[go: up one dir, main page]

JP2010243085A - Refrigeration equipment - Google Patents

Refrigeration equipment Download PDF

Info

Publication number
JP2010243085A
JP2010243085A JP2009093124A JP2009093124A JP2010243085A JP 2010243085 A JP2010243085 A JP 2010243085A JP 2009093124 A JP2009093124 A JP 2009093124A JP 2009093124 A JP2009093124 A JP 2009093124A JP 2010243085 A JP2010243085 A JP 2010243085A
Authority
JP
Japan
Prior art keywords
vapor compression
refrigerant
refrigerator
solenoid valve
solution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2009093124A
Other languages
Japanese (ja)
Other versions
JP5434208B2 (en
Inventor
Mitsushi Kawai
満嗣 河合
Keisuke Tanimoto
啓介 谷本
Tadashi Nishimura
忠史 西村
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.)
Daikin Industries Ltd
Original Assignee
Daikin Industries 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 Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP2009093124A priority Critical patent/JP5434208B2/en
Publication of JP2010243085A publication Critical patent/JP2010243085A/en
Application granted granted Critical
Publication of JP5434208B2 publication Critical patent/JP5434208B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

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

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

【課題】蒸気圧縮式冷凍機と吸収式冷凍機を組合せて構成される冷凍装置において、冷房運転時と暖房運転時の双方において性能改善効果を得る。
【解決手段】蒸気圧縮式冷凍機Xと吸収式冷凍機Yとを備えた冷凍装置において、
吸収式冷凍機Yの吸収器12に流入する溶液を過冷却熱交換器15で過冷却して吸収器12へ流入させる一方、蒸気圧縮式冷凍機Xの冷媒と吸収式冷凍機Yの発生器11内の溶液との間で熱交換可能に構成するとともに、蒸気圧縮式冷凍機Xの冷媒回路に、発生器11をバイパスして吸収式冷凍機Yの蒸発器13に接続されるバイパス路75を設け、ここに電磁弁45を備える。そして、この、電磁弁45を、蒸気圧縮式冷凍機Xの冷房運転時で且つ上記バイパス路75の入口の冷媒の温度が設定温度未満である場合に開弁することで冷媒の過度の温度低下が防止され、設定温度以上の場合に閉弁することで蒸気圧縮式冷凍機Xの冷媒排熱が発生器11の駆動熱源に利用できる。
【選択図】図1
In a refrigeration apparatus configured by combining a vapor compression refrigeration machine and an absorption refrigeration machine, a performance improvement effect is obtained both during cooling operation and during heating operation.
In a refrigeration apparatus including a vapor compression refrigerator X and an absorption refrigerator Y,
While the solution flowing into the absorber 12 of the absorption refrigerator Y is supercooled by the supercooling heat exchanger 15 and flows into the absorber 12, the refrigerant of the vapor compression refrigerator X and the generator of the absorption refrigerator Y 11 is configured to be capable of exchanging heat with the solution in 11, and to the refrigerant circuit of the vapor compression refrigeration machine X, bypass the generator 11 and connected to the evaporator 13 of the absorption refrigeration machine Y. And an electromagnetic valve 45 is provided here. The solenoid valve 45 is opened when the vapor compression refrigerator X is in the cooling operation and when the temperature of the refrigerant at the inlet of the bypass passage 75 is lower than the set temperature, thereby excessively reducing the temperature of the refrigerant. The refrigerant exhaust heat of the vapor compression refrigeration machine X can be used as a drive heat source for the generator 11 by closing the valve when the temperature is equal to or higher than the set temperature.
[Selection] Figure 1

Description

本願発明は、蒸気圧縮式冷凍機に吸収式冷凍機を組み合わせて構成される冷凍装置に関するものである。   The present invention relates to a refrigeration apparatus configured by combining a vapor compression refrigerator and an absorption refrigerator.

蒸気圧縮式冷凍機においてその性能を改善する手法の一つとして、該蒸気圧縮式冷凍機に吸収式冷凍機を組合せ、該吸収式冷凍機をガスエンジンやその他の排熱を熱源として駆動し、ここで得られる冷熱によって上記蒸気圧縮式冷凍機の冷媒を過冷却する方法や、得られる冷熱によって蒸気圧縮式冷凍機の圧縮後の冷媒を冷却することによって該冷媒の凝縮温度を低下させてその性能を改善するようにした冷凍装置が知られている(例えば、特許文献1参照)。   As one of the methods for improving the performance of the vapor compression refrigerator, an absorption refrigerator is combined with the vapor compression refrigerator, the absorption refrigerator is driven using a gas engine or other exhaust heat as a heat source, A method of supercooling the refrigerant of the vapor compression refrigeration machine using the cold heat obtained here, or a method of reducing the condensation temperature of the refrigerant by cooling the refrigerant after compression of the vapor compression refrigeration machine using the obtained cold heat. A refrigeration apparatus that improves performance is known (see, for example, Patent Document 1).

また、蒸気圧縮式冷凍機に吸収式冷凍機を組合せてなる冷凍装置において、特許文献1に示される冷凍装置よりもさらに性能向上を図る手法として、吸収式冷凍機の駆動熱源として、ガスエンジンやその他の排熱に加えて、蒸気圧縮式冷凍機の排熱を利用する技術も提案されている(特許文献2参照)。   Further, in a refrigeration apparatus in which an absorption refrigeration machine is combined with a vapor compression refrigeration machine, as a method for further improving the performance as compared with the refrigeration apparatus disclosed in Patent Document 1, In addition to other waste heat, a technology that utilizes waste heat of a vapor compression refrigerator has also been proposed (see Patent Document 2).

