JPH07127911A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPH07127911A
JPH07127911A JP5278634A JP27863493A JPH07127911A JP H07127911 A JPH07127911 A JP H07127911A JP 5278634 A JP5278634 A JP 5278634A JP 27863493 A JP27863493 A JP 27863493A JP H07127911 A JPH07127911 A JP H07127911A
Authority
JP
Japan
Prior art keywords
combustion
exhaust gas
heat exchanger
heat absorption
casing
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.)
Granted
Application number
JP5278634A
Other languages
Japanese (ja)
Other versions
JP2879297B2 (en
Inventor
Masayoshi Takayama
正義 高山
Shinji Umemura
慎二 梅村
Kenji Nakamura
憲司 中村
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.)
Rinnai Corp
Original Assignee
Rinnai Corp
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 Rinnai Corp filed Critical Rinnai Corp
Priority to JP5278634A priority Critical patent/JP2879297B2/en
Publication of JPH07127911A publication Critical patent/JPH07127911A/en
Application granted granted Critical
Publication of JP2879297B2 publication Critical patent/JP2879297B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
  • Details Of Fluid Heaters (AREA)

Abstract

PURPOSE:To make it possible to prevent a clogged state on fins and dew condensation on a heat absorption pipe located above by installing a guide board which guides a combustion exhaust gas current rising along an inner wall in a casing in such a fashion that it may face an area near the upper part of the heat absorption pipe located at the uppermost position in the casing. CONSTITUTION:Since the size of a combustion surface of a burner B is designed to be smaller than a cross section of a casing K, a combustion exhaust gas current is mixed with a combustion exhaust gas rising from the peripheral edge of the combustion face and a fresh air prevailing further on the outer peripheral side of the combustion face where the fresh air component in the exhaust gas is more increased compared with the combustion exhaust gas above the combustion face. Dew condensation is apt to be produced on the top of a heat absorption pipe H located at the uppermost position out of groups of heat absorption pipe H. A guide board 10 is installed so as to face near the heat absorption pipe H at its high position in the upper part of the casing K. Therefore, the mixed gas rising along the inner surface of the casing is guided slightly to the center of the casing by the guide board 10 and reaches the top area of the heat absorption pipe at the uppermost position, thereby preventing the generation of dew condensation in this area.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、熱交換器、特に、缶体
上部にて複数の吸熱管が上下に並設される形式の熱交換
器に関するものであり、熱交換器の結露防止技術に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger, and more particularly to a heat exchanger of a type in which a plurality of endothermic tubes are vertically arranged at the top of a can body. It is about.

【0002】[0002]

【従来技術及び課題】最近の給湯器等の熱交換器では、
小さなスペースで大量の熱交換を可能にする為に、熱交
換器の缶体上部の熱交換部は、相互に平行となる様に並
設された多数のフィンを複数の吸熱管が平行に貫通し、
全体としてはこれら吸熱管が一連となる様に連通接続さ
れて蛇行する。
2. Description of the Related Art In recent heat exchangers such as water heaters,
In order to enable a large amount of heat exchange in a small space, the heat exchange section at the top of the heat exchanger can body has multiple fins that are arranged side by side in parallel with each other, with multiple heat absorption tubes penetrating in parallel. Then
As a whole, these endothermic tubes are connected and connected so as to form a series, and meander.

【0003】この熱交換器の断面構造は図1及び図2の
様になっており、通常は、熱交換効率を向上させる為に
フィン(F) に対して吸熱管(H)(H)は上下に並設されると
共に水平方向にも並設されている。このような熱交換器
では、上記した熱交換部(1) の下方の缶体(K) 内にファ
ン(M) によって燃焼用空気が分散板(S) を介して供給さ
れる形式のバーナ(B) が配設されて、この燃焼排気が前
記熱交換部のフィン(F)(F)間を通過して上昇し、缶体上
端の開放端から排気筒(E) を介して排出される。
The cross-sectional structure of this heat exchanger is as shown in FIGS. 1 and 2, and normally, in order to improve the heat exchange efficiency, the heat absorbing tubes (H) (H) are provided to the fins (F). They are arranged side by side vertically and horizontally. In such a heat exchanger, a burner (a type in which combustion air is supplied through a dispersion plate (S) by a fan (M) into the can body (K) below the heat exchange section (1) is used. B) is arranged, and this combustion exhaust gas passes through between the fins (F) (F) of the heat exchange section to rise, and is discharged from the open end of the upper end of the can body through the exhaust pipe (E). .

