JPS5919876Y2 - Blazing open rack vaporizer - Google Patents
Blazing open rack vaporizerInfo
- Publication number
- JPS5919876Y2 JPS5919876Y2 JP11950779U JP11950779U JPS5919876Y2 JP S5919876 Y2 JPS5919876 Y2 JP S5919876Y2 JP 11950779 U JP11950779 U JP 11950779U JP 11950779 U JP11950779 U JP 11950779U JP S5919876 Y2 JPS5919876 Y2 JP S5919876Y2
- Authority
- JP
- Japan
- Prior art keywords
- heat exchange
- header tank
- exchange section
- vaporizer
- refrigerant
- 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
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
【考案の詳細な説明】
この考案は、装置の小型化を図ったブレージング型オー
プンラック式気化装置に関する。[Detailed Description of the Invention] This invention relates to a brazing type open rack type vaporizer which is designed to be miniaturized.
従来より、波形フィンを挾んで二枚の平板を相対向し、
その流路の両端をスペーサーバーにて閉鎖し、平板、ス
ペーサーバーおよび波形フィンをろう着により一体化し
て熱交換部を構成し、該熱交換部の上下両端にヘッダー
タンクを固着し、液化冷媒を下部ヘッダータンクから導
入し、上部ヘッダータンクより気体冷媒として送出する
ブレージング型オープンラック式気化装置がある。Traditionally, two flat plates are placed opposite each other with a corrugated fin in between,
Both ends of the flow path are closed with spacer bars, and the flat plate, spacer bar, and corrugated fins are integrated by soldering to form a heat exchange section, and a header tank is fixed to both the upper and lower ends of the heat exchange section, and the liquefied refrigerant is There is a brazing type open rack type vaporizer that introduces refrigerant from a lower header tank and sends it out as a gaseous refrigerant from an upper header tank.
該気化装置は、伝達面積が大きく熱媒の流れが安定して
おり熱伝達率が良く、製造コストが安価であるという長
所があるが、該熱交換部が大型であるため据付面積が大
きいという欠点があった。This vaporizer has the advantages of a large transfer area, stable flow of heat medium, good heat transfer rate, and low manufacturing cost, but it requires a large installation area because the heat exchange part is large. There were drawbacks.
そこで、上記一層の熱交換部を二層ないし三層にして小
型化を図ったが、熱交換部の表面を熱媒が流れるため、
中央の流路は外側の流路に比較して非常に熱伝達率が悪
く、上部ヘッダータンクより送出される気体冷媒の温度
分布および流れが不均一となり、熱交換性能の低下、装
置の寿命短縮等、種々の不都合を来すという欠点があっ
た。Therefore, we attempted to downsize the single-layer heat exchange section by changing it to two or three layers, but since the heat medium flows on the surface of the heat exchange section,
The heat transfer coefficient of the central flow path is extremely poor compared to the outer flow paths, resulting in uneven temperature distribution and flow of the gas refrigerant sent from the upper header tank, resulting in a decrease in heat exchange performance and shortened equipment life. It has the disadvantage of causing various inconveniences.
この考案は、上記欠点の解消を目的とするブレージング
型オープンラック式気化装置を提案するもので、図に示
すごとく、4枚の平板3と3枚の波形フィン5を交互に
積層し、その流路の両端をスペーサーバー4にて閉鎖し
て三層の熱交換部6を形威し、該熱交換部6の上端に上
部ヘッダータンク2を、下端に下部ヘッダータンク1を
固着し、該下部ヘッダータンク1の下面に送入管7によ
り液化冷媒を導入する多数の枝管9を並設し、かつ、上
記熱交換部6の波形フィン5に挾まれた平板3に多数の
孔8を穿設してなる。This invention proposes a brazed open rack type vaporizer with the aim of eliminating the above-mentioned drawbacks.As shown in the figure, four flat plates 3 and three corrugated fins 5 are stacked alternately, and the Both ends of the passage are closed with spacer bars 4 to form a three-layer heat exchange section 6, and an upper header tank 2 is fixed to the upper end of the heat exchange section 6, a lower header tank 1 is fixed to the lower end of the heat exchange section 6, and the lower header tank 1 is fixed to the lower end of the heat exchange section 6. A large number of branch pipes 9 for introducing liquefied refrigerant through feed pipes 7 are arranged in parallel on the lower surface of the header tank 1, and a large number of holes 8 are bored in the flat plate 3 sandwiched between the corrugated fins 5 of the heat exchange section 6. It will be set up.
なお、上記熱交換部6は三層のものを示したが、それに
限定するものではなく、また、孔8は平板3の全面に流
路と直交して等間隔に穿設されているが、その他種々考
えられる。Although the heat exchange section 6 is shown as having three layers, the present invention is not limited thereto, and the holes 8 are formed on the entire surface of the flat plate 3 at equal intervals perpendicular to the flow path. Various other possibilities can be considered.
