JPS6161022B2 - - Google Patents

Info

Publication number
JPS6161022B2
JPS6161022B2 JP56075202A JP7520281A JPS6161022B2 JP S6161022 B2 JPS6161022 B2 JP S6161022B2 JP 56075202 A JP56075202 A JP 56075202A JP 7520281 A JP7520281 A JP 7520281A JP S6161022 B2 JPS6161022 B2 JP S6161022B2
Authority
JP
Japan
Prior art keywords
outer shell
shell
heat exchanger
protrusion
combustion chamber
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
Application number
JP56075202A
Other languages
Japanese (ja)
Other versions
JPS57188959A (en
Inventor
Takehiro Nagatoshi
Tomomasa Bandai
Yoshiaki Inui
Shuji Ochiai
Hajime Satoda
Mitsutomo Yoshida
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP7520281A priority Critical patent/JPS57188959A/en
Publication of JPS57188959A publication Critical patent/JPS57188959A/en
Publication of JPS6161022B2 publication Critical patent/JPS6161022B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/22Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
    • F24H1/24Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water mantle surrounding the combustion chamber or chambers
    • F24H1/26Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water mantle surrounding the combustion chamber or chambers the water mantle forming an integral body
    • F24H1/263Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water mantle surrounding the combustion chamber or chambers the water mantle forming an integral body with a dry-wall combustion chamber

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 本発明は気体等の流体を流通させて熱交換を行
なう暖房用または給湯用に使用する熱交換器に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger used for heating or hot water supply, which exchanges heat by circulating a fluid such as gas.

従来は、筒状の燃焼室の上部または側面部の開
口にバーナを嵌合させ、バーナより放出された燃
料を燃焼室で燃焼させ、排出口より放出するタイ
プの熱交換器においては、熱交換効率を向上する
ために、燃焼室内にバツフル等の抵抗体を装備し
たりしていた。
Conventionally, in heat exchangers, a burner is fitted into an opening at the top or side of a cylindrical combustion chamber, and the fuel released from the burner is combusted in the combustion chamber and discharged from the exhaust port. In order to improve efficiency, a resistor such as a buttful was installed inside the combustion chamber.

しかし上記構成では、熱交換器の中央部を流れ
る燃焼ガスは熱交換器壁と接することなくそのま
ま流れる。すなわちガスと熱交換壁との接触度合
が悪いため熱交換効率は十分向上されず、同様に
放熱フイン等を装備したものについても、高温ガ
スにより高温に加熱される燃焼室壁および熱交換
器内壁や放熱フインと被熱媒体との距離が長く、
熱移動がスムーズに行なわれないため熱交換効果
がそれほど高くなかつた。また加工面において
も、燃焼室と熱交換器の溶接等が複雑になつた
り、流路に屈折部を設けたりすると流路抵抗が著
しく増え、流路抵抗が増えると燃焼室内圧も著し
く大きくなりバーナ、燃焼に大きな支障を与えて
いた。
However, in the above configuration, the combustion gas flowing through the center of the heat exchanger flows as it is without coming into contact with the heat exchanger wall. In other words, the degree of contact between the gas and the heat exchanger wall is poor, so the heat exchange efficiency cannot be sufficiently improved. Similarly, even in devices equipped with heat radiation fins, the combustion chamber wall and the heat exchanger inner wall are heated to a high temperature by the high-temperature gas. or the distance between the heat dissipation fins and the heated medium is long,
Since heat transfer was not carried out smoothly, the heat exchange effect was not very high. Also, in terms of machining, if welding between the combustion chamber and the heat exchanger becomes complicated, or if bends are provided in the flow path, the flow path resistance will increase significantly, and as the flow path resistance increases, the pressure in the combustion chamber will also increase significantly. The burner was causing a major hindrance to combustion.

本発明はこのような欠点を解消したもので、以
下その一実施例を説明する。
The present invention eliminates these drawbacks, and one embodiment thereof will be described below.

燃焼室を形成する外胴1はバーナ7側が広いテ
ーパ状で、燃焼室3側へ突出した円形(第2
図)、楕円形(第3図)の平面を有する個々の独
立した多数の突起部(突部)2を有し、その配列
は等間隔(第4図)あるいはランダム(第5図)
に行なう。外胴1底部と反対近傍の外胴1上部に
熱交換媒体である燃焼ガスの排出口8を装備して
いる。
The outer shell 1 that forms the combustion chamber has a tapered shape that is wide on the burner 7 side, and has a circular (second round) shape that protrudes toward the combustion chamber 3 side.
(Fig.), has a large number of independent protrusions (protrusions) 2 with elliptical (Fig. 3) planes, and their arrangement can be at regular intervals (Fig. 4) or randomly (Fig. 5).
go to A discharge port 8 for combustion gas, which is a heat exchange medium, is provided at the top of the outer shell 1 in the opposite vicinity to the bottom of the outer shell 1.

