JPS6345636Y2 - - Google Patents
Info
- Publication number
- JPS6345636Y2 JPS6345636Y2 JP13720880U JP13720880U JPS6345636Y2 JP S6345636 Y2 JPS6345636 Y2 JP S6345636Y2 JP 13720880 U JP13720880 U JP 13720880U JP 13720880 U JP13720880 U JP 13720880U JP S6345636 Y2 JPS6345636 Y2 JP S6345636Y2
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- hot water
- endothermic
- heat absorption
- water storage
- 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
- 238000010521 absorption reaction Methods 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 23
- 230000000694 effects Effects 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
Description
【考案の詳細な説明】
[産業上の利用分野]
本考案は温水用の貯湯式熱交換器装置に関す
る。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a hot water storage type heat exchanger device for hot water.
[従来技術]
従来この種の装置として、バーナの上側に上部
吸熱管と下部吸熱管とを上下2段に並設して成る
熱交換器本体を設け、これをその流出側において
貯湯槽に連通させる式のものは知られる。[Prior art] Conventionally, this type of device has a heat exchanger main body, which is made up of an upper endothermic pipe and a lower endothermic pipe arranged side by side in two stages above the burner, and is connected to a hot water storage tank on the outflow side. It is known that the formula is
[考案が解決しようとする問題点]
貯湯式熱交換器装置の上部吸熱管と該下部吸熱
管はバーナにより作用される熱気温度が互いに相
違し、例えば下部吸熱管の下側で800℃、上部吸
熱管の上側で90℃、その中間部で200℃となり、
かくて両吸熱管を互いに等径とした場合、これを
介して導かれる湯水の温度が互いに大きく相違
し、該貯湯槽を介して得られる出湯温度が極めて
不安定となり勝ちである不都合を伴う。[Problems to be solved by the invention] The upper endothermic pipe and the lower endothermic pipe of the hot water storage heat exchanger device have different hot air temperatures applied by the burner, for example, 800°C below the lower endothermic pipe and 800°C above. The temperature is 90℃ at the top of the heat absorption tube and 200℃ at the middle part.
If both heat absorption pipes are made to have the same diameter, the temperature of the hot water introduced through the pipes will be greatly different from each other, and the temperature of the hot water obtained through the hot water storage tank will tend to be extremely unstable, which is a disadvantage.
[問題を解決するための手段]
バーナ1の上側に、集合管6を介して上部吸熱
管2と下部吸熱管3とを上下2段に分岐並設して
成る熱交換器本体4を設け、これをその流出側に
おいて貯湯槽5に連通させて、該上部吸熱管2を
該下部吸熱管3に比し小径として貯湯槽に連通さ
せた。[Means for solving the problem] A heat exchanger main body 4 is provided above the burner 1, which is made up of an upper endothermic pipe 2 and a lower endothermic pipe 3 that are branched and arranged in two stages, upper and lower, through a collecting pipe 6. This was communicated with a hot water storage tank 5 on its outflow side, and the upper endothermic pipe 2 was made smaller in diameter than the lower endothermic pipe 3 and communicated with the hot water storage tank.
[作用]
給水管7を介して導かれる水は集合管6を介し
て上部吸熱管2と下部吸熱管3とに分流し、各吸
熱管2,3内で加熱されて湯となつて貯湯槽5に
導かれ、必要に応じ出湯管10から外部に導かれ
るもので、上部吸熱管2を比較的小径とし、その
流量を減少させるもので、「流量×吸熱量」の比
率を略同一にして各吸熱管2,3を介して得られ
る出湯温度は比較的安定となる。[Function] Water led through the water supply pipe 7 is divided into the upper endothermic pipe 2 and the lower endothermic pipe 3 through the collecting pipe 6, heated in each endothermic pipe 2 and 3, and turned into hot water, which is then stored in the hot water storage tank. The upper heat absorption pipe 2 is made relatively small in diameter to reduce the flow rate, and the ratio of "flow rate x amount of heat absorbed" is kept approximately the same. The outlet temperature obtained through each heat absorption pipe 2, 3 is relatively stable.
