JP2010012419A - Cleaning method of filter in dust collector - Google Patents

Cleaning method of filter in dust collector Download PDF

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JP2010012419A
JP2010012419A JP2008175206A JP2008175206A JP2010012419A JP 2010012419 A JP2010012419 A JP 2010012419A JP 2008175206 A JP2008175206 A JP 2008175206A JP 2008175206 A JP2008175206 A JP 2008175206A JP 2010012419 A JP2010012419 A JP 2010012419A
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gas
dust
filter
cleaning
valve
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JP5149089B2 (en
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Yasuhiro Takahashi
康弘 高橋
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Taiyo Nippon Sanso Corp
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<P>PROBLEM TO BE SOLVED: To provide a cleaning method of a filter in a dust collector which is capable of improving the back-washing effect by reliably carrying out expansion and contraction of the filter. <P>SOLUTION: During back-washing of a filter by jetting a cleaning gas in the reverse direction to that in a dust collecting step, an operation of flowing gas in the same direction as that in the dust collecting step is intermittently carried out to forcibly contract the filter expanded by the jetting of the cleaning gas by the gas flowing in the same direction as that in the dust collecting step, and thus the efficiency of the back-washing by repeating expansion and contraction is improved. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、集塵機におけるフィルタの洗浄方法に関し、詳しくは、集塵工程時とは逆方向に洗浄用ガスを流してフィルタを逆洗浄する逆洗浄工程を有する集塵機におけるフィルタの洗浄方法に関する。   The present invention relates to a filter cleaning method in a dust collector, and more particularly, to a filter cleaning method in a dust collector having a reverse cleaning step in which a filter is reversely cleaned by flowing a cleaning gas in a direction opposite to that in the dust collection step.

フィルタによってガス中の塵を除去する集塵機では、洗浄用ガスを集塵工程時とは逆方向にフィルタ内に噴出することにより、フィルタ表面に付着した塵を払い落とす逆洗浄工程を行うことで集塵能力を回復させ、集塵処理を長時間連続的に行えるようにしている(例えば、特許文献1参照。)。
特開2007−175635号公報
In a dust collector that removes dust in the gas using a filter, the cleaning gas is ejected into the filter in the direction opposite to that during the dust collection process, thereby performing a reverse cleaning process in which dust attached to the filter surface is removed. The dust capacity is recovered, and the dust collection process can be performed continuously for a long time (see, for example, Patent Document 1).
JP 2007-175635 A

しかし、フィルタの表面に付着した塵が付着性を有するものである場合は、逆洗浄工程で洗浄用ガスを集塵工程とは逆方向にフィルタに流通させただけでは、十分に塵を払い落とすことができず、次第に厚く堆積し、付着性を有しない塵の場合に比べて連続運転時間が短くなってしまう。   However, if the dust adhering to the surface of the filter is adhering, the dust can be removed sufficiently by simply passing the cleaning gas through the filter in the reverse direction of the dust collection process in the reverse cleaning process. However, the continuous operation time is shortened as compared with the case of dust that gradually accumulates thick and does not have adhesiveness.

このため、洗浄用ガスを間欠的にフィルタ内に噴出させ、洗浄用ガスの噴出によって膨張したフィルタを、洗浄用ガスの非導入時にフィルタ自身の復元力によって収縮させ、この膨張と収縮とを繰り返すことで逆洗浄効果を向上させるようにしている。しかし、表面に付着性の塵が大量に付着していると、フィルタ自身の復元力だけでは十分に収縮しないことがあり、膨張と収縮との繰り返しによる逆洗浄の効果を十分に達成できないことがあった。   Therefore, the cleaning gas is intermittently ejected into the filter, and the filter expanded by the cleaning gas is contracted by the restoring force of the filter itself when the cleaning gas is not introduced, and this expansion and contraction are repeated. By doing so, the reverse cleaning effect is improved. However, if a large amount of adhesive dust adheres to the surface, the filter may not sufficiently shrink only with the restoring force of the filter itself, and the effect of backwashing by repeated expansion and contraction may not be achieved sufficiently. there were.

