JPH06201216A - Absorption / compression hybrid refrigerator - Google Patents

Absorption / compression hybrid refrigerator

Info

Publication number
JPH06201216A
JPH06201216A JP34921492A JP34921492A JPH06201216A JP H06201216 A JPH06201216 A JP H06201216A JP 34921492 A JP34921492 A JP 34921492A JP 34921492 A JP34921492 A JP 34921492A JP H06201216 A JPH06201216 A JP H06201216A
Authority
JP
Japan
Prior art keywords
heat
regenerator
compression
absorption
heat pump
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.)
Withdrawn
Application number
JP34921492A
Other languages
Japanese (ja)
Inventor
Hajime Endo
肇 遠藤
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding 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 Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP34921492A priority Critical patent/JPH06201216A/en
Publication of JPH06201216A publication Critical patent/JPH06201216A/en
Withdrawn legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

(57)【要約】 【目的】 吸収式冷凍機の再生器の加熱源として圧縮式
ヒートポンプを用い、再生器のエネルギー消費を大幅に
削減できる吸収・圧縮ハイブリッド冷凍機を提供する。 【構成】 蒸発器・吸収器・再生器・凝縮器から構成さ
れる吸収式冷凍機において、凝縮器14における凝縮潜
熱を圧縮式ヒートポンプ50の蒸発器11の熱源とし、
圧縮式ヒートポンプ50の熱出力を再生器13の熱源と
して使用する。
(57) [Summary] [Objective] To provide an absorption-compression hybrid refrigerator in which a compression heat pump is used as a heating source of a regenerator of an absorption chiller and the energy consumption of the regenerator can be significantly reduced. In an absorption refrigerator including an evaporator, an absorber, a regenerator, and a condenser, latent heat of condensation in the condenser 14 is used as a heat source of the evaporator 11 of the compression heat pump 50.
The heat output of the compression heat pump 50 is used as the heat source of the regenerator 13.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、吸収式冷凍機の再生器
の加熱源に圧縮式ヒートポンプを用い、再生器のエネル
ギー消費を削減するようにした吸収・圧縮ハイブリッド
冷凍機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption / compression hybrid refrigerator in which a compression heat pump is used as a heating source of a regenerator of an absorption chiller to reduce energy consumption of the regenerator.

【0002】[0002]

【従来の技術】従来、図2に示すように、例えば、リチ
ウムブロマイドの水溶液を使用した吸収式冷凍機があ
る。この吸収式冷凍機の運転は、次のように行われる。
すなわち、 (a) 冷媒としての水wは蒸発器11において管路25
から供給される熱源hと熱交換して蒸発し、これによっ
て熱源hは冷却される。
2. Description of the Related Art Conventionally, as shown in FIG. 2, for example, there is an absorption refrigerator using an aqueous solution of lithium bromide. The operation of this absorption refrigerator is performed as follows.
That is, (a) the water w as a refrigerant is
The heat source h is supplied to the heat source h to evaporate by exchanging heat with the heat source h, whereby the heat source h is cooled.

【0003】(b) 蒸発した蒸気vは吸収器12に導か
れ、管路23から供給されるリチウムブロマイドの濃縮
液sに吸収される。このとき、吸収液は水蒸気潜熱と吸
収熱により昇温するが、管路26から供給される冷却水
Wにより冷却され一定温度を保つ。 (c) 蒸気vを吸収して濃度の低下したリチウムブロマ
イドの希溶液sは管路22からポンプ21により再生器
13に送られる。
(B) The vaporized vapor v is guided to the absorber 12 and absorbed by the concentrated liquid s of lithium bromide supplied from the pipe line 23. At this time, the absorption liquid rises in temperature due to the latent heat of steam and the absorption heat, but is cooled by the cooling water W supplied from the conduit 26 to maintain a constant temperature. (c) The dilute solution s of lithium bromide, which has absorbed vapor v and has a reduced concentration, is sent from the line 22 to the regenerator 13 by the pump 21.

