JP2001082821A - Absorption heat pump - Google Patents

Absorption heat pump

Info

Publication number
JP2001082821A
JP2001082821A JP25476499A JP25476499A JP2001082821A JP 2001082821 A JP2001082821 A JP 2001082821A JP 25476499 A JP25476499 A JP 25476499A JP 25476499 A JP25476499 A JP 25476499A JP 2001082821 A JP2001082821 A JP 2001082821A
Authority
JP
Japan
Prior art keywords
refrigerant
liquid
reservoir
supplied
absorbing liquid
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.)
Pending
Application number
JP25476499A
Other languages
Japanese (ja)
Inventor
Takao Tanaka
貴雄 田中
Yonezo Ikumi
米造 井汲
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 JP25476499A priority Critical patent/JP2001082821A/en
Publication of JP2001082821A publication Critical patent/JP2001082821A/en
Pending 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
    • 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
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Abstract

PROBLEM TO BE SOLVED: To enhance COP by reducing the quantity of heat being thrown into an evaporator through an arrangement wherein refrigerant liquid generated from a condenser is heated in a refrigerant/absorbing liquid heat exchanger with high temperature absorbing liquid returned from a desorber through an absorbing liquid return pipe before being supplied to the evaporator. SOLUTION: The absorption heat pump comprises a regenerator 1, a condenser 2, an evaporator 3, an absorber 4, a resorber 5 where refrigerant vapor supplied from the evaporator 3 is absorbed into absorbing liquid, and a desorber 6 for heating the absorbing liquid having high refrigerant concentration supplied from the resorber 5 to separate the refrigerant from the absorbing liquid through evaporation, supplying the absorbing liquid having lowered refrigerant concentration to a heat exchanger 8 also supplied with absorbing liquid from the resorber 5 and returning the heat exchanged absorbing liquid back to the resorber 5, and supplying refrigerant vapor separated from the absorbing liquid through evaporation to the absorber 4. The absorption heat pump further comprises a heat exchanger 9 for exchanging heat between refrigerant liquid supplied from the condenser 2 to the evaporator 3 and absorbing liquid being returned from the desorber 6 back to the resorber 5, and a heat exchanger 10 for exchanging heat between absorbing liquid being supplied from the regenerator 1 to the absorber 4 and refrigerant liquid being returned from the desorber 6 back to the resorber 5.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、再生器、凝縮器、
蒸発器、吸収器などと共に、リソーバとデソーバとを備
えて構成される吸収ヒートポンプ装置に関する。
The present invention relates to a regenerator, a condenser,
The present invention relates to an absorption heat pump device including a evaporator, an absorber, and the like, as well as a reservoir and a desorber.

【0002】[0002]

【従来の技術】冷媒の蒸発熱と溶液の再生熱を温排水な
どから供給し、図2に示したように蒸発器は中間圧力と
し、蒸発した冷媒を第二種サイクルのリソーバである中
間濃度の溶液に吸収させ、吸収後の溶液を低圧力のデソ
ーバで再生し、発生した冷媒を第一種サイクルの吸収器
で吸収させる、第一種吸収ヒートポンプと第二種吸収ヒ
ートポンプとを組み合わせた吸収ヒートポンプ装置にお
いては、蒸発器とデソーバとで吸熱し、凝縮器と第二種
サイクルのリソーバおよび第一種サイクルの吸収器で放
熱するので、暖房時のCOPが2以上となると云った利
点がある。
2. Description of the Related Art The heat of evaporation of a refrigerant and the heat of regeneration of a solution are supplied from hot waste water or the like, and the evaporator is set at an intermediate pressure as shown in FIG. Absorbed by a combination of a first-class absorption heat pump and a second-class absorption heat pump, in which the absorbed solution is regenerated by a low-pressure desorber and the generated refrigerant is absorbed by a first-class cycle absorber. In the heat pump device, heat is absorbed by the evaporator and the desorber, and the heat is released by the condenser, the second-cycle reactor and the first-cycle absorber, so that there is an advantage that the COP during heating becomes 2 or more. .

【0003】[0003]

【発明が解決しようとする課題】そして、上記構成の吸
収ヒートポンプ装置においても、効率化をさらに一層進
める必要があり、これが解決すべき課題となっていた。
In the absorption heat pump apparatus having the above structure, it is necessary to further improve the efficiency, and this has been a problem to be solved.

【0004】[0004]

【課題を解決するための手段】上記課題を解決すべく本
発明は、吸収液を加熱して吸収液から冷媒を蒸発分離す
る再生器と、再生器から供給される冷媒蒸気を冷却して
凝縮させる凝縮器と、凝縮器から供給される冷媒液を加
熱して蒸発させる蒸発器と、冷媒を蒸発分離して再生器
から供給される冷媒の濃度が低下した吸収液に冷媒を吸
収させ、再生器から供給されている吸収液と熱交換させ
て再生器に戻す吸収器と、蒸発器から供給される冷媒蒸
気を吸収液に吸収させるリソーバと、冷媒を吸収してリ
ソーバから供給される冷媒の濃度が上昇した吸収液を加
熱して冷媒を吸収液から蒸発分離し、冷媒の濃度が低下
した吸収液をリソーバから供給されている吸収液と熱交
換させてリソーバに戻すと共に、吸収液から蒸発分離し
た冷媒蒸気を吸収器に供給するデソーバとを備えた吸収
ヒートポンプ装置において、
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides a regenerator for heating an absorption liquid to evaporate and separate a refrigerant from the absorption liquid, and cooling and condensing refrigerant vapor supplied from the regenerator. A condenser for heating and evaporating a refrigerant liquid supplied from the condenser, and an evaporator for evaporating and separating the refrigerant to absorb the refrigerant in an absorbent having a reduced concentration of the refrigerant supplied from the regenerator, thereby regenerating the refrigerant. An absorber that exchanges heat with the absorbing liquid supplied from the evaporator and returns to the regenerator; a absorber that absorbs the refrigerant vapor supplied from the evaporator into the absorbing liquid; and a refrigerant that absorbs the refrigerant and is supplied from the reservoir. Heating the absorbing liquid with the increased concentration causes the refrigerant to evaporate and separate from the absorbing liquid, and heat-exchanging the absorbing liquid with the decreasing concentration of the absorbing liquid with the absorbing liquid supplied from the reservoir to return to the reservoir and evaporating from the absorbing liquid. Absorbs separated refrigerant vapor In the absorption heat pump apparatus having a Desoba supplied to,

