JPH07247005A - Rubbish separating and storing device - Google Patents
Rubbish separating and storing deviceInfo
- Publication number
- JPH07247005A JPH07247005A JP3848594A JP3848594A JPH07247005A JP H07247005 A JPH07247005 A JP H07247005A JP 3848594 A JP3848594 A JP 3848594A JP 3848594 A JP3848594 A JP 3848594A JP H07247005 A JPH07247005 A JP H07247005A
- Authority
- JP
- Japan
- Prior art keywords
- dust
- chamber
- storage chamber
- pipe
- storage
- 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.)
- Granted
Links
Landscapes
- Refuse Collection And Transfer (AREA)
- Air Transport Of Granular Materials (AREA)
- Loading Or Unloading Of Vehicles (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、建物等のごみ投入口に
投入されたごみを輸送管により空気輸送し、収集センタ
ーに収集するごみ空気輸送プラントにおいて、輸送管内
を空気輸送されてきたごみと空気とを分離するに好適な
ごみ分離貯留装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a refuse pneumatic transportation plant in which refuse introduced into a refuse introduction port of a building or the like is pneumatically transported by a transportation pipe and collected at a collection center. The present invention relates to a waste separation / storage device suitable for separating air and air.
【0002】[0002]
【従来の技術】従来より、輸送管内を空気輸送されてき
たごみと空気とを分離して貯留するごみ分離貯留装置は
知られている。図23はこのような従来のごみ分離貯留
装置を説明するためのごみ空気輸送プラントの系統図、
図24はその要部を拡大して示す説明図である。2. Description of the Related Art Conventionally, there is known a dust separating / storing device which separates and stores dust and air that have been pneumatically transported in a transport pipe. FIG. 23 is a system diagram of a waste pneumatic transportation plant for explaining such a conventional waste separation and storage device,
FIG. 24 is an explanatory view showing an enlarged main part thereof.
【0003】ごみ空気輸送プラントは、建物に設置され
た貯留筒式のごみ貯留排出装置1や回転ドラム式のごみ
貯留排出装置11より排出されたごみを輸送管6によっ
て空気輸送し、収集センター20に収集するようになっ
ている。貯留筒式のごみ貯留排出装置1は、建物のごみ
投入口2に上部が接続され、投入されたごみを一旦貯留
するごみ貯留筒3と、ごみ貯留筒3の下端に設けられた
排出弁4と、排出弁4と輸送管6側の分岐管6aとを接
続する輸送支管5とから構成されている。また、分岐管
6aの排出弁4よりも下流側には遮断弁7が設けられる
とともに、分岐管6aの最上流端には吸気弁8が設置さ
れている。回転ドラム式のごみ貯留排出装置11は、建
物のごみ投入口2に上部が接続された投入シュート12
と、内面に螺旋羽根を有しかつ一端が投入シュート12
の下端に接続され、図示しない駆動源により回転させら
れて、一旦貯留したごみを螺旋羽根の押し出し作用によ
り他端側に搬送し排出する回転ドラム13と、回転ドラ
ム13から排出されたごみを受け取る排出シュート14
と、排出シュート14の下端に設けられた排出弁4と、
排出弁4と輸送管6側の分岐管6bとを接続する輸送支
管5とから構成されている。また、分岐管6bの排出弁
4よりも下流側には遮断弁7が設けられるとともに、分
岐管6bの最上流端には吸気弁8が設置されている。収
集センター20には、ごみと空気とを分離するサイクロ
ン集塵機からなる分離機21と、分離機21で分離され
たごみを貯留排出するごみ排出装置22と、分離機21
で分離されない微細なダストを濾布等を透過させること
により捕集するバグフィルタ23と、バグフィルタ23
で捕集したダストをごみ排出装置22側に搬送するスク
リュコンベヤ等からなる搬送装置24と、輸送管6内の
空気を分離機21およびバグフィルタ23を経由して吸
引することにより輸送管6内に空気流を発生させるブロ
ワ25と、ブロワ25の吸引側と排出側にそれぞれ配置
されてブロワ25から発生する騒音を減衰させる一対の
消音器26と、排出側の消音器26よりも下流側に配置
され、ブロワ25の圧縮により昇温した空気を冷却する
冷却器27と、冷却器27よりも下流側に配置され、空
気に含まれるごみのにおいを除く脱臭装置28と、脱臭
された空気を大気に放出するための排気ダクト29と、
ブロワ25や搬送装置24の駆動系を制御するととも
に、各排出弁4や各遮断弁7及び各吸気弁8の開閉タイ
ミング制御等を行う制御装置30とが設置されている。
そして、ごみ排出装置22に貯留されたごみは、例えば
コンテナ輸送方式によってごみ焼却場31に二次輸送さ
れるようになっている。The waste pneumatic transportation plant pneumatically transports the waste discharged from the storage cylinder type waste storage and discharge device 1 and the rotating drum type waste storage and discharge device 11 installed in the building by the transport pipe 6 to collect the waste at the collection center 20. It is supposed to be collected. The storage cylinder type waste storage and discharge device 1 has an upper portion connected to a waste input port 2 of a building, and a waste storage cylinder 3 that temporarily stores the input waste, and a discharge valve 4 provided at the lower end of the waste storage cylinder 3. And a transport branch pipe 5 that connects the discharge valve 4 and the branch pipe 6a on the transport pipe 6 side. A cutoff valve 7 is provided downstream of the discharge valve 4 of the branch pipe 6a, and an intake valve 8 is provided at the most upstream end of the branch pipe 6a. The rotary drum type waste storage and discharge device 11 includes a charging chute 12 whose upper part is connected to a waste charging port 2 of a building.
And has a spiral blade on the inner surface and one end is a charging chute 12
The rotary drum 13 connected to the lower end of the rotary drum 13 and rotated by a drive source (not shown) to convey and discharge the dust once stored to the other end by the pushing action of the spiral blade, and to receive the dust discharged from the rotary drum 13. Discharge chute 14
And the discharge valve 4 provided at the lower end of the discharge chute 14,
It is composed of a transport branch pipe 5 that connects the discharge valve 4 and a branch pipe 6b on the transport pipe 6 side. Further, a cutoff valve 7 is provided downstream of the discharge valve 4 of the branch pipe 6b, and an intake valve 8 is provided at the most upstream end of the branch pipe 6b. In the collection center 20, a separator 21 that is a cyclone dust collector that separates waste from air, a waste discharge device 22 that stores and discharges the waste separated by the separator 21, and a separator 21.
And a bag filter 23 for collecting fine dust that is not separated by a filter cloth or the like.
Inside the transport pipe 6 by sucking the air inside the transport pipe 6 through the separator 21 and the bag filter 23, and the transport device 24 including a screw conveyor that transports the dust collected in step 1 to the dust discharge device 22 side. To the blower 25, a pair of silencers 26 disposed on the suction side and the discharge side of the blower 25 for attenuating the noise generated from the blower 25, and on the downstream side of the silencer 26 on the discharge side. The cooler 27 that is arranged to cool the air heated by the compression of the blower 25, the deodorizer 28 that is arranged on the downstream side of the cooler 27 to remove the odor of dust contained in the air, and the deodorized air An exhaust duct 29 for release to the atmosphere,
A control device 30 that controls the drive system of the blower 25 and the transport device 24 and that controls the opening / closing timing of each discharge valve 4, each shutoff valve 7, and each intake valve 8 is installed.
Then, the waste stored in the waste discharging device 22 is secondarily transported to the waste incinerator 31 by, for example, a container transportation system.
【0004】図24は分離機とごみ排出装置の詳細を示
すものである。分離機21は、その内部に後段のバグフ
ィルタ23への空気排出通路21aを遮るようにエリミ
ネータ32が設けられている。エリミネータ32は、か
ご形に形成された多数のフィン32aを有し、このかご
形のフィン32aが図示しない駆動装置により高速で回
転させられることによりフィルタとして機能するように
なっている。ごみ排出装置22は、3つの方式に大別で
きる。1つはコンテナ・コンパクタ22Aである。コン
テナ・コンパクタ22Aは、分離機21で分離されたご
みを真空圧下で連続的にコンテナ33に圧縮充填するも
のであり、ごみが圧縮充填されたコンテナ33はコンテ
ナ・コンパクタ22Aから分離されて車両34に積載さ
れ、焼却場や埋め立て地に二次輸送される。他の1つは
貯留排出装置22Bである。貯留排出装置22Bは、分
離機21で分離されたごみを、内面に螺旋羽根を有する
回転ドラム35内に真空圧下で連続的に圧縮貯留するも
ので、図23で示した回転ドラム13と基本的に同様の
構成を有するものである。回転ドラム35内に貯留され
たごみは、既存のごみ運搬車で焼却場や埋め立て地に二
次輸送される。更に他の1つは連続排出装置22Cであ
る。連続排出装置22Cは、分離機21で分離されたご
みを連続的に焼却場やパイプラインに直接排出するもの
である。FIG. 24 shows the details of the separator and the waste discharging device. The separator 21 is provided therein with an eliminator 32 so as to block the air discharge passage 21a to the bag filter 23 in the subsequent stage. The eliminator 32 has a large number of cage-shaped fins 32a, and the cage-shaped fins 32a are rotated at a high speed by a driving device (not shown) to function as a filter. The waste discharging device 22 can be roughly classified into three types. One is the container compactor 22A. The container compactor 22A continuously compresses and fills the waste separated by the separator 21 into the container 33 under a vacuum pressure. The container 33 filled with the compressive waste is separated from the container compactor 22A, and the vehicle 34 It is loaded onto the premises and secondarily transported to the incinerator and landfill. The other one is the storage and discharge device 22B. The storage / discharge device 22B is for continuously compressing and storing the dust separated by the separator 21 in a rotating drum 35 having spiral blades on the inner surface thereof under vacuum pressure, and is basically the same as the rotating drum 13 shown in FIG. It has the same configuration as that of. The waste stored in the rotary drum 35 is secondarily transported to an incinerator or a landfill by an existing waste carrier. Still another one is the continuous discharge device 22C. The continuous discharge device 22C continuously discharges the waste separated by the separator 21 directly to the incinerator or the pipeline.
【0005】また、後段のバグフィルタ23には、濾布
により捕集されて下方に堆積したダストを掻き集めて搬
送装置24に排出するための図示しない回転掻き羽根や
その駆動装置が設けられている。Further, the bag filter 23 in the subsequent stage is provided with a rotary scraping blade (not shown) and a driving device for scraping the dust collected by the filter cloth and accumulated below and discharging it to the conveying device 24. .
【0006】このようなものにおいて、輸送管6内を空
気輸送されてきたごみは分離機21内で空気と分離され
下方へ落下する。またエリミネータ32を通過してバグ
フィルタ23で捕集された微細なダストは搬送装置24
によりごみ排出装置22側に搬送され、分離機21内で
分離されたごみと共にごみ排出装置22内に運ばれ、排
出装置22すなわちコンテナ・コンパクタ22Aや貯留
排出装置22Bまたは連続排出装置22Cから二次輸送
手段を介して焼却場等に輸送され、廃棄処分される。一
方、分離機21内でごみと分離され、更にバグフィルタ
23で微細なダストとも分離された空気は、ブロワ25
により吸引されて吸引側の消音器26からブロワ25内
を通過し、圧縮されて排出側の消音器26から冷却器2
7を経て脱臭装置28に導入され、脱臭された後、排気
ダクト29から大気に放出される。[0006] In such a case, the dust that has been pneumatically transported in the transportation pipe 6 is separated from the air in the separator 21 and drops downward. Further, the fine dust collected by the bag filter 23 after passing through the eliminator 32 is conveyed by the transport device 24.
Is carried to the waste discharging device 22 side, and is carried into the waste discharging device 22 together with the waste separated in the separator 21, and is discharged from the discharging device 22, that is, the container compactor 22A, the storage discharging device 22B, or the continuous discharging device 22C. It is transported to the incineration site, etc. via transportation and disposed of. On the other hand, the air separated from the dust in the separator 21 and further separated from the fine dust by the bag filter 23 is the blower 25.
Is sucked by and passes through the blower 25 from the muffler 26 on the suction side, and is compressed from the muffler 26 on the discharge side to the cooler 2.
After being introduced into the deodorizing device 28 via 7 and being deodorized, it is discharged from the exhaust duct 29 to the atmosphere.
【0007】上記以外にごみを空気輸送して分離貯留す
るものとしては、特開昭55ー145906号公報に示
されるものがある。この公報のものは、図24で示した
貯留排出装置22Bの回転ドラム35と基本的に同様の
構成を有する貯留排出用回転ドラム、すなわち内面に螺
旋羽根を有する回転ドラムの入口部の外部の基台上にエ
アフィルタを摺動自在に固定設置するとともに、建物等
のごみ投入口に連なる輸送管をエアフィルタを貫通させ
てドラム内に引き込み、エアフィルタの外面側を小容積
のエアチャンバで覆い、エアチャンバとブロワとを吸気
管により接続するようにしている。[0007] In addition to the above, there is another one disclosed in Japanese Patent Laid-Open No. 145906/55 as a device for pneumatically transporting and separating and storing dust. This publication discloses a storage / discharge rotary drum basically having the same structure as the rotary drum 35 of the storage / discharge device 22B shown in FIG. 24, that is, a base outside the inlet of the rotary drum having spiral blades on its inner surface. The air filter is slidably fixed on the table, and the transportation pipe connected to the dust inlet of the building, etc. is drawn through the air filter into the drum, and the outer surface of the air filter is covered with a small volume air chamber. The air chamber and the blower are connected by an intake pipe.
【0008】この特開昭55ー145906号公報のも
のにおいて、輸送管内を空気輸送されてきたごみは回転
ドラム内で空気と分離されて輸送管の排出口近傍の下方
へ落下する。落下したごみは回転ドラムの回転による螺
旋羽根の回転により前方に押し進められ、回転ドラムの
排出口部の外部の基台上に設置された蓋の開放により回
転ドラムから押し出されれ、排出口下方のコンベヤ上に
移載される。In this Japanese Patent Laid-Open No. 145906/55, the dust that has been pneumatically transported in the transport pipe is separated from the air in the rotary drum and falls below the discharge port of the transport pipe. The dust that has fallen is pushed forward by the rotation of the spiral blade due to the rotation of the rotary drum, and is pushed out from the rotary drum by the opening of the lid installed on the base outside the discharge port of the rotary drum, and the conveyor below the discharge port. Reprinted on top.
