JPH0940179A - Gas carrier - Google Patents
Gas carrierInfo
- Publication number
- JPH0940179A JPH0940179A JP19230495A JP19230495A JPH0940179A JP H0940179 A JPH0940179 A JP H0940179A JP 19230495 A JP19230495 A JP 19230495A JP 19230495 A JP19230495 A JP 19230495A JP H0940179 A JPH0940179 A JP H0940179A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- path
- transport
- transfer
- transport path
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Air Transport Of Granular Materials (AREA)
- Combined Means For Separation Of Solids (AREA)
Abstract
(57)【要約】
【目的】 被搬送物が焼却残渣の如き、易気体搬送物と
難気体搬送物とが混合された状態にあるものでも、その
搬送状態にあって、難気体搬送物を易気体搬送物から分
離するとともに、所望の搬送終点まで易気体搬送物を気
体搬送でき、さらに、気体搬送を極めて簡単な構成で達
成できる気体搬送装置を得る。
【構成】 搬送起点より被搬送物を分離部12に導く起
点側搬送路11と、分離部12において分離される易気
体搬送物を搬送終点まで搬送する第1搬送路13と、分
離部12において分離される難気体搬送物を回収部7ま
で搬送する第2搬送路14とを備え、第2搬送路14
を、水平方向より傾いた傾斜姿勢に構成するとともに、
第2搬送路14の上端側に第1搬送路13の下端側を接
続して、接続部近傍を分離部12として構成し、第1搬
送路13の搬送終点側に、気体搬送用の吸引流を誘起す
る吸引機構16を備える。
(57) [Summary] [Purpose] Even if the object to be conveyed is in a state in which an easily gas-carrying substance and a difficult gas-carrying substance are mixed, such as incineration residue, even if the substance is in the carrying state, (EN) A gas transfer device that separates from an easy gas transfer object and can transfer the easy gas transfer object to a desired transfer end point, and further achieves gas transfer with an extremely simple configuration. [Structure] A starting point side conveying path 11 for guiding an object to be conveyed to a separating section 12 from a conveying starting point, a first conveying path 13 for conveying an easily gas conveyed object separated in the separating section 12 to a conveying end point, and a separating section 12 The second transport path 14 for transporting the separated difficult-gas transport material to the recovery unit 7, and the second transport path 14
Is configured in a tilted posture that is inclined from the horizontal direction,
The lower end side of the first transfer path 13 is connected to the upper end side of the second transfer path 14 to configure the separation part 12 in the vicinity of the connection part, and the suction flow for gas transfer is provided on the transfer end side of the first transfer path 13. The suction mechanism 16 for inducing
Description
【0001】[0001]
【産業上の利用分野】本発明は、固体粉粒体よりなる被
搬送物を搬送起点から搬送終点まで気体搬送する気体搬
送装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas transfer device for transferring an object to be transferred, which is made of solid particles, from a transfer start point to a transfer end point by gas.
【0002】[0002]
【従来の技術】従来、この種の気体搬送装置において
は、被搬送物は、例えば粒度等が一定の範囲内に入るも
のからなっており、被搬送物の全量を、搬送起点から搬
送終点まで搬送するように構成されている。2. Description of the Related Art Conventionally, in this type of gas transfer device, the transferred object is composed of particles having a granularity within a certain range, and the total amount of transferred object is from the starting point to the ending point. It is configured to be transported.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、気体搬
送をおこないたい固体粉粒体よりなる被搬送物として、
気体搬送が容易な易気体搬送物と気体搬送が困難な難気
体搬送物が混在した状態にある被搬送物から、易気体搬
送物のみを分離して搬送終点まで気体搬送する必要があ
る場合がある。この様な搬送の例としては、ゴミ焼却炉
でゴミ焼却処理により生成される焼却残渣を、溶融処理
のために溶融炉に導く場合を挙げることができる。従
来、このような搬送系においては、クリンカ、カン、金
属固形物、石等の分離を、これら専用の篩い等の機械式
分離装置によっておこない、上記以外の残留物をコンベ
ア等で溶融炉に導いていた。焼却残渣に含まれる易気体
搬送物としては、焼却灰等を挙げることができ、難気体
搬送物としては、比較的大粒のクリンカ、カン等、さら
には、比較的粒度は小さいものの気体搬送には不向きな
金属固形物、石等を挙げることができる。このような易
気体搬送物と難気体搬送物とは、気体搬送性を異にする
搬送物と言えるが、比重や形状を等しくする粉粒体にあ
っては、粒径が大きくなるに従って難気体搬送性とな
る。また、形状、粒径の等しいものについては、比重が
大きい程難気体搬送性となる。これらを、焼却炉に備え
られる灰ピットから、溶融炉に、比較的簡便で有用な搬
送技術である気体搬送で導こうとすると、上述の難気体
搬送物を分離しながら、焼却灰を炉側に導く必要が生じ
る。しかしながら、従来、このような分離機能と気体搬
送機能とを共に、比較的簡単な機構構成で実現するもの
はなく、比較的複雑で高価な装置系でしか、これを実現
できなかった。図3に、従来のゴミ焼却残渣の分離・搬
送システムの構成を示した。同図に示すように、システ
ムは、焼却残渣200等の原料を供給する供給コンベア
111の搬出側に篩い112付の分離用ホッパー113
を備え、このホッパー113の排出側に振動フィーダ1
14等を備えて、焼却灰を主成分とする易気体搬送物を
所定部(図3に示す場合はホッパー116)に導いてい
た。さらに、篩い112によって分離された分離物は、
別途、所定の集積部115に集積処理される構造が取ら
れていた。この構造においては、上記の問題の他、比較
