JP4868924B2 - Chimney and waste heat recovery boiler - Google Patents

Chimney and waste heat recovery boiler Download PDF

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JP4868924B2
JP4868924B2 JP2006114874A JP2006114874A JP4868924B2 JP 4868924 B2 JP4868924 B2 JP 4868924B2 JP 2006114874 A JP2006114874 A JP 2006114874A JP 2006114874 A JP2006114874 A JP 2006114874A JP 4868924 B2 JP4868924 B2 JP 4868924B2
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chimney
heat recovery
recovery boiler
damper
support beam
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JP2007285631A (en
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貢 武蔵
宏昭 細井
充 中本
正憲 西村
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Mitsubishi Power Ltd
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Babcock Hitachi KK
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本発明はガスタービンと排熱回収ボイラ(HRSG)を組み合わせた複合発電プラントの排熱回収ボイラと、該排熱回収ボイラに使用する煙突に関する。    The present invention relates to an exhaust heat recovery boiler of a combined power plant combining a gas turbine and an exhaust heat recovery boiler (HRSG), and a chimney used for the exhaust heat recovery boiler.

ガスタービン排熱回収ボイラを組み合わせた複合発電プラントは他の火力発電プラントに比較して発電効率が高く、燃料として主に天然ガスを用いる場合が多く硫黄酸化物および煤塵の発生量が少ないため、排ガスの浄化処理の負担が少なく、将来性の高い発電プラントとして注目されている。   A combined power plant combined with a gas turbine exhaust heat recovery boiler has higher power generation efficiency than other thermal power plants, and natural gas is often used as fuel, and there is little generation of sulfur oxide and soot, It is attracting attention as a power plant with a high future with a low burden of exhaust gas purification treatment.

従来の複合発電プラントの機器構成の概略図を図10に示す。ガスタービン1からの排気ガスは排熱回収ボイラ2に導かれる。排熱回収ボイラ2では、節炭器3、蒸発管4などの伝熱管群により排ガスから熱回収し、蒸気を発生させる。その蒸気は過熱器5で過熱され、主蒸気管8を通って蒸気を工場等で利用したり、蒸気タービンへ供給して発電に利用する。   FIG. 10 shows a schematic diagram of the device configuration of a conventional combined power plant. Exhaust gas from the gas turbine 1 is guided to the exhaust heat recovery boiler 2. In the exhaust heat recovery boiler 2, heat is recovered from the exhaust gas by a heat transfer tube group such as the economizer 3 and the evaporator tube 4 to generate steam. The steam is superheated by the superheater 5, and the steam is used in a factory or the like through the main steam pipe 8 or supplied to a steam turbine for power generation.

また、排ガス中には窒素酸化物(以下NOxと略す)が含まれているため、排熱回収ボイラ2に脱硝装置6を組み込み、排ガス中にアンモニア(NH3)を注入し、脱硝装置6でNOxの除去を行う。これに対し、ガスタービン1の燃料として油類、例えばA重油を使用する場合、燃料中の硫黄分によりガスタービン1の排ガス中には硫黄酸化物(以下SOxと略す)が多く含まれている。この場合、NOx除去のために注入されるアンモニアとSOxとの化学反応により、ガス温度が220℃から150℃の領域(図10の節炭器3の領域に相当)で酸性硫安が生成し、伝熱管群に付着する。この酸性硫安は腐食性があり、伝熱管群を錆させる。また、酸性硫安は冷却されると粉末状になるが、排熱回収ボイラ2が停止して冷却されると、酸性硫安が排熱回収ボイラ2内で粉末状になる。このような状態で、ガスタービン1を起動させると、錆や酸性硫安がガスに搬送されて排熱回収ボイラ2の出口の煙突9(高さは約50〜80m)から飛散したり、錆や酸性硫安で周囲の機器を汚したり、腐食させたりするおそれがある。また、排ガス中に含まれる煤塵が伝熱管群に付着するので、排熱回収ボイラ2の再起動時に錆や酸性硫安と共に煙突9から大気中に飛散するおそれがある。 Further, since the exhaust gas contains nitrogen oxides (hereinafter abbreviated as NOx), a denitration device 6 is incorporated in the exhaust heat recovery boiler 2 and ammonia (NH 3 ) is injected into the exhaust gas. NOx removal is performed. On the other hand, when oils, for example, A heavy oil is used as fuel for the gas turbine 1, the exhaust gas of the gas turbine 1 contains a large amount of sulfur oxide (hereinafter abbreviated as SOx) due to the sulfur content in the fuel. . In this case, acidic ammonium sulfate is generated in a region where the gas temperature is 220 ° C. to 150 ° C. (corresponding to the region of the economizer 3 in FIG. 10) due to a chemical reaction between ammonia and SOx injected for NOx removal. It adheres to the heat transfer tube group. This acidic ammonium sulfate is corrosive and rusts the heat transfer tube group. Further, the acidic ammonium sulfate becomes powdery when cooled, but when the exhaust heat recovery boiler 2 is stopped and cooled, the acidic ammonium sulfate becomes powdery in the exhaust heat recovery boiler 2. When the gas turbine 1 is started in such a state, rust and acidic ammonium sulfate are conveyed to the gas and scattered from the chimney 9 (height is about 50 to 80 m) at the outlet of the exhaust heat recovery boiler 2, or rust and There is a risk of soiling or corroding surrounding equipment with acid ammonium sulfate. Moreover, since the dust contained in the exhaust gas adheres to the heat transfer tube group, when the exhaust heat recovery boiler 2 is restarted, it may be scattered from the chimney 9 together with rust and acidic ammonium sulfate into the atmosphere.

