JPH0670535B2 - Absorption heat pump - Google Patents
Absorption heat pumpInfo
- Publication number
- JPH0670535B2 JPH0670535B2 JP6290282A JP6290282A JPH0670535B2 JP H0670535 B2 JPH0670535 B2 JP H0670535B2 JP 6290282 A JP6290282 A JP 6290282A JP 6290282 A JP6290282 A JP 6290282A JP H0670535 B2 JPH0670535 B2 JP H0670535B2
- Authority
- JP
- Japan
- Prior art keywords
- fluid
- heated
- heat
- temperature
- 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 - Lifetime
Links
- 238000010521 absorption reaction Methods 0.000 title claims description 23
- 239000012530 fluid Substances 0.000 claims description 72
- 239000003507 refrigerant Substances 0.000 claims description 40
- 239000006096 absorbing agent Substances 0.000 claims description 32
- 239000007788 liquid Substances 0.000 claims description 20
- 238000009833 condensation Methods 0.000 claims description 10
- 230000005494 condensation Effects 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000000446 fuel Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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、蒸発器に熱源流体を供給し、吸収器における
吸収液の冷媒を吸収する際に発生する熱(以下、吸収熱
と云う)と凝縮器における冷媒の凝縮熱で温水等被加熱
流体を加熱して取り出す吸収ヒートポンプの改良に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to heat (hereinafter referred to as absorption heat) generated when a heat source fluid is supplied to an evaporator and a refrigerant of an absorbing liquid in an absorber is absorbed, and condensation of the refrigerant in a condenser. The present invention relates to improvement of an absorption heat pump that heats and heats a fluid to be heated such as hot water.
此種吸収ヒートポンプにおいては、蒸発器に供給する熱
源流体の温度が低くなり過ぎたり、或いは吸収器に供給
する被加熱流体の温度が高くなり過ぎると、吸収器に散
布される吸収液の飽和蒸気圧が冷媒蒸気圧より高くな
り、冷媒蒸気が吸収器から蒸発器へ逆移動し蒸発器にお
いて凝縮する現象を生じ、正常なヒートポンプ運転が行
なわれなくなる問題がある。In this type of absorption heat pump, when the temperature of the heat source fluid supplied to the evaporator becomes too low or the temperature of the fluid to be heated supplied to the absorber becomes too high, saturated vapor of the absorption liquid sprayed to the absorber There is a problem that the pressure becomes higher than the refrigerant vapor pressure, the refrigerant vapor moves backward from the absorber to the evaporator and condenses in the evaporator, and normal heat pump operation cannot be performed.
すなわち、此種吸収ヒートポンプにおいては、被加熱流
体の温度が熱源流体の温度より高いときには、吸収器に
供給された被加熱流体の熱が蒸発器に供給された熱源流
体に逆放熱されると云う問題点がある。尚、ここに云う
被加熱流体温度が熱源流体温度より高いときは、被加熱
流体温度と熱源流体温度とが吸収器に散布される吸収液
の飽和蒸気圧を蒸発器内の冷媒蒸気圧より高くならしめ
るような関係にあるときを云う。That is, in this type of absorption heat pump, when the temperature of the heated fluid is higher than the temperature of the heat source fluid, the heat of the heated fluid supplied to the absorber is radiated to the heat source fluid supplied to the evaporator. There is a problem. When the temperature of the fluid to be heated here is higher than the temperature of the heat source fluid, the saturated vapor pressure of the absorbing liquid sprayed to the absorber by the temperature of the fluid to be heated and the heat source fluid temperature is higher than the refrigerant vapor pressure in the evaporator. It is said that there is a relationship that can be trained.
本発明は、斯る点に鑑み、此種吸収ヒートポンプにおい
て、吸収器及び凝縮器からの放熱を利用して被加熱流体
を取り出すヒートポンプ系と、発生器からの冷媒蒸気の
凝縮熱を利用して被加熱流体を取り出すボイラー系とを
構成し、かつ蒸発器に供給する熱源流体の温度と吸収器
に供給する被加熱流体の温度とを検出して比較する機構
並びに該機構からの信号によりヒートポンプ系とボイラ
ー系とを切替える機構を備えた構成を採ることにより、
被加熱流体を安定的に昇温することを目的としたもので
ある。In view of this point, the present invention, in this type of absorption heat pump, uses a heat pump system for taking out a fluid to be heated by utilizing heat radiation from an absorber and a condenser, and heat of condensation of refrigerant vapor from a generator. A mechanism that constitutes a boiler system for taking out a fluid to be heated, detects a temperature of a heat source fluid supplied to an evaporator and a temperature of a fluid to be heated supplied to an absorber, and a heat pump system based on a signal from the mechanism. By adopting a configuration with a mechanism that switches between the and the boiler system,
The purpose is to stably raise the temperature of the fluid to be heated.
