JPS59198222A - Pneumatic transport apparatus - Google Patents

Pneumatic transport apparatus

Info

Publication number
JPS59198222A
JPS59198222A JP7305183A JP7305183A JPS59198222A JP S59198222 A JPS59198222 A JP S59198222A JP 7305183 A JP7305183 A JP 7305183A JP 7305183 A JP7305183 A JP 7305183A JP S59198222 A JPS59198222 A JP S59198222A
Authority
JP
Japan
Prior art keywords
discharge
storage
solids
valve
separator
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
JP7305183A
Other languages
Japanese (ja)
Inventor
Shunichi Mitsuya
三矢 俊一
Takeshi Ikeda
健 池田
Yasuo Doi
土井 康男
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.)
Taisei Corp
Ebara Corp
Original Assignee
Taisei Corp
Ebara Corp
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 Taisei Corp, Ebara Corp filed Critical Taisei Corp
Priority to JP7305183A priority Critical patent/JPS59198222A/en
Publication of JPS59198222A publication Critical patent/JPS59198222A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/04Conveying materials in bulk pneumatically through pipes or tubes; Air slides
    • B65G53/24Gas suction systems

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Refuse Collection And Transfer (AREA)
  • Air Transport Of Granular Materials (AREA)

Abstract

PURPOSE:To enable smooth transport by connecting a distribution conveyer to a discharge port of a separator and disposing a plurality of storing and discharging machines. CONSTITUTION:A separator 8 is connected to a pipeline for pneumatic transport of a solid, and a plurality of storing and discharging machines 12a, 12b are disposed corresponding to a plurality of discharge ports 16a, 16b of a distribution conveyer 15 connected to a solid discharge port 81 of the separator through pipelines. Intercepting valves 18a, 18b are disposed respectively in pipelines connecting the storing and discharging machines 12a and 12b. In this arrangement, a solid can be smoothly transported from a throwing-in station to a collecting station, and each speed of discharging the solid from the storing and discharging machines at the collecting station is made equal.

Description

【発明の詳細な説明】 本発明はごみや粉粒体等の固形物の空気輸送装置に関し
、特に、気流によって輸送したごみ等を気流から分離す
る分離機に複数個の貯留排出機を接続してなる空気輸送
装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a pneumatic transportation device for solid materials such as garbage and powder, and in particular, a plurality of storage and discharge devices are connected to a separator that separates garbage, etc. transported by an airflow from the airflow. This article relates to pneumatic transportation equipment.

一般に、ごみや粉粒体等の固形物の空気輸送システムは
、複数個所に設置された投入ステーションと・中央の収
集ステーションとを管路で接続し、この管路を介して各
々の投入ステーションから収集ステーションへとごみや
粉粒体を気流で輸送するものである。この概略を第1図
を参照して述べれば所望の位置に設置された多数の投入
ステーション1a11b、1Cと固形物を一個所に収集
する収集ステーション2とはそれぞれ分岐された管路3
によって連絡されるものである。そして投入ステーショ
ン1a、lb、1cは基本的には固形物投入口、貯留槽
および排出弁から成るものであって、例えば投入ステー
ション1aでは投入シュート4に複数の固形物投入口5
を設け、さらに投入シュート4の下端は一時的に固形物
を貯留する回転ドラム6の一端に接続され、さらに回転
ドラム6は排出弁7を介して管路3と接続されている。
In general, pneumatic transportation systems for solid materials such as garbage and powder and granules connect input stations installed at multiple locations to a central collection station via pipes, and transport the waste from each input station via the pipes. It uses airflow to transport garbage and powder to the collection station. To describe this outline with reference to FIG. 1, a large number of input stations 1a11b and 1C installed at desired positions and a collection station 2 that collects solids in one place are connected to pipe lines 3 that are branched from each other.
will be contacted by. The charging stations 1a, lb, and 1c basically consist of a solids input port, a storage tank, and a discharge valve.For example, in the charging station 1a, a plurality of solids input ports 5 are provided in the charging chute 4.
Furthermore, the lower end of the input chute 4 is connected to one end of a rotating drum 6 for temporarily storing solids, and the rotating drum 6 is further connected to the pipe line 3 via a discharge valve 7.

