JPS58195762A - Absorption heat pump - Google Patents

Absorption heat pump

Info

Publication number
JPS58195762A
JPS58195762A JP7716782A JP7716782A JPS58195762A JP S58195762 A JPS58195762 A JP S58195762A JP 7716782 A JP7716782 A JP 7716782A JP 7716782 A JP7716782 A JP 7716782A JP S58195762 A JPS58195762 A JP S58195762A
Authority
JP
Japan
Prior art keywords
temperature
fluid
liquid
heat source
absorption
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.)
Granted
Application number
JP7716782A
Other languages
Japanese (ja)
Other versions
JPH0321826B2 (en
Inventor
宮城 龍雄
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 Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
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 Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP7716782A priority Critical patent/JPS58195762A/en
Publication of JPS58195762A publication Critical patent/JPS58195762A/en
Publication of JPH0321826B2 publication Critical patent/JPH0321826B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は吸収冷凍サイクルの放熱側即ち吸収器及び凝縮
器での放熱を利用して温水等被加熱流体を昇温する吸収
ヒートポンプの改良に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in an absorption heat pump that raises the temperature of a fluid to be heated, such as hot water, by utilizing heat radiation on the heat radiation side of an absorption refrigeration cycle, that is, in an absorber and a condenser.

此種吸収ヒートポンプは被加熱流体を効率良(昇温する
利点を有するものであるが、蒸発器に流通させる熱源流
体の温度条件によって、取り出される被加熱流体の温度
に制限を受け、熱源流体温度が定格値より低下すると被
加熱流体が所定温度に達しないことはもとより、逆に吸
収器側から蒸発器側へ放熱されて正常な運転が行なわれ
ない等の問題点があり、また、熱源流体に例えば河川水
を利用する場合等には熱源流体の凍結を生じて運転を休
止せざるを得ない問題点もある。
This type of absorption heat pump has the advantage of efficiently raising the temperature of the heated fluid, but is limited by the temperature of the heated fluid that is taken out depending on the temperature conditions of the heat source fluid flowing to the evaporator. If the temperature drops below the rated value, not only will the heated fluid not reach the specified temperature, but conversely, heat will be radiated from the absorber side to the evaporator side, preventing normal operation. For example, when river water is used, there is a problem that the heat source fluid freezes and the operation has to be stopped.

本発明は、斯る点に鑑み、熱源流体の温度が定格値即ち
設定温度以下になった場合に濃縮吸収液(以下、濃液と
略称する)が吸収器内に収納した流体取り出し管を側路
するようにして吸収液を循環せしめ、かつ被神熱流体の
取り出し温度を検出し【発生器への加熱量を調節する構
成を採ることにより、熱源流体の温度条件の如何に拘わ
らず、所定温度の被加熱流体を安定的に取り出すことを
目的としたものである。
In view of the above, the present invention provides a system in which when the temperature of the heat source fluid becomes lower than the rated value, that is, the set temperature, the concentrated absorption liquid (hereinafter referred to as concentrated liquid) is removed from the fluid extraction pipe housed in the absorber. By circulating the absorption liquid in a manner similar to that of the heat source fluid, and by detecting the temperature at which the heated thermal fluid is taken out and adjusting the amount of heating to the generator, the temperature of the heat source fluid can be adjusted to a specified level regardless of the temperature conditions of the heat source fluid. The purpose is to stably extract heated fluid at a certain temperature.

以下、本発明の実施例を図面に基き説明する。Embodiments of the present invention will be described below with reference to the drawings.

