JPH02623Y2 - - Google Patents
Info
- Publication number
- JPH02623Y2 JPH02623Y2 JP1981116298U JP11629881U JPH02623Y2 JP H02623 Y2 JPH02623 Y2 JP H02623Y2 JP 1981116298 U JP1981116298 U JP 1981116298U JP 11629881 U JP11629881 U JP 11629881U JP H02623 Y2 JPH02623 Y2 JP H02623Y2
- Authority
- JP
- Japan
- Prior art keywords
- condenser
- refrigerant
- regenerator
- gas
- absorption liquid
- 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
- Sorption Type Refrigeration Machines (AREA)
Description
【考案の詳細な説明】
本案は吸収冷凍機の再生凝縮器に係り、特に、
再生器で発生した冷媒の熱を凝縮器で回収する再
生凝縮器に関する。[Detailed description of the invention] This invention relates to a regenerative condenser for an absorption refrigerator, and in particular,
The present invention relates to a regeneration condenser in which heat of refrigerant generated in a regenerator is recovered in a condenser.
一般に、吸収冷凍機は、第1図に示すように筒
状の再生凝縮胴1と蒸発吸収胴2とを架台3に取
り付け、夫々を冷媒管および吸収液管で気密に接
続することにより再生器、凝縮器、蒸発器、吸収
器と流れる冷媒サイクルと、再生器、吸収器と循
環する吸収液サイクルとを構成しており、再生凝
縮胴1の内部は、一般に、第2図に示すような再
生器4と凝縮器5との配置構造を有していた。 Generally, an absorption refrigerator is constructed by attaching a cylindrical regeneration condensation shell 1 and an evaporation absorption shell 2 to a frame 3, and connecting them airtightly with a refrigerant pipe and an absorption liquid pipe. , a refrigerant cycle that circulates through a condenser, an evaporator, and an absorber, and an absorption liquid cycle that circulates through a regenerator and absorber. Generally, the inside of the regenerated condensation shell 1 is as shown in FIG. It had an arrangement structure of a regenerator 4 and a condenser 5.
しかし、このような構造の再生凝縮胴では、加
熱器6で加熱され、吸収液から分離された高温ガ
ス体が器胴1の上方にも充満しているため、加熱
器6によつて吸収液溜7に与えられる熱が器胴の
底壁8のみならず器胴の上側壁9からも失なわれ
ていく欠点を有していた。すなわち、第2図の構
造の再生凝縮胴は、その器壁からの熱ロスが大き
いために、凝縮器5で冷媒ガスの熱を回収して例
えば温水を取出す再生凝縮器として不向なもので
あつた。又、第2図の構造では、吸収冷凍機の容
量が増大するに従い、再生器4から凝縮器5に流
れるガスの流速が増大し、再生凝縮の効率を増す
上での障害となる上に、ガス流から吸収液滴を分
離し難くする欠点を有するものでもあつた。な
お、ガス流速を減じるための従来の技術として、
例えば特公昭40−15395号公報にみられるように、
器胴内底部に再生器を設けると共に器胴内上部の
両側にそれぞれ冷媒ガスの通路を設け、これら通
路の間に凝縮器を配備した再生凝縮器が提案され
ている。しかし、この再生凝縮器も、再生器から
の高温レベルのままの冷却ガススを器胴両側の内
壁に沿つて流しつつ凝縮器側へ導くものであるた
め、器壁からの冷却ガスの放熱即ち熱ロスが大き
いという欠点を有している。 However, in the regenerating condensation barrel having such a structure, the upper part of the barrel 1 is also filled with high-temperature gas that has been heated by the heater 6 and separated from the absorption liquid. It has a drawback that the heat given to the reservoir 7 is lost not only from the bottom wall 8 of the container body but also from the upper side wall 9 of the container body. In other words, the regenerating condensing cylinder having the structure shown in FIG. 2 is not suitable as a regenerating condenser for recovering hot water, for example, by recovering the heat of the refrigerant gas in the condenser 5, since the heat loss from the vessel wall is large. It was hot. In addition, in the structure shown in FIG. 2, as the capacity of the absorption refrigerator increases, the flow rate of gas flowing from the regenerator 4 to the condenser 5 increases, which becomes an obstacle to increasing the efficiency of regeneration condensation. They also had the disadvantage of making it difficult to separate the absorbed droplets from the gas stream. In addition, as a conventional technique for reducing the gas flow velocity,
For example, as seen in Japanese Patent Publication No. 15395/1973,
A regeneration condenser has been proposed in which a regenerator is provided at the bottom of the container body, refrigerant gas passages are provided on both sides of the top of the container body, and a condenser is provided between these passages. However, in this regeneration condenser, the cooling gas still at a high temperature from the regenerator is guided to the condenser side while flowing along the inner walls on both sides of the vessel body, so the heat dissipation of the cooling gas from the vessel walls is caused. It has the disadvantage of large loss.
