JPS60216103A - Guide structure of combustion gas - Google Patents

Guide structure of combustion gas

Info

Publication number
JPS60216103A
JPS60216103A JP7225084A JP7225084A JPS60216103A JP S60216103 A JPS60216103 A JP S60216103A JP 7225084 A JP7225084 A JP 7225084A JP 7225084 A JP7225084 A JP 7225084A JP S60216103 A JPS60216103 A JP S60216103A
Authority
JP
Japan
Prior art keywords
combustion gas
gas guide
boiler
guide member
combustion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP7225084A
Other languages
Japanese (ja)
Inventor
和彦 山崎
曜明 松本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP7225084A priority Critical patent/JPS60216103A/en
Publication of JPS60216103A publication Critical patent/JPS60216103A/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明はボイラ等の燃焼室内部における燃焼ガス流の案
内構造に係り、特に水管式ボイラなどの高温燃焼領域に
おいて、燃焼ガスの偏流ならびに剥離を防止するための
効果的な燃焼ガス案内構造に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a structure for guiding a combustion gas flow inside a combustion chamber of a boiler or the like. The present invention relates to an effective combustion gas guide structure for preventing combustion.

〔発明の背景〕[Background of the invention]

まず、従来のボイラ等の燃焼室内部における燃焼ガスの
案内構造について図面を参照しながら説明する。第1図
は、従来の水管式ボイラなどにおける燃焼室内部の概略
構造および燃焼ガスの流動状態の一例を示す断面図であ
る。図から明らかなごとく、ボイラ水冷壁管1で囲まれ
るボイラの燃焼室内部に、入口管寄せ2および出口管寄
せ3を有する過熱器あるいは再゛熱器が、3種類の伝熱
管群4,5および6から構成されている場合には。
First, a structure for guiding combustion gas inside a combustion chamber of a conventional boiler or the like will be described with reference to the drawings. FIG. 1 is a sectional view showing an example of a schematic structure inside a combustion chamber and a flow state of combustion gas in a conventional water tube boiler or the like. As is clear from the figure, a superheater or reheater having an inlet header 2 and an outlet header 3 is installed inside the combustion chamber of the boiler surrounded by the boiler water-cooled wall tubes 1, and is connected to three types of heat exchanger tube groups 4, 5. and 6.

伝熱管群6に対する燃焼ガスの流れはほぼ一様に伝熱管
に対して垂直に流れるが、伝熱管群4および5.特に伝
熱管群5においては、燃焼ガス流が上昇流から下降流へ
と向きを変えた(第1図A部)直後に設置されているた
め、伝熱管群5におi)ては燃焼ガスの流れが大きく偏
流して、燃焼ガスがほとんど流れない部分、いわゆる燃
焼ガス流の剥離部分が生じる(第1図B部)。この剥離
部における伝熱管は伝熱に対して有効に寄与しないこと
になり、また燃焼ガスが著しく偏流した偏流部において
は、伝熱管に対して燃焼ガスが垂直に流れなくなり、伝
熱効率が低下することになる。さらに、燃焼ガス流に剥
離現象が生ずると流体力学的損失となって、燃焼ガス系
の圧力損失(ドラフトロス)の増大を招き、押込み送風
機のみによる加圧燃焼の場合には、送風機に過剰の負荷
を与える結果となる。
The flow of combustion gas to heat exchanger tube group 6 is substantially uniform and perpendicular to the heat exchanger tubes; In particular, heat exchanger tube group 5 is installed immediately after the combustion gas flow changes direction from upward flow to downward flow (section A in Figure 1), so in heat exchanger tube group 5 i), combustion gas The flow of the combustion gas is greatly biased, resulting in a section where almost no combustion gas flows, a so-called separation section of the combustion gas flow (section B in Fig. 1). The heat transfer tubes in this separated area do not effectively contribute to heat transfer, and in the uneven flow area where the combustion gas is significantly skewed, the combustion gas no longer flows perpendicularly to the heat transfer tube, reducing heat transfer efficiency. It turns out. Furthermore, when a separation phenomenon occurs in the combustion gas flow, it becomes a hydrodynamic loss, leading to an increase in pressure loss (draft loss) in the combustion gas system. This results in a load.