的目の詰まった篩いを用いる必要があるため、目詰まり
の問題、さらに、焼却残渣は篩いの金網を磨耗しやす
く、搬送システムに問題を発生しやすい等の問題があっ
た。従って、本発明の目的は、例え、被搬送物が焼却残
渣の如き、易気体搬送物と難気体搬送物とが混合された
状態にあるものであっても、その搬送状態にあって、難
気体搬送物を易気体搬送物から分離するとともに、所望
の搬送終点まで易気体搬送物を気体搬送でき、さらに、
気体搬送を極めて簡単な構成で達成できる気体搬送装置
を得ることにある。However, as an object to be conveyed, which is made of solid powder or granules for which gas is desired to be conveyed,
In some cases, it may be necessary to separate only the easy-to-gas carrier from the transferred object in a state where the easily-to-be-carried easy-to-carry carrier and the difficult-to-carry difficult-to-carry carrier are mixed to carry the gas to the end point. is there. An example of such transportation is a case where the incineration residue produced by the refuse incineration process in the refuse incinerator is guided to the melting furnace for the melting process. Conventionally, in such a transport system, separation of clinker, can, metal solids, stones, etc. is carried out by a mechanical separation device such as a dedicated sieve, and the residue other than the above is introduced into a melting furnace by a conveyor or the like. Was there. Examples of easy-gas carriers contained in the incineration residue include incineration ash, and as difficult-gas carriers, relatively large-sized clinker, can, etc. Unsuitable metal solids, stones and the like can be mentioned. It can be said that such an easy-gas carrier and a difficult-gas carrier are carriers having different gas-transporting properties, but in the case of a powder or granular material having the same specific gravity and shape, the gas-resistant carrier becomes difficult as the particle size increases. It becomes transportable. Further, for those having the same shape and particle size, the larger the specific gravity is, the more difficult the gas is to be transported. When trying to introduce these from the ash pit provided in the incinerator to the melting furnace by gas transport, which is a relatively simple and useful transport technology, the incinerator ash is separated from the incinerator ash while separating the above-mentioned difficult-to-gas transport products. Need to lead to. However, heretofore, there has been no implementation of both the separation function and the gas transfer function with a relatively simple mechanical structure, and this can be achieved only with a relatively complicated and expensive device system. Fig. 3 shows the configuration of a conventional waste incineration residue separating / transporting system. As shown in the figure, the system includes a separation hopper 113 having a sieve 112 on the carry-out side of a supply conveyor 111 that supplies raw materials such as incineration residue 200.
And a vibration feeder 1 on the discharge side of the hopper 113.
It was equipped with 14 grade | etc., And guided the easy-gas conveyance material which has incineration ash as a main component to the predetermined part (the hopper 116 in the case shown in FIG. 3). Further, the separated substance separated by the sieve 112 is
Separately, a structure is adopted in which a predetermined stacking unit 115 performs a stacking process. In this structure, in addition to the above problems, it is necessary to use a sieve that is relatively clogged, so there is a problem of clogging, and incineration residue easily wears the wire mesh of the sieve, causing problems in the transport system. There was a problem that it was easy. Therefore, an object of the present invention is that even if the transported object is in a state where the easily gas-transported material and the difficult-gas-transported material are mixed, such as incineration residue, it is difficult to carry in the transportation state. In addition to separating the gas carrier from the easy gas carrier, the easy gas carrier can be transported to the desired transport end point.
An object of the present invention is to obtain a gas transfer device that can achieve gas transfer with an extremely simple structure.