【0005】凝縮器から蒸発器に供給されている冷媒液
と、デソーバからリソーバに戻されている吸収液とが熱
交換する冷媒/吸収液熱交換器を備えるようにした第1
の構成の吸収ヒートポンプ装置と、
[0005] A first refrigerant / absorbent heat exchanger for exchanging heat between the refrigerant liquid supplied from the condenser to the evaporator and the absorbing liquid returned from the desorber to the reservoir.
An absorption heat pump device having the structure of

【0006】再生器から吸収器に供給されている吸収液
と、デソーバからリソーバに戻されている吸収液とが熱
交換する吸収液/吸収液熱交換器を備えるようにした第
2の構成の吸収ヒートポンプ装置と、
[0006] A second structure is provided with an absorbing liquid / absorbing liquid heat exchanger for exchanging heat between the absorbing liquid supplied to the absorber from the regenerator and the absorbing liquid returned from the desorber to the reservoir. An absorption heat pump device,

【0007】凝縮器から蒸発器に供給されている冷媒液
とデソーバからリソーバに戻されている吸収液とが熱交
換する冷媒/吸収液熱交換器と、再生器から吸収器に供
給されている吸収液とデソーバからリソーバに戻されて
いる吸収液とが熱交換する吸収液/吸収液熱交換器とを
備えるようにした第3の構成の吸収ヒートポンプ装置
と、
[0007] A refrigerant / absorbent heat exchanger for exchanging heat between the refrigerant liquid supplied from the condenser to the evaporator and the absorbing liquid returned from the desorber to the reservoir, and supplied from the regenerator to the absorber. An absorption heat pump device having a third configuration, comprising: an absorption liquid / absorption liquid heat exchanger that exchanges heat between the absorption liquid and the absorption liquid returned from the desorber to the reservoir;

【0008】前記第1または第3の構成の吸収ヒートポ
ンプ装置において、冷媒/吸収液熱交換器を、凝縮器か
ら蒸発器に至る冷媒液管においては下方に屈曲形成され
た液シール部に、デソーバからリソーバに至る吸収液戻
し管においてはリソーバからデソーバに供給されている
吸収液とデソーバからリソーバに戻されている吸収液と
が熱交換する熱交換器よりデソーバ側に設置するように
した第4の構成の吸収ヒートポンプ装置と、
[0008] In the absorption heat pump device of the first or third configuration, the refrigerant / absorbent liquid heat exchanger is provided with a desorber at a liquid seal portion bent downward in a refrigerant liquid pipe from the condenser to the evaporator. In the absorption liquid return pipe from the reservoir to the reservoir, the absorption liquid supplied from the reservoir to the reservoir and the absorption liquid returned from the reservoir to the reservoir are disposed closer to the reservoir than the heat exchanger that exchanges heat. An absorption heat pump device having the structure of

【0009】前記第2または第3の構成の吸収ヒートポ
ンプ装置において、吸収液/吸収液熱交換器を、再生器
から吸収器に至る冷媒液供給管においては再生器から吸
収器に供給されている吸収液と吸収器から再生器に戻さ
れている吸収液とが熱交換する熱交換器より吸収器側
に、デソーバからリソーバに至る吸収液戻し管において
はリソーバからデソーバに供給されている吸収液とデソ
ーバからリソーバに戻されている吸収液とが熱交換する
熱交換器よりリソーバ側に設置するようにした第5の構
成の吸収ヒートポンプ装置と、
In the absorption heat pump device of the second or third configuration, the absorption liquid / absorption liquid heat exchanger is supplied from the regenerator to the absorber in a refrigerant liquid supply pipe from the regenerator to the absorber. Absorbent liquid being supplied to the reservoir from the reservoir in the absorbent return pipe from the heat exchanger to the absorber, where heat is exchanged between the absorbent and the absorbent returned from the absorber to the regenerator. And an absorption heat pump device having a fifth configuration in which the absorption liquid is returned to the reservoir from the heat exchanger in which the absorption liquid returned to the reservoir from the desorber exchanges heat.

