JPH0253715B2 - - Google Patents
Info
- Publication number
- JPH0253715B2 JPH0253715B2 JP56115143A JP11514381A JPH0253715B2 JP H0253715 B2 JPH0253715 B2 JP H0253715B2 JP 56115143 A JP56115143 A JP 56115143A JP 11514381 A JP11514381 A JP 11514381A JP H0253715 B2 JPH0253715 B2 JP H0253715B2
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- wear
- heat exchanger
- fluidized
- resistant material
- 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 - Lifetime
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/02—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings
- F28F19/06—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings of metal
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
【発明の詳細な説明】
この発明は流動層内に配置した伝熱管の摩耗損
傷を防止する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for preventing wear and tear on heat exchanger tubes placed in a fluidized bed.
砂等の流動媒体を流動化させた流動層内で燃料
(焼却物)を燃焼させる流動層炉は燃焼効率が高
く難燃性の物質でも良好に燃焼できるため各種廃
棄物の焼却処理を始めとして幅広い分野において
利用されている。この流動層炉で発生した熱を蒸
気または温水として回収する場合、空塔部に比較
して流動層内の伝熱効率は格段に優れているため
流動層内に伝熱管を配置することが多い。 Fluidized bed furnaces, which burn fuel (incineration materials) in a fluidized bed made of fluidized fluidized media such as sand, have high combustion efficiency and can burn even flame-retardant materials well, so they are used for incineration of various kinds of waste, etc. It is used in a wide range of fields. When the heat generated in this fluidized bed furnace is recovered as steam or hot water, heat transfer tubes are often placed within the fluidized bed because the heat transfer efficiency within the fluidized bed is much superior to that in the empty column.
第1図は流動層炉の概略を示し、流動層炉本体
1の空気室2に流入した流動化空気(燃焼用空
気)Aは多孔板3を経て砂等の流動媒体が充填し
てある層内に供給され、これを流動化することに
より流動層4を形成する。流動層内に供給された
燃料(焼却物)は流動媒体と混合攪拌しながら燃
焼し、発生した熱は層内に配置した層内伝熱管5
において熱回収されて蒸気もしくは温水として回
収される。この場合、流動層4内は加熱した流動
媒体が激しく流動しており、層内伝熱管5はきわ
めて過酷な条件下に置かれることになる。流動媒
体の運動の激しさは、流動化空気の供給量が多す
ぎて空気のみが層内を吹き抜けてしまう状態が生
じるまではほぼ空気の通過速度に比例する。空気
通過速度は供給した燃料の性状、流動媒体の真比
重等によつても相違するが、層内平均で2.4m/
sec.程度が一般的である。 Figure 1 shows an outline of a fluidized bed furnace. Fluidized air (combustion air) A that has flowed into the air chamber 2 of the fluidized bed furnace body 1 passes through a perforated plate 3 into a bed filled with a fluidized medium such as sand. A fluidized bed 4 is formed by fluidizing the fluidized fluid. The fuel (incineration material) supplied into the fluidized bed burns while being mixed with the fluidized medium and stirred, and the generated heat is transferred to the intrabed heat transfer tube 5 arranged in the bed.
The heat is recovered and recovered as steam or hot water. In this case, the heated fluidized medium is flowing violently in the fluidized bed 4, and the intrabed heat exchanger tubes 5 are placed under extremely severe conditions. The intensity of the movement of the fluidized medium is approximately proportional to the air passage speed until a situation occurs in which the amount of fluidized air supplied is so large that only air is blown through the bed. The air passing speed varies depending on the properties of the supplied fuel, the true specific gravity of the fluidizing medium, etc., but the average speed within the layer is 2.4 m/
sec. degree is common.
