JPH085013A - Perforated plate cleaning device for fluidized bed type/ heat exchanger - Google Patents
Perforated plate cleaning device for fluidized bed type/ heat exchangerInfo
- Publication number
- JPH085013A JPH085013A JP16319094A JP16319094A JPH085013A JP H085013 A JPH085013 A JP H085013A JP 16319094 A JP16319094 A JP 16319094A JP 16319094 A JP16319094 A JP 16319094A JP H085013 A JPH085013 A JP H085013A
- Authority
- JP
- Japan
- Prior art keywords
- pressure air
- perforated plate
- fluidized bed
- heat exchanger
- exhaust gas
- 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.)
- Granted
Links
- 238000004140 cleaning Methods 0.000 title claims abstract description 15
- 239000007787 solid Substances 0.000 claims abstract description 27
- 239000002245 particle Substances 0.000 claims description 24
- 238000009423 ventilation Methods 0.000 claims description 11
- 239000000428 dust Substances 0.000 abstract description 8
- 239000004071 soot Substances 0.000 abstract description 8
- 238000007599 discharging Methods 0.000 abstract 3
- 238000013022 venting Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 238000004891 communication Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000003809 water extraction Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000010349 pulsation Effects 0.000 description 1
Landscapes
- Cleaning In General (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、ディーゼルエンジン
等から出る排ガスを利用した流動層式熱交換器の多孔板
クリーニング装置の改良に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement of a porous plate cleaning device for a fluidized bed heat exchanger using exhaust gas emitted from a diesel engine or the like.
【0002】[0002]
【従来の技術】従来、この種の流動層式熱交換器は、図
5〜6に示すように、排ガス入口21aと排ガス出口2
1bを備えたケーシング21内の略中央部に、多数の通
気孔を有する多孔板22を設け、この多孔板22上に固
体粒子(例えば硅砂)からなる適当な厚さの固体粒子層
23を形成している。また、ケーシング21内には、略
U字状のパイプからなる被加熱流体としての水を移送す
る伝熱管24が設けてあって、前記U字状の伝熱管24
の一方の平行部を前記固体粒子層23内に挿入し、他方
の平行部を前記固体粒子層23の上方に配置している。
そして、前記一方の平行部の先端部を水取入路25に接
続し、他方の平行部の先端部を水取出路26に接続して
いる。前記排ガス出口21bの下方近傍にバツフル板2
7を設け、排ガスの流入により飛散する固体粒子の流出
を防止するようにしている。図中28は、前記多孔板2
2の下面に設けたブラシを装着した回動式のクリーニン
グ装置である。2. Description of the Related Art Conventionally, a fluidized bed heat exchanger of this type has an exhaust gas inlet 21a and an exhaust gas outlet 2 as shown in FIGS.
A porous plate 22 having a large number of vent holes is provided in a substantially central portion of a casing 21 having 1b, and a solid particle layer 23 of solid particles (for example, silica sand) having an appropriate thickness is formed on the porous plate 22. are doing. In the casing 21, a heat transfer tube 24, which is a substantially U-shaped pipe for transferring water as a fluid to be heated, is provided, and the U-shaped heat transfer tube 24 is provided.
One parallel part is inserted in the solid particle layer 23, and the other parallel part is arranged above the solid particle layer 23.
The tip of one of the parallel portions is connected to the water intake passage 25, and the tip of the other parallel portion is connected to the water outlet passage 26. The baffle plate 2 is provided near the lower part of the exhaust gas outlet 21b.
7 is provided to prevent the outflow of solid particles scattered by the inflow of exhaust gas. In the figure, 28 is the perforated plate 2
2 is a rotation type cleaning device equipped with a brush provided on the lower surface of 2.
