JPS58200994A - Dispersing plate for fluidized-bed heat exchanger - Google Patents

Dispersing plate for fluidized-bed heat exchanger

Info

Publication number
JPS58200994A
JPS58200994A JP8316682A JP8316682A JPS58200994A JP S58200994 A JPS58200994 A JP S58200994A JP 8316682 A JP8316682 A JP 8316682A JP 8316682 A JP8316682 A JP 8316682A JP S58200994 A JPS58200994 A JP S58200994A
Authority
JP
Japan
Prior art keywords
openings
plate
heat
state
fluidized
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
Application number
JP8316682A
Other languages
Japanese (ja)
Inventor
Kenichi Hashizume
健一 橋詰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Original Assignee
Toshiba Corp
Tokyo Shibaura Electric Co Ltd
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 by Toshiba Corp, Tokyo Shibaura Electric Co Ltd filed Critical Toshiba Corp
Priority to JP8316682A priority Critical patent/JPS58200994A/en
Publication of JPS58200994A publication Critical patent/JPS58200994A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D13/00Heat-exchange apparatus using a fluidised bed

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)

Abstract

PURPOSE:To keep the state of a flow, in which grains are under an excellent state, by constituting the dispersing plate for the fluidized-bed heat exchanger by a porous plate with openings larger than grain size and a gauze, the openings of meshes thereof are small, in heat recovery for an industrial waste gas, etc. CONSTITUTION:A high-temperature waste gas (a) brings grains on the openings 10 of the dispersing plate 3 to a fluidized state as jets, and exchanges heat with a medium to be heat-exchanged through a heat-transfer pipe in a grain layer. The dispersing plate 3 consists of the porous plate 11 with a large number of conical projections 9 and having the openings 10, diameters thereof are larger than grain size, at the centers and the gauze 12, the openings of meshes thereof are smaller than grain size, and the outer circumference 13 of the plate 3 is welded to the porous plate 11. Accordingly, clogging is not generated in the openings of the porous plate, and a gas ejected from the openings passes through concave sections 14 among the projections and is ejected from sections not clogged even when clogging is generated partially in the gauze, thus keeping the state of the flow in which grains are under the excellent state, hence no lowering in the performance of heat transfer.

Description

【発明の詳細な説明】 〔発明の属する技術分野〕 本発明は流動床熱交換器の分散板に関する。[Detailed description of the invention] [Technical field to which the invention pertains] The present invention relates to a distribution plate for a fluidized bed heat exchanger.

〔発明の技術的背景とその問題点〕[Technical background of the invention and its problems]

近年の省エネルギ化への社会的な要蛸の中で、従来大気
中に捨てられていた工場廃ガスや内燃機関の廃ガスから
の熱回収が着目されている。これらの廃ガスは一般には
腐食性物質を含むなど低質でiす、その保有する熱を有
効に回収するだめの熱交換器としては、高い熱伝達率と
共に、常に伝熱面が粒子で清浄に保たれているという特
徴を有する流動床熱交換器が有望とされている、以下第
1図を引用しながら従来技術と問題点を説明する。
In recent years, amid the social imperative for energy conservation, attention has been paid to the recovery of heat from factory waste gas and internal combustion engine waste gas, which had previously been discarded into the atmosphere. These waste gases are generally of low quality, including corrosive substances.A heat exchanger that can effectively recover the heat contained in this waste gas must have a high heat transfer coefficient and a heat transfer surface that is always clean with particles. A fluidized bed heat exchanger is considered to be promising because it has the characteristic of maintaining the same temperature.The conventional technology and problems will be explained below with reference to FIG.

