JPS5953465B2 - Automatic hot air temperature control device for grain dryer - Google Patents
Automatic hot air temperature control device for grain dryerInfo
- Publication number
- JPS5953465B2 JPS5953465B2 JP8805877A JP8805877A JPS5953465B2 JP S5953465 B2 JPS5953465 B2 JP S5953465B2 JP 8805877 A JP8805877 A JP 8805877A JP 8805877 A JP8805877 A JP 8805877A JP S5953465 B2 JPS5953465 B2 JP S5953465B2
- Authority
- JP
- Japan
- Prior art keywords
- hot air
- grain
- temperature
- tank
- injection nozzles
- 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
Links
- 238000002347 injection Methods 0.000 claims description 26
- 239000007924 injection Substances 0.000 claims description 26
- 238000002485 combustion reaction Methods 0.000 claims description 15
- 238000001035 drying Methods 0.000 claims description 12
- 239000000446 fuel Substances 0.000 claims description 11
- 230000007423 decrease Effects 0.000 claims description 6
- 230000008859 change Effects 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims 1
- 239000011888 foil Substances 0.000 description 8
- 230000009471 action Effects 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 4
- 230000005284 excitation Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
Description
【発明の詳細な説明】
本発明は穀物乾燥機の熱風温度自動調節装置の改良に係
り、穀物乾燥機に設けた穀物槽の側壁面に、上下に適宜
な間隔を介して縦列状に配置したそれぞれの設定位置で
槽内穀物量を測定する複数個のレベル計を植設し、その
乾燥部機体に装設した火熱発生機に複数個の噴射ノズル
を嵌装し、該噴射ノズルの給油管にそれぞれ開閉弁を設
け、また前記火熱発生機に連設した熱風室に任意の異種
温度で個別的に作動する複数個の温度スイッチを設け、
これらを関連的に、かつ電気的に接続して前記穀物槽に
対する供給穀物量の増減即ち給穀量に順応して前記噴射
ノズルの燃料噴射量を直ちに増減変更し所定の熱風温度
に補正すると共に、その熱風の温度変化を適正な範囲に
規正し、穀物の乾燥作用を高性能に改善合理化し、かつ
自動化した新規な装置を開発し提供せんとするものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in an automatic hot air temperature control device for a grain dryer. A plurality of level gauges are installed to measure the amount of grain in the tank at each setting position, and a plurality of injection nozzles are fitted to a heat generator installed in the drying section body, and a fuel supply pipe of the injection nozzle is installed. are each provided with an on-off valve, and a plurality of temperature switches that individually operate at arbitrary different temperatures are provided in the hot air chamber connected to the fire heat generator,
These are connected electrically in relation to each other to immediately increase or decrease the fuel injection amount of the injection nozzle in accordance with the increase or decrease in the amount of grain supplied to the grain tank, that is, the amount of grain fed, and to correct it to a predetermined hot air temperature. The purpose of this project is to develop and provide a new and automated device that regulates the temperature change of the hot air within an appropriate range, improves and streamlines the drying action of grains, and is automated.
本発明の実施態様を例示図について説明すると、図中符
号1はその内部に熱風室2.穀物流路3.3.排風室4
,4を並立し、また排風機5゜火熱発生機6を具備した
乾燥部機体であって、該機体1の上部に穀物槽7を塔載
し、またその一側に昇降機8を立設して一体的に形成し
た循環式穀物乾燥機である。The embodiment of the present invention will be described with reference to illustrative drawings. In the drawing, reference numeral 1 indicates a hot air chamber 2. Grain channel 3.3. Exhaust room 4
, 4 in parallel, and is also equipped with a 5° exhaust fan and a heat generator 6. A grain tank 7 is mounted on the top of the machine 1, and an elevator 8 is installed upright on one side. This is a circulating grain dryer that is integrally formed.
