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JP3841691B2 - Heat exchanger - Google Patents
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JP3841691B2 - Heat exchanger - Google Patents

Heat exchanger Download PDF

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Publication number
JP3841691B2
JP3841691B2 JP2002025213A JP2002025213A JP3841691B2 JP 3841691 B2 JP3841691 B2 JP 3841691B2 JP 2002025213 A JP2002025213 A JP 2002025213A JP 2002025213 A JP2002025213 A JP 2002025213A JP 3841691 B2 JP3841691 B2 JP 3841691B2
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JP
Japan
Prior art keywords
heat exchange
exchange chamber
heat
heat medium
medium
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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 - Fee Related
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JP2002025213A
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Japanese (ja)
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JP2003222484A (en
Inventor
博臣 釜野
賢一 蓬莱
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Kurimoto Ltd
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Kurimoto Ltd
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Filing date
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Priority to JP2002025213A priority Critical patent/JP3841691B2/en
Publication of JP2003222484A publication Critical patent/JP2003222484A/en
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Description

【0001】
【発明の属する技術分野】
この発明は、粒状の熱媒体を循環使用して、高温ガスの顕熱を低温ガスに回収する熱交換装置に関するものである。
【0002】
【従来の技術】
粒状の熱媒体を循環使用して、高温ガスの顕熱を低温ガスに回収する熱交換装置では、循環使用中の熱媒体の表面に各種の付着物が付着し、熱交換効率を低下させる。また、高温ガスとして溶融炉等で発生する高温排ガスを用いる場合は、高温排ガス中に含まれるガス状の金属塩化物が温度低下に伴い液化して粘着性の高い付着物となる。このような粘着性付着物は、熱交換効率を低下させるのみでなく、熱媒体同士を粘着により凝集させ、この凝集した熱媒体が熱交換装置内の狭い通路等を閉塞することがある。
【0003】
このように凝集した熱媒体を解砕する手段を設けた熱交換装置としては、特開2000−283673号公報に記載されたものがある。この熱交換装置は、図4に示すように、高温排ガス51が流通する上部熱交換室52と、低温ガス53が流通する下部熱交換室54が上下に配置され、これらの熱交換室52、54が連通管(連通部)55で連通されて、各熱交換室52、54にそれぞれトレイ56、57が複数段に設けられており、連通管55の中と下部熱交換室54上部のネック状通路58とに、それぞれ回転羽根59、60が設けられている。
【0004】
粒状の熱媒体61はホッパ62から投入され、上部熱交換室52の各トレイ56、連通管55、下部熱交換室54の各トレイ57、下部熱交換室54の底部へと順次落下し、下部熱交換室54の底部に設けられた排出口63から戻し経路64でホッパ62に戻されて循環使用され、凝集した熱媒体61が前記連通管55とネック状通路58とに設けられた各回転羽根59、60により解砕されるようになっている。
【0005】
【発明が解決しようとする課題】
上述した従来の熱交換装置は、凝集した熱媒体を解砕することはできるが、金属塩化物等の粘着性付着物は熱媒体の表面に付着したまま除去されない。特に、金属塩化物は高温で粘着性が高く、低温では粘着性が低下して硬くなる。このため、熱媒体の表面に付着した金属塩化物が除去されずに上部熱交換室に戻されると、再び粘着性を帯びて熱媒体が凝集する問題がある。また、付着物が付着した熱媒体は熱交換効率を低下させる問題もある。
【0006】
そこで、この発明の課題は、熱媒体の表面から粘着性付着物を効率よく除去できる熱交換装置を提供することである。
【0007】
【課題を解決するための手段】
上記の課題を解決するために、この発明は、高温ガスが流通する上部熱交換室から、低温ガスが流通する下部熱交換室へと粒状の熱媒体を通して熱交換させ、前記下部熱交換室の底部に溜まる熱交換した熱媒体を、前記上部熱交換室へ戻し経路で戻して循環使用する熱交換装置において、前記高温ガスとして高温排ガスを用い、前記下部熱交換室の底部に溜まる熱媒体を攪拌する攪拌手段を設け、これらの熱媒体の表面に付着する付着物を剥離させる構成を採用した。
【0008】
すなわち、下部熱交換室の底部には、熱交換した熱媒体が重なり合って溜まり、この重なり合った熱媒体でマテリアルシールが行われる。この下部熱交換室の底部では、熱媒体は低温ガスとの熱交換により温度が低下しているので、その表面に付着した金属塩化物は固化して粘着性を失っている。このため、これらの下部熱交換室底部に溜まった熱媒体を攪拌して熱媒体同士を擦り合わせることにより、その表面の付着物を効率よく剥離させることができる。
【0009】
前記戻し経路に、前記攪拌手段により熱媒体の表面から剥離した剥離物を除去するスクリーンを設けることにより、剥離した粘着性物質が再び熱媒体に付着するのを防止することができる。
【0010】
【発明の実施の形態】
以下、図1乃至図3に基づき、この発明の実施形態を説明する。図1および図2は、第1の実施形態を示す。この熱交換装置は、図1に示すように、高温排ガス1が流通する上部熱交換室2と、低温ガス3が流通する下部熱交換室4が上下に配置され、これらの熱交換室2、4が連通部5で連通されて、各熱交換室2、4に、それぞれトレイ6、7が複数段に設けられている。ホッパ8の投入口9から上部熱交換室2の上部に投入される粒状の熱媒体10は、上部熱交換室2の各トレイ6、連通部5、下部熱交換室4の各トレイ7、下部熱交換室4の底部へと順次落下し、上部熱交換室2で通気口11から排気口12へと流通する高温排ガス1との接触で顕熱を回収し、下部熱交換室4で通気口13から排気口14へと流通する低温ガス3に回収した顕熱を放出して熱交換する。
【0011】
前記熱交換して下部熱交換室4の底部に溜まった熱媒体10は、順次排出口15から排出されてエアリフタ16に移送され、空気により戻し経路17を上方のホッパ8へと戻し搬送されて循環使用される。
【0012】
図2に示すように、前記熱媒体10が溜まった下部熱交換室4の底部には、モータ18で回転駆動される攪拌羽根19が設けられている。下部熱交換室4の底部に溜まった熱媒体10は、低温ガス3との熱交換により温度が低下しており、熱媒体10の表面に付着した金属塩化物は固化して粘着性を失っている。したがって、この底部に重なり合って溜まった熱媒体10同士が攪拌羽根19の攪拌で擦り合わされ、高温排ガス1中から熱媒体10の表面に付着した金属塩化物等の粘着性物質が剥離する。この剥離物は、熱媒体10とともにエアリフタ16により戻し経路18を空気搬送されて、ホッパ8から上部熱交換室2に入るが、剥離物は軽いので熱交換済の高温排ガス1と一緒に排気口12から排出され、排気経路に設けられたバグフィルタ(図示省略)で捕集される。
【0013】
図3は、第2の実施形態を示す。この熱交換装置は、基本的な構成は第1の実施形態のものと同じであり、前記排出口15からエアリフタ16への移送経路に、スクリーン20が設けられている点のみが異なる。この実施形態では、前記攪拌羽根19の攪拌で熱媒体10から剥離する剥離物が、スクリーン20を通して除去され、熱媒体10のみがエアリフタ16に移送される。
【0014】
上述した各実施形態では、下部熱交換室の底部に溜まった熱媒体を攪拌する攪拌羽根の回転軸を垂直としたが、攪拌羽根の回転軸は、下部熱交換室の底部の形状に応じて任意の角度に設定することができる。
【0015】
【発明の効果】
以上のように、この発明の熱交換装置は、熱交換して下部熱交換室の底部に重なり合って溜まる熱媒体を攪拌する手段を設け、この重なり合った熱媒体同士を擦り合わせて、熱媒体の表面に付着する高温排ガスに含まれる金属塩化物等の粘着性物質を剥離させるようにしたので、熱媒体の熱交換効率を高めるとともに、高温の上部熱交換室に戻される熱媒体の粘着性物質による凝集をなくして、熱交換装置内の狭い通路等の閉塞を防止することができる。
【図面の簡単な説明】
【図1】第1の実施形態の熱交換装置を示す概略縦断面図
【図2】図1の下部熱交換室の底部を拡大して示す縦断面図
【図3】第2の実施形態の熱交換装置の下部熱交換室底部を拡大して示す縦断面図
【図4】従来の熱交換装置を示す概略縦断面図
【符号の説明】
1 高温排ガス
2 熱交換室
3 低温ガス
4 熱交換室
5 連通部
6、7 トレイ
8 ホッパ
9 投入口
10 熱媒体
11 通気口
12 排気口
13 通気口
14 排気口
15 排出口
16 エアリフタ
17 戻し経路
18 モータ
19 攪拌羽根
20 スクリーン
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a heat exchange device that circulates and uses a granular heat medium to recover sensible heat of a high-temperature gas into a low-temperature gas.
