JPH0577947B2 - - Google Patents

Info

Publication number
JPH0577947B2
JPH0577947B2 JP56021869A JP2186981A JPH0577947B2 JP H0577947 B2 JPH0577947 B2 JP H0577947B2 JP 56021869 A JP56021869 A JP 56021869A JP 2186981 A JP2186981 A JP 2186981A JP H0577947 B2 JPH0577947 B2 JP H0577947B2
Authority
JP
Japan
Prior art keywords
generator
hot water
low
heat source
temperature
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
Application number
JP56021869A
Other languages
Japanese (ja)
Other versions
JPS57136065A (en
Inventor
Kenichi Ooyama
Junzo Kato
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP2186981A priority Critical patent/JPS57136065A/en
Publication of JPS57136065A publication Critical patent/JPS57136065A/en
Publication of JPH0577947B2 publication Critical patent/JPH0577947B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 本発明は二重効用吸収冷凍機と吸収式ヒートポ
ンプとの切替運転を可能にすることにより、低温
度レベルの熱源を有効に活用して夏期には冷房用
冷水、冬期には暖房用温水を一台の吸収冷凍機で
安定して供給できるようにした吸収冷温水装置に
関する。
Detailed Description of the Invention The present invention enables switching operation between a dual-effect absorption chiller and an absorption heat pump, thereby effectively utilizing a low-temperature level heat source to provide cold water for air conditioning in the summer and cold water for air conditioning in the winter. The present invention relates to an absorption chiller/heater that can stably supply hot water for heating with a single absorption chiller.

以下に本発明の実施例を図面に従い説明する
と、1は例えば水等の冷媒を吸収して濃度が低下
した吸収液(稀液又は中間液)を加熱量が2段に
切替可能なガスバーナー等の加熱器2によつて直
接に加熱して冷媒を気化分離するようにした高温
発生器、3は気状冷媒と共に揚液された吸収液と
冷媒とを分離する分離器、4は該高温発生器1で
発生した気状冷媒による加熱器5を有し、高温発
生器1或いは後述する吸収器から流入してくる吸
収液から冷媒を気化分離する低温発生器、7は流
体による凝縮熱交換器8を内蔵し器内に流入する
気状の冷媒ガスを凝集液化する凝縮器、9は凝縮
器7から流入する液冷媒を低圧容器10に導びき
気化熱交換器11中の流体から気化潜熱を得るよ
うにした蒸発器、6は発生器、1,4で濃縮され
た濃液を散布しつつ、吸収反応熱を吸収熱交換器
9で気化した冷媒と共に吸収させ、蒸発器9にお
ける連続した気化機能を保つようにした吸収器、
13は冷媒を吸収して稀釈された稀液を発生器1
に還流する吸収液ポンプ、14は吸収器6に流出
する高温の濃液と吸収器6から発生器1に戻る低
温の稀液とを熱交換し稀液の予熱、濃液の予冷を
する低温熱交換器、15は高温発生器1に戻る稀
液と濃液とを熱交換する高温熱交換器でありそれ
ぞれ揚液管16冷媒管17,18,19、稀液管
20,21、中間液管22,23、濃液管24、
側路管25,26で接続されて冷媒と吸収液との
密閉循環サイクルを形成している。
Embodiments of the present invention will be described below with reference to the drawings. 1 is a gas burner capable of heating an absorbing liquid (dilute liquid or intermediate liquid) whose concentration has been reduced by absorbing a refrigerant such as water in two stages, etc. 3 is a separator that separates the refrigerant from the absorption liquid pumped together with the gaseous refrigerant; 4 is the high temperature generator A low-temperature generator includes a heater 5 using gaseous refrigerant generated in the reactor 1, and vaporizes and separates the refrigerant from an absorption liquid flowing from the high-temperature generator 1 or an absorber described later, and 7 is a fluid condensation heat exchanger. 8 is a built-in condenser that condenses and liquefies the gaseous refrigerant gas flowing into the vessel; 9 guides the liquid refrigerant flowing from the condenser 7 to the low-pressure vessel 10 to extract latent heat of vaporization from the fluid in the vaporization heat exchanger 11; The evaporator 6 is a generator, which distributes the concentrated liquid in the generators 1 and 4, absorbs the absorption reaction heat together with the vaporized refrigerant in the absorption heat exchanger 9, and continuously vaporizes it in the evaporator 9. Absorber that maintains its functionality,
13 is the generator 1 which absorbs the refrigerant and generates the diluted diluted liquid.
A low-temperature pump 14 exchanges heat between the high-temperature concentrated liquid flowing into the absorber 6 and the low-temperature diluted liquid that returns from the absorber 6 to the generator 1 to preheat the diluted liquid and pre-cool the concentrated liquid. Heat exchanger 15 is a high-temperature heat exchanger that exchanges heat between the dilute liquid and the concentrated liquid that return to the high-temperature generator 1. Pipes 22, 23, concentrated liquid pipe 24,
They are connected by side pipes 25 and 26 to form a closed circulation cycle of the refrigerant and the absorption liquid.

