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JP2004003840A - Heat transfer fin structure of heat exchanger for gas boiler - Google Patents

Heat transfer fin structure of heat exchanger for gas boiler Download PDF

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Publication number
JP2004003840A
JP2004003840A JP2003145261A JP2003145261A JP2004003840A JP 2004003840 A JP2004003840 A JP 2004003840A JP 2003145261 A JP2003145261 A JP 2003145261A JP 2003145261 A JP2003145261 A JP 2003145261A JP 2004003840 A JP2004003840 A JP 2004003840A
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JP
Japan
Prior art keywords
heat exchanger
combustion chamber
heat transfer
gas boiler
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.)
Pending
Application number
JP2003145261A
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Japanese (ja)
Inventor
Youn Cheol Shin
シン,ユンチェル
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.)
Kyung Dong Boiler Co Ltd
Original Assignee
Kyung Dong Boiler 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 Kyung Dong Boiler Co Ltd filed Critical Kyung Dong Boiler Co Ltd
Publication of JP2004003840A publication Critical patent/JP2004003840A/en
Pending legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]

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  • Details Of Fluid Heaters (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a heat transfer fin structure of a heat exchanger for a gas boiler capable of increasing heat transfer area to extremely increase heat exchanging efficiency, reducing cost of a product, and compacting the product. <P>SOLUTION: The gas boiler has a combustion chamber cover 10 having a combustion chamber 10a inside, the heat exchangers 24 disposed in the upper and lower parts of the combustion chamber, and a bas burner 22. The heat exchangers have a tubular tube 24a in which water circulates and a plurality of high fins 24b of not shorter than 9 mm extending from a plate surface to the radial outside on the outside of the tube. The high fins 24b are preferably rolled and fabricated to the tube 24a. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明はガスボイラー用熱交換器の伝熱フィン構造に係り、より詳しくは伝熱面積を増加させ熱交換効率を遥かに高められるのみならず、製品のコストを節減させ製品をコンパクト化させうるようにしたガスボイラー用熱交換器の伝熱フィン構造に関する。
【0002】
【従来の技術】
一般家庭や公共建物などで使用されるボイラーは暖房用や温水用として用いられる。このようなボイラーは提供される燃料の形態によってオイルボイラーとガスボイラーとに大別される。
【0003】
同一容量のオイルボイラーとガスボイラーを比較してみれば、購入価格においてオイルボイラーがガスボイラーに比べて低価格であるが、ガスボイラーがオイルボイラーに比べて燃料消耗量が少ないという利点がある。
しかし、長期的にみる際、消費者が負担すべき経費はオイル及びガスボイラーの両方が殆んど同一であると言える。そこで、都市ガスが供給される地域ならばガスボイラーを使用し、都市ガスが供給されていないその他の地域ではオイルボイラーを多用している実情である。
【0004】
近年、都市ガスが供給される地域の増加に伴って次第にガスボイラーの使用が高まりつつある。従来のガスボイラーは内部に燃焼室が形成され、燃焼室の下部にはガスバーナが設けられており、上部には熱交換器が設けられている。
これに、ガスバーナが作動されると燃焼室内に流入された水は熱交換器により熱交換されその温度が上昇した後、暖房及び温水配管などに提供される。
【0005】
ところで、このような従来のガスボイラーにおいては、燃焼室内に設けられた熱交換器自体だけで熱交換がなされていることから、その伝熱面積に限界がある。従って、伝熱面積を増加させるためには熱交換器サイズを大きくしなければならないので、ガスボイラーをコンパクト化できない欠点がある。
【0006】
また、従来のガスボイラーに採用される熱交換器はハイフィンチューブ(High finned tube)を使用せずに水管部のパイプに伝熱フィンを溶接して使用しているため、熱伝達性能が低下するしかない。もし、伝熱面積を確保するために伝熱フィンをより多く使えば、使用する伝熱フィンだけ材料費がアップし、製品のサイズが大きくなり、伝熱フィンの別途の生産、溶接工程の追加などに伴う生産コストのアップという問題点がある。
【0007】
【発明が解決しようとする課題】
従って、本発明は前述した問題点を解決するために案出されたもので、その目的は伝熱面積を増加させて熱交換効率を格段に高められるようにしたガスボイラー用熱交換器の伝熱フィン構造を提供することにある。
本発明の他の目的は、製品のコストを節減できるのみならず、製品をコンパクト化し得るようにしたガスボイラー用熱交換器の伝熱フィン構造を提供することにある。
【0008】
【課題を解決するための手段】
前述した目的は、内部に燃焼室が形成された燃焼室カバーと、前記燃焼室の上部及び下部にそれぞれ設けられた熱交換器及びガスバーナを有するガスボイラーにおいて、前記熱交換器は、内部に水が循環する管状のチューブと、該チューブの外側に板面から径方向の外側に延びた複数のハイフィンを含むことを特徴とするガスボイラー用熱交換器の伝熱フィン構造により達成される。
ここで、前記ハイフィンの高さは約9mm以上のものが有利である。
そして、前記ハイフィンは前記チューブに転造加工によって製造できる。
【0009】
【発明の実施の形態】
以下、添付した図面に基づき本発明の各実施例について説明する。
図1は本発明の一実施例によるガスボイラーの概略的な構成図である。同図に示した通り、本発明に係るガスボイラーは、外観を形成する燃焼室カバー10と、燃焼室カバー10の上部に設けられた排気ガス案内板20を有する。
【0010】
燃焼室カバー10は通常四角ボックス状よりなる。しかし、設置される場所あるいはガスボイラーの効率及び容量、そしてデザインによって円筒形やその他別の形状をなしても良い。燃焼室カバー10内には燃焼室10aが形成されている。
【0011】
燃焼室カバー10の一側には図示していない暖房及び温水配管から水が還水される還水管12が設けられており、他側には後述する内部熱交換管28及び熱交換器24によって暖まった温水が再び暖房及び温水配管に供給される供給管14が設けられている。
【0012】
燃焼室カバー10の上部に設けられた排気ガス案内板20には後述するガスバーナ22により発生した排気ガスが外部に排出される排気ガス排出孔20aが形成されている。排気ガス排出孔20aは煙筒(図示せず)に連結された後、排気ガスを外部に排出する。
【0013】
燃焼室10a内の下部には都市ガスのような燃料により作動され炎を発生させるガスバーナ22が設けられている。そして、燃焼室10aの上部には熱交換器24が設けられている。熱交換器24は詳しく後述する内部熱交換管28と共にガスバーナ22によって冷たい水を温水に暖める2次の熱交換過程を行なう。
【0014】
一方、転造加工などにより製造できる熱交換器24は図2に示した通り、内部に水が循環する管状のチューブ24aと、チューブ24aの外側に板面から径方向の外側に延びた複数のハイフィン24bを有する。この際、ハイフィン24bの高さ(H)は例えば9mm以上に形成することによりその伝熱面積を増加させうる。
【0015】
このようにハイフィン24bを設けることにより、従来のように伝熱面積を確保するために溶接による伝熱フィン(図示せず)を使用するに伴う材料費の上昇問題と製品のサイズが大きくなる問題及びコストがアップする問題点を適切に解消できる。また、ハイフィン24bにより伝熱面積が増加されるため、製品をコンパクト化できるという著しい効果を奏す。
【0016】
熱交換器24には連結管26が結合されている。連結管26はその一端が熱交換器24と結合され、他端は燃焼室カバー10の内側に配置される。
燃焼室カバー10の内側連結管26と還水管12との間には両端がそれぞれ連結管26及び還水管12に連通する内部熱交換管28が設けられている。内部熱交換管28はガスバーナ22によって冷水を温水に暖める1次の熱交換過程を行なう。
