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JPH06100400B2 - Absorption heat pump device - Google Patents
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JPH06100400B2 - Absorption heat pump device - Google Patents

Absorption heat pump device

Info

Publication number
JPH06100400B2
JPH06100400B2 JP59262396A JP26239684A JPH06100400B2 JP H06100400 B2 JPH06100400 B2 JP H06100400B2 JP 59262396 A JP59262396 A JP 59262396A JP 26239684 A JP26239684 A JP 26239684A JP H06100400 B2 JPH06100400 B2 JP H06100400B2
Authority
JP
Japan
Prior art keywords
pump
liquid
evaporator
refrigerant
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 - Lifetime
Application number
JP59262396A
Other languages
Japanese (ja)
Other versions
JPS61140757A (en
Inventor
雅裕 古川
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 JP59262396A priority Critical patent/JPH06100400B2/en
Publication of JPS61140757A publication Critical patent/JPS61140757A/en
Publication of JPH06100400B2 publication Critical patent/JPH06100400B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は装置に供給する熱源流体よりも高温の被加熱流
体を取出すことのできる吸収ヒートポンプ装置(以下、
この種の装置という)の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to an absorption heat pump device (hereinafter, referred to as a heat pump device) capable of extracting a fluid to be heated whose temperature is higher than that of a heat source fluid supplied to the device.
This type of device)) improvement.

(ロ)従来の技術 この種の装置の従来の技術として、例えば特開昭58-693
72号公報にみられるもの(以下、第1従来装置という)
や特開昭58-136956号公報にみられるもの(以下、第2
従来装置という)など、発生器および蒸発器に廃蒸気や
排温水などの低温の熱源流体を供給して、吸収器から高
温水を取出すように構成したものが知られている。そし
て、第1従来装置においては、凝縮器内の冷媒液量が過
度に減少するのを防ぐために、凝縮器から蒸発器の冷媒
液溜めへ冷媒液を送るポンプが発停制御されるようにな
っている。また、第2従来装置においては、発生器およ
び蒸発器に供給される熱エネルギー量(以下、熱入力と
いう)の変化に伴なって凝縮器内の冷媒液量が変化した
場合、凝縮器から蒸発器の冷媒液溜へ送る冷媒液の流量
を制御するようになっている。
(B) Conventional technology As a conventional technology of this type of apparatus, for example, Japanese Patent Laid-Open No. 58-693
What is found in Japanese Patent Publication No. 72 (hereinafter referred to as "first conventional device")
And those found in JP-A-58-136956 (hereinafter, referred to
Known as a conventional device), a low temperature heat source fluid such as waste steam or waste hot water is supplied to a generator and an evaporator to take out high temperature water from an absorber. Then, in the first conventional device, in order to prevent the refrigerant liquid amount in the condenser from excessively decreasing, the pump for sending the refrigerant liquid from the condenser to the refrigerant liquid reservoir of the evaporator is controlled to be started and stopped. ing. Further, in the second conventional device, when the amount of the refrigerant liquid in the condenser changes due to the change in the amount of heat energy supplied to the generator and the evaporator (hereinafter referred to as heat input), the evaporation from the condenser The flow rate of the refrigerant liquid sent to the refrigerant liquid reservoir of the container is controlled.

(ハ)発明が解決しようとする問題点 この種の装置は、凝縮器および発生器を蒸発器および吸
収器よりも低温低圧で動作させるので、ポンプ発停条制
御により凝縮器からの低温の冷媒液を蒸発器の冷媒液溜
め内の高温の冷媒液中に間けつ的に送るとその冷媒液溜
め内の冷媒液の温度にハンチングを生じる。
(C) Problems to be Solved by the Invention In this type of device, the condenser and the generator are operated at a lower temperature and pressure than the evaporator and the absorber. Therefore, the low temperature refrigerant from the condenser is controlled by the pump start / stop control. When the liquid is intermittently sent into the high temperature refrigerant liquid in the refrigerant liquid reservoir of the evaporator, hunting occurs in the temperature of the refrigerant liquid in the refrigerant liquid reservoir.