次に、前記火熱発生機6を第2図について詳述すると、
送風機9に連設した円筒状吹口10の前半部に複数個の
噴射ノズルlla、llbを略軸心方向平行に嵌装集設
すると共に、その付近に点火プラグ12を突設し、また
前記吹口10の吐出側13に複数個の異径多孔壁筒冠状
籠体14,15を適宜な間隔16を介して略同心的に重
設した燃焼室17を臨設し、該燃焼室17の前記側壁に
遮蔽板18を、後部側壁にスワール壁19をそれぞれ装
設し、これら機部9,10,17を一体的に形成しであ
る。Next, the fire heat generator 6 will be explained in detail with reference to FIG.
A plurality of injection nozzles lla, llb are fitted and arranged substantially parallel to the axial direction in the front half of a cylindrical blower 10 connected to the blower 9, and a spark plug 12 is protruded from the vicinity thereof. A combustion chamber 17 is provided on the discharge side 13 of the combustion chamber 10, in which a plurality of porous-wall cylinder crown-shaped cages 14 and 15 of different diameters are superimposed substantially concentrically at an appropriate interval 16, and on the side wall of the combustion chamber 17. A shielding plate 18 and a swirl wall 19 are installed on the rear side wall, respectively, and these machine parts 9, 10, and 17 are integrally formed.
なお、20は前記各ノズル11a、llbにそれぞれ給
油するための送油管で、容管20,20にはそれぞれ開
閉弁を備えた電磁バルブ21a、21bを介装し、また
前記プラグ12の電線にはトランス22が介装しである
。Incidentally, reference numeral 20 denotes an oil supply pipe for supplying oil to each of the nozzles 11a and llb, and electromagnetic valves 21a and 21b each having an on-off valve are installed in the container pipes 20 and 20, and the electric wire of the plug 12 is connected to the oil pipe 20. A transformer 22 is installed.
なお前記各噴射ノズルlla、llbはその口径を1対
2の比率に開口されているが、その個数および口径比は
任意で何ら限定されるものでない。Although each of the injection nozzles lla and llb has an aperture ratio of 1:2, the number and aperture ratio are arbitrary and are not limited in any way.
次に、前記穀物槽7であるが、穀物槽7の一側壁面に上
下に適宜な間隔を介して縦列状に配置したそれぞれの設
定位置a、 l)、 cで槽内穀物量を測定する複
数個のレベル計23a、23b、23Cを植設し、その
各部位a、 l)、 cにおいて供給穀物量を測定
した場合、直ちに各レベル計に設けた制御回路Aの励磁
コイルR4,R5,R6を個別的に作動しその信号によ
り、別に設けた熱風温度調節回路24の接点R4,R5
,R6を適宜に開閉するように形成しである。Next, regarding the grain tank 7, the amount of grain in the tank is measured at respective set positions a, l), and c, which are arranged vertically in a column on one side wall surface of the grain tank 7 at appropriate intervals. When a plurality of level meters 23a, 23b, and 23C are installed and the amount of grain to be supplied is measured at each of the locations a, l), and c, the excitation coils R4, R5, and The contacts R4 and R5 of the separately provided hot air temperature control circuit 24 are activated by individually operating R6 and using the signal.
, R6 are formed to open and close as appropriate.
また、前記熱風室2の内部側壁には、前述の穀物槽7の
各部位a、 l)、 cにおける穀物量に対応した
適宜な熱風温度(40℃)(50℃)(60℃)を選択
して作動する自動復帰型サーモスタット25a、25b
、25Cから成る温度スイッチ25が装設され、その各
接点は前記調節回路24に介在させである。Further, on the inner side wall of the hot air chamber 2, appropriate hot air temperatures (40°C) (50°C) (60°C) are selected corresponding to the amount of grain in each part a, l), and c of the grain tank 7. Automatic return type thermostats 25a, 25b that operate by
, 25C is installed, each contact of which is interposed in the regulating circuit 24.
