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JPH0733957B2 - Particle circulation heat exchange method - Google Patents
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JPH0733957B2 - Particle circulation heat exchange method - Google Patents

Particle circulation heat exchange method

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Publication number
JPH0733957B2
JPH0733957B2 JP62048541A JP4854187A JPH0733957B2 JP H0733957 B2 JPH0733957 B2 JP H0733957B2 JP 62048541 A JP62048541 A JP 62048541A JP 4854187 A JP4854187 A JP 4854187A JP H0733957 B2 JPH0733957 B2 JP H0733957B2
Authority
JP
Japan
Prior art keywords
air
circulating particles
particles
heat
circulating
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
Application number
JP62048541A
Other languages
Japanese (ja)
Other versions
JPS63213795A (en
Inventor
洋 武内
利昌 平間
惣吾 佐山
秀敏 青木
Original Assignee
工業技術院長
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 工業技術院長 filed Critical 工業技術院長
Priority to JP62048541A priority Critical patent/JPH0733957B2/en
Publication of JPS63213795A publication Critical patent/JPS63213795A/en
Publication of JPH0733957B2 publication Critical patent/JPH0733957B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、大気から採熱する熱交換方法に関し、さらに
詳しくは、外気温が氷点下になるような寒冷地の大気か
ら採熱する場合に好適な、粒子循環式熱交換方法に関す
るものである。
Description: TECHNICAL FIELD The present invention relates to a heat exchange method for collecting heat from the atmosphere, and more specifically, when collecting heat from the atmosphere in a cold region where the outside air temperature is below freezing. The present invention relates to a suitable particle circulation heat exchange method.

〔従来の技術及びその問題点〕[Conventional technology and its problems]

外気温が氷点下になるような寒冷地では、一般に用いら
れているフィンチューブタイプの大気採熱熱交換器を使
用すると、伝熱面に着霜し採熱が不能になる。このた
め、間欠的に伝熱面に熱を加えて除霜しているが、この
場合エネルギー効率の低下はさけられない。
In a cold region where the outside air temperature is below freezing, if a fin-tube type heat collecting heat exchanger that is generally used is used, the heat transfer surface is frosted and heat cannot be collected. For this reason, heat is intermittently applied to the heat transfer surface for defrosting, but in this case, reduction in energy efficiency cannot be avoided.

また、広く普及している気泡流動層を利用した熱交換方
式による熱交換器を用いて採熱すると、条件によっては
流動化粒子の作用によって着霜が防げるが、空気分散器
を含めた圧力損失が大きくなって、エネルギー的に不利
である。また、気泡流動層では、外気温の変化に伴う負
荷変動に対して十分に応答できないなどの問題もある。
In addition, when heat is collected using a heat exchanger that uses a widely used bubbling fluidized bed heat exchange method, frost formation can be prevented by the action of fluidized particles under some conditions, but pressure loss including the air disperser can be prevented. Is large, which is disadvantageous in terms of energy. Further, the bubbling fluidized bed has a problem that it cannot sufficiently respond to a load change due to a change in outside temperature.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

本発明は、以上のような従来技術の問題点を解決し、外
気温が氷点下になるような寒冷地においても、伝熱面で
の着霜が防止され、かつ圧力損失を低減してエネルギー
効率を向上させることができる熱交換方法を提供するこ
とをその課題とする。
The present invention solves the problems of the conventional techniques as described above, prevents frost formation on the heat transfer surface, reduces pressure loss, and reduces energy efficiency even in cold regions where the outside air temperature is below freezing. It is an object of the present invention to provide a heat exchange method capable of improving the temperature.

〔課題を解決するための手段〕[Means for Solving the Problems]