このため、第1従来装置においては、蒸発器および吸収
器の動作温度がポンプの発停毎に変動し、吸収器から取
出される温水の温度や熱量(以下、熱出力という)が不
安定となる問題点を有している。
Therefore, in the first conventional device, the operating temperatures of the evaporator and the absorber fluctuate every time the pump starts and stops, and the temperature and heat quantity (hereinafter referred to as heat output) of the hot water taken out from the absorber are unstable. There is a problem that becomes.

一方、第2従来装置においては、熱出力を安定化させる
ことができるものの、高価な流量制御弁もしくは吐出量
可変ポンプを用いる必要がある上に高精度の制御を要す
るため、制御機構が高価で複雑となる問題点を有してい
る。また、例えば特開昭58-69372号公報には凝縮器から
蒸発器へ冷媒を送るポンプの運転を凝縮器に設けられた
液面制御器によって制御する吸収ヒートポンプが開示さ
れている。吸収ヒートポンプにおいては液面検出器の接
続部などから機器内に外気が侵入すると運転効率が低下
するため、流路の機密性が需要な課題になり、上記吸収
ヒートポンプのように英面制御器を冷媒の流路である凝
縮器に設けた場合には、接続部から外気が侵入する虞が
ある。
On the other hand, in the second conventional device, although the heat output can be stabilized, it is necessary to use an expensive flow rate control valve or a variable discharge amount pump and highly accurate control is required, so that the control mechanism is expensive. It has a complicated problem. Further, for example, Japanese Patent Laid-Open No. 58-69372 discloses an absorption heat pump in which the operation of a pump for sending a refrigerant from a condenser to an evaporator is controlled by a liquid level controller provided in the condenser. In the absorption heat pump, operating efficiency decreases when outside air enters the equipment from the connection part of the liquid level detector, so the confidentiality of the flow path becomes a demanding issue. When it is provided in the condenser which is the flow path of the refrigerant, there is a possibility that outside air may enter from the connecting portion.

本発明は、これら問題点に鑑み、冷媒および吸収液の流
路への外気の侵入を抑え、運転効率を安定させると共
に、安価で簡便な制御機構を用いて熱入力の変動に伴な
う蒸発器および吸収器の動作温度のハンチングを軽減
し、熱出力を安定化し得るこの種の装置の提供を目的と
したものである。
In view of these problems, the present invention suppresses the invasion of the outside air into the flow paths of the refrigerant and the absorbing liquid, stabilizes the operation efficiency, and uses an inexpensive and simple control mechanism to evaporate with the fluctuation of the heat input. It is an object of the present invention to provide a device of this type capable of stabilizing the heat output by reducing the hunting of the operating temperature of the absorber and the absorber.

(ニ)問題点を解決するための手段 本発明は、この種の装置において、吸収液を発生器から
吸収器へ送るポンプおよび冷媒液を凝縮器から蒸発器へ
送るポンプとして用いられて逆通電時には正常通電時よ
りも吐出液量の少ない可逆転ポンプと、発生器および蒸
発器から流出した廃蒸気及びドレンの流路の途中に設け
られドレンが溜まるドレンタンクと、このドレンタンク
に設けられた液面検出器と、この液面検出器から信号を
入力して検出値が設定値を超えたときには各可逆転ポン
プに正常通電し、設定値以下となったときには各可逆転
ポンプに逆通電する制御機構とを備えたものである。
(D) Means for Solving the Problems In the device of this type, the present invention is used as a pump for sending the absorbing liquid from the generator to the absorber and as a pump for sending the refrigerant liquid from the condenser to the evaporator, and reverse energization. A reversible pump that sometimes discharges less liquid than when normally energized, a drain tank that is installed in the middle of the flow path of waste vapor and drain that flows out of the generator and evaporator, and a drain tank, and this drain tank When the liquid level detector and a signal from this liquid level detector are input and the detected value exceeds the set value, each reversible pump is energized normally, and when the detected value is below the set value, each reversible pump is energized reversely. And a control mechanism.

