JP2015027641A - Dust collection installation, heat treatment system and method of operating dust collection installation - Google Patents

Dust collection installation, heat treatment system and method of operating dust collection installation Download PDF

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JP2015027641A
JP2015027641A JP2013157571A JP2013157571A JP2015027641A JP 2015027641 A JP2015027641 A JP 2015027641A JP 2013157571 A JP2013157571 A JP 2013157571A JP 2013157571 A JP2013157571 A JP 2013157571A JP 2015027641 A JP2015027641 A JP 2015027641A
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flow path
dust collection
side flow
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inlet
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JP6136010B2 (en
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洋一 中田
Yoichi Nakada
洋一 中田
知則 渡會
Tomonori Watarai
知則 渡會
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Tsukishima Kikai Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a dust collection installation without possibility of backflow of fine particles in back washing, a heat treatment system and a method of operating the dust collection installation.SOLUTION: A dust collection installation X1 for exhaust gas G1 includes a plurality of filter chambers 11A and 11B connected with an inlet passage 3 and an outlet passage 4, a filter material 12 arranged in the filter chambers 11A and 11B and back washing means for the filter material 12 with a back wash gas A. The individual filter chambers 11A and 11B are connected with inlet passages 3A and 3B and outlet passages 4A and 4B, respectively. Inlet valve means 15A and 15B of opening and closing separately the inlet passages 3A and 3B and outlet valve means 16A and 16B of opening and closing separately the outlet passages 4A and 4B are provided, and pressure release means 17 of releasing the inner pressures of the filter chambers 11A and 11B is also provided. Back washing is carried out, while a dust collection treatment is carried out continuously, by switching the valve means between the opening and the closing state.

Description

本発明は、排気ガス中に含まれる微粒子の集塵設備、熱処理システム及び集塵設備の運転方法に関するものである。特に排気ガスが、熱処理室内を臨む摺動部を有する熱処理装置から排出される場合に関するものである。   The present invention relates to a dust collection facility, a heat treatment system, and a method for operating a dust collection facility for fine particles contained in exhaust gas. In particular, the present invention relates to a case where exhaust gas is exhausted from a heat treatment apparatus having a sliding portion facing the heat treatment chamber.

現在、乾燥、燃焼、熱分解、冷却等の熱処理を行う熱処理装置としては、装置が回転、又は一部が振り動くことにより被処理物を前に送りながら処理をおこなう装置があり、例えば、ロータリーキルンやスチームチューブドライヤー(STD)等の種々の装置が存在している。これらの熱処理装置は、熱処理室たる可動部と、可動部を支持する固定部とから構成され、可動部と固定部とが当接する摺動部を介して接続されている。しかるに、これらの熱処理装置から排出された排気ガスは、微粒子を含む場合がある。そこで、従来から、排気ガス中の微粒子を集塵する装置として、バグフィルタ装置が汎用されている。   Currently, as a heat treatment apparatus that performs heat treatment such as drying, combustion, thermal decomposition, cooling, etc., there is an apparatus that performs processing while feeding an object to be processed by rotating or partially moving the apparatus, for example, a rotary kiln. There are various devices such as a steam tube dryer (STD). These heat treatment apparatuses are composed of a movable part that is a heat treatment chamber and a fixed part that supports the movable part, and are connected via a sliding part that contacts the movable part and the fixed part. However, the exhaust gas discharged from these heat treatment apparatuses may contain fine particles. Therefore, conventionally, a bag filter device has been widely used as a device for collecting particulates in exhaust gas.

このバグフィルタ装置は、排気ガスが送り込まれるフィルタ室と、このフィルタ室内に配置されたフィルタ材とで主に構成される。フィルタ室内に送り込まれた排気ガス中の微粒子は、フィルタ材によって捕捉され、フィルタ室からは清浄ガスが排出される。また、微粒子を捕捉したフィルタ材は濾過抵抗が高まる等の問題を有することから、定期的に洗浄される。   This bag filter device is mainly composed of a filter chamber into which exhaust gas is sent and a filter material arranged in the filter chamber. The particulates in the exhaust gas sent into the filter chamber are captured by the filter material, and the clean gas is discharged from the filter chamber. Further, since the filter material that has captured the fine particles has a problem such as an increase in filtration resistance, it is periodically cleaned.

この洗浄の方法としては、圧縮エア等の逆洗ガスを使用してフィルタ材を逆洗する方法が存在する。この逆洗は、フィルタ室の下流側から当該フィルタ室内に逆洗ガスを吹き込み、この吹き込んだ逆洗ガスによってフィルタ材に付着した微粒子を払い落すというものである(例えば、特許文献1参照。)。この微粒子の払い落しは、特に逆洗ガスをパルス状に吹き込むと効果的に行われる。   As a cleaning method, there is a method of backwashing the filter material using a backwashing gas such as compressed air. In this backwashing, backwashing gas is blown into the filter chamber from the downstream side of the filter chamber, and fine particles adhering to the filter material are removed by the blown backwashing gas (see, for example, Patent Document 1). . The fine particles are effectively removed particularly when the backwash gas is blown in pulses.

以上のようなバグフィルタ装置やこのバグフィルタ装置に逆洗手段が備え付けられてなる集塵設備は、現在においても、集塵効率の向上や逆洗効率の向上等を課題して種々の改良が加えられている。また、微粒子が臭気物質である場合等、微粒子の特性に応じた改良も模索されている(例えば、特許文献2参照。)。   The bag filter apparatus as described above and the dust collection equipment provided with the back washing means in the bag filter apparatus are still variously improved to improve dust collection efficiency and back washing efficiency. It has been added. In addition, when the fine particles are odorous substances, an improvement in accordance with the characteristics of the fine particles has been sought (for example, see Patent Document 2).

このように集塵設備の改良は、集塵・逆洗性能の向上等を課題とするのが一般的であり、本発明者等も種々の課題を設定して集塵設備の改良を行っている。しかるに、本発明者等は、種々の改良、試験等を行う過程において、現在の集塵設備には、全く異なる観点からの課題が存在することを認識した。
すなわち、この新たな課題は、処理の対象となる排気ガスが、熱処理室内を臨む摺動部を有する熱処理装置、例えば、ロータリーキルンやSTD等から排出される場合に生じるというものである。
より具体的には、例えば、図4に示すように、集塵設備100の逆洗に際しては、フィルタ室101内に下流側から圧縮エアAを吹き込み、フィルタ材102に付着した微粒子Zを払い落すことになる。しかるに、フィルタ材102から払い落された微粒子Zは、フィルタ室101の底部に堆積するのみではなく、熱処理装置110から排出された排気ガスG1を集塵設備100に送るための流路103を通して熱処理装置110の熱処理室113内に逆流する。そして、この熱処理室113内に逆流した微粒子Zは、熱処理室113内を臨む摺動部Cに噛み込んでしまい、当該摺動部C自体や、この摺動部Cをシールするシール材を摩耗させる。
As described above, improvement of dust collection equipment is generally aimed at improving dust collection and backwash performance, etc., and the present inventors also set various problems to improve dust collection equipment. Yes. However, the present inventors have recognized that current dust collection equipment has problems from completely different viewpoints in the course of various improvements, tests, and the like.
In other words, this new problem occurs when the exhaust gas to be processed is discharged from a heat treatment apparatus having a sliding portion facing the heat treatment chamber, such as a rotary kiln or STD.
More specifically, for example, as shown in FIG. 4, when backwashing the dust collection equipment 100, compressed air A is blown into the filter chamber 101 from the downstream side, and the fine particles Z adhering to the filter material 102 are removed. It will be. However, the fine particles Z removed from the filter material 102 are not only accumulated at the bottom of the filter chamber 101 but also heat treated through the flow path 103 for sending the exhaust gas G1 discharged from the heat treatment device 110 to the dust collecting facility 100. It flows backward into the heat treatment chamber 113 of the apparatus 110. The fine particles Z that have flowed back into the heat treatment chamber 113 bite into the sliding portion C facing the heat treatment chamber 113 and wear the sliding portion C itself and the sealing material that seals the sliding portion C. Let

この点、熱処理設備110は、回動部111及び固定部112を有する。回動部111は、軸心回りに回動する部位であり、内空部が熱処理室113を構成する。他方、固定部112は、被処理物SやキャリアガスG2の供給路、あるいは排気ガスG1を排出する流路103が接続された部位であり、回動することがない。したがって、回動部111及び固定部112が接触する部位の一部は、その構造上、熱処理室113内を臨むことになってしまい、この部位が上記摺動部Cに該当し、摩耗の問題が生じる。この問題は、特に上記微粒子Zが硬質物質である場合は、大きなものとなる。   In this regard, the heat treatment facility 110 includes a rotating part 111 and a fixed part 112. The rotating part 111 is a part that rotates around the axis, and the inner space constitutes the heat treatment chamber 113. On the other hand, the fixing part 112 is a part to which the supply path for the workpiece S or the carrier gas G2 or the flow path 103 for discharging the exhaust gas G1 is connected, and does not rotate. Therefore, a part of the part where the rotating part 111 and the fixed part 112 are in contact with each other faces the inside of the heat treatment chamber 113 due to its structure, and this part corresponds to the sliding part C, and there is a problem of wear. Occurs. This problem is particularly serious when the fine particles Z are hard substances.

