JPS5828902B2 - Steam↓-exhaust gas switching type absorption refrigerator - Google Patents
Steam↓-exhaust gas switching type absorption refrigeratorInfo
- Publication number
- JPS5828902B2 JPS5828902B2 JP53030705A JP3070578A JPS5828902B2 JP S5828902 B2 JPS5828902 B2 JP S5828902B2 JP 53030705 A JP53030705 A JP 53030705A JP 3070578 A JP3070578 A JP 3070578A JP S5828902 B2 JPS5828902 B2 JP S5828902B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- temperature
- steam
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
- F25B29/006—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は水を冷媒、塩類溶液を吸収剤とする蒸気−排ガ
ス切換形吸収冷凍機に関するもので、加熱源として工場
排ガスと蒸気の切換使用によシ吸収冷凍機の経済的な運
転を行うことを目的とする。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a steam-exhaust gas switching type absorption refrigerator using water as a refrigerant and a salt solution as an absorbent. The purpose is to perform economical driving.
例えば、排ガスを加熱源とする吸収冷凍機を設置して空
調等に用いる冷水を製造しようとする場合、工場プロセ
スによっては1日のうち数時間排ガスを排出する場合、
又日によって排ガスを出すときと出さない場合がある。For example, if you are installing an absorption chiller that uses exhaust gas as a heating source to produce chilled water for use in air conditioning, etc., or if some factory processes emit exhaust gas for several hours a day,
Also, depending on the day, there are times when exhaust gas is emitted and times when it is not.
このような場合にはいずれも別に補助熱源が必要となっ
てくる。In all of these cases, a separate auxiliary heat source is required.
一方工場プロセスにおいては排ガス以外にボイラからの
蒸気を比較的容易に得られるために排ガスの供給停止時
にはこの蒸気を有効に活用して吸収冷凍機の運転コスト
の低減を計ることが期待出来る。On the other hand, in factory processes, in addition to exhaust gas, steam from the boiler can be obtained relatively easily, so when the supply of exhaust gas is stopped, this steam can be effectively utilized to reduce the operating cost of the absorption chiller.
本発明は上記の点に鑑みてなされたもので以下図に示す
実施例について説明する。The present invention has been made in view of the above points, and an embodiment shown in the drawings will be described below.
1は多数の排ガス煙管2,2・・・・・・を具備し稀液
から冷媒を加熱分離する排ガス用高温発生器、3は前記
高温発生器1から送出された冷媒蒸気を加熱源として中
間液を再熱し更に冷媒を分離する低温発生器、4は前記
円発生器1,3から流入する冷媒を冷却器5で冷却して
液化する凝縮器、6は前記凝縮器4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7から冷房用冷
水を得るようにした蒸発器、8は前記低温発生器3で冷
媒が分離された後の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6の内部を低圧に維持し連
続した冷水の供給を可能とする吸収器、9及び10は濃
液と稀液及び濃液と中間液を夫々熱交換する低温熱交換
器と高温熱交換器でこれらは冷媒蒸気管11、冷媒液流
下管12、冷媒ポンプ13を有する冷媒循環路14、吸
収液ポンプ15を有する稀液管路16、中間液管路11
及び濃液管路18により接続されて冷凍サイクルを構成
している。1 is a high temperature generator for exhaust gas that is equipped with a large number of flue gas smoke pipes 2, 2, etc. and heats and separates the refrigerant from the dilute liquid; 3 is an intermediate generator that uses the refrigerant vapor sent from the high temperature generator 1 as a heating source; A low temperature generator reheats the liquid and further separates the refrigerant; 4 is a condenser that cools and liquefies the refrigerant flowing from the circular generators 1 and 3 in a cooler 5; 6 is a condenser that liquefies the liquid refrigerant from the condenser 4; The evaporator 8 is designed to obtain cold water for cooling from the water cooler 7 by utilizing the latent heat generated during spraying and vaporization. Absorbers 9 and 10, which maintain the inside of the evaporator 6 at a low pressure by absorbing refrigerant vapor and enable a continuous supply of cold water, exchange heat between the concentrated liquid and the dilute liquid, and between the concentrated liquid and the intermediate liquid, respectively. The low-temperature heat exchanger and the high-temperature heat exchanger include a refrigerant vapor pipe 11, a refrigerant liquid downflow pipe 12, a refrigerant circuit 14 with a refrigerant pump 13, a dilute liquid pipe 16 with an absorption liquid pump 15, and an intermediate liquid pipe 11.
and are connected by a concentrated liquid pipe line 18 to constitute a refrigeration cycle.
19は凝縮器4と吸収器8を冷却する冷却水循環路で該
循環路には排ガス用高温発生器1に附設される放熱器2
0と、冷却塔21及び冷却水ポンプ22が設けられてい
る。Reference numeral 19 denotes a cooling water circulation path for cooling the condenser 4 and absorber 8, and the circulation path includes a radiator 2 attached to the high temperature generator 1 for exhaust gas.
