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JPS646084B2 - - Google Patents
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JPS646084B2 - - Google Patents

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Publication number
JPS646084B2
JPS646084B2 JP5684881A JP5684881A JPS646084B2 JP S646084 B2 JPS646084 B2 JP S646084B2 JP 5684881 A JP5684881 A JP 5684881A JP 5684881 A JP5684881 A JP 5684881A JP S646084 B2 JPS646084 B2 JP S646084B2
Authority
JP
Japan
Prior art keywords
relay station
central processing
processing unit
separator
waste
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP5684881A
Other languages
Japanese (ja)
Other versions
JPS57170301A (en
Inventor
Takeshi Hirota
Tsutomu Ooba
Shunichi Mitsuya
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Taisei Corp
Ebara Corp
Original Assignee
Taisei Corp
Ebara Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Taisei Corp, Ebara Corp filed Critical Taisei Corp
Priority to JP5684881A priority Critical patent/JPS57170301A/en
Publication of JPS57170301A publication Critical patent/JPS57170301A/en
Publication of JPS646084B2 publication Critical patent/JPS646084B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Refuse Collection And Transfer (AREA)
  • Air Transport Of Granular Materials (AREA)

Description

【発明の詳細な説明】 〔発明の目的〕 「産業上の利用分野」 本発明はごみの空気輸送及びその装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION OBJECTS OF THE INVENTION "Field of Industrial Application" The present invention relates to pneumatic transport of waste and its apparatus.

「従来の技術と発明が解決しようとする課題」 第1図は従来例のごみの空気輸送方法を示す斜
視図である。1は建物内に設けたごみの投入口2
を備えたダストシユートであつてダストシユート
1より直接又は貯留排出機4を介して排出弁3に
つながれており、排出弁3より輸送配管5に連結
され、輸送配管5は各地域毎に集められて中央処
理装置6の分離機7に送られて空気とごみは分離
され、ごみはセンタ貯留排出機8を経て排出さ
れ、空気は空気管9、バグフイルタ等の集塵器1
0を経て除塵されて送風機11によつて吸引され
る。
"Prior Art and Problems to be Solved by the Invention" FIG. 1 is a perspective view showing a conventional pneumatic transport method for waste. 1 is a garbage input port 2 installed in the building
The dust chute 1 is connected directly or via a storage discharger 4 to a discharge valve 3, and the discharge valve 3 is connected to a transport pipe 5, and the transport pipes 5 are collected in each region and centrally connected. The air is sent to the separator 7 of the processing device 6, where it is separated from the dust.The dust is discharged through the center storage and discharge machine 8, and the air is sent to the air pipe 9 and the dust collector 1, such as a bag filter.
0, the dust is removed, and the air is sucked by the blower 11.

以上のような空気輸送方法においては輸送配管
5は同断面積のものが用いられ、限られた端末の
ごみ投入部近くの配管のみが輸送配管5よりも細
く作られる。処がごみ処理の輸送配管5は次第に
枝分れしてごみの投入口に至るため、その中間の
輸送配管5は総延長が極めて長くなりその建設費
は膨大なものとなつている。又このような方法に
よればセンタ機器である送風機11、分離機7等
を運転する時間がどうしても長くかゝるという欠
点もある。
In the above-described pneumatic transportation method, the transportation piping 5 has the same cross-sectional area, and only the piping near the waste input section at a limited terminal is made thinner than the transportation piping 5. However, since the transport pipe 5 for waste treatment gradually branches to reach the waste input port, the total length of the intermediate transport pipe 5 is extremely long, and the construction cost thereof is enormous. Furthermore, this method has the disadvantage that it takes a long time to operate the center equipment such as the blower 11 and the separator 7.

そこでローカルごみ投入部を或程度まとめて中
継ステーシヨンを置き、中継ステーシヨンを中央
処理装置と同じく空気分離機、貯留排出機、集塵
機、送風機を備えて中継ステーシヨンへ一旦ごみ
を集めて更に中央処理装置により吸引してごみを
集めるものが提案されている。処がこのような方
法はローカルごみ投入部より中央処理装置までの
輸送配管はほぼ同じ断面積のものであるから輸送
配管の建設費は安くはならないし、又、中継ステ
ーシヨンに集塵機、送風機を備えなければならな
い。
Therefore, we put together a relay station that consolidates the local garbage input sections to some extent, and the relay station is equipped with an air separator, a storage/discharge device, a dust collector, and a blower in the same way as the central processing unit, and once the garbage is collected at the relay station, it is further processed by the central processing unit. A device that collects dust by suction has been proposed. However, in this method, the transportation piping from the local garbage input section to the central processing unit has almost the same cross-sectional area, so the construction cost of the transportation piping is not cheap, and the transfer station is not equipped with a dust collector and a blower. There must be.

更に特公昭54−16358号の発明は中継ステーシ
ヨンには分離機と貯留排出機のみを備え、ローカ
ルごみ投入部から集めたごみを中央処理装置の一
台の送風機にて吸引して中継ステーシヨンに一旦
貯留し、中継ステーシヨンに集められたごみを更
に該送風機により吸引している。このようにする
と地域別のごみ収集に際して、中継ステーシヨン
から中央処理装置へ中継ステーシヨンのごみを輸
送する能力のある送風機が常に運転されることに
なり、ランニングコストがかゝる。又、輸送配管
についてもローカルごみ投入部より中央処理装置
までの各輸送配管は吸引空気量からほぼ同断面積
のものとなるから輸送配管の建設費は安くならな
いし、ローカルごみの収集はローカルごみの輸送
配管毎となるので時間がかゝる欠点がある。
Furthermore, in the invention of Japanese Patent Publication No. 54-16358, the relay station is equipped with only a separator and a storage/discharge machine, and the garbage collected from the local garbage input section is sucked up by one blower of the central processing unit and sent to the relay station once. The dust stored and collected at the relay station is further sucked up by the blower. In this case, when garbage is collected by region, a blower capable of transporting the garbage from the relay station to the central processing unit is constantly operated, which increases running costs. In addition, regarding the transportation piping, each transportation piping from the local garbage input section to the central processing unit has approximately the same cross-sectional area based on the amount of suction air, so the construction cost of the transportation piping will not be reduced, and the collection of local garbage is The disadvantage is that it takes time because each transport pipe is required.

本願第1発明は以上のような従来のごみの空気
輸送方法の課題のうち、ごみの収集を早めて中央
処理装置のランニングコストの低減を計れる空気
輸送方法を提供することを目的とするものであ
る。
The first invention of the present application aims to solve the above-mentioned problems of the conventional pneumatic transport method for waste by providing a pneumatic transport method that can speed up the collection of waste and reduce the running cost of the central processing unit. be.

