JP2009202142A - Dust removal apparatus - Google Patents

Dust removal apparatus Download PDF

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JP2009202142A
JP2009202142A JP2008050032A JP2008050032A JP2009202142A JP 2009202142 A JP2009202142 A JP 2009202142A JP 2008050032 A JP2008050032 A JP 2008050032A JP 2008050032 A JP2008050032 A JP 2008050032A JP 2009202142 A JP2009202142 A JP 2009202142A
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dust
duct
baffle plate
flow path
gas flow
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Masao Taguma
昌夫 田熊
Shinya Tsuneizumi
慎也 常泉
Shigetaka Odaka
成貴 小高
Yasushi Takigawa
靖史 滝川
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Mitsubishi Heavy Industries Environmental Engineering Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a dust removal apparatus for removing dust from an exhaust gas which is space-saving, structually simple, and operable at a low cost. <P>SOLUTION: Provided is a dust removal apparatus for removing dust (such as, particulate matter of powdery dust, fly ash, or pulverized coal) from a duct 1 through which a gas containing the dust passes, wherein a baffle plate 2 is installed in that passage part of the inside duct wall which is situated downstream, in the gas flow direction, of a duct bent part 6 formed by an angle change or curving of the duct 1 and on which the gas flow exerts a centrifugal force, the dust moved to the side of the passage part is trapped by the baffle plate 2, and an openable and closable port 3 is formed in a position 4 where the trapped dust deposits. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は粉塵、飛灰、微粉炭等の粉粒物(以下ダストという)を含んだガスが通流するダクト、例えば燃焼炉の排ガス通路若しくは煙道、若しくは微粉炭を空気などと混合して搬送する搬送路して機能するダクトよりダストを除去するダスト除去装置に関する。   The present invention relates to a duct through which a gas containing particulate matter (hereinafter referred to as dust) such as dust, fly ash, and pulverized coal flows, such as an exhaust gas passage or flue of a combustion furnace, or pulverized coal mixed with air. The present invention relates to a dust removing device that removes dust from a duct that functions as a conveying path.

従来、例えばごみ固形燃料化設備、ごみ焼却炉、一般焼却炉などにおいて、粉塵、飛灰、微粉炭等の粉粒物(以下ダストという)を含んだ排ガスが排出され、排ガス中に含まれる多くのダストにより周囲環境が悪化するので、その環境の悪化を防止するため排気する際に除塵するようにされている。このダストを含んだ排ガスは高温であるため、途中で発火して下流に設置される集塵器に送込まれることがある。このダストを除去する装置の一つにサイクロンがある。サイクロンは、ダストまたは固体粒子とガス体との混相流すなわち含塵気流からダストを遠心分離する除塵装置の一種であるが、設置スペースの確保が困難であり、コストもかかる。   Conventionally, exhaust gas containing particulate matter (hereinafter referred to as dust) such as dust, fly ash, and pulverized coal has been discharged in many cases, such as waste solid fuel conversion facilities, waste incinerators, and general incinerators. Since the surrounding environment deteriorates due to the dust, the dust is removed when exhausting in order to prevent the deterioration of the environment. Since the exhaust gas containing dust is high in temperature, it may ignite halfway and sent to a dust collector installed downstream. One device for removing this dust is a cyclone. A cyclone is a kind of dust removing device that centrifuges dust from a mixed phase flow of dust or solid particles and a gas body, that is, a dust-containing airflow, but it is difficult to secure an installation space and costs high.