【0004】この燃焼排気は、フィン(F) の表面と熱交
換しながら上昇することから、フィン(F) の上端部に近
付くに従って、排気温度が低下する。従って、熱交換効
率が十分な場合には、上方の吸熱管(H)(H)と接触する排
気温度が結露温度近傍にまで低下していることがあり、
この場合、この吸熱管(H)(H)の表面で結露することがあ
る。そして、この結露水により、狭い間隔のフィン(F)
(F)の上端部に於いてフィン詰まりを招来し、最終的に
は燃焼不良を引き起こすことがある。
Since this combustion exhaust rises while exchanging heat with the surface of the fin (F), the exhaust temperature decreases as it approaches the upper end of the fin (F). Therefore, if the heat exchange efficiency is sufficient, the exhaust gas temperature in contact with the upper endothermic pipe (H) (H) may have dropped to near the condensation temperature,
In this case, dew condensation may occur on the surface of the heat absorbing tubes (H) (H). Then, this condensed water causes fins (F) with a narrow space
Fins may be clogged at the upper end of (F), which may eventually cause combustion failure.

【0005】本発明はかかる点に鑑みてなされたもので
あり、『缶体(K) の上部に多数並設されたフィン(F)(F)
を多数の吸熱管(H)(H)が貫通し、これら吸熱管(H)(H)内
に被加熱水を挿通させると共に、前記フィン(F)(F)群の
下方の缶体(K) 内にバーナを配置し、このバーナの燃焼
排気から前記被加熱水に熱交換するようにした熱交換
器』に於いて、フィン詰まりを防止できる様にする為、
上方に位置する吸熱管(H)(H)の表面での結露を防止でき
る様にすることをその課題とする。
The present invention has been made in view of the above point, and is described in detail as follows: "Fin (F) (F) arranged in parallel on the upper part of the can body (K).
A large number of endothermic tubes (H) (H) penetrates, and the heated water is inserted into these endothermic tubes (H) (H), and the cans (K) below the fins (F) (F) group are inserted. ), A burner is placed inside the heat exchanger to heat exchange from the burner exhaust gas to the heated water.
An object of the invention is to prevent condensation on the surface of the heat absorbing tubes (H) (H) located above.

【0006】[0006]

【技術的手段】上記課題を解決するための本発明の技術
的手段は、『缶体(K) 内の内壁に沿って上昇する燃焼排
気流を缶体(K) の内側に案内する案内板(10)を缶体(K)
の上部で最上位に位置する吸熱管(H)(H)の上方近傍に臨
ませた』ことである。
[Technical Means] A technical means of the present invention for solving the above-mentioned problem is to provide a "guide plate for guiding the combustion exhaust flow rising along the inner wall of the can body (K) to the inside of the can body (K). (10) can body (K)
It was made to face the upper end of the endothermic tube (H) (H) in the upper part of.

【0007】[0007]

【作用】上記技術的手段は次のように作用する。一般的
に缶体(K) 内に配設されるバーナの燃焼面は缶体(K) の
横断面よりも小さく設定される。そして、この燃焼面か
らの燃焼排気が缶体(K) 内を上昇してフィン(F)(F)が並
設された熱交換部に達し、吸熱管(H)(H)を流れる被加熱
水に熱交換される。
The above technical means operates as follows. Generally, the combustion surface of the burner arranged in the can body (K) is set smaller than the cross section of the can body (K). Then, the combustion exhaust gas from this combustion surface rises in the can body (K) and reaches the heat exchange section where the fins (F) and (F) are arranged side by side, and the heated pipes (H) and (H) are heated. Heat is exchanged with water.

