JPS6321112B2 - - Google Patents
Info
- Publication number
- JPS6321112B2 JPS6321112B2 JP58030623A JP3062383A JPS6321112B2 JP S6321112 B2 JPS6321112 B2 JP S6321112B2 JP 58030623 A JP58030623 A JP 58030623A JP 3062383 A JP3062383 A JP 3062383A JP S6321112 B2 JPS6321112 B2 JP S6321112B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- fins
- heat exchanger
- tube
- exchanger tube
- 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
Links
- 239000000428 dust Substances 0.000 claims description 9
- 239000007789 gas Substances 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000005684 electric field Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/16—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying an electrostatic field to the body of the heat-exchange medium
Description
【発明の詳細な説明】
本発明は熱交換器のうち、伝熱管内を流動する
媒体と伝熱管との間で伝熱を行う熱交換器に関
し、さらに詳しくは該熱交換器の収塵構造に係る
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger that transfers heat between a medium flowing in a heat transfer tube and a heat transfer tube, and more specifically relates to a dust collection structure of the heat exchanger. This is related to.
熱交換器のうち、伝熱管内を流動する媒体の熱
を伝熱管外へ放出するものとして、燃焼排ガスの
熱交換器などがある。 Among the heat exchangers, there is a combustion exhaust gas heat exchanger and the like that release the heat of a medium flowing inside the heat exchanger tube to the outside of the heat exchanger tube.
ボイラ等の燃焼ガスは未だ十分な熱エネルギを
有しているので、熱交換器を通して熱回収を行わ
している。この場合、熱交換効率の高い熱交換器
を用いると、熱交換器を小型、軽量化でき、かつ
低コスト化できるものとなる。 Since combustion gas from boilers and the like still has sufficient thermal energy, heat is recovered through a heat exchanger. In this case, if a heat exchanger with high heat exchange efficiency is used, the heat exchanger can be made smaller, lighter, and lower in cost.
従来、熱交換効率を向上させるため、高性能伝
熱面など種々の手段を施していたが、排気ガス中
に存在する塵芥等の異物が伝熱面に付着して熱伝
達率を低下させるものとなつていた。このため、
排気ガス中の異物を除去する手段を設けなければ
ならないが、そのための効果的な手段がなかつ
た。 Conventionally, various measures such as high-performance heat transfer surfaces have been used to improve heat exchange efficiency, but foreign matter such as dust present in the exhaust gas adheres to the heat transfer surfaces and reduces the heat transfer coefficient. It was becoming. For this reason,
Although it is necessary to provide a means to remove foreign matter from the exhaust gas, there has been no effective means for this purpose.
一方、通常の排気ガス熱交換器は対流熱伝達及
び熱伝導を利用しており、輻射熱を利用するもの
とはなつていない。このため、熱伝達率の向上が
望めないものとなつていた。 On the other hand, conventional exhaust gas heat exchangers utilize convection heat transfer and heat conduction, and do not utilize radiant heat. For this reason, it has become impossible to expect an improvement in the heat transfer coefficient.
本発明の目的は、媒体中の塵芥が伝熱管内面に
付着することを防止し、かつ輻射伝熱をも行うよ
うにして熱交換効率を向上させた収塵装置を与え
んとすることにある。 An object of the present invention is to provide a dust collection device that prevents dust in a medium from adhering to the inner surface of a heat transfer tube and also performs radiant heat transfer to improve heat exchange efficiency. .
本発明の特徴とするところは、十字フインなど
のフインを伝熱管内に設け、該フインに電圧を与
えて排気ガス中の塵芥をフインに吸着させ、かつ
排気ガスの温度まで昇温されたフイン外表面の輻
射熱で伝熱管内を加熱して熱伝達を向上させたと
ころにある。 The present invention is characterized in that fins such as cross fins are provided in the heat transfer tube, and a voltage is applied to the fins to cause dust in the exhaust gas to be adsorbed to the fins, and the fins are heated to the temperature of the exhaust gas. The radiant heat from the outside surface heats the inside of the heat transfer tube to improve heat transfer.
以下、図によつて詳しく説明する。 This will be explained in detail below using figures.
先ず、第1図は本発明の一実施例を説明する断
面図、第2図は第1図のA−A断面図である。 First, FIG. 1 is a sectional view illustrating an embodiment of the present invention, and FIG. 2 is a sectional view taken along the line AA in FIG.