よって、より簡便なダスト除去として、排気ガス中に含まれるダストを集塵器以外の手段で除去する特許文献1(特開平10−230116号公報)が開示されている。特許文献1は、ダストを含む排ガスが流れる流路の断面積を拡大して排ガス流速を低減させ、ダストを分離して除去しようとするものである。詳しくは、粉状化した廃棄物または灰を高温で溶融処理する連続式溶融炉の排ガス通路構造において、前記溶融炉の上部に接続したテーパー状の接続部を下部に備え、且つダスト除去手段を上部に備えたダスト分離室を設け、ダスト分離室の上方に分離室上部径より小径のダクトを接続させた構成とし、流速を低減させることでダストの分離を促進している。   Therefore, Patent Document 1 (Japanese Patent Laid-Open No. 10-230116) that removes dust contained in exhaust gas by means other than a dust collector is disclosed as simpler dust removal. Patent Document 1 attempts to separate and remove dust by increasing the cross-sectional area of a flow path through which exhaust gas containing dust flows to reduce the exhaust gas flow velocity. Specifically, in an exhaust gas passage structure of a continuous melting furnace that melts powdered waste or ash at a high temperature, a tapered connection part connected to the upper part of the melting furnace is provided at the lower part, and dust removing means is provided. A dust separation chamber provided in the upper portion is provided, and a duct having a smaller diameter than the upper diameter of the separation chamber is connected above the dust separation chamber, and dust separation is promoted by reducing the flow velocity.

また、特許文献2(特開平10−183232号公報)には、真空脱ガス装置のガスクーラーあるいはその隣接するダクトに、ガスクーラーの水管の表面に向かってガス体を吹き付けるノズルを有するランスを設けてダストを除去する発明が開示されている。特許文献2では、排ガスが流れているガスクーラーの水管に付着したダストを、ランスにガス体を供給して吹きつけることにより、水管の表面についているダストを除去している。なお、ここで用いられているガス体としては、蒸気、窒素ガス、空気、Arなどの不活性ガスやCO等が挙げられる。 Further, in Patent Document 2 (Japanese Patent Laid-Open No. 10-183232), a lance having a nozzle for blowing a gas body toward the surface of the water pipe of the gas cooler is provided in the gas cooler of the vacuum degassing apparatus or its adjacent duct. An invention for removing dust is disclosed. In patent document 2, the dust adhering to the water pipe of the gas cooler in which exhaust gas flows is supplied to the lance and blown to remove dust attached to the surface of the water pipe. As the gas material used here, steam, nitrogen gas, air, inert gas or CO 2 or the like, such as Ar and the like.

特開平10−230116号公報JP-A-10-230116 特開平10−183232号公報Japanese Patent Laid-Open No. 10-183232

しかしながら、特許文献1に開示された発明では、構造的に簡単で設置スペースを少なくできるダスト除去の構造ではあるが、小粒径ダストの捕集、除去についての具体的な方法は提案されておらず、排ガス流速を低減させることで比較的粒径が大きいダストは分離することができても小粒径ダストを分離するには不十分であると考えられる。
また、特許文献2に開示された発明では、連続的に吹き付けを行った場合、ガス体の消費量が増大し、コストがかかる。またコストの問題を解消するために、一定時間おきに駆動して吹き付けを行なった場合、効率が低下してダストの堆積が進行するという問題点が挙げられる。
However, in the invention disclosed in Patent Document 1, although it is a structure for dust removal that is structurally simple and can reduce installation space, a specific method for collecting and removing small particle size dust has not been proposed. However, even if dust having a relatively large particle size can be separated by reducing the exhaust gas flow rate, it is considered that it is insufficient for separating the small particle size dust.
Further, in the invention disclosed in Patent Document 2, when spraying is performed continuously, the consumption of the gas body increases and costs increase. Further, in order to solve the problem of cost, when spraying is performed at regular intervals, efficiency is lowered and dust accumulation proceeds.

従って、本発明は上記従来技術の問題点に鑑み、省スペースで構造的に簡単且つ低コストで運転可能な排ガス中のダストを除去するダスト除去装置を提供することを目的とする。   Therefore, in view of the above-described problems of the prior art, an object of the present invention is to provide a dust removing device that removes dust in exhaust gas that is space-saving, structurally simple and can be operated at low cost.

そこで、本発明はかかる課題を解決するために、粉塵、飛灰、微粉炭等の粉粒物(以下ダストという)を含んだガスが通流するダクトよりダストを除去するダスト除去装置において、
前記ダクトの角度変向若しくは湾曲により形成されるダクト曲がり部のガス通流方向下流側に位置するダクト内壁部の、ガスの流れによる遠心力が作用する流路部位に邪魔板を設置し、該邪魔板により遠心力が作用する流路部位側に振られたダストを捕集すると共に、該捕集されたダストの堆積位置に開閉可能な開口部を設けたことを特徴とする。
Therefore, in order to solve such a problem, the present invention provides a dust removing apparatus for removing dust from a duct through which a gas containing dust (flying ash), pulverized coal, etc. (hereinafter referred to as dust) flows.
A baffle plate is installed at a flow path portion where a centrifugal force due to gas flow acts on a duct inner wall portion located downstream of the duct bending portion formed by an angle turning or bending of the duct, Dust shaken by the baffle plate toward the flow path portion where the centrifugal force acts is collected, and an opening that can be opened and closed is provided at the collected dust accumulation position.

