JPH0439596B2 - - Google Patents
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- Publication number
- JPH0439596B2 JPH0439596B2 JP61018875A JP1887586A JPH0439596B2 JP H0439596 B2 JPH0439596 B2 JP H0439596B2 JP 61018875 A JP61018875 A JP 61018875A JP 1887586 A JP1887586 A JP 1887586A JP H0439596 B2 JPH0439596 B2 JP H0439596B2
- Authority
- JP
- Japan
- Prior art keywords
- grain
- grains
- temperature
- drying
- hot air
- 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
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- 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、循環型穀物乾燥機を用い穀粒を循環
させながら熱風を浴せて乾燥させる穀物乾燥方法
についての改良に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an improvement in a grain drying method in which grains are dried by being exposed to hot air while being circulated using a circulating grain dryer.
[従来の技術]
循環型穀物乾燥機Aは、通常、第1図に示して
いるように、箱状に形成した機体aの内部の上半
側に乾燥すべき穀粒を張込む穀槽1を装設し、そ
の機体aの底部に、前記穀槽1の底部の排出口か
ら排出量を制御して穀粒を排出せしめる回転シヤ
ツター2と、その回転シヤツター2で排出される
穀粒を機体aの外に排出するための下部コンベア
3とを装設し、機体aの外面側に前記下部コンベ
ア3で排出されてくる穀粒を揚穀する昇降機4
(バケツトエレベーター)を立設し、機体aの上
部に前記昇降機4で揚送した穀粒を穀槽内の上部
に投入する上部コンベア5を装設し、また、機体
a内の下部側に寄せた中間部位で、穀槽1の底部
を占める部位には、その穀槽1の底部を横切るよ
うに乾燥風(熱風)を送給する導風路6と、その
導風路6から吹出して乾燥部となる穀槽1の底部
を横切つた排風を機外に導く排風路(図面では明
示していない)と、その排風路に連通する排風ダ
クト7とを装設し、前記導風路6の入口に前記乾
燥風を生成する熱風生成装置(バーナー装置)8
を配設し、前記排風ダクト7には送風機9を配設
して構成してある。[Prior Art] As shown in FIG. 1, a circulating grain dryer A normally has a grain tank 1 in which grains to be dried are placed inside the upper half of a box-shaped body a. A rotary shutter 2 is installed at the bottom of the machine body a to control the discharge amount and discharge grains from the discharge port at the bottom of the grain tank 1, and a rotary shutter 2 is installed at the bottom of the machine body a, and the grains discharged by the rotary shutter 2 are transported to the machine body. An elevator 4 is installed with a lower conveyor 3 for discharging the grains to the outside of the machine body a, and lifts the grains discharged by the lower conveyor 3 on the outer surface side of the machine body a.
(bucket elevator) is installed in the upper part of the machine a, and an upper conveyor 5 is installed on the upper part of the machine a to feed the grains lifted by the elevator 4 into the upper part of the grain tank. The intermediate part of the grain tank 1 that occupies the bottom of the grain tank 1 has an air guide path 6 that sends dry air (hot air) across the bottom of the grain tank 1, and an air guide path 6 that blows out from the air guide path 6. It is equipped with an exhaust passage (not clearly shown in the drawing) that guides the exhaust air that crosses the bottom of the grain tank 1 serving as the drying part to the outside of the machine, and an exhaust duct 7 that communicates with the exhaust passage. a hot air generating device (burner device) 8 that generates the drying air at the entrance of the air guide path 6;
The exhaust duct 7 is provided with a blower 9.