【0017】
本実施例において内部熱交換管28は図示したように、燃焼室カバー10の内壁面に沿ってコイル状に複数回巻き付けられている。この際、巻き付けられる各側面は相互接触しないようにすることで、ガスバーナ22の炎によるその伝熱面積が増加して熱交換効率を一層高められるものが望ましい。
【0018】
このような構成によって、ガスバーナ22が作動された状態で冷たくなった水が還水管12を通して燃焼室カバー10内に流入されると、流入された水は内部熱交換管28の内部に沿って流動する過程において増加しただけの伝熱面積によって1次の熱交換過程が行われる。
【0019】
1次の熱交換過程が行なわれた水は連結管26を通して熱交換器24に向かって2次の熱交換過程が行なわれる。2次の熱交換過程が行なわれる過程において、本発明に係る熱交換器24はチューブ24aと、チューブ24aの板面から径方向の外側に延びた複数のハイフィン24bで構成されていることから、伝熱面積が増加して熱交換効率が著しく高められる。
内部熱交換管28及び熱交換器24によりそれぞれ熱交換された水は供給管14を通して暖房及び温水配管に向かうようになる。
【0020】
このように本発明では熱交換器24をチューブ24aと、チューブ24aの板面から径方向の外側に延びた複数のハイフィン24b(High fin)で構成されているので、従来のように熱交換器24を大きく形成する必要がなく、製品をコンパクト化し得る。
【0021】
一方、前述した実施例では内部熱交換管28が設けられたガスボイラーをその例として説明した。しかし、図3に示した通り、内部熱交換管28が設けられていないガスボイラーにも本発明の思想が適用され得る。
図3に示した通り、本発明の他の実施例によるガスボイラーは、内部に燃焼室110aが形成された燃焼室カバー110の下部にはガスバーナ122が設けられており、上部には熱交換器124が設けられている。
【0022】
このような熱交換器124も、詳しく図示されていないが転造加工などにより製造され、内部に水が循環する管状のチューブと、チューブの外側に板面から径方向の外側に延びた複数のハイフィンの構成を取る。この際、ハイフィンの高さは例えば9mm以上に形成されてその伝熱面積を高めることができる。
【0023】
燃焼室カバー110の上部には排気ガス案内板120が設けられている。そして、燃焼室カバー110の一側には暖房及び温水配管に連結されて水が還水する還水管112が設けられており、他側には熱交換器124により暖められた温水が図示されていない暖房及び温水配管に供給される供給管114が設けられている。
【0024】
ここで、ガスバーナ122が作動された状態で冷たくなった水が還水管112を通して燃焼室カバー110内に流入されると、流入された水は伝熱面積の増加した熱交換器124によって熱交換されてその温度が上昇した後、供給管114を通して再び暖房及び温水配管に供給される。
【0025】
このように本発明によれば、伝熱面積を増加させ熱交換効率を著しく高められるのみならず、製品のコストを節減させ、製品をコンパクト化し得る。
前述した一実施例では、ガスボイラー内に内部熱交換管28を設けているが、このような内部熱交換管28の代りに、外部熱交換管(図示せず)が設けられたガスボイラーにも本発明の思想が十分適用され得る。
【0026】
【発明の効果】
以上述べた通り、本発明によれば転造加工を通して9mm以上のハイフィン形態の伝熱フィンを提供することにより、伝熱面積を増加させ熱交換効率を著しく高められる効果がある。
また、本発明によれば、製品のコストを節減できるのみならず、製品をコンパクト化し得るガスボイラー用熱交換器の伝熱フィン構造を提供する効果がある。
【図面の簡単な説明】
【図1】本発明の一実施例によるガスボイラーの概略的な構成図。
【図2】図1に示した熱交換器の拡大構成図。
【図3】本発明の他の実施例によるガスボイラーの概略的な構成図である。
【符号の説明】
10:燃焼室カバー、   10a:燃焼室、
12:還水管、      14:供給管、
20:排気ガス案内板、  22:ガスバーナ、
24:熱交換器、     24a:チューブ、
24b:ハイフィン、   26:連結管、
28:内部熱交換管
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a heat transfer fin structure of a heat exchanger for a gas boiler, and more particularly, not only can increase a heat transfer area to increase heat exchange efficiency, but also can reduce product cost and make the product compact. The present invention relates to a heat transfer fin structure for a gas boiler heat exchanger.
[0002]
[Prior art]
Boilers used in general homes and public buildings are used for heating and hot water. Such boilers are roughly classified into oil boilers and gas boilers according to the type of fuel provided.
[0003]
Comparing an oil boiler and a gas boiler with the same capacity, the oil boiler is lower in price than the gas boiler at the purchase price, but has the advantage that the gas boiler consumes less fuel than the oil boiler.
However, in the long run, the costs to be borne by consumers can be said to be almost identical for both oil and gas boilers. Therefore, gas boilers are used in areas where city gas is supplied, and oil boilers are heavily used in other areas where city gas is not supplied.
[0004]
In recent years, the use of gas boilers has been gradually increasing with an increase in the area where city gas is supplied. A conventional gas boiler has a combustion chamber formed therein, a gas burner provided at a lower portion of the combustion chamber, and a heat exchanger provided at an upper portion.
When the gas burner is operated, the water flowing into the combustion chamber is exchanged by the heat exchanger, and the temperature of the water is increased.
[0005]
By the way, in such a conventional gas boiler, heat exchange is performed only by the heat exchanger itself provided in the combustion chamber, and therefore, the heat transfer area is limited. Therefore, in order to increase the heat transfer area, the size of the heat exchanger must be increased, so that there is a disadvantage that the gas boiler cannot be made compact.
[0006]
In addition, the heat exchanger used in the conventional gas boiler uses a heat transfer fin welded to the pipe of the water pipe without using a high finned tube, so that heat transfer performance is deteriorated. There is only. If more heat transfer fins are used to secure the heat transfer area, the material cost will increase only for the heat transfer fins to be used, the size of the product will increase, additional production of heat transfer fins and additional welding process will be required. There is a problem that the production cost is increased due to the above.
[0007]
[Problems to be solved by the invention]
Accordingly, the present invention has been devised to solve the above-mentioned problems, and has as its object to increase the heat transfer area and thereby significantly improve the heat exchange efficiency. It is to provide a thermal fin structure.