以下、本発明の実施例を図面に基いて説明する。第1図
において(1)は灯油等の燃焼加熱室(2)を有し、吸
収液から冷媒蒸気を加熱分離する発生器、(3)は発生
器(1)からの冷媒蒸気を凝縮冷却する凝縮器、(4)
は凝縮器(3)からの冷媒液を気化せしめる蒸発器、
(5)は蒸発器(4)からの気化冷媒を吸収液に吸収せ
しめる吸収器、(6)は溶液熱交換器で、これらは冷媒
蒸気管(7)、開閉弁(8)を有する冷媒液流下管
(9)、冷媒ポンプ(10)を有する冷媒循環路(11)、
溶液ポンプ(12)を有する稀液管(13)及び濃液管(1
4)で接続されて吸収ヒートポンプサイクルを形成す
る。Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, (1) has a combustion heating chamber (2) for kerosene or the like, and a generator that heat-separates the refrigerant vapor from the absorbing liquid, and (3) condenses and cools the refrigerant vapor from the generator (1). Condenser, (4)
Is an evaporator for vaporizing the refrigerant liquid from the condenser (3),
(5) is an absorber that absorbs the vaporized refrigerant from the evaporator (4) into an absorbing liquid, (6) is a solution heat exchanger, and these are refrigerant liquids having a refrigerant vapor pipe (7) and an on-off valve (8) A refrigerant pipe (9), a refrigerant circulation path (11) having a refrigerant pump (10),
Dilute liquid pipe (13) with solution pump (12) and concentrated liquid pipe (1)
4) Connected to form an absorption heat pump cycle.
(15)は凝縮器(3)と発生器(1)とを接続した開閉
弁(16)付きの冷媒液管で、該管と冷媒蒸気管(7)を
通して発生器(1)と凝縮器(3)間の冷媒循環サイク
ルが形成される。(15) is a refrigerant liquid pipe with an on-off valve (16) that connects the condenser (3) and the generator (1), and the generator (1) and the condenser ( A refrigerant circulation cycle between 3) is formed.
(17)は冷媒循環路(11)と吸収器(5)とを接続した
開閉弁(18)付きの冷媒ブロー管であり、(19)は燃焼
加熱室(2)への燃料供給管で、該管には燃料制御弁
(20)が配設されている。(17) is a refrigerant blow pipe with an on-off valve (18) that connects the refrigerant circulation path (11) and the absorber (5), and (19) is a fuel supply pipe to the combustion heating chamber (2), A fuel control valve (20) is arranged in the pipe.
(21)は蒸発器(4)に収納した熱源管、(22)は吸収
器(5)及び凝縮器(3)に収納した被加熱流体取り出
し管で、該管には三方弁(23)を介して吸収器(5)を
側路するバイパス管(24)が配設されている。(21) is a heat source tube housed in the evaporator (4), (22) is a heated fluid take-out tube housed in the absorber (5) and the condenser (3), and has a three-way valve (23) in the tube. A bypass pipe (24) is provided to bypass the absorber (5).
