JP2011050824A - Pulse type dust collector - Google Patents

Pulse type dust collector Download PDF

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JP2011050824A
JP2011050824A JP2009200644A JP2009200644A JP2011050824A JP 2011050824 A JP2011050824 A JP 2011050824A JP 2009200644 A JP2009200644 A JP 2009200644A JP 2009200644 A JP2009200644 A JP 2009200644A JP 2011050824 A JP2011050824 A JP 2011050824A
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air
end side
compressed air
dust
proximal end
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JP5140048B2 (en
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Takamasa Kijima
敬昌 木嶋
Sadanobu Uyama
貞信 夘山
Tsugumasa Matsuda
承真 松田
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Nihon Spindle Manufacturing Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a pulse type dust collector capable of extremly accelerating pressure rising speed in an injector tube accompanying the opening operation of an on-off valve without causing problems that the device is made large in size and the air consumption is increased, and improving dust shaking off performance by means of the propagation of a pressure wave to inside of a filter part. <P>SOLUTION: In a compressed air jetting part of the pulse type dust collector, a plurality of jetting holes 17 connecting a compressed air source for independently jetting the compressed air H to a plurality of filters from the compressed air source are provided in the longitudinal direction and an induction part 30 capable of inducing outside air OA into an injector tube by the air stream of the compressed air H supplied to the inside of the injector tube 15 from the base end side to the tip side through the on-off valve is provided in a base end side area P between the base end where the on-off valve is provided and a place where the jetting holes 17a most closed to the base end in the plurality of the jetting holes 17 is provided in the injector tube 15 connected to the compressed air source through the on-off valve at the base end. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、区画壁により内部が含塵空気導入室と浄化空気室とに区画された筐体と、区画壁のうち含塵空気導入室と浄化空気室とを連通する複数の連通部のそれぞれに設けられ、含塵空気導入室側から浄化空気室側に通流する含塵空気中に含まれる塵埃を捕集する複数のフィルタを有するフィルタ部と、浄化空気室側からフィルタ部を介して含塵空気導入室側に圧縮空気を噴出させて、フィルタ部に付着した塵埃を清掃する圧縮空気噴出部とを備えたパルス式集塵装置に関する。   The present invention includes a housing whose interior is partitioned into a dust-containing air introduction chamber and a purified air chamber by a partition wall, and each of a plurality of communication portions that communicate the dust-containing air introduction chamber and the purified air chamber among the partition walls. A filter unit having a plurality of filters for collecting dust contained in the dust-containing air flowing from the dust-containing air introduction chamber side to the purified air chamber side, and from the purified air chamber side through the filter unit The present invention relates to a pulse type dust collector including a compressed air ejection unit that ejects compressed air to a dust-containing air introduction chamber side and cleans dust adhering to a filter unit.

上記パルス式集塵装置は、筐体内において含塵空気導入室側から浄化空気室側に通流する含塵空気中に含まれる塵埃をフィルタ部にて捕集して、焼却炉や破砕設備等から供給される含塵空気を浄化する装置であり、さらに、フィルタ部に捕集され付着した塵埃を、圧縮空気噴出部により浄化空気室側からフィルタ部を介して含塵空気導入室側に圧縮空気を噴出させて払い落とし、清掃することができるように構成されている(例えば、特許文献1参照)。   The pulse type dust collector collects dust contained in the dust-containing air flowing from the dust-containing air introduction chamber side to the purified air chamber side in the housing by the filter unit, and incinerators, crushing facilities, etc. This is a device that purifies the dust-containing air supplied from the filter. Further, the dust collected and adhered to the filter unit is compressed from the purified air chamber side to the dust-containing air introduction chamber side through the filter unit by the compressed air ejection unit. It is configured such that air can be ejected, cleaned, and cleaned (see, for example, Patent Document 1).

上記特許文献1に記載のパルス式集塵装置では、圧縮空気噴出部は、基端が圧縮空気源に接続されるとともに先端が閉塞されたインジェクターチューブ(管部材)と、圧縮空気源から圧縮空気をインジェクターチューブ内へ断続的に供給可能な開閉弁と、インジェクターチューブの長手方向に複数設けられ、インジェクターチューブ内に供給された圧縮空気を複数のフィルタに各別に噴出させる噴出孔とを備えている。
これにより、フィルタ部に塵埃が捕集され付着して当該フィルタ部における圧力損失が大きくなった場合であっても、フィルタ部への塵埃の捕集を継続したままの状態で開閉弁を開操作し、インジェクターチューブを介して複数の噴出孔から圧縮空気を複数のフィルタの内部に噴出させることで、浄化空気室側からフィルタを介して含塵空気導入室側に圧力波(パルス波)を伝播させることができ、フィルタの外表面(含塵空気導入室側)に付着した塵埃を払い落とすことができる。
In the pulse dust collector described in Patent Document 1, the compressed air ejection part includes an injector tube (tube member) having a proximal end connected to a compressed air source and a closed end, and compressed air from the compressed air source. Is provided with a plurality of on-off valves that can be intermittently supplied into the injector tube, and a plurality of ejection holes that are provided in the longitudinal direction of the injector tube and that individually eject the compressed air supplied into the injector tube into the plurality of filters. .
As a result, even if dust is collected and adhered to the filter part and the pressure loss in the filter part increases, the opening / closing valve is opened while the dust is still collected on the filter part. Then, the pressure air (pulse wave) is propagated from the purified air chamber side to the dust-containing air introduction chamber side through the filter by ejecting compressed air from the plurality of ejection holes into the inside of the plurality of filters through the injector tube. The dust adhering to the outer surface of the filter (on the dust-containing air introduction chamber side) can be removed.

ここで、例えば、特許文献1に記載のパルス式集塵装置においては、フィルタ部が区画壁の連通部に垂下された複数のバグフィルタ、すなわち、かご型形状の支持体に被せられた袋状のフィルタ(濾布)で構成されている。このバグフィルタの清掃時には、噴出孔から圧縮空気を噴出させることで、その噴出方向に伝播する圧力波がバグフィルタ内において開口端部側から先端部側に向けて伝播し、濾布自身が瞬間的に外径方向に膨張させられて、当該濾布の外表面に付着していた塵埃が外径方向に向けて払い落とされて清掃され、目詰まりを解消することができる。なお、取り除かれた塵埃は、筐体の下部に落下し回収される。   Here, for example, in the pulse type dust collector described in Patent Document 1, a plurality of bag filters having a filter portion suspended from the communication portion of the partition wall, that is, a bag shape covered with a cage-shaped support body Filter (filter cloth). When cleaning the bag filter, the compressed air is ejected from the ejection hole, so that the pressure wave propagating in the direction of ejection propagates from the opening end to the tip in the bag filter, and the filter cloth itself instantaneously In general, the dust that has been expanded in the outer diameter direction and adhered to the outer surface of the filter cloth is wiped off and cleaned in the outer diameter direction, thereby eliminating clogging. The removed dust falls to the bottom of the housing and is collected.

実開平6−15713号公報Japanese Utility Model Publication No. 6-15713

上記パルス式集塵装置においては、インジェクターチューブは、基端が開閉弁を介して圧縮空気源に接続されるとともに先端が閉塞されて構成されているため、このインジェクターチューブ内は、圧縮空気源から開閉弁を介した圧縮空気の供給のみにより昇圧され、その昇圧により噴出孔から圧縮空気が噴出されることとなる。そのため、フィルタ部に付着した塵埃の払い落とし効果の向上を図るためには、インジェクターチューブ内の圧力(静圧)をできるだけ短時間で上昇させ、噴出孔から一気に圧縮空気をフィルタ部内に噴出させることで、高エネルギ状態の圧力波を形成することが重要である。   In the pulse dust collector, the injector tube is configured such that the proximal end is connected to the compressed air source via the on-off valve and the distal end is closed. The pressure is increased only by the supply of compressed air through the on-off valve, and the compressed air is ejected from the ejection holes by the pressure increase. Therefore, in order to improve the effect of removing dust adhering to the filter part, the pressure (static pressure) in the injector tube is increased in as short a time as possible, and compressed air is ejected from the ejection hole into the filter part at once. Thus, it is important to form a pressure wave in a high energy state.

しかしながら、上記特許文献1に記載のパルス式集塵装置では、インジェクターチューブ内の昇圧が開閉弁を介した圧縮空気の供給のみによるものであるから、開閉弁における圧力損失等の制限により、インジェクターチューブ内の圧力上昇速度を向上させるには限度がある。
また、インジェクターチューブの長手方向に複数の噴出孔が設けられているので、必然的にインジェクターチューブの長さが長くなり、インジェクターチューブ内の圧力上昇速度が低下する傾向にある。
さらに、インジェクターチューブ内の圧力上昇速度を向上させるために、開閉弁等を大型化することが考えられるが、装置の大型化、消費空気量の上昇やコストの増大等の問題が生じる。
However, in the pulse dust collector described in Patent Document 1, since the pressure increase in the injector tube is only due to the supply of compressed air through the on-off valve, the injector tube is limited due to pressure loss and the like in the on-off valve. There is a limit to improving the rate of pressure increase inside.
Moreover, since the several injection hole is provided in the longitudinal direction of the injector tube, the length of an injector tube inevitably becomes long and it exists in the tendency for the pressure rise speed in an injector tube to fall.
Furthermore, it is conceivable to increase the size of the on-off valve or the like in order to improve the pressure increase rate in the injector tube, but problems such as an increase in the size of the device, an increase in the amount of air consumption, and an increase in cost arise.

本発明は、上記の事情に鑑みてなされたものであって、その目的は、装置の大型化及び消費空気量の上昇等の問題を生じることなく、開閉弁の開操作に伴うインジェクターチューブ内の圧力上昇速度を極めて迅速なものとして、噴出孔からの圧縮空気の噴出により極めて高エネルギ状態の圧力波を形成し、その圧力波のフィルタ部内への伝播による塵埃の払い落とし性能を向上することが可能なパルス式集塵装置を提供することにある。   The present invention has been made in view of the above circumstances, and its purpose is not to cause problems such as an increase in the size of the apparatus and an increase in the amount of air consumed, and the purpose of the present invention As the pressure rise speed is extremely rapid, the pressure wave in the extremely high energy state is formed by the jet of compressed air from the jet hole, and the dust removal performance by the propagation of the pressure wave into the filter part can be improved. The object is to provide a pulse-type dust collector capable.