また、10は気体冷媒を送出する管である。上記気化装
置において、熱媒散水管(図面省略)より例えば海水を
散水し、熱交換部6に沿って海水を膜状に落下した状態
で、送入管7より液化冷媒を枝管9を経て下部ヘッダー
タンク1内に導入する。Moreover, 10 is a pipe for sending out a gaseous refrigerant. In the vaporizer, for example, seawater is sprinkled from a heat medium water distribution pipe (not shown), and the seawater falls in a film along the heat exchanger 6, and then the liquefied refrigerant is introduced from the feed pipe 7 through the branch pipe 9. It is introduced into the lower header tank 1.
このとき、送入管7内の液化冷媒に圧力変動が生じても
、枝管9を通して下部ヘッダータンク1内への流入に対
する抵抗を増大させたので、あまり問題にならない。At this time, even if a pressure fluctuation occurs in the liquefied refrigerant in the feed pipe 7, it does not pose much of a problem because the resistance to flowing into the lower header tank 1 through the branch pipe 9 is increased.
下部ヘッダータンク1内に流入した液化冷媒は、熱交換
部6の各流路内へ均等に流入し、該熱交換部6外表面を
流れる海水により熱を与えられ、上昇するに従って気化
される。The liquefied refrigerant that has entered the lower header tank 1 equally flows into each flow path of the heat exchange section 6, is given heat by the seawater flowing on the outer surface of the heat exchange section 6, and is vaporized as it rises.
このとき、中央の流路内の液化冷媒は、平板3の孔8に
より、外側の流路内の液化冷媒と上昇するにつれて混合
し、熱の伝達を行なうため、各流路とも均一に気化しな
がら熱交換部6上端では完全なガスとなり、上部ヘッダ
ータンク2を経て送出管10より外部へ送出される。At this time, the liquefied refrigerant in the central flow path mixes with the liquefied refrigerant in the outer flow paths as it rises through the holes 8 of the flat plate 3, and heat is transferred, so that each flow path is uniformly vaporized. However, the gas becomes a complete gas at the upper end of the heat exchange section 6, and is sent out through the upper header tank 2 and the delivery pipe 10 to the outside.
この考案によれば、上記のごとく、気化装置の熱交換性
能を低下させることなく、その熱交換部を多層となして
小型化を図ったため、該気化装置の据付面積を縮小でき
、製造も容易となる。According to this invention, as mentioned above, the heat exchange part of the vaporizer is made multi-layered and miniaturized without reducing the heat exchange performance of the vaporizer, so the installation area of the vaporizer can be reduced and manufacturing is easy. becomes.
第1図はこの考案のブレージング型オープンラック式気
化装置を示す一部破断斜視図である。
図中 1・・・・・・下部ヘッダータンク、2・・・・
・・上部ヘッダータンク、3・・・・・・平板、4・・
・・・・スペーサーバー5・・・・・・波形フィン、6
・・・・・・熱交換部、7・・・・・・送入管、8・・
・・・・孔、9・・・・・・枝管、10・・・・・・送
出管。FIG. 1 is a partially cutaway perspective view showing the brazed open rack type vaporizer of this invention. In the diagram: 1...lower header tank, 2...
...Upper header tank, 3...Flat plate, 4...
... Spacer bar 5 ... Waveform fin, 6
...Heat exchange section, 7...Feed pipe, 8...
... hole, 9 ... branch pipe, 10 ... delivery pipe.
Claims (1)
媒を下部ヘッダータンクから導入し、上部ヘッダータン
クより気体冷媒として送出する気化装置において、平板
と波形フィンを交互に積層し、その流路の両端をスペー
サーバーにて閉鎖して熱交換部を形威し、該熱交換部の
上端に上部ヘッダータンクを、下端に下部ヘッダータン
クを固着し、該下部ヘッダータンクの下面に送入管より
液化冷媒を導入する多数の枝管を並設し、かつ、上記熱
交換部の波形フィンに挾まれた平板に多数の孔を穿設し
てなることを特徴とするブレージング型オープンラック
式気化装置。In a vaporizer, header tanks are fixed to both the upper and lower ends of the heat exchange section, liquefied refrigerant is introduced from the lower header tank, and gaseous refrigerant is sent out from the upper header tank. Both ends are closed with spacer bars to form a heat exchange section, an upper header tank is fixed to the upper end of the heat exchange section, a lower header tank is fixed to the lower end of the heat exchange section, and liquefaction is carried out from the feed pipe to the bottom of the lower header tank. A brazed open rack type vaporizer characterized in that a large number of branch pipes for introducing a refrigerant are arranged in parallel, and a large number of holes are bored in a flat plate sandwiched between corrugated fins of the heat exchange section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11950779U JPS5919876Y2 (en) | 1979-08-29 | 1979-08-29 | Blazing open rack vaporizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11950779U JPS5919876Y2 (en) | 1979-08-29 | 1979-08-29 | Blazing open rack vaporizer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5636978U JPS5636978U (en) | 1981-04-08 |
JPS5919876Y2 true JPS5919876Y2 (en) | 1984-06-08 |
Family
ID=29351712
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11950779U Expired JPS5919876Y2 (en) | 1979-08-29 | 1979-08-29 | Blazing open rack vaporizer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5919876Y2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH026098Y2 (en) * | 1984-12-19 | 1990-02-14 |
-
1979
- 1979-08-29 JP JP11950779U patent/JPS5919876Y2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5636978U (en) | 1981-04-08 |
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