そこで第3図において、前記熱風温度調節回路24を説
明すると、電源端子R−5の間に前述した設定温度(4
0℃)で開閉作動するb接点のサーモスタツ)−253
と励磁コイルR1,b接点のR5,R6,a接点のR4
を直列状に連絡し、また設定温度(50℃)で開閉作動
するb接点のサーモスタット25bと励磁コイルR2,
b接点のR6,a接点のR5を直列状に連絡し、また設
定温度(60℃)で開閉作動するb接点のサーモスタッ
ト25Cと励磁コイルR3,a接点のR6を直列状に連
結し、各サーモスタットの接点回路は並列状に配置され
て接続しである。Therefore, in FIG. 3, to explain the hot air temperature adjustment circuit 24, the above-mentioned set temperature (4
B contact thermostat that opens and closes at 0°C) -253
and excitation coil R1, R5, R6 of B contact, R4 of A contact
are connected in series, and a B contact thermostat 25b that opens and closes at a set temperature (50°C) and an exciting coil R2,
The B contact R6 and the A contact R5 are connected in series, and the B contact thermostat 25C, which opens and closes at the set temperature (60°C), the exciting coil R3 and the A contact R6 are connected in series, and each thermostat is connected in series. The contact circuits are arranged and connected in parallel.
次に、前記噴射ノズル11aの送油管に介在させた電磁
バルブ21aとa接点のR1,b接点のR2を直列状に
連結し、この両接点R1,R2の外部にはa接点R6の
回路が添加され、また前記噴射ノズル11bの送油管に
介在させた電磁バルブ21bにa接点のR2とb接点の
R3とが並列して連結され、各電磁バルブ21a、21
bの回路を並列状に配置して接続しである。Next, the electromagnetic valve 21a interposed in the oil feed pipe of the injection nozzle 11a, the a contact R1, and the b contact R2 are connected in series, and a circuit of the a contact R6 is connected to the outside of both contacts R1 and R2. The a contact R2 and the b contact R3 are connected in parallel to the electromagnetic valve 21b interposed in the oil feed pipe of the injection nozzle 11b, and each electromagnetic valve 21a, 21
The circuits b are arranged and connected in parallel.
なお、本実施例では、前記穀物槽7側壁面に設けた各レ
ベル計の所定位置a、 l)、 cを穀物槽7の穀
物貯蔵の有効体積を上下に均量的に3区分し、その層高
の上限位置に下段から上段にa。In this example, the effective grain storage volume of the grain tank 7 is equally divided into three areas, upper and lower, by predetermined positions a, l), and c of each level gauge provided on the side wall surface of the grain tank 7. A from the bottom to the top at the upper limit of the layer height.
b、Cの順に配列し、各設定位置に各レベル計23a、
23b、23Cをそれぞれ植設し、また前記設定位置a
、 b、 cにおける、それぞれの穀物量に対応す
る適正熱風温度が前記温度スイッチの各設定温度(40
℃)(50℃)(60℃)となるように形設した場合を
例示し、従って前記レベル計の個数並びに設定位置およ
び前記熱風室の温度スイッチの個数並びに設定値などは
必要により適宜に変更されるものであり、また前記噴射
ノズルの開閉弁を例図では電磁バルブに設けたが、電磁
バルブ、ソレノイドバルブ等にする場合もある。Arranged in the order of b and c, each level meter 23a at each setting position,
23b and 23C, respectively, and the setting position a.
, b, c, the appropriate hot air temperature corresponding to each amount of grain is the set temperature of the temperature switch (40
℃) (50℃) (60℃); therefore, the number and setting positions of the level meters and the number and setting values of the temperature switches in the hot air chamber may be changed as necessary. Although the opening/closing valve of the injection nozzle is provided as a solenoid valve in the example diagram, it may also be a solenoid valve, a solenoid valve, or the like.
そして、前記温度スイッチ25の所定温度(40℃)(
50℃)(60℃)は使用する機器により適宜な補正数
値が加算されるものである。Then, a predetermined temperature (40° C.) of the temperature switch 25 (
50°C) (60°C), an appropriate correction value is added depending on the equipment used.