また、近年では、例えば、金属微粒子を含有するスラリーを乾燥するために、熱処理装置110が使用され、乾燥後に金属微粒子を排気ガスG1中から回収するために集塵設備100が使用されることもある。この場合、金属微粒子は硬質物質であるため、摺動部Cやシール材が激しく摩耗する。しかも、摺動部Cやシール材を構成していた材料が、摩耗により微粒子状となって金属微粒子中に混入するため、得られる金属微粒子(製品)の品質が低下するという問題も生じる。   In recent years, for example, the heat treatment apparatus 110 is used to dry a slurry containing metal fine particles, and the dust collection facility 100 is used to recover the metal fine particles from the exhaust gas G1 after drying. is there. In this case, since the metal fine particles are a hard substance, the sliding portion C and the sealing material are worn abruptly. In addition, since the material constituting the sliding portion C and the sealing material becomes fine particles due to wear and is mixed in the metal fine particles, there is a problem that the quality of the obtained metal fine particles (product) is deteriorated.

特開平11−264525号公報JP-A-11-264525 特開2009−66563号公報JP 2009-66563 A

本発明が解決しようとする主たる課題は、逆洗に際して微粒子が逆流するおそれのない集塵設備、熱処理システム及び集塵設備の運転方法を提供することにある。   The main problem to be solved by the present invention is to provide a dust collection facility, a heat treatment system, and a method for operating the dust collection facility, in which fine particles do not flow back during backwashing.

この課題を解決するための本発明は、次の通りである。
〔請求項1記載の発明〕
熱処理室内を臨む摺動部を有する熱処理装置から排出された排気ガス中の微粒子を集塵して清浄ガスとして排出する設備であって、
前記排気ガスの入側流路及び前記清浄ガスの出側流路が接続されたフィルタ室と、このフィルタ室内に配置され、微粒子を集塵するフィルタ材と、前記フィルタ室内に逆洗ガスを吹き込んで前記フィルタ材を逆洗する逆洗手段とが備えられ、
前記フィルタ室が複数備わり、当該フィルタ室にはそれぞれ前記排気ガスの入側流路及び前記清浄ガスの出側流路が接続され、
前記排気ガスの入側流路を各別に開閉可能な入側弁手段、及び前記清浄ガスの出側流路を各別に開閉可能な出側弁手段が備わり、
更に前記フィルタ室の内圧を開放可能な圧開放手段が備わる、
ことを特徴とする集塵設備。
The present invention for solving this problem is as follows.
[Invention of Claim 1]
A facility for collecting particulates in exhaust gas discharged from a heat treatment apparatus having a sliding portion facing the heat treatment chamber and discharging it as clean gas,
A filter chamber to which the exhaust gas inlet-side flow path and the clean gas outlet-side flow path are connected, a filter material disposed in the filter chamber for collecting particulates, and backwash gas is blown into the filter chamber. And backwashing means for backwashing the filter material,
A plurality of the filter chambers are provided, and the filter chambers are connected to the exhaust gas inlet-side flow path and the clean gas outlet-side flow path, respectively.
Inlet valve means capable of opening and closing the inlet side flow path of the exhaust gas, and outlet side valve means capable of opening and closing the outlet side flow path of the clean gas separately,
Furthermore, a pressure release means capable of releasing the internal pressure of the filter chamber is provided.
Dust collection equipment characterized by that.

〔請求項2記載の発明〕
前記入側弁手段が前記排気ガスの入側流路それぞれに各別に備わり、
前記出側弁手段が前記清浄ガスの出側流路それぞれに各別に備わり、
前記入側弁手段及び前記出側弁手段の開状態又は閉状態の少なくとも一方を検知する検知手段が備わる、
請求項1記載の集塵設備。
[Invention of Claim 2]
The inlet side valve means is provided separately for each of the inlet side flow paths of the exhaust gas,
The outlet valve means is provided for each outlet flow path of the clean gas,
A detecting means for detecting at least one of an open state or a closed state of the inlet valve means and the outlet valve means;
The dust collection facility according to claim 1.

〔請求項3記載の発明〕
請求項1又は請求項2記載の集塵設備と、スチームチューブドライヤ又はロータリーキルンからなる熱処理装置と、が備わる、
ことを特徴とする熱処理システム。
[Invention of Claim 3]
The dust collection facility according to claim 1 or 2, and a heat treatment apparatus comprising a steam tube dryer or a rotary kiln are provided.
A heat treatment system characterized by that.

〔請求項4記載の発明〕
熱処理室内を臨む摺動部を有する熱処理装置から排出された排気ガス中の微粒子を集塵して清浄ガスとして排出する設備の運転方法であり、
前記排気ガスの入側流路及び前記清浄ガスの出側流路が接続されたフィルタ室と、このフィルタ室内に配置され、微粒子を集塵するフィルタ材と、前記フィルタ室内に逆洗ガスを吹き込んで前記フィルタ材を逆洗する逆洗手段と、が備えられた集塵設備の運転方法であって、
前記集塵設備として、前記フィルタ室が複数備わり、当該フィルタ室にはそれぞれ前記排気ガスの入側流路及び前記清浄ガスの出側流路が接続され、かつ前記フィルタ材が備わる設備を用意し、
それぞれの前記フィルタ室において、前記排気ガスの入側流路及び前記清浄ガスの出側流路を開状態として前記微粒子の集塵する集塵作業と、前記排気ガスの入側流路及び前記清浄ガスの出側流路を閉状態とした後に、前記逆洗ガスを吹き込んで前記フィルタ材を洗浄する逆洗作業と、が行われ、
かつ、複数の前記フィルタ室のうち少なくとも1のフィルタ室においては前記集塵作業が行われるように、前記入側流路及び前記出側流路の開閉状態を制御する、
ことを特徴とする集塵設備の運転方法。
[Invention of Claim 4]
It is an operation method of equipment for collecting fine particles in exhaust gas discharged from a heat treatment apparatus having a sliding part facing the heat treatment chamber and discharging it as clean gas,
A filter chamber to which the exhaust gas inlet-side flow path and the clean gas outlet-side flow path are connected, a filter material disposed in the filter chamber for collecting particulates, and backwash gas is blown into the filter chamber. And a backwashing means for backwashing the filter material, and a method of operating a dust collection facility comprising:
A plurality of the filter chambers are provided as the dust collection facility, and the filter chambers are connected to the exhaust gas inlet side flow path and the clean gas outlet side flow path, respectively, and are equipped with the filter material. ,
In each of the filter chambers, the exhaust gas inlet-side flow path and the clean gas outlet-side flow path are opened to collect dust, and the exhaust gas inlet-side flow path and the clean gas are collected. After the gas outlet side flow path is closed, the backwashing operation of cleaning the filter material by blowing the backwash gas is performed,
And, in at least one filter chamber among the plurality of filter chambers, the opening and closing states of the inlet-side channel and the outlet-side channel are controlled so that the dust collection operation is performed.
The operation method of the dust collection equipment characterized by this.

〔請求項5記載の発明〕
いずれかの前記フィルタ室において逆洗作業が行われた後、他の前記フィルタ室において逆洗作業が行われるに先立って、全ての前記フィルタ室において集塵作業が行われる、
請求項4記載の集塵設備の運転方法。
[Invention of Claim 5]
After the backwashing operation is performed in any of the filter chambers, the dust collection operation is performed in all the filter chambers before the backwashing operation is performed in the other filter chambers.
The operation method of the dust collection equipment of Claim 4.

