of grain dried by hot air generated by a burner 5 with a moisture meter 6, stopping the combustion at the burner 5 upon reaching of the measured water content value to a dried target water content to finish the hot air drying work. The grain drier comprises moisture returning correction control means. When the water content is measured while circulating the grain in the drier after finishing of the drying work based on the drying work finishing control means and the measured water content value exceeds the dried target water content upon finishing of the drying work, the moisture returning correction control means executes a circulating and drying work in a state where the burner 5 is kept stopped and a suction discharging fan 7 is driven or stopped, and when the measured water content value reaches the dried target water content, the moisture returning correction control means stops the circulating and drying work.SELECTED DRAWING: Figure 7

Description

本発明は、穀物乾燥機に関するものである。   The present invention relates to a grain dryer.

バーナからの熱風で乾燥する穀物の水分値を水分計で測定し、その水分測定値が停止水分値設定手段で設定している水分値に一致するときに、バーナの燃焼を停止して乾燥作業を終了する乾燥終了制御手段を有する穀物乾燥機において、乾燥途中の所定のタイミングでバーナの燃焼を停止して休止乾燥をし、所定時間経過後にバーナを再燃焼させる休止乾燥制御手段と、その休止乾燥制御手段による休止乾燥の開始時及び終了時における水分値の各測定値を読み込み、その両測定値から水分の戻りを検出する戻り水分値検出手段と、その戻り水分値に応じて前記停止水分値設定手段で設定してある停止水分値を補正する停止水分値補正手段を設けた停止水分補正装置は、公知である(特許文献1)。   Measure the moisture value of the grains to be dried with hot air from the burner with a moisture meter, and when the measured moisture value matches the moisture value set by the stop moisture value setting means, stop burning the burner and dry In the grain dryer having the drying end control means for ending the drying, the pause drying control means for stopping the combustion of the burner at a predetermined timing during the drying and performing the pause drying, and re-burning the burner after a predetermined time has elapsed, and the pause Read each measured value of the moisture value at the start and end of the rest drying by the drying control means, return moisture value detecting means for detecting the return of moisture from both measured values, and the stopped moisture according to the returned moisture value A stop moisture correction apparatus provided with a stop moisture value correction means for correcting a stop moisture value set by a value setting means is known (Patent Document 1).

特公平7−89023号公報Japanese Patent Publication No. 7-89023

前記先行技術の発明は、穀物乾燥機の停止水分値補正装置に関するもので、熱風乾燥工程中にバーナの燃焼を停止した所定時間の休止乾燥を実行し、その休止乾燥の開始時と終了時の測定水分値から乾燥終了後の所定時間における水分値の戻りを予測し、目標乾燥水分値に予測戻り水分値を加算して目標乾燥水分値を変更設定し熱風乾燥作業を再開するものである。   The invention of the prior art relates to a stop moisture value correction device for a grain dryer, which performs a pause drying for a predetermined time during which a burner is stopped during a hot air drying process, and starts and ends the pause drying. The return of the moisture value at a predetermined time after the drying is predicted from the measured moisture value, the predicted return moisture value is added to the target dry moisture value, the target dry moisture value is changed and set, and the hot air drying operation is resumed.

従って、乾燥作業終了後の天候変化や、未熟米比率の大小などの乾燥穀物の品質事情により乾燥作業終了後に所定時間が経過すると、予測に反して戻り水分値が変化し乾燥目標水分値が維持されない場合が発生する。   Therefore, when the predetermined time elapses after the drying operation ends due to the weather change after the drying operation and the quality of the dried cereal such as the ratio of immature rice, the return moisture value changes unexpectedly and the drying target moisture value is maintained. It may not happen.

このような場合には、オペレータは乾燥目標水分値になるように乾燥作業を再開しなければならず、籾摺作業を迅速に実施できないという問題が発生する。
本発明は、このような問題点を解決しようとするものであって、穀物乾燥機の乾燥制御装置において、乾燥目標水分値に到達した乾燥終了後に穀物を機内循環し水分値の戻り状態を測定し、水分値の戻りが発生している場合には追い乾燥し乾燥目標水分値に戻すことにより、前記問題点を解決しようとするものである。
In such a case, the operator must restart the drying operation so as to reach the drying target moisture value, and there arises a problem that the hulling operation cannot be performed quickly.
The present invention is intended to solve such problems, and in a drying control device of a grain dryer, the grain is circulated in the machine after completion of drying when the drying target moisture value is reached, and the return state of the moisture value is measured. However, when the moisture value is returned, the above-mentioned problem is solved by additional drying and returning to the dry target moisture value.

本発明は、前記課題を解決するために次の技術的手段を講じた。
請求項1の発明は、バーナ5の生成する熱風で乾燥される穀物の水分値を水分計6で測定し測定水分値が乾燥目標水分値に到達するとバーナ5の燃焼を停止し熱風乾燥作業を終了する乾燥作業終了制御手段を備えた穀物乾燥機において、前記乾燥作業終了制御手段に基づく乾燥作業の終了後において機内穀物を循環しながら水分値を測定し該測定水分値が前記乾燥作業終了時の乾燥目標水分値を上回る場合には、バーナ5の停止状態で且つ吸引排気フアン7を駆動あるいは停止した循環乾燥作業を実行し、測定水分値が乾燥目標水分値に到達すると循環乾燥作業を停止する水分戻り補正制御手段を備えた穀物乾燥機の戻り水分補正装置とする。
The present invention has taken the following technical means in order to solve the above problems.
In the invention of claim 1, the moisture value of the grain dried with the hot air generated by the burner 5 is measured by the moisture meter 6, and when the measured moisture value reaches the drying target moisture value, the combustion of the burner 5 is stopped and the hot air drying operation is performed. In the grain dryer having the drying operation end control means to be finished, after the drying operation based on the drying operation end control means, the moisture value is measured while circulating the grain in the machine, and the measured moisture value is determined when the drying operation is completed. If the measured moisture value reaches the drying target moisture value, the circulation drying operation is stopped when the burner 5 is stopped and the suction exhaust fan 7 is driven or stopped. It is set as the return moisture correction apparatus of the grain dryer provided with the moisture return correction control means to perform.