【0004】[0004]
【課題を解決するための手段】この目的を達成するため
の本発明による請求項1に係わる気体搬送装置の特徴構
成は、被搬送物に、気体搬送が容易な易気体搬送物と困
難な難気体搬送物が含まれる場合に、搬送起点より被搬
送物を分離部に導く起点側搬送路と、分離部において分
離される易気体搬送物を搬送終点まで搬送する第1搬送
路と、分離部において分離される難気体搬送物を回収部
まで搬送する第2搬送路とを備え、第2搬送路を、水平
方向より傾いた傾斜姿勢に構成するとともに、第2搬送
路の上端側に第1搬送路の下端側を接続して、接続部近
傍を分離部として構成し、第1搬送路の搬送終点側に、
気体搬送用の吸引流を誘起する吸引機構を備えたことに
ある。さらに、前記請求項1に係わる気体搬送装置の特
徴構成において、水平方向に対して傾斜して配設される
単一の直管の中間部位に、前記起点側搬送路を接続し、
接続部近傍を前記分離部として構成するとともに、前記
分離部より下側に位置する直管部を前記第2搬送路とし
て、前記分離部より上側に位置する直管部を前記第1搬
送路として構成することが好ましい。これが、本願の請
求項2に係わる気体搬送装置の特徴構成である。さら
に、請求項1または請求項2に係わる気体搬送装置にお
いて、吸引機構に吸引流の流量を設定自在な流量設定機
構を備えることがさらに好ましい。これが、本願の請求
項3に係わる気体搬送装置の特徴構成である。さらに、
請求項1、2、または3に係わる気体搬送装置におい
て、前記被搬送物が、前記易気体搬送物としての焼却灰
を含む焼却残渣であることが好ましい。これが、請求項
4に係わる気体搬送装置の特徴構成である。そして、そ
れらの作用・効果は次の通りである。In order to achieve this object, the characteristic structure of the gas transfer device according to claim 1 according to the present invention is that an object to be transferred is an easy gas transfer object and a difficult gas transfer object. When a gas carrier is included, a starting-side carrier path that guides the transferred object from the carrier start point to the separation unit, a first carrier path that carries the easily gas-carried object separated in the separation unit to the carrier end point, and a separation unit And a second transport path for transporting the difficult-to-gas transported material separated to the collecting section, the second transport path is configured in an inclined posture inclined from the horizontal direction, and the first transport path is provided on the upper end side of the first transport path. By connecting the lower end side of the conveying path, the vicinity of the connecting portion is configured as a separating portion, and the conveying end point side of the first conveying path is
There is a suction mechanism for inducing a suction flow for gas transportation. Further, in the characteristic configuration of the gas transfer device according to claim 1, the starting point side transfer path is connected to an intermediate portion of a single straight pipe that is arranged to be inclined with respect to the horizontal direction,
The vicinity of the connection portion is configured as the separation portion, the straight pipe portion positioned below the separation portion is used as the second transport path, and the straight pipe portion positioned above the separation portion is used as the first transport path. It is preferable to configure. This is the characteristic configuration of the gas transfer device according to claim 2 of the present application. Further, in the gas transfer device according to claim 1 or 2, it is further preferable that the suction mechanism is provided with a flow rate setting mechanism capable of setting the flow rate of the suction flow. This is a characteristic configuration of the gas transfer device according to claim 3 of the present application. further,
In the gas transfer device according to claim 1, 2, or 3, it is preferable that the transferred object is an incineration residue containing incinerated ash as the easy-gas transfer object. This is a characteristic configuration of the gas transfer device according to claim 4. The actions and effects thereof are as follows.
【0005】[0005]
【作用】つまり、本願の請求項1に係わる気体搬送装置
においては、被搬送物は分離部まで起点側搬送路を介し
て、易気体搬送物と難気体搬送物とが混在したまま、搬
送されてくる。そして、分離部に到った被搬送物の内、
気体搬送が容易な易気体搬送物は、吸引機構により生成
される第1搬送路内の気体搬送流に乗って、搬送終点ま
で導かれる。一方、難気体搬送物は、傾斜姿勢にある第
2搬送路内を下方に落下し、回収部に回収される。ここ
では、第2搬送路が水平方向に対して傾斜姿勢に構成さ
れるとともに、吸引機構が第1搬送路の搬送終点側に位
置されることにより、上記の分離機能と搬送機能を共に
達成することができる。さらに、本願の請求項2に係わ
る気体搬送装置においては、単一直管の中間部位に起点
側搬送路が接続されて、この接続部位より上部側の部位
が前述の第1搬送路として、下部側の部位が前述の第2
搬送路として構成される。当然、この直管は水平に対し
て傾いて配設され、前述の分離機能と搬送機能を果たせ
る。さらに、単一の直管のみにより第1搬送路、第2搬
送路を構成することができるため、構成が簡単となると
ともに、搬送物の滞留、詰まり等の問題を起こすことも
ない。さらに、本願の請求項3に係わる気体搬送装置に
おいては、吸引機構に、その吸引流量が設定自在な流量
設定機構が備えられる。先に説明したように、基本的に
は吸引流により易気体搬送物が搬送終点側へ、難気体搬
送物を回収部へ導くことが可能となっているが、装置に
投入される被搬送物の性状は変化する。本願装置に於け
る易気体搬送物と難気体搬送物との区分けは、吸引流の
流量に依存する。従って、この項に係わる気体搬送装置
にあっては、例えば、被搬送物として比較的気体搬送が
容易な軽量の灰に、小さな金属固形物が多い場合は、そ
の吸引流量を低下設定して、灰のみを効率的に分離搬送
する。一方、被搬送物として比較的重量のある灰に、比
較的大粒の石を含む場合は、その吸引流量を多めに設定
して、効率的な分離搬送をおこなうのである。即ち、こ
の流量設定機構により、吸引流の流量を易気体搬送物を
気体搬送でき、難気体搬送物を搬送しえない流量に適切
に設定して、被搬送物の分離と搬送を良好に、行い得る
のである。さらに、請求項4に係わる気体搬送装置にお
いては、焼却残渣を取り扱う場合に、容易に気体搬送可
能な易気体搬送物としての焼却灰等を、前述した、クリ
ンカ、石、罐等から分離して、例えば溶融炉に導いて、
所定の用に供することができる。That is, in the gas transfer device according to the first aspect of the present application, the transferred object is transferred to the separation section via the starting side transfer path while the easy-gas transferred object and the difficult-gas transferred object are mixed. Come on. Then, of the transported objects that have reached the separation unit,
