JPS6246790B2 - - Google Patents

Info

Publication number
JPS6246790B2
JPS6246790B2 JP55009113A JP911380A JPS6246790B2 JP S6246790 B2 JPS6246790 B2 JP S6246790B2 JP 55009113 A JP55009113 A JP 55009113A JP 911380 A JP911380 A JP 911380A JP S6246790 B2 JPS6246790 B2 JP S6246790B2
Authority
JP
Japan
Prior art keywords
temperature
heating
absorber
detected
condenser
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
Application number
JP55009113A
Other languages
Japanese (ja)
Other versions
JPS56108065A (en
Inventor
Koichi Katayama
Seiichi Ito
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP911380A priority Critical patent/JPS56108065A/en
Publication of JPS56108065A publication Critical patent/JPS56108065A/en
Publication of JPS6246790B2 publication Critical patent/JPS6246790B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 本発明は吸収式冷凍機に関し、特に、冷房運
転、ならびに冷房および暖房運転を同時に行なう
ヒートポンプ運転を切換えて使用する吸収式冷凍
機に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption refrigerating machine, and more particularly to an absorption refrigerating machine that switches between cooling operation and heat pump operation that simultaneously performs cooling and heating operations.

従来からの二重効用吸収式冷凍機を示す第1図
を参照して、二重効用吸収式冷凍機は高温再生器
1、低温再生器2、凝縮器3、蒸発器4および吸
収器5などによつて構成されている。この二重効
用吸収式冷凍機をヒートポンプ運転すると、蒸発
器4内のコイル7を流通する水から熱量を汲上げ
て、凝縮器3および吸収器5内のコイル8を流通
する水が加熱される。したがつてコイル7からは
冷水が得られ、コイル8からは温水が得られる。
このようなヒートポンプ運転時において、前記冷
水を利用する負荷の変動によつて冷水温度が変化
するのを防ぐために、従来では、冷水温度を温度
検出器6で検出し、温度調節器9によつて調節弁
10の開度を調節して高温再生器1の加熱量を調
節していた。その結果、コイル8から得られる温
水温度は、温水負荷とは無関係に、冷水負荷が小
になると低下し、また冷水負荷が大になると高く
なつていた。したがつて、従来では、コイル8か
ら得られる温水温度を調節するための温熱源を別
個に設ける必要があつた。
Referring to FIG. 1 showing a conventional dual-effect absorption refrigerator, the double-effect absorption refrigerator includes a high temperature regenerator 1, a low temperature regenerator 2, a condenser 3, an evaporator 4, an absorber 5, etc. It is composed of. When this dual-effect absorption refrigerator is operated with a heat pump, the amount of heat is pumped up from the water flowing through the coil 7 in the evaporator 4, and the water flowing through the coil 8 in the condenser 3 and absorber 5 is heated. . Therefore, cold water is obtained from the coil 7 and hot water is obtained from the coil 8.
During such heat pump operation, in order to prevent the chilled water temperature from changing due to fluctuations in the load using the chilled water, conventionally, the chilled water temperature is detected by a temperature detector 6 and controlled by a temperature controller 9. The heating amount of the high temperature regenerator 1 was adjusted by adjusting the opening degree of the control valve 10. As a result, the temperature of the hot water obtained from the coil 8 decreased as the cold water load became small, and increased as the cold water load became large, regardless of the hot water load. Therefore, in the past, it was necessary to separately provide a heat source for adjusting the temperature of the hot water obtained from the coil 8.

本発明は、上述の技術的課題を解決し、ヒート
ポンプ運転時に温水負荷に応じた温度の温水を得
ることのできる吸収式冷凍機を提供することを目
的とする。
An object of the present invention is to solve the above-mentioned technical problems and provide an absorption refrigerator that can obtain hot water at a temperature that corresponds to the hot water load during heat pump operation.