また別の投入ステーション1b11cは投入シコート4
が貯留槽の役割をなづものであって回転ドラム6のよう
に大きな空間を占める貯留槽を設置する余裕がない場合
に多用されている。さらに、収集ステーション2は固形
物が輸送される管路3の一端が接続されたチイクロンや
バグフィルタなどの分離機8と空気を吸引するための送
!iA機9と送Jl1機9に流入する空気中に含まれる
固形分を除去するために送風機9と分離機8とを接続す
る管路10に設けられた除塵装置11と、分離v18で
気流から分離された固形物を受は入れ、そして適当な時
点で排出する貯留排出vIA12とから構成されている
。そして固形物を輸送するための管路3は全ての投入ス
テーション1a、1b11Cと収集ステーション2とを
合理的に接続するため適当な位置で分岐されており、そ
の上流部には吸気弁13或いは遮断弁14が設けられて
いる。投入ステーション1a11b11Cに貯留された
固形物を収集ステーション2へ収集する場合は、先ず送
風11!9を起動し、吸気弁13又は遮断弁14を開き
、管路3内に所定の速度の気流を生ぜしめ、その後排出
弁7を開き投入ステーションに貯留された固形物を管路
3内へ供給し、気流によって分離機8まで輸送する。そ
して1つの投入ステーションの固形物の輸送が終了した
ならば、順次別の投入ステーションの排出弁を開け、貯
留された固形物を輸送するものである。一般に送風If
a9を起動してから′投入ステーションの排出弁7を開
は得る状態になるまでは若干の時間を要するものである
から効率的な運転を行うために、−回の送風I9の運転
において全ての投入ステーシーコンに貯留された固形物
を収集ステーションに収集するように運転されているも
のである。
Another loading station 1b11c is loading station 4.
It is often used when there is no room to install a storage tank that occupies a large space like the rotating drum 6. Furthermore, the collection station 2 is connected to one end of a pipe line 3 through which the solids are transported, to a separator 8 such as a cyclone or a bag filter, and a feeder 8 for suctioning air. A dust removal device 11 is installed in a pipe 10 that connects the blower 9 and the separator 8 to remove solids contained in the air flowing into the iA machine 9 and the Jl1 machine 9, and a dust removal device 11 is installed in the pipe 10 that connects the blower 9 and the separator 8 to remove the solid content from the airflow with the separation v18. It consists of a storage and discharge vIA 12 that receives the separated solids and discharges them at an appropriate time. The pipe line 3 for transporting solids is branched at an appropriate position to rationally connect all input stations 1a, 1b11C and the collection station 2, and the upstream part thereof has an intake valve 13 or a shutoff valve. A valve 14 is provided. When collecting the solids stored in the input station 1a11b11C to the collection station 2, first start the air blower 11!9, open the intake valve 13 or the cutoff valve 14, and generate an airflow at a predetermined speed in the pipe line 3. After that, the discharge valve 7 is opened and the solids stored in the input station are supplied into the pipe line 3 and transported to the separator 8 by the air flow. When the transportation of the solids from one loading station is completed, the discharge valves of the other loading stations are sequentially opened and the stored solids are transported. In general, if
It takes some time after starting a9 to open the discharge valve 7 of the input station, so in order to operate efficiently, all the It is operated to collect solids stored in the input station into a collection station.

ところで固形物の発生量は必ずしも常に一定しているも
のではなく、それ故に全ての投入ステーションに貯留さ
れた固形物が輸送される前に収集ステーションの貯留排
出機12の貯留容量の限界に達することがある。この場
合、貯留排出機12に貯留された固形物を排出し、その
後再び収集を再開することとなるが、できるだけ短時間
に貯留排出機12内の固形物を排出することが望ましい
However, the amount of solids generated is not always constant, and therefore the storage capacity of the collection station's storage/discharge machine 12 may reach its limit before the solids stored at all input stations are transported. There is. In this case, the solids stored in the storage/discharge machine 12 are discharged, and then collection is restarted again, but it is desirable to discharge the solids in the storage/discharge machine 12 as quickly as possible.

