JPS6231821Y2 - - Google Patents

Info

Publication number
JPS6231821Y2
JPS6231821Y2 JP1982020990U JP2099082U JPS6231821Y2 JP S6231821 Y2 JPS6231821 Y2 JP S6231821Y2 JP 1982020990 U JP1982020990 U JP 1982020990U JP 2099082 U JP2099082 U JP 2099082U JP S6231821 Y2 JPS6231821 Y2 JP S6231821Y2
Authority
JP
Japan
Prior art keywords
plate
heat exchanger
drain
bodies
water heater
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
JP1982020990U
Other languages
Japanese (ja)
Other versions
JPS58124731U (en
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 filed Critical
Priority to JP2099082U priority Critical patent/JPS58124731U/en
Publication of JPS58124731U publication Critical patent/JPS58124731U/en
Application granted granted Critical
Publication of JPS6231821Y2 publication Critical patent/JPS6231821Y2/ja
Granted legal-status Critical Current

Links

Description

【考案の詳細な説明】 この考案は熱交換において排気ガスよりドレン
(凝縮水)が発生する湯沸器に関し、そのドレン
回収構造に改良を施してドレン回収の確実性と燃
焼排ガス分布の均一性を図つて熱効率の向上等を
企図したものである。
[Detailed explanation of the invention] This invention relates to water heaters that generate condensate (condensed water) from exhaust gas during heat exchange, and improves the condensate recovery structure to ensure reliable condensate recovery and uniform combustion exhaust gas distribution. This is intended to improve thermal efficiency, etc.

従来、ガス湯沸器におけるドレン回収手段とし
て例えば上下に離間して熱交換器を配設し、上段
の熱交換器と下段の熱交換器との間に第6図に示
したようにドレン受板1′の中央に穿つた通気口
2′の直上に一定の間隙を存して該通気口2′を覆
隠する覆板1″を設け、かつドレン受板1′の上面
一側をドレン排水口3′に連通させた構造とし
て、下段の熱交換器B′を通過した燃焼排ガスが通
気口2′を通つてドレン受板1′と覆板1″との間
隙を通じて上方に導かれて上段の熱交換器A′に
接触通過し(第6図矢印b′参照)該部において低
温となつた燃焼排ガスから凝縮したドレンがドレ
ン受板1′上に滴下して溜り、その溜つたドレン
は一側のドレン排水口3′へ導かれるようにした
もの、又は第7図に示したように多数の通気口
2′を等間隔を保つて列穿した下板1′と、同じく
多数の通気口2″を等間隔を保つて列穿した上板
1″を通気口2′,2″の位置を異ならせてそれぞ
れの通気口2′,2″を上下からみて互いに覆隠す
るように上下に一定の間隙を存して並設し、かつ
下板1′の上面一側をドレン排水口3′に連通させ
た構造として、下段の熱交換B′を通過した燃焼排
ガスが上下板1′,1″の変位せる通気口2′,
2″を迂回して流過し上方に導かれて上段の熱交
換器A′に接触通過し(第7図矢印b″参照)前記
と同様に下板1′上に溜つたドレンは一側のドレ
ン排水口3′へ導かれるようにしたものはすでに
公知であるが、特に前者にあつては上段の熱交換
器A′に対する燃焼排ガスがその外周部を集中的
に流過するため、燃焼排ガスの分布が悪いことに
よる熱交換器A′の全体的効果が悪く、また後者
にあつては燃焼排ガスが上下の通気口2′,2″を
通過するときの抵抗が大きく、その加工工数が多
く多くの手数を要するなどの欠点があつた。
Conventionally, as a drain recovery means in a gas water heater, for example, heat exchangers are arranged vertically apart, and a drain receiver is installed between the upper heat exchanger and the lower heat exchanger as shown in Fig. 6. A cover plate 1'' is provided directly above a vent hole 2' bored in the center of the plate 1', leaving a certain gap to cover the vent hole 2'. The structure is connected to the drain port 3', so that the combustion exhaust gas that has passed through the lower heat exchanger B' is guided upward through the vent port 2' and through the gap between the drain receiving plate 1' and the cover plate 1''. Condensate condensed from the combustion exhaust gas that passed through the upper heat exchanger A' (see arrow b' in Figure 6) and became low temperature in this section drips and accumulates on the drain receiving plate 1', and the accumulated condensate A lower plate 1' with a number of vent holes 2' bored in rows at equal intervals as shown in Fig. The upper plate 1'' has ventilation holes 2'' drilled in rows at equal intervals, and the ventilation holes 2' and 2'' are placed in different positions so that the ventilation holes 2' and 2'' are hidden from each other when viewed from above and below. The upper and lower plates 1' are arranged side by side with a certain gap between them, and one side of the upper surface of the lower plate 1' is connected to the drain outlet 3'. ', 1'' displaceable vent 2',
The condensate that has accumulated on the lower plate 1' is drained to one side. It is already known that the exhaust gas is led to the drain outlet 3' of the upper stage heat exchanger A', but especially in the former case, the combustion exhaust gas for the upper stage heat exchanger A' flows intensively around the outer periphery of the upper heat exchanger A'. The overall effect of the heat exchanger A' is poor due to the poor distribution of exhaust gas, and in the latter case, the resistance when the combustion exhaust gas passes through the upper and lower vents 2' and 2'' is large, resulting in a reduction in the number of man-hours required for processing. It had drawbacks such as requiring a lot of work.