本発明は、冷房用流体が供給されて冷房を行な
う冷房器19と、暖房用流体が供給されて暖房を
行なう暖房器25とを有する冷暖房装置に用いら
れる吸収式冷凍機において、 ヒートポンプ運転時に、蒸発器14内の冷媒ま
たは蒸発器14で冷却される前記冷房用流体の出
口の温度を第1温度検出器28,29によつて検
出し、この第1温度検出器28,29によつて検
出された温度が低下するにつれて、吸収器15お
よび凝縮器13内で加熱される前記暖房用流体の
一部が吸収器15を多くバイパスして凝縮器13
に流通するように構成し、 この冷房用流体を冷房器19に循環し、 凝縮器13で加熱された暖房用流体の出口の温
度を第2温度検出器31によつて検出し、この第
2温度検出器31によつて検出された温度が低下
するにつれて再生器11の加熱量を増大し、 暖房用流体を暖房器25に循環することを特徴
とする吸収式冷凍機である。
The present invention provides an absorption refrigerating machine used in an air-conditioning apparatus that has an air conditioner 19 that is supplied with a cooling fluid to perform air conditioning, and a heater 25 that is supplied with a heating fluid and that performs heating. The temperature of the refrigerant in the evaporator 14 or the outlet of the cooling fluid cooled by the evaporator 14 is detected by first temperature detectors 28 and 29; As the heated temperature decreases, more of the heating fluid heated in the absorber 15 and condenser 13 bypasses the absorber 15 and flows into the condenser 13.
The cooling fluid is circulated to the air conditioner 19, and the temperature at the outlet of the heating fluid heated by the condenser 13 is detected by the second temperature detector 31. This absorption refrigerator is characterized in that as the temperature detected by the temperature detector 31 decreases, the heating amount of the regenerator 11 is increased and the heating fluid is circulated to the heater 25.

以下、図面によつて本発明の実施例を説明す
る。第2図は本発明の一実施例の系統図であり、
ヒートポンプ運転状態を示す。この二重効用吸収
式冷凍機は、第1図に示す従来のものと同様に高
温再生器11、低温再生器12、凝縮器13、蒸
発器14、吸収器15、高温熱交換器16および
低温熱交換器17を含む。蒸発器14内のコイル
18は管路20,21を介して冷房器19と連結
され、それによつて冷水循環回路が形成される。
凝縮器13および吸収器15のコイル22は管路
23,24を介して暖房器25に連結され、それ
によつて温水循環回路が形成される。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 2 is a system diagram of an embodiment of the present invention,
Indicates the heat pump operating status. This dual-effect absorption refrigerator, like the conventional one shown in FIG. It includes a heat exchanger 17. A coil 18 in the evaporator 14 is connected to a cooler 19 via pipes 20, 21, thereby forming a cold water circulation circuit.
The coils 22 of the condenser 13 and the absorber 15 are connected via lines 23, 24 to a heater 25, thereby forming a hot water circulation circuit.

管路24の途中には、三方弁26が設けられ
る。この三方弁26の残余の接続端には、バイパ
ス管路27の一端部が連結され、バイパス管路2
7の他端部はコイル22の途中に連結される。蒸
発器14のコイル18に連結された管路21の途
中には温度検出器28が備えられる。この温度検
出器28の信号に応答して温度調節器30を介し
て三方弁26が制御され、温度検出器28によつ
て検出される冷水の温度が低下すると、三方弁2
6は、バイパス管路27への流量が大となるよう
に制御される。この温度検出器28に代えて、蒸
発器14内の冷媒の温度を検出する温度検出器2
9を設けてもよい。管路23の途中には温度検出
器31が設けられる。高温再生器11内に高温蒸
気または燃料を供給する管路33の途中には調節
弁34が備えられる。調節弁34は、温度検出器
31の信号に応答する温度調節器32によつて制
御される。
A three-way valve 26 is provided in the middle of the conduit 24. One end of the bypass pipe 27 is connected to the remaining connection end of the three-way valve 26, and the bypass pipe 27 is connected to one end of the bypass pipe 27.
The other end of 7 is connected to the middle of coil 22 . A temperature detector 28 is provided in the middle of the pipe line 21 connected to the coil 18 of the evaporator 14 . The three-way valve 26 is controlled via the temperature regulator 30 in response to the signal from the temperature sensor 28, and when the temperature of the cold water detected by the temperature sensor 28 decreases, the three-way valve 26
6 is controlled so that the flow rate to the bypass pipe line 27 is large. In place of this temperature detector 28, a temperature detector 2 that detects the temperature of the refrigerant in the evaporator 14
9 may be provided. A temperature detector 31 is provided in the middle of the pipe line 23. A control valve 34 is provided in the middle of a pipe line 33 that supplies high-temperature steam or fuel into the high-temperature regenerator 11 . Regulating valve 34 is controlled by temperature regulator 32 which is responsive to the signal of temperature sensor 31 .