〔請求項6記載の発明〕
前記排気ガスの入側流路及び前記清浄ガスの出側流路を開状態に変えるに先立って、当該入側流路及び出側流路が接続されたフィルタ室内の圧力を開放しておく、
請求項4又は請求項5記載の集塵設備の運転方法。
[Invention of Claim 6]
Prior to changing the inlet side flow path of the exhaust gas and the outlet side flow path of the clean gas to the open state, the pressure in the filter chamber to which the inlet side flow path and the outlet side flow path are connected is released.
The operation method of the dust collection equipment of Claim 4 or Claim 5.

〔請求項7記載の発明〕
前記排気ガスの入側流路及び前記清浄ガスの出側流路を閉状態に変えるに先立って、開状態とされた排気ガスの入側流路及び清浄ガスの出側流路が存在することを確認する、
請求項4〜6のいずれか1項に記載の集塵設備の運転方法。
[Invention of Claim 7]
Prior to changing the exhaust gas inlet-side flow path and the clean gas outlet-side flow path to the closed state, the exhaust gas inlet-side flow path and the clean gas outlet-side flow path exist. Check the
The operation method of the dust collection equipment of any one of Claims 4-6.

本発明によると、逆洗に際して微粒子が逆流するおそれのない集塵設備、熱処理システム及び集塵設備の運転方法となる。   According to the present invention, the dust collection facility, the heat treatment system, and the operation method of the dust collection facility are free from the risk of the fine particles flowing back during backwashing.

第1の実施の形態に係る集塵設備である。It is the dust collection equipment which concerns on 1st Embodiment. 第2の実施の形態に係る集塵設備である。It is the dust collection equipment which concerns on 2nd Embodiment. 第3の実施の形態に係る集塵設備である。It is the dust collection equipment which concerns on 3rd Embodiment. 従来の集塵設備である。It is a conventional dust collection facility.

次に、本発明を実施するための形態を説明する。なお、以下に示す実施形態の説明は、例示に過ぎず、本発明、その適用、あるいはその用途を制限することを意図するものではない。   Next, the form for implementing this invention is demonstrated. Note that the following description of the embodiment is merely an example, and is not intended to limit the present invention, its application, or its use.

〔第1の実施の形態〕
図1に、第1の実施の形態に係る集塵設備X1を示した。
本形態の集塵設備X1は、熱処理装置110から排出された排気ガスG1中の微粒子を集塵して清浄ガスG3として排出する設備である。熱処理装置110は、図4を参照しつつ説明した前述熱処理装置110と同様の構造を有しており、熱処理室113内を臨む摺動部を有する。なお、この摺動部は、図4中において符号Cで示す部位であるが、図1並びに以下で参照する図2及び図3においては、図面の理解を容易とするために、当該摺動部の符号を省略している。
[First Embodiment]
FIG. 1 shows a dust collection facility X1 according to the first embodiment.
The dust collection facility X1 of this embodiment is a facility that collects particulates in the exhaust gas G1 discharged from the heat treatment apparatus 110 and discharges it as a clean gas G3. The heat treatment apparatus 110 has the same structure as the heat treatment apparatus 110 described with reference to FIG. 4 and has a sliding portion that faces the heat treatment chamber 113. This sliding portion is a portion indicated by reference numeral C in FIG. 4, but in FIG. 1 and FIGS. 2 and 3 referred to below, the sliding portion is shown in order to facilitate understanding of the drawings. The symbol of is omitted.

熱処理装置110としては、例えば、ロータリーキルンやスチームチューブドライヤ(STD)、コールインチューブ等を例示することができる。また、熱処理としては、例えば、乾燥や燃焼、熱分解、冷却等を例示することができる。さらに、熱処理の対象となる被処理物Sとしては、例えば、金属微粒子等の微粒子を含有するスラリーや、微粒子の集合物自体、つまり粉体等を例示することができる。なお、微粒子は、金属微粒子に限定されず、例えば、電池、電子材、触媒食品、顔料用途向けの無機、有機微粒子等の摺動部に付着したり、摺動部を摩耗させたりするおそれのある種々のものを例示することができる。   Examples of the heat treatment apparatus 110 include a rotary kiln, a steam tube dryer (STD), a call-in tube, and the like. Moreover, as heat processing, drying, combustion, thermal decomposition, cooling, etc. can be illustrated, for example. Furthermore, examples of the object to be processed S to be heat-treated include a slurry containing fine particles such as metal fine particles, an aggregate of fine particles themselves, that is, a powder and the like. The fine particles are not limited to metal fine particles. For example, the fine particles may adhere to sliding parts such as batteries, electronic materials, catalytic foods, pigments, and inorganic and organic fine particles, or may cause the sliding parts to wear. A variety of things can be illustrated.

熱処理装置110から排出された排気ガスG1は、ダクト等からなる入側流路3を通して集塵設備X1に送られる。入側流路3は、先端側、つまり集塵装置X1側が2以上の複数路に、図示例では第1の入側流路3A及び第2の入側流路3Bに分岐している。   The exhaust gas G1 discharged from the heat treatment apparatus 110 is sent to the dust collection facility X1 through the inlet-side flow path 3 formed of a duct or the like. The inlet side flow path 3 is branched into two or more paths on the front end side, that is, the dust collector X1 side, and in the illustrated example, is branched into a first inlet side flow path 3A and a second inlet side flow path 3B.

第1の入側流路3Aには第1の入側開閉弁15Aが備えられており、当該第1の入側開閉弁15Aの開閉に応じて第1の入側流路3A内を流れる排気ガスG1の流通が制御可能となるように構成されている。同様に、第2の入側流路3Bには第2の入側開閉弁15Bが備えられており、当該第2の入側開閉弁15Bの開閉に応じて第2の入側流路3B内を流れる排気ガスG1の流通が制御可能となるように構成されている。   The first inlet-side channel 3A is provided with a first inlet-side on-off valve 15A, and the exhaust gas flowing in the first inlet-side channel 3A according to the opening and closing of the first inlet-side on-off valve 15A. The flow of the gas G1 is configured to be controllable. Similarly, the second inlet-side channel 3B is provided with a second inlet-side on / off valve 15B, and the second inlet-side channel 3B is opened and closed according to the opening / closing of the second inlet-side on / off valve 15B. The flow of the exhaust gas G1 flowing through the engine can be controlled.

第1の入側開閉弁15A及び第2の入側開閉弁15B、並びに後述する第1の出側開閉弁16A及び第2の出側開閉弁16Bとしては、例えば、バタフライ弁、ボール弁、グローブ弁、スライドゲート等を使用することができる。また、本形態の集塵設備Xには、これらの開閉弁15A,15B,16A,16Bの開閉状態を検知するリミットスイッチや開閉センサ等の図示しない検知手段を備えるとより好適なものとなる。好適である理由については、後述する。なお、開閉弁15A,15B,16A,16Bの開閉状態は開状態、閉状態の少なくとも一方を検知できれば良いが、具体的開度を検知する手段を用いることもできる。   Examples of the first inlet-side on-off valve 15A and the second inlet-side on-off valve 15B, and a first outlet-side on-off valve 16A and a second outlet-side on-off valve 16B described later include butterfly valves, ball valves, and globes. Valves, slide gates, etc. can be used. In addition, it is more preferable that the dust collection equipment X of the present embodiment is provided with detection means (not shown) such as a limit switch and an open / close sensor that detect the open / close state of these open / close valves 15A, 15B, 16A, and 16B. The reason why it is suitable will be described later. The open / close state of the open / close valves 15A, 15B, 16A, and 16B only needs to detect at least one of the open state and the closed state, but a means for detecting a specific opening degree can also be used.

なお、以下では、第1の入側開閉弁15A及び第2の入側開閉弁15Bを単に「入側開閉弁15A,15B」ともいい、同様に、第1の出側開閉弁16A及び第2の出側開閉弁16Bを単に「出側開閉弁15A,15B」ともいう。また、第1の入側開閉弁15A及び第1の出側開閉弁16Aを単に「第1の開閉弁15A,16A」ともいい、同様に、第2の入側開閉弁15A及び第2の出側開閉弁16Bを単に「第2の開閉弁15B,16B」ともいう。   In the following description, the first inlet side on / off valve 15A and the second inlet side on / off valve 15B are also simply referred to as “entry side on / off valves 15A and 15B”, and similarly, the first outlet side on / off valve 16A and second The outlet side on-off valve 16B is also simply referred to as “outside on-off valves 15A, 15B”. In addition, the first inlet-side on-off valve 15A and the first outlet-side on-off valve 16A are also simply referred to as “first on-off valves 15A, 16A”. Similarly, the second inlet-side on-off valve 15A and the second outlet-side on-off valve 15A The side opening / closing valve 16B is also simply referred to as “second opening / closing valves 15B, 16B”.