【0008】前記燃焼面の大きさは缶体(K) の横断面よ
りも小さいことから、缶体(K) の内面に沿って上昇する
燃焼排気流は、燃焼面の周縁部から上昇する燃焼排気
と、燃焼面の更に外周側のフレッシュエアーとが混合し
たものとなり、燃焼排気中のフレッシュエアー成分が燃
焼面の上方の燃焼排気に比べて多いものとなる。上記し
たように吸熱管(H)(H)群のうち最上位の吸熱管(H)(H)の
上面に結露が生じ易いが、案内板(10)を缶体(K) の上部
で最上位に位置する吸熱管(H)(H)の上方近傍に臨ませた
から、缶体(K) の内面に沿って上昇する混合気が、前記
案内板(10)によって缶体の中心よりに案内されて最上位
の吸熱管(H)(H)の上面部分に達する。
Since the size of the combustion surface is smaller than the cross section of the can body (K), the combustion exhaust flow rising along the inner surface of the can body (K) is burned up from the peripheral edge of the combustion surface. The exhaust gas and the fresh air further on the outer peripheral side of the combustion surface are mixed, and the fresh air component in the combustion exhaust gas is larger than that in the combustion exhaust gas above the combustion surface. As mentioned above, dew condensation is likely to occur on the upper surface of the uppermost endothermic tube (H) (H) of the endothermic tube (H) (H) group, but the guide plate (10) is the uppermost part of the can body (K). Since it was exposed near the upper part of the upper endothermic tube (H) (H), the air-fuel mixture rising along the inner surface of the can body (K) was guided from the center of the can body by the guide plate (10). Then, the uppermost heat absorption tubes (H) and (H) are reached.

【0009】この混合気は、上記した様にフレッシュエ
ア−成分の比率が多いものであるから、吸熱管(H)(H)の
上面やその近傍部分で結露しにくいものとなる。なお、
バーナの燃焼面と缶体(K) の横断面との間に殆ど差がな
い形式の熱交換器で、缶体(K) の外部から缶体内の熱交
換部の下方にフレッシュエアーを投入する形式の熱交換
器の場合においても、同様なことがいえる。缶体(K) の
側壁内面に添って上昇する燃焼排気中のフレッシュエア
ー成分が他の部分に比べて多いものとなるから、この場
合にも案内板(10)は同様に機能するからである。
Since the air-fuel mixture has a large proportion of fresh air components as described above, it is difficult for dew to condense on the upper surface of the heat absorbing tubes (H) (H) or in the vicinity thereof. In addition,
There is almost no difference between the burning surface of the burner and the cross section of the can body (K).
A heat exchanger of a different type that allows heat exchange from outside the can (K) to the inside of the can.
Heat exchange of the type in which fresh air is introduced below the exchange section
The same can be said in the case of vessels. Can (K)
Fresh air in combustion exhaust rising along the inner wall surface
-Because the amount of ingredients is higher than other parts,
This is because the guide plate (10) also functions in the same way.

【0010】[0010]

【効果】熱交換器に於ける最も結露し易い部分となる最
上位の吸熱管の上面は燃焼排気中のフレッシュエアー成
分が多いものとなるから、この部分での結露が生じにく
くなり、結露によるフィン詰まりが防止できる。
[Effect] The upper surface of the uppermost heat-absorbing pipe, which is the most condensing part in the heat exchanger, contains a large amount of fresh air components in the combustion exhaust, so that dew condensation is less likely to occur in this part. Fins can be prevented from clogging.