特開2004−28374号公報JP 2004-28374 A 特開2006−17350号公報JP 2006-17350 A

しかし、特許文献2に示される技術では、蒸気圧縮式冷凍機の排熱量が少なく且つ排熱温度も低いことから、この排熱を吸収式冷凍機の駆動熱源として利用したとしてもその効果が限定され、大きくないこと、上記排熱を利用するための吸収式冷凍機を組み合せる等に多大な費用がかかる等コスト面での課題より、実用性は限定されたものであると言える。   However, in the technique shown in Patent Document 2, since the exhaust heat amount of the vapor compression refrigerator is small and the exhaust heat temperature is also low, even if this exhaust heat is used as a drive heat source for the absorption refrigerator, its effect is limited. However, it can be said that the practicality is limited because it is not large and it takes a lot of cost to combine the absorption refrigerator for using the exhaust heat.

このような特許文献2に示される冷凍装置については、該冷凍装置では冷房運転時における性能向上のみに着目し、暖房運転時における性能向上を考慮していない点にも一因があり、冷房運転時と暖房運転時の双方において性能改善が図れるならば、トータル的にみて、その実用性は高まるものと考えられる。   With regard to the refrigeration apparatus shown in Patent Document 2, the refrigeration apparatus focuses only on the performance improvement during the cooling operation, and is also due to the fact that the performance improvement during the heating operation is not considered. If the performance can be improved both at the time and during the heating operation, it is considered that the practicality will increase as a whole.

そこで、蒸気圧縮式冷凍機と吸収式冷凍機を組み合せるに関しては、基本構成は、特許文献2に記載の冷凍装置に類似するものであるが、特許文献2に記載の吸収式冷凍機は水冷方式であるが、吸収式冷凍機は空冷方式を基本構成とし、これに四路切換弁を設けて冷房運転及び暖房運転が可能に構成した冷凍装置を従来方式として想定し、その一例として、図6にその回路図を示している。   Therefore, regarding the combination of the vapor compression refrigerator and the absorption refrigerator, the basic configuration is similar to the refrigeration apparatus described in Patent Document 2, but the absorption refrigerator described in Patent Document 2 is water-cooled. Although the absorption chiller is based on an air cooling system, a four-way switching valve is provided on the absorption chiller so that cooling and heating operations are possible as a conventional system. The circuit diagram is shown in FIG.

図6において、符号Xは蒸気圧縮式冷凍機、Yは吸収式冷凍機である。上記蒸気圧縮式冷凍機Xは、圧縮機1と四路切換弁2と利用側熱交換器3と膨張弁4と熱源側熱交換器7及びアキュームレーター5を備えて構成される。また、上記吸収式冷凍機Yは、発生器11と吸収器12と蒸発器13と凝縮器14と過冷却熱交換器15と溶液熱交換器16及び溶液ポンプ17を備えて構成される。   In FIG. 6, symbol X is a vapor compression refrigerator, and Y is an absorption refrigerator. The vapor compression refrigerator X includes a compressor 1, a four-way switching valve 2, a use side heat exchanger 3, an expansion valve 4, a heat source side heat exchanger 7, and an accumulator 5. The absorption refrigerator Y includes a generator 11, an absorber 12, an evaporator 13, a condenser 14, a supercooling heat exchanger 15, a solution heat exchanger 16, and a solution pump 17.

そして、この冷凍装置では、吸収式冷凍機Yの蒸発器13において上記蒸気圧縮式冷凍機Xの冷媒を過冷却するために、上記利用側熱交換器3と熱源側熱交換器7の間の管路54を上記吸収式冷凍機Yの上記蒸発器13の熱交換器13aに接続するとともに、上記蒸気圧縮式冷凍機X側の冷媒の排熱を上記吸収式冷凍機Yの発生器11においてその駆動熱源として利用するために該蒸気圧縮式冷凍機Xの上記熱源側熱交換器7と上記四路切換弁2の間の管路58を上記発生器11内に配置された熱交換器11bに接続している。   In this refrigeration apparatus, in order to supercool the refrigerant of the vapor compression refrigeration machine X in the evaporator 13 of the absorption refrigeration machine Y, between the use side heat exchanger 3 and the heat source side heat exchanger 7, The pipe 54 is connected to the heat exchanger 13a of the evaporator 13 of the absorption refrigeration machine Y, and the exhaust heat of the refrigerant on the vapor compression refrigeration machine X side is connected to the generator 11 of the absorption refrigeration machine Y. In order to use it as a driving heat source, a heat exchanger 11b in which a pipe line 58 between the heat source side heat exchanger 7 and the four-way switching valve 2 of the vapor compression refrigerator X is disposed in the generator 11 is used. Connected to.

係る構成とすることで、上記蒸気圧縮式冷凍機Xの冷房運転時には、上記圧縮機1で圧縮された後の冷媒が上記発生器11に導入され、ここで該発生器11内の溶液との間での熱交換によって上記蒸気圧縮式冷凍機Xの冷媒熱が該溶液側に回収され、該発生器11の駆動熱源として利用される。また、上記熱源側熱交換器7を出た冷媒は、上記蒸発器13に流入しここで冷却、または過冷却され冷媒温度が低下することで、上記利用側熱交換器3における冷媒の入口の比エンタルピーが低下し、上記利用側熱交換器3の冷房能力が向上する。即ち冷房運転時においては、蒸気圧縮式冷凍機Xに吸収式冷凍機Yを組み合わせた構成による本来的な目的が達せられる。   With this configuration, during the cooling operation of the vapor compression refrigeration machine X, the refrigerant compressed by the compressor 1 is introduced into the generator 11, where the refrigerant in the generator 11 The refrigerant heat of the vapor compression refrigerator X is recovered to the solution side by heat exchange between them, and is used as a driving heat source for the generator 11. In addition, the refrigerant that has exited the heat source side heat exchanger 7 flows into the evaporator 13 and is cooled or supercooled here, so that the refrigerant temperature decreases, so that the refrigerant inlet of the usage side heat exchanger 3 is reduced. The specific enthalpy is reduced and the cooling capacity of the use side heat exchanger 3 is improved. That is, during the cooling operation, the original purpose can be achieved by the configuration in which the vapor compression refrigerator X and the absorption refrigerator Y are combined.