特許文献1記載の発明では、図10(a)に示すように粉末状の酸性硫安、錆及び煤塵がガスタービン1の再起動によりに排熱回収ボイラ2出口の煙突9から飛散することを防止するために煙突9内に網状のダンパー11とそのガス上流側(図1では煙突9下部)に板状のダンパー10を設置する。図10(b)には板状のダンパー10を示し、図10(c)には網状のダンパー11の斜視図を示す。   In the invention described in Patent Document 1, powdered acidic ammonium sulfate, rust and dust are prevented from scattering from the chimney 9 at the outlet of the exhaust heat recovery boiler 2 due to restart of the gas turbine 1 as shown in FIG. For this purpose, a net-like damper 11 and a plate-like damper 10 are installed in the chimney 9 on the gas upstream side (lower part of the chimney 9 in FIG. 1). FIG. 10B shows a plate-like damper 10, and FIG. 10C shows a perspective view of the net-like damper 11.

図10(a)に示す排熱回収ボイラ2では規定時間の間、複合発電プラントを運転した後に停止させ、同時にガスタービン1も停止させた状態で板状のダンパー10で煙突9を閉止状態にして、作業員が煙突9内部に入り、当該ダンパー10を足場代わりに利用して、網状ダンパー11に付着した酸性硫安、錆及び煤塵を除去する。
特開2005−241075号公報
In the exhaust heat recovery boiler 2 shown in FIG. 10A, the chimney 9 is closed with the plate-like damper 10 in a state where the combined power plant is operated for a specified time and then stopped, and at the same time the gas turbine 1 is also stopped. Then, the worker enters the chimney 9 and uses the damper 10 as a scaffold to remove acid ammonium sulfate, rust, and dust attached to the mesh damper 11.
JP 2005-241075 A

上記特許文献1記載の発明は、網状ダンパー11の構造が多少複雑になり、構造上金網の隙間に付着した煤塵等の除去に手間がかかる欠点がある。
そこで、本発明の課題は、比較的簡単な構造を備え、扱いが容易な煤塵等の除去手段を設置した煙突と該煙突を用いる排熱回収ボイラを提供することである。
The invention described in Patent Document 1 has a drawback that the structure of the mesh damper 11 is somewhat complicated, and it takes time to remove dust and the like adhering to the gaps of the metal mesh.
SUMMARY OF THE INVENTION An object of the present invention is to provide a chimney having a relatively simple structure and easy-to-handle removal means such as dust, and an exhaust heat recovery boiler using the chimney.

本発明の課題は次の解決手段で解決される。
すなわち、請求項1記載の発明は、内部にダンパーを有する排ガス用の鉛直方向に向いた煙突において、ダンパーの上部に複数の金網枠を着脱可能にサポート梁に載置した煤塵捕獲装置を設置した煙突である。
The problems of the present invention are solved by the following means.
That is, the invention according to claim 1 is provided with a dust trapping device in which a plurality of wire mesh frames are detachably mounted on a support beam in an upper part of a damper in a vertically-directed chimney for exhaust gas having a damper inside. It is a chimney.

