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JPH0745989B2 - Absorption heat pump capacity controller - Google Patents
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JPH0745989B2 - Absorption heat pump capacity controller - Google Patents

Absorption heat pump capacity controller

Info

Publication number
JPH0745989B2
JPH0745989B2 JP6475687A JP6475687A JPH0745989B2 JP H0745989 B2 JPH0745989 B2 JP H0745989B2 JP 6475687 A JP6475687 A JP 6475687A JP 6475687 A JP6475687 A JP 6475687A JP H0745989 B2 JPH0745989 B2 JP H0745989B2
Authority
JP
Japan
Prior art keywords
temperature
heat pump
absorption heat
signal
refrigerant
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 - Fee Related
Application number
JP6475687A
Other languages
Japanese (ja)
Other versions
JPS63231147A (en
Inventor
成実 赤木
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 JP6475687A priority Critical patent/JPH0745989B2/en
Publication of JPS63231147A publication Critical patent/JPS63231147A/en
Publication of JPH0745989B2 publication Critical patent/JPH0745989B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は、再生器に高温レベルの熱源流体〔例えば100
℃以上の加熱蒸気〕を供給しつつ蒸発器で低温レベルの
熱源流体〔例えば100℃以下の熱源水〕の熱を汲み上げ
吸収器および凝縮器で放出する熱を取出すようにした吸
収ヒートポンプの容量制御装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention provides a regenerator with a heat source fluid at a high temperature level [eg 100
Capacity control of the absorption heat pump that pumps up the heat of the heat source fluid at a low temperature level (for example, heat source water of 100 ° C. or less) while supplying the heating steam) and takes out the heat released by the absorber and the condenser. Regarding the device.

(ロ)従来の技術 上記した吸収ヒートポンプ用容量制御装置の従来の技術
として、吸収ヒートポンプの再生器の加熱量を凝縮器出
口側の被加熱流体温度により調節するもの(例えば実開
昭61−3371号公報参照)やこのものにその調節量をヒー
トポンプ内部の状態量に基いて修正する手段を備えたも
の(例えば特開昭58−208551号公報参照)が知られてい
る。
(B) Conventional technology As a conventional technology of the capacity control device for the absorption heat pump described above, one which adjusts the heating amount of the regenerator of the absorption heat pump by the temperature of the fluid to be heated at the outlet side of the condenser (for example, actual development Sho 61-3371). (See Japanese Patent Laid-Open No. 58-551551), as well as the one provided with means for correcting the adjustment amount based on the state quantity inside the heat pump.

(ハ)発明が解決しようとする問題点 上記した従来の装置において、前者は吸収ヒートポンプ
から取出される被加熱流体をほぼ所望温度に保ち得る利
点をもつ反面、被加熱流体の流量を減らした場合、その
取出し温度の上昇を防ぐように再生器の加熱量を減らす
制御を行うため、再生器で濃縮される溶液言い代えれば
吸収器へ送られる溶液の濃度降下を生じ、吸収器の冷媒
吸収能力の低下延いては蒸発器の冷媒気化能力の低下す
なわち蒸発器の熱の汲み上げ能力の低下を招く欠点をも
っている。
(C) Problems to be Solved by the Invention In the above-mentioned conventional device, the former has an advantage that the heated fluid taken out from the absorption heat pump can be maintained at a substantially desired temperature, but when the flow rate of the heated fluid is reduced. , The heating amount of the regenerator is controlled so as to prevent the temperature at which it is taken out, so that the concentration of the solution concentrated in the regenerator, in other words, the solution sent to the absorber, drops, and the refrigerant absorption capacity of the absorber. As a result, the refrigerant vaporization ability of the evaporator is reduced, that is, the heat pumping ability of the evaporator is reduced.

また、後者の装置は、再生器の加熱量調節器の過不足を
吸収ヒートポンプ内部の状態量に基いて是正する利点を
もつものの、被加熱流体を所望温度に保つよう加熱量調
節器を行う点で前者の装置と同じであるため、被加熱流
体の流量を減らした場合、前者の装置と同様に蒸発器の
熱の汲み上げ能力の低下を招く欠点をもっている。
In addition, the latter device has the advantage of correcting the excess or deficiency of the heating amount controller of the regenerator based on the state amount inside the absorption heat pump, but the point that the heating amount controller is used to keep the fluid to be heated at the desired temperature. Since it is the same as the former device, it has a drawback that when the flow rate of the fluid to be heated is reduced, the heat pumping ability of the evaporator is lowered as in the former device.