本願第2発明は上記本願第1発明の目的に加え
て輸送配管の建設コストの低減を計ることを目的
とするものである。
The second invention of the present application, in addition to the object of the first invention of the present application, aims to reduce the construction cost of transportation piping.

〔発明の構成〕[Structure of the invention]

「課題を解決するための手段」 本願第1発明は多数のごみ投入部を地域的に一
括してこれらに比較的近い地点に、ごみ出口側と
空気出口側とを選択的に中央処理装置と結ぶ二次
輸送配管に接続可能な弁装置を備えた分離機を有
する共通の中継ステーシヨンを設置して、中継ス
テーシヨンを一次輸送配管により各ごみ投入部と
接続流通させ、各中継ステーシヨンを適宜一括し
て共通の中央処理装置に二次輸送配管により接続
して、各中継ステーシヨンに地域のごみ投入部で
捨てられるごみを一旦収集し、各中継ステーシヨ
ンに収集されたごみを中継ステーシヨンから中央
処理装置に二次輸送配管を通じて移送するように
したごみの空気輸送方法において、中央処理装置
は一つの分離機と、一つの分離機に見合う全能力
を持つと共にごみ投入地域から中継ステーシヨン
にごみを収集するに足る一部能力を出力する送風
機を備え、中央処理装置の送風機の一部能力でも
つて運転して、一つの二次輸送配管により連結さ
れている一つの中継ステーシヨンの空気出口に前
記弁装置により該二次輸送配管を接続してごみ投
入部から捨てられたごみを順次に各中継ステーシ
ヨンに収集し、次に二次輸送配管を一つの中継ス
テーシヨンに設けた分離機のごみ出口に接続し
て、中央処理装置の分離機を介在させて全能力で
送風機を運転し、一つの中継ステーシヨンに集め
られたごみを中央処理装置の分離機に移送するこ
とを各中継ステーシヨンについて順次行うことを
特徴とするごみの空気輸送方法である。
``Means for Solving the Problems'' The first invention of the present application is to locally collectively install a large number of garbage input sections, and to selectively install a central processing unit on the garbage outlet side and the air outlet side at a point relatively close to these sections. A common relay station with a separator equipped with a valve device that can be connected to the secondary transport piping will be installed, and the relay station will be connected and distributed to each waste input section through the primary transport pipe, and each relay station will be bundled as appropriate. The terminals are connected to a common central processing unit by secondary transport piping, and each relay station collects waste that is discarded at the local waste input section, and the waste collected at each relay station is transferred from the relay station to the central processing unit. In the pneumatic transport method of waste, which is transported through secondary transport piping, the central processing unit has one separator and the full capacity of one separator, and is capable of collecting waste from the waste input area to the transfer station. It is equipped with a blower that outputs a sufficient partial capacity, and is operated with a partial capacity of the blower of the central processing unit, and the air outlet of one relay station connected by one secondary transport pipe is supplied by the valve device. The secondary transport pipe is connected to sequentially collect the waste discarded from the waste input section to each relay station, and then the secondary transport pipe is connected to the waste outlet of the separator provided at one relay station. The method is characterized in that the blower is operated at full capacity with the separator of the central processing unit interposed, and the waste collected at one relay station is transferred to the separator of the central processing unit in sequence for each relay station. It is a method of pneumatic transportation of waste.

本願第2発明は分離機と、一つの分離機に対し
て複数の送風機と、全送風機を分離機を介して二
次輸送配管に連通させるか、一部送風機を連通さ
せるかを行なう配管とを備えた中央処理装置と、
適宜の中継ステーシヨンを一括して前記中央処理
装置に夫々連結された二次輸送配管と、各地域に
配された多数のごみ投入部と、各ごみ投入部を一
括して中継ステーシヨンに連結する一次輸送配管
と、一次輸送配管に空気入口が連結され、貯留排
出機を備えた分離機と、この分離機の貯留排出機
の出口と分離機の空気出口とに連結された二次輸
送配管に選択的に連通する弁装置とを備えた中継
ステーシヨンを備えてなり、二次輸送配管の断面
積に対して各一次輸送配管の断面積が中央処理装
置に接続された二次輸送配管の数をNとしたとき
ほぼ1/Nであることを特徴とするごみの空気輸
送装置である。
The second invention of the present application includes a separator, a plurality of blowers for one separator, and piping that connects all the blowers to the secondary transportation piping via the separator, or connects some of the blowers to the secondary transportation piping. a central processing unit equipped with;
Secondary transport pipes that collectively connect appropriate relay stations to the central processing unit, a large number of garbage input sections arranged in each area, and a primary system that connects each garbage input section collectively to the relay station. A transport pipe, a separator with an air inlet connected to the primary transport pipe and a storage discharger, and a secondary transport pipe connected to an outlet of the storage discharger of this separator and an air outlet of the separator. a relay station with a valve device that communicates with the central processing unit, and the cross-sectional area of each primary transport pipe is equal to the number of secondary transport pipes connected to the central processing unit, with respect to the cross-sectional area of the secondary transport pipe. This pneumatic waste transportation device is characterized in that the ratio is approximately 1/N.

「実施例」 以下、本発明の実施例を図面により説明する。
本願第1発明を具現するための手段の一例は本願
第2発明の実施例に示されており、重複する部分
については併せて説明されるが重複を避けるため
他方の説明を省略する。
"Example" Hereinafter, an example of the present invention will be described with reference to the drawings.
An example of the means for implementing the first invention of the present application is shown in the embodiment of the second invention of the present application, and the overlapping parts will be explained together, but the explanation of the other will be omitted to avoid duplication.

第2図中には中継ステーシヨン12a,12bにお
ける機器の側面図が示されている。地域a,bの
一次輸送配管5a,5bは夫々総合一括されて空
気とごみの分離機14に結合され、分離機14の
ごみの排出口は貯留排出機15に結合され、分離
機14により空気管16は開閉弁17を介して二
次輸送配管13a,13bに結合されている。貯
留排出機15の出口は排出弁18を介して二次輸
送配管13a,13bに夫々連結されている。2
0は吸気弁である。尚、分離機14、貯留排出機
15については一具体例であり、ごみと空気とを
分離しかつごみを貯留できる装置であればよい。
FIG. 2 shows a side view of the equipment at the relay stations 12a, 12b. The primary transport pipes 5a and 5b in regions a and b are respectively integrated and connected to an air and waste separator 14, and the waste outlet of the separator 14 is connected to a storage discharger 15, and the separator 14 separates air from the air. The pipe 16 is connected to secondary transport pipes 13a and 13b via an on-off valve 17. The outlet of the storage discharger 15 is connected to secondary transport pipes 13a and 13b via a discharge valve 18, respectively. 2
0 is the intake valve. Note that the separator 14 and the storage/discharge device 15 are just one specific example, and any device that can separate dust and air and store dust may be used.