そして、この循環型穀物乾燥機Aを用いて穀粒
を乾燥するときは、まず、熱風生成装置8および
回転シヤツター2の作動を停めた状態で、機体a
の底部側面に設けてある張込口から下部コンベア
3に穀粒を送給するか、昇降機4の底部に設けて
ある張込口から穀粒を供給して、下部コンベア
3、昇降機4、上部コンベア5等の作動により穀
槽1内に所定量の穀粒を張込み、次いでその状態
から、回転シヤツター2および前記下部コンベア
3、昇降機4、上部コンベア5等の送穀装置を作
動させて穀槽1内の穀粒を循環させるとともに、
熱風生成装置8及び送風機9を作動させて、その
循環流動する穀粒に熱風(乾燥風)を浴せ、この
循環型穀物乾燥機Aを運転・稼動した状態を、所
定時間続けることで乾燥作業を行なうようにして
いる。 When drying grains using this circulating grain dryer A, first, with the operation of the hot air generator 8 and the rotary shutter 2 stopped,
The grains are fed to the lower conveyor 3 from the loading port provided on the side of the bottom of the elevator 4, or the grains are fed from the loading port provided at the bottom of the elevator 4 to the lower conveyor 3, the elevator 4, and the upper portion. A predetermined amount of grain is loaded into the grain tank 1 by operating the conveyor 5, and then from this state, the rotary shutter 2 and grain feeding devices such as the lower conveyor 3, elevator 4, and upper conveyor 5 are operated to produce grain. While circulating the grains in tank 1,
Drying work is carried out by activating the hot air generator 8 and the blower 9 to blow hot air (drying air) onto the circulating grains, and by continuing to operate the circulating grain dryer A for a predetermined period of time. I try to do this.
[発明が解決しようとする課題]
ところで、このように循環型穀物乾燥機Aを用
いて行なう穀粒の乾燥手段には、乾燥作業中にお
いて時間の経過とともに穀粒の乾燥が進行してく
るに従い乾燥効率が低下してくることと、穀粒の
変質をさけるために循環流動する穀粒に対して浴
びせる熱風の温度を高くし得ないことで、通常12
時間前後の比較的長い作業時間をかけるようにし
ていることから、能率が上らない問題がある。[Problems to be Solved by the Invention] By the way, the means for drying grains using the circulating grain dryer A has a problem in that as the drying of the grains progresses over time during the drying operation. Normally, drying efficiency decreases, and the temperature of the hot air applied to circulating grains cannot be increased to avoid deterioration of the grains.
There is a problem that efficiency cannot be improved because the work takes a relatively long time before and after the scheduled time.
本発明は、この問題を解消せしめるためになさ
れたものであつて、穀粒に変質を生ぜしめること
なく循環型穀物乾燥機を用いて能率のよい乾燥が
行なえる新たな乾燥方法を提供することを目的と
する。 The present invention has been made to solve this problem, and the object is to provide a new drying method that can perform efficient drying using a circulating grain dryer without causing deterioration of grains. With the goal.
[課題を解決するための手段]
しかして、本発明は上述の目的を達成するため
に種々の研究と実験を重ねて得られた知見に基づ
いてなされたものである。[Means for Solving the Problems] The present invention has been made based on knowledge obtained through various studies and experiments in order to achieve the above-mentioned objects.
即ち、上述の乾燥手段において、乾燥行程の進
行で穀粒が乾燥してくるに伴ない次第に乾燥効率
が低下してくるのは、乾燥の進行に伴ない穀粒の
堆積状態が密になつてくることにより通風抵抗が
増加してくることによるものであることが判つた
ことから、乾燥行程の進行により穀粒の含水率が
低下してくるのに伴ない穀粒の循環系の送穀装置
の送穀速度を増加させて、循環回数が多くなるよ
うにしたところ、乾燥部となる前記熱風が吹抜け
る部位における穀粒の堆積状態が、送穀速度の増
大で疎になつてくることで通風抵抗が減少して乾
燥効率が良くなつて、乾燥能率を上げ得るように
なり、同時に、乾燥行程中の穀温の上昇が抑えら
れるという結果を得た。そして、この循環速度を
増大させることによる穀温の上昇の抑制は、第2
図の実験結果の図表にあきらかなように、略一定
の循環速度で穀粒を循環させながら熱風を浴びせ
る従前の乾燥方法において、穀温の上昇がその穀
粒に品質の低下をきたさない範囲の上限に抑えら
れるように熱風温度を設定して穀粒の乾燥を行な
う場合の理想の穀温変化のカーブよりも、!?か
に低い穀温変化のカーブとなつた。 That is, in the above-mentioned drying means, the drying efficiency gradually decreases as the grains dry as the drying process progresses because the grains become denser as the drying progresses. As the moisture content of grains decreases as the drying process progresses, the grain feeding device of the grain circulation system increases. When the grain feeding speed was increased to increase the number of circulations, the accumulation of grains in the area where the hot air blows through, which is the drying part, became sparse due to the increase in the grain feeding speed. The results showed that the ventilation resistance was reduced and the drying efficiency was improved, making it possible to increase the drying efficiency and at the same time suppressing the rise in grain temperature during the drying process. Suppression of the increase in grain temperature by increasing this circulation speed is the second
As is clear from the diagram of the experimental results shown in the figure, in the conventional drying method in which hot air is applied to the grains while circulating them at a substantially constant circulation rate, the increase in grain temperature does not cause a decrease in the quality of the grains. The grain temperature change curve was much lower than the ideal grain temperature change curve when grains were dried by setting the hot air temperature to the upper limit.