請求項2記載の発明は、金網方式の煤塵捕獲装置は、煙突の水平断面方向に互いに並列配置され、鉛直方向に平面を有する垂直梁部分と該垂直梁部分の下端部に水平方向に平面を有する水平梁部分からなる断面T字型であるサポート梁と、サポート梁の水平梁部分に載置される着脱自在な金網枠を備えた請求項1の煙突である。   According to a second aspect of the present invention, there is provided a wire netting type dust trapping device, wherein a vertical beam portion having a plane in the vertical direction and a horizontal plane at the lower end of the vertical beam portion are arranged in parallel in the horizontal cross-sectional direction of the chimney. The chimney according to claim 1, comprising a support beam having a T-shaped cross section comprising a horizontal beam portion and a detachable wire mesh frame placed on the horizontal beam portion of the support beam.

請求項3記載の発明は、金網方式の煤塵捕獲装置をダンパーより0.5mから2.5m上方に設けた請求項1又は2記載の煙突である。
請求項4記載の発明は、ガスタービンからの燃焼排ガスを流すダクト内に多数の伝熱管群と脱硝装置を配置した排熱回収ボイラにおいて、伝熱管群で熱交換した後のガスタービン燃焼排ガスを大気中に排出する煙突として、請求項1から3のいずれかに記載の煙突を使用する排熱回収ボイラである。
A third aspect of the present invention is the chimney according to the first or second aspect, wherein the wire netting type dust trapping device is provided 0.5 m to 2.5 m above the damper.
According to a fourth aspect of the present invention, in the exhaust heat recovery boiler in which a large number of heat transfer tube groups and a denitration device are arranged in a duct through which the combustion exhaust gas from the gas turbine flows, the gas turbine combustion exhaust gas after heat exchange in the heat transfer tube group is It is a waste heat recovery boiler which uses the chimney in any one of Claim 1 to 3 as a chimney discharged | emitted in air | atmosphere.

請求項1記載の発明により、煤塵などの大気飛散が懸念される煙突においても、金網方式の煤塵捕獲装置が着脱が容易な複数の金網枠をサポート梁に載置した構成であるので、金網枠に付着した煤煙などを金網枠をサポート梁から取り外すことで容易に大気への飛散を防止することができる。
請求項2記載の発明により、請求項1記載の発明の効果に加えて、サポート梁の水平梁部分に金網枠を着脱自在に載置しているだけであるので、必要なときにだけ金網枠をサポート梁に載置できる。
According to the first aspect of the present invention, even in a chimney in which air dust such as dust is concerned, the wire mesh type dust trapping device has a structure in which a plurality of wire mesh frames that can be easily attached and detached are placed on the support beam. It is possible to easily prevent the soot and the like adhering to the air from being scattered into the atmosphere by removing the wire mesh frame from the support beam.
According to the second aspect of the present invention, in addition to the effect of the first aspect of the invention, the metal mesh frame is merely detachably mounted on the horizontal beam portion of the support beam. Can be placed on the support beam.

請求項3記載の発明により、請求項1又は2記載の発明の効果に加えて、ダンパー上に作業者が乗って金網枠の着脱作業が容易に行える。
請求項4記載の発明により、排熱回収ボイラの運転再開時に煤煙などが大気中に飛散することを防止できる。
According to the invention described in claim 3, in addition to the effect of the invention described in claim 1 or 2, an operator can easily attach and detach the wire mesh frame on the damper.
According to the fourth aspect of the present invention, it is possible to prevent smoke and the like from being scattered in the atmosphere when the operation of the exhaust heat recovery boiler is resumed.