しかし、貯留排出機12の後の工程としてベルトコンベ
ヤなどの搬送工程や固形物の分別装置が付設されている
システムにおいては貯留排出機12の排出速度が大きく
なれば、それに対応して搬送速度や分別処理3i!度を
大ぎなものとしな【ノればならず、当然それらを構成す
る設備ら大型化しなければならいものであった。
However, in a system in which a conveyance process such as a belt conveyor or a solid matter separation device is attached as a process after the storage and discharger 12, if the discharge speed of the storage and discharger 12 increases, the conveyance speed will increase accordingly. Separation processing 3i! As a result, the equipment that comprised them had to be made larger as well.

従来の空気輸送システムにおいて、収集ステーションの
貯留排出機から排出される固形物の量の安定化を図る装
置としては特開昭56 = ’165605号公報の装
置が知られいるが、なお設備が人がかりなものとなる問
題があった。
In a conventional pneumatic transportation system, the device disclosed in Japanese Patent Application Laid-open No. 165605 is known as a device for stabilizing the amount of solids discharged from the storage and discharge machine at the collection station, but the equipment There was a problem that became a clue.

本発明は、上記従来の問題点を解消し固形物の投入ステ
ーションから収集ステーションへの固形物の輸送を円滑
に行い、かつ収集ステーションにおいては貯留排出機か
らの固形物の排出速度を平均化し、以て貯留排出機の後
の工程の諸設備の処理量を軽減すると共にこれら諸設備
をより小型で安価なものとした空気輸送装置を提供する
ことを目的とするものである。
The present invention solves the above-mentioned conventional problems, smoothly transports solids from a solids input station to a collection station, and averages the discharge speed of solids from a storage discharger at the collection station. It is an object of the present invention to provide a pneumatic transportation device that reduces the throughput of various equipment in the process subsequent to the storage and discharge machine, and also makes these equipment smaller and cheaper.

本発明は、固形物の空気輸送用の管路に接続された分1
1tlと、核力1IIIlaの固形物排出口に接続され
た分配コンベヤと、該分配コンベヤの複数の排出口に対
応して管路を介して設けられた複数の貯留排出機と、該
分配コンベヤと該貯留排出機とを接続する管路に設けら
れた遮断弁とを具備する空気輸送装置である。本発明の
空気輸送装置は吸引式および圧送式のいずれの空気輸送
システムにおいても適用することができる。
The present invention is directed to a pipe for pneumatic transportation of solids.
1tl, a distribution conveyor connected to the solids discharge port of the nuclear power 1IIIa, a plurality of storage and discharge machines provided via pipes corresponding to the plurality of discharge ports of the distribution conveyor, and the distribution conveyor. This pneumatic transportation device is equipped with a shutoff valve provided in a pipe line connecting the storage and discharge machine. The pneumatic transport device of the present invention can be applied to both suction-type and pressure-feeding pneumatic transport systems.

