JPS6017679Y2 - Fluidized bed furnace - Google Patents
Fluidized bed furnaceInfo
- Publication number
- JPS6017679Y2 JPS6017679Y2 JP14497179U JP14497179U JPS6017679Y2 JP S6017679 Y2 JPS6017679 Y2 JP S6017679Y2 JP 14497179 U JP14497179 U JP 14497179U JP 14497179 U JP14497179 U JP 14497179U JP S6017679 Y2 JPS6017679 Y2 JP S6017679Y2
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- bottom plate
- furnace
- air
- bed furnace
- 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
Links
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
- Furnace Housings, Linings, Walls, And Ceilings (AREA)
Description
【考案の詳細な説明】 この考案は流動層炉の構造に関する。[Detailed explanation of the idea] This invention relates to the structure of a fluidized bed reactor.
流動層炉は廃棄物の焼却用として使用されるがその発生
熱エネルギーを有効利用するため、側壁を水冷壁にする
構造が提案されている。Fluidized bed furnaces are used to incinerate waste, and in order to effectively utilize the heat energy generated, a structure in which the side walls are water-cooled has been proposed.
また一方におい石炭等を燃料とし、これをボイラとして
使用する流動層ボイラが開発使用されている。On the other hand, a fluidized bed boiler that uses coal as a fuel and uses it as a boiler has been developed and used.
流動層内の温度は焼却する材料によって500°C乃至
1000℃と高温になっており、粉粒体の石炭燃焼の場
合には約700℃にしてNOxの発生防止をしている。The temperature in the fluidized bed is as high as 500°C to 1000°C depending on the material to be incinerated, and in the case of granular coal combustion, it is set at about 700°C to prevent the generation of NOx.
そのため底板については高温に耐えるステンレス板に空
気通路用の孔を多数穿設したものや、耐火材等が使用さ
れている。For this reason, the bottom plate is made of a stainless steel plate that can withstand high temperatures with many holes for air passages, or a fireproof material.
これでは高価なものとなり、炉の起動又は停止に際し底
板の上面の炉内側と下面の空気室側との間の温度差に基
く底板の湾曲、変形の繰返しにより亀裂による損傷等の
問題がある。This is expensive and causes problems such as damage due to cracks due to repeated bending and deformation of the bottom plate due to the temperature difference between the top of the bottom plate inside the furnace and the bottom side of the air chamber when starting or stopping the furnace.
この考案は通常の鋼板鋼管を使用し、材料費を低下させ
かつ伝熱面として底板を有効利用することを提案するも
のである。This idea uses ordinary steel plates and pipes to reduce material costs and proposes effective use of the bottom plate as a heat transfer surface.
要するにこの考案は、流動層炉において炉側壁を冷却管
構造とし、かつ流動層炉底部を冷却管を含む底板構造と
し、該底板には流動用空気通路を設け、上記底板下方に
は前記空気通路に流動用空気を供給する空気室を設けた
流動層炉であることを特徴とする。In short, this idea is that in a fluidized bed furnace, the furnace side wall has a cooling tube structure, the bottom of the fluidized bed furnace has a bottom plate structure including a cooling tube, the bottom plate is provided with a flow air passage, and the air passage is provided below the bottom plate. The furnace is characterized by being a fluidized bed furnace equipped with an air chamber for supplying fluidizing air to the furnace.
この考案を以下図面により説明する。This idea will be explained below with reference to the drawings.
第1図は流動層炉の流動層部を含む底部の縦断面図であ
る。FIG. 1 is a longitudinal sectional view of the bottom of the fluidized bed furnace including the fluidized bed section.
ここに流動層炉とは廃棄物焼却炉、熱分解炉、流動層ボ
イラ等を含む炉をいう。Here, the fluidized bed furnace refers to a furnace including a waste incinerator, a pyrolysis furnace, a fluidized bed boiler, and the like.
第1図は水冷壁構造の流動層ボイラ1を示すもので側壁
は木管壁構造(以下単にメンブレンパネルと称す)とし
ている。FIG. 1 shows a fluidized bed boiler 1 having a water-cooled wall structure, and the side walls have a wood tube wall structure (hereinafter simply referred to as a membrane panel).
