JPH0447224B2 - - Google Patents
Info
- Publication number
- JPH0447224B2 JPH0447224B2 JP17326985A JP17326985A JPH0447224B2 JP H0447224 B2 JPH0447224 B2 JP H0447224B2 JP 17326985 A JP17326985 A JP 17326985A JP 17326985 A JP17326985 A JP 17326985A JP H0447224 B2 JPH0447224 B2 JP H0447224B2
- Authority
- JP
- Japan
- Prior art keywords
- solution
- liquid
- liquid level
- temperature regenerator
- gas
- 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
- 239000007788 liquid Substances 0.000 claims description 70
- 238000001514 detection method Methods 0.000 claims description 19
- 239000003507 refrigerant Substances 0.000 claims description 12
- 238000010521 absorption reaction Methods 0.000 claims description 10
- 239000006096 absorbing agent Substances 0.000 claims description 8
- 230000009977 dual effect Effects 0.000 claims description 8
- 238000005086 pumping Methods 0.000 claims description 7
- 238000005057 refrigeration Methods 0.000 claims description 2
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- 238000004891 communication Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、高温再生器上方に揚液管にて接続さ
れて気液分離器を有し、かつ溶液ポンプ吐出側溶
液経路に溶液流量制御弁を有する二重効用吸収冷
凍機に関するものである。Detailed Description of the Invention [Industrial Application Field] The present invention has a gas-liquid separator connected above a high-temperature regenerator with a liquid pumping pipe, and a solution flow rate control device in the solution path on the discharge side of the solution pump. The present invention relates to a dual-effect absorption refrigerator with valves.
発明者らは、溶液流量制御の安定化を目的とし
て第3図のフロー図に示される如き冷凍機を発明
し、これにつき同時に出願をしているが、本発明
はその発明改良に係わるものである。
The inventors invented a refrigerator as shown in the flow diagram of FIG. 3 for the purpose of stabilizing solution flow rate control, and filed an application for this invention at the same time, but the present invention does not relate to improvements in that invention. be.
第3図において、1は吸収器、2は蒸発器、3
は高温再生器、4は低温再生器、5は凝縮器、6
は高温熱交換器、7は低温熱交換器、8は溶液ボ
ンプ、9は冷媒ポンプ、10は気液分離器、11
は揚液管、12は液面検出室、13は液面検出器
であるフロートと溶液流量制御弁とが一体となつ
た自力式フロート弁、14は溶液戻り配管、15
は溶液連絡管を示す。 In Fig. 3, 1 is an absorber, 2 is an evaporator, and 3
is a high temperature regenerator, 4 is a low temperature regenerator, 5 is a condenser, 6
is a high temperature heat exchanger, 7 is a low temperature heat exchanger, 8 is a solution pump, 9 is a refrigerant pump, 10 is a gas-liquid separator, 11
12 is a liquid lift pipe, 12 is a liquid level detection chamber, 13 is a self-powered float valve in which a float serving as a liquid level detector and a solution flow rate control valve are integrated, 14 is a solution return pipe, 15
indicates a solution communication tube.
吸収器1内の希溶液は溶液ポンプ8により駆動
され、低温熱交換器7、高温熱交換器6で加熱さ
れ、高温再生器3、低温再生器4に導かれる。 The dilute solution in the absorber 1 is driven by a solution pump 8, heated by a low-temperature heat exchanger 7 and a high-temperature heat exchanger 6, and guided to a high-temperature regenerator 3 and a low-temperature regenerator 4.
高温再生器3内で加熱され濃縮された溶液は、
発生した冷媒蒸気と共に揚液管11にて気液分離
器10へ導かれ冷媒蒸気と溶液に分離される。分
離された溶液は、高温再生器3内の圧力即ち気液
分離器10内の圧力と低温再生器4内の圧力との
圧力差により溶液戻り配管14にて高温熱交換器
6に導かれ、希溶液を加熱後吸収器1に導かれ
る。 The solution heated and concentrated in the high temperature regenerator 3 is
Together with the generated refrigerant vapor, it is guided to the gas-liquid separator 10 through a liquid lift pipe 11 and separated into refrigerant vapor and solution. The separated solution is guided to the high temperature heat exchanger 6 through the solution return pipe 14 due to the pressure in the high temperature regenerator 3, that is, the pressure difference between the pressure in the gas-liquid separator 10 and the pressure in the low temperature regenerator 4. After heating the dilute solution, it is introduced into the absorber 1.