上記課題を解決するため、本発明によれば、隔壁を隔て
て、空気と循環粒子との混合流が上昇する上昇部と、循
環粒子の移動層とに区画され、その上側にセパレータ及
び空気排出口を備えた空気拡散部を有し、前記移動層内
部に伝熱体を有するとともに前記移動層下方の前記上昇
部との連通部に排出バルブを有し、かつ前記上昇部下方
に空気流入口を有する粒子循環型熱交換器を用い、前記
空気流入口から大気中の空気を、該空気中に供給された
循環粒子が乱流あるいは高速流動化状態となるような高
速の上昇流として取り入れ、循環粒子を前記移動層から
前記排出バルブでその循環量を制御しつつ前記高速の空
気上昇流中に供給し、供給された循環粒子と空気との混
合流との上昇過程で空気と循環粒子との間の熱交換を行
わせ、上昇した循環粒子と空気との混合流を、前記空気
拡散部にて前記セパレータで循環粒子の外部への流出を
防止しながら循環粒子と空気とに分離し、分離した空気
を前記空気排出口より外部に排出するとともに、分離し
た循環粒子を前記移動層に回収し、回収した循環粒子の
熱を前記移動層中に設けた伝熱体で採熱することからな
る粒子循環式熱交換方法が提供される。
In order to solve the above-mentioned problems, according to the present invention, a partition wall is provided between the rising portion where the mixed flow of air and circulating particles rises, and a moving layer of circulating particles, and a separator and air exhaust are provided above the moving portion. An air diffusing section having an outlet, a heat transfer member inside the moving bed, a discharge valve in a communication section with the rising section below the moving bed, and an air inlet port below the rising section. Using a particle circulation type heat exchanger having, the air in the atmosphere from the air inlet is taken in as a high-speed upward flow such that the circulating particles supplied into the air are in a turbulent or high-speed fluidized state, Circulating particles are supplied from the moving bed into the high-speed air rising flow while controlling the circulation amount thereof with the discharge valve, and air and circulating particles are generated in the ascending process of the supplied circulating particles and a mixed flow of air. Heat exchange between The mixed flow of particles and air is separated into circulating particles and air while preventing the circulating particles from flowing out to the outside in the air diffusion unit, and the separated air is discharged to the outside from the air discharge port. In addition, there is provided a particle circulation type heat exchange method comprising collecting the separated circulating particles in the moving bed and collecting the heat of the collected circulating particles by a heat transfer body provided in the moving bed.

〔作用〕[Action]

排出バルブからその循環量を調整して上昇部に供給され
る循環粒子は、空気流入口から取り入れられた高速の空
気により乱流あるいは高速流動化状態を形成して上昇す
る。その過程で空気と循環粒子との間で熱交換が行わ
れ、採熱される。空気と循環粒子の混合流は空気拡散部
で空気と循環粒子とに分離され、循環粒子は移動層に流
入し、空気は空気排出口から外部から排出される。
The circulating particles, which are supplied to the ascending section by adjusting the circulation amount from the discharge valve, rise in a turbulent or high-speed fluidized state due to the high-speed air taken in from the air inlet. In the process, heat is exchanged between the air and the circulating particles to collect heat. The mixed flow of air and circulating particles is separated into air and circulating particles in the air diffusing section, the circulating particles flow into the moving bed, and the air is discharged from the outside through the air outlet.

従って、大きな圧力損失を招く分散器が不要となり、ま
たサイクロン等を用いずに上記空気拡散部により循環粒
子を移動層内へ流入させることによって、熱交換器の圧
力損失を低減できる。
Therefore, a disperser that causes a large pressure loss is not necessary, and the pressure loss of the heat exchanger can be reduced by causing the circulating particles to flow into the moving bed by the air diffusion section without using a cyclone or the like.

移動層に流入した帯熱循環粒子は、排出バルブから上昇
部に排出される粒子循環の量に応じて移動層内を移動す
る間に伝熱体と熱交換する。
The heat-heated circulating particles that have flowed into the moving bed exchange heat with the heat transfer member while moving in the moving bed according to the amount of particle circulation discharged from the discharge valve to the rising portion.

この場合、伝熱体を、着霜の原因となる水蒸気を含む空
気が殆ど存在しない移動層に設けた熱交換器を用いてい
るので、伝熱面での着霜が起こらない。
In this case, since the heat exchanger is provided in the moving bed in which the air containing water vapor that causes frost is hardly present, frost does not occur on the heat transfer surface.

〔実施例〕〔Example〕

第1図は本発明の方法に使用される熱交換器を示し、直
立に設置された熱交換器の本体1は、隔壁2によって区
画された上昇部3と移動層4、及びこれらの上方の空気
拡散部5を備え、本体1の下部には上昇部3に開口する
空気の流入口6が、空気拡散部5の上方には空気の排出
口7がそれぞれ開設されており、これらの開口6、7に
は、後記する循環粒子8の本体外への流出を防止するセ
パレータ9、9が設けられている。
FIG. 1 shows a heat exchanger used in the method of the present invention, in which the body 1 of the heat exchanger installed upright has a rising part 3 and a moving bed 4 which are partitioned by partition walls 2 and above them. An air diffuser 5 is provided, an air inlet 6 opening to the rising portion 3 is provided in the lower portion of the main body 1, and an air outlet 7 is opened above the air diffuser 5, respectively. , 7 are provided with separators 9, 9 for preventing the circulating particles 8 described later from flowing out of the main body.

移動層4は、中間に伝熱体10を、下端に上昇部3の下方
に開口する開口部をそれぞれ有し、該開口部には、循環
粒子8を上昇部3に排出する排出バルブ12が設けられて
いる。
The moving bed 4 has a heat transfer body 10 in the middle and an opening at the lower end that opens below the rising portion 3, and an exhaust valve 12 for discharging the circulating particles 8 to the rising portion 3 is provided in the opening. It is provided.