まず本発明の実施例につき図面によって説明すれば、第
2図は本発明の一実施例であって、ごみや粉粒体の固形
物は管路3内を気流によって輸送され、投入ステーショ
ン1a11b、1cがら分離機8へ送られるようになっ
ている。分離機8ではサイクロンやバグフィルタなどの
任意の固気分離手段によって気流中から固形物を分離し
、分離された固形分を下部の排出口8′から後続の分配
コンベヤ15へ落下供給する。分配コンベヤ15には逆
回転が可能なスクリュウ15′が内蔵されており、分離
機8から供給される固形分を左右に任意に搬送できるも
のであって、スクリュウ15′を駆動するモータは図示
されていない。分配コンベヤ15の両側の端部には、排
出口16a116bが設けられ、さらに排出口16a、
16bにはエキスパンション17a、17bが接続され
ている。このエキスパンション17a 、 17bは分
配コンベヤ14側と貯留排出、*i 2a 、i2b側
との振動の伝播を抑制するものである。そしてエキスパ
ンション17a、17bから順次遮断弁18a、”18
b、管路19a、19b、および回転ドラム式の貯留排
出11t12a、12bが接続されている。従って分配
コンベヤ15のスクリュウ15′が矢印六方向へ固形物
を搬送覆れば分離機8で分離された固形物は右側の貯留
排出1fi12aへ貯留されることになり、他方スクリ
ュウ15′が矢印Aと反対方向へ固形物を搬送すれば、
固形物は左側の貯留排出1112bへ貯留されることと
なる。さらに遮断弁18a、18bの上流側と下流側と
の圧力を等しくするための連通管20a、2obと連通
管20a 、20bを任意に開閉可能な弁21a 、2
1bが設けられている。また弁22a、22bは貯留排
出機12a 、1’2b内を一大気圧と等しくするため
のものである。
First, an embodiment of the present invention will be described with reference to the drawings. Fig. 2 shows an embodiment of the present invention, in which solid matter such as garbage and powder is transported by airflow in the pipe 3, and the input station 1a11b, 1c is sent to the separator 8. In the separator 8, solids are separated from the air stream by any solid/gas separation means such as a cyclone or a bag filter, and the separated solids are supplied to the subsequent distribution conveyor 15 from a lower discharge port 8'. The distribution conveyor 15 has a built-in screw 15' that can rotate in reverse, and can arbitrarily convey the solids supplied from the separator 8 to the left and right, and the motor that drives the screw 15' is not shown in the figure. Not yet. Discharge ports 16a116b are provided at both ends of the distribution conveyor 15, and further discharge ports 16a,
Expansion 17a and 17b are connected to 16b. These expansions 17a and 17b suppress the propagation of vibrations between the distribution conveyor 14 side and the storage/discharge, *i 2a and i2b sides. Then, from the expansions 17a and 17b, the shutoff valves 18a and 18
b, pipe lines 19a and 19b, and rotating drum type storage and discharge 11t12a and 12b are connected. Therefore, if the screw 15' of the distribution conveyor 15 conveys the solids in the six directions of the arrows, the solids separated by the separator 8 will be stored in the storage discharge 1fi12a on the right side, If solids are transported in the opposite direction,
The solid matter will be stored in the storage discharge 1112b on the left side. Furthermore, communication pipes 20a and 2ob are used to equalize the pressures on the upstream and downstream sides of the cutoff valves 18a and 18b, and valves 21a and 2 that can open and close the communication pipes 20a and 20b as desired.
1b is provided. Further, the valves 22a and 22b are used to equalize the pressure inside the storage and discharge machines 12a and 1'2b to one atmospheric pressure.

次に第2図の空気輸送装置の作動について説明すると、
送風機9を作動させ、投入ステーションIa、1b、1
cから順次固形物を管路3へ投入し、気流によって分1
lll1機8へ輸送する。分離機8で分離された固形物
は分離機8の下部に設けられた排出口8−から分配コン
ベヤ15へと落下供給される。分配コンベヤ15では、
まずスクリュウ15′が矢印Aの方向へ固形物を搬送し
、固形物は排出口16a1エキスパンシヨン17a1遮
断弁18a、管路19aを通過して貯留排出機12aへ
貯留される。
Next, the operation of the pneumatic transport device shown in Fig. 2 will be explained.
The blower 9 is operated and the loading stations Ia, 1b, 1
Solids are sequentially introduced into pipe 3 starting from c, and separated by air flow.
Transport to ll1 aircraft 8. The solids separated by the separator 8 are supplied falling to the distribution conveyor 15 from a discharge port 8- provided at the bottom of the separator 8. On the distribution conveyor 15,
First, the screw 15' transports the solids in the direction of arrow A, and the solids pass through the discharge port 16a1, the expansion 17a1, the shutoff valve 18a, and the conduit 19a, and are stored in the storage/discharge machine 12a.