【0009】[0009]
【発明が解決しようとする課題】しかしながら、輸送管
6内を空気輸送されてきたごみを分離機21で分離する
とともに、微細なダストを分離機21内のエリミネータ
32と後段のバグフィルタ23により2段階で捕集し、
このようにして空気から分離されたごみとダストとを排
出装置22内に貯留しかつ圧縮、排出するようにした前
者のものにあっては、ごみの分離、ダストの捕集、分離
された空気からの脱臭、分離・捕集されたごみやダスト
の貯留、圧縮、排出が、それぞれ別々の機器にて行われ
ているので、装置が大掛かりとなり、それに合せて収集
センター20のスぺース(従来は700m3 )も大きく
ならざるを得ない。更に、分離機21のエリミネータ3
2駆動用の電動機やバグフィルタ23の回転掻き羽根駆
動用の電動機、更にコンテナ・コンパクタ22A用の油
圧装置や連続排出装置22C用の油圧装置、貯留排出装
置22B用の螺旋羽根等の設備が必要となり、設備費も
高く付いてしまう。更にまた、脱臭装置28をブロワ2
5よりも下流側(排出側)に配置しているので、脱臭装
置28の脱臭能率の低下を防ぐためには、脱臭装置28
の手前に冷却器27を設置し、ブロワ25により圧縮さ
れて昇温した空気を冷却する必要があった。したがっ
て、脱臭装置28をブロワ25の吸引側に配置すれば冷
却器27を不要にできる。しかし、この場合には、脱臭
装置28の容器をブロワ25の吸引能力分の耐圧容器に
構成する必要がある。すなわち、脱臭装置28をブロワ
25の排出側に配置した場合は100mmH2Oの圧力
に耐える比較的安価な容器ですむのに対し、脱臭装置2
8をブロワ25の吸引側に配置した場合には6000m
mH2Oもの圧力(排出側の60倍の圧力)に耐える高
価な高耐圧容器が必要になる。このため、従来は脱臭装
置28をブロワ25の排出側に配置し、ブロワ25によ
って圧縮され昇温した空気を脱臭装置28の手前で冷却
器27によって冷却することにより、脱臭装置28の脱
臭能率が低下するのを防ぐようにしているのが実情であ
った。However, the dust that has been pneumatically transported in the transport pipe 6 is separated by the separator 21, and fine dust is separated by the eliminator 32 in the separator 21 and the bag filter 23 in the subsequent stage. Collect in stages,
In the former case in which the dust and dust separated from the air in this way are stored in the discharge device 22 and compressed and discharged, the separation of dust, the collection of dust, and the separated air Deodorization from the equipment and storage, compression and discharge of separated and collected dust and dust are carried out by different equipment, so the equipment becomes bulky and the space of the collection center 20 (conventional) Has to grow as large as 700 m 3 ). Further, the eliminator 3 of the separator 21
A motor for driving two, a motor for driving the rotary scraping blades of the bag filter 23, a hydraulic device for the container compactor 22A, a hydraulic device for the continuous discharge device 22C, and a spiral blade for the storage and discharge device 22B are required. Therefore, the equipment cost will be high. Furthermore, the deodorizing device 28 is installed in the blower 2
Since it is arranged on the downstream side (discharging side) of No. 5, in order to prevent the deodorizing efficiency of the deodorizing device 28 from decreasing, the deodorizing device 28
It was necessary to install the cooler 27 in front of, and cool the air that was compressed by the blower 25 and heated. Therefore, if the deodorizing device 28 is arranged on the suction side of the blower 25, the cooler 27 can be omitted. However, in this case, it is necessary to configure the container of the deodorizing device 28 to be a pressure resistant container for the suction capacity of the blower 25. That is, when the deodorizing device 28 is arranged on the discharge side of the blower 25, a relatively inexpensive container that can withstand a pressure of 100 mmH 2 O is sufficient, whereas the deodorizing device 2
When 8 is placed on the suction side of the blower 25, 6000m
An expensive high pressure container that can withstand a pressure of mH 2 O (60 times the pressure on the discharge side) is required. Therefore, conventionally, the deodorizing device 28 is disposed on the discharge side of the blower 25, and the air compressed and heated by the blower 25 is cooled by the cooler 27 before the deodorizing device 28. The reality is that we try to prevent it from dropping.
【0010】また、内面に螺旋羽根を有する貯留排出用
回転ドラムの入口部の外部の基台上にエアフィルタを摺
動自在に固定設置するとともに、輸送管をエアフィルタ
を貫通させ、エアフィルタの外面側を小容積のエアチャ
ンバを介してブロワ側の吸気管と接続するようにした後
者のものは以下のような問題があった。 イ)エアフィルタの面積を大きくすることができず、こ
のためブロワの吸引力を上げながらエアフィルタ部にお
ける空気通過速度を小さくすることが困難で、風量の大
きい(ごみ輸送管径の大きい)プラントには適用できな
い。 ロ)基台上に固定設置されたエアフィルタや排出口部の
蓋と回転体である貯留排出用回転ドラムとの間の気密を
保つために、シール部の構造が複雑となり、装置が高価
となってしまうのみならず、エアフィルタの面積を大き
くすればするほど特殊な構造のシール部を大きくしなけ
ればならい。 ハ)エアフィルタの面積を大きくできずかつエアチャン
バの容積が小さいため、ブロワの吸引力を上げると、エ
アフィルタ部における空気通過速度が増大し、搬送され
てきたごみのエアフィルタ部への吸引付着を招くので、
ブロワの吸引圧力ならびに風量とも通常の空気輸送より
かなり小さく抑えざるを得ない。 ニ)上記ハ)の理由から輸送管内を空気輸送されてきた
ごみの慣性力が小さく、空気輸送されてきたごみを遠方
へ飛ばして圧縮することができないため、回転ドラム内
に螺旋羽根からなるごみ圧縮装置およびその駆動装置を
設ける必要があり、装置が複雑で高価にならざるを得な
いばかりでなく、ごみ貯留部(貯留排出用回転ドラム)
そのものが回転するので、一旦降下したごみが舞い上が
り、エアフィルタ部への吸引付着を招き易くなる。 ホ)貯留排出用回転ドラム、入口部のエアフィルタ、排
出口部の蓋のいずれも基台上に設置されているため、ご
み貯留部(エアフィルタや蓋を含む貯留排出用回転ドラ
ム部)そのものをコンテナ車にて搬出することが不可能
である。 ヘ)空気輸送されるごみが袋に収容されたごみである場
合、回転ドラム内の螺旋羽根に当り破けてしまい、上記
ニ)のような問題が発生する。In addition, an air filter is slidably fixedly installed on a base outside the inlet of the storage / drainage rotary drum having a spiral blade on the inner surface, and a transport pipe is passed through the air filter so that the air filter The latter one, in which the outer surface side is connected to the intake pipe on the blower side through the small-volume air chamber, has the following problems. B) The area of the air filter cannot be increased, so it is difficult to increase the suction force of the blower while reducing the air passage speed in the air filter section, and the plant has a large air volume (large dust transport pipe diameter). Not applicable to. B) In order to maintain airtightness between the air filter fixedly installed on the base and the cover of the discharge port and the rotary drum for storage and discharge, which is the rotating body, the structure of the seal part becomes complicated and the device is expensive. Not only that, but the larger the area of the air filter, the larger the size of the seal with a special structure. C) Since the area of the air filter cannot be increased and the volume of the air chamber is small, increasing the suction force of the blower increases the air passage speed in the air filter section, and sucks the transferred dust to the air filter section. Because it causes adhesion
Both the suction pressure of the blower and the air volume must be kept much smaller than in ordinary air transportation. D) For the reason of c) above, the inertial force of the dust that has been pneumatically transported in the transport pipe is small, and the dust that has been pneumatically transported cannot be flown away and compressed, so dust that consists of spiral blades inside the rotating drum. It is necessary to provide a compression device and its drive device, and the device is inevitably complicated and expensive, as well as a waste storage part (rotation drum for storage and discharge).
Since it itself rotates, dust that has dropped once rises up, and it becomes easy to cause suction and adhesion to the air filter portion. E) Since the storage and discharge rotary drum, the inlet air filter, and the discharge port lid are all installed on the base, the waste storage unit (storage and discharge rotary drum including the air filter and lid) itself It is impossible to carry out the container car. F) If the dust transported by air is the dust contained in the bag, it will hit the spiral blades in the rotary drum and be broken, and the above problems d) will occur.
【0011】本発明は、叙上の点に鑑み、収集センター
内の設備の統合、共有化が図れ、収集センターのスぺー
スを圧縮できるとともに、ごみ空気輸送時の慣性力を利
用してごみの圧縮、貯留を行えるごみ分離貯留装置を提
供することを目的とする。In view of the above points, the present invention makes it possible to integrate and share the facilities in the collection center, compress the space of the collection center, and utilize the inertial force during pneumatic transportation of dust to collect dust. It is an object of the present invention to provide a waste separation storage device that can compress and store waste.
【0012】[0012]
【課題を解決するための手段】本発明のごみ分離貯留装
置は、耐圧容器内を高強度フィルタにより2室に画成し
て、一方に建物のごみ投入口に連なる輸送管を、他方に
ブロワの吸引側に連なる風管を、それぞれ接続して、輸
送管側の室を貯留室に、ブロワ側の室を排気室に、それ
ぞれ形成し、かつ貯留室にはごみ排出用の排出弁を設け
たものである。A waste separation and storage device according to the present invention has a pressure-resistant container having two chambers defined by a high-strength filter, a transport pipe connected to a waste inlet of a building on one side, and a blower on the other side. The air pipes connected to the suction side are connected to form a chamber on the transport pipe side as a storage chamber and a chamber on the blower side as an exhaust chamber, and a discharge valve for discharging dust is provided in the storage chamber. It is a thing.
【0013】また、貯留室内に空気輸送されてきたごみ
がその重力により貯留室底面まで降下する前に貯留室の
最奥部の壁面に衝突するように、輸送管内の風速を13
m/sec 〜35m/sec 、ごみ輸送速度を、比重0.1
5t/m3 以上の重量物の場合で5m/sec 以上、比重
0.15t/m3 以下の軽量物の場合で10m/sec以
上に設定したものである。Further, the wind speed in the transportation pipe is set to 13 so that dust that has been pneumatically transported into the storage chamber collides with the innermost wall surface of the storage chamber before it falls to the bottom surface of the storage chamber due to its gravity.
m / sec-35m / sec, refuse transportation speed, specific gravity 0.1
It is set to 5 m / sec or more for a heavy object of 5 t / m 3 or more and 10 m / sec or more for a lightweight object of a specific gravity of 0.15 t / m 3 or less.
【0014】また、高強度フィルタの面積を、高強度フ
ィルタ部での空気通過速度が一般ごみの場合で2m/se
c 以下、袋ごみの場合で5m/sec 以下、瓶・缶の場合
で10m/sec 以下となる面積に設定したものである。Further, the area of the high-strength filter is set to 2 m / se when the air passage speed in the high-strength filter portion is general dust.
Below c, the area is set to 5 m / sec or less for bag waste and 10 m / sec or less for bottles and cans.
【0015】また、輸送管の貯留室との接続部に、輸送
管直径の2倍以上の直管部を設けたものである。Further, a straight pipe portion having a diameter equal to or more than twice the diameter of the transport pipe is provided at the connecting portion of the transport pipe with the storage chamber.
【0016】また、輸送管と風管との内部圧力の差を調
整して貯留室内に貯留されるごみの圧縮度を制御するご
み圧縮度制御手段を設けたものである。Further, a dust compressibility control means for adjusting the difference in internal pressure between the transport pipe and the wind pipe to control the compressibility of the dust stored in the storage chamber is provided.
【0017】また、輸送管と風管との内部圧力の差の変
動をみて貯留室内のごみの満杯を検出するごみ満杯検出
手段を設けたものである。Further, there is provided dust full detection means for detecting the fullness of dust in the storage chamber by observing the fluctuation of the internal pressure difference between the transport pipe and the wind pipe.
【0018】また、貯留室内の底部に、貯留室内に貯留
したごみの排出装置を設置したものである。Further, a device for discharging the dust stored in the storage chamber is installed at the bottom of the storage chamber.
【0019】また、貯留室内に、空気輸送されてきた軽
量ごみの高強度フィルタ側への飛翔を規制する通気性を
備えたじゃま板を設けたものである。Further, a baffle plate having air permeability is provided in the storage chamber for restricting the flying of the air-transported lightweight dust to the high-strength filter side.
【0020】また、排気室内の空気流通経路の途中に脱
臭フィルタを設置したものである。Further, a deodorizing filter is installed in the middle of the air circulation path in the exhaust chamber.
【0021】また、排気室に、高強度フィルタ洗浄用の
外気導入弁を設けたものである。Further, the exhaust chamber is provided with an outside air introduction valve for cleaning the high-strength filter.
【0022】また、輸送管の貯留室接続部の近傍に遮断
弁を設けるとともに、風管の排気室接続部の近傍に、ブ
ロワへの流路を排気室と外気との間で切り換える切換弁
を設けたものである。Further, a shut-off valve is provided near the connecting portion of the storage chamber of the transport pipe, and a switching valve for switching the flow path to the blower between the exhaust chamber and the outside air is provided near the connecting portion of the exhaust chamber of the wind pipe. It is provided.
【0023】また、耐圧容器を輸送管および風管から分
離可能に構成したものである。Further, the pressure resistant container can be separated from the transportation pipe and the wind pipe.
【0024】[0024]
【作用】本発明において、輸送管内を空気輸送されてき
たごみやダストは、耐圧容器内を大きく2室に画成して
いる高強度フィルタによって貯留室内で空気と分離さ
れ、貯留室内に全て貯留される。そして貯留室内に貯留
されたごみやダストは、排出弁より外部に排出される。
このように、耐圧容器内を高強度フィルタにより画成
し、輸送管側の貯留室内にてごみやダストを全て空気か
ら分離させ、貯留することにより、耐圧容器部で、ごみ
の分離、ダストの捕集、分離・捕集されたごみやダスト
の貯留、排出を全て行うことができ、従来の分離機、エ
リミネータ、バグフィルタ、排出装置等の統合、共有化
を図ることができる。このため、分離機のエリミネータ
駆動用の電動機やバグフィルタの回転掻き羽根駆動用の
電動機等の設備が不要となり、設備費を安価にできると
ともに、収集センターのスぺースを圧縮することができ
る。In the present invention, the dust and dirt that have been pneumatically transported in the transportation pipe are separated from the air in the storage chamber by the high-strength filter that largely divides the pressure vessel into two chambers, and are all stored in the storage chamber. To be done. Then, the dust and the dust stored in the storage chamber are discharged to the outside through the discharge valve.