【0011】[0011]

【実施例】次に、上記した本発明の実施例を図面に従っ
て詳述する。 [実施例1]図3に示す実施例1は、図1に示す熱交換
器と同様に、缶体(K) の上部に熱交換部(1) が設けら
れ、この熱交換部はフィン(F)(F)が一定の間隔で並設さ
れ、これに上下及び水平方向に並設された複数の吸熱管
(H)(H)が前記フィン(F)(F)を貫通し、これら吸熱管(H)
(H)が直列に連通されて全体的には蛇行した被加熱回路
となり、この缶体(K) の下部にバーナ(B) が収容され
る。
Embodiments of the present invention described above will now be described in detail with reference to the drawings. [Embodiment 1] In Embodiment 1 shown in FIG. 3, similarly to the heat exchanger shown in FIG. 1, a heat exchanging portion (1) is provided on an upper portion of a can body (K), and this heat exchanging portion has fins ( F) (F) are arranged in parallel at a fixed interval, and a plurality of endothermic tubes are arranged in parallel in the vertical and horizontal directions.
(H) (H) penetrates the fins (F) (F), and these endothermic tubes (H)
(H) is connected in series to form a meandering heated circuit as a whole, and the burner (B) is housed in the lower part of the can body (K).

【0012】この熱交換器の横断面は、図3のように構
成され、上段の3つの吸熱管(H)(H)と、中段の2つの吸
熱管(H)(H)と、下段の3つの吸熱管(H)(H)がフィン(F)
(F)を貫通する。下段の各吸熱管(H) の上方に夫々上段
の各吸熱管(H) が配設され、中段の吸熱管(H) は、下段
及び上段の吸熱管(H)(H)の中間に位置する。そして、被
加熱水は下段の一方の端部の吸熱管(H) から入水されて
他端の吸熱管(H) から中段の吸熱管(H)(H)に至り、その
後、上段の吸熱管(H)(H)を通って出湯される。
The cross section of this heat exchanger is constructed as shown in FIG. 3, and includes three upper endothermic tubes (H) and (H), two middle endothermic tubes (H) and (H), and a lower one. Three endothermic tubes (H) (H) are fins (F)
Go through (F). The upper endothermic tubes (H) are arranged above the lower endothermic tubes (H), and the middle endothermic tubes (H) are located between the lower and upper endothermic tubes (H) (H). To do. Then, the water to be heated enters from the endothermic pipe (H) at one end of the lower stage and reaches the endothermic pipe (H) (H) at the other end from the endothermic pipe (H) at the other end, and then the endothermic pipe at the upper stage. Hot water is discharged through (H) (H).

【0013】なお、この下方に配設されるバーナ(B) の
燃焼面(B1)は、缶体(K) の断面よりも小さくなってお
り、バーナ(B) と缶体(K) の間をフラッシュエアーが流
れる様になっている。このフレッシュエアーは缶体(K)
を冷却してこれの熱歪み等を防止する。また、缶体(K)
は矩形断面の直方体の箱となっており、左右に長く前後
に短い扁平な箱体に構成されている。そして、前記各吸
熱管(H) は左右に延びる様に配設されている。
The combustion surface (B 1 ) of the burner (B) disposed below this is smaller than the cross section of the can body (K), and the burner (B) and the can body (K) are Flash air flows between them. This fresh air is a can (K)
To prevent heat distortion and the like. Also, can body (K)
Is a rectangular parallelepiped box with a rectangular cross section, and is configured as a flat box that is long in the left and right and short in the front and back. The heat absorbing tubes (H) are arranged so as to extend left and right.