本発明は、上記の問題点に鑑み、蒸発器の熱の汲み上げ
能力の低下を軽減して吸収ヒートポンプの運転効率を高
く維持し、かつ、被加熱流体の過熱も防ぐことの可能な
装置の提供を目的としたものである。
In view of the above problems, the present invention provides an apparatus capable of reducing the deterioration of the heat pumping capacity of an evaporator, maintaining a high operating efficiency of an absorption heat pump, and preventing overheating of a fluid to be heated. It is intended for.

(ニ)問題点を解決するための手段 本発明は、上記の問題点を解決するための吸収ヒートポ
ンプの容量制御装置として、再生器の加熱量を蒸発器内
の冷媒液量のセンサーもしくは凝縮器出口側の被加熱流
体の温度センサーのいずれかの信号で調節する構成と
し、かつ温度センサーの感知温度が設定温度より高い場
合に温度センサーの信号により調節する一方、低い場合
に冷媒液量センサーの信号により調節する構成としたも
のである。
(D) Means for Solving the Problems The present invention provides a capacity control device for an absorption heat pump for solving the above problems, in which a heating amount of a regenerator is a sensor of a refrigerant liquid amount in an evaporator or a condenser. The temperature of the fluid to be heated on the outlet side is adjusted by one of the signals of the temperature sensor, and when the temperature sensed by the temperature sensor is higher than the set temperature, it is adjusted by the signal of the temperature sensor. The configuration is adjusted by a signal.

(ホ)作用 本発明の制御装置によれば、被加熱流体が過熱域に近い
温度〔設定温度〕に達した場合に温度センサーの信号に
より再生器の加熱を制限して吸収ヒートポンプへの熱入
力を減らす作用を発揮させることができる。このため、
被加熱流体の過熱を防ぐことができる。
(E) Action According to the control device of the present invention, when the fluid to be heated reaches a temperature [set temperature] close to the overheat region, the heating of the regenerator is limited by the signal of the temperature sensor to input heat to the absorption heat pump. It is possible to exert the effect of reducing. For this reason,
Overheating of the fluid to be heated can be prevented.

かつまた、被過熱流体が過熱域から遠い温度領域にある
場合には冷媒液量センサーの信号により再生器の加熱量
を調節しつつ蒸発器内の冷媒液貯留量を調整する機能、
換言すれば、吸収ヒートポンプ内を循環する溶液の濃度
を所望の値に調整する作用を発揮させることができる。
このため、吸収ヒートポンプへの被加熱流体の流量を減
らしたときにも、吸収器の冷媒吸収能力の低下を緩和し
て蒸発器の冷媒気化能力すなわち蒸発器の熱の汲み上げ
能力の低下を軽減することができ、ヒートポンプの運転
効率を高く維持することが可能となる。
And also, when the superheated fluid is in a temperature region far from the superheat region, the function of adjusting the refrigerant liquid storage amount in the evaporator while adjusting the heating amount of the regenerator by the signal of the refrigerant liquid amount sensor,
In other words, the effect of adjusting the concentration of the solution circulating in the absorption heat pump to a desired value can be exhibited.
Therefore, even when the flow rate of the fluid to be heated to the absorption heat pump is reduced, the decrease in the refrigerant absorption capacity of the absorber is mitigated to reduce the decrease in the refrigerant vaporization capacity of the evaporator, that is, the heat pumping capacity of the evaporator. Therefore, it is possible to maintain high operation efficiency of the heat pump.

(ヘ)実施例 図面は本発明による吸収ヒートポンプの容量制御装置の
一実施例を示した概略構成説明図である。
(F) Embodiments The drawings are schematic configuration diagrams showing an embodiment of the capacity control device for an absorption heat pump according to the present invention.