この場合、弁2 ’2 aと、貯留JJ+出機12aの
排出弁23aとを閉とし、遮断弁18aは開となってい
る。また左側の連断弁181)、弁21b 、22bお
よび排出弁23bは分配コンベヤ15内が大気と連通し
ない状態となるべく設定されておれば良いが、後述の切
換操作のために、弁21b、22bおよび排出弁23b
を閉とし、遮断弁18bを開として待機するのが望まし
い。
In this case, the valve 2'2a and the discharge valve 23a of the storage JJ+ outlet 12a are closed, and the cutoff valve 18a is open. Furthermore, the left-side connection valve 181), the valves 21b, 22b, and the discharge valve 23b may be set so that the inside of the distribution conveyor 15 does not communicate with the atmosphere. and discharge valve 23b
It is desirable to close the valve and wait with the shutoff valve 18b open.

貯留排出1112aの貯留量が限界となれば図示しない
検知器が検知し、スクリュウ15′の回転が逆転し固形
物は矢印Aと反対方向へ搬送され同様に貯留排出1ml
 2bへ貯留される。そこで右側の遮断弁18aを閉じ
、さらに弁21aが閉じていることを確認して、弁22
aを閉とし、貯留排出機12a内の気圧を大気圧となし
、排出弁23aを開けて貯留排出機12a内に貯留され
た固形物を排出する。この貯留排出t112aからの固
形物の排出操作の間、分配コンベヤ15のスクリュウ1
5′は固形物を他方の貯留排出機12bへ搬送している
ので、投入ステーションからの収集操作は継続されてい
る。
When the storage amount of the storage discharge 1112a reaches its limit, a detector (not shown) detects this, and the rotation of the screw 15' is reversed, and the solids are conveyed in the opposite direction to the arrow A, and 1 ml of storage and discharge is similarly carried out.
It is stored in 2b. Then, close the right shutoff valve 18a, confirm that the valve 21a is closed, and then close the valve 21a.
a is closed, the pressure inside the storage and discharge machine 12a is brought to atmospheric pressure, and the discharge valve 23a is opened to discharge the solid matter stored in the storage and discharge machine 12a. During this operation of discharging solids from the storage discharge t112a, the screw 1 of the distribution conveyor 15
5' is conveying the solids to the other storage discharger 12b, so that the collection operation from the input station is continued.

貯留排出1a12aの排出操作が完了したならば排出弁
23a、弁22aを閉となし、弁21aを開どし、貯留
排出機12a内の気圧を徐々に1・ばて遮断弁18a前
後の圧力差をなくし、その後遮断弁18aを開け、さら
に弁21aを閉じておくと、次の切換操作が容易となる
When the discharge operation of the storage discharge 1a12a is completed, the discharge valve 23a and the valve 22a are closed, the valve 21a is opened, and the atmospheric pressure inside the storage discharge machine 12a is gradually released to reduce the pressure difference before and after the cutoff valve 18a. , then open the shutoff valve 18a, and then close the valve 21a to facilitate the next switching operation.

他方、収集された固形分を貯留している貯留排出+!1
12bの貯留量が限界にきたならば同様にスクリュウ1
5′を逆回転させ固形物を貯留排出機12aへ貯留し、
貯留限界に達した貯留排出機12bの排出操作を行う。
On the other hand, the storage discharge + which stores the collected solids! 1
If the storage capacity of 12b reaches its limit, screw 1 in the same way.
5' is reversely rotated to store the solids in the storage/discharge machine 12a,
A discharge operation is performed for the storage and discharge machine 12b that has reached its storage limit.

このように、本発明の空気輸送装置は分配コンベヤ15
および遮断弁18a、18bの作動によって所望の貯留
排出Ill 2a 、12bに対し固形物を貯留するこ
とができ、さらには固形物の貯留が行われつつある貯留
排出機以外においては、同時に遮断弁を閉じて貯留され
た固形物を排出することができるものである。
Thus, the pneumatic conveyance device of the present invention has a distribution conveyor 15
By operating the shutoff valves 18a and 18b, the solids can be stored for the desired storage and discharge Ill 2a and 12b, and furthermore, in the storage and discharge machine other than the storage and discharge machine where solids are being stored, the shutoff valves are activated at the same time. It can be closed and the accumulated solids can be discharged.