【0014】缶体(K) の内面上部で前面壁及び後面壁の
上端近傍には、缶体(K) の側壁から内側に屈曲する案内
板(10)(10)がこれら側壁の略全域に取付けられており、
その突出端部は上段の両側の吸熱管(H)(H)の断面中心上
方に臨ませている。この実施例のものでは、上段の吸熱
管(H)(H)の内の両側に位置する吸熱管(H)(H)の上面部に
結露が生じ易いが、既述した作用により、燃焼面(B1)か
ら外れた部分から上昇するフレッシュエアーが缶体(K)
の内面に添って上昇することから、案内板(10)によって
内側に屈曲されて上段両側の吸熱管(H)(H)の上面に達す
る燃焼排気はエアーリッチなものとなり、この部分での
結露を抑制する。この部分に達する燃焼排気の湿り度合
いが他の部分に比べて大幅に少ないから、最も結露が生
じ易い部分での結露が確実に防止できるのである。ま
た、熱交換部(1) に対するバーナ(B) の燃焼面(B1)の関
係、及び、前記バーナ(B) を収容するバーナ箱に燃焼用
空気をファン(M) によって強制的に分散板(S) を介して
供給する方式を採用している点では、図1のものと同様
である。
In the upper part of the inner surface of the can body (K) and near the upper ends of the front wall and the rear wall, guide plates (10) (10) bent inward from the side wall of the can body (K) are provided over substantially the entire area of these side walls. Is installed,
The projecting ends are located above the center of the cross sections of the heat absorbing tubes (H) (H) on both sides of the upper stage. In this embodiment, dew condensation is likely to occur on the upper surface of the heat absorption tubes (H) (H) located on both sides of the upper end heat absorption tubes (H) (H), but due to the above-described action, the combustion surface The fresh air rising from the part outside (B 1 ) cans (K)
As it rises along the inner surface of the combustion chamber, the combustion exhaust gas that is bent inward by the guide plate (10) and reaches the upper surface of the endothermic tubes (H) and (H) on both sides of the upper stage becomes air-rich, and dew condensation at this part occurs. Suppress. Since the degree of wetness of the combustion exhaust gas reaching this portion is significantly smaller than that of the other portions, it is possible to reliably prevent dew condensation at the portion where dew condensation is most likely to occur. In addition, the relationship between the combustion surface (B 1 ) of the burner (B) with respect to the heat exchange section (1) and the combustor air forcibly distributed by the fan (M) in the burner box containing the burner (B). It is similar to that of FIG. 1 in that the method of supplying via (S) is adopted.

【0015】[実施例2]次に、図4に示す実施例2
は、上記対策に加えて上段中央部での結露が生じない様
にするものであり、この実施例では、上段の吸熱管(H)
(H)を実施例1における両側の吸熱管(H)(H)のみとした
ものである。下段の吸熱管(H) では結露が殆ど生じない
が、上段に行くに従って、吸熱管(H) に結露が生じ易い
傾向にある。
[Second Embodiment] Next, a second embodiment shown in FIG.
In addition to the above measures, is to prevent dew condensation in the central part of the upper stage, in this embodiment, the endothermic tube (H) of the upper stage
(H) is only the heat absorbing tubes (H) and (H) on both sides in Example 1. Condensation hardly occurs in the lower endothermic tube (H), but it tends to occur in the upper end tube (H) as it goes up.

【0016】従って、上段中央に位置する吸熱管(H) に
も結露が生じる可能性がなくはないが、この実施例で
は、この部分に吸熱管(H) がなく、両側の吸熱管(H)(H)
の上方には、実施例1と同様に案内板(10)(10)を臨ませ
ているから、熱交換器全体に於ける結露防止効果が一層
確実となる。 [実施例3]なお、上記構成の場合、結露防止効果が向
上するものの、中段の吸熱管(H)(H)の間を通過する燃焼
排気は直接外部に排出されるから、熱交換効率の点で不
十分となる。この不都合を解消するには、図5及び図6
に示す様に、上段の両側の吸熱管(H)(H)の中間にフィン
(F) から突出する隆起部(F1)を設け、この隆起部(F1)の
頂面が隣接するフィン(F) に対接する構成とすれば良
い。この場合、中段の吸熱管(H)(H)の間を通過した燃焼
排気は前記隆起部(F1)の断面下部によって両側に偏向さ
れて上段両側の吸熱管(H)(H)に達することとなることか
ら、この部分の燃焼排気が吸熱管(H)(H)を加熱すること
なくそのまま排出される不都合が解消できる。
Therefore, there is a possibility that dew condensation may occur in the endothermic tube (H) located at the center of the upper stage, but in this embodiment, there is no endothermic tube (H) in this portion, and the endothermic tubes (H ) (H)
Since the guide plates (10) and (10) face the upper part of the heat exchanger as in the first embodiment, the effect of preventing dew condensation in the entire heat exchanger becomes more reliable. [Embodiment 3] In the case of the above configuration, although the dew condensation prevention effect is improved, the combustion exhaust gas passing between the intermediate heat absorption tubes (H) and (H) is directly discharged to the outside, so that the heat exchange efficiency is improved. In terms of being insufficient. In order to eliminate this inconvenience, FIG. 5 and FIG.
As shown in, the fins are placed in the middle of the heat absorbing tubes (H) (H) on both sides of the upper stage.
A ridge (F 1 ) protruding from (F) may be provided, and the top surface of the ridge (F 1 ) may be in contact with the adjacent fin (F). In this case, the combustion exhaust gas passing between the middle-stage endothermic tubes (H) (H) is deflected to both sides by the lower section of the ridge (F 1 ) and reaches the upper-end side endothermic tubes (H) (H). Therefore, it is possible to eliminate the inconvenience that the combustion exhaust gas in this portion is discharged as it is without heating the heat absorption tubes (H) (H).