(1)は燃焼バーナー(2)を備え、稀釈吸収液(以下
、槽液と略称する)から冷媒を加熱分離して濃液に再生
する発生器、(3)は発生器(1)からの濃液と冷媒蒸
気とを分ける分離器、(4)は分離器(3)からの冷媒
蒸気を器内に収納した流体取り出し管(5)内の被加熱
流体で冷却して凝縮させる凝縮器、(6)は凝縮器(4
)から流下する凝縮冷媒液を器内に収納した熱源管(7
)に散布して気化させる蒸発器、(8)は分離器(3)
からの濃液を器内に収納した流体取り出し管(5)に散
布して咳管内の被加熱流体で冷却1つつ、濃液に気化冷
媒を吸収させる吸収器及び(9)は溶液熱交換器で、こ
れらは揚液管間、濃液管(ロ)、溶液ポンプ(2)を有
する補液管(2)、冷媒蒸気管(ロ)及び冷媒液流下管
(ト)で接続されて冷媒と吸収液との循環径路を形成し
ている。
(1) is a generator that is equipped with a combustion burner (2) and heats and separates the refrigerant from the diluted absorption liquid (hereinafter referred to as tank liquid) and regenerates it into a concentrated liquid; (3) is a generator that a separator that separates concentrated liquid and refrigerant vapor; (4) a condenser that cools and condenses the refrigerant vapor from the separator (3) with the heated fluid in the fluid extraction pipe (5) stored in the container; (6) is the condenser (4
) The heat source tube (7) houses the condensed refrigerant liquid flowing down from the
), the evaporator (8) is the separator (3).
The absorber (9) is a solution heat exchanger and the concentrated liquid is sprayed onto a fluid take-out pipe (5) housed in the vessel and cooled by the heated fluid in the cough pipe, while the concentrated liquid absorbs the vaporized refrigerant. These are connected by the liquid pumping pipes, the concentrated liquid pipe (b), the replenishing liquid pipe (2) with the solution pump (2), the refrigerant vapor pipe (b), and the refrigerant liquid down pipe (g) to absorb the refrigerant. It forms a circulation path with the liquid.

(ト)は、吸収器(8)内に収納した流体取り出し管(
5)を側路するように、濃液”Q)@液熱交換器(9)
出口側の濃液管(ロ)と吸収器(8)内め吸収液溜め(
ロ)上方の器壁とを接続したバイパス管で、該バイパス
管には開閉弁(至)が備えである。また濃液管(ロ)に
も開閉弁(6)が備えである。尚、これら開閉弁(至)
(1’Jに代えて濃液管(ロ)とバイパス管(転)との
接続部に三方弁(図示せず)を備えるようにしても良い
(G) is the fluid extraction tube (
5), concentrate liquid “Q) @ liquid heat exchanger (9)
The concentrated liquid pipe (b) on the outlet side and the absorption liquid reservoir inside the absorber (8)
b) A bypass pipe connected to the upper vessel wall, and the bypass pipe is equipped with an on-off valve. The concentrated liquid pipe (b) is also equipped with an on-off valve (6). In addition, these on-off valves (to)
(Instead of 1'J, a three-way valve (not shown) may be provided at the connection between the concentrated liquid pipe (b) and the bypass pipe (vertical).

■は蒸発器(6)入口側若しくは出口側の熱源管(7)
に備えた温度検出器で、該検出器の信号により開閉弁o
8(6)の開閉を切替える。またQυは被加熱流体の凝
縮器(4)出口側の流体取り出し管(5)に備えた温度
検出器で、該検出器の信号により前記バーナー(2)の
燃焼量を制御する。
■ is the heat source tube (7) on the inlet side or outlet side of the evaporator (6)
A temperature sensor is installed in the
Switch the opening/closing of 8(6). Further, Qυ is a temperature detector provided in the fluid take-out pipe (5) on the outlet side of the condenser (4) for the fluid to be heated, and the combustion amount of the burner (2) is controlled by the signal from this detector.

而して、前記温度検出器(ホ)で検知される熱源流体温
度が設定温度よりも高(・ときには、前記開閉弁(至)
を閉とし、開閉弁(6)を開として運転し、冷媒と吸収
液の循環径路を形成して吸収器(8)及び凝縮器(4)
での放熱作用により被加熱流体を昇温させ、かつ温度検
出器禦で検知される被加熱流体温度が定格値以下にな禾
と前記バーナー(2)の燃焼量を増して発生器(1)ヘ
ム加熱量を増大させ、凝縮器(4)へ1:・1゜ 流入する冷媒蒸気の温度及び流入量を高めることにより
被加熱流体温度が定格値に達するように調整する。
Therefore, the temperature of the heat source fluid detected by the temperature detector (E) is higher than the set temperature (in some cases, the temperature of the heat source fluid detected by the temperature detector (E) is higher than the set temperature).
is closed, and the on-off valve (6) is opened to form a circulation path for the refrigerant and absorption liquid, and the absorber (8) and condenser (4) are operated.
The temperature of the fluid to be heated is increased by the heat dissipation action of the burner (2), and when the temperature of the fluid to be heated as detected by the temperature sensor becomes lower than the rated value, the combustion amount of the burner (2) is increased and the generator (1) is heated. The temperature of the heated fluid is adjusted to reach the rated value by increasing the heme heating amount and increasing the temperature and flow rate of the refrigerant vapor flowing into the condenser (4) by 1:.1°.