一方、暖房運転時には、上記四路切換弁2を切換え、蒸気圧縮式冷凍機Xの冷媒を冷房運転とは逆方向に流入させるが、上記圧縮機1で圧縮された後の冷媒が上記利用側熱交換器3で熱交換され、上記吸収式冷凍機Yの蒸発器13内の熱交換器13aから管路54を経て、発生器11に流入する。上記吸収式冷凍機Yの凝縮器14及び過冷却熱交換器15の運転を停止し、上記管路60から供給されるガスエンジンやその他の排熱によって駆動される発生器11内の溶液から、上記発生器11内の蒸気圧縮式冷凍機Xの冷媒が吸熱し、4路切換弁2を経て圧縮機1に戻る。この場合に、蒸気圧縮式のサイクルを形成するためには発生器11内の熱交換器11bを、上記溶液ポンプ17によって循環させたとしても、該発生器11内の蒸気圧縮式冷凍機Xの冷媒が吸熱するための熱容量は、冷房運転時の蒸気圧縮式冷凍機Xの冷媒が発生器11で回収される熱量よりも遥かに大きく、且つ該発生器11内に上記熱交換器11bが配置されていることから、該熱交換器11bを介して行なわれる該発生器11内の溶液と上記蒸気圧縮式冷凍機X側の冷媒との間における熱交換効率は低いために、溶液温度によって冷媒を加熱して該冷媒の蒸発温度を高める効果は少なく、結果的に、蒸気圧縮式冷凍機Xの性能向上に寄与するところは少ないものとなる。また、十分にその効果を得ようと、発生器11内の熱交換器11bを大きくした場合は、その効果に見合う発生器11や熱交換器11bのコスト高より実用的ではない。   On the other hand, during the heating operation, the four-way switching valve 2 is switched and the refrigerant of the vapor compression refrigeration machine X flows in the opposite direction to the cooling operation, but the refrigerant after being compressed by the compressor 1 is used on the usage side. Heat is exchanged in the heat exchanger 3 and flows into the generator 11 from the heat exchanger 13a in the evaporator 13 of the absorption refrigeration machine Y through the pipe line 54. The operation of the condenser 14 and the supercooling heat exchanger 15 of the absorption refrigerator Y is stopped, and from the solution in the generator 11 driven by the gas engine or other exhaust heat supplied from the pipe 60, The refrigerant of the vapor compression refrigerator X in the generator 11 absorbs heat and returns to the compressor 1 through the four-way switching valve 2. In this case, in order to form a vapor compression cycle, even if the heat exchanger 11b in the generator 11 is circulated by the solution pump 17, the vapor compression refrigerator X in the generator 11 is The heat capacity for absorbing the heat of the refrigerant is much larger than the amount of heat collected by the generator 11 in the vapor compression refrigerator X during the cooling operation, and the heat exchanger 11b is disposed in the generator 11. Therefore, since the heat exchange efficiency between the solution in the generator 11 and the refrigerant on the vapor compression refrigerator X side performed via the heat exchanger 11b is low, the refrigerant depends on the solution temperature. The effect of increasing the evaporation temperature of the refrigerant by heating the refrigerant is small, and as a result, there are few places that contribute to improving the performance of the vapor compression refrigerator X. Moreover, when the heat exchanger 11b in the generator 11 is enlarged so as to obtain the effect sufficiently, it is not practical because of the high cost of the generator 11 and the heat exchanger 11b corresponding to the effect.

このように、特許文献2に示されるように蒸気圧縮式冷凍機と吸収式冷凍機を組合せて冷凍装置において、冷房運転及び暖房運転が可能となるように図6の如く構成したとしても、冷房運転時と暖房運転時の双方において、特に暖房運転時は、大きな性能改善効果を期待することはできず、従って、依然として実用性に乏しいものとならざるを得ない。   In this way, even if the refrigeration apparatus is configured as shown in FIG. 6 so that the cooling operation and the heating operation can be performed by combining the vapor compression refrigerator and the absorption refrigerator as shown in Patent Document 2, In both the operation and the heating operation, particularly during the heating operation, a great performance improvement effect cannot be expected, and thus the practicality is still poor.

ところが、近年のエネルギーコストの上昇とか、自然冷媒を利用した空気調和機の開発の進行等を背景に、蒸気圧縮式冷凍機の性能改善と該蒸気圧縮式冷凍機の排熱利用の促進という課題が再注目され、ガスエンジンやその他の排熱を利用するに止まらず、蒸気圧縮式冷凍機の排熱も利用して冷熱に変換して冷房運転時の性能向上を図ると同時に、暖房運転時においても蒸気圧縮式冷凍機の排熱を有効に利用してさらなる性能改善を図る技術の開発が要請されるに至った。   However, against the background of rising energy costs in recent years and the progress of development of air conditioners using natural refrigerants, there are issues of improving the performance of steam compression refrigerators and promoting the use of waste heat from the steam compression refrigerators However, not only does it take advantage of exhaust heat from gas engines and other wastewater, but it also uses the exhaust heat from the vapor compression refrigeration machine to convert it into cold heat to improve the performance during cooling operation and at the same time during heating operation. In Japan, the development of technology to further improve performance by effectively using the exhaust heat of the vapor compression refrigerator has been requested.