【0003】ところで、上記構成の流動層式熱交換器に
おいて、通常運転時には、排ガス入口21aより流入す
る高熱の排ガスは、排ガス入口21aから排ガス出口2
1bに向って通過するが、このとき、ケーシング21内
に設けた多孔板22の通気孔から固体粒子層23内へ噴
出する。この排気ガスの噴出によって、前記固体粒子層
23が激しく攪拌および加熱されて流動状態となり、い
わゆる流動層が形成される。一方伝熱管24の2つの平
行部は共にこの流動層内にあって、これと接触してお
り、前記水取入路25から伝熱管24内に流入した水
が、伝熱管24内を通過しながら流動層によって加熱さ
れた後、水取出路26から流出し、ボイラの温水または
蒸気循環系内を循環する。By the way, in the fluidized bed heat exchanger having the above structure, during normal operation, high-heat exhaust gas flowing from the exhaust gas inlet 21a flows from the exhaust gas inlet 21a to the exhaust gas outlet 2a.
Although it passes toward 1b, at this time, it jets out into the solid particle layer 23 from the ventilation hole of the perforated plate 22 provided in the casing 21. By the jet of the exhaust gas, the solid particle layer 23 is vigorously stirred and heated to be in a fluidized state, and a so-called fluidized bed is formed. On the other hand, the two parallel portions of the heat transfer tube 24 are both in and in contact with this fluidized bed, and the water flowing into the heat transfer tube 24 from the water intake passage 25 passes through the heat transfer tube 24. Meanwhile, after being heated by the fluidized bed, it flows out from the water extraction passage 26 and circulates in the hot water or steam circulation system of the boiler.
【0004】上記流動層式熱交換器を長時間稼動する
と、その間に排ガス中に含まれている煤やダストが、前
記多孔板22の下面に付着して通気孔を塞ぎ排ガスの流
通を阻害する。そこで、前記クリーニング装置28を図
5に示すように作動させて多孔板22の下面を清掃して
いる。しかしながら、前記ブラシを装着した回動式のク
リーニング装置28では次のような問題がある。 (1) ブラシの変形により多孔板の通気孔にブラシ先端
部が噛み込み、排ガス脈動のためブラシの脱落や作動不
能等が発生する。 (2) 構造上、多孔板下面全域の清掃ができない。 (3) 1本のブラシを作動して清掃するので稼動範囲が
大きく、ブラシの作動開始時におけるブラシ移動部に排
ガスが集中し、固体粒子層の流動不良や固体粒子の飛散
等の問題が発生する。 (4) ブラシの停止部分は排ガスの流れが阻害され固体
粒子層の流動不良部が発生する。When the fluidized bed heat exchanger is operated for a long time, soot and dust contained in the exhaust gas during that time adhere to the lower surface of the porous plate 22 to block the ventilation holes and hinder the flow of the exhaust gas. . Therefore, the cleaning device 28 is operated as shown in FIG. 5 to clean the lower surface of the perforated plate 22. However, the rotary cleaning device 28 equipped with the brush has the following problems. (1) The tip of the brush is caught in the ventilation hole of the perforated plate due to the deformation of the brush, and the pulsation of the exhaust gas causes the brush to drop or become inoperable. (2) Due to the structure, the entire lower surface of the perforated plate cannot be cleaned. (3) Since one brush is operated and cleaned, the operating range is large, and exhaust gas concentrates on the brush moving part at the start of brush operation, causing problems such as poor flow of the solid particle layer and scattering of solid particles. To do. (4) The flow of exhaust gas is obstructed at the stopping portion of the brush, and a poor flow portion of the solid particle layer occurs.
【0005】[0005]
【発明が解決しようとする課題】この発明は、上述した
従来の回動式クリーニング装置の問題点を解決できる流
動層式熱交換器の多孔板クリーニング装置を提供するこ
とを目的とするものである。SUMMARY OF THE INVENTION It is an object of the present invention to provide a perforated plate cleaning device for a fluidized bed heat exchanger which can solve the above-mentioned problems of the conventional rotary cleaning device. .