上述したボイラにおける燃焼ガスの偏流ならびに剥離現
象を防止するために、燃焼ガス案内板等の部材を設置す
ることが考えられるが、この燃焼ガス案内部材の設置場
所が、ボイラ燃焼室における約900℃〜700℃と高
温領域であるために、高温酸化が激しく、かつ燃焼ガス
中に含まれる硫黄酸化物(SOX)または窒素酸化物(
NOX)および燃焼灰中に含まれるバナジウムやナトリ
ウム等によって高温腐食される結果となり、燃焼ガス案
内部材の寿命は非常に短く、たかだか1年程度であった
In order to prevent the uneven flow and separation phenomenon of combustion gas in the boiler mentioned above, it is possible to install a member such as a combustion gas guide plate, but this combustion gas guide member is installed at a temperature of approximately 900°C in the boiler combustion chamber. Because the temperature is ~700°C, high-temperature oxidation is severe and sulfur oxides (SOX) or nitrogen oxides (
This resulted in high-temperature corrosion due to vanadium, sodium, etc. contained in the combustion ash, and the lifespan of the combustion gas guide member was extremely short, at most one year.

また、燃焼ガスの偏流ならびに剥離現象によって伝熱効
率が低下することから、伝熱管群の伝熱面積をその伝熱
効率の低下分だけ大きくした伝熱管群を使用しなければ
、所定の蒸気温度が得られないという欠点があった。
In addition, because the heat transfer efficiency decreases due to the uneven flow and separation phenomenon of combustion gas, it is necessary to use a heat transfer tube group whose heat transfer area is increased by the amount of the decrease in heat transfer efficiency, in order to obtain the specified steam temperature. The disadvantage was that it could not be done.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、上述した従来構造の欠点を解消し、ボ
イラ燃焼室の高温燃焼領域における燃焼ガス流の偏流な
らびに剥離現象を恒久的に防止して、伝熱管群の熱交換
効率の向上と、燃焼ガスのドラフトロス(通気抵抗)を
低減させるための新規で効果的な燃焼ガスの案内構造を
提供するにある。
The purpose of the present invention is to eliminate the above-mentioned drawbacks of the conventional structure, permanently prevent uneven flow and separation of combustion gas flow in the high-temperature combustion region of a boiler combustion chamber, and improve the heat exchange efficiency of a group of heat transfer tubes. The object of the present invention is to provide a new and effective combustion gas guiding structure for reducing draft loss (ventilation resistance) of combustion gas.

〔発明の概要〕[Summary of the invention]

要するに本発明は、ボイラ等の燃焼室における高温燃焼
領域において、燃焼ガスの偏流ならびに剥離を防止する
ために、低温部のボイラの伝熱管に、金属またはセラミ
ックス等の耐火材料からなる燃焼ガス案内部材を設け、
上記ボイラ伝熱管の冷却作用を利用して、該燃焼ガス案
内部材を冷却して、案内部材が高温で腐食性のある燃焼
ガスによって酸化あるいは腐食されるのを防止する。寿
命の長い恒久的なボイラ等における燃焼ガスの効果的な
案内構造である。
In short, the present invention provides a combustion gas guide member made of a refractory material such as metal or ceramics in a heat exchanger tube of a boiler in a low temperature section in order to prevent drift and separation of combustion gas in a high temperature combustion region of a combustion chamber of a boiler or the like. established,
The combustion gas guide member is cooled by utilizing the cooling effect of the boiler heat transfer tube to prevent the guide member from being oxidized or corroded by the high temperature and corrosive combustion gas. This is an effective guide structure for combustion gas in permanent boilers with a long life.

そして、ボイラの低温部の伝熱管に取付ける案内部材の
形状は、板状、アングル状あるいはチャンネル状でもよ
く、要は高温の燃焼ガス流が偏流あるいは剥離現象を生
じさせない形のガス案内構造であればよく、またその材
質としては適度の耐熱性、耐食性ならびに強度のある金
属あるいはセラミックス等の耐熱材料であってもよい。
The shape of the guide member attached to the heat exchanger tube in the low-temperature part of the boiler may be plate-shaped, angled or channel-shaped, and in short, the gas guide structure must be such that the high-temperature combustion gas flow does not cause drift or separation phenomenon. The material may be a heat-resistant material such as a metal or ceramic having appropriate heat resistance, corrosion resistance, and strength.

そして本発明による燃焼ガス案内構造は、燃焼ガス偏流
ならびに剥離を効果的に防止することができるから、燃
焼ガスが伝熱管群に対して垂直に流れる結果、伝熱管群
における熱交換効率が向上し、かつ燃焼ガスのドラフト
ロスを軽減させることができるから、伝熱管群の伝熱面
積ならびに送風ブロワの負荷を低減せしめる効果がある
Since the combustion gas guide structure according to the present invention can effectively prevent combustion gas drift and separation, the combustion gas flows perpendicularly to the heat exchanger tube group, and as a result, the heat exchange efficiency in the heat exchanger tube group is improved. , and the draft loss of the combustion gas can be reduced, which has the effect of reducing the heat transfer area of the heat transfer tube group and the load on the blower.