そこで本願発明は、蒸気圧縮式冷凍機と吸収式冷凍機を組合せて構成される冷凍装置において、冷房運転時と暖房運転時の双方において性能改善効果を得ることを主たる目的としてなされたものである。   Therefore, the present invention is mainly intended to obtain a performance improvement effect in both the cooling operation and the heating operation in the refrigeration apparatus configured by combining the vapor compression refrigerator and the absorption refrigerator. .

本願発明ではかかる課題を解決するための具体的手段として次のような構成を採用している。   In the present invention, the following configuration is adopted as a specific means for solving such a problem.

本願の第1の発明では、蒸気圧縮式冷凍機Xとエンジン等の排熱で駆動される吸収式冷凍機Yとを備えて構成される冷凍装置において、上記吸収式冷凍機Yの吸収器12に流入する溶液を空冷式の過冷却熱交換器15によって過冷却して上記吸収器12へ流入させるとともに、上記蒸気圧縮式冷凍機Xの冷媒と上記吸収式冷凍機Yの発生器11内の溶液との間で熱交換可能に構成する一方、上記蒸気圧縮式冷凍機Xの冷媒回路に、上記吸収式冷凍機Yの上記発生器11をバイパスして該吸収式冷凍機Yの上記蒸発器13に接続されるバイパス路75を設けるとともに該バイパス路75に電磁弁45を備え、上記蒸気圧縮式冷凍機Xの冷房運転時で且つ該バイパス路75の入口の上記蒸気圧縮式冷凍機Xの冷媒の温度が設定温度未満である場合には上記電磁弁45を開弁し、冷媒の温度が設定温度以上である場合には上記電磁弁45を閉弁する一方、上記蒸気圧縮式冷凍機Xの暖房運転時には上記電磁弁45を閉弁することを特徴としている。   In the first invention of the present application, in the refrigerating apparatus including the vapor compression refrigerator X and the absorption refrigerator Y driven by exhaust heat from the engine or the like, the absorber 12 of the absorption refrigerator Y described above. The solution flowing into the refrigerant is supercooled by the air-cooled supercooling heat exchanger 15 and flows into the absorber 12, and the refrigerant in the vapor compression refrigerator X and the generator 11 of the absorption refrigerator Y are contained in the absorber 11. While being configured to be able to exchange heat with the solution, the evaporator of the absorption refrigerator Y is bypassed in the refrigerant circuit of the vapor compression refrigerator X by bypassing the generator 11 of the absorption refrigerator Y. 13 is provided with a bypass path 75 and an electromagnetic valve 45 in the bypass path 75, and the vapor compression refrigeration machine X of the vapor compression refrigeration machine X at the inlet of the bypass path 75 is in the cooling operation of the vapor compression refrigeration machine X. When the refrigerant temperature is lower than the set temperature Opens the solenoid valve 45 and closes the solenoid valve 45 when the temperature of the refrigerant is equal to or higher than a set temperature, while closing the solenoid valve 45 during the heating operation of the vapor compression refrigerator X. It is characterized by doing.

本願の第2の発明では、上記第1の発明に係る冷凍装置において、上記吸収式冷凍機Yの上記吸収器12の出口から溶液ポンプ17を経て溶液熱交換器16に至る管路67に電磁弁41を設けるとともに、上記吸収式冷凍機Yの上記吸収器12の入口側の管路66と上記蒸発器13の冷媒入口側の管路62を、第3電磁弁43を備えた管路76によって接続し、上記蒸気圧縮式冷凍機Xの冷房運転時には上記電磁弁45は上記蒸気圧縮式冷凍機Xの上記バイパス路75の入口の冷媒温度の設定温度により開閉されるが、上記電磁弁43を閉弁し、上記電磁弁41を開弁する一方、上記蒸気圧縮式冷凍機Xの暖房運転時には上記電磁弁43を開弁し、上記電磁弁41と電磁弁45を閉弁するように構成したことを特徴としている。   According to a second invention of the present application, in the refrigeration apparatus according to the first invention, an electromagnetic wave is connected to a pipe line 67 from the outlet of the absorber 12 of the absorption refrigerator Y to the solution heat exchanger 16 via the solution pump 17. A valve 41 is provided, and a pipe 66 on the inlet side of the absorber 12 of the absorption refrigerator Y and a pipe 62 on the refrigerant inlet side of the evaporator 13 are connected to a pipe 76 provided with a third electromagnetic valve 43. In the cooling operation of the vapor compression refrigeration machine X, the electromagnetic valve 45 is opened and closed by the set temperature of the refrigerant temperature at the inlet of the bypass passage 75 of the vapor compression refrigeration machine X. Is closed and the solenoid valve 41 is opened, while the steam compression refrigerator X is in a heating operation, the solenoid valve 43 is opened, and the solenoid valve 41 and the solenoid valve 45 are closed. It is characterized by that.