In this way, by defining the inside of the pressure-resistant container with a high-strength filter, separating all the dust and dust from the air in the storage chamber on the transport pipe side and storing it, the pressure-resistant container section separates dust and dust. Collection, separation and collection and collection of collected dust and dust can be performed, and conventional separators, eliminators, bag filters, discharge devices, etc. can be integrated and shared. Therefore, equipment such as an electric motor for driving the eliminator of the separator and an electric motor for driving the rotary scraping blade of the bag filter are not required, and the equipment cost can be reduced and the space of the collection center can be compressed.
【0025】更に、本装置が設置される地域のごみの特
性に合わせて、輸送管内の風速を13m/sec 〜35m
/sec 、ごみ輸送速度を、比重0.15t/m3 以上の
重量物の場合で5m/sec 以上、比重0.15t/m3
以下の軽量物の場合で10m/sec 以上に設定すること
により、貯留室内に空気輸送されてきたごみがその重力
により貯留室底面まで降下する前に貯留室の最奥部の壁
面に衝突させることができ、空気輸送時の慣性力を利用
して貯留室の最奥部より順次ごみを圧縮貯留することが
できる。このため、コンテナ・コンパクタ用の油圧装置
や連続排出装置用の油圧装置、貯留排出装置用の螺旋羽
根等の設備が不要となり、設備費を更に安価にすること
ができる。Furthermore, the wind speed in the transportation pipe is set to 13 m / sec to 35 m according to the characteristics of the waste in the area where this device is installed.
/ Sec, the waste transportation speed is 5 m / sec or more for a heavy object having a specific gravity of 0.15 t / m 3 or more, and a specific gravity of 0.15 t / m 3
In the case of the following lightweight products, by setting it to 10 m / sec or more, the dust that has been pneumatically transported into the storage chamber collides with the innermost wall surface of the storage chamber before it falls to the bottom surface of the storage chamber due to its gravity. Therefore, it is possible to compress and store dust sequentially from the innermost portion of the storage chamber by utilizing the inertial force during pneumatic transportation. Therefore, equipment such as a hydraulic device for a container / compactor, a hydraulic device for a continuous discharge device, and a spiral blade for a storage / discharge device is not required, and the cost of the device can be further reduced.
【0026】更にまた、高強度フィルタの面積を、高強
度フィルタ部での空気通過速度が一般ごみの場合で2m
/sec 以下、袋ごみの場合で5m/sec 以下、瓶・缶の
場合で10m/sec 以下となる面積に設定することによ
り、ブロワの吸引力を上げながらフィルタ部における空
気通過速度を小さくすることができ、微細なダストのフ
ィルタ部への吸引付着を抑えることができる。Furthermore, the area of the high-strength filter is set to 2 m when the air passing speed in the high-strength filter portion is general dust.
/ Sec or less, 5 m / sec or less for bag waste and 10 m / sec or less for bottles / cans to reduce the air passage speed in the filter while increasing the suction power of the blower. Therefore, suction and adhesion of fine dust to the filter portion can be suppressed.
【0027】更に、輸送管の貯留室との接続部に、輸送
管直径の2倍以上の直管部を設けることにより、貯留室
に投入されるごみの進入速度を安定させることができ、
ごみ輸送速度の調整を容易にすることができる。Furthermore, by providing a straight pipe portion having a diameter of at least twice the diameter of the transport pipe at the connection portion of the transport pipe with the storage chamber, it is possible to stabilize the entry speed of the dust thrown into the storage chamber,
It is possible to easily adjust the waste transportation speed.
【0028】更にまた、輸送管と風管との内部圧力の差
を調整して貯留室内に貯留されるごみの圧縮度を制御す
るごみ圧縮度制御手段を設けることにより、本装置が設
置される地域のごみの特性に合わせた輸送速度や圧縮度
の調整が容易となり、ごみの輸送速度や圧縮度の調整の
自動化が可能となる。Furthermore, the present apparatus is installed by providing a dust compression degree control means for adjusting the difference in internal pressure between the transportation pipe and the wind pipe to control the compression degree of the dust stored in the storage chamber. It becomes easy to adjust the transportation speed and compression degree according to the characteristics of local waste, and it becomes possible to automate the adjustment of the transportation speed and compression degree of waste.
【0029】更に、輸送管と風管との内部圧力の差の変
動をみて貯留室内のごみの満杯を検出するごみ満杯検出
手段を設けることにより、ごみの満杯を自動的に検出さ
せることができ、これによりブロワが過負荷状態に至る
のを防ぐことができる。Further, by providing a dust full detection means for detecting the fullness of the dust in the storage chamber by observing the fluctuation of the internal pressure difference between the transport pipe and the wind pipe, the fullness of the dust can be automatically detected. Thus, it is possible to prevent the blower from being overloaded.
【0030】更にまた、貯留室内の底部に、貯留室内に
貯留したごみの排出装置を設置することにより、空気輸
送によって貯留室内に圧縮貯留されたごみを排出時に排
出弁まで搬送でき、外部へのごみの排出を容易に行うこ
とができる。Furthermore, by installing a device for discharging the dust stored in the storage chamber at the bottom of the storage chamber, it is possible to convey the dust compressed and stored in the storage chamber by air transportation to the discharge valve at the time of discharge, and to the outside. The waste can be easily discharged.
【0031】更に、貯留室内に、空気輸送されてきた軽
量ごみの高強度フィルタ側への自由飛翔を規制する通気
性を備えたじゃま板を設けることにより、紙片や微細な
ダストの高強度フィルタ側への自由飛翔を規制でき、フ
ィルタ部への紙片や微細なダストの吸引付着を確実に抑
えることができる。Further, by providing a baffle plate having air permeability in the storage chamber, which restricts free flight of pneumatically transported light dust to the high-strength filter side, the high-strength filter side of paper pieces and fine dust is provided. It is possible to restrict free flight to the filter, and it is possible to reliably suppress suction and adhesion of paper chips and fine dust to the filter section.
【0032】更にまた、排気室内の空気流通経路の途中
に脱臭フィルタを設置することにより、排気室すなわち
耐圧容器に脱臭装置の容器を兼用させて脱臭フィルタを
ブロワの吸引側に配置することができ、従来必要として
いた脱臭装置の容器と冷却器を不要のものとすることが
できる。Furthermore, by installing a deodorizing filter in the middle of the air circulation path in the exhaust chamber, the exhaust chamber, that is, the pressure resistant container, can also serve as the container of the deodorizing device, and the deodorizing filter can be arranged on the suction side of the blower. The container and cooler of the deodorizing device, which have been conventionally required, can be eliminated.
【0033】更に、排気室に高強度フィルタ洗浄用の外
気導入弁を設けることにより、排気室内に外気を導入す
ることが可能となって、ブロワの運転を止めなくても、
排気室の内圧を貯留室の内圧よりも高くすることができ
る。このため、高強度フィルタ部に、排気室から貯留室
への空気の流れ(定常運転時とは逆の流れ)を発生させ
ることができ、これにより高強度フィルタに付着してい
る微細なダスト等を吹き飛ばし除去することができ、高
強度フィルタを洗浄することができる。Further, by providing the outside air introduction valve for cleaning the high-strength filter in the exhaust chamber, it becomes possible to introduce the outside air into the exhaust chamber, without stopping the operation of the blower.
The internal pressure of the exhaust chamber can be made higher than the internal pressure of the storage chamber. Therefore, the high-strength filter section can be caused to generate a flow of air from the exhaust chamber to the storage chamber (a flow that is the reverse of that during normal operation), which results in fine dust, etc. adhering to the high-strength filter. Can be blown off and removed, and the high-strength filter can be washed.
【0034】更にまた、輸送管の貯留室接続部の近傍に
遮断弁を設けるとともに、風管の排気室接続部の近傍
に、ブロワへの流路を排気室と外気との間で切り換える
切換弁を設けることにより、ブロワの運転を止めること
なく、貯留室と排気室とを真空状態のまま配管系から遮
断することができる。そしてこの状態で外気導入弁によ
って排気室内に外気を導入することにより、高強度フィ
ルタ部を排気室から貯留室へ流れる空気の速度を速くす
ることができ、高強度フィルタの洗浄効果を高めること
ができる。Furthermore, a shutoff valve is provided near the connecting portion of the storage chamber of the transport pipe, and a switching valve for switching the flow path to the blower between the exhaust chamber and the outside air is provided near the connecting portion of the exhaust chamber of the wind pipe. By providing the above, the storage chamber and the exhaust chamber can be shut off from the piping system in a vacuum state without stopping the operation of the blower. Then, in this state, by introducing the outside air into the exhaust chamber by the outside air introduction valve, the velocity of the air flowing from the exhaust chamber to the storage chamber can be increased in the high-strength filter portion, and the cleaning effect of the high-strength filter can be enhanced. it can.
【0035】更に、耐圧容器を輸送管および風管から分
離可能に構成することにより、耐圧容器にコンテナ機能
を持たせることができ、そのまま車両にて搬出すること
ができる。Further, by making the pressure-resistant container separable from the transportation pipe and the wind pipe, the pressure-resistant container can have a container function and can be carried out by the vehicle as it is.
【0036】[0036]
実施例1.以下、図示実施例により本発明を説明する。
図1は本発明の第1の実施例に係るごみ分離貯留装置を
説明するためのごみ空気輸送プラントの系統図、図2は
その運転条件を説明するための要部拡大斜視図であり、
各図中、従来に相当する部分には同一符号を付してあ
る。Example 1. The present invention will be described below with reference to illustrated embodiments.
FIG. 1 is a system diagram of a waste pneumatic transportation plant for explaining a waste separation / storage device according to a first embodiment of the present invention, and FIG. 2 is an enlarged perspective view of an essential part for explaining its operating conditions.
In each of the drawings, parts corresponding to conventional ones are designated by the same reference numerals.
【0037】本実施例のごみ分離貯留装置は、収集セン
ター20内に耐圧容器40を設置し、耐圧容器40内を
高強度フィルタ41により上下2室に画成して、一方に
建物のごみ投入口2に連なる輸送管6を、他方にブロワ
25の吸引側に連なる風管42を、それぞれ接続して、
輸送管6側の室を貯留室43に、ブロワ25側の室を排
気室44に、それぞれ形成し、かつ貯留室43にはごみ
排出用の排出弁45を設けて構成したものである。In the refuse separating and storing apparatus of this embodiment, a pressure-resistant container 40 is installed in the collection center 20, and the inside of the pressure-resistant container 40 is divided into upper and lower two chambers by a high-strength filter 41. Connect the transportation pipe 6 connected to the mouth 2 and the air pipe 42 connected to the suction side of the blower 25 to the other side,
The chamber on the side of the transport pipe 6 is formed in the storage chamber 43, the chamber on the side of the blower 25 is formed in the exhaust chamber 44, and the storage chamber 43 is provided with a discharge valve 45 for discharging dust.
【0038】本実施例のごみ分離貯留装置において、耐
圧容器40の形状は特に限定するものでなく、例えば円
錐でも、又は断面が多角形でも良く、更に建物の一室や
その一部(壁、床など)を利用しても良い。要するに必
要な耐圧強度が得られて、内部を2室に画成する高強度
フィルタ41の面積を大きくできるものであれば如何様
な形状をも採用することができる。また、高強度フィル
タ41の材質も特に限定するものでなく、例えばプラス
チックフィルタ、パンチングメタル等、必要な強度が得
られかつ通気性が良いものであれば如何様な材質をも採
用することができる。したがって、比較的強度の確保が
容易なプラスチックフィルタやパンチングメタル等をベ
ースにするならば、これらに金網やテトロンフェルト等
を組み合わせてフィルタを構成しても良い。更に、高強
度フィルタ41の周縁部の取付け位置は、耐圧容器40
内の上面、側面、底面のどの部分に設けても良い。In the waste separation / storage apparatus of this embodiment, the shape of the pressure container 40 is not particularly limited, and may be, for example, a cone or a polygonal cross section. You can also use the floor). In short, any shape can be adopted as long as the required pressure resistance can be obtained and the area of the high-strength filter 41 that defines the interior into two chambers can be increased. Further, the material of the high-strength filter 41 is not particularly limited, and any material such as a plastic filter and punching metal can be adopted as long as the required strength is obtained and the air permeability is good. . Therefore, if a plastic filter, punching metal, or the like, whose strength is relatively easy to secure, is used as the base, a wire mesh, tetron felt, or the like may be combined therewith to form the filter. Furthermore, the mounting position of the peripheral portion of the high-strength filter 41 is set to the pressure resistant container 40.
It may be provided on any of the upper surface, side surface, and bottom surface inside.
【0039】なお、収集センター20内には制御装置4
6が設置されている。制御装置46は、ブロワ25を後
述の運転条件下で制御するとともに、建物側の各排出弁
4や各遮断弁7及び各吸気弁8の開閉タイミングを制御
する。The control device 4 is installed in the collection center 20.
6 is installed. The control device 46 controls the blower 25 under the operating conditions described later, and also controls the opening / closing timing of each discharge valve 4, each cutoff valve 7, and each intake valve 8 on the building side.