上記目的を達成するための本発明に係るパルス式集塵装置は、区画壁により内部が含塵空気導入室と浄化空気室とに区画された筐体と、前記区画壁のうち前記含塵空気導入室と前記浄化空気室とを連通する複数の連通部のそれぞれに設けられ、前記含塵空気導入室側から前記浄化空気室側に通流する含塵空気中に含まれる塵埃を捕集する複数のフィルタを有するフィルタ部と、前記浄化空気室側から前記フィルタ部を介して前記含塵空気導入室側に圧縮空気を噴出させて、前記フィルタ部に付着した塵埃を清掃する圧縮空気噴出部とを備え、
前記圧縮空気噴出部が、基端が圧縮空気源に接続されるとともに先端が閉塞されたインジェクターチューブと、前記圧縮空気源から前記圧縮空気を前記インジェクターチューブ内へ断続的に供給可能な開閉弁と、前記インジェクターチューブの長手方向に複数設けられ、前記インジェクターチューブ内に供給された前記圧縮空気を前記複数のフィルタに各別に噴出させる噴出孔とを備えたパルス式集塵装置であって、その特徴構成は、
前記圧縮空気噴出部の前記インジェクターチューブにおいて、前記開閉弁が設けられる基端と前記複数の噴出孔のうち前記基端に最も近接する噴出孔が設けられる箇所との間である基端側領域に、前記開閉弁を介して前記インジェクターチューブ内に前記基端側から前記先端側に向けて供給された前記圧縮空気の空気流により、外部空気を前記インジェクターチューブ内に誘引可能な誘引部を備えた点にある。
In order to achieve the above object, a pulse dust collector according to the present invention includes a housing whose interior is partitioned by a partition wall into a dust-containing air introduction chamber and a purified air chamber, and the dust-containing air among the partition walls. Dust contained in the dust-containing air that is provided in each of a plurality of communicating portions that communicate between the introduction chamber and the purified air chamber and that flows from the dust-containing air introduction chamber side to the purified air chamber side is collected. A filter unit having a plurality of filters, and a compressed air ejection unit that ejects compressed air from the purified air chamber side to the dust-containing air introduction chamber side through the filter unit to clean dust adhering to the filter unit And
An injector tube having a proximal end connected to a compressed air source and closed at a distal end; and an on-off valve capable of intermittently supplying the compressed air from the compressed air source into the injector tube. A pulse-type dust collecting device provided with a plurality of nozzles provided in the longitudinal direction of the injector tube, and each having a plurality of jets for injecting the compressed air supplied into the injector tube into the plurality of filters. The configuration is
In the injector tube of the compressed air ejection part, in a proximal side region between a proximal end where the on-off valve is provided and a location where an ejection hole closest to the proximal end is provided among the plurality of ejection holes. And an attracting portion capable of attracting external air into the injector tube by an air flow of the compressed air supplied from the proximal end side toward the distal end side into the injector tube through the on-off valve. In the point.

本特徴構成によれば、インジェクターチューブにおける基端側領域に、外部空気をインジェクターチューブ内に誘引可能な誘引部を備えるので、開閉弁を開操作することにより圧縮空気源から開閉弁を介して圧縮空気の空気流が高速でインジェクターチューブ内に供給された際には、基端側領域を当該高速の空気流が通流することによるベンチュリー効果により当該空気流の周りに陰圧が生じて、この基端側領域に設けられた誘引部を介して外部空気がインジェクターチューブ内に強制的に誘引される。なお、上記高速の空気流の流速は、例えば、音速程度、すなわち、300〜350m/sec程度である。
つまり、インジェクターチューブ内の誘引部よりも先端側には、開閉弁を介して供給された圧縮空気のみならず、誘引部を介して強制的に誘引された外部空気も瞬時に供給されることとなり、当該インジェクターチューブ内の圧力を極めて迅速に上昇させることが可能となる。
また、開閉弁の構成を改変等することなく従来と同様の構成の開閉弁を用いた場合でも、上記のように誘引部から外部空気を強制的に誘引することにより、インジェクターチューブ内の圧力を極めて迅速に上昇させることが可能となる。
よって、装置の大型化及び消費空気量の上昇等の問題を生じることなく、開閉弁の開操作に伴うインジェクターチューブ内の圧力上昇速度を極めて迅速なものとして、噴出孔からの圧縮空気のフィルタ部内への噴出により極めて高エネルギ状態の圧力波を形成し、その圧力波のフィルタ部内への伝播による塵埃の払い落とし性能を向上することが可能となる。
According to this characteristic configuration, the proximal end region of the injector tube is provided with an attracting portion capable of attracting external air into the injector tube, so that the compressed air source is compressed via the on-off valve by opening the on-off valve. When the air flow of air is supplied into the injector tube at a high speed, a negative pressure is generated around the air flow due to the venturi effect caused by the flow of the high-speed air flow through the proximal end region. External air is forcibly attracted into the injector tube via an attracting portion provided in the proximal end region. Note that the flow velocity of the high-speed air flow is, for example, about the speed of sound, that is, about 300 to 350 m / sec.
In other words, not only the compressed air supplied through the opening / closing valve but also the external air forced through the induction part is instantaneously supplied to the tip side of the induction part in the injector tube. The pressure in the injector tube can be increased very quickly.
In addition, even when an on-off valve having the same configuration as the conventional one is used without modifying the on-off valve configuration, the pressure in the injector tube is reduced by forcibly attracting external air from the attraction portion as described above. It can be raised very quickly.
Therefore, without causing problems such as an increase in the size of the device and an increase in the amount of air consumed, the pressure rise rate in the injector tube accompanying the opening operation of the on-off valve can be made extremely quick, and the compressed air from the outlet hole can be filtered. As a result, the pressure wave in an extremely high energy state is formed by jetting into the filter, and it is possible to improve dust removal performance by propagation of the pressure wave into the filter portion.

本発明に係るパルス式集塵装置の更なる特徴構成は、前記インジェクターチューブが、前記基端側に設けられる基端側管部材と、前記先端側に設けられる先端側管部材とを備えて構成され、前記誘引部が、前記基端側管部材と前記先端側管部材との間に径方向の隙間を形成した状態で前記基端側管部材が前記先端側管部材に内挿されることにより構成されている点にある。   A further characteristic configuration of the pulse dust collector according to the present invention is such that the injector tube includes a proximal end side tube member provided on the proximal end side and a distal end side tube member provided on the distal end side. The proximal end side tube member is inserted into the distal end side tube member in a state where the attracting portion forms a radial gap between the proximal end side tube member and the distal end side tube member. It is in the point which is comprised.

本特徴構成によれば、インジェクターチューブに設けられる誘引部が、基端側に設けられる基端側管部材と先端側に設けられる先端側管部材との間に径方向の隙間を形成した状態で基端側管部材が先端側管部材に内挿されているので、非常に単純な構成で、ベンチュリー効果を利用して外部空気を誘引する誘引部を形成することが可能となる。また、誘引される外部空気の通流方向が、圧縮空気Hの空気流の通流方向と略同一の先端側方向となるので、ベンチュリー効果による外部空気の誘引を良好に行うことができる。なお、両管部材間の径方向での隙間は、誘引部近傍を通流する圧縮空気の空気流の速度、空気量、誘引部の形状、管部材の径等にも影響されるが、当該空気流の周りにベンチュリー効果で生じた陰圧により外部空気をインジェクターチューブ内に誘引可能な程度の比較的狭い間隔に形成されている。   According to this characteristic configuration, the attracting portion provided in the injector tube forms a radial gap between the proximal end side tube member provided on the proximal end side and the distal end side tube member provided on the distal end side. Since the proximal end side pipe member is inserted into the distal end side pipe member, it is possible to form an attracting part that attracts external air using the Venturi effect with a very simple configuration. In addition, since the flow direction of the external air to be attracted is the front end side direction substantially the same as the flow direction of the air flow of the compressed air H, the external air can be favorably attracted by the Venturi effect. The gap in the radial direction between the two pipe members is also affected by the speed of the compressed air flowing through the vicinity of the attracting part, the amount of air, the shape of the attracting part, the diameter of the pipe member, etc. The air flow is formed at a relatively narrow interval so that external air can be attracted into the injector tube by the negative pressure generated by the venturi effect around the air flow.

本発明に係るパルス式集塵装置の更なる特徴構成は、前記先端側管部材の基端部が基端側ほど拡径する拡径部を有し、拡径された前記先端側管部材の基端部に前記基端側管部材が内挿されている点にある。   A further characteristic configuration of the pulse dust collector according to the present invention is that the proximal end portion of the distal end side pipe member has an enlarged diameter portion whose diameter is increased toward the proximal end side. The proximal end side pipe member is inserted in the proximal end portion.

本特徴構成によれば、拡径部により拡径された先端側管部材の基端部に基端側管部材が内挿されているので、インジェクターチューブ内において先端側管部材の拡径部よりも先端側(拡径されていない部分)の断面積を基端側管部材の先端部の断面積と同等程度とすることができる。よって、圧縮空気の空気流が基端側管部材を通過した後、先端側管部材を通流する際において、先端側管部材の断面積の拡大に伴う空気流の速度の減速を抑制することができ、当該空気流によるインジェクターチューブ内の圧力上昇速度の低下を防止することができる。   According to this characteristic configuration, since the proximal end side tube member is inserted into the proximal end portion of the distal end side tube member whose diameter has been expanded by the expanded diameter portion, in the injector tube, from the expanded diameter portion of the distal end side tube member In addition, the cross-sectional area of the distal end side (the portion where the diameter is not expanded) can be made substantially equal to the cross-sectional area of the distal end portion of the proximal end side pipe member. Therefore, when the compressed air flow passes through the proximal end side pipe member and then flows through the distal end side pipe member, the reduction in the speed of the air flow accompanying the increase in the sectional area of the distal end side pipe member is suppressed. It is possible to prevent a decrease in the pressure increase rate in the injector tube due to the air flow.

本発明に係るパルス式集塵装置の更なる特徴構成は、前記基端側管部材の先端部には、前記基端側管部材の先端部の先端側ほど縮径する先細部が形成されている点にある。   A further characteristic configuration of the pulse dust collector according to the present invention is that a distal end portion of the proximal end side tube member is formed with a tapered portion that is reduced in diameter toward the distal end side of the distal end portion of the proximal end side tube member. There is in point.

本特徴構成によれば、基端側管部材の先端部には先端側ほど縮径する先細部が設けられており、この先細部がいわゆる絞りとして機能するので、基端側管部材内における圧縮空気の空気流の流速を、先細部にて加速して、基端側管部材から先端側管部材に通流させることができる。これにより、基端側管部材と先端側管部材との間に形成された誘引部近傍においてベンチュリー効果による陰圧の発生をより増大させて、当該誘引部からインジェクターチューブ内への外部空気の誘引力を増大させることができ、結果、インジェクターチューブ内の圧力上昇速度をより一層上昇させることができる。   According to this characteristic configuration, the distal end portion of the proximal end side pipe member is provided with a tapered portion that is reduced in diameter toward the distal end side, and this tapered portion functions as a so-called throttle, so that the compressed air in the proximal end side tube member is compressed. The velocity of the air flow can be accelerated with a taper and allowed to flow from the proximal tube member to the distal tube member. This further increases the generation of negative pressure due to the venturi effect in the vicinity of the attracting portion formed between the proximal end side tube member and the distal end side tube member, and attracts external air from the attracting portion into the injector tube. The force can be increased, and as a result, the pressure increase rate in the injector tube can be further increased.