これにより、ダストを含んだ排ガスがダクト曲がり部を通過する際、排ガス中のダスト粒子の中でも粒径の大きいダストは、遠心力により曲がりの外側に振られて堆積する。また、ダクト曲がり部で堆積しない粒径が小さいダストも、ダクト曲がり部のガス通流方向下流側に位置するダクト内壁部のガスの流れによる遠心力が作用する流路部位に設置された邪魔板により、衝突させて重力で落下させて捕集することができる。
また、ダストの堆積位置に開閉可能な開口部を設けたことより、ダストの堆積が顕著になった場合にダストを開口部より抜き出して除去することが可能である。
As a result, when the exhaust gas containing dust passes through the duct bend, dust having a large particle size among dust particles in the exhaust gas is shaken and accumulated outside the curve by centrifugal force. Dust with a small particle size that does not accumulate at the bent part of the duct is also a baffle plate installed in the flow path part where the centrifugal force due to the gas flow on the duct inner wall part located downstream of the duct bent part in the gas flow direction acts. By this, it can collide and drop by gravity and can be collected.
In addition, since an opening that can be opened and closed is provided at the dust accumulation position, the dust can be extracted and removed from the opening when dust accumulation becomes significant.

また本発明において、前記開口部形成位置が、邪魔板取付位置よりガス流れ方向上流側に位置するダクト曲がり部の角度変向位置または曲がり部の最大曲率部、若しくは変曲点における重力が作用する位置であることを特徴とする。
上述したようなダストが堆積する位置に開口部を設けて堆積したダストを断続的に除去し、排ガスから分離されたダストが再び排ガスの流路に戻らないようにする。
Further, in the present invention, the opening forming position is the angle turning position of the duct bending portion located at the upstream side in the gas flow direction from the baffle plate mounting position, the maximum curvature portion of the bending portion, or gravity at the inflection point. It is a position.
An opening is provided at a position where dust is accumulated as described above, and the accumulated dust is intermittently removed so that the dust separated from the exhaust gas does not return to the exhaust gas flow path again.

さらに、粉塵、飛灰、微粉炭等の粉粒物(以下ダストという)を含んだガスが通流するダクトよりダストを除去するダスト除去装置において、
前記少なくとも45°以下の傾き方向若しくは水平方向にほぼ直線状に流路が形成されている部位に、重力方向に向けて拡幅化されてなるバッファ部を設けると共に、バッファ部のガス流れ方向下流側位置(好ましくは終端側位置)に邪魔板を設置し、該邪魔板により前記ガスが重力方向に迂回してバッファ部終端より下流側に位置する流路に流れるように邪魔板の取付位置と高さ及び幅域を設定するとともに、前記迂回時にダストに作用する遠心力によりダストをバッファ底壁側に捕集し、該バッファ底壁側の前記ダストの堆積位置に開閉可能な開口部を設けたことを特徴とする。
Furthermore, in a dust removing device that removes dust from a duct through which gas containing dust, fly ash, pulverized coal, etc. (hereinafter referred to as dust) flows,
A buffer portion that is widened in the direction of gravity is provided at a portion where the flow path is formed substantially linearly in the inclination direction or the horizontal direction of at least 45 ° or less, and downstream of the buffer portion in the gas flow direction A baffle plate is installed at a position (preferably the end side position), and the baffle plate is installed at a height higher than the baffle plate so that the baffle plate bypasses the gas in the direction of gravity and flows into the flow path located downstream from the buffer unit end. In addition to setting the height and width range, the dust is collected on the buffer bottom wall side by centrifugal force acting on the dust during the detour, and an opening that can be opened and closed is provided at the dust accumulation position on the buffer bottom wall side It is characterized by that.