【0040】上述の構成を有する本実施例のごみ分離貯
留装置において、輸送管6内を空気輸送されてきたごみ
やダストは、耐圧容器40内を大きく2室に画成してい
る高強度フィルタ41によって貯留室43内で空気と分
離され、貯留室43内に全て貯留される。そして貯留室
43内に貯留されたごみやダストは、排出弁45より外
部に排出される。このように、本実施例のごみ分離貯留
装置は、耐圧容器40内を高強度フィルタ41により画
成し、輸送管6側の貯留室43内にてごみやダストを全
て空気から分離させ、貯留した後、外部に排出するよう
にしているので、従来の分離機、エリミネータ、バグフ
ィルタ、排出装置の機能であるごみの分離、ダストの捕
集、分離・捕集されたごみやダストの貯留、排出の機能
を、単一の耐圧容器40部に全て持たせることができ
る。このため、分離機のエリミネータ駆動用の電動機や
バグフィルタの回転掻き羽根駆動用の電動機等の設備も
不要となり、設備費を安価にできるとともに、収集セン
ター20のスぺースを従来の1/2まで圧縮することが
できる。つまり、収集センター20のスぺースとして従
来700m3 必要であったものを350m3 まで圧縮す
ることができる。In the waste separation / storage device of the present embodiment having the above-mentioned structure, the dust and the dust that has been pneumatically transported through the transport pipe 6 has a high-strength filter in which the pressure vessel 40 is largely divided into two chambers. It is separated from the air in the storage chamber 43 by 41, and is entirely stored in the storage chamber 43. Then, the dust and the dust stored in the storage chamber 43 are discharged to the outside through the discharge valve 45. As described above, in the waste separation / storage device of the present embodiment, the inside of the pressure-resistant container 40 is defined by the high-strength filter 41, and all the dust and dust are separated from the air in the storage chamber 43 on the side of the transport pipe 6 and stored. After that, since it is designed to be discharged to the outside, the conventional separator, eliminator, bag filter, and dust removal that are the functions of the discharge device, the collection of dust, the storage of separated / collected dust and dust, The single pressure-resistant container 40 part can have all the functions of discharging. For this reason, equipment such as an electric motor for driving the eliminator of the separator and an electric motor for driving the rotary scraping blade of the bag filter are not required, and the equipment cost can be reduced and the space of the collecting center 20 can be reduced to half that of the conventional one. Can be compressed up to. That is, it is possible to compress the space of the collection center 20 which was required to be 700 m 3 in the past to 350 m 3 .
【0041】また、本実施例のごみ分離貯留装置におい
て、運転条件は以下のように設定した。即ち、輸送管6
内の風速を13m/sec 〜35m/sec 、ごみ輸送速度
を、比重0.15t/m3 以上の重量物の場合で5m/
sec 以上、比重0.15t/m3 以下の軽量物(例えば
紙や布、ビニールなど)の場合で10m/sec 以上に設
定した。この運転条件は、本装置が設置される地域で発
生するごみの特性(ごみの重量)をみて、事前に設定し
た。ここで、風速の下限値を13m/sec としたことの
理由は、軽量ごみでも安定した空気輸送を確保できるよ
うにするためである。また風速の上限値を35m/sec
としたことの理由は、厨芥でも空気輸送できるようにす
るためである。この風速の上限値35m/sec は、言い
換えれば厨芥の空気輸送を可能とするための下限値であ
る。このように風速の上限値35m/sec を低く抑える
のは、風速が上がると圧力損失が風速に2乗して大きく
なり、そのために動力(ブロワ)を大きくしなければな
らないからであり、それ以上風速を上げるとデメリット
が大きくなるからである。これにより、貯留室43内に
空気輸送されてきたごみを、その重力により貯留室43
底面まで降下する前に貯留室43の最奥部の壁面に衝突
させることができて、空気輸送時の慣性力を利用して貯
留室43の最奥部より順次ごみを圧縮貯留することがで
きた。このため、従来必要であったコンテナ・コンパク
タ用の油圧装置や連続排出装置用の油圧装置、貯留排出
装置用の螺旋羽根等の設備が不要となり、設備費を更に
安価にできた。また、空気輸送されるごみが袋に収容さ
れたごみである場合、本実施例の装置では空気輸送時の
慣性力を利用してごみを圧縮貯留するため、この袋の破
損が防止される。このため、一端降下したごみが舞い上
がることがなくなり、軽量ごみのフィルタ部への吸引付
着を抑えることができる。In addition, in the waste separation / storage device of this embodiment, the operating conditions were set as follows. That is, the transport pipe 6
The internal wind speed is 13 m / sec to 35 m / sec, and the dust transport speed is 5 m / in the case of heavy objects with a specific gravity of 0.15 t / m 3 or more.
It is set to 10 m / sec or more in the case of a lightweight object having a specific gravity of 0.15 t / m 3 or less (for example, paper, cloth, vinyl, etc.). This operating condition was set in advance by taking into consideration the characteristics of the dust (waste weight) generated in the area where this device is installed. Here, the reason why the lower limit value of the wind speed is set to 13 m / sec is to ensure stable pneumatic transportation even for lightweight dust. Also, the upper limit of wind speed is 35 m / sec.
The reason for doing so is to enable air transportation even in kitchen waste. The upper limit value of the wind speed of 35 m / sec is, in other words, the lower limit value for enabling the air transportation of garbage. The reason why the upper limit value of wind speed of 35 m / sec is kept low is that when the wind speed rises, the pressure loss increases with the square of the wind speed, and therefore the power (blower) must be increased. This is because the disadvantages increase as the wind speed increases. As a result, the dust that has been pneumatically transported into the storage chamber 43 is stored in the storage chamber 43 due to its gravity.
Before falling to the bottom, it can be collided with the innermost wall surface of the storage chamber 43, and the inertial force during pneumatic transportation can be used to sequentially compress and store dust from the innermost portion of the storage chamber 43. It was Therefore, the conventional equipment such as a hydraulic device for a container / compactor, a hydraulic device for a continuous discharge device, and a spiral blade for a storage / discharge device is not required, and the cost of the device can be further reduced. Further, when the dust to be transported by air is the dust contained in the bag, the apparatus of the present embodiment uses the inertial force at the time of transporting the air to compress and store the dust, so that the bag is prevented from being damaged. For this reason, the dust that has dropped once does not rise, and it is possible to suppress the suction adhesion of the lightweight dust to the filter portion.
【0042】また、本実施例のごみ分離貯留装置におい
て、高強度フィルタ41の面積は以下のように設定し
た。即ち、フィルタ部での空気通過速度が一般ごみの場
合で2m/sec 以下、袋ごみの場合で5m/sec 以下、
瓶・缶の場合で10m/sec 以下となる面積に設定し
た。これにより、ブロワ25の吸引力を上げながらフィ
ルタ部における空気通過速度を小さくすることができ
て、微細なダストのフィルタ部への吸引付着を抑えるこ
とができた。In the waste separation / storage device of this embodiment, the area of the high-strength filter 41 is set as follows. That is, the air passage speed in the filter part is 2 m / sec or less for general waste and 5 m / sec or less for bag waste,
In the case of bottles and cans, the area was set to 10 m / sec or less. As a result, the air passing speed in the filter portion can be reduced while increasing the suction force of the blower 25, and the suction and adhesion of fine dust to the filter portion can be suppressed.
【0043】上記運転条件およびフィルタ面積について
図2に基づき具体的数値を挙げて説明する。図に示す如
く、耐圧容器40は直方体の箱体からなり、高強度フィ
ルタ41はその縦寸法が2m、その横寸法が4mで、輸
送管6は400A(直径約400mm)の管を使用し、
一般ごみの収集を行う場合、輸送管6内の風速を20m
/sec とすると、風量Qは Q=0.4×0.4×π÷4×20=2.5m3 /sec フィルタ面積Aは A=4×2=8m2 従ってフィルタ部における空気通過速度Vは V=Q÷A=2.5÷8=0.3m/sec となり 0.3m/sec <2m/sec の範囲内に収まる。The above operating conditions and filter area will be described with reference to FIG. As shown in the figure, the pressure-resistant container 40 is made of a rectangular parallelepiped box, the high-strength filter 41 has a longitudinal dimension of 2 m and a lateral dimension of 4 m, and the transport pipe 6 is a pipe of 400 A (diameter of about 400 mm).
When collecting general waste, the wind speed in the transport pipe 6 should be 20m.
/ Sec, the air volume Q is Q = 0.4 × 0.4 × π ÷ 4 × 20 = 2.5 m 3 / sec The filter area A is A = 4 × 2 = 8 m 2 Therefore, the air passage velocity V in the filter section Becomes V = Q ÷ A = 2.5 ÷ 8 = 0.3m / sec, which is within the range of 0.3m / sec <2m / sec.
【0044】ところで、従来のコンテナ・コンパクタ
は、ごみをコンテナ(10m3 )内に油圧(約25ton
)で押し込み、一般ごみの場合、コンテナ内に1/
2.5に圧縮貯留している。本実施例装置はこの圧縮貯
留をブロワ25の吸引力を利用して行っている。これを
具体的数値を挙げて説明する。ブロワ25の吸引圧力
(又は貯留室と排気室との差圧)を−0.3kg/cm2
Gとすると、図2におけるフィルタ部に発生する荷重P
は P=400cm×200cm×0.3kg/cm2 =24000kg=24ton となる。即ち、フィルタの強度を大きくすることによ
り、ブロワ25の吸引力のみで貯留室43内のごみに対
し、24ton の荷重を加えて押し込むことができる。By the way, in the conventional container compactor, the dust is put into the container (10 m 3 ) under hydraulic pressure (about 25 tons).
), And in the case of general garbage, 1 / in the container
It is compressed and stored at 2.5. The apparatus of this embodiment performs this compression storage by using the suction force of the blower 25. This will be described with specific numerical values. Set the suction pressure of the blower 25 (or the differential pressure between the storage chamber and the exhaust chamber) to -0.3 kg / cm 2.
Let G be the load P generated in the filter section in FIG.
Is P = 400 cm × 200 cm × 0.3 kg / cm 2 = 24000 kg = 24 tons. That is, by increasing the strength of the filter, it is possible to apply a load of 24 tons to the dust in the storage chamber 43 and push it in only with the suction force of the blower 25.
【0045】また、本実施例のごみ分離貯留装置におい
て、輸送管6の貯留室43との接続部は、図3に示すよ
うに輸送管6の直径の2倍以上の長さL(直径400m
mの配管ならLは800mm以上に設定)を有する直管
部6Aから構成した。これにより、貯留室43内に投入
されるごみの進入速度が安定し、ごみ輸送速度の調整が
容易となった。Further, in the waste separation / storage apparatus of this embodiment, the connecting portion of the transport pipe 6 with the storage chamber 43 has a length L (diameter 400 m or more) which is more than twice the diameter of the transport pipe 6, as shown in FIG.
In the case of the m pipe, L is set to 800 mm or more) and is constituted by the straight pipe portion 6A. This stabilizes the entry speed of the dust thrown into the storage chamber 43 and facilitates the adjustment of the dust transport speed.
【0046】実施例2.図4は本発明の第2の実施例に
係るごみ分離貯留装置の要部の構成を概略的に示す断面
図であり、図中、上述の実施例1に相当する部分には同
一符号を付してある。Example 2. FIG. 4 is a cross-sectional view schematically showing the configuration of the main parts of the waste separation / storage device according to the second embodiment of the present invention. In the figure, the parts corresponding to the above-mentioned first embodiment are designated by the same reference numerals. I am doing it.
【0047】この実施例のごみ分離貯留装置は、耐圧容
器40内を高強度フィルタ41により左右2室に画成し
て、左側の室に建物のごみ投入口に連なる輸送管6を高
強度フィルタ41を貫通させて接続するとともに、右側
の室にはブロワの吸引側に連なる風管42を接続して、
左側の室を貯留室43に、右側の室を排気室44に、そ
れぞれ形成したものであり、それ以外の構成は上述の実
施例1と同様である。In the waste separation / storage device of this embodiment, the pressure resistant container 40 is divided into two chambers by a high-strength filter 41 into left and right chambers, and a transportation pipe 6 connected to the dust inlet of the building is provided in the left chamber. 41 is penetrated and connected, and a right side chamber is connected with a wind pipe 42 connected to the suction side of the blower,
The left chamber is formed in the storage chamber 43, and the right chamber is formed in the exhaust chamber 44. The other configurations are the same as those in the first embodiment.
【0048】この実施例においては、耐圧容器40の図
に直交する方向の奥行を高強度フィルタ41の必要とす
る面積を確保できる分広く設定している。これにより、
耐圧容器40の高さ寸法を圧縮することができて、収集
センター20のスぺースを高さ方向で圧縮することがで
きる。なお、この実施例においても収集センター20の
スぺースを従来に比し幅方向にも圧縮できることは言う
までもない。In this embodiment, the depth of the pressure vessel 40 in the direction orthogonal to the drawing is set wide enough to secure the area required by the high-strength filter 41. This allows
The height dimension of the pressure resistant container 40 can be compressed, and the space of the collection center 20 can be compressed in the height direction. Needless to say, also in this embodiment, the space of the collection center 20 can be compressed in the width direction as compared with the conventional case.
【0049】実施例3.図5は本発明の第3の実施例に
係るごみ分離貯留装置の要部を示す構成図であり、図
中、上述の実施例1に相当する部分には同一符号を付し
てある。Example 3. FIG. 5 is a configuration diagram showing a main part of a refuse separation and storage device according to a third embodiment of the present invention. In the figure, parts corresponding to the above-described first embodiment are designated by the same reference numerals.
【0050】この実施例のごみ分離貯留装置は、輸送管
6と風管42との間に導圧管51a,51bを介して差
圧計52を設けて、輸送管6と風管42との内部圧力の
差を検出し、検出された内部圧力の差に基づきごみ圧縮
度制御手段53がブロワ25の吸引力を制御することに
より貯留室43内に貯留されるごみの圧縮度を制御する
ようにしたものである。In the refuse separating and storing apparatus of this embodiment, a differential pressure gauge 52 is provided between the transport pipe 6 and the wind pipe 42 via pressure guiding pipes 51a and 51b, so that the internal pressure between the transport pipe 6 and the wind pipe 42 is increased. Is detected, and the dust compression degree control means 53 controls the suction force of the blower 25 based on the detected difference in internal pressure to control the compression degree of the dust stored in the storage chamber 43. It is a thing.
【0051】これを図5に基づき更に詳述すると、ごみ
圧縮度制御手段53は、本装置が設置される地域で発生
するごみの特性に合わせて所定のごみ圧縮度が得られる
ような内部圧力の差の値を事前に検出してこれを設定値
とし、この設定値と差圧計52により検出された内部圧
力の差の値とを比較してその結果を出力する比較器54
と、比較器54の比較結果に基づきごみの圧縮度を判定
し、判定結果に基づき制御量を算出してドライバ55に
出力する圧縮度判定部56とから構成されている。ドラ
イバ55は圧縮度判定部56から入力した制御量に基づ
きブロワ25の吸引力を調整する。これにより、空気輸
送時の慣性力を利用して貯留室43の最奥部より順次圧
縮貯留されるごみの圧縮度が調整される。それ以外の構
成は上述の実施例1と同様である。This will be described in more detail with reference to FIG. 5. The dust compression degree control means 53 uses an internal pressure to obtain a predetermined dust compression degree according to the characteristics of dust generated in the area where this device is installed. Of the difference between the internal pressures detected by the differential pressure gauge 52, and outputs the result.