そこで本発明は、フィルタの膨張と収縮とを確実に行うことによって逆洗浄の効果を向上させることができる集塵機におけるフィルタの洗浄方法を提供することを目的としている。   Therefore, an object of the present invention is to provide a filter cleaning method in a dust collector that can improve the effect of back cleaning by reliably performing expansion and contraction of the filter.

上記目的を達成するため、本発明の集塵機におけるフィルタの洗浄方法は、集塵工程時とは逆方向に洗浄用ガスを噴出させてフィルタの逆洗浄を行う集塵機におけるフィルタの洗浄方法において、前記逆洗浄を行っている間に、集塵工程時と同方向にガスを流す操作を間欠的に行うことを特徴としている。   In order to achieve the above object, the filter cleaning method in the dust collector of the present invention is the reverse of the filter cleaning method in the dust collector in which the cleaning gas is jetted in the reverse direction to that in the dust collection step to perform reverse cleaning of the filter. During the cleaning, the gas flow operation is intermittently performed in the same direction as in the dust collection process.

また、本発明の集塵機におけるフィルタの洗浄方法は、筐体内を流入室と流出室とに区画する区画壁と、該区画壁から流入室側に突設した有底筒状のバグフィルタと、前記流出室側から前記バグフィルタ内に洗浄用ガスを噴出する洗浄用ガス噴出部と、前記流入室に含塵ガスを導入する含塵ガス導入経路と、該含塵ガス導入経路に設けられた含塵ガス導入弁と、前記流出室から無塵ガスを導出する無塵ガス導出経路と、該無塵ガス導出経路に設けられた無塵ガス導出弁と、前記無塵ガス導出経路における前記無塵ガス導出弁の下流側に設けられたガス吸引装置と、前記流出室内を外気に開放する開放経路と、該開放経路に設けられた開放弁とを備えた集塵機におけるフィルタの洗浄方法であって、前記含塵ガス導入弁及び前記無塵ガス導出弁を閉じ、前記開放弁を開いた状態で前記洗浄用ガス噴出部から前記洗浄用ガスを前記バグフィルタ内に噴出して該バグフィルタの逆洗浄を行っている間に、前記無塵ガス導出弁を開くとともに前記開放弁を閉じて前記流出室内のガスを前記ガス吸引装置にて吸引する操作を間欠的に行うことを特徴としている。   The filter cleaning method in the dust collector of the present invention includes a partition wall that divides the inside of the housing into an inflow chamber and an outflow chamber, a bottomed cylindrical bag filter that protrudes from the partition wall toward the inflow chamber, A cleaning gas jetting part for jetting cleaning gas into the bag filter from the outflow chamber side, a dust-containing gas introduction path for introducing dust-containing gas into the inflow chamber, and a dust-containing gas provided in the dust-containing gas introduction path A dust gas introduction valve, a dust-free gas lead-out path for drawing dust-free gas from the outflow chamber, a dust-free gas lead-out valve provided in the dust-free gas lead-out path, and the dust-free gas in the dust-free gas lead-out path A method for cleaning a filter in a dust collector comprising a gas suction device provided on the downstream side of a gas outlet valve, an open path for opening the outflow chamber to outside air, and an open valve provided in the open path, The dust-containing gas inlet valve and the dust-free gas outlet valve The dust-free gas outlet valve is closed while the cleaning gas is jetted into the bag filter by reversely cleaning the bag filter while the opening valve is closed. The opening valve is closed and the operation of sucking the gas in the outflow chamber with the gas suction device is intermittently performed.

本発明の集塵機におけるフィルタの洗浄方法によれば、集塵工程時とは逆方向の流れのガスによって膨張したフィルタを強制的に収縮させることができるので、膨張と収縮との繰り返しによるフィルタの逆洗浄を効率よく行うことができる。   According to the filter cleaning method in the dust collector of the present invention, the filter expanded by the gas flowing in the direction opposite to that during the dust collection process can be forcibly contracted. Cleaning can be performed efficiently.