0, a cooling tower 21 and a cooling water pump 22 are provided.
而して23は蒸気加熱管24を具備し補液より冷媒を加
熱分離する蒸気用高温発生器で該発生器は夫々自動切換
開閉弁25.26.27を介在した冷媒管28、補液管
29及び中間液管30により排ガス用高温発生器1と並
列になるように冷凍サイクルの冷媒蒸気管11、補液管
路16及び中間液管路17に接続されている。Reference numeral 23 is a high-temperature steam generator that is equipped with a steam heating pipe 24 and heats and separates the refrigerant from the replacement fluid.The generator includes a refrigerant pipe 28, a replacement fluid pipe 29, and The intermediate liquid pipe 30 is connected to the refrigerant vapor pipe 11, the replacement liquid pipe line 16, and the intermediate liquid pipe line 17 of the refrigeration cycle so as to be in parallel with the high temperature generator 1 for exhaust gas.
31,32゜33は前記冷媒蒸気管11、補液管路16
及び中間液管路17に設けた自動切換開閉弁である。31, 32, and 33 are the refrigerant vapor pipe 11 and the replacement fluid pipe 16.
and an automatic switching on/off valve provided in the intermediate liquid pipe line 17.
次に上記の構成において動作を説明する。Next, the operation in the above configuration will be explained.
イ)排ガス用高温発生器を使用の場合
この場合は蒸気用高温発生器23側の各自動切換開閉弁
25.26.27はいずれも閉止、排ガス用高温発生器
1側の各自動切換開閉弁31.32.33はいずれも開
放されている。b) When using a high-temperature generator for exhaust gas In this case, the automatic switching valves 25, 26, and 27 on the high-temperature steam generator 23 side are all closed, and the automatic switching valves on the high-temperature generator 1 side for exhaust gas are closed. 31, 32, and 33 are all open.
そして蒸発器6の冷水器Tから得られる冷水の温度が設
定値に達すると夫々温度検出器34゜35の検出により
温度制御器36.37が作動して冷媒蒸気制御弁38を
絞ると共に冷媒液制御弁39を開放して排ガス用高温発
生器1の熱を冷却水循環路19の放熱器20に放熱し且
つ冷媒ポンプ13の運転を停止して容量制御を行う。When the temperature of the chilled water obtained from the water cooler T of the evaporator 6 reaches a set value, the temperature controllers 36 and 37 are actuated by detection by the temperature detectors 34 and 35, respectively, to throttle the refrigerant vapor control valve 38 and reduce the temperature of the refrigerant liquid. The control valve 39 is opened to radiate the heat of the exhaust gas high temperature generator 1 to the radiator 20 of the cooling water circulation path 19, and the operation of the refrigerant pump 13 is stopped to perform capacity control.
口)蒸気用高温発生器を使用の場合
この場合は蒸気用高温発生器23側の各自動切換開閉弁
25.26.27はいずれも開放、排ガス用高温発生器
1側の各自動切換開閉弁31.32.33はいずれも閉
止される。When using a high-temperature generator for steam In this case, the automatic switching valves 25, 26, and 27 on the high-temperature steam generator 23 side are all open, and the automatic switching valves 25, 26, and 27 on the high-temperature generator 1 side for exhaust gas are open. 31, 32, and 33 are all closed.
そして蒸発器6の冷水器1から得られる冷水の温度が設
定値に達すると夫々温度検出器34.35の検出により
温度制御器36.37が作動して冷媒蒸気制御弁38及
び蒸気制御弁40を絞ると共に冷媒ポンプ13の運転を
停止して容量制御を行う。When the temperature of the cold water obtained from the water cooler 1 of the evaporator 6 reaches a set value, the temperature controllers 36 and 37 are activated by detection by the temperature detectors 34 and 35, respectively, and the refrigerant vapor control valve 38 and the vapor control valve 40 are activated. At the same time, the operation of the refrigerant pump 13 is stopped to perform capacity control.
本発明による蒸気−排ガス切換形吸収冷凍機は上述の如
く、水を冷媒、塩類溶液を吸収剤とし排ガス用高温発生
器、低温発生器、凝縮器、蒸発器、吸収器、低温用熱交
換器及び高温用熱交換器を配管接続して冷凍サイクルを
構成すると共に切換開閉弁を介して前記排ガス用高温発
生器と並列に蒸気用高温発生器を接続し、加熱源に応じ
て前記高温発生器の一方を選択使用するようにしたもの
であるから、補助熱源として別個のボイラーを必要とす
ることなく工場プロセスにおける排ガス及び蒸気に応じ
てコストの安い経済的な運転が可能となる。As described above, the steam-exhaust gas switching type absorption refrigerating machine according to the present invention uses water as a refrigerant and a salt solution as an absorbent, and has a high temperature generator for exhaust gas, a low temperature generator, a condenser, an evaporator, an absorber, and a heat exchanger for low temperature. A high-temperature heat exchanger is connected via piping to form a refrigeration cycle, and a high-temperature generator for steam is connected in parallel with the high-temperature generator for exhaust gas via a switching valve, and the high-temperature generator Since one of these is selectively used, it is possible to operate economically at low cost depending on the exhaust gas and steam in the factory process without requiring a separate boiler as an auxiliary heat source.