第3図は中央処理装置6の配置図である。二次
輸送配管13a,13bは中央処理装置6の入口
にて夫々偏位した逆Y字に分れて二次輸送配管1
3a,13bは同断面にて直通してごみと空気の
分離機19に連結され、分離機19はごみの排出
口が貯留排出機21に連結されている。上記した
形で二次輸送配管13a,13bより分岐した空
気管22a,22bは夫々開閉弁23a,23b
を介してバグフイルタ24a,24bに向う途中
で分離機19の空気吸入口に連結された空気管2
5a,25bが夫々開閉弁26a,26bを介し
て合流すべく連結されて空気管27a,27bに
連なり、空気管27a,27bは夫々バグフイル
タ24a,24bに連結され、空気管27a,2
7bはバグフイルタ24a,24bより出て流量
調整弁28a,28bを介して送風機29a,2
9bの吸込口に連結されている。送風機29a,
29bの吐出口よりは空気吐出管31a,31b
を通じて脱臭器32を介して大気に通じている。
FIG. 3 is a layout diagram of the central processing unit 6. The secondary transport pipes 13a and 13b are divided into deviated inverted Y-shapes at the entrance of the central processing unit 6, and the secondary transport pipe 1
3a and 13b are connected to a dust and air separator 19 through direct communication with the same cross section, and the separator 19 has a dust discharge port connected to a storage discharge machine 21. The air pipes 22a and 22b branched from the secondary transport pipes 13a and 13b in the above-described manner have on-off valves 23a and 23b, respectively.
The air pipe 2 is connected to the air intake port of the separator 19 on the way to the bag filters 24a and 24b via the
5a and 25b are connected to join together via on-off valves 26a and 26b, respectively, and are connected to air pipes 27a and 27b, and air pipes 27a and 27b are connected to bag filters 24a and 24b, respectively, and air pipes 27a and 2
7b comes out from the bag filters 24a, 24b and goes to the blowers 29a, 2 through the flow rate regulating valves 28a, 28b.
It is connected to the suction port 9b. Blower 29a,
Air discharge pipes 31a and 31b are connected to the discharge port 29b.
The deodorizer 32 communicates with the atmosphere through the deodorizer 32 .

中継ステーシヨン12a,12bは中継ステー
シヨンの作用としては同一なので中継ステーシヨ
ン12aのみ作用をのべると、先ず弁装置の開閉
弁17を開き、排出弁18を閉じて二次輸送配管
13aから吸気すると一次輸送配管5aからご
み、空気が分離機14へ入りごみと空気が分離さ
れ、ごみは貯留排出機15に貯留され、空気は空
気管16、開いている開閉弁17を通つて二次輸
送配管13aに流れる。
The relay stations 12a and 12b have the same function as the relay stations, so if only the function of the relay station 12a is considered, first the on-off valve 17 of the valve device is opened, the discharge valve 18 is closed, and air is taken in from the secondary transport pipe 13a, and then the primary transport pipe is 5a, garbage and air enter the separator 14, where the garbage and air are separated.The garbage is stored in the storage/discharge device 15, and the air flows through the air pipe 16 and the open on-off valve 17 to the secondary transportation pipe 13a. .

次に分離機14につながる一次輸送配管5aが
閉止されておる状態において、開閉弁17を閉
じ、排出弁18を開いて二次輸送配管13aから
空気吸引すると大気が吸気弁20より吸込まれ
て、貯留排出機15のごみと共に排出弁18から
出て二次輸送配管13aに送り出される。
Next, when the primary transport pipe 5a connected to the separator 14 is closed, the on-off valve 17 is closed and the discharge valve 18 is opened to suck air from the secondary transport pipe 13a. Atmospheric air is sucked in through the intake valve 20. It comes out from the discharge valve 18 together with the garbage in the storage discharger 15 and is sent to the secondary transportation pipe 13a.

二次輸送配管13aからの空気吸引に対して中
継ステーシヨン12aを非作用とするには弁装置
を閉じる。即ち、開閉弁17、排出弁18を閉じ
る。
To make the relay station 12a inactive against air suction from the secondary transport pipe 13a, the valve device is closed. That is, the on-off valve 17 and the discharge valve 18 are closed.

中央処理装置6は本例では同能力の送風機29
a,29bを持つている。従つて、一部送風機2
9a,又は29bを運転する場合即ち、全能力に
対して一部能力で運転する場合は同一なので送風
機29aを運転する場合についてのべると、中継
ステーシヨン12aを作動する際は二次輸送配管
13bにつながつている中継ステーシヨン12b
の弁装置は閉じている。即ち、開閉弁23b,2
6bは常に閉じる。開閉弁23a,23aは何れ
かを開くか或は両方共開いてもよい。そして送風
機29aが運転されると二次輸送配管13aから
吸込まれた空気は分離機19をバイパスしている
空気管22a、開いている開閉弁23a、を経て
バグフイルタ24aに到るか、分離機19に入
り、開いている開閉弁26aを通じてバグフイル
タ24aに到るか或は上記両経路を分流してバグ
フイルタ24aに到る。バグフイルタ24aを通
過した空気は流量調整弁28aを介して送風機2
9aに吸込まれ、増速昇圧されて空気吐出管31
aに吐出され、脱臭器32により脱臭され排出さ
れる。
In this example, the central processing unit 6 is a blower 29 with the same capacity.
It has a, 29b. Therefore, some blower 2
When operating the fan 9a or 29b, that is, when operating at a partial capacity compared to the full capacity, the same is true, so when operating the blower 29a, when operating the relay station 12a, it is connected to the secondary transport pipe 13b. relay station 12b
The valve device is closed. That is, the on-off valves 23b, 2
6b is always closed. Either or both of the on-off valves 23a, 23a may be opened. Then, when the blower 29a is operated, the air sucked from the secondary transport pipe 13a passes through the air pipe 22a bypassing the separator 19 and the open on-off valve 23a, and reaches the bag filter 24a, or the separator 19 The water then enters the bag filter 24a through the opened on-off valve 26a, or the above-mentioned two routes are divided to reach the bag filter 24a. The air that has passed through the bag filter 24a is sent to the blower 2 via the flow rate adjustment valve 28a.
9a, the air is accelerated and the pressure is increased, and the air is discharged into the discharge pipe 31.
a, and is deodorized by the deodorizer 32 and discharged.