本願の第3の発明では、上記第1の発明に係る冷凍装置において、上記吸収式冷凍機Yの上記吸収器12の出口から溶液ポンプ17を経て溶液熱交換器16に至る管路67に電磁弁41を設けるとともに、上記吸収式冷凍機Yの上記吸収器12の入口側の管路66を、第3電磁弁43を備えた管路77を介して上記蒸発器13に接続し、上記蒸気圧縮式冷凍機Xの冷房運転時には上記第1電磁弁41は上記蒸気圧縮式冷凍機Xの上記バイパス路75の入口の冷媒温度の設定温度により開閉されるが、上記電動弁43を閉弁し、上記電磁弁41を開弁する一方、上記蒸気圧縮式冷凍機Xの暖房運転時には上記電磁弁43を開弁し、上記電磁弁41と電磁弁45を閉弁するように構成したことを特徴としている。   According to a third invention of the present application, in the refrigeration apparatus according to the first invention, the pipe 67 extending from the outlet of the absorber 12 of the absorption refrigerator Y to the solution heat exchanger 16 via the solution pump 17 is electromagnetically connected. A valve 41 is provided, and a pipe 66 on the inlet side of the absorber 12 of the absorption refrigeration machine Y is connected to the evaporator 13 via a pipe 77 having a third electromagnetic valve 43, and the steam During the cooling operation of the compression refrigeration machine X, the first electromagnetic valve 41 is opened and closed by the set temperature of the refrigerant temperature at the inlet of the bypass passage 75 of the vapor compression refrigeration machine X, but the motor operated valve 43 is closed. The solenoid valve 41 is opened, while the vapor compression refrigerator X is in a heating operation, the solenoid valve 43 is opened, and the solenoid valve 41 and the solenoid valve 45 are closed. It is said.

本願の第4の発明では、上記第2又は第3の発明に係る冷凍装置において、上記吸収式冷凍機Yの上記吸収器12の入口側の管路66に電磁弁44を設け、上記蒸気圧縮式冷凍機Xの冷房運転時には上記電磁弁44を開弁し、暖房運転時には上記電磁弁44を閉弁するように構成したことを特徴としている。   According to a fourth invention of the present application, in the refrigeration apparatus according to the second or third invention, an electromagnetic valve 44 is provided in a pipe 66 on the inlet side of the absorber 12 of the absorption refrigerator Y, and the vapor compression is performed. The electromagnetic valve 44 is opened during the cooling operation of the refrigerator-type refrigerator X, and the electromagnetic valve 44 is closed during the heating operation.

本願の第5の発明では、上記第1、第2、第3又は第4の発明に係る冷凍装置において、上記発生器11の排熱入口側の管路60に電磁弁46を設け、冷房運転時には上記電磁弁46を開弁する一方、暖房運転時には上記発生器11の溶液温度が設定温度以上のとき上記電磁弁46を閉弁し、該設定温度未満のとき上記電磁弁46を開弁させるように構成したことを特徴としている。   According to a fifth invention of the present application, in the refrigeration apparatus according to the first, second, third, or fourth invention, an electromagnetic valve 46 is provided in the pipe line 60 on the exhaust heat inlet side of the generator 11 for cooling operation. The solenoid valve 46 is sometimes opened, while the solenoid valve 46 is closed when the solution temperature of the generator 11 is equal to or higher than a set temperature during heating operation, and the solenoid valve 46 is opened when the temperature is lower than the set temperature. It is characterized by being configured as described above.

本願の第6の発明では、上記第3又は第4の発明に係る冷凍装置において、上記蒸発器13における溶液散布用の散布器と冷媒液散布用の散布器を、別体構成又は共用可能な一体構成としたことを特徴としている。   In the sixth invention of the present application, in the refrigeration apparatus according to the third or fourth invention, the sprayer for spraying the solution and the sprayer for spraying the refrigerant liquid in the evaporator 13 can be configured separately or shared. It is characterized by having an integrated structure.

本願の第7の発明では、上記第1、第2、第3、第4、第5又は第6の発明に係る冷凍装置において、上記蒸発器13を、冷媒液が一過性で該蒸発器13の伝熱面を流れ、未蒸発の冷媒液は上記吸収器12側へ移動して該吸収器12側の溶液に吸収されるように構成したことを特徴としている。   According to a seventh invention of the present application, in the refrigeration apparatus according to the first, second, third, fourth, fifth or sixth invention, the evaporator 13 is provided with a transient refrigerant liquid. The refrigerant liquid which flows through the heat transfer surface 13 and has not evaporated yet moves to the absorber 12 side and is absorbed by the solution on the absorber 12 side.

本願の第8の発明では、上記第1、第2、第3、第4、第5、第6又は第7の発明に係る冷凍装置において、上記蒸気圧縮式冷凍機Xを複数台設置して該各蒸気圧縮式冷凍機Xの冷媒の排熱を上記吸収式冷凍機Yの上記発生器11で回収するように構成したことを特徴としている。   In an eighth invention of the present application, in the refrigeration apparatus according to the first, second, third, fourth, fifth, sixth or seventh invention, a plurality of the vapor compression refrigerators X are installed. The exhaust heat of the refrigerant of each of the vapor compression refrigerators X is collected by the generator 11 of the absorption refrigerator Y.

本願発明では次のような効果が得られる。   In the present invention, the following effects can be obtained.