次に、前記温度検出器(ホ)で検知さfLる熱源流体温
度が設定温度以下となった場合には、前記開閉弁(財)
を開、開閉弁(6)を閉に切替えて濃液を前記バイパス
管(ト)に通し、吸収液の循環を切替えて運転し、凝縮
器(4)での放熱作用により被加熱流体を昇温する。且
つ温度検出器@l)で検知される被加熱流体温度が、定
格値以下になると前記バーナー(2)の燃焼量を増して
、定格値に達するように調整する。
Next, when the temperature of the heat source fluid detected by the temperature detector (e) becomes lower than the set temperature, the on-off valve
The on-off valve (6) is opened, the on-off valve (6) is closed, the concentrated liquid is passed through the bypass pipe (G), the circulation of the absorption liquid is switched, and the heated fluid is raised by the heat dissipation action of the condenser (4). Warm up. In addition, when the temperature of the heated fluid detected by the temperature detector @l) becomes below the rated value, the combustion amount of the burner (2) is increased and adjusted so as to reach the rated value.

このようにして、熱源流体の温度条件の如何に拘わらず
、所定温度の被加熱流体を安定的に取り出すことができ
る。
In this way, the fluid to be heated at a predetermined temperature can be stably taken out regardless of the temperature conditions of the heat source fluid.

尚、熱源流体の設定温度は吸収ヒートポンプの容量等の
設計仕様値に基いて適宜選定される。前記温度検出器(
1)を蒸発器(6)入口側に備えた場合は、しl 温度検出器(ホ)を蒸発器(6)出口側に備えた場合よ
りもその設定温度を高く選定している。前者の場合は供
給される熱源流体温度を直接検知できるメリットがあり
、また後者の場合はヒートポンプ運転中の熱源流体の凍
結の危険性を未然に検知できるメリットがある。
Note that the set temperature of the heat source fluid is appropriately selected based on design specification values such as the capacity of the absorption heat pump. The temperature sensor (
When 1) is provided on the inlet side of the evaporator (6), the set temperature is selected higher than when the temperature detector (e) is provided on the outlet side of the evaporator (6). The former case has the advantage of being able to directly detect the temperature of the supplied heat source fluid, and the latter case has the advantage of being able to detect the risk of freezing of the heat source fluid during operation of the heat pump.

以上のように、本発明は、濃液が吸収器に収納した流体
取り出し管を側路するバイパス径路を形成し、蒸発器に
収納した熱源管を流通する熱源流体が設定温度以下とな
った場合に濃液なバイパス径路に通して吸収液の循環を
切替える機構を備え、かつ被加熱流体の凝縮器出口側温
度を検出して発生器への加熱量を調節する機構を備えた
吸収ヒートポンプであるから、論わば、従来の吸収ヒー
トポンプに吸収液循環の簡便な切替機構を付設した丈の
簡単なもので、熱源流体の温度条件の如何に拘わらず、
所定温度の被加熱流体を安定的に取り出゛;シ得、実用
上有益である。
As described above, the present invention forms a bypass path in which the concentrated liquid bypasses the fluid extraction pipe stored in the absorber, and when the heat source fluid flowing through the heat source pipe stored in the evaporator becomes lower than the set temperature. This is an absorption heat pump that is equipped with a mechanism that switches the circulation of the absorption liquid by passing it through a concentrated liquid bypass path, and a mechanism that detects the temperature of the heated fluid at the condenser outlet side and adjusts the amount of heating to the generator. In other words, it is a simple version of a conventional absorption heat pump with a simple switching mechanism for absorption liquid circulation, regardless of the temperature conditions of the heat source fluid.
It is possible to stably take out the fluid to be heated at a predetermined temperature; this is useful in practice.

引回である。It's a turnaround.