第1の入側流路3A内や第2の入側流路3B内を流れた排気ガスG1は、集塵設備X1を構成するバグフィルタ装置によって集塵処理される。このバグフィルタ装置は、2以上の複数のフィルタ室を備えている。図示例では複数のフィルタ室を備えたバグフィルタ装置を採用したが、本発明は1台のバグフィルタにより構成されるものに限定されない。例えば、1のフィルタ室を備えたバグフィルタを2台以上並列に設置し、複数台のバグフィルタからなるバグフィルタ装置としても良い。   The exhaust gas G1 that has flowed through the first inlet-side channel 3A or the second inlet-side channel 3B is collected by a bag filter device that constitutes the dust collection facility X1. This bag filter device includes two or more filter chambers. In the illustrated example, a bag filter device having a plurality of filter chambers is employed, but the present invention is not limited to one constituted by a single bag filter. For example, two or more bug filters having one filter chamber may be installed in parallel to form a bug filter device including a plurality of bug filters.

本形態においては、第1の入側流路3Aが接続された第1のフィルタ室11A及び第2の入側流路3Bが接続された第2のフィルタ室11Bを有する。第1の入側流路3A内を流れた排気ガスG1は第1のフィルタ室11A内に流入し、第2の入側流路3B内を流れた排気ガスG1は第2のフィルタ室11B内に流入する。   In this embodiment, the first filter chamber 11A to which the first inlet-side channel 3A is connected and the second filter chamber 11B to which the second inlet-side channel 3B is connected are provided. The exhaust gas G1 that has flowed through the first inlet-side flow path 3A flows into the first filter chamber 11A, and the exhaust gas G1 that has flowed through the second inlet-side flow path 3B is within the second filter chamber 11B. Flow into.

複数のフィルタ室内には、それぞれ排気ガスG1中の微粒子を捕捉するフィルタ材が備えられている。図示例では、第1のフィルタ室11A内に第1のフィルタ材12Aが備えられており、この第1のフィルタ材12Aによって第1のフィルタ室11A内が上流側の集塵領域と下流側の清浄領域とに分割されている。同様に、第2のフィルタ室11B内には第2のフィルタ材12Bが備えられており、この第2のフィルタ材12Bによって第2のフィルタ室11B内が上流側の集塵領域と下流側の清浄領域とに分割されている。   Each of the plurality of filter chambers is provided with a filter material that captures particulates in the exhaust gas G1. In the illustrated example, a first filter material 12A is provided in the first filter chamber 11A, and the first filter material 12A causes the inside of the first filter chamber 11A to be in the upstream dust collection region and the downstream side. It is divided into clean areas. Similarly, a second filter material 12B is provided in the second filter chamber 11B, and the second filter material 12B causes the second filter chamber 11B to have an upstream dust collection region and a downstream side. It is divided into clean areas.

第1のフィルタ室11A内に流入した排気ガスG1は、第1のフィルタ材12Aを通過する際に、当該排気ガスG1中に含まれる微粒子が捕捉されて清浄ガスG3なる。同様に、第2のフィルタ室11B内に流入した排気ガスG1は、第2のフィルタ材12Bを通過する際に、当該排気ガスG1中に含まれる微粒子が捕捉されて清浄ガスG3となる。   When the exhaust gas G1 flowing into the first filter chamber 11A passes through the first filter material 12A, particulates contained in the exhaust gas G1 are captured and become the clean gas G3. Similarly, when the exhaust gas G1 flowing into the second filter chamber 11B passes through the second filter material 12B, particulates contained in the exhaust gas G1 are captured and become the clean gas G3.

第1のフィルタ室11A及び第2のフィルタ室11Bを有するバグフィルタ装置には、清浄ガスG3が流れるダクト等からなる出側流路4が接続されている。この出側流路4は、基端側、つまりバグフィルタ装置側が2以上の複数路に、図示例では第1の出側流路4A及び第2の出側流路4Bに分岐している。第1のフィルタ室11A内の清浄ガスG3は、第1の出側流路4Aを通して排出される。同様に、第2のフィルタ室11B内の清浄ガスG3は、第2の出側流路4Bを通して排出される。なお、出側流路4の先端側に備えられた符号Bで示す装置は、吸引ブロワ等からなる吸引手段である。   The bag-side filter device having the first filter chamber 11A and the second filter chamber 11B is connected to the outlet-side flow path 4 including a duct through which the clean gas G3 flows. The outlet side flow path 4 is branched into a plurality of two or more paths on the base end side, that is, the bag filter device side, and in the illustrated example, is branched into a first output side flow path 4A and a second output side flow path 4B. The clean gas G3 in the first filter chamber 11A is discharged through the first outlet channel 4A. Similarly, the clean gas G3 in the second filter chamber 11B is discharged through the second outlet channel 4B. Note that the device indicated by reference numeral B provided on the distal end side of the outlet side flow path 4 is a suction means including a suction blower or the like.

第1の出側流路4Aには第1の出側開閉弁16Aが備えられており、当該第1の出側開閉弁16Aの開閉に応じて第1の出側流路4A内を流れる清浄ガスG3の流通が制御可能となるように構成されている。同様に、第2の出側流路4Bには第2の出側開閉弁16Bが備えられており、当該第2の出側開閉弁16Bの開閉に応じて第2の出側流路4B内を流れる清浄ガスG3の流通が制御可能となるように構成されている。   The first outlet-side flow path 4A is provided with a first outlet-side on-off valve 16A, and the clean flowing in the first outlet-side channel 4A according to the opening and closing of the first outlet-side on-off valve 16A. The flow of the gas G3 is configured to be controllable. Similarly, the second outlet channel 4B is provided with a second outlet valve 16B, and the second outlet channel 4B is opened and closed according to the opening and closing of the second outlet valve 16B. The flow of the clean gas G3 flowing through the gas can be controlled.

また、第1の出側開閉弁16Aよりも上流側の第1の出側流路4Aには分岐路が接続されており、この分岐路には圧開放手段たる逆止弁17Aが備えられている。同様に、第2の出側開閉弁16Bよりも上流側の第2の出側流路4Bには分岐路が接続されており、この分岐路には圧開放手段たる逆止弁17Bが備えられている。逆止弁17A,17Bは、清浄ガスG3や後述する圧縮エアA等のガスが出側流路4A,4B側から分岐路を通って系外に流れるが、系外のガスが分岐路内には流入しないように構成されている。   Further, a branch path is connected to the first outlet flow path 4A upstream of the first outlet side opening / closing valve 16A, and a check valve 17A serving as a pressure release means is provided in the branch path. Yes. Similarly, a branch passage is connected to the second outlet flow passage 4B upstream of the second outlet on-off valve 16B, and a check valve 17B as pressure release means is provided in the branch passage. ing. In the check valves 17A and 17B, gas such as clean gas G3 and compressed air A to be described later flows from the outlet side passages 4A and 4B through the branch passage to the outside of the system, but the gas outside the system enters the branch passage. Is configured not to flow in.

また、入側開閉弁15A,15B及び出側開閉弁16A,16Bは、図示しない制御手段によって開閉制御される。この制御手段には、各弁に設置されたリミットスイッチや開閉センサ等の検知手段から入側開閉弁15A,15B及び出側開閉弁16A,16Bの開閉状態が入力され、各弁の開閉状態が所望の状態となるよう各弁に対して開閉信号を発信する。   In addition, the on / off valves 15A and 15B and the outlet on / off valves 16A and 16B are controlled to open and close by a control means (not shown). The control means receives the opening / closing states of the inlet side opening / closing valves 15A, 15B and the outlet side opening / closing valves 16A, 16B from detection means such as limit switches and opening / closing sensors installed in the valves, and the opening / closing states of the valves are determined. An open / close signal is transmitted to each valve so as to obtain a desired state.