本発明は上述のように構成したので、原料穀物を昇降機
8の供給口に投入し、火熱発生機6を発火可能の状態に
して該装置を駆動すると、原料穀物は昇降機8により上
部の穀物槽7に順次に揚穀供給される。Since the present invention is constructed as described above, when the raw material grain is put into the supply port of the elevator 8 and the device is driven with the fire heat generator 6 in a state where it can be ignited, the raw material grain is transferred to the upper grain tank by the elevator 8. Fried grains are sequentially supplied at 7.
金板りに前記レベル計23を設けた穀物槽7の設定位置
すまで給穀し前記昇降機8における穀物投入を停止する
と、前記レベル計233,23bは共に穀物を測定して
作動し、直ちに制御回路Aの励磁コイルR4,R5の作
動信号により熱風温度調節回路24の接点R4,R5を
共に閉成する。When grain is fed to the set position of the grain tank 7 in which the level gauge 23 is provided on the metal plate and the grain feeding in the elevator 8 is stopped, both the level gauges 233 and 23b are activated to measure the grain, and control is immediately performed. Contacts R4 and R5 of the hot air temperature control circuit 24 are both closed by activation signals of the excitation coils R4 and R5 of circuit A.
これに関連して噴射ノズルlla、llb回路の接点は
作動し、大口径の噴射ノズルllbは開口して燃料を噴
射し、熱風室2に50℃に近い熱風を発生し、その熱風
は各穀物流路3,3の穀物層を横切って排風室4,4側
に流出して乾燥作用を行ない、また流路3内の乾燥穀物
は下部の流穀槽に流下し昇降機8を介して再び上部穀物
槽7に返還され、謂ゆる循環式のテンパリング乾燥が継
続的に実施されることになる。In connection with this, the contacts of the injection nozzles lla and llb circuits are activated, and the large-diameter injection nozzle llb opens to inject fuel, generating hot air close to 50°C in the hot air chamber 2, and the hot air is distributed to each grain. It crosses the grain layer in the channels 3, 3 and flows out to the exhaust chambers 4, 4 side to perform a drying action, and the dried grain in the channel 3 flows into the grain tank at the bottom and is returned via the elevator 8. The grain is returned to the upper grain tank 7, and so-called circulating tempering drying is carried out continuously.
このようにして乾燥作用を実施すると、必然的に前記熱
風室2の熱風温度は経時的に上昇することになる。When the drying action is carried out in this manner, the temperature of the hot air in the hot air chamber 2 inevitably increases over time.
そこで本装置では、前記熱風室2側壁に設定温度(40
℃)(50℃)(60℃)で作動する自動復帰型サーモ
スタット25a、25b、25Cが装設してあり、前述
の状態で熱風温度が50℃を超えると、前記サーモスタ
ツ)25bが作動してその接点を開成し、これに関関連
して噴射ノズルlla、llb回路の接点R2は作動し
て反転的に開閉し、大口径の噴射ノズルllbは閉口し
、小口径の噴射ノズル11aは開口して火熱発生機6の
燃料噴射量が減少するため、前記熱風室2の熱風温度は
徐々に下降する。Therefore, in this device, the set temperature (40
Automatic reset type thermostats 25a, 25b, and 25C that operate at temperatures of The contact R2 of the injection nozzle lla, llb circuit is actuated to open and close the injection nozzle lla, llb in a reversible manner, and the large-diameter injection nozzle llb is closed and the small-diameter injection nozzle 11a is opened. Since the amount of fuel injected by the fire heat generator 6 decreases, the temperature of the hot air in the hot air chamber 2 gradually decreases.
そして前記サーモスタツ)25bは適宜な復帰温度でそ
の接点を反転開閉して熱風室2の熱風は50℃付近の適
性な範囲に自動的に規正されて常時効率的な穀物の乾燥
作用が実施されるものである。Then, the thermostat 25b reversely opens and closes its contacts at an appropriate return temperature, and the hot air in the hot air chamber 2 is automatically regulated to an appropriate range of around 50°C, so that efficient grain drying is always carried out. It is something.