【0010】前記第3の構成の吸収ヒートポンプ装置に
おいて、冷媒/吸収液熱交換器を、凝縮器から蒸発器に
至る冷媒液管においては下方に屈曲形成された液シール
部に、デソーバからリソーバに至る吸収液戻し管におい
てはリソーバからデソーバに供給されている吸収液とデ
ソーバからリソーバに戻されている吸収液とが熱交換す
る熱交換器よりデソーバ側に設置し、吸収液/吸収液熱
交換器を、再生器から吸収器に至る冷媒液供給管におい
ては再生器から吸収器に供給されている吸収液と吸収器
から再生器に戻されている吸収液とが熱交換する熱交換
器より吸収器側に、デソーバからリソーバに至る吸収液
戻し管においてはリソーバからデソーバに供給されてい
る吸収液とデソーバからリソーバに戻されている吸収液
とが熱交換する熱交換器よりリソーバ側に設置するよう
にした第6の構成の吸収ヒートポンプ装置と、を提供す
るものである。
[0010] In the absorption heat pump device of the third configuration, the refrigerant / absorbent liquid heat exchanger is connected to the liquid seal portion bent downward in the refrigerant liquid pipe from the condenser to the evaporator, and from the desorber to the reservoir. In the absorption liquid returning pipe, the absorption liquid supplied from the reservoir to the desorber and the absorption liquid returned from the desorber to the reservoir are installed on the desorber side from a heat exchanger where heat exchange is performed. In the refrigerant liquid supply pipe from the regenerator to the absorber, the heat exchanger exchanges heat between the absorbent supplied from the regenerator to the absorber and the absorbent returned from the absorber to the regenerator. On the absorber side, in the absorbent return pipe from the reservoir to the reservoir, heat is exchanged between the absorbent supplied from the reservoir to the reservoir and the absorbent returned from the reservoir to the reservoir. 6 the absorption heat pump apparatus of the configuration of which is adapted to placed in Risoba side of exchanger, there is provided a.

【0011】[0011]

【発明の実施の形態】以下、本発明の実施形態を図面に
基づいて詳細に説明する。図1に例示したものは、冷媒
に水を、吸収液に臭化リチウム水溶液などを使用して、
暖房などの加熱作用を行うための吸収ヒートポンプ装置
である。
Embodiments of the present invention will be described below in detail with reference to the drawings. The example illustrated in FIG. 1 uses water as a refrigerant and an aqueous solution of lithium bromide as an absorbing liquid.
It is an absorption heat pump device for performing a heating function such as heating.

【0012】同図に示した吸収ヒートポンプ装置は、吸
収液を加熱して吸収液から冷媒を蒸発分離する再生器1
と、この再生器1から供給される冷媒蒸気を冷却して凝
縮させる凝縮器2と、この凝縮器2から冷媒液供給管1
1を介して供給される冷媒液を加熱して蒸発させる蒸発
器3と、冷媒を蒸発分離して再生器1から吸収液供給管
12を介して供給される冷媒の濃度が低下した吸収液に
冷媒を吸収させ、再生器1から吸収液供給管12を介し
て供給されている吸収液と熱交換器7で熱交換させて再
生器1に吸収液戻し管13を介して戻す吸収器4と、蒸
発器3から供給される冷媒蒸気を吸収液に吸収させるリ
ソーバ5と、冷媒を吸収してリソーバ5から吸収液供給
管14を介して供給される冷媒の濃度が上昇した吸収液
を加熱して冷媒を吸収液から蒸発分離し、冷媒の濃度が
低下した吸収液をリソーバ5から吸収液供給管14を介
して供給されている吸収液と熱交換器8で熱交換させて
リソーバ5に吸収液戻し管15を介して戻すと共に、吸
収液から蒸発分離した冷媒蒸気を吸収器4に供給するデ
ソーバ6とを備えている。
The absorption heat pump device shown in FIG. 1 is a regenerator 1 for heating an absorption liquid and evaporating and separating a refrigerant from the absorption liquid.
And a condenser 2 for cooling and condensing the refrigerant vapor supplied from the regenerator 1, and a refrigerant liquid supply pipe 1 from the condenser 2.
The evaporator 3 heats and evaporates the refrigerant liquid supplied through the evaporator 1, and the evaporator 3 evaporates and separates the refrigerant to reduce the concentration of the refrigerant supplied from the regenerator 1 via the absorbent supply pipe 12. An absorber 4 for absorbing the refrigerant, exchanging heat in the heat exchanger 7 with the absorbing liquid supplied from the regenerator 1 via the absorbing liquid supply pipe 12 and returning the heat to the regenerator 1 via the absorbing liquid return pipe 13; A absorber 5 that absorbs the refrigerant vapor supplied from the evaporator 3 into the absorbing liquid, and an absorbing liquid that absorbs the refrigerant and has an increased concentration of the refrigerant supplied from the reservoir 5 through the absorbing liquid supply pipe 14. The refrigerant is evaporated and separated from the absorbing liquid, and the absorbing liquid having the reduced concentration of the refrigerant is heat-exchanged by the heat exchanger 8 with the absorbing liquid supplied from the reservoir 5 through the absorbing liquid supply pipe 14 and absorbed by the reservoir 5. The liquid is returned through the liquid return pipe 15 and separated from the absorbent by evaporation. And a Desoba 6 supplied to the absorber 4 refrigerant vapors.