このことは、循環型穀物乾燥機により穀粒を循
環させながら熱風を浴びせて穀粒を乾燥させる
際、その穀粒の循環速度を、乾燥行程中の穀粒の
乾燥の進行に伴ない増大させる場合には、穀温が
従前手段における理想の穀温カーブになるまで
は、供給する熱風温度を上昇させてよいというこ
とである。 This means that when a circulating grain dryer dries grains by blowing hot air while circulating them, the circulation speed of the grains increases as the grains dry during the drying process. In this case, the temperature of the supplied hot air may be increased until the grain temperature reaches the ideal grain temperature curve in the conventional means.
そこで、穀粒の循環速度を、穀粒の乾燥の進行
に伴ない増大させながら、それにより生ずる穀温
の低下を埋めるように供給する熱風温度を上昇せ
しめて乾燥を行なつたところ、通風抵抗の減少と
熱風温度の上昇とで、著しく乾燥効率が上昇し
て、穀粒に品質の劣化を生ぜしめることなく乾燥
行程を短縮し得る結果が得られたことから、本発
明においては、上述の目的を達成するための手段
として、循環型穀物乾燥機を用い穀粒を循環させ
ながら熱風を浴びせて乾燥させる穀粒の乾燥方法
において、乾燥行程中における穀粒の乾燥の進行
により穀粒の含水率が低下してくるに従い穀粒の
循環速度を増大させるとともに、穀粒に浴びせる
熱風の温度を、穀粒の循環速度の増大により生ず
る穀温の低下を埋めるように上昇せしめて穀粒を
乾燥せしめることを特徴とする循環型穀物乾燥機
を用いる穀粒の乾燥方法を提起するものである。 Therefore, when drying was carried out by increasing the circulation speed of the grains as the grains dried, and by increasing the temperature of the hot air supplied to compensate for the resulting drop in grain temperature, we found that the ventilation resistance The reduction in drying efficiency and the increase in hot air temperature significantly increased the drying efficiency, resulting in the shortening of the drying process without causing quality deterioration of the grains. Therefore, in the present invention, the above-mentioned As a means to achieve this purpose, in a grain drying method that uses a circulating grain dryer to dry the grains by blowing hot air while circulating the grains, moisture content of the grains is reduced by the progress of drying of the grains during the drying process. As the grain circulation speed decreases, the grain circulation speed is increased, and the temperature of the hot air applied to the grains is increased to compensate for the drop in grain temperature caused by the increase in the grain circulation speed, thereby drying the grains. The present invention proposes a method for drying grain using a circulating grain dryer characterized by drying.
[実施例]
次に実施例を図面に従い詳述する。なお、図面
符号は、同効の構成部材については従前手段のも
のと同一の符号を用いる。[Example] Next, an example will be described in detail with reference to the drawings. Note that the same reference numerals as in the previous means are used for constituent members having the same effect.