(1)・・・・・・発生器、(2)・・・・・・バーナ
ー、(4)・・・・・・凝縮器、(5)・・・・・・流
体取り出し管、(6)・・・・・・蒸発器、(7)・・
・・・・熱源管、(8)・・・・・・吸収器、(9)・
・・・・・溶液熱交換器、0υ・・・・・濃液管、(ト
)・・・・・・バイパス管、(ト)(1’J・・・・・
・、開閉弁、停し・・・・・温度検出器 出願人 三洋電機株式会社 外1名
(1)... Generator, (2)... Burner, (4)... Condenser, (5)... Fluid extraction pipe, (6 )...Evaporator, (7)...
... Heat source tube, (8) ... Absorber, (9)
...Solution heat exchanger, 0υ...Concentrated liquid pipe, (G)...Bypass pipe, (G) (1'J...
・, open/close valve, stop...Temperature detector Applicant: Sanyo Electric Co., Ltd. and 1 other person

Claims (1)

【特許請求の範囲】[Claims] (1)発生器、凝縮器、蒸発器、吸収器及び醪液熱交換
器を配管接続して冷媒と吸収液の循環経路を形成し、吸
収器及び凝縮器に収納した液体取り出し管内の被加熱流
体を昇温する吸収ヒートポンプにおいて、発生器よりの
濃縮吸収液が吸収器に収納した流体取り出し管を側路す
るバイパス径路を形成し、蒸発器に収納した熱源管を流
通する熱源流体が設定温度以下となった場合に濃縮吸収
液をバイパス径路に通して吸収液の循環を切替える機構
を備え、かつ被加熱流体の凝縮器出口側温度を検出して
発生器への加熱量を調節する機構を備えたことを特徴と
する吸収ヒートポンプ。
(1) Connect the generator, condenser, evaporator, absorber, and liqueur heat exchanger with piping to form a circulation path for the refrigerant and absorption liquid, and use the heated liquid in the liquid extraction pipe housed in the absorber and condenser. In an absorption heat pump that raises the temperature of a fluid, the concentrated absorption liquid from the generator forms a bypass path that bypasses the fluid extraction pipe stored in the absorber, and the heat source fluid flowing through the heat source pipe stored in the evaporator reaches the set temperature. Equipped with a mechanism that switches the circulation of the absorbed liquid by passing the concentrated absorption liquid through a bypass path when the following occurs, and a mechanism that detects the temperature of the heated fluid at the condenser outlet side and adjusts the amount of heating to the generator. An absorption heat pump characterized by:
JP7716782A 1982-05-08 1982-05-08 Absorption heat pump Granted JPS58195762A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7716782A JPS58195762A (en) 1982-05-08 1982-05-08 Absorption heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7716782A JPS58195762A (en) 1982-05-08 1982-05-08 Absorption heat pump

Publications (2)

Publication Number Publication Date
JPS58195762A true JPS58195762A (en) 1983-11-15
JPH0321826B2 JPH0321826B2 (en) 1991-03-25

Family

ID=13626225

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7716782A Granted JPS58195762A (en) 1982-05-08 1982-05-08 Absorption heat pump

Country Status (1)

Country Link
JP (1) JPS58195762A (en)

Also Published As

Publication number Publication date
JPH0321826B2 (en) 1991-03-25

Similar Documents

Publication Publication Date Title
JPH0886530A (en) Absorption type water cooling and heating machine
JPS58195762A (en) Absorption heat pump
JPH0522828B2 (en)
JPS59229139A (en) Solar heat-utilizing hot-water supply device
JP3381094B2 (en) Absorption type heating and cooling water heater
JPS58195760A (en) Absorption heat pump
JPS6135900Y2 (en)
JP3133154B2 (en) Hot water multi-circuit extraction absorption chiller / heater and hot water extraction automatic switching method
JPH0355741B2 (en)
JPS6018763Y2 (en) Double effect water - lithium salt absorption air conditioner
JPS59115951A (en) Absorption heat pump
KR100364773B1 (en) puvging device in ammonia absorption heat pump
JP3244774B2 (en) Automatic cooling / heating switching method and apparatus in absorption chiller / heater
JP3663008B2 (en) Absorption chiller / heater
JPH0230691Y2 (en)
JP3663006B2 (en) Absorption chiller / heater
JPH0643654Y2 (en) Absorption type water heater
JPH0575942B2 (en)
JPS58195761A (en) Absorption heat pump
JPS54131160A (en) Controller for absorption machines
JPS60114697A (en) Heat transfer device
JPH0510598B2 (en)
JPH06137706A (en) Control method for absorption type cooling and hot water equipment
JPH0638009B2 (en) Air-cooled absorption cold / hot water unit
JPH0357391B2 (en)