JPH0435305Y2 - - Google Patents

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Publication number
JPH0435305Y2
JPH0435305Y2 JP1987048418U JP4841887U JPH0435305Y2 JP H0435305 Y2 JPH0435305 Y2 JP H0435305Y2 JP 1987048418 U JP1987048418 U JP 1987048418U JP 4841887 U JP4841887 U JP 4841887U JP H0435305 Y2 JPH0435305 Y2 JP H0435305Y2
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JP
Japan
Prior art keywords
tank
discharge
powder
information
pressure
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
Application number
JP1987048418U
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Japanese (ja)
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JPS63154539U (en
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Priority to JP1987048418U priority Critical patent/JPH0435305Y2/ja
Publication of JPS63154539U publication Critical patent/JPS63154539U/ja
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Expired legal-status Critical Current

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Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、セメント或いは大豆などの粉粒体を
タンクに詰めて運搬する手段において、送り込み
場所の設備サイロ等に前記タンク内の粉粒体を荷
下しする際に、粉粒体の排出制御を自動的に行う
ようになした粉粒体運搬車における自動圧送排出
装置に関する。
[Detailed description of the invention] [Industrial application field] The present invention is a means for transporting powder and granules such as cement or soybeans in a tank, and the powder and granules in the tank are stored in a facility silo or the like at a delivery location. The present invention relates to an automatic pressure-feeding and discharging device for a powder transport vehicle that automatically controls the discharge of powder and granular materials when unloading.

〔従来の技術〕[Conventional technology]

従来のこの種粉粒体運搬車としては、実公昭57
ー4029号公報或いは実公昭57ー42898号公報等に
開示されるものが知られている。即ち、搬送した
粉粒体を設備サイロの離れた投入口又は高所投入
口に落し込むには、搬送用タンクの内圧を加圧す
ると共に粉粒体との空気混合を計つてこれを流動
化させて、タンク排出管から輸送管を通して、圧
送する手段が採られている。
As a conventional powder transport vehicle of this kind, the Jikko 57
Those disclosed in Publication No. 4029 or Publication No. 42898 of 1987 are known. In other words, in order to drop the transported powder into the remote or high-place charging port of the equipment silo, the internal pressure of the transport tank must be increased, and at the same time, air must be mixed with the powder to fluidize it. Therefore, a method is adopted in which the liquid is fed under pressure from the tank discharge pipe through the transport pipe.

そして、この場合の粉粒体運搬車における圧送
排出作業において、適切な排出条件は、粉粒体の
性状及び供給空気量と設備側の配管サイズ及びレ
イアウトによつて大きく変わり、かつ、作業中の
粉粒体のタンク内残存量及び空気湿度などによつ
て変化する。
In this case, the appropriate discharge conditions for the forced discharge work using the powder transport vehicle vary greatly depending on the properties of the powder, the amount of air supplied, and the piping size and layout of the equipment. It varies depending on the amount of powder remaining in the tank and air humidity.

従つて、従来のこの種作業では、タンクまた
は、輸送管の内圧を圧力計にて目視確認しなが
ら、タンク内に送り込み空気量と排出口に設置し
た排出弁直後の固気混合部分に入る空気量との割
合を、これ等両送気管中に夫々設けたバルブを手
動操作し、粉粒体の流れを確認しながら作業者が
調節していた。
Therefore, in conventional work of this kind, while visually checking the internal pressure of the tank or transport pipe with a pressure gauge, the amount of air fed into the tank and the air entering the solid-gas mixture section immediately after the discharge valve installed at the discharge port are determined. An operator manually operated valves provided in both air pipes to adjust the ratio between the amount and the amount while checking the flow of the powder and granules.

また、このような空気量の調節の他に、前記排
出弁の開度調節更にはテイツピング機能を有すタ
ンクにおけるテイツピング角度の調節などを人為
的に行つていた。
In addition to adjusting the amount of air, the opening degree of the discharge valve and the taping angle of a tank having a taping function have also been manually adjusted.

