JPS5941705A - Fluidized bed apparatus - Google Patents
Fluidized bed apparatusInfo
- Publication number
- JPS5941705A JPS5941705A JP15172682A JP15172682A JPS5941705A JP S5941705 A JPS5941705 A JP S5941705A JP 15172682 A JP15172682 A JP 15172682A JP 15172682 A JP15172682 A JP 15172682A JP S5941705 A JPS5941705 A JP S5941705A
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- wall surface
- spacer plate
- temperature
- thermal conducting
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C10/00—Fluidised bed combustion apparatus
- F23C10/18—Details; Accessories
- F23C10/28—Control devices specially adapted for fluidised bed, combustion apparatus
Abstract
Description
【発明の詳細な説明】
この発明は流動層装置に係り、特に内部に形成した流動
層の層高を正確に検知することのできる流動層装置に関
する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fluidized bed apparatus, and more particularly to a fluidized bed apparatus capable of accurately detecting the bed height of a fluidized bed formed therein.
流動層を利用した装置は各種の反応装置として、また燃
焼装置として利用されている。このうち、第1図を用い
て燃焼装置として使用される場合を例に説明すると、流
動化気体(燃焼用空気)Aにより砂等の媒体を流動化さ
せて形成した流動層1に対して供給された燃料(焼却物
)2は流動媒体と混合撹拌しながら燃焼するため、比較
的難燃性の物質でも良好に燃焼させることができる。こ
のため流動層燃焼装置は生ゴミ。Devices using fluidized beds are used as various reaction devices and combustion devices. Among these, to explain the case where it is used as a combustion device using Fig. 1 as an example, fluidizing gas (combustion air) is supplied to a fluidized bed 1 formed by fluidizing a medium such as sand. Since the fuel (incineration material) 2 is burned while being mixed and stirred with the fluidized medium, even relatively flame-retardant substances can be burnt well. For this reason, fluidized bed combustion equipment is garbage.
脱水汚泥等の廃棄物の焼却をはじめとして各種の分野に
おいてその能力が注目されている。このことは燃焼装置
としてのみでなく、石炭のガス化反応等、反応装置とし
て利用する分野においても同様であり、反応の促進能力
が注目されている。この場合、層内での燃焼もしくは反
応を良好に行なうためには流動層の層高を十分に制御し
、燃料(反応物質)の混合撹拌を良好に行なう必要があ
る。しかし、流動層自体が高温であり、かつ装置本体3
の壁面は厚い耐火構造となっている等の理由により層高
を検知することは困難であった。このため従来は空気室
4内に供給する流動化気体Aの圧力損失を計測する等の
方法により層高を間接的に計測する方法を行なっている
が、誤差が相当に大きく実用上程々の問題がある。Its capabilities are attracting attention in various fields, including incineration of waste such as dehydrated sludge. This is true not only as a combustion device, but also in fields where it is used as a reaction device, such as in coal gasification reactions, and its ability to promote reactions is attracting attention. In this case, in order to perform combustion or reaction well within the bed, it is necessary to sufficiently control the bed height of the fluidized bed and to mix and stir the fuel (reactant) well. However, the fluidized bed itself is high temperature, and the device main body 3
It was difficult to detect the layer height due to the thick fireproof structure of the walls. For this reason, conventional methods have been used to indirectly measure the bed height by, for example, measuring the pressure loss of the fluidizing gas A supplied into the air chamber 4, but the error is quite large and is not a practical problem. There is.
この発明の目的は上述した問題点を除去し、装置内に形
成した流1動層の層高を正確に計測できる流動層装置を
提供することにある。An object of the present invention is to eliminate the above-mentioned problems and provide a fluidized bed device that can accurately measure the bed height of the fluidized bed formed within the device.
要するにこの発明は、流動層装置本体の壁面の一部に対
し、はぼ重力方向に沿って層内温度を外部に伝達する伝
熱部を形成し、この伝熱部の重力方向の温度変化により
流動層の層高を検知し得るよう構成した流動層装置であ
る。In short, this invention forms a heat transfer part on a part of the wall surface of the main body of the fluidized bed apparatus, which transmits the temperature inside the bed to the outside along the direction of gravity. This is a fluidized bed device configured to be able to detect the bed height of a fluidized bed.
以下この発明の実施例を図面により説明する。Embodiments of the present invention will be described below with reference to the drawings.
第2図および第3図において、符号5は流動層装置の壁
面を形成する壁面構造の一例を示す。In FIGS. 2 and 3, reference numeral 5 indicates an example of a wall structure forming a wall of the fluidized bed apparatus.