請求項2の発明は、請求項1の発明において、前記水分戻り補正制御手段における戻り水分値の測定を機内穀物の1循環する間に複数回水分値を測定しその平均値により戻り水分値を算出することを特徴とする穀物乾燥機の戻り水分補正装置とする。   According to a second aspect of the present invention, in the first aspect of the invention, the water content is measured a plurality of times during one circulation of the in-flight grain in the moisture return correction control means, and the return water value is determined by the average value. It is set as the return moisture correction apparatus of the grain dryer characterized by calculating.

請求項3の発明は、請求項1又は請求項2の発明において、前記乾燥作業終了後において所定設定時間毎に前記水分戻り補正制御手段により水分値を測定し乾燥目標水分値に対する戻り水分値を確認することを特徴とする穀物乾燥機の戻り水分補正装置とする。   According to a third aspect of the present invention, in the first or second aspect of the present invention, the moisture value is measured by the moisture return correction control means every predetermined set time after the drying operation, and the return moisture value relative to the drying target moisture value is determined. It is set as the return moisture correction apparatus of the grain dryer characterized by confirming.

請求項4の発明は、請求項1乃至請求項3のいずれかの発明において、前記乾燥作業終了後において前記水分戻り補正制御手段を自動的に実行する水分戻り補正操作手段SW12を設けたことを特徴とする穀物乾燥機の戻り水分補正装置とする。   According to a fourth aspect of the present invention, in any one of the first to third aspects of the present invention, a moisture return correction operation unit SW12 that automatically executes the moisture return correction control unit after the drying operation is provided. It is set as the return moisture correction apparatus of the grain dryer characterized by the above.

請求項5の発明は、請求項1乃至請求項3のいずれかの発明において、前記水分戻り補正制御手段の実行時における戻り水分値の測定にあたり乾燥目標水分値よりも設定水分値以上の高い戻りがある場合には、前記循環乾燥作業に代えてバーナ5を燃焼した熱風乾燥作業を開始するようにしたことを特徴とする穀物乾燥機の戻り水分補正装置とする。   According to a fifth aspect of the present invention, in the invention according to any one of the first to third aspects, in the measurement of the return moisture value at the time of the execution of the moisture return correction control means, the return is higher than the set target moisture value by the drying target moisture value. If there is, the return moisture correction device for a grain dryer is characterized in that a hot air drying operation in which the burner 5 is combusted is started instead of the circulation drying operation.

請求項1の発明によると、特許請求の範囲の項の特徴構成に基づき、乾燥作業終了後における乾燥目標水分値に対する水分の戻りを補正し、次工程の籾摺作業を迅速に実行することができる。穀物乾燥機の乾燥作業は夜間に終了し、翌日籾摺作業をすることが多いが、このような場合にも籾摺作業を予定通り実行することができる。   According to the invention of claim 1, based on the characteristic configuration of the claims, it is possible to correct the return of moisture with respect to the drying target moisture value after the completion of the drying operation and to quickly perform the hulling operation of the next process. it can. The drying operation of the grain dryer ends at night, and the hulling work is often performed the next day. Even in such a case, the hulling work can be performed as scheduled.

請求項2の発明によると、請求項1記載の発明の前記効果に加えて、特許請求の範囲の項の特徴構成に基づき、乾燥作業終了後の戻り水分値を乾燥終了後の天候や時間帯に合わせて精度よく測定することができる。   According to the invention of claim 2, in addition to the effect of the invention of claim 1, the return moisture value after the completion of the drying operation is calculated based on the characteristic configuration of the claim, the weather and time zone after the completion of the drying operation Can be measured with high accuracy.

請求項3の発明によると、請求項1又は請求項2記載の発明の前記効果に加えて、特許請求の範囲の項の特徴構成に基づき、穀物乾燥機で長期にわたり穀物を保管する場合にも穀物の水分値を乾燥目標水分値に安定して保持し、穀物の品質を良好に保つことができる。   According to the invention of claim 3, in addition to the effects of the invention of claim 1 or 2, in addition to the above-mentioned effect of the invention of claim 1, the case of storing grains for a long time with a grain dryer It is possible to stably maintain the grain moisture value at the drying target moisture value and maintain good grain quality.

請求項4の発明によると、請求項1乃至請求項3のいずれかの発明の前記効果に加えて、特許請求の範囲の項の特徴構成に基づき、夜間に乾燥作業が終了する場合には水分戻り補正操作手段SW12を予め操作しておくことにより、オペレータは乾燥作業の終了後に操作する必要がなくなり操作を簡単にすることができる。   According to the invention of claim 4, in addition to the effect of the invention of any one of claims 1 to 3, in accordance with the characteristic configuration of the claims of claim 1, when the drying operation is completed at night, moisture By operating the return correction operation means SW12 in advance, the operator does not need to operate after the drying operation is completed, and the operation can be simplified.