〔考案が解決しようとする問題点〕[Problem that the invention attempts to solve]

そのために、上述の調節操作で管理される粉粒
体の排出作業には、熟練した作業者を必要とする
と共に、作業者の技術力によつて排出能力に差異
が生じる結果となつていた。加えて、20乃至45分
程度の排出作業時中、作業者の監視が必要であつ
た。
Therefore, the work of discharging the powder and granular material managed by the above-mentioned adjustment operation requires a skilled worker, and the discharging ability varies depending on the technical ability of the worker. In addition, it was necessary to supervise the worker during the 20 to 45 minute discharge operation.

そこで、本考案は、粉粒体運搬車における空気
等の輸送媒体による設備サイロへの圧送排出作業
において、設備側との排出管接続作業以外を自動
化し、排出作業を無人化すると共に、常に最適な
排出条件で粉粒体の自動圧送排出が可能で効率良
く作業できる装置の開発を目的とする。
Therefore, the present invention aims to automate the work of pumping and discharging equipment silos using transport media such as air in powder and granule transport vehicles, except for the work of connecting the discharge pipes to the equipment side, making the discharge work unmanned and always optimal. The purpose of this project is to develop a device that can automatically pump and discharge powder and granular materials under suitable discharge conditions and that can be operated efficiently.

〔問題点を解決するための手段〕[Means for solving problems]

かかる目的を達成するために、本考案では運搬
用タンク内の粉粒体を加圧空気などの輸送媒体に
より設備サイロ等に圧送排出する機構において、
最適の排出条件となるタンク内圧力変化のパター
ンを認識させたコントローラを搭載して、前記タ
ンク内への輸送媒体の送り込みを制御するバルブ
装置と該タンクにおける排出管の開閉を制御する
排出弁装置及び該排出管における固気混合部分へ
の輸送媒体の送り込みを制御するバルブ装置等の
排出条件設定装置を、稼働時に検出したタンク内
圧センサーからの圧力情報を基に前記コントロー
ラで先の認識パターンと比較した差異を補正する
向きに自動的に制御するように構成してなる粉粒
体運搬車における自動圧装排出装置を提案する。
In order to achieve this purpose, the present invention provides a mechanism for pumping and discharging powder and granules in a transportation tank to a facility silo or the like using a transportation medium such as pressurized air.
A valve device that is equipped with a controller that recognizes a pattern of pressure changes in the tank that provides optimal discharge conditions, and that controls the feeding of the transport medium into the tank, and a discharge valve device that controls the opening and closing of the discharge pipe in the tank. And a discharge condition setting device such as a valve device that controls the feeding of the transport medium to the solid-gas mixing part in the discharge pipe is set to the previously recognized pattern by the controller based on the pressure information from the tank internal pressure sensor detected during operation. An automatic pressurization and discharge device for a powder transport vehicle is proposed, which is configured to automatically control in a direction to correct the difference between the comparisons.

そして、この場合に前記コントローラによる制
御を、タンク内粉粒体のレベル情報、排出流速情
報及びタンクの総重量情報等で修正をして有効で
あり、前記排出条件設定装置にタンクのテイツピ
ング角度を制御する装置を含ませることも可能で
ある。
In this case, it is effective to modify the control by the controller using information on the level of powder and granular material in the tank, information on the discharge flow rate, information on the total weight of the tank, etc., and set the taping angle of the tank on the discharge condition setting device. It is also possible to include a controlling device.

〔作用〕[Effect]