次に、集塵設備X1の運転方法の一例を説明する。
本形態の運転方法においては、まず、必要により、全ての開閉弁15A,15B,16A,16Bをいったん開状態とする。この開状態は、前述検知手段を使用する等して確認することができる。
Next, an example of the operation method of the dust collection equipment X1 will be described.
In the operation method of this embodiment, first, if necessary, all the on-off valves 15A, 15B, 16A, and 16B are once opened. This open state can be confirmed, for example, by using the detection means.

次に、第1の開閉弁15A,16A及び第2の開閉弁15B,16Bのいずれか一方の開閉弁を、例えば、第2の開閉弁15B,16Bを閉状態に変える。この状態においては、熱処理装置100から排出された排気ガスG1が、第1の入側流路3Aを通して所定のフィルタ室たる第1のフィルタ室11A内に流入する。第1のフィルタ室11A内に流入した排気ガスG1は、第1のフィルタ材12Aによって当該排気ガスG1中の微粒子が捕捉された後、つまり集塵処理をされた後、清浄ガスG3として第1の出側流路4Aを通して排出される(集塵工程)。他方、第2の開閉弁15B,16Bは閉状態とされているため、他のフィルタ室たる第2のフィルタ室11B内には排気ガスG1が流入することがなく、集塵処理という観点では第2のフィルタ室11Bが系外におかれることになる。   Next, one of the first on-off valves 15A and 16A and the second on-off valves 15B and 16B is changed to, for example, the second on-off valves 15B and 16B are closed. In this state, the exhaust gas G1 discharged from the heat treatment apparatus 100 flows into the first filter chamber 11A, which is a predetermined filter chamber, through the first inlet-side flow path 3A. The exhaust gas G1 flowing into the first filter chamber 11A is the first clean gas G3 after the particulate matter in the exhaust gas G1 is captured by the first filter material 12A, that is, after dust collection processing is performed. Is discharged through the outlet side flow path 4A (dust collection step). On the other hand, since the second on-off valves 15B and 16B are closed, the exhaust gas G1 does not flow into the second filter chamber 11B, which is another filter chamber. The second filter chamber 11B is placed outside the system.

次に、第1の開閉弁15A,16Aを閉状態に変えると共に、第2の開閉弁15B,16Bを開状態に変える。この状態においては、熱処理装置110から排出された排気ガスG1は、第2の入側流路3Bを通して第2のフィルタ室11B内に流入する。第2のフィルタ室11B内に流入した排気ガスG1は、第2のフィルタ材12Bによって当該排気ガスG1中の微粒子が捕捉された後、つまり集塵処理をされた後、清浄ガスG3として第2の出側流路4Bを通して排出される。他方、第1の開閉弁15A,16Aは閉状態に変わっているため、第1のフィルタ室11A内には排気ガスG1が流入しなくなり、集塵処理という観点では第1のフィルタ室11Aが系外におかれることになる。   Next, the first on-off valves 15A and 16A are changed to the closed state, and the second on-off valves 15B and 16B are changed to the open state. In this state, the exhaust gas G1 discharged from the heat treatment apparatus 110 flows into the second filter chamber 11B through the second inlet channel 3B. The exhaust gas G1 that has flowed into the second filter chamber 11B is the second clean gas G3 after the particulate matter in the exhaust gas G1 is captured by the second filter material 12B, that is, after dust collection processing. Is discharged through the outlet side flow path 4B. On the other hand, since the first on-off valves 15A and 16A are changed to the closed state, the exhaust gas G1 does not flow into the first filter chamber 11A, and the first filter chamber 11A is a system in terms of dust collection processing. I will be outside.

ところで、第1の開閉弁15A,16Aを閉状態に変えるのと、第2の開閉弁15B,16Bを開状態に変えるのとは同時に行うこともできるが、全ての開閉弁15A,15B,16A,16Bが閉状態になると問題が生じるおそれがある。
すなわち、熱処理装置110の熱処理室113内にはキャリアガスG2が流入し続けるため、全ての開閉弁15A,15B,16A,16Bが閉状態になると、排気ガスG1の行き場がなくなり、熱処理装置内の温度変化、圧力上昇を惹き起こしたり、熱処理室113内の微粒子が滞留して摺動部に噛み込んだりするおそれがある。
By the way, changing the first on-off valves 15A and 16A to the closed state and changing the second on-off valves 15B and 16B to the open state can be performed at the same time, but all the on-off valves 15A, 15B and 16A. , 16B may be in a closed state.
That is, since the carrier gas G2 continues to flow into the heat treatment chamber 113 of the heat treatment apparatus 110, when all the on-off valves 15A, 15B, 16A, and 16B are closed, the exhaust gas G1 has no place to go, so There is a risk of causing a temperature change and a pressure increase, and fine particles in the heat treatment chamber 113 may stay and be caught in the sliding portion.

そこで、開閉弁15A,15B,16A,16Bの開閉状態を変えるにあたっては、まず、第2の開閉弁15B,16Bを開状態に変え、前述検知手段を使用してこの開状態を確認した後、第1の開閉弁15A,16Aを閉状態に変えるのが好ましい。この形態によると、全ての開閉弁15A,15B,16A,16Bが開状態になっている間、第1のフィルタ室11A及び第2のフィルタ室11Bの両方に排気ガスG1が流入し、両フィルタ室11A,11Bにおいて集塵処理が行われることになるが、このことによる問題は特に存在せず、逆に、上記排気ガスG1の行き場がなくなるとの問題が解決される。なお、この趣旨から明らかな通り、第2の開閉弁15B,16Bを開状態は、全開状態に限定されず、少なくとも第2のフィルタ室11B内を排ガスG1が通過できるだけの開度となっていればよい。   Therefore, in changing the open / close state of the open / close valves 15A, 15B, 16A, 16B, first, the second open / close valve 15B, 16B is changed to the open state, and after confirming this open state using the detection means, It is preferable to change the first on-off valves 15A and 16A to the closed state. According to this embodiment, the exhaust gas G1 flows into both the first filter chamber 11A and the second filter chamber 11B while all the on-off valves 15A, 15B, 16A, 16B are open, and both filters Dust collection processing is performed in the chambers 11A and 11B, but there is no particular problem due to this, and conversely, the problem that the exhaust gas G1 has no place to go is solved. As is apparent from this point of view, the open state of the second on-off valves 15B and 16B is not limited to the fully open state, and the opening may be at least enough to allow the exhaust gas G1 to pass through the second filter chamber 11B. That's fine.

以上のようにして第1の開閉弁15A,16Aを閉状態とし、第2の開閉弁15B,16Bを開状態としたら、図示しない逆洗手段を使用して第1のフィルタ材12Aの逆洗を行う(逆洗工程)。この逆洗工程では、逆洗ガス、図示例では圧縮エアAをフィルタ材12Aの清浄領域側表面から集塵領域側表面に向けて噴射する。圧縮ガスAは、例えばパルス状に吹き込むことで行うことができる。この圧縮エアAの吹き込みにより、フィルタ材12Aに付着している微粒子は、当該フィルタ材12Aから払い落される。この点、従来の集塵設備(100)であれば、払い落された微粒子が入側流路を通して熱処理室113内に逆流するおそれが存在した。しかるに、本形態の集塵設備X1においては、入側流路3Aが第1の入側開閉弁15Aによって閉じられており、第1のフィルタ室11Aが系外とされているため、微粒子が逆流するおそれはない。   When the first on-off valves 15A and 16A are closed and the second on-off valves 15B and 16B are opened as described above, backwashing of the first filter material 12A is performed using backwashing means (not shown). (Back washing process). In this backwashing process, backwashing gas, compressed air A in the illustrated example, is sprayed from the clean area side surface of the filter material 12A toward the dust collection area side surface. The compressed gas A can be performed by blowing in a pulse shape, for example. Due to the blowing of the compressed air A, the fine particles adhering to the filter material 12A are removed from the filter material 12A. In this regard, with the conventional dust collection facility (100), there is a possibility that the fine particles that have been wiped out will flow back into the heat treatment chamber 113 through the inlet-side flow path. However, in the dust collection equipment X1 of this embodiment, the inlet side flow path 3A is closed by the first inlet side opening / closing valve 15A, and the first filter chamber 11A is out of the system, so that the fine particles flow backward. There is no risk.