請求項5の発明によると、請求項1乃至請求項3のいずれかの発明の前記効果に加えて、特許請求の範囲の項の特徴構成に基づき、穀物乾燥機で長期に乾燥穀物を保存する場合に水分値の戻りが大きいときにも、戻り水分値を迅速に乾燥し乾燥目標水分値に戻し穀物品質を良好に保持することができる。   According to the invention of claim 5, in addition to the effect of the invention of any one of claims 1 to 3, based on the characteristic configuration of the claims, the dried grain is stored in the grain dryer for a long period of time. Even in the case where the return of the moisture value is large, the returned moisture value can be quickly dried and returned to the dry target moisture value, so that the grain quality can be maintained well.

穀物乾燥機の切断側面図。A cut side view of a grain dryer. 穀物乾燥機の切断正面図。The cutting front view of a grain dryer. 操作盤の正面図。The front view of an operation panel. 操作パネルの表示内容を示す図。The figure which shows the display content of an operation panel. 操作パネルの表示内容を示す図。The figure which shows the display content of an operation panel. 制御ブロック図。Control block diagram. フローチャート。flowchart. 穀物乾燥機の斜視図。The perspective view of a grain dryer. 穀物乾燥機のブロック図。Block diagram of a grain dryer.

前記技術思想に基づいて具体的に構成された実施の形態について以下図面を参照しつつ説明する。
まず、図1及び図2に基づきこの発明を具備する循環式穀物乾燥機の全体構成について説明する。
An embodiment specifically configured based on the technical idea will be described below with reference to the drawings.
First, based on FIG.1 and FIG.2, the whole structure of the circulation type grain dryer which comprises this invention is demonstrated.

1は乾燥機の機枠で、この機枠1内には貯溜室2,乾燥室3,集穀室4を上方から下方に順次配設している。乾燥室3には複数の左右穀粒流下通路9,9を形成し、左右穀粒流下通路9,9の前後一側にはバーナ5のバーナ風胴25に通じる熱風室6を配設し、左右穀粒流下通路9,9の前後他側には吸引排気ファン7のファン胴7aに通じる排風室8,8を配設し、左右穀粒流下通路9,9の下端部に繰出バルブ10を設けている。   Reference numeral 1 denotes a machine frame of a dryer. In the machine frame 1, a storage chamber 2, a drying chamber 3, and a grain collection chamber 4 are sequentially arranged from the upper side to the lower side. A plurality of left and right grain flow passages 9, 9 are formed in the drying chamber 3, and a hot air chamber 6 leading to the burner wind tunnel 25 of the burner 5 is disposed on one side of the left and right grain flow passages 9, 9; Exhaust chambers 8, 8 communicating with the fan body 7 a of the suction exhaust fan 7 are arranged on the other side of the left and right grain flow passages 9, 9, and the feeding valve 10 is provided at the lower end of the left and right grain flow passages 9, 9. Is provided.

前記機枠1の外側には集穀室4の前後一側に集めた穀粒を貯溜室2に揚穀還元する昇降機11を立設している。該昇降機11内の上下の駆動プーリ,従動プーリにバケットベルト13を巻き掛け、集穀室4の底部に設ける下部搬送装置14により乾燥穀粒を前後一側に移送し、昇降機11により揚穀する。昇降機11で揚穀された穀粒を上部搬送装置16の始端側に供給し、更に上部搬送装置16により横送して貯溜室2の上部中央に配設する回転拡散板18に送り、貯溜室2内に拡散落下させる。   On the outer side of the machine frame 1, an elevator 11 is erected to reduce the grains collected on the front and rear sides of the cereal collection chamber 4 to the storage chamber 2. The bucket belt 13 is wound around the upper and lower drive pulleys and driven pulleys in the elevator 11, the dried grains are transferred to the front and rear sides by the lower transport device 14 provided at the bottom of the cereal collection chamber 4, and the cereal is lifted by the elevator 11. . The grains that have been cerealed by the elevator 11 are supplied to the starting end side of the upper conveying device 16, and are further fed laterally by the upper conveying device 16 and sent to the rotary diffusion plate 18 disposed in the upper center of the storage chamber 2. Diffusion and fall into 2.

前記繰出バルブ10,昇降機11,下部搬送装置14,上部搬送装置16から構成されている穀粒循環系は、機体の下部後側に配設している昇降機モータ29により駆動される。また、昇降機11における上下中途部の壁面には水分計26を設け、バケットベルト13の上昇行程と下降行程の間隔部に設けた取込み口(図示省略)からサンプル粒を取り込み、水分値を測定する。この水分計26は、例えば一対の電極ロール間でサンプル粒を1粒ずつ圧縮粉砕し、その抵抗値を電気的に処理し一粒ずつの水分値に換算する公知のものである。   The grain circulation system composed of the feeding valve 10, the elevator 11, the lower conveying device 14, and the upper conveying device 16 is driven by an elevator motor 29 disposed on the lower rear side of the machine body. Further, a moisture meter 26 is provided on the wall surface of the elevator 11 in the middle of the upper and lower parts, sample grains are taken in from intake ports (not shown) provided in the interval between the ascending stroke and the descending stroke of the bucket belt 13, and the moisture value is measured. . The moisture meter 26 is a known one that compresses and pulverizes sample particles one by one between a pair of electrode rolls, and electrically converts the resistance value into a moisture value for each particle.