第3図において、aは機体、1はその機体aに
装設せる穀槽、2はその穀槽1の底部に形成せる
乾燥部(図面にては明示していない)の下端の排
出口に軸架した回転シヤツター、3はその回転シ
ヤツター2の下方に配設せる下部コンベア、4は
機体aの外面に装設せる昇降機、5は上部コンベ
ア、5aは上部コンベア5の回転軸に伝導して回
転する均分機、6は熱風の導風路、7は排風路に
通ずる排風ダクト、8は導風路6の入口部位に設
けたバーナー装置よりなる熱風生成装置、9は排
風ダクト7に設けた送風機、10は除塵機、Pは
前記熱風生成装置8の燃料供給ポンプをそれぞれ
示す。 In Fig. 3, a is the fuselage, 1 is a grain tank installed in the fuselage a, and 2 is an outlet at the lower end of a drying section (not clearly shown in the drawing) formed at the bottom of the grain tank 1. 3 is a lower conveyor installed below the rotating shutter 2; 4 is an elevator installed on the outer surface of the machine body a; 5 is an upper conveyor; A rotating equalizer, 6 a hot air guide path, 7 an air exhaust duct communicating with the air exhaust path, 8 a hot air generation device consisting of a burner device provided at the entrance of the air guide path 6, 9 an exhaust duct 7 10 is a dust remover, and P is a fuel supply pump for the hot air generating device 8, respectively.
また、Wは前記穀槽1から回転シヤツター2→
下部コンベア3→昇降機4→上部コンベア5→穀
槽1の順に循環する穀粒の循環系路から穀粒をサ
ンプリングして水分値(含水率)を検出するよう
装設した水分値検出装置、M1は前述の送風機9
を駆動するモーター、M2は下部コンベア3を駆
動するモーター、M3は昇降機4の揚穀塔4a内
のバケツトコンベア4b及び上部コンベア5なら
びに均分機5aを駆動するモーター、M4は回転
シヤツター2を駆動するモーター、M5は前述の
水分値検出装置Wを駆動するモーター、M6は昇
降機4の揚穀塔4aの上部の放出筒部に装設せる
取出樋4cと前述の上部コンベアとを、前記放出
筒部に対し交互に連通するように切換える切換シ
ヤツター4bを作動せしめるモーター、M7は除
塵機10を駆動するモーター、M8は熱風生成装
置8のバーナーフアンを駆動するモーター、M9
は熱風生成装置8の燃料供給ポンプPの駆動用モ
ーターを示し、これらモーターは、機体aの外面
側の適宜の場所に設けられるコントロールボツク
スb内の制御回路で制御される。 In addition, W is from the grain tank 1 to the rotary shutter 2→
Moisture value detection device M1 installed to sample grains from a circulation system path of grains circulating in the order of lower conveyor 3 → elevator 4 → upper conveyor 5 → grain tank 1 and detect the moisture value (moisture content). is the aforementioned blower 9
M2 is a motor that drives the lower conveyor 3, M3 is a motor that drives the bucket conveyor 4b in the grain lifting tower 4a of the elevator 4, the upper conveyor 5, and the equalizer 5a, M4 is the motor that drives the rotary shutter 2. M5 is a motor that drives the above-mentioned moisture value detection device W, M6 is a motor that drives the above-mentioned upper conveyor and the take-out gutter 4c installed in the upper discharge cylinder part of the grain lifting tower 4a of the elevator 4, and the above-mentioned upper conveyor. M7 is a motor that drives the dust remover 10; M8 is a motor that drives the burner fan of the hot air generator 8; M9 is a motor that drives the burner fan of the hot air generator 8;
1 shows a motor for driving the fuel supply pump P of the hot air generator 8, and these motors are controlled by a control circuit in a control box b provided at an appropriate location on the outer surface of the aircraft body a.
また、S1は外気温を検出するよう機体aの外
面に装設せるサーミスタ等よりなる外気温セン
サ、S2は熱風生成装置8で生成して導風路6に
送給される熱風温度を検出するよう導風路6内に
配設せるサーミスタ等よりなる熱風温センサ、S
3は穀槽1内の穀粒の温度を検出するよう穀槽1
の貯留部に配設したサーミスタ等よりなる穀温セ
ンサ、S4は穀槽1の乾燥部を吹抜けた熱風の排
風の温度を検出するよう排風ダクト7(または排
風路)に設けたサーミスタ等よりなる排風温セン
サ、S5は穀槽1内に張込まれた穀粒の量を検出
するよう穀槽1の内壁面に装設せるレベルスイツ
チ等よりなる穀物量センサ、S6は水分値検出装
置Wがサンプリングする穀粒の水分値を検出する
よう該水分値検出装置W内に装設せるロール電極
などよりなる水分検出センサを示し、これらは前
記コントロールボツクスb内の制御回路に接続し
ている。 Further, S1 is an outside temperature sensor including a thermistor or the like installed on the outer surface of the aircraft body a to detect the outside temperature, and S2 is an outside temperature sensor that detects the temperature of the hot air generated by the hot air generation device 8 and sent to the air guide path 6. A hot air temperature sensor consisting of a thermistor etc. disposed in the air guide path 6, S
3 is installed in grain tank 1 to detect the temperature of grains in grain tank 1.