本発明の実施例を図面と共に説明する。
図1には、本実施例の排熱回収ボイラ出口の煙突の全体構造を示す。
排熱回収ボイラ2の出口の煙突9の下部に排熱回収ボイラ出口排ガスGを受け入れ、上方の煙突9の出口より排ガスGは大気の放出される。途中に排熱回収ボイラ2の停止時の保温と煙突9上部からの雨切りのためにダンパー10が設置されている。ダンパー10の上部に金網式煤塵捕獲装置12が設けられている。この煤塵捕獲装置12は常時設置していると長期間運転時の汚れ等で排ガスの流動抵抗が増え、排熱回収ボイラ2の運転効率の低下につながるので常時設置部分は必要最小限にとどめる。
Embodiments of the present invention will be described with reference to the drawings.
FIG. 1 shows the overall structure of the chimney at the outlet of the exhaust heat recovery boiler of this embodiment.
The exhaust heat recovery boiler outlet exhaust gas G is received in the lower part of the chimney 9 at the outlet of the exhaust heat recovery boiler 2, and the exhaust gas G is released into the atmosphere from the outlet of the upper chimney 9. A damper 10 is installed on the way for heat retention when the exhaust heat recovery boiler 2 is stopped and for draining rain from the top of the chimney 9. A wire net type dust trap 12 is provided on the upper portion of the damper 10. If this dust trap device 12 is always installed, the flow resistance of the exhaust gas increases due to dirt during long-term operation and leads to a decrease in the operating efficiency of the exhaust heat recovery boiler 2, so the always installed portion is kept to the minimum necessary.

したがって、上記煤塵捕獲装置12は煙突9から着脱容易な構造にしておくと便利である。通常煤塵などの飛散が問題になるのは長期の排熱回収ボイラの運転中にボイラ内部の壁面などに付着した酸性硫安や硫安および灰からなる煤塵が定期検査後の運転再開時にまとまって壁面などから剥がれて大気中に飛散する場合であり、それを防ぐために排熱回収ボイラ2の運転再開時に機能を発揮すればよい。   Therefore, it is convenient to make the dust trapping device 12 easy to attach to and detach from the chimney 9. Scattering of dust usually becomes a problem when long-term exhaust heat recovery boilers are in operation, such as acid ammonium sulfate, ammonium sulfate, and ash dust that adheres to the internal wall of the boiler, etc. In order to prevent this, the function may be exhibited when the operation of the exhaust heat recovery boiler 2 is resumed.

図2には煙突9内に配置された金網式煤塵捕獲装置12の全体の平面図を示し、図3に一部側面図を示す。また、図4には煙突9内に予め取り付けられる金網式煤塵捕獲装置12のサポート梁14と梁支持部材21の配置図を示し、図5には図4のA−A線断面図、図6は図4のB−B線又はC−C線断面図を示す。また、図7は図4に示す金網式煤塵捕獲装置12のサポート梁14上に配置する金網枠12dの側面図を示し、図8には該金網枠の各種枠体の平面図(図8(a)〜(d))を示す。   2 shows a plan view of the entire wire net type dust trap 12 arranged in the chimney 9, and FIG. 3 shows a partial side view thereof. 4 shows a layout of the support beam 14 and the beam support member 21 of the wire net type dust trap 12 that is mounted in advance in the chimney 9. FIG. 5 is a cross-sectional view taken along line AA in FIG. Shows a sectional view taken along line BB or CC in FIG. 7 shows a side view of a wire mesh frame 12d arranged on the support beam 14 of the wire mesh dust trapping device 12 shown in FIG. 4, and FIG. 8 is a plan view of various frames of the wire mesh frame (FIG. 8 ( a) to (d)).

図4のA−A線断面図である図5に示す煤塵捕獲装置12のサポート梁14は煙突9の水平面に複数本(本実施例では9本)が互いに平行位置に配置される。
図2に示すように煙突9は耐火材15と該耐火材15の内側に鋼材16を張り付けた構成からなり、また、図3に示すようにサポート梁14は、鉛直方向に平面を備えた垂直部分14aと該垂直部分14aの下端に溶接接続された水平部分14bからなる断面がT字型をしている。また、煙突9の内壁の鋼材16の円周方向に溶接接続され水平面を備えたリング状の水平片19に、例えば溶接によりシール板20を接続し、該シール板20の上にサポート梁14の水平部分14bを載置する。
A plurality of support beams 14 of the dust trapping device 12 shown in FIG. 5, which is a cross-sectional view taken along the line AA of FIG. 4, are arranged in parallel with each other on the horizontal surface of the chimney 9.
As shown in FIG. 2, the chimney 9 is composed of a refractory material 15 and a steel material 16 attached to the inside of the refractory material 15, and as shown in FIG. 3, the support beam 14 is a vertical having a plane in the vertical direction. A cross section composed of a portion 14a and a horizontal portion 14b welded to the lower end of the vertical portion 14a is T-shaped. Further, a seal plate 20 is connected to a ring-shaped horizontal piece 19 welded and connected in the circumferential direction of the steel material 16 on the inner wall of the chimney 9, for example, by welding, and the support beam 14 is placed on the seal plate 20. The horizontal portion 14b is placed.

