JPH05223451A - Drying control system for grain drier - Google Patents

Drying control system for grain drier

Info

Publication number
JPH05223451A
JPH05223451A JP2771292A JP2771292A JPH05223451A JP H05223451 A JPH05223451 A JP H05223451A JP 2771292 A JP2771292 A JP 2771292A JP 2771292 A JP2771292 A JP 2771292A JP H05223451 A JPH05223451 A JP H05223451A
Authority
JP
Japan
Prior art keywords
drying
grain
grains
taste
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.)
Pending
Application number
JP2771292A
Other languages
Japanese (ja)
Inventor
Eiji Nishino
栄治 西野
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.)
Iseki and Co Ltd
Iseki Agricultural Machinery Mfg Co Ltd
Original Assignee
Iseki and Co Ltd
Iseki Agricultural Machinery Mfg 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 Iseki and Co Ltd, Iseki Agricultural Machinery Mfg Co Ltd filed Critical Iseki and Co Ltd
Priority to JP2771292A priority Critical patent/JPH05223451A/en
Publication of JPH05223451A publication Critical patent/JPH05223451A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To perform draft drying by means of the open air during a time in which the taste and the grade of grains intended to be dried are detected and to effect switching to dehumidifying drying and hot blast drying after detection. CONSTITUTION:When a sample drying system is employed, draft drying by means of the open air is applied to grains under flow down through a grain drying chamber 15. A part of grains under draft drying are selected into large grains and unriped grains by a grain side selecting device 3 and the selected large grains are dried and hulled. A taste and a grade are detected by means of a taste detecting device 8 and grade detecting devices 6 and 7. From the detected results, a dehumidifying drying mode or a hot blast drying mode is selected, and through switching control to a selected drying mode, drying is executed. This system performs automatic switching to the dehumidifying drying mode and the hot blast drying mode from draft drying and realizes automation and stabilization of quality of dried grains.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、穀粒乾燥機の乾燥制
御方式に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a drying control system for a grain dryer.

【0002】[0002]

【従来の技術】従来は、穀粒貯留室から穀粒乾燥室へ穀
粒を繰出し流下させながら、熱風、又は除湿風を該乾燥
室へ通過させることにより、該乾燥室を流下中の穀粒
は、これら熱風、又は除湿風に晒されて乾燥される。こ
の乾燥作業中に、一部の穀粒は粒径選別装置へ供給さ
れ、この粒径選別装置を通過することにより、大粒径穀
粒と未熟粒とに選別され、選別済大粒径穀粒は食味検出
装置と品位検出装置とへ供給されて、この穀粒の食味と
品位とが検出され、これらの検出結果により、熱風によ
る熱風乾燥か、又は除湿風による除湿乾燥かが選定され
て乾燥される。
2. Description of the Related Art Conventionally, while feeding and flowing down the grains from the grain storage chamber to the grain drying chamber, hot air or dehumidifying air is passed through the drying chamber to allow the grains flowing down the drying chamber. Is exposed to these hot air or dehumidified air and dried. During this drying operation, some grains are supplied to the grain size selection device, and by passing through this grain size selection device, they are sorted into large grain grains and immature grains, and sorted large grain grains. The grain is supplied to the taste detecting device and the quality detecting device, the taste and quality of the grain are detected, and by these detection results, hot air drying by hot air or dehumidifying drying by dehumidifying air is selected. To be dried.

【0003】[0003]

【発明が解決しようとする課題】穀粒乾燥機の穀粒貯留
室内へ収容された穀粒は、この貯留室から穀粒乾燥室内
を繰出し流下されながら、熱風、又は除湿風が該乾燥室
を通過することにより、該乾燥室内を流下中の穀粒は、
これら熱風、又は除湿風に晒されて乾燥され、この乾燥
中の穀粒の水分が仕上目標水分に達すると、乾燥が終了
したとして、該乾燥機が停止されて穀粒の乾燥が停止さ
れる。
The grains stored in the grain storage chamber of the grain dryer are fed from the storage chamber into the grain drying chamber and flowed down while hot air or dehumidified air blows through the drying chamber. By passing, the grains flowing down in the drying chamber,
When exposed to these hot air or dehumidified air and dried, and when the moisture content of the grain being dried reaches the finishing target moisture content, it is determined that the drying is completed, the dryer is stopped, and the drying of the grain is stopped. ..

【0004】この乾燥作業中に、一部の穀粒は粒径選別
装置へ供給され、この粒径選別装置を通過することによ
り、大粒径穀粒と未熟粒とに選別され、選別済大粒径穀
粒は食味検出装置と品位検出装置とへ供給され、この穀
粒の食味と品位とが検出され、これら検出結果により、
熱風による熱風乾燥か、又は除湿風による除湿乾燥かが
選定され、これらいずれかの方式で乾燥される。
During this drying operation, some grains are supplied to the grain size sorting device, and by passing through this grain size sorting device, they are sorted into large grain size grains and immature grains, and are sorted into large grains. Grain size grain is supplied to the taste detection device and the quality detection device, the taste and quality of this grain is detected, by these detection results,
Either hot air drying with hot air or dehumidifying drying with dehumidifying air is selected, and drying is performed by either of these methods.

【0005】この乾燥作業で穀粒の食味及び品位が検出
されるまでは、外気風を通過させて乾燥する通風乾燥と
し、穀粒の食味及び品位検出後に、これら食味及び品位
の検出結果によって乾燥方式である熱風乾燥、又は除湿
乾燥を自動選定させて穀粒を乾燥させようとするもので
ある。
Until the taste and quality of the grains are detected in this drying operation, ventilation drying is performed by passing the outside air, and after the taste and quality of the grains are detected, they are dried according to the detection results of the taste and quality. The method is to dry the grain by automatically selecting hot air drying or dehumidifying drying.