And a compression degree determination unit 56 that determines the degree of compression of dust based on the comparison result of the comparator 54, calculates a control amount based on the determination result, and outputs the control amount to the driver 55. The driver 55 adjusts the suction force of the blower 25 based on the control amount input from the compression degree determination unit 56. As a result, the degree of compression of the dust that is sequentially compressed and stored from the innermost portion of the storage chamber 43 is adjusted by utilizing the inertial force during pneumatic transportation. The other structure is the same as that of the first embodiment.
【0052】したがって、この実施例においては、本装
置が設置される地域で発生するごみの特性に合わせてオ
ペレータが設定値(内部圧力の差の値)を入力すれば、
ごみの圧縮度が自動的に調整される。このため、ごみ圧
縮度の調整が容易となり、更に高強度フィルタ41にそ
の強度以上の差圧による荷重が加わるのを防ぐこともで
きる。Therefore, in this embodiment, if the operator inputs the set value (the value of the difference in the internal pressure) according to the characteristics of the dust generated in the area where the present apparatus is installed,
The degree of compaction of dust is automatically adjusted. Therefore, it becomes easy to adjust the degree of compression of dust, and it is also possible to prevent the high-strength filter 41 from being applied with a load due to a differential pressure higher than the strength.
【0053】実施例4.図6は本発明の第4の実施例に
係るごみ分離貯留装置の要部を示す構成図であり、図
中、上述の実施例3に相当する部分には同一符号を付し
てある。Example 4. FIG. 6 is a configuration diagram showing a main part of a refuse separation and storage device according to a fourth embodiment of the present invention. In the figure, parts corresponding to the above-mentioned third embodiment are designated by the same reference numerals.
【0054】この実施例のごみ分離貯留装置は、輸送管
6と風管42との間に導圧管51a,51bを介して差
圧計52を設けて、輸送管6と風管42との内部圧力の
差を検出し、検出された内部圧力の差の変動からごみ満
杯検出手段61が貯留室43内のごみの満杯を検出する
ようにしたものである。In the waste separation / storage device of this embodiment, a differential pressure gauge 52 is provided between the transport pipe 6 and the wind pipe 42 via pressure guiding pipes 51a and 51b, so that the internal pressure between the transport pipe 6 and the wind pipe 42 is increased. Is detected, and the dust full detection means 61 detects the full amount of dust in the storage chamber 43 from the fluctuation of the detected internal pressure difference.
【0055】これを図6に基づき更に詳述すると、ごみ
満杯検出手段61は、貯留室43内にごみが満杯になっ
た時の輸送管6と風管42との内部圧力の差の値を事前
に検出してこれを設定値とし、この設定値と差圧計52
により検出された内部圧力の差の値とを比較してその結
果を出力する比較器62と、比較器62の比較結果に基
づきごみの満杯を判定し、内部圧力の差の値が設定値と
なればドライバ55とアラーム63に対しごみが満杯と
なったことを知らせるごみ満杯判定部64とから構成さ
れている。ドライバ55はごみ満杯判定部64からごみ
が満杯となったことが知らせられるとブロワ25を停止
させる。またアラーム63はごみ満杯判定部64からご
みが満杯となったことが知らせられると警報を発し、オ
ペレータに貯留室43内にごみが満杯になったことを知
らせる。それ以外の構成は上述の実施例3と同様であ
る。This will be described in more detail with reference to FIG. 6. The dust full detection means 61 indicates the value of the difference in internal pressure between the transport pipe 6 and the wind pipe 42 when the storage chamber 43 is full of dust. It is detected in advance and used as a set value, and this set value and the differential pressure gauge 52
Is compared with the value of the difference in internal pressure detected by the comparator 62, and the result of the comparison is compared with the comparator 62 to determine whether the dust is full. In this case, it is composed of a driver 55 and a dust full determination section 64 for notifying the alarm 63 that the dust is full. The driver 55 stops the blower 25 when the dust full determination unit 64 notifies that the dust is full. Further, the alarm 63 issues an alarm when the garbage full determination unit 64 informs that the garbage is full, and informs the operator that the storage chamber 43 is full of garbage. The other configurations are the same as those in the above-described third embodiment.
【0056】したがって、この実施例においては、オペ
レータが設定値(ごみ満杯時の内部圧力の差の値)を入
力すれば、ごみの満杯が自動的に検出される。このた
め、ブロワ25が過負荷状態に至るのを防ぐことができ
る。Therefore, in this embodiment, if the operator inputs the set value (the value of the difference in the internal pressure when the dust is full), the fullness of the dust is automatically detected. Therefore, it is possible to prevent the blower 25 from being overloaded.
【0057】実施例5.図7は本発明の第5の実施例に
係るごみ分離貯留装置の要部の構成を概略的に示す断面
図であり、図中、上述の各実施例に相当する部分には同
一符号を付してある。Example 5. FIG. 7 is a cross-sectional view schematically showing the configuration of the essential parts of a waste separation and storage device according to the fifth embodiment of the present invention, in which the same reference numerals are given to the parts corresponding to the above-mentioned respective embodiments. I am doing it.
【0058】この実施例のごみ分離貯留装は、貯留室4
3における反輸送管6側の底部にごみ排出用の排出弁4
5を設けるとともに、空気輸送時の慣性力を利用して貯
留室43内に圧縮貯留したごみを排出時に排出弁45ま
で搬送するベルトコンベヤからなる排出装置71を設置
したものであるが、排出装置71としてはその他に例え
ばスクリューコンベヤやプッシャー等、他の方式のもの
も採用可能である。それ以外の構成は上述の各実施例と
同様である。The waste separating and storing apparatus of this embodiment has a storage chamber 4
3, a discharge valve 4 for discharging dust at the bottom of the side opposite to the transport pipe 6
5 is provided, and the discharging device 71 including a belt conveyor that conveys the waste compressed and stored in the storage chamber 43 to the discharging valve 45 at the time of discharging by utilizing the inertial force at the time of pneumatic transportation is installed. Besides 71, other types such as a screw conveyor and a pusher can also be adopted. The other configurations are the same as those in the above-described embodiments.
【0059】この実施例においては、空気輸送時の慣性
力を利用して貯留室43内に圧縮貯留したごみを排出時
に排出装置71によって排出弁45まで搬送できるの
で、外部へのごみの排出が容易となる。In this embodiment, since the dust compressed and stored in the storage chamber 43 can be conveyed to the discharge valve 45 by the discharge device 71 at the time of discharge by utilizing the inertial force during air transportation, the discharge of the dust to the outside can be prevented. It will be easy.
【0060】実施例6.図8は本発明の第6の実施例に
係るごみ分離貯留装置の要部の構成を概略的に示す断面
図、図9は図8のAーA線矢視断面図であり、各図中、
上述の各実施例に相当する部分には同一符号を付してあ
る。Example 6. FIG. 8 is a cross-sectional view schematically showing the configuration of the main parts of the waste separation / storage device according to the sixth embodiment of the present invention, and FIG. 9 is a cross-sectional view taken along the line AA of FIG. ,
The same reference numerals are given to the parts corresponding to the above-mentioned respective embodiments.
【0061】この実施例のごみ分離貯留装置は、耐圧容
器40が建物の一室からなり、またごみを排出するため
の排出弁としてエアタイトドア81を使用し、かつ貯留
室43内に、空気輸送されてきた軽量ごみの高強度フィ
ルタ41側への自由飛翔を規制する通気性を備えたじゃ
ま板82を設けたものである。In the refuse separating and storing apparatus of this embodiment, the pressure-resistant container 40 is formed of one room in the building, the airtight door 81 is used as a discharge valve for discharging the waste, and the air is transported into the storing chamber 43. A baffle plate 82 having air permeability is provided for restricting free flight of the existing lightweight dust toward the high-strength filter 41 side.
【0062】この実施例のごみ分離貯留装において、じ
ゃま板82は、多数の孔82aを有するパンチングメタ
ルから形成した。また、風管42の排気室44との接続
部の末端にレデューサ42aを設けた。レデューサ42
aの拡径側の周縁部は排気室44の断面形状に合わせて
矩形状に形成し、レデューサ42aが排気室44内の高
強度フィルタ41よりも下流側における空気流路の途中
に配置されるようにした。このように風管42の排気室
44との接続部の末端にレデューサ42aを設けること
の意味は、この実施例では耐圧容器40が建物の一室か
らなり容積が大きいため、配管系に対する開口比が大き
く、空気圧力損失が高くなるからであり、レデューサ4
2aを設けることによりこの空気圧力損失を低減できる
からである。それ以外の構成は上述の各実施例と同様で
ある。In the refuse separating and storing apparatus of this embodiment, the baffle plate 82 is formed of punching metal having a large number of holes 82a. Further, a reducer 42a is provided at the end of the connecting portion of the wind pipe 42 with the exhaust chamber 44. Reducer 42
The peripheral edge portion on the diameter expansion side of a is formed in a rectangular shape in accordance with the cross-sectional shape of the exhaust chamber 44, and the reducer 42a is arranged in the exhaust chamber 44 in the middle of the air flow path downstream of the high-strength filter 41. I did it. In this way, the meaning of providing the reducer 42a at the end of the connecting portion of the wind pipe 42 with the exhaust chamber 44 is that the pressure vessel 40 is a single chamber of the building and has a large volume in this embodiment. Is large and the air pressure loss is high, and the reducer 4
This is because the air pressure loss can be reduced by providing 2a. The other configurations are the same as those in the above-described embodiments.
【0063】この実施例においては、空気輸送されてき
た軽量ごみの高強度フィルタ41側への自由飛翔をじゃ
ま板82により規制できるので、フィルタ部への紙片や
微細なダスト等の軽量ごみの吸引付着を確実に抑えるこ
とができる。In this embodiment, since the baffle plate 82 can restrict the free flight of the airborne lightweight dust toward the high-strength filter 41 side, the suction of the lightweight dust such as paper chips and fine dust to the filter portion. Adhesion can be reliably suppressed.
【0064】実施例7.図10は本発明の第7の実施例
に係るごみ分離貯留装置の要部の構成を概略的に示す断
面図、図11は図10のBーB線矢視断面図であり、各
図中、上述の実施例6に相当する部分には同一符号を付
してある。Example 7. FIG. 10 is a cross-sectional view schematically showing the configuration of the main parts of the waste separation / storage device according to the seventh embodiment of the present invention, and FIG. 11 is a cross-sectional view taken along the line BB of FIG. The same reference numerals are given to the portions corresponding to the above-mentioned sixth embodiment.
【0065】この実施例のごみ分離貯留装置は、上述の
実施例6のものに更に脱臭フィルタ91を付加したもの
である。The waste separation / storage device of this embodiment is the same as that of the above-mentioned sixth embodiment with a deodorizing filter 91 added.
【0066】これを図10及び図11に基づき更に詳述
すると、脱臭フィルタ91は排気室44内の高強度フィ
ルタ41よりも下流側における空気流路の途中に位置を
異ならせて直列に2つ配置されており、高強度フィルタ
41を通過した空気はこれら脱臭フィルタ91a,91
bにより2段階に脱臭されてから、レデューサ42aよ
り風管42内に吸引されるようになっている。それ以外
の構成は上述の実施例6と同様である。This will be described in further detail with reference to FIGS. 10 and 11. Two deodorizing filters 91 are arranged in series at different positions in the air passage downstream of the high-strength filter 41 in the exhaust chamber 44. The air that has been placed and that has passed through the high-strength filter 41 is used as the deodorizing filters 91a, 91
After being deodorized in two stages by b, it is sucked into the wind pipe 42 from the reducer 42a. The other structure is the same as that of the sixth embodiment.
【0067】この実施例においては、排気室44内に脱
臭フィルタ91を設置しているので、排気室44すなわ
ち耐圧容器40に脱臭装置の容器を兼用させることがで
きて、脱臭フィルタ91をブロワの吸引側に配置するこ
とができるので、従来必要としていた脱臭装置の容器と
冷却器を不要のものとすることができ、その分、収集セ
ンターのスぺースを更に圧縮することができる。In this embodiment, since the deodorizing filter 91 is installed in the exhaust chamber 44, the exhaust chamber 44, that is, the pressure resistant container 40 can be used also as the container of the deodorizing device, and the deodorizing filter 91 can be used as a blower. Since it can be arranged on the suction side, the container and the cooler of the deodorizing device which are conventionally required can be eliminated, and the space of the collecting center can be further compressed by that much.
【0068】実施例8.図12は本発明の第8の実施例
に係るごみ分離貯留装置の要部の構成を概略的に示す断
面図、図13はその動作を説明するための説明図であ
り、各図中、上述の各実施例に相当する部分には同一符
号を付してある。Example 8. FIG. 12 is a cross-sectional view schematically showing the configuration of the main parts of the waste separation / storage device according to the eighth embodiment of the present invention, and FIG. 13 is an explanatory view for explaining the operation thereof, and in each of the drawings, the above description is given. The same reference numerals are given to the portions corresponding to the respective embodiments.
【0069】この実施例のごみ分離貯留装置は、耐圧容
器40の排気室44頂壁を形成する部位に、高強度フィ
ルタ41洗浄用の外気導入弁101を設置するととも
に、その外側に、外気導入時の排気室44内に引き込ま
れる外気による弁配管部の振動により引き起こされる騒
音やブロワ側から伝わってくる騒音を低減させるための
消音器102を設けたものである。それ以外の構成は上
述の各実施例と同様である。In the refuse separating and storing apparatus of this embodiment, the outside air introducing valve 101 for cleaning the high-strength filter 41 is installed at a portion forming the top wall of the exhaust chamber 44 of the pressure resistant container 40, and outside air is introduced to the outside thereof. The silencer 102 is provided to reduce noise caused by vibration of the valve pipe portion due to the outside air drawn into the exhaust chamber 44 and noise transmitted from the blower side. The other configurations are the same as those in the above-described embodiments.