粉粒体運搬用タンクからの粉粒体圧送排出が安
定かつ効率良く行われるときのタンク内圧の圧力
変化を模擬的に示すと、第3図にようになる。即
ち、横軸の時間軸に対してタンク内圧力を縦軸に
採ると、搬送後の排出作業の開始時t0に密封した
タンクに空気を送り込み、圧力をタンク許容圧以
下の範囲で充分に高圧化する。タンク内圧が充分
な圧力に達した時点t1で排出弁を開弁すると、高
いタンク内圧と未だ初期空洞状態の輸送管の低負
荷によつて一時的に粉粒体が高速排出して、タン
ク内圧は急激に低下するが、送り込まれた粉粒体
によつて輸送管での流路抵抗が次第に増加するな
どの排出負荷増大と引き続く送気圧との釣合下
に、タンク内圧が安定すると共に定速流での圧送
排出動作でタンク内の粉粒体が殆んどなくなる迄
(時点t2)継続する。この圧送排出の終段では、
排出口への粉粒体の充分な供給がなされず、空気
量の多い固気混合体が送り出されるので、タンク
内圧は徐々に低下し、遂には時点t3で外気圧とな
り、作業を終了する。
FIG. 3 shows a simulated change in the internal pressure of the tank when the powder and granular material is pumped and discharged stably and efficiently from the granular material transport tank. In other words, if we take the pressure inside the tank on the vertical axis with respect to the time axis on the horizontal axis, air is pumped into the sealed tank at t 0 at the start of the discharge operation after transportation, and the pressure is kept within the tank's allowable pressure range. Increase pressure. When the discharge valve is opened at time t 1 when the tank internal pressure reaches a sufficient pressure, the powder and granules are temporarily discharged at high speed due to the high tank internal pressure and the low load on the transport pipe, which is still in the initial hollow state, and the tank The internal pressure drops rapidly, but as the discharge load increases due to the gradual increase in flow path resistance in the transport pipe due to the injected powder and granules, and the continued supply pressure is balanced, the tank internal pressure stabilizes. The pressure-feeding and discharging operation at a constant velocity continues until the powder and granules in the tank are almost completely gone (time t 2 ). At the final stage of this forced discharge,
As the powder and granules are not sufficiently supplied to the discharge port and a solid-gas mixture containing a large amount of air is sent out, the internal pressure of the tank gradually decreases and finally reaches the external pressure at time t 3 , ending the work. .

このタンク内圧力の変化を最適パターンとして
コントローラ内にサンプリングしておき、実際の
稼働時におけるタンク内圧をこの最適パターンと
逐次比較して、その時々の差異を補正する向きに
排出条件設定装置殊にタンク内への送気バルブ装
置、排出弁装置、排出管における固気混合部分へ
の送気バルブ装置及び運搬車がテイツピング機能
を備えている場合のテイツピング角度を制御す
る。
This change in tank internal pressure is sampled in the controller as an optimal pattern, and the tank internal pressure during actual operation is successively compared with this optimal pattern, and the discharge condition setting device is designed to correct the differences from time to time. Controls the taping angle when the air supply valve device into the tank, the discharge valve device, the air supply valve device to the solid-air mixing part in the discharge pipe, and the transport vehicle are equipped with a taping function.

これによつつて、第4図に示す如く最適の排出
条件パターンを示す曲線Lに対して稼働中無制御
のタンク内圧力が示す曲線lが上回る(タンク内
圧上昇)の部分域Aでは、タンク内への送気バル
ブ装置の開度を絞つて輸送媒体のタンク内送り込
み量を減らし、同時に排出弁の開度を絞ると共に
固気混合部分への送気バルブ装置の開度を広げる
ことで、それまでのタンク内過剰圧の低下を計る
と共に過剰圧によつて余分に送り込まれた排出管
並びに輸送管内の輸送中の粉粒体による目詰まり
を防止して、安定排出動作への復帰を待つように
機能する。また、前記タンク内圧力が曲線Lを下
回る部分域Bでは、上記の制御と逆向きに各装置
の開度制御を行ない、それまで低下しいた粉粒体
排出量の回復を計ると共に安定排出動作への復帰
を待機するように機能する。
As a result, as shown in FIG. 4, in the partial region A where the curve L showing the uncontrolled tank internal pressure during operation exceeds the curve L showing the optimal discharge condition pattern (tank internal pressure rise), the tank By narrowing the opening of the air supply valve device to the inside of the tank to reduce the amount of transport medium sent into the tank, and at the same time narrowing the opening of the discharge valve and widening the opening of the air supply valve device to the solid-air mixing section, Measure the reduction of the excess pressure in the tank, prevent clogging due to excess pressure in the discharge pipe and transportation pipe due to powder and granules being transported, and wait for a return to stable discharge operation. It works like this. In addition, in the partial region B where the tank internal pressure is lower than the curve L, the opening degree control of each device is performed in the opposite direction to the above control to recover the previously decreased amount of powder and granular material discharge and to ensure stable discharge operation. It functions to wait for the return to .