【0006】[0006]

【課題を解決するための手段】この発明は、上部の穀粒
貯留室14から下部の穀粒乾燥室15ヘ穀粒を繰出し流
下させながら熱風を該乾燥室15へ通風して乾燥しなが
ら循環乾燥中の一部の穀粒を粒径選別装置3へ供給して
大粒径穀粒と未熟粒とに選別する穀粒乾燥機において、
選別した該大粒径穀粒と該未熟粒との両者を該乾燥機へ
還元して乾燥するサンプリング乾燥方式で該選別済大粒
径穀粒の一部を食味検出装置8へ供給して食味検出、又
は胴割や着色粒等を判別しうる品位検出装置6,7等へ
供給して品位検出のときは、熱風乾燥を中止して該乾燥
室15へ外気風が通過して乾燥する通風乾燥に乾燥制御
手段で制御することを特徴とする乾燥制御方式の構成と
する。
According to the present invention, hot air is ventilated into the drying chamber 15 and is circulated while being dried while the grains are being fed from the upper grain storage chamber 14 to the lower grain drying chamber 15 and flowing down. In a grain dryer that supplies a part of the grain being dried to the grain size selection device 3 and sorts it into a large grain size grain and an immature grain,
The sampling and drying method in which both the selected large-sized grain and the immature grain are reduced to the dryer and dried to supply part of the selected large-sized grain to the taste detecting device 8 Ventilation for detecting or supplying quality to the quality detecting devices 6, 7 or the like capable of discriminating the body splitting, colored particles, etc., and stopping the hot air drying to pass the outside air to the drying chamber 15 for drying. A drying control system is characterized in that the drying is controlled by a drying control means.

【0007】[0007]

【発明の作用】穀粒乾燥機の穀粒貯留室14内へ収容さ
れた穀粒は、この貯留室14から穀粒乾燥室15内を繰
出し流下されながら、外気風が該乾燥室15を通過する
ことにより、この外気風に晒されて乾燥される通風乾燥
しながら、一部の穀粒は粒径選別装置3へ供給され、大
粒径穀粒と未熟粒とに選別され、サンプル乾燥方式のと
きは、この選別済大粒径穀粒の一部は食味検出装置8及
び品位検出装置6,7等へ供給され、又選別済大粒径穀
粒の残りと選別済未熟粒とは該乾燥機へ還元され、該乾
燥機内を循環乾燥中の穀粒と混合されて通風乾燥され
る。
The grain stored in the grain storage chamber 14 of the grain dryer is fed from the storage chamber 14 into the grain drying chamber 15 and is allowed to flow while the outside air is passing through the drying chamber 15. By doing so, some of the grains are supplied to the particle size sorting device 3 while being air-dried by being exposed to the outside air and dried, and are sorted into large grain size grains and immature grain sizes, and the sample drying method is used. In this case, a part of the sorted large-sized grain is supplied to the taste detection device 8 and the quality detection devices 6 and 7, and the rest of the sorted large-sized grain and the sorted immature grain are It is reduced to a drier, mixed with the grains being circulated and dried in the drier, and dried by ventilation.

【0008】前記食味検出装置8及び品位検出装置6,
7等へ供給された選別済大粒径穀粒は、食味及び品位が
検出され、これらの検出結果により、乾燥モードである
熱風で乾燥する熱風乾燥の低温一定熱風による低温一定
熱風乾燥モード、低温ステップ乾燥モード及び張込量熱
風乾燥モードか、又は除湿風で乾燥する除湿乾燥の除湿
乾燥モードかが自動選定され、これらの内のいずれかの
モードで乾燥され、この乾燥中の穀粒の水分が仕上目標
水分に達すると、乾燥が終了したとして該乾燥機が停止
されて穀粒の乾燥が停止される。
The taste detecting device 8 and the quality detecting device 6,
The taste and quality of the sorted large-sized grain supplied to 7 etc. are detected. Based on these detection results, low temperature constant hot air drying mode, low temperature constant temperature hot air drying mode, low temperature of hot air drying which is drying mode Step drying mode and overhang amount Hot air drying mode, or dehumidification drying mode of dehumidification drying with dehumidification air is automatically selected, and drying is performed in any of these modes, and the moisture content of the grain during this drying is selected. When reaches the finishing target water content, it is determined that the drying is completed, the dryer is stopped, and the drying of the grain is stopped.

【0009】[0009]

【発明の効果】この発明により、穀粒の食味及び品位等
が検出されるまでの間は、穀粒は外気風で乾燥する通風
乾燥で行われ、食味及び品位が検出されると、これらの
検出結果により、乾燥方式が自動選定されて乾燥される
ことにより、自動化ができ、又穀粒の品質を安定させる
ことができた。
EFFECTS OF THE INVENTION According to the present invention, until the taste and quality of the grain are detected, the grain is dried by ventilation, which is dried by the outside air. According to the detection result, the drying method was automatically selected and dried, so that automation was possible and the quality of the grain could be stabilized.

【0010】[0010]

【実施例】以下、本発明の一実施例を図面に基づいて説
明する。図例は、穀粒を乾燥する循環型の穀粒乾燥機1
に穀粒の水分を検出する水分センサ2、穀粒を選別する
粒径選別装置3、サンプル穀粒を乾燥する乾燥装置4、
サンプル穀粒を籾摺する籾摺装置5、穀粒の胴割を検出
する胴割品位検出装置6、外観品位を検出する外観品位
検出装置7、食味を検出する食味検出装置8、及び熱風
が発生する熱風装置9等を装着し、又除湿風が発生する
除湿装置10を配設した状態を示すものである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. The illustrated example is a circulation type grain dryer 1 for drying grains.
A moisture sensor 2 for detecting the moisture of the grain, a particle size sorting device 3 for sorting the grain, a drying device 4 for drying the sample grain,
The hulling device 5 for hulling the sample grains, the drum split quality detecting device 6 for detecting the barrel split of the grains, the external quality detecting device 7 for detecting the external grade, the taste detecting device 8 for detecting the taste, and the hot air are It shows a state in which a hot air device 9 or the like for generating is installed and a dehumidifying device 10 for generating dehumidified air is provided.

【0011】前記乾燥機1は、前後方向に長い長方形状
で機壁11上部には、移送螺旋を回転自在に内装した移
送樋12及び天井板13を設け、この天井板13下側に
は穀粒を貯留する穀粒貯留室14を形成している。穀粒
乾燥室15,15は、該貯留室14下側において、左右
両側の排風室16,16と中央の送風室17との間に設
け、これら乾燥室15,15下部には、穀粒を繰出し流
下させる繰出バルブ18を夫々回転自在に軸支してい
る。
The dryer 1 has a rectangular shape that is long in the front-rear direction and has a transfer gutter 12 and a ceiling plate 13 in which a transfer spiral is rotatably installed in the upper part of the machine wall 11. Below the ceiling plate 13, grains are provided. A grain storage chamber 14 for storing grains is formed. The grain drying chambers 15 and 15 are provided below the storage chamber 14 between the left and right air exhaust chambers 16 and 16 and the central air blowing chamber 17, and the grain drying chambers 15 and 15 have lower grains. The pay-out valves 18 for paying-out and paying off are respectively rotatably supported.