図において、(1)は再生器、(2)は凝縮器、(3)
は蒸発器(4)および吸収器(5)を形成した蒸発吸収
器である。そして、これら機器は図示しない溶液流路と
冷媒流路とにより結ばれて従来の吸収ヒートポンプと同
様の冷媒および溶液の循環路を形成している。
In the figure, (1) is a regenerator, (2) is a condenser, and (3)
Is an evaporative absorber forming an evaporator (4) and an absorber (5). Then, these devices are connected by a solution flow path and a refrigerant flow path (not shown) to form a refrigerant and solution circulation path similar to the conventional absorption heat pump.

(6)は再生器(1)の加熱器、(7)は蒸発器(4)
の給熱器であり、(8),(9)はそれぞれ吸収器
(5)、凝縮器(2)の冷却器である。また、(10)は
蒸発器(4)の冷媒液溜めである。
(6) is a heater of the regenerator (1), (7) is an evaporator (4)
And (8) and (9) are the coolers of the absorber (5) and the condenser (2), respectively. Further, (10) is a refrigerant liquid reservoir of the evaporator (4).

(11)は加熱器(6)と接続した管で、この管には過熱
蒸気が流れる。(12)は図示しない水源と冷却器(8)
入口側と接続した水管、(13)は冷却器(8)出口側と
冷却器(9)入口側と接続した水管、(14)は冷却器
(9)出口側と図示しない負荷側例えば貯湯槽やボイラ
ーなどと接続した水管である。また、(15),(16)は
給熱器(7)と接続した管で、この管には排温水などの
熱源水が流れる。なお、(17)は発電機用タービンで、
これには管(11)の分岐管(18)が接続されている。
Reference numeral (11) is a pipe connected to the heater (6), and superheated steam flows through this pipe. (12) is a water source and cooler (8) not shown
A water pipe connected to the inlet side, (13) a water pipe connected to the cooler (8) outlet side and the cooler (9) inlet side, and (14) a cooler (9) outlet side and a load side not shown, for example, a hot water tank It is a water pipe connected to a boiler or the like. Further, (15) and (16) are pipes connected to the heat supply device (7), through which heat source water such as hot waste water flows. In addition, (17) is a turbine for generator,
The branch pipe (18) of the pipe (11) is connected to this.

そして、(SL)は蒸発器(4)の冷媒液溜め(10)に備
えた液面センサー、(V)は管(11)に配備した流量制
御弁であり、(CL)は液面センサー(SL)の信号を入力
して流量制御弁(V)への制御信号を出力するコントロ
ーラーである。また、(CT)は水管(14)に備えた温度
センサー(ST)の信号を入力して前記流量制御弁(V)
への制御信号を出力する温度調節器であり、この調節器
には温度設定部(CSET)およびその設定温度と温度セン
サー(ST)の感知温度との高低を判別する温度比較部
(CJ)が設けてある。かつまた、(RC)はリレー式切替
スイッチで、このスイッチのリレー接片は、前記設定温
度よりも温度センサー(ST)の感知温度の方が高い場合
の温度比較部(CJ)の判別信号によりH側へ接続される
一方、感知温度が設定温度以下である場合の判別信号に
よりC側へ接続されるようになっている。つまり、流量
制御弁(V)は管(14)内の水の上限温度を基準にして
コントローラー(CL)もしくは温度調節器(CT)の制御
信号のいずれかにより、換言すれば、液面センサー
(SL)もしくは温度センサー(ST)のいずれかの信号に
より制御されるのである。
Further, (S L ) is a liquid level sensor provided in the refrigerant liquid reservoir (10) of the evaporator (4), (V) is a flow control valve provided in the pipe (11), and (C L ) is a liquid level. It is a controller that inputs the signal of the sensor (S L ) and outputs the control signal to the flow control valve (V). Further, (C T ) receives a signal from a temperature sensor (S T ) provided in the water pipe (14) to input the flow control valve (V).
Is a temperature controller that outputs a control signal to the temperature controller (C SET ) and a temperature comparator (C C) that determines whether the set temperature and the temperature sensed by the temperature sensor ( ST ) are high or low. J ) is provided. Also, (R C ) is a relay type changeover switch, and the relay contact piece of this switch has a temperature comparison unit (C J ) when the sensed temperature of the temperature sensor (S T ) is higher than the set temperature. While being connected to the H side by the discrimination signal, it is connected to the C side by the discrimination signal when the sensed temperature is equal to or lower than the set temperature. That is, the flow control valve (V) is controlled by either the controller ( CL ) or the temperature controller ( CT ) control signal based on the upper limit temperature of the water in the pipe (14), in other words, the liquid level. It is controlled by the signal of either the sensor (S L ) or the temperature sensor (S T ).