全送風機29a,29bを運転する場合は二次
輸送配管13a,13bの何れかから空気とごみ
を吸引するが同じであるので二次輸送配管13a
についてのべると、開閉弁23a,23bを閉
じ、開閉弁26a,26bを開ける。二次輸送配
管13bは吸引すべき先の中継ステーシヨン12
bで閉止されている。これによつて二次輸送配管
13aを通じて分離機19にごみと空気は送り込
まれて分離し、ごみは貯留排出機21に貯留さ
れ、分離した空気は開閉弁26a,26bからバ
グフイルタ24a,24bに流れて除塵され、流
量調整弁28a,28b、送風機29a,29b
と流れて送風機29a,29bより空気吐出管3
1a,31bに出た空気は合流し脱臭器32を介
して排出される。
When all the blowers 29a and 29b are operated, air and dust are sucked from either the secondary transport pipe 13a or 13b, but since they are the same, the secondary transport pipe 13a
Specifically, the on-off valves 23a and 23b are closed, and the on-off valves 26a and 26b are opened. The secondary transport pipe 13b is connected to the relay station 12 to which suction is to be performed.
It is closed at b. As a result, garbage and air are sent to the separator 19 through the secondary transportation pipe 13a and separated, the garbage is stored in the storage discharger 21, and the separated air flows from the on-off valves 26a, 26b to the bag filters 24a, 24b. dust is removed, flow rate adjustment valves 28a, 28b, blowers 29a, 29b
The air flows from the blowers 29a and 29b to the air discharge pipe 3.
The air discharged from 1a and 31b is combined and discharged via the deodorizer 32.

次に配管のレイアウトについてのべる。第2図
はローカルごみの収集地域に分けて収集する場合
であるがN地域(N:整数)に分けて収集する場
合も同様である。各地域において1は建物内に設
けたごみの投入口2を備えたダイトシユートであ
つて、排出弁3によりその地域における一次輸送
配管5a,5bに夫々つながれている。一次輸送
配管5a,5bは夫々が集められて中継ステーシ
ヨン12a,12bに一括して引込まれている。
一次輸送配管5a,5bの端末にはローカル吸気
弁33〜36,37〜40が設けられている。中
継ステーシヨン12a,12bと中央処理装置6
間は二次輸送配管13a,13bにより連結され
ている。尚、大量のごみを発生する施設12cよ
りは附加して例えば二次輸送管13aに分岐二次
輸送配管13cが連結される。尚、極めて大量の
ごみを発生する施設がある場合は中継スチーシヨ
ンとその中継ステーシヨンのごみ収集の地域を一
括した程度と相当するので直接中央処理装置6へ
直結した輸送配管により連結される。こゝでは地
域a,bとそれらに対する中継ステーシヨン12
a,12b、中継ステーシヨン12a,12bよ
り中央処理装置6までのみある最も簡略な場合に
ついてのべるが地域が更に多数となつても同要旨
である。
Next, let's talk about the piping layout. Although FIG. 2 shows the case where local garbage is collected by dividing it into collection areas, the same applies to the case where it is divided into N areas (N: an integer). In each region, reference numeral 1 is a die chute provided with a waste input port 2 provided in a building, and connected by a discharge valve 3 to primary transport pipes 5a and 5b in that region, respectively. The primary transport pipes 5a, 5b are collected and drawn into relay stations 12a, 12b as a unit.
Local intake valves 33-36, 37-40 are provided at the ends of the primary transport pipes 5a, 5b. Relay stations 12a, 12b and central processing unit 6
They are connected by secondary transport pipes 13a and 13b. Note that a branch secondary transport pipe 13c is additionally connected to, for example, a secondary transport pipe 13a from the facility 12c that generates a large amount of waste. Incidentally, if there is a facility that generates an extremely large amount of garbage, the relay station and the garbage collection area of the relay station are equivalent to a single unit, so they are connected by a transportation pipe directly connected to the central processing unit 6. Here, areas a and b and relay station 12 for them are shown.
The following describes the simplest case in which there are only the relay stations 12a, 12b and the central processing unit 6, but the gist remains the same even if there are many more areas.

地域aの一次輸送配管5aの一つについてその
一次輸送配管5aのロール吸気弁33〜36の何
れか一つのみを開いて、他を閉じ中央処理装置6
より送風機の一部能力で空気を吸引することによ
り、即ち、送風機29aを用いて、その一次輸送
配管5aに排出弁3を介してつながるダストシユ
ート1のごみは中継ステーシヨン12aに集めら
れる。
For one of the primary transport pipes 5a in region a, only one of the roll intake valves 33 to 36 of the primary transport pipe 5a is opened, and the others are closed.
By sucking air with a partial capacity of the blower, that is, by using the blower 29a, the dust in the dust chute 1 connected to the primary transport pipe 5a via the discharge valve 3 is collected at the relay station 12a.

尚、以後シユート1のごみを中継ステーシヨン
へごみ収集する際のローカル吸気弁33〜40の
作用の説明は、当該シユート1が属する一次輸送
配管の端末のローカル吸気弁のみを開くことであ
るのでその説明は略される。中継ステーシヨン1
2aではごみと空気は分離せられごみは貯留され
る。同様にして残りの一次輸送配管5aの一つ宛
について中継ステーシヨン12aにごみは収集せ
られる。従つて二次輸送配管13a中は空気のみ
流れるのである。
In addition, the explanation of the function of the local intake valves 33 to 40 when collecting garbage in chute 1 to the relay station will be explained below because only the local intake valve at the end of the primary transport pipe to which the chute 1 belongs is opened. Explanation will be omitted. Relay station 1
In 2a, garbage and air are separated and the garbage is stored. In the same manner, garbage destined for one of the remaining primary transport pipes 5a is collected at the relay station 12a. Therefore, only air flows through the secondary transport pipe 13a.

地域bについても地域aと同様に一次輸送配管
5bの一つについてのみ中央処理装置6より送風
機の一部能力で空気を吸引することにより、即
ち、送風機29bを用いて、その一次輸送配管5
bに排出弁3を介してつながるダストシユート1
のごみは中継ステーシヨン12bに集められる。
中継ステーシヨン12bではごみと空気は分離せ
られごみを貯留する機能をもたせる。同様にして
残りの一次輸送配管5bの一つ宛について同様に
して中継ステーシヨン12bにごみは収集せられ
る。二次輸送配管13bには空気のみ流れる。
In region b, as in region a, air is sucked from only one of the primary transport pipes 5b from the central processing unit 6 using a partial capacity of the blower, that is, by using the blower 29b, the primary transport pipe 5 is
Dust chute 1 connected to b via discharge valve 3
The garbage is collected at the transfer station 12b.
The relay station 12b separates dirt and air and has the function of storing dirt. In the same way, garbage is collected at the relay station 12b for one of the remaining primary transport pipes 5b. Only air flows through the secondary transport pipe 13b.