【0012】集穀樋19は、移送螺旋を回転自在に軸支
し、該各乾燥室15,15下側に設けて連通させてい
る。前記熱風装置9は、バーナ20をバーナケース21
に内装して設け、このバーナケース21は、前記機壁1
1正面側において、前記送風室17入口側に対応すべく
この機壁11外側面に形成する熱風路室22外側部に着
脱自在に設け、又前記乾燥機1等を張込、乾燥及び排出
の各作業別に始動及び停止操作する操作装置23を前側
の該機壁11に着脱自在に設けている。
The grain collecting trough 19 rotatably supports a transfer spiral and is provided below the drying chambers 15 and 15 to communicate with each other. The hot air device 9 includes a burner 20 and a burner case 21.
The burner case 21 is installed in the interior of the machine wall 1
1 On the front side, it is detachably provided on the outer side of the hot air passage chamber 22 formed on the outer side of the machine wall 11 so as to correspond to the inlet side of the blower chamber 17, and the dryer 1 and the like are installed, dried and discharged. An operation device 23 for starting and stopping each work is detachably provided on the machine wall 11 on the front side.

【0013】排風機24は、前記背面側の機壁11で、
左右の前記排風室16,16に連通すべく設けた排風路
室25中央後部側排風胴26に設け、又この背面側の機
壁11には、この排風機24を回転駆動する排風機モー
タ27を設けている。28は、バルブモータで前記繰出
バルブ18,18を減速機構を介して回転駆動させてい
る。
The blower 24 is a machine wall 11 on the rear side,
The exhaust passage chamber 25 provided to communicate with the left and right exhaust chambers 16, 16 is provided in the central rear side exhaust cylinder 26, and the exhaust wall 24 on the rear side of the exhaust passage rotates the exhaust fan 24. A fan motor 27 is provided. A valve motor 28 rotationally drives the delivery valves 18, 18 via a speed reduction mechanism.

【0014】前記粒径選別装置3は、前記横側機壁11
の外側部に設け、内部には大粒径穀粒と未熟粒とに選別
する粒径選別モータで回転駆動する選別網を回転自在に
軸支し、該選別網を漏下した未熟粒は、流下漏斗29の
一側部へ集穀される。この流下漏斗29下部には開閉自
在な未熟粒開閉弁30を設け、この未熟粒開閉弁30の
開状態で未熟粒は、未熟粒流下筒31を経て未熟粒タン
ク32内へ供給される。又該未熟粒開閉弁30の閉状態
で未熟粒は、未熟粒流下筒33を経て前記乾燥機1の昇
穀機34下部に設けた張込ホッパ35内へ供給される。
乾燥開始初期の選別のときは該選別網の回転を増速、又
は傾斜させて、未熟粒を早期に多量除去させている。
The particle size selecting device 3 includes the lateral machine wall 11
Of the immature grain that leaks through the sorting net is rotatably rotatably supported by a sorting net that is rotatably driven by a particle size sorting motor that sorts large-grained grains and immature grains in the inside. Grains are collected on one side of the downflow funnel 29. An immature grain opening / closing valve 30 that can be opened and closed is provided below the downflow funnel 29, and in the opened state of the immature grain opening / closing valve 30, the immature grains are supplied into the immature grain tank 32 through the immature grain downflow cylinder 31. When the immature grain opening / closing valve 30 is closed, the immature grains are supplied through the immature grain flow-down cylinder 33 into the squeeze hopper 35 provided below the grain raising machine 34 of the dryer 1.
At the time of sorting at the initial stage of the start of drying, the rotation of the sorting net is accelerated or inclined to remove a large amount of immature grains early.

【0015】未熟粒計量機36は、該未熟粒タンク32
下側に設け、この未熟粒タンク32内へ供給されて貯留
される未熟粒の重量が計測される。前記選別網内で選別
されて移送される大粒径穀粒は、この選別網終端部から
大粒径受漏斗37内へ供給され、この大粒径受漏斗37
下部には開閉自在な大粒径開閉弁38を設け、この大粒
径開閉弁38の半開状態で一部の大粒径穀粒は、大粒径
流下筒39を経て前記乾燥装置4へサンプル穀粒として
供給され、残りは大粒径流下筒40を経て前記昇穀機3
4の前記張込ホッパ35内へ供給される。又該大粒径開
閉弁38の閉状態で全ての大粒径穀粒は、該大粒径流下
筒40を経て該昇穀機34の該張込ホッパ35内へ供給
される。これらの内のいずれか一方が行われる。
The immature grain weighing machine 36 is provided in the immature grain tank 32.
The weight of the immature grains provided on the lower side and supplied to and stored in the immature grain tank 32 is measured. The large particle size grains that are sorted and transferred in the sorting net are supplied into the large particle size funnel 37 from the terminal end of the sorting net, and the large particle size funnel 37 is supplied.
A large particle size opening / closing valve 38 that can be opened and closed is provided in the lower portion, and when the large particle size opening / closing valve 38 is in a half-opened state, a part of the large particle size grain is sampled to the drying device 4 via the large particle size downflow tube 39. The grain is supplied as the grain, and the rest is passed through the large grain size falling pipe 40 and the grain raising machine 3
4 is fed into the tensioning hopper 35. Further, when the large particle size opening / closing valve 38 is closed, all the large particle size grains are supplied into the hopper 35 of the grain raising machine 34 through the large particle size downflow cylinder 40. Either one of these is done.

【0016】前記乾燥装置4は、供給された一部の大粒
径穀粒を乾燥するサンプル乾燥室41を中央部に設け、
このサンプル乾燥室41下部には移送螺旋を設け、この
サンプル乾燥室41一方側には遠赤外線ヒータ42を内
装したサンプル熱風装置を設け、又他方側には熱風を吸
引排風するサンプル排風機43を設けている。この乾燥
装置4下側には、このサンプル乾燥室41内の大粒径穀
粒の重量を計測する大粒径計量機44を設けている。
The drying device 4 is provided with a sample drying chamber 41 for drying a part of the supplied large-sized grains in a central portion,
A transfer spiral is provided in the lower portion of the sample drying chamber 41, a sample hot air device having a far infrared heater 42 therein is provided on one side of the sample drying chamber 41, and a sample exhaust device 43 for sucking and exhausting hot air is provided on the other side. Is provided. A large particle size measuring machine 44 for measuring the weight of the large particle size grains in the sample drying chamber 41 is provided below the drying device 4.