工場や内燃機関などからの高温の廃ガス(a)はガス入
口ノズル(1)からウィンドボックス(2)内に流入し
、分数板(3)に設けられている開孔(4)からジェッ
トとなって粒子(5)の層に噴出する。粒子(5)はこ
の噴流により流動状態を呈し、粒子の層内に埋設さねて
いる伝熱管(6)の中を流れる熱交換媒体(b)に有効
に熱を伝達する。熱交換を終えて温度が低下した廃ガス
は空塔部(7)を経て、ガス出口ノズル(8)から流出
して大気に放出される。熱交換媒体(b)としては通常
は水が用いられ、伝熱管の中で蒸発して水蒸気となって
プロセススチーム、発電、暖房。
High-temperature waste gas (a) from factories, internal combustion engines, etc. flows into the wind box (2) through the gas inlet nozzle (1), and is jetted through the opening (4) provided in the fraction plate (3). and ejects into a layer of particles (5). The particles (5) assume a fluid state due to this jet and effectively transfer heat to the heat exchange medium (b) flowing in the heat transfer tubes (6) embedded within the layer of particles. After completing the heat exchange, the waste gas whose temperature has decreased passes through the empty column section (7), flows out from the gas outlet nozzle (8), and is discharged into the atmosphere. Water is usually used as the heat exchange medium (b), and it evaporates in heat transfer tubes to become water vapor, which is used for process steam, power generation, and space heating.

吸収式冷凍機駆動などに利用される。あるいは伝熱管の
中で蒸発せずに単なる漏水として暖房や給湯などに利用
されることもおる。
Used to drive absorption refrigerators, etc. Alternatively, water may not evaporate in the heat transfer tubes and may simply leak water and be used for heating, hot water supply, etc.

以上説明した従来技術においては、分散板(3)の開孔
(4)の直径は粒子の層を保持するために粒子(5)の
直径よりも小さくなければならない。粒子の直径は通常
05〜2s+s+が多く用いられるが、これよりも小さ
い開孔では孔がつまり易く、多数の開孔の一部がつまっ
てしまえば粒子の良好な流動状態は得られなくなり、そ
の結果廃ガスと熱交換媒体との間の伝熱効果が低下して
しまうという問題点がめった。
In the prior art described above, the diameter of the apertures (4) in the dispersion plate (3) must be smaller than the diameter of the particles (5) in order to retain the layer of particles. The diameter of the particles is usually 05~2s+s+, but if the pores are smaller than this, the pores are likely to clog, and if some of the many pores become clogged, it will not be possible to obtain a good fluidity state of the particles. As a result, a problem occurred in that the heat transfer effect between the waste gas and the heat exchange medium was reduced.

〔発明の目的〕[Purpose of the invention]

本発明の目的は目づやすの起こりKくい分散板を提供す
ることであり、粒子の直径より目開きの小さい金網と、
その下に置かれた粒子より直径の大きな開孔を有する多
孔板から成る分散板によって上記問題点を解決すること
にある。
An object of the present invention is to provide a K-shaped dispersion plate that causes pores, which includes a wire mesh with a mesh size smaller than the diameter of the particles;
The object of the present invention is to solve the above-mentioned problems by using a dispersion plate consisting of a perforated plate having apertures having a diameter larger than that of the particles placed therebelow.

〔発明の概要〕[Summary of the invention]

、 本発明は粒子径より大きな直径の開孔を有する゛ 
多孔板と、上記粒子径よりも目開きの小さな金網とから
なる流動床熱交換器の分散板である。
, the present invention has pores with a diameter larger than the particle size.
This is a dispersion plate for a fluidized bed heat exchanger consisting of a perforated plate and a wire mesh with a mesh size smaller than the above particle size.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、伝熱性能の低下を招くことがなく、粒
子の良好な流動状態を保つことができる。
According to the present invention, a favorable fluid state of particles can be maintained without causing a decrease in heat transfer performance.

〔発明の実施例〕[Embodiments of the invention]

以下本発明の実施例を第2図、第3図を引用しながら説
明する。
Embodiments of the present invention will be described below with reference to FIGS. 2 and 3.

第2図は本発明による分散板を示したものであ粒子径よ
シも大きな直径の開孔ααを有する多孔板θUと、粒子
径より小さい目開きの金網aりとから成る。第3図は第
2図を上から見た部分図である。
FIG. 2 shows a dispersion plate according to the present invention, which is composed of a perforated plate θU having openings αα having a diameter larger than the particle diameter, and a wire mesh a having apertures smaller than the particle diameter. FIG. 3 is a partial view of FIG. 2 viewed from above.

