JPH07111307B2 - Grain drying control system of grain dryer - Google Patents
Grain drying control system of grain dryerInfo
- Publication number
- JPH07111307B2 JPH07111307B2 JP61248041A JP24804186A JPH07111307B2 JP H07111307 B2 JPH07111307 B2 JP H07111307B2 JP 61248041 A JP61248041 A JP 61248041A JP 24804186 A JP24804186 A JP 24804186A JP H07111307 B2 JPH07111307 B2 JP H07111307B2
- Authority
- JP
- Japan
- Prior art keywords
- grain
- temperature
- hot air
- green rice
- grain 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
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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〕 この発明は、穀粒乾燥機の穀粒乾燥制御方式に関する。TECHNICAL FIELD The present invention relates to a grain drying control system for a grain dryer.
従来、乾燥中の穀粒の温度(穀温)を検出しながら、所
定のリミット値以上ならないようバーナによる発生熱風
温度を抑制する形態が公知である(例えば、特開昭58-1
87779号公報)。Conventionally, a mode is known in which the hot air temperature generated by the burner is suppressed so that the temperature does not exceed a predetermined limit value while detecting the temperature of the grain during drying (grain temperature) (for example, JP-A-58-1).
87779).
しかしながら、この設定穀温を一定値に設定すると都合
が悪い。一般にこの設定穀温は穀粒温度の異常上昇に伴
う弊害を未然に防止しようとするが、余り効きすぎると
却って乾燥速度が遅くなりすぎ、作業時間を長くしてし
まう欠点があるから、適宜に設定されるのが通例であ
る。例えば乾燥中の穀粒に混入する青米比率が大のとき
には、当該余り穀粒温度を高くすると、乾燥時間は短縮
できるが、穀粒内の水分移行を活発化して、高水分の青
米から整粒への水分移行も活発化しその結果所謂胴割れ
現象を生じて品質低下を生じる。穀温が上昇すると水分
除去効果も増し、整粒と青米との水分格差が大きくな
り、上記傾向を一層助長する。However, it is not convenient to set the set grain temperature to a constant value. Generally, this set grain temperature tries to prevent adverse effects caused by abnormally high grain temperature, but if it is too effective, the drying speed will be too slow and the working time will be lengthened. It is usually set. For example, when the ratio of green rice mixed in the grain during drying is high, the drying time can be shortened by raising the temperature of the grain too much, but moisture transfer in the grain is activated, and blue rice with high moisture content Moisture transfer to sieving also becomes active, resulting in a so-called barrel cracking phenomenon, resulting in deterioration of quality. When the grain temperature rises, the water removal effect also increases, and the water gap between the sized rice and the green rice increases, further promoting the above tendency.
乾燥室2内穀粒を流下しながらバーナ1からの発生熱風
によって予め設定した仕上目標水分値に達するまで乾燥
させる乾燥制御装置35を構成すると共に、乾燥中の穀粒
の穀温を検出する穀温センサ4を設けて該穀温センサ4
が検出する検出穀温が予め設定した設定穀温を越えると
当該設定穀温に略同じになるように上記バーナ1による
発生熱風の温度を制御する燃料制御装置36を構成するも
のにおいて、穀粒内に混入する青米の比率を算出する青
米混入比率算出手段、この青米混入比率と予め設定した
設定青米混入比率とを比較する比較手段、算出青米混入
比率が設定青米混入比率を越えるとき上記発生熱風の温
度を所定温度減少させる穀温低下手段を設けてなる穀粒
乾燥機の穀粒乾燥制御方式の構成とする。The drying control device 35 is configured to dry the grains in the drying chamber 2 while flowing down the grains by the hot air generated from the burner 1 until the preset target moisture value is reached, and the grain temperature of the grain being dried is detected. The grain temperature sensor 4 is provided with the temperature sensor 4.