(ホ)作用 本発明によるこの種の装置においては、その作用とし
て、蒸発器の冷媒液溜めへ送る凝縮冷媒の量の変動幅を
第1従来装置よりも小さくでき、かつ、熱入力の増減変
動に対して吸収液および冷媒液の循環を継続させつつ循
環量を増減制御することができるので、第1、第2従来
装置にくらべて冷媒の発生量の変動も少なくなり、装置
の動作圧力・温度のハンチングが小さくなる。また、可
逆転ポンプの運転制御用の液面検出器は冷媒および吸収
液の循環路と異なるドレンタンクに設けられており、液
面検出器の接続部に漏れが発生した場合にも吸収ヒート
ポンプ装置内への外気の侵入を回避でき、運転効率を安
定する。また、検出値の設定値を基準にポンプの通電を
切換える制御であるので、オン・オフ制御に類似した制
御であり、簡便で安価な制御機構を用い得る。
(E) Action In this type of device according to the present invention, as its action, the fluctuation range of the amount of condensed refrigerant sent to the refrigerant sump of the evaporator can be made smaller than that of the first conventional device, and the fluctuation of the heat input is increased or decreased. On the other hand, since the circulation amount can be controlled to increase or decrease while continuing the circulation of the absorbing liquid and the refrigerant liquid, the fluctuation of the amount of refrigerant generated is smaller than that of the first and second conventional devices, and the operating pressure of the device Reduced temperature hunting. In addition, the liquid level detector for operation control of the reversible pump is installed in the drain tank different from the circulation path of the refrigerant and the absorbing liquid, and even if a leak occurs at the connection part of the liquid level detector, the absorption heat pump device Ingress of outside air can be avoided and operation efficiency is stabilized. Further, since the control is to switch the energization of the pump based on the set value of the detected value, the control is similar to the on / off control, and a simple and inexpensive control mechanism can be used.

このように、本発明によるこの種の装置は、熱入力の変
動に伴なう蒸発器および吸収器の動作温度のハンチング
を簡便で安価な制御機構によって軽減でき、かつ、機器
内への外気の侵入を回避して従来の装置にくらべ、熱出
力を安定化させ得る装置として実用的価値の高いもので
ある。
As described above, the device of this type according to the present invention can reduce hunting of the operating temperature of the evaporator and the absorber due to the fluctuation of the heat input by a simple and inexpensive control mechanism, and can prevent external air from entering the device. This device has a high practical value as a device that can avoid the intrusion and stabilize the heat output as compared with the conventional device.

(ヘ)実施例 第1図は本発明によるこの種の装置の一実施例を示した
概略構成説明図である。第1図において、(1)、
(2)、(3)、(4)および(5)はそれぞれ発生
器、凝縮器、蒸発器、吸収器および溶液熱交換器であ
り、(6)、(7)および(8)はそれぞれ凝縮冷媒
用、冷媒液循環用および吸収液用のポンプである。そし
て、これら機器は凝縮冷媒の送られる管(9)、(1
0)、冷媒液の還流する管(11)、(12)、吸収液の送
られる管(13)、(14)、(15)、吸収液の流れる管
(16)、(17)により接続されて従来のこの種の装置と
同様の冷媒〔水〕および吸収液〔臭化リチウム水溶液〕
の循環路を構成している。なお、(18)は溶液熱交換器
(5)に内蔵した伝熱コイルである。
(F) Embodiment FIG. 1 is a schematic structural explanatory view showing an embodiment of an apparatus of this kind according to the present invention. In FIG. 1, (1),
(2), (3), (4) and (5) are a generator, a condenser, an evaporator, an absorber and a solution heat exchanger, respectively, and (6), (7) and (8) are condensed respectively. Pumps for refrigerant, refrigerant liquid circulation, and absorption liquid. Then, these devices are equipped with pipes (9), (1
0), refrigerant liquid recirculation pipes (11), (12), absorption liquid sending pipes (13), (14), (15), absorption liquid flowing pipes (16), (17) Refrigerant [water] and absorption liquid [lithium bromide aqueous solution] similar to conventional devices of this type
It constitutes the circulation circuit of. In addition, (18) is a heat transfer coil built in the solution heat exchanger (5).