It is another object of the present invention to provide a heat transfer fin structure of a heat exchanger for a gas boiler, which not only can reduce the cost of the product but also can make the product compact.
[0008]
[Means for Solving the Problems]
The above-described object is to provide a gas boiler having a combustion chamber cover in which a combustion chamber is formed and heat exchangers and gas burners provided in upper and lower portions of the combustion chamber, respectively, wherein the heat exchanger has water inside. This is achieved by a heat transfer fin structure of a gas boiler heat exchanger, characterized by including a tubular tube through which circulates, and a plurality of high fins extending radially outward from a plate surface outside the tube.
Here, the height of the high fins is advantageously about 9 mm or more.
The high fins can be manufactured by rolling the tube.
[0009]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings.
FIG. 1 is a schematic configuration diagram of a gas boiler according to one embodiment of the present invention. As shown in the figure, the gas boiler according to the present invention has a combustion chamber cover 10 forming an external appearance, and an exhaust gas guide plate 20 provided on an upper portion of the combustion chamber cover 10.
[0010]
The combustion chamber cover 10 usually has a square box shape. However, it may be cylindrical or another shape depending on the installation location or the efficiency and capacity of the gas boiler, and the design. A combustion chamber 10 a is formed in the combustion chamber cover 10.
[0011]
One side of the combustion chamber cover 10 is provided with a return water pipe 12 for returning water from a heating and hot water pipe (not shown), and the other side is provided with an internal heat exchange pipe 28 and a heat exchanger 24 described later. A supply pipe 14 is provided for supplying the heated hot water to the heating and hot water pipe again.
[0012]
An exhaust gas guide plate 20 provided at an upper portion of the combustion chamber cover 10 has an exhaust gas discharge hole 20a through which exhaust gas generated by a gas burner 22 described later is discharged to the outside. After being connected to a smoke tube (not shown), the exhaust gas discharge hole 20a discharges exhaust gas to the outside.
[0013]
A gas burner 22 which is operated by a fuel such as city gas and generates a flame is provided at a lower portion in the combustion chamber 10a. A heat exchanger 24 is provided above the combustion chamber 10a. The heat exchanger 24 performs a secondary heat exchange process in which cold water is warmed to warm water by the gas burner 22 together with an internal heat exchange tube 28 described later in detail.
[0014]
On the other hand, as shown in FIG. 2, the heat exchanger 24 that can be manufactured by rolling or the like has a tubular tube 24a in which water circulates, and a plurality of tubes extending radially outward from the plate surface outside the tube 24a. It has a high fin 24b. At this time, the height (H) of the high fins 24b can be increased to, for example, 9 mm or more to increase the heat transfer area.
[0015]
By providing the high fins 24b in this manner, there is a problem of an increase in material costs and an increase in the size of a product due to the use of a heat transfer fin (not shown) by welding to secure a heat transfer area as in the related art. In addition, the problem that the cost increases can be appropriately solved. Further, since the heat transfer area is increased by the high fins 24b, there is a remarkable effect that the product can be made compact.
[0016]
The connection pipe 26 is connected to the heat exchanger 24. The connecting pipe 26 has one end connected to the heat exchanger 24 and the other end disposed inside the combustion chamber cover 10.
Between the inner connection pipe 26 of the combustion chamber cover 10 and the return water pipe 12, there are provided internal heat exchange pipes 28 whose both ends communicate with the connection pipe 26 and the return water pipe 12, respectively. The internal heat exchange pipe 28 performs a primary heat exchange process in which cold water is warmed to warm water by the gas burner 22.
[0017]
In this embodiment, the internal heat exchange tube 28 is wound in a coil shape a plurality of times along the inner wall surface of the combustion chamber cover 10 as shown. At this time, it is preferable that the side surfaces to be wound are not in contact with each other, so that the heat transfer area of the gas burner 22 due to the flame can be increased to further enhance the heat exchange efficiency.
[0018]