In the fuel control device 36 for controlling the temperature of the hot air generated by the burner 1 such that the detected grain temperature detected by the burner 1 becomes substantially the same as the preset grain temperature when it exceeds a preset grain temperature, Green rice mixing ratio calculating means for calculating the ratio of green rice mixed in the inside, comparing means for comparing this green rice mixing ratio with a preset setting green rice mixing ratio, calculated blue rice mixing ratio is set green rice mixing ratio The grain drying control system of the grain dryer is provided with grain temperature lowering means for reducing the temperature of the generated hot air by a predetermined temperature.
乾燥中、バーナ1の熱風温度は穀粒の乾燥に必要な温度
に設定されるが、その間穀温センサ4で乾燥中の穀粒の
温度が検出され、あらかじめ設定した設定穀温と比較さ
れ、当該設定穀温以下であるときは、そのままの熱風温
度で継続乾燥されるが、設定穀温を越えるときは当該設
定穀温に同じくなるよう燃料制御装置36がバーナ1への
供給燃料を減少制御させる。加えて青米混入率を算出
し、この算出青米混入率があらかじめ設定する設定青米
混入率を越えるときは、燃料制御装置36の指令信号を出
力して更に供給燃料を減少する。During drying, the hot air temperature of the burner 1 is set to a temperature required for drying the grain, while the temperature of the grain being dried is detected by the grain temperature sensor 4, and compared with the preset grain temperature set in advance, When the temperature is equal to or lower than the set grain temperature, the hot air temperature is continuously dried as it is, but when the temperature is higher than the set grain temperature, the fuel control device 36 controls to reduce the fuel supplied to the burner 1 so that the set grain temperature becomes the same. Let In addition, the green rice mixing rate is calculated, and when the calculated green rice mixing rate exceeds a preset green rice mixing rate, a command signal of the fuel control device 36 is output to further reduce the supplied fuel.
従って、青米の混入率によって設定穀温状態からさらに
バーナ1の燃焼状態を小にして穀温の低下を促すもの
で、乾燥される速度はやや遅くなる。高い青米比率の場
合では穀粒間同志の水分移行が活発で整粒の胴割れを助
長するが、上記のように燃焼状態を小にすることにより
穀温を低下させることができるから、青米と整粒との水
分格差の拡大を抑制し品質低下を防止できる。Therefore, the burning rate of the burner 1 is further reduced from the set grain temperature state by the mixing ratio of green rice to promote the reduction of the grain temperature, and the drying speed is slightly slowed. In the case of a high ratio of green rice, water transfer between grains is active and promotes cracking of the sizing. However, the grain temperature can be lowered by reducing the combustion state as described above. It is possible to prevent the deterioration of quality by suppressing the expansion of the water content difference between rice and sized rice.
この発明の一実施例を図面に基づき説明する。 An embodiment of the present invention will be described with reference to the drawings.
乾燥機5の機壁6は前後方向に長い平面視長方形状で、
前後壁板及び左右壁板よりなり、この前壁板にはこの乾
燥機5を始動及び停止等の運転操作を行う操作装置7及
びバーナ1を内装したバーナケース8を設け、該後壁板
には排風機9を設けている。The machine wall 6 of the dryer 5 has a rectangular shape in plan view which is long in the front-rear direction.
The front wall plate includes front and rear wall plates, and left and right wall plates. The front wall plate is provided with an operating device 7 for operating the dryer 5 such as starting and stopping, and a burner case 8 having the burner 1 installed therein. Is equipped with a blower 9.
上記機壁6内下部中央には前後方向に亘る間に、移送螺
旋を内装した集穀樋10を設け、この集穀樋10上には下位
に繰出バルブ11を回転自在に軸支した乾燥室2を重設し
ている。乾燥室2,2は左右一対に形成され、それらの間
にはバーナ1に通じる熱風室12を形成している。13は熱
風室12に設ける熱風温度センサである。上記乾燥室2,2
の外側には排風室14,14を形成し、排風機9を連通す
る。At the center of the lower part of the machine wall 6 is provided a grain collecting trough 10 having a transfer spiral installed in the longitudinal direction, and a drying chamber in which a feeding valve 11 is rotatably supported at a lower position on the grain collecting trough 10. Two are piled up. The drying chambers 2, 2 are formed in a left-right pair, and a hot air chamber 12 communicating with the burner 1 is formed between them. Reference numeral 13 is a hot air temperature sensor provided in the hot air chamber 12. Above drying room 2,2
The exhaust chambers 14, 14 are formed on the outer side of, and the exhaust fan 9 is communicated therewith.