【0013】そして、冷媒液供給管11を介して凝縮器
2から蒸発器3に供給されている冷媒液と、吸収液戻し
管15を介してデソーバ6からリソーバ5に戻されてい
る吸収液とが熱交換する冷媒/吸収液熱交換器9が図示
した位置に、すなわち冷媒液が空となることがないよう
に蒸発器3への連結部より下方に屈曲形成された冷媒液
供給管11の液シール部11Aの部分と、デソーバ6と
熱交換器8との間の吸収液戻し管15の部分とに設置さ
れている。
The refrigerant liquid supplied from the condenser 2 to the evaporator 3 via the refrigerant liquid supply pipe 11 and the absorption liquid returned from the desorber 6 to the reservoir 5 via the absorption liquid return pipe 15 The refrigerant / absorbent liquid heat exchanger 9 for exchanging heat is located at the position shown in the drawing, that is, the refrigerant liquid supply pipe 11 bent below the connecting portion to the evaporator 3 so that the refrigerant liquid does not become empty. The liquid seal portion 11A and the absorbent return pipe 15 between the desorber 6 and the heat exchanger 8 are provided.

【0014】また、吸収液供給管12を介して再生器1
から吸収器4に供給されている吸収液と、吸収液戻し管
15を介してデソーバ6からリソーバ5に戻されている
冷媒液とが熱交換する吸収液/吸収液熱交換器10が図
示した位置に、すなわち熱交換器7と吸収器4との間の
吸収液供給管12の部分と、熱交換器8とリソーバ5と
の間の吸収液戻し管15の部分とに設置されている。
Further, the regenerator 1 is connected to the
The absorbent / absorbent heat exchanger 10 in which the heat exchange between the absorbent supplied to the absorber 4 and the refrigerant liquid returned from the desorber 6 to the reservoir 5 via the absorbent return pipe 15 is shown. At the position, that is, at the portion of the absorbent supply pipe 12 between the heat exchanger 7 and the absorber 4 and at the portion of the absorbent return pipe 15 between the heat exchanger 8 and the reservoir 5.

【0015】また、再生器1の内部には伝熱管1Aが設
けられ、この伝熱管1Aの内部に駆動熱源として、例え
ば170℃程度の高温の飽和蒸気が供給され、吸収器4
から吸収液ポンプP1により吸収液戻し管13を介して
戻され、散布器1Bから伝熱管1Aの上に散布される吸
収液を加熱して、凝縮器2に供給する冷媒蒸気を発生さ
せるようになっている。
A heat transfer tube 1A is provided inside the regenerator 1, and a high-temperature saturated steam of, for example, about 170 ° C. is supplied as a driving heat source into the heat transfer tube 1A.
Is heated by the absorbing liquid pump P1 through the absorbing liquid return pipe 13 to spray the absorbing liquid from the sprayer 1B onto the heat transfer pipe 1A to generate refrigerant vapor to be supplied to the condenser 2. Has become.

【0016】凝縮器2の内部には伝熱管2Aが設けら
れ、この伝熱管2Aの内部を流れる冷却水が、再生器1
から供給されて放熱液化する冷媒の凝縮熱によって加熱
され、例えば80℃程度の利用温水となって熱負荷に供
給されるようになっている。
A heat transfer tube 2A is provided inside the condenser 2, and the cooling water flowing inside the heat transfer tube 2A is supplied to the regenerator 1
Is heated by the condensing heat of the refrigerant supplied and liquefied by the heat, and is supplied to a heat load as hot water of about 80 ° C., for example.

【0017】蒸発器3の内部には伝熱管3Aが設けら
れ、この伝熱管3Aの内部に熱源として、例えば60℃
程度の温排水が供給され、凝縮器2から冷媒液供給管1
1を介して供給され、冷媒液管16の冷媒ポンプP3に
よって散布器3Bから伝熱管3Aの上に散布される冷媒
液を加熱して、リソーバ5に供給する冷媒蒸気を発生さ
せるようになっている。
A heat transfer tube 3A is provided inside the evaporator 3, and a heat source such as 60 ° C. is provided inside the heat transfer tube 3A.
Is supplied to the refrigerant liquid supply pipe 1 from the condenser 2.
1 and is heated by the refrigerant pump P3 of the refrigerant liquid pipe 16 and sprayed from the sprayer 3B onto the heat transfer pipe 3A to generate refrigerant vapor to be supplied to the reservoir 5. I have.

【0018】デソーバ6の内部には伝熱管6Aが設けら
れ、この伝熱管6Aの内部に熱源として例えば60℃程
度の温排水が供給され、リソーバ5から吸収液供給管1
4を介して供給され散布器6Bから伝熱管6Aの上に散
布される吸収液を加熱して、吸収器4に供給する冷媒蒸
気を発生させるようになっている。
A heat transfer tube 6A is provided inside the desorber 6, and hot drainage of, for example, about 60 ° C. is supplied as a heat source into the heat transfer tube 6A.
Heating the absorbing liquid supplied via the sprayer 4 onto the heat transfer tube 6A from the sprayer 6B generates refrigerant vapor to be supplied to the absorber 4.

【0019】吸収器4の内部には伝熱管4Aが設けら
れ、この伝熱管4Aの内部を流れる冷却水により再生器
1から供給されて散布器4Bから伝熱管4Aの上に散布
される吸収液を冷却し、デソーバ6から供給される冷媒
蒸気を吸収し易くしている。
A heat transfer tube 4A is provided inside the absorber 4, and the absorbing liquid supplied from the regenerator 1 by the cooling water flowing inside the heat transfer tube 4A and sprayed from the sprayer 4B onto the heat transfer tube 4A. Is cooled, and the refrigerant vapor supplied from the desorber 6 is easily absorbed.