【0006】[0006]
【課題を解決するための手段】この発明は、上記課題を
解決するためになされたものであって、請求項1の発明
は、排ガス入口と排ガス出口を備えたケーシング内の略
中央部に、多数の通気孔を有する多孔板を設け、この多
孔板上に固体粒子からなる適当な厚さの固体粒子層を形
成し、該固体粒子層内に伝熱管を挿入して排熱を回収す
る流動層式熱交換器において、前記多孔板の下部に複数
のノズルを有する高圧空気吐出管を単数または複数設
け、この高圧空気吐出管に高圧空気を提供する高圧空気
供給路を接続し、この高圧空気供給路に電磁弁を設けた
ことを特徴とし、請求項2の発明は、前記高圧空気吐出
管を回動自在に設けたことを特徴とし、請求項3の発明
は、前記高圧空気吐出管を軸方向に摺動自在に設けたこ
とを特徴としている。SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and the invention of claim 1 is such that a substantially central portion in a casing having an exhaust gas inlet and an exhaust gas outlet is provided. A flow for providing a perforated plate having a large number of ventilation holes, forming a solid particle layer of solid particles on the perforated plate with an appropriate thickness, and inserting a heat transfer tube into the solid particle layer to recover exhaust heat In the layered heat exchanger, one or more high-pressure air discharge pipes having a plurality of nozzles are provided below the perforated plate, and a high-pressure air supply path for supplying high-pressure air is connected to the high-pressure air discharge pipes. An electromagnetic valve is provided in the supply passage, the invention of claim 2 is characterized in that the high-pressure air discharge pipe is rotatably provided, and the invention of claim 3 is characterized in that the high-pressure air discharge pipe is provided. Characterized by being provided so as to be slidable in the axial direction
【0007】[0007]
【作用】この発明によれば、多孔板の下面に設けた高圧
空気吐出管のノズルより高圧空気を吹きつけて、多孔板
下面に付着した煤やダストを除去する。According to the present invention, high pressure air is blown from the nozzle of the high pressure air discharge pipe provided on the lower surface of the perforated plate to remove soot and dust adhering to the lower surface of the perforated plate.
【0008】[0008]
【実施例】以下、この発明の実施例を図面に基づいて詳
細に説明する。図1は、この発明を実施した流動層式熱
交換器の各機器の配置を示す第1実施例の概略説明図で
ある。図中1は、排ガス入口1aと排ガス出口1bを備
えたケーシング、2は、前記ケーシング1の略中央部に
設けた多数の通気孔を有する多孔板である。前記多孔板
2上に固体粒子(例えば硅砂)からなる適当な厚さの固
体粒子層3を形成している。4は、略U字状のパイプか
らなる被加熱流体としての水を移送する伝熱管であっ
て、U字状の一方の平行部を前記固体粒子層3内に挿入
し、他方の平行部は前記固体粒子層3の上方に配置して
いる。5は、前記伝熱管4の平行部に付着したフィンで
あって、熱交換効率を向上させている。6は水取入路、
7は水取出路であって、それぞれ前記伝熱管4に接続
し、他端はボイラの温水または蒸気循環系等に接続され
ている。8は、バッフル板で排ガスの流入により飛散す
る固体粒子の流出を防止する。Embodiments of the present invention will be described below in detail with reference to the drawings. FIG. 1 is a schematic explanatory view of a first embodiment showing the arrangement of each device of a fluidized bed heat exchanger embodying the present invention. In the figure, 1 is a casing provided with an exhaust gas inlet 1a and an exhaust gas outlet 1b, and 2 is a perforated plate having a large number of vent holes provided in a substantially central portion of the casing 1. A solid particle layer 3 made of solid particles (for example, silica sand) and having an appropriate thickness is formed on the porous plate 2. Reference numeral 4 denotes a heat transfer tube made of a substantially U-shaped pipe for transferring water as a fluid to be heated. One parallel part of the U-shape is inserted into the solid particle layer 3 and the other parallel part is It is arranged above the solid particle layer 3. Reference numeral 5 is a fin attached to the parallel portion of the heat transfer tube 4 to improve heat exchange efficiency. 6 is a water intake path,
Reference numeral 7 is a water take-out path, which is connected to the heat transfer tubes 4 and has the other end connected to hot water of the boiler or a steam circulation system. 8 is a baffle plate which prevents the outflow of solid particles scattered by the inflow of exhaust gas.