以後、第1の開閉弁15A,16A及び第2の開閉弁15B,16Bの開閉状態の切り替えを繰り返すことで、集塵処理を連続的に行いつつ、フィルタ材12A,12Bの逆洗も定期的に行うことができる。ただし、例えば、第1の開閉弁15A,16A、又は第2の開閉弁15B,16Bを閉状態とするに先立って、第1の開閉弁15A,16A及び第2の開閉弁15B,16Bの両方を開状態とし、第1のフィルタ室11A及び第2のフィルタ室11Bの両方において集塵作業を行い、その後、第1の開閉弁15A,16A、又は第2の開閉弁15B,16Bを閉状態とすることもできる。つまり、本発明は、複数のフィルタ室のいずれかにおいて常に逆洗作業が行われていなければならないとするものではなく、複数のフィルタ室のうち少なくとも1のフィルタ室において集塵作業が行われている限り、適宜いずれかのフィルタ室において逆洗作業を行うことができるとするものであり、したがって、全てのフィルタ室において集塵作業が行われている状態も想定することができる。   Thereafter, by repeatedly switching the open / close state of the first on-off valves 15A and 16A and the second on-off valves 15B and 16B, the back-washing of the filter materials 12A and 12B is performed periodically while continuously performing the dust collection process. Can be done. However, for example, before the first on-off valves 15A and 16A or the second on-off valves 15B and 16B are closed, both the first on-off valves 15A and 16A and the second on-off valves 15B and 16B are used. Is opened, dust collection is performed in both the first filter chamber 11A and the second filter chamber 11B, and then the first on-off valve 15A, 16A or the second on-off valve 15B, 16B is closed. It can also be. In other words, the present invention does not always require that the backwashing operation is performed in any one of the plurality of filter chambers, and the dust collection operation is performed in at least one of the plurality of filter chambers. As long as there is a backwashing operation in any one of the filter chambers as appropriate, it is possible to assume a state in which the dust collection operation is performed in all the filter chambers.

なお、逆洗工程を実施するタイミングは、タイマーにより所定の時間経過毎に行うことや、フィルタ室の圧力損失を計測し、圧力損失が所定の数値以上となった場合に行うなどの制御により行うことができる。   In addition, the timing of performing the backwashing process is performed by a control such as a timer that is performed every predetermined time, or a pressure loss in the filter chamber is measured and the pressure loss is a predetermined numerical value or more. be able to.

ところで、フィルタ材12A,12Bの逆洗を行うために圧縮エアAをフィルタ室11A,11B内に吹き込むと、特にパルス状に吹き込むと、当該フィルタ室11A,11Bの内圧が上昇する。そして、フィルタ室11A,11Bの内圧が上昇した状態において入側開閉弁15A,15Bを閉状態から開状態に変えると、フィルタ室11A,11B内の微粒子が入側流路3A,3Bを通して熱処理室113内に逆流するおそれがある。しかしながら、本形態の集塵設備X1においては、出側流路4A,4Bから分岐する分岐路の途中に圧開放手段たる逆止弁17A,17Bが備えられている。したがって、当該逆止弁17A,17Bを通してフィルタ室11A,11Bの内圧が開放されるため、入側開閉弁15A,15Bを開状態に変えた際にフィルタ室11A,11B内から熱処理室113に向かってガスが流れるおそれはなく、フィルタ室11A,11B内の微粒子が入側流路3A,3Bを通して熱処理室113内に逆流するおそれがない。   By the way, when the compressed air A is blown into the filter chambers 11A and 11B in order to backwash the filter materials 12A and 12B, particularly when the compressed air is blown in a pulse shape, the internal pressure of the filter chambers 11A and 11B increases. When the inlet side on-off valves 15A and 15B are changed from the closed state to the opened state in a state where the internal pressures of the filter chambers 11A and 11B are increased, the fine particles in the filter chambers 11A and 11B pass through the inlet side flow paths 3A and 3B. There is a risk of backflow in 113. However, in the dust collection equipment X1 of this embodiment, check valves 17A and 17B, which are pressure release means, are provided in the middle of the branch paths branched from the outlet-side flow paths 4A and 4B. Therefore, since the internal pressure of the filter chambers 11A and 11B is released through the check valves 17A and 17B, when the inlet-side on-off valves 15A and 15B are changed to the open state, the filter chambers 11A and 11B are directed toward the heat treatment chamber 113. Therefore, there is no possibility that the gas flows, and there is no possibility that the fine particles in the filter chambers 11A and 11B flow backward into the heat treatment chamber 113 through the inlet-side flow paths 3A and 3B.

なお、分岐路は出側流路4A,4Bに接続されており、出側流路4A,4Bはフィルタ室12A,12Bの清浄領域側に接続されているため、逆止弁17A,17Bを通してフィルタ室11A,11B内の微粒子が流出するおそれはない。また、出側開閉弁16A,16Bを先に開方向に駆動させた後、入側開閉弁15A,15Bを開方向に駆動させることで、逆止弁17A,17Bが作動しない場合であってもフィルタ内の圧力を出側流路4A、4Bに開放することができる。   Since the branch passages are connected to the outlet flow paths 4A and 4B, and the outlet flow paths 4A and 4B are connected to the clean region side of the filter chambers 12A and 12B, the filter is passed through the check valves 17A and 17B. There is no possibility that the fine particles in the chambers 11A and 11B will flow out. Even if the check valves 17A and 17B are not actuated by driving the outlet side opening / closing valves 16A and 16B in the opening direction first and then driving the inlet side opening and closing valves 15A and 15B in the opening direction. The pressure in the filter can be released to the outlet channels 4A and 4B.

〔第2の実施の形態〕
次に、図2を参照しつつ、第2の実施の形態に係る集塵設備X2について、第1の実施の形態に係る集塵設備X1と相違する点を中心に説明する。
本形態の集塵設備X2も、熱処理装置110から排出された排気ガスG1中の微粒子を集塵して清浄ガスG3として排出する設備である。しかるに、本形態の集塵設備X2は、以下の点において前述した集塵設備X1と相違している。
[Second Embodiment]
Next, with reference to FIG. 2, the dust collection facility X2 according to the second embodiment will be described focusing on differences from the dust collection facility X1 according to the first embodiment.
The dust collection facility X2 of this embodiment is also a facility that collects particulates in the exhaust gas G1 discharged from the heat treatment apparatus 110 and discharges it as a clean gas G3. However, the dust collection equipment X2 of the present embodiment is different from the dust collection equipment X1 described above in the following points.

まず、集塵設備X1においては、入側弁手段が、第1の入側流路3Aの途中に備わる第1の入側開閉弁15Aと、第2の入側流路3Bの途中に備わる第2の入側開閉弁15Bとで構成されていた。しかるに、集塵設備X2においては、入側弁手段が、入側流路3が第1の入側流路3A及び第2の入側流路3Bに分岐する位置に備わる三方弁15Cで構成されている。この三方弁15Cを制御することで、入側流路3A,3Bを各別に開閉することができ、具体的には、排気ガスG1が第1の入側流路3A内においてのみ流通するように、又は第2の入側流路3B内においてのみ流通するように切り換えることができる。   First, in the dust collection facility X1, the inlet side valve means is provided in the middle of the first inlet side opening / closing valve 15A provided in the middle of the first inlet side channel 3A and in the middle of the second inlet side channel 3B. 2 entrance side on-off valve 15B. However, in the dust collection facility X2, the inlet side valve means is configured by a three-way valve 15C provided at a position where the inlet side channel 3 branches into the first inlet side channel 3A and the second inlet side channel 3B. ing. By controlling the three-way valve 15C, the inlet-side flow paths 3A and 3B can be opened and closed separately. Specifically, the exhaust gas G1 flows only in the first inlet-side flow path 3A. Alternatively, it can be switched so as to circulate only in the second inlet-side flow path 3B.

同様に、集塵設備X1においては、出側弁手段が、第1の出側流路4Aの途中に備わる第1の出側開閉弁16Aと、第2の出側流路4Bの途中に備わる第2の出側開閉弁16Bとで構成されていた。しかるに、集塵設備X2においては、出側弁手段が、第1の出側流路4A及び第2の出側流路4Bが合流する位置に備わる三方弁16Cで構成されている。この三方弁16Cを制御することで、出側流路4A,4Bを各別に開閉することができ、具体的には、清浄ガスG3が第1の出側流路4A内においてのみ流通するように、又は第2の出側流路4B内においてのみ流通するように切り替えることができる。   Similarly, in the dust collection equipment X1, the outlet valve means is provided in the middle of the first outlet side opening / closing valve 16A provided in the middle of the first outlet side flow path 4A and in the middle of the second outlet side flow path 4B. It comprised with the 2nd exit side on-off valve 16B. However, in the dust collection equipment X2, the outlet valve means is configured by a three-way valve 16C provided at a position where the first outlet flow path 4A and the second outlet flow path 4B join. By controlling the three-way valve 16C, the outlet channels 4A and 4B can be opened and closed separately. Specifically, the clean gas G3 flows only in the first outlet channel 4A. Or it can switch so that it may distribute | circulate only in the 2nd exit side flow path 4B.