以上の状態の流動層内に伝熱管を配置した場
合、伝熱管のベンド部、および流動層の上層部に
位置した武分が流動媒体の擦過により摩耗するこ
とが確認された。先ずベンド部の摩耗について
は、ベンド部近傍においては例えば通過空気速度
が3.4m/sec程度と他の部分より高くなつてお
り、従つて流動媒体の運動も激しく、このため短
期間に摩耗する。これは流動層内に静止物として
配置された層内伝熱管のうちベンド部は流動層炉
側壁と対向位置し、抵抗物のない通路に面してい
るためベンド部管壁近傍において空気通過速度が
速くなり、従つて流動媒体の擦過速度も速くなる
からであると考えられる。また流動層上層部とく
に燃料供給方式が上込めの場合には下層部に比較
して供給された流動化空気の加熱による膨張と、
燃焼ガスが加わることにより、媒体粒子の移動速
度が大となり、伝熱管のうち上層部に位置する部
分はベンド部のみでなく伝熱管全体が激しく摩耗
し、さらに燃料が下込め方式の場合には、給炭ノ
ズル附近が激しく摩耗することになる。これを第
1図で示すと、ベンド部5a,5b,5c,5
d,5e,5fおよび流動層上層部に位置する5
g,5hが特に摩耗が激しい。この様な状態で流
動層炉の運転を続行していると内部流体が流動層
中に漏出し大事故を生ずる虞れがある。 It was confirmed that when a heat transfer tube is placed in a fluidized bed in the above state, the bend portion of the heat transfer tube and the portion located in the upper layer of the fluidized bed are worn out due to friction by the fluidized medium. First, regarding the wear of the bend portion, the passing air velocity near the bend portion is, for example, about 3.4 m/sec, which is higher than other portions, and therefore the movement of the fluid medium is also intense, which causes wear in a short period of time. This is due to the fact that the bend part of the bed heat exchanger tube, which is placed as a stationary object in the fluidized bed, is located opposite the side wall of the fluidized bed furnace and faces a passage with no resistance, so the air passing rate is low near the pipe wall at the bend part. It is thought that this is because the friction speed of the fluid medium becomes faster, and therefore the friction speed of the fluid medium also becomes faster. In addition, in the upper part of the fluidized bed, especially when the fuel supply method is top-filling, the supplied fluidized air expands due to heating compared to the lower part.
Due to the addition of combustion gas, the moving speed of the medium particles increases, and the upper part of the heat transfer tube is severely worn not only at the bend part but also the entire heat transfer tube. , the area around the coal feeding nozzle will be severely worn. When this is shown in FIG. 1, bend portions 5a, 5b, 5c, 5
d, 5e, 5f and 5 located in the upper part of the fluidized bed.
g and 5h have particularly severe wear. If the fluidized bed furnace continues to operate in such a state, there is a risk that the internal fluid will leak into the fluidized bed and cause a major accident.
この発明の目的は上述した問題点を解決し、層
内伝熱管の損傷を防止する方法を提供することに
ある。 An object of the present invention is to solve the above-mentioned problems and provide a method for preventing damage to an interlayer heat exchanger tube.
要するにこの発明は、流動層内に配置した伝熱
管の摩耗を防止する方法において、該伝熱管のベ
ンド部および少なくとも伝熱管のうちの最上部に
位置する部分の外層部を耐摩耗材質で形成したこ
とを特徴とする流動層内伝熱管の摩耗防止方法で
ある。 In short, this invention provides a method for preventing wear of a heat exchanger tube arranged in a fluidized bed, in which the bend portion of the heat exchanger tube and at least the outer layer of the uppermost portion of the heat exchanger tube are formed of a wear-resistant material. This is a method for preventing wear of heat exchanger tubes in a fluidized bed.
以下この発明の実施例を図面を参考に説明す
る。 Embodiments of the present invention will be described below with reference to the drawings.