なお連通管20a 、20bは必ずしも必須のものでは
ないが遮断弁18a、18bを開ける場合に遮断弁18
a、18bの前後の気圧を等しくしておけば遮断弁18
a、18bの開操作がより容易に実行できるので設けた
ものである。そして連通管20a 、20bの接続は必
ずしも第2図に限定されるものではな′り、遮断fr1
8a、18bの上流側は1本の管に統一することも可能
であり、その接続位置も分離機8とすることもできる。
Note that the communication pipes 20a and 20b are not necessarily essential, but when the cutoff valves 18a and 18b are opened, the communication pipes 20a and 20b are
If the air pressures before and after a and 18b are equalized, the shutoff valve 18
This is provided because the opening operation of the openings a and 18b can be performed more easily. The connection between the communication pipes 20a and 20b is not necessarily limited to that shown in FIG.
The upstream sides of 8a and 18b can be unified into one pipe, and the connection position thereof can also be the separator 8.

弁22a 、22bは貯留排出機12a112bに対 
 。
The valves 22a and 22b are connected to the storage discharger 12a112b.
.

応して、それぞれに設けなければならないが、ぞの場合
の接続は第2図に限定されるべぎものではなく、用は排
出弁23a 、23bを開けるに際して貯留排出111
2a、12b内の圧力を大気圧となし得るものであれば
よく、その結果排出弁23a、23bの開操作が極めて
容易に実行できる。
Accordingly, the connections must be provided in each case, but the connections in that case are not limited to those shown in FIG.
Any pressure can be used as long as it can bring the pressure inside 2a, 12b to atmospheric pressure, and as a result, the opening operation of the discharge valves 23a, 23b can be performed very easily.

第3図は本発明の実施例の要部であって、貯留排出va
12a〜12dを4つ設けた例である。第3図において
貯留排出I112a〜12dは各々モータ24a〜24
dによって駆動されるチェーン25a〜25dによって
回転されるものであり、また貯留排出Ill 2a〜1
2dはローラー26によって回転可能に支承されている
。27は4つの貯留排出1112a〜12dの排出弁2
38〜23dの下方に設けられたベルトコンベヤであっ
て、図示しない分別機、破砕機等の後の工程へ固形物を
搬送するものである。また28a〜28dは排、出片2
3a〜23dを開閉する場合の支点であって図示しない
固定されたアームによって支持されている。
FIG. 3 shows the main part of the embodiment of the present invention, showing the storage discharge va
This is an example in which four 12a to 12d are provided. In FIG. 3, the storage and discharge I112a to 12d are driven by motors 24a to 24, respectively.
It is rotated by the chains 25a to 25d driven by the storage and discharge Ill 2a to 1.
2d is rotatably supported by rollers 26. 27 is a discharge valve 2 for four storage discharges 1112a to 12d.
This is a belt conveyor provided below 38 to 23d, which conveys the solids to subsequent processes such as a separator and a crusher (not shown). In addition, 28a to 28d are discharge and protrusion pieces 2
It is a fulcrum when opening and closing 3a to 23d, and is supported by a fixed arm (not shown).

なお、第3図においては排出弁23a〜23dおよび遮
断弁18a〜18dの作動を容易とするための第2図の
連通管2Qa 、20b t)′よび弁2Ia 、21
b 、22a 122bに相当するものが設けられてい
ないが、必要に応じて設けることができる。
In addition, in FIG. 3, the communication pipes 2Qa, 20bt)' and valves 2Ia, 21 of FIG.
b, 22a, and 122b are not provided, but they can be provided if necessary.