The easily-gas-transported material, which facilitates gas transport, is guided to the transport end point by riding on the gas-transport flow in the first transport path generated by the suction mechanism. On the other hand, the difficult-to-gas carrier material falls downward in the inclined second carrier path and is recovered by the recovery unit. Here, the second transport path is configured to be inclined with respect to the horizontal direction, and the suction mechanism is located on the transport end point side of the first transport path, thereby achieving both the above-described separation function and transport function. be able to. Further, in the gas conveying device according to claim 2 of the present application, the starting side conveying path is connected to the intermediate portion of the single straight pipe, and the portion above the connecting portion is the above-mentioned first conveying passage and the lower side. Is the second part
It is configured as a transport path. As a matter of course, this straight pipe is disposed so as to be inclined with respect to the horizontal, and can perform the above-mentioned separating function and carrying function. Furthermore, since the first transport path and the second transport path can be configured by using only a single straight pipe, the configuration is simple and problems such as retention and clogging of transported objects do not occur. Further, in the gas transfer device according to claim 3 of the present application, the suction mechanism is provided with a flow rate setting mechanism capable of setting the suction flow rate. As described above, basically, it is possible to guide the easily gas-carrying object toward the end point of the carrier and the difficult-gas-carrying object to the recovery part by the suction flow, but the object to be conveyed to the apparatus is transferred. The nature of changes. The easy gas carrier and the difficult gas carrier in the device of the present application are distinguished from each other depending on the flow rate of the suction flow. Therefore, in the gas transfer device according to this section, for example, when a small amount of small metal solids is contained in light ash that is relatively easy to transfer as an object to be transferred, the suction flow rate is set to be low, Efficiently separates and transports only ash. On the other hand, when ash, which is relatively heavy as a material to be transported, contains relatively large-sized stones, the suction flow rate is set to a large amount for efficient separation and transportation. That is, by this flow rate setting mechanism, the flow rate of the suction flow can be set to a flow rate at which an easily gas-carrying object can be carried by a gas, and a difficult-gas-carrying object cannot be carried, and the separation and the carrying of the carried object can be carried out well, It can be done. Furthermore, in the gas transfer device according to claim 4, when handling incineration residue, incinerator ash or the like as an easily gas transfer material that can easily transfer gas is separated from the above-mentioned clinker, stone, canister, etc. , Leading to, for example, a melting furnace,
It can be used for a predetermined purpose.
【0006】[0006]
【発明の効果】従って、たとえ、被搬送物が焼却残渣の
如き、易気体搬送物と難気体搬送物とが混合された状態
にあるものであっても、被搬送物から、その搬送状態に
あって、難気体搬送物を分離するとともに、所望の搬送
終点まで易気体搬送物を気体搬送できる気体搬送装置を
得ることができた。ここで、固体粉粒体を含んだ排ガス
等から固体粉粒体を分離して排ガスのみを、搬送下手側
へ送るサイクロンとの比較をすると、サイクロンは分離
部において主に、遠心力により固体粉粒体を分離するも
のであり、本願は、基本的には吸引流の搬送能力に依存
した分離をおこなうものであることが異なる。そして、
本願のほうが、格段に構造が簡単である。そして、請求
項2に係わる構成を採用する場合は、単一直管で第1、
第2搬送路を構成するため、装置構成が、大幅に簡略化
されるとともに、メンテナンス容易で、詰まり等の問題
を起こし難い効果を備えることとなる。さらに、請求項
3に係わる構成を採用する場合は、被搬送物の状態に応
じて吸引流の流量を適切に設定しながら、所望の分離、
搬送機能を発揮できるようになった。さらに、請求項4
に係わる構成を採用する場合は、焼却残渣の取扱が容易
となった。Therefore, even if the transported object is in a state in which the easily gas-transported material and the difficult gas-transported material are mixed, such as incineration residue, the transported object is changed to the transportation state. Therefore, it is possible to obtain a gas transfer device that can separate the difficult-to-gas transferred product and can transfer the easily-transferred gas to the desired transfer end point. Here, when the solid powder and granules are separated from the exhaust gas containing the solid powder and granules, and only the exhaust gas is compared with a cyclone that sends the lower side of the conveyance, the cyclone mainly separates solid powder by centrifugal force. The present application is different in that the present invention basically separates the particles, and the present invention basically separates the particles depending on the conveying ability of the suction flow. And
The structure of the present application is remarkably simple. When the configuration according to claim 2 is adopted, the first straight pipe is used for the first,
Since the second transport path is configured, the device configuration is greatly simplified, maintenance is easy, and problems such as clogging are unlikely to occur. Furthermore, when the configuration according to claim 3 is adopted, the desired separation, while appropriately setting the flow rate of the suction flow according to the state of the transported object,
The transport function can now be demonstrated. Claim 4
When adopting the configuration related to, it became easier to handle the incineration residue.