(25)及び(26)は熱源管(21)及び被加熱流体取出し
管(22)に供給される夫々の流体の温度を検出する検出
器、(27)は検出器(25)、(26)からの信号を受け、
熱源流体の温度が被加熱流体の温度より高いときは前記
開閉弁(8)を開、三方弁(23)の吸収器(5)側流路
を開、開閉弁(16)を閉、三方弁(23)のバイパス管
(24)側流路を閉に、また熱源流体の温度が被加熱流体
の温度と同一若しくは低いときは前記開閉弁(8)を
閉、三方弁(23)の吸収器(5)側流路を閉、開閉弁
(16)を開、三方弁(23)のバイパス管(24)側流路を
開に切替える制御器である。熱源流体の温度と被加熱流
体の温度との比較は前記検出器(25)(26)からの信号
を比較演算することによって行なう。この比較演算は、
熱源流体温度をx、被加熱流体温度をy、温度定数をk
とすると、(x+k)の値とyの値のいずれが大きいか
を比較して行なう。尚、温度定数kの値は吸収器(5)
に散布される吸収液の設計濃度によって適宜設定され
る。(25) and (26) are detectors for detecting the temperature of the respective fluids supplied to the heat source pipe (21) and the heated fluid take-out pipe (22), and (27) are detectors (25), (26). Received the signal from
When the temperature of the heat source fluid is higher than the temperature of the fluid to be heated, the on-off valve (8) is opened, the absorber (5) side flow path of the three-way valve (23) is opened, the on-off valve (16) is closed, the three-way valve. The bypass pipe (24) side flow path of (23) is closed, and when the temperature of the heat source fluid is the same as or lower than the temperature of the fluid to be heated, the on-off valve (8) is closed, and the absorber of the three-way valve (23). It is a controller that closes the (5) side flow passage, opens the on-off valve (16), and opens the three-way valve (23) bypass pipe (24) side flow passage. The temperature of the heat source fluid and the temperature of the fluid to be heated are compared by comparing and calculating the signals from the detectors (25) and (26). This comparison operation
The heat source fluid temperature is x, the heated fluid temperature is y, and the temperature constant is k.
Then, which of the value of (x + k) and the value of y is larger is compared. The value of the temperature constant k is the absorber (5)
It is appropriately set according to the designed concentration of the absorbing solution to be sprayed on.
而して、前記熱源管(21)には工場温排水や太陽熱温水
等の熱源流体を供給し、前記燃焼加熱室(2)に燃料供
給して発生器(1)を駆動し、前記被加熱流体取り出し
管(22)に水等の被加熱流体を流して運転する。Then, a heat source fluid such as factory hot waste water or solar hot water is supplied to the heat source pipe (21), fuel is supplied to the combustion heating chamber (2) to drive the generator (1), and the heated object is heated. The fluid take-out pipe (22) is operated by flowing a heated fluid such as water.
(イ)x+k>yの場合(即ち、熱源流体温度>被加熱
流体温度の場合) この場合は、制御器(27)により、開閉弁(16)(18)
を全閉にし、又、三方弁(23)のバイパス管(24)側流
路も全閉とし、開閉弁(8)及び三方弁(23)の吸収器
(5)側流路を開いて吸収ヒートポンプ運転を行ない、
前記取り出し管(22)から昇温された被加熱流体を得
る。(A) In the case of x + k> y (that is, in the case of heat source fluid temperature> heated fluid temperature) In this case, the controller (27) controls the on-off valves (16) (18)
Fully closed, the bypass pipe (24) side flow path of the three-way valve (23) is also fully closed, and the absorber (5) side flow path of the on-off valve (8) and the three-way valve (23) is opened for absorption. Heat pump operation,
A heated fluid to be heated is obtained from the take-out pipe (22).
すなわち、吸収ヒートポンプサイクルを形成して吸収器
(5)での吸収熱及び凝縮器(3)での冷媒凝縮熱で加
熱するヒートポンプ系から昇温された被加熱流体を取り
出す。That is, the heated fluid to be heated is taken out from the heat pump system that forms an absorption heat pump cycle and heats with the absorption heat in the absorber (5) and the refrigerant condensation heat in the condenser (3).
(ロ)x+k≦yの場合(即ち、熱源流体温度≦被加熱
流体温度の場合) この場合は、制御器(27)により、三方弁(23)のバイ
パス管(24)側流路を開き、吸収器(5)側流路を閉
じ、開閉弁(16)を開くと共に開閉弁(8)を閉じて運
転し、前記取り出し管(22)から昇温された被加熱流体
を得る。(B) When x + k ≦ y (that is, when heat source fluid temperature ≦ heated fluid temperature) In this case, the bypass pipe (24) side flow path of the three-way valve (23) is opened by the controller (27), The absorber (5) side flow path is closed, the on-off valve (16) is opened, and the on-off valve (8) is closed to operate, and the heated fluid to be heated is obtained from the take-out pipe (22).