地域a,bのごみの中継ステーシヨン12a,
12bへのごみの収集は送風機29a,29bを
夫々制御して同時又は各々独立して行われる。
Garbage relay station 12a for areas a and b,
The collection of garbage to 12b is performed simultaneously or independently by controlling the blowers 29a and 29b, respectively.

ただし、中継ステーシヨン12a,12bに同
時にごみ収集する場合には中央処理装置6の開閉
弁23a,23bを開き、開閉弁26a,26b
を閉じることにより、各二次輸送配管13a,1
3bを流れる風量が安定する。
However, when garbage is collected at the relay stations 12a and 12b at the same time, the on-off valves 23a and 23b of the central processing unit 6 are opened, and the on-off valves 26a and 26b are
By closing each secondary transport pipe 13a, 1
The amount of air flowing through 3b becomes stable.

次の段階では中継ステーシヨン12aに貯留さ
れたごみを吸引すべく中継ステーシヨン12bの
弁装置の開閉弁17、排出弁18を閉じ、中央処
理装置6の開閉弁23a,23bを閉じ、他の開
閉弁26a,26bを開いて送風機の全能力で空
気吸引する。即ち、全送風機29a,29bが運
転され、地域a,b夫々において中継ステーシヨ
ン12a,12bにごみを集める際に二次輸送配
管13a,13b夫々を流れた空気の風量の合計
したものが二次輸送配管13aに流され、中継ス
テーシヨン12aのごみは二次輸送配管13aを
とおり中央処理装置6に集められ、ごみと空気に
分離され、ごみは貯留排出される。同様に中継ス
テーシヨン12bに貯留されたごみは地域a,b
夫々において中継ステーシヨン12a,12bに
ごみを集める際に二次輸送配管13a,13bを
流れた合計の風量の空気が二次輸送配管13bを
流され、中継ステーシヨン12bのごみは二次輸
送配管13bをとおり、中央処理装置6に集めら
れ、空気とごみは分離せられ、ごみは貯留排出さ
れる。
In the next step, the on-off valve 17 and discharge valve 18 of the valve device of the relay station 12b are closed in order to suck out the garbage stored in the relay station 12a, the on-off valves 23a and 23b of the central processing unit 6 are closed, and the other on-off valves are closed. 26a and 26b are opened to suck air with the full capacity of the blower. That is, when all the blowers 29a and 29b are operated and garbage is collected at the relay stations 12a and 12b in areas a and b, the total amount of air flowing through the secondary transport pipes 13a and 13b is the secondary transport. The waste in the relay station 12a passes through the secondary transport pipe 13a and is collected in the central processing unit 6, where it is separated into dirt and air, and the waste is stored and discharged. Similarly, the garbage stored at the transfer station 12b is in areas a and b.
When collecting garbage at the relay stations 12a and 12b, the total amount of air flowing through the secondary transport pipes 13a and 13b is passed through the secondary transport pipe 13b, and the waste at the relay station 12b is collected through the secondary transport pipe 13b. As described above, the air is collected in the central processing unit 6, air and dust are separated, and the dust is stored and discharged.

このようなごみの空気輸送方法によれば中継ス
テーシヨンとローカルごみ投入部とを結ぶ一本の
一次輸送配管5a,5bについてはそのごみ投入
部に発生するごみを収集するに付一次輸送配管5
a,5bの一本にのみ空気を流すからそのごみ輸
送についての少ない風量でよく、又一次輸送配管
5a,5b中の風速を適度にするため一次輸送配
管5a,5bの断面積は小さくする。
According to this pneumatic waste transport method, the single primary transport pipe 5a, 5b that connects the relay station and the local waste input part is used to collect the waste generated at the waste input part.
Since the air flows through only one of the pipes 5a and 5b, a small amount of air is required for transporting the waste, and the cross-sectional area of the primary transport pipes 5a and 5b is made small in order to moderate the wind speed in the primary transport pipes 5a and 5b.

そして、中央処理装置6では一部送風機29a
又は29bにより送風機の一部能力でローカルの
ごみ投入口2から投入されたごみが中継ステーシ
ヨン12a又は12bに夫々集められるので、従
来のように中継ステーシヨンから中央処理装置ま
で中継ステーシヨンに貯留されたごみを吸引する
に足る大風量、即ち送風機29a,29bの合計
能力の送風機を一次のごみ収集即ち、中継ステー
シヨン12a,12bへのごみ収集にも運転して
いたという不経済が解消する。
In the central processing unit 6, some blowers 29a
Alternatively, the garbage inputted from the local garbage input port 2 is collected at the relay station 12a or 12b, respectively, using a part of the capacity of the blower by the blower 29b, so that the garbage stored at the relay station is transferred from the relay station to the central processing unit as in the past. This eliminates the uneconomical situation of having to operate the blowers with a large air volume sufficient to suck in the air, that is, the total capacity of the blowers 29a and 29b, also for primary garbage collection, that is, garbage collection to the relay stations 12a and 12b.

次に本願第2発明のごみの空気輸送装置の実施
例について説明する。既に第2図、第3図に説明
した構成は重複をさけ、説明を省略する。第2図
において地域の数は中央処理装置6より出る二次
輸送配管13a,13bの数と等しくN=2であ
り中継ステーシヨンの数もN=2となる。このよ
うな場合一次輸送配管5a,5bが等しくとられ
ている場合において内経400mmの内管とすると二
次輸送配管13a,13bは√4002×2として求
められる近い標準寸法のおよそ内経600mm又は500
mmの内管が選ばれる。
Next, an embodiment of the pneumatic transport device for waste according to the second invention of the present application will be described. The explanation of the configurations already explained in FIGS. 2 and 3 will be omitted to avoid duplication. In FIG. 2, the number of regions is equal to the number of secondary transport pipes 13a, 13b coming out of the central processing unit 6, N=2, and the number of relay stations is also N=2. In such a case, if the primary transport pipes 5a and 5b are equal and have an inner diameter of 400 mm, then the secondary transport pipes 13a and 13b have an inner diameter of approximately 600 mm, which is a close standard dimension calculated as √400 2 × 2. or 500
mm inner tube is chosen.