上記循環粒子8は、衝突や摩擦によって容易に粉砕され
ない固体粒子で形成されており、一方排出バルブ12は粒
子循環量を制御することができるものである。
The circulating particles 8 are formed of solid particles that are not easily crushed by collision or friction, while the discharge valve 12 can control the amount of circulating particles.

第1図中→は空気の流れを、⇒は循環粒子8の流れを示
す。
In FIG. 1, → indicates the flow of air and ⇒ indicates the flow of circulating particles 8.

本発明では、熱交換される空気は、流入口6近傍に設置
されているセパレータ9を通って上昇部3内に高速流と
して供給され、循環粒子8は、排出バルブ12から上昇部
3内に供給される。この場合、空気拡散部5の上部には
セパレータ9が設置されているため、高速な空気流にも
かかわらず、循環粒子8が外部へ流出することはない。
In the present invention, the air to be heat-exchanged is supplied as a high-speed flow into the rising part 3 through the separator 9 installed near the inflow port 6, and the circulating particles 8 are discharged from the discharge valve 12 into the rising part 3. Supplied. In this case, since the separator 9 is installed above the air diffusing unit 5, the circulating particles 8 never flow out to the outside despite the high-speed air flow.

上昇部3に供給された循環粒子は、乱流あるいは高速流
動化状態で空気と激しく混合・熱交換しながら上昇部3
内を上昇して空気拡散部5へ運ばれ、ここで減速されて
空気と分離され移動層4の上部に落下する。一方、空気
は、排出口7から本体外に排出される。
The circulating particles supplied to the rising part 3 are violently mixed and heat-exchanged with air in a turbulent or high-speed fluidized state, and the rising part 3
It rises inside and is carried to the air diffusing section 5, where it is decelerated and separated from the air, and falls onto the moving layer 4. On the other hand, the air is discharged from the discharge port 7 to the outside of the main body.

移動層4に落下した循環粒子8は、排出バルブ12から排
出される循環量に応じて下方のバルブ側に移動し、移動
層4内に設けた伝熱体10に空気からの熱を伝える。
The circulating particles 8 dropped on the moving layer 4 move to the lower valve side according to the circulation amount discharged from the discharge valve 12, and transfer the heat from the air to the heat transfer body 10 provided in the moving layer 4.

上記では、排出バルブ12によって粒子の循環量を調節
し、また空気の流速を変化させることによって上昇部3
における循環粒子8の滞留時間を制御し、これによって
伝熱速度を調節し、外気温の変動に容易に対応可能とな
る。
In the above, by adjusting the circulation amount of the particles by the discharge valve 12 and changing the flow velocity of the air, the rising portion 3
By controlling the residence time of the circulating particles 8 in the above, the heat transfer rate is adjusted by this, and it becomes possible to easily cope with the fluctuation of the outside air temperature.

また、移動層内4内で流れ方向に温度分布がつくので、
伝熱体10内部の流体を向流に流すことにより、交換熱量
を多くすることもできる。
Also, since there is a temperature distribution in the moving direction within the moving bed 4,
The amount of heat exchanged can be increased by causing the fluid inside the heat transfer body 10 to flow countercurrently.

〔発明の効果〕〔The invention's effect〕

本発明によれば、循環粒子を高速の空気流によって乱流
あるいは高速流動化状態として上昇させる過程で空気か
ら採熱するとともに、移動層で伝熱体と熱交換するよう
にしたので、氷点下の温度を有する寒冷地の冬季の大気
からでも、伝熱面への着霜なしに、しかも低い圧力損失
で採熱して、熱交換器のエネルギー効率を向上させるこ
とができる。
According to the present invention, heat is taken from the air in the process of raising the circulating particles as a turbulent flow or a high-speed fluidized state by a high-speed air flow, and heat is exchanged with the heat transfer body in the moving bed. It is possible to improve the energy efficiency of the heat exchanger by collecting heat even from the winter atmosphere of a cold region having a temperature without frost formation on the heat transfer surface and with low pressure loss.

また、循環粒子の循環量あるいは空気の流速を変えるこ
とによって、上昇部での循環粒子の滞留時間を制御する
ことができるので、外気温の変動に容易に対処すること
ができる。
Further, since the residence time of the circulating particles in the rising portion can be controlled by changing the circulating amount of the circulating particles or the flow velocity of the air, it is possible to easily cope with the fluctuation of the outside air temperature.