[0002]
[Prior art]
In a heat exchange device that circulates and uses a granular heat medium and recovers the sensible heat of a high-temperature gas into a low-temperature gas, various deposits adhere to the surface of the heat medium that is being used in circulation, thereby reducing the heat exchange efficiency. In addition, when high-temperature exhaust gas generated in a melting furnace or the like is used as the high-temperature gas, the gaseous metal chloride contained in the high-temperature exhaust gas is liquefied as the temperature decreases and becomes a highly sticky deposit. Such sticky deposits not only lower the heat exchange efficiency, but also cause the heat media to aggregate due to adhesion, and this aggregated heat medium may block a narrow passage or the like in the heat exchange device.
[0003]
As a heat exchange device provided with a means for crushing the heat medium thus aggregated, there is one described in JP-A-2000-283673. As shown in FIG. 4, the heat exchange device includes an upper heat exchange chamber 52 through which the high-temperature exhaust gas 51 circulates and a lower heat exchange chamber 54 through which the low-temperature gas 53 circulates, and these heat exchange chambers 52, 54 is communicated by a communication pipe (communication part) 55, and trays 56 and 57 are provided in a plurality of stages in each of the heat exchange chambers 52 and 54, respectively, and the necks in the communication pipe 55 and the upper part of the lower heat exchange chamber 54 are provided. Rotating blades 59 and 60 are provided in the channel 58, respectively.
[0004]
The granular heat medium 61 is introduced from the hopper 62 and sequentially falls to each tray 56 of the upper heat exchange chamber 52, the communication pipe 55, each tray 57 of the lower heat exchange chamber 54, and the bottom of the lower heat exchange chamber 54. Each rotation provided in the communicating pipe 55 and the neck-shaped passage 58 is a heat medium 61 which is returned from the discharge port 63 provided at the bottom of the heat exchange chamber 54 to the hopper 62 through the return path 64 and used in circulation. The blades 59 and 60 are crushed.
[0005]
[Problems to be solved by the invention]
The conventional heat exchange apparatus described above can crush the agglomerated heat medium, but sticky deposits such as metal chlorides are not removed while adhering to the surface of the heat medium. In particular, metal chlorides are highly sticky at high temperatures, and become sticky and hard at low temperatures. For this reason, if the metal chloride adhering to the surface of the heat medium is returned to the upper heat exchange chamber without being removed, there is a problem that the heat medium is condensed again due to stickiness. In addition, the heat medium to which the deposits are attached has a problem of reducing the heat exchange efficiency.
[0006]
Then, the subject of this invention is providing the heat exchange apparatus which can remove an adhesive deposit | attachment from the surface of a heat medium efficiently.
[0007]
[Means for Solving the Problems]
In order to solve the above-described problems, the present invention allows heat exchange through a granular heat medium from an upper heat exchange chamber in which a high-temperature gas circulates to a lower heat exchange chamber in which a low-temperature gas circulates. In a heat exchange device that circulates and uses the heat exchange medium that has accumulated heat at the bottom, returning it to the upper heat exchange chamber via a return path, the high temperature exhaust gas is used as the high temperature gas, and the heat medium that accumulates at the bottom of the lower heat exchange chamber is used. A configuration was adopted in which stirring means for stirring was provided, and deposits adhering to the surface of these heat media were peeled off.
[0008]
That is, the heat exchanged heat medium accumulates and accumulates at the bottom of the lower heat exchange chamber, and material sealing is performed with the overlapped heat medium. At the bottom of the lower heat exchange chamber, the temperature of the heat medium is lowered by heat exchange with the low-temperature gas, so that the metal chloride adhered to the surface is solidified and loses its adhesiveness. For this reason, the adhering substance on the surface can be efficiently peeled by stirring the heat medium accumulated at the bottom of the lower heat exchange chamber and rubbing the heat mediums together.
[0009]