本案ではこれらの欠点を除去し、例えば大容量
の冷温水同時取出し型吸収冷凍機にも適用できる
よう再生器を器胴の底部に、凝縮器を器胴上部に
左右に配設し、器胴の軸線に沿つた凝縮器の中間
に再生器から凝縮器への冷媒ガス通路を形成し、
かつ、一方の凝縮器を通常の冷却水系凝縮器と
し、他方の凝縮器を冷媒ガスの熱の回収用の凝縮
器としたことを特徴とするものである。 In this project, these shortcomings are eliminated, and the regenerator is placed at the bottom of the container body, and the condenser is placed on the left and right sides at the top of the container body, so that it can be applied to, for example, a large capacity absorption chiller with simultaneous extraction of hot and cold water. forming a refrigerant gas passage from the regenerator to the condenser in the middle of the condenser along the axis of
Further, one of the condensers is a normal cooling water system condenser, and the other condenser is a condenser for recovering heat of the refrigerant gas.
第3図において、10は再生凝縮胴1の底部に
配され、加熱器11を吸収液溜12に浸漬し、吸
収液を加熱することにより吸収液中に含まれる冷
媒をガス化して分離する再生器、13,13′は
再生凝縮胴1の上半分において該器胴の軸線と平
行となるように熱交換器14,14′を有して配
された凝縮器であり、一方の凝縮器13は冷却水
の通水される熱交換器14を有した冷却水系凝縮
器となつており、他方の凝縮器13′は例えば温
水の通水される熱交換器14′を有した熱回収用
の凝縮器となつている。15,15′は該凝縮器
で凝集液化した冷媒液を溜めて蒸発器(図示省
略)に供給する冷媒溜、16は再生器10から発
生するガス流に含まれる吸収液滴を分離するエリ
ミネータ17を有し、冷媒ガスを凝縮器13,1
3′に導びくため凝縮器13,13′の中間に配設
された冷媒通路である。 In FIG. 3, reference numeral 10 is placed at the bottom of the regeneration condensation cylinder 1, and a heater 11 is immersed in the absorption liquid reservoir 12, and by heating the absorption liquid, the refrigerant contained in the absorption liquid is gasified and separated. The vessels 13 and 13' are condensers arranged in the upper half of the regenerated condensation shell 1 and have heat exchangers 14 and 14' parallel to the axis of the vessel. The other condenser 13' is a cooling water system condenser having a heat exchanger 14 through which cooling water is passed, and the other condenser 13' is a heat recovery condenser having a heat exchanger 14' through which hot water is passed, for example. It acts as a condenser. Reference numerals 15 and 15' refer to a refrigerant reservoir for storing the refrigerant liquid condensed and liquefied in the condenser and supplying the same to an evaporator (not shown); 16 an eliminator 17 for separating absorbed droplets contained in the gas flow generated from the regenerator 10; The refrigerant gas is transferred to the condenser 13,1.
3' is a refrigerant passage arranged between the condensers 13 and 13'.
而して、再生器の加熱器11で吸収液が加熱さ
れて冷媒ガスが発生するのは、吸収液が沸騰し、
液中の冷媒ガスが気化して吸収液から分離するの
であるから、本案のように器胴の底部全体に液溜
が形成されるように再生器を配設すると、再生器
の液柱を浅くして沸騰し易くできると共に、気化
面積を広くして再生効率を上昇させることができ
る。又、再生器10で気化された冷媒ガスは、エ
リミネータ17、冷媒通路16を経て凝縮器1
3,13′に分かれて流入するため、蒸気流速は
半減し、効率良く冷媒の分離、凝集が可能となる
上に、冷却ガスが熱交換器14,14′の管群間
を流れてその大部分が凝縮しつつ除温する結果、
再生凝縮器1上半部の内壁周辺における高温領域
を減らして該器胴1上半部の器壁からの放熱すな
わち熱ロスを少なくすることができ、その分、熱
回収用凝縮器13′の熱回収量が増え、この凝縮
器から例えば温水を熱効率良く取出すこともでき
るものである。 Therefore, the absorption liquid is heated by the heater 11 of the regenerator and refrigerant gas is generated because the absorption liquid boils and
Since the refrigerant gas in the liquid vaporizes and separates from the absorption liquid, if the regenerator is arranged so that a liquid reservoir is formed at the entire bottom of the vessel body as in this proposal, the liquid column in the regenerator will be shallower. In addition to making it easier to boil, it is also possible to increase the regeneration efficiency by widening the vaporization area. Further, the refrigerant gas vaporized in the regenerator 10 passes through the eliminator 17 and the refrigerant passage 16 to the condenser 1.