パルス式集塵装置の概略側断面視図Schematic side sectional view of pulse dust collector パルス式集塵装置の概略上面視図Schematic top view of the pulse dust collector 誘引部近傍の構成を示す拡大断面視図Enlarged cross-sectional view showing the configuration near the attracting part 通常運転時における動作を示すパルス式集塵装置の概略側断面視図Schematic side cross-sectional view of a pulse dust collector showing operation during normal operation 清掃運転時における動作を示すパルス式集塵装置の概略側断面視図Schematic side cross-sectional view of pulse dust collector showing operation during cleaning operation 実施例に係るパルス式集塵装置の清掃運転時におけるインジェクターチューブ内の静圧分布を示すグラフ図The graph which shows the static pressure distribution in the injector tube at the time of the cleaning operation of the pulse type dust collector which concerns on an Example. 比較例に係るパルス式集塵装置の清掃運転時におけるインジェクターチューブ内の静圧分布を示すグラフ図The graph which shows the static pressure distribution in the injector tube at the time of the cleaning operation of the pulse type dust collector which concerns on a comparative example 空気開閉弁の開操作からの経過時間と、ある噴出孔位置での圧力との関係を示すグラフ図The graph which shows the relationship between the elapsed time from opening operation of an air on-off valve, and the pressure in a certain nozzle hole position 別実施形態に係る誘引部近傍の構成を示す拡大断面視図Enlarged sectional view showing a configuration in the vicinity of the attracting portion according to another embodiment 別実施形態に係る誘引部近傍の構成を示す拡大断面視図Enlarged sectional view showing a configuration in the vicinity of the attracting portion according to another embodiment 別実施形態に係る誘引部近傍の構成を示す拡大断面視図Enlarged sectional view showing a configuration in the vicinity of the attracting portion according to another embodiment

以下、本発明に係るパルス式集塵装置Aにおいて、フィルタ部としてバグフィルタ5を用いた場合の実施形態を説明する。
図1及び図2に示すように、パルス式集塵装置Aは、区画壁4により内部が含塵空気導入室2と浄化空気室3とに区画された筐体1と、区画壁4のうち含塵空気導入室2と浄化空気室3とを連通する複数の連通部6のそれぞれに設けられ、含塵空気導入室2側から浄化空気室3側に通流する含塵空気G中に含まれる塵埃Dを捕集する複数のバグフィルタ5(フィルタ部の一例)と、浄化空気室3側からバグフィルタ5を介して含塵空気導入室2側に圧縮空気Hを噴出させて、バグフィルタ5に付着した塵埃Dを清掃する圧縮空気噴出部7と、圧縮空気噴出部7の作動等のパルス式集塵装置Aの運転を制御する制御部8等を備えて構成されている。また、パルス式集塵装置Aは、バグフィルタ5の内側と外側との圧力差を検出する圧力差検出部9を備えて構成されている。
Hereinafter, in the pulse dust collector A according to the present invention, an embodiment in which a bag filter 5 is used as a filter unit will be described.
As shown in FIG. 1 and FIG. 2, the pulse dust collector A includes a housing 1 whose interior is partitioned by a partition wall 4 into a dust-containing air introduction chamber 2 and a purified air chamber 3, and the partition wall 4. Included in the dust-containing air G that is provided in each of the plurality of communication portions 6 that communicate the dust-containing air introduction chamber 2 and the purified air chamber 3 and flows from the dust-containing air introduction chamber 2 side to the purified air chamber 3 side. Bag filter 5 (an example of a filter unit) that collects dust D to be collected, and compressed air H is jetted from the purified air chamber 3 side to the dust-containing air introduction chamber 2 side through the bag filter 5, 5 includes a compressed air ejection part 7 for cleaning the dust D adhering to 5 and a control part 8 for controlling the operation of the pulse dust collector A such as the operation of the compressed air ejection part 7. Further, the pulse dust collector A includes a pressure difference detection unit 9 that detects a pressure difference between the inside and the outside of the bag filter 5.

筐体1は、内部が上下方向で区画壁4により区画され、下部に含塵空気Gが通流する含塵空気導入室2、上部に区画壁4の連通部6に設けられたバグフィルタ5により浄化された浄化空気Cが通流する浄化空気室3が形成されている。筐体1は、含塵空気導入室2におけるバグフィルタ5が配置される箇所及び浄化空気室3が形成される箇所における外形が上面視概略矩形に形成され、含塵空気導入室2におけるバグフィルタ5が配置される箇所の下側の外形が漏斗形状に形成されている。
そして、筐体1の漏斗形状に形成された上端箇所には焼却炉等(図示せず)からの含塵空気Gを含塵空気導入室2内に導入する含塵空気導入路10が形成されており、筐体1の矩形に形成された上部箇所には、バグフィルタ5により浄化された浄化空気Cを浄化空気室3から排出する浄化空気排出路11が形成されている。この浄化空気排出路11の下流側には吸引装置(図示せず)が設けられ、浄化空気室3内の浄化空気Cを外部空間に吸引することができるように構成されている。なお、筐体1の漏斗形状に形成された箇所の下端部には、ロータリーバルブが設けられた排出口12が形成され、後述するバグフィルタ5の清掃等により生じた含塵空気導入室2内の塵埃D等を排出できるように構成されている。
したがって、焼却炉等(図示せず)で発生した含塵空気Gは、吸引装置(図示せず)の吸引力により含塵空気導入路10を介して含塵空気導入室2内に導入され、バグフィルタ5により塵埃Dが捕集されて浄化空気Cとなって、浄化空気室3内から浄化空気排出路11を介して、集塵装置Aの下流側に接続された外部空間に排出される。
The housing 1 is partitioned by a partition wall 4 in the vertical direction, a dust-containing air introduction chamber 2 through which dust-containing air G flows, and a bag filter 5 provided at a communication portion 6 of the partition wall 4 at the top. A purified air chamber 3 is formed through which the purified air C purified by the air flows. The casing 1 is formed in a rectangular shape in a top view when the bag filter 5 is disposed in the dust-containing air introduction chamber 2 and the portion where the purified air chamber 3 is formed, and the bag filter in the dust-containing air introduction chamber 2 is formed. The lower outer shape of the place where 5 is arranged is formed in a funnel shape.
A dust-containing air introduction path 10 for introducing dust-containing air G from an incinerator or the like (not shown) into the dust-containing air introduction chamber 2 is formed at the upper end portion of the housing 1 formed in the funnel shape. A purified air discharge path 11 for discharging the purified air C purified by the bag filter 5 from the purified air chamber 3 is formed at an upper portion formed in the rectangular shape of the housing 1. A suction device (not shown) is provided on the downstream side of the purified air discharge passage 11 so that the purified air C in the purified air chamber 3 can be sucked into the external space. In addition, a discharge port 12 provided with a rotary valve is formed at the lower end of the portion formed in the funnel shape of the housing 1, and the inside of the dust-containing air introduction chamber 2 generated by cleaning the bag filter 5 described later or the like. The dust D and the like can be discharged.
Therefore, the dust-containing air G generated in an incinerator or the like (not shown) is introduced into the dust-containing air introduction chamber 2 through the dust-containing air introduction path 10 by the suction force of the suction device (not shown). Dust D is collected by the bag filter 5 to become purified air C, which is discharged from the purified air chamber 3 to the external space connected to the downstream side of the dust collector A via the purified air discharge passage 11. .

バグフィルタ5は、図1、図4、図5に示すように、有底のかご形状(例えば、複数の直線棒状体を、環状に形成された複数のリング状枠体に取り付けた有底筒状のかご形状)に形成された支持体5aの外側に、含塵空気Gを通流可能に構成された袋状のバグ5b(フィルタの一例)が被せられて構成されている。
バグ5bは、含塵空気G中の塵埃Dを良好に捕集できる濾布により構成され、例えば、内側が布で当該布の外側に貼り付けた不織布により形成される基布、或いは不織布や織布等により構成される。また、濾布の素材は、合成繊維やガラス繊維等から成る。バグ5bの下部は袋状で、上部は開口を備えて構成され、当該開口に後述する圧縮空気噴出部7の案内管13が取り付けられ、バグ5bの上端部が案内管13と支持体5aにより挟持されて区画壁4の連通部6に固定されている。
そして、バグフィルタ5は、区画壁4の連通部6に垂下状態で取り付けられる。なお、本実施形態では、縦に(図2の上下方向に)4個、横に(図2の左右方向に)5個をそれぞれ配列させた状態で20個のバグフィルタ5を設けているが、その配列箇所、配列数、支持体5aの形状、バグ5bの形状及び案内管13の有無等については、塵埃Dの処理量等との関係で適宜変更することが可能である。
As shown in FIGS. 1, 4 and 5, the bag filter 5 has a bottomed cage shape (for example, a plurality of straight rod-shaped bodies attached to a plurality of ring-shaped frame bodies formed in an annular shape. A bag-like bug 5b (an example of a filter) configured to allow the dust-containing air G to flow is covered on the outside of the support 5a formed in a shape of a cage).
The bug 5b is composed of a filter cloth that can satisfactorily collect the dust D in the dust-containing air G. For example, a base cloth formed by a non-woven cloth attached on the outside of the cloth or a non-woven cloth or a woven cloth. Composed of cloth or the like. The material of the filter cloth is made of synthetic fiber or glass fiber. The lower part of the bug 5b is formed in a bag shape, and the upper part is provided with an opening. A guide pipe 13 of a compressed air ejection part 7 to be described later is attached to the opening, and the upper end part of the bug 5b is formed by the guide pipe 13 and the support 5a. It is clamped and fixed to the communication part 6 of the partition wall 4.
The bag filter 5 is attached to the communication portion 6 of the partition wall 4 in a suspended state. In the present embodiment, 20 bag filters 5 are provided in a state where 4 pieces are arranged vertically (up and down in FIG. 2) and 5 pieces are arranged horizontally (in the left and right direction in FIG. 2). The arrangement location, the number of arrangements, the shape of the support 5a, the shape of the bug 5b, the presence / absence of the guide tube 13, and the like can be appropriately changed in relation to the amount of dust D processed.

圧縮空気噴出部7は、各バグフィルタ5の内側に圧縮空気Hを断続的に(パルス状に)噴出することができるように構成されている。
圧縮空気噴出部7は、基端15Aがヘッダ部14(圧縮空気源の一例)に接続されるとともに先端15Bが閉塞されたインジェクターチューブ15と、ヘッダ部14から圧縮空気Hをインジェクターチューブ15内へ断続的に供給可能な空気開閉弁16(開閉弁の一例)と、インジェクターチューブ15の長手方向に複数設けられ、インジェクターチューブ15内に供給された圧縮空気Hを複数のバグフィルタ5の内側に各別に噴出させる複数の噴出孔17とを備えている。
さらに、圧縮空気噴出部7は、コンプレッサ等からの圧縮空気Hを圧縮空気供給路18に設けられた圧力調整弁19を介して圧力を調整した上で、各ヘッダ部14内(図2では、14a、14b、14c、14dの4つ)に貯留することができるように構成されている。そして、圧縮空気噴出部7は、各ヘッダ部14内に貯留された圧縮空気Hを、各ヘッダ部14内にそれぞれ設けられた空気開閉弁16(図示しないが、16a、16b、16c、16dの4つ)を介して複数のインジェクターチューブ15(図2では、15a、15b、15c、15dの4本)のそれぞれに分配し、分配された圧縮空気Hをインジェクターチューブ15に設けられた複数の噴出孔17から各案内管13を介して各バグフィルタ5の内側に噴出可能に構成されている。なお、図1に示す例では、一つのインジェクターチューブ15(例えば、15d)に対し、5つの噴出孔17(例えば、17a、17b、17c、17d、17e)が設けられている。
The compressed air ejection section 7 is configured to be able to eject the compressed air H intermittently (in a pulse shape) to the inside of each bag filter 5.
The compressed air ejection part 7 includes an injector tube 15 having a proximal end 15A connected to a header part 14 (an example of a compressed air source) and a closed end 15B, and compressed air H from the header part 14 into the injector tube 15. A plurality of air on-off valves 16 (an example of on-off valves) that can be intermittently supplied and a plurality of compressed air H provided in the longitudinal direction of the injector tube 15 and supplied to the inside of the plurality of bag filters 5. A plurality of ejection holes 17 are separately ejected.
Further, the compressed air ejection section 7 adjusts the pressure of compressed air H from a compressor or the like via a pressure regulating valve 19 provided in the compressed air supply path 18, and then in each header section 14 (in FIG. 14a, 14b, 14c, and 14d). Then, the compressed air ejection section 7 converts the compressed air H stored in each header section 14 into air on / off valves 16 (not shown, but 16a, 16b, 16c, 16d) provided in the header sections 14, respectively. 4), and is distributed to each of the plurality of injector tubes 15 (four in FIG. 2, four of 15a, 15b, 15c, 15d), and the plurality of jets provided in the injector tube 15 is distributed. It is configured to be able to eject from the hole 17 to the inside of each bag filter 5 through each guide tube 13. In the example shown in FIG. 1, five ejection holes 17 (for example, 17a, 17b, 17c, 17d, and 17e) are provided for one injector tube 15 (for example, 15d).