伝熱管1内には十字状のフイン2が設けられて
いる。伝熱管内には排気ガス等の熱回収媒体が流
動されている。伝熱管1とフイン2との間には電
界が形成されるようにフイン2を陽極に伝熱管1
を陰極に電気的に接続する。伝熱管1の内面には
フイン2の数と同数の突起電極3が設けられ、突
起電極3はフインの中間位置に配置されることが
望ましい。突起電極3の極性は伝熱管1と同じ陰
極となつている。なお、電極の極性は排気ガス中
のダスト成分によつては逆となる場合もある。 A cross-shaped fin 2 is provided inside the heat exchanger tube 1. A heat recovery medium such as exhaust gas is flowing inside the heat transfer tube. The heat exchanger tube 1 is connected with the fin 2 as an anode so that an electric field is formed between the heat exchanger tube 1 and the fins 2.
is electrically connected to the cathode. It is desirable that the same number of protruding electrodes 3 as the number of fins 2 are provided on the inner surface of the heat exchanger tube 1, and that the protruding electrodes 3 are arranged at intermediate positions between the fins. The polarity of the protruding electrode 3 is the same as that of the heat exchanger tube 1, which is a cathode. Note that the polarity of the electrodes may be reversed depending on the dust components in the exhaust gas.
フイン2は長手方向にらせん状にねじられても
よい。又、突起電極3は長手方向に伸びる突条電
極でもよく、一列に並んで多数設けられる突起電
極でもよい。 The fins 2 may be spirally twisted in the longitudinal direction. Further, the protruding electrodes 3 may be protruding electrodes extending in the longitudinal direction, or may be protruding electrodes arranged in a large number in a row.
上記の如く構成された本発明の一実施例につい
て説明する。 An embodiment of the present invention configured as described above will be described.
排気ガスがPの如く流動するとき、排気ガスの
熱がフイン2及び伝熱管1へ与えられる。伝熱管
1の外側には水又はフレオン等の被加熱媒体が在
り、排気ガス中の熱が水又はフレオン等へ回収さ
れるものとなつている。 When the exhaust gas flows like P, the heat of the exhaust gas is given to the fins 2 and the heat exchanger tubes 1. A medium to be heated, such as water or Freon, is present outside the heat exchanger tube 1, and the heat in the exhaust gas is recovered to water, Freon, or the like.
本発明では、フイン2が高温となつて輻射熱を
Qの如く伝熱管1に与える。 In the present invention, the fins 2 reach a high temperature and give radiant heat to the heat transfer tube 1 as indicated by Q.
このため、熱の回収効果が一層高いものとな
る。今、排気ガス中の異物等が伝熱管1内に付着
せんとしても、電界の作用によりフイン2へ全て
付着するものとなる。このため、伝熱管1内面に
付着する異物がなくなつて、伝熱管1に与えられ
て伝熱管1の外面へ伝導される熱量が低下するこ
とがない。 Therefore, the heat recovery effect becomes even higher. Even if foreign matter in the exhaust gas does not adhere to the inside of the heat exchanger tube 1, it will all adhere to the fins 2 due to the action of the electric field. Therefore, there is no foreign matter adhering to the inner surface of the heat exchanger tube 1, and the amount of heat applied to the heat exchanger tube 1 and conducted to the outer surface of the heat exchanger tube 1 does not decrease.
又、フイン2に付着した異物Sがフイン2の輻
射熱量を低下させるかと云うと、輻射熱は絶対温
度によつて定まるものであるため、付着異物Sの
温度による輻射熱が伝熱管1へ与えられて、輻射
熱の格別の低下はない。 Also, whether the foreign matter S attached to the fins 2 reduces the amount of heat radiated from the fins 2 is because radiant heat is determined by absolute temperature, so the radiant heat due to the temperature of the foreign matter S attached to the fins is given to the heat transfer tube 1. , there is no particular decrease in radiant heat.
以上のとおり、本発明によるとフイン2を収塵
兼輻射熱源として利用するため、伝熱管1の熱交
換率を著しく改善するものとなる。又、突起電極
が管内面に設けられているので、突起電極とフイ
ンとの間隙を流動する気体からなる媒体中への放
電が効果的に行なわれるものとなり、塵芥が確実
に電荷を持つものとなつてフインに付着し易いも
のとなる。 As described above, according to the present invention, since the fins 2 are used as dust collectors and radiant heat sources, the heat exchange efficiency of the heat exchanger tubes 1 is significantly improved. In addition, since the protruding electrode is provided on the inner surface of the tube, the discharge into the medium made of gas flowing through the gap between the protruding electrode and the fin is effectively carried out, and the dust is reliably charged. It becomes easy to adhere to the fins.