層内伝熱管のうち摩耗の激しい部分5a〜5h
は前述の如く、擦過する流動媒体の速度が流動層
内を通過する流動化空気(燃焼ガスを含む)の平
均通過速度より速い部分であるが、これをより具
体的に観察すると上記5a〜5hの部分は擦過す
る流動媒体の速度が流動層炉内の多孔板3を通過
する流動化空気の見做し速度よりも30%以上速い
速度となる部分であつて、この部分が特に摩耗が
激しいことが解つた。 Severely worn parts 5a to 5h of the interlayer heat exchanger tubes
As mentioned above, these are the parts where the speed of the rubbing fluidized medium is higher than the average passing speed of the fluidized air (including combustion gas) passing through the fluidized bed. This part is a part where the speed of the abrasive fluidized medium is 30% or more higher than the estimated speed of fluidized air passing through the perforated plate 3 in the fluidized bed furnace, and this part is particularly abraded. I understand.
第2図は流動層炉1に配置した層内伝熱管5に
対する耐摩耗材質の形成状態を示す。図中符号6
a,6b,6c,6d,6e,6fはベンド部5
a,5b,5c,5d,5e,5fに各々形成し
た耐摩耗材層、6g,6hは流動層上層部に位置
する伝熱管5g,5hに各々形成した耐摩耗材層
である。 FIG. 2 shows the state of formation of the wear-resistant material on the intrabed heat exchanger tubes 5 disposed in the fluidized bed furnace 1. As shown in FIG. Code 6 in the diagram
a, 6b, 6c, 6d, 6e, 6f are bend parts 5
Wear-resistant material layers were formed on a, 5b, 5c, 5d, 5e, and 5f, respectively, and wear-resistant material layers 6g and 6h were formed on heat exchanger tubes 5g and 5h, respectively, located in the upper layer of the fluidized bed.
第3図は第2図のベンド部5bに対する耐摩耗
材層の形成方法の一例を示す。図中符号7aおよ
び7bはベンド部5bの外壁部に密着するよう形
成した耐摩耗材から成る耐摩耗材層形成部材であ
り、部材7aをベンド部5bの内側に、同7bを
外側に配置することによりベンド部5bを完全に
覆い、接合部を溶接により固着する。第4図は第
3図に示す方法で耐摩耗材層を形成した場合の伝
熱管の横断面図であり、符号8,8は溶接部を示
す。この方法により耐摩耗材層を形成すれば、現
在使用している流動層炉であつても、炉内の流動
媒体を抜き去ることにより容易に耐摩耗材層を形
成することができる。なお耐摩耗材としては例え
ば25%Cr、12%Niのステンレス材等が好適であ
る。 FIG. 3 shows an example of a method of forming a wear-resistant material layer on the bend portion 5b of FIG. 2. Reference numerals 7a and 7b in the figure are wear-resistant material layer forming members made of wear-resistant material formed so as to be in close contact with the outer wall of the bend portion 5b. The bend portion 5b is completely covered and the joint portion is fixed by welding. FIG. 4 is a cross-sectional view of a heat exchanger tube in which a wear-resistant material layer is formed by the method shown in FIG. 3, and numerals 8 and 8 indicate welded portions. If the wear-resistant material layer is formed by this method, the wear-resistant material layer can be easily formed even in the currently used fluidized bed furnace by removing the fluidized medium in the furnace. As the wear-resistant material, for example, a stainless steel material of 25% Cr and 12% Ni is suitable.
次に第3図の如く耐摩耗材料をあらかじめ一定
の形状に成形しておく方法の外に、耐摩耗材料を
所定の部分に溶射または溶接肉盛りして耐摩耗材
層を形成してもよい。 Next, instead of forming the wear-resistant material into a predetermined shape as shown in FIG. 3, the wear-resistant material layer may be formed by thermal spraying or welding the wear-resistant material onto a predetermined portion.
以上の方法により摩耗の激しい伝熱管ベンド
部、流動層上層部伝熱管表面に耐摩耗材層を形成
する。 By the above method, a wear-resistant material layer is formed on the surface of the heat exchanger tube at the bend portion of the heat exchanger tube and the upper layer of the fluidized bed, which are subject to severe wear.