メンブレンパネルとは管を平行に必要幅だけ複数本並べ
かつ管相互を細幅根板で溶接し一枚の板状体(パネル)
にしたもので、ガス漏れを生ずることなく伝熱が効率良
く行なわれる等の特質をもち広くボイラにおいては採用
されているものである。A membrane panel is a single plate-like body (panel) made by arranging multiple tubes in parallel with the required width and welding the tubes together with narrow root plates.
It is widely used in boilers because of its characteristics such as efficient heat transfer without causing gas leakage.
符号2は流動層内に設けた蒸発管又は過熱器管である。Reference numeral 2 represents an evaporator tube or a superheater tube provided within the fluidized bed.
層中バーナ、起動用バーナ、被焼却物供給ノズルはこの
図面においては省略した。The in-bed burner, starting burner, and incineration material supply nozzle are omitted in this drawing.
3は空気室でその上方に冷却管を含む底板4を装着する
。3 is an air chamber, and a bottom plate 4 including a cooling pipe is mounted above the air chamber.
この場合底板の冷却管の管軸を含む面は水平に対し約7
°傾斜させる。In this case, the surface of the bottom plate containing the pipe axis of the cooling pipe is about 7
° Tilt.
この傾斜は冷却水の循環上必要でありかつ好適なものと
なっている。This slope is necessary and preferred for the circulation of cooling water.
この底板の冷却管を相互に接続するフラットフィン5の
部分にバブルキャップ6を流動用空気通路として多数設
け、多孔板として使用する。A large number of bubble caps 6 are provided as flowing air passages in the flat fins 5 that connect the cooling pipes of the bottom plate, and are used as a perforated plate.
バブルキャップは通常その一例を第3図に示すようなも
ので、小径の管の上面に蓋6aを設け、側方に空気孔7
をもつものである。An example of a bubble cap is normally shown in Fig. 3, with a lid 6a provided on the top surface of a small-diameter tube and an air hole 7 on the side.
It is something that has.
蓋6aは炉停止時流動媒体の空気室内への侵入を防止す
るものである。The lid 6a prevents the fluidized medium from entering the air chamber when the furnace is shut down.
空気通路はフィン部に小孔を多数設けたものであっても
よい。The air passage may be formed by providing a large number of small holes in the fin portion.
流動用空気の供給は傾斜する底板の低位側に設けた空気
室を拡大通路型にし、図面右方に空気供給口11を設け
、これより空気を供給すると各バブルキャップより均等
量の空気噴出をするという効果がある。For the supply of flowing air, the air chamber provided on the lower side of the sloping bottom plate is made into an enlarged passage type, and an air supply port 11 is provided on the right side of the drawing, and when air is supplied from this, an equal amount of air is ejected from each bubble cap. It has the effect of
また低位側に媒体の抜き出し口10を設けるときは底板
の傾斜により流動化した媒体の抜き出しを容易にする。Further, when the medium extraction port 10 is provided on the lower side, the inclination of the bottom plate facilitates extraction of the fluidized medium.
底板の上位端を側壁の冷却管の下端が接続しているヘッ
ダ8に接続することができる。The upper end of the bottom plate can be connected to a header 8 to which the lower ends of the cooling pipes of the side walls are connected.
また層内温度を適正に保持するため各メンブレンパネル
にスタッド12を設はプラスティッククロームオア等の
耐火材層9を設けてもよい。Further, in order to properly maintain the internal temperature of the layer, studs 12 may be provided on each membrane panel, and a layer 9 of refractory material such as plastic chrome ore may be provided.
この考案を実施することにより、層内のに発生する熱を
底板で吸収腰蒸気発生させることができ、底板の構成部
材たる冷却管内を冷却水が流れるので、底板の火炉側た
る上面と、空気室側たる下面との間に温度差を生ずるこ
となく、底板の変形による亀裂を生ずることなく、その
寿命も永くなるという効果を奏するものである。By implementing this idea, the heat generated in the layer can be absorbed by the bottom plate to generate steam, and since the cooling water flows through the cooling pipes that are the constituent members of the bottom plate, the upper surface of the bottom plate on the furnace side and the air This has the effect that there is no temperature difference between the base plate and the lower surface on the chamber side, no cracks are generated due to deformation of the bottom plate, and the life of the bottom plate is extended.