ヒートポンプ運転時に、冷房器19の負荷が変
動して小になり、それに応じて管路21内の冷水
または蒸発器14内の冷媒の温度が低下すると、
バイパス管路27を流通する温水の流量が大とな
る。そのため、吸収器15内の温度が上昇し、吸
収器15内で溶液温度が上昇する。したがつて溶
液の吸収能力が低下して、冷水の温度が制御され
る。また、管路23内を流通する温水の温度が低
下すると、調節弁34の開度が大とされ、それに
よつて高温再生器11の加熱量が増大し、したが
つてコイル22で得られる温水の温度を高めるこ
とができる。
During heat pump operation, when the load on the air conditioner 19 fluctuates and becomes smaller, and the temperature of the cold water in the pipe line 21 or the refrigerant in the evaporator 14 decreases accordingly,
The flow rate of hot water flowing through the bypass pipe line 27 becomes large. Therefore, the temperature inside the absorber 15 rises, and the solution temperature inside the absorber 15 rises. Therefore, the absorption capacity of the solution is reduced and the temperature of the cold water is controlled. Furthermore, when the temperature of the hot water flowing through the pipe line 23 decreases, the opening degree of the control valve 34 is increased, thereby increasing the heating amount of the high temperature regenerator 11, and therefore the hot water obtained by the coil 22 is increased. temperature can be increased.

高温再生器11の加熱量が増大するのに応じ
て、高温再生器11における冷媒の蒸発量が増大
するとともに、吸収器15に流入する溶液の濃度
が大となるので、コイル18における冷却能力が
増大する。このとき、冷房器19の負荷が小さい
と、冷水および冷媒の温度が低下する。この冷水
または冷媒の温度は、温度検出器28または29
で検出されており、温度低下に応じてバイパス管
路27への温水流量が増大する方向に三方弁26
が制御される。それによつて、吸収器15におけ
る溶液の温度が上昇して吸収能力が回復する。そ
の結果、前記冷水および冷媒温度が低下し過ぎる
ことが防止され、冷房器19および暖房器25の
各負荷に対応した温度の冷水および温水をそれぞ
れ得ることができる。
As the heating amount of the high-temperature regenerator 11 increases, the amount of evaporation of the refrigerant in the high-temperature regenerator 11 increases, and the concentration of the solution flowing into the absorber 15 increases, so that the cooling capacity of the coil 18 increases. increase At this time, if the load on the air conditioner 19 is small, the temperatures of the cold water and the refrigerant decrease. The temperature of this cold water or refrigerant is measured by a temperature sensor 28 or 29.
The three-way valve 26 increases the flow rate of hot water to the bypass pipe 27 as the temperature decreases.
is controlled. Thereby, the temperature of the solution in the absorber 15 increases and the absorption capacity is restored. As a result, the cold water and refrigerant temperatures are prevented from dropping too much, and cold water and hot water can be obtained at temperatures corresponding to the loads of the air conditioner 19 and the heater 25, respectively.

上述の実施例は、暖房器25の負液が冷房器1
9に相当する負荷量よりも大の場合に有効である
が、暖房器25の負荷が前記負荷量よりも小の場
合には、第1図に示す従来の運転方法に切換えて
使用することができる。すなわち、高温再生器1
の加熱量を制御するための温度検出器6を蒸発器
4から得られる冷水の温度を検出すべく設け、そ
の温度検出器6の信号に応答して温度調節器9を
介して調節弁10を制御すればよい。
In the above embodiment, the negative liquid of the heater 25 is connected to the cooler 1.
This method is effective when the load amount is larger than the load amount corresponding to 9, but when the load on the heater 25 is smaller than the load amount, it is possible to switch to the conventional operating method shown in FIG. can. That is, high temperature regenerator 1
A temperature detector 6 is provided to detect the temperature of cold water obtained from the evaporator 4, and a control valve 10 is activated via a temperature controller 9 in response to a signal from the temperature detector 6. Just control it.