本願第2発明の作用は第1発明の作用と同様で
あるがローカルごみ投入口2に投入されたごみ
は、中継ステーシヨン12a,12bへのごみの
一次収集における一次輸送配管5a中を通る風速
をごみを輸送するのに最適なものとする結果、二
次輸送配管13a,13bの断面積を一次輸送配
管5aのほぼ2倍としたので、二次輸送配管13
a,13b中の空気の速度はゆるやかであり、空
気の流体摩擦損失は少なく、動力が有効に用いら
れる。又、二次輸送配管13a,13bは大径の
内端600mm又は500mmの管となつているが全送風機
19を通じて吸込み、中継ステーシヨン12a,
12bのごみを中央処理装置6へ二次収集できる
のである。
The operation of the second invention of the present application is similar to that of the first invention, but the garbage put into the local garbage input port 2 has a lower wind speed passing through the primary transport pipe 5a during the primary collection of garbage to the relay stations 12a and 12b. As a result, the cross-sectional area of the secondary transport pipes 13a and 13b is approximately twice that of the primary transport pipe 5a, so that the secondary transport pipe 13
The speed of the air in a and 13b is slow, the fluid friction loss of the air is small, and the power is used effectively. In addition, the secondary transport pipes 13a and 13b are large-diameter pipes with an inner end of 600 mm or 500 mm, and are sucked in through the entire blower 19 and transferred to the relay station 12a,
12b can be collected secondary to the central processing unit 6.

第4図は一般化されたごみの空気輸送方法を示
す斜視図である。前述した本発明の説明は二系統
の夫々の二次輸送配管13a,13bに対して中
継ステーシヨンが夫々1つ宛の場合をのべた。第
4図においては二次輸送配管13aは分岐二次輸
送配管13a―1,13a―2,13a―3を有
し、夫々に中継ステーシヨン12a―1,12a
―2,12a―3が設けられる。即ち、中継ステ
ーシヨンは適宜一括して中央処理装置6に接続さ
れる。該中継ステーシヨンより先は夫々一次輸送
配管5a―1,5a―2,5a―3群にて夫々利
用者のごみ投入口に結ばれる。41は高層住宅、
42は一戸建住宅である。尚43は大量のごみ発
生個所であり、このような場所は直接、中継ステ
ーシヨン12a―3と中央処理装置6との間の分
岐二次輸送配管13a―3に連結される。同様に
二次輸送配管13bは分岐二次輸送配管13b―
1,13b―2を有し、夫々中継ステーシヨン1
2b―1,12b―2を介して一次輸送配管5b
―1,5b―2群により利用者のごみ投入口に結
ばれる。
FIG. 4 is a perspective view showing a generalized pneumatic transportation method for waste. The above description of the present invention is based on the case where one relay station is provided for each of the two secondary transport pipes 13a and 13b. In FIG. 4, the secondary transport pipe 13a has branch secondary transport pipes 13a-1, 13a-2, 13a-3, and relay stations 12a-1, 12a, respectively.
-2, 12a-3 are provided. That is, the relay stations are appropriately connected to the central processing unit 6 all at once. Beyond the relay station, each group of primary transport pipes 5a-1, 5a-2, and 5a-3 connects to the user's waste input port. 41 is a high-rise residential building,
42 is a single-family house. Reference numeral 43 indicates a location where a large amount of waste is generated, and such a location is directly connected to the branch secondary transportation pipe 13a-3 between the relay station 12a-3 and the central processing unit 6. Similarly, the secondary transport pipe 13b is branched secondary transport pipe 13b-
1 and 13b-2, each with relay station 1
Primary transport piping 5b via 2b-1, 12b-2
-1,5b-2 group connects to the user's garbage input port.

中継ステーシヨンは以上の説明では中継ステー
シヨンより中央処理装置のみへごみは輸送される
ものとしたが中継ステーシヨンにて選択的に中央
処理装置へ送ることができると共に中継ステーシ
ヨンにて集められたごみを搬出できるようにして
もよい。
In the above explanation, the relay station assumes that garbage is transported only from the relay station to the central processing unit, but it is also possible to selectively send the garbage to the central processing unit at the relay station, and also to carry out the garbage collected at the relay station. It may be possible to do so.

この場合のごみの収集は先ず中央処理装置6の
夫々の送風機は夫々二次輸送配管13a,13b
より空気のみを吸引するように中継ステーシヨン
12a―1を開閉弁17を開き、排出弁3を閉じ
てごみ収集状態にして一次輸送配管5a―1群の
夫々の管について順次中継ステーシヨン12a―
1にごみを集め終らせる。続いて中継ステーシヨ
ン12a―2を開閉弁17を開き、排出弁3を閉
じてごみ収集状態にして一次輸送配管5a―2群
の夫々の管について順次中継ステーシヨン12a
―2にごみを集積する。全く同様にして中継ステ
ーシヨン12a―3にごみを集積する。二次輸送
配管13bに連なる中継ステーシヨン12b―
1,12b―2についても同じくしてごみを集積
する。
In this case, garbage collection is performed by first using the blowers of the central processing unit 6 and the secondary transport pipes 13a and 13b, respectively.
The on-off valve 17 of the relay station 12a-1 is opened to suck only more air, and the discharge valve 3 is closed to set the garbage collection state to the relay station 12a-1 for each pipe of the primary transport pipe 5a-1 group.
1. Finish collecting the garbage. Next, the on-off valve 17 of the relay station 12a-2 is opened, and the discharge valve 3 is closed to set the garbage collection state to the relay station 12a for each pipe of the primary transport pipe 5a-2 group.
- Collect garbage in 2. Garbage is accumulated at the relay station 12a-3 in exactly the same manner. Relay station 12b connected to secondary transportation pipe 13b-
1 and 12b-2, garbage is accumulated in the same manner.

次に第3図でのべたようにして分離機19を通
じて二台の全送風機29a,29bを作動させて
中継ステーシヨン12a―1,12a―2,12
a―3,12b―1,12b―2の一つ宛の中継
ステーシヨン毎に中央処理装置6にごみを集め
る。
Next, as shown in FIG.
Garbage is collected in the central processing unit 6 for each relay station addressed to one of a-3, 12b-1, and 12b-2.