【0017】上記各実施例の結露防止作用についてさら
に詳述する。ところで、露点と燃焼排気の空気比との関
係は、図7のような関係にあり、空気比が高くなるに従
って、露点は低下する。一方、缶体(K) の側壁の近傍の
排気流の空気比は、通常の給湯器の熱交換器では、図8
のような関係にあり、缶体(K) の内壁から遠ざかるに従
って空気比が低くなり、缶体(K) の内壁に沿って流れる
排気流の空気比は最大で2.1程度である。案内板(10)
を設けないものでは、缶体(K) の側壁内面から離れた排
気流で空気比1.5程度の排気のみが前記上段の吸熱管
(H) で且缶体(K) の側壁内面の近傍に位置する吸熱管
(H) に接触することととなり、この場合、この吸熱管
(H) の上面に同図のような結露が生じる。ところが、上
記した様に前記吸熱管(H) の上方近傍に案内板(10)を設
けると、図9の様に、缶体(K) の側壁内面を沿って流れ
る空気比の高い(2.1程度)燃焼排気が混入されて前
記吸熱管(H) に接触することとなり、露点が上昇して結
露が防止できる。
The dew condensation preventing action of each of the above embodiments will be described in more detail. By the way, the relationship between the dew point and the air ratio of the combustion exhaust gas is as shown in FIG. 7, and the higher the air ratio, the lower the dew point. On the other hand, the air ratio of the exhaust flow near the side wall of the can body (K) is
The air ratio decreases with distance from the inner wall of the can body (K), and the air ratio of the exhaust flow flowing along the inner wall of the can body (K) is about 2.1 at maximum. Information board (10)
In the case where the above is not provided, only the exhaust gas having an air ratio of about 1.5 in the exhaust flow away from the inner surface of the side wall of the can body (K) is in the upper end heat-absorbing tube.
(H) and endothermic tube located near the inner surface of the side wall of the can body (K)
It comes into contact with (H). In this case, this endothermic tube
Condensation occurs on the upper surface of (H) as shown in the figure. However, when the guide plate (10) is provided near the upper end of the heat absorbing tube (H) as described above, the ratio of air flowing along the inner surface of the side wall of the can body (K) is high (2. (About 1) Combustion exhaust gas is mixed and comes into contact with the endothermic tube (H), and the dew point rises to prevent dew condensation.

【0018】なお、上記各実施例では、各別に設けた案
内板(10)(10)を缶体(K) の内面に添設したが、缶体(K)
の上端に止着してもよい。例えば、図10、図11に示
すような枠体(11)の周縁部が、缶体(K) のフランジと排
気筒(E) のフランジとの間に挟圧され、前記両フランジ
をカシメ止め、ネジ止め、溶着等で結合することにより
止着される様にしてもよい。枠体(11)に於ける長辺が缶
体(K) の上端から内側に突出する突出片(12)(12)とな
り、これが前記案内板(10)(10)として機能することとな
るからである。この場合、枠体(11)の長辺の外側から下
方に屈曲させた舌片(13)が缶体(K) 内に嵌入され、位置
決め手段として機能することとなる。
In each of the above embodiments, the guide plates (10) (10) provided separately are attached to the inner surface of the can body (K).
It may be attached to the upper end of. For example, the peripheral edge of the frame body (11) as shown in FIGS. 10 and 11 is clamped between the flange of the can body (K) and the flange of the exhaust pipe (E), and the both flanges are caulked. Alternatively, they may be fixed by screwing, welding or the like. The long side of the frame body (11) serves as a protruding piece (12) (12) protruding inward from the upper end of the can body (K), and this will function as the guide plates (10) (10). Is. In this case, the tongue piece (13) bent downward from the outside of the long side of the frame body (11) is fitted into the can body (K) and functions as a positioning means.