By providing the return path with a screen for removing the exfoliated material exfoliated from the surface of the heat medium by the stirring means, the exfoliated adhesive substance can be prevented from adhering to the heat medium again.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to FIGS. 1 to 3. 1 and 2 show a first embodiment. As shown in FIG. 1, the heat exchange device includes an upper heat exchange chamber 2 through which high-temperature exhaust gas 1 circulates and a lower heat exchange chamber 4 through which low-temperature gas 3 circulates. 4 is communicated by the communication part 5, and the trays 6 and 7 are provided in a plurality of stages in the heat exchange chambers 2 and 4, respectively. The granular heat medium 10 charged into the upper part of the upper heat exchange chamber 2 from the inlet 9 of the hopper 8 is divided into the trays 6 of the upper heat exchange chamber 2, the communication part 5, the trays 7 of the lower heat exchange chamber 4, and the lower part. It falls sequentially to the bottom of the heat exchange chamber 4, collects sensible heat in contact with the high temperature exhaust gas 1 flowing from the vent 11 to the exhaust port 12 in the upper heat exchange chamber 2, and vents in the lower heat exchange chamber 4. The sensible heat recovered in the low-temperature gas 3 flowing from 13 to the exhaust port 14 is released and heat exchange is performed.
[0011]
The heat medium 10 accumulated at the bottom of the lower heat exchange chamber 4 after the heat exchange is sequentially discharged from the discharge port 15 and transferred to the air lifter 16, and is returned and conveyed to the upper hopper 8 through the return path 17 by air. Used cyclically.
[0012]
As shown in FIG. 2, a stirring blade 19 that is rotationally driven by a motor 18 is provided at the bottom of the lower heat exchange chamber 4 where the heat medium 10 is accumulated. The temperature of the heat medium 10 accumulated at the bottom of the lower heat exchange chamber 4 is lowered due to heat exchange with the low temperature gas 3, and the metal chloride adhering to the surface of the heat medium 10 is solidified and loses its adhesiveness. Yes. Accordingly, the heat medium 10 accumulated on the bottom is rubbed with the stirring blade 19 and the sticky substance such as metal chloride attached to the surface of the heat medium 10 is peeled off from the high temperature exhaust gas 1. The exfoliated material is conveyed along the return path 18 by the air lifter 16 together with the heat medium 10 and enters the upper heat exchanging chamber 2 from the hopper 8. 12 is collected by a bag filter (not shown) provided in the exhaust path.
[0013]
FIG. 3 shows a second embodiment. The basic structure of this heat exchange device is the same as that of the first embodiment, except that a screen 20 is provided in the transfer path from the discharge port 15 to the air lifter 16. In this embodiment, the peeled material that peels off from the heat medium 10 by stirring of the stirring blade 19 is removed through the screen 20, and only the heat medium 10 is transferred to the air lifter 16.
[0014]
In each of the above-described embodiments, the rotation axis of the stirring blade that stirs the heat medium accumulated at the bottom of the lower heat exchange chamber is vertical, but the rotation axis of the stirring blade depends on the shape of the bottom of the lower heat exchange chamber. Any angle can be set.
[0015]
【The invention's effect】
As described above, the heat exchanging device of the present invention is provided with means for exchanging heat and agitating the heat medium accumulated and accumulated on the bottom of the lower heat exchange chamber, and rubbing the overlapping heat mediums together. The adhesive material such as metal chloride contained in the high-temperature exhaust gas adhering to the surface is peeled off, so that the heat exchange efficiency of the heat medium is improved and the adhesive material of the heat medium returned to the high temperature upper heat exchange chamber It is possible to prevent the blockage of a narrow passage in the heat exchange device by eliminating the aggregation due to.
[Brief description of the drawings]
FIG. 1 is a schematic longitudinal sectional view showing a heat exchange device of a first embodiment. FIG. 2 is a longitudinal sectional view showing an enlarged bottom portion of a lower heat exchange chamber in FIG. Fig. 4 is an enlarged longitudinal sectional view showing the bottom of the lower heat exchange chamber of the heat exchange device. Fig. 4 is a schematic longitudinal sectional view showing a conventional heat exchange device.
DESCRIPTION OF SYMBOLS 1 High temperature exhaust gas 2 Heat exchange chamber 3 Low temperature gas 4 Heat exchange chamber 5 Communication part 6, 7 Tray 8 Hopper 9 Input port 10 Heat medium 11 Ventilation port 12 Exhaust port 13 Vent port 14 Exhaust port 15 Exhaust port 16 Air lifter 17 Return path 18 Motor 19 stirring blade 20 screen