図1乃至図3は、本発明の集塵機におけるフィルタの洗浄方法を適用した集塵機の一形態例を示す説明図であって、図1は集塵工程を行っているときの集塵機の状態を示す説明図、図2は逆洗浄操作を行っているときの集塵機の状態を示す説明図、図3は収縮操作を行っているときの集塵機の状態を示す説明図である。また、図4及び図5はバグフィルタの膨張、収縮を説明するためのもので、図4は逆洗浄操作中に膨張したバグフィルタの状態を示す説明図、図5は収縮操作中に収縮したバグフィルタの状態を示す説明図である。なお、図1〜図3において、白抜きの弁は開状態を、黒塗りの弁は閉状態を表している。   FIG. 1 to FIG. 3 are explanatory views showing an embodiment of a dust collector to which the filter cleaning method in the dust collector of the present invention is applied, and FIG. 1 is an explanation showing the state of the dust collector when the dust collecting step is performed. FIG. 2 is an explanatory view showing the state of the dust collector when performing a reverse cleaning operation, and FIG. 3 is an explanatory view showing the state of the dust collector when performing a shrinking operation. 4 and 5 are for explaining the expansion and contraction of the bag filter. FIG. 4 is an explanatory view showing the state of the bag filter expanded during the back washing operation. FIG. 5 is contracted during the contraction operation. It is explanatory drawing which shows the state of a bug filter. In FIGS. 1 to 3, the white valve represents an open state, and the black valve represents a closed state.

この集塵機は、筐体11内を区画壁12によって流入室13と流出室14とに区画し、前記区画壁12から流入室13側に向けて有底筒状のバグフィルタ15を複数突設したものであって、流入室13には、燃焼除害装置のような燃焼器16などで発生した含塵ガスを導入する含塵ガス導入経路17が接続され、流入室13の底部には、逆洗浄によってバグフィルタ15から剥離して落下した塵を回収する回収容器18が着脱可能に設けられている。また、流出室14には、バグフィルタ15にて除塵された無塵ガスを導出する無塵ガス導出経路19が接続されるとともに、バグフィルタ15の開口からバグフィルタ15の内部に洗浄用ガスを噴出する洗浄用ガス噴出部20が設けられている。   In the dust collector, the inside of the housing 11 is partitioned into an inflow chamber 13 and an outflow chamber 14 by a partition wall 12, and a plurality of bottomed cylindrical bag filters 15 project from the partition wall 12 toward the inflow chamber 13. The inflow chamber 13 is connected to a dust-containing gas introduction path 17 for introducing dust-containing gas generated in a combustor 16 such as a combustion abatement device. A collection container 18 that collects dust that has fallen off the bag filter 15 by cleaning is detachably provided. The outflow chamber 14 is connected to a dust-free gas extraction path 19 for extracting the dust-free gas removed by the bag filter 15, and cleaning gas is introduced into the bag filter 15 from the opening of the bag filter 15. A cleaning gas ejection portion 20 is provided for ejection.

前記含塵ガス導入経路17と前記無塵ガス導出経路19とはバイパス弁21を有するバイパス経路22によって接続されており、含塵ガス導入経路17には含塵ガス導入弁23が、無塵ガス導出経路19には無塵ガス導出弁24がそれぞれ設けられている。さらに、含塵ガス導入経路17には、バグフィルタ15の状態を監視するための圧力計25が設けられ、無塵ガス導出経路19には前記流出室14から無塵ガスを吸引して導出するためのガス吸引装置26が設けられるとともに、逆洗浄時に流出室14内を外気に開放するための開放弁27を有する開放経路28が設けられている。   The dust-containing gas introduction path 17 and the dust-free gas outlet path 19 are connected by a bypass path 22 having a bypass valve 21, and a dust-containing gas introduction valve 23 is connected to the dust-containing gas introduction path 17 with a dust-free gas. A dust-free gas outlet valve 24 is provided in the outlet path 19. Further, the dust-containing gas introduction path 17 is provided with a pressure gauge 25 for monitoring the state of the bag filter 15, and the dust-free gas extraction path 19 draws out the dust-free gas from the outflow chamber 14. A gas suction device 26 is provided, and an open path 28 having an open valve 27 for opening the outflow chamber 14 to the outside air during backwashing is provided.