【0007】[0007]
【実施例】ゴミ焼却炉1で生成される焼却残渣を、焼却
炉1から溶融炉2まで搬送する場合に、本願の気体搬送
装置3を使用する場合について、図1に基づいて説明す
る。この例の場合は、被搬送物としてのゴミ焼却残渣
は、灰コンベア4によって装置の入口5部位(この部位
が実質上搬送起点となっている)に投入され、装置を経
た後、クリンカ、カン等が回収される第1回収部6、金
属、石等の小型固形物が回収される第2回収部7と溶融
炉2に投入される焼却灰等が搬送回収されるホッパー8
(この部位が実質上搬送終点となっている)との3ケ所
に、夫々、分離されて搬送、回収される。EXAMPLE A case where the gas transfer device 3 of the present application is used to transfer an incineration residue generated in the refuse incinerator 1 from the incinerator 1 to the melting furnace 2 will be described with reference to FIG. In the case of this example, the refuse incineration residue as the transported object is put into the entrance 5 part of the device (this part is substantially the starting point of the transfer) by the ash conveyor 4 and, after passing through the device, the clinker and the can. And the like, a second recovery unit 7 for recovering small solids such as metals and stones, and a hopper 8 for transporting and recovering incineration ash and the like to be charged into the melting furnace 2.
(This part is substantially the end point of the conveyance) are separated and conveyed and collected respectively.
【0008】以下、さらに詳細に装置の構成について、
被搬送物であるゴミ焼却残渣の移動経路に沿って説明す
る。図1に示すように、気体搬送装置3は、投入路9、
分離装置10、下降傾斜路として構成される起点側搬送
路11、分離部12、第1搬送路13、ホッパー8を、
灰の搬送順路に沿って備えている。前記分離装置10の
下手には前述の第1回収部6が備えられている。前記分
離部12の下手には、第2搬送路14を介して前述の第
2回収部7が備えられている。ここで、第2回収部7
は、図示するように閉構造の箱として構成されており、
金属、石等の小型固形物が底面側に回収される。さら
に、この部位には、前記第2搬送路14とは別に、気体
取り入れ口15が設けられており、この気体搬送装置3
に備えられる吸引機構(具体的には吸引ブロア16)に
よって、この気体取り入れ口15から、第2回収部7、
第2搬送路14、第1搬送路13、吸引ブロア16に渡
る搬送流が誘起される。この吸引ブロア16には、流量
設定用のダンパ16aが備えられており、このダンパ1
6aにより搬送流量は、第1搬送路13において前述の
易気体搬送物である焼却灰等を、小径のクリンカ、石、
金属等から分離して、この路13を介してホッパ8側に
搬送できる量に設定される。従って、このダンパ16a
は、流量設定機構となっている。こういった流量設定機
構としては、吸引ブロア16の回転数設定機構(図外)
も、この役割を果たす。ここで、吸引ブロア16の代わ
りに、吹き込み型のブロアを、例えば、図1に於けるA
部位に設けることも可能である。ただし、この構造を採
用する場合は、起点側搬送路11に於ける搬送状態を不
安定にしたり、ゴミ焼却残渣に含まれる埃等を装置外に
吹き出す等の問題を生じる場合もあり、前記の吸引型の
ものが好ましい。In more detail, the structure of the apparatus will be described below.
A description will be given along the moving route of the refuse incineration residue that is the transported object. As shown in FIG. 1, the gas transfer device 3 includes a charging path 9,
The separating device 10, the starting-side conveying path 11 configured as a descending inclined path, the separating section 12, the first conveying path 13, and the hopper 8,
It is provided along the ash transport route. The first recovery unit 6 is provided below the separating device 10. Below the separation unit 12, the above-mentioned second recovery unit 7 is provided via the second transport path 14. Here, the second recovery unit 7
Is configured as a closed box as shown in the figure,
Small solids such as metals and stones are collected on the bottom side. Further, a gas intake port 15 is provided in this portion in addition to the second transfer passage 14, and this gas transfer device 3
The suction mechanism (specifically, the suction blower 16) provided in the
A carrier flow across the second carrier path 14, the first carrier path 13, and the suction blower 16 is induced. The suction blower 16 is equipped with a damper 16a for setting the flow rate.
The transport flow rate by 6a is such that incineration ash, which is the above-mentioned easy-gas transport product, in the first transport path 13, a small-diameter clinker, stone,
The amount is set so that it can be separated from metal or the like and conveyed to the hopper 8 side through this path 13. Therefore, this damper 16a
Is a flow rate setting mechanism. As such a flow rate setting mechanism, a rotation speed setting mechanism of the suction blower 16 (not shown)
Also plays this role. Here, instead of the suction blower 16, a blower type blower, for example, A in FIG.
It is also possible to provide it in a part. However, when this structure is adopted, there may be a problem that the transportation state in the starting point side transportation path 11 becomes unstable, and dust or the like contained in the refuse incineration residue is blown out of the apparatus. The suction type is preferable.