この第2の実施形態によると、入側弁手段及び出側弁手段がシンプルな構造になるため、設備コストを下げることができる。また、三方弁15C,16Cは、第1の入側流路3A又は第2の入側流路3Bの一方、あるいは第1の出側流路4A又は第2の出側流路4Bの一方にしか排気ガスG1や清浄ガスG3を流通させない構造となっている。したがって、開閉弁を使用した場合におけるような誤動作の問題、例えば、誤動作によって逆洗中にフィルタ室11A,11B内のガスが熱処理室113に逆流してしまうような問題が生じるのを避けることができる。また、集塵処理及び逆洗処理の切替えを迅速に行うことができ、場合によって検知手段の設置を不要とすることもできる。   According to the second embodiment, since the inlet side valve means and the outlet side valve means have a simple structure, the equipment cost can be reduced. The three-way valves 15C and 16C are provided in one of the first inlet side channel 3A or the second inlet side channel 3B, or one of the first outlet side channel 4A or the second outlet side channel 4B. However, the exhaust gas G1 and the clean gas G3 are not circulated. Therefore, it is possible to avoid the problem of malfunction such as when the on-off valve is used, for example, the problem that the gas in the filter chambers 11A and 11B flows back to the heat treatment chamber 113 during backwashing due to malfunction. it can. In addition, switching between the dust collection process and the backwash process can be performed quickly, and in some cases, the installation of the detection means can be eliminated.

〔第3の実施の形態〕
次に、図3を参照しつつ、第3の実施の形態に係る集塵設備X3について、第2の実施の形態に係る集塵設備X2と相違する点を中心に説明する。
本形態の集塵設備X3も、熱処理装置110から排出された排気ガスG1中の微粒子を集塵して清浄ガスG3として排出する設備である。しかるに、本形態の集塵設備X3は、以下の点において前述した集塵設備X2と相違している。
[Third Embodiment]
Next, with reference to FIG. 3, the dust collection facility X3 according to the third embodiment will be described focusing on differences from the dust collection facility X2 according to the second embodiment.
The dust collection facility X3 of this embodiment is also a facility that collects particulates in the exhaust gas G1 discharged from the heat treatment apparatus 110 and discharges it as a clean gas G3. However, the dust collection facility X3 of the present embodiment is different from the dust collection facility X2 described above in the following points.

まず、集塵設備X2においては、第1のフィルタ室11A及び第2のフィルタ室11Bが各別の集塵容器によって構成されていた。しかるに、集塵設備X3においては、1つの集塵容器11の内空部が隔壁11xによって仕切られることで複数のフィルタ室が形成されており、図示例では第1のフィルタ室11A及び第2のフィルタ室11Bが形成されている。   First, in the dust collection facility X2, the first filter chamber 11A and the second filter chamber 11B are configured by separate dust collection containers. However, in the dust collection facility X3, a plurality of filter chambers are formed by partitioning the inner space of one dust collection container 11 by the partition wall 11x. In the illustrated example, the first filter chamber 11A and the second filter chamber 11 A filter chamber 11B is formed.

また、この集塵設備X3においては、入側流路3A,3Bがフィルタ室11A,11Bの底面に接続されている。同様に、出側流路4A,4Bがフィルタ室11A,11Bの天面に接続されている。   Further, in the dust collection equipment X3, the inlet-side flow paths 3A and 3B are connected to the bottom surfaces of the filter chambers 11A and 11B. Similarly, the outlet channels 4A and 4B are connected to the top surfaces of the filter chambers 11A and 11B.

なお、集塵設備X3においては、集塵設備X2と同様に、入側弁手段が三方弁15Cによって構成され、出側弁手段が三方弁16Cによって構成されている。しかるに、集塵設備X1の場合と同様に、集塵設備X3においても、入側弁手段を入側開閉弁15A,15Bで構成し、出側弁手段を出側開閉弁16A,16Bで構成することができる。   In the dust collection facility X3, as in the dust collection facility X2, the inlet side valve means is constituted by the three-way valve 15C, and the outlet side valve means is constituted by the three-way valve 16C. However, as in the case of the dust collection equipment X1, in the dust collection equipment X3, the inlet side valve means is constituted by the inlet side opening / closing valves 15A, 15B, and the outlet side valve means is constituted by the outlet side opening / closing valves 16A, 16B. be able to.

〔その他〕
以上の第1の実施形態から第3の実施形態においては、フィルタ室が2室存在する場合を説明したが、必要により、3室以上の複数室とすることもできる。
[Others]
In the above first to third embodiments, the case where there are two filter chambers has been described. However, if necessary, a plurality of chambers of three or more may be used.

本発明は、熱処理室内を臨む摺動部を有する熱処理装置から排出された排気ガス中に含まれる微粒子の集塵設備、熱処理システム及び集塵設備の運転方法として適用可能である。   INDUSTRIAL APPLICABILITY The present invention is applicable as a dust collection facility, a heat treatment system, and a method for operating a dust collection facility for fine particles contained in exhaust gas discharged from a heat treatment apparatus having a sliding portion that faces a heat treatment chamber.

3…入側流路、3A…第1の入側流路、3B…第2の入側流路、4…出側流路、4A…第1の出側流路、4B…第2の出側流路、11A…第1のフィルタ室、11B…第2のフィルタ室、12A…第1のフィルタ材、12B…第2のフィルタ材、15A…第1の入側開閉弁、15B…第2の入側開閉弁、15C…三方弁、16A…第1の出側開閉弁、16B…第2の出側開閉弁、16C…三方弁、17A…第1の逆止弁、17B…第2の逆止弁、100…熱処理手段、101…フィルタ室、102…フィルタ材、111…回動部、112…固定部、113…熱処理室、A…エア(空気)、C…摺動部、G1…排気ガス、G2…キャリアガス、G3…清浄ガス、X1〜3…集塵設備。   DESCRIPTION OF SYMBOLS 3 ... Input side flow path, 3A ... 1st input side flow path, 3B ... 2nd input side flow path, 4 ... Output side flow path, 4A ... 1st output side flow path, 4B ... 2nd output Side flow path, 11A ... first filter chamber, 11B ... second filter chamber, 12A ... first filter material, 12B ... second filter material, 15A ... first inlet side on-off valve, 15B ... second Inlet side on-off valve, 15C ... three-way valve, 16A ... first outlet-side on-off valve, 16B ... second outlet-side on-off valve, 16C ... three-way valve, 17A ... first check valve, 17B ... second Check valve, 100 ... heat treatment means, 101 ... filter chamber, 102 ... filter material, 111 ... rotating portion, 112 ... fixed portion, 113 ... heat treatment chamber, A ... air (air), C ... sliding portion, G1 ... Exhaust gas, G2 ... carrier gas, G3 ... clean gas, X1-3 ... dust collection equipment.