この集塵機は、図1に示す集塵工程と、図2及び図3に示す逆洗浄工程とを繰り返すことによって連続的な集塵工程を行う。まず、図1に示す集塵工程では、含塵ガス導入弁23及び無塵ガス導出弁24が開、バイパス弁21及び開放弁27が閉、ガス吸引装置26が作動中、洗浄用ガス噴出部20は停止中となっている。   This dust collector performs a continuous dust collection process by repeating the dust collection process shown in FIG. 1 and the back washing process shown in FIGS. 2 and 3. First, in the dust collection step shown in FIG. 1, the dust-containing gas introduction valve 23 and the dust-free gas outlet valve 24 are open, the bypass valve 21 and the open valve 27 are closed, and the gas suction device 26 is operating. 20 is stopped.

したがって、ガス吸引装置26によって流出室14内の無塵ガスが無塵ガス導出弁24、無塵ガス導出経路19を介して吸引され、流出室14に比べて相対的に圧力が高くなる流入室13内の含塵ガスがバグフィルタ15を通って流出室14に流れることにより、含塵ガスに含まれる塵(固形物)がバグフィルタ15の外周面に捕捉されてガス中から除去される。含塵ガス導入経路17から流入室13に吸引される含塵ガスの圧力が圧力計25により測定され、あらかじめ設定された圧力に達したとき、すなわち、フィルタ前後の差圧が一定の値に達したときに集塵工程から逆洗浄工程に切り替えられる。   Accordingly, the gas suction device 26 sucks the dust-free gas in the outflow chamber 14 through the dust-free gas lead-out valve 24 and the dust-free gas lead-out path 19, and the inflow chamber has a relatively higher pressure than the outflow chamber 14. When the dust-containing gas in 13 flows through the bag filter 15 to the outflow chamber 14, dust (solid matter) contained in the dust-containing gas is captured by the outer peripheral surface of the bag filter 15 and removed from the gas. When the pressure of the dust-containing gas sucked into the inflow chamber 13 from the dust-containing gas introduction path 17 is measured by the pressure gauge 25 and reaches a preset pressure, that is, the differential pressure before and after the filter reaches a constant value. The dust collection process is switched to the back washing process.

逆洗浄工程では、まず、一般的に行われている逆洗浄工程と同様の洗浄用ガスによる逆洗浄操作が行われる。この逆洗浄操作では、図2に示すように、開放弁27が開、含塵ガス導入弁23、無塵ガス導出弁24及びバイパス弁21が閉、ガス吸引装置26が作動中で、洗浄用ガス噴出部20が作動を開始する。   In the reverse cleaning step, first, a reverse cleaning operation with a cleaning gas is performed, which is the same as a generally performed reverse cleaning step. In this reverse cleaning operation, as shown in FIG. 2, the opening valve 27 is opened, the dust-containing gas introduction valve 23, the dust-free gas outlet valve 24 and the bypass valve 21 are closed, the gas suction device 26 is in operation, The gas ejection part 20 starts operation.