With such a configuration, when the cooled water flows into the combustion chamber cover 10 through the return water pipe 12 in a state where the gas burner 22 is operated, the flowed water flows along the inside of the internal heat exchange pipe 28. The primary heat exchange process is performed by the increased heat transfer area in the process.
[0019]
Water subjected to the primary heat exchange process is subjected to a secondary heat exchange process toward the heat exchanger 24 through the connecting pipe 26. In the process in which the secondary heat exchange process is performed, the heat exchanger 24 according to the present invention includes the tube 24a and the plurality of high fins 24b extending radially outward from the plate surface of the tube 24a. The heat transfer area is increased and the heat exchange efficiency is significantly increased.
The water that has been heat-exchanged by the internal heat exchange pipe 28 and the heat exchanger 24 respectively flows through the supply pipe 14 to the heating and hot water pipes.
[0020]
As described above, in the present invention, the heat exchanger 24 is constituted by the tube 24a and the plurality of high fins 24b (High fin) extending radially outward from the plate surface of the tube 24a. 24 does not need to be made large, and the product can be made compact.
[0021]
On the other hand, in the above-described embodiment, the gas boiler provided with the internal heat exchange tube 28 has been described as an example. However, as shown in FIG. 3, the idea of the present invention can be applied to a gas boiler in which the internal heat exchange tube 28 is not provided.
As shown in FIG. 3, in a gas boiler according to another embodiment of the present invention, a gas burner 122 is provided below a combustion chamber cover 110 in which a combustion chamber 110a is formed, and a heat exchanger is provided above. 124 are provided.
[0022]
Although not shown in detail, such a heat exchanger 124 is also manufactured by rolling or the like, and has a tubular tube through which water circulates, and a plurality of tubes extending radially outward from a plate surface outside the tube. Take the configuration of high fins. At this time, the height of the high fin is, for example, 9 mm or more, so that the heat transfer area can be increased.
[0023]
An exhaust gas guide plate 120 is provided above the combustion chamber cover 110. On one side of the combustion chamber cover 110, a return water pipe 112 connected to a heating and hot water pipe for returning water is provided, and on the other side, hot water heated by a heat exchanger 124 is shown. A supply pipe 114 is provided to supply no heating and hot water piping.
[0024]
Here, when the cooled water flows into the combustion chamber cover 110 through the return water pipe 112 while the gas burner 122 is operated, the flow of water is exchanged by the heat exchanger 124 having an increased heat transfer area. After the temperature rises, it is supplied again to the heating and hot water pipe through the supply pipe 114.
[0025]
Thus, according to the present invention, not only the heat transfer area can be increased and the heat exchange efficiency can be significantly increased, but also the cost of the product can be reduced and the product can be made compact.
In the above-described embodiment, the internal heat exchange tube 28 is provided in the gas boiler. However, instead of such an internal heat exchange tube 28, a gas boiler provided with an external heat exchange tube (not shown) is provided. Also, the idea of the present invention can be sufficiently applied.
[0026]
【The invention's effect】
As described above, according to the present invention, by providing a heat transfer fin in the form of a high fin of 9 mm or more through rolling, there is an effect that the heat transfer area can be increased and the heat exchange efficiency can be significantly increased.
Further, according to the present invention, there is an effect of providing a heat transfer fin structure of a heat exchanger for a gas boiler which can not only reduce the cost of the product but also make the product compact.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram of a gas boiler according to an embodiment of the present invention.
FIG. 2 is an enlarged configuration diagram of the heat exchanger shown in FIG.
FIG. 3 is a schematic structural view of a gas boiler according to another embodiment of the present invention.
[Explanation of symbols]
10: combustion chamber cover, 10a: combustion chamber,
12: return water pipe, 14: supply pipe,
20: exhaust gas guide plate, 22: gas burner,
24: heat exchanger, 24a: tube,
24b: high fin, 26: connecting pipe,
28: Internal heat exchange tube