15は機壁の後壁板下部に設けるモータで、上記移送螺
旋,繰出バルブ11,11及び排風機9を回転連動する構成
である。Reference numeral 15 denotes a motor provided below the rear wall plate of the machine wall, which is configured to rotate and interlock the transfer spiral, the feeding valves 11, 11 and the exhaust fan 9.
前記バーナケース8の外側下方には燃料バルブ,燃料ポ
ンプ18を配設し、これらの動作によって所定流量に調節
設定された燃料をバーナ1に供給できる構成である。
又、バーナケース8の上部板側には送風機18及びモータ
19を設ける。送風機18は燃焼用空気をバーナ1内に供給
する構成である。A fuel valve and a fuel pump 18 are provided on the lower outside of the burner case 8 so that the fuel adjusted to a predetermined flow rate can be supplied to the burner 1 by these operations.
Further, the blower 18 and the motor are provided on the upper plate side of the burner case 8.
19 is provided. The blower 18 is configured to supply combustion air into the burner 1.
前記乾燥室2,2の上部には貯留室20を設け、この貯留室2
0の天井板21,21には移送螺旋を内装する上部移送樋22を
設けてある。23は拡散盤で、上部移送樋22からの穀粒を
受けて飛散供給する構成である。A storage chamber 20 is provided above the drying chambers 2, 2 and the storage chamber 2
An upper transfer gutter 22 that houses a transfer spiral is provided on the ceiling plates 21 and 21 of 0. Reference numeral 23 denotes a diffuser, which is configured to receive and scatter the grains from the upper transfer gutter 22.
24は前記機壁6前方にあって、内部にバケットコンベア
25のベルトを上下プーリ間に張設する昇穀機で、上部側
は投出筒26を介して上部移送樋22の始端部に連通し、下
端側は前記集穀樋10の終端部との間に供給樋27を設けて
連通している。昇降機24の途中にはモータ28を固定し、
バケットコンベア25ベルト,上記上部移送樋22内の移送
螺旋,拡散盤23等を回転連動する。24 is in front of the machine wall 6 and has a bucket conveyor inside.
In the grain raising machine which stretches the belt of 25 between the upper and lower pulleys, the upper side communicates with the starting end of the upper transfer gutter 22 via the throwing tube 26, and the lower end side with the end of the grain collecting gutter 10. A supply gutter 27 is provided between them for communication. A motor 28 is fixed in the middle of the elevator 24,
The bucket conveyor 25 belt, the transfer spiral in the upper transfer gutter 22 and the diffuser 23 are interlocked in rotation.
4は昇降機の上下略中央部に設ける水分センサ、3は上
記供給樋27内壁部にあって、通過する穀粒の穀温を検出
できる構成である。Reference numeral 4 denotes a moisture sensor provided substantially in the upper and lower central portions of the elevator, and 3 denotes an inner wall portion of the supply gutter 27, which has a configuration capable of detecting the grain temperature of the passing grain.
前記水分センサ4は、バケットコンベア25による上方移
送中の穀粒の内の落下穀粒を導入し、圧砕しながら水分
値を検出する構成である。該水分センサ4はなお、前記
操作装置7からの所定時間間隔で発信する発信信号に基
づいてモータ29を回転連動しセンサ4各部を始動させる
構成である。The moisture sensor 4 is configured to introduce a falling grain in the grain being transferred upward by the bucket conveyor 25 and detect the moisture value while crushing. The moisture sensor 4 has a structure in which the motor 29 is rotationally interlocked with each other to start each part of the sensor 4 based on a transmission signal transmitted from the operation device 7 at a predetermined time interval.