左右穀粒流下通路9,9の左右中間部に位置する乾燥室3には、遠赤外線放射体23を配設している。この遠赤外線放射体23は、熱風室6内にあってバーナ5の燃焼面と対向するように配設している前後方向に沿う内側遠赤外線放射体23aと、内側遠赤外線放射体23aを被覆する外側遠赤外線放射体23bとで構成されている。   A far-infrared radiator 23 is disposed in the drying chamber 3 located at the left and right intermediate portions of the left and right grain flow passages 9 and 9. The far-infrared radiator 23 covers the inner far-infrared radiator 23a and the inner far-infrared radiator 23a along the front-rear direction disposed in the hot air chamber 6 so as to face the combustion surface of the burner 5. The outer far-infrared radiator 23b.

内側遠赤外線放射体23a,外側遠赤外線放射体23bには遠赤外線放射塗料を塗布し、内側,外側遠赤外線放射体23a,23bを通過した熱風は無数の小孔から左右に吹き出し、集穀室4の左右穀粒流下通路9,9を流下する穀粒に遠赤外線放射熱を浴びせ穀粒の乾燥を促進させる。   A far-infrared radiation paint is applied to the inner far-infrared radiator 23a and the outer far-infrared radiator 23b, and the hot air that has passed through the inner and outer far-infrared radiators 23a and 23b is blown from the countless small holes to the left and right, The left and right grain flow passages 9, 9 are subjected to far-infrared radiant heat to promote the drying of the grains.

バーナ5で生成された熱風はバーナ送風ファン(図示省略)の圧風作用,吸引排気ファン7の吸引作用で内側遠赤外線放射体23a,外側遠赤外線放射体23bを通過し熱風室6内に熱風として供給される。次いで、熱風は左右穀粒流下通路9,9,左右排風室8,8を流れながら穀粒を乾燥し、吸引排気ファン7により機外へ吸引排出される。   The hot air generated by the burner 5 passes through the inner far-infrared radiator 23a and the outer far-infrared radiator 23b by the pressure air action of the burner blower fan (not shown) and the suction action of the suction exhaust fan 7, and passes through the hot air chamber 6 into the hot air chamber 6. Supplied as Subsequently, the hot air dries the grain while flowing through the left and right grain flow down passages 9 and 9 and the left and right exhaust air chambers 8 and 8, and is sucked and discharged outside the apparatus by the suction exhaust fan 7.

また、図1,図8に示すように、バーナ風胴25の上方にコントロールボックス35を設け、コントロールボックス35の前側面に操作盤36を設けている。操作盤36には、図3に示すように、張り込み運転用の張込スイッチSW1,通風乾燥運転用の通風スイッチSW2,熱風乾燥運転用の乾燥スイッチSW3,穀物排出運転用の排出スイッチSW4,運転停止用の停止スイッチSW5,緊急停止スイッチSW6を設けている。   As shown in FIGS. 1 and 8, a control box 35 is provided above the burner wind tunnel 25, and an operation panel 36 is provided on the front side surface of the control box 35. As shown in FIG. 3, the operation panel 36 includes a tension switch SW1 for tension operation, a ventilation switch SW2 for ventilation drying operation, a drying switch SW3 for hot air drying operation, a discharge switch SW4 for grain discharge operation, and an operation. A stop switch SW5 for stopping and an emergency stop switch SW6 are provided.

操作盤36には運転表示画面36aを設け、乾燥運転中の検出熱風温度,測定水分値,乾燥運転終了までの残時間などを順次切換え表示するようにしている。
また、操作盤36の操作パネル36bには、図4に示すように穀物種類を設定する穀物種類スイッチSW7,張込量を設定する張込量スイッチSW8,到達目標水分値を設定する水分スイッチSW9,乾燥速度を設定する乾燥速度スイッチSW10,乾燥モードを設定する乾燥モードスイッチSW11,水分値の戻りを補正する水分戻り補正スイッチSW12を設け、これらスイッチの右側に設定内容を表示する表示部をそれぞれ設けている。
The operation panel 36 is provided with an operation display screen 36a for sequentially switching and displaying the detected hot air temperature during the drying operation, the measured moisture value, the remaining time until the end of the drying operation, and the like.
Further, as shown in FIG. 4, the operation panel 36b of the operation panel 36 has a grain type switch SW7 for setting the grain type, an overhang amount switch SW8 for setting the overhang amount, and a moisture switch SW9 for setting the reaching target moisture value. , A drying speed switch SW10 for setting the drying speed, a drying mode switch SW11 for setting the drying mode, and a moisture return correction switch SW12 for correcting the return of the moisture value, and a display unit for displaying the setting contents on the right side of these switches. Provided.

なお、穀物乾燥機には熱風室6内の温度を検出する熱風温度検出センサSE1,排風室8内の温度を検出する排気温度センサSE2,外気温度を検出する外気温度センサSE3,外気湿度を検出する外気湿度センサSE4,穀物流下通路9を流下中の穀物温度を検出する穀温センサSE5を設けている。   The grain dryer has a hot air temperature detection sensor SE1 for detecting the temperature in the hot air chamber 6, an exhaust temperature sensor SE2 for detecting the temperature in the exhaust air chamber 8, an outside air temperature sensor SE3 for detecting the outside air temperature, and an outside air humidity. An outside air humidity sensor SE4 to detect and a grain temperature sensor SE5 to detect the temperature of the grain flowing down through the grain flow passage 9 are provided.