【0017】前記籾摺装置5は、前記乾燥装置4下側に
設け、該サンプル乾燥室41の該移送螺旋より供給され
る大粒径穀粒を、内装した移送籾摺螺旋で籾摺して玄米
と籾殻とに選別し、籾殻は機外へ排出され、玄米は玄米
漏斗45へ供給される。この玄米漏斗45下部には、玄
米切換弁46を設け、この玄米切換弁46の半開状態で
下側の前記食味検出装置8へ玄米流下筒47を経て供給
と、下側の前記胴割品位検出装置6へ玄米流下筒48を
経て供給とが行われ、更に下側の前記外観品位検出装置
7へ供給される。
The hulling device 5 is provided below the drying device 4, and the large grain grains supplied from the transfer spiral of the sample drying chamber 41 are hulled by an internal transfer hulling spiral. The rice is separated into brown rice and rice husk, the rice husk is discharged to the outside of the machine, and the brown rice is supplied to the brown rice funnel 45. A brown rice switching valve 46 is provided below the brown rice funnel 45, and when the brown rice switching valve 46 is in a half-opened state, it is supplied to the taste detecting device 8 on the lower side through a brown rice falling tube 47, and the lower splitting quality is detected. It is supplied to the apparatus 6 through the brown rice falling tube 48, and is further supplied to the appearance quality detecting apparatus 7 on the lower side.

【0018】前記食味検出装置8は、光源が発する近赤
外分光分析装置及び食味評価値計算の係数を記憶する記
憶装置等からなる。これらにより該玄米流下筒47を経
て供給されたサンプル用の玄米を受けて食味を、例えば
良い、普通及び悪いの3段階に検出され、検出済玄米
は、玄米排出筒49を経て前記昇穀機34の前記張込ホ
ッパ35へ供給される。
The taste detecting device 8 comprises a near-infrared spectroscopic analysis device emitted from a light source and a storage device for storing the coefficient for calculating the taste evaluation value. By these, the brown rice for the sample supplied through the brown rice lowering cylinder 47 is received and the taste is detected in three stages, for example, good, normal and bad, and the detected brown rice is passed through the brown rice discharging cylinder 49 and the grain refiner. It is supplied to the tension hopper 35 of 34.

【0019】前記品位検出装置6,7は、前記胴割品位
検出装置6と該外観品位検出装置7とからなる。このう
ち該胴割品位検出装置6は、透過光検出部を備え、この
透過光量検出によって胴割れの有無乃至その程度を判定
しうる。一方該外観品位検出装置7は、透過光量及び反
射光量等を照射して得られるデータに基づいて、前記玄
米流下筒48を経て供給されたサンプル用の玄米を受
け、この玄米内に混入する被害粒、異種穀粒、異物、死
米及び着色粒等の混入量が検出される。こうして、例え
ば良い、普通及び悪いの3段階に検出され、検出済玄米
は、玄米排出筒50を経て前記集穀樋19へ供給され
る。
The quality detecting devices 6 and 7 include the body split quality detecting device 6 and the appearance quality detecting device 7. Of these, the body split quality detection device 6 includes a transmitted light detection unit, and the presence or extent of the body crack can be determined by detecting the amount of transmitted light. On the other hand, the appearance quality detecting device 7 receives the brown rice for the sample supplied through the brown rice flow down tube 48 based on the data obtained by irradiating the transmitted light amount, the reflected light amount, etc., and damages that are mixed into the brown rice. The amount of mixed grains, foreign grains, foreign matter, dead rice, colored grains, etc. is detected. Thus, for example, the detected brown rice is detected in three stages of good, normal and bad, and the detected brown rice is supplied to the grain collecting trough 19 through the brown rice discharge pipe 50.

【0020】燃料ポンプ51は、燃料バルブを有して、
前記バーナケース21下板外側に設け、この燃料バルブ
の開閉により、この燃料ポンプ51で燃料タンク52内
の燃料を吸入して、前記バーナ20へ供給させている。
送風機53は、上板外側に設け、変速用の送風機モータ
54で変速回転駆動させ、供給燃料量に見合った燃焼用
空気を該バーナ20へこの送風機53で送風させてい
る。
The fuel pump 51 has a fuel valve,
The fuel pump 51 is provided outside the lower plate of the burner case 21, and by opening and closing the fuel valve, the fuel in the fuel tank 52 is sucked by the fuel pump 51 and supplied to the burner 20.
The blower 53 is provided on the outer side of the upper plate, is rotationally driven at a variable speed by a blower motor 54 for shifting, and blows the combustion air corresponding to the supplied fuel amount to the burner 20 by the blower 53.

【0021】前記除湿装置10は、前記乾燥機1前方部
に配置され、吸入口から吸入された外気風を除湿風に変
換するために、冷媒である低温低圧ガスは、圧縮機にて
高温高圧ガスへ断熱圧縮されて凝縮器を通過する際に熱
を奪われて高温高圧液体へ変化し、その後膨張弁にて低
温低圧液体へ圧力降下され、さらに蒸発器を通過する際
に熱を吸収して低温低圧ガスへ変化し、順次冷媒がこの
サイクルの繰返しが行われ、これにより該除湿装置10
内を通過する外気風は除湿されて除湿風に変換され、こ
の除湿風は、前記熱風路室25から前記送風室17を経
て前記乾燥室15,15を通過する。
The dehumidifying device 10 is arranged at the front part of the dryer 1, and in order to convert the outside air sucked from the suction port into dehumidified wind, the low temperature low pressure gas which is a refrigerant is high temperature high pressure in the compressor. When it is adiabatically compressed to gas, it is deprived of heat when it passes through the condenser and changes to a high-temperature high-pressure liquid, after which it is reduced in pressure to a low-temperature low-pressure liquid by an expansion valve, and then absorbs heat when it passes through the evaporator. Is changed to low-temperature low-pressure gas, and the refrigerant is sequentially repeated in this cycle.
The outside air passing through the inside is dehumidified and converted into dehumidified air, and the dehumidified air passes from the hot air passage chamber 25, the blower chamber 17, and the drying chambers 15, 15.