各空気開閉弁16の開閉は、各空気開閉弁16にそれぞれ対応して設けられた作動部20(図2では、20a、20b、20c、20dの4つ)により制御可能に構成されている。各噴出孔17は、各バグフィルタ5に一対一で対応するように当該各バグフィルタ5の上部に配置されている。なお、第1空気開閉弁16aに対応する第1インジェクターチューブ15aには5つのバグフィルタ5が並列で配置され、同様に、第2空気開閉弁16bに対応する第2インジェクターチューブ15b、第3空気開閉弁16cに対応する第3インジェクターチューブ15c、及び第4空気開閉弁16dに対応する第4インジェクターチューブ15dには、それぞれ5つのバグフィルタ5が並列で配置されている。従って、ヘッダ部14内に貯留された圧縮空気Hは、制御部8により各作動部20が制御されて、当該各作動部20に対応する各空気開閉弁16の開閉が設定された開閉状態となるように制御されることにより、各噴出孔17を介して各バグフィルタ5の内側に断続的に(パルス状に)噴出可能とされている。各ヘッダ部14内に貯留される圧縮空気Hの圧力及び空気量は、噴出することが必要な圧縮空気Hの圧力や空気量に応じて適宜設定することができるが、例えば、圧力を2MPa、容量を450cm3程度に設定することができ、空気開閉弁16を開操作した場合の圧縮空気Hの空気流は、例えば、音速程度、すなわち、300〜350m/sec程度である。 The opening / closing of each air on / off valve 16 is configured to be controllable by operating sections 20 (four in FIG. 2, 20 a, 20 b, 20 c, and 20 d) provided corresponding to each air on / off valve 16. Each ejection hole 17 is arranged on the upper part of each bag filter 5 so as to correspond to each bug filter 5 on a one-to-one basis. In addition, five bag filters 5 are arranged in parallel in the first injector tube 15a corresponding to the first air on-off valve 16a, and similarly, the second injector tube 15b corresponding to the second air on-off valve 16b, the third air Five bag filters 5 are arranged in parallel in the third injector tube 15c corresponding to the on-off valve 16c and the fourth injector tube 15d corresponding to the fourth air on-off valve 16d, respectively. Therefore, the compressed air H stored in the header portion 14 is in an open / closed state in which the operation portions 20 are controlled by the control portion 8 and the opening / closing of the air on / off valves 16 corresponding to the operation portions 20 is set. By being controlled so as to be, it is possible to eject intermittently (in a pulse form) inside each bag filter 5 through each ejection hole 17. The pressure and the air amount of the compressed air H stored in each header portion 14 can be appropriately set according to the pressure and the air amount of the compressed air H that needs to be ejected. For example, the pressure is 2 MPa, The capacity can be set to about 450 cm 3, and the air flow of the compressed air H when the air on-off valve 16 is opened is, for example, about the speed of sound, that is, about 300 to 350 m / sec.

制御部8は、中央演算処理装置(CPU)、メモリ、記憶部等(図示せず)からなり、当該CPUにより所定のプログラムを実行して情報を処理することができる公知の情報処理手段で構成され、パルス式集塵装置Aの運転を制御することができるように構成されている。   The control unit 8 includes a central processing unit (CPU), a memory, a storage unit, and the like (not shown), and includes known information processing means that can execute a predetermined program and process information by the CPU. The operation of the pulse dust collector A can be controlled.

圧力差検出部9は公知の圧力検出手段からなり、図1に示すように、含塵空気導入路10に設けられ、バグフィルタ5の外側(含塵空気導入室2側)の圧力を検出する第1圧力検出部9aと、浄化空気排出路11に設けられ、バグフィルタ5の内側(浄化空気室3側)の圧力を検出する第2圧力検出部9bとを備え、これら第1圧力検出部9a及び第2圧力検出部9bからの検出圧力に基づいて、バグフィルタ5の内外差圧を検出することができるように構成されている。検出されたバグフィルタ5の内外差圧は、制御部8に出力するように構成されている。
また、圧力差検出部9は、バグフィルタ5の内側(バグフィルタ5のバグ5bの内部)の圧力を検出する第3圧力検出部9cを備え、第1圧力検出部9a及び第3圧力検出部9cからの検出圧力の差を、バグフィルタ5の内外圧力差として測定することができる。また、バグフィルタ5の外側に塵埃Dが付着して効率よく塵埃Dを捕集できない状態となったと判断する基準となる所定の圧力差が、予め設定されている。すなわち、このバグフィルタ5の内外圧力差は、当該バグフィルタ5の外側から内側へ通流する含塵空気Gの圧力損失であり、それに対し、上記所定の圧力差はバグフィルタ5の清掃が必要な状態となった場合における圧力損失の値として設定される。なお、所定の圧力差は、制御部8に出力し、予め当該制御部8の記憶部に記憶可能に構成されている。
なお、浄化空気排出路11には、浄化空気室3から外部空間に排出される浄化空気Cの流量を検出する公知の流量検出部21が設けられ、検出された流量は、制御部8に出力するように構成されている。
As shown in FIG. 1, the pressure difference detection unit 9 is provided in a dust-containing air introduction path 10 and detects the pressure outside the bag filter 5 (on the dust-containing air introduction chamber 2 side). A first pressure detection unit 9a; and a second pressure detection unit 9b that is provided in the purified air discharge passage 11 and detects the pressure inside the bag filter 5 (purified air chamber 3 side). These first pressure detection units Based on the detected pressure from 9a and the 2nd pressure detection part 9b, it is comprised so that the internal / external differential pressure | voltage of the bag filter 5 can be detected. The detected internal / external differential pressure of the bag filter 5 is configured to be output to the control unit 8.
The pressure difference detection unit 9 includes a third pressure detection unit 9c that detects the pressure inside the bag filter 5 (inside the bag 5b of the bag filter 5), and includes a first pressure detection unit 9a and a third pressure detection unit. The difference in detected pressure from 9c can be measured as the internal / external pressure difference of the bag filter 5. Further, a predetermined pressure difference serving as a reference for determining that the dust D has adhered to the outside of the bag filter 5 and the dust D cannot be efficiently collected is set in advance. That is, the pressure difference between the inside and outside of the bag filter 5 is a pressure loss of the dust-containing air G flowing from the outside to the inside of the bag filter 5, whereas the predetermined pressure difference requires the bag filter 5 to be cleaned. It is set as the value of the pressure loss in the case of a new state. The predetermined pressure difference is output to the control unit 8 and can be stored in the storage unit of the control unit 8 in advance.
The purified air discharge path 11 is provided with a known flow rate detection unit 21 that detects the flow rate of the purified air C discharged from the purified air chamber 3 to the external space, and the detected flow rate is output to the control unit 8. Is configured to do.

次に、本願の特徴構成である圧縮空気噴出部7の更なる構成について説明する。
本実施形態における圧縮空気噴出部7は、図1〜図5に示すように、基端15Aがヘッダ部14(圧縮空気源の一例)に接続されるとともに先端15Bが閉塞されたインジェクターチューブ15を備える。
このインジェクターチューブ15は、基端15A側に設けられる円筒状の基端側管部材31と、先端15B側に設けられる円筒状の先端側管部材32とを備えて構成されている。
そして、インジェクターチューブ15には、図3に示すように、これら基端側管部材31と先端側管部材32との間に径方向の隙間Sを形成した状態で基端側管部材31が先端側管部材32に所定部位まで内挿されることにより、誘引部30が構成されている。なお、図3では、基端側管部材31と先端側管部材32とはそれぞれの軸芯を共通にする同芯状態で内挿されている。
すなわち、このインジェクターチューブ15において、空気開閉弁16が設けられる基端15Aと複数の噴出孔17のうち基端15Aに最も近接する噴出孔17aが設けられる箇所との間である基端側領域Pに、空気開閉弁16を介してインジェクターチューブ15内に基端15A側から先端15B側に向けて供給された圧縮空気Hの空気流により、外部空気OAをインジェクターチューブ15内に誘引可能な誘引部30が形成されている。
Next, the further structure of the compressed air ejection part 7 which is the characteristic structure of this application is demonstrated.
As shown in FIGS. 1 to 5, the compressed air ejection portion 7 in the present embodiment includes an injector tube 15 having a proximal end 15 </ b> A connected to a header portion 14 (an example of a compressed air source) and a distal end 15 </ b> B closed. Prepare.
The injector tube 15 includes a cylindrical proximal end side tube member 31 provided on the proximal end 15A side and a cylindrical distal end side tube member 32 provided on the distal end 15B side.
As shown in FIG. 3, the injector tube 15 has the proximal tube member 31 at the distal end with a radial gap S formed between the proximal tube member 31 and the distal tube member 32. The attracting portion 30 is configured by being inserted into the side tube member 32 up to a predetermined site. In FIG. 3, the proximal end side pipe member 31 and the distal end side pipe member 32 are inserted in a concentric state in which the respective axial centers are made common.
That is, in this injector tube 15, the base end side region P between the base end 15 </ b> A where the air opening / closing valve 16 is provided and the location where the ejection hole 17 a closest to the base end 15 </ b> A is provided among the plurality of ejection holes 17. Further, an attracting portion capable of attracting the external air OA into the injector tube 15 by the air flow of the compressed air H supplied from the base end 15A side toward the distal end 15B side into the injector tube 15 via the air opening / closing valve 16 30 is formed.

基端側管部材31は、図3に示すように、基端側管部材31の先端部31aに、基端側管部材31の基端筒部31dの内径X(先端部31aの最大内径でもある)よりも先端15B側ほど縮径する先細部31bが形成され、この先細部31bは基端側管部材31内を基端側から先端側に通流する圧縮空気Hの空気流に対して、いわゆる絞りとして機能する。また、先端部31aにおける先細部31bのさらに先端15B側には、先細部31bの最小内径(図示せず)と略同じ内径の先端筒部31cが形成されている。   As shown in FIG. 3, the proximal end side pipe member 31 is connected to the distal end portion 31a of the proximal end side tube member 31 with the inner diameter X of the proximal end cylindrical portion 31d of the proximal end side tube member 31 (even the maximum inner diameter of the distal end portion 31a). A tapered portion 31b that is reduced in diameter toward the distal end 15B side is formed, and this tapered portion 31b is in response to the air flow of the compressed air H that flows from the proximal end side to the distal end side in the proximal end side pipe member 31. It functions as a so-called diaphragm. Further, a distal end cylindrical portion 31c having an inner diameter substantially the same as the minimum inner diameter (not shown) of the tapered portion 31b is formed on the distal end 15B side of the tapered portion 31b in the distal end portion 31a.