液面検出室12内の溶液液面が低い場合は自力
式フロート弁13が内蔵せる溶液流量弁を開方向
に制御し、高温再生器3が空焚きとなるのを防止
し、逆に高い場合には、自力式フロート弁13の
溶液流量制御弁を閉方向に制御し、液面検出室1
2及び上方の気液分離気10内の溶液液面の過度
の上昇による溶液の冷媒蒸気流中へのキヤリーオ
ーバー現象を防止し、合わせて吸収器1内の溶液
量の過度の減少による溶液ポンプ8のキヤビテー
シヨン現象を防止している。 When the solution level in the liquid level detection chamber 12 is low, the self-powered float valve 13 controls the built-in solution flow rate valve in the open direction to prevent the high temperature regenerator 3 from running dry; To do this, the solution flow rate control valve of the self-powered float valve 13 is controlled in the closing direction, and the liquid level detection chamber 1 is closed.
2 and the carry-over phenomenon of the solution into the refrigerant vapor flow due to an excessive rise in the solution level in the upper gas-liquid separation gas 10, and also prevent the solution from being excessively reduced in the amount of solution in the absorber 1. Cavitation phenomenon of the pump 8 is prevented.
しかるに揚液管11による気液分離器10への
揚液作用は高温再生器3内で発生した冷媒蒸気に
よる気泡ポンプ作用によるものである為、断続的
であり、均一な流量が得られにくく、気液分離器
10内の液面も比較的不安定である。しかるに溶
液戻り配管14の戻り口と液面検出室12の戻り
口とが気液分離器10の底部にある為溶液戻り口
上に安定な液面が形成されず、溶液戻り配管14
からの戻り流量が安定しない為液面検出室12内
の溶液液面にて溶液流入量を自力式フロート弁1
3の制御が不安定になる問題点がまだ十分には解
決されていなかつた。
However, since the liquid pumping action to the gas-liquid separator 10 by the liquid pumping pipe 11 is due to the bubble pumping action of the refrigerant vapor generated in the high-temperature regenerator 3, it is intermittent, making it difficult to obtain a uniform flow rate. The liquid level within the gas-liquid separator 10 is also relatively unstable. However, since the return port of the solution return pipe 14 and the return port of the liquid level detection chamber 12 are located at the bottom of the gas-liquid separator 10, a stable liquid level is not formed above the solution return port, and the solution return pipe 14
Since the return flow rate from
3, the problem of unstable control had not yet been fully resolved.
本発明は、上記の如き、前述の別途出願した発
明において十分解決しきれていない問題点を解決
し、液面検出室内の液面を安定として溶液流量制
御を安定となすことができる二重効用吸収冷凍機
を提供することを目的とする。 The present invention solves the problems that have not been fully solved in the above-mentioned separately filed inventions, and has a dual effect of stabilizing the liquid level in the liquid level detection chamber and stably controlling the solution flow rate. The purpose is to provide an absorption refrigerator.
本発明は、上記の問題点を解決する手段とし
て、吸収器、蒸発器、凝縮器、低温再生器、高温
再生器高温溶液熱交換器、低温溶液熱交換器、溶
液ポンプ及びこれらを接続する溶液経路、冷媒経
路より二重効用吸収冷凍サイクルを形成し、前記
高温再生器上方に揚液管にて接続された気液分離
器を有し、かつ前記溶液ポンプ吐出側溶液経路に
前記高温再生器への溶液流入量を制御する溶液流
量制御弁を有する二重効用吸収冷凍機において、
前記気液分離器にはオーバーフローせきを設けて
液溜りを形成し、該オーバーフローせきの下流側
に液面検出室を備え、該液面検出室中の液面を検
出する液面検出器を備え、前記気液分離器の下部
は溶液経路を経て前記高温溶液熱交換器に接続
し、
前記液面検出室の下部は溶液経路を経て前記高
温再生器の下部に接続し、前記液面検出器の検出
信号により前記溶液流量制御弁を制御するように
したことを特徴とする二重効用吸収冷凍機を提供
するものである。
The present invention provides an absorber, an evaporator, a condenser, a low-temperature regenerator, a high-temperature regenerator, a high-temperature solution heat exchanger, a low-temperature solution heat exchanger, a solution pump, and a solution connecting these as means for solving the above problems. A double-effect absorption refrigeration cycle is formed from the refrigerant path and the refrigerant path, and a gas-liquid separator is connected above the high-temperature regenerator by a pumping pipe, and the high-temperature regenerator is connected to the solution path on the discharge side of the solution pump. In a dual-effect absorption refrigerator having a solution flow control valve that controls the amount of solution flowing into the
The gas-liquid separator is provided with an overflow weir to form a liquid reservoir, a liquid level detection chamber is provided downstream of the overflow weir, and a liquid level detector is provided to detect the liquid level in the liquid level detection chamber. , a lower part of the gas-liquid separator is connected to the high temperature solution heat exchanger via a solution route, a lower part of the liquid level detection chamber is connected to a lower part of the high temperature regenerator via a solution route, and a lower part of the liquid level detector is connected to the high temperature regenerator via a solution route. The present invention provides a dual-effect absorption refrigerator characterized in that the solution flow rate control valve is controlled by the detection signal.
