JPH0449441Y2 - - Google Patents

Info

Publication number
JPH0449441Y2
JPH0449441Y2 JP1984162054U JP16205484U JPH0449441Y2 JP H0449441 Y2 JPH0449441 Y2 JP H0449441Y2 JP 1984162054 U JP1984162054 U JP 1984162054U JP 16205484 U JP16205484 U JP 16205484U JP H0449441 Y2 JPH0449441 Y2 JP H0449441Y2
Authority
JP
Japan
Prior art keywords
heat transfer
fins
circumferential
fluidized
tube
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.)
Expired
Application number
JP1984162054U
Other languages
Japanese (ja)
Other versions
JPS6179701U (en
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 filed Critical
Priority to JP1984162054U priority Critical patent/JPH0449441Y2/ja
Priority to CN 85107812 priority patent/CN85107812A/en
Publication of JPS6179701U publication Critical patent/JPS6179701U/ja
Application granted granted Critical
Publication of JPH0449441Y2 publication Critical patent/JPH0449441Y2/ja
Expired legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Details Of Fluid Heaters (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、流動燃焼層内に伝熱器管が配置され
た流動床ボイラに関する。
[Detailed Description of the Invention] [Industrial Field of Application] The present invention relates to a fluidized bed boiler in which heat transfer tubes are arranged within a fluidized combustion bed.

〔従来の技術〕[Conventional technology]

流動床ボイラは、第4図に示されているように
流動燃焼層11内に、蒸発管、過熱器管、或いは
再熱器管等の伝熱器管12が設置されたものであ
り、流動材として一般に石灰石(CaCO3)を使
用しており、層内脱硫効果を有するので、近年、
石炭焚きボイラとして利用されるケースが増えて
きた。
As shown in FIG. 4, a fluidized bed boiler has heat transfer tubes 12 such as evaporator tubes, superheater tubes, or reheater tubes installed in a fluidized combustion bed 11. Limestone (CaCO 3 ) is generally used as a material and has an intralayer desulfurization effect, so in recent years,
More and more cases are being used as coal-fired boilers.

〔従来技術の問題点〕[Problems with conventional technology]

ところが、流動燃焼層11内は燃料である石炭
と流動材である石灰石の粒子が混合し、炉底から
供給される空気により流動しているため、流動燃
焼層11内に設置された伝熱器管12が浮上して
くる流動粒子により第5図に示すように、管の下
側にエロージヨンを起こし、管の寿命が著しく短
縮される問題が発生している。
However, inside the fluidized combustion bed 11, coal as a fuel and limestone particles as a fluidized material are mixed and are fluidized by the air supplied from the bottom of the furnace. As shown in FIG. 5, the floating particles of the tube 12 cause erosion on the lower side of the tube, resulting in a problem that the life of the tube is significantly shortened.

〔考案の目的〕[Purpose of invention]

そこで本考案は、伝熱器管の伝熱効果の低下を
防止しつつ伝熱器管の摩耗を防止することができ
る流動床ボイラを提供することを目的とするもの
である。
SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a fluidized bed boiler that can prevent the heat transfer tubes from being worn out while preventing the heat transfer effect of the heat transfer tubes from decreasing.

〔問題を解決するための手段〕[Means to solve the problem]

上記目的を達成するため、本考案は、流動燃焼
層内に伝熱器管が配置された流動床ボイラにおい
て、前記伝熱器管の全外周表面に9%以上のCr
を含有する高Cr鋼からなる外周が円形の円周フ
インを適宜間隔で複数条に溶着し、前記円周フイ
ンの下側外周のみに前記円周フインの外周に適合
し断面が半円形の曲面形状板からなる耐摩耗性の
プロテクタを設けたことを特徴とする流動床ボイ
ラを提供する。
In order to achieve the above object, the present invention provides a fluidized bed boiler in which a heat exchanger tube is disposed within a fluidized combustion bed, in which 9% or more of Cr is added to the entire outer peripheral surface of the heat exchanger tube.
A plurality of circumferential fins with a circular outer periphery made of high Cr steel containing Cr are welded at appropriate intervals, and only the lower outer periphery of the circumferential fin has a curved surface that conforms to the outer periphery of the circumferential fin and has a semicircular cross section. A fluidized bed boiler is provided, characterized in that it is equipped with a wear-resistant protector made of a shaped plate.