【0009】この発明に係る多孔板クリーニング装置
は、図1〜2に示すように、前記多孔板2の下面近傍に
複数のノズル9aを有する高圧空気吐出管9を複数併設
し、この複数の高圧空気吐出管9のそれぞれの一端面を
封止するとともに他端面に両端面を封止した連絡管10
を接続し、この連結管10に高圧空気を供給する高圧空
気供給路11を接続し、この高圧空気供給路11の途中
にクイックオープン型電磁弁12を挿入し、他端は図示
省略のコンプレッサに接続している。As shown in FIGS. 1 and 2, the perforated plate cleaning apparatus according to the present invention is provided with a plurality of high pressure air discharge pipes 9 having a plurality of nozzles 9a in the vicinity of the lower surface of the perforated plate 2. Communication pipe 10 in which one end face of each air discharge pipe 9 is sealed and both end faces are sealed in the other end face
And a high pressure air supply path 11 for supplying high pressure air to the connecting pipe 10, a quick open solenoid valve 12 is inserted in the middle of the high pressure air supply path 11, and the other end is connected to a compressor not shown. Connected.
【0010】つぎに、前記構成の流動層式熱交換器の作
用を説明する。前記ケーシング1の排ガス入口1aに、
排ガス供給源(ディーゼルエンジン等)に接続してある
排気ダクト(図示省略)から高熱の排ガスが流入する。
この流入した高熱の排ガスは、排ガス入口1aから排ガ
ス出口1bに向って通過するが、このとき、ケーシング
1内に設けた多孔板2の通気孔から固体粒子層3内へ噴
出する。この排気ガスの噴出によって、前記固体粒子層
3が激しく攪拌および加熱されて流動状態となり、いわ
ゆる流動層が形成される。一方、伝熱管4の2つの平行
部は共にこの流動層内にあって、これと接触しており、
前記水取入路6から伝熱管4内に流入した水が、伝熱管
4内を通過しながら流動層によって加熱された後、水取
出路7から流出し、ボイラの温水または蒸気循環系内を
循環する。Next, the operation of the fluidized bed heat exchanger having the above construction will be described. At the exhaust gas inlet 1a of the casing 1,
High-heat exhaust gas flows from an exhaust duct (not shown) connected to an exhaust gas supply source (diesel engine or the like).
The inflowing high-heat exhaust gas passes from the exhaust gas inlet 1a toward the exhaust gas outlet 1b, but at this time, it is ejected into the solid particle layer 3 from the ventilation hole of the perforated plate 2 provided in the casing 1. Due to the jet of the exhaust gas, the solid particle layer 3 is vigorously stirred and heated to be in a fluidized state, so that a so-called fluidized bed is formed. On the other hand, the two parallel portions of the heat transfer tube 4 are both in this fluidized bed and are in contact therewith,
The water that has flowed into the heat transfer tube 4 from the water intake path 6 is heated by the fluidized bed while passing through the heat transfer tube 4, and then flows out from the water extraction path 7 to flow in the hot water or steam circulation system of the boiler. Circulate.
【0011】前記流動層式熱交換器を長時間連続運転す
ると、排ガス中の煤やダストが前記多孔板2の下面に付
着し通気孔を塞ぎ排ガスの流通を阻害するので、予め設
定した運転時間に基づき前記高圧空気供給路11の電磁
弁12を所定時間開弁する。電磁弁12を開弁すること
により、高圧空気を前記連絡管10を介してそれぞれの
高圧空気吐出管9のノズル9aより多孔板2の下面全体
に吹きつけ、付着している煤やダストを除去して通気孔
の流通をよくする。When the fluidized bed heat exchanger is continuously operated for a long time, soot and dust in the exhaust gas adhere to the lower surface of the perforated plate 2 to block the ventilation holes and hinder the flow of the exhaust gas. Based on the above, the solenoid valve 12 of the high pressure air supply path 11 is opened for a predetermined time. By opening the solenoid valve 12, high pressure air is blown to the entire lower surface of the perforated plate 2 from the nozzles 9a of the respective high pressure air discharge pipes 9 through the communication pipes 10 to remove soot and dust adhering thereto. And improve the circulation of the ventilation holes.