而して、27はオーバーフロー開口28を有
し、太陽熱により加熱された温水などの低温熱源
水(以下低熱源水という)を熱源とする加熱器2
9を有して吸収液から冷媒を加熱分離する温水式
発生器、30は低温発生器4から凝縮器7に流入
する液冷媒の熱で吸収器6から温水式発生器27
に流入する稀液を加熱するようにした熱回収器、
31,32,33はいずれも後述する温水供給時
に閉止し、冷水供給時には開放するようにして冷
媒管19、側路管26、稀液管21に配設された
開閉弁、34は温水供給時に開放し、冷水供給時
に閉止するようにして冷媒管18に配設された開
放弁、35は側路管26に配設された調節弁36
は高温熱交換器15と低温熱交換器14との間に
配設された三方切替弁である。
27 has an overflow opening 28, and a heater 2 whose heat source is low-temperature heat source water (hereinafter referred to as low-heat source water) such as hot water heated by solar heat.
9 is a hot water generator that heats and separates the refrigerant from the absorption liquid; 30 is a hot water generator 27 that uses the heat of the liquid refrigerant flowing from the low temperature generator 4 to the condenser 7 from the absorber 6;
a heat recovery device designed to heat the dilute liquid flowing into the
31, 32, and 33 are all provided in the refrigerant pipe 19, the side pipe 26, and the diluted liquid pipe 21 so as to be closed when hot water is supplied, which will be described later, and opened when cold water is supplied. 34 is a shut-off valve when hot water is supplied. A release valve 35 is disposed in the refrigerant pipe 18 so as to be opened and closed when cold water is supplied; reference numeral 35 is a control valve 36 disposed in the side pipe 26;
is a three-way switching valve disposed between the high temperature heat exchanger 15 and the low temperature heat exchanger 14.

斯かる構成の吸収冷温水装置による冷水供給時
において、温水式発生器27を作動させる低熱源
水が充分に得られないときは、弁31,33を開
放し弁32,34,35を閉じ、三方弁36を第
2図のaの状態にしガスバーナ2による加熱を強
の状態にすると、発生器1で加熱された吸収液は
揚液管16を経て分離器3に流入し、冷媒は冷媒
管19、低温発生器4、熱回収器30、凝縮器7
を経て蒸発器9で散布される一方、吸収液は高温
熱交換器15、低温発生器4、低温熱交換器14
を経て吸収器6に散布され、これにより気化熱交
換器11を循環する流体(例えば冷水)を冷却し
て冷房に供することができる。
When cold water is supplied by the absorption cold/hot water device having such a configuration, if sufficient low heat source water is not available to operate the hot water generator 27, the valves 31 and 33 are opened and the valves 32, 34, and 35 are closed. When the three-way valve 36 is placed in the state shown in FIG. 19, low temperature generator 4, heat recovery device 30, condenser 7
The absorption liquid is distributed in the evaporator 9 through the
The fluid (for example, cold water) circulating through the vaporization heat exchanger 11 can be cooled and used for air conditioning.

斯る運転において凝縮熱交換器8および吸収熱
交換器12には冷却水が流され、又、充分でない
といえ、低熱源水が利用できるときは加熱器29
に低熱源水を送り、かつ、三方弁36を第2図の
bの状態にして温水式発生器27での冷媒発生が
行なえるので、高温発生器1における燃料ガスの
使用量を低減することができ、ガスバーナー2を
弱燃焼にしても先の強燃焼と同様な冷水供給機能
を維持することができる。
In such an operation, cooling water is flowed into the condensing heat exchanger 8 and the absorption heat exchanger 12, and when low heat source water is available even though it is insufficient, the heater 29 is
Since the hot water generator 27 can generate refrigerant by sending low heat source water to the hot water generator 27 and setting the three-way valve 36 to the state shown in FIG. 2b, the amount of fuel gas used in the high temperature generator 1 can be reduced. Therefore, even if the gas burner 2 is set to weak combustion, the same cold water supply function as in the case of strong combustion can be maintained.

尚、低熱源水が充分に得られるときは、上述の
各弁の状態から、三方弁36を第2図cに、又、
開放されていた弁33を閉止にすることにより、
吸収液ポンプ13からの稀液はすべて液管25を
経て温水式発生器27に流入し、該発生器27で
分離された冷媒は凝縮器7から蒸発器9に流入す
る一方、吸収液はオーバーフロー開口28、低温
発生器4、低温熱交換器14を経て吸収器6に流
入するため、先に述べたと同様に気化熱交換器1
1から冷却された流体が得られることとなる。
In addition, when low heat source water is sufficiently obtained, the three-way valve 36 is set as shown in FIG.
By closing the open valve 33,
All the dilute liquid from the absorption liquid pump 13 flows into the hot water generator 27 through the liquid pipe 25, and the refrigerant separated in the generator 27 flows from the condenser 7 to the evaporator 9, while the absorption liquid overflows. In order to flow into the absorber 6 via the opening 28, the low temperature generator 4, and the low temperature heat exchanger 14, the vaporization heat exchanger 1
A cooled fluid is obtained from 1.