〔作用〕[Effect]

本考案は、伝熱管の外周全部を複数条の円周フ
インで覆い、かつ円周フインの下側外周のみを覆
う断面が半円形のプロテクターを装着することに
より、プロテクターを設けたことによる有効伝熱
面積の減少を防ぎ、伝熱効率の低下を防止でき
る。また、同フインを9%以上のCrを含有した
高Cr鋼とすることで、摂氏約500度以上のメタル
温度分布において、同フインの表面に硬質の酸化
物保護膜を形成させ、これによつて同フインの摩
耗を一層効果的に防止することができる。
The present invention covers the entire outer periphery of the heat transfer tube with multiple circumferential fins and attaches a protector with a semicircular cross section that covers only the lower outer periphery of the circumferential fins. It is possible to prevent a decrease in heat area and a decrease in heat transfer efficiency. In addition, by making the fins of high Cr steel containing 9% or more of Cr, a hard oxide protective film is formed on the surface of the fins in a metal temperature distribution of approximately 500 degrees Celsius or higher. Therefore, wear of the fins can be more effectively prevented.

〔実施例〕〔Example〕

本考案を、第1図ないし第3図に示された実施
例に基づいて説明する。
The present invention will be explained based on the embodiment shown in FIGS. 1 to 3.

第1図ないし第3図において、流動燃焼層1内
に、フイン3が全外周表面に複数条に溶着された
蒸発管、過熱器管、或いは再熱器管等の伝熱器管
2が配置されている。フイン3の下側外周には、
9%以上のCrを含有した高Cr鋼からなるプロテ
クタ4が配置され、プロテクタ4は9%以上の
Crを含有した高Cr鋼からなるバンド5で保持さ
れている。
In FIGS. 1 to 3, a heat transfer tube 2 such as an evaporator tube, a superheater tube, or a reheater tube, in which a plurality of fins 3 are welded to the entire outer peripheral surface, is arranged in a fluidized combustion bed 1. has been done. On the lower outer periphery of the fin 3,
A protector 4 made of high Cr steel containing 9% or more of Cr is arranged;
It is held by a band 5 made of high Cr steel containing Cr.

なお、プロテクタ4は装着の容易さからみると
高Cr鋼が望ましいが、セラミツクを使用しても
よい。
The protector 4 is preferably made of high Cr steel from the viewpoint of ease of installation, but ceramic may also be used.