【0020】リソーバ5の内部には伝熱管5Aが設けら
れ、吸収器4で冷却作用を果たして伝熱管4Aから冷却
水管17に流れ出した冷却水が伝熱管5Aの内部を流
れ、デソーバ6から吸収液ポンプP2により吸収液戻し
管15を介して戻され、散布器5Bから伝熱管5Aの上
に散布される吸収液を冷却し、蒸発器3から供給される
冷媒蒸気を吸収し易くしている。
A heat transfer tube 5A is provided in the interior of the reservoir 5, and the cooling water flowing out from the heat transfer tube 4A to the cooling water tube 17 by performing a cooling action in the absorber 4 flows through the inside of the heat transfer tube 5A. The pump P <b> 2 cools the absorbing liquid returned through the absorbing liquid return pipe 15 and sprayed from the sprayer 5 </ b> B onto the heat transfer pipe 5 </ b> A, thereby facilitating absorption of the refrigerant vapor supplied from the evaporator 3.

【0021】そして、吸収器4の伝熱管4Aとリソーバ
5の伝熱管5Aとを通って冷却作用を果たし、自身の温
度を高めた冷却水が例えば75℃にまで加熱され、利用
温水となって冷却水管17を介して熱負荷に供給される
ようにしてある。
Then, the cooling water passes through the heat transfer tube 4A of the absorber 4 and the heat transfer tube 5A of the reservoir 5 to perform a cooling action, and the cooling water whose own temperature has been increased is heated to, for example, 75 ° C. to be used hot water. The heat load is supplied through a cooling water pipe 17.

【0022】上記構成の本発明の吸収ヒートポンプ装置
においては、凝縮器2で凝縮生成された冷媒液が、デソ
ーバ6から吸収液戻し管15を介してリソーバ5に戻さ
れている温度の高い吸収液により冷媒/吸収液熱交換器
9で加熱されて蒸発器3に供給されるので、蒸発器3に
投入する熱量が少なくて済みCOPの改善が図れる。
In the absorption heat pump apparatus of the present invention having the above-described structure, the refrigerant liquid condensed and generated in the condenser 2 is returned from the desorber 6 to the reservoir 5 through the absorption liquid return pipe 15 to the high-temperature absorption liquid. As a result, the heat is supplied to the evaporator 3 by being heated by the refrigerant / absorbent liquid heat exchanger 9, so that the amount of heat to be supplied to the evaporator 3 is small, and the COP can be improved.

【0023】また、冷媒/吸収液熱交換器9で冷却さ
れ、吸収液戻し管15を通ってリソーバ5に戻されてい
る吸収液により、再生器1で駆動熱源によって加熱さ
れ、冷媒を蒸発分離して吸収液供給管12に吐出した高
温の吸収液は吸収液/吸収液熱交換器10で冷却されて
吸収器4に供給されるので、吸収器4においては冷媒蒸
気が吸収液に速やかに吸収され、これによってもCOP
の改善が図れる。
The regenerator 1 is heated by a driving heat source by the absorbing liquid cooled in the refrigerant / absorbing liquid heat exchanger 9 and returned to the reservoir 5 through the absorbing liquid return pipe 15, thereby evaporating and separating the refrigerant. The high-temperature absorbing liquid discharged to the absorbing liquid supply pipe 12 is cooled by the absorbing liquid / absorbing liquid heat exchanger 10 and supplied to the absorbing member 4. In the absorbing member 4, the refrigerant vapor is quickly converted into the absorbing liquid. Absorbed, this also leads to COP
Can be improved.

【0024】なお、本発明は上記実施形態に限定される
ものではないので、特許請求の範囲に記載の趣旨から逸
脱しない範囲で各種の変形実施が可能である。
Since the present invention is not limited to the above embodiment, various modifications can be made without departing from the spirit of the appended claims.

【0025】例えば、凝縮器2から蒸発器3に至る冷媒
液配管11にスチームトラップを設ける場合には、この
トラップと蒸発器3との間に冷媒/吸収液熱交換器を設
けるようにしても良い。
For example, when a steam trap is provided in the refrigerant liquid pipe 11 from the condenser 2 to the evaporator 3, a refrigerant / absorbent liquid heat exchanger may be provided between the trap and the evaporator 3. good.

【0026】[0026]

【発明の効果】上記したように、本発明によればCOP
の一層の改善が図れる。
As described above, according to the present invention, COP
Can be further improved.

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

【図1】本発明になる吸収ヒートポンプ装置の構成を示
す説明図である。
FIG. 1 is an explanatory diagram showing a configuration of an absorption heat pump device according to the present invention.

【図2】従来技術を示す説明図である。FIG. 2 is an explanatory diagram showing a conventional technique.

【符号の説明】[Explanation of symbols]

1 再生器 1A 伝熱管 1B 散布器 2 凝縮器 2A 伝熱管 3 蒸発器 3A 伝熱管 3B 散布器 4 吸収器 4A 伝熱管 4B 散布器 5 リソーバ 5A 伝熱管 5B 散布器 6 デソーバ 6A 伝熱管 6B 散布器 7・8 熱交換器 9 冷媒/吸収液熱交換器 10 吸収液/吸収液熱交換器 11 冷媒液供給管 11A 液シール部 12 吸収液供給管 13 吸収液戻し管 14 吸収液供給管 15 吸収液戻し管 16 冷媒液管 17 冷却水管 P1・P2 吸収液ポンプ P3 冷媒ポンプ DESCRIPTION OF SYMBOLS 1 Regenerator 1A Heat transfer tube 1B Spreader 2 Condenser 2A Heat transfer tube 3 Evaporator 3A Heat transfer tube 3B Spreader 4 Absorber 4A Heat transfer tube 4B Spreader 5 Resolver 5A Heat transfer tube 5B Spreader 6 Desorber 6A Heat spreader 6A Heat spreader 6A Heat spreader・ 8 Heat exchanger 9 Refrigerant / absorbent liquid heat exchanger 10 Absorbent / absorbent liquid heat exchanger 11 Refrigerant liquid supply pipe 11A Liquid seal part 12 Absorbent liquid supply pipe 13 Absorbent liquid return pipe 14 Absorbent liquid supply pipe 15 Absorbent liquid return Pipe 16 Refrigerant liquid pipe 17 Cooling water pipe P1, P2 Absorbent pump P3 Refrigerant pump