【0012】つぎに、第2実施例を図3により説明す
る。尚、第1実施例と共通する部材には同一番号を付し
重複する説明は省略する。図3に示す第2実施例は、前
記多孔板2の下面近傍の前記ケーシング1内の両側壁
(この実施例は伝熱管4に平行)に軸受部13を設け、
この軸受部13に複数のノズル9aを有する高圧空気吐
出管9の両端部を回動自在に挿入し、この高圧空気吐出
管9の一方の端面を封止し、この端面に図示省略の回動
手段(自動又は手動)を設けるとともに、他方の端面に
は高圧空気を供給する高圧空気供給路11を接続してい
る。Next, a second embodiment will be described with reference to FIG. The same members as those in the first embodiment are designated by the same reference numerals, and the duplicated description will be omitted. In the second embodiment shown in FIG. 3, bearing portions 13 are provided on both side walls (in this embodiment, parallel to the heat transfer tube 4) in the casing 1 near the lower surface of the perforated plate 2.
Both ends of a high-pressure air discharge pipe 9 having a plurality of nozzles 9a are rotatably inserted into the bearing portion 13, one end face of the high-pressure air discharge pipe 9 is sealed, and a rotation (not shown) is provided on this end face. Means (automatic or manual) are provided, and a high pressure air supply path 11 for supplying high pressure air is connected to the other end surface.
【0013】図3に示す第2実施例の作用は、第1実施
例に示す実施例と同様に、予め設定した運転時間に基づ
き前記高圧空気供給路11の電磁弁12を所定時間開弁
し、この電磁弁12の開弁に連動して前記高圧空気吐出
管9を前記回動手段を介して所定角度間を回動させる。
高圧空気吐出管9を回動させることにより高圧空気をノ
ズル9aより多孔板2の下面全体に吹きつけ、付着して
いる煤やダストを除去して通気孔の流通をよくすること
ができる。The operation of the second embodiment shown in FIG. 3 is similar to that of the first embodiment, in which the solenoid valve 12 of the high-pressure air supply passage 11 is opened for a predetermined time based on a preset operating time. The high-pressure air discharge pipe 9 is rotated through a predetermined angle in conjunction with the opening of the electromagnetic valve 12.
By rotating the high-pressure air discharge pipe 9, high-pressure air is blown from the nozzle 9a onto the entire lower surface of the porous plate 2, soot and dust adhering to the high-pressure air can be removed to improve the circulation of the ventilation holes.
【0014】つぎに、第3実施例を図4により説明す
る。尚、第1実施例および第2実施例と共通する部材に
は同一番号を付し重複する説明は省略する。図4に示す
第3実施例は、前記多孔板2の下面近傍の前記ケーシン
グ1内の両側壁(この実施例は伝熱管4に平行)に軸受
部13を設け、この軸受部13に複数のノズル9aを有
する高圧空気吐出管9を前記両側壁を貫通するように摺
動自在に挿入し、この高圧空気吐出管9の一方の端面を
封止し、この端部に図示省略のスライド手段(自動又は
手動)を設けるとともに、他方の端面には高圧空気を供
給する高圧空気供給路11を摺動自在に接続し、この高
圧空気供給路11の途中にクイックオープン型電磁弁1
2を挿入し、他端は図示省略のコンプレッサに接続して
いる。Next, a third embodiment will be described with reference to FIG. The same members as those in the first and second embodiments are designated by the same reference numerals, and the duplicated description will be omitted. In the third embodiment shown in FIG. 4, bearing portions 13 are provided on both side walls (in this embodiment parallel to the heat transfer tube 4) in the casing 1 near the lower surface of the perforated plate 2, and a plurality of bearing portions 13 are provided in the bearing portion 13. A high-pressure air discharge pipe 9 having a nozzle 9a is slidably inserted so as to penetrate the both side walls, one end surface of the high-pressure air discharge pipe 9 is sealed, and a slide means (not shown) is attached to this end portion. A high-pressure air supply path 11 for supplying high-pressure air is slidably connected to the other end surface of the quick-open solenoid valve 1 in the middle of the high-pressure air supply path 11.
2 is inserted and the other end is connected to a compressor (not shown).