すなわち、発生器(1)と凝縮器(3)との間の冷媒の
循環サイクルを形成して凝縮器(3)での冷媒凝縮熱で
加熱するヒートポンプ系から昇温された被加熱流体を取
り出す。That is, a heated fluid to be heated is taken out from a heat pump system that forms a refrigerant circulation cycle between the generator (1) and the condenser (3) and heats with the heat of refrigerant condensation in the condenser (3). .
尚、この場合には、開閉弁(18)を開いて蒸発器(4)
内の未蒸発冷媒液を吸収器(5)内の吸収液に混入さ
せ、発生器(1)に還流する吸収液濃度をうすめて、該
発生器内の吸収液沸騰温度を低下せしめ、吸収液を昇温
するためのエネルギーを節約することが好ましい。尤も
開閉弁(18)付きの冷媒ブロー管(17)を設けなくても
良い。In this case, open the on-off valve (18) to open the evaporator (4).
The non-evaporated refrigerant liquid inside is mixed with the absorption liquid inside the absorber (5) to dilute the concentration of the absorption liquid flowing back to the generator (1) to lower the absorption liquid boiling temperature inside the generator, It is preferable to save energy for raising the temperature. However, the refrigerant blow pipe (17) with the opening / closing valve (18) may not be provided.
このように、熱源流体の温度と被加熱流体の温度を比較
して被加熱流体を吸収ヒートポンプ系とボイラー系との
いずれかに切替えて取り出すようにすることにより、被
加熱流体からの逆放熱を防止し、安定的に被加熱流体を
昇温することができる。In this way, by comparing the temperature of the heat source fluid and the temperature of the heated fluid and switching the heated fluid to either the absorption heat pump system or the boiler system, the reverse heat radiation from the heated fluid can be eliminated. It is possible to prevent and stably raise the temperature of the fluid to be heated.
尚、(28)は被加熱流体の凝縮器(3)出口側温度を検
知する検出器で、該検出器の信号により温度調節器(2
9)を介して燃料制御弁(20)の開度を制御し、被加熱
流体の取り出し温度を負荷に応じて調節する。Reference numeral (28) is a detector for detecting the temperature of the outlet side of the condenser (3) of the fluid to be heated, and the temperature controller (2
The opening of the fuel control valve (20) is controlled via 9), and the temperature at which the fluid to be heated is taken out is adjusted according to the load.
第2図は、本発明の他の実施例を示す図面で、第1図の
構成要素と同様のものは同一の図番を使用している。第
2図において、(30)は発生器(1)に付設した温水器
で、該温水器の上部を前記冷媒蒸気管(7)の分岐管
(31)と接続し、下部を発生器(1)に接続された冷媒
ドレン管(15)′と接続し、温水器(30)と発生器
(1)との間に冷媒の循環サイクルを形成するようにし
ている。(16)′は冷媒ドレン管(15)′に配設した開
閉弁である。そして、吸収器(5)及び凝縮器(3)に
収納している前記被加熱流体取り出し管(22)を更に温
水器(30)に収納し、被加熱流体取り出し管(22)には
三方弁(23)′を介して吸収器(5)及び凝縮器(3)
を側路するバイパス管(24)′を設けている。また(2
5)′は蒸発器(4)内の蒸気圧を検知する圧力検出
器、(26)′は吸収器(5)内の蒸気圧を検知する圧力
検出器である。尚、(28)′は被加熱流体の温水器(3
0)出口側温度を検知する検出器である。FIG. 2 is a drawing showing another embodiment of the present invention, in which the same elements as those in FIG. 1 use the same drawing numbers. In FIG. 2, (30) is a water heater attached to the generator (1), the upper part of the water heater is connected to the branch pipe (31) of the refrigerant vapor pipe (7), and the lower part is connected to the generator (1). ) Is connected to the refrigerant drain pipe (15) 'to form a refrigerant circulation cycle between the water heater (30) and the generator (1). (16) 'is an on-off valve arranged in the refrigerant drain pipe (15)'. Further, the heated fluid take-out pipe (22) housed in the absorber (5) and the condenser (3) is further housed in a water heater (30), and the heated fluid take-out pipe (22) has a three-way valve. (23) 'through absorber (5) and condenser (3)
A bypass pipe (24) 'is provided for bypassing. Also (2
5) 'is a pressure detector for detecting the vapor pressure in the evaporator (4), and (26)' is a pressure detector for detecting the vapor pressure in the absorber (5). In addition, (28) 'is a water heater (3
0) A detector that detects the outlet temperature.