次に、前記火熱発生機6の燃焼状況について述べると、
従来の噴射ノズル型式のものは、燃焼量調節を燃料の流
量または圧力の変化により行なうので、同一口径のノズ
ルでは燃料の流速変化を生じて各噴霧粒子は拡大するた
め、その燃焼ガスにCO,HCなどの混入率が高くなる
欠陥を有していた。Next, the combustion status of the heat generator 6 will be described.
Conventional injection nozzle types adjust the combustion amount by changing the fuel flow rate or pressure, so if the nozzle has the same diameter, the fuel flow rate changes and each spray particle expands, so the combustion gas contains CO, It had a defect that increased the mixing rate of HC and the like.
そこで、本火熱発生機には、複数個の噴射ノズルを嵌装
集設し、各ノズルに対して燃料の供給・停止のみを行な
う開閉弁を個別的に設けて噴射し燃焼させるので、前記
欠点を除去することができる。Therefore, this fire heat generator is fitted with a plurality of injection nozzles and is individually provided with an on-off valve that only supplies and stops fuel to each nozzle for injection and combustion. can be removed.
しかも完全燃焼を促進させるように、その燃焼室を多重
状箔体に形成しであるから、その内側箔体14において
なお少量的に発生する一酸化炭素、未燃粒子などは燃焼
ガスと共に両籠体14.150通気孔を介して外部に流
出するが、赤熱化した各箔体14,15の多孔壁通気孔
を前述の一酸化炭素、未燃粒子が接触状に通過するとき
加熱されてそれぞれに分解燃焼し、しかも多重状箔体で
あるからその分解燃焼は各箔体の多孔壁面毎に実施され
てよく燃え上がって完全燃焼し、火力を盛んにして燃焼
効率を高める効果を有するもので゛ある。Moreover, in order to promote complete combustion, the combustion chamber is formed into multiple foil bodies, so that carbon monoxide, unburned particles, etc. still generated in small amounts in the inner foil body 14 are trapped in both the combustion gas and the combustion chamber. The carbon monoxide and unburnt particles are heated when they pass in contact with the porous wall vents of each of the foil bodies 14 and 15, which become red hot. Moreover, since the foil is made of multiple foils, the decomposition and combustion is carried out on each porous wall surface of each foil, resulting in good flaming and complete combustion, which has the effect of increasing the thermal power and increasing the combustion efficiency. be.
要するに本発明は、穀物槽の側壁面に上下に適宜な間隔
を介して縦列状に配置したそれぞれの設定位置で槽内穀
物量を測定する複数個のレベル計を植設し、また前記火
熱発生機に複数個の燃料噴射ノズルを設けてその給油管
にそれぞれ開閉弁を介装すると共に、前記穀物槽に対す
る給穀量に順応して前記噴射ノズルの開閉弁を個別的に
開閉し燃焼する噴射ノズルの個数を増減して前記熱風室
の熱風を適宜な設定温度に変更すると共に、その熱風の
温度変化を適正な範囲に規制するようにした構成である
から、従来の装置の如く、熱風の温度調節のため各噴射
ノズルを大小口径に取替えたり、圧送空気の調節を行な
うなどの繁雑な作業または操作の必要なく、穀物槽の給
穀量の変化に対応して直ちに適正な設定温度に変化し、
しかもその熱風の温度変化を適正な範囲に自動的に規制
する状態で穀物の乾燥作用を継続的に実施するから、温
度調節の不良に起因する胴割粒の多発や熱損傷粒・食味
の低下などの品質面での障害は完全に防止され、穀物の
乾燥作用を改善合理化し、極めて高能率に実施できると
共に、過熱による火災発生を防止し、またその制御管理
を正確に、かつ自動的に行なうので、優良な乾燥穀物が
常に期待できるなどの顕著な効果を奏するものである。In short, the present invention has a plurality of level meters installed on the side wall surface of a grain tank to measure the amount of grain in the tank at respective set positions arranged vertically in a column at appropriate intervals, and A machine is provided with a plurality of fuel injection nozzles, each of which is equipped with an on-off valve in its fuel supply pipe, and the on-off valves of the injection nozzles are individually opened and closed according to the amount of grain fed to the grain tank for combustion. The number of nozzles is increased or decreased to change the temperature of the hot air in the hot air chamber to an appropriate set temperature, and the temperature change of the hot air is regulated within an appropriate range. The temperature immediately changes to the appropriate set temperature in response to changes in the amount of grain fed to the grain tank, without the need for complicated work or operations such as replacing each injection nozzle with a larger or smaller diameter or adjusting the compressed air to adjust the temperature. death,
Moreover, since the drying action of the grain is continuously carried out while the temperature change of the hot air is automatically regulated within an appropriate range, there is a large number of cracked grains due to poor temperature control, heat-damaged grains, and a decrease in taste. This completely prevents quality defects such as grain drying, improves and streamlines the drying process of grains, and allows it to be carried out with extremely high efficiency. It also prevents fires caused by overheating, and controls and manages them accurately and automatically. Since this process is carried out, it produces remarkable effects such as the fact that high-quality dried grains can always be expected.