ここで金網a3の外周は多孔板allK溶接(112図
および第3図の接合部分α3)されている。
Here, the outer periphery of the wire mesh a3 is welded to a perforated plate all K (joint portion α3 in FIG. 112 and FIG. 3).

本発明による分散板では粒子を保持する機能を金網が受
は持つので多孔板の開孔直径を粒子径より大きくできて
、開孔の目づまシが起こらない。
In the dispersion plate according to the present invention, since the wire mesh has the function of holding the particles, the aperture diameter of the perforated plate can be made larger than the particle diameter, and clogging of the apertures does not occur.

また、万一金網で部分的に目づまりが起こったとしても
開孔から噴出するガスは突起間の凹部α4を通って、金
網の目づまりの起っていない部分から噴出することがで
きるので、粒子の良好な流動状態が保たれ、伝熱性能の
低下を招くことは避けられる。
In addition, even if the wire mesh becomes partially clogged, the gas ejected from the openings can pass through the recess α4 between the protrusions and eject from the unclogged portion of the wire mesh. A good fluid state is maintained, and deterioration in heat transfer performance is avoided.

第2図および第3図に示した本発明による分散板は、プ
レス加工で容易に製作できる多孔板と広く市場に出まわ
っている通常の金網とから成っているので特に、小型の
大量生産機種に対しての適用が有効である。
The dispersion plate according to the present invention shown in FIGS. 2 and 3 is composed of a perforated plate that can be easily manufactured by press working and an ordinary wire mesh that is widely available on the market, so it is particularly suitable for small mass-produced models. It is effective to apply to

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

第1図は従来の流動床熱交換器を示す図、第2図は本発
明による分散板の一実施例を示十図、第3図は第2図を
上から見た部分図である。 10・・・開孔   11・・・多孔板   12・・
金網(7317)代理人弁理士  則 近 憲 佑(ほ
か1名)W4211!1 第  1 因
FIG. 1 is a diagram showing a conventional fluidized bed heat exchanger, FIG. 2 is a diagram showing an embodiment of a distribution plate according to the present invention, and FIG. 3 is a partial view of FIG. 2 viewed from above. 10... Open hole 11... Perforated plate 12...
Chainlink (7317) Representative Patent Attorney Noriyuki Noriyuki (and 1 other person) W4211!1 1st cause

Claims (1)

【特許請求の範囲】[Claims] 粒子径よシ大きな直径の開孔を有する多孔板と、前記粒
子径よシも目開きの小さな金網とから成る流動床熱交換
器の分散板。
A dispersion plate for a fluidized bed heat exchanger, comprising a perforated plate having openings with a diameter larger than the particle size, and a wire mesh having a smaller opening than the particle size.
JP8316682A 1982-05-19 1982-05-19 Dispersing plate for fluidized-bed heat exchanger Pending JPS58200994A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8316682A JPS58200994A (en) 1982-05-19 1982-05-19 Dispersing plate for fluidized-bed heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8316682A JPS58200994A (en) 1982-05-19 1982-05-19 Dispersing plate for fluidized-bed heat exchanger

Publications (1)

Publication Number Publication Date
JPS58200994A true JPS58200994A (en) 1983-11-22

Family

ID=13794675

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8316682A Pending JPS58200994A (en) 1982-05-19 1982-05-19 Dispersing plate for fluidized-bed heat exchanger

Country Status (1)

Country Link
JP (1) JPS58200994A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6217595A (en) * 1985-03-22 1987-01-26 Mayekawa Mfg Co Ltd Air jet injector

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6217595A (en) * 1985-03-22 1987-01-26 Mayekawa Mfg Co Ltd Air jet injector
JPH0467111B2 (en) * 1985-03-22 1992-10-27 Maekawa Seisakusho Kk

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