[実施例]
上部吸熱管2と該下部吸熱管3とを例えば第2
図に明示するように夫々横方向の複数本とし、こ
れらを第1図にに明示するように一方の端部で集
合管6を介して吸水管7と、他方の端部でその上
側の該貯湯槽5とに連通させるようにしている。[Example] For example, the upper heat absorption pipe 2 and the lower heat absorption pipe 3 are
As clearly shown in the figure, there are a plurality of pipes in the horizontal direction, and as shown in FIG. He is trying to communicate with the hot water storage tank 5.
上部吸熱管2を比較的小径とするもので、かく
て流量が減少されてそれに応じて湯温が上昇され
るようにした。図面で10は貯湯槽5の上部の出
湯管を示す。 The upper heat absorption pipe 2 is made to have a relatively small diameter, so that the flow rate is reduced and the hot water temperature is increased accordingly. In the drawing, numeral 10 indicates a hot water outlet pipe in the upper part of the hot water storage tank 5.
尚、考案者の実験によれば、バーナ1を
28000Kcal/h程度のインプツトとしたときA部
が800℃、B部が200℃、C部が90℃の温度分布と
なり、この際上部吸熱管2を内径12mm、下部吸熱
管3を内径19mmとして各吸熱管2,3の「流量×
吸熱量」の比率が略同一となり良好な結果を得ら
れた。 According to the inventor's experiments, burner 1
When the input is about 28000Kcal/h, the temperature distribution will be 800°C in part A, 200°C in part B, and 90°C in part C. “Flow rate × of heat absorption pipes 2 and 3
The ratio of "absorbed heat amount" was almost the same, and good results were obtained.
[効果]
上部吸熱管2と下部吸熱管3とから略同温度の
湯を得られて貯湯槽5にて均一化され出湯温度を
安定化することが出来る貯湯式熱交換器独特の効
果が増してしかも高温出湯に際し生じ易い蒸気に
よる吹出しの異常音がない。また構成は上部吸熱
管2を比較的小径とするのみで足りて簡単である
等の効果を有する。[Effect] Hot water of approximately the same temperature is obtained from the upper endothermic pipe 2 and the lower endothermic pipe 3 and is made uniform in the hot water storage tank 5, thereby increasing the unique effect of the hot water storage type heat exchanger, which can stabilize the hot water temperature. What's more, there is no abnormal sound from steam blowing out, which is likely to occur when hot water is tapped at high temperatures. Further, the structure is simple, as it is sufficient to make the upper heat absorption tube 2 relatively small in diameter.
第1図は本案装置の1例の截断正面図、第2図
はその截断側面図である。
1……バーナ、2……上部吸熱管、3……下部
吸熱管、4……熱交換器本体、5……貯湯槽。
FIG. 1 is a cutaway front view of an example of the present device, and FIG. 2 is a cutaway side view thereof. 1... Burner, 2... Upper heat absorption pipe, 3... Lower heat absorption pipe, 4... Heat exchanger body, 5... Hot water storage tank.
Claims (1)
管2と下部吸熱管3とを上下2段に分岐並設して
成る熱交換器本体4を設け、これをその流出側に
おいて貯湯槽5に連通させる式のものにおいて、
該上部吸熱管2を該下部吸熱管3に比し小径と
し、上部吸熱管2及び下部吸熱管3において「流
量×吸熱量」の比率を略同一にしたことを特徴と
する熱交換装置。 Above the burner 1, there is provided a heat exchanger main body 4, which is made up of an upper endothermic pipe 2 and a lower endothermic pipe 3 branched and arranged in parallel in two stages, upper and lower, via a collecting pipe 6. In the type that communicates with
A heat exchange device characterized in that the upper endothermic tube 2 has a smaller diameter than the lower endothermic tube 3, and the ratio of "flow rate x heat absorption amount" in the upper endothermic tube 2 and the lower endothermic tube 3 is made approximately the same.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13720880U JPS6345636Y2 (en) | 1980-09-29 | 1980-09-29 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13720880U JPS6345636Y2 (en) | 1980-09-29 | 1980-09-29 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5761430U JPS5761430U (en) | 1982-04-12 |
JPS6345636Y2 true JPS6345636Y2 (en) | 1988-11-28 |
Family
ID=29497297
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13720880U Expired JPS6345636Y2 (en) | 1980-09-29 | 1980-09-29 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6345636Y2 (en) |
-
1980
- 1980-09-29 JP JP13720880U patent/JPS6345636Y2/ja not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5761430U (en) | 1982-04-12 |
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