【0009】前記第1搬送路13は、前記分離部12の
上部側に備えられており、上部側に位置する搬送終点側
に、バクフィルター17を備えた鉛直拡大筒状部18を
備えている。そして、前記バグフィルター17の下流側
に、前述の吸引ブロア16が備えられている。前記鉛直
拡大筒状部18の下部位置には、溶融炉2に接続される
ホッパー8が備えられている。図示するように、前述の
第1搬送路13と第2搬送路14とは、水平方向に対し
て傾斜して配設される単一の直管100に於ける特定の
部位として構成されており、この単一直管100の中間
部位に、起点側搬送路11が接続され、この接続部近傍
が分離部12として構成されている。従って、分離部1
2より下側に位置する直管部が前記第2搬送路14とし
て、分離部12より上側に位置する直管部が第1搬送路
13として構成されている。The first conveying path 13 is provided on the upper side of the separating section 12, and the vertically enlarged cylindrical portion 18 having the back filter 17 is provided on the conveying end point side located on the upper side. . The suction blower 16 is provided downstream of the bag filter 17. A hopper 8 connected to the melting furnace 2 is provided at a lower position of the vertically enlarged cylindrical portion 18. As shown in the figure, the above-described first transport path 13 and second transport path 14 are configured as specific portions in a single straight pipe 100 that is arranged so as to be inclined with respect to the horizontal direction. The starting side conveying path 11 is connected to an intermediate portion of the single straight pipe 100, and the vicinity of this connecting portion is configured as a separating portion 12. Therefore, the separation unit 1
The straight pipe portion located below 2 is configured as the second transport path 14, and the straight pipe portion located above the separation unit 12 is configured as the first transport path 13.
【0010】以下、本願の気体搬送装置に、ゴミ焼却残
渣を投入した場合の動作について説明する。気体搬送装
置3を運転する状態においては、吸引ブロア16は運転
状態に維持される。気体搬送装置入口5より投入された
ゴミ焼却残渣は、分離装置10上に落下して分散され、
大径のクリンカ、カン等が第1回収部6に回収される。
分離装置10を通過した通過物は、起点側搬送路11を
経て分離部12に導かれる。分離部12に到った被搬送
物の内、気体搬送が容易な焼却灰等は、第1搬送路13
を上昇移動し、鉛直拡大筒状部18に到達する。ここ
で、比較的重量のある焼却灰はホッパー8内に落下、堆
積する。一方、非常に微細な埃等は、バクフィルター1
7に補足される。さらに、分離部12において、小型の
粒状物ではあるものの比較的重量のある金属、石等の難
気体搬送物は、第2搬送路14を落下し、第2回収部7
に回収される。また、このような金属、石等に付着して
いる焼却灰等も、これらの落下に伴って、金属、石等か
ら分離されるため、本願の装置においては充分な分離機
能を発揮できる。The operation when the refuse incineration residue is put into the gas transfer device of the present application will be described below. When the gas transfer device 3 is in operation, the suction blower 16 is maintained in operation. The waste incineration residue introduced from the gas transfer device inlet 5 is dropped and dispersed on the separation device 10,
Large-sized clinker, can, etc. are recovered by the first recovery unit 6.
The passing matter that has passed through the separation device 10 is guided to the separation unit 12 via the starting point side transport path 11. Among the transported objects that have reached the separation unit 12, the incinerated ash or the like, which is easily transported by gas, is transferred to the first transportation path 13
To reach the vertically enlarged cylindrical portion 18. Here, the relatively heavy incinerated ash falls and accumulates in the hopper 8. On the other hand, very fine dust, etc.
7 is supplemented. Further, in the separating unit 12, a relatively heavy gas, such as metal or stone, which is a small granular material but relatively heavy, falls through the second conveying path 14, and the second collecting unit 7
Will be collected. In addition, incineration ash and the like adhering to such metals and stones are also separated from the metals and stones when they fall, so that the apparatus of the present invention can exhibit a sufficient separation function.
【0011】〔別実施例〕本願の別実施例を以下に説明
する。 (イ) 上記の実施例においては、ゴミ焼却残渣を処理
する場合に、起点側搬送路11の入口部位に分離装置1
0を備えて気体搬送装置を構成したが、大型のクリン
カ、カン等が混入され難い場合は、図2に示すような構
成とすることができる。図示する例は、先に示した従来
技術に対応したシステムを構成した例である。この例の
場合は、ゴミ焼却残渣が、原料受けホッパー21に投入
された後、振動フィダー22によって定量毎に切りわけ
られて、鉛直方向に配設される起点側搬送路11に送り
込まれる。この搬送路11の下端部が前述の実施例と同
様に分離部12とされている。そして、この分離部12
よりも下部に位置する配管部が第2搬送路14を、上部
に位置する配管部が第1搬送路13を構成している。第
2搬送路14は、水平方向から傾斜して配設されてい
る。第2搬送路14の下部には、分離物受けホッパー2
3が備えられるとともに、第1搬送路13の下流側にバ
グフィルター17を備えたホッパー8が備えられてい
る。この場合もまた、搬送吸引用の吸引ブロアー16及
び流量設定用のダンパ16aが備えられている。さら
に、第2搬送路14の上部側に振動装置24が備えら
れ、この部位14に堆積することがある難気体搬送物の
分離物受けホッパー23側へ落下を促進する構造が採用
されている。[Other Embodiment] Another embodiment of the present application will be described below. (A) In the above-mentioned embodiment, when treating the refuse incineration residue, the separation device 1 is installed at the inlet of the starting side transport path 11.