【0070】この実施例において、外気導入弁101を
開くと、排気室44内に外気が導入され、排気室44の
内圧が貯留室43の内圧よりも高くなり、図13に矢印
で示すように排気室44から高強度フィルタ41を通過
して貯留室43へ空気の流れが発生する。このような空
気の流れは、ブロワの運転を止めなくても、外気導入弁
101を開くことにより発生する。そして、このような
定常運転時とは逆方向の空気の流れにより、高強度フィ
ルタ41の貯留室43側の下面に付着している微細なダ
スト等が吹き飛ばされて除去され、高強度フィルタ41
が洗浄される。In this embodiment, when the outside air introduction valve 101 is opened, outside air is introduced into the exhaust chamber 44, the internal pressure of the exhaust chamber 44 becomes higher than the internal pressure of the storage chamber 43, and as shown by the arrow in FIG. Air flows from the exhaust chamber 44 through the high-strength filter 41 to the storage chamber 43. Such an air flow is generated by opening the outside air introduction valve 101 without stopping the operation of the blower. Then, due to the air flow in the direction opposite to that in the steady operation, fine dust and the like adhering to the lower surface of the high-strength filter 41 on the storage chamber 43 side is blown away and removed, and the high-strength filter 41 is removed.
Are washed.
【0071】実施例9.図14は本発明の第9の実施例
に係るごみ分離貯留装置の要部の構成を概略的に示す断
面図であり、図中、上述の実施例8に相当する部分には
同一符号を付してある。Example 9. FIG. 14 is a cross-sectional view schematically showing the structure of the essential parts of a waste separation and storage device according to a ninth embodiment of the present invention, in which the portions corresponding to the above-mentioned eighth embodiment are designated by the same reference numerals. I am doing it.
【0072】この実施例のごみ分離貯留装置は、上述の
実施例8で示した外気導入弁101と消音器102の組
付体を、耐圧容器40の排気室44頂壁を形成する部位
に位置を異ならせて複数組(この実施例では2組)設置
したものである。それ以外の構成は上述の実施例8と同
様である。In the refuse separating and storing apparatus of this embodiment, the assembly of the outside air introducing valve 101 and the silencer 102 shown in the above-mentioned Embodiment 8 is located at a portion forming the top wall of the exhaust chamber 44 of the pressure resistant container 40. A plurality of sets (two sets in this embodiment) are installed with different numbers. The other configurations are the same as those in the above-described eighth embodiment.
【0073】この実施例においては、排気室44内に複
数個所より外気を導入することができるため、高強度フ
ィルタ41の洗浄をムラなく行うことができる。In this embodiment, since the outside air can be introduced into the exhaust chamber 44 from a plurality of places, the high-strength filter 41 can be uniformly washed.
【0074】実施例10.図15は本発明の第10の実
施例に係るごみ分離貯留装置の要部の構成を概略的に示
す断面図、図16は図15のCーC線矢視断面図であ
り、各図中、上述の実施例8及び実施例9に相当する部
分には同一符号を付してある。Example 10. FIG. 15 is a cross-sectional view schematically showing the configuration of the main parts of the waste separation / storage device according to the tenth embodiment of the present invention, and FIG. 16 is a cross-sectional view taken along the line CC of FIG. The portions corresponding to those in the above-described eighth and ninth embodiments are designated by the same reference numerals.
【0075】この実施例のごみ分離貯留装置は、排気室
44内の上部に高強度フィルタ41と平行な複数本(こ
の実施例では3本)のブローチューブ111,112,
113を並設するとともに、各ブローチューブ111,
112,113の各一端側を排気室44の側壁を貫通さ
せて開口させ、かつ各ブローチューブ111,112,
113の排気室44からの突出部の途中にはそれぞれ外
気導入弁114,115,116を設置し、一方のブロ
ーチューブ111側の外気導入弁114から他方のブロ
ーチューブ113側の外気導入弁116にかけて順次時
間をずらせて間歇的に開閉させることにより、排気室4
4内に外気を導入できるようにしている。また、各ブロ
ーチューブ111,112,113の高強度フィルタ4
1と対向する側の面には、それぞれ軸方向に位置をずら
せて複数の空気吹出口(図示せず)が設けられ、更に各
ブローチューブ111,112,113と高強度フィル
タ41との間の空間部には、各空気吹出口に対応させて
複数のベンチュリ117が配置されている。それ以外の
構成は上述の実施例8及び実施例9と同様である。The waste separation / storage device of this embodiment has a plurality (three in this embodiment) of blow tubes 111, 112 parallel to the high-strength filter 41 in the upper portion of the exhaust chamber 44.
113 are installed side by side, and each blow tube 111,
One end side of each of the blow tubes 111, 112, 112, 113 is opened by penetrating the side wall of the exhaust chamber 44.
Outside air introduction valves 114, 115, and 116 are installed in the middle of the protruding portion of the exhaust chamber 44 of 113, and the outside air introduction valve 114 on the side of one blow tube 111 to the outside air introduction valve 116 on the side of the other blow tube 113 is installed. The exhaust chamber 4 can be opened and closed intermittently by shifting the time.
The outside air can be introduced into the inside. In addition, the high-strength filter 4 of each blow tube 111, 112, 113
A plurality of air outlets (not shown) are provided on the surface on the side opposite to 1 in positions axially displaced from each other, and further between the blow tubes 111, 112, 113 and the high-strength filter 41. A plurality of venturis 117 are arranged in the space corresponding to the air outlets. Other configurations are the same as those in the above-described eighth and ninth embodiments.
【0076】この実施例においては、排気室44内に外
気を導入するための空気吹出口を多数設けることができ
るため、高強度フィルタ41の洗浄をよりムラなく行う
ことができる。また、各空気吹出口に対応させてベンチ
ュリ117を設けているので、外気導入時に排気室44
内に存在する低圧空気をも引き込ませて利用することが
でき、これによって排気室44内に導入する外気の量を
少なくすることができる。In this embodiment, since a large number of air outlets for introducing outside air can be provided in the exhaust chamber 44, the high-strength filter 41 can be cleaned more evenly. Further, since the venturi 117 is provided so as to correspond to each air outlet, the exhaust chamber 44 is introduced when the outside air is introduced.
The low-pressure air existing therein can also be drawn in and used, whereby the amount of outside air introduced into the exhaust chamber 44 can be reduced.
【0077】実施例11.図17は本発明の第11の実
施例に係るごみ分離貯留装置の要部の構成を概略的に示
す断面図、図18は図17のDーD線矢視断面図であ
り、各図中、上述の実施例10に相当する部分には同一
符号を付してある。Example 11. FIG. 17 is a cross-sectional view schematically showing the configuration of the main parts of the waste separation / storage device according to the eleventh embodiment of the present invention, and FIG. 18 is a cross-sectional view taken along the line DD in FIG. The same reference numerals are given to the portions corresponding to those in the tenth embodiment.
【0078】この実施例のごみ分離貯留装置は、上述の
実施例10のものの各ブローチューブ111,112,
113の排気室44からの突出部の各末端をヘッダ12
1を介してコンプレッサ122の吐出側に接続したもの
である。それ以外の構成は上述の実施例10と同様であ
る。The waste separating and storing device of this embodiment is the blow tubes 111, 112 of the above-mentioned tenth embodiment.
Each end of the protruding portion 113 of the exhaust chamber 44 is attached to the header 12
It is connected to the discharge side of the compressor 122 through 1. The other structure is the same as that of the tenth embodiment.
【0079】この実施例においては、各ブローチューブ
111,112,113にコンプレッサ122からの圧
縮空気を供給するようにしているので、ブロワの停止中
(ごみ空気輸送プラントの停止中)でも高強度フィルタ
41の洗浄を行うことができる。また、このようにブロ
ワの停止中に高強度フィルタ41の洗浄を行う場合に
は、各外気導入弁114,115,116を同時に開閉
させてもよい。In this embodiment, since the compressed air from the compressor 122 is supplied to each of the blow tubes 111, 112, 113, the high-strength filter is provided even when the blower is stopped (the refuse air transportation plant is stopped). 41 can be washed. Further, when the high-strength filter 41 is washed while the blower is stopped in this way, the outside air introduction valves 114, 115, 116 may be opened and closed at the same time.
【0080】実施例12.図19は本発明の第12の実
施例に係るごみ分離貯留装置の要部の構成を概略的に示
す断面図であり、図中、上述の実施例8に相当する部分
には同一符号を付してある。Example 12 FIG. 19 is a cross-sectional view schematically showing the configuration of the main parts of the waste separation / storage device according to the twelfth embodiment of the present invention. In the figure, parts corresponding to the above-mentioned eighth embodiment are designated by the same reference numerals. I am doing it.
【0081】この実施例のごみ分離貯留装置は、排気室
44内を脱臭フィルタ131により上下2室に画成し
て、上方の室、つまり脱臭フィルタ131よりも下流側
の室に風管42を接続するとともに、上述の実施例8で
示した外気導入弁101および消音器102を取付ける
ための配管132を排気室44内に延出させ、かつその
延出端を脱臭フィルタ131を貫通させて、排気室44
内における脱臭フィルタ131よりも上流側の室内に開
口させ、脱臭フィルタ131と高強度フィルタ41との
間の空間部に外気を導入できるようにしたものである。
それ以外の構成は上述の実施例8と同様である。In the refuse separating and storing apparatus of this embodiment, the inside of the exhaust chamber 44 is divided into upper and lower chambers by the deodorizing filter 131, and the air pipe 42 is provided in the upper chamber, that is, the chamber downstream of the deodorizing filter 131. Along with the connection, the pipe 132 for attaching the outside air introduction valve 101 and the silencer 102 shown in the above-described Embodiment 8 is extended into the exhaust chamber 44, and the extended end thereof is passed through the deodorizing filter 131, Exhaust chamber 44
The inside of the interior is opened upstream of the deodorizing filter 131 so that the outside air can be introduced into the space between the deodorizing filter 131 and the high-strength filter 41.
The other configurations are the same as those in the above-described eighth embodiment.
【0082】この実施例においては、脱臭フィルタ13
1がブロワ側に流れる導入外気の抵抗となるため、高強
度フィルタ41の洗浄効果が高まる。In this embodiment, the deodorizing filter 13
Since 1 becomes the resistance of the introduced outside air flowing to the blower side, the cleaning effect of the high-strength filter 41 is enhanced.
【0083】実施例13.図20は本発明の第13の実
施例に係るごみ分離貯留装置の要部の構成を概略的に示
す断面図、図21はその動作を説明するための説明図で
あり、各図中、上述の実施例8に相当する部分には同一
符号を付してある。Example 13 FIG. 20 is a cross-sectional view schematically showing the configuration of the main part of the waste separation / storage device according to the thirteenth embodiment of the present invention, and FIG. 21 is an explanatory view for explaining the operation thereof, and in each of the drawings, the above description is given. The same reference numerals are attached to the portions corresponding to the eighth embodiment.
【0084】この実施例のごみ分離貯留装置は、輸送管
6の貯留室43接続部の近傍に遮断弁141を設けると
ともに、風管42の排気室44接続部の近傍に、ブロワ
への流路を排気室44と外気との間で切り換える切換弁
142を設け、遮断弁141と切換弁142とによって
貯留室43と排気室44とを真空状態のまま配管系から
遮断できるようにし、この状態で外気導入弁101を開
くことにより排気室44内に外気を導入して、排気室4
4から貯留室43側への空気の流れを発生させるように
したものである。それ以外の構成は上述の実施例8と同
様である。In the refuse separating and storing apparatus of this embodiment, the shutoff valve 141 is provided in the vicinity of the connecting portion of the storage chamber 43 of the transport pipe 6, and the flow path to the blower is provided in the vicinity of the connecting portion of the exhaust chamber 44 of the wind pipe 42. Is provided between the exhaust chamber 44 and the outside air, and the shutoff valve 141 and the switching valve 142 allow the storage chamber 43 and the exhaust chamber 44 to be shut off from the piping system in a vacuum state. The outside air is introduced into the exhaust chamber 44 by opening the outside air introduction valve 101, and the exhaust chamber 4
The flow of air from No. 4 to the storage chamber 43 side is generated. The other configurations are the same as those in the above-described eighth embodiment.
【0085】これを図20及び図21に基づき更に詳述
すると、高強度フィルタ41の洗浄に当たっては、まず
ブロワの運転中に輸送管6側の遮断弁141を閉じ、こ
の状態で所定時間、耐圧容器40内の真空引きを行わせ
て、貯留室43と排気室44の内部を真空状態にする。
貯留室43と排気室44の内部が真空状態になると、排
気室44側の切換弁142を外気側に切換えて、ブロワ
に外気が直接導入されるようにして、ブロワの負荷を軽
減する。次いで、外気導入弁101を開き、排気室44
内に外気を導入し、排気室44から貯留室43側への空
気の流れを発生させ、高強度フィルタ41を洗浄する。This will be described in more detail with reference to FIGS. 20 and 21. In cleaning the high-strength filter 41, first, the shutoff valve 141 on the side of the transport pipe 6 is closed during operation of the blower, and in this state, the pressure resistance is maintained for a predetermined time. The container 40 is evacuated, and the inside of the storage chamber 43 and the exhaust chamber 44 is evacuated.
When the insides of the storage chamber 43 and the exhaust chamber 44 are in a vacuum state, the switching valve 142 on the exhaust chamber 44 side is switched to the outside air side so that the outside air is directly introduced into the blower, thereby reducing the load on the blower. Next, the outside air introduction valve 101 is opened, and the exhaust chamber 44
The outside air is introduced into the inside, and a flow of air from the exhaust chamber 44 to the storage chamber 43 side is generated to clean the high-strength filter 41.
【0086】このように、この実施例のごみ分離貯留装
置は、ブロワの運転を止めることなく、貯留室43と排
気室44とを真空状態のまま配管系から遮断できるの
で、外気導入弁101より排気室44内に導入された外
気を真空力によって貯留室43側へ勢いよく流すことが
できる。このため、高強度フィルタ41部を排気室44
から貯留室43へ流れる空気の速度を速くすることがで
き、高強度フィルタ41の洗浄効果を更に高めることが
できる。As described above, in the waste separation / storage device of this embodiment, the storage chamber 43 and the exhaust chamber 44 can be shut off from the piping system in a vacuum state without stopping the operation of the blower. The outside air introduced into the exhaust chamber 44 can be vigorously flown to the storage chamber 43 side by the vacuum force. For this reason, the high-strength filter 41 is connected to the exhaust chamber 44.