そして、この排出条件設定装置への実際の開度
制御量は、タンク内粉粒体の残存量及び排出口等
における目詰まり或いはタンク内での粉粒体の片
寄りなど不測の事態を発生を考慮して、これを決
定して有効であるが、この制御量の決定に、タン
ク内粉粒体のレベル情報(タンク内での粉粒体の
片寄り検知)、排出流速情報(排出口等における
目詰まり検知)及びタンク総重量情報(タンク内
粉粒体の残存量検知)が有効に作用する。
The actual opening control amount for this discharge condition setting device is determined to prevent unforeseen situations such as the amount of powder remaining in the tank and clogging at the discharge port, or unevenness of the powder and granules in the tank. Taking this into account, it is effective to determine this, but in determining this control amount, information on the level of powder and granular material in the tank (detection of unevenness of powder and granular material in the tank), discharge flow rate information (discharge port, etc.) clogging detection) and tank total weight information (detection of remaining amount of powder and granular material in the tank) are effective.

その結果、最適パターンに自動制御された排出
作業は、第4図示のように無制御による作業の終
了時t3に比べて、t3−t2時間だけ短縮することが
可能となるに加えて、この間の作業者の監視を必
要としない無人化作業が可能となる。
As a result, the discharge work that is automatically controlled to the optimal pattern can be shortened by t 3 −t 2 hours compared to the end time t 3 of the work without control as shown in Figure 4. This enables unmanned work that does not require operator supervision during this time.

次に、本考案の好ましい実施例について説明す
る。
Next, a preferred embodiment of the present invention will be described.

〔実施例〕〔Example〕

第1図は本考案の一実施例を示す制御機構の構
成図で、運搬用のタンク1には、そのタンク内底
部に圧縮空気等の輸送媒体を噴出させるエアスラ
イドベルト2を配置してあり、上方の投入口3か
ら収容した粉粒体4をタンク後方下部の排出口5
から排出できるようになしてある。
Fig. 1 is a configuration diagram of a control mechanism showing an embodiment of the present invention.A transport tank 1 has an air slide belt 2 disposed at the bottom of the tank for spouting a transport medium such as compressed air. , the granular material 4 received from the upper input port 3 is transferred to the discharge port 5 at the rear lower part of the tank.
It is designed so that it can be discharged from the

また、該タンク1自体をその後方外端で枢支し
て、タンク前方と支持台との間に配置したチルト
シリンダ6の伸縮によつて、これをテイツピング
可能に構成してある。
Further, the tank 1 itself is pivotally supported at its rear outer end so that it can be tapped by expanding and contracting a tilt cylinder 6 disposed between the front of the tank and a support base.

前記排出管口5には排出弁7を設けてあり、そ
の直後の管内に粉粒体4と圧縮空気との混合を計
る固気混合部8を設け、排出用接続ホースを介し
て設備サイロ9の受給管10と接続するようにな
してある。
A discharge valve 7 is provided at the discharge pipe port 5, and a solid-gas mixing section 8 for mixing the powder and granular material 4 with compressed air is provided in the pipe immediately after the discharge valve 7. It is designed to be connected to the receiving pipe 10 of.

そして、タンク1内には、収容した粉粒体4の
嵩量を検知する複数のレベルセンサー11,11
が適宜位置に配置してあり、排出管内には流速セ
ンサー12を設置する一方、前記タンク枢支部及
びチルトシリンダ6の基部に重量センサー13を
夫々配置してタンク1の総重量を検出するように
なしてあると共に、タンク内圧力を検出する圧力
センサー14及び前記固気混合部8への送気圧力
センサー15を設けてある。
Inside the tank 1, there are a plurality of level sensors 11, 11 for detecting the bulk of the contained powder and granular material 4.
are placed at appropriate positions, and a flow rate sensor 12 is installed inside the discharge pipe, while weight sensors 13 are placed at the tank pivot portion and the base of the tilt cylinder 6, respectively, to detect the total weight of the tank 1. In addition, a pressure sensor 14 for detecting the internal pressure of the tank and a pressure sensor 15 for supplying air to the solid-air mixing section 8 are also provided.

