JPS5844183B2 - Single and double effect absorption chiller - Google Patents

Single and double effect absorption chiller

Info

Publication number
JPS5844183B2
JPS5844183B2 JP13638978A JP13638978A JPS5844183B2 JP S5844183 B2 JPS5844183 B2 JP S5844183B2 JP 13638978 A JP13638978 A JP 13638978A JP 13638978 A JP13638978 A JP 13638978A JP S5844183 B2 JPS5844183 B2 JP S5844183B2
Authority
JP
Japan
Prior art keywords
generator
heat exchanger
low
low temperature
temperature 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
Application number
JP13638978A
Other languages
Japanese (ja)
Other versions
JPS5563361A (en
Inventor
伯一 久保田
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.)
Tokyo Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
Sanyo Denki 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 Tokyo Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP13638978A priority Critical patent/JPS5844183B2/en
Publication of JPS5563361A publication Critical patent/JPS5563361A/en
Publication of JPS5844183B2 publication Critical patent/JPS5844183B2/en
Expired legal-status Critical Current

Links

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熱エネルギーの有効利用を図ると共
に安定した切替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 and dual effect absorption refrigerator,
The purpose is to effectively utilize thermal energy according to the heat source and load, and to perform stable switching operation.

すなわち1台の吸収冷凍機を、太陽熱温水や低温水、廃
熱等の低温熱源による場合は一重効用として運転し、都
市ガスや灯油、高温蒸気等の高温熱源による場合には二
重効用として運転数は一重効用と二重効用の併用運転を
任意に行ない得るようにしたものである。
In other words, one absorption chiller is operated as single-effect when using low-temperature heat sources such as solar hot water, low-temperature water, and waste heat, and as double-effect when using high-temperature heat sources such as city gas, kerosene, and high-temperature steam. The number is such that a combination of single effect and double effect operation can be carried out at will.

以下本発明を図に示す実施例について説明する。The present invention will be described below with reference to embodiments shown in the drawings.

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稀液より冷媒を
加熱分離する第1低温発生器、5は冷却器6によって前
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から冷房用冷水を得
るようにした蒸発器、9は前記両発生器1,4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1
2、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、溶
液管路18及び濃液管路19並びに、図示していないが
、第1低温発生器4から低温熱交換器10、高温熱交換
器11間の濃縮管路19へ至る吸収液管路により配管接
続して二重効用吸収冷凍サイクルを構成している。
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 exhaust heat pipes 3, 3, etc. of the heating chamber, and heats and separates a refrigerant from a dilute liquid; 4; 5 is a first low temperature generator that heats and separates the refrigerant from a dilute liquid using the refrigerant vapor sent from the high temperature generator 1 as a heat source; 5 is a cooler 6 that condenses the refrigerant flowing from both generators 1 and 4; a condenser for cooling, 7 an evaporator which obtains cold water for cooling from a water cooler 8 by utilizing latent heat when the liquid refrigerant from the condenser 5 is dispersed and vaporized; 9 a both generators 1; an absorber 10, which maintains the inside of the evaporator 7 at a low pressure and continuously supplies cold water by scattering the concentrated liquid from which the refrigerant is separated in step 4 and absorbing the refrigerant vapor in the container; 11 is a low temperature heat exchanger and a high temperature heat exchanger, these are refrigerant vapor pipe 1
2, a refrigerant circulation path 15 having a refrigerant liquid flow down pipe 13, a refrigerant pump 14, a dilute liquid pipe line 17 having an absorption liquid pump 16, a solution pipe line 18, a concentrated liquid pipe line 19, and, although not shown, a first A double-effect absorption refrigeration cycle is constructed by connecting the low temperature generator 4 to the low temperature heat exchanger 10 and the absorption liquid pipe line 19 between the high temperature heat exchanger 11 and concentrating pipe line 19 .

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。
20 is a hot water heat exchanger provided between the high temperature generator 1 and the refrigerant vapor pipe 12.

而して21は凝縮器5を中心として第1低温発生器4と
対設し且つ稀液の上流側に設けた低温熱源により加熱さ
れる第2低温発生器で、該発生器の底部は前記溶液管路
18により前記第1低温発生器4及び高温熱交換器11
を介して高温発生器1と夫々接続すると共に前記溶液管
路18には開閉弁22と溶液ポンプ23が設げられてい
る。
Reference numeral 21 denotes a second low-temperature generator that is heated by a low-temperature heat source that is disposed opposite to the first low-temperature generator 4 with the condenser 5 at its center and provided upstream of the diluted liquid. The first low temperature generator 4 and the high temperature heat exchanger 11 are connected by the solution line 18.
The solution pipe line 18 is connected to the high temperature generator 1 through the respective opening/closing valves 22 and a solution pump 23 .