コントロールボックス35には制御部38を設け、図6に示すように、制御部38の入力側には各種スイッチ,センサ類を接続し、出力側には、出力回路,駆動回路を経由して吸引排気ファンモータ(図示省略),昇降機モータ29,繰出バルブモータ(図示省略),バーナ駆動手段(図示省略),水分計駆動手段(図示省略),運転状態を表示する張込み表示ランプL1,通風表示ランプL2,乾燥表示ランプL3,排出表示ランプL4などを接続している。   The control box 35 is provided with a control unit 38. As shown in FIG. 6, various switches and sensors are connected to the input side of the control unit 38, and suction is performed on the output side via an output circuit and a drive circuit. Exhaust fan motor (not shown), elevator motor 29, feed valve motor (not shown), burner driving means (not shown), moisture meter driving means (not shown), tension display lamp L1 for displaying the operating state, ventilation display The lamp L2, the dry display lamp L3, the discharge display lamp L4, and the like are connected.

次に、穀物乾燥機の乾燥運転の概要について説明する。
オペレータが張込スイッチSW1を操作すると、昇降機11,上部ラセン16が駆動され張込穀粒が順次貯溜室2に張り込まれる。張込運転が終了すると、オペレータは張込量スイッチSW8を操作し張込穀粒量を設定する(張込量検出手段(図示省略)で張込量を自動検出し自動設定するようにしてもよい)。次いで、水分スイッチSW9を操作し到達目標水分値(例えば14%)を設定し、次いで、穀物スイッチSW7を操作し乾燥対象穀物を設定し、乾燥速度スイッチSW10を操作し乾燥速度を設定し、乾燥モードスイッチSW11を操作し通風乾燥,休止乾燥の有無を設定し乾燥モードを設定する。
Next, an outline of the drying operation of the grain dryer will be described.
When the operator operates the tension switch SW <b> 1, the elevator 11 and the upper spiral 16 are driven, and the tension grains are sequentially tensioned in the storage chamber 2. When the tensioning operation is completed, the operator operates the tensioning amount switch SW8 to set the tensioning grain amount (even if the tensioning amount detecting means (not shown) automatically detects and sets the tensioning amount). Good). Next, the moisture switch SW9 is operated to set the target moisture value (for example, 14%), then the grain switch SW7 is operated to set the grain to be dried, the drying speed switch SW10 is operated to set the drying speed, and the drying is performed. The mode switch SW11 is operated to set the presence / absence of ventilation drying and pause drying to set the drying mode.

次いで、乾燥スイッチSW3を操作すると、制御部38の熱風乾燥作業指令に基づきバーナ5が燃焼を開始し、繰出バルブ10,下部ラセン14,昇降機11,上部ラセン16の循環系の駆動が開始し、熱風乾燥作業が開始される。次いで、穀粒張込量,設定乾燥速度,水分計26の測定穀物水分値,検出外気温度などの条件によりバーナ5の燃焼量が調節されつつ熱風乾燥運転を実行し、水分計26の測定水分値が設定乾燥目標水分値に到達すると、バーナ5の燃焼を停止し循環系の駆動を停止し乾燥運転を終了する。   Next, when the drying switch SW3 is operated, the burner 5 starts burning based on the hot air drying operation command of the control unit 38, and the driving of the circulation system of the feeding valve 10, the lower spiral 14, the elevator 11, and the upper spiral 16 is started. Hot air drying operation is started. Next, a hot air drying operation is performed while the amount of combustion of the burner 5 is adjusted according to conditions such as the amount of grain inserted, the set drying speed, the measured grain moisture value of the moisture meter 26, and the detected outside air temperature, and the measured moisture content of the moisture meter 26 When the value reaches the set drying target moisture value, the combustion of the burner 5 is stopped, the driving of the circulation system is stopped, and the drying operation is ended.

次に、図7に基づき熱風乾燥作業の終了後の水分値戻り補正制御について説明する。
穀物乾燥機に乾燥穀物が張り込まれ(ステップS1)、オペレータの水分スイッチSW9の設定操作により乾燥目標水分値が設定され,張込量スイッチSW8の操作により張込み穀物量が設定され,乾燥速度スイッチSW10の操作により乾燥速度が設定され、乾燥モードスイッチSW11の操作により乾燥モードが設定される(ステップS2)。
Next, the moisture value return correction control after the hot air drying operation is completed will be described with reference to FIG.
The dried grain is put into the grain dryer (step S1), the drying target moisture value is set by the setting operation of the moisture switch SW9 by the operator, the amount of the putting grain is set by the operation of the setting amount switch SW8, and the drying speed is set. The drying speed is set by operating the switch SW10, and the drying mode is set by operating the drying mode switch SW11 (step S2).

次いで、オペレータの乾燥スイッチSW3のオン操作により(ステップS3)、制御部38の熱風乾燥作業開始指令に基づきバーナ5を点火し熱風乾燥作業を開始する(ステップS4)。次いで、乾燥作業が進行し水分計26の測定水分値が乾燥目標水分値に到達すると(ステップS5)、熱風乾燥運転を終了する(ステップS6)。   Next, when the operator turns on the drying switch SW3 (step S3), the burner 5 is ignited based on the hot air drying work start command of the control unit 38 and the hot air drying work is started (step S4). Next, when the drying operation proceeds and the measured moisture value of the moisture meter 26 reaches the drying target moisture value (step S5), the hot air drying operation is terminated (step S6).