図4の矢印Dに示す円内の拡大図を図9に示す。煙突9は耐火材15と該耐火材15の内側に鋼材16を張り付けた構成からなり、前記鋼材16に設けた一対の鋼材製の差し込み片18、18にT字型サポート梁14の垂直部分14aの端部を差し込みボルト結合して着脱可能にしている。   FIG. 9 shows an enlarged view in a circle indicated by an arrow D in FIG. The chimney 9 has a structure in which a steel material 16 is attached to the inside of the refractory material 15 and the refractory material 15, and a pair of steel insertion pieces 18, 18 provided on the steel material 16 and a vertical portion 14 a of a T-shaped support beam 14. The end of this is inserted and bolted to make it detachable.

また、図6の図4のB−B線又はC−C線断面図に示すようにT字型サポート梁14の水平部分14bの下面にはT字型サポート梁14の長手方向に直交する方向に設けた4本のサポート梁支持部材21をボルト接続している。図4に示すように該4本の梁支持部材21の内2本は互いに同一直線上に配置している。
サポート梁支持部材21で一部支持されたT字型サポート梁14の上に載置する煤塵捕獲装置12は、その側面図を図7に示すように3重の金網12a〜cとそれをボルトで挟み込んで固定する枠体12dと止め部材12eから成る。
Further, as shown in the sectional view taken along the line BB or CC in FIG. 4 in FIG. 6, the bottom surface of the horizontal portion 14 b of the T-shaped support beam 14 is orthogonal to the longitudinal direction of the T-shaped support beam 14. The four support beam support members 21 provided in are connected by bolts. As shown in FIG. 4, two of the four beam support members 21 are arranged on the same straight line.
The dust trapping device 12 placed on the T-shaped support beam 14 partially supported by the support beam support member 21 has a triple wire mesh 12a to 12c and bolts as shown in FIG. It consists of a frame body 12d and a fixing member 12e that are sandwiched and fixed.

また、煤塵捕獲装置12の枠体12dは、1個の質量を手持ちできるような大きさに分割し、煙突9の中心部に載置される一番大きなサイズの枠体を有するもの12d1(図8(a))から一番小さいサイズの枠体を有するもの12d4(図8(d))まで4種類のサイズの枠体12d1〜12dからなる。これらの煤塵捕獲装置12をそれぞれ図4に示すサポート梁支持部材21で一部支持されたT字型サポート梁14の上に載置する。しかし煙突9の内部周辺部には矩形の平面形状を有する煤塵捕獲装置12が載置出来ない変形の空間が出来るが、その部分にはシール板20を載置する。なお煙突9の煤塵捕獲装置12を載置する部分には煙突9の内壁を構成する鋼材16に設けた水平片19を溶接接続しているので、この水平片19とサポート梁14の水平部分14bの上に前記シール板20を溶接接続することができる。煤塵捕獲装置12の載置後は、煤塵捕獲装置12をサポート梁14の水平部分14bにボルト止めする。 Further, the frame body 12d of the dust trapping device 12 is divided into a size that can hold a single mass and has a frame body of the largest size placed on the center of the chimney 9 12d 1 ( consists to FIG. 8 (a)) that has the frame of the smallest size from 12d 4 (to FIG. 8 (d)) to four of the frame 12d 1 to 12d 4 size. Each of these dust traps 12 is placed on a T-shaped support beam 14 partially supported by a support beam support member 21 shown in FIG. However, there is a deformation space in which the dust trapping device 12 having a rectangular planar shape cannot be placed in the inner peripheral portion of the chimney 9, but the seal plate 20 is placed in that portion. In addition, since the horizontal piece 19 provided in the steel material 16 which comprises the inner wall of the chimney 9 is weld-connected to the part in which the dust trap 12 of the chimney 9 is mounted, this horizontal piece 19 and the horizontal part 14b of the support beam 14 are connected. The seal plate 20 can be welded to the top. After the dust trapping device 12 is placed, the dust trapping device 12 is bolted to the horizontal portion 14 b of the support beam 14.