Claims (7)

熱処理室内を臨む摺動部を有する熱処理装置から排出された排気ガス中の微粒子を集塵して清浄ガスとして排出する設備であって、
前記排気ガスの入側流路及び前記清浄ガスの出側流路が接続されたフィルタ室と、このフィルタ室内に配置され、微粒子を集塵するフィルタ材と、前記フィルタ室内に逆洗ガスを吹き込んで前記フィルタ材を逆洗する逆洗手段とが備えられ、
前記フィルタ室が複数備わり、当該フィルタ室にはそれぞれ前記排気ガスの入側流路及び前記清浄ガスの出側流路が接続され、
前記排気ガスの入側流路を各別に開閉可能な入側弁手段、及び前記清浄ガスの出側流路を各別に開閉可能な出側弁手段が備わり、
更に前記フィルタ室の内圧を開放可能な圧開放手段が備わる、
ことを特徴とする集塵設備。
A facility for collecting particulates in exhaust gas discharged from a heat treatment apparatus having a sliding portion facing the heat treatment chamber and discharging it as clean gas,
A filter chamber to which the exhaust gas inlet-side flow path and the clean gas outlet-side flow path are connected, a filter material disposed in the filter chamber for collecting particulates, and backwash gas is blown into the filter chamber. And backwashing means for backwashing the filter material,
A plurality of the filter chambers are provided, and the filter chambers are connected to the exhaust gas inlet-side flow path and the clean gas outlet-side flow path, respectively.
Inlet valve means capable of opening and closing the inlet side flow path of the exhaust gas, and outlet side valve means capable of opening and closing the outlet side flow path of the clean gas separately,
Furthermore, a pressure release means capable of releasing the internal pressure of the filter chamber is provided.
Dust collection equipment characterized by that.
前記入側弁手段が前記排気ガスの入側流路それぞれに各別に備わり、
前記出側弁手段が前記清浄ガスの出側流路それぞれに各別に備わり、
前記入側弁手段及び前記出側弁手段の開状態又は閉状態の少なくとも一方を検知する検知手段が備わる、
請求項1記載の集塵設備。
The inlet side valve means is provided separately for each of the inlet side flow paths of the exhaust gas,
The outlet valve means is provided for each outlet flow path of the clean gas,
A detecting means for detecting at least one of an open state or a closed state of the inlet valve means and the outlet valve means;
The dust collection facility according to claim 1.
請求項1又は請求項2記載の集塵設備と、スチームチューブドライヤ又はロータリーキルンからなる熱処理装置と、が備わる、
ことを特徴とする熱処理システム。
The dust collection facility according to claim 1 or 2, and a heat treatment apparatus comprising a steam tube dryer or a rotary kiln are provided.
A heat treatment system characterized by that.
熱処理室内を臨む摺動部を有する熱処理装置から排出された排気ガス中の微粒子を集塵して清浄ガスとして排出する設備の運転方法であり、
前記排気ガスの入側流路及び前記清浄ガスの出側流路が接続されたフィルタ室と、このフィルタ室内に配置され、微粒子を集塵するフィルタ材と、前記フィルタ室内に逆洗ガスを吹き込んで前記フィルタ材を逆洗する逆洗手段と、が備えられた集塵設備の運転方法であって、
前記集塵設備として、前記フィルタ室が複数備わり、当該フィルタ室にはそれぞれ前記排気ガスの入側流路及び前記清浄ガスの出側流路が接続され、かつ前記フィルタ材が備わる設備を用意し、
それぞれの前記フィルタ室において、前記排気ガスの入側流路及び前記清浄ガスの出側流路を開状態として前記微粒子の集塵する集塵作業と、前記排気ガスの入側流路及び前記清浄ガスの出側流路を閉状態とした後に、前記逆洗ガスを吹き込んで前記フィルタ材を洗浄する逆洗作業と、が行われ、
かつ、複数の前記フィルタ室のうち少なくとも1のフィルタ室においては前記集塵作業が行われるように、前記入側流路及び前記出側流路の開閉状態を制御する、
ことを特徴とする集塵設備の運転方法。
It is an operation method of equipment for collecting fine particles in exhaust gas discharged from a heat treatment apparatus having a sliding part facing the heat treatment chamber and discharging it as clean gas,
A filter chamber to which the exhaust gas inlet-side flow path and the clean gas outlet-side flow path are connected, a filter material disposed in the filter chamber for collecting particulates, and backwash gas is blown into the filter chamber. And a backwashing means for backwashing the filter material, and a method of operating a dust collection facility comprising:
A plurality of the filter chambers are provided as the dust collection facility, and the filter chambers are connected to the exhaust gas inlet side flow path and the clean gas outlet side flow path, respectively, and are equipped with the filter material. ,
In each of the filter chambers, the exhaust gas inlet-side flow path and the clean gas outlet-side flow path are opened to collect dust, and the exhaust gas inlet-side flow path and the clean gas are collected. After the gas outlet side flow path is closed, the backwashing operation of cleaning the filter material by blowing the backwash gas is performed,
And, in at least one filter chamber among the plurality of filter chambers, the opening and closing states of the inlet-side channel and the outlet-side channel are controlled so that the dust collection operation is performed.
The operation method of the dust collection equipment characterized by this.
いずれかの前記フィルタ室において逆洗作業が行われた後、他の前記フィルタ室において逆洗作業が行われるに先立って、全ての前記フィルタ室において集塵作業が行われる、
請求項4記載の集塵設備の運転方法。
After the backwashing operation is performed in any of the filter chambers, the dust collection operation is performed in all the filter chambers before the backwashing operation is performed in the other filter chambers.
The operation method of the dust collection equipment of Claim 4.
前記排気ガスの入側流路及び前記清浄ガスの出側流路を開状態に変えるに先立って、当該入側流路及び出側流路が接続されたフィルタ室内の圧力を開放しておく、
請求項4又は請求項5記載の集塵設備の運転方法。
Prior to changing the inlet side flow path of the exhaust gas and the outlet side flow path of the clean gas to the open state, the pressure in the filter chamber to which the inlet side flow path and the outlet side flow path are connected is released.
The operation method of the dust collection equipment of Claim 4 or Claim 5.
前記排気ガスの入側流路及び前記清浄ガスの出側流路を閉状態に変えるに先立って、開状態とされた排気ガスの入側流路及び清浄ガスの出側流路が存在することを確認する、
請求項4〜6のいずれか1項に記載の集塵設備の運転方法。
Prior to changing the exhaust gas inlet-side flow path and the clean gas outlet-side flow path to the closed state, the exhaust gas inlet-side flow path and the clean gas outlet-side flow path exist. Check the
The operation method of the dust collection equipment of any one of Claims 4-6.
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Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5445874A (en) * 1977-09-17 1979-04-11 Toyota Motor Corp Bag filter type dust collector and method of collecting dust therefor
JPS60222123A (en) * 1984-04-20 1985-11-06 Hitachi Plant Eng & Constr Co Ltd Mechanism for controlling backwashing cycle for bag filter
JPS6190719A (en) * 1984-10-11 1986-05-08 Hitachi Plant Eng & Constr Co Ltd Controller of bag filter
JPS61256180A (en) * 1985-05-09 1986-11-13 川崎製鉄株式会社 Method of controlling powdered and granular body drier
JPS63258616A (en) * 1987-04-15 1988-10-26 Shintou Dasutokorekutaa Kk Dust collector
JPH0312210A (en) * 1989-06-12 1991-01-21 Kawasaki Steel Corp Backwashing method of dry dust collector
JPH11264525A (en) * 1998-03-18 1999-09-28 Kubota Corp Waste treating system and operating method of waste treating system
JP2003038922A (en) * 2001-07-30 2003-02-12 Kawasaki Steel Corp Bag filter-type dust collector
JP2009097783A (en) * 2007-10-16 2009-05-07 Kobe Steel Ltd Indirect heating/drying device, indirect heating/drying method for object to be dried, method for manufacturing solid fuel, and its manufacturing device
JP2010207702A (en) * 2009-03-10 2010-09-24 Taiyo Nippon Sanso Corp Dust collection apparatus

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5445874A (en) * 1977-09-17 1979-04-11 Toyota Motor Corp Bag filter type dust collector and method of collecting dust therefor
JPS60222123A (en) * 1984-04-20 1985-11-06 Hitachi Plant Eng & Constr Co Ltd Mechanism for controlling backwashing cycle for bag filter
JPS6190719A (en) * 1984-10-11 1986-05-08 Hitachi Plant Eng & Constr Co Ltd Controller of bag filter
JPS61256180A (en) * 1985-05-09 1986-11-13 川崎製鉄株式会社 Method of controlling powdered and granular body drier
JPS63258616A (en) * 1987-04-15 1988-10-26 Shintou Dasutokorekutaa Kk Dust collector
JPH0312210A (en) * 1989-06-12 1991-01-21 Kawasaki Steel Corp Backwashing method of dry dust collector
JPH11264525A (en) * 1998-03-18 1999-09-28 Kubota Corp Waste treating system and operating method of waste treating system
JP2003038922A (en) * 2001-07-30 2003-02-12 Kawasaki Steel Corp Bag filter-type dust collector
JP2009097783A (en) * 2007-10-16 2009-05-07 Kobe Steel Ltd Indirect heating/drying device, indirect heating/drying method for object to be dried, method for manufacturing solid fuel, and its manufacturing device
JP2010207702A (en) * 2009-03-10 2010-09-24 Taiyo Nippon Sanso Corp Dust collection apparatus

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