図面は本発明の実施態様を例示し、第1図は本装置の一
部切欠側面図、第2図はその火熱発生機の断面図、第3
図はその電気回路図である。
1・・・・・・乾燥部機体、2・・・・・・熱風室、3
・・・・・・穀物流路、4・・・・・・排風室、5・・
・・・・排風機、6・・・・・・火熱発生機、7・・・
・・・穀物槽、8・・・・・・昇降機、9・・・・・・
送風機、10・・・・・・吹口、lla・・・・・・噴
射ノズル、11b・・・・・・噴射ノズル、12・・・
・・・点火プラグ、13・・・・・・吹口10の吐出側
、14・・・・・・箔体、15・・・・・・箔体、16
・・・・・・間隔、17・・・・・・燃焼室、18・・
・・・・遮蔽板、19・・・・・・スワール壁、20・
・・・・・送油管、21a・・・・・・電磁バルブ、2
1b・・・・・・電磁バルブ、22・・・・・件ランス
、23a・・・・・・レベル計、23b・・・・・・レ
ベル計、23C・・・・・・レベル計、24・・・・・
・熱風温度調節回路、25・・・・・・温度スイッチ、
25a・・・・・・サーモスタット、25b・・・・・
・サーモスタット、25C・・・・・・サーモスタット
、R1,R2,R3゜R4,R5,R6・・・・・・励
磁コイル、接点、A・・・・・・制御回路。The drawings illustrate embodiments of the present invention; FIG. 1 is a partially cutaway side view of the device, FIG. 2 is a sectional view of the heat generator, and FIG.
The figure is its electrical circuit diagram. 1...Drying section fuselage, 2...Hot air chamber, 3
... Grain channel, 4 ... Exhaust chamber, 5 ...
...Exhaust fan, 6...Fire heat generator, 7...
...Grain tank, 8...Elevator, 9...
Blower, 10...Blower mouth, lla...Injection nozzle, 11b...Injection nozzle, 12...
... Spark plug, 13 ... Discharge side of outlet 10, 14 ... Foil body, 15 ... Foil body, 16
...... Interval, 17... Combustion chamber, 18...
... Shielding plate, 19 ... Swirl wall, 20.
... Oil pipe, 21a ... Solenoid valve, 2
1b... Solenoid valve, 22... Lance, 23a... Level meter, 23b... Level meter, 23C... Level meter, 24・・・・・・
・Hot air temperature control circuit, 25...Temperature switch,
25a...Thermostat, 25b...
・Thermostat, 25C...Thermostat, R1, R2, R3゜R4, R5, R6...Exciting coil, contact, A...Control circuit.
Claims (1)
排風機を具備した乾燥部機体に穀物槽を組合せた乾燥装
置において、前記穀物槽の側壁面に上下に適宜な間隔を
介して縦列状に配置したそれぞれの設定位置で槽内穀物
量を測定する複数個のレベル計を植設し、また前記火熱
発生機に複数個の燃料噴射ノズルを設けてその給油管に
それぞれ開閉弁を介装すると共に、前記熱風室に任意の
異種温度により個別的に作動する複数個の温度スイッチ
を装着し、前記穀物槽に対する給穀量に順応して前記噴
射ノズルの開閉弁を個別的に開閉し燃焼する噴射ノズル
の個数を増減して前記熱風室の熱風を適宜な設定温度に
変更すると共に、その熱風の温度変化を適正な範囲に規
制するようにした穀物乾燥機の熱風温度自動調節装置。1 Fire heat generator with parallel grain flow path, hot air chamber, and exhaust chamber.