このようにガス流路にバッファ部を設けることにより、ガス流路の断面積が急激に大きくなるバッファ部の入口部で流れが剥離し、よどんだ部分が形成されダストが捕集されやすくなり、バッファ部にダストが堆積される。また、上述した剥離域で堆積されずにガス流路にのったままダストも、バッファ部のガス流れ方向下流側位置に設置された邪魔板に衝突し重力で落下するため捕集することができる。
また、ダストの堆積位置に開口部を設けることにより、ダストの堆積が顕著になった場合にダストを開口部より抜き出して除去することが可能である。
By providing the buffer part in the gas flow path in this way, the flow is separated at the inlet part of the buffer part where the cross-sectional area of the gas flow path increases rapidly, and a stagnation part is formed and dust is easily collected, Dust is deposited on the buffer. In addition, dust that is not deposited in the above-described separation zone but remains on the gas flow path collides with a baffle plate installed at a downstream position in the gas flow direction of the buffer unit and is collected because it falls by gravity. it can.
Further, by providing an opening at the dust accumulation position, when dust accumulation becomes significant, the dust can be extracted and removed from the opening.

また、前記邪魔板はバッファ部のガス流れ方向下流側に位置するバッファ部上壁よりガス流れ方向(投影方向)において下流側流路を塞ぐ如くその下方延在長さを設定したことを特徴とする。
このように、バッファ部のガス流れ方向下流側位置に設置された邪魔板は、ガス流路を塞いで排ガス中のダストの分離除去を促進する。
In addition, the baffle plate has a length extending downward from the upper wall of the buffer portion located downstream of the buffer portion in the gas flow direction so as to block the downstream flow path in the gas flow direction (projection direction). To do.
Thus, the baffle plate installed at the downstream position in the gas flow direction of the buffer portion closes the gas flow path and promotes the separation and removal of dust in the exhaust gas.

以上記載のごとく本発明によれば、ダストを含んだ排ガスがダクト曲がり部を通過する際、排ガス中のダスト粒子の中でも粒径の大きいダストは、遠心力により曲がりの外側に振られて堆積する。また、ダクト曲がり部で堆積しない粒径が小さいダストも、ダクト曲がり部のガス通流方向下流側に位置するダクト内壁部のガスの流れによる遠心力が作用する流路部位に設置された邪魔板により、衝突させて重力で落下させて捕集することができる。
さらに、ガス流路にバッファ部を設けることにより、ガス流路の断面積が急激に大きくなるバッファ部の入口部で流れが剥離し、よどんだ部分が形成されダストが捕集されやすくなり、バッファ部にダストが堆積される。また、上述した剥離域で堆積されずにガス流路にのったままダストも、バッファ部のガス流れ方向下流側位置に設置された邪魔板に衝突し重力で落下するため捕集することができる。
このようにして捕集して堆積されたダストは、ダクトに設けられた開閉可能な開口部により、ダストの堆積が顕著になった場合にダストを開口部より抜き出して除去することが可能である。
As described above, according to the present invention, when the exhaust gas containing dust passes through the duct bend, dust having a large particle size among the dust particles in the exhaust gas is shaken and accumulated outside the curve by centrifugal force. . Dust with a small particle size that does not accumulate at the bent part of the duct is also a baffle plate installed in the flow path part where the centrifugal force due to the gas flow on the duct inner wall part located downstream of the duct bent part in the gas flow direction acts. By this, it can collide and drop by gravity and can be collected.
Furthermore, by providing a buffer part in the gas flow path, the flow is separated at the inlet part of the buffer part where the cross-sectional area of the gas flow path suddenly increases, and a stagnation part is formed and dust is easily collected. Dust is deposited on the part. In addition, dust that is not deposited in the above-described separation zone but remains on the gas flow path collides with a baffle plate installed at a downstream position in the gas flow direction of the buffer unit and is collected because it falls by gravity. it can.
The dust collected and accumulated in this way can be removed by removing the dust from the opening when dust accumulation becomes significant by the openable / closable opening provided in the duct. .