【0015】図4に示す第3実施例の作用は、第1実施
例および第2実施例と同様に、予め設定した運転時間に
基づき前記高圧空気供給路11の電磁弁12を所定時間
開弁し、この電磁弁12の開弁に連動して前記高圧空気
吐出管9を前記スライド手段を介して所定寸法間を往復
摺動させる。高圧空気吐出管9を往復摺動させることに
より高圧空気をノズル9aより多孔板2の下面全体に吹
きつけ、付着している煤やダストを除去して通気孔の流
通をよくすることができる。The operation of the third embodiment shown in FIG. 4 is, similar to the first and second embodiments, that the solenoid valve 12 of the high pressure air supply passage 11 is opened for a predetermined time based on a preset operating time. Then, interlocking with the opening of the solenoid valve 12, the high-pressure air discharge pipe 9 is slid back and forth between the predetermined dimensions through the slide means. By moving the high-pressure air discharge pipe 9 back and forth, high-pressure air is blown from the nozzle 9a onto the entire lower surface of the porous plate 2, soot and dust adhering to the high-pressure air can be removed to improve the circulation of the ventilation holes.
【0016】前記実施例において、前記高圧空気吐出管
9に関して、固定方式、回動方式、摺動方式について説
明したが、この発明は、前記実施例に限定されるもので
はなく、例えば、回動方式と摺動方式を組合せることに
より、前記高圧空気吐出管9を回動しながら摺動させ、
よりクリーニング効果を上げることができる。したがっ
て、実施に応じ適宜選択あるいは組合せることができ
る。In the above embodiment, the fixing system, the rotating system, and the sliding system were described for the high-pressure air discharge pipe 9, but the present invention is not limited to the above embodiment, and for example, the rotating system can be used. By combining the method and the sliding method, the high pressure air discharge pipe 9 is slid while rotating,
The cleaning effect can be improved. Therefore, they can be appropriately selected or combined depending on the implementation.
【0017】[0017]
【発明の効果】以上説明したように、この発明は、流動
層式熱交換器の多孔板の下部に複数のノズルを備えた高
圧空気吐出管を複数設け、この高圧空気吐出管に高圧空
気を供給する高圧空気供給路を接続して、多孔板下面に
高圧空気を吹きつけるようにしたので、多孔板の下面に
付着する煤やダストを除去し、通気孔の流通をよくする
ことができる。したがって、従来のように、多孔板下面
の清掃不充分や排ガス流通阻害等を解消し、効率よく熱
交換することができる。また、従来のブラシ式クリーニ
ング装置に比し、多孔板下部の高さが構造上短くできる
ので、装置全体を小型化することができる。As described above, according to the present invention, a plurality of high pressure air discharge pipes provided with a plurality of nozzles are provided below the porous plate of the fluidized bed heat exchanger, and high pressure air discharge pipes are provided with high pressure air. Since the high-pressure air supply path for supply is connected to blow the high-pressure air to the lower surface of the perforated plate, soot and dust adhering to the lower surface of the perforated plate can be removed and the circulation of the ventilation holes can be improved. Therefore, it is possible to eliminate the insufficient cleaning of the lower surface of the perforated plate, the obstruction of exhaust gas flow, etc., as in the conventional case, and to efficiently perform heat exchange. Further, the height of the lower part of the perforated plate can be made structurally shorter than that of the conventional brush type cleaning device, so that the entire device can be downsized.
【図1】この発明を実施した流動層式熱交換器の各機器
の配置を示す第1実施例の概略説明図である。FIG. 1 is a schematic explanatory view of a first embodiment showing an arrangement of respective devices of a fluidized bed heat exchanger embodying the present invention.
【図2】図1のA−A面を断面して示す概略説明図であ
る。FIG. 2 is a schematic explanatory view showing a cross section taken along the line AA of FIG.
【図3】この発明の第2実施例を示す概略説明図であ
る。FIG. 3 is a schematic explanatory view showing a second embodiment of the present invention.
【図4】この発明の第3実施例を示す概略説明図であ
る。FIG. 4 is a schematic explanatory view showing a third embodiment of the present invention.
【図5】従来の流動層式熱交換器の各機器の配置を示す
概略説明図である。FIG. 5 is a schematic explanatory view showing an arrangement of each device of a conventional fluidized bed heat exchanger.