したがつて、冷房器19の負荷が大となり、冷
水温度が上昇し過ぎる場合には、第1図で示す従
来の制御方法とし、一方、暖房器25の負荷が増
大し、温水温度が低下し過ぎる場合には、第2図
で示す本発明の制御方法となるように切換えて使
用することができる。
Therefore, when the load on the air conditioner 19 becomes large and the cold water temperature rises too much, the conventional control method shown in FIG. If it is too long, the control method of the present invention shown in FIG. 2 can be used.

本発明は上述の二重効用吸収式冷凍機に限定さ
れるものではなく、一重効用吸収式冷凍機に関連
して実施することもできる。
The invention is not limited to the dual-effect absorption refrigerators described above, but can also be implemented in conjunction with single-effect absorption refrigerators.

以上のように本発明によれば、蒸発器14内の
冷媒または蒸発器14で冷却される冷房用流体の
出口の温度を、第1温度検出器28,29によつ
て検出し、この温度が低下するにつれて、吸収器
15をバイパスする暖房用流体の流量を大きくす
るようにしたので、再生器11,12内の温度が
上昇して吸収器15内の吸収能力が低下しても、
吸収器15内の温度が増大し、その吸収能力を回
復させることができる。したがつて冷房器19お
よび暖房器25の負荷に対応して、冷房用および
暖房用熱源としての冷房用流体および暖房用流体
の温度を制御することができる。
As described above, according to the present invention, the temperature at the outlet of the refrigerant in the evaporator 14 or the cooling fluid cooled by the evaporator 14 is detected by the first temperature detectors 28 and 29, and this temperature is detected by the first temperature detectors 28 and 29. As the temperature decreases, the flow rate of the heating fluid that bypasses the absorber 15 is increased, so even if the temperature in the regenerators 11 and 12 rises and the absorption capacity in the absorber 15 decreases,
The temperature within the absorber 15 increases and its absorption capacity can be restored. Therefore, the temperatures of the cooling fluid and the heating fluid, which serve as cooling and heating heat sources, can be controlled in accordance with the loads on the air conditioner 19 and the heater 25.

しかもまた本発明によれば、吸収器15および
凝縮器13で順次加熱される暖房用流体の、凝縮
器13からの出口の温度を第2温度検出器31に
よつて検出し、この温度が低下するにつれて再生
器11の加熱量を増大するようにしたので、暖房
用流体の温度を増大することができる。
Furthermore, according to the present invention, the second temperature detector 31 detects the temperature of the heating fluid heated sequentially in the absorber 15 and the condenser 13 at the outlet from the condenser 13, and the temperature decreases. Since the heating amount of the regenerator 11 is increased accordingly, the temperature of the heating fluid can be increased.

さらにまた本発明によれば、再生器11の加熱
量を増大することによつて、冷房用流体の温度が
低下する結果になる。したがつて上述のように吸
収器15をバイパスする暖房用流体の流量が増大
し、これによつて吸収器15における吸収能力を
回復することができる。このようにして冷房用流
体が、低下し過ぎることを上首尾に防ぐことがで
きるという優れた効果が達成される。
Furthermore, according to the present invention, increasing the heating amount of the regenerator 11 results in a decrease in the temperature of the cooling fluid. Therefore, as described above, the flow rate of the heating fluid that bypasses the absorber 15 increases, thereby allowing the absorption capacity in the absorber 15 to be restored. In this way, an excellent effect is achieved in that the cooling fluid can be successfully prevented from dropping too low.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の二重効用吸収式冷凍機の系統
図、第2図は本発明の一実施例の二重効用吸収式
冷凍機の系統図である。 11……高温再生器、12……低温再生器、1
3……凝縮器、14……蒸発器、15……吸収
器、19……冷房器、25……暖房器、26……
三方弁、27……バイパス管路、28,29,3
1……温度検出器、30,32……温度調節器。
FIG. 1 is a system diagram of a conventional dual-effect absorption refrigerating machine, and FIG. 2 is a system diagram of a dual-effect absorption refrigerating machine according to an embodiment of the present invention. 11...High temperature regenerator, 12...Low temperature regenerator, 1
3... Condenser, 14... Evaporator, 15... Absorber, 19... Air conditioner, 25... Heater, 26...
Three-way valve, 27... Bypass pipeline, 28, 29, 3
1... Temperature detector, 30, 32... Temperature regulator.