先端側管部材32は、図3に示すように、先端側管部材32の基端部32aに基端15A側ほど拡径する拡径部32bが形成されている。また、基端部32aにおける拡径部32bのさらに基端15A側には、拡径部32bの最大内径Zと略同じ内径Zの基端筒部32dを備えている。さらに、先端側管部材32は、拡径部32bの先端15B側に、拡径部32bの最小内径Yと略同じ内径Yの先端筒部32cを備えている。
すなわち、先端側管部材32の基端部32aに基端側管部材31が内挿された状態で、先端側管部材32における内径が、基端15A側ほど拡径する形態で、基端側管部材31の先端部31aの内径以上、かつ、先端側管部材32の基端筒部32dの内径Z未満に設定された拡径部32bを有する。なお、図3では、先端側管部材32の拡径部32bの最小内径Yが、基端側管部材31の先端部31aの最大内径Xと略同一である場合の例を示している。
As shown in FIG. 3, the distal end side tube member 32 is formed with a diameter-expanded portion 32 b that increases in diameter toward the proximal end 15 </ b> A side at the proximal end portion 32 a of the distal end side tube member 32. Further, a proximal end cylindrical portion 32d having an inner diameter Z substantially the same as the maximum inner diameter Z of the enlarged diameter portion 32b is provided on the proximal end 15A side of the enlarged diameter portion 32b in the proximal end portion 32a. Further, the distal end side pipe member 32 includes a distal end cylindrical portion 32c having an inner diameter Y substantially the same as the minimum inner diameter Y of the expanded diameter portion 32b on the distal end 15B side of the expanded diameter portion 32b.
That is, in a state where the proximal end side pipe member 31 is inserted into the proximal end portion 32a of the distal end side tube member 32, the inner diameter of the distal end side tube member 32 is increased toward the proximal end 15A side, and the proximal end side It has an enlarged diameter portion 32b that is set to be equal to or larger than the inner diameter of the distal end portion 31a of the tube member 31 and less than the inner diameter Z of the proximal end cylindrical portion 32d of the distal end side tube member 32. FIG. 3 shows an example in which the minimum inner diameter Y of the enlarged diameter portion 32 b of the distal end side tube member 32 is substantially the same as the maximum inner diameter X of the distal end portion 31 a of the proximal end side tube member 31.

従って、インジェクターチューブ15の誘引部30は、先端側管部材32の基端部32aに基端側管部材31を内挿することにより、これら両管部材31,32との間に径方向における所定間隔の隙間Sを形成して構成されている。これにより、誘引部30は、隙間Sを介してインジェクターチューブ15の外部とインジェクターチューブ15の内部とを連通しており、基端側管部材31と先端側管部材32とを通流する圧縮空気Hの空気流の周りにベンチュリー効果で生じた陰圧により、外部空気OAをインジェクターチューブ15内に誘引可能である。
なお、これら両管部材31,32間の径方向での所定間隔の隙間Sは、誘引部30近傍を通流する圧縮空気Hの空気流の速度、空気量、誘引部30の形状、管部材31,32の径等にも影響されるが、当該空気流の周りにベンチュリー効果で生じた陰圧により外部空気OAをインジェクターチューブ15内に誘引可能な程度の比較的狭い間隔に形成されている。また、図3では、両管部材31,32間の径方向での所定間隔の隙間Sは、基端側管部材31が内挿されている部位において、略同一間隔となるように形成されている。
Therefore, the attracting part 30 of the injector tube 15 inserts the proximal end side pipe member 31 into the proximal end part 32 a of the distal end side pipe member 32, thereby providing a predetermined radial direction between these pipe members 31 and 32. The gaps S are formed at intervals. Thereby, the attraction | suction part 30 is connecting the exterior of the injector tube 15 and the inside of the injector tube 15 through the clearance gap S, and the compressed air which flows through the base end side pipe member 31 and the front end side pipe member 32 The external air OA can be attracted into the injector tube 15 by the negative pressure generated by the venturi effect around the H air flow.
The gap S having a predetermined interval in the radial direction between the pipe members 31 and 32 is the speed of the compressed air H flowing through the vicinity of the attracting part 30, the amount of air, the shape of the attracting part 30, the pipe member Although it is influenced by the diameters 31 and 32, the external air OA is formed at a relatively narrow interval around the air flow so that the external air OA can be attracted into the injector tube 15 by the negative pressure generated by the venturi effect. . Further, in FIG. 3, the gap S having a predetermined interval in the radial direction between the pipe members 31 and 32 is formed so as to be substantially the same interval at a portion where the proximal end side pipe member 31 is inserted. Yes.

基端側管部材31の先細部31bの先端側の先端筒部31cには、この先端筒部31cと先端側管部材32の先端筒部32cとに亘って隙間Sを閉鎖するように、逆止弁としての規制部材33が設けられている。この規制部材33は、圧縮空気Hの空気流のベンチュリー効果による陰圧により誘引部30の隙間Sを介して外部空間から外部空気OAがインジェクターチューブ15内に誘引されるのを許容するが、隙間Sを介してインジェクターチューブ15内から圧縮空気Hが外部空間に通流するのを規制可能に構成されている。また、この規制部材33は、例えば、断面視で舌形状の部材であり、圧縮空気Hの空気流による陰圧が発生すると開状態となり、陰圧が発生しなくなると閉状態となる逆止弁としての機能を発揮可能な可撓性の部材により構成することができる。   The distal end tubular portion 31c on the distal end side of the tapered portion 31b of the proximal end side tube member 31 is reversely arranged so as to close the gap S across the distal end tubular portion 31c and the distal end tubular portion 32c of the distal end side tube member 32. A restricting member 33 as a stop valve is provided. The restricting member 33 allows the external air OA to be attracted into the injector tube 15 from the external space through the clearance S of the attracting portion 30 due to the negative pressure due to the venturi effect of the air flow of the compressed air H. It is configured to be able to regulate the flow of compressed air H from the injector tube 15 to the external space via S. The regulating member 33 is, for example, a tongue-shaped member in a cross-sectional view, and is open when a negative pressure is generated by the air flow of the compressed air H, and is a check valve that is closed when no negative pressure is generated. It can comprise with the flexible member which can exhibit the function as.

次に、制御部8の制御により制御されるパルス式集塵装置Aの運転状態について、通常運転と清掃運転について説明する。
パルス式集塵装置Aの通常運転において、制御部8は、図4に示すように、浄化空気排出路11の下流側に接続された吸引装置(図示せず)による吸引を開始させ、含塵空気導入路10の上流側に接続された焼却炉等(図示せず)から含塵空気Gを筐体1内の含塵空気導入室2に導入する。これにより、含塵空気Gを含塵空気導入室2側からバグフィルタ5を介して浄化空気室3側に(バグフィルタ5の外側から内側に)通流させ、当該含塵空気G中の塵埃Dをバグフィルタ5のバグ5bにより捕集して、含塵空気Gを浄化して浄化空気Cとして処理する。ここで、通常運転の開始前におけるバグフィルタ5は、バグ5bが支持体5aの外側に単に被さった状態となっているが、通常運転が開始されると、図4に示すように、バグ5bが支持体5aの内側に吸い寄せられて当該バグ5bが支持体5aの外側に密着した状態となる。この通常運転では、捕集された塵埃Dは、バグフィルタ5のバグ5bの外表面に付着することとなる。なお、制御部8は、通常運転において、圧力差検出部9(第1圧力検出部9a及び第2圧力検出部9b)からバグフィルタ5の内側と外側の内外差圧の情報をモニターしている。また、制御部8は、通常運転において、浄化空気排出路11から排出される浄化空気Cの流量を流量検出部21で検出し、当該検出された流量が所定の流量となるように、吸引装置等(図示せず)を制御する。
これにより、含塵空気G中の塵埃Dをバグフィルタ5により捕集して含塵空気Gを良好に浄化して浄化空気Cとすることができる。
Next, the normal operation and the cleaning operation will be described for the operation state of the pulse dust collector A controlled by the control of the control unit 8.
In the normal operation of the pulse dust collector A, as shown in FIG. 4, the control unit 8 starts suction by a suction device (not shown) connected to the downstream side of the purified air discharge path 11 to contain dust. Dust-containing air G is introduced into the dust-containing air introduction chamber 2 in the housing 1 from an incinerator or the like (not shown) connected to the upstream side of the air introduction path 10. As a result, the dust-containing air G is caused to flow from the dust-containing air introduction chamber 2 side to the purified air chamber 3 side through the bag filter 5 (from the outside to the inside of the bag filter 5). D is collected by the bug 5b of the bag filter 5 to purify the dust-containing air G and process it as purified air C. Here, the bag filter 5 before the start of the normal operation is in a state in which the bug 5b is simply covered on the outside of the support 5a. However, when the normal operation is started, as shown in FIG. Is attracted to the inside of the support 5a, and the bug 5b comes into close contact with the outside of the support 5a. In this normal operation, the collected dust D adheres to the outer surface of the bag 5b of the bag filter 5. In addition, the control part 8 monitors the information of the internal / external differential pressure inside and outside the bag filter 5 from the pressure difference detection part 9 (the 1st pressure detection part 9a and the 2nd pressure detection part 9b) in normal driving | operation. . Further, the control unit 8 detects the flow rate of the purified air C discharged from the purified air discharge passage 11 in the normal operation by the flow rate detection unit 21, and the suction device so that the detected flow rate becomes a predetermined flow rate. Etc. (not shown) are controlled.
Thereby, the dust D in the dust-containing air G can be collected by the bag filter 5 and the dust-containing air G can be purified well to obtain purified air C.

一方で、この通常運転が継続されると、バグフィルタ5の外表面に付着する塵埃Dが増加し、塵埃Dがバグ5bの外側に層状に付着するとともに、さらに、塵埃Dはバグ5bの外側表面のみではなく、バグ5bを形成する濾布の繊維状部分の内部にまで入り込む状態で付着する。このような状態ではバグフィルタ5において圧力損失が生じるとともに、効率よく塵埃Dを捕集することが困難となる。そこで、制御部8は、このような塵埃Dの層が形成されたことを、圧力差検出部9(第1圧力検出部9a及び第2圧力検出部9b)により検出されたバグフィルタ5の内外差圧が、上記所定の圧力差(予め設定された内外差圧)になったことにより認識し、バグフィルタ5の清掃が必要であると判定する。なお、所定の圧力差は、例えば、バグフィルタ5に塵埃Dの層が形成された状態となり、効率よく塵埃Dを捕集できない状態となったときの圧力差を予め設定しておき、制御部8の記憶部に記憶しておいたものを用いることができる。
このような状態において、本願では、通常運転を行ったままの状態(塵埃Dを捕集している状態)で、バグフィルタ5の清掃運転を行う。
On the other hand, if this normal operation is continued, the dust D adhering to the outer surface of the bag filter 5 increases, the dust D adheres in layers to the outside of the bug 5b, and further, the dust D is outside the bug 5b. It adheres not only on the surface but also into the fibrous portion of the filter cloth forming the bug 5b. In such a state, pressure loss occurs in the bag filter 5 and it is difficult to efficiently collect the dust D. Therefore, the control unit 8 detects that the dust D layer has been formed by detecting whether the pressure difference detecting unit 9 (the first pressure detecting unit 9a and the second pressure detecting unit 9b) detects the inside or outside of the bag filter 5. Recognizing that the differential pressure has reached the predetermined pressure differential (predetermined internal / external differential pressure), it is determined that the bag filter 5 needs to be cleaned. The predetermined pressure difference is set in advance as a pressure difference when, for example, a layer of dust D is formed on the bag filter 5 and dust D cannot be efficiently collected, Those stored in the storage unit 8 can be used.
In such a state, in the present application, the cleaning operation of the bag filter 5 is performed in a state where the normal operation is performed (a state where dust D is collected).