【0004】(d) リチウムブロマイドの希溶液は再生
器において、管路27から供給される加熱蒸気Sにより
加熱・蒸留され、水分のみが蒸発し濃縮 (再生) され、
管路23を経由して再び吸収器12に戻される。 (e) 再生器13において蒸発した水蒸気vは凝縮器1
4において、管路26で供給される冷却水Wにより冷却
され、凝縮し凝縮水wとなる。
(D) In the regenerator, the dilute solution of lithium bromide is heated and distilled by the heating steam S supplied from the pipe 27, only water is evaporated and concentrated (regenerated),
It is returned to the absorber 12 again via the line 23. (e) The water vapor v evaporated in the regenerator 13 is the condenser 1
4, the water is cooled by the cooling water W supplied through the pipe line 26 and condensed to become condensed water w.

【0005】(f) 凝縮水wは管路24を経由して蒸発
器11に還流する。 以上、冷凍機を例として挙げたが、冷却水Wは吸収器1
2及び凝縮器14において温度上昇しており、冷却水の
加熱に注目すればヒートポンプと見做すこともできる。
(F) The condensed water w is returned to the evaporator 11 via the pipe line 24. Although the refrigerator has been described above as an example, the cooling water W is absorbed by the absorber 1
2 and the condenser 14 have risen in temperature, and can be regarded as a heat pump if attention is paid to the heating of the cooling water.

【0006】[0006]

【発明が解決しようとする課題】ところが、上記吸収式
冷凍機は、再生器において希溶液を再生 (濃縮) するた
め蒸留操作を行う際、加熱蒸気が系内に与えた熱は蒸留
された蒸気の形で凝縮器に輸送され、冷却水に放出され
る。ヒートポンプの場合は、この熱を凝縮器において加
熱源として利用されるが、冷凍サイクルの場合は、これ
が全て冷却損失となり冷凍サイクルの成績係数を低下さ
せている。また、ヒートポンプサイクルの場合でも供給
された1次エネルギー (加熱蒸気の熱) は単純に加熱に
使用されるのみであるため全体としての成績係数は低
い。
However, in the absorption refrigerating machine, when the distilling operation is performed in order to regenerate (concentrate) the dilute solution in the regenerator, the heat given to the system by the heating steam is the distilled steam. It is transported to the condenser in the form of and released into the cooling water. In the case of a heat pump, this heat is used as a heating source in the condenser, but in the case of a refrigeration cycle, this all becomes a cooling loss, which lowers the coefficient of performance of the refrigeration cycle. Even in the case of heat pump cycle, the primary energy supplied (heat of heated steam) is simply used for heating, so the overall coefficient of performance is low.

【0007】本発明は、かかる従来の問題を克服するた
めになされたものであり、その目的は、吸収式冷凍機の
再生器の加熱源として圧縮式ヒートポンプを用い、再生
器のエネルギー消費を大幅に削減できる吸収・圧縮ハイ
ブリッド冷凍機を提供することにある。
The present invention has been made in order to overcome such a conventional problem, and an object thereof is to use a compression heat pump as a heating source of a regenerator of an absorption chiller, thereby significantly reducing energy consumption of the regenerator. It is to provide an absorption / compression hybrid refrigerator that can be reduced to

【0008】[0008]

【課題を解決するための手段】上記目的を達成し得る本
発明の吸収・圧縮ハイブリッド冷凍機は、蒸発器・吸収
器・再生器・凝縮器から構成される吸収式冷凍機におい
て、凝縮器における凝縮潜熱を圧縮式ヒートポンプの蒸
発器の熱源とし、該圧縮式ヒートポンプの熱出力を再生
器の熱源として使用することを特徴とするものである。
The absorption / compression hybrid refrigerator of the present invention which can achieve the above object is an absorption refrigerator comprising an evaporator, an absorber, a regenerator, and a condenser. The present invention is characterized in that latent heat of condensation is used as a heat source of an evaporator of a compression heat pump, and heat output of the compression heat pump is used as a heat source of a regenerator.