第1図はこの考案にかかる流動層炉の縦断面図、第2図
は第1図のA−A断面図図、第3図は第2図のB−B断
面部分親図である。
1・・・・・・流動層ボイラ、2・・・・・・蒸発管、
3・・・・・・空気室、4・・・・・・底板、5・・・
・・・フラットフィン、6・・・・・・バブルキャップ
、7・・・・・・空気孔、訃・・・・・ヘッダ、9・・
・・・・耐火材層、10・・・・・・抜き出し口、11
・・・・・・空気供給口、12・・・・・・スタッド。FIG. 1 is a longitudinal sectional view of a fluidized bed furnace according to this invention, FIG. 2 is a sectional view taken along the line AA in FIG. 1, and FIG. 3 is a partial partial sectional view taken along the line BB in FIG. 1... Fluidized bed boiler, 2... Evaporation tube,
3...Air chamber, 4...Bottom plate, 5...
...Flat fin, 6...Bubble cap, 7...Air hole, butt...Header, 9...
...Fireproof material layer, 10... Outlet port, 11
...Air supply port, 12...Stud.
Claims (1)
層底部を冷却管を含む底板構造とし、該底板には流動用
空気通路を設け、上記底板下方には前記空気通路に流動
用空気を供給する空気室を設けたことを特徴とする流動
層炉。In a fluidized bed reactor, the furnace side wall has a cooling tube wall structure, the bottom of the fluidized bed has a bottom plate structure including a cooling tube, a fluidizing air passage is provided in the bottom plate, and a fluidizing air is provided in the air passage below the bottom plate. A fluidized bed furnace characterized by having a supply air chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14497179U JPS6017679Y2 (en) | 1979-10-22 | 1979-10-22 | Fluidized bed furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14497179U JPS6017679Y2 (en) | 1979-10-22 | 1979-10-22 | Fluidized bed furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5666633U JPS5666633U (en) | 1981-06-03 |
JPS6017679Y2 true JPS6017679Y2 (en) | 1985-05-30 |
Family
ID=29376156
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14497179U Expired JPS6017679Y2 (en) | 1979-10-22 | 1979-10-22 | Fluidized bed furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6017679Y2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6055813U (en) * | 1983-08-04 | 1985-04-19 | 三菱重工業株式会社 | fluidized bed boiler |
-
1979
- 1979-10-22 JP JP14497179U patent/JPS6017679Y2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5666633U (en) | 1981-06-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6817354B2 (en) | Wood burning furnace | |
JPH0313482B2 (en) | ||
JPS599830B2 (en) | Fluidized bed heat exchanger with fluid cooled air distribution plate assembly | |
CA1165649A (en) | Furnaces | |
JPS6017679Y2 (en) | Fluidized bed furnace | |
JPH0726721B2 (en) | boiler | |
US20060124077A1 (en) | Continuous steam generator with circulating atmospheric fluidised-bed combustion | |
JPS5837403A (en) | Steam generator with main boiler and fluid bed furnace | |
JP4173791B2 (en) | Fluidized incinerator system and method for operating the system | |
JPH01203801A (en) | Fluidized bed boiler having vertical heat transfer pipe and fluidized bed hot water boiler employing said boiler | |
RU2663435C1 (en) | Method of solid fuel combustion and high-temperature reactor with steam boiler for its implementation | |
JP2551779Y2 (en) | Furnace smoke tube boiler | |
JPS5918302A (en) | Combustion apparatus with catalyst type heat exchanger for heat recovery | |
JPS5878010A (en) | Boiler | |
IE48624B1 (en) | Improvements in and relating to boilers | |
JP3765555B2 (en) | Fluidized bed combustor | |
JP2528711B2 (en) | Double bed fluidized bed boiler | |
CN106545996A (en) | A kind of efficient pillar heat exchange boiler | |
JPH0337081B2 (en) | ||
WO2021031435A1 (en) | Ultra-low nitrogen gas steam boiler | |
US4257357A (en) | Furnaces | |
JPS6042254Y2 (en) | Incinerator with steam energy extraction function | |
JP2003336819A (en) | Air diffuser for fluidized bed incinerator | |
JPS6314191Y2 (en) | ||
GB2086755A (en) | Fluidised bed boilers |