これ等各センサーからの状況検出情報はコント
ローラ16へ入力される。該コントローラ16に
は予め最適の排出条件となるタンク内圧を想定し
た圧力変化のパターンを認識させてあり、先の状
況検出情報の内圧力センサー14からのタンク内
圧情報を基に、その時々のタンク内圧を前記認識
パターンと比較し、その結果の制御信号を出力す
る。
The situation detection information from each of these sensors is input to the controller 16. The controller 16 is made to recognize in advance a pressure change pattern assuming the tank internal pressure that is the optimal discharge condition, and based on the tank internal pressure information from the internal pressure sensor 14 of the previous situation detection information, the tank internal pressure at that time is adjusted. The internal pressure is compared with the recognition pattern, and a control signal resulting from the comparison is output.

この制御信号を受ける排出条件設定装置として
は、その一つがモータ17で駆動されてエアフイ
ルタ18を介して吸気するエアコンプレツサ19
からの圧縮空気の供給を受ける二系統の送気回路
中に夫々設けた電動バルブ20及び21であり、
他の一つが油圧パワーユニツト22からの作動油
の供給を受ける二系統の油圧回路中に夫々設けた
電磁バルブ23及び24である。
One of the exhaust condition setting devices that receives this control signal is an air compressor 19 that is driven by a motor 17 and sucks air through an air filter 18.
Electric valves 20 and 21 are respectively provided in two air supply circuits receiving compressed air from the
The other one is electromagnetic valves 23 and 24 provided in two hydraulic circuits that receive hydraulic oil from the hydraulic power unit 22, respectively.

そして、前記電動バルブ20及び21で前記タ
ンク1と固気混合部8への送気量が夫々制御され
ると共に、前記電磁バルブ23及び24で前記排
出弁7の開度が作動シリンダ25で制御され、し
かも、前記チルトシリンダ6の伸縮(タンク1に
おけるイツピング角度)の制御が行われる。この
コントローラ16における上記制御のための各入
力要素と各出力要素とを第2図に示す。
The electric valves 20 and 21 control the amount of air supplied to the tank 1 and the solid-air mixing section 8, respectively, and the electromagnetic valves 23 and 24 control the opening degree of the discharge valve 7 using the operating cylinder 25. Moreover, the expansion and contraction of the tilt cylinder 6 (the tilting angle in the tank 1) is controlled. FIG. 2 shows each input element and each output element for the above control in this controller 16.

なお、これ等排出条件設定装置の各制御におい
て、前記圧力センサー14からのタンク内圧情報
を基に制御の向きを決定し、その時々の制御量を
その他の入力要素による総合的な修正の下で決定
して、タンク内圧が最適な排出条件のパターンに
近づく向きの制御がなされる。また、排出時に粉
粒体を流動化し該体の圧送を計る輸送媒体として
は前記空気の他に圧縮性の各種流体が適用可能で
ある。
In addition, in each control of these discharge condition setting devices, the direction of control is determined based on the tank internal pressure information from the pressure sensor 14, and the control amount at each time is comprehensively corrected by other input elements. Based on this determination, control is performed so that the tank internal pressure approaches the optimal discharge condition pattern. In addition to the above-mentioned air, various compressible fluids can be used as the transport medium for fluidizing the granular material and pumping the granular material during discharge.