S4 is a thermistor installed in the air exhaust duct 7 (or air exhaust path) to detect the temperature of the hot air that has blown through the drying area of the grain tank 1. S5 is a grain amount sensor including a level switch installed on the inner wall of the grain tank 1 to detect the amount of grain loaded in the grain tank 1, and S6 is a moisture value. A moisture detection sensor consisting of a roll electrode or the like is installed in the moisture value detection device W so as to detect the moisture value of the grain sampled by the detection device W, and these are connected to the control circuit in the control box b. ing.
第4図は前記コントロールボツクスbの正面図
で、D1は穀物温度の設定用のダイヤル、D2は
乾燥しようとする穀物の種類を、例えば、稲・麦
等と変更したときに、その穀粒に適応する条件で
乾燥が行なえるように切換える穀物種類設定ダイ
ヤル、D3は仕上水分値を設定する仕上水分設定
ダイヤルを示す。 Fig. 4 is a front view of the control box b, where D1 is a dial for setting the grain temperature, and D2 is a dial for setting the grain temperature, and D2 is a dial for setting the grain temperature. A grain type setting dial is used to change the grain type so that drying can be performed under suitable conditions, and D3 is a finishing moisture setting dial that sets the finishing moisture value.
次に第5図は、前記コントロールボツクスb内
に設けられる循環速度制御用の制御回路のブロツ
ク図を示す。 Next, FIG. 5 shows a block diagram of a control circuit for controlling the circulation speed provided in the control box b.
同図において、S6は前述の水分値検出装置W
の水分検出センサ、K1は前記水分検出センサS
6から送り出される信号により穀物水分値(含水
率)の信号に変換する穀物水分検出回路、K2は
前記穀物水分検出回路K1から送り出される穀物
水分値の信号から所定のパターンに従い穀物の循
環量を演算するコンピユーターを組込んだ循環量
設定演算回路、K3は前記循環量設定演算回路K
2から送り出される設定信号に従い下部コンベア
3・昇降機4・上部コンベア5・均分機5a等の
穀物の循環系の送穀装置のモーターの回転速度を
制御する循環系モーター速度制御回路、Mnは前
述の下部コンベア3を駆動するモーターM2およ
び昇降機4・上部コンベア5・均分機5aを駆動
するモーターM3ならびに回転シヤツター2を駆
動するモーターM4らの循環系のモーターを示し
ている。 In the same figure, S6 is the above-mentioned moisture value detection device W.
The moisture detection sensor K1 is the moisture detection sensor S.
A grain moisture detection circuit converts the signal sent from the grain moisture detection circuit K1 into a grain moisture value (moisture content) signal, and K2 calculates the circulating amount of grain according to a predetermined pattern from the grain moisture value signal sent from the grain moisture detection circuit K1. A circulation amount setting calculation circuit incorporating a computer, K3 is the circulation amount setting calculation circuit K.
A circulation system motor speed control circuit that controls the rotational speed of the motor of the grain feeding device of the grain circulation system, such as the lower conveyor 3, elevator 4, upper conveyor 5, equalizer 5a, etc., according to the setting signal sent from 2, Mn is the above-mentioned The motors in the circulation system include a motor M2 that drives the lower conveyor 3, a motor M3 that drives the elevator 4, the upper conveyor 5, and the equalizer 5a, and a motor M4 that drives the rotary shutter 2.