次いで、乾燥運転開始前または乾燥運転終了後にオペレータが水分戻り補正スイッチSW12をオンし水分戻り補正制御を選択している場合には(ステップS7)、制御部38の水分戻り補正制御指令に基づき所定時間毎に吸引排気フアン7の駆動を停止あるいは駆動した状態で機内穀粒を循環する循環運転を開始し、水分計26の測定水分値を運転表示画面36aに表示しながら穀物張込み量と循環量とから機内穀物が1循環終了する間に所定時間毎に複数回の水分値を測定し平均水分値を算出する(ステップS8)。   Next, when the operator turns on the moisture return correction switch SW12 and selects moisture return correction control before starting the drying operation or after finishing the drying operation (step S7), a predetermined value is determined based on the moisture return correction control command of the control unit 38. The circulation operation is started to circulate the in-machine grain with the suction / exhaust fan 7 being stopped or driven every time, and the measured amount of moisture measured by the moisture meter 26 is displayed on the operation display screen 36a, and the amount of cereal filling and the circulation. Based on the amount, the moisture value is measured a plurality of times at predetermined time intervals during the end of one cycle of the in-machine grain, and the average moisture value is calculated (step S8).

次いで、平均水分値が所定水分値以上乾燥目標水分値より高い場合には(ステップS9)、前記通風循環乾燥運転を実行し(ステップS10)、ステップ9に戻る。
また、ステップ9で平均測定水分値が乾燥目標水分値より高くない場合には(ステップS9)、オペレータにより停止スイッチSW5または排出スイッチSW4がオンされている場合には(ステップS11)、水分戻り補正制御を終了し、乾燥作業を終了する。また、オペレータにより停止スイッチSW5または排出スイッチSW4がオンされていない場合には(ステップS11)、前記ステップ8に戻る。
Next, when the average moisture value is higher than the predetermined moisture value and higher than the drying target moisture value (step S9), the ventilation circulation drying operation is executed (step S10), and the process returns to step 9.
If the average measured moisture value is not higher than the drying target moisture value in step 9 (step S9), if the stop switch SW5 or the discharge switch SW4 is turned on by the operator (step S11), the moisture return correction is performed. Control is terminated and the drying operation is terminated. If the stop switch SW5 or the discharge switch SW4 is not turned on by the operator (step S11), the process returns to step 8.

また、前記水分戻り補正制御において、例えば水分戻り補正制御の実行間隔を設定できる水分戻り補正制御時間設定スイッチ(図示省略)を設け、制御部38の水分戻り補正制御実行時間間隔を、例えば1時間毎あるいは3時間毎と測定間隔を設定できるようにしてもよい。このようにすると、種々の天候に応じて保管時の穀物の水分値を安定させて保持することができる。   In the moisture return correction control, for example, a moisture return correction control time setting switch (not shown) that can set an execution interval of moisture return correction control is provided, and the moisture return correction control execution time interval of the control unit 38 is set to 1 hour, for example. The measurement interval may be set every 3 hours or every 3 hours. If it does in this way, according to various weathers, the moisture value of the grain at the time of storage can be stabilized and held.

また、前記水分戻り補正制御において、吸引排気フアン7の駆動停止状態あるいは駆動状態で機内の穀物を循環する循環運転を開始し、穀物1循環中における測定平均水分値が乾燥目標水分値より所定水分値以上高い場合に追い乾燥作業を実行するにあたり、乾燥目標水分値より高い所定水分値を例えば上下2段階に区分し、乾燥目標水分値以上で目標水分値に近い場合には通風循環乾燥を実行し、乾燥目標水分値以上で目標水分値から離れて高い場合にはバーナ燃焼による熱風乾燥運転を実行するようにしてもよい。このようにすると、外気湿度や未熟米の多い穀物による水分値の戻りを確実に抑制することができる。   In the moisture return correction control, the circulation operation for circulating the grain in the machine is started in the driving stop state or the driving state of the suction exhaust fan 7, and the measured average moisture value in the circulation of the grain 1 is the predetermined moisture value from the drying target moisture value. When the additional drying operation is performed when the value is higher than the value, the predetermined moisture value higher than the drying target moisture value is divided into two stages, for example, upper and lower, and if the drying moisture value is higher than the target moisture value and close to the target moisture value, ventilation circulation drying is executed. However, when it is equal to or higher than the drying target moisture value and is far from the target moisture value, a hot air drying operation by burner combustion may be executed. If it does in this way, return of the moisture value by grain with much outside air humidity or immature rice can be controlled certainly.

また、次のように構成してもよい。前記水分戻り補正制御を備えた穀物乾燥機において、熱風乾燥運転の終了後にオペレータが水分スイッチSW9を操作し乾燥目標水分値を下げ設定した場合には、制御部38の追い乾燥運転機能に基づき乾燥運転終了時の水分値及び当該乾燥運転の乾減率から熱風乾燥運転あるいは通風循環乾燥の追い乾燥時間を設定し乾燥作業を開始する。そして、操作盤36の運転表示画面36aに追い乾燥運転開始時の内容(乾減率,設定追い乾燥時間)を表示し、追い乾燥の進行に伴い所定時間毎に測定水分値(あるいは前記乾減率で算出された推定水分値)を表示し、測定水分値が追い設定乾燥目標水分値に到達すると乾燥運転を終了する。   Moreover, you may comprise as follows. In the grain dryer equipped with the moisture return correction control, when the operator operates the moisture switch SW9 to lower the drying target moisture value after completion of the hot air drying operation, the drying is performed based on the additional drying operation function of the control unit 38. From the moisture value at the end of the operation and the drying rate of the drying operation, the additional drying time of the hot air drying operation or the circulation circulation drying is set and the drying operation is started. Then, the contents (drying rate, set additional drying time) at the start of the additional drying operation are displayed on the operation display screen 36a of the operation panel 36, and the measured moisture value (or the aforementioned decreased drying value) is determined every predetermined time as the additional drying progresses. When the measured moisture value reaches the additional drying target moisture value, the drying operation is terminated.