(19)、(20)、(21)および(22)はそれぞれ発生器
(1)、凝縮器(2)、蒸発器(3)および吸収器
(4)に内蔵した加熱器、冷却器、給熱器および被加熱
器であり、(23)、(24)、(25)および(26)はそれ
ぞれ発生器(1)、凝縮器(2)、蒸発器(3)および
吸収器(4)の液溜めである。また、(27)、(28)は
吸収液の散布器であり、(29)は冷媒液の散布器であ
る。
(19), (20), (21) and (22) are a heater, a cooler, and a supply unit built in the generator (1), the condenser (2), the evaporator (3) and the absorber (4), respectively. And (23), (24), (25) and (26) of the generator (1), condenser (2), evaporator (3) and absorber (4), respectively. It is a liquid reservoir. Further, (27) and (28) are sprayers for absorbing liquid, and (29) is a sprayer for refrigerant liquid.

(30)、(31)、(32)、(33)、(34)は加熱器(1
9)と給熱器(21)とに並列に接続した廃蒸気や排温水
などの低温の熱源流体の流れる管、(35)、(36)は冷
却器(20)と接続した冷却水や冷却用空気などの冷却流
体の流れる管、(37)、(38)は被加熱器(22)と接続
した温水や温風などの被加熱流体の流れる管である。
(30), (31), (32), (33), (34) are heaters (1
9) and a heat supply device (21) connected in parallel to a pipe through which a low temperature heat source fluid such as waste steam or waste hot water flows, and (35) and (36) are cooling water and cooling connected to a cooler (20). Pipes (37) and (38) through which a cooling fluid such as working air flows are pipes through which a heated fluid such as hot water or hot air that is connected to the heated device (22) flows.

このように構成された装置(以下、本装置という)にお
いては、従来のこの種の装置と同様に、冷媒と吸収液の
循環による吸収ヒートポンプサイクルが形成され、発生
器(1)および凝縮器(2)が蒸発器(3)および吸収
器(4)よりも低温低圧で動作し、吸収器(4)の被加
熱器(22)に散布された吸収液が蒸発器(3)からの冷
媒蒸気を吸収する際に発生する熱で蒸発器(3)に供給
された熱源流体よりも高温の被加熱流体が被加熱器(2
2)から得られるのである。
In the device configured as described above (hereinafter referred to as the present device), an absorption heat pump cycle is formed by circulation of the refrigerant and the absorbing liquid, as in the conventional device of this type, and the generator (1) and the condenser ( 2) operates at a lower temperature and pressure than the evaporator (3) and the absorber (4), and the absorption liquid sprinkled on the heated device (22) of the absorber (4) is the refrigerant vapor from the evaporator (3). The fluid to be heated having a temperature higher than that of the heat source fluid supplied to the evaporator (3) by the heat generated when absorbing the
It is obtained from 2).

図の2点鎖線で示した(39)は熱源流体に廃蒸気を用い
た場合のドレンタンクであり、加熱器19及び吸熱器21か
ら流出した廃蒸気およびドレンは矢印にて示したように
ドレンタンク(39)に流入する。また、ドレンタンク
(39)には廃蒸気の排出管(40)、弁(V)付きのドレ
ン排出管(41)および液面検出器(LS1)が設けられて
いる。ここで、熱源流体の廃蒸気を用いた場合、この廃
蒸気の本装置での凝縮量すなわちドレンタンク(39)に
おける液位の増減変動が本装置の熱入力の増減変動を示
すことになる。
(39) indicated by the chain double-dashed line in the figure is a drain tank when waste steam is used as the heat source fluid, and the waste steam and drain flowing out from the heater 19 and the heat absorber 21 are drained as indicated by the arrows. It flows into the tank (39). Further, the drain tank (39) is provided with a waste vapor discharge pipe (40), a drain discharge pipe (41) with a valve (V), and a liquid level detector (LS1). Here, when the waste steam of the heat source fluid is used, the amount of condensation of this waste steam in this device, that is, the increase / decrease change in the liquid level in the drain tank (39) indicates the increase / decrease change in the heat input of this device.