この考案は上記従来の欠点を解消するために複
数の板状体を一定の排気間隙を存して端部を互に
若干重合させ排水口に向けて斜状に配設したもの
であつて、以下にその一実施例を図面に基づき具
体的に説明する。
In order to solve the above-mentioned conventional drawbacks, this invention consists of a plurality of plate-like bodies arranged with a certain exhaust gap, their ends slightly overlapping each other, and slanted toward the drain port. One embodiment will be specifically described below based on the drawings.

第1図ないし第5図においてAは上段に設けた
補助熱交換器、Bは下段に設けた主熱交換器、C
は上段の補助熱交換器Aと下段の主熱交換器Bと
の間に形成した排気通路、1は該排気通路C内に
配設した複数の板状体であつて、相隣接する板状
体1,1間に排気間隙2を存しかつ端部にて互に
水平方向に重合して排気通路Cの下部一側に設け
た後記ドレン排水口3に向けて下り傾斜して個別
に配列する(第2図参照)とともに最下部の板状
体1の下端上面部をドレン排水口3に連通せし
め、かつ、水密を保つて溶着している。又第3図
に示したように1枚の長い板体を屈折して階段状
に複数の板状体1を一体的に連続して形成し屈折
部1bに排気口1aを穿つたもの、又は、第4図
に示したように別体の板状体1を中央部を低くし
て略V字状に屈折した複数の板状体1を排気間隙
2を存して端部にて水平方向に若干重合した状態
のもとにドレン排水口3に向けて一定の下り勾配
をもつて配設するとともに最下部の板状体1の下
端上面部をドレン排水口3に連通せしめたもの、
又第5図に示したように、1枚板の中央を低くし
て略V字状に屈折し、これを階段状に屈折して複
数の板状体1を一体的に連続して形成し、屈折部
1bに排気口1aを穿設することにより前記と同
じ作用を達成することもできるものである。な
お、4はドレン排水口3に接続した排水管で、そ
の途中をU字状に屈曲した溜部5を設けて該溜部
5に溜つたドレンにより排水管4において排気通
路Cと外気を遮断し、排気通路C内の燃焼排ガス
が排水管4から器外に漏洩するのを防ぐようにし
ている。6は内胴、7は吸熱管である。なお、第
3図に示したように板状体1を1枚板にて構成し
たものは器体への固定は非常に容易である。以上
の実施例では上下に二個の熱交換器を配設した場
合を示したが、下段の熱交換器のない1個の熱交
換器にも適用し得ることは勿論である。
In Figures 1 to 5, A is the auxiliary heat exchanger installed in the upper stage, B is the main heat exchanger installed in the lower stage, and C is the main heat exchanger installed in the lower stage.
1 is an exhaust passage formed between the upper stage auxiliary heat exchanger A and the lower stage main heat exchanger B; 1 is a plurality of plate-like bodies disposed in the exhaust passage C; There is an exhaust gap 2 between the bodies 1 and 1, and they overlap each other in the horizontal direction at the ends, and are arranged individually so as to be inclined downward toward a drain outlet 3, which will be described later, provided on one side of the lower part of the exhaust passage C. At the same time, the lower end upper surface of the lowermost plate-shaped body 1 is made to communicate with the drain outlet 3 and is welded to maintain watertightness (see FIG. 2). Also, as shown in FIG. 3, a single long plate is bent to form a plurality of plate-like bodies 1 integrally and continuously in a stepwise manner, and an exhaust port 1a is bored in the bent part 1b, or , as shown in FIG. 4, a plurality of separate plate bodies 1 are bent into a substantially V-shape with the central part lowered, and the ends of the plate bodies 1 are bent horizontally with an exhaust gap 2. is arranged with a certain downward slope toward the drain outlet 3 in a state where it is slightly overlapped with the drain outlet 3, and the lower end upper surface of the lowermost plate-like body 1 is communicated with the drain outlet 3,
Further, as shown in FIG. 5, the center of one plate is lowered and bent into a substantially V-shape, and this is bent into a step-like shape to form a plurality of plate-like bodies 1 integrally and continuously. The same effect as described above can also be achieved by providing an exhaust port 1a in the bending portion 1b. In addition, 4 is a drain pipe connected to the drain outlet 3, and a reservoir part 5 bent in a U-shape is provided in the middle of the drain pipe, and the drain collected in the reservoir part 5 blocks the exhaust passage C and the outside air in the drain pipe 4. However, the combustion exhaust gas in the exhaust passage C is prevented from leaking out of the vessel from the drain pipe 4. 6 is an inner shell, and 7 is a heat absorption tube. Incidentally, when the plate-like body 1 is constructed of a single plate as shown in FIG. 3, it is very easy to fix it to the container body. Although the above embodiment shows a case in which two heat exchangers are disposed above and below, it is of course applicable to a single heat exchanger without a lower heat exchanger.