炉底から浮上してくる空気泡は、流動燃焼層1
内の伝熱器管2の下側のプロテクタ4に衝突して
小さな空気泡に分解する。このとき、流動材の挙
動が活発化するために、プロテクタ4がないと、
伝熱器管2の下表面は摩耗するが、プロテクタ4
により伝熱器管2が保護されているので、伝熱器
管2の摩耗を防止している。しかし、プロテクタ
4の設置は伝熱器管2の有効伝熱面積を減少させ
ているため、伝熱効率の低下を来す。伝熱効率の
低下は、伝熱器管2の全外周表面にフイン3を溶
着して、有効伝熱面積の実質的な低下を防ぐこと
で防止している。フイン3を9%以上のCr鋼を
含有する高Cr鋼で形成し、フイン3の先端部を
含む大部分のメタル温度分布が摂氏約500度以上
となるように、伝熱器管2の肉厚、フイン3の厚
さ、フイン3の高さを設計することにより、フイ
ン3の表面に硬質で安定した酸化物保護膜を形成
させることができ、これにより、プロテクタ4が
設けられていない伝熱器管2の上側の摩耗も防止
している。即ち、プロテクタ4が設けられていな
い伝熱器管2の上側の摩耗は、度合は伝熱器管2
の下側より低いが、残存大粒空気泡、或いは小粒
空気泡の合流による再成長空気泡の分解で起る。
これによる摩耗をフイン3が残存大粒空気泡、再
成長空気泡を分解することで果たし、伝熱器管2
の上側表面を保護する。このとき、上記したよう
に、フイン3の表面には硬質の酸化物保護膜が形
成されているので、フイン3の摩耗は発生しな
い。プロテクタ付円周フイン伝熱管の場合、伝熱
管2の上側の流動材の動きは、円周フインの高さ
とピツチを適切に選定することにより、フインの
付け根即ち伝熱管表面附近で極めて緩慢になるこ
とがモデル実験で確かめていること、及びフイン
の先端に近いほどメタル温度が高くなるので硬質
の酸化物保護膜が形成され、このため伝熱管2及
びフイン3の摩耗は発生しない。
Air bubbles rising from the bottom of the furnace form the fluidized combustion bed 1.
It collides with the protector 4 on the lower side of the heat exchanger tube 2 inside and decomposes into small air bubbles. At this time, since the behavior of the fluid material becomes active, without the protector 4,
Although the lower surface of the heat transfer tube 2 is worn out, the protector 4
Since the heat exchanger tube 2 is protected by this, wear of the heat exchanger tube 2 is prevented. However, the installation of the protector 4 reduces the effective heat transfer area of the heat transfer tube 2, resulting in a decrease in heat transfer efficiency. A decrease in heat transfer efficiency is prevented by welding fins 3 to the entire outer peripheral surface of the heat transfer tube 2 to prevent a substantial decrease in the effective heat transfer area. The fins 3 are made of high Cr steel containing 9% or more of Cr steel, and the thickness of the heat transfer tube 2 is adjusted such that the temperature distribution of most of the metal, including the tip of the fins 3, is approximately 500 degrees Celsius or higher. By designing the thickness, the thickness of the fins 3, and the height of the fins 3, it is possible to form a hard and stable oxide protective film on the surface of the fins 3. Wear on the upper side of the heating tube 2 is also prevented. That is, the degree of wear on the upper side of the heat exchanger tube 2 where the protector 4 is not provided is
Although it is lower than the lower side, it occurs due to the decomposition of regrown air bubbles due to the merging of remaining large air bubbles or small air bubbles.
The wear caused by this is resolved by the fins 3 decomposing the remaining large air bubbles and regrowth air bubbles, and the heat transfer tube 2
protect the upper surface of the At this time, as described above, since a hard oxide protective film is formed on the surface of the fins 3, the fins 3 are not worn. In the case of a circumferential fin heat exchanger tube with a protector, the movement of the fluid material above the heat exchanger tube 2 becomes extremely slow at the base of the fins, that is, near the surface of the heat exchanger tube, by appropriately selecting the height and pitch of the circumferential fins. This has been confirmed through model experiments, and since the metal temperature increases closer to the tips of the fins, a hard oxide protective film is formed, so that the heat exchanger tubes 2 and fins 3 do not wear out.

〔考案の効果〕[Effect of idea]