Claims (3)

内部に燃焼室が形成された燃焼室カバーと、前記燃焼室の上部及び下部にそれぞれ設けられた熱交換器及びガスバーナを有するガスボイラーにおいて、
前記熱交換器は、内部に水が循環する管状のチューブと、該チューブの外側に板面から径方向の外側に延びた複数のハイフィンを含むことを特徴とするガスボイラー用熱交換器の伝熱フィン構造。
In a gas boiler having a combustion chamber cover in which a combustion chamber is formed, and a heat exchanger and a gas burner provided in upper and lower portions of the combustion chamber, respectively.
The heat exchanger according to claim 1, wherein the heat exchanger includes a tubular tube through which water circulates, and a plurality of high fins extending radially outward from a plate surface outside the tube. Thermal fin structure.
前記ハイフィンの高さは約9mm以上であることを特徴とする請求項1に記載のガスボイラー用熱交換器の伝熱フィン構造。The heat transfer fin structure of a gas boiler heat exchanger according to claim 1, wherein the height of the high fin is about 9mm or more. 前記ハイフィンは前記チューブに転造加工されることを特徴とする請求項1または2に記載のガスボイラー用熱交換器の伝熱フィン構造。The heat transfer fin structure of a heat exchanger for a gas boiler according to claim 1, wherein the high fin is rolled into the tube.
JP2003145261A 2002-05-23 2003-05-22 Heat transfer fin structure of heat exchanger for gas boiler Pending JP2004003840A (en)