【0022】拡散盤55は、前記移送樋12底板の前後
方向中央部で、移送穀粒を前記貯留室14へ供給する供
給口の下側に設け、この貯留室14へ穀粒を均等に拡散
還元させている。排出漏斗55′は、前記移送樋12始
端部の底板部に設け、又この底板部には開閉自在な排出
切換弁59を設け、この排出漏斗55′下部には開閉自
在な排出開閉弁56を設け、排出作業のときは、この排
出開閉弁56の開状態と該排出切換弁59の全開状態と
により、排出筒57を経て乾燥済穀粒は、機外へ排出さ
れる。乾燥作業のときは、該排出開閉弁56の閉状態と
該排出切換弁59の半開状態とにより、穀粒は該移送樋
12を経て前記貯留室14内へ循環供給と、排出筒58
を経て一部の穀粒は、前記粒径選別装置3へ供給とが行
われるか、又は該排出切換弁59の閉状態により、穀粒
は該移送樋12を経て該貯留室14内へのみ循環供給
か、これらの内のいずれか一方が行われる。又張込作業
のときは、該排出切換弁59の閉状態により、穀粒は該
移送樋12を経て該貯留室14内へ張込される。
The diffusion board 55 is provided at the center of the bottom plate of the transfer gutter 12 in the front-rear direction, below the supply port for supplying the transfer grains to the storage chamber 14, and evenly diffusing the grains into the storage chamber 14. I'm giving back. The discharge funnel 55 'is provided on the bottom plate portion of the starting end of the transfer gutter 12, and a discharge switching valve 59 that can be opened and closed is provided on the bottom plate portion. A discharge on-off valve 56 that can be opened and closed is provided below the discharge funnel 55'. During the installation and discharge operation, the dried grains are discharged to the outside of the machine through the discharge cylinder 57 by the opened state of the discharge opening / closing valve 56 and the fully opened state of the discharge switching valve 59. During the drying operation, the discharge opening / closing valve 56 is closed and the discharge switching valve 59 is half-opened so that the grains are circulated and supplied into the storage chamber 14 through the transfer gutter 12 and the discharge cylinder 58.
Some of the grains are supplied to the particle size selection device 3 through the above or the discharge switching valve 59 is closed, so that the grains only pass through the transfer gutter 12 into the storage chamber 14. Either circulation supply or one of these is performed. In addition, during the staking operation, the discharge switching valve 59 is closed, so that the grains are stretched into the storage chamber 14 through the transfer gutter 12.

【0023】前記昇穀機34は、前記機壁11前側外部
に設けられ、内部にはバケットコンベア60付ベルトを
張設してなり、上端部は、前記移送樋12始端部との間
において投出筒61を設けて連通させ、下端部は、前記
集穀樋19終端部との間において供給樋62を設けて連
通させている。63は昇穀機モータで、該バケットコン
ベア60付ベルト、前記移送樋12内の前記移送螺旋、
前記拡散盤55及び前記集穀樋19内の前記移動螺旋等
を回転駆動させている。
The grain raising machine 34 is provided outside the front side of the machine wall 11 and has a belt with a bucket conveyor 60 stretched inside. The upper end portion is thrown between the transfer gutter 12 and the starting end portion. An outlet pipe 61 is provided for communication, and a lower end portion thereof is provided with a supply gutter 62 between the terminal end portion of the grain collecting trough 19 for communication. 63 is a sublimator motor, the belt with the bucket conveyor 60, the transfer spiral in the transfer gutter 12,
The moving spiral and the like in the diffusion board 55 and the grain collecting trough 19 are rotationally driven.

【0024】前記水分センサ2は、前記昇穀機34の上
下方向ほぼ中央部に設け、この水分センサ2は、前記操
作装置23からの電気的測定信号の発信により、水分モ
ータ64が回転してこの水分センサ2の各部が回転駆動
され、前記バケットコンベア60で上部へ搬送中に落下
する穀粒を受け、この穀粒を挾圧粉砕しながら、この粉
砕穀粒の水分を検出させている。
The moisture sensor 2 is provided substantially vertically in the center of the grain raising machine 34. The moisture sensor 2 is rotated by a moisture motor 64 when an electric measurement signal is transmitted from the operating device 23. Each part of the moisture sensor 2 is rotationally driven, and receives the grains falling while being conveyed to the upper portion by the bucket conveyor 60. While crushing the grains by pressure, the moisture of the crushed grains is detected.

【0025】前記操作装置23は、箱形状でこの箱体の
表面板には、前記乾燥機1、前記水分センサ2、前記熱
風装置9、又は前記除湿装置10等を張込、乾燥及び排
出の各作業別に始動操作する各始動スイッチ65、停止
操作する停止スイッチ66、穀粒の仕上目標水分を操作
位置によって設定する水分設定抓み67、該熱風装置
9、又は該除湿装置10から発生する熱風温度、又は除
湿風温度を操作位置によって設定する穀物種類設定抓み
68、張込量設定抓み69及び乾燥処理方法を設定する
処理設定抓み69′、各種表示項目をデジタル表示する
表示部70及びモニタ表示等を設けている。
The operating device 23 has a box shape, and the drier 1, the moisture sensor 2, the hot air device 9, the dehumidifying device 10, etc. are put on the surface plate of the box for drying, discharging. Each start switch 65 for starting operation for each work, stop switch 66 for stopping operation, moisture setting picker 67 for setting target finishing moisture of grain by operation position, hot air device 9 or hot air generated from dehumidifying device 10 Grain type setting scoop 68 for setting temperature or dehumidifying air temperature according to the operation position, scooping amount setting scoop 69 and processing setting scoop 69 'for setting the drying processing method, display unit 70 for digitally displaying various display items Also, a monitor display is provided.