(a) 本願の第1の発明
本願の第1の発明では、図1に例示するように、蒸気圧縮式冷凍機Xとエンジン等の排熱で駆動される吸収式冷凍機Yとを備えて構成される冷凍装置において、上記吸収式冷凍機Yの吸収器12に流入する溶液を空冷式の過冷却熱交換器15によって過冷却して上記吸収器12へ流入させるとともに、上記蒸気圧縮式冷凍機Xの冷媒と上記吸収式冷凍機Yの発生器11内の溶液との間で熱交換可能に構成する一方、上記蒸気圧縮式冷凍機Xの冷媒回路に、上記吸収式冷凍機Yの上記発生器11をバイパスして該吸収式冷凍機Yの上記蒸発器13に接続されるバイパス路を設けるとともに該バイパス路75に電磁弁45を備え、上記蒸気圧縮式冷凍機Xの冷房運転時で且つ上記バイパス路75の入口の冷媒の温度が設定温度未満である場合には上記電磁弁45を開弁し、冷媒の温度が設定温度以上である場合には上記電磁弁45を閉弁する一方、上記蒸気圧縮式冷凍機Xの暖房運転時には上記電磁弁45を閉弁するように構成している。
(A) 1st invention of this application In 1st invention of this application, as illustrated in FIG. 1, it has the vapor | steam compression refrigerator X and the absorption refrigerator Y driven by exhaust heat, such as an engine. In the refrigeration apparatus configured, the solution flowing into the absorber 12 of the absorption chiller Y is supercooled by the air-cooled supercooling heat exchanger 15 to flow into the absorber 12, and the vapor compression refrigeration is performed. While the heat exchange between the refrigerant of the machine X and the solution in the generator 11 of the absorption refrigeration machine Y is configured to be possible, the refrigerant circuit of the vapor compression refrigeration machine X includes the above-mentioned absorption refrigeration machine Y. A bypass path that bypasses the generator 11 and is connected to the evaporator 13 of the absorption refrigeration machine Y is provided, and an electromagnetic valve 45 is provided in the bypass path 75 so that the vapor compression refrigeration machine X can be operated during cooling operation. In addition, the refrigerant temperature at the inlet of the bypass passage 75 is set. When the temperature is lower than the temperature, the electromagnetic valve 45 is opened, and when the temperature of the refrigerant is equal to or higher than the set temperature, the electromagnetic valve 45 is closed, while the vapor compression refrigerator X is in the heating operation. The electromagnetic valve 45 is configured to be closed.

従って、上記蒸気圧縮式冷凍機Xの冷房運転時と暖房運転時においてそれぞれ以下の作用効果が得られる。   Therefore, the following functions and effects can be obtained during the cooling operation and the heating operation of the vapor compression refrigerator X, respectively.

本願の第1の発明に係る冷凍装置によれば、上記蒸気圧縮式冷凍機Xの冷房運転時には、上記電磁弁45は上記蒸気圧縮式冷凍機Xの冷媒温度が設定温度未満である場合には開弁され、冷媒の温度が設定温度以上である場合には上記電磁弁45は閉弁される。   According to the refrigeration apparatus according to the first invention of the present application, during the cooling operation of the vapor compression refrigeration machine X, the electromagnetic valve 45 is used when the refrigerant temperature of the vapor compression refrigeration machine X is lower than a set temperature. When the valve is opened and the refrigerant temperature is equal to or higher than the set temperature, the electromagnetic valve 45 is closed.

従って、上記蒸気圧縮式冷凍機Xの冷媒温度が上記バイパス路75の入口の設定温度未満である場合には上記電磁弁45が開弁されることで、上記蒸気圧縮式冷凍機Xの圧縮機1で圧縮された後の冷媒が上記吸収式冷凍機Yの上記発生器11をバイパスして上記吸収式冷凍機Yの上記蒸発器13に流入され、該蒸発器13において、上記吸収式冷凍機Y側の溶液との熱交換によって冷却、または過冷却される。このため、上記蒸気圧縮式冷凍機X側においては、上記過冷却分だけ該蒸気圧縮式冷凍機Xの利用側熱交換器3における冷媒の入口の比エンタルピーが低下し、これによって蒸気圧縮式冷凍機Xの冷房性能が改善される。また、上記吸収式冷凍機Y側においては、上記蒸気圧縮式冷凍機X側の冷媒は上記吸収式冷凍機Yの発生器11で放熱されることがなく過度の温度低下が防止されることで、上記蒸発器13における上記溶液からの冷媒蒸発が促進され、上記吸収式冷凍機Yが適正に駆動される。   Therefore, when the refrigerant temperature of the vapor compression refrigerator X is lower than the set temperature at the inlet of the bypass 75, the electromagnetic valve 45 is opened, so that the compressor of the vapor compression refrigerator X is opened. The refrigerant compressed in 1 bypasses the generator 11 of the absorption refrigerator Y and flows into the evaporator 13 of the absorption refrigerator Y. In the evaporator 13, the absorption refrigerator It is cooled or supercooled by heat exchange with the solution on the Y side. For this reason, on the vapor compression refrigerator X side, the specific enthalpy of the refrigerant inlet in the use side heat exchanger 3 of the vapor compression refrigerator X is lowered by the amount of the supercooling. The cooling performance of the machine X is improved. On the absorption refrigeration machine Y side, the refrigerant on the vapor compression refrigeration machine X side is not radiated by the generator 11 of the absorption refrigeration machine Y, and an excessive temperature drop is prevented. Then, evaporation of the refrigerant from the solution in the evaporator 13 is promoted, and the absorption refrigerator Y is driven appropriately.