〔発明の実施例〕[Embodiments of the invention]

以下に本発明の一実施例を図面によって説明する。なお
図において、同一符号を付した部分は同一構成部品を示
す。第2図は9本発明によるボイラ燃焼室内部の概略構
造を示す断面図である。図に示すとおり、ボイラ水冷壁
管1で囲まれるボイラの燃焼室内部に、入口管寄せ2お
よび出口管寄せ3を有する過熱器あるいは再熱器が、3
種類の伝熱管群4,5および6によって構成されている
An embodiment of the present invention will be described below with reference to the drawings. Note that in the figures, parts with the same reference numerals indicate the same components. FIG. 2 is a sectional view schematically showing the internal structure of the boiler combustion chamber according to the present invention. As shown in the figure, a superheater or reheater having an inlet header 2 and an outlet header 3 is installed inside the combustion chamber of the boiler surrounded by boiler water-cooled wall tubes 1.
It is composed of heat exchanger tube groups 4, 5 and 6 of different types.

そして、燃焼ガス流が上昇流から下降流へと向きを変え
る部分(第2図C部)には、第3図に示すごとく、ボイ
ラ伝熱管にフィン構造の金属リレートを溶接し、その表
面をキャスタブル耐火物でコーティングした低温(約3
50℃〜500℃)の蒸気伝熱管を、燃焼ガス流に偏流
あるいは剥離を生ぜしめないように、燃焼ガスを案内す
る構造に配設されている。この燃焼ガス流が上昇流から
下降流へと向きを変える第2図における0部での燃焼ガ
ス温度は、約900℃〜700℃であるが、上記の低温
の蒸気伝熱管にフィン構造の金属プレートを溶接した燃
焼ガス案内構造の場合には、フィン構造の金属プレート
の温度は約500℃程度となり、高温酸化および高温腐
食はほとんど発生しない状態となり、高温領域における
燃焼ガス案内構造として寿命が長く、恒久的に使用する
4とができる。
As shown in Figure 3, in the part where the combustion gas flow changes direction from upward flow to downward flow (section C in Figure 2), a metal relate with a fin structure is welded to the boiler heat exchanger tube, and its surface is Low temperature coated with castable refractory (approximately 3
The steam heat transfer tubes (50° C. to 500° C.) are arranged in a structure to guide the combustion gas so as not to cause drift or separation in the combustion gas flow. The combustion gas temperature at part 0 in Figure 2, where the direction of the combustion gas flow changes from an upward flow to a downward flow, is approximately 900°C to 700°C. In the case of a combustion gas guide structure with welded plates, the temperature of the metal plate of the fin structure is approximately 500℃, which means that high-temperature oxidation and high-temperature corrosion hardly occur, resulting in a long life as a combustion gas guide structure in high-temperature areas. , 4 for permanent use.

しかし、上述の蒸気伝熱管に金属プレートを取付けた燃
焼ガス案内構造において2周囲の燃焼ガス温度が700
℃で、冷却用の蒸気の温度が500℃であるとすると、
伝熱管の金属プレートの温度は約700℃となる。この
場合9通常のオイル焚あるいは石炭焚のボイラにおいて
は、燃焼ガス中に腐食性の強いガス(SO,またはNo
X)および灰(バナジウムまたはナトリウム化合物)を
含んでいるため、金属プレートの温度が約700℃にお
いては。
However, in the combustion gas guide structure in which a metal plate is attached to the steam heat transfer tube described above, the temperature of the surrounding combustion gas is 700°C.
℃, and if the temperature of the cooling steam is 500℃,
The temperature of the metal plate of the heat exchanger tube is approximately 700°C. In this case 9 In a normal oil-fired or coal-fired boiler, highly corrosive gas (SO or NO) is contained in the combustion gas.
X) and ash (vanadium or sodium compounds) when the temperature of the metal plate is about 700°C.

腐食減肉割合が約2mm/10’h (金属プレートの
片面において)以上の激しい高温腐食を生じるため1例
えば内厚4WI+の金属プレートを案内板として使用し
ても約1年間で消耗してしまうことになる。
Severe high-temperature corrosion occurs with a corrosion thinning rate of approximately 2mm/10'h (on one side of the metal plate).1For example, even if a metal plate with an inner thickness of 4WI+ is used as a guide plate, it will wear out in about a year. It turns out.