【0026】前記処理設定抓み69′の操作位置によ
り、図4の如く乾燥方式が、普通乾燥、粗選乾燥、サン
プル乾燥及びサンプル粗選乾燥方式が選定され、これら
乾燥方式により、穀粒の供給個所及び選別済穀粒の供給
個所が制御される。制御装置71は、前記操作装置23
内に設けられ、前記水分センサ2、前記未熟粒計量機3
6、前記大粒径計量機44及び熱風温センサ72が検出
する検出値、該各スイッチ65,66の操作及び該各設
定抓み67,68,69,69′の操作等が入力され、
これらの入力を算術論理演算及び比較演算するCPU7
3等よりなり、このCPU73で前記各モータ27,2
8,54,63,64、前記燃料バルブ及び前記燃料ポ
ンプ51等を始動、停止及び制御等を行い、又前記各開
閉弁30,38,46,56,59を全開閉及び半開す
る各モータを回転及び停止制御を行う構成である。該各
設定抓み67,68,69,69′はロータリースイッ
チ方式とし、操作位置によって所定の数値及び種類等が
設定される。
Depending on the operation position of the processing setting scoop 69 ′, the drying method as shown in FIG. 4 is selected from normal drying, coarse drying, sample drying and sample rough drying. The feeding point and the feeding point of the sorted grain are controlled. The control device 71 is the operation device 23.
The moisture sensor 2 and the immature grain weighing machine 3 provided inside
6, the detection values detected by the large particle size measuring machine 44 and the hot air temperature sensor 72, the operation of each of the switches 65 and 66, the operation of each of the setting scoops 67, 68, 69 and 69 ', etc. are input,
CPU 7 that performs arithmetic logic operation and comparison operation on these inputs
3 and the like, and the CPU 73 operates the motors 27, 2
8, 54, 63, 64, motors for starting, stopping and controlling the fuel valve and the fuel pump 51, and for fully opening and closing and half-opening the on-off valves 30, 38, 46, 56, 59. This is a configuration for performing rotation and stop control. Each of the setting knobs 67, 68, 69, 69 'is of a rotary switch type, and predetermined numerical values and types are set according to the operating position.

【0027】前記制御装置71による穀粒の乾燥制御
は、下記の如く行われる構成である。即ち、前記処理設
定抓み69′がサンプル乾燥位置へ操作され、乾燥作業
を開始する前記始動スイッチ65が操作され、これらの
操作が該CPU73へ入力される。この入力により、乾
燥作業が開始され(ステップ101)、前記熱風装置9
及び前記除湿装置10は、始動されず外気風が前記乾燥
室15,15を通過する通風乾燥が開始され(ステップ
102)、穀粒は前記貯留室14と前記粒径選別装置3
との両者へ供給され、この粒径選別装置3で大粒径穀粒
と未熟粒とに選別され(ステップ103)、選別済大粒
径穀粒の一部がサンプリング穀粒として抽出され(ステ
ップ104)、このサンプリング穀粒の一部は、前記胴
割品位検出装置6及び前記外観品位検出装置7へ供給さ
れ、図5の如く死米混入量以外の被害粒、着色粒、異種
穀粒及び異物等の混入率による品位が、例えば良い、普
通及び悪いと検出され、死米混入が無い及び有ると検出
され、又残りのサンプリング穀粒は、前記食味検出装置
8へ供給され、食味が、例えば良い、普通及び悪いと検
出される(ステップ105)。
The drying control of the grain by the control unit 71 is configured as follows. That is, the processing setting knob 69 'is operated to the sample drying position, the start switch 65 for starting the drying operation is operated, and these operations are input to the CPU 73. By this input, the drying work is started (step 101), and the hot air device 9
Further, the dehumidifying device 10 is not started, and the ventilation drying in which the outside air passes through the drying chambers 15 and 15 is started (step 102), and the grains are stored in the storage chamber 14 and the particle size selection device 3
And large grain size grains and immature grain size are sorted by the grain size sorting device 3 (step 103), and a part of the sorted large grain size grains is extracted as a sampling grain grain (step 103). 104), a part of the sampled grains is supplied to the body splitting quality detection device 6 and the appearance quality detection device 7, and as shown in FIG. 5, damaged grains other than the amount of dead rice mixed, colored grains, different grains, and The quality due to the mixing ratio of foreign matters and the like is detected as, for example, good, normal and bad, and it is detected that there is and is not mixed with dead rice, and the remaining sampling grains are supplied to the taste detecting device 8 and the taste is For example, good, normal and bad are detected (step 105).

【0028】これら品位、死米量及び食味の検出結果に
より、図5の如く乾燥モードは、前記除湿装置10から
の除湿風による除湿乾燥モード、前記熱風装置9からの
熱風による熱風乾燥の外気温度より、例えば10℃高い
低温一定熱風による低温一定熱風乾燥モード、外気温度
より10℃高い低温度より順次所定時間経過毎、又は所
定水分毎に所定温度上昇する低温ステップ乾燥モード、
及び張込穀粒量によって熱風温度が設定される張込量熱
風乾燥モードの4モード分類された、これら4モードか
ら乾燥モードが選定され(ステップ106)、通風乾燥
が選定された乾燥モードに切換される(ステップ10
7)。
Based on the detection results of the quality, the amount of dead rice and the taste, the drying mode as shown in FIG. 5 is the dehumidifying and drying mode by the dehumidifying air from the dehumidifying device 10, and the outside air temperature of the hot air drying by the hot air from the hot air device 9. For example, a low temperature constant hot air drying mode with a low temperature constant hot air that is higher by 10 ° C., a low temperature step drying mode in which a predetermined temperature is sequentially increased from a low temperature that is higher than the outside air temperature by 10 ° C. or a predetermined temperature is increased every predetermined moisture,
And the hot air temperature is set according to the amount of grain to be inflated, the four modes of the infiltration amount hot air drying mode are classified, and the drying mode is selected from these four modes (step 106), and ventilation drying is switched to the selected drying mode. (Step 10
7).

【0029】除湿乾燥モード及び低温一定熱風乾燥モー
ドが選定されると、前記粒径選別装置3へ供給された所
定穀粒量の内の前記乾燥装置4へ供給された選別済大粒
径穀粒の重量は、前記大粒径計量機44で計量され、又
前記未熟粒タンク32へ排出された選別済未熟粒の重量
は、前記未熟粒計量機36で計量され、これら計量され
た大粒径穀粒重量と未熟粒重量とによって未熟粒の混入
量が多いか、又は少ないかが検出され、選別は継続か、
又は中止かが決定される(ステップ108)。
When the dehumidifying and drying mode and the low temperature constant hot air drying mode are selected, the selected large grain size grains supplied to the drying device 4 out of the predetermined grain amount supplied to the grain size selecting device 3 are selected. Is weighed by the large grain size measuring machine 44, and the weight of the sorted immature grains discharged to the immature grain tank 32 is weighed by the immature grain weighing machine 36. Whether the amount of immature grains is large or small is detected by the weight of grains and the weight of immature grains, and the selection is continued,
Alternatively, it is determined whether to stop (step 108).