通常は煤塵捕獲金網12は煙突9から外しておき、サポート梁14とサポート梁支持部材21は常設とする。定期検査後の排熱回収ボイラ2の再起動運転時にはダンパー10を全閉固定し、その上部を作業用の足場として利用する。煤塵捕獲金網12を上部から吊り降ろすか、または煙突9のダンパー10上方に設けられたマンホール(図示せず)から搬入し、サポート梁14にボルトにて固定する。   Normally, the dust trapping wire mesh 12 is removed from the chimney 9, and the support beam 14 and the support beam support member 21 are permanently installed. During the restart operation of the exhaust heat recovery boiler 2 after the periodic inspection, the damper 10 is fully closed and fixed, and the upper part thereof is used as a working scaffold. The dust trapping wire mesh 12 is suspended from the upper part or is carried from a manhole (not shown) provided above the damper 10 of the chimney 9 and fixed to the support beam 14 with bolts.

煤塵などの飛散は排熱回収ボイラ2の再起動時の初期の集中飛散するので排ガス源を適宜起動停止しながら付着状況を監視する。煤塵などの付着が増大し、流動抵抗が増した場合はダンパー10の上面にシートを張り、煤塵捕獲金網12を上方からエアーブロー又はダンパー10の上面から清掃を行う。これを何回か繰り返すと煤塵などの飛散はほとんどなくなり煤塵捕獲装置12なしでも排熱回収ボイラ2を運転できる。
その際には煤塵捕獲金網12を再度外して通常運転時の流動抵抗増大を回避すればよい。
Since dust such as dust is scattered at the initial concentration when the exhaust heat recovery boiler 2 is restarted, the state of adhesion is monitored while the exhaust gas source is properly started and stopped. When adhesion of dust or the like increases and flow resistance increases, a sheet is stretched on the upper surface of the damper 10, and the dust trapping wire mesh 12 is cleaned from above by air blow or from the upper surface of the damper 10. If this is repeated several times, the scattering of soot and the like hardly occurs and the exhaust heat recovery boiler 2 can be operated without the soot trap 12.
In that case, the dust trapping wire mesh 12 may be removed again to avoid an increase in flow resistance during normal operation.

上記煤塵捕獲金網12の着脱作業、清掃作業のためにはダンパー10と煤塵捕獲金網12との隙間はダンパー10へのアプローチを考慮して作業床等が設けられているので、それを利用できることから作業性を考慮して、0.5〜2.5m前後が最適である。   Since the clearance between the damper 10 and the dust trapping wire mesh 12 is provided with a work floor in consideration of the approach to the damper 10 for attaching / detaching and cleaning the dust trapping wire mesh 12, it can be used. In consideration of workability, about 0.5 to 2.5 m is optimal.

本発明は、燃焼物に起因する硫黄分が含まれている燃焼装置排ガスを利用する装置の煙突部分に適用でき、当該装置としては排熱回収ボイラや、煤塵などが生成し易い燃焼装置などである。   The present invention can be applied to a chimney portion of an apparatus that uses exhaust gas from a combustion apparatus that contains a sulfur content resulting from combustion products. Examples of the apparatus include an exhaust heat recovery boiler and a combustion apparatus that easily generates soot and the like. is there.

本実施例の排熱回収ボイラ出口の煙突の全体構造を示す。The whole structure of the chimney of the exhaust heat recovery boiler exit of a present Example is shown. 図1の煙突内に配置された金網式煤塵捕獲装置の全体の平面図を示す。The top view of the whole wire-mesh type | mold dust capture device arrange | positioned in the chimney of FIG. 1 is shown. 図2の金網式煤塵捕獲装置の一部側面図を示す。The partial side view of the wire-mesh type dust trapping device of FIG. 2 is shown. 図2の金網式煤塵捕獲装置のサポート梁の配置図を示す。FIG. 3 is a layout view of support beams of the wire net type dust trap of FIG. 2. 図4のA−A線断面図を示す。FIG. 5 is a cross-sectional view taken along line AA in FIG. 4. 図4のB−B線又はC−C線断面図を示す。The BB line or CC line sectional drawing of FIG. 4 is shown. 図4に示す金網式煤塵捕獲装置のサポート梁上に配置する金網枠の側面図を示す。The side view of the wire-mesh frame arrange | positioned on the support beam of the wire-mesh type dust trap shown in FIG. 4 is shown. 図7に示す金網枠の各種枠体の平面図(図8(a)〜(d))を示す。The top view (FIG. 8 (a)-(d)) of the various frame bodies of the wire-mesh frame shown in FIG. 7 is shown. 図4の矢印Dに示す円内の拡大図である。FIG. 5 is an enlarged view in a circle indicated by an arrow D in FIG. 4. 従来の複合発電プラントの機器構成の概略図を示す。The schematic of the apparatus structure of the conventional combined power plant is shown.