Claims (2)

高温ガスが流通する上部熱交換室から、低温ガスが流通する下部熱交換室へと粒状の熱媒体を通して熱交換させ、前記下部熱交換室の底部に溜まる熱交換した熱媒体を、前記上部熱交換室へ戻し経路で戻して循環使用する熱交換装置において、前記高温ガスとして高温排ガスを用い、前記下部熱交換室の底部に溜まる熱媒体を攪拌する攪拌手段を設け、熱媒体同士を擦り合わせることにより、これらの熱媒体の表面に付着する金属塩化物を剥離させるようにしたことを特徴とする熱交換装置。The upper heat exchange chamber through which the high-temperature gas circulates is exchanged through a granular heat medium from the lower heat exchange chamber through which the low-temperature gas circulates, and the heat exchange heat medium accumulated at the bottom of the lower heat exchange chamber is converted into the upper heat exchange chamber. In a heat exchange device that is circulated and returned to the exchange chamber through a return path, a high-temperature exhaust gas is used as the high-temperature gas, and a stirring means for stirring the heat medium accumulated at the bottom of the lower heat exchange chamber is provided, and the heat media are rubbed together Thus, the metal chloride adhering to the surface of the heat medium is peeled off. 前記戻し経路に、前記攪拌手段により熱媒体の表面から剥離した剥離物を除去するスクリーンを設けた請求項1に記載の熱交換装置。The heat exchange apparatus according to claim 1, wherein a screen is provided on the return path to remove the exfoliated material exfoliated from the surface of the heat medium by the stirring means.
JP2002025213A 2002-02-01 2002-02-01 Heat exchanger Expired - Fee Related JP3841691B2 (en)

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JP3841691B2 true JP3841691B2 (en) 2006-11-01

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