上述のとおり、制御部8は、図5に示すように、吸引装置(図示せず)の吸引を継続し通常運転を行った状態のまま、バグフィルタ5の内外差圧が所定の圧力差になった場合に、圧縮空気噴出部7を作動させてバグフィルタ5の清掃運転を行う。清掃運転として、まず、制御部8は、圧力調整弁19の開度を調節して、コンプレッサ(図示せず)からヘッダ部14内に圧縮空気Hを貯留し、ヘッダ部14内での圧縮空気Hの圧力が2MPa程度となるように制御する。   As described above, as shown in FIG. 5, the control unit 8 keeps the suction of the suction device (not shown) and performs the normal operation, and the internal / external differential pressure of the bag filter 5 becomes a predetermined pressure difference. When it becomes, the compressed air ejection part 7 is operated and the bag filter 5 is cleaned. As the cleaning operation, first, the control unit 8 adjusts the opening degree of the pressure regulating valve 19 to store the compressed air H from the compressor (not shown) in the header unit 14, and the compressed air in the header unit 14. Control is performed so that the pressure of H is about 2 MPa.

そして、制御部8は、特定の空気開閉弁16(例えば、ヘッダ部14dに対応する空気開閉弁)の開閉を制御して、各バグフィルタ5の内側からバグ5bを介して外側に通流するように、圧縮空気Hを断続的に(パルス状に)噴出させる。なお、圧縮空気Hの噴出が継続する時間は、例えば、0.1〜0.5秒程度である。
具体的には、制御部8は、図5に示すように、特定の空気開閉弁16を開操作して、圧縮空気Hの空気流を、インジェクターチューブ15内に基端15A側から先端15B側に向けて一気に高速で噴出させる。
この圧縮空気Hの空気流は、基端側管部材31内を通流し、さらに、先端側管部材32内を通流して、インジェクターチューブ15内の圧力が充分に上昇することで、先端側管部材32に設けられた複数の噴出孔17から噴出され、バグフィルタ5の内側からバグ5bを介して外側に向けて通流することとなる。
And the control part 8 controls opening and closing of the specific air on-off valve 16 (for example, air on-off valve corresponding to the header part 14d), and flows outside from each bag filter 5 via the bug 5b. Thus, the compressed air H is ejected intermittently (in a pulse form). The time for which the compressed air H continues to be ejected is, for example, about 0.1 to 0.5 seconds.
Specifically, as shown in FIG. 5, the control unit 8 opens a specific air on-off valve 16 to cause the compressed air H to flow into the injector tube 15 from the proximal end 15 </ b> A side to the distal end 15 </ b> B side. It spouts at a high speed at a stretch toward the.
The air flow of the compressed air H flows through the proximal end side pipe member 31 and further flows through the distal end side pipe member 32, and the pressure in the injector tube 15 is sufficiently increased, so that the distal end side pipe It is ejected from a plurality of ejection holes 17 provided in the member 32, and flows from the inside of the bag filter 5 to the outside through the bag 5b.

ここで、この圧縮空気Hの空気流の流れについて説明すると、ヘッダ部14から空気開閉弁16を介してインジェクターチューブ15内に一気に噴出された圧縮空気Hは、基端側管部材31内を通流し、基端筒部31dの内径Xよりも縮径した内径を有する先端部31aの先細部31bを通流するので、この先細部31bにより流速が加速されることとなる。この加速された空気流は、先細部31bの先端部の内径(図示せず)と略同じ内径の先端筒部31cを通流し、速度を維持したまま先端側管部材32内に流入する。
この際、先端側管部材32内に流入した圧縮空気Hの空気流は、非常に高速であるので、当該空気流の周りにはベンチュリー効果により陰圧が生じており、誘引部30近傍は大気圧よりも低い圧力となる。これにより、基端側管部材31と先端側管部材32との間に形成された隙間Sを介して外部空気OA(例えば、大気圧程度)がインジェクターチューブ15内の誘引部30に強制的に誘引されることとなる。この外部空気OAが誘引される際には、当該陰圧により規制部材33が開状態となっており、また、隙間Sは、比較的狭い所定の間隔であるとともに径方向で同一の間隔で形成されているので、圧縮空気Hの空気流と略同一方向に通流する外部空気OAの誘引は、より良好に行われる。
したがって、インジェクターチューブ15の誘引部30よりも先端15B側には、空気開閉弁16を介して供給された圧縮空気Hのみならず、誘引部30を介して強制的に誘引された外部空気OAも瞬時に供給されることとなり、当該インジェクターチューブ15内の圧力を極めて迅速に上昇させることが可能となる。
Here, the flow of the compressed air H will be described. The compressed air H blown into the injector tube 15 from the header portion 14 through the air on-off valve 16 passes through the proximal end side pipe member 31. Since the tip 31b of the distal end portion 31a having an inner diameter smaller than the inner diameter X of the base end cylindrical portion 31d is passed through, the flow velocity is accelerated by the tip 31b. The accelerated air flow flows through the distal end cylindrical portion 31c having the same inner diameter as the inner diameter (not shown) of the distal end portion of the tapered portion 31b, and flows into the distal end side tube member 32 while maintaining the speed.
At this time, since the air flow of the compressed air H flowing into the distal end side pipe member 32 is very high speed, a negative pressure is generated around the air flow due to the venturi effect, and the vicinity of the attracting portion 30 is large. The pressure is lower than atmospheric pressure. Thereby, the external air OA (for example, about atmospheric pressure) is forcibly applied to the attracting portion 30 in the injector tube 15 through the gap S formed between the proximal end side tube member 31 and the distal end side tube member 32. Will be attracted. When the external air OA is attracted, the regulating member 33 is opened by the negative pressure, and the gap S is formed with a relatively narrow predetermined interval and the same interval in the radial direction. Therefore, the attraction of the external air OA that flows in substantially the same direction as the air flow of the compressed air H is performed better.
Therefore, not only the compressed air H supplied via the air opening / closing valve 16 but also the external air OA forcedly attracted via the attracting part 30 is located on the tip 15B side of the attracting part 30 of the injector tube 15. It is supplied instantaneously, and the pressure in the injector tube 15 can be increased very quickly.

このようにインジェクターチューブ15内の圧力を極めて迅速に上昇させることが可能となったことを、図6〜図8を用いて説明する。図6は、本実施形態の実施例に係るパルス式集塵装置Aの清掃運転時におけるインジェクターチューブ15内の静圧分布を示すグラフ図、図7は、比較例に係るパルス式集塵装置の清掃運転時におけるインジェクターチューブ内の静圧分布を示すグラフ図、図8は、空気開閉弁の開操作からの経過時間と、ある噴出孔位置での圧力(静圧)との関係を示すグラフ図である。なお、静圧は、インジェクターチューブ15内を通流する圧縮空気Hの空気流の速度と平行な面の圧力である。   The fact that the pressure in the injector tube 15 can be increased extremely quickly will be described with reference to FIGS. FIG. 6 is a graph showing the static pressure distribution in the injector tube 15 during the cleaning operation of the pulse dust collector A according to the example of the present embodiment, and FIG. 7 shows the pulse dust collector according to the comparative example. Fig. 8 is a graph showing the static pressure distribution in the injector tube during the cleaning operation, and Fig. 8 is a graph showing the relationship between the elapsed time from the opening operation of the air on-off valve and the pressure (static pressure) at a certain ejection hole position. It is. The static pressure is a pressure on a plane parallel to the velocity of the air flow of the compressed air H flowing through the injector tube 15.

図6に示すように、本実施形態の実施例では、空気開閉弁16の開操作を行った直後のインジェクターチューブ15内の壁面付近での静圧分布は、負圧(陰圧)状態の基端15A側から先端15B側に向かうにつれて静圧が上昇するが、誘引部30近傍で一気に上昇して、0(大気圧)付近にまで押し上げられている。これは、基端側管部材31内において高速の圧縮空気Hの空気流により負圧となっていたものが、大気開放された隙間Sを介して誘引部30に誘引された外部空気OAにより、誘引部30近傍が瞬時に0(大気圧)付近にまで昇圧されたことによるものである。また、圧縮空気Hに加えて、外部空気OAが誘引されたことにより、インジェクターチューブ15内の静圧を全体(特に、先端側管部材32内)にわたり上昇させるために必要な空気量が供給されているので、複数の噴出孔17が配置された領域及び先端部15B付近でも既に静圧が比較的高い状態となっている。   As shown in FIG. 6, in the example of the present embodiment, the static pressure distribution near the wall surface in the injector tube 15 immediately after the opening operation of the air on-off valve 16 is based on a negative pressure (negative pressure) state. The static pressure rises from the end 15A side toward the tip 15B side, but rises all at once in the vicinity of the attracting portion 30 and is pushed up to near 0 (atmospheric pressure). This is because the negative pressure due to the air flow of the high-speed compressed air H in the proximal end side pipe member 31 is caused by the external air OA attracted to the attracting part 30 through the clearance S opened to the atmosphere, This is because the vicinity of the attracting unit 30 is instantaneously boosted to near 0 (atmospheric pressure). In addition to the compressed air H, the external air OA is attracted, so that an air amount necessary for raising the static pressure in the injector tube 15 over the whole (in particular, the distal end side pipe member 32) is supplied. Therefore, the static pressure is already relatively high even in the region where the plurality of ejection holes 17 are arranged and in the vicinity of the tip portion 15B.

一方、図7に示すように、誘引部30を備えない比較例のパルス式集塵装置において、実施例と同様に清掃運転を行った場合には、空気開閉弁の開操作を行った直後のインジェクターチューブ内の壁面付近での静圧分布は、負圧(陰圧)状態の基端側から先端に向かうにつれて静圧が上昇するが、上記のように誘引部30での急激な静圧の上昇が無く、静圧が0(大気圧)付近となる箇所が先端側にずれている。すなわち、実施例では誘引部30近傍で0付近となっているのに対し、比較例では誘引部30に対応する箇所よりも先端側で静圧が0付近となっている。また、インジェクターチューブ内には、圧縮空気Hが供給されているのみであるので、インジェクターチューブ内の静圧を全体にわたり上昇させるために必要な空気量が十分に供給されていないので、複数の噴出孔が配置された領域及び先端部15B付近では静圧が比較的低い状態となっている。   On the other hand, as shown in FIG. 7, in the pulse type dust collector of the comparative example that does not include the attracting unit 30, when the cleaning operation is performed in the same manner as in the example, immediately after the opening operation of the air on-off valve is performed. In the static pressure distribution near the wall surface in the injector tube, the static pressure increases from the base end side in the negative pressure (negative pressure) state to the tip end. There is no increase and the point where the static pressure is near 0 (atmospheric pressure) is shifted to the tip side. That is, in the embodiment, the vicinity of the attracting portion 30 is near 0, whereas in the comparative example, the static pressure is near 0 on the tip side of the portion corresponding to the attracting portion 30. In addition, since only the compressed air H is supplied into the injector tube, a sufficient amount of air is not supplied to increase the static pressure in the injector tube as a whole. The static pressure is relatively low in the region where the holes are arranged and in the vicinity of the tip portion 15B.