而して、圧力検出器(25)′、(26)′からの信号を前
記制御器(27)に入力して演算させ、蒸発器(4)内圧
の方が吸収器(5)内圧より高い場合換言すれば熱源流
体温度の方が被加熱流体温度より高い場合には、制御器
(27)により三方弁(23)′のバイパス管(24)′側流
路を閉じると共に開閉弁(16)′を閉じ、三方弁(2
3)′の凝縮器(3)側流路を開き、吸収ヒートポンプ
サイクルを形成して吸収器(5)での吸収熱及び凝縮器
(3)での冷媒凝縮熱で加熱すヒートポンプ系から昇温
された被加熱流体を取り出し、蒸発器(4)内圧の方が
吸収器(5)内圧より低い場合換言すれば熱源流体温度
の方が被加熱流体温度より低い場合には、制御器(27)
により三方弁(23)′のバイパス管(24)′側流路を開
くと共に開閉弁(16)′を開き、三方弁(23)′の凝縮
器(3)側流路を閉じ、発生器(1)と温水器(30)と
の間の冷媒循環サイクルを形成して温水器(1)での冷
媒凝縮熱で加熱するボイラー系から昇温された被加熱流
体を取り出す。Then, the signals from the pressure detectors (25) 'and (26)' are input to the controller (27) for calculation, and the internal pressure of the evaporator (4) is higher than the internal pressure of the absorber (5). In other words, when the temperature of the heat source fluid is higher than the temperature of the fluid to be heated, the controller (27) closes the flow path on the bypass pipe (24) 'side of the three-way valve (23)' and the open / close valve (16). ′ Is closed and the three-way valve (2
3) ′ opens the flow path on the condenser (3) side, forms an absorption heat pump cycle, and heats up with heat absorbed by the absorber (5) and heat of refrigerant condensation in the condenser (3). When the fluid to be heated is taken out and the internal pressure of the evaporator (4) is lower than the internal pressure of the absorber (5), in other words, when the heat source fluid temperature is lower than the heated fluid temperature, the controller (27)
To open the bypass pipe (24) 'side flow path of the three-way valve (23)' and open the on-off valve (16) 'to close the condenser (3) side flow path of the three-way valve (23)' to generate the generator ( A refrigerant circulation cycle is formed between 1) and the water heater (30), and the heated fluid to be heated is taken out from the boiler system that is heated by the heat of condensation of the refrigerant in the water heater (1).
尚、吸収器(5)内圧を直接検知して制御器(27)に信
号を入力する代りに吸収器(5)内に散布される吸収液
の比重を測定する検出器(26)″および吸収液の温度を
検知する検出器(26)からの信号を演算器(32)に入
力し、該演算器において吸収液濃度を算出し、かつ吸収
液の飽和蒸気圧を算出するようにして、制御器(27)に
信号を入力しても良い。Incidentally, instead of directly detecting the internal pressure of the absorber (5) and inputting a signal to the controller (27), a detector (26) ″ for measuring the specific gravity of the absorbing liquid dispersed in the absorber (5) and the absorption Control is performed by inputting a signal from a detector (26) that detects the temperature of the liquid into a calculator (32), calculating the concentration of the absorbing liquid and calculating the saturated vapor pressure of the absorbing liquid in the calculator. A signal may be input to the container (27).