なお、液面検出手段は液面センサーに限らず例えばフロ
ートスイッチなどを用いても良く、また、温度検出手段
は温度センサーに限らず例えばサーモスイッチなどを用
いても良い。
The liquid level detecting means is not limited to the liquid level sensor and may be, for example, a float switch, and the temperature detecting means is not limited to the temperature sensor and may be, for example, a thermoswitch.

次に、このように構成された吸収ヒートポンプの容量制
御装置(以下、本装置という)の動作例をヒートポンプ
の動作と併せて説明する。
Next, an operation example of the absorption heat pump capacity control device (hereinafter referred to as the present device) configured as described above will be described together with the operation of the heat pump.

吸収ヒートポンプの運転中、水管(14)内の水が上限温
度〔例えば100℃〕以下である場合、切替スイッチ
(RC)の接片はC側へ接続されている。そして、流量制
御弁(V)は液面センサー(SL)の信号によりコントロ
ーラー(CL)を介して制御される。
During operation of the absorption heat pump, when the water in the water pipe (14) is at or below the upper limit temperature (for example, 100 ° C. ), the contact piece of the changeover switch (R C ) is connected to the C side. Then, the flow control valve (V) is controlled by the signal of the liquid level sensor (S L ) via the controller (C L ).

上記の場合において、被過熱流体が定格の条件で吸収ヒ
ートポンプを流通するとき、ちなみに被加熱流体として
の水の吸収ヒートポンプへの流通量を100m3/h、吸収ヒ
ートポンプ入口側の水温を30℃、出口側の水温を70℃の
条件〔温水出力4000Mcal/h〕でヒートポンプが運転され
ているとき、蒸発器(4)の冷媒液溜め(10)の液位は
定格のレベル〔例えば液溜め(10)の上限レベル近く〕
にあり、流量制御弁(V)は定格の開度に保たれてい
る。今、例えば水の流量が50m3/hに減少したとき、吸収
器(5)の冷媒吸収能力が低下し、これに伴ない蒸発器
(4)の冷媒気化能力換言すれば蒸発器(4)による熱
源水からの熱の汲み上げ能力が低下して吸収ヒートポン
プの運転効率が悪くなる。そして、このとき、蒸発器
(4)の冷媒液溜め(10)の液位も上昇するため、これ
をそのまま放置すると冷媒液溜め(10)から冷媒液が溢
れ出て吸収器(5)内の溶液へ混入することになり、吸
収ヒートポンプの運転効率がさらに悪くなる。
In the above case, when the fluid to be superheated flows through the absorption heat pump under rated conditions, by the way, the flow rate of water as the fluid to be heated to the absorption heat pump is 100 m 3 / h, the water temperature on the inlet side of the absorption heat pump is 30 ° C., When the heat pump is operated under the condition that the water temperature at the outlet side is 70 ° C [warm water output 4000Mcal / h], the liquid level of the refrigerant sump (10) of the evaporator (4) is at a rated level [eg, sump (10 ) Near the upper limit level)
The flow rate control valve (V) is maintained at the rated opening. Now, for example, when the flow rate of water is reduced to 50 m 3 / h, the refrigerant absorption capacity of the absorber (5) decreases, and with this, the refrigerant vaporization capacity of the evaporator (4) In other words, the evaporator (4) As a result, the ability to pump heat from the heat source water decreases, and the operating efficiency of the absorption heat pump deteriorates. At this time, since the liquid level of the refrigerant liquid reservoir (10) of the evaporator (4) also rises, if this is left as it is, the refrigerant liquid overflows from the refrigerant liquid reservoir (10) and the inside of the absorber (5) It will be mixed in the solution, and the operation efficiency of the absorption heat pump will be further deteriorated.