さらに、図8に示すように、ある噴出孔17が設けられた位置における静圧は、空気開閉弁16の開操作から時間が経過するにつれて、実施例では、グラフの傾きが急で非常に短時間で一気に圧力が上昇しており(図8の1点鎖線参照)、比較例では、グラフの傾きが比較的緩やかで圧力が上昇するまでに比較的長い時間が必要であることが判明した。   Furthermore, as shown in FIG. 8, the static pressure at the position where a certain ejection hole 17 is provided is very short with a steep slope of the graph as time elapses from the opening operation of the air on-off valve 16. The pressure increased at a stroke over time (see the one-dot chain line in FIG. 8), and in the comparative example, it was found that the slope of the graph was relatively gentle and a relatively long time was required until the pressure increased.

したがって、本実施形態に係るパルス式集塵装置Aのように上記特徴構成を備えたインジェクターチューブ15を採用することにより、当該インジェクターチューブ15内の圧力を極めて迅速に上昇させることが可能となる。また、空気開閉弁16の構成を改変等することなく従来と同様の構成の空気開閉弁16を用いた場合でも、インジェクターチューブ15内の圧力を極めて迅速に上昇させることが可能となる。   Therefore, by adopting the injector tube 15 having the above-described characteristic configuration as in the pulse dust collector A according to the present embodiment, the pressure in the injector tube 15 can be increased extremely quickly. Further, even when the air on / off valve 16 having the same configuration as the conventional one is used without modifying the configuration of the air on / off valve 16, the pressure in the injector tube 15 can be increased very quickly.

そして、空気開閉弁16の開操作に伴って供給された圧縮空気H及び誘引部30により誘引された外部空気OAは、インジェクターチューブ15内の圧力を極めて迅速に上昇させながら、インジェクターチューブ15の先端15B側に到達し、再度、基端側15Aに通流を始めることとなる。この段階では、インジェクターチューブ15内の圧力が十分に上昇しているため、この基端15A側に向かう圧縮空気Hの空気流により、先端側管部材32に設けられた複数の噴出孔17から順次各バグフィルタ5の内部に噴出されることとなる。具体的には、この圧縮空気Hは主として、図5に示す、噴出孔17e、17d、17c、17b、17aの順に噴出されることとなる。
このように極めて迅速に圧力を上昇させた状態で、噴出孔17から圧縮空気Hをバグフィルタ5内へ噴出することにより、極めて高エネルギ状態の圧力波をバグフィルタ5内へ伝播させることができる。これにより、バグ5bは内側に収縮した状態(図4に示す状態)から反転して、バグ5bが外側に向けて確実に膨張し緊張状態となり(図5参照)、バグ5bを構成する繊維状部分の目開きが大きくなって、当該バグ5bの外側表面に層状に付着した塵埃Dを払い落として良好に清掃できる。
Then, the compressed air H supplied by the opening operation of the air on-off valve 16 and the external air OA attracted by the attracting unit 30 increase the pressure in the injector tube 15 very rapidly, and the tip of the injector tube 15. It reaches the 15B side and starts flowing again to the base end side 15A. At this stage, since the pressure in the injector tube 15 is sufficiently increased, the air flow of the compressed air H toward the proximal end 15A side sequentially causes the plurality of ejection holes 17 provided in the distal end side pipe member 32 to sequentially flow. It will be ejected inside each bag filter 5. Specifically, the compressed air H is mainly ejected in the order of the ejection holes 17e, 17d, 17c, 17b, and 17a shown in FIG.
In this manner, the pressure wave in the extremely high energy state can be propagated into the bag filter 5 by ejecting the compressed air H into the bag filter 5 from the ejection hole 17 in a state where the pressure is increased very quickly. . As a result, the bug 5b is reversed from the state contracted inward (the state shown in FIG. 4), and the bag 5b is surely expanded outward and is in a tension state (see FIG. 5). The opening of the portion becomes large, and the dust D adhering in a layered manner to the outer surface of the bug 5b can be removed to clean well.

よって、装置の大型化及び消費空気量の上昇等の問題を生じることなく、開閉弁の開操作に伴うインジェクターチューブ15内の圧力上昇速度を極めて迅速なものとして、噴出孔17からの圧縮空気Hのフィルタ部内への噴出により極めて高エネルギ状態の圧力波を形成し、その圧力波のフィルタ部内への伝播による塵埃の払い落とし性能を向上することが可能となる。   Therefore, without causing problems such as an increase in the size of the apparatus and an increase in the amount of consumed air, the pressure rise speed in the injector tube 15 accompanying the opening operation of the on-off valve can be made extremely quick, and the compressed air H from the ejection hole 17 can be obtained. The pressure wave in an extremely high energy state is formed by jetting into the filter part, and it is possible to improve the dust removal performance by propagation of the pressure wave into the filter part.

〔別実施形態〕
(1)上記実施形態では、インジェクターチューブ15の誘引部30を、基端側管部材31と先端側管部材32との間に径方向の隙間Sを形成した状態で基端側管部材31を先端側管部材32の基端部32aに所定部位まで内挿することにより構成し、基端側管部材31はその先端部31aに先細部31b及び先端筒部31cを、その基端部(図示せず)に基端筒部31dを備え、先端側管部材32はその先端部(図示せず)に先端筒部32cを、その基端部32aに縮径部32b及び基端筒部32dを備えるように構成したが、誘引部30に外部空気OAを良好に誘引することができる構成であれば、特にこの構成に限定されるものではない。例えば、以下の(1−A)から(1−C)の構成を例示することができる。
[Another embodiment]
(1) In the above-described embodiment, the proximal end side tube member 31 is moved in a state where the radial gap S is formed between the proximal end side tube member 31 and the distal end side tube member 32. The proximal end tube member 31 is configured to be inserted into the proximal end portion 32a of the distal end side tube member 32 up to a predetermined portion. The proximal end side tube member 31 has a distal end portion 31a and a distal end portion 31b and a distal end cylindrical portion 31c, and a proximal end portion (see FIG. (Not shown) is provided with a proximal end cylindrical portion 31d, and the distal end side tube member 32 has a distal end cylindrical portion 32c at the distal end portion (not shown), and a reduced diameter portion 32b and a proximal end cylindrical portion 32d at the proximal end portion 32a. Although it comprised so that it might comprise, if it is the structure which can attract the external air OA to the attracting part 30 favorably, it will not be specifically limited to this structure. For example, the following configurations (1-A) to (1-C) can be exemplified.

(1−A)例えば、図9に示すように、内径の変化する箇所がない円筒状の先端側管部材42に、内径の変化する箇所がない円筒状の基端側管部材41を、両管部材41、42の間に径方向の隙間Sを形成した状態で所定部位まで内挿することにより、誘引部40を構成することも可能である。これにより、非常に単純な構成で、ベンチュリー効果を利用して外部空気OAを誘引する誘引部40を形成することが可能となる。
この場合には、基端側管部材41の先端部(先端側開口部、図示せず)の内周面と先端側管部材42の内周面とに亘って隙間Sを閉鎖するように、逆止弁としての規制部材43を設けることができる。
(1-A) For example, as shown in FIG. 9, a cylindrical proximal tube member 41 having no inner diameter change portion is connected to a cylindrical distal tube member 42 having no inner diameter change portion. It is also possible to configure the attracting part 40 by inserting up to a predetermined part in a state where a radial gap S is formed between the pipe members 41 and 42. Thereby, it is possible to form the attracting part 40 that attracts the external air OA using the Venturi effect with a very simple configuration.
In this case, the gap S is closed over the inner peripheral surface of the distal end portion (distal end opening, not shown) of the proximal end side tube member 41 and the inner peripheral surface of the distal end side tube member 42. A regulating member 43 as a check valve can be provided.

(1−B)また、例えば、図10に示すように、上記実施形態の先端側管部材32と同様の構成の先端側管部材52における基端部52aに、内径の変化する箇所がない円筒状の基端側管部材51を、両管部材51、52の間に径方向の隙間Sを形成した状態で所定部位まで内挿することにより、誘引部50を構成することも可能である。この場合、図10の先端側管部材52において、基端部52aが先端側管部材32における基端部32aに、拡径部52bが拡径部32bに、先端筒部52cが先端筒部32cに、基端筒部52dが基端筒部32dにそれぞれ相当することとなる。
これにより、先端側管部材52の拡径部52bの最小内径及び先端筒部52cの内径が基端側管部材51の先端部(先端側開口部、図示せず)の内径以上、かつ、先端側管部材52の基端筒部52dの内径未満となっているので、圧縮空気Hの空気流が基端側管部材51を通過した後、先端側管部材52を通流する際において、先端側管部材52の断面積の拡大に伴う空気流の速度の減速を抑制することができ、当該空気流によるインジェクターチューブ15内の圧力上昇速度の低下を防止することができる。
この場合、基端側管部材51の先端部(先端側開口部、図示せず)の内周面には、当該内周面と先端側管部材52の先端筒部52cの内周面とに亘って隙間Sを閉鎖するように、逆止弁としての規制部材53を設けることができる。
(1-B) Further, for example, as shown in FIG. 10, the base end portion 52a of the distal end side tube member 52 having the same configuration as the distal end side tube member 32 of the above-described embodiment does not have a portion where the inner diameter changes. It is also possible to configure the attracting portion 50 by inserting a cylindrical proximal end pipe member 51 up to a predetermined site with a radial gap S formed between the pipe members 51 and 52. In this case, in the distal end side tube member 52 of FIG. 10, the proximal end portion 52a is the proximal end portion 32a of the distal end side tube member 32, the enlarged diameter portion 52b is the enlarged diameter portion 32b, and the distal end tubular portion 52c is the distal end tubular portion 32c. Further, the base end cylinder part 52d corresponds to the base end cylinder part 32d.
As a result, the minimum inner diameter of the enlarged diameter portion 52b of the distal end side tube member 52 and the inner diameter of the distal end tubular portion 52c are equal to or larger than the inner diameter of the distal end portion (distal end opening, not shown) of the proximal end side tube member 51. Since the inner diameter of the proximal tube portion 52d of the side tube member 52 is smaller than the inner diameter, the distal end of the compressed air H flows through the distal tube member 52 after passing through the proximal tube member 51. It is possible to suppress a reduction in the speed of the air flow accompanying an increase in the cross-sectional area of the side pipe member 52, and it is possible to prevent a decrease in the pressure increase rate in the injector tube 15 due to the air flow.
In this case, the inner peripheral surface of the distal end portion (distal end opening, not shown) of the proximal end side tube member 51 is connected to the inner peripheral surface and the inner peripheral surface of the distal end tubular portion 52 c of the distal end side tube member 52. A regulating member 53 as a check valve can be provided so as to close the gap S.