【0009】このように凝縮器における凝縮潜熱を圧縮
式ヒートポンプの蒸発器の熱源とし、該圧縮式ヒートポ
ンプの熱出力を再生器の熱源として使用することによ
り、再生器のエネルギー消費を大幅に削減できる。
By using the latent heat of condensation in the condenser as the heat source of the evaporator of the compression heat pump and using the heat output of the compression heat pump as the heat source of the regenerator, the energy consumption of the regenerator can be greatly reduced. .

【0010】[0010]

【実施例】以下、図面により本発明の実施例を説明す
る。図1に示すように、本発明は、凝縮器14で冷媒で
ある水蒸気vが放出する熱を熱源とし、圧縮式ヒートポ
ンプ50により昇温し、該圧縮式ヒートポンプ50の熱
出力を再生器13の熱源として利用するようになってい
る。
Embodiments of the present invention will be described below with reference to the drawings. As shown in FIG. 1, according to the present invention, the heat released by the steam v as a refrigerant in the condenser 14 is used as a heat source, the temperature is raised by the compression heat pump 50, and the heat output of the compression heat pump 50 is supplied to the regenerator 13. It is designed to be used as a heat source.

【0011】即ち、再生器13においてリチウムブロマ
イドの希溶液sから蒸発した水蒸気vを、凝縮器14内
の熱交換部4において冷却・凝縮させる際に回収される
熱を熱源として、圧縮ヒートポンプ50の熱媒体 (ここ
ではフロン22を前提として説明する。以下、F22と
記す) 液を蒸発させる。即ち、凝縮器14内の熱交換部
4は圧縮式ヒートポンプ50の蒸発器とみなされる。こ
の熱媒体 (F22) の蒸気は圧縮機1により圧縮され、
再生器13に導かれる。再生器13の熱交換部2で圧縮
式ヒートポンプ50の熱媒体 (F22) の蒸気は、吸収
式ヒートポンプ50の希薄溶液sと熱交換し凝縮する。
即ち、熱交換部2は圧縮式ヒートポンプ50の凝縮器に
相当する。この熱交換によりリチウムブロマイドの希薄
溶液sが蒸発し濃縮される。濃縮したリチウムブロマイ
ドの溶液sは管路23より吸収器12に還流する。一
方、熱交換器3で凝縮したF22の液は管路7より膨張
弁3を経由して凝縮器14内の圧縮式ヒートポンプ50
の熱交換部4に還流する。
That is, the steam v evaporated from the dilute lithium bromide solution s in the regenerator 13 is recovered by the heat exchange section 4 in the condenser 14 when it is cooled and condensed. Heat medium (here, description will be made on the assumption of Freon 22. Hereinafter, referred to as F22) Liquid is evaporated. That is, the heat exchange section 4 in the condenser 14 is regarded as an evaporator of the compression heat pump 50. This heat medium (F22) vapor is compressed by the compressor 1,
It is guided to the regenerator 13. In the heat exchange section 2 of the regenerator 13, the vapor of the heat medium (F22) of the compression heat pump 50 exchanges heat with the dilute solution s of the absorption heat pump 50 and is condensed.
That is, the heat exchange unit 2 corresponds to the condenser of the compression heat pump 50. Due to this heat exchange, the dilute solution of lithium bromide s is evaporated and concentrated. The concentrated lithium bromide solution s is returned to the absorber 12 through the pipe line 23. On the other hand, the liquid of F22 condensed in the heat exchanger 3 passes through the expansion valve 3 from the pipe 7 and the compression heat pump 50 in the condenser 14
Reflux to the heat exchange section 4.

【0012】ここで、符号5,6,7は圧縮式ヒートポ
ンプ50の配管である。また、蒸発器11や吸収器12
等については、従来例と変更がないので説明を省略する
こととする。
Reference numerals 5, 6, and 7 are pipes of the compression heat pump 50. In addition, the evaporator 11 and the absorber 12
Since there is no change from the conventional example, the description will be omitted.