【0019】この場合、枠体(11)の取付によって前記突
出片(12)が上記各実施例の場合と同様に上段の吸熱管
(H) の上方近傍に位置する様に構成されることは言うま
でもない。上記何れの実施例も、缶体(K) 内には燃焼用
空気を含めて缶体底部のみからフレッシュエアーを供給
するようにしてるが、別経路でフレッシュエアーを投入
する方式の熱交換器にも本発明は利用できる。
In this case, by mounting the frame body (11), the projecting piece (12) has the upper endothermic tube as in the above-mentioned respective embodiments.
It goes without saying that it is configured so as to be located near the upper part of (H). In any of the above examples, the fresh air is supplied only from the bottom of the can body including the combustion air in the can body (K), but in a heat exchanger of the type in which fresh air is fed in through another route. The present invention can also be used.

【0020】又、このフレッシュエアーが缶体(K) の温
度を下げる効果に加えて、二次空気供給用又は白煙防止
用の空気として機能する場合もあり、主としてこの後者
のために供給されるフレッシュエアーであってもよい。
In addition to the effect of lowering the temperature of the can body (K), this fresh air may function as secondary air supply air or white smoke prevention air, and is mainly supplied for the latter. It may be fresh air.

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

【図1】従来例の説明図FIG. 1 is an explanatory diagram of a conventional example.

【図2】その熱交換部(1) の詳細断面図[Fig. 2] Detailed sectional view of the heat exchange section (1).

【図3】本発明の実施例1の要部断面図FIG. 3 is a sectional view of a main part of the first embodiment of the present invention.

【図4】実施例2の要部断面図FIG. 4 is a cross-sectional view of a main part of the second embodiment.

【図5】実施例3の熱交換部(1) の要部断面図FIG. 5 is a sectional view of an essential part of a heat exchange section (1) of Example 3.

【図6】そのX−X断面図FIG. 6 is a sectional view taken along line XX.

【図7】空気比と露点との関係図[Fig. 7] Relational diagram of air ratio and dew point

【図8】結露が生じる場合の熱交換部(1) の要部詳細図[Figure 8] Detailed view of the main part of the heat exchange part (1) when condensation occurs

【図9】案内板(10)を設けた場合の排気流の詳細図[Fig. 9] Detailed view of exhaust flow when a guide plate (10) is provided

【図10】案内板(10)を装備させる場合の他の例の説明
FIG. 10 is an explanatory view of another example in which the guide plate (10) is equipped.

【図11】枠体(11)を装着した状態の要部断面図FIG. 11 is a cross-sectional view of main parts with the frame body (11) attached.

【符号の説明】[Explanation of symbols]

(K) ・・・缶体 (F) ・・・フィン (H) ・・・吸熱管 (F1)・・・隆起部 (10)・・・案内板(K) ・ ・ ・ Can body (F) ・ ・ ・ Fin (H) ・ ・ ・ Endothermic tube (F 1 ) ・ ・ ・ Raised part (10) ・ ・ ・ Guide plate