このようなとき、本装置においては、液面センサー
(SL)が液位の上昇を感知しつつこれをコントローラー
(CL)へ信号で送り、この信号を受けたコントローラー
(CL)は液位を定格レベルまで復帰させるように流量制
御弁(V)の開度を減少制御して再生器(1)の加熱量
を減らす。その結果、再生器(1)で溶液から分離され
る冷媒量が減り、延いては凝縮器(2)経由で蒸発器
(4)に流入する冷媒液量が減少し、冷媒液溜め(10)
からの冷媒液の溢流が防止される。すなわち、この溢流
に伴なう吸収ヒートポンプの運転効率の低下が防止され
るのである。なお、再生器(1)への熱源蒸気の供給量
を減らした分は発電機用タービン(17)へ供給されるこ
とになる。ちなみに、被加熱流体としての水の流量が50
m3/hに減少し、かつ、吸収ヒートポンプの入口側の水温
が10℃に変化したとき、本装置の容量制御によって冷媒
液溜め(10)の液位は定格レベルに保たれ、吸収ヒート
ポンプ出口側の水温は90℃となり、4000Mcal/hの温水出
力が得られる。
In such a case, in this device, the liquid level sensor (S L ) detects the rise of the liquid level and sends it to the controller (C L ) as a signal, and the controller (C L ) receiving this signal The opening amount of the flow control valve (V) is controlled to be decreased so that the position of the regenerator (1) is returned to the rated level. As a result, the amount of the refrigerant separated from the solution in the regenerator (1) decreases, and the amount of the refrigerant liquid flowing into the evaporator (4) via the condenser (2) decreases, and the refrigerant sump (10)
The overflow of the refrigerant liquid from the inside is prevented. That is, it is possible to prevent the operation efficiency of the absorption heat pump from being lowered due to the overflow. The reduced amount of the heat source steam supplied to the regenerator (1) will be supplied to the generator turbine (17). By the way, the flow rate of water as the fluid to be heated is 50
reduced to m 3 / h, and when the water temperature on the inlet side of the absorption heat pump is changed to 10 ° C., the liquid level of the reservoir the refrigerant fluid (10) by the capacity control of the apparatus is maintained at the rated level, the absorption heat pump outlet The water temperature on the side is 90 ° C, and a hot water output of 4000Mcal / h can be obtained.

一方、被加熱流体としての水の流量が逆に200m3/hに増
えたとき、水の流量が減ったときとは逆に冷媒液溜め
(10)の液位が降下するので、液面センサー(SL)の信
号によりコントローラー(CL)は流量制御弁(V)の開
度を増大制御する。その結果、再生器(1)での溶液の
濃縮が高められ、換言すれば、溶液から分離される冷媒
量が増え、凝縮器(2)経由で蒸発器(4)に流入する
冷媒液量が増大して冷媒液溜め(10)内の液位が再び上
昇し始める。そして、ヒートポンプを循環する溶液の濃
度は被加熱流体〔水〕の流量の増加前と同じに戻され、
かつ、吸収器(5)の冷却器(8)内の水流量は増えて
溶液の冷媒吸収力は強まるので、蒸発器(4)の冷媒気
化能力は水流量の増加前よりも向上する。このため、ヒ
ートポンプの蒸発器での熱の汲み上げ能力が向上してヒ
ートポンプの運転効率が高まると共に温水出力も高ま
る。
On the other hand, when the flow rate of water as the fluid to be heated is increased to 200 m 3 / h, the liquid level in the refrigerant sump (10) drops, contrary to the decrease in the flow rate of water. signal by the controller (C L) of (S L) increases controlling the opening of the flow control valve (V). As a result, the concentration of the solution in the regenerator (1) is increased, in other words, the amount of refrigerant separated from the solution is increased, and the amount of refrigerant liquid flowing into the evaporator (4) via the condenser (2) is increased. It increases and the liquid level in the refrigerant liquid reservoir (10) begins to rise again. Then, the concentration of the solution circulating through the heat pump is returned to the same as before the flow rate of the heated fluid [water] was increased,
Moreover, since the water flow rate in the cooler (8) of the absorber (5) increases and the refrigerant absorbing power of the solution is strengthened, the refrigerant vaporizing capacity of the evaporator (4) improves more than before the increase of the water flow rate. Therefore, the heat pumping capacity of the evaporator of the heat pump is improved, the operating efficiency of the heat pump is increased, and the hot water output is also increased.