6は内部に給水を通過させる水管、7はこれら平行に配
置した水管6の間に介在配置したメンブレンバーと称す
る介在板であり、これら介在板7と水管を一体的に構成
することにより壁面全体をメンブレン構造としている。Reference numeral 6 indicates a water pipe through which water supply passes, and reference numeral 7 indicates an intervening plate called a membrane bar interposed between these water pipes 6 arranged in parallel. has a membrane structure.
この壁面のうち一部の介在板の幅を他の介在板の幅より
も大きくシ(符号7aで示す)、両側部の水管による冷
却効果がこの介在板7aの中央部まで及ばないように構
成しておく。次に流動層1と接する壁面内側には第3図
に示す如く耐火材層8が形成しであるが、前記介在板7
aの中央部を中心として層高方向つまり重力方向に沿っ
て耐火材層8を削除し、伝熱部9を形成する。The width of some of the intervening plates on this wall surface is made larger than the width of other intervening plates (indicated by reference numeral 7a), so that the cooling effect of the water pipes on both sides does not reach the center of this intervening plate 7a. I'll keep it. Next, a refractory material layer 8 is formed on the inner side of the wall surface in contact with the fluidized bed 1 as shown in FIG.
The heat transfer portion 9 is formed by removing the refractory material layer 8 along the layer height direction, that is, the direction of gravity, centering on the central portion of a.
以上の装置において、流動層1を形成する流動媒体は第
4図に示す如く、この伝熱部9において介在板7aに直
接接触し、流動層1の熱を外部に直接伝熱する。In the above apparatus, the fluidized medium forming the fluidized bed 1 directly contacts the intervening plate 7a in the heat transfer section 9, as shown in FIG. 4, and directly transfers the heat of the fluidized bed 1 to the outside.
ここで流動層装置を燃焼装置として使用する場合の装置
内温度分布について考察すると、流動層1の温度は約8
50°Cであり、流動層1の表面近傍の空塔部10の温
度は約800°Cが一般的である。また、流動層1にお
いては赤熱した流動媒体が被加熱物に対して直接接触す
るので伝熱率は空塔部10の4〜5倍に達する。このた
め伝熱部9の介在板7aのメタル温度は流動層1に接触
する部分と空塔部では明瞭に差が生じる。Considering the temperature distribution inside the fluidized bed device when it is used as a combustion device, the temperature of the fluidized bed 1 is about 8
50°C, and the temperature of the empty column 10 near the surface of the fluidized bed 1 is generally about 800°C. Further, in the fluidized bed 1, the red-hot fluidized medium is in direct contact with the object to be heated, so that the heat transfer rate reaches 4 to 5 times that of the empty column part 10. Therefore, there is a clear difference in the metal temperature of the intervening plate 7a of the heat transfer part 9 between the part that contacts the fluidized bed 1 and the empty column part.
従って伝熱部9のメタル温度の分布を計測すれば流動層
1の層高は外部から正確に検知し得る。Therefore, by measuring the metal temperature distribution in the heat transfer section 9, the height of the fluidized bed 1 can be accurately detected from the outside.
この伝熱部9の温度検知は、伝熱部9に対して 4゜複
数個のサーモカップルを配置して行なう外、第4図に示
す赤外線影像装置11を用いてもよい。The temperature of the heat transfer section 9 may be detected by arranging a plurality of thermocouples at 4 degrees with respect to the heat transfer section 9, or alternatively, an infrared imaging device 11 shown in FIG. 4 may be used.
この装置は対象物から発する赤外線量に対応して熱画像
信号を発信し、カラーテレビ等の画像表示装置により温
度分布を画像表示するものであり、この装置によれば伝
熱部9の温度分布は正確かつ容易に把握できる。また、
介在板7aの熱伝導率が解っていれば、介在板7aのメ
タル温度から流動層1の温度自体を算出することができ
る。This device transmits a thermal image signal corresponding to the amount of infrared rays emitted from the object and displays the temperature distribution as an image on an image display device such as a color television. can be accurately and easily determined. Also,
If the thermal conductivity of the intervening plate 7a is known, the temperature itself of the fluidized bed 1 can be calculated from the metal temperature of the intervening plate 7a.