【0030】低温ステップ乾燥モード及び張込量熱風乾
燥モードのときは、前記粒径選別装置3による選別は行
われない。併せて、前記制御装置71は次の機能を有す
る。前記水分設定抓み67を操作して設定した仕上目標
水分と同じ穀粒水分を、前記水分センサ2が検出する
と、穀粒の乾燥が終了したと検出されて、前記乾燥機1
を自動停止制御する。
In the low temperature step drying mode and the swelling amount hot air drying mode, sorting by the grain size sorting device 3 is not performed. In addition, the control device 71 has the following functions. When the moisture sensor 2 detects the same grain moisture as the finishing target moisture set by operating the moisture setting knob 67, it is detected that the drying of the grain has been completed, and the dryer 1
Automatic stop control.

【0031】前記水分センサ2が検出する複数回の穀粒
水分から算出する平均穀粒水分より、高水分の多い穀粒
は未熟粒が多いと検出され、又水分の少ない穀粒は未熟
粒が少ないと検出され、この穀粒の精粒比率が算出さ
れ、算出された精粒比率の高い、例えば95%以上の穀
粒のときは、一般的に食味が良いとされる穀粒であり、
図8の如くこの精粒比率95%の穀粒のときは、乾燥モ
ードを前記熱風装置9からの熱風による熱風乾燥の内の
低温一定熱風乾燥モードが選定される。精粒比率が標準
の90%〜95%の穀粒のときは、低温ステップ乾燥モ
ードが選定される。又精粒比率が低い90%以下の穀粒
のときは、張込量熱風乾燥モードが選定されて乾燥され
る方式とするもよい。
From the average grain moisture calculated from a plurality of grain moistures detected by the moisture sensor 2, it is detected that grains having a high moisture content have a large amount of immature grains, and grains having a low moisture content have an immature grain. Detected as low, the grain ratio of this grain is calculated, the calculated grain ratio is high, for example, when the grain is 95% or more, the grain is generally considered to have a good taste,
As shown in FIG. 8, when the grain ratio is 95%, the drying mode is the low temperature constant hot air drying mode of the hot air drying by the hot air from the hot air device 9. The low temperature step drying mode is selected for grains having a standard grain ratio of 90% to 95%. Further, when the grain ratio is 90% or less, which has a low refined grain ratio, it is possible to adopt a method in which a swelling amount hot air drying mode is selected and dried.

【0032】又前記未熟粒計量機36と前記大粒径計量
機44とが計量する未熟粒と大粒径穀粒との計量結果に
より、精粒比率が算出され、この算出された精粒比率に
より、上記の如く乾燥モードが、低温一定熱風乾燥モー
ド、低温ステップ乾燥モード及び張込量熱風乾燥モード
が選定されて乾燥される方式とするもよい。以下、上記
実施例の作用について説明する。
Further, the fine grain ratio is calculated based on the weighing result of the immature grain and the large grain grain measured by the immature grain weighing machine 36 and the large grain size weighing machine 44, and the calculated fine grain ratio is calculated. Accordingly, as described above, the drying mode may be a method in which a low temperature constant hot air drying mode, a low temperature step drying mode, and a stake amount hot air drying mode are selected and dried. The operation of the above embodiment will be described below.

【0033】操作装置23の各設定抓み67,68,6
9,69′を所定位置へ操作し、処理設定抓み69′を
サンプル乾燥位置へ操作し、乾燥作業を開始する始動ス
イッチ65を操作することにより、乾燥方式はサンプル
乾燥が選定され、穀粒乾燥機1の各部及び水分センサ2
等が始動し、外気風が熱風路室22、送風室17から各
穀粒乾燥室15,15を通過して各排風室16,16及
び排風路室25を経て排風機24で吸引排風される。
Setting knobs 67, 68, 6 of the operating device 23
The sample drying is selected as the drying method by operating 9, 69 'to a predetermined position, operating the processing setting knob 69' to the sample drying position, and operating the start switch 65 for starting the drying operation. Each part of the dryer 1 and the moisture sensor 2
Etc. are started, and the outside air is passed from the hot air passage chamber 22, the air blowing chamber 17 through the grain drying chambers 15, 15 and then through the air exhaust chambers 16, 16 and the air exhaust passage chamber 25 to be sucked and discharged by the air blower 24. To be winded.

【0034】穀粒貯留室14内へ収容された穀粒は、こ
の貯留室14から該各乾燥室15,15内を流下中に、
この外風に晒されて乾燥され、各繰出バルブ18,18
で下部へと繰出されて流下して集穀樋19から供給樋6
2を経て昇穀機34内へ下部の移送螺旋で移送供給さ
れ、バケットコンベア60で上部へ搬送されて投出筒6
1を経て移送樋12内へ供給され、この移送樋12から
拡散盤55上へ上部の移送螺旋で移送供給され、この拡
散盤55で該貯留室14内へ均等に拡散還元されて外気
風による通風循環乾燥される。
The grains stored in the grain storage chamber 14 are flowing from the storage chamber 14 into the drying chambers 15 and 15,
Each of the feeding valves 18, 18 is exposed to the outside wind and dried.
It is fed to the lower part at the bottom and flows down and is supplied from the grain collecting gutter 19 to the gutter 6
2 is transferred and fed by the lower transfer spiral into the grain-raising machine 34, and is conveyed to the upper part by the bucket conveyor 60 and the ejection cylinder 6
1 is supplied into the transfer gutter 12 and is then supplied from the transfer gutter 12 onto the diffusion plate 55 by an upper transfer spiral, and is uniformly diffused and reduced into the storage chamber 14 by the diffusion plate 55 and is supplied by outside air. Draft circulation drying.

【0035】又乾燥中の一部の穀粒は、粒径選別装置3
へ供給され、この粒径選別装置3内で大粒径穀粒と未熟
粒とに選別され、選別済未熟粒は流下漏斗29から未熟
粒流下筒33を経て前記昇穀機34の張込ホッパ35内
へ供給され、前記乾燥機1へ還元される。選別済大粒径
穀粒は、大粒径漏斗37から大粒径流下筒39を経て乾
燥装置4へ供給されて乾燥され、乾燥済大粒径穀粒は籾
摺装置5へ供給されて籾摺され、一部の籾摺済玄米は玄
米漏斗45から玄米流下筒47を経て食味検出装置8へ
供給されて、玄米の食味が、良い、普通及び悪いと検出
され、又他の一部の籾摺済玄米は該玄米漏斗45から玄
米流下筒48を経て胴割品位検出装置6へ供給され、更
に外観品位検出装置7へ供給されて、玄米の品位が、良
い、普通及び悪いと検出されると同時に、死米の混入が
無い、又は有ると検出される。
Further, a part of the grains which are being dried has a particle size selection device 3
Is fed to the grain size selection device 3 to be sorted into large grain size grains and immature grain size, and the sorted immature grain size is fed from the downflow funnel 29 through the immature grain flow down tube 33 to the hopper of the grain raising machine 34. It is supplied into the dryer 35 and returned to the dryer 1. The sorted large grain grain is supplied from the large grain funnel 37 through the large grain downflow tube 39 to the drying device 4 and dried, and the dried large grain grain is supplied to the hulling device 5 and paddy. Some of the hulled brown rice is then fed from the brown rice funnel 45 to the taste detecting device 8 through the brown rice falling tube 47, and the taste of the brown rice is detected as good, normal and bad, and another part of the rice is detected. The grain-polished brown rice is supplied from the brown rice funnel 45 through the brown rice falling tube 48 to the body split quality detecting device 6 and further to the external appearance quality detecting device 7 to detect that the quality of the brown rice is good, normal or bad. At the same time, it is detected that dead rice is not mixed in or is present.