前記操作装置7の表面板には、始動,停止等のための始
動スイッチ30,停止スイッチ31、穀粒の仕上目標水分値
を設定する目標水分設定つまみ32,バーナ1からの発生
熱風温度を設定する熱風温度設定つまみ33,水分センサ1
3の検出値と、熱風温度とを交互に表示する表示部34を
有する。一方内部には制御装置35及び燃料制御装置36が
構成される。例えば設定つまみ33を穀粒量(前壁板の形
成する表示窓の表示数字)に合わせると、バーナ1から
発生する熱風温度が設定される構成である。On the surface plate of the operating device 7, a start switch 30 for starting and stopping, a stop switch 31, a target moisture setting knob 32 for setting a finish target moisture value of grain, and a hot air temperature generated from the burner 1 are set. Hot air temperature setting knob 33, moisture sensor 1
The display unit 34 alternately displays the detected value of 3 and the hot air temperature. Meanwhile, a control device 35 and a fuel control device 36 are formed inside. For example, the hot air temperature generated from the burner 1 is set when the setting knob 33 is adjusted to the grain amount (display number of the display window formed by the front wall plate).
又、燃料制御装置36は、前記熱風温度センサ13及び穀温
センサ3からの検出信号をA/D変換するA/D変換器37、入
力回路38,39、これら各入力回路38,39から入力される各
種入力値を算術論理演算及び比較演算等を行なうCPU4
0、このCPU40から指令される各種指令を受けて出力する
出力回路41等から構成される。Further, the fuel control device 36 inputs from the A / D converter 37 for A / D converting the detection signals from the hot air temperature sensor 13 and the grain temperature sensor 3, the input circuits 38 and 39, and these input circuits 38 and 39. CPU4 that performs arithmetic logic operation and comparison operation on various input values
0, an output circuit 41 that receives various commands from the CPU 40 and outputs the commands.
前記制御装置35は、前記水分センサ4が検出する検出値
をA/D変換するA/D変換器42、入力回路43、各スイッチ3
0,31及び設定つまみ32の入力信号を受ける入力回路44を
構成し、これら入力回路43,44からの各種入力値は、上
記CPU40によって算術論理演算及び比較演算を行なう構
成である。45は出力回路。The control device 35 includes an A / D converter 42 for A / D converting the detection value detected by the moisture sensor 4, an input circuit 43, and each switch 3
An input circuit 44 that receives the input signals of 0, 31 and the setting knob 32 is configured, and various input values from these input circuits 43, 44 are configured to perform arithmetic logic operation and comparison operation by the CPU 40. 45 is an output circuit.
該燃料制御装置36は次の機能を有する。制御装置35へ
の始動スイッチ30及び目標水分設定つまみ32の操作入力
を条件に、該燃料制御装置36に熱風温度設定つまみ33の
設定値が入力されると、バーナ1の熱風温度が設定され
る。乾燥中は穀温センサ3からの検出穀温をあらかじ
め設定してある設定穀温と比較し、検出穀温>設定穀温
の場合には、燃料バルブの開閉回数を減少して供給燃料
量を減少せしめ、設定穀温以下になるように制御する。
例えば籾粒で設定穀温が38℃のとき、検出穀温が42℃で
あると、38℃になるよう燃料供給量を減少制御すること
となる。逆に検出穀温<設定穀温の場合には、熱風設定
温度を確保すべく制御される(穀温制御手段)。The fuel control device 36 has the following functions. When the set value of the hot air temperature setting knob 33 is input to the fuel control device 36 on condition that the start switch 30 and the target moisture setting knob 32 are input to the control device 35, the hot air temperature of the burner 1 is set. . During drying, the grain temperature detected by the grain temperature sensor 3 is compared with a preset grain temperature, and if the detected grain temperature> the set grain temperature, the number of times the fuel valve is opened and closed is reduced to reduce the amount of fuel supplied. The grain temperature is controlled to be less than the set grain temperature.