以上述べたように本発明の空気輸送装置は、固形物の空
気輸送用の管路に接続された分離機と、該分離機の固形
物排出口に接続された分配コンベヤと該分配コンベヤの
複数の排出口に対応して管路を介して設けられた貯留排
出機と、該貯留排出機と該分配コンベVの排出口とを接
続する管路に設けられた遮断弁とを具備するものである
As described above, the pneumatic transportation device of the present invention includes a separator connected to a pipeline for pneumatic transportation of solids, a distribution conveyor connected to the solids discharge port of the separator, and a plurality of distribution conveyors. A storage discharger is provided via a pipe line in correspondence with the discharge port of the distribution conveyor V, and a shutoff valve is provided in the pipe line connecting the storage discharger and the discharge port of the distribution conveyor V. be.

本発明の空気輸送装置にあっては、分離機で分離したご
みや粉粒体等の固形物は分配コンベヤによって任意の貯
留排出機へ貯留され、また貯留操作を行っていない他の
貯留排出機は、同時に貯留排出機と分配コンベヤとの間
を接続する管路に設けられた遮断弁によってil!%さ
れた状態において内部に貯留された固形物を排出するこ
とができるものであるから、一部の貯留排出機の貯留量
が限界に達しても収集された固形物を分配コンベヤや遮
断弁の適切な操作によって他の貯留容量に余裕のある貯
留排出機へ導くことができ、しかもその切換操作に際し
、固形物の収集操作を停止する必要がないので、極めて
効率的な固形物の収集が可能であり、さらには貯留排出
機からの固形物の排出速度も排出操作中に他の貯留排出
機への貯留が行えるので、さほど速いものとはならず、
したがって、貯留排出機から後だ段の搬送機、分別機、
破砕機等の諸設備の処理能力を小さくすることができる
という効果がある。
In the pneumatic conveyance device of the present invention, the solids such as garbage and powder separated by the separator are stored in any storage and discharge machine by the distribution conveyor, and also in other storage and discharge machines that are not performing storage operation. At the same time, a shutoff valve installed in the pipe connecting between the storage discharger and the distribution conveyor allows the il! Since the solids stored inside can be discharged in a state where the amount of solids stored in With proper operation, it is possible to guide the system to another storage/discharge machine with sufficient storage capacity, and there is no need to stop the solids collection operation when switching operations, making extremely efficient collection of solids possible. Furthermore, the speed of discharging solids from the storage and discharge machine is not very fast because it can be stored in other storage and discharge machines during the discharge operation.
Therefore, from the storage/discharge machine to the subsequent conveyor, sorter,
This has the effect of reducing the processing capacity of various equipment such as a crusher.

さらに本発明の空気輸送装置において、上述の遮断弁前
後の連通手段或いは大気と連通ずるための弁等を設けれ
ば遮断弁の作動や貯留排出機の排出弁の作動が容易とな
る効果がある。
Furthermore, in the air transport device of the present invention, if a communication means before and after the above-mentioned cutoff valve or a valve for communicating with the atmosphere is provided, the operation of the cutoff valve and the discharge valve of the storage discharger can be easily operated. .

また本発明によれば、分配コンベヤを延長するだけで貯
留排出機を所望の数だけ設【プることができ、水平方向
へ延長するとしたならば装置の高さを増すことなく貯留
容量を増すことが可能となる。
Furthermore, according to the present invention, a desired number of storage and discharge machines can be installed simply by extending the distribution conveyor, and if the distribution conveyor is extended horizontally, the storage capacity can be increased without increasing the height of the device. becomes possible.

すなわら分離機を含めた装置の高さをいたずらに高くす
ることがないので架台等の強度も容易に得られやすい利
点がある。
In other words, since the height of the apparatus including the separator is not increased unnecessarily, there is an advantage that the strength of the pedestal etc. can be easily increased.