The velocity of the air flowing from the storage chamber 43 to the storage chamber 43 can be increased, and the cleaning effect of the high-strength filter 41 can be further enhanced.
【0087】実施例14.図22は本発明の第14の実
施例に係るごみ分離貯留装置を説明するためのごみ空気
輸送プラントの系統図であり、図中、上述の実施例1に
相当する部分には同一符号を付してある。Example 14 FIG. 22 is a system diagram of a waste pneumatic transportation plant for explaining a waste separation / storage device according to a fourteenth embodiment of the present invention. In the figure, parts corresponding to the above-mentioned first embodiment are designated by the same reference numerals. I am doing it.
【0088】この実施例のごみ分離貯留装置は、輸送管
6と風管42とをカップリング151,152により耐
圧容器40に接続するようにして、耐圧容器40を配管
系から分離可能に構成したものである。In the refuse separating and storing apparatus of this embodiment, the pressure vessel 40 is separable from the piping system by connecting the transport pipe 6 and the wind pipe 42 to the pressure vessel 40 by the couplings 151 and 152. It is a thing.
【0089】この実施例においては、耐圧容器40を配
管系から分離できるため、耐圧容器40にコンテナ機能
を持たせることができ、そのまま車両34にて搬出する
ことができる。In this embodiment, since the pressure-resistant container 40 can be separated from the piping system, the pressure-resistant container 40 can have a container function and can be carried out by the vehicle 34 as it is.
【0090】なお、上述の各実施例においては、いずれ
も貯留室43に設けられるごみ排出用の排出弁45を開
いた状態に図示して説明したが、これは各実施例の構成
の理解を容易にするためであり、ごみ空気輸送プラント
の運転中は閉じていることは言うまでもない。また、上
述の各実施例の要部を単一の装置内に組み込んで構成で
きることも言うまでもない。In each of the above-mentioned embodiments, the discharge valve 45 for discharging dust provided in the storage chamber 43 is shown in the open state, but this is for understanding the structure of each embodiment. Needless to say, it is closed for the purpose of facilitating the operation of the waste pneumatic transportation plant. Further, it goes without saying that the essential parts of each of the above-described embodiments can be incorporated in a single device.
【0091】[0091]
【発明の効果】以上述べたように、本発明によれば、耐
圧容器内を高強度フィルタにより2室に画成して、一方
に建物のごみ投入口に連なる輸送管を、他方にブロワの
吸引側に連なる風管を、それぞれ接続して、輸送管側の
室を貯留室に、ブロワ側の室を排気室に、それぞれ形成
し、かつ貯留室にはごみ排出用の排出弁を設け、輸送管
側の貯留室内にてごみやダストを全て空気から分離さ
せ、貯留させるようにしたので、耐圧容器部で、ごみの
分離、ダストの捕集、分離・捕集されたごみやダストの
貯留、排出を全て行うことができ、従来の分離機、エリ
ミネータ、バグフィルタ、排出装置等の統合、共有化を
図ることができる。このため、分離機のエリミネータ駆
動用の電動機やバグフィルタの回転掻き羽根駆動用の電
動機等の設備が不要となり、設備費を安価にできるとと
もに、収集センターのスぺースを圧縮することができ
る。As described above, according to the present invention, the inside of the pressure resistant container is defined by the high-strength filter into two chambers, and the transport pipe connected to the dust inlet of the building is provided on one side and the blower of the blower on the other side. The air pipes connected to the suction side are respectively connected, the chamber on the transport pipe side is formed as a storage chamber, the chamber on the blower side is formed as an exhaust chamber, and a discharge valve for discharging dust is provided in the storage chamber. All the dust and dust are separated from the air and stored in the storage chamber on the side of the transport pipe, so the pressure-resistant container section separates dust, collects dust, and stores the collected dust and dust. It is possible to discharge all, and it is possible to integrate and share the conventional separator, eliminator, bag filter, discharge device, and the like. Therefore, equipment such as an electric motor for driving the eliminator of the separator and an electric motor for driving the rotary scraping blade of the bag filter are not required, and the equipment cost can be reduced and the space of the collection center can be compressed.
【0092】また、本発明によれば、本装置が設置され
る地域のごみの特性に合わせて、輸送管内の風速を13
m/sec 〜35m/sec 、ごみ輸送速度を、比重0.1
5t/m3 以上の重量物の場合で5m/sec 以上、比重
0.15t/m3 以下の軽量物の場合で10m/sec 以
上に設定するようにしたので、貯留室内に空気輸送され
てきたごみがその重力により貯留室底面まで降下する前
に貯留室の最奥部の壁面に衝突させることができ、空気
輸送時の慣性力を利用して貯留室の最奥部より順次ごみ
を圧縮貯留することができる。このため、コンテナ・コ
ンパクタ用の油圧装置や連続排出装置用の油圧装置、貯
留排出装置用の螺旋羽根等の設備が不要となり、設備費
を更に安価にすることができる。Further, according to the present invention, the wind speed in the transportation pipe can be set to 13 depending on the characteristics of the refuse in the area where the present apparatus is installed.
m / sec-35m / sec, refuse transportation speed, specific gravity 0.1
Since it is set to 5 m / sec or more for a heavy object of 5 t / m 3 or more and 10 m / sec or more for a lightweight object of a specific gravity of 0.15 t / m 3 or less, it has been pneumatically transported into the storage chamber. Before the dust falls to the bottom of the storage chamber due to its gravity, it can collide with the innermost wall surface of the storage chamber, and the inertial force during pneumatic transportation is used to compress and store the waste sequentially from the innermost part of the storage chamber. can do. Therefore, equipment such as a hydraulic device for a container / compactor, a hydraulic device for a continuous discharge device, and a spiral blade for a storage discharge device is not required, and the cost of the device can be further reduced.
【0093】また、本発明によれば、高強度フィルタの
面積を、高強度フィルタ部での空気通過速度が一般ごみ
の場合で2m/sec 以下、袋ごみの場合で5m/sec 以
下、瓶・缶の場合で10m/sec 以下となる面積に設定
するようにしたので、ブロワの吸引力を上げながらフィ
ルタ部における空気通過速度を小さくすることができ、
微細なダストのフィルタ部への吸引付着を抑えることが
できる。According to the present invention, the area of the high-strength filter is 2 m / sec or less when the air passing speed in the high-strength filter portion is general waste, 5 m / sec or less when bag waste, and In the case of a can, the area is set to 10 m / sec or less, so the air passing speed in the filter can be reduced while increasing the suction force of the blower.
It is possible to suppress suction and adhesion of fine dust to the filter section.
【0094】また、本発明によれば、輸送管の貯留室と
の接続部に、輸送管直径の2倍以上の直管部を設けたの
で、貯留室に投入されるごみの進入速度を安定させるこ
とができ、ごみ輸送速度の調整を容易にすることができ
る。Further, according to the present invention, since the straight pipe portion having a diameter equal to or more than twice the diameter of the transport pipe is provided at the connecting portion of the transport pipe with the storage chamber, the intrusion speed of the dust thrown into the storage chamber is stabilized. It is possible to facilitate the adjustment of the waste transportation speed.
【0095】また、本発明によれば、輸送管と風管との
内部圧力の差を調整して貯留室内に貯留されるごみの圧
縮度を制御するごみ圧縮度制御手段を設けたので、本装
置が設置される地域のごみの特性に合わせた輸送速度や
圧縮度の調整が容易となり、ごみの輸送速度や圧縮度の
調整の自動化が可能となる。Further, according to the present invention, the dust compression degree control means for controlling the compression degree of the dust stored in the storage chamber by adjusting the difference in internal pressure between the transport pipe and the wind pipe is provided. It becomes easy to adjust the transportation speed and compression degree according to the characteristics of the waste in the area where the device is installed, and it becomes possible to automate the adjustment of the transportation speed and compression degree of the waste.
【0096】また、本発明によれば、輸送管と風管との
内部圧力の差の変動をみて貯留室内のごみの満杯を検出
するごみ満杯検出手段を設けたので、ごみの満杯を自動
的に検出させることができ、これによりブロワが過負荷
状態に至るのを防ぐことができる。Further, according to the present invention, since the dust full detection means for detecting the fullness of dust in the storage chamber by observing the fluctuation of the internal pressure difference between the transportation pipe and the wind pipe is provided, the fullness of dust is automatically detected. It is possible to prevent the blower from being overloaded.
【0097】また、本発明によれば、貯留室内の底部
に、貯留室内に貯留したごみの排出装置を設置したの
で、空気輸送によって貯留室内に圧縮貯留されたごみを
排出時に排出弁まで搬送でき、外部へのごみの排出を容
易に行うことができる。Further, according to the present invention, since the device for discharging the dust stored in the storage chamber is installed at the bottom of the storage chamber, the dust compressed and stored in the storage chamber by pneumatic transportation can be conveyed to the discharge valve at the time of discharge. , It is possible to easily discharge the dust to the outside.
【0098】また、本発明によれば、貯留室内に、空気
輸送されてきた軽量ごみの高強度フィルタ側への自由飛
翔を規制する通気性を備えたじゃま板を設けたので、紙
片や微細なダストの高強度フィルタ側への自由飛翔を規
制でき、フィルタ部への紙片や微細なダストの吸引付着
を確実に抑えることができる。Further, according to the present invention, since the baffle plate having the air permeability for restricting the free flight of the air-transported lightweight dust to the high-strength filter side is provided in the storage chamber, a piece of paper or fine particles is provided. It is possible to restrict free flight of dust to the high-strength filter side, and reliably suppress suction and adhesion of paper pieces and fine dust to the filter section.
【0099】また、本発明によれば、排気室内の空気流
通経路の途中に脱臭フィルタを設置したので、排気室す
なわち耐圧容器に脱臭装置の容器を兼用させて脱臭フィ
ルタをブロワの吸引側に配置することができ、従来必要
としていた脱臭装置の容器と冷却器を不要のものとする
ことができる。Further, according to the present invention, since the deodorizing filter is installed in the middle of the air circulation path in the exhaust chamber, the deodorizing filter is arranged on the suction side of the blower by using the exhaust chamber, that is, the pressure resistant container as the container of the deodorizing device. Therefore, the container and the cooler of the deodorizing device which have been conventionally required can be eliminated.
【0100】また、本発明によれば、排気室に高強度フ
ィルタ洗浄用の外気導入弁を設けたので、排気室内に外
気を導入することが可能となって、ブロワの運転を止め
なくても、排気室の内圧を貯留室の内圧よりも高くする
ことができる。このため、高強度フィルタ部に、排気室
から貯留室への空気の流れ(定常運転時とは逆の流れ)
を発生させることができ、これにより高強度フィルタに
付着している微細なダスト等を吹き飛ばし除去すること
ができ、高強度フィルタを洗浄することができる。Further, according to the present invention, since the exhaust chamber is provided with the external air introduction valve for cleaning the high-strength filter, the external air can be introduced into the exhaust chamber without stopping the operation of the blower. The internal pressure of the exhaust chamber can be made higher than the internal pressure of the storage chamber. Therefore, the flow of air from the exhaust chamber to the storage chamber in the high-strength filter section (the flow opposite to that during steady operation)
It is possible to generate fine particles and the like, whereby fine dust and the like adhering to the high-strength filter can be blown off and removed, and the high-strength filter can be washed.
【0101】また、本発明によれば、輸送管の貯留室接
続部の近傍に遮断弁を設けるとともに、風管の排気室接
続部の近傍に、ブロワへの流路を排気室と外気との間で
切り換える切換弁を設けたので、ブロワの運転を止める
ことなく、貯留室と排気室とを真空状態のまま配管系か
ら遮断することができ、この状態で外気導入弁によって
排気室内に外気を導入することにより、高強度フィルタ
部を排気室から貯留室へ流れる空気の速度を速くするこ
とができる。このため、高強度フィルタの洗浄効果を高
めることができる。Further, according to the present invention, the shutoff valve is provided in the vicinity of the storage chamber connecting portion of the transport pipe, and the flow passage to the blower is provided in the vicinity of the exhaust chamber connecting portion of the wind pipe to connect the exhaust chamber and the outside air. Since the switching valve that switches between the two is provided, the storage chamber and the exhaust chamber can be shut off from the piping system in a vacuum state without stopping the operation of the blower.In this state, the outside air is introduced into the exhaust chamber by the outside air introduction valve. By introducing the high-strength filter portion, the velocity of the air flowing from the exhaust chamber to the storage chamber can be increased. Therefore, the cleaning effect of the high-strength filter can be enhanced.
【0102】また、本発明によれば、耐圧容器を輸送管
および風管から分離可能に構成したので、耐圧容器にコ
ンテナ機能を持たせることができ、そのまま車両にて搬
出することができる。Further, according to the present invention, since the pressure-resistant container is constructed so as to be separable from the transport pipe and the wind pipe, the pressure-resistant container can have a container function and can be carried out by the vehicle as it is.
【図1】本発明の第1の実施例に係るごみ分離貯留装置
を説明するためのごみ空気輸送プラントの系統図であ
る。FIG. 1 is a system diagram of a waste pneumatic transportation plant for explaining a waste separation / storage device according to a first embodiment of the present invention.
【図2】第1の実施例に係るごみ分離貯留装置の運転条
件を説明するための要部拡大斜視図である。FIG. 2 is an enlarged perspective view of essential parts for explaining operating conditions of the waste separation and storage device according to the first embodiment.
【図3】第1の実施例に係るごみ分離貯留装置の配管系
の説明図である。FIG. 3 is an explanatory diagram of a piping system of the waste separation storage device according to the first embodiment.
【図4】本発明の第2の実施例に係るごみ分離貯留装置
の要部の構成を概略的に示す断面図である。FIG. 4 is a cross-sectional view schematically showing a configuration of a main part of a refuse separation and storage device according to a second embodiment of the present invention.
【図5】本発明の第3の実施例に係るごみ分離貯留装置
の要部を示す構成図である。FIG. 5 is a configuration diagram showing a main part of a refuse separation and storage device according to a third embodiment of the present invention.