前記構成において、下段の熱交換器Bを通過し
た燃焼排ガスは各々の板状体1間の排気間隙2あ
るいは排気口1aを迂回して通つてその直上に上
昇し(第1図矢印b参照)、上段の熱交換器Aの
各部に均等に接触流過するため上段の熱交換器A
が燃焼排ガスの残余熱を確実にとつて熱交換器A
の吸熱管7内を流過する通水を効率よく加熱昇温
せしめる。又低温となつた燃焼排ガスから凝縮す
るドレンは各板状体1上をその勾配に沿つて流下
し、各板状体1の端部が重合されているので、ド
レンが隣の下段の板状体1に落下誘導されて下段
の熱交換器B上又は器体内へ流下することなく、
ドレンを確実にドレン排水口3へ導いて排水管4
を介して器外へ放出するものである。第4図及び
第5図に例示したように板状体1をV字状に屈折
せしめると、ドレンが中央部に集まつて板状体1
の左右端より下段の熱交換器B上又は器体内に落
下する恐れがなく、板状体1に滴下したドレンを
全て一辺側中央部に設けたドレン排水口3から排
出し得る。
In the above configuration, the combustion exhaust gas that has passed through the lower heat exchanger B bypasses the exhaust gap 2 between the plate bodies 1 or the exhaust port 1a and rises directly above it (see arrow b in FIG. 1). , in order to evenly contact and flow through each part of the upper heat exchanger A.
Heat exchanger A reliably removes the residual heat of the combustion exhaust gas
To efficiently heat and raise the temperature of water flowing through the heat absorption pipe 7. In addition, condensate condensed from the low-temperature combustion exhaust gas flows down on each plate-like body 1 along its slope, and since the ends of each plate-like body 1 are polymerized, the condensate flows into the adjacent lower plate-like body. without being guided by the body 1 and flowing onto the lower heat exchanger B or into the vessel body.
Guide the drain securely to the drain outlet 3 and connect it to the drain pipe 4.
It is released outside the vessel through the . When the plate-like body 1 is bent into a V-shape as illustrated in FIGS. 4 and 5, the drain gathers in the center of the plate-like body 1
There is no fear of the drain dripping onto the lower heat exchanger B or into the container body than the left and right ends of the plate body 1, and all drain dripping onto the plate-like body 1 can be discharged from the drain outlet 3 provided at the center of one side.

この考案は以上説明したように熱交換器の下方
部に複数の板状体を一定の排気間隙あるいは排気
口を存して端部を互に水平方向に重合させ排気口
に向けて下り傾斜して配設したという簡単な構造
で、ドレンの回収が確実に行えるとともに、燃焼
排ガス流の分布も均等化するので熱効率は著しく
向上し、燃焼排ガスの通過抵抗を小さくする効果
がある。
As explained above, this idea consists of a plurality of plate-like bodies in the lower part of the heat exchanger with a certain exhaust gap or exhaust port, the ends of which overlap each other in the horizontal direction, and slope downward toward the exhaust port. With a simple structure in which the drain is disposed in a straight line, the drain can be reliably collected, and the distribution of the flue gas flow is evened out, so the thermal efficiency is significantly improved and the resistance to passage of the flue gas is reduced.