そしてこの溶液管路18の上流側と低温熱交換器10は
開閉弁24を有した導管25により接続されている。
The upstream side of this solution pipe line 18 and the low temperature heat exchanger 10 are connected by a conduit 25 having an on-off valve 24.

次に動作について説明する。Next, the operation will be explained.

(イ)−型動用運転 この場合は、開閉弁22を閉、開閉弁24を開とし、溶
液ポンプ23は停止する。
(a)-Type dynamic operation In this case, the on-off valve 22 is closed, the on-off valve 24 is opened, and the solution pump 23 is stopped.

そして低温熱源により第2低温発生器21を加熱するこ
とにより、前記第2低温発生器21.凝縮器5、蒸発器
γ、吸収器9及び低温熱交換器10により吸収冷凍サイ
クルが構成され、冷水器8から冷房用冷水が供給される
Then, by heating the second low temperature generator 21 with the low temperature heat source, the second low temperature generator 21. The condenser 5, the evaporator γ, the absorber 9, and the low-temperature heat exchanger 10 constitute an absorption refrigeration cycle, and cold water for cooling is supplied from the water cooler 8.

(ロ)二重効用運転 この場合は開閉弁22は開、開閉弁24を閉とし、溶液
ポンプ23は運転する。
(b) Double effect operation In this case, the on-off valve 22 is open, the on-off valve 24 is closed, and the solution pump 23 is operated.

そして都市ガス或は灯油等の高温熱源の燃焼により高温
発生器1を加熱すると、吸収器9からの稀液は補液管路
11を通して第2低温発生器21へ至り更に溶液管路1
8を通して高温発生器1と第1低温発生器4とに分流し
、第1低温発生器4に流入した稀液は該発生器で再生さ
れた溶液となり、この再生溶液が、吸収液管路(図示せ
ず)を通して、高温発生器1から高温熱交換器11経由
で濃液管路19を通して流れる濃液と合流〔換言すれば
、高温発生器1に分流した稀液が該発生器で再生されて
濃液となり、この濃液と再び合流〕し、この合流した吸
収液が濃液管路19を通して低温熱交換器10経由で吸
収器9へ環流される結果、前述の二重効用吸収冷凍サイ
クルが構成されて、冷水器8から冷房用冷水が、また温
水熱交換器20から調温用温水が供給される。
When the high-temperature generator 1 is heated by combustion of a high-temperature heat source such as city gas or kerosene, the diluted liquid from the absorber 9 passes through the replacement fluid pipe 11 to the second low-temperature generator 21 and is further transferred to the solution pipe 1.
8 to the high temperature generator 1 and the first low temperature generator 4, and the dilute liquid flowing into the first low temperature generator 4 becomes a solution regenerated by the generator, and this regenerated solution is passed through the absorption liquid pipe ( (not shown), and joins the concentrated liquid flowing from the high-temperature generator 1 via the high-temperature heat exchanger 11 through the concentrated liquid line 19 (in other words, the diluted liquid diverted to the high-temperature generator 1 is regenerated in the generator). This combined absorption liquid is returned to the absorber 9 via the low-temperature heat exchanger 10 through the concentrated liquid pipe 19, resulting in the above-mentioned double-effect absorption refrigeration cycle. The water cooler 8 supplies cold water for cooling, and the hot water heat exchanger 20 supplies hot water for temperature control.

尚温水により暖房を行う場合は、冷媒蒸気管12溶液管
路18及び濃液管路19に夫々設けた開閉弁26,27
,28をいずれも閉じて、高温発生器1と温水熱交換器
20の間で冷媒を循環せしめる。
In addition, when performing heating with hot water, on-off valves 26 and 27 provided in the refrigerant vapor pipe 12, solution pipe line 18, and concentrated liquid pipe line 19, respectively.
, 28 are closed to circulate refrigerant between the high temperature generator 1 and the hot water heat exchanger 20.