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 缶体(K) の上部に多数並設されたフィン
(F)(F)を多数の吸熱管(H)(H)が貫通し、これら吸熱管
(H)(H)内に被加熱水を挿通させると共に、前記フィン
(F)(F)群の下方の缶体(K) 内にバーナを配置し、このバ
ーナの燃焼排気から前記被加熱水に熱交換するようにし
た熱交換器に於いて、缶体(K) 内の内壁に沿って上昇す
る燃焼排気流を缶体(K) の内側に案内する案内板(10)を
缶体(K) の上部で最上位に位置する吸熱管(H)(H)の上方
近傍に臨ませた熱交換器。
1. A plurality of fins arranged in parallel on an upper part of a can body (K)
(F) (F) is penetrated by many endothermic tubes (H) and (H),
(H) Insert the water to be heated in (H) and
(F) In a heat exchanger in which a burner is arranged in the lower can body (K) of the (F) group, and heat is exchanged from the combustion exhaust of the burner to the heated water, the can body (K The guide plate (10) that guides the combustion exhaust flow rising along the inner wall of the inside of the can body (K) to the inside of the can body (K) is the heat absorption pipes (H) (H) located at the top of the can body (K). Heat exchanger facing near the upper part of.
【請求項2】 最上位に位置する吸熱管(H) (H) が缶体
(K) の対向側壁内面に沿ってその近傍にのみ配設される
ようにした請求項1に記載の熱交換器。
2. The endothermic tube (H) (H) located at the top is a can body.
The heat exchanger according to claim 1, wherein the heat exchanger is arranged along the inner surface of the opposing side wall of (K) only in the vicinity thereof.
【請求項3】 各フィン(F) における最上位に位置する
吸熱管(H) (H) の中間部に隆起部(F1)を突出させてその
頂面を隣接する一方のフィン(F) に対接させる様にした
請求項2に記載の熱交換器。
3. One of the fins (F) adjacent to the top surface of the fin (F) by projecting a ridge (F 1 ) in the middle of the uppermost endothermic tube (H) (H) The heat exchanger according to claim 2, wherein the heat exchanger is in contact with the heat exchanger.
JP5278634A 1993-11-08 1993-11-08 Heat exchanger Expired - Fee Related JP2879297B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5278634A JP2879297B2 (en) 1993-11-08 1993-11-08 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5278634A JP2879297B2 (en) 1993-11-08 1993-11-08 Heat exchanger

Publications (2)

Publication Number Publication Date
JPH07127911A true JPH07127911A (en) 1995-05-19
JP2879297B2 JP2879297B2 (en) 1999-04-05

Family

ID=17600013

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5278634A Expired - Fee Related JP2879297B2 (en) 1993-11-08 1993-11-08 Heat exchanger

Country Status (1)

Country Link
JP (1) JP2879297B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000234809A (en) * 1999-02-10 2000-08-29 Rinnai Corp Heat exchanger
CN100416174C (en) * 2001-07-02 2008-09-03 林内株式会社 Heat exchanger
KR20160050731A (en) * 2014-10-30 2016-05-11 린나이코리아 주식회사 Body and heat exchanger having the same
JP2018031551A (en) * 2016-08-26 2018-03-01 株式会社ノーリツ Method for manufacturing burner case and burner case

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49124661A (en) * 1972-09-12 1974-11-28
JPS50134168U (en) * 1974-04-19 1975-11-05
JPS5137651U (en) * 1974-09-14 1976-03-19
JPH0160152U (en) * 1987-10-09 1989-04-17
JPH0377154U (en) * 1989-11-27 1991-08-02

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49124661A (en) * 1972-09-12 1974-11-28
JPS50134168U (en) * 1974-04-19 1975-11-05
JPS5137651U (en) * 1974-09-14 1976-03-19
JPH0160152U (en) * 1987-10-09 1989-04-17
JPH0377154U (en) * 1989-11-27 1991-08-02

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000234809A (en) * 1999-02-10 2000-08-29 Rinnai Corp Heat exchanger
CN100416174C (en) * 2001-07-02 2008-09-03 林内株式会社 Heat exchanger
KR20160050731A (en) * 2014-10-30 2016-05-11 린나이코리아 주식회사 Body and heat exchanger having the same
JP2018031551A (en) * 2016-08-26 2018-03-01 株式会社ノーリツ Method for manufacturing burner case and burner case

Also Published As

Publication number Publication date
JP2879297B2 (en) 1999-04-05

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