このように、本装置は再生器(1)の加熱量を調節しつ
つ蒸発器(4)内の冷媒液貯留量を定格値〔冷媒液溜め
(10)のほぼ全容量〕に保つ機能換言すれば溶液の濃度
を吸収ヒートポンプにおいて可能な最高濃度に保つ機能
を発揮するのである。そして、本装置によれば、ヒート
ポンプへの水〔被加熱流体〕の流量を減らしたときや水
のヒートポンプへの流入温度を高くしたときにはその変
化前と同程度の溶液の濃度に維持して溶液への冷媒液の
溢流を防ぎ、大きな熱ロスの発生を防止することができ
る一方、水の流量を増やしたときや流入温度を低くした
ときにはその変化前よりも大きな冷媒吸収力を発揮させ
ることができる。このため、ヒートポンプの蒸発器
(4)による熱の汲み上げ能力すなわちヒートポンプの
運転効率を高い水準に維持することができる。
In this way, this device maintains the refrigerant liquid storage amount in the evaporator (4) at the rated value [almost the entire capacity of the refrigerant liquid reservoir (10)] while adjusting the heating amount of the regenerator (1). For example, it exerts the function of keeping the concentration of the solution at the highest concentration possible in the absorption heat pump. Then, according to this device, when the flow rate of water (fluid to be heated) to the heat pump is reduced or when the inflow temperature of water to the heat pump is increased, the solution is maintained at the same concentration as before the change. It is possible to prevent the overflow of the refrigerant liquid to the refrigerant and prevent the generation of a large heat loss, but when the flow rate of the water is increased or the inflow temperature is lowered, it is possible to exert a larger refrigerant absorption force than before the change. You can Therefore, the heat pumping ability of the evaporator (4) of the heat pump, that is, the operation efficiency of the heat pump can be maintained at a high level.

なお、上述の定格レベルを冷媒液溜め(10)の上限レベ
ル以外の任意のレベルに設定し得ることは勿論である。
この設定はコントローラー(CL)のレベル設定器(図示
せず)のボリューム〔抵抗値〕を任意にセットすること
によってなされる。
It is needless to say that the above-mentioned rated level can be set to any level other than the upper limit level of the refrigerant liquid reservoir (10).
This setting is made by arbitrarily setting the volume (resistance value) of the level setter (not shown) of the controller ( CL ).

また、本装置においては、ヒートポンプから流出する水
〔被加熱流体〕の温度が100℃を越えた場合、温度調節
器(CT)の温度比較部(CJ)の判別信号により切替スイ
ッチ(RC)のリレー接片がH側へ切換えられ、温度セン
サー(ST)の信号で流量制御弁(V)が絞られる。これ
により吸収ヒートポンプの熱入力が減り、それに伴ない
凝縮器(2)の放熱量も減るので、この凝縮器で加熱さ
れる水〔被加熱流体〕が100℃以下に降温し、その過熱
が防止される。このように、本装置によれば、凝縮器
(2)の冷却器(9)内の水が100℃以下に抑えられそ
の飽和蒸気圧が大気圧以下に保たれるので、冷却器
(9)を耐圧構造のものにしなくて済み、そのコスト低
減、軽量化などを図り得る。
Also, in this device, when the temperature of the water (fluid to be heated) flowing out from the heat pump exceeds 100 ° C, the changeover switch (R) is turned on by the discrimination signal of the temperature comparison unit (C J ) of the temperature controller (C T ). relay contact piece of C) is switched to the H side, the flow control valve (V) is throttled by a signal of the temperature sensor (S T). As a result, the heat input of the absorption heat pump is reduced, and the amount of heat released from the condenser (2) is also reduced, so that the water (fluid to be heated) heated by this condenser is cooled to below 100 ° C, and its overheating is prevented. To be done. As described above, according to the present device, the water in the cooler (9) of the condenser (2) is suppressed to 100 ° C. or lower, and the saturated vapor pressure thereof is maintained at the atmospheric pressure or lower. Therefore, the cooler (9) Since it does not have to be a pressure resistant structure, cost reduction and weight reduction can be achieved.