前記構成によると、オペレータの追い乾燥の設定操作を簡単化し利便性を向上させることができる。
また、乾燥自動運転手段を備えた穀物乾燥機において、乾燥運転開始時の測定水分値と乾燥目標水分値とが所定水分値(例えば3%)以下の少ない場合には、自動でタイマ乾燥運転に入るようにし、所定の乾減率から熱風乾燥運転時間あるいは通風循環乾燥時間を設定し乾燥運転を開始し、オペレータの利便性を向上するようにしてもよい。
According to the above configuration, it is possible to simplify the operator's additional drying setting operation and improve convenience.
In a grain dryer equipped with automatic drying operation means, if the measured moisture value at the start of the drying operation and the target moisture value are less than a predetermined moisture value (eg 3%), the timer drying operation is automatically performed. It is possible to improve the convenience for the operator by setting the hot air drying operation time or the ventilation circulation drying time from a predetermined drying rate and starting the drying operation.

また、乾燥運転の終了後にオペレータが水分スイッチSW9を操作し乾燥目標水分値を下げ設定した場合には、制御部38の追い乾燥運転機能に基づき乾燥運転終了時の水分値及び当該乾燥運転の乾減率から熱風乾燥運転あるいは通風循環乾燥の追い乾燥時間を設定し乾燥作業を開始し、操作盤36の運転表示画面36aに追い乾燥運転の内容を表示し、測定水分値が追い乾燥で設定した乾燥目標水分値に到達すると乾燥運転を終了するようにしてもよい。   In addition, when the operator operates the moisture switch SW9 to set the drying target moisture value to a lower value after the drying operation is completed, the moisture value at the end of the drying operation and the drying value of the drying operation are set based on the additional drying operation function of the control unit 38. The additional drying time of hot air drying operation or circulation circulation drying is set from the rate of decrease, and the drying operation is started. The content of the additional drying operation is displayed on the operation display screen 36a of the operation panel 36, and the measured moisture value is set by additional drying. When the drying target moisture value is reached, the drying operation may be terminated.

次に、図9の穀物乾燥調製設備51の穀物乾燥機への穀物張込み構成について説明する。
穀物乾燥調製設備51には複数の穀物乾燥機52A,52B,52Cと、穀物張込ピット53を備え、コンバイン(図示省略)で収穫した穀物を穀物張込ピット53のエレベータ54から複数の穀物乾燥機52A,52B,52Cに張込み可能に構成している。
Next, a configuration of cereal grain insertion in the grain dryer of the grain drying preparation facility 51 of FIG. 9 will be described.
The grain drying preparation facility 51 includes a plurality of grain dryers 52A, 52B, 52C and a grain embedding pit 53, and the grains harvested by the combiner (not shown) are dried from the elevator 54 of the grain embedding pit 53 to a plurality of grains. The machine 52A, 52B, 52C is configured to be able to be stretched.

穀物乾燥調整設備51には運転制御用のコントローラ(図示省略)を備えていて、複数の穀物乾燥機52A,52B,52Cの乾燥運転を制御し、エレベータ53の搬送方向を複数の穀物乾燥機に切換えできるようにしている。   The grain drying adjustment equipment 51 includes a controller (not shown) for operation control, controls the drying operation of the plurality of grain dryers 52A, 52B, and 52C, and sets the conveying direction of the elevator 53 to the plurality of grain dryers. It can be switched.

また、前記コンバインには水分計を備え収穫穀物の水分値を測定できるようにし、例えば無線通信で測定した水分値を前記コントローラ(図示省略)に送信可能にしている。
コンバインから穀物張込ピット53へ穀物が搬入されエレベータ54で穀物乾燥機への張込が開始されると、コンバインから水分値情報(例えば水分値21%)がコントローラに送信され、次いで、コントローラから複数の穀物乾燥機52A,52B,52Cの中で当該水分値の最も近い水分値20%の穀物を乾燥している穀物乾燥機52Aへの搬送指令が出され、エレベータ54の搬送方向が切換えられ、穀物乾燥機52Aへ張込まれ乾燥作業中の穀物と一緒に乾燥作業がなされる。
Further, the combine is provided with a moisture meter so that the moisture value of the harvested cereal can be measured. For example, the moisture value measured by wireless communication can be transmitted to the controller (not shown).
When the grain is carried from the combine into the grain pit 53 and the elevator 54 starts to be fed into the grain dryer, the combine sends moisture value information (for example, a moisture value of 21%) to the controller. A conveyance command is issued to the grain dryer 52A, which is drying the grain having a moisture value of 20% closest to the moisture value among the plurality of grain dryers 52A, 52B, 52C, and the conveyance direction of the elevator 54 is switched. Then, the drying operation is performed together with the cereal being put into the grain dryer 52A and being dried.

前記構成によると、コンバインで収穫した穀物を複数の穀物乾燥機の中から乾燥水分値の近い穀物乾燥機に張込み一緒に乾燥することができ、水分むらを少なくしながら乾燥効率を高め迅速に乾燥することができる。   According to the above configuration, grains harvested with a combine can be dried together by putting them in a grain dryer with a dry moisture value close to one another from a plurality of grain dryers, and quickly increasing the drying efficiency while reducing moisture unevenness. Can be dried.