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 吸収液を加熱して吸収液から冷媒を蒸発
分離する再生器と、再生器から供給される冷媒蒸気を冷
却して凝縮させる凝縮器と、凝縮器から供給される冷媒
液を加熱して蒸発させる蒸発器と、冷媒を蒸発分離して
再生器から供給される冷媒の濃度が低下した吸収液に冷
媒を吸収させ、再生器から供給されている吸収液と熱交
換させて再生器に戻す吸収器と、蒸発器から供給される
冷媒蒸気を吸収液に吸収させるリソーバと、冷媒を吸収
してリソーバから供給される冷媒の濃度が上昇した吸収
液を加熱して冷媒を吸収液から蒸発分離し、冷媒の濃度
が低下した吸収液をリソーバから供給されている吸収液
と熱交換させてリソーバに戻すと共に、吸収液から蒸発
分離した冷媒蒸気を吸収器に供給するデソーバとを備え
た吸収ヒートポンプ装置において、凝縮器から蒸発器に
供給されている冷媒液と、デソーバからリソーバに戻さ
れている吸収液とが熱交換する冷媒/吸収液熱交換器を
備えたことを特徴とする吸収ヒートポンプ装置。
1. A regenerator for heating an absorbing liquid to evaporate and separate a refrigerant from an absorbing liquid, a condenser for cooling and condensing a refrigerant vapor supplied from the regenerator, and a refrigerant liquid supplied from the condenser. An evaporator that heats and evaporates and an evaporator that separates the refrigerant by evaporation and absorbs the refrigerant into a reduced concentration of the refrigerant supplied from the regenerator, and exchanges heat with the absorbent supplied from the regenerator for regeneration An absorber that returns to the vessel, a reservoir that absorbs the refrigerant vapor supplied from the evaporator into the absorbing liquid, and an absorbent that absorbs the refrigerant and heats the absorbing liquid in which the concentration of the refrigerant supplied from the reservoir has increased to absorb the refrigerant. And a desorber that supplies heat to the absorbing liquid having a reduced concentration of the refrigerant with the absorbing liquid supplied from the reservoir and returns the absorbing liquid to the absorber, and supplies the refrigerant vapor evaporated and separated from the absorbing liquid to the absorber. Absorption heat pump An absorption heat pump device, comprising: a refrigerant / absorbent heat exchanger for exchanging heat between a refrigerant liquid supplied from a condenser to an evaporator and an absorbing liquid returned from a desorber to a reservoir. .
【請求項2】 吸収液を加熱して吸収液から冷媒を蒸発
分離する再生器と、再生器から供給される冷媒蒸気を冷
却して凝縮させる凝縮器と、凝縮器から供給される冷媒
液を加熱して蒸発させる蒸発器と、冷媒を蒸発分離して
再生器から供給される冷媒の濃度が低下した吸収液に冷
媒を吸収させ、再生器から供給されている吸収液と熱交
換させて再生器に戻す吸収器と、蒸発器から供給される
冷媒蒸気を吸収液に吸収させるリソーバと、冷媒を吸収
してリソーバから供給される冷媒の濃度が上昇した吸収
液を加熱して冷媒を吸収液から蒸発分離し、冷媒の濃度
が低下した吸収液をリソーバから供給されている吸収液
と熱交換させてリソーバに戻すと共に、吸収液から蒸発
分離した冷媒蒸気を吸収器に供給するデソーバとを備え
た吸収ヒートポンプ装置において、再生器から吸収器に
供給されている吸収液と、デソーバからリソーバに戻さ
れている吸収液とが熱交換する吸収液/吸収液熱交換器
を備えたことを特徴とする吸収ヒートポンプ装置。
2. A regenerator for heating an absorption liquid to evaporate and separate a refrigerant from the absorption liquid, a condenser for cooling and condensing refrigerant vapor supplied from the regenerator, and a refrigerant liquid supplied from the condenser. An evaporator that heats and evaporates and an evaporator that separates the refrigerant by evaporation and absorbs the refrigerant into a reduced concentration of the refrigerant supplied from the regenerator, and exchanges heat with the absorbent supplied from the regenerator for regeneration An absorber that returns to the vessel, a reservoir that absorbs the refrigerant vapor supplied from the evaporator into the absorbing liquid, and an absorbent that absorbs the refrigerant and heats the absorbing liquid in which the concentration of the refrigerant supplied from the reservoir has increased to absorb the refrigerant. And a desorber that supplies heat to the absorbing liquid having a reduced concentration of the refrigerant with the absorbing liquid supplied from the reservoir and returns the absorbing liquid to the absorber, and supplies the refrigerant vapor evaporated and separated from the absorbing liquid to the absorber. Absorption heat pump An absorption heat pump, comprising: an absorption liquid / absorption liquid heat exchanger for exchanging heat between an absorption liquid supplied from a regenerator to an absorber and an absorption liquid returned from a desorber to a reservoir. apparatus.
【請求項3】 吸収液を加熱して吸収液から冷媒を蒸発
分離する再生器と、再生器から供給される冷媒蒸気を冷
却して凝縮させる凝縮器と、凝縮器から供給される冷媒
液を加熱して蒸発させる蒸発器と、冷媒を蒸発分離して
再生器から供給される冷媒の濃度が低下した吸収液に冷
媒を吸収させ、再生器から供給されている吸収液と熱交
換させて再生器に戻す吸収器と、蒸発器から供給される
冷媒蒸気を吸収液に吸収させるリソーバと、冷媒を吸収
してリソーバから供給される冷媒の濃度が上昇した吸収
液を加熱して冷媒を吸収液から蒸発分離し、冷媒の濃度
が低下した吸収液をリソーバから供給されている吸収液
と熱交換させてリソーバに戻すと共に、吸収液から蒸発
分離した冷媒蒸気を吸収器に供給するデソーバとを備え
た吸収ヒートポンプ装置において、凝縮器から蒸発器に
供給されている冷媒液とデソーバからリソーバに戻され
ている吸収液とが熱交換する冷媒/吸収液熱交換器と、
再生器から吸収器に供給されている吸収液とデソーバか
らリソーバに戻されている吸収液とが熱交換する吸収液
/吸収液熱交換器とを備えたことを特徴とする吸収ヒー
トポンプ装置。
