JPS6113549B2 - - Google Patents
Info
- Publication number
- JPS6113549B2 JPS6113549B2 JP12764478A JP12764478A JPS6113549B2 JP S6113549 B2 JPS6113549 B2 JP S6113549B2 JP 12764478 A JP12764478 A JP 12764478A JP 12764478 A JP12764478 A JP 12764478A JP S6113549 B2 JPS6113549 B2 JP S6113549B2
- Authority
- JP
- Japan
- Prior art keywords
- low
- heat exchanger
- temperature heat
- temperature generator
- generator
- 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 24
- 230000000694 effects Effects 0.000 claims description 15
- 238000010521 absorption reaction Methods 0.000 claims description 9
- 239000006096 absorbing agent Substances 0.000 claims description 6
- 238000005057 refrigeration Methods 0.000 claims description 4
- 230000009977 dual effect Effects 0.000 claims description 2
- 239000003507 refrigerant Substances 0.000 description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 238000010438 heat treatment Methods 0.000 description 6
- 238000004378 air conditioning Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000003350 kerosene Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は一重二重効用併用吸収冷凍機に関する
もので、熱源や負荷に応じて経済的で安定な運転
を行うことを目的とする。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a single/double effect absorption refrigerator, and aims to provide economical and stable operation depending on the heat source and load.
すなわち1台の吸収冷凍機を、太陽熱温水や低
温水等の低温熱源による場合は一重効用として作
動し、都市ガスや灯油、高温水等の高温熱源によ
る場合は二重効用として作動或は一重効用との併
用により熱源の有効利用を計るものである。 In other words, one absorption chiller operates as a single effect when using a low temperature heat source such as solar hot water or low temperature water, and operates as a double effect or single effect when using a high temperature heat source such as city gas, kerosene, or high temperature water. This is used in combination with the heat source to make effective use of the heat source.
以下本発明を図に示す実施例について説明す
る。1は都市ガス或は灯油等の高温熱源の燃焼加
熱室2及び該加熱室からの排熱管3,3…を有し
稀液から冷媒を加熱分離する直焚高温発生器、4
は前記高温発生器1から送出された冷媒蒸気を熱
源として再熱し中間液の冷媒を更に加熱分離する
第1低温発生器、5は冷却器6によつて前記両発
生器1,4から流入する冷媒を凝縮し且つ冷却す
る凝縮器、7は前記凝縮器5からの液冷媒を散布
し気化させる際の潜熱を利用して冷水器8から冷
房用の冷水を得るようにした蒸発器、9は前記第
1低温発生器4で冷媒が分離された濃液を散布し
て器内の冷媒蒸気を吸収することにより前記蒸発
器7の内部を低圧に維持し連続した冷水の供給を
行なえるようにした吸収器、10及び11は低温
熱交換器と高温熱交換器で、これらは冷媒蒸気管
12、冷媒液流下管13、冷媒ポンプ14を有す
る冷媒循環路15、吸収液ポンプ16を有する稀
液管路17、中間液管路18及び濃液管路19に
より配管接続して冷凍サイクルを構成している。
20は前記高温発生器1と冷媒蒸気管12の間に
設けた温水熱交換器である。 The present invention will be described below with reference to embodiments shown in the drawings. 1 is a direct-fired high-temperature generator that has a combustion heating chamber 2 for a high-temperature heat source such as city gas or kerosene, and heat exhaust pipes 3, 3, etc. from the heating chamber, and heats and separates a refrigerant from a dilute liquid; 4;
5 is a first low temperature generator that reheats the refrigerant vapor sent from the high temperature generator 1 as a heat source and further heats and separates the intermediate liquid refrigerant; A condenser that condenses and cools the refrigerant; 7 is an evaporator that obtains cold water for air conditioning from a water cooler 8 using latent heat when the liquid refrigerant from the condenser 5 is dispersed and vaporized; By scattering the concentrated liquid from which the refrigerant has been separated in the first low-temperature generator 4 and absorbing the refrigerant vapor in the container, the inside of the evaporator 7 can be maintained at a low pressure and a continuous supply of cold water can be performed. The absorbers 10 and 11 are a low-temperature heat exchanger and a high-temperature heat exchanger, which include a refrigerant vapor pipe 12, a refrigerant liquid downflow pipe 13, a refrigerant circuit 15 with a refrigerant pump 14, and a dilute liquid absorber with an absorption liquid pump 16. A refrigeration cycle is constructed by connecting the pipes through a pipe 17, an intermediate liquid pipe 18, and a concentrated liquid pipe 19.
20 is a hot water heat exchanger provided between the high temperature generator 1 and the refrigerant vapor pipe 12.