Although the gas transfer device is configured by including 0, if it is difficult to mix a large clinker, a can, or the like, the gas transfer device can be configured as shown in FIG. The illustrated example is an example in which the system corresponding to the above-described conventional technique is configured. In the case of this example, after the waste incineration residue is put into the raw material receiving hopper 21, it is cut into a fixed amount by the vibrating feeder 22 and sent to the starting point side conveying path 11 arranged in the vertical direction. The lower end of the transport path 11 serves as a separating section 12 as in the above-described embodiment. Then, this separating unit 12
The pipe portion located at the lower portion constitutes the second transport passage 14, and the pipe portion located at the upper portion constitutes the first transport passage 13. The second transport path 14 is arranged so as to be inclined from the horizontal direction. At the bottom of the second transport path 14, the separated material receiving hopper 2 is provided.
3 is provided, and a hopper 8 having a bag filter 17 is provided downstream of the first transport path 13. Also in this case, a suction blower 16 for carrying suction and a damper 16a for setting the flow rate are provided. Further, a vibrating device 24 is provided on the upper side of the second transport path 14, and a structure is adopted to promote the falling of the difficult-gas-transported product that may be deposited on this portion 14 toward the separated product receiving hopper 23 side.
【0012】(ロ) 上記の実施例においては、第1搬
送路と第2搬送路の主要部を、共に、傾斜配置される直
管の一部部位として構成したが、両者の傾斜度は異なっ
ていてもよい。即ち、分離したい易気体搬送物と難気体
搬送物との関係において、充分な気体搬送状態が得られ
るように、第1搬送路を比較的穏やかな傾斜姿勢(比較
的水平に近い)に、第2搬送路を大きな傾斜姿勢(比較
的鉛直に近い)に設定してもよい。この場合は、被搬送
物に含まれる物の性状に対応して、各路の傾斜度を変更
することにより、吸引ブロアの能力を充分引き出せる搬
送構造を得ることができる。 (ハ) 上記の実施例においては、起点側搬送路の入口
部位に分離装置を設けて、大粒物の除去をおこなった
が、こういった分離装置の他に、分離装置としては、目
皿や格子状の篩等の機械式分離装置を備えておいてもよ
い。さらに、この設置位置としては、分離部に対して、
その上流側であれば、いかなる位置にあってもよい。(B) In the above embodiment, both the main parts of the first and second conveying paths are constructed as a part of the straight pipe which is arranged in an inclined manner, but the inclination degrees of both are different. May be. That is, in order to obtain a sufficient gas transfer state in the relationship between the easy gas transfer object and the difficult gas transfer object to be separated, the first transfer path is placed in a relatively gentle inclined posture (relatively horizontal). The two transport paths may be set in a large inclined posture (relatively close to vertical). In this case, by changing the inclination of each path according to the property of the material contained in the material to be transported, it is possible to obtain a transportation structure in which the ability of the suction blower can be sufficiently brought out. (C) In the above embodiment, a separating device was provided at the entrance site of the starting side conveying path to remove large particles. However, in addition to such a separating device, a separating device such as a plate or A mechanical separation device such as a lattice-shaped sieve may be provided. Furthermore, as for this installation position, with respect to the separation part,
It may be located at any position on the upstream side.
【0013】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。It should be noted that reference numerals are given in the claims for convenience of comparison with the drawings, but the present invention is not limited to the configurations of the accompanying drawings by the entry.
【図1】本願の気体搬送装置の構成を示す図FIG. 1 is a diagram showing a configuration of a gas transfer device of the present application.
【図2】本願の気体搬送装置の別構成例を示す図FIG. 2 is a diagram showing another configuration example of the gas transfer device of the present application.
【図3】ゴミ焼却残渣の分離・搬送システムの従来構成
を示す図FIG. 3 is a diagram showing a conventional configuration of a waste incineration residue separation / transportation system.