洗浄用ガス噴出部20は、洗浄用ガス導入経路20aから導入される洗浄用ガスを、複数のバグフィルタ15の開口に対して噴出ノズル20bを順次移動させながら連続して噴出することにより、各バグフィルタ15の内部に順番に洗浄用ガスを噴出する。これにより、各バグフィルタ15においては、間欠的に洗浄用ガスが導入される状態となり、洗浄用ガス導入時にはバグフィルタ15がガス圧力によって膨張し、噴出ノズル20bが他のバグフィルタ15の部分に移動したときには、フィルタ自身の復元力によって収縮する状態となる。   The cleaning gas ejection unit 20 ejects the cleaning gas introduced from the cleaning gas introduction path 20a continuously while sequentially moving the ejection nozzles 20b with respect to the openings of the plurality of bag filters 15. The cleaning gas is jetted into the bag filter 15 in order. Thereby, in each bag filter 15, the cleaning gas is intermittently introduced. When the cleaning gas is introduced, the bag filter 15 is expanded by the gas pressure, and the ejection nozzle 20 b is moved to the other bag filter 15. When moved, the filter contracts due to the restoring force of the filter itself.

そして、前記逆洗浄操作を行っている間に、図3に示すように、開放弁27を閉じて無塵ガス導出弁24を開き、流出室14内のガスを前記ガス吸引装置26にて吸引することによりバグフィルタ15を収縮させる収縮操作を間欠的に行う。このように吸引装置25にて流出室14内のガスを吸引することにより、バグフィルタ15におけるガスの流れが集塵工程と同方向に流れることになり、逆洗浄用の洗浄用ガスによって膨張したバグフィルタ15を、吸引装置25に吸引されるガスの流れによって強制的に収縮させることができる。   During the reverse cleaning operation, as shown in FIG. 3, the open valve 27 is closed and the dust-free gas outlet valve 24 is opened, and the gas in the outflow chamber 14 is sucked by the gas suction device 26. By doing so, the contraction operation which contracts the bag filter 15 is performed intermittently. By sucking the gas in the outflow chamber 14 with the suction device 25 in this way, the gas flow in the bag filter 15 flows in the same direction as the dust collection process, and is expanded by the cleaning gas for back cleaning. The bag filter 15 can be forcibly contracted by the gas flow sucked into the suction device 25.

図4に示すように、前記逆洗浄操作中のバグフィルタ15は、噴出ノズル20bから噴射した逆洗浄用ガスGAの流入によって内周の支持部材15aからフィルタ膜15bが離れて膨張し、フィルタ膜15bの表面(外周面)に付着した塵Dを、逆洗浄用ガスの流れ及び膨張時のエネルギーによって払い落とすとともに付着性のものも剥離させる。噴出ノズル20bが他のバグフィルタ15の開口部分に移動することによって洗浄用ガスGAの噴出が止まると、フィルタ膜15bは、フィルタ自身の復元力によってフィルタ内部のガスを流出室14に押し出し、開放弁27から開放経路28を介してガスを装置外部に放出しながら収縮する。   As shown in FIG. 4, in the bag filter 15 during the reverse cleaning operation, the filter film 15b expands away from the inner support member 15a due to the inflow of the reverse cleaning gas GA injected from the ejection nozzle 20b. The dust D adhering to the surface (outer peripheral surface) of 15b is removed by the flow of the reverse cleaning gas and the energy during expansion, and the adhering material is also peeled off. When the ejection of the cleaning gas GA stops when the ejection nozzle 20b moves to the opening part of the other bag filter 15, the filter film 15b pushes the gas inside the filter into the outflow chamber 14 by the restoring force of the filter itself and opens it. The gas is contracted while being released from the valve 27 through the open path 28 to the outside of the apparatus.

このとき、装置外部の圧力は通常は大気圧であるから、バグフィルタ15の復元力と大気圧とが均衡した状態でフィルタ膜15bの収縮は終了する。したがって、フィルタ膜15bの表面に、払い落とされやすい塵だけでなく、付着性を有する固形物が付着していた場合には、付着している固形物の影響でフィルタ膜15bの収縮性が損なわれ、十分に収縮しない状態になるときがある。   At this time, since the pressure outside the apparatus is normally atmospheric pressure, the contraction of the filter film 15b ends in a state where the restoring force of the bag filter 15 and the atmospheric pressure are balanced. Therefore, in the case where not only dust that is easily removed but also solid matter having adhesiveness is attached to the surface of the filter film 15b, the shrinkability of the filter film 15b is impaired due to the influence of the attached solid matter. There are times when it becomes in a state where it does not contract sufficiently.