而して21は前記低温熱交換器10と高温熱交
換器11との間に位置する稀液管路17aに設け
た低温熱源を加熱源とする第2低温発生器で該発
生器と前記高温熱交換器11の間には溶液循環ポ
ンプ22を介在すると共に前記第2低温発生器2
1の上部空間と凝縮器5は冷媒配管23により接
続されている。 Reference numeral 21 denotes a second low-temperature generator whose heat source is a low-temperature heat source provided in the dilute liquid pipe line 17a located between the low-temperature heat exchanger 10 and the high-temperature heat exchanger 11. A solution circulation pump 22 is interposed between the heat exchanger 11 and the second low temperature generator 2
The upper space of 1 and the condenser 5 are connected by a refrigerant pipe 23.
24は前記第2低温発生器21と濃液管路19
を接続するバイパス配管で該配管により高温発生
器1、高温熱交換器11及び第1低温発生器4が
適宜バイパスされる。また稀液管路17aと中間
液管路18には開閉弁25,26を設けると共に
これらの開閉弁の上流側と下流側に夫々U字状シ
ール管部27,28を形成している。なお、管路
17a、18には必ずしもU字状シール管部を形
成しなくても良い。 24 is the second low temperature generator 21 and the concentrated liquid pipe line 19;
The high temperature generator 1, the high temperature heat exchanger 11, and the first low temperature generator 4 are appropriately bypassed by the bypass pipe connecting the high temperature generator 1, the high temperature heat exchanger 11, and the first low temperature generator 4. Further, the dilute liquid pipe line 17a and the intermediate liquid pipe line 18 are provided with on-off valves 25 and 26, and U-shaped seal pipe portions 27 and 28 are formed on the upstream and downstream sides of these on-off valves, respectively. Note that the pipes 17a and 18 do not necessarily have to be formed with a U-shaped seal pipe portion.
次に動作について説明する。 Next, the operation will be explained.
イ 一重効用運転
この場合は溶液循環ポンプ22を停止し低温熱
源により第2低温発生器21を加熱することによ
り稀液から加熱分離された冷媒は凝縮器5で液化
した後蒸発器7に流入しここで気化する。この時
の潜熱により冷水器8より冷房用冷水が得られ
る。(a) Single-effect operation In this case, the solution circulation pump 22 is stopped and the second low-temperature generator 21 is heated by a low-temperature heat source, so that the refrigerant is heated and separated from the dilute liquid, liquefied in the condenser 5, and then flows into the evaporator 7. vaporize here. Cold water for air conditioning is obtained from the water cooler 8 due to the latent heat at this time.
一方溶液循環ポンプ22は運転を停止している
ために第2低温発生器21の液面は上昇し、稀液
より冷媒を分離した濃液はバイパス配管24に流
入して低温熱交換器10を通り吸収器9に散布さ
れて気化冷媒を吸収して稀液となる。この稀液は
吸収液ポンプ16により前記低温熱交換器10を
通り第2低温発生器21に流入し再び前述のサイ
クルを繰返す。 On the other hand, since the solution circulation pump 22 has stopped operating, the liquid level in the second low temperature generator 21 rises, and the concentrated liquid from which the refrigerant has been separated from the dilute liquid flows into the bypass pipe 24 and passes through the low temperature heat exchanger 10. The refrigerant is dispersed into the absorber 9, absorbs the vaporized refrigerant, and becomes a dilute liquid. This diluted liquid flows into the second low temperature generator 21 through the low temperature heat exchanger 10 by the absorption liquid pump 16, and the above-described cycle is repeated again.
ロニ重効用運転
この場合は溶液循環ポンプ22を運転し、都市
ガス等の高温熱源を燃焼加熱室2で燃焼せしめる
ことにより、高温発生器1、第1低温発生器4、
凝縮器5、蒸発器7、吸収器9、低温熱交換器1
0及び高温熱交換器11により冷凍サイクルが構
成され、冷水器8から冷房用冷水が、また温水用
熱交換器20から調温用温水が供給される。Roni heavy-effect operation In this case, the solution circulation pump 22 is operated and a high-temperature heat source such as city gas is combusted in the combustion heating chamber 2, thereby generating the high-temperature generator 1, the first low-temperature generator 4,
Condenser 5, evaporator 7, absorber 9, low temperature heat exchanger 1
0 and the high-temperature heat exchanger 11 constitute a refrigeration cycle, and cold water for cooling is supplied from the water cooler 8 and hot water for temperature adjustment is supplied from the hot water heat exchanger 20.
尚この場合に第2低温発生器21を低温加熱源
で加熱して一重効用と二重効用の併用運転を行つ
てもよい。 In this case, the second low temperature generator 21 may be heated with a low temperature heating source to perform a combined single effect and double effect operation.
また温水により暖房を行う場合は、開閉弁2
5,26及び冷媒蒸気管12の開閉弁29を閉じ
て高温発生器1と温水熱交換器20の間で冷媒の
循環を行い前記温水用熱交換器20で温水を製造
する。 Also, when heating with hot water, open/close valve 2
5, 26 and the on-off valve 29 of the refrigerant steam pipe 12 are closed to circulate the refrigerant between the high temperature generator 1 and the hot water heat exchanger 20, and the hot water heat exchanger 20 produces hot water.