これに対して、上記蒸気圧縮式冷凍機X側の冷媒の温度が上記バイパス路75の入口の設定温度以上である場合には上記電磁弁45が閉弁される。従って、上記蒸気圧縮式冷凍機Xの圧縮機1で圧縮された後の冷媒は、上記吸収式冷凍機Yの上記発生器11に流入し、上記蒸気圧縮式冷凍機Xの冷媒排熱が上記発生器11の駆動熱源に利用され、該発生器11をエンジン等の排熱のみで駆動する場合に比して、冷媒排熱の利用分だけ、排熱の有効利用が促進される。   On the other hand, when the temperature of the refrigerant on the vapor compression refrigerator X side is equal to or higher than the set temperature at the inlet of the bypass passage 75, the electromagnetic valve 45 is closed. Therefore, the refrigerant after being compressed by the compressor 1 of the vapor compression refrigerator X flows into the generator 11 of the absorption refrigerator Y, and the refrigerant exhaust heat of the vapor compression refrigerator X is Compared to the case where the generator 11 is used as a driving heat source for driving the generator 11 with only exhaust heat from the engine or the like, effective use of exhaust heat is promoted by the amount of refrigerant exhaust heat used.

さらに、上記蒸気圧縮式冷凍機Xの冷媒の冷却、または過冷却が上記吸収式冷凍機Yの上記蒸発器13において行なわれることで、上記吸収式冷凍機Y側においては、例えば、上記蒸発器13に冷水を循環させる場合に比して、該蒸発器13における上記吸収式冷凍機Yの冷媒の蒸発温度を高くすることができることから、例えば、必要な冷媒の蒸発能力を一定とした場合には、冷媒に対する蒸発温度の上昇分だけ、上記蒸発器13の能力を低く抑えてその低コスト化あるいはコンパクト化を図ることが可能となる。   Furthermore, the cooling or supercooling of the refrigerant of the vapor compression refrigeration machine X is performed in the evaporator 13 of the absorption refrigeration machine Y, so that on the absorption refrigeration machine Y side, for example, the evaporator Compared with the case where cold water is circulated through the refrigerant 13, the evaporation temperature of the refrigerant of the absorption refrigeration machine Y in the evaporator 13 can be made higher. Therefore, it is possible to reduce the cost or the size of the evaporator 13 by reducing the capacity of the evaporator 13 by the increase in the evaporation temperature with respect to the refrigerant.

(b) 本願の第2の発明
本願の第2の発明では、上記(a)に記載の効果に加えて以下のような特有の効果が得られる。即ち、この発明に係る冷凍装置では、図2に例示するように、上記第1の発明に係る冷凍装置において、上記吸収式冷凍機Yの上記吸収器12の出口から溶液ポンプ17を経て溶液熱交換器16に至る管路67に電磁弁41を設けるとともに、上記吸収式冷凍機Yの上記吸収器12の入口側の管路66と上記蒸発器13の冷媒入口側の管路62を、第3電磁弁43を備えた管路76によって接続し、上記蒸気圧縮式冷凍機Xの冷房運転時には上記電磁弁45は上記蒸気圧縮式冷凍機Xの上記バイパス路75の入口の冷媒温度の設定温度により開閉されるが、上記第3電磁弁43を閉弁し、上記電磁弁41を開弁する一方、上記蒸気圧縮式冷凍機Xの暖房運転時には上記第3電磁弁43を開弁し、上記電磁弁41と電磁弁45を閉弁するように構成している。
(B) Second invention of the present application In the second invention of the present application, in addition to the effects described in (a) above, the following specific effects are obtained. That is, in the refrigeration apparatus according to the present invention, as illustrated in FIG. 2, in the refrigeration apparatus according to the first invention, the solution heat from the outlet of the absorber 12 of the absorption refrigerator Y passes through the solution pump 17. A solenoid valve 41 is provided in a pipeline 67 leading to the exchanger 16, and a pipeline 66 on the inlet side of the absorber 12 of the absorption refrigerator Y and a pipeline 62 on the refrigerant inlet side of the evaporator 13 When the steam compression refrigerator X is in cooling operation, the solenoid valve 45 is connected to the pipe 76 having the three solenoid valves 43. The set temperature of the refrigerant temperature at the inlet of the bypass path 75 of the vapor compression refrigerator X Is opened and closed by closing the third solenoid valve 43 and opening the solenoid valve 41, while opening the third solenoid valve 43 during the heating operation of the vapor compression refrigerator X, and To close the solenoid valve 41 and the solenoid valve 45 Forms.

従って、上記蒸気圧縮式冷凍機Xの冷房運転時と暖房運転時においてそれぞれ以下の作用効果が得られる。
(b−1)上記蒸気圧縮式冷凍機Xの冷房運転時には、上記電磁弁45は上記蒸気圧縮式冷凍機Xの上記バイパス路75の入口の冷媒温度の設定温度により開閉されるが、上記電磁弁41が開弁され、上記第3電磁弁43が閉弁される。従って、その回路構成は、上記第1の発明に係る冷凍装置の冷房運転時における回路構成と同様となり、これと同様の作用効果(上記(a)参照)が得られるので、その該当説明を援用し、ここでの説明を省略する。
(b−2)上記蒸気圧縮式冷凍機Xの暖房運転時には、上記吸収式冷凍機Yにおいては、上記凝縮器14はその運転が停止され、上記過冷却熱交換器15と溶液ポンプ17のみが運転される。また、上記発生器11への排熱の供給は継続される。
Therefore, the following functions and effects can be obtained during the cooling operation and the heating operation of the vapor compression refrigerator X, respectively.
(B-1) During the cooling operation of the vapor compression refrigeration machine X, the electromagnetic valve 45 is opened and closed by the set temperature of the refrigerant temperature at the inlet of the bypass passage 75 of the vapor compression refrigeration machine X. The valve 41 is opened, and the third electromagnetic valve 43 is closed. Accordingly, the circuit configuration is the same as the circuit configuration during the cooling operation of the refrigeration apparatus according to the first invention, and the same operational effects (see (a) above) can be obtained. The description here is omitted.
(B-2) During the heating operation of the vapor compression refrigerator X, in the absorption refrigerator Y, the operation of the condenser 14 is stopped, and only the supercooling heat exchanger 15 and the solution pump 17 are operated. Driven. Further, the supply of exhaust heat to the generator 11 is continued.