次に本発明の実施例を第1図にもとづいて説明
する。
Next, an embodiment of the present invention will be described based on FIG.
気液分離器10にはオーバーフローせき16を
設けて溶液溜り17を形成し、このオーバーフロ
ーせき16の下流側に液面検出室12を備えてい
る。その他第1図において第3図と同一符号の部
分は同様な構成作用を有する。 The gas-liquid separator 10 is provided with an overflow weir 16 to form a solution reservoir 17, and a liquid level detection chamber 12 is provided downstream of the overflow weir 16. Other parts in FIG. 1 having the same reference numerals as in FIG. 3 have similar structural functions.
高温再生器3内で加熱され濃縮された溶液は発
生した冷媒蒸気と共に揚液管11にて気液分離器
10へ導かれ、冷媒蒸気と溶液に分離される。分
離された溶液は揚液管11の溶液出口部にオーバ
ーフローせき16にて形成された液溜り17に溜
り、液溜り17底部に接続された溶液戻り配管1
4により高温熱交換器6に導かれ、希溶液を加熱
後吸収器1へ導かれる。 The solution heated and concentrated in the high-temperature regenerator 3 is guided along with the generated refrigerant vapor to the gas-liquid separator 10 through a liquid lift pipe 11, and is separated into refrigerant vapor and solution. The separated solution collects in a liquid reservoir 17 formed by an overflow weir 16 at the solution outlet of the liquid pumping pipe 11, and then passes through the solution return pipe 1 connected to the bottom of the liquid reservoir 17.
4 leads to a high temperature heat exchanger 6, where the dilute solution is heated and then led to an absorber 1.
一方揚液管11にて余剰に気液分離器10へ導
かれた溶液は、オーバーフローせき16からあふ
れて、その下流側の液面検出室12に流入し、液
面検出室12下部より連絡管15により高温再生
器3に速やかに戻される。この為、溶液戻り配管
14の戻り口部にオーバーフローせき16によつ
て常にオーバーフロー液面が存在し、溶液戻り量
が安定し、液面ヘツドが高くなることにより溶液
戻り能力も改善される。また液面検出室12内の
自力式フロート弁13の動作も確実なものとな
り、安定した溶液流量制御を行うことができる利
点がある。 On the other hand, the excess solution guided to the gas-liquid separator 10 by the liquid lift pipe 11 overflows from the overflow weir 16 and flows into the liquid level detection chamber 12 on the downstream side, and is passed from the lower part of the liquid level detection chamber 12 into the connecting pipe. 15, it is quickly returned to the high temperature regenerator 3. Therefore, an overflow liquid level is always present at the return port of the solution return pipe 14 due to the overflow weir 16, the amount of solution returned is stabilized, and the liquid level head is raised, thereby improving the solution return ability. Further, the operation of the self-powered float valve 13 in the liquid level detection chamber 12 becomes reliable, and there is an advantage that stable solution flow rate control can be performed.
なお、溶液流量制御弁は、液面検出器(例えば
フロート)と一体でなく、別個に希溶液経路に設
けられ、電気信号などにより操作されるものでも
よい。 Note that the solution flow rate control valve may not be integrated with the liquid level detector (for example, a float), but may be provided separately in the dilute solution path and operated by electrical signals or the like.
さらに揚液管11の出口部をオーバーフロー液
面より上方に設けた例を第2図に示す。第2図に
おいて第1図、第3図と同一符号の部分は同様な
構成、部分を有する。本方式では揚液管11の出
口部にて冷媒蒸気が吹き上げる溶液量を減少でき
る為第1図に示した例に比べ気液分離器10の大
きさを小さくできる利点がある。 Further, FIG. 2 shows an example in which the outlet portion of the liquid lift pipe 11 is provided above the overflow liquid level. In FIG. 2, parts having the same reference numerals as those in FIGS. 1 and 3 have the same configuration and portions. This method has the advantage that the size of the gas-liquid separator 10 can be made smaller than the example shown in FIG. 1 because the amount of solution blown up by the refrigerant vapor at the outlet of the liquid lift pipe 11 can be reduced.
本発明によれば、高温再生器の気液分離器内の
液面検出部の溶液液面を安定にでき、溶液戻り能
力が改善され、溶液流量制御を安定して行うこと
のできる信頼性の高い二重効用吸収冷凍機を提供
でき実用上極めて大なる効果を奏する。
According to the present invention, it is possible to stabilize the solution level in the liquid level detection section in the gas-liquid separator of a high-temperature regenerator, improve the solution return ability, and improve reliability by stably controlling the solution flow rate. It is possible to provide a high dual-effect absorption refrigerator, which has extremely great practical effects.