7 回収部 11 起点側搬送路 12 分離部 13 第1搬送路 14 第2搬送路 100 直管 7 Recovery Section 11 Starting Side Transport Path 12 Separation Section 13 First Transport Path 14 Second Transport Path 100 Straight Pipe
Claims (4)
から搬送終点まで気体搬送する気体搬送装置であって、 前記被搬送物に、気体搬送が容易な易気体搬送物と困難
な難気体搬送物が含まれる場合に、 前記搬送起点より前記被搬送物を分離部(12)に導く
起点側搬送路(11)と、前記分離部(12)において
分離される前記易気体搬送物を前記搬送終点まで搬送す
る第1搬送路(13)と、前記分離部(12)において
分離される前記難気体搬送物を回収部(7)まで搬送す
る第2搬送路(14)とを備え、 前記第2搬送路(14)を、水平方向より傾いた傾斜姿
勢に構成するとともに、前記第2搬送路(14)の上端
側に前記第1搬送路(13)の下端側を接続して、接続
部近傍を前記分離部(12)として構成し、 前記第1搬送路(13)の搬送終点側に、気体搬送用の
吸引流を誘起する吸引機構(16)を備えた気体搬送装
置。1. A gas carrying device for carrying a gas from a transport starting point to a transport ending point, which is made of a solid powder or granular material, wherein the gas is easily transported to the transported object and is difficult. When a gas carrier is included, a starting point-side carrier path (11) that guides the transferred object from the carrier starting point to the separating unit (12) and the easy-gas carrier that is separated in the separating unit (12) are provided. A first transport path (13) for transporting to the transport end point, and a second transport path (14) for transporting the difficult gas transport product separated in the separation section (12) to a recovery section (7), The second transport path (14) is configured in an inclined posture inclined from the horizontal direction, and the lower end side of the first transport path (13) is connected to the upper end side of the second transport path (14), The vicinity of the connection portion is configured as the separation portion (12), and the first transfer (13) the transport end point of a gas conveying device provided with a suction mechanism for inducing suction flow of gas transport (16).
一の直管(100)の中間部位に、前記起点側搬送路
(11)を接続し、接続部近傍を前記分離部(12)と
して構成するとともに、前記分離部(12)より下側に
位置する直管部を前記第2搬送路(14)として、前記
分離部(12)より上側に位置する直管部を前記第1搬
送路(13)として構成した請求項1記載の気体搬送装
置。2. The starting side conveying path (11) is connected to an intermediate portion of a single straight pipe (100) arranged to be inclined with respect to the horizontal direction, and the vicinity of the connecting portion is connected to the separating portion ( 12), the straight pipe portion located below the separating portion (12) is used as the second transport path (14), and the straight pipe portion above the separating portion (12) is formed into the first pipe portion. 2. The gas transfer device according to claim 1, which is configured as one transfer path (13).
量を設定自在な流量設定機構を備えた請求項1又は2記
載の気体搬送装置。3. The gas transfer device according to claim 1, wherein the suction mechanism (16) is provided with a flow rate setting mechanism capable of setting a flow rate of the suction flow.
ての焼却灰を含む焼却残渣である請求項1、2又は3記
載の気体搬送装置。4. The gas transfer device according to claim 1, wherein the transferred object is an incineration residue containing incinerated ash as the easy-gas transfer object.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19230495A JPH0940179A (en) | 1995-07-27 | 1995-07-27 | Gas carrier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19230495A JPH0940179A (en) | 1995-07-27 | 1995-07-27 | Gas carrier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0940179A true JPH0940179A (en) | 1997-02-10 |
Family
ID=16289053
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19230495A Pending JPH0940179A (en) | 1995-07-27 | 1995-07-27 | Gas carrier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0940179A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002059083A (en) * | 2000-08-18 | 2002-02-26 | Sato Ayako | Apparatus for segregating crushed empty can |
-
1995
- 1995-07-27 JP JP19230495A patent/JPH0940179A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002059083A (en) * | 2000-08-18 | 2002-02-26 | Sato Ayako | Apparatus for segregating crushed empty can |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5333797A (en) | Commingled recyclables recovery and recycling process and related apparatuses | |
| RU2521891C2 (en) | Method of powder conveying | |
| US8695903B2 (en) | Processing of steel making slag | |
| EP0257434B1 (en) | Recovery of useful materials from refuse fuel ash | |
| AU2019305683B2 (en) | Sizing and separating granular particles | |
| CN208661394U (en) | A kind of sand device processed | |
| JP5885957B2 (en) | Particle classifier | |
| JP3732429B2 (en) | Pretreatment equipment and pretreatment method for ash melting furnace | |
| JPH0940179A (en) | Gas carrier | |
| WO2011041828A1 (en) | Pneumatic separation of loose materials | |
| JP3494216B2 (en) | Recovery and utilization method of activated carbon in sintering exhaust gas treatment equipment | |
| CN116438019B (en) | Apparatus and methods for screening particle streams | |
| CN119212795A (en) | Crusher feeding station | |
| JP2003185104A (en) | Fluidized-bed boiler equipment | |
| JP7528831B2 (en) | Combustible material sorting and recovery device, combustible material sorting and recovery method, and waste treatment facility equipped with combustible material sorting and recovery device | |
| JP7589399B2 (en) | Foreign matter removal device, gypsum-based building surface material manufacturing device, and foreign matter removal method | |
| JPH0691119A (en) | Dust collecting hood | |
| JP3934894B2 (en) | Fluidized bed gasifier exhaust gas processing apparatus and processing method | |
| JPH0889899A (en) | Apparatus for sorting waste | |
| JP2024063580A (en) | Vibrating screen device, stoker incinerator, and method for recovering valuable metals from ash of a stoker incinerator | |
| JPH0311219A (en) | Method of supplying incineration ash in incineration ash melting furnace | |
| JP3880264B2 (en) | Plastic bottle sorter used in sorting system | |
| JPH09249435A (en) | Slag crushing method | |
| JPH059683U (en) | Classifier | |
| JPH04132999A (en) | Decontamination of radioactive waste |