(ト)発明の効果 以上のとおり、本発明は、ヒートポンプの被加熱流体の
温度や流量などの条件の変化に伴なう、熱ロスの軽減効
果を吸収ヒートポンプにもたらし、その熱の汲み上げ能
力の低下を軽減する効果あるいは熱の汲み上げ能力の向
上効果をもたらし、ヒートポンプの運転効率を高い水準
に維持し、かつ、被加熱流体の過熱も防ぎ得るものとし
て実用的価値の高いものである。
(G) Effects of the Invention As described above, the present invention provides the absorption heat pump with the effect of reducing heat loss that accompanies changes in the conditions such as the temperature and flow rate of the heated fluid of the heat pump, and improves the heat pumping ability. It has a high practical value as an effect of reducing the decrease or an effect of improving the heat pumping ability, maintaining the operation efficiency of the heat pump at a high level, and preventing overheating of the fluid to be heated.

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

図面は本発明による吸収ヒートポンプの容量制御装置の
一実施例を示した概略構成説明図である。 (1)……再生器、(2)……凝縮器、(4)……蒸発
器、(5)……吸収器、(9)……冷却器、(10)……
冷媒液溜め、(CL)……コントローラー、(CT)……温
度調節器、(CSET)……温度設定部、(CJ)……温度比
較部、(ST)……温度センサー、(SL)……液面センサ
ー、(RC)……切替スイッチ、(V)……流量制御弁。
The drawings are schematic structural explanatory views showing an embodiment of a capacity control device for an absorption heat pump according to the present invention. (1) …… Regenerator, (2) …… Condenser, (4) …… Evaporator, (5) …… Absorber, (9) …… Cooler, (10) ……
Refrigerant sump, (C L ) …… Controller, (C T ) …… Temperature controller, (C SET ) …… Temperature setting section, (C J ) …… Temperature comparison section, (S T ) …… Temperature sensor , (S L ) ... Liquid level sensor, (R C ) ... Changeover switch, (V) ... Flow control valve.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】再生器の加熱量を調節する制御弁と、これ
への制御信号を蒸発器の冷媒液量センサーなどの液量検
出手段からの入力信号により出力するコントローラー
と、凝縮器出口側の被加熱流体の温度センサーなどの温
度検出手段からの信号により前記制御弁への制御信号を
出力する温度調節器とを備え、かつ、この温度調節器に
温度設定部およびこれにより設定された温度と前記温度
センサーの感知温度との高低を判別する温度比較部を設
け、この温度比較部の判別信号により前記制御弁への制
御信号を切換えるスイッチを備えて構成した吸収ヒート
ポンプの容量制御装置。
1. A control valve for adjusting a heating amount of a regenerator, a controller for outputting a control signal to the control valve according to an input signal from a liquid amount detecting means such as a refrigerant liquid amount sensor of an evaporator, and a condenser outlet side. A temperature controller for outputting a control signal to the control valve in response to a signal from a temperature detecting means such as a temperature sensor for the fluid to be heated, and a temperature setting unit and a temperature set by the temperature controller. A capacity control device for an absorption heat pump, comprising a temperature comparison unit for determining whether the temperature is higher or lower than the temperature sensed by the temperature sensor, and a switch for switching a control signal to the control valve according to a determination signal of the temperature comparison unit.
JP6475687A 1987-03-19 1987-03-19 Absorption heat pump capacity controller Expired - Fee Related JPH0745989B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6475687A JPH0745989B2 (en) 1987-03-19 1987-03-19 Absorption heat pump capacity controller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6475687A JPH0745989B2 (en) 1987-03-19 1987-03-19 Absorption heat pump capacity controller

Publications (2)

Publication Number Publication Date
JPS63231147A JPS63231147A (en) 1988-09-27
JPH0745989B2 true JPH0745989B2 (en) 1995-05-17

Family

ID=13267336

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6475687A Expired - Fee Related JPH0745989B2 (en) 1987-03-19 1987-03-19 Absorption heat pump capacity controller

Country Status (1)

Country Link
JP (1) JPH0745989B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6399263B1 (en) 1999-05-10 2002-06-04 Konica Corporation Electrophotographic photoreceptor, electrophotographic process, and electrophotographic image forming method

Also Published As

Publication number Publication date
JPS63231147A (en) 1988-09-27

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