【0013】[0013]

【発明の効果】上記のように、本発明によれば、吸収式
冷凍機 (ヒートポンプ) の再生器において使用される従
来の加熱装置が不要になり、再生に必要な外部エネルギ
ーは圧縮器ヒートポンプの駆動動力のみとなる。そのた
め、吸収式冷凍機の成績係数が大幅に上昇する。例え
ば、圧縮式ヒートポンプの成績係数が10とすると、圧
縮式ヒートポンプの駆動動力は吸収式冷凍機の冷凍容量
の約1/10の動力で冷凍が可能となる。即ち、吸収式
冷凍機の成績係数は殆ど圧縮式ヒートポンプの成績係数
と同一となる。
As described above, according to the present invention, the conventional heating device used in the regenerator of the absorption refrigerator (heat pump) is unnecessary, and the external energy required for the regeneration is the compressor heat pump. Only drive power. Therefore, the coefficient of performance of the absorption refrigerator is significantly increased. For example, if the coefficient of performance of the compression heat pump is 10, the driving power of the compression heat pump can be frozen with about 1/10 of the refrigeration capacity of the absorption refrigerator. That is, the coefficient of performance of the absorption refrigerator is almost the same as that of the compression heat pump.

【0014】なお、圧縮式ヒートポンプを直接冷凍機と
した場合は、その成績係数は冷却水の温度と冷凍温度と
の温度差に規定され一般に3〜4程度であるが、本方式
だと再生器と凝縮器の温度差は小さく、そのため圧縮式
ヒートポンプの成績係数は数倍となり、本例のごとく成
績係数10程度も容易に達成される。
When the compression type heat pump is directly used as a refrigerator, the coefficient of performance thereof is regulated by the temperature difference between the cooling water temperature and the freezing temperature and is generally about 3 to 4. However, with this method, the regenerator is used. The temperature difference between the condenser and the condenser is small, so that the coefficient of performance of the compression heat pump is several times higher, and a coefficient of performance of about 10 is easily achieved as in this example.

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

【図1】本発明に係る吸収・圧縮ハイブリッド冷凍機の
概念図である。
FIG. 1 is a conceptual diagram of an absorption / compression hybrid refrigerator according to the present invention.

【図2】従来の吸収式冷凍機の概念図である。FIG. 2 is a conceptual diagram of a conventional absorption refrigerator.

【符号の説明】[Explanation of symbols]

11 蒸発器 12 吸収器 13 再生器 14 凝縮器 50 圧縮式ヒートポンプ 11 Evaporator 12 Absorber 13 Regenerator 14 Condenser 50 Compression heat pump

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 蒸発器・吸収器・再生器・凝縮器から構
成される吸収式冷凍機において、凝縮器における凝縮潜
熱を圧縮式ヒートポンプの蒸発器の熱源とし、該圧縮式
ヒートポンプの熱出力を再生器の熱源として使用するこ
とを特徴とする吸収・圧縮ハイブリッド冷凍機。
1. In an absorption refrigerator comprising an evaporator, an absorber, a regenerator, and a condenser, latent heat of condensation in the condenser is used as a heat source of the evaporator of the compression heat pump, and the heat output of the compression heat pump is used. An absorption / compression hybrid refrigerator characterized by being used as a heat source for a regenerator.
JP34921492A 1992-12-28 1992-12-28 Absorption / compression hybrid refrigerator Withdrawn JPH06201216A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34921492A JPH06201216A (en) 1992-12-28 1992-12-28 Absorption / compression hybrid refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34921492A JPH06201216A (en) 1992-12-28 1992-12-28 Absorption / compression hybrid refrigerator

Publications (1)

Publication Number Publication Date
JPH06201216A true JPH06201216A (en) 1994-07-19

Family

ID=18402255

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34921492A Withdrawn JPH06201216A (en) 1992-12-28 1992-12-28 Absorption / compression hybrid refrigerator

Country Status (1)

Country Link
JP (1) JPH06201216A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110214435A1 (en) * 2008-11-17 2011-09-08 Beijing Lianliyuan Technology Co., Ltd. Heat pump cycle system and method of providing combined cooling and heating supply

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110214435A1 (en) * 2008-11-17 2011-09-08 Beijing Lianliyuan Technology Co., Ltd. Heat pump cycle system and method of providing combined cooling and heating supply

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Effective date: 20000307