以下、図面を参照して本発明の好適な実施例を例示的に詳しく説明する。但しこの実施例に記載されている構成部品の寸法、材質、形状、その相対的配置等は特に特定的な記載がない限りは、この発明の範囲をそれに限定する趣旨ではなく、単なる説明例に過ぎない。   Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the components described in this embodiment are not intended to limit the scope of the present invention unless otherwise specified, but are merely illustrative examples. Not too much.

図1は実施例1に係るダスト除去装置を示す概略側面図である。図1において、1はダスト(粉塵、飛灰、微粉炭等の粉粒物)を含んだガスが通流するダクト(ガス流路)、2はダクト内に設けられた邪魔板、3は開口部であり、4はダスト堆積位置、6はダクト1の角度変向若しくは湾曲により形成されるダクト曲がり部である。
なお、ダクト曲がり部6はダクト1の角度変向若しくは湾曲により形成されるものであり、ここでは例えばダクト1が直角に曲がって形成された曲がり部を示している。
FIG. 1 is a schematic side view showing the dust removing apparatus according to the first embodiment. In FIG. 1, 1 is a duct (gas flow path) through which a gas containing dust (dust particles such as dust, fly ash, and pulverized coal) flows, 2 is a baffle plate provided in the duct, and 3 is an opening. 4 is a dust accumulation position, and 6 is a bent part of the duct formed by an angle change or curvature of the duct 1.
The duct bent portion 6 is formed by changing the angle or bending of the duct 1, and here, for example, a bent portion formed by bending the duct 1 at a right angle is shown.

ダクト1を通流する排ガス中のダストは、ダクト曲がり部6を通過する際に、遠心力により曲がりの外側に振られてダスト堆積位置4に堆積する。この遠心力により曲がりの外側に振られるダストは、排ガス中有のダストの中でも比較的粒径の大きいものであるので、排ガスの流れに乗らず落下・沈降する。
一方、粒径の小さいダストは曲がりの外側に振られるものの、落下・沈降せず排ガスの流れにのったまま堆積しない場合が考えられ、これを捕集するために邪魔板2を設ける。ダストを含む排ガスの流路を塞ぐ邪魔板2にダストを衝突させることにより、ダストが落下し、ダスト堆積位置4に堆積するので分離を促進することができる。
When the dust in the exhaust gas flowing through the duct 1 passes through the bent portion 6 of the duct, it is swung to the outside of the bend due to centrifugal force and accumulated at the dust accumulation position 4. The dust swung to the outside of the bend due to the centrifugal force has a relatively large particle size among the dusts contained in the exhaust gas, and therefore falls and settles without riding on the flow of the exhaust gas.
On the other hand, although dust with a small particle diameter is swung to the outside of the bend, it may be considered that it does not fall and settle and does not accumulate on the flow of exhaust gas, and a baffle plate 2 is provided to collect this. By causing the dust to collide with the baffle plate 2 that blocks the flow path of the exhaust gas containing dust, the dust falls and accumulates at the dust accumulation position 4, so that the separation can be promoted.

なお、邪魔板2はダクト曲がり部6のガス通流方向下流側に位置するダクト内壁部のガスの流れによる遠心力が作用する流路部位に設ける。邪魔板2の設置位置は、ガス流路径(ガス流路幅)をD、ダクト曲がり部6から邪魔板設置位置までの長さをLとしたとき、流路を塞がないL≦1D〜20Dの範囲で設置することが好ましく、特に排ガスの流速との関係からL≦3Dがより好ましい。
また、邪魔板2の高さHは、ガス流路径Dの半分である1/D以上であることが好ましく、邪魔板2の面積はダクト1の流路面積の半分以上であることが望ましい。
In addition, the baffle plate 2 is provided in the flow path part where the centrifugal force by the gas flow of the duct inner wall part located in the gas flow direction downstream of the duct bending part 6 acts. The installation position of the baffle plate 2 is such that the gas flow path diameter (gas flow path width) is D and the length from the duct bent portion 6 to the baffle plate installation position is L, so that the flow path is not blocked L ≦ 1D to 20D In particular, L ≦ 3D is more preferable from the relationship with the flow rate of exhaust gas.
The height H of the baffle plate 2 is preferably 1 / D or more, which is half of the gas flow path diameter D, and the area of the baffle plate 2 is preferably at least half of the flow path area of the duct 1.