For example, when the set grain temperature of rice grain is 38 ° C and the detected grain temperature is 42 ° C, the fuel supply amount is controlled to decrease to 38 ° C. On the contrary, when the detected grain temperature <the set grain temperature, the temperature is controlled to secure the hot air set temperature (grain temperature control means).
前記制御装置35は次の機能を有する。目標水分設定つ
まみ32や始動スイッチ30の操作入力を条件に、各乾燥機
5の各モータ15,19,28,29を回転連動する軌道信号が出
力される。水分センサ4が検出する穀粒水分値が仕上
目標水分値に達すると乾燥機5に停止信号を出力する。The control device 35 has the following functions. On the condition that the target moisture setting knob 32 and the start switch 30 are operated, a trajectory signal for rotating the motors 15, 19, 28, 29 of the dryers 5 is output. When the grain moisture value detected by the moisture sensor 4 reaches the finishing target moisture value, a stop signal is output to the dryer 5.
上記水分センサ4は、所定粒数(例えば36粒)の検出穀
粒水分値によって平均値を算出する構成であるが、この
演算によって得た平均値より1%以上高い水分値の対象
は青米と推定し、これの検出粒数によって青米混入比率
を算出でき、この青米混入比率の値に基づいて、先の穀
温制御手段による設定穀温を上下に変更する構成であ
る。上例で検出穀温>設定穀温の場合であって、青米混
入比率が非常に高いとき(例えば30%を越えるとき)、
燃料制御装置36はさらに所定温度(例えば5℃)に見合
う燃料の減少制御を加えるものである(穀温低下手
段)。これらの数値はテスト結果によって得た最良の値
を記憶するものである。The moisture sensor 4 is configured to calculate an average value based on the moisture value of a detected grain of a predetermined grain number (for example, 36 grains), and the target of the moisture value higher than the average value obtained by this calculation is 1% or more. The ratio of green rice can be calculated based on the number of detected grains, and the grain temperature set by the grain temperature control means is changed up and down based on the value of the ratio of green rice. In the above example, if the detected grain temperature> the set grain temperature, and the ratio of green rice is very high (for example, if it exceeds 30%),
The fuel control device 36 further controls the reduction of fuel corresponding to a predetermined temperature (for example, 5 ° C.) (grain temperature lowering means). These numbers store the best values obtained from the test results.
上例の作用について説明する。The operation of the above example will be described.
操作装置7の各設定つまみ32,33を所定位置に操作し、
始動スイッチ30をオンすることにより、乾燥機5各部が
始動する。バーナ1からの熱風は設定温度とされ、該熱
風が熱風室12から乾燥室2を通風し、穀粒を乾燥する。
乾燥された穀粒は集穀樋10内に集められ、移送螺旋で横
送りされた後、供給樋27を経て昇穀機24に供給される。
昇穀機24では、上昇搬送され、上部移送樋22を経て拡散
盤23に供給される。この拡散盤23の回転によって均分落
下される穀粒は貯留室20にて調質されることとなる。こ
のような行程を繰返し、水分センサ4の検出値があらか
じめ設定した仕上目標水分値以下に達すると、制御装置
35は乾燥機5運転を自動停止する。Operate each setting knob 32, 33 of the operating device 7 to the predetermined position,
By turning on the start switch 30, each part of the dryer 5 is started. The hot air from the burner 1 is set to a preset temperature, and the hot air flows from the hot air chamber 12 to the drying chamber 2 to dry the grain.
The dried grains are collected in the grain collecting trough 10, traversed by a transfer spiral, and then supplied to the grain raising machine 24 via the supply gutter 27.
In the grain raising machine 24, it is conveyed up and supplied to the diffusion board 23 through the upper transfer gutter 22. Grains that are evenly dropped by the rotation of the diffusion plate 23 are conditioned in the storage chamber 20. When such a process is repeated and the detection value of the moisture sensor 4 reaches the preset target moisture value or less, the control device
35, the dryer 5 operation is automatically stopped.