本発明は上述の如く、高温発生器、第1低温発
生器、凝縮器、蒸発器、吸収器、低温熱交換器及
び高温熱交換器を接続して冷凍サイクルを構成す
る二重効用吸収冷凍機において、前記低温熱交換
器と高温熱交換器の間に位置する稀液管路には低
温熱源により加熱される第2低温発生器と溶液循
環ポンプを設けると共に前記第2低温発生器と濃
液管路に前記高温発生器、高温熱交換器及び第1
低温発生器をバイパスするバイパス配管を設け、
前記溶液循環ポンプを一重効用時に停止、二重効
用時には運転するようにしたものであるから、1
台の吸収冷凍機を加熱源や負荷状態に応じて一重
効用又は二重効用或は両者の併用運転を行うこと
が出来エネルギーの有効利用と経済的な運転が可
能となる。また溶液循環ポンプの発停により切替
運転を簡単に行うことが出来る等実用上有益な効
果がある。 As described above, the present invention provides a dual-effect absorption refrigerator that connects a high temperature generator, a first low temperature generator, a condenser, an evaporator, an absorber, a low temperature heat exchanger, and a high temperature heat exchanger to form a refrigeration cycle. A second low temperature generator heated by a low temperature heat source and a solution circulation pump are installed in the dilute liquid pipe line located between the low temperature heat exchanger and the high temperature heat exchanger, and the second low temperature generator and the concentrated liquid The high temperature generator, the high temperature heat exchanger and the first
Install bypass piping to bypass the low temperature generator,
Since the solution circulation pump is configured to stop when there is a single effect and to operate when there is a double effect, 1.
The absorption chiller can be operated in single effect, double effect, or a combination of both depending on the heating source and load condition, allowing effective use of energy and economical operation. Further, there are practical effects such as being able to easily perform switching operation by turning on and off the solution circulation pump.
図面は本発明による一重二重効用併用吸収冷凍
機の回路構成図である。
1…高温発生器、4…第1低温発生器、5…凝
縮器、10…低温熱交換器、11…高温熱交換
器、21…第2低温発生器、22…溶液ポンプ、
24…バイパス配管。
The drawing is a circuit diagram of a single/double effect absorption refrigerator according to the present invention. 1... High temperature generator, 4... First low temperature generator, 5... Condenser, 10... Low temperature heat exchanger, 11... High temperature heat exchanger, 21... Second low temperature generator, 22... Solution pump,
24...Bypass piping.
Claims (1)
器、吸収器、低温熱交換器及び高温熱交換器を接
続して冷凍サイクルを構成する二重効用吸収冷凍
機において、前記低温熱交換器と高温熱交換器の
間に位置する稀液管路には低温熱源により加熱さ
れる第2低温発生器と溶液循環ポンプを設けると
共に前記第2低温発生器と濃液管路に前記高温発
生器、高温熱交換器及び第1低温発生器をバイパ
スするバイパス配管を設け、前記溶液循環ポンプ
を一重効用時に停止、二重効用時には運転するこ
とを特徴とする一重二重効用併用吸収冷凍機。1. In a dual-effect absorption refrigerator that connects a high-temperature generator, a first low-temperature generator, a condenser, an evaporator, an absorber, a low-temperature heat exchanger, and a high-temperature heat exchanger to form a refrigeration cycle, the low-temperature heat exchanger A second low-temperature generator heated by a low-temperature heat source and a solution circulation pump are installed in the diluted liquid line located between the container and the high-temperature heat exchanger, and the high-temperature generator and the concentrated liquid line are provided with a second low-temperature generator heated by a low-temperature heat source and a solution circulation pump. A single/double effect absorption refrigerating machine, characterized in that the solution circulation pump is provided with a bypass pipe that bypasses the heat exchanger, the high temperature heat exchanger, and the first low temperature generator, and the solution circulation pump is stopped when the single effect is used and is operated when the double effect is used.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12764478A JPS5553665A (en) | 1978-10-12 | 1978-10-12 | Absorption refrigerating machine for either single effect or double ellects |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12764478A JPS5553665A (en) | 1978-10-12 | 1978-10-12 | Absorption refrigerating machine for either single effect or double ellects |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5553665A JPS5553665A (en) | 1980-04-19 |
JPS6113549B2 true JPS6113549B2 (en) | 1986-04-14 |
Family
ID=14965182
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12764478A Granted JPS5553665A (en) | 1978-10-12 | 1978-10-12 | Absorption refrigerating machine for either single effect or double ellects |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5553665A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57155068A (en) * | 1981-03-20 | 1982-09-25 | Sanyo Electric Co | Absorption water cooler/heater |
-
1978
- 1978-10-12 JP JP12764478A patent/JPS5553665A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5553665A (en) | 1980-04-19 |
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