【図6】本発明の第4の実施例に係るごみ分離貯留装置
の要部を示す構成図である。FIG. 6 is a configuration diagram showing a main part of a refuse separation and storage device according to a fourth embodiment of the present invention.
【図7】本発明の第5の実施例に係るごみ分離貯留装置
の要部の構成を概略的に示す断面図である。FIG. 7 is a sectional view schematically showing a configuration of a main part of a refuse separation and storage device according to a fifth embodiment of the present invention.
【図8】本発明の第6の実施例に係るごみ分離貯留装置
の要部の構成を概略的に示す断面図である。FIG. 8 is a sectional view schematically showing a configuration of a main part of a refuse separation and storage device according to a sixth embodiment of the present invention.
【図9】図8のAーA線矢視断面図である。9 is a sectional view taken along the line AA of FIG.
【図10】本発明の第7の実施例に係るごみ分離貯留装
置の要部の構成を概略的に示す断面図である。FIG. 10 is a sectional view schematically showing a configuration of a main part of a refuse separation and storage device according to a seventh embodiment of the present invention.
【図11】図10のBーB線矢視断面図である。11 is a sectional view taken along the line BB of FIG.
【図12】本発明の第8の実施例に係るごみ分離貯留装
置の要部の構成を概略的に示す断面図である。FIG. 12 is a sectional view schematically showing a configuration of a main part of a refuse separation and storage device according to an eighth embodiment of the present invention.
【図13】第8の実施例に係るごみ分離貯留装置の動作
を説明するための説明図である。FIG. 13 is an explanatory diagram for explaining the operation of the waste separation and storage device according to the eighth embodiment.
【図14】本発明の第9の実施例に係るごみ分離貯留装
置の要部の構成を概略的に示す断面図である。FIG. 14 is a sectional view schematically showing a configuration of a main part of a refuse separation and storage device according to a ninth embodiment of the present invention.
【図15】本発明の第10の実施例に係るごみ分離貯留
装置の要部の構成を概略的に示す断面図である。FIG. 15 is a sectional view schematically showing a configuration of a main part of a refuse separation and storage device according to a tenth embodiment of the present invention.
【図16】図15のCーC線矢視断面図である。16 is a sectional view taken along the line CC of FIG.
【図17】本発明の第11の実施例に係るごみ分離貯留
装置の要部の構成を概略的に示す断面図である。FIG. 17 is a sectional view schematically showing a configuration of a main part of a refuse separation and storage device according to an eleventh embodiment of the present invention.
【図18】図17のDーD線矢視断面図である。18 is a sectional view taken along the line DD of FIG.
【図19】本発明の第12の実施例に係るごみ分離貯留
装置の要部の構成を概略的に示す断面図である。FIG. 19 is a cross sectional view schematically showing a configuration of a main part of a refuse separation and storage device according to a twelfth embodiment of the present invention.
【図20】本発明の第13の実施例に係るごみ分離貯留
装置の要部の構成を概略的に示す断面図である。FIG. 20 is a cross sectional view schematically showing a configuration of a main part of a refuse separation and storage device according to a thirteenth embodiment of the present invention.
【図21】第13の実施例に係るごみ分離貯留装置の動
作を説明するための説明図である。FIG. 21 is an explanatory diagram for explaining the operation of the waste separation and storage device according to the thirteenth embodiment.
【図22】本発明の第14の実施例に係るごみ分離貯留
装置を説明するためのごみ空気輸送プラントの系統図で
ある。FIG. 22 is a system diagram of a waste pneumatic transportation plant for explaining a waste separation / storage device according to a fourteenth embodiment of the present invention.
【図23】従来のごみ分離貯留装置を説明するためのご
み空気輸送プラントの系統図である。FIG. 23 is a system diagram of a waste pneumatic transportation plant for explaining a conventional waste separation / storage device.
【図24】従来のごみ分離貯留装置の要部を拡大して示
す説明図である。FIG. 24 is an explanatory diagram showing an enlarged main part of a conventional refuse separation and storage device.
2 ごみ投入口 6 輸送管 6A 直管部 25 ブロワ 40 耐圧容器 41 高強度フィルタ 42 風管 43 貯留室 44 排気室 45 排出弁 52 差圧計 53 ごみ圧縮度制御手段 61 ごみ満杯検出手段 71 排出装置 82 じゃま板 82a 孔 91,131 脱臭フィルタ 101,114,115,116 外気導入弁 141 遮断弁 142 切換弁 151,152 カップリング 2 Waste input port 6 Transport pipe 6A Straight pipe part 25 Blower 40 Pressure resistant container 41 High-strength filter 42 Wind pipe 43 Storage chamber 44 Exhaust chamber 45 Discharge valve 52 Differential pressure gauge 53 Waste compaction control means 61 Waste fullness detection means 71 Discharge device 82 Baffle plate 82a Hole 91,131 Deodorizing filter 101,114,115,116 Outside air introduction valve 141 Shutoff valve 142 Switching valve 151,152 Coupling
Claims (12)
に画成して、一方に建物のごみ投入口に連なる輸送管
を、他方にブロワの吸引側に連なる風管を、それぞれ接
続して、輸送管側の室を貯留室に、ブロワ側の室を排気
室に、それぞれ形成し、かつ該貯留室にはごみ排出用の
排出弁を設けてなるごみ分離貯留装置。1. A pressure-resistant container is divided into two chambers by a high-strength filter, one of which is connected to a transport pipe connected to a building waste inlet, and the other is connected to a wind pipe connected to a suction side of a blower. A waste separation / storage device in which a chamber on the transport pipe side is formed as a storage chamber and a chamber on the blower side is formed as an exhaust chamber, and a discharge valve for discharging dust is provided in the storage chamber.
の重力により該貯留室底面まで降下する前に該貯留室の
最奥部の壁面に衝突するように、輸送管内の風速を13
m/sec 〜35m/sec 、ごみ輸送速度を、比重0.1
5t/m3 以上の重量物の場合で5m/sec 以上、比重
0.15t/m3 以下の軽量物の場合で10m/sec 以
上に設定してなる請求項1記載のごみ分離貯留装置。2. The wind speed in the transportation pipe is set to 13 so that dust that has been pneumatically transported into the storage chamber collides with the innermost wall surface of the storage chamber before it falls to the bottom surface of the storage chamber due to its gravity.
m / sec-35m / sec, refuse transportation speed, specific gravity 0.1
The waste separation / storage device according to claim 1, wherein the weight is set to 5 m / sec or more in the case of a heavy object of 5 t / m 3 or more and 10 m / sec or more in the case of a lightweight object of a specific gravity of 0.15 t / m 3 or less.
ルタ部での空気通過速度が一般ごみの場合で2m/sec
以下、袋ごみの場合で5m/sec 以下、瓶・缶の場合で
10m/sec 以下となる面積に設定してなる請求項1又
は請求項2記載のごみ分離貯留装置。3. The area of the high-strength filter is set to 2 m / sec when the air passage speed in the high-strength filter is general dust.
The waste separation and storage device according to claim 1 or 2, wherein the area is set to 5 m / sec or less for bag garbage and 10 m / sec or less for bottles / cans.
直径の2倍以上の直管部を設けてなる請求項1乃至請求
項3のいずれかに記載のごみ分離貯留装置。4. The waste separation / storage device according to claim 1, wherein a straight pipe portion having a diameter equal to or more than twice the diameter of the transport pipe is provided at a connection portion of the transport pipe with the storage chamber.
て貯留室内に貯留されるごみの圧縮度を制御するごみ圧
縮度制御手段を設けてなる請求項1乃至請求項4のいず
れかに記載のごみ分離貯留装置。5. The dust compressibility control means for adjusting the difference in internal pressure between the transport pipe and the wind pipe to control the compressibility of the dust stored in the storage chamber. The waste separation and storage device according to any one of the above.
みて貯留室内のごみの満杯を検出するごみ満杯検出手段
を設けてなる請求項1乃至請求項4のいずれかに記載の
ごみ分離貯留装置。6. The dust full detection means for detecting fullness of dust in the storage chamber by observing a change in a difference in internal pressure between the transport pipe and the wind pipe, according to any one of claims 1 to 4. Waste separation and storage device.
たごみの排出装置を設置してなる請求項1乃至請求項6
のいずれかに記載のごみ分離貯留装置。7. The discharge device for the dust stored in the storage chamber is installed at the bottom of the storage chamber.
The waste separation and storage device according to any one of 1.
みの高強度フィルタ側への飛翔を規制する通気性を備え
たじゃま板を設けてなる請求項1乃至請求項7のいずれ
かに記載のごみ分離貯留装置。8. The baffle plate having air permeability for restricting the flying of pneumatically transported light-weight dust to the high-strength filter side in the storage chamber, according to claim 1. Waste separation and storage device.
ィルタを設置してなる請求項1乃至請求項8のいずれか
に記載のごみ分離貯留装置。9. The waste separation / storage device according to claim 1, wherein a deodorizing filter is installed in the middle of an air circulation path in the exhaust chamber.
気導入弁を設けてなる請求項1乃至請求項9のいずれか
に記載のごみ分離貯留装置。10. The waste separation / storage device according to claim 1, wherein the exhaust chamber is provided with an outside air introduction valve for cleaning a high-strength filter.
を設けるとともに、風管の排気室接続部の近傍に、ブロ
ワへの流路を排気室と外気との間で切り換える切換弁を
設けてなる請求項10記載のごみ分離貯留装置。11. A shutoff valve is provided in the vicinity of the connecting portion of the storage chamber of the transportation pipe, and a switching valve for switching the flow path to the blower between the exhaust chamber and the outside air is provided in the vicinity of the connecting portion of the exhaust chamber of the wind pipe. The waste separation and storage device according to claim 10, which is provided.
可能に構成してなる請求項1乃至請求項11のいずれか
に記載のごみ分離貯留装置。12. The waste separation / storage device according to claim 1, wherein the pressure-resistant container is configured to be separable from the transportation pipe and the wind pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6038485A JP3013281B2 (en) | 1994-03-09 | 1994-03-09 | Waste separation storage device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6038485A JP3013281B2 (en) | 1994-03-09 | 1994-03-09 | Waste separation storage device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07247005A true JPH07247005A (en) | 1995-09-26 |
JP3013281B2 JP3013281B2 (en) | 2000-02-28 |
Family
ID=12526569
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6038485A Expired - Fee Related JP3013281B2 (en) | 1994-03-09 | 1994-03-09 | Waste separation storage device |
Country Status (1)
Country | Link |
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JP (1) | JP3013281B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008120501A (en) * | 2006-11-10 | 2008-05-29 | Akio Aoki | Pneumatic transportation article separating device |
JP2013071035A (en) * | 2011-09-27 | 2013-04-22 | Sekisui Chem Co Ltd | Cleaning system of building |
KR20150123819A (en) * | 2013-03-05 | 2015-11-04 | 마리캡 오이 | Method and apparatus in pneumatic materials handling and a waste container/separating device |
JP6435566B1 (en) * | 2018-01-26 | 2018-12-12 | 三菱重工環境・化学エンジニアリング株式会社 | Waste vacuum transportation system and method of remodeling waste vacuum transportation system |
CN112678371A (en) * | 2020-12-11 | 2021-04-20 | 吴廷贵 | Garbage storage device and outdoor garbage can convenient to use |
JP2022097103A (en) * | 2020-12-18 | 2022-06-30 | 株式会社御池鐵工所 | Separator |
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CN105883268B (en) * | 2016-05-10 | 2018-05-11 | 成都易顺通环保科技有限公司 | Pneumatic rubbish collects separation compression transferring box |
Citations (6)
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JPS5574915A (en) * | 1978-12-01 | 1980-06-05 | Taisei Corp | Separation exhauster for air carrier |
JPS63139208U (en) * | 1987-03-04 | 1988-09-13 | ||
JPH05132107A (en) * | 1991-11-13 | 1993-05-28 | Nkk Corp | Pneumatic transportation equipment for refuse |
JPH05162810A (en) * | 1991-12-17 | 1993-06-29 | Nkk Corp | Pneumatic transport method and facility for refuse |
JPH0582908U (en) * | 1992-04-17 | 1993-11-09 | 株式会社イワセカムパニー | Waste treatment equipment |
JPH0616205A (en) * | 1992-06-30 | 1994-01-25 | Toshiba Corp | Waste disposal device |
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1994
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Patent Citations (6)
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JPS5574915A (en) * | 1978-12-01 | 1980-06-05 | Taisei Corp | Separation exhauster for air carrier |
JPS63139208U (en) * | 1987-03-04 | 1988-09-13 | ||
JPH05132107A (en) * | 1991-11-13 | 1993-05-28 | Nkk Corp | Pneumatic transportation equipment for refuse |
JPH05162810A (en) * | 1991-12-17 | 1993-06-29 | Nkk Corp | Pneumatic transport method and facility for refuse |
JPH0582908U (en) * | 1992-04-17 | 1993-11-09 | 株式会社イワセカムパニー | Waste treatment equipment |
JPH0616205A (en) * | 1992-06-30 | 1994-01-25 | Toshiba Corp | Waste disposal device |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008120501A (en) * | 2006-11-10 | 2008-05-29 | Akio Aoki | Pneumatic transportation article separating device |
JP2013071035A (en) * | 2011-09-27 | 2013-04-22 | Sekisui Chem Co Ltd | Cleaning system of building |
KR20150123819A (en) * | 2013-03-05 | 2015-11-04 | 마리캡 오이 | Method and apparatus in pneumatic materials handling and a waste container/separating device |
JP2016509984A (en) * | 2013-03-05 | 2016-04-04 | マリキャップ オーワイ | Pneumatic material handling method and mechanism, and waste container / separator |
JP6435566B1 (en) * | 2018-01-26 | 2018-12-12 | 三菱重工環境・化学エンジニアリング株式会社 | Waste vacuum transportation system and method of remodeling waste vacuum transportation system |
CN112678371A (en) * | 2020-12-11 | 2021-04-20 | 吴廷贵 | Garbage storage device and outdoor garbage can convenient to use |
CN112678371B (en) * | 2020-12-11 | 2022-10-28 | 池州市金城工程管理服务有限责任公司 | Garbage storage device and outdoor garbage can convenient to use |
JP2022097103A (en) * | 2020-12-18 | 2022-06-30 | 株式会社御池鐵工所 | Separator |
Also Published As
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---|---|
JP3013281B2 (en) | 2000-02-28 |
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