上記の乾燥作業中に、穀温センサ3が穀温2を検出す
る。この検出穀温はあらかじめ設定している設定穀温と
比較される。検出穀温>設定穀温のときは、燃料制御装
置36の穀温制御手段によって燃料供給量が所定に減少さ
れ、熱風温度が低下し、穀温の上昇は抑制され併せてそ
の低下が表われ、胴割れ等の品質低下の恐れのない安全
範囲で乾燥を継続できる。During the above drying operation, the grain temperature sensor 3 detects the grain temperature 2. This detected grain temperature is compared with the preset grain temperature. When the detected grain temperature> the set grain temperature, the fuel supply amount is reduced by the grain temperature control means of the fuel control device 36 to a predetermined amount, the hot air temperature is lowered, the rise of the grain temperature is suppressed, and the decrease is also shown. Drying can be continued within a safe range where there is no risk of quality deterioration such as cracking of the body.
又、水分センサ4の検出結果によって青米の混入比率が
所定以上にあると、上記に加えてさらに燃料供給量が所
定温度分減少され、熱風温度は低下するものである。従
って、青米混入によって水分バラツキが顕著であっても
穀温を比較的低温に推移させることができ、胴割れ等の
影響が少ない。Further, if the mixing ratio of green rice is more than a predetermined value according to the detection result of the moisture sensor 4, in addition to the above, the fuel supply amount is further reduced by a predetermined temperature, and the hot air temperature is lowered. Therefore, the grain temperature can be changed to a relatively low temperature even if the water content is significantly varied due to the mixture of green rice, and the influence of cracking of the barrel or the like is small.
図は、この発明の一実施例を示すもので、第1図はブロ
ック図、第2図はフローチャート図、第3図は一部断面
せる乾燥機の全体正面図、第4図は一部断面せる乾燥機
の全体側面図、第5図は乾燥機の一部の拡大正面図であ
る。 1……バーナ、2……乾燥室、3……穀温センサ、4…
…水分センサ、5……乾燥機、6……機壁、7……操作
装置、8……バーナケース、9……排風機、10……集穀
機、11……繰出バルブ、12……熱風室、13……熱風温度
センサ、14……排風室、15……モータ、16……燃料ポン
プ、17……燃料タンク、18……送風機、19……モータ、
20……貯留室、21……天井板、22……上部移送樋、23…
…拡散盤、24……昇穀機、25……バケットコンベア、26
……投出筒、27……供給樋、28……モータ、29……モー
タ、30……始動スイッチ、31……停止スイッチ、32……
目標水分設定つまみ、33……熱風温度設定つまみ、34…
…表示窓、35……制御装置、36……燃料制御装置、37…
…A/D変換器、38……入力回路、39……入力回路、40…
…CPU、41……出力回路、42……A/D変換器、43……入力
回路、44……入力回路、45……出力回路FIG. 1 shows an embodiment of the present invention. FIG. 1 is a block diagram, FIG. 2 is a flow chart diagram, FIG. 3 is an overall front view of a dryer with a partial cross section, and FIG. 4 is a partial cross section. FIG. 5 is an enlarged front view of a part of the dryer, which shows the entire dryer. 1 ... Burner, 2 ... Drying room, 3 ... Grain temperature sensor, 4 ...
... Moisture sensor, 5 ... Dryer, 6 ... Machine wall, 7 ... Operating device, 8 ... Burner case, 9 ... Air blower, 10 ... Grain collector, 11 ... Feeding valve, 12 ... Hot air chamber, 13 ... Hot air temperature sensor, 14 ... Exhaust chamber, 15 ... Motor, 16 ... Fuel pump, 17 ... Fuel tank, 18 ... Blower, 19 ... Motor,
20 ... Storage room, 21 ... Ceiling plate, 22 ... Upper transfer gutter, 23 ...