〔考案の効果〕[Effect of idea]

このように、本考案装置によれば、運搬用タン
ク内の粉粒体を加圧空気などの輸送媒体により設
備サイロ等に圧送排出する機構において、タンク
内圧力が最適の排出条件となる圧力変化のパター
ンを予めコントローラに認識させておき、該コン
トローラで稼働中のタンク内圧の変化を逐次先の
パターンと比較して、その結果を基にタンク内へ
の輸送流体の送り込みを制御するバルブ装置、該
タンクにおける排出管の開閉を制御する排出弁装
置及び固気混合部への輸送媒体の送り込みを制御
するバルブ装置などの各排出条件設定装置を、タ
ンク内圧が前記最適のパターンに近づくように自
動的に制御出来るので、かかる排出作業時に作業
者の監視操作を必要とすることなく、しかも、最
適の排出状態に最も近い状態で効率良く且つ安定
して粉粒体の圧送排出を行うことが出来て、作業
性の向上を顕著に計ることが出来る。
As described above, according to the device of the present invention, in a mechanism for pumping and discharging powder and granules in a transportation tank to a facility silo, etc. using a transport medium such as pressurized air, the pressure change that makes the tank internal pressure the optimal discharge condition is achieved. A valve device that causes a controller to recognize the pattern in advance, and sequentially compares changes in the internal pressure of the tank during operation with the previous pattern, and controls the feeding of transport fluid into the tank based on the results. Each discharge condition setting device, such as the discharge valve device that controls the opening and closing of the discharge pipe in the tank and the valve device that controls the feeding of the transport medium to the solid-gas mixing section, is automatically set so that the tank internal pressure approaches the optimal pattern. Since the system can be controlled visually, the powder and granules can be efficiently and stably pumped and discharged in a state that is closest to the optimum discharge condition without requiring operator monitoring during such discharge work. As a result, work efficiency can be significantly improved.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本考案装置を備えた粉粒体の圧送排出
機構の一実施例を示す構成図、第2図は本考案装
置におけるコントローラでの制御要素を例示する
ブロツク図、第3図は圧送排出時のタンク内圧力
の最適条件を示す圧力特性図、第4図は同じく前
記最適条件の圧力特性と無制御下の稼動タンク内
圧力特性とを示す特性図である。 1……タンク、4……粉粒体、5……排出管
口、6……チルトシリンダー、7……排出弁、8
……固気混合部、9……設備サイロ、11……レ
ベルセンサー、12……流速センサー、13……
重量センサー、14,15……圧力センサー、1
6……コントローラ、20,21……電動バル
ブ、23,24……電磁バルブ。
Fig. 1 is a block diagram showing an example of a mechanism for pumping and discharging powder and granular material equipped with the device of the present invention, Fig. 2 is a block diagram illustrating the control elements of the controller in the device of the present invention, and Fig. 3 is a pressure-feeding mechanism. FIG. 4 is a pressure characteristic diagram showing the optimum conditions for the tank internal pressure at the time of discharge. Similarly, FIG. 4 is a characteristic diagram showing the pressure characteristics under the optimum conditions and the tank internal pressure characteristics under uncontrolled operation. 1...tank, 4...powder, 5...discharge pipe port, 6...tilt cylinder, 7...discharge valve, 8
... solid-gas mixing section, 9 ... equipment silo, 11 ... level sensor, 12 ... flow rate sensor, 13 ...
Weight sensor, 14, 15...Pressure sensor, 1
6... Controller, 20, 21... Electric valve, 23, 24... Solenoid valve.

Claims (1)