(C)は液面検出器(LS1)の信号を受けてその検出器
と基準となる設定値とを比較してポンプ(6)およびポ
ンプ(8)への通電の正逆切換えを行なう制御器であ
る。そして、(6)およびポンプ(8)には逆通電時に
正常通電時よりも吐出液量の減少する可逆転ポンプが用
いられている。第2図はこのような可逆転ポンプの性能
曲線の一例を示したもので、正常通電時の正転で100%
の液吐出量に対して逆通電時の逆転では60〜40%の液吐
出量となっている。
(C) is a controller that receives a signal from the liquid level detector (LS1), compares the detector with a reference set value, and switches the energization to the pump (6) and the pump (8) between normal and reverse directions. Is. The (6) and the pump (8) are reversible pumps in which the amount of discharged liquid is smaller during reverse energization than during normal energization. Fig. 2 shows an example of the performance curve of such a reversible pump.
With respect to the liquid discharge amount of, the liquid discharge amount is 60 to 40% in the reverse rotation during reverse energization.

次に、第2図に示すような性能を有する可逆転ポンプを
用いた本装置の動作例を簡単に説明する。
Next, an operation example of this device using a reversible pump having the performance shown in FIG. 2 will be briefly described.

本装置の運転中に例えば熱入力が半分(50%)に減った
とき、加熱器(19)への吸収液の散布量に対して熱入力
が不足し、発生器(1)における冷媒蒸気の発生量が急
減する。それに伴なって凝縮器(2)での冷媒蒸気の凝
縮量も減る。また、ドレンタンク(39)に流入するドレ
ンの量が減少し、ドレン液位が設定値以下になる。そし
て、液面検出器(LS1)の信号により制御器(C)を介
してポンプ(6)、(8)の通電が正常通電から逆通電
へ切換えられ、これらポンプの液吐出量がほぼ半分に減
じられる。その結果、発生器(1)と吸収器(4)間で
の吸収液の循環量がおよそ半分に減り、半減した熱入力
に対して加熱器(19)への吸収液の散布量もほぼ半減す
るので、発生器(1)において冷媒蒸気が効率良く安定
的に発生する。また、液溜め(24)からの冷媒液の流出
量は、ほぼ半減し、かつ、発生器(1)から凝縮器
(2)へ流れつつ凝縮する冷媒の量とほぼ釣合うので、
液溜め(24)の液位は設定値近傍に保たれ、蒸発器
(3)には冷媒液が安定的に送られる。それ故、本装置
においては、発生器(1)、凝縮器(2)、蒸発器
(3)および吸収器(4)などの機器の動作温度・動作
圧力が半減した熱入力に見合う値に保たれ、安定した運
転が継続されるのである。そして、熱入力が100%に戻
った場合には、ポンプ(6)、(8)の通電が逆通電か
ら再び正常通電に戻されるのである。
For example, when the heat input is reduced to half (50%) during the operation of this device, the heat input becomes insufficient with respect to the amount of the absorbed liquid sprayed to the heater (19), and the refrigerant vapor in the generator (1) The amount of generation decreases sharply. Along with that, the amount of condensation of the refrigerant vapor in the condenser (2) also decreases. Further, the amount of drain flowing into the drain tank (39) is reduced, and the drain liquid level becomes equal to or lower than the set value. Then, the energization of the pumps (6) and (8) is switched from normal energization to reverse energization via the controller (C) by the signal of the liquid level detector (LS1), and the liquid discharge amount of these pumps is almost halved. Reduced. As a result, the circulation amount of the absorbing liquid between the generator (1) and the absorber (4) is reduced to about half, and the amount of the absorbing liquid sprayed to the heater (19) is almost halved with respect to the half heat input. Therefore, the refrigerant vapor is efficiently and stably generated in the generator (1). Further, the outflow amount of the refrigerant liquid from the liquid reservoir (24) is almost halved, and is almost balanced with the amount of the refrigerant condensed while flowing from the generator (1) to the condenser (2).
The liquid level of the liquid reservoir (24) is maintained near the set value, and the refrigerant liquid is stably sent to the evaporator (3). Therefore, in this device, the operating temperature and operating pressure of the devices such as the generator (1), the condenser (2), the evaporator (3), and the absorber (4) are maintained at a value commensurate with the heat input at half. Stable operation is continued. Then, when the heat input returns to 100%, the energization of the pumps (6) and (8) is returned from the reverse energization to the normal energization again.