本発明は上述の如く、高温発生器、該発生器からの冷媒
蒸気により加熱される第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配管接続し
て構成する二重効用吸収冷凍機において、前記第1低温
発生器に対する稀液の上流側に低温熱源により加熱され
る第2低温発生器を設け、該発生器の底部と前記第1低
温発生器及び高温熱交換器を介して高温発生器とを開閉
弁と溶液ポンプを有した管路で接続すると共に該管路と
前記低温熱交換器とを開閉弁を有した導管で接続し、該
導管の開閉弁と前記管路の開閉弁と溶液ポンプの作動に
より任意運転の選択を行うようにしたものであるから、
熱源に応じて1台の吸収冷凍機を一重効用又は二重効用
として運転が出来ると共にその切替も簡単となりエネル
ギーの有効利用と経済的な運転が可能となる。
As described above, the present invention connects a high temperature generator, a first low temperature generator heated by refrigerant vapor from the generator, a condenser, an evaporator, an absorber, a low temperature heat exchanger, and a high temperature heat exchanger through piping. In a dual-effect absorption refrigerator, a second low-temperature generator heated by a low-temperature heat source is provided upstream of the diluted liquid with respect to the first low-temperature generator, and the bottom of the generator and the first low-temperature generator and a high temperature generator via a high temperature heat exchanger, connected to the high temperature generator by a conduit having an on-off valve and a solution pump, and connecting the conduit to the low temperature heat exchanger by a conduit having an on-off valve, the conduit Since the operation is selected by the operation of the on-off valve of the pipe, the on-off valve of the pipeline, and the solution pump,
One absorption refrigerating machine can be operated as single effect or double effect depending on the heat source, and switching between them is also simple, making effective use of energy and economical operation possible.

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

図面は本発明による一重二重効用併用吸収冷凍機の構成
図である。 1・・・・・・高温発生器、4・・・・・・第1低温発
生器、10・・・・・・低温熱交換器、11・・・・・
・高温熱交換器、21・・・・・・第2低温発生器、2
2・・・・・・開閉弁、23・・・・・・溶液ポンプ、
18・・・・・・管路、24・・・・・・開閉弁、25
・・・・・・導管。
The drawing is a block diagram of a single and dual effect absorption refrigerator according to the present invention. 1... High temperature generator, 4... First low temperature generator, 10... Low temperature heat exchanger, 11...
・High temperature heat exchanger, 21...Second low temperature generator, 2
2...Opening/closing valve, 23...Solution pump,
18...Pipe line, 24...Opening/closing valve, 25
······conduit.

Claims (1)

【特許請求の範囲】[Claims] 1 高温発生器、該発生器からの冷媒蒸気により加熱さ
れる第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配管接続して構成する二重効
用吸収冷凍機において、前記第1低温発生器に対する稀
液の上流側に低温熱源により加熱される第2低温発生器
を設け、該発生器の底部と前記第1低温発生器及び高温
熱交換器を介して高温発生器とを開閉弁と溶液ポンプを
有した管路で接続すると共に該管路と前記低温熱交換器
とを開閉弁を有した導管で接続し、該導管の開閉弁と前
記管路の開閉弁と溶液ポンプの作動により任意運転の選
択を行なうことを特徴とする一重二重効用併用吸収冷凍
機。
1. Dual effect, consisting of a high temperature generator, a first low temperature generator heated by refrigerant vapor from the generator, a condenser, an evaporator, an absorber, a low temperature heat exchanger, and a high temperature heat exchanger connected by piping. In the absorption refrigerator, a second low temperature generator heated by a low temperature heat source is provided upstream of the diluted liquid with respect to the first low temperature generator, and a bottom of the generator, the first low temperature generator and the high temperature heat exchanger are connected to each other. A conduit having an on-off valve and a solution pump is connected to the high-temperature generator via the conduit, and the low-temperature heat exchanger is connected to the high-temperature generator through a conduit having an on-off valve, and the on-off valve of the conduit and the pipe A single/double effect absorption refrigerating machine, characterized in that an arbitrary operation can be selected by operating a channel opening/closing valve and a solution pump.
JP13638978A 1978-11-02 1978-11-02 Single and double effect absorption chiller Expired JPS5844183B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13638978A JPS5844183B2 (en) 1978-11-02 1978-11-02 Single and double effect absorption chiller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13638978A JPS5844183B2 (en) 1978-11-02 1978-11-02 Single and double effect absorption chiller

Publications (2)

Publication Number Publication Date
JPS5563361A JPS5563361A (en) 1980-05-13
JPS5844183B2 true JPS5844183B2 (en) 1983-10-01

Family

ID=15174006

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13638978A Expired JPS5844183B2 (en) 1978-11-02 1978-11-02 Single and double effect absorption chiller

Country Status (1)

Country Link
JP (1) JPS5844183B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57155068A (en) * 1981-03-20 1982-09-25 Sanyo Electric Co Absorption water cooler/heater
JPS57182061A (en) * 1981-04-30 1982-11-09 Sanyo Electric Co Absorbing cold and hot water device

Also Published As

Publication number Publication date
JPS5563361A (en) 1980-05-13

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