〔発明の効果〕〔Effect of the invention〕

本願第1発明は多数のごみ投入部を地域的に一
括してこれらに比較的近い地点に、ごみ出口側と
空気出口側とを選択的に中央処理装置と結び二次
輸送配管に接続可能な弁装置を備えた分離機を有
する共通の中継ステーシヨンを設置して、中継ス
テーシヨンを一次輸送配管により各ごみ投入部と
接続流通させ、各中継ステーシヨンを適宜一括し
て共通の中央処理装置に二次輸送配管により接続
して、各中継ステーシヨンに地域のごみ投入部で
捨てられるごみを一旦収集し、各中継ステーシヨ
ンに収集されたごみを中継ステーシヨンから中央
処理装置に二次輸送配管を通じて移送するように
したごみの空気輸送方法において、中央処理装置
は一つの分離機と、一つの分離機に見合う全能力
を持つと共にごみ投入地域から中継ステーシヨン
にごみを収集するに足る一部能力を出力する送風
機を備え、中央処理装置の送風機の一部能力でも
つて運転して、一つの二次輸送配管により連結さ
れている一つの中継ステーシヨンの空気出口に前
記弁装置により該二次輸送配管を接続してごみ投
入部から捨てられたごみを順次に各中継ステーシ
ヨンに収集し、次に二次輸送配管を一つの中継ス
テーシヨンに設けた分離機のごみ出口に接続し
て、中央処理装置の分離機を介在させて全能力で
送風機を運転し、一つの中継ステーシヨンに集め
られたごみを中央処理装置の分離機に移送するこ
とを各中継ステーシヨンについて順次行うことを
特徴とするごみの空気輸送方法としたから、中継
ステーシヨンへのごみの一次収集は中央処理装置
の送風機の一部能力により行われ、且つ二次輸送
配管における圧力損失が小さいから、ランニング
コストが低減される。又、中央処理装置の送風機
の能力を分けて複数の中継ステーシヨンへのごみ
の一次収集を同時に行うことが出来るのでごみの
収集が早い。更に又、中継ステーシヨンより中央
処理装置へ中継ステーシヨンにある限りのごみを
連続して輸送するから輸送効率がよく動力費がこ
の面からも節減される。
The first invention of the present application is capable of regionally bulking up a large number of garbage input sections, connecting the garbage outlet side and the air outlet side selectively to a central processing unit at a point relatively close to these units, and connecting them to secondary transportation piping. A common relay station with a separator equipped with a valve device will be installed, and the relay station will be connected to each waste input section through primary transport piping, and each relay station will be distributed in bulk to the common central processing unit as appropriate. Connected by transport piping, garbage discarded at the local waste input section is once collected at each relay station, and the garbage collected at each relay station is transferred from the relay station to the central processing unit through secondary transport piping. In the method of pneumatic transportation of waste, the central processing unit includes one separator and a blower that has the full capacity of one separator and a partial capacity that is sufficient to collect the waste from the waste input area to the transfer station. In addition, the blower of the central processing unit is operated at a partial capacity, and the secondary transport pipe is connected to the air outlet of one relay station connected by one secondary transport pipe by the valve device to collect waste. The waste discarded from the input section is sequentially collected at each relay station, and then the secondary transport pipe is connected to the waste outlet of the separator installed at one relay station, and the separator of the central processing unit is interposed. This pneumatic waste transportation method is characterized by operating the blower at full capacity and transferring the waste collected at one relay station to the separator of the central processing unit in turn for each relay station. The primary collection of garbage to the relay station is performed by a portion of the capacity of the blower of the central processing unit, and the pressure loss in the secondary transport piping is small, so running costs are reduced. Further, since the capacity of the blower of the central processing unit can be divided to perform the primary collection of garbage to a plurality of relay stations at the same time, the garbage can be collected quickly. Furthermore, since as much garbage as is present at the relay station is continuously transported from the relay station to the central processing unit, transportation efficiency is high and power costs are also reduced from this point of view.

本願第2発明は分離機と、一つの分離機に対し
て複数の送風機と、全送風機を分離機を介して二
次輸送配管に連通させるか、一部送風機を連通さ
せるかを行う配管とを備えた中央処理装置と、適
宜の中継ステーシヨンを一括して前記中央処理装
置に夫々連結された二次輸送配管と、各地域に配
された多数のごみ投入部と、各ごみ投入部を一括
して中継ステーシヨンに連結する一次輸送配管
と、一次輸送配管に空気入口が連結され、貯留排
出機を備えた分離機と、この分離機の貯留排出機
の出口と分離機の空気出口とに連結された二次輸
送配管に選択的に連結する弁装置とを備えた中継
ステーシヨンを備えてなり、二次輸送配管の断面
積に対して各一次輸送配管の断面積が中央処理装
置に接続された二次輸送配管の数をNとしたとき
ほぼ1/Nであることを特徴とするごみの空気輸
送装置としたから、上記本願第1発明の効果に加
えるに一次輸送配管の断面積を著しく細くするこ
とができ、総延長が最も長い一次輸送配管の建設
費を低減することができる。
The second invention of the present application includes a separator, a plurality of blowers for one separator, and piping that connects all the blowers to the secondary transportation piping via the separator, or connects some of the blowers to the secondary transportation piping. A central processing unit equipped with a central processing unit, secondary transportation pipes connected to the central processing unit, appropriate relay stations, a large number of garbage input units arranged in each region, and a plurality of garbage input units that collectively connect each garbage input unit. a separator having an air inlet connected to the primary transport piping and a storage discharger; an outlet of the storage discharger of the separator connected to an air outlet of the separator; a relay station equipped with a valve device selectively connected to the secondary transport pipes connected to the central processing unit; Since the pneumatic waste transport device is characterized in that the number of secondary transport pipes is approximately 1/N, the cross-sectional area of the primary transport pipes can be significantly reduced in addition to the effects of the first invention of the present application. Therefore, the construction cost of the primary transportation piping, which has the longest total length, can be reduced.

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

第1図は従来例のごみの輸送系の斜視図、第2
図は本発明のごみの輸送方法を示す配置図、第3
図は第2図における中央処理装置の機器の配置
図、第4図は一般化して示す本発明のごみの輸送
方法の斜視図である。 1……ダストシユート、2……投入口、3……
排出弁、4……貯留排出機、5a,5b……一次
輸送配管、6……中央処理装置、12a,12b
……中継ステーシヨン、13a,13b……二次
輸送配管、14……分離機、15……貯留排出
機、16……空気管、17……開閉弁、18……
排出弁、19……分離機、20……吸気弁、21
……貯留排出機、22a,22b……空気管、2
3a,23b……開閉弁、24a,24b……バ
グフイルタ、25a,25b……空気管、26
a,26b……開閉弁、27a,27b……空気
管、28a,28b……流量調整弁、29a,2
9b……送風機、31a,31b……空気吐出
管、32……脱臭器、33〜40……ローカル吸
気弁。
Figure 1 is a perspective view of a conventional waste transportation system;
The figure is a layout diagram showing the method of transporting waste according to the present invention.
This figure is a layout diagram of the equipment of the central processing unit in FIG. 2, and FIG. 4 is a perspective view of a generalized method of transporting waste according to the present invention. 1...Dust shoot, 2...Inlet, 3...
Discharge valve, 4...Storage discharge machine, 5a, 5b...Primary transport piping, 6...Central processing unit, 12a, 12b
... Relay station, 13a, 13b ... Secondary transport piping, 14 ... Separator, 15 ... Storage discharger, 16 ... Air pipe, 17 ... Opening/closing valve, 18 ...
Discharge valve, 19...Separator, 20...Intake valve, 21
... Storage and discharge machine, 22a, 22b ... Air pipe, 2
3a, 23b...Opening/closing valve, 24a, 24b...Bag filter, 25a, 25b...Air pipe, 26
a, 26b...Opening/closing valve, 27a, 27b...Air pipe, 28a, 28b...Flow rate adjustment valve, 29a, 2
9b...Blower, 31a, 31b...Air discharge pipe, 32...Deodorizer, 33-40...Local intake valve.