以上、本考案を実施例により説明したように、
本考案は、流動燃焼層内に伝熱器管が配置された
流動床ボイラにおいて、前記伝熱器管の全外周表
面に9%以上のCrを含有する高Cr鋼からなる外
周が円形の円周フインを適宜間隔で複数条に溶着
し、前記円周フインの下側外周のみに前記円周フ
インの外周に適合し断面が半円形の曲面形状板か
らなる耐摩耗性のプロテクタを設けたことを特徴
とする流動床ボイラを提供するものであり、これ
により流動燃焼層内に配置された伝熱器管の伝熱
効率の低下を防ぎつつ、伝熱器管の摩耗を防止す
ることができる。
As described above, the present invention has been explained using examples.
The present invention provides a fluidized bed boiler in which a heat exchanger tube is arranged in a fluidized combustion bed, in which the entire outer circumferential surface of the heat exchanger tube is made of a high chromium steel containing 9% or more of Cr and has a circular outer circumference. A plurality of circumferential fins are welded at appropriate intervals, and a wear-resistant protector made of a curved plate with a semicircular cross section that conforms to the outer circumference of the circumferential fin is provided only on the lower outer periphery of the circumferential fin. The present invention provides a fluidized bed boiler characterized by the following, whereby it is possible to prevent wear of the heat transfer tubes while preventing a decrease in heat transfer efficiency of the heat transfer tubes arranged in the fluidized combustion bed.

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

第1図は、本考案の実施例の正面断面図、第2
図は、第1図中の部の拡大図、第3図は、第2
図中の−矢視図、第4図は、従来の流動床ボ
イラの正面断面図、第5図は、第4図中のV−V
矢視図である。 1,11……流動燃焼層、2,12……伝熱器
管、3……フイン、4……プロテクタ、5……バ
ンド。
FIG. 1 is a front sectional view of an embodiment of the present invention, and FIG.
The figure is an enlarged view of the part in Figure 1, and Figure 3 is an enlarged view of the part in Figure 2.
4 is a front sectional view of a conventional fluidized bed boiler, and FIG. 5 is a view taken along the line V-V in FIG. 4.
It is an arrow view. 1, 11... fluidized combustion bed, 2, 12... heat transfer tube, 3... fin, 4... protector, 5... band.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 流動燃焼層内に伝熱器官が配置された流動床ボ
イラにおいて、前記伝熱器管の全外周表面に9%
以上のCrを含有する高Cr鋼からなる外周が円形
の円周フインを適宜間隔で複数条に溶着し、前記
円周フインの下側外周のみに前記円周フインの外
周に適合し断面が半円形の曲面形状板からなる耐
摩耗性のプロテクタを設けたことを特徴とする流
動床ボイラ。
In a fluidized bed boiler in which a heat transfer device is arranged in a fluidized combustion bed, 9% is applied to the entire outer peripheral surface of the heat transfer tube.
A plurality of circumferential fins with a circular outer circumference made of high Cr steel containing the above Cr are welded at appropriate intervals, and only the lower outer circumference of the circumferential fin matches the outer circumference of the circumferential fin and has a half cross section. A fluidized bed boiler characterized by being equipped with a wear-resistant protector made of a circular curved plate.
JP1984162054U 1984-10-26 1984-10-26 Expired JPH0449441Y2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP1984162054U JPH0449441Y2 (en) 1984-10-26 1984-10-26
CN 85107812 CN85107812A (en) 1984-10-26 1985-10-23 Fluid-bed boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1984162054U JPH0449441Y2 (en) 1984-10-26 1984-10-26

Publications (2)

Publication Number Publication Date
JPS6179701U JPS6179701U (en) 1986-05-28
JPH0449441Y2 true JPH0449441Y2 (en) 1992-11-20

Family

ID=15747217

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1984162054U Expired JPH0449441Y2 (en) 1984-10-26 1984-10-26

Country Status (2)

Country Link
JP (1) JPH0449441Y2 (en)
CN (1) CN85107812A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4936765U (en) * 1972-07-13 1974-04-01
JPS5324654A (en) * 1976-08-19 1978-03-07 Matsushita Electric Ind Co Ltd High-frequency heating device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58158904U (en) * 1982-04-13 1983-10-22 川崎重工業株式会社 Fluidized bed boiler heat transfer tube

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4936765U (en) * 1972-07-13 1974-04-01
JPS5324654A (en) * 1976-08-19 1978-03-07 Matsushita Electric Ind Co Ltd High-frequency heating device

Also Published As

Publication number Publication date
CN85107812A (en) 1986-04-10
JPS6179701U (en) 1986-05-28

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