… Diffuser, 24 …… Grain elevator, 25 …… Bucket conveyor, 26
…… Spout tube, 27 …… Supply gutter, 28 …… Motor, 29 …… Motor, 30 …… Start switch, 31 …… Stop switch, 32 ……
Target moisture setting knob, 33 ...... Hot air temperature setting knob, 34 ...
... Display window, 35 ... Control device, 36 ... Fuel control device, 37 ...
… A / D converter, 38 …… input circuit, 39 …… input circuit, 40…
… CPU, 41 …… output circuit, 42 …… A / D converter, 43 …… input circuit, 44 …… input circuit, 45 …… output circuit
Claims (1)
らの発生熱風によって予め設定した仕上目標水分値に達
するまで乾燥させる乾燥制御装置35を構成すると共に、
乾燥中の穀粒の穀温を検出する穀温センサー4を設けて
該穀温センサー4が検出する検出穀温が予め設定した設
定穀温を越えると当該設定穀温に略同じになるように上
記バーナ1による発生熱風の温度を制御する燃料制御装
置36を構成するものにおいて、穀粒内に混入する青米の
比率を算出する青米混入比率算出手段、この青米混入比
率と予め設定した設定青米混入比率とを比較する比較手
段、算出青米混入比率が設定青米混入比率を越えるとき
上記発生熱風の温度を所定温度減少させる穀温低下手段
を設けてなる穀粒乾燥機の穀粒乾燥制御方式。1. A drying control device 35 for drying the grains in the drying chamber 2 while flowing down the grains until the preset target moisture value is reached by the hot air generated from the burner 1,
When the grain temperature sensor 4 for detecting the grain temperature of the grain being dried is provided and the detected grain temperature detected by the grain temperature sensor 4 exceeds a preset grain temperature, the grain temperature sensor 4 is set to be substantially the same as the preset grain temperature. In the fuel control device 36 for controlling the temperature of the hot air generated by the burner 1, green rice mixing ratio calculation means for calculating the ratio of green rice mixed in the grain, and this green rice mixing ratio is preset. Comparison means for comparing with the set green rice mixing ratio, when the calculated green rice mixing ratio exceeds the set green rice mixing ratio, the grain of the grain dryer provided with grain temperature lowering means for decreasing the temperature of the generated hot air by a predetermined temperature Grain drying control method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61248041A JPH07111307B2 (en) | 1986-10-17 | 1986-10-17 | Grain drying control system of grain dryer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61248041A JPH07111307B2 (en) | 1986-10-17 | 1986-10-17 | Grain drying control system of grain dryer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63101690A JPS63101690A (en) | 1988-05-06 |
JPH07111307B2 true JPH07111307B2 (en) | 1995-11-29 |
Family
ID=17172316
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61248041A Expired - Lifetime JPH07111307B2 (en) | 1986-10-17 | 1986-10-17 | Grain drying control system of grain dryer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07111307B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008064352A (en) * | 2006-09-05 | 2008-03-21 | Yamamoto Co Ltd | Operation panel for grain drier |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58187779A (en) * | 1982-04-27 | 1983-11-02 | 株式会社クボタ | Circulation type cereal drier |
JPS61217679A (en) * | 1985-03-25 | 1986-09-27 | 井関農機株式会社 | Cereal grain drying controller for cereal grain drier |
-
1986
- 1986-10-17 JP JP61248041A patent/JPH07111307B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58187779A (en) * | 1982-04-27 | 1983-11-02 | 株式会社クボタ | Circulation type cereal drier |
JPS61217679A (en) * | 1985-03-25 | 1986-09-27 | 井関農機株式会社 | Cereal grain drying controller for cereal grain drier |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008064352A (en) * | 2006-09-05 | 2008-03-21 | Yamamoto Co Ltd | Operation panel for grain drier |
Also Published As
Publication number | Publication date |
---|---|
JPS63101690A (en) | 1988-05-06 |
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