In a drying device in which a grain tank is combined with a drying section body equipped with an air exhaust fan, the amount of grain in the tank is measured at each set position arranged vertically in a column on the side wall of the grain tank at appropriate intervals. A plurality of level gauges are installed, a plurality of fuel injection nozzles are installed in the fire heat generator, and an on-off valve is installed in each of the fuel supply pipes, and the hot air chamber is individually injected at different temperatures. A plurality of operating temperature switches are installed, and the opening/closing valves of the injection nozzles are individually opened and closed according to the amount of grain fed to the grain tank to increase or decrease the number of injection nozzles for combustion, thereby discharging the hot air in the hot air chamber. An automatic hot air temperature adjustment device for a grain dryer that changes the temperature to an appropriate setting and regulates the temperature change of the hot air within an appropriate range.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8805877A JPS5953465B2 (en) | 1977-07-21 | 1977-07-21 | Automatic hot air temperature control device for grain dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8805877A JPS5953465B2 (en) | 1977-07-21 | 1977-07-21 | Automatic hot air temperature control device for grain dryer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5424762A JPS5424762A (en) | 1979-02-24 |
| JPS5953465B2 true JPS5953465B2 (en) | 1984-12-25 |
Family
ID=13932232
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8805877A Expired JPS5953465B2 (en) | 1977-07-21 | 1977-07-21 | Automatic hot air temperature control device for grain dryer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5953465B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61182181A (en) * | 1985-02-07 | 1986-08-14 | Nichiden Mach Ltd | Picture recognizing device |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0775922B2 (en) * | 1985-03-01 | 1995-08-16 | 住友ゴム工業株式会社 | Radial tire |
| JPS649002A (en) * | 1985-04-24 | 1989-01-12 | Sumitomo Rubber Ind | High performance (low profile radial) tire |
| JPS62137201A (en) * | 1985-12-09 | 1987-06-20 | Bridgestone Corp | Pneumatic tire pair |
| JPS62194904A (en) * | 1986-02-20 | 1987-08-27 | Bridgestone Corp | Heavy duty pneumatic radial tire |
| JPS62283002A (en) * | 1986-02-20 | 1987-12-08 | Bridgestone Corp | Pneumatic radial tire for heavy load |
| JPS63159113A (en) * | 1986-12-22 | 1988-07-02 | Yokohama Rubber Co Ltd:The | Pneumatic tire |
| JPS63227403A (en) * | 1987-03-18 | 1988-09-21 | Sumitomo Rubber Ind Ltd | Pneumatic radial tire |
| JPS63219402A (en) * | 1987-05-16 | 1988-09-13 | Bridgestone Corp | Pneumatic radial tire with reduced rolling resistance |
| JPH01141104A (en) * | 1987-11-27 | 1989-06-02 | Sumitomo Rubber Ind Ltd | Pneumatic radial type for heavy load |
| JPH01285404A (en) * | 1988-05-11 | 1989-11-16 | Sumitomo Rubber Ind Ltd | Pneumatic tire |
| JPH01273704A (en) * | 1988-04-22 | 1989-11-01 | Sumitomo Rubber Ind Ltd | Pneumatic tire |
| JPH02133201A (en) * | 1988-11-12 | 1990-05-22 | Sumitomo Rubber Ind Ltd | Pneumatic radial tire |
-
1977
- 1977-07-21 JP JP8805877A patent/JPS5953465B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61182181A (en) * | 1985-02-07 | 1986-08-14 | Nichiden Mach Ltd | Picture recognizing device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5424762A (en) | 1979-02-24 |
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