このように、フィルタ膜15bが十分に収縮しない状態になってしまったときでも、図5に示すように、あらかじめ設定された時間間隔で前述の吸引装置25によって流出室14内からガスを吸引して集塵工程と同方向にガスGBを流すことにより、フィルタ膜15bの内周面が支持部材15aの外周に密着した状態になるまでフィルタ膜15bを収縮させることができる。これにより、膨張、収縮の際の変形量を周分に確保することが可能となり、フィルタ膜15bの表面に付着した払い落としやすい塵だけでなく、付着性を有する塵Dも確実にバグフィルタ15のフィルタ膜15b表面から剥離させて除去することができ、バグフィルタ15の除塵機能を確実に回復させることができる。   Thus, even when the filter film 15b is not sufficiently contracted, as shown in FIG. 5, gas is sucked from the outflow chamber 14 by the suction device 25 at a preset time interval as shown in FIG. By flowing the gas GB in the same direction as the dust collection process, the filter film 15b can be contracted until the inner peripheral surface of the filter film 15b comes into close contact with the outer periphery of the support member 15a. As a result, it is possible to secure a sufficient amount of deformation during expansion and contraction, and not only the dust that adheres to the surface of the filter film 15b but also the dust D that has adhesiveness assuredly. The filter film 15b can be peeled off and removed from the surface, and the dust removal function of the bag filter 15 can be reliably recovered.

太陽電池製造装置から排出された排ガスを燃焼式排ガス処理装置で燃焼させて除害処理し、その際に発生したSiOなどの塵(固形分)を含むガスを、前記形態例に示した構成の集塵機を使用して捕捉する実験を行った。前記排ガスの組成は、有害成分である微量のSiH,B,PH,GeHと、少量のHとを含み、残部がNである。集塵機における処理条件は、集塵工程におけるろ過速度を0.4m/min、逆洗浄工程における洗浄用ガスの圧力を0.6MPa、各バグフィルタ毎の逆洗浄操作の周期を12秒、逆洗浄工程全体の時間を60分、吸引装置によりフィルタを間欠的に収縮させる収縮操作の周期を10分とした。 The exhaust gas discharged from the solar cell manufacturing apparatus is burned by the combustion type exhaust gas processing apparatus and detoxified, and the gas containing dust (solid content) such as SiO 2 generated at that time is the configuration shown in the embodiment. A trapping experiment was conducted using a dust collector. The composition of the exhaust gas contains trace amounts of SiH 4 , B 2 H 6 , PH 3 , GeH 4 , which are harmful components, and a small amount of H 2 with the balance being N 2 . The processing conditions in the dust collector are as follows: the filtration rate in the dust collection process is 0.4 m / min, the pressure of the cleaning gas in the reverse cleaning process is 0.6 MPa, the period of the reverse cleaning operation for each bag filter is 12 seconds, and the reverse cleaning process The total time was 60 minutes, and the period of the contraction operation for intermittently contracting the filter with the suction device was 10 minutes.

この条件で集塵工程と逆洗浄工程とを繰り返して連続運転を行った。そして、吸引装置によりフィルタを間欠的に収縮させる操作を行わないとき(従来例)と、収縮操作を行ったとき(本発明の実施例)とにおいて、集塵工程から逆洗浄工程に切り替える直前に圧力計で測定した圧力(P1)と、逆洗浄工程から集塵工程に切り替えた直後に圧力計で測定した圧力(P2)とから逆洗浄工程前後の圧力の差(ΔP=P1−P2)をそれぞれ算出した。その結果、従来例では圧力の差(ΔP)が1.0kPaであったのに対し、実施例では圧力差(ΔP)が1.7kPaとなり、実施例の方が集塵能力の回復力が大きいことがわかる。   Under these conditions, the dust collection process and the back washing process were repeated to perform continuous operation. When the operation of contracting the filter intermittently with the suction device is not performed (conventional example) and when the contraction operation is performed (example of the present invention), immediately before switching from the dust collection process to the back washing process. The pressure difference (ΔP = P1−P2) before and after the reverse cleaning process is calculated from the pressure (P1) measured with the pressure gauge and the pressure (P2) measured with the pressure gauge immediately after switching from the reverse cleaning process to the dust collecting process. Each was calculated. As a result, in the conventional example, the pressure difference (ΔP) was 1.0 kPa, whereas in the example, the pressure difference (ΔP) was 1.7 kPa, and the recovery of the dust collection capacity was larger in the example. I understand that.