このように、本装置においては、熱入力の増減変動すな
わち廃蒸気の量の変動をドレンタンク(39)内のドレン
量の増減変動で検知して、ポンプ(6)、(8)を制御
することにより、装置の動作温度・動作圧力のハンチン
グを軽減し、運転を安定化することができる。さらに、
第1図に示したように冷媒および吸収液の流路の途中に
液面検出器(LS1)、(LS2)、温度検出器(TS)および
圧力検出器(PS)を取り付けポンプ(6)、(8)を制
御するようにした場合には不凝縮ガスである外気が侵入
する可能性が高くなるが、本発明のようにドランタンク
(39)に液面検出器(LS1)を設けた場合には取付部か
ら吸収ヒートポンプ装置の冷媒流路および吸収液流路へ
の外気の侵入を回避することができ、この結果、運転効
率を高く維持することができる。
In this way, in this device, the fluctuations in the heat input, that is, the fluctuations in the amount of waste steam, are detected by the fluctuations in the drain amount in the drain tank (39), and the pumps (6) and (8) are controlled. As a result, hunting of the operating temperature and operating pressure of the device can be reduced and the operation can be stabilized. further,
As shown in FIG. 1, the liquid level detectors (LS1), (LS2), the temperature detector (TS) and the pressure detector (PS) are attached in the middle of the flow paths of the refrigerant and the absorbing liquid, and the pump (6), When (8) is controlled, there is a high possibility that outside air, which is a non-condensable gas, will enter, but when the liquid level detector (LS1) is provided in the drain tank (39) as in the present invention. In addition, it is possible to prevent outside air from entering the refrigerant flow path and the absorption liquid flow path of the absorption heat pump device from the mounting portion, and as a result, it is possible to maintain high operation efficiency.