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

第1図は従来の空気輸送システムの概略図、第2図は本
発明の実施例を示す図、第3図は本発明の他の実施例の
要部を示す図である。 1a、1b11c ・・・投入ステーション2・・・収
集ステーション  3・・・管路4・・・投入シュート
  5・・・投入口  6・・・回転ドラム  7・・
・排出弁  8・・・分離機  8′・・・固形物排出
口  11・・・除塵装置  12.12a、12b1
12c112d ・・・貯留排出機  13・・・吸気
弁14・・・遮断弁  15・・・分配コンベヤ15′
・・・スフIJ 1ウ  18a、18b。 180.18d ・・・連断弁 特許出願人  株式会社荏原製作所
FIG. 1 is a schematic diagram of a conventional pneumatic transportation system, FIG. 2 is a diagram showing an embodiment of the present invention, and FIG. 3 is a diagram showing essential parts of another embodiment of the present invention. 1a, 1b11c...Input station 2...Collection station 3...Pipe line 4...Input chute 5...Input port 6...Rotating drum 7...
・Discharge valve 8...Separator 8'...Solid discharge port 11...Dust removal device 12.12a, 12b1
12c112d... Storage discharger 13... Intake valve 14... Shutoff valve 15... Distribution conveyor 15'
...Suf IJ 1u 18a, 18b. 180.18d ... Connection valve patent applicant Ebara Corporation

Claims (1)

【特許請求の範囲】[Claims] 固形物の空気輸送用の管路に接続された分111tlと
、該分離機の固形物排出口に接続された分配コンベヤと
、該分配コンベヤの複数の排出口に対応して管路を介し
て設けられた複数の貯留排出機と、該分配コンベヤと該
貯留排出機とを接続する管路に設けられた遮断弁とを具
備することを特徴とする空気輸送装置。
111 liters connected to a pipe line for pneumatic transportation of solids, a distribution conveyor connected to a solids discharge port of the separator, and a plurality of pipes corresponding to the plurality of discharge ports of the distribution conveyor. A pneumatic transport device comprising: a plurality of storage and discharge machines provided; and a shutoff valve provided in a conduit connecting the distribution conveyor and the storage and discharge machines.
JP7305183A 1983-04-27 1983-04-27 Pneumatic transport apparatus Pending JPS59198222A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7305183A JPS59198222A (en) 1983-04-27 1983-04-27 Pneumatic transport apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7305183A JPS59198222A (en) 1983-04-27 1983-04-27 Pneumatic transport apparatus

Publications (1)

Publication Number Publication Date
JPS59198222A true JPS59198222A (en) 1984-11-10

Family

ID=13507177

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7305183A Pending JPS59198222A (en) 1983-04-27 1983-04-27 Pneumatic transport apparatus

Country Status (1)

Country Link
JP (1) JPS59198222A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS628217U (en) * 1985-07-02 1987-01-19
JPH0376806U (en) * 1990-10-24 1991-08-01
EP4090610A4 (en) * 2020-01-14 2024-02-07 Maricap Oy Method for conveying material in a pneumatic material conveying system, and pneumatic material conveying system

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH561147A5 (en) * 1972-10-17 1975-04-30 Buehler Miag Gmbh
JPS52108668A (en) * 1976-03-09 1977-09-12 Shin Meiwa Ind Co Ltd Apparatus for treating refuse in pneumatic conveyer
JPS5574915A (en) * 1978-12-01 1980-06-05 Taisei Corp Separation exhauster for air carrier

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH561147A5 (en) * 1972-10-17 1975-04-30 Buehler Miag Gmbh
JPS52108668A (en) * 1976-03-09 1977-09-12 Shin Meiwa Ind Co Ltd Apparatus for treating refuse in pneumatic conveyer
JPS5574915A (en) * 1978-12-01 1980-06-05 Taisei Corp Separation exhauster for air carrier

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS628217U (en) * 1985-07-02 1987-01-19
JPH0376806U (en) * 1990-10-24 1991-08-01
JPH0524641Y2 (en) * 1990-10-24 1993-06-23
EP4090610A4 (en) * 2020-01-14 2024-02-07 Maricap Oy Method for conveying material in a pneumatic material conveying system, and pneumatic material conveying system
US11939174B2 (en) 2020-01-14 2024-03-26 Maricap Oy Method for conveying material in a pneumatic material conveying system, and pneumatic material conveying system

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