尚、低温発生器4の加熱器5には冷媒が流入し
てこないので、該発生器4は事実上作動を休止し
ており、又37は斯る発生器4側への気状冷媒の
流入を妨げる抵抗板である。
Note that since no refrigerant flows into the heater 5 of the low-temperature generator 4, the generator 4 is virtually inactive, and 37 indicates the flow of gaseous refrigerant into the generator 4 side. It is a resistance plate that prevents

次に、冬期や中間期等冷房負荷よりもむしろ温
水等の高温流体の需要のある場合は、弁32,3
4,35を開き、弁31,33を閉じ、三方弁3
6を第2図cの状態にしてガスバーナー2で高温
発生器1の吸収液を加熱すると、揚液管16を上
つた高温の冷媒と吸収液とは分離器3で分離さ
れ、冷媒管18を経て凝縮器7に流入し、ここで
冷媒は凝縮熱交換器8を流れる流体を加熱する一
方、分離器3で分離された吸収液は液管22、高
温熱交換器15、側路管26′、低温熱交換器1
4を経て吸収器6に流入し、吸収熱交換器12を
流れる流体を加熱するので夫々の熱交換器8,1
2の温水を合流して機外に供給することができる
ものである。
Next, when there is a demand for high-temperature fluid such as hot water rather than cooling load such as winter or intermediate season, valves 32 and 3
4, 35 open, valves 31, 33 closed, three-way valve 3
When the absorption liquid in the high temperature generator 1 is heated with the gas burner 2 in the state shown in FIG. The refrigerant flows through the condenser 7, where the refrigerant heats the fluid flowing through the condensing heat exchanger 8, while the absorption liquid separated in the separator 3 flows through the liquid pipe 22, the high temperature heat exchanger 15, and the side pipe 26. ', low temperature heat exchanger 1
4 to the absorber 6 and heats the fluid flowing through the absorption heat exchanger 12.
The two hot waters can be combined and supplied to the outside of the machine.

尚、凝縮器7から蒸発器9に流入した冷媒液は
気化熱交換器11を循環する水を熱源として、い
わゆるヒートポンプ運転が行なわれ、低熱源水の
得られるときは同様に気化熱交換器11に低熱源
水を循環させて該装置の温水供給能力を向上させ
ることもできる。
The refrigerant liquid that has flowed into the evaporator 9 from the condenser 7 is subjected to so-called heat pump operation using the water circulating through the vaporization heat exchanger 11 as a heat source, and when low heat source water is obtained, it is also transferred to the vaporization heat exchanger 11 when low heat source water is obtained. It is also possible to improve the hot water supply capacity of the device by circulating low heat source water.

尚、弁32は低熱源水のないときに開放して冷
媒の循環を妨げないようにするものである。
It should be noted that the valve 32 is opened when there is no low heat source water so as not to interfere with the circulation of the refrigerant.

このように本発明の吸収冷温水装置は、二重効
用吸収冷凍機の吸収液ポンプの吐出側を、加熱燃
料及び低温熱源水を利用した二重効用の冷水供給
運転時に開放する弁を介して温水式発生器と高温
発生器とへ、低温熱源水のみを利用した一重効用
の冷水供給時に開放する弁を介して温水式発生器
へ、温水供給時に開放する弁を介して高温発生器
へ接続したので、吸収器から高温発生器及び温水
式発生器に至る配管構造を簡略化し、且つ二重効
用運転時にも加熱燃料の消費を削減し、一重効用
運転時の加熱燃料の消費削減と合わせて大幅に加
熱燃料の消費を削減した冷温水供給が可能になる
ものである。
In this manner, the absorption chilled/heated water apparatus of the present invention opens the discharge side of the absorption liquid pump of the dual-effect absorption chiller through the valve that opens during the dual-effect cold water supply operation using heated fuel and low-temperature heat source water. Connected to the hot water generator and high temperature generator via a single-effect valve that opens when cold water is supplied using only low-temperature heat source water, and to the high temperature generator via a valve that opens when hot water is supplied. Therefore, we simplified the piping structure from the absorber to the high-temperature generator and the hot water generator, and also reduced heating fuel consumption during dual-effect operation, as well as reducing heating fuel consumption during single-effect operation. This makes it possible to supply cold and hot water with significantly reduced consumption of heating fuel.