3. A regenerator for heating the absorbing liquid to evaporate and separate the refrigerant from the absorbing liquid, a condenser for cooling and condensing the refrigerant vapor supplied from the regenerator, and a refrigerant liquid supplied from the condenser. An evaporator that heats and evaporates and an evaporator that separates the refrigerant by evaporation and absorbs the refrigerant into a reduced concentration of the refrigerant supplied from the regenerator, and exchanges heat with the absorbent supplied from the regenerator for regeneration An absorber that returns to the vessel, a reservoir that absorbs the refrigerant vapor supplied from the evaporator into the absorbing liquid, and an absorbent that absorbs the refrigerant and heats the absorbing liquid in which the concentration of the refrigerant supplied from the reservoir has increased to absorb the refrigerant. And a desorber that supplies heat to the absorbing liquid having a reduced concentration of the refrigerant with the absorbing liquid supplied from the reservoir and returns the absorbing liquid to the absorber, and supplies the refrigerant vapor evaporated and separated from the absorbing liquid to the absorber. Absorption heat pump A refrigerant / absorptive liquid heat exchanger in which the refrigerant liquid supplied from the condenser to the evaporator exchanges heat with the absorbing liquid returned from the desorber to the reservoir;
An absorption heat pump device comprising: an absorption liquid / absorption liquid heat exchanger for exchanging heat between an absorption liquid supplied from a regenerator to an absorber and an absorption liquid returned from a desorber to a reservoir.
【請求項4】 冷媒/吸収液熱交換器が、凝縮器から蒸
発器に至る冷媒液管においては下方に屈曲形成された液
シール部に、デソーバからリソーバに至る吸収液戻し管
においてはリソーバからデソーバに供給されている吸収
液とデソーバからリソーバに戻されている吸収液とが熱
交換する熱交換器よりデソーバ側に設置されたことを特
徴とする請求項1または3記載の吸収ヒートポンプ装
置。
4. A refrigerant / absorbent liquid heat exchanger is provided with a liquid seal section bent downward in a refrigerant liquid pipe extending from a condenser to an evaporator, and is provided with a reservoir in an absorbing liquid return pipe extending from a desorber to a reservoir. The absorption heat pump device according to claim 1 or 3, wherein the absorption liquid supplied to the desorber and the absorption liquid returned from the desorber to the reservoir are disposed on the desorber side with respect to a heat exchanger that exchanges heat.
【請求項5】 吸収液/吸収液熱交換器が、再生器から
吸収器に至る冷媒液供給管においては再生器から吸収器
に供給されている吸収液と吸収器から再生器に戻されて
いる吸収液とが熱交換する熱交換器より吸収器側に、デ
ソーバからリソーバに至る吸収液戻し管においてはリソ
ーバからデソーバに供給されている吸収液とデソーバか
らリソーバに戻されている吸収液とが熱交換する熱交換
器よりリソーバ側に設置されたことを特徴とする請求項
2または3記載の吸収ヒートポンプ装置。
5. An absorbing liquid / absorbing liquid heat exchanger is connected to a refrigerant liquid supply pipe extending from a regenerator to an absorber. The absorbing liquid supplied from the regenerator to the absorber and returned from the absorber to the regenerator. On the absorber side from the heat exchanger where the absorbed liquid exchanges heat with the absorber, in the absorbent return pipe from the reservoir to the reservoir, the absorbent supplied from the reservoir to the reservoir and the absorbent returned from the reservoir to the reservoir The absorption heat pump device according to claim 2 or 3, wherein the heat exchanger is disposed closer to the reservoir than the heat exchanger that exchanges heat.
【請求項6】 冷媒/吸収液熱交換器が、凝縮器から蒸
発器に至る冷媒液管においては下方に屈曲形成された液
シール部に、デソーバからリソーバに至る吸収液戻し管
においてはリソーバからデソーバに供給されている吸収
液とデソーバからリソーバに戻されている吸収液とが熱
交換する熱交換器よりデソーバ側に設置され、吸収液/
吸収液熱交換器が、再生器から吸収器に至る冷媒液供給
管においては再生器から吸収器に供給されている吸収液
と吸収器から再生器に戻されている吸収液とが熱交換す
る熱交換器より吸収器側に、デソーバからリソーバに至
る吸収液戻し管においてはリソーバからデソーバに供給
されている吸収液とデソーバからリソーバに戻されてい
る吸収液とが熱交換する熱交換器よりリソーバ側に設置
されたことを特徴とする請求項3記載の吸収ヒートポン
プ装置。
6. A refrigerant / absorbent liquid heat exchanger is provided with a liquid seal section bent downward in a refrigerant liquid pipe extending from a condenser to an evaporator, and is provided with a reservoir in an absorbing liquid return pipe extending from a desorber to a reservoir. The absorption liquid that is supplied to the desorber and the absorption liquid that is returned from the desorber to the reservoir is installed on the desorber side from a heat exchanger that exchanges heat.
In the refrigerant liquid supply pipe from the regenerator to the absorber, the absorbent heat exchanger exchanges heat between the absorbent supplied from the regenerator to the absorber and the absorbent returned from the absorber to the regenerator. On the absorber side from the heat exchanger, in the absorption liquid return pipe from the reservoir to the reservoir, from the heat exchanger where heat is exchanged between the absorption liquid supplied from the reservoir to the reservoir and the absorption liquid returned from the reservoir to the reservoir The absorption heat pump device according to claim 3, wherein the absorption heat pump device is provided on a reservoir side.
JP25476499A 1999-09-08 1999-09-08 Absorption heat pump Pending JP2001082821A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25476499A JP2001082821A (en) 1999-09-08 1999-09-08 Absorption heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25476499A JP2001082821A (en) 1999-09-08 1999-09-08 Absorption heat pump