ダスト堆積位置4に堆積されたダストは、ダクトに形成された開口部3により抜き出されて除去される。開口部3は通常は閉められており、ダスト堆積位置4のダストの堆積が顕著になった場合に開かれてダストを断続的に除去している。このようにして、ダストを含む排ガスからダストを分離除去することができる。   The dust accumulated at the dust accumulation position 4 is extracted and removed by the opening 3 formed in the duct. The opening 3 is normally closed, and is opened when dust accumulation at the dust accumulation position 4 becomes significant, and dust is intermittently removed. In this way, dust can be separated and removed from the exhaust gas containing dust.

図2は、実施例2に係るダスト除去装置を示す概略側面図である。図1と同様に、1はダスト(粉塵、飛灰、微粉炭等の粉粒物)を含んだガスが通流するダクト(ガス流路)、2はダクト内に設けられた邪魔板、3は開口部であり、4はダスト堆積位置、6はダクト1の角度変向若しくは湾曲により形成されるダクト曲がり部を示しており、図1とほぼ同一の構成であるが、排ガスがダクト1の上方から下方へ流れる点が異なる。   FIG. 2 is a schematic side view illustrating the dust removing apparatus according to the second embodiment. As in FIG. 1, 1 is a duct (gas flow path) through which a gas containing dust (dust particles such as dust, fly ash, pulverized coal) flows, 2 is a baffle plate provided in the duct, 3 1 is an opening, 4 is a dust accumulation position, and 6 is a duct bend formed by an angle change or curve of the duct 1, which has almost the same configuration as FIG. It differs in that it flows from top to bottom.

図2のように、ダクト1を通流する排ガス中のダストは、ダクト曲がり部6を通過する際に、遠心力により曲がりの外側に振られて重力によりダスト堆積位置4に堆積する。図2の場合、小粒径のダストも曲がりの外側に振られて重力によりダスト堆積位置4に堆積する。ダクト堆積位置4は邪魔板2上であるので、排ガスから分離されたダストが再び排ガスの流路に戻らないように、開口部3を開いて断続的にダストを除去する。   As shown in FIG. 2, when the dust in the exhaust gas flowing through the duct 1 passes through the duct bending portion 6, it is shaken to the outside of the bending by centrifugal force and is accumulated at the dust accumulation position 4 by gravity. In the case of FIG. 2, dust having a small particle diameter is also swung to the outside of the bend and accumulated at the dust accumulation position 4 by gravity. Since the duct accumulation position 4 is on the baffle plate 2, the dust is intermittently removed by opening the opening 3 so that the dust separated from the exhaust gas does not return to the exhaust gas flow path again.

図3(a)は、実施例3に係るダスト除去装置を示す概略側面図を示し、図3(b)は図3(a)のA―A線に沿う断面図である。
図3において、1はダスト(粉塵、飛灰、微粉炭等の粉粒物)を含んだガスが通流するダクト(ガス流路)、2は邪魔板、3は開口部であり、7,8はダスト堆積位置、5はダクト1を拡幅して形成されたバッファである。
FIG. 3A is a schematic side view showing the dust removing apparatus according to the third embodiment, and FIG. 3B is a cross-sectional view taken along the line AA in FIG.
In FIG. 3, 1 is a duct (gas flow path) through which a gas containing dust (dust particles such as dust, fly ash and pulverized coal) flows, 2 is a baffle plate, 3 is an opening, 8 is a dust accumulation position, and 5 is a buffer formed by widening the duct 1.