【図6】図5のB−B面を断面して示す概略説明図であ
る。6 is a schematic explanatory view showing a cross section taken along the line BB of FIG.
1 ケーシング 1a 排ガス入口 1b 排ガス出口 2 多孔板 3 固体粒子層 4 伝熱管 9 高圧空気吐出管 9a ノズル 11 高圧空気供給路 12 電磁弁 1 Casing 1a Exhaust Gas Inlet 1b Exhaust Gas Outlet 2 Perforated Plate 3 Solid Particle Layer 4 Heat Transfer Tube 9 High Pressure Air Discharge Pipe 9a Nozzle 11 High Pressure Air Supply Channel 12 Solenoid Valve
Claims (3)
たケーシング1内の略中央部に、多数の通気孔を有する
多孔板2を設け、この多孔板2上に固体粒子からなる適
当な厚さの固体粒子層3を形成し、該固体粒子層3内に
伝熱管4を挿入した流動層式熱交換器において、前記多
孔板2の下部に複数のノズル9aを有する高圧空気吐出
管9を単数または複数設け、この高圧空気吐出管9に高
圧空気を供給する高圧空気供給路11を接続し、この高
圧空気供給路11に電磁弁12を設けたことを特徴とす
る流動層式熱交換器の多孔板クリーニング装置。1. A perforated plate 2 having a large number of ventilation holes is provided at a substantially central portion in a casing 1 having an exhaust gas inlet 1a and an exhaust gas outlet 1b, and an appropriate thickness of solid particles is provided on the perforated plate 2. In the fluidized bed heat exchanger in which the solid particle layer 3 is formed and the heat transfer tube 4 is inserted in the solid particle layer 3, a single high pressure air discharge tube 9 having a plurality of nozzles 9a at the bottom of the porous plate 2 is provided. Alternatively, a high-pressure air supply passage 11 for supplying high-pressure air is connected to the high-pressure air discharge pipe 9, and a solenoid valve 12 is provided in the high-pressure air supply passage 11, which is a fluidized bed heat exchanger. Perforated plate cleaning device.
たことを特徴とする請求項1に記載の流動層式熱交換器
の多孔板クリーニング装置。2. The perforated plate cleaning device for a fluidized bed heat exchanger according to claim 1, wherein the high-pressure air discharge pipe 9 is rotatably provided.
在に設けたことを特徴とする請求項1に記載の流動層式
熱交換器の多孔板クリーニング装置。3. The perforated plate cleaning device for a fluidized bed heat exchanger according to claim 1, wherein the high-pressure air discharge pipe 9 is provided slidably in the axial direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6163190A JP2768272B2 (en) | 1994-06-21 | 1994-06-21 | Perforated plate cleaning device for fluidized bed heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6163190A JP2768272B2 (en) | 1994-06-21 | 1994-06-21 | Perforated plate cleaning device for fluidized bed heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH085013A true JPH085013A (en) | 1996-01-12 |
| JP2768272B2 JP2768272B2 (en) | 1998-06-25 |
Family
ID=15768983
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6163190A Expired - Lifetime JP2768272B2 (en) | 1994-06-21 | 1994-06-21 | Perforated plate cleaning device for fluidized bed heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2768272B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6595094B1 (en) | 1999-01-29 | 2003-07-22 | Sumitomo Special Metals Co., Ltd. | Working cutting apparatus and method for cutting work |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63148070U (en) * | 1987-03-17 | 1988-09-29 | ||
| JPH02106594U (en) * | 1989-02-14 | 1990-08-24 |
-
1994
- 1994-06-21 JP JP6163190A patent/JP2768272B2/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63148070U (en) * | 1987-03-17 | 1988-09-29 | ||
| JPH02106594U (en) * | 1989-02-14 | 1990-08-24 |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6595094B1 (en) | 1999-01-29 | 2003-07-22 | Sumitomo Special Metals Co., Ltd. | Working cutting apparatus and method for cutting work |
| US6889586B2 (en) | 1999-01-29 | 2005-05-10 | Neomax Co., Ltd. | Work cutting apparatus and method for cutting work |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2768272B2 (en) | 1998-06-25 |
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