そして、これらにより、乾燥作業中に水分値検
出装置Wの水分検出センサS6および穀物水分検
出回路K1により検出される穀物水分値に応じ、
循環量設定演算回路K2で所定のパターンに従い
演算して、循環系のモーターMnの回転速度を変
更していくよう制御するが、前述の循環量設定演
算回路K2で行なわれる演算内容は、第6図の如
く穀物の含水分率(%)Mのときの最適の循環量
Svとする循環速度を実験から見出して一つのパ
ターンを作り、そのパターンに従うようにしてあ
り、乾燥行程の進行により穀物の含水率(%)が
低下してくるに従い循環量の増加割合が次第に増
大するようにしてある。 Then, according to the grain moisture value detected by the moisture detection sensor S6 of the moisture value detection device W and the grain moisture detection circuit K1 during the drying operation,
The circulation rate setting calculation circuit K2 performs calculations according to a predetermined pattern to control the rotational speed of the motor Mn of the circulation system to be changed. As shown in the figure, the optimum circulation amount when the grain moisture content (%) is M
A pattern is created by finding the circulation speed Sv through experiments, and the pattern is followed.As the moisture content (%) of the grain decreases as the drying process progresses, the rate of increase in the circulation amount gradually increases. It is designed to do so.
次に第7図は前記コントロールボツクスb内に
設けられる熱風温度制御用の制御回路のブロツク
図を示す。 Next, FIG. 7 shows a block diagram of a control circuit for hot air temperature control provided in the control box b.
同図において、K4は外気温センサS1から送
られてくる信号により外気温を検出する外気温検
出回路、K5は穀物量センサS5から送られてく
る信号により穀物量を検出する穀物量検出回路、
K6は穀物種類設定ダイヤルD2から送られてく
る選択した穀物の種類の信号によりその穀物に適
応する条件を設定する穀物種類検出回路、K7は
前記外気温検出回路K4および穀物量検出回路K
5ならびに穀物種類検出回路K6から送り出され
てくる検出信号により、前記第2図にて符号に
示している普通循環速度における設定すべき理想
の穀温を演算する穀温設定演算回路、K8は穀温
センサS3(または排風温センサS4)から送ら
れる信号により穀温を検出する穀温検出回路、K
9はその穀温検出回路K8から送られてくる温度
信号と前述の穀温設定演算回路K7から送られて
くる温度信号とを比較する比較回路、K10は前
記比較回路K9から送り出される比較結果の信号
により設定すべき熱風温度を演算する熱風温度設
定演算回路、K11はその熱風温度設定演算回路
K10で演算された熱風温度の信号により熱風発
生装置系の出力を制御する熱風発生装置出力制御
回路、Bはその制御回路K11により制御される
燃料供給ポンプP・バーナーフアンのモータM
8・送風機9のモーターM1等よりなる熱風発生
装置系を示している。 In the figure, K4 is an outside temperature detection circuit that detects the outside temperature based on a signal sent from the outside temperature sensor S1, and K5 is a grain amount detection circuit that detects the amount of grain based on a signal sent from the grain amount sensor S5.
K6 is a grain type detection circuit that sets conditions suitable for the selected grain based on the signal of the selected grain type sent from the grain type setting dial D2, and K7 is the outside temperature detection circuit K4 and the grain amount detection circuit K.
K8 is a grain temperature setting calculation circuit that calculates the ideal grain temperature to be set at the normal circulation speed indicated by the symbol in FIG. Grain temperature detection circuit K that detects grain temperature based on a signal sent from temperature sensor S3 (or exhaust air temperature sensor S4)
9 is a comparison circuit that compares the temperature signal sent from the grain temperature detection circuit K8 with the temperature signal sent from the aforementioned grain temperature setting calculation circuit K7; A hot air temperature setting calculation circuit that calculates the hot air temperature to be set based on the signal; K11 is a hot air generator output control circuit that controls the output of the hot air generator system based on the hot air temperature signal calculated by the hot air temperature setting calculation circuit K10; B is a fuel supply pump P/burner fan motor M controlled by the control circuit K11.