3 and 13', the vapor flow rate is halved, making it possible to efficiently separate and condense the refrigerant.In addition, the cooling gas flows between the tube groups of the heat exchangers 14 and 14', reducing its size. As a result of cooling the parts while condensing,
By reducing the high-temperature area around the inner wall of the upper half of the regeneration condenser 1, it is possible to reduce heat radiation, that is, heat loss, from the wall of the upper half of the vessel body 1, and the heat recovery condenser 13' is reduced accordingly. The amount of heat recovered is increased, and hot water, for example, can be taken out from the condenser with high thermal efficiency.
又、本案の再生凝縮器は、熱交換器14,1
4′を構成する水熱交換器を独立して複数個収納
でき、外観上の変化をもたらさずに熱回収用凝縮
器13′を設け得るため、大型の吸収冷凍機用の
もとして好適である。以上のとおり、本案は、効
率良く冷媒を分離、凝縮する効果と、器壁からの
熱ロスを軽減する効果すなわち熱回収用の凝縮器
で冷媒の熱を効率良く回収する効果とを再生凝縮
器にもたらし、大容量で高効率の吸収冷凍機用の
再生凝縮器を提供するものとして特に有用であ
る。 Moreover, the regeneration condenser of the present invention has heat exchangers 14, 1
It is suitable as a base for a large-sized absorption refrigerator because a plurality of water heat exchangers composing the refrigeration unit 4' can be independently housed, and a heat recovery condenser 13' can be installed without causing any change in appearance. . As described above, this proposal has the effect of efficiently separating and condensing the refrigerant, and the effect of reducing heat loss from the vessel wall, that is, the effect of efficiently recovering the heat of the refrigerant in the heat recovery condenser. It is particularly useful as a regenerative condenser for high-capacity, high-efficiency absorption refrigerators.
第1図は吸収冷凍機の一例を示す斜視図、第2
図は一般の再生凝縮胴の内部構造を示す模式的横
断面図、第3図は本案による再生凝縮胴の内部構
造を示す対応横断面図である。
1……再生凝縮胴、10……再生器、13……
凝縮器、13′……熱回収用凝縮器、16……冷
媒通路。
Figure 1 is a perspective view showing an example of an absorption refrigerator, Figure 2 is a perspective view showing an example of an absorption refrigerator.
The figure is a schematic cross-sectional view showing the internal structure of a general regenerating condensing cylinder, and FIG. 3 is a corresponding cross-sectional view showing the internal structure of the regenerating condensing cylinder according to the present invention. 1... Regeneration condensation cylinder, 10... Regenerator, 13...
Condenser, 13'... Condenser for heat recovery, 16... Refrigerant passage.
Claims (1)
分離された冷媒ガスを冷却凝集して液冷媒にする
凝縮器とを内蔵する筒状の器胴にして、該器胴の
底部には吸収液を加熱する加熱器及び吸収液溜
が、又、該器胴の上半部には凝縮器が、夫々、器
胴の軸線に平行となるよう配設され、かつ、再生
器から凝縮器に流れるガス流から吸収液滴を分離
し、冷媒ガスを凝縮器に導びくエリミネータ付の
冷媒通路が凝縮器の中間に配設され、かつ、この
冷媒通路によつて分割された凝縮器の一方を熱回
収用の凝縮器としたことを特徴とする吸収冷凍機
用再生凝縮器。 a regenerator that heats and separates refrigerant gas from the absorption liquid;
A cylindrical container housing a built-in condenser that cools and condenses the separated refrigerant gas to form a liquid refrigerant, and a heater for heating the absorption liquid and an absorption liquid reservoir at the bottom of the container, A condenser is disposed in the upper half of the vessel, each parallel to the axis of the vessel, and separates the absorbed droplets from the gas stream flowing from the regenerator to the condenser, and separates the refrigerant gas. An absorption device characterized in that a refrigerant passage with an eliminator leading to the condenser is disposed in the middle of the condenser, and one of the condensers divided by the refrigerant passage is used as a condenser for heat recovery. Regenerative condenser for refrigerators.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11629881U JPS5820877U (en) | 1981-08-04 | 1981-08-04 | Regeneration condenser for absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11629881U JPS5820877U (en) | 1981-08-04 | 1981-08-04 | Regeneration condenser for absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5820877U JPS5820877U (en) | 1983-02-08 |
| JPH02623Y2 true JPH02623Y2 (en) | 1990-01-09 |
Family
ID=29910531
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11629881U Granted JPS5820877U (en) | 1981-08-04 | 1981-08-04 | Regeneration condenser for absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5820877U (en) |
-
1981
- 1981-08-04 JP JP11629881U patent/JPS5820877U/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5820877U (en) | 1983-02-08 |
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