ダクト1を通流する排ガス中は、ガス流路の断面積が急激に大きくなるバッファ5の入口部で流れが剥離し、よどんだ部分が形成されダストが捕集されやすくなり、バッファ5のダスト堆積位置7にダストが堆積される。
一方、剥離域で堆積されずにガス流路にのったままのダスト(小粒径のダスト)は、バッファ5のガス流れ方向下流側位置に設置された邪魔板2に衝突し重力で落下する。このため、ダストはダスト堆積位置8に堆積し、捕集することができる。このようにしてダスト堆積位置7,8に堆積したダストは、堆積が顕著になった場合に開口部3を開き抜き出して除去される。
In the exhaust gas flowing through the duct 1, the flow is separated at the inlet portion of the buffer 5 where the cross-sectional area of the gas flow path suddenly increases, and a stagnation portion is formed and dust is easily collected. Dust is deposited at the deposition position 7.
On the other hand, the dust (small particle size dust) that is not deposited in the separation zone but remains on the gas flow path collides with the baffle plate 2 installed downstream of the buffer 5 in the gas flow direction and falls by gravity. To do. For this reason, dust accumulates at the dust accumulation position 8 and can be collected. The dust accumulated in the dust accumulation positions 7 and 8 in this way is removed by opening the opening 3 when the accumulation becomes significant.

図3(a)に示すように、邪魔板2はダストと衝突させるために、バッファ5のガス流れ方向下流側位置に設置されており、バッファ5の上壁よりガス流れ方向(投影方向)において下流側流路を塞ぐ如くその下方延在長さを設定することが望ましい。つまり、邪魔板2の高さHはガス流路径Dよりも大とし、また邪魔板2の断面積はダクト1の断面積よりも大になるように形成する(図3(b))。
このように、バッファ5とともに邪魔板2を設けることにより、排ガス中のダストの分離除去を行なう。
As shown in FIG. 3A, the baffle plate 2 is installed at a downstream position in the gas flow direction of the buffer 5 in order to collide with dust, and in the gas flow direction (projection direction) from the upper wall of the buffer 5. It is desirable to set the downward extension length so as to block the downstream channel. That is, the height H of the baffle plate 2 is larger than the gas flow path diameter D, and the cross-sectional area of the baffle plate 2 is larger than the cross-sectional area of the duct 1 (FIG. 3B).
Thus, by providing the baffle plate 2 together with the buffer 5, the dust in the exhaust gas is separated and removed.

本発明によれば、ダスト(粉塵、飛灰、微粉炭等の粉粒物)を含んだガスが通流するダクト、例えば燃焼炉の排ガス通路若しくは煙道、若しくは微粉炭を空気などと混合して搬送する搬送路して機能するダクトよりダストを除去するダスト除去装置として有益である。   According to the present invention, a duct through which gas containing dust (dust, fly ash, pulverized coal, etc.) flows, such as an exhaust gas passage or flue of a combustion furnace, or pulverized coal is mixed with air or the like. It is useful as a dust removing device that removes dust from a duct that functions as a conveying path.

実施例1に係るダスト除去装置を示す概略側面図である。1 is a schematic side view showing a dust removing device according to Embodiment 1. FIG. 実施例2に係るダスト除去装置を示す概略側面図である。It is a schematic side view which shows the dust removal apparatus which concerns on Example 2. FIG. (a)は実施例3に係るダスト除去装置を示す概略側面図、(b)は図3(a)のA―A線に沿う断面図である。(A) is a schematic side view which shows the dust removal apparatus which concerns on Example 3, (b) is sectional drawing which follows the AA line of Fig.3 (a).

符号の説明Explanation of symbols

1 ダクト(ガス流路)
2 邪魔板
3 開口部
4 ダスト堆積位置
5 バッファ
6 ダクト曲がり部
1 Duct (gas flow path)
2 Baffle plate 3 Opening 4 Dust accumulation position 5 Buffer 6 Duct bent part

Claims (4)