Claims (1)

【特許請求の範囲】 1 多数のごみ投入部を地域的に一括してこれら
に比較的近い地点に、ごみ出口側と空気出口側と
を選択的に中央処理装置と結ぶ二次輸送配管に接
続可能な弁装置を備えた分離機を有する共通の中
継ステーシヨンを設置して、中継ステーシヨンを
一次輸送配管により各ごみ投入部と接続流通さ
せ、各中継ステーシヨンを適宜一括して共通の中
央処理装置に二次輸送配管により接続して、各中
継ステーシヨンに地域のごみ投入部で捨てられる
ごみを一旦収集し、各中継ステーシヨンに収集さ
れたごみを中継ステーシヨンから中央処理装置に
二次輸送配管を通じて移送するようにしたごみの
空気輸送方法において、中央処理装置は一つの分
離機と、一つの分離機に見合う全能力を持つと共
にごみ投入地域から中継ステーシヨンにごみを収
集するに足る一部能力を出力する送風機を備え、
中央処理装置の送風機の一部能力でもつて運転し
て、一つの二次輸送配管により連結されている一
つの中継ステーシヨンの空気出口に前記弁装置に
より該二次輸送配管を接続してごみ投入部から捨
てられたごみを順次に各中継ステーシヨンに収集
し、次に二次輸送配管を一つの中継ステーシヨン
に設けた分離機のごみ出口に接続して、中央処理
装置の分離機を介在させて全能力で送風機を運転
し、一つの中継ステーシヨンに集められたごみを
中央処理装置の分離機に移送することを各中継ス
テーシヨンについて順次行うことを特徴とするご
みの空気輸送方法。 2 分離機と、一つの分離機に対して複数の送風
機と、全送風機を分離機を介して二次輸送配管に
連通させるか、一部送風機を連通させるかを行う
配管とを備えた中央処理装置と、適宜の中継ステ
ーシヨンを一括して前記中央処理装置に夫々連結
された二次輸送配管と、各地域に配された多数の
ごみ投入部と、各ごみ投入部を一括して中継ステ
ーシヨンに連結する一次輸送配管と、一次輸送配
管に空気入口が連結され、貯留排出機を備えた分
離機と、この分離機の貯留排出機の出口と分離機
の空気出口とに連結された二次輸送配管に選択的
に連通する弁装置とを備えた中継ステーシヨンを
備えてなり、二次輸送配管の断面積に対して各一
次輸送配管の断面積が中央処理装置に接続された
二次輸送配管の数をNとしたときほぼ1/Nであ
ることを特徴とするごみの空気輸送装置。
[Scope of Claims] 1. A large number of garbage input sections are connected to a point relatively close to them regionally to a secondary transportation pipe that selectively connects the garbage outlet side and the air outlet side to the central processing unit. A common relay station with a separator equipped with a suitable valve device is installed, and the relay station is connected and distributed to each waste input section by a primary transport piping, and each relay station is appropriately batched and connected to a common central processing unit. Connected by secondary transport piping, each relay station temporarily collects the garbage discarded at the local waste input section, and transports the garbage collected at each relay station from the relay station to the central processing unit through the secondary transport piping. In the pneumatic waste transportation method, the central processing unit outputs one separator and a full capacity corresponding to one separator, and a partial capacity sufficient to collect the waste from the waste input area to the transfer station. Equipped with a blower,
The air blower of the central processing unit is operated at a partial capacity, and the secondary transport pipe is connected to the air outlet of one relay station connected by one secondary transport pipe by the valve device, and the waste input section is connected. The waste discarded from the central processing unit is collected sequentially at each relay station, and then the secondary transport pipe is connected to the waste outlet of the separator installed at one relay station, and all waste is collected through the separator of the central processing unit. A method for pneumatic transport of waste characterized by operating a blower at its maximum capacity and sequentially transferring waste collected at one relay station to a separator of a central processing unit for each relay station. 2 Central processing equipped with a separator, multiple blowers for one separator, and piping that connects all the blowers to the secondary transport piping via the separator, or connects some of the blowers to the secondary transport piping. The device, a secondary transportation pipe that connects the appropriate relay station to the central processing unit, a large number of garbage input units arranged in each region, and a relay station that connects each garbage input unit to the central processing unit. a separator with an air inlet connected to the primary transport pipe and a storage discharger; a secondary transport connected to the storage discharger outlet of the separator and the air outlet of the separator; a relay station equipped with a valve device that selectively communicates with the pipes, the cross-sectional area of each primary transport pipe being equal to the cross-sectional area of the secondary transport pipe connected to the central processing unit; A pneumatic waste transport device characterized in that the number is approximately 1/N.
JP5684881A 1981-04-15 1981-04-15 Method and device for pneumatically transporting dust Granted JPS57170301A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5684881A JPS57170301A (en) 1981-04-15 1981-04-15 Method and device for pneumatically transporting dust

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5684881A JPS57170301A (en) 1981-04-15 1981-04-15 Method and device for pneumatically transporting dust

Publications (2)

Publication Number Publication Date
JPS57170301A JPS57170301A (en) 1982-10-20
JPS646084B2 true JPS646084B2 (en) 1989-02-02

Family

ID=13038830

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5684881A Granted JPS57170301A (en) 1981-04-15 1981-04-15 Method and device for pneumatically transporting dust

Country Status (1)

Country Link
JP (1) JPS57170301A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0415288U (en) * 1990-05-25 1992-02-06

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60242103A (en) * 1984-05-15 1985-12-02 三菱重工業株式会社 Vacuum conveying system of dust
JPH05132107A (en) * 1991-11-13 1993-05-28 Nkk Corp Air transport equipment for garbage
JPH05162809A (en) * 1991-12-17 1993-06-29 Nkk Corp Pneumatic transport facility for refuse
KR101049766B1 (en) 2008-12-16 2011-07-19 엔백 주식회사 Relay system that does not emit exhaust gas
FI20106150A0 (en) * 2010-11-03 2010-11-03 Maricap Oy Method and pneumatic material transfer system

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5711924Y2 (en) * 1976-11-26 1982-03-09
JPS5943288Y2 (en) * 1977-06-20 1984-12-21 石川島播磨重工業株式会社 Constant air flow control device for pneumatic conveyance equipment
JPS5416358A (en) * 1977-07-07 1979-02-06 Masaichi Kitagawa Super table roller

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0415288U (en) * 1990-05-25 1992-02-06

Also Published As

Publication number Publication date
JPS57170301A (en) 1982-10-20

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