なお、以上の実施例において、伝熱管1は必ず
しも円管に限定されない。 In addition, in the above embodiment, the heat exchanger tube 1 is not necessarily limited to a circular tube.
又、フイン2も十字以外に一字状又は3枚羽根
など複数枚が伝熱管の中心から放射状に伸びるも
のであればよい。 Further, the fins 2 may also have a shape other than a cross, as long as they have a linear shape or a plurality of blades, such as three blades, extending radially from the center of the heat exchanger tube.
さらにフイン2は真直又はねじりの両者を含む
ものであり、ねじりのあるものではより均等な輻
射熱を伝熱管に与えるものとなる。 Further, the fins 2 include both straight and twisted fins, and those with twist provide more uniform radiant heat to the heat transfer tube.
さらに又、伝熱管1内の流動流体は排気ガスに
限定されるものでなく、非導電性の気体であれば
よい。伝熱管1外の媒体も水又はフレオンに限定
されないことは明白である。 Furthermore, the flowing fluid within the heat exchanger tube 1 is not limited to exhaust gas, but may be any non-conductive gas. It is clear that the medium outside the heat exchanger tube 1 is not limited to water or Freon either.
又、伝熱管の外側の媒体から伝熱管内側の媒体
へ熱交換する装置も本発明に含まれるものであ
る。 The present invention also includes a device for exchanging heat from a medium outside the heat exchanger tube to a medium inside the heat exchanger tube.
第1図は本発明の一実施例を示す断面図、第2
図は第1図のA−A断面図である。
1:伝熱管、2:フイン。
FIG. 1 is a cross-sectional view showing one embodiment of the present invention, and FIG.
The figure is a sectional view taken along the line AA in FIG. 1. 1: heat exchanger tube, 2: fin.
Claims (1)
管と、該管内に配置され、放射状に複数枚設けら
れたフインとからなり、該フインは前記伝熱管内
面と間隙を有しており、前記管の内面には突起電
極が設けられ、該フインと伝熱管との間に電位差
を与え、前記非導電性媒体中の塵芥を低減せしめ
るとともにフインによる輻射熱伝熱を行なわせし
めた熱交換器。1 Consisting of a heat exchanger tube through which a non-conductive medium made of gas flows, and a plurality of fins arranged in the tube and provided radially, the fins have a gap with the inner surface of the heat exchanger tube, and the fins have a gap with the inner surface of the heat exchanger tube, A heat exchanger in which protruding electrodes are provided on the inner surface of the tube to apply a potential difference between the fins and the heat transfer tube to reduce dust in the non-conductive medium and to perform radiant heat transfer by the fins.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58030623A JPS59157487A (en) | 1983-02-25 | 1983-02-25 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58030623A JPS59157487A (en) | 1983-02-25 | 1983-02-25 | Heat exchanger |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59157487A JPS59157487A (en) | 1984-09-06 |
JPS6321112B2 true JPS6321112B2 (en) | 1988-05-02 |
Family
ID=12308980
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58030623A Granted JPS59157487A (en) | 1983-02-25 | 1983-02-25 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59157487A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61276606A (en) * | 1985-05-29 | 1986-12-06 | 株式会社 平川鉄工所 | Once-through boiler |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5150051A (en) * | 1974-10-29 | 1976-05-01 | Inoue Japax Res | Osenboshisochio gubishita netsukokansochi |
JPS5320155A (en) * | 1976-08-07 | 1978-02-24 | Matsushita Refrig Co | Heat exchanger |
-
1983
- 1983-02-25 JP JP58030623A patent/JPS59157487A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5150051A (en) * | 1974-10-29 | 1976-05-01 | Inoue Japax Res | Osenboshisochio gubishita netsukokansochi |
JPS5320155A (en) * | 1976-08-07 | 1978-02-24 | Matsushita Refrig Co | Heat exchanger |
Also Published As
Publication number | Publication date |
---|---|
JPS59157487A (en) | 1984-09-06 |
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