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

第1図は本発明の方法に使用する熱交換器を示す縦断正
面図である。 3……上昇部、4……移動層 5……空気拡散部、6……空気流入口 7……空気排出口、8……循環粒子 10……伝熱体、12……排出バルブ
FIG. 1 is a vertical sectional front view showing a heat exchanger used in the method of the present invention. 3 ... Ascending part, 4 ... Moving layer 5 ... Air diffusing part, 6 ... Air inlet 7 ... Air outlet, 8 ... Circulating particles 10 ... Heat transfer element, 12 ... Exhaust valve

───────────────────────────────────────────────────── フロントページの続き (72)発明者 佐山 惣吾 北海道札幌市豊平区月寒東二条17丁目2番 1号 工業技術院北海道工業開発試験所内 (72)発明者 青木 秀敏 青森県八戸市大字妙字大開88の1 (56)参考文献 実開 昭58−82845(JP,U) 実開 昭58−116037(JP,U) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Syogo Sayama, Hokkaidou, Sapporo-shi, Hokkaido, Tsukikanto Nijo 17-chome 22-1-1, Hokkaido Industrial Development Laboratory (72) Inventor Hidetoshi Aoki Hachinohe City, Aomori 1 of Daiji 88 (56) Bibliographic Reference Sho 58-82845 (JP, U) Actual 58-116037 (JP, U)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】隔壁を隔てて、空気と循環粒子との混合流
が上昇する上昇部と、循環粒子の移動層とに区画され、
その上側にセパレータ及び空気排出口を備えた空気拡散
部を有し、前記移動層内部に伝熱体を有するとともに前
記移動層下方の前記上昇部との連通部に排出バルブを有
し、かつ前記上昇部下方に空気流入口を有する粒子循環
型熱交換器を用い、 前記空気流入口から大気中の空気を、該空気中に供給さ
れた循環粒子が乱流あるいは高速流動化状態となるよう
な高速の上昇流として取り入れ、 循環粒子を前記移動層から前記排出バルブでその循環量
を制御しつつ前記高速の空気上昇流中に供給し、 供給された循環粒子と空気との混合流との上昇過程で空
気と循環粒子との間の熱交換を行わせ、 上昇した循環粒子と空気との混合流を、前記空気拡散部
にて前記セパレータで循環粒子の外部への流出を防止し
ながら循環粒子と空気とに分離し、 分離した空気を前記空気排出口より外部に排出するとと
もに、分離した循環粒子を前記移動層に回収し、 回収した循環粒子の熱を前記移動層中に設けた伝熱体で
採熱することからなる粒子循環式熱交換方法。
1. A partition wall is divided into an ascending section where a mixed flow of air and circulating particles rises, and a moving layer of circulating particles,
An air diffusion part having a separator and an air discharge port is provided on the upper side thereof, a heat transfer member is provided inside the moving layer, and an exhaust valve is provided at a communication part with the rising part below the moving layer, and Using a particle circulation type heat exchanger having an air inlet below the ascending portion, the air in the atmosphere from the air inlet is such that the circulating particles supplied into the air are in a turbulent or high-speed fluidized state. Taking in as a high-speed upward flow, supplying circulating particles from the moving bed into the high-speed air upward flow while controlling the circulation amount with the discharge valve, and raising the supplied mixed flow of circulating particles and air. The heat exchange between the air and the circulating particles is performed in the process, and the rising mixed flow of the circulating particles and the air is circulated particles while preventing the outflow of the circulating particles to the outside by the separator in the air diffusion section. Separated into air and minutes The collected air is discharged to the outside through the air outlet, the separated circulating particles are collected in the moving bed, and the heat of the collected circulating particles is collected by a heat transfer body provided in the moving bed. Particle circulation heat exchange method.
JP62048541A 1987-03-02 1987-03-02 Particle circulation heat exchange method Expired - Lifetime JPH0733957B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62048541A JPH0733957B2 (en) 1987-03-02 1987-03-02 Particle circulation heat exchange method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62048541A JPH0733957B2 (en) 1987-03-02 1987-03-02 Particle circulation heat exchange method

Publications (2)

Publication Number Publication Date
JPS63213795A JPS63213795A (en) 1988-09-06
JPH0733957B2 true JPH0733957B2 (en) 1995-04-12

Family

ID=12806227

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62048541A Expired - Lifetime JPH0733957B2 (en) 1987-03-02 1987-03-02 Particle circulation heat exchange method

Country Status (1)

Country Link
JP (1) JPH0733957B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2927599B2 (en) * 1992-03-11 1999-07-28 シャープ株式会社 Particle flow heat exchanger
JP2927603B2 (en) * 1992-04-08 1999-07-28 シャープ株式会社 Particle flow heat exchanger

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5882845U (en) * 1981-12-01 1983-06-04 三菱重工業株式会社 Heat recovery device from condensable high temperature gas using solid-gas contact

Also Published As

Publication number Publication date
JPS63213795A (en) 1988-09-06

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