2 貯溜室
3 乾燥室
4 集穀室
5 バーナ
7 吸引排気ファン
10 繰出バルブ
11 昇降機
14 下部搬送装置
16 上部搬送装置
38 制御部
SW1 張込スイッチ
SW2 通風乾燥スイッチ
SW3 乾燥スイッチ
SW4 排出スイッチ
SW5 停止スイッチ
SW12 水分戻り補正操作手段(水分戻り補正スイッチ)
DESCRIPTION OF SYMBOLS 2 Reservoir 3 Drying room 4 Graining room 5 Burner 7 Suction exhaust fan 10 Feeding valve 11 Elevator 14 Lower conveyance device 16 Upper conveyance device 38 Control part SW1 Tension switch SW2 Ventilation drying switch SW3 Drying switch SW4 Discharge switch SW5 Stop switch SW12 Moisture return correction operation means (moisture return correction switch)

Claims (5)

バーナの生成する熱風で乾燥される穀物の水分値を水分計で測定し測定水分値が乾燥目標水分値に到達するとバーナの燃焼を停止し熱風乾燥作業を終了する乾燥作業終了制御手段を備えた穀物乾燥機において、前記乾燥作業終了制御手段に基づく乾燥作業の終了後において機内穀物を循環しながら水分値を測定し該測定水分値が前記乾燥作業終了時の乾燥目標水分値を上回る場合には、バーナの停止状態で且つ吸引排気フアンを駆動あるいは停止した循環乾燥作業を実行し、測定水分値が乾燥目標水分値に到達すると循環乾燥作業を停止する水分戻り補正制御手段を備えた穀物乾燥機。   Measured moisture content of grain dried with hot air generated by burner, and equipped with drying operation end control means to stop burning of burner and end hot air drying operation when measured moisture value reaches drying target moisture value In the grain dryer, when the moisture value is measured while circulating the grain in the machine after the drying operation based on the drying operation end control means is finished, and the measured moisture value exceeds the drying target moisture value at the end of the drying operation, Grain dryer equipped with moisture return correction control means for executing a circulation drying operation with the burner stopped and driving or stopping the suction exhaust fan and stopping the circulation drying operation when the measured moisture value reaches the drying target moisture value . 請求項1の発明において、前記水分戻り補正制御手段における戻り水分値の測定を機内穀物の1循環する間に複数回水分値を測定しその平均値により戻り水分値を算出することを特徴とする穀物乾燥機。   The invention according to claim 1 is characterized in that the water content is measured a plurality of times during one circulation of the in-machine grain during the measurement of the water content returned by the moisture return correction control means, and the return water value is calculated from the average value. Grain dryer. 請求項1又は請求項2の発明において、前記乾燥作業終了後において所定設定時間毎に前記水分戻り補正制御手段により水分値を測定し乾燥目標水分値に対する戻り水分値を確認することを特徴とする穀物乾燥機。   In the invention of claim 1 or 2, the moisture value is measured by the moisture return correction control means every predetermined set time after the drying operation is completed, and the return moisture value with respect to the drying target moisture value is confirmed. Grain dryer. 請求項1乃至請求項3のいずれかの発明において、前記乾燥作業終了後において前記水分戻り補正制御手段を自動的に実行する水分戻り補正操作手段を設けたことを特徴とする穀物乾燥機。   4. The grain dryer according to claim 1, further comprising a moisture return correction operation means for automatically executing the moisture return correction control means after completion of the drying operation. 請求項1乃至請求項3のいずれかの発明において、前記水分戻り補正制御手段の実行時における戻り水分値の測定にあたり乾燥目標水分値よりも設定水分値以上の高い戻りがある場合には、前記循環乾燥作業に代えてバーナを燃焼した熱風乾燥作業を開始するようにしたことを特徴とする穀物乾燥機。   In the invention according to any one of claims 1 to 3, when the return moisture value is measured when the moisture return correction control means is executed, when there is a return higher than a set moisture value than the dry target moisture value, A grain dryer characterized in that a hot air drying operation in which a burner is burned is started instead of a circulation drying operation.
JP2014189163A 2014-09-17 2014-09-17 Dry preparation equipment Expired - Fee Related JP6492477B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109271712A (en) * 2018-09-25 2019-01-25 北京石油化工学院 A kind of Moisture Method during segmented is dry

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Publication number Priority date Publication date Assignee Title
JPS61205777A (en) * 1985-03-07 1986-09-11 金子農機株式会社 Automatic mixing drying method and device in cereal common drying facility
JPH02233987A (en) * 1989-03-03 1990-09-17 Yamamoto Mfg Co Ltd Controller of grain dryer
JPH06201262A (en) * 1993-01-07 1994-07-19 Yanmar Agricult Equip Co Ltd Drier mainly for grain
JP2006254758A (en) * 2005-03-16 2006-09-28 Yanmar Co Ltd Field crop harvest processing system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61205777A (en) * 1985-03-07 1986-09-11 金子農機株式会社 Automatic mixing drying method and device in cereal common drying facility
JPH02233987A (en) * 1989-03-03 1990-09-17 Yamamoto Mfg Co Ltd Controller of grain dryer
JPH06201262A (en) * 1993-01-07 1994-07-19 Yanmar Agricult Equip Co Ltd Drier mainly for grain
JP2006254758A (en) * 2005-03-16 2006-09-28 Yanmar Co Ltd Field crop harvest processing system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109271712A (en) * 2018-09-25 2019-01-25 北京石油化工学院 A kind of Moisture Method during segmented is dry

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