以上のように、本発明は、発生器、凝縮器、蒸発器、吸
収器及び溶液熱交換器を配管接続し、吸収ヒートポンプ
サイクルを形成して被加熱流体を吸収熱及び冷媒の凝縮
熱で加熱するヒートポンプ系と、冷媒の循環サイクルを
形成して被加熱流体を冷媒の凝縮熱で加熱するボイラー
系とを構成し、かつ蒸発器に供給する熱源流体の温度と
吸収器に供給する被加熱流体の温度とを検出して比較す
る機構を備えると共に熱源流体の温度の方が高いときに
はヒートポンプ系から被加熱流体を取り出し、被加熱流
体の温度の方が高いときにはボイラー系から被加熱流体
を取り出す切替機構を備えたものであるから、被加熱流
体からの逆放熱を防止し、安定的に被加熱流体を昇温す
ることができる。As described above, according to the present invention, the generator, the condenser, the evaporator, the absorber, and the solution heat exchanger are connected by piping, and an absorption heat pump cycle is formed to heat the fluid to be heated by the absorption heat and the condensation heat of the refrigerant. Heat pump system and a boiler system that forms a refrigerant circulation cycle to heat the fluid to be heated with the heat of condensation of the refrigerant, and the temperature of the heat source fluid to be supplied to the evaporator and the fluid to be heated to be supplied to the absorber. A switch for extracting the heated fluid from the heat pump system when the temperature of the heat source fluid is higher and extracting the heated fluid from the boiler system when the temperature of the heated fluid is higher Since it has a mechanism, it is possible to prevent reverse heat radiation from the fluid to be heated and to stably raise the temperature of the fluid to be heated.
第1図は、本発明の一実施例を示した回路構成概略説明
図、第2図は本発明の他の実施例を示した回路構成概略
説明図である。 (1)…発生器、(2)…凝縮器、(4)…蒸発器、
(5)…吸収器、(6)…溶液熱交換器、(8)…開閉
弁、(15)…冷媒液管、(15)′…冷媒ドレイン管、
(16)(16)′…開閉弁、(23)(23)′…三方弁、
(24)(24)′…バイパス管、(25)(25)′…検出
器、(26)(26)′(26)″(26)…検出器、(27)
…制御器、(30)…温水器。FIG. 1 is a schematic explanatory diagram of a circuit configuration showing one embodiment of the present invention, and FIG. 2 is a schematic explanatory diagram of a circuit configuration showing another embodiment of the present invention. (1) ... Generator, (2) ... Condenser, (4) ... Evaporator,
(5) ... Absorber, (6) ... Solution heat exchanger, (8) ... Open / close valve, (15) ... Refrigerant liquid pipe, (15) '... Refrigerant drain pipe,
(16) (16) '... open / close valve, (23) (23)' ... three-way valve,
(24) (24) '... bypass pipe, (25) (25)' ... detector, (26) (26) '(26) "(26) ... detector, (27)
… Controller, (30)… Water heater.
Claims (1)
熱交換器を配管接続し、吸収ヒートポンプサイクルを形
成して被加熱流体を吸収液の冷媒吸収熱及び冷媒の凝縮
熱で加熱するヒートポンプ系と、冷媒の循環サイクルを
形成して被加熱流体を冷媒の凝縮熱で加熱するボイラー
系とを構成し、かつ蒸発器に供給する熱源流体の温度と
吸収器に供給する被加熱流体の温度とを検出して比較す
る機構を備えると共に熱源流体の温度の方が高いときに
はヒートポンプ系から被加熱流体を取り出し、被加熱流
体の温度の方が高いときにはボイラー系から被加熱流体
を取り出す切替機構を備えたことを特徴とする吸収ヒー
トポンプ。1. A generator, a condenser, an evaporator, an absorber, and a solution heat exchanger are connected by piping to form an absorption heat pump cycle to heat a fluid to be heated by heat of absorption of refrigerant of absorption liquid and heat of condensation of refrigerant. Heat pump system and a boiler system that forms a refrigerant circulation cycle to heat the fluid to be heated with the heat of condensation of the refrigerant, and the temperature of the heat source fluid to be supplied to the evaporator and the fluid to be heated to be supplied to the absorber. A switch for extracting the heated fluid from the heat pump system when the temperature of the heat source fluid is higher and extracting the heated fluid from the boiler system when the temperature of the heated fluid is higher An absorption heat pump characterized by having a mechanism.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6290282A JPH0670535B2 (en) | 1982-04-14 | 1982-04-14 | Absorption heat pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6290282A JPH0670535B2 (en) | 1982-04-14 | 1982-04-14 | Absorption heat pump |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58179779A JPS58179779A (en) | 1983-10-21 |
| JPH0670535B2 true JPH0670535B2 (en) | 1994-09-07 |
Family
ID=13213641
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6290282A Expired - Lifetime JPH0670535B2 (en) | 1982-04-14 | 1982-04-14 | Absorption heat pump |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0670535B2 (en) |
-
1982
- 1982-04-14 JP JP6290282A patent/JPH0670535B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58179779A (en) | 1983-10-21 |
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