符号の説明Explanation of symbols

1 ガスタービン 2 排熱回収ボイラ
3 節炭器 4 蒸発管
5 過熱器 8 主蒸気管
9 煙突 10 ダンパー
11 網状ダンパー 12 金網式煤塵捕獲装置
12a〜c 金網 12d 枠体
12e 止め部材 14 サポート梁
14a サポート梁垂直部分 14b サポート梁水平部分
15 耐火材 16 鋼材
18 差し込み片 19 水平片
20 シール板 21 サポート梁支持部材
DESCRIPTION OF SYMBOLS 1 Gas turbine 2 Exhaust heat recovery boiler 3 Cargo saver 4 Evaporating pipe 5 Superheater 8 Main steam pipe 9 Chimney 10 Damper 11 Net-like damper 12 Wire mesh type dust trap 12a-c Wire net 12d Frame 12e Stopping member 14 Support beam 14a Support Beam vertical portion 14b Support beam horizontal portion 15 Refractory material 16 Steel material 18 Insert piece 19 Horizontal piece 20 Seal plate 21 Support beam support member

Claims (4)

内部にダンパーを有する排ガス用の鉛直方向に向いた煙突において、
ダンパーの上部に複数の金網枠を着脱可能にサポート梁に載置した煤塵捕獲装置を設置したことを特徴とする煙突。
In the vertical chimney for exhaust gas with a damper inside,
A chimney characterized in that a dust trap is installed on the support beam so that a plurality of wire mesh frames are detachably mounted on the upper part of the damper.
金網方式の煤塵捕獲装置は、煙突の水平断面方向に互いに並列配置され、鉛直方向に平面を有する垂直梁部分と該垂直梁部分の下端部に水平方向に平面を有する水平梁部分からなる断面T字型であるサポート梁と、サポート梁の水平梁部分に載置される着脱自在な金網枠を備えたことを特徴とする請求項1の煙突。   The wire netting type dust trapping device includes a vertical beam portion having a plane in the vertical direction and a horizontal beam portion having a plane in the horizontal direction at the lower end of the vertical beam portion. The chimney according to claim 1, further comprising a support beam having a letter shape and a detachable wire mesh frame placed on a horizontal beam portion of the support beam. 金網方式の煤塵捕獲装置をダンパーより0.5mから2.5m上方に設けたことを特徴とする請求項1又は2記載の煙突。   The chimney according to claim 1 or 2, wherein a metal net type dust trap device is provided 0.5m to 2.5m above the damper. ガスタービンからの燃焼排ガスを流すダクト内に多数の伝熱管群と脱硝装置を配置した排熱回収ボイラにおいて、
伝熱管群で熱交換した後のガスタービン燃焼排ガスを大気中に排出する煙突として、請求項1から3のいずれかに記載の煙突を使用することを特徴とする排熱回収ボイラ。
In an exhaust heat recovery boiler in which a large number of heat transfer tube groups and a denitration device are arranged in a duct through which combustion exhaust gas from a gas turbine flows,
An exhaust heat recovery boiler using the chimney according to any one of claims 1 to 3 as a chimney for discharging the gas turbine combustion exhaust gas after heat exchange with the heat transfer tube group to the atmosphere.
JP2006114874A 2006-04-18 2006-04-18 Chimney and waste heat recovery boiler Expired - Fee Related JP4868924B2 (en)

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Publication number Priority date Publication date Assignee Title
JP2018132279A (en) * 2017-02-17 2018-08-23 三菱日立パワーシステムズ株式会社 Waste heat recovery boiler and scattering matter recovery method therefor

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CN108426261A (en) * 2018-03-05 2018-08-21 湖南湘讯企业管理有限公司 A kind of bolts of inclined column type ash-cleaning energy saving residual heat from boiler fume recovery channel

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018132279A (en) * 2017-02-17 2018-08-23 三菱日立パワーシステムズ株式会社 Waste heat recovery boiler and scattering matter recovery method therefor

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