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

第1図はこの考案の一実施例を示す全体の概略
断面図、第2図ないし第5図は要部の実施例を示
す斜視図、第6図及び第7図は従来例の概略断面
図である。 A……上段の熱交換器、B……下段の熱交換
器、1……板状体、2……排気間隙、3……排水
口、1a……排気口。
Fig. 1 is a schematic cross-sectional view of the entire structure showing an embodiment of this invention, Figs. 2 to 5 are perspective views showing the embodiment of the main part, and Figs. 6 and 7 are schematic cross-sectional views of a conventional example. It is. A... Upper heat exchanger, B... Lower heat exchanger, 1... Plate body, 2... Exhaust gap, 3... Drain port, 1a... Exhaust port.

Claims (1)

【実用新案登録請求の範囲】 1 熱交換器の下方部に複数の板状体1を一定の
排気間隙2あるいは排気口1aを存して端部を
互に水平方向に若干重合させてその高所より下
部一側に設けた排水口3に向けて順次に下り傾
斜して配設したことを特徴とする湯沸器。 2 複数の板状体1を1枚板にて形成した実用新
案登録請求の範囲第1項記載の湯沸器。
[Claims for Utility Model Registration] 1. A plurality of plate-like bodies 1 are arranged in the lower part of a heat exchanger with a certain exhaust gap 2 or exhaust port 1a, and their ends are slightly overlapped in the horizontal direction, so that the height of the plate-like bodies 1 is increased. A water heater characterized in that the water heater is arranged so as to be sloped downward sequentially toward a drain port 3 provided on one side of the lower part of the water heater. 2. The water heater according to claim 1 of the utility model registration claim, in which the plurality of plate-like bodies 1 are formed of a single plate.
JP2099082U 1982-02-17 1982-02-17 water heater Granted JPS58124731U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2099082U JPS58124731U (en) 1982-02-17 1982-02-17 water heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2099082U JPS58124731U (en) 1982-02-17 1982-02-17 water heater

Publications (2)

Publication Number Publication Date
JPS58124731U JPS58124731U (en) 1983-08-25
JPS6231821Y2 true JPS6231821Y2 (en) 1987-08-14

Family

ID=30033126

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2099082U Granted JPS58124731U (en) 1982-02-17 1982-02-17 water heater

Country Status (1)

Country Link
JP (1) JPS58124731U (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030026607A (en) * 2001-09-26 2003-04-03 주식회사 경동보일러 Upper Type Condensing Gas Boiler Using Cover
JP5212703B2 (en) * 2008-06-25 2013-06-19 株式会社ノーリツ Water heater
JP5376224B2 (en) * 2008-06-25 2013-12-25 株式会社ノーリツ Water heater

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4922045U (en) * 1972-05-31 1974-02-25

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4922045U (en) * 1972-05-31 1974-02-25

Also Published As

Publication number Publication date
JPS58124731U (en) 1983-08-25

Similar Documents

Publication Publication Date Title
US4448136A (en) Boiler with waste heat recovery
US4645001A (en) Heat exchanger
US4896411A (en) Method of making a multiple cell condensing heat exchanger
US4480591A (en) Condensing boiler
JPS6231821Y2 (en)
EP0685698B1 (en) Heat exchanger and gas burner assembly
GB2103351A (en) Flue arrangements for boilers
JPS623648Y2 (en)
CN207317578U (en) A kind of five pipe single channel efficient heat exchangers
CN207407708U (en) A kind of five pipes band water box type efficient heat exchanger
JPS604026Y2 (en) heat exchanger equipment
CN210251760U (en) Heat transfer plate type tail gas heating and white removing device
JPS593260Y2 (en) Heat exchanger
JP2000205658A (en) Combustion equipment
JPH09189491A (en) Heat exchanger
JPS6130113Y2 (en)
JPS5770395A (en) Heat exchanger
RU55457U1 (en) HEAT EXCHANGER
JPH0129439Y2 (en)
SU1132120A2 (en) Device for heat-moisture treatment of air
KR800001673Y1 (en) Instant continuous water supply device
RU1810726C (en) Heating appliance
JPS5834385Y2 (en) solar heat collector plate
JPH064230Y2 (en) Heat pipe heat exchanger for exhaust heat recovery
JPS59172945U (en) Water heater