これに対し2本発明の低温蒸気の伝熱管によって冷却さ
れる燃焼ガス案内構造の場合には、金属プレートの温度
は約500℃以下となり、高温腐食がほとんど発生しな
い領域となり恒久的なガス案内構造となる。
On the other hand, in the case of the combustion gas guide structure cooled by the low-temperature steam heat transfer tube of the present invention, the temperature of the metal plate is approximately 500°C or less, which is an area where high-temperature corrosion hardly occurs, and the gas guide structure is permanent. becomes.

次に本発明の他の実施例について説明する。第4図は、
ボイラの伝熱管に燃焼ガス案内板を、U字形ボルトおよ
びナツトで固着した場合の一例を示す。また、第5図は
ボイラの伝熱管にフィン状金属板を溶接して、ボイラ水
冷壁のごとくいわゆるメンブレン壁(Membrane
 Wall)構造にしたものであり、このタイプのもの
が最も冷却効率がよく、燃焼ガス温度がより高い部分に
有効である。
Next, other embodiments of the present invention will be described. Figure 4 shows
An example is shown in which a combustion gas guide plate is fixed to a heat exchanger tube of a boiler using U-shaped bolts and nuts. In addition, Figure 5 shows a so-called membrane wall (membrane wall), such as a boiler water cooling wall, by welding a fin-shaped metal plate to the heat exchanger tube of a boiler.
This type has the highest cooling efficiency and is effective in areas where the combustion gas temperature is higher.

〔発明の効果〕〔Effect of the invention〕

以上詳細に説明したごとく1本発明によるボイラ等の燃
焼ガス案内構造において、ボイラ伝熱管に取付けたガス
案内板である金属部材が、低温の蒸気によって冷却され
るため、燃焼ガスによる高温酸化および高温腐食が防止
でき、従来構造のものはその寿命が一年程度であるのに
比べ2本発明のガス案内構造は恒久的に使用可能である
As explained in detail above, in the combustion gas guide structure of a boiler or the like according to the present invention, the metal member, which is the gas guide plate attached to the boiler heat transfer tube, is cooled by low-temperature steam. Corrosion can be prevented, and the gas guide structure of the present invention can be used permanently, whereas the conventional structure has a lifespan of about one year.

また、ガス案内板としての金属部材の材質も。Also, the material of the metal member used as the gas guide plate.

従来用いられていた耐熱鋼あるいはステンレス鋼から低
合金鋼ないしは炭素鋼へとより低級鋼に変更することが
でき経済的である。
It is economical to be able to change from conventionally used heat-resistant steel or stainless steel to lower grade steel, such as low alloy steel or carbon steel.

さらに2本発明による燃焼ガス案内構造によると、燃焼
ガスの線流ならびに剥離現象が恒久的に防止でき、燃焼
ガス流がボイラ伝熱管群に対して垂直に流れるため伝熱
管群の熱交換効率が向上し。
Furthermore, according to the combustion gas guide structure according to the present invention, the linear flow and separation phenomenon of combustion gas can be permanently prevented, and the combustion gas flow flows perpendicularly to the boiler heat exchanger tube group, so that the heat exchange efficiency of the heat exchanger tube group is improved. Improve.

従来構造の燃焼ガス流の偏流ならびに剥離現象を生じて
いた部分の伝熱管群の伝熱面積よりも約lθ〜25%程
度伝熱面積も低減した伝熱管群でよく。
It is sufficient to use a heat transfer tube group whose heat transfer area is reduced by about lθ to 25% compared to the heat transfer area of the heat transfer tube group in the portion where the uneven flow and separation phenomenon of the combustion gas flow occurs in the conventional structure.