(1−C)さらに、例えば、図11に示すように、内径の変化する箇所がない円筒状の先端側管部材62に、上記実施形態の基端側管部材31の先細部31bと同様の構成を備えた基端側管部材61を、両管部材61、62の間に径方向の隙間Sを形成した状態で所定部位まで内挿することにより、誘引部60を構成することも可能である。この場合、基端側管部材61における先端部61aが上記実施形態における先端部31aに、先細部61bが先細部31bに相当し、上記実施形態における先端筒部31cに相当する構成は存在しないこととなる。これにより、基端側管部材61の先細部61bの先端側から先端側管部材62内に連通した箇所に形成された誘引部60近傍においてベンチュリー効果による陰圧の発生をより増大させて、当該誘引部60からインジェクターチューブ15内への外部空気の誘引力を増大させることができ、結果、インジェクターチューブ15内の圧力上昇速度をより一層上昇させることができる。 (1-C) Further, for example, as shown in FIG. 11, the cylindrical distal end side tube member 62 having no portion where the inner diameter changes is similar to the tapered portion 31 b of the proximal end side tube member 31 of the above embodiment. It is also possible to configure the attracting part 60 by inserting the proximal end side pipe member 61 having the configuration into a predetermined part with a radial gap S formed between the pipe members 61 and 62. is there. In this case, the distal end portion 61a of the proximal end side pipe member 61 corresponds to the distal end portion 31a in the above embodiment, the tapered portion 61b corresponds to the tapered detail 31b, and there is no configuration corresponding to the distal end tubular portion 31c in the above embodiment. It becomes. This further increases the generation of negative pressure due to the Venturi effect in the vicinity of the attracting portion 60 formed in the portion communicating from the distal end side of the tapered portion 61b of the proximal end side tube member 61 into the distal end side tube member 62, The attraction force of the external air from the attracting part 60 into the injector tube 15 can be increased, and as a result, the pressure increase speed in the injector tube 15 can be further increased.

(2)上記実施形態では、インジェクターチューブ15の断面が円筒状である構成について説明したが、圧縮空気Hが良好に通流することができる構成であれば、特にこの構成に限定されるものではなく、例えば、三角、矩形、多角形状等種々の形状を採用することができる。 (2) In the above-described embodiment, the configuration in which the cross section of the injector tube 15 is cylindrical has been described. However, the configuration is not particularly limited to this configuration as long as the compressed air H can flow well. For example, various shapes such as a triangle, a rectangle, and a polygon can be employed.

(3)上記実施形態では、フィルタ部としてバグフィルタ5を用いて構成したが、含塵空気G中の塵埃Dを良好に捕集することができるフィルタであれば、特に制限なく用いることができる。例えば、フィルタ部としてセラミックフィルタを採用することも可能である。この場合、セラミックフィルタは比較的硬く、圧縮空気Hが内側に噴出された場合であってもバグフィルタ5のように外側に膨張して緊張状態となることは殆どないが、圧縮空気Hによりインジェクターチューブ15内の圧力上昇速度を極めて迅速なものとすることにより、噴出孔17の圧縮空気Hのセラミックフィルタへの噴出により極めて高エネルギ状態の圧力波を形成し、その圧力波のセラミックフィルタ内への伝播による塵埃の払い落とし性能を向上することが可能となる。 (3) In the above embodiment, the bag filter 5 is used as the filter unit. However, any filter can be used as long as it is a filter that can satisfactorily collect the dust D in the dust-containing air G. . For example, it is possible to employ a ceramic filter as the filter unit. In this case, the ceramic filter is relatively hard, and even when the compressed air H is jetted inward, the ceramic filter hardly swells outward and becomes in tension like the bag filter 5. By making the pressure rise rate in the tube 15 extremely rapid, a pressure wave in an extremely high energy state is formed by the jet of the compressed air H from the jet hole 17 to the ceramic filter, and the pressure wave enters the ceramic filter. It is possible to improve the dust removal performance due to the propagation of.

以上説明したように、装置の大型化及び消費空気量の上昇等の問題を生じることなく、開閉弁の開操作に伴うインジェクターチューブ内の圧力上昇速度を極めて迅速なものとして、噴出孔の圧縮空気の噴出により極めて高エネルギ状態の圧力波を形成し、その圧力波のフィルタ部内への伝播による塵埃の払い落とし性能を向上することが可能なパルス式集塵機を提供できた。   As described above, the compressed air in the ejection hole can be set to an extremely rapid pressure increase rate in the injector tube accompanying the opening operation of the on-off valve without causing problems such as an increase in the size of the device and an increase in the amount of air consumed. It was possible to provide a pulse type dust collector capable of forming a pressure wave in an extremely high energy state by jetting and improving dust removal performance by propagation of the pressure wave into the filter part.

1 筐体
2 含塵空気導入室
3 浄化空気室
4 区画壁
5 バグフィルタ(フィルタ部)
6 連通部
7 圧縮空気噴出部
14 ヘッダ部(圧縮空気源)
15 インジェクターチューブ
15A 基端
15B 先端
16 空気開閉弁(開閉弁)
17 噴出孔
30 誘引部
31 基端側管部材
31a 基端側管部材の先端部
31b 先細部(基端側管部材の先端部)
32 先端側管部材
32a 先端側管部材の基端部
32b 拡径部(先端側管部材の基端部)
A パルス式集塵装置
D 塵埃
G 含塵空気
C 浄化空気
H 圧縮空気
OA 外部空気
P 基端側領域
S 隙間
X 基端側管部材の先端部の最大内径(基端側管部材の基端筒部の内径)
Y 先端側管部材の基端部の最小内径(先端側管部材の先端筒部の内径)
Z 先端側管部材の基端部の最大内径(先端側管部材の基端筒部の内径)
DESCRIPTION OF SYMBOLS 1 Case 2 Dust-containing air introduction chamber 3 Purified air chamber 4 Partition wall 5 Bag filter (filter part)
6 Communication part 7 Compressed air ejection part 14 Header part (compressed air source)
15 Injector tube 15A Base end 15B Tip 16 Air on-off valve (on-off valve)
17 Ejection hole 30 Attraction part 31 Base end side pipe member 31a Tip end part 31b of base end side pipe member Taper (tip part of base end side pipe member)
32 distal end side pipe member 32a proximal end part 32b of distal end side pipe member expanded diameter part (proximal end part of distal end side pipe member)
A Pulse-type dust collector D Dust G Dust-containing air C Purified air H Compressed air OA External air P Base end region S Clearance X Maximum inner diameter of the base end tube member (base tube of the base end tube member Inside diameter)
Y Minimum inner diameter of the proximal end of the distal tube member (inner diameter of the distal tube portion of the distal tube member)
Z Maximum inner diameter of the proximal end of the distal tube member (inner diameter of the proximal tube of the distal tube member)

Claims (4)

区画壁により内部が含塵空気導入室と浄化空気室とに区画された筐体と、
前記区画壁のうち前記含塵空気導入室と前記浄化空気室とを連通する複数の連通部のそれぞれに設けられ、前記含塵空気導入室側から前記浄化空気室側に通流する含塵空気中に含まれる塵埃を捕集する複数のフィルタを有するフィルタ部と、
前記浄化空気室側から前記フィルタ部を介して前記含塵空気導入室側に圧縮空気を噴出させて、前記フィルタ部に付着した塵埃を清掃する圧縮空気噴出部とを備え、
前記圧縮空気噴出部が、基端が圧縮空気源に接続されるとともに先端が閉塞されたインジェクターチューブと、前記圧縮空気源から前記圧縮空気を前記インジェクターチューブ内へ断続的に供給可能な開閉弁と、前記インジェクターチューブの長手方向に複数設けられ、前記インジェクターチューブ内に供給された前記圧縮空気を前記複数のフィルタに各別に噴出させる噴出孔とを備えたパルス式集塵装置であって、
前記圧縮空気噴出部の前記インジェクターチューブにおいて、前記開閉弁が設けられる基端と前記複数の噴出孔のうち前記基端に最も近接する噴出孔が設けられる箇所との間である基端側領域に、前記開閉弁を介して前記インジェクターチューブ内に前記基端側から前記先端側に向けて供給された前記圧縮空気の空気流により、外部空気を前記インジェクターチューブ内に誘引可能な誘引部を備えたパルス式集塵装置。
A housing whose interior is partitioned into a dust-containing air introduction chamber and a purified air chamber by a partition wall;
Dust-containing air that is provided in each of a plurality of communicating portions that communicate the dust-containing air introduction chamber and the purified air chamber in the partition wall and flows from the dust-containing air introduction chamber side to the purified air chamber side. A filter unit having a plurality of filters for collecting dust contained therein;
A compressed air ejecting section for ejecting compressed air from the purified air chamber side to the dust-containing air introducing chamber side through the filter section and cleaning dust adhering to the filter section;
An injector tube having a proximal end connected to a compressed air source and closed at a distal end; and an on-off valve capable of intermittently supplying the compressed air from the compressed air source into the injector tube. A pulse-type dust collector provided with a plurality of nozzle tubes in the longitudinal direction of the injector tube, each of which includes a jet hole for jetting the compressed air supplied into the injector tube separately to the plurality of filters,
In the injector tube of the compressed air ejection part, in a proximal side region between a proximal end where the on-off valve is provided and a location where an ejection hole closest to the proximal end is provided among the plurality of ejection holes. And an attracting portion capable of attracting external air into the injector tube by an air flow of the compressed air supplied from the proximal end side toward the distal end side into the injector tube through the on-off valve. Pulse type dust collector.
前記インジェクターチューブが、前記基端側に設けられる基端側管部材と、前記先端側に設けられる先端側管部材とを備えて構成され、
前記誘引部が、前記基端側管部材と前記先端側管部材との間に径方向の隙間を形成した状態で前記基端側管部材が前記先端側管部材に内挿されることにより構成されている請求項1に記載のパルス式集塵装置。
The injector tube is configured to include a proximal side tube member provided on the proximal side and a distal side tube member provided on the distal side,
The attraction portion is configured by the proximal end side tube member being inserted into the distal end side tube member in a state where a radial gap is formed between the proximal end side tube member and the distal end side tube member. The pulse dust collector according to claim 1.
前記先端側管部材の基端部が基端側ほど拡径する拡径部を有し、拡径された前記先端側管部材の基端部に前記基端側管部材が内挿されている請求項2に記載のパルス式集塵装置。   The proximal end portion of the distal end side tube member has an enlarged diameter portion whose diameter increases toward the proximal end side, and the proximal end side tube member is inserted into the proximal end portion of the expanded distal end side tube member. The pulse type dust collector according to claim 2. 前記基端側管部材の先端部には、前記基端側管部材の先端部の先端側ほど縮径する先細部が形成されている請求項2又は3に記載のパルス式集塵装置。   The pulse type dust collector according to claim 2 or 3, wherein a tip end portion of the base end side pipe member is formed with a taper that decreases in diameter toward a tip end side of the tip end portion of the base end side tube member.
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JP2013107054A (en) * 2011-11-22 2013-06-06 Nippon Spindle Mfg Co Ltd Dust collector
JP2015166059A (en) * 2014-03-04 2015-09-24 日本スピンドル製造株式会社 dust collector
CN113332803A (en) * 2021-07-08 2021-09-03 安徽国能亿盛环保科技有限公司 Water curtain cleaning device of bag type dust collector and implementation method thereof

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