8. Shows a hot air generator system consisting of the motor M1 of the blower 9, etc.
そして、これらにより、外気温検出回路K4で
検出される温度信号をto、穀物量検出回路K5で
検出される穀物量の信号をG、穀物種類検出回路
K6で検出される穀物の種類の信号をDとしたと
き、設定すべき穀温tを、t=f(to・G/D)
の式によつて前記第2図の符号のパターンに従
い穀物設定演算回路K7で演算し、その穀温tを
穀温検出回路K8で検出する乾燥途上の実際の穀
温と比較し、その比較結果に基づき、設定した穀
温と実際の穀温との差を埋める分だけ穀温を上昇
せしめるように熱風発生装置8で送給する熱風の
温度が上昇するよう熱風発生装置系Bの出力を制
御せしめるようにしている。 With these, the temperature signal detected by the outside temperature detection circuit K4 is set to G, the grain amount signal detected by the grain amount detection circuit K5 is set to G, and the grain type signal detected by the grain type detection circuit K6 is set to G. When D, the grain temperature t to be set is t=f(to・G/D)
The grain temperature t is calculated by the grain setting calculation circuit K7 according to the symbol pattern in FIG. Based on this, the output of the hot air generator system B is controlled so that the temperature of the hot air sent by the hot air generator 8 is increased so as to increase the grain temperature by an amount that compensates for the difference between the set grain temperature and the actual grain temperature. I try to force myself to do so.
[発明の効果]
以上説明したように本発明による循環型穀物乾
燥機を用いる穀粒の乾燥方法は、循環型穀物乾燥
機を用い穀粒を循環させながら熱風を浴びせて乾
燥させる穀粒の乾燥方法において、乾燥行程中に
おける穀粒の乾燥の進行により穀粒の含水率が低
下してくるに従い穀粒の循環速度を増大させると
ともに、穀粒に浴びせる熱風の温度を、穀粒の循
環速度の増大により生ずる穀温の低下を埋めるよ
う上昇せしめて穀粒を乾燥せしめる構成としてい
ることから、乾燥の進行による穀粒の含水率の低
下に従う循環速度の増大により、熱風が吹き抜け
る部位における穀粒の密度が疎になることで、通
風抵抗が減少し、穀温が低下してくることを利用
して、品質の劣化をきたさずに熱風温度を上昇せ
しめ得ることになつて、乾燥効率を著しく向上さ
せ得るようになり、作業時間を短くした能率のよ
い乾燥が行なえるようになる。[Effects of the Invention] As explained above, the method of drying grains using the circulating grain dryer according to the present invention is a drying method of drying grains by blowing hot air while circulating the grains using the circulating grain dryer. In this method, the circulation speed of the grain is increased as the moisture content of the grain decreases due to the progress of drying of the grain during the drying process, and the temperature of the hot air applied to the grain is adjusted to reduce the circulation speed of the grain. Since the grain temperature is raised to compensate for the drop in grain temperature caused by the increase in grain temperature and dry the grains, the circulation speed increases as the moisture content of the grains decreases as drying progresses. The sparser density reduces ventilation resistance and lowers grain temperature, making it possible to increase hot air temperature without deteriorating quality, significantly improving drying efficiency. This makes it possible to perform efficient drying with shortened working time.
第1図は循環型穀物乾燥機の説明図、第2図は
本発明法の説明図、第3図は本発明の実施に用い
る循環型穀物乾燥機の縦断側面図、第4図は同上
のコントロールボツクスの正面図、第5図は同上
の制御装置のブロツク回路図、第6図は循環量設
定演算回路に組込むパターンの説明図、第7図は
熱風発生装置の制御装置のブロツク回路図であ
る。
図面符号の説明、A……循環型穀物乾燥機、a
……機体、b……コントロールボツクス、1……
穀槽、2……回転シヤツター、3……下部コンベ
ア、4……昇降機、4a……揚穀塔、4b……バ
ケツトコンベア、4c……取出樋、4d……切換
シヤツター、5……上部コンベア、5a……均分
機、6……導風路、7……排風ダクト、8……熱
風生成装置、9……送風機、10……除塵機、P
……燃料供給ポンプ、W……水分値検出装置、M
1,M2,M3,M4,M5,M6,M7,M
8,M9……モーター、Mn……循環系のモータ
ー、D1,D2,D3……ダイヤル、S1……外
気温センサ、S2……熱風温センサ、S3……穀
温センサ、S4……排風温センサ,S5……穀物
量センサ、S6……水分検出センサ、Sv……循
環量、K1……穀物水分検出回路、K2……循環
量設定演算回路、K3……循環系モーター速度制
御回路、K4……外気温検出回路、K5……穀物
量検出回路、K6……穀物種類検出回路、K7…
…穀温設定演算回路、K8……穀温検出回路、K
9……比較回路、K10……熱風温度設定演算回
路、K11……熱風発生装置出力制御回路。
Fig. 1 is an explanatory diagram of a circulating grain dryer, Fig. 2 is an explanatory diagram of the method of the present invention, Fig. 3 is a longitudinal cross-sectional side view of a circulating grain dryer used for carrying out the present invention, and Fig. 4 is the same as above. A front view of the control box, Fig. 5 is a block circuit diagram of the same control device as above, Fig. 6 is an explanatory diagram of a pattern incorporated in the circulation rate setting calculation circuit, and Fig. 7 is a block circuit diagram of the control device of the hot air generator. be. Explanation of drawing symbols, A... Circulating grain dryer, a
...Aircraft, b...Control box, 1...