集塵工程を行っているときの集塵機の状態を示す説明図である。It is explanatory drawing which shows the state of a dust collector when performing the dust collection process. 逆洗浄操作を行っているときの集塵機の状態を示す説明図である。It is explanatory drawing which shows the state of a dust collector when performing reverse washing operation. 収縮操作を行っているときの集塵機の状態を示す説明図である。It is explanatory drawing which shows the state of a dust collector when performing shrinkage | contraction operation. 逆洗浄操作中に膨張したバグフィルタの状態を示す説明図である。It is explanatory drawing which shows the state of the bag filter which expanded during back washing operation. 収縮操作中に収縮したバグフィルタの状態を示す説明図である。It is explanatory drawing which shows the state of the bag filter shrink | contracted during shrinkage | contraction operation.

符号の説明Explanation of symbols

11…筐体、12…区画壁、13…流入室、14…流出室、15…バグフィルタ、15a…支持部材、15b…フィルタ膜、16…燃焼器、17…含塵ガス導入経路、18…回収容器、19…無塵ガス導出経路、20…洗浄用ガス噴出部、20a…洗浄用ガス導入経路、20b…噴出ノズル、21…バイパス弁、22…バイパス経路、23…含塵ガス導入弁、24…無塵ガス導出弁、25…圧力計、26…ガス吸引装置、27…開放弁、28…開放経路   DESCRIPTION OF SYMBOLS 11 ... Housing | casing, 12 ... Partition wall, 13 ... Inflow chamber, 14 ... Outflow chamber, 15 ... Bag filter, 15a ... Supporting member, 15b ... Filter membrane, 16 ... Combustor, 17 ... Dust-containing gas introduction path, 18 ... Recovery container, 19 ... dust-free gas outlet path, 20 ... cleaning gas ejection section, 20a ... cleaning gas introduction path, 20b ... ejection nozzle, 21 ... bypass valve, 22 ... bypass path, 23 ... dust-containing gas introduction valve, 24 ... Dust-free gas outlet valve, 25 ... Pressure gauge, 26 ... Gas suction device, 27 ... Open valve, 28 ... Open path

Claims (2)