Claims (1)

【特許請求の範囲】 1 冷房用流体が供給されて冷房を行なう冷房器
19と、暖房用流体が供給されて暖房を行なう暖
房器25とを有する冷暖房装置に用いられる吸収
式冷凍機において、 ヒートポンプ運転時に、蒸発器14内の冷媒ま
たは蒸発器14で冷却される前記冷房用流体の出
口の温度を第1温度検出器28,29によつて検
出し、この第1温度検出器28,29によつて検
出された温度が低下するにつれて、吸収器15お
よび凝縮器13内で加熱される前記暖房用流体の
一部が吸収器15を多くバイパスして凝縮器13
に流通するように構成し、 この冷房用流体を冷房器19に循環し、 凝縮器13で加熱された暖房用流体の出口の温
度を第2温度検出器31によつて検出し、この第
2温度検出器31によつて検出された温度が低下
するにつれて再生器11の加熱量を増大し、 暖房用流体を暖房器25に循環することを特徴
とする吸収式冷凍機。
[Scope of Claims] 1. In an absorption chiller used in an air-conditioning device, which has an air conditioner 19 that performs air conditioning by being supplied with a cooling fluid, and a heater 25 that performs heating by being supplied with a heating fluid, a heat pump is provided. During operation, the temperature of the refrigerant in the evaporator 14 or the outlet of the cooling fluid cooled by the evaporator 14 is detected by the first temperature detectors 28, 29; Thus, as the detected temperature decreases, more of the heating fluid heated in the absorber 15 and condenser 13 bypasses the absorber 15 and flows into the condenser 13.
The cooling fluid is circulated to the air conditioner 19, and the temperature at the outlet of the heating fluid heated by the condenser 13 is detected by the second temperature detector 31. An absorption refrigerator characterized in that as the temperature detected by the temperature detector 31 decreases, the heating amount of the regenerator 11 is increased, and the heating fluid is circulated to the heater 25.
JP911380A 1980-01-28 1980-01-28 Absorption type refrigerator Granted JPS56108065A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP911380A JPS56108065A (en) 1980-01-28 1980-01-28 Absorption type refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP911380A JPS56108065A (en) 1980-01-28 1980-01-28 Absorption type refrigerator

Publications (2)

Publication Number Publication Date
JPS56108065A JPS56108065A (en) 1981-08-27
JPS6246790B2 true JPS6246790B2 (en) 1987-10-05

Family

ID=11711570

Family Applications (1)

Application Number Title Priority Date Filing Date
JP911380A Granted JPS56108065A (en) 1980-01-28 1980-01-28 Absorption type refrigerator

Country Status (1)

Country Link
JP (1) JPS56108065A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5857670U (en) * 1981-10-14 1983-04-19 三洋電機株式会社 absorption refrigerator

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5818573B2 (en) * 1975-07-26 1983-04-13 オオサカガス カブシキガイシヤ Kiyushyuushiyushikireitouki
JPS5747665Y2 (en) * 1977-05-20 1982-10-19

Also Published As

Publication number Publication date
JPS56108065A (en) 1981-08-27

Similar Documents

Publication Publication Date Title
US3837174A (en) Control device for an absorption system hot and cold water supply apparatus
JP4248099B2 (en) Control method of refrigerator or hot and cold water machine
US5259202A (en) Absorption air-conditioning system
US4894998A (en) Absorption system hot and cold water supply apparatus
JPH01189436A (en) environmental test equipment
US5275010A (en) Control method and apparatus of absorption chiller heater
US4324288A (en) Level supply air temperature multi-zone heat pump system and method
JPS6246790B2 (en)
JPH038453B2 (en)
JPH062982A (en) Absorption cooling and heating system and its control method
JP3588144B2 (en) Operating number control of absorption chillers installed in parallel
JP3138164B2 (en) Absorption refrigerator
JPS6021721Y2 (en) Absorption chiller control device
JPH0221499B2 (en)
JPH03129264A (en) Absorption cool and hot water system
JP2654009B2 (en) Absorption refrigerator
JPS6338868A (en) Controller for double effect absorption water chiller and heater
JPH04110572A (en) Control device for absorption type freezer
JP3280261B2 (en) Absorption refrigeration equipment
JPS6157537B2 (en)
SU1597500A1 (en) Absorption refrigeration unit
JPH0355748B2 (en)
JPS5844303B2 (en) How to control absorption chiller operation
JPS6222056B2 (en)
JPS5921957A (en) Absorption cold and hot water machine