【実用新案登録請求の範囲】 (1) 運搬用タンク内の粉粒体を加圧空気などの輸
送媒体により設備サイロ等に圧送排出する機構
において、最適の排出条件となるタンク内圧力
変化のパターンを認識させたコントローラを搭
載し、前記タンク内への輸送媒体の送り込みを
制御するバルブ装置と該タンクにおける排出管
の開閉を制御する排出弁装置及び該排出管にお
ける固気混合部分への輸送媒体の送り込みを制
御するバルブ装着等の排出条件設定装置を、稼
動時に検出したタンク内圧センサーからの圧力
情報を基に前記コントローラで先の認識パター
ンと比較した差異を補正する向きに自動的に制
御するように構成してなることを特徴とする粉
粒体運搬車における自動圧装排出装置。 (2) 前記差異を補正する向きの制御条件を、タン
ク内粉粒体のレベル情報、排出流速情報及びタ
ンクの総重量情報等で修正するようになしたと
ころの実用新案登録請求の範囲第1項記載の粉
粒体運搬車における自動圧装排出装置。 (3) 前記排出条件設定装置がタンクのテイツピン
グ角度を制御する装置を含むところの実用新案
登録請求の範囲第1項記載の粉粒体運搬車にお
ける自動圧装排出装置。
[Scope of Claim for Utility Model Registration] (1) A pattern of pressure changes in the tank that provides the optimal discharge conditions in a mechanism that pumps and discharges powder and granules in a transportation tank to a facility silo, etc. using a transport medium such as pressurized air. A valve device that controls the feeding of the transport medium into the tank, a discharge valve device that controls the opening and closing of the discharge pipe in the tank, and a transport medium to the solid-gas mixture part of the discharge pipe, which is equipped with a controller that recognizes the The controller automatically controls the discharge condition setting device, such as a valve installed to control the feeding of the tank, to correct the difference compared to the previous recognition pattern based on pressure information from the tank internal pressure sensor detected during operation. An automatic compression and discharge device for a powder transport vehicle, characterized in that it is configured as follows. (2) Claim 1 of the utility model registration in which the control conditions for correcting the difference are modified using information on the level of powder and granular material in the tank, information on the discharge flow rate, information on the total weight of the tank, etc. An automatic compression discharge device for a powder and granular material transport vehicle as described in 2. (3) The automatic compression discharge device for a powder transport vehicle according to claim 1, wherein the discharge condition setting device includes a device for controlling the taping angle of the tank.
JP1987048418U 1987-03-31 1987-03-31 Expired JPH0435305Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987048418U JPH0435305Y2 (en) 1987-03-31 1987-03-31

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987048418U JPH0435305Y2 (en) 1987-03-31 1987-03-31

Publications (2)

Publication Number Publication Date
JPS63154539U JPS63154539U (en) 1988-10-11
JPH0435305Y2 true JPH0435305Y2 (en) 1992-08-21

Family

ID=30869928

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987048418U Expired JPH0435305Y2 (en) 1987-03-31 1987-03-31

Country Status (1)

Country Link
JP (1) JPH0435305Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007537958A (en) * 2004-04-28 2007-12-27 マシーネンファブリーク グスタフ アイリッヒ ゲーエムベーハー ウント コー.カーゲー Method and apparatus for continuous controlled discharge of solids

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5716308B2 (en) * 2010-07-29 2015-05-13 井関農機株式会社 Granule dispenser

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5639434A (en) * 1979-09-08 1981-04-15 Hiraki Kawaguchi Nipple type clinical thermometer
JPS5832339B2 (en) * 1981-04-16 1983-07-12 日立工機株式会社 Ultracentrifuge rotor temperature measuring device
JPS6025929B2 (en) * 1978-01-25 1985-06-21 ソニー株式会社 PWM modulation circuit

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5832339U (en) * 1981-08-20 1983-03-02 シャープ株式会社 electronic thermometer
JPS59176940U (en) * 1983-05-12 1984-11-27 シャープ株式会社 electronic thermometer
JPS6025929U (en) * 1983-07-27 1985-02-21 大塚製薬株式会社 electronic thermometer
JPS6170741U (en) * 1984-10-16 1986-05-14

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6025929B2 (en) * 1978-01-25 1985-06-21 ソニー株式会社 PWM modulation circuit
JPS5639434A (en) * 1979-09-08 1981-04-15 Hiraki Kawaguchi Nipple type clinical thermometer
JPS5832339B2 (en) * 1981-04-16 1983-07-12 日立工機株式会社 Ultracentrifuge rotor temperature measuring device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007537958A (en) * 2004-04-28 2007-12-27 マシーネンファブリーク グスタフ アイリッヒ ゲーエムベーハー ウント コー.カーゲー Method and apparatus for continuous controlled discharge of solids

Also Published As

Publication number Publication date
JPS63154539U (en) 1988-10-11

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