Publications (1)

Publication Number Publication Date
JP2001082821A true JP2001082821A (en) 2001-03-30

Family

ID=17269566

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25476499A Pending JP2001082821A (en) 1999-09-08 1999-09-08 Absorption heat pump

Country Status (1)

Country Link
JP (1) JP2001082821A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7398656B2 (en) * 2002-09-26 2008-07-15 Ebara Corporation Absorption refrigerating machine
CN101995111A (en) * 2009-11-11 2011-03-30 李华玉 Two-stage first type absorption type heat pump using heat return type single stage as first stage
CN102012128A (en) * 2009-11-11 2011-04-13 李华玉 Two-stage first type absorption heat pump with double effects as first stage
WO2012088650A1 (en) * 2010-12-31 2012-07-05 Li Huayu Regenerative absorbing/generating system and regenerative third-type absorption heat pump
CN102589186A (en) * 2012-02-08 2012-07-18 李华玉 Third type absorption heat pump for fractional condensation
WO2012094775A1 (en) * 2011-01-10 2012-07-19 Li Huayu Regenerative two-stage absorbing-generating system and regenerative third-type absorption heat pump
CN102679612A (en) * 2012-05-14 2012-09-19 李华玉 Fractional condensation third-class absorption type heat pump
WO2013143042A1 (en) * 2012-03-27 2013-10-03 Li Huayu Dual action recuperative absorption-generating system and recuperative type ii absorption heat pump
KR101914487B1 (en) * 2016-12-14 2018-11-05 전북대학교산학협력단 Hybrid system of absorption type refrigeration and heat pupm for supplying cooling and steam simultaneously
CN110220303A (en) * 2019-02-26 2019-09-10 华北电力大学 A kind of low * damage heat exchanger

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7398656B2 (en) * 2002-09-26 2008-07-15 Ebara Corporation Absorption refrigerating machine
US7827821B2 (en) 2002-09-26 2010-11-09 Ebara Corporation Absorption refrigerating machine
CN101995111A (en) * 2009-11-11 2011-03-30 李华玉 Two-stage first type absorption type heat pump using heat return type single stage as first stage
CN102012128A (en) * 2009-11-11 2011-04-13 李华玉 Two-stage first type absorption heat pump with double effects as first stage
WO2012088650A1 (en) * 2010-12-31 2012-07-05 Li Huayu Regenerative absorbing/generating system and regenerative third-type absorption heat pump
WO2012094775A1 (en) * 2011-01-10 2012-07-19 Li Huayu Regenerative two-stage absorbing-generating system and regenerative third-type absorption heat pump
CN102589186A (en) * 2012-02-08 2012-07-18 李华玉 Third type absorption heat pump for fractional condensation
CN102589186B (en) * 2012-02-08 2014-06-25 李华玉 Third type absorption heat pump for fractional condensation
WO2013143042A1 (en) * 2012-03-27 2013-10-03 Li Huayu Dual action recuperative absorption-generating system and recuperative type ii absorption heat pump
CN102679612A (en) * 2012-05-14 2012-09-19 李华玉 Fractional condensation third-class absorption type heat pump
CN102679612B (en) * 2012-05-14 2014-07-30 李华玉 Fractional condensation third-class absorption type heat pump
KR101914487B1 (en) * 2016-12-14 2018-11-05 전북대학교산학협력단 Hybrid system of absorption type refrigeration and heat pupm for supplying cooling and steam simultaneously
CN110220303A (en) * 2019-02-26 2019-09-10 华北电力大学 A kind of low * damage heat exchanger
CN110220303B (en) * 2019-02-26 2024-03-29 华北电力大学 Low exergy -loss heat exchanger

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