第1図及び第2図は本発明の実施例のフロー図
を示し、第3図は従来の例のフロー図を示す。
1……吸収器、2……蒸発器、3……高温再生
器、4……低温再生器、5……凝縮器、6……高
温熱交換器、7……低温熱交換器、8……溶液ポ
ンプ、9……冷媒ポンプ、10……気液分離器、
11……揚液管、12……液面検出室、13……
自力式フロート弁、14……溶液戻り配管、15
……溶液連絡管、16……オーバーフローせき、
17……液溜り。
1 and 2 show a flow diagram of an embodiment of the present invention, and FIG. 3 shows a flow diagram of a conventional example. 1... Absorber, 2... Evaporator, 3... High temperature regenerator, 4... Low temperature regenerator, 5... Condenser, 6... High temperature heat exchanger, 7... Low temperature heat exchanger, 8... ... solution pump, 9 ... refrigerant pump, 10 ... gas-liquid separator,
11...liquid lift pipe, 12...liquid level detection chamber, 13...
Self-powered float valve, 14...Solution return piping, 15
...Solution connecting pipe, 16...Overflow weir,
17...Liquid pool.
Claims (1)
再生器、高温溶液熱交換器、低温溶液熱交換器、
溶液ポンプ及びこれらを接続する溶液経路、冷媒
経路より二重効用吸収冷凍サイクルを形成し、前
記高温再生器上方に揚液管にて接続された気液分
離器を有し、かつ前記溶液ポンプ吐出側溶液経路
に前記高温再生器への溶液流入量を制御する溶液
流量制御弁を有する二重効用吸収冷凍機におい
て、 前記気液分離器にはオーバーフローせきを設け
て液溜りを形成し、該オーバーフローせきの下流
側に液面検出室を備え、該液面検出室中の液面を
検出する液面検出器を備え、 前記気液分離器の下部は溶液経路を経て前記高
温溶液熱交換器に接続し、 前記液面検出室の下部は溶液経路を経て前記高
温再生器の下部に接続し、 前記液面検出器の検出信号により前記溶液流量
制御弁を制御するようにした ことを特徴とする二重効用吸収冷凍機。 2 前記揚液管の出口部を前記溶液溜りのオーバ
ーフロー液面よりも上方に設けた特許請求の範囲
第1項記載の二重効用吸収冷凍機。[Claims] 1. Absorber, evaporator, condenser, low temperature regenerator, high temperature regenerator, high temperature solution heat exchanger, low temperature solution heat exchanger,
A dual-effect absorption refrigeration cycle is formed by a solution pump, a solution path connecting these, and a refrigerant path, and a gas-liquid separator is connected above the high-temperature regenerator by a liquid pumping pipe, and the solution pump discharges In a dual-effect absorption refrigerator having a solution flow rate control valve in a side solution path for controlling the amount of solution flowing into the high-temperature regenerator, the gas-liquid separator is provided with an overflow weir to form a liquid reservoir, and the overflow A liquid level detection chamber is provided on the downstream side of the weir, and a liquid level detector is provided to detect the liquid level in the liquid level detection chamber, and the lower part of the gas-liquid separator is connected to the high temperature solution heat exchanger via a solution path. The lower part of the liquid level detection chamber is connected to the lower part of the high temperature regenerator via a solution path, and the solution flow rate control valve is controlled by a detection signal from the liquid level detector. Dual effect absorption refrigerator. 2. The double-effect absorption refrigerator according to claim 1, wherein the outlet portion of the liquid lift pipe is provided above the overflow liquid level of the solution reservoir.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17326985A JPS6237651A (en) | 1985-08-08 | 1985-08-08 | Double effect absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17326985A JPS6237651A (en) | 1985-08-08 | 1985-08-08 | Double effect absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6237651A JPS6237651A (en) | 1987-02-18 |
| JPH0447224B2 true JPH0447224B2 (en) | 1992-08-03 |
Family
ID=15957317
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17326985A Granted JPS6237651A (en) | 1985-08-08 | 1985-08-08 | Double effect absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6237651A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011185511A (en) * | 2010-03-08 | 2011-09-22 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011220623A (en) * | 2010-04-12 | 2011-11-04 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011220622A (en) * | 2010-04-12 | 2011-11-04 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011226678A (en) * | 2010-04-16 | 2011-11-10 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011226679A (en) * | 2010-04-16 | 2011-11-10 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
-
1985
- 1985-08-08 JP JP17326985A patent/JPS6237651A/en active Granted
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011185511A (en) * | 2010-03-08 | 2011-09-22 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011220623A (en) * | 2010-04-12 | 2011-11-04 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011220622A (en) * | 2010-04-12 | 2011-11-04 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011226678A (en) * | 2010-04-16 | 2011-11-10 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011226679A (en) * | 2010-04-16 | 2011-11-10 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6237651A (en) | 1987-02-18 |
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