粉塵、飛灰、微粉炭等の粉粒物(以下ダストという)を含んだガスが通流するダクトよりダストを除去するダスト除去装置において、
前記ダクトの角度変向若しくは湾曲により形成されるダクト曲がり部のガス通流方向下流側に位置するダクト内壁部の、ガスの流れによる遠心力が作用する流路部位に邪魔板を設置し、該邪魔板により遠心力が作用する流路部位側に振られたダストを捕集すると共に、該捕集されたダストの堆積位置に開閉可能な開口部を設けたことを特徴とするダスト除去装置。
In a dust removal device that removes dust from a duct through which gas containing dust, fly ash, pulverized coal, etc. (hereinafter referred to as dust) flows,
A baffle plate is installed at a flow path portion where a centrifugal force due to gas flow acts on a duct inner wall portion located downstream of the duct bending portion formed by an angle turning or bending of the duct, A dust removing apparatus characterized by collecting dust shaken by a baffle plate toward a flow path portion where a centrifugal force acts, and providing an openable / closable opening at a position where the collected dust is accumulated.
前記開口部形成位置が、邪魔板取付位置よりガス流れ方向上流側に位置するダクト曲がり部の角度変向位置または曲がり部の最大曲率部、若しくは変曲点における重力が作用する位置であることを特徴とする請求項1記載のダスト除去装置。   The opening forming position is an angle turning position of a bent part of the duct positioned upstream of the baffle plate mounting position or a maximum curvature part of the bent part, or a position where gravity acts at the inflection point. The dust removing device according to claim 1, wherein 粉塵、飛灰、微粉炭等の粉粒物(以下ダストという)を含んだガスが通流するダクトよりダストを除去するダスト除去装置において、
前記少なくとも45°以下の傾き方向若しくは水平方向にほぼ直線状に流路が形成されている部位に、重力方向に向けて拡幅化されてなるバッファ部を設けると共に、バッファ部のガス流れ方向下流側位置(好ましくは終端側位置)に邪魔板を設置し、該邪魔板により前記ガスが重力方向に迂回してバッファ部終端より下流側に位置する流路に流れるように邪魔板の取付位置と高さ及び幅域を設定するとともに、前記迂回時にダストに作用する遠心力によりダストをバッファ底壁側に捕集し、該バッファ底壁側の前記ダストの堆積位置に開閉可能な開口部を設けたことを特徴とするダスト除去装置。
In a dust removal device that removes dust from a duct through which gas containing dust, fly ash, pulverized coal, etc. (hereinafter referred to as dust) flows,
A buffer portion that is widened in the direction of gravity is provided at a portion where the flow path is formed substantially linearly in the inclination direction or the horizontal direction of at least 45 ° or less, and downstream of the buffer portion in the gas flow direction A baffle plate is installed at a position (preferably the end side position), and the baffle plate is installed at a height higher than the baffle plate so that the baffle plate bypasses the gas in the direction of gravity and flows into the flow path located downstream from the buffer unit end. In addition to setting the height and width range, the dust is collected on the buffer bottom wall side by centrifugal force acting on the dust during the detour, and an opening that can be opened and closed is provided at the dust accumulation position on the buffer bottom wall side A dust removing device characterized by that.
前記邪魔板はバッファ部のガス流れ方向下流側に位置するバッファ部上壁よりガス流れ方向(投影方向)において下流側流路を塞ぐ如くその下方延在長さを設定したことを特徴とする請求項3記載のダスト除去装置。
The length of the baffle plate extending downward is set so as to block the downstream flow path in the gas flow direction (projection direction) from the upper wall of the buffer portion located downstream of the buffer portion in the gas flow direction. Item 4. A dust removing apparatus according to Item 3.
JP2008050032A 2008-02-29 2008-02-29 Dust removal apparatus Pending JP2009202142A (en)

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JP2011080386A (en) * 2009-10-05 2011-04-21 Ebara Refrigeration Equipment & Systems Co Ltd Canned motor pump system and heat transfer device
JP2013103214A (en) * 2011-11-16 2013-05-30 Mitsubishi Heavy Ind Ltd Exhaust gas treatment apparatus
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WO2021180356A1 (en) * 2020-03-11 2021-09-16 Walter Kramer Separator for separating a conveyed medium, preferably air, from a conveyed material, and method for separating conveyed material from a conveyed medium/conveyed material mixture
CN114590596A (en) * 2022-01-19 2022-06-07 上海隆麦机械设备工程有限公司 Power plant is with pneumatic conveyor who has preheating dust removal function

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Publication number Priority date Publication date Assignee Title
JP2011080386A (en) * 2009-10-05 2011-04-21 Ebara Refrigeration Equipment & Systems Co Ltd Canned motor pump system and heat transfer device
JP2013103214A (en) * 2011-11-16 2013-05-30 Mitsubishi Heavy Ind Ltd Exhaust gas treatment apparatus
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