外胴1底部と反対面は次に説明する内胴、およ
びバーナ7の押入を行うための開口となつてい
る。
The surface opposite to the bottom of the outer shell 1 is an opening into which an inner shell and a burner 7, which will be described next, are inserted.

無底筒状の内胴4は、外胴1同様バーナ7側が
広いテーパ状で外胴1に有した多数の突起部2の
平面に密着するような径にし、無底部片方を外胴
1内面に密着するように拡管した構成である。
Like the outer shell 1, the bottomless cylindrical inner shell 4 has a tapered shape with a wide side on the burner 7 side, and has a diameter such that it comes into close contact with the plane of the many protrusions 2 on the outer shell 1, and one side of the bottomless part is attached to the inner surface of the outer shell 1. The tube is expanded so that it comes into close contact with the tube.

外胴1の底部反対面開口より、内胴4を圧入す
る事で、内胴4の拡管部と外胴1が密着され、ま
た内胴4、外胴1間には突起部2により燃焼ガス
の流路6が形成される。
By press-fitting the inner shell 4 through the opening on the opposite side of the bottom of the outer shell 1, the expanded tube part of the inner shell 4 and the outer shell 1 are brought into close contact, and the protrusion 2 between the inner shell 4 and the outer shell 1 allows combustion gas to be A flow path 6 is formed.

上記組み合せで、バーナ7より放出された燃料
は燃焼室3で燃焼し燃焼ガスとなり、バーナ7と
反対側の外胴1と内胴4のすきまより、流路6へ
流入し、外胴1上部の排気口8より器外へ放出さ
れる。
With the above combination, the fuel released from the burner 7 burns in the combustion chamber 3 and becomes combustion gas, which flows into the flow path 6 through the gap between the outer shell 1 and the inner shell 4 on the opposite side of the burner 7, and flows into the upper part of the outer shell 1. is discharged outside the device from the exhaust port 8.

燃焼室3内の燃焼ガスは、内胴4より熱を奪わ
れる。その熱が内胴4と外胴1の突起部2の密着
面10を伝わり器外の被熱交換媒体9(水)へ放
熱される。また、流路6を通過する際に燃焼ガス
はその大部分が外胴1の内壁および突起部2に強
制的に接触して流路接触面より熱を奪われ被熱交
換媒体9へ放熱される。さらに突起部2はその配
列によりガスの流れを整流および乱流、スパイラ
ル状にして胴体との接触面積を増やす事もでき
る。
The combustion gas in the combustion chamber 3 loses heat from the inner shell 4. The heat is transmitted through the contact surfaces 10 of the projections 2 of the inner shell 4 and the outer shell 1, and is radiated to the heat exchange medium 9 (water) outside the vessel. Furthermore, when passing through the flow path 6, most of the combustion gas is forced into contact with the inner wall of the outer shell 1 and the protrusion 2, and heat is removed from the flow path contact surface and radiated to the heat exchange medium 9. Ru. Furthermore, the arrangement of the protrusions 2 allows the gas flow to be rectified, turbulent, or spiral, thereby increasing the contact area with the body.

また外胴1の突起部2を第6図のごとくスパイ
ラル状に形成すると突起部2と外胴1との接触面
積が増えることになり燃焼室3内の燃焼ガスのよ
り有効な活用が図れる。
Further, if the protrusion 2 of the outer shell 1 is formed in a spiral shape as shown in FIG. 6, the contact area between the protrusion 2 and the outer shell 1 increases, so that the combustion gas in the combustion chamber 3 can be used more effectively.

以上の説明から明らかなように本発明では次の
ような効果が得られる。
As is clear from the above description, the following effects can be obtained in the present invention.

内外胴により2重筒状にしたので内胴内の熱
交換媒体を内外胴間に通してその大部分を熱交
換に利用できるとともに内胴と外胴を突部で密
着させる事により、内胴内の高温ガスも有効に
活用が出来、トータルの熱交換効率は著しく向
上し省エネルギーにも結びつく。
Since it has a double cylindrical shape with the inner and outer shells, the heat exchange medium in the inner shell can be passed between the inner and outer shells and most of it can be used for heat exchange. The high-temperature gas inside can also be used effectively, significantly improving the total heat exchange efficiency and leading to energy savings.