【0036】これら検出された食味、品位及び死米混入
によって、前記除湿装置10から発生する除湿熱風で、
乾燥する除湿乾燥モードか、又は熱風装置9から発生す
る熱風で熱風乾燥する低温一定熱風乾燥モード、低温ス
テップ乾燥モード及び張込量熱風乾燥モードかに選定さ
れ、選定された乾燥モードに切換制御され、上記の通風
乾燥と同じように穀粒は循環され、選定された乾燥モー
ドで乾燥される。
The dehumidifying hot air generated from the dehumidifying device 10 due to the detected taste, quality and dead rice mixture,
It is selected from a dehumidification drying mode for drying, a low temperature constant hot air drying mode for hot air drying with hot air generated from the hot air device 9, a low temperature step drying mode and a stake amount hot air drying mode, and switching control is performed to the selected drying mode. , Grains are circulated and dried in the selected drying mode in the same manner as draft drying.

【0037】前記水分センサ2で検出される穀粒水分
が、前記水分設定抓み67を操作して設定した仕上目標
水分と同じ穀粒水分が検出されると、穀粒の乾燥が終了
したと検出され、制御装置71で自動制御して前記乾燥
機1が自動停止され、穀粒の乾燥が停止される。
When the grain moisture detected by the moisture sensor 2 is the same as the finishing target moisture set by operating the moisture setting scoop 67, it is determined that the drying of the grain is completed. It is detected, and is automatically controlled by the control device 71 to automatically stop the dryer 1, and the drying of the grain is stopped.

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

図は、この発明の一実施例を示す。 The figure shows an embodiment of the invention.

【図1】穀粒乾燥機の全体側面図。FIG. 1 is an overall side view of a grain dryer.

【図2】図1のA−A拡大断面図。FIG. 2 is an enlarged sectional view taken along line AA of FIG.

【図3】ブロック図。FIG. 3 is a block diagram.

【図4】乾燥方式と穀粒供給個所との関係図。FIG. 4 is a diagram showing the relationship between the drying method and the grain supply points.

【図5】乾燥モードと粒径選別装置による選別との関係
図。
FIG. 5 is a diagram showing the relationship between a drying mode and sorting by a particle size sorting device.

【図6】フローチャート。FIG. 6 is a flowchart.

【図7】穀粒乾燥機の一部の一部破断せる拡大正面図。FIG. 7 is an enlarged front view in which a part of the grain dryer is partially broken.

【図8】他の実施例の精粒比率と乾燥モードとの関係
図。
FIG. 8 is a relationship diagram between a fine grain ratio and a drying mode in another example.

【符号の説明】 3 粒径選別装置 6,7 品位検出装置 8 食味検出装置 14 穀粒貯留室 15 穀粒乾燥室[Explanation of Codes] 3 Particle Size Sorting Device 6, 7 Quality Detection Device 8 Taste Detection Device 14 Grain Storage Room 15 Grain Drying Room

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 上部の穀粒貯留室14から下部の穀粒乾
燥室15ヘ穀粒を繰出し流下させながら熱風を該乾燥室
15へ通風して乾燥しながら循環乾燥中の一部の穀粒を
粒径選別装置3へ供給して大粒径穀粒と未熟粒とに選別
する穀粒乾燥機において、選別した該大粒径穀粒と該未
熟粒との両者を該乾燥機へ還元して乾燥するサンプリン
グ乾燥方式で該選別済大粒径穀粒の一部を食味検出装置
8へ供給して食味検出、又は胴割や着色粒等を判別しう
る品位検出装置6,7等へ供給して品位検出のときは、
熱風乾燥を中止して該乾燥室15へ外気風が通過して乾
燥する通風乾燥に乾燥制御手段で制御することを特徴と
する乾燥制御方式。
1. A part of the grains being circulated and dried while hot air is blown into the drying chamber 15 while the grains are being drawn from the upper grain storage chamber 14 to the lower grain drying chamber 15 and flowing down. In a grain drier for selecting the large grain size grain and the immature grain size by supplying the grain size sorting device 3 to the large grain size grain and the immature grain size, and reducing both the sorted large grain grain size grain and the immature grain grain to the drier. A part of the selected large-sized grain is supplied to the taste detecting device 8 by the sampling drying method of drying by detecting the taste, or is supplied to the quality detecting devices 6, 7 etc. capable of distinguishing the taste split or the colored particles. When detecting the quality,
A drying control method characterized in that hot-air drying is stopped and ventilation drying is performed in which outside air is allowed to pass through the drying chamber 15 for drying, which is controlled by a drying control means.
JP2771292A 1992-02-14 1992-02-14 Drying control system for grain drier Pending JPH05223451A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2771292A JPH05223451A (en) 1992-02-14 1992-02-14 Drying control system for grain drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2771292A JPH05223451A (en) 1992-02-14 1992-02-14 Drying control system for grain drier

Publications (1)

Publication Number Publication Date
JPH05223451A true JPH05223451A (en) 1993-08-31

Family

ID=12228613

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2771292A Pending JPH05223451A (en) 1992-02-14 1992-02-14 Drying control system for grain drier

Country Status (1)

Country Link
JP (1) JPH05223451A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10306978A (en) * 1997-05-08 1998-11-17 Iseki & Co Ltd Sample grain inspection device for grain drying apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10306978A (en) * 1997-05-08 1998-11-17 Iseki & Co Ltd Sample grain inspection device for grain drying apparatus

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