また伝熱管群における伝熱特性が、′設計値と実際の運
転時の特性とほぼ一致してくるため、計算上の蒸気温度
特性の信頼性が極めて高くなる。そして、さらに燃焼ガ
スの偏流ならびに剥離を防止することができるため通気
抵抗が減少し、送風機の負荷を低減せしめることができ
る。
Furthermore, since the heat transfer characteristics in the heat transfer tube group almost match the design values and the characteristics during actual operation, the reliability of the calculated steam temperature characteristics becomes extremely high. Furthermore, since drifting and separation of the combustion gas can be prevented, ventilation resistance is reduced, and the load on the blower can be reduced.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、従来のボイラ燃焼室内部の概略構造を示す断
面図、第2図は本発明によるボイラ燃焼室内部の概略構
造を示す断面図、第3図は本発明の一実施例である燃焼
ガス案内構造を示す断面図。 第4図および第5図は本発明の他の実施例である燃焼ガ
ス案内構造を示す断面図である。 1・・・ボイラ水冷壁管 2・・・入口管寄せ3・・・
出口管寄せ 4,5.6・・・伝熱管群7・・・案内板
付伝熱管 8・・・ボイラ伝熱管9・・・フィン 10
・・・キャスタブル耐火物11・・・U字型ボルト 1
2・・・ナツト13・・・案内板 14・・・メンブレ
ン壁構造代理人弁理士 中 村 純之助 才1 図 A IF5図 才3々1 才4図 士5図 只
FIG. 1 is a sectional view showing a schematic structure inside a conventional boiler combustion chamber, FIG. 2 is a sectional view showing a schematic structure inside a boiler combustion chamber according to the present invention, and FIG. 3 is an embodiment of the present invention. FIG. 3 is a sectional view showing a combustion gas guide structure. FIGS. 4 and 5 are cross-sectional views showing combustion gas guide structures according to other embodiments of the present invention. 1... Boiler water cooling wall tube 2... Inlet header 3...
Outlet pipe header 4,5.6... Heat exchanger tube group 7... Heat exchanger tube with guide plate 8... Boiler heat exchanger tube 9... Fin 10
... Castable refractory 11 ... U-shaped bolt 1
2...Natsuto 13...Guidance board 14...Membrane wall structure representative patent attorney Junnosuke Nakamura 1 figure A IF5 figure 3 and 1 figure 4 figure 5 figure only

Claims (1)

【特許請求の範囲】 1、複数の伝熱管群によって構成されるボイラの燃焼室
において、燃焼ガス流が方向変換をする高温燃焼領域に
、低温部のボイラ伝熱管に燃焼ガス案内部材を設けた冷
却式ガス案内部材を、上記高温燃焼領域に配設し、該冷
却式ガス案内部材によって、高温の燃焼ガスの偏流なら
びに剥離を防止することを特徴とする燃焼ガス案内構造
。 2、冷却式ガス案内部材が、伝熱管にフィンとして、プ
レート、アングルもしくはチャンネル状の金属を溶接し
て、高温燃焼ガスが接触する片面もしくは両面を、耐火
物で被覆することを特徴とする特許請求の範囲第1項記
載の燃焼ガス案内構造。 3、冷却式ガス案内部材が、プレート、アングルもしく
はチャンネル状の金属をボルトおよびナツトで固着する
ことを特徴とする特許請求の範囲第1項または第2項記
載の燃焼ガス案内構造。 4、冷却式ガス案内部材が、伝熱管にフィンとして、プ
レー1−、アングルもしくはチャンネル状の金属を溶接
して、メンブレン(Membrane)構造とすること
を特徴とする特許請求の範囲第1項または第2項記載の
燃焼ガス案内構造。
[Claims] 1. In a boiler combustion chamber composed of a plurality of heat exchanger tube groups, a combustion gas guide member is provided in a boiler heat exchanger tube in a low temperature section in a high temperature combustion region where the combustion gas flow changes direction. A combustion gas guide structure characterized in that a cooling type gas guide member is disposed in the high temperature combustion region, and the cooling type gas guide member prevents drifting and separation of high temperature combustion gas. 2. A patent in which the cooling type gas guide member is characterized in that a plate, angle or channel-shaped metal is welded to the heat exchanger tube as a fin, and one or both surfaces in contact with high temperature combustion gas are covered with a refractory material. A combustion gas guide structure according to claim 1. 3. The combustion gas guide structure according to claim 1 or 2, wherein the cooling type gas guide member is fixed to a plate, angle or channel-shaped metal with bolts and nuts. 4. The cooling type gas guide member is characterized in that it has a membrane structure by welding metal plates, angles or channels as fins to the heat transfer tube, or Combustion gas guide structure according to item 2.
JP7225084A 1984-04-11 1984-04-11 Guide structure of combustion gas Pending JPS60216103A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7225084A JPS60216103A (en) 1984-04-11 1984-04-11 Guide structure of combustion gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7225084A JPS60216103A (en) 1984-04-11 1984-04-11 Guide structure of combustion gas

Publications (1)

Publication Number Publication Date
JPS60216103A true JPS60216103A (en) 1985-10-29

Family

ID=13483859

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7225084A Pending JPS60216103A (en) 1984-04-11 1984-04-11 Guide structure of combustion gas

Country Status (1)

Country Link
JP (1) JPS60216103A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012117794A (en) * 2010-12-03 2012-06-21 Mitsubishi Heavy Ind Ltd Boiler

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012117794A (en) * 2010-12-03 2012-06-21 Mitsubishi Heavy Ind Ltd Boiler

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