また内胴と外胴をテーパ状にしているので両
者間に少々の寸法誤差があつても圧入する事に
より、突起部と外胴とを確実に密着させること
ができるとともに気密性を必要とする溶接等が
不要となり加工コストの低減に結びつく。
In addition, since the inner and outer shells are tapered, even if there is a slight dimensional error between the two, by press-fitting, the protrusion and the outer shell can be reliably brought into close contact, and airtightness is required. This eliminates the need for welding, etc., leading to a reduction in processing costs.

また外胴は被熱交換媒体と接していて比較的
低温に維持されるので例え多数の突部を設けて
いて複雑な熱収縮力が加わるような場合であつ
てもその熱変形は少なく長期間にわたつての使
用が可能となる。
In addition, since the outer shell is in contact with the heat exchange medium and is maintained at a relatively low temperature, even if it has many protrusions and is subjected to complex thermal contraction forces, its thermal deformation is small and long-term. It can be used for many years.

なお、外胴に独立した多数の突部、スパイラル
状の突部を設けたので被熱交換媒体との伝熱面積
が大きく取れ、小形でコンパクトな熱交換器が得
られる。
In addition, since a large number of independent protrusions and spiral protrusions are provided on the outer shell, a large heat transfer area with the heat exchange medium can be obtained, and a small and compact heat exchanger can be obtained.

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

第1図は本発明の一実施例にかかる熱交換器の
断面図、第2図は外胴の斜視図、第3図は他の外
胴の断面図、第4〜第6図は他の外胴の斜視図で
ある。 1……外胴、2……突起部(突部)、3……燃
焼室、4……内胴、7……バーナ。
Fig. 1 is a sectional view of a heat exchanger according to an embodiment of the present invention, Fig. 2 is a perspective view of an outer shell, Fig. 3 is a sectional view of another outer shell, and Figs. 4 to 6 are a sectional view of another outer shell. It is a perspective view of an outer body. 1...Outer shell, 2...Protrusion (protrusion), 3...Combustion chamber, 4...Inner shell, 7...Burner.

Claims (1)

【特許請求の範囲】 1 燃焼室を形成する外胴と、この外胴内に配設
した内胴とからなり、上記内、外胴間に熱交換媒
体が通る間隙を形成するとともに、外胴に内胴へ
接する突部を設け、かつ上記外胴と内胴をテーパ
ー状に形成し、外胴は前記内胴を圧入嵌合させた
熱交換器。 2 突部は個々に独立した多数の小突起からなる
ことを特徴とする特許請求の範囲第1項に記載の
熱交換器。 3 突部はスパイラル状の突条からなることを特
徴とする特許請求の範囲第1項に記載の熱交換
器。
[Claims] 1. Consisting of an outer shell forming a combustion chamber and an inner shell disposed within the outer shell, a gap is formed between the inner and outer shells through which a heat exchange medium passes, and the outer shell The heat exchanger is provided with a protrusion that contacts the inner shell, the outer shell and the inner shell are formed into a tapered shape, and the outer shell is press-fitted with the inner shell. 2. The heat exchanger according to claim 1, wherein the protrusions are composed of a large number of individually independent small protrusions. 3. The heat exchanger according to claim 1, wherein the protrusion is formed of a spiral protrusion.
JP7520281A 1981-05-18 1981-05-18 Heat exchanger Granted JPS57188959A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7520281A JPS57188959A (en) 1981-05-18 1981-05-18 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7520281A JPS57188959A (en) 1981-05-18 1981-05-18 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS57188959A JPS57188959A (en) 1982-11-20
JPS6161022B2 true JPS6161022B2 (en) 1986-12-23

Family

ID=13569369

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7520281A Granted JPS57188959A (en) 1981-05-18 1981-05-18 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS57188959A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59139843U (en) * 1983-03-08 1984-09-18 高村 公弥 Tank fluid heating device
DE3602706A1 (en) * 1986-01-30 1987-08-06 Nargang Gudrun Heating boiler
DE19749821C1 (en) * 1997-11-11 1999-03-18 Webasto Thermosysteme Gmbh Combustion heater for motor vehicle

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5246365U (en) * 1975-09-30 1977-04-01

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5246365U (en) * 1975-09-30 1977-04-01

Also Published As

Publication number Publication date
JPS57188959A (en) 1982-11-20

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