Applications Claiming Priority (1)

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KR1020020028777A KR20030090916A (en) 2002-05-23 2002-05-23 Gas boiler

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014044203A1 (en) * 2012-09-21 2014-03-27 苏州成强换热器有限公司 Forced finned straight pipe condensation heat-supplying heat exchanger
CN104266361A (en) * 2014-09-26 2015-01-07 苏州巨浪热水器有限公司 Heat exchange water tank of gas water heater

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CN104776734A (en) * 2015-04-01 2015-07-15 威能(无锡)供热设备有限公司 Heat exchanger and gas-fired boiler adopting same

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JPS60140045A (en) * 1983-12-28 1985-07-24 Nobuyoshi Kuboyama Instantaneous water heater
JPS6338852A (en) * 1986-07-30 1988-02-19 Dainichi Kogyo Kk Two-waterway heat exchanger
JPH09280657A (en) * 1996-04-11 1997-10-31 Matsushita Electric Ind Co Ltd Heat exchanger
KR200146333Y1 (en) * 1997-01-24 1999-06-15 최병숙 Condensing heat exchanger
KR100296559B1 (en) * 1998-11-13 2001-10-26 전주범 Condensing gas boiler with up and down exhaust
KR200275766Y1 (en) * 2001-11-15 2002-05-16 임관호 Heat Pipe for Collecting Disuse heat

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014044203A1 (en) * 2012-09-21 2014-03-27 苏州成强换热器有限公司 Forced finned straight pipe condensation heat-supplying heat exchanger
CN104266361A (en) * 2014-09-26 2015-01-07 苏州巨浪热水器有限公司 Heat exchange water tank of gas water heater

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