さらに上述の場合においては装置壁面を゛メンブレン構
造としたが、これに限るものではなく、壁面の一部に対
して、空塔部と流動層部の温度差が検知し得る程度に熱
伝達率を高めるよう構成すればこの発明の目的を達成す
ることができる。Furthermore, in the above case, the wall surface of the apparatus has a membrane structure, but the structure is not limited to this, and the heat transfer coefficient for a part of the wall surface is such that the temperature difference between the empty column part and the fluidized bed part can be detected. The object of the present invention can be achieved by configuring it to increase.
この発明を実施することにより装置外部から流動層の層
高を容易かつ正確に計測することができる。By implementing this invention, the bed height of the fluidized bed can be easily and accurately measured from outside the apparatus.
第1図は流動層装置の断面図、第2図はこの発明に係る
流動装置壁面の正面部分図、第3図は第2図のI−I線
による断面図、第4図は第3図のn−n線による断面図
である。
1・・・・・・流動層 5・・・・・・装置壁面6
・・・・・・水管 7,7a・・呻介在板8・・・
・・・耐火材層 9・・・・・・伝熱部10・・・・
・・空塔部 11・・・赤外線影像装置代理人弁理士
岡 1)梧 部FIG. 1 is a sectional view of a fluidized bed apparatus, FIG. 2 is a partial front view of a wall surface of a fluidized bed apparatus according to the present invention, FIG. 3 is a sectional view taken along line I-I in FIG. 2, and FIG. FIG. 2 is a cross-sectional view taken along line nn of FIG. 1...Fluidized bed 5...Device wall surface 6
...Water pipes 7, 7a... Groaning interposition plate 8...
... Refractory material layer 9 ... Heat transfer part 10 ...
...Soratobe 11...Patent attorney representing infrared imaging device Oka 1) Gobebe
Claims (1)
流動層部と空塔部の温度差を外部に伝熱しこれを検知し
得る熱伝導率を有する伝熱部をほぼ重力方向に形成し、
この伝熱部の温度分布を検知して流動層の層高を計測す
ることを特徴とする流動層装置。 2、前記壁面を水管と介在板とから成るメンブレン構造
とし、各介在板のうち一部を幅広介在板として両側に位
置する水管の冷却影響を受けることの少ない部分をこの
幅広介在板に形成させ、かつ重力方向については炉内の
耐火材層の厚さを減少させ、もしくはこの耐火材層を除
去することにより介在板で炉内層高を検知しうるごとく
形成したことを特徴とする特許請求の範囲第1項記載の
流動層装置。 3、伝熱部の温度分布を赤外線影像装置を用いて計測す
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
記載の流動層装置。[Scope of Claims] 1. A heat transfer section having a thermal conductivity capable of transmitting and detecting the temperature difference between at least the fluidized bed section and the empty column section to the outside is provided on a part of the wall surface constituting the main body of the apparatus. Formed almost in the direction of gravity,
A fluidized bed device characterized by measuring the bed height of the fluidized bed by detecting the temperature distribution in the heat transfer section. 2. The wall surface has a membrane structure consisting of a water pipe and an intervening plate, and a part of each intervening plate is made into a wide intervening plate, and a part that is less affected by the cooling effect of the water pipes located on both sides is formed on this wide intervening plate. , and in the direction of gravity, the thickness of the refractory layer inside the furnace is reduced or the refractory layer is removed so that the height of the layer inside the furnace can be detected with the intervening plate. The fluidized bed apparatus according to scope 1. 3. The fluidized bed apparatus according to claim 1 or 2, wherein the temperature distribution in the heat transfer section is measured using an infrared imaging device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15172682A JPS5941705A (en) | 1982-09-02 | 1982-09-02 | Fluidized bed apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15172682A JPS5941705A (en) | 1982-09-02 | 1982-09-02 | Fluidized bed apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5941705A true JPS5941705A (en) | 1984-03-08 |
Family
ID=15524939
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15172682A Pending JPS5941705A (en) | 1982-09-02 | 1982-09-02 | Fluidized bed apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5941705A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6196114U (en) * | 1984-11-30 | 1986-06-20 | ||
US5563803A (en) * | 1992-03-19 | 1996-10-08 | Hitachi, Ltd. | Fluidized-bed equipment and pressurized fluidized-bed (combustion) combined cycle apparatus |
-
1982
- 1982-09-02 JP JP15172682A patent/JPS5941705A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6196114U (en) * | 1984-11-30 | 1986-06-20 | ||
JPH053844Y2 (en) * | 1984-11-30 | 1993-01-29 | ||
US5563803A (en) * | 1992-03-19 | 1996-10-08 | Hitachi, Ltd. | Fluidized-bed equipment and pressurized fluidized-bed (combustion) combined cycle apparatus |
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