Grain tank, 2...Rotary shutter, 3...Lower conveyor, 4...Elevator, 4a...Grain lifting tower, 4b...Bucket conveyor, 4c...Takeout gutter, 4d...Switching shutter, 5...Upper part Conveyor, 5a... Equalizer, 6... Air guiding path, 7... Exhaust duct, 8... Hot air generator, 9... Air blower, 10... Dust remover, P
... Fuel supply pump, W ... Moisture value detection device, M
1, M2, M3, M4, M5, M6, M7, M
8, M9...Motor, Mn...Circulation system motor, D1, D2, D3...Dial, S1...Outside temperature sensor, S2...Hot air temperature sensor, S3...Grain temperature sensor, S4...Exhaust air Temperature sensor, S5...Grain amount sensor, S6...Moisture detection sensor, Sv...Circulation amount, K1...Grain moisture detection circuit, K2...Circulation amount setting calculation circuit, K3...Circulation system motor speed control circuit, K4...Outside temperature detection circuit, K5...Grain amount detection circuit, K6...Grain type detection circuit, K7...
...Grain temperature setting calculation circuit, K8...Grain temperature detection circuit, K
9... Comparison circuit, K10... Hot air temperature setting calculation circuit, K11... Hot air generator output control circuit.
Claims (1)
ら熱風を浴びせて乾燥させる穀粒の乾燥方法にお
いて、乾燥行程中における穀粒の乾燥の進行によ
り穀粒の含水率が低下してくるに従い穀粒の循環
速度を増大させるとともに、穀粒に浴びせる熱風
の温度を、穀粒の循環速度の増大により生ずる穀
温の低下を埋めるように上昇せしめて穀粒を乾燥
せしめることを特徴とする循環型穀物乾燥機を用
いる穀粒の乾燥方法。1 In a grain drying method in which the grain is dried by blowing hot air while circulating the grain using a circulating grain dryer, as the moisture content of the grain decreases as the grain continues to dry during the drying process, the grain A circulation type that is characterized by increasing the circulation speed of the grains and increasing the temperature of the hot air applied to the grains to compensate for the drop in grain temperature caused by the increased circulation speed of the grains, thereby drying the grains. A method of drying grain using a grain dryer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1887586A JPS62175576A (en) | 1986-01-30 | 1986-01-30 | Method of drying cereal grain by using circulation type cereal drier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1887586A JPS62175576A (en) | 1986-01-30 | 1986-01-30 | Method of drying cereal grain by using circulation type cereal drier |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62175576A JPS62175576A (en) | 1987-08-01 |
| JPH0439596B2 true JPH0439596B2 (en) | 1992-06-30 |
Family
ID=11983721
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1887586A Granted JPS62175576A (en) | 1986-01-30 | 1986-01-30 | Method of drying cereal grain by using circulation type cereal drier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62175576A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0217381A (en) * | 1988-07-06 | 1990-01-22 | Yamamoto Mfg Co Ltd | Controller for grain drying device |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57124680A (en) * | 1981-01-24 | 1982-08-03 | Yamamoto Mfg | Drying of grain particles |
| JPS58145876A (en) * | 1982-02-25 | 1983-08-31 | 株式会社 サタケ | Drier with detector for crack of drum |
-
1986
- 1986-01-30 JP JP1887586A patent/JPS62175576A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62175576A (en) | 1987-08-01 |
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