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

第1図は本発明装置の構成図、第2図a,b,
cはそれぞれ、各作動条件下における弁の開閉状
態を示す図である。 1……高温発生器、4……低温発生器、6……
吸収器、7……凝縮器、9……蒸発器、13……
吸収液ポンプ、31,32,33,34,35…
…開放弁、36……三方弁。
Fig. 1 is a configuration diagram of the device of the present invention, Fig. 2 a, b,
3c is a diagram showing the opening and closing states of the valve under each operating condition. 1... High temperature generator, 4... Low temperature generator, 6...
Absorber, 7... Condenser, 9... Evaporator, 13...
Absorption liquid pump, 31, 32, 33, 34, 35...
...Release valve, 36...Three-way valve.

Claims (1)

【特許請求の範囲】[Claims] 1 ガス等の加熱燃料を熱源とする高温発生器、
低温発生器、太陽熱等により加熱された低温熱源
水を熱源とする温水式発生器、凝縮器、蒸発器、
吸収器を稀液管、中間液管、冷煤管等で接続して
吸収液と冷煤との循環サイクルを構成すると共に
吸収器から各発生器に稀液を還流する吸収液ポン
プの吐出側は、加熱燃料及び低温熱源水を利用し
た二重効用の冷水供給運転時に開放する弁を介し
て温水式発生器と高温発生器とへ、低温熱源水の
みを利用した一重効用の冷水供給時に開放する弁
を介して温水式発生器へ、温水供給時に開放する
弁を介して高温発生器へ接続されていることを特
徴とする吸収冷温水装置。
1 High temperature generator using heating fuel such as gas as a heat source,
Low-temperature generators, hot water generators whose heat source is low-temperature heat source water heated by solar heat, etc., condensers, evaporators,
The discharge side of the absorption liquid pump that connects the absorber with a diluted liquid pipe, intermediate liquid pipe, cold soot pipe, etc. to form a circulation cycle of the absorption liquid and cold soot, and also returns the diluted liquid from the absorber to each generator. is a valve that is opened during dual-effect cold water supply operation using heating fuel and low-temperature heat source water to the hot water generator and high-temperature generator, and opened during single-effect cold water supply using only low-temperature heat source water. An absorption cold/hot water device characterized in that it is connected to a hot water generator via a valve that opens when hot water is supplied, and to a high temperature generator via a valve that opens when hot water is supplied.
JP2186981A 1981-02-17 1981-02-17 Absorption cold/hot water feeder Granted JPS57136065A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2186981A JPS57136065A (en) 1981-02-17 1981-02-17 Absorption cold/hot water feeder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2186981A JPS57136065A (en) 1981-02-17 1981-02-17 Absorption cold/hot water feeder

Publications (2)

Publication Number Publication Date
JPS57136065A JPS57136065A (en) 1982-08-21
JPH0577947B2 true JPH0577947B2 (en) 1993-10-27

Family

ID=12067126

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2186981A Granted JPS57136065A (en) 1981-02-17 1981-02-17 Absorption cold/hot water feeder

Country Status (1)

Country Link
JP (1) JPS57136065A (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5844182B2 (en) * 1978-06-29 1983-10-01 株式会社荏原製作所 absorption refrigerator
JPS5621869A (en) * 1979-07-31 1981-02-28 Toshiba Corp Printing head for wire dot printer

Also Published As

Publication number Publication date
JPS57136065A (en) 1982-08-21

Similar Documents

Publication Publication Date Title
JP4287705B2 (en) Single double effect absorption refrigerator and operation control method thereof
JP2002357370A (en) Control method of absorption refrigerator
JPS5828903B2 (en) Single and double effect absorption chiller
JP2003343940A (en) Absorption water cooler/heater
JPS5886357A (en) Air-conditioning method utilizing solar heat and its device
JP2000121196A (en) Cooling/heating system utilizing waste heat
KR100512827B1 (en) Absorption type refrigerator
CN115751759A (en) Solar energy coupling air source heat pump system suitable for severe cold high irradiation area
JP3444203B2 (en) Absorption refrigerator
KR100493598B1 (en) Absorption Type Refrigerator
JPS6135900Y2 (en)
JPH0355741B2 (en)
JPS6113550B2 (en)
JP2895974B2 (en) Absorption refrigerator
JPS6113546B2 (en)
JP2001263851A (en) Method for controlling absorption refrigerating machine
JPH0355739B2 (en)
JPH0443264A (en) Absorption type heat source device
JPH03105171A (en) Absorption type water cooler/heater
JPS6149586B2 (en)
JPS5828508B2 (en) Absorption cold/hot water supply device
JPH0446341B2 (en)
JP2538389B2 (en) Absorption air conditioner
JPS6113548B2 (en)
JPH11281185A (en) Single and double effect absorption refrigerating machine