−!た加熱源の切換えも簡単に行うことが出来る。-! The heating source can also be easily switched.
さらに、排ガス用高温発生器を使用した場合には、冷水
温度検出器の信号により温度調節器を介して放熱器から
排ガス用高温発生器へ還流する冷媒液の流量制御弁の開
度を調節するようにしているので、負荷に応じた冷水供
給が可能であり、また、吸収冷凍機に供給される排ガス
流量を調節する必要も解消できる結果、工場プロセス側
の稼動にも悪影響を及ぼさないという実用的効果を奏す
る。Furthermore, when a high-temperature generator for exhaust gas is used, the opening degree of the flow rate control valve for the refrigerant liquid that flows back from the radiator to the high-temperature generator for exhaust gas is adjusted via a temperature controller based on the signal from the chilled water temperature detector. As a result, it is possible to supply chilled water according to the load, and it also eliminates the need to adjust the flow rate of exhaust gas supplied to the absorption chiller, which is a practical solution that does not adversely affect the operation of the factory process side. It has the desired effect.
尚切換弁の操作を排ガスを発生するプロセスとのインタ
ーロック回路で行えば、プロセスを運転するときは排ガ
スで運転しない時は蒸気で吸収冷凍機を稼動することが
できる。If the switching valve is operated in an interlock circuit with the process that generates exhaust gas, the absorption chiller can be operated with steam when the process is operated and not with exhaust gas.
図面は本発明吸収冷凍機の回路構成図である。
1・・・排ガス用高温発生器、23・・・蒸気用高温発
生器、25.26.27.31.32.33・・・自動
切換開閉弁、20・・・放熱器、34・・・温度検出器
、36・・・温度調節器、39・・・冷媒液制御弁。The drawing is a circuit diagram of the absorption refrigerator of the present invention. 1... High temperature generator for exhaust gas, 23... High temperature generator for steam, 25.26.27.31.32.33... Automatic switching on/off valve, 20... Heat radiator, 34... Temperature detector, 36... Temperature regulator, 39... Refrigerant liquid control valve.
Claims (1)
器、低温発生器、凝縮器、蒸発器、吸収器、低温用熱交
換器及び高温用熱交換器を配管接続して冷凍サイクルを
構成すると共に切換開閉弁を介して前記排ガス用高温発
生器と並列に蒸気用高温発生器を接続し、加熱源に応じ
て前記高温発生器の一方を選択使用し、かつ、冷却水を
前記吸収器から凝縮器経由で排ガス用高温発生器に付設
した放熱器へ流通せしめるようにし、前記排ガス用高温
発生器を使用した場合には1、冷水温度検出器の信号に
より温度調節器を介して放熱器から排ガス用高温発生器
へ還流する冷媒液の流量制御弁の開度を調節するように
したことを特徴とする蒸気−排ガス切換形吸収冷凍機。1 A refrigeration cycle is constructed by using water as a refrigerant and a salt solution as an absorbent, and connecting a high-temperature generator for exhaust gas, a low-temperature generator, a condenser, an evaporator, an absorber, a low-temperature heat exchanger, and a high-temperature heat exchanger with piping. At the same time, a high-temperature generator for steam is connected in parallel with the high-temperature generator for exhaust gas through a switching valve, one of the high-temperature generators is selectively used depending on the heating source, and the cooling water is connected to the absorber. When the high-temperature generator for exhaust gas is used, the signal from the chilled water temperature detector is used to flow the water to the radiator attached to the high-temperature generator for exhaust gas via the condenser. 1. A steam-exhaust gas switching type absorption refrigerating machine, characterized in that the opening degree of a flow rate control valve for refrigerant liquid flowing back from the refrigerant liquid back to the exhaust gas high-temperature generator is adjusted.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53030705A JPS5828902B2 (en) | 1978-03-15 | 1978-03-15 | Steam↓-exhaust gas switching type absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53030705A JPS5828902B2 (en) | 1978-03-15 | 1978-03-15 | Steam↓-exhaust gas switching type absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54122453A JPS54122453A (en) | 1979-09-22 |
| JPS5828902B2 true JPS5828902B2 (en) | 1983-06-18 |
Family
ID=12311057
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53030705A Expired JPS5828902B2 (en) | 1978-03-15 | 1978-03-15 | Steam↓-exhaust gas switching type absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5828902B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5043416U (en) * | 1973-08-21 | 1975-05-01 |
-
1978
- 1978-03-15 JP JP53030705A patent/JPS5828902B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54122453A (en) | 1979-09-22 |
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