集塵工程時とは逆方向に洗浄用ガスを噴出させてフィルタの逆洗浄を行う集塵機におけるフィルタの洗浄方法において、前記逆洗浄を行っている間に、集塵工程時と同方向にガスを流す操作を間欠的に行うことを特徴とする集塵機におけるフィルタの洗浄方法。   In the filter cleaning method in the dust collector that reversely cleans the filter by jetting cleaning gas in the opposite direction to the dust collection process, the gas is supplied in the same direction as in the dust collection process during the reverse cleaning. A method for cleaning a filter in a dust collector, wherein the flow operation is intermittently performed. 筐体内を流入室と流出室とに区画する区画壁と、該区画壁から流入室側に突設した有底筒状のバグフィルタと、前記流出室側から前記バグフィルタ内に洗浄用ガスを噴出する洗浄用ガス噴出部と、前記流入室に含塵ガスを導入する含塵ガス導入経路と、該含塵ガス導入経路に設けられた含塵ガス導入弁と、前記流出室から無塵ガスを導出する無塵ガス導出経路と、該無塵ガス導出経路に設けられた無塵ガス導出弁と、前記無塵ガス導出経路における前記無塵ガス導出弁の下流側に設けられたガス吸引装置と、前記流出室内を外気に開放する開放経路と、該開放経路に設けられた開放弁とを備えた集塵機におけるフィルタの洗浄方法であって、前記含塵ガス導入弁及び前記無塵ガス導出弁を閉じ、前記開放弁を開いた状態で前記洗浄用ガス噴出部から前記洗浄用ガスを前記バグフィルタ内に噴出して該バグフィルタの逆洗浄を行っている間に、前記無塵ガス導出弁を開くとともに前記開放弁を閉じて前記流出室内のガスを前記ガス吸引装置にて吸引する操作を間欠的に行うことを特徴とする集塵機におけるフィルタの洗浄方法。   A partition wall that divides the inside of the housing into an inflow chamber and an outflow chamber, a bottomed cylindrical bag filter protruding from the partition wall toward the inflow chamber, and a cleaning gas from the outflow chamber side into the bag filter A cleaning gas jetting part, a dusty gas introduction path for introducing dusty gas into the inflow chamber, a dusty gas introduction valve provided in the dusty gas introduction path, and a dust-free gas from the outflow chamber , A dust-free gas lead-out valve provided in the dust-free gas lead-out path, and a gas suction device provided downstream of the dust-free gas lead-out valve in the dust-free gas lead-out path And a filter cleaning method in a dust collector comprising: an open path for opening the outflow chamber to the outside air; and an open valve provided in the open path, the dust-containing gas introduction valve and the dust-free gas outlet valve The cleaning gas is blown out with the open valve closed. During the reverse cleaning of the bag filter by jetting the cleaning gas from the bag filter, the dust-free gas outlet valve is opened and the open valve is closed to release the gas in the outflow chamber to the gas A method for cleaning a filter in a dust collector, wherein an operation of sucking with a suction device is intermittently performed.
JP2008175206A 2008-07-04 2008-07-04 Cleaning method of filter in dust collector Expired - Fee Related JP5149089B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102728161A (en) * 2012-07-12 2012-10-17 中国石油大学(北京) Pulse reverse-blowing ash-removing device with flexible blowing pipes
CN103143530A (en) * 2013-01-18 2013-06-12 全利机械股份有限公司 Automatic cleaning device
CN115477366A (en) * 2022-10-20 2022-12-16 重庆海通环保科技有限公司 Antipollution reverse osmosis membrane device

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Publication number Priority date Publication date Assignee Title
JPS49127526U (en) * 1973-03-03 1974-11-01
JPS5876121A (en) * 1981-10-30 1983-05-09 Color Toronitsuku Kk Method and apparatus for filtering fine powder-containing gas
JPS63291615A (en) * 1987-05-21 1988-11-29 Kawasaki Heavy Ind Ltd Dust collector
JPH11156129A (en) * 1997-11-26 1999-06-15 Daido Steel Co Ltd Dust removing apparatus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49127526U (en) * 1973-03-03 1974-11-01
JPS5876121A (en) * 1981-10-30 1983-05-09 Color Toronitsuku Kk Method and apparatus for filtering fine powder-containing gas
JPS63291615A (en) * 1987-05-21 1988-11-29 Kawasaki Heavy Ind Ltd Dust collector
JPH11156129A (en) * 1997-11-26 1999-06-15 Daido Steel Co Ltd Dust removing apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102728161A (en) * 2012-07-12 2012-10-17 中国石油大学(北京) Pulse reverse-blowing ash-removing device with flexible blowing pipes
CN103143530A (en) * 2013-01-18 2013-06-12 全利机械股份有限公司 Automatic cleaning device
CN115477366A (en) * 2022-10-20 2022-12-16 重庆海通环保科技有限公司 Antipollution reverse osmosis membrane device
CN115477366B (en) * 2022-10-20 2023-11-28 重庆海通环保科技有限公司 Anti-pollution reverse osmosis membrane device

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