(ト)発明の効果 本発明は、以上のように構成された吸収ヒートポンプ装
置であり、熱入力が減少して可逆転ポンプを逆通電した
おき吸収液および冷媒液の循環量を減少させることがで
きるので、熱入力の変動に対して吸収ヒートポンプ装置
の運転を安定化させることができ、この結果、従来の装
置に比べて装置の動作温度のハンチングを低減でき、熱
出力を安定することができるのはもちろん、熱入力すな
わち廃蒸気の増減に関連して変化する液面の検出器を冷
媒および吸収液の流路とは異なるドレンタンクに取り付
けたので、液面検出器の取付部から吸収ヒートポンプ装
置の冷媒流路および吸収液流路への外気の侵入を回避す
ることができ、この結果運転効率を高く維持することが
できる。また、凝縮冷媒用および吸収液用のポンプとし
て用いた可逆転ポンプの通電を切換える簡便な制御であ
るので、従来の装置にくらべ、制御機構も安価でかつ簡
単なもので済む。
(G) Effect of the Invention The present invention is an absorption heat pump device configured as described above, and it is possible to reduce the circulation amount of the absorbing liquid and the refrigerant liquid by reducing the heat input and reversely energizing the reversible pump. Therefore, the operation of the absorption heat pump device can be stabilized against the fluctuation of the heat input, and as a result, the hunting of the operating temperature of the device can be reduced as compared with the conventional device, and the heat output can be stabilized. Of course, since the detector for the liquid level that changes in relation to the increase or decrease of heat input, that is, the amount of waste steam, was installed in the drain tank different from the flow paths for the refrigerant and the absorbing liquid, The outside air can be prevented from entering the refrigerant channel and the absorbing fluid channel of the device, and as a result, the operating efficiency can be maintained high. In addition, the control mechanism is simple and easy to switch the energization of the reversible pump used as the pump for the condensed refrigerant and the pump for the absorbing liquid, so that the control mechanism is cheaper and simpler than the conventional device.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明によるこの種の装置の一実施例を示した
概略構成説明図、第2図は本発明による装置に用いた可
逆転ポンプの性能曲線の一例を示した線図である。 (1)……発生器、(2)……凝縮器、(3)……蒸発
器、(4)……吸収器、(5)……溶液熱交換器、
(6)、(7)、(8)……ポンプ、(19)……加熱
器、(20)……冷却器、(21)……給熱器、(22)……
被加熱器、(23)、(24)、(25)、(26)……液溜
め、(27)、(28)、(29)……散布器、(30)、(3
1)、(32)、(33)、(34)……管、(39)……ドレ
ンタンク、(C)……制御器、(LS1)、(LS2)、(LS3)……
液面検出器、(PS)……圧力検出器、(TS)……温度検
出器。
FIG. 1 is a schematic configuration explanatory view showing an embodiment of an apparatus of this type according to the present invention, and FIG. 2 is a diagram showing an example of a performance curve of a reversible pump used in the apparatus according to the present invention. (1) ... Generator, (2) ... Condenser, (3) ... Evaporator, (4) ... Absorber, (5) ... Solution heat exchanger,
(6), (7), (8) ... Pump, (19) ... Heater, (20) ... Cooler, (21) ... Heater, (22) ...
Heated device, (23), (24), (25), (26) ... Liquid reservoir, (27), (28), (29) ... Sprayer, (30), (3
1), (32), (33), (34) …… pipe, (39) …… drain tank, (C) …… controller, (LS 1 ), (LS 2 ), (LS 3 ) ……
Liquid level detector, (PS) ... pressure detector, (TS) ... temperature detector.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】凝縮器に冷却流体を流通させ、発生器およ
び蒸発器に廃蒸気を供給して吸収器から廃蒸気の温度レ
ベル以上の被加熱流体を取出すように発生器、凝縮器、
蒸発器および吸収器を配管構成した装置において、吸収
液を発生器から吸収器へ送るポンプおよび冷媒液を凝縮
器から蒸発器へ送るポンプとして用いられて逆通電時に
は正常通電時よりも吐出液量の少ない可逆転ポンプと、
発生器および蒸発器から流出した廃蒸気及びドレンの流
路の途中に設けられドレンが溜まるドレンタンクと、こ
のドレンタンクに設けられた液面検出器と、この液面検
出器から信号を入力して検出値が設定値を超えたときに
は各可逆転ポンプに正常通電し、設定値以下となったと
きには可逆転ポンプに逆通電する制御機構とを備えたこ
とを特徴とした吸収ヒートポンプ装置。
1. A generator, a condenser, so as to circulate a cooling fluid through a condenser, supply waste steam to a generator and an evaporator, and take out a heated fluid above a temperature level of waste steam from an absorber.
In a device with an evaporator and an absorber piped, it is used as a pump that sends absorption liquid from the generator to the absorber and as a pump that sends refrigerant liquid from the condenser to the evaporator. Reversible pump with few
A drain tank is provided in the middle of the flow path of waste vapor and drain that flows out from the generator and evaporator, and a drain level sensor is installed in this drain tank, and a signal is input from this level sensor. The absorption heat pump device is provided with a control mechanism for normally energizing each reversible pump when the detected value exceeds a set value and reversely energizing the reversible pump when the detected value is less than the set value.
JP59262396A 1984-12-12 1984-12-12 Absorption heat pump device Expired - Lifetime JPH06100400B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59262396A JPH06100400B2 (en) 1984-12-12 1984-12-12 Absorption heat pump device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59262396A JPH06100400B2 (en) 1984-12-12 1984-12-12 Absorption heat pump device

Publications (2)

Publication Number Publication Date
JPS61140757A JPS61140757A (en) 1986-06-27
JPH06100400B2 true JPH06100400B2 (en) 1994-12-12

Family

ID=17375183

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59262396A Expired - Lifetime JPH06100400B2 (en) 1984-12-12 1984-12-12 Absorption heat pump device

Country Status (1)

Country Link
JP (1) JPH06100400B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2645835B2 (en) * 1987-09-07 1997-08-25 三洋電機株式会社 Type 2 absorption heat pump device

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57164262A (en) * 1981-04-02 1982-10-08 Sanyo Electric Co Absorption refrigerating machine
JPS582569U (en) * 1981-06-29 1983-01-08 矢崎総業株式会社 Water-lithium salt double effect absorption refrigerator
JPS5869372A (en) * 1981-10-19 1983-04-25 三洋電機株式会社 Absorption heat pump

Also Published As

Publication number Publication date
JPS61140757A (en) 1986-06-27

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