この発明を実施することにより流動層内に配置
した伝熱管の摩耗を大幅に減少させることができ
るので伝熱管の寿命を延長させることが可能で、
内部流体の漏出による事故の虞れもない。 By carrying out this invention, it is possible to significantly reduce the wear of heat exchanger tubes placed in a fluidized bed, thereby extending the life of the heat exchanger tubes.
There is no risk of accidents due to leakage of internal fluid.
第1図は従来の流動層炉の断面図、第2図はこ
の発明に係る耐摩耗方法を実施した層内伝熱管を
有する流動層炉の断面図、第3図は耐摩耗材層の
形成方法を示す耐摩耗材層形成部材の斜視図、第
4図は耐摩耗材層を形成した状態における第3図
のA−A断面図である。
1……流動層炉本体、3……多孔板、4……流
動層、5a,5b,5c,5d,5e,5f……
ベンド部、5g,5h……流動層上層部伝熱管、
6a,6b,6c,6d,6e,6f,6g,6
h……耐摩耗材層、7a,7b……耐摩耗材層形
成部材。
Fig. 1 is a cross-sectional view of a conventional fluidized bed furnace, Fig. 2 is a cross-sectional view of a fluidized bed furnace having an intrabed heat exchanger tube in which the wear-resistant method according to the present invention is implemented, and Fig. 3 is a method for forming a wear-resistant material layer. FIG. 4 is a perspective view of the wear-resistant material layer forming member, and FIG. 4 is a cross-sectional view taken along the line AA in FIG. 3 with the wear-resistant material layer formed. 1...Fluidized bed furnace main body, 3...Perforated plate, 4...Fluidized bed, 5a, 5b, 5c, 5d, 5e, 5f...
Bend part, 5g, 5h...Fluidized bed upper heat exchanger tube,
6a, 6b, 6c, 6d, 6e, 6f, 6g, 6
h...Wear-resistant material layer, 7a, 7b... Wear-resistant material layer forming member.
Claims (1)
方法において、該伝熱管のベンド部および少なく
とも伝熱管のうちの最上部に位置する部分の外層
部を耐摩耗材質で形成したことを特徴とする流動
層内伝熱管の摩耗防止方法。1. A method for preventing wear of a heat exchanger tube arranged in a fluidized bed, characterized in that the bend portion of the heat exchanger tube and the outer layer of at least the uppermost portion of the heat exchanger tube are formed of a wear-resistant material. A method for preventing wear of heat transfer tubes in a fluidized bed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11514381A JPS5818089A (en) | 1981-07-24 | 1981-07-24 | Method of preventing wear of heat exchanger tube arranged in fluidized bed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11514381A JPS5818089A (en) | 1981-07-24 | 1981-07-24 | Method of preventing wear of heat exchanger tube arranged in fluidized bed |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5818089A JPS5818089A (en) | 1983-02-02 |
| JPH0253715B2 true JPH0253715B2 (en) | 1990-11-19 |
Family
ID=14655358
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11514381A Granted JPS5818089A (en) | 1981-07-24 | 1981-07-24 | Method of preventing wear of heat exchanger tube arranged in fluidized bed |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5818089A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4619314A (en) * | 1983-08-05 | 1986-10-28 | Ishikawajima-Harima Jukogyo Kabushiki Kaisha | Device for preventing wear of heat transfer tubes in fluidized-bed boiler |
| JPS6314086A (en) * | 1986-07-03 | 1988-01-21 | Ebara Corp | Fluidized bed layer heat recovery device |
| NO349002B1 (en) * | 2024-07-16 | 2025-08-25 | Vecs As | An inflatable bladder, a system comprising the bladder, and a method for bringing the bladder into and out of a vessel |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5790596A (en) * | 1980-11-27 | 1982-06-05 | Mitsubishi Heavy Ind Ltd | Heat transfer pipe |
-
1981
- 1981-07-24 JP JP11514381A patent/JPS5818089A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5818089A (en) | 1983-02-02 |
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