そして、この状態において、上記第3電磁弁43が開弁され、上記電磁弁41と電磁弁45が閉弁される。   In this state, the third electromagnetic valve 43 is opened, and the electromagnetic valve 41 and the electromagnetic valve 45 are closed.

従って、上記吸収式冷凍機Yの上記蒸発器13には上記溶液ポンプ17によって上記吸収式冷凍機Y側の溶液が循環され、上記蒸気圧縮式冷凍機X側の上記利用側熱交換器3において凝縮した後の冷媒は、上記蒸発器13において上記吸収式冷凍機Y側の溶液との熱交換によって吸熱することで蒸発する。上記吸収式冷凍機Y側の溶液は蒸発器13内で冷却されるが、溶液ポンプにより過冷却熱交換器15に送られ、外気より熱を奪って温度が上がり、蒸発器13に送液される。また、上記蒸発器13で蒸発した上記蒸気圧縮式冷凍機X側の冷媒は、上記発生器11内でエンジン等の排熱により加熱された溶液と熱交換器11bにより温度が上げられ、上記蒸気圧縮式冷凍機Xの上記圧縮機1側に吸入され、蒸気圧縮式Xの冷媒の蒸発温度が上昇する。このため、例えば、上記発生器11に供給される排熱量が少なくても、上記蒸気圧縮式冷凍機Xの冷媒は外気より吸熱することで、蒸発温度が維持されることから、上記蒸気圧縮式冷凍機Xの暖房性能はそのままで、エンジン等の排熱により上記発生器11内の熱交換器11bでの加熱分が、上記蒸気圧縮式冷凍機Xの暖房性能の改善に寄与することになる。   Therefore, the solution on the absorption refrigeration machine Y side is circulated through the evaporator 13 of the absorption refrigeration machine Y by the solution pump 17, and in the use side heat exchanger 3 on the vapor compression refrigeration machine X side. The condensed refrigerant evaporates by absorbing heat in the evaporator 13 by heat exchange with the solution on the absorption refrigerator Y side. The solution on the absorption refrigerator Y side is cooled in the evaporator 13, but is sent to the supercooling heat exchanger 15 by the solution pump, takes heat from the outside air, rises in temperature, and is sent to the evaporator 13. The The refrigerant on the vapor compression refrigerator X side evaporated by the evaporator 13 is heated by the heat exchanger 11b and the solution heated by exhaust heat from the engine or the like in the generator 11, and the vapor The refrigerant is sucked into the compressor 1 side of the compression refrigerator X, and the evaporation temperature of the vapor compression X refrigerant is increased. For this reason, for example, even when the amount of exhaust heat supplied to the generator 11 is small, the refrigerant of the vapor compression refrigerator X absorbs heat from the outside air, so that the evaporation temperature is maintained. Heating performance of the heat exchanger 11b in the generator 11 due to exhaust heat from the engine or the like contributes to improvement of the heating performance of the vapor compression refrigerator X while the heating performance of the refrigerator X remains unchanged. .

(b−3) 上記(b−1)と(b−2)に記載の効果の相乗効果として、冷房運転時と暖房運転時の双方において蒸気圧縮式冷凍機Xの性能改善効果が得られ、実用性に富む冷凍装置が得られることになる。   (B-3) As a synergistic effect of the effects described in the above (b-1) and (b-2), the performance improvement effect of the vapor compression refrigeration machine X can be obtained both during the cooling operation and during the heating operation. A refrigeration apparatus rich in practicality can be obtained.

(c) 本願の第3の発明
本願の第3の発明では、上記(a)に記載の効果に加えて以下のような特有の効果が得られる。即ち、この発明に係る冷凍装置では、図3に例示するように、上記第1の発明に係る冷凍装置において、上記吸収式冷凍機Yの上記吸収器12の出口から溶液ポンプ17を経て溶液熱交換器16に至る管路67に電磁弁41を設けるとともに、上記吸収式冷凍機Yの上記吸収器12の入口側の管路66を、電磁弁43を備えた管路77を介して上記蒸発器13に接続し、上記蒸気圧縮式冷凍機Xの冷房運転時には上記電磁弁45は上記蒸気圧縮式冷凍機Xの上記バイパス路75の入口の冷媒温度の設定温度により開閉されるが、上記電磁弁43を閉弁し、上記電磁弁41を開弁する一方、上記蒸気圧縮式冷凍機Xの暖房運転時には上記電磁弁43を開弁し、上記電磁弁41と電磁弁45を閉弁するように構成している。
(C) Third invention of the present application In the third invention of the present application, in addition to the effects described in (a) above, the following specific effects are obtained. That is, in the refrigeration apparatus according to the present invention, as illustrated in FIG. 3, in the refrigeration apparatus according to the first invention, the solution heat from the outlet of the absorber 12 of the absorption chiller Y passes through the solution pump 17. The electromagnetic valve 41 is provided in the pipe line 67 leading to the exchanger 16, and the pipe line 66 on the inlet side of the absorber 12 of the absorption refrigeration machine Y is passed through the pipe line 77 provided with the electromagnetic valve 43 to evaporate the vapor. When the vapor compression refrigerator X is in a cooling operation, the solenoid valve 45 is opened and closed by the set temperature of the refrigerant temperature at the inlet of the bypass passage 75 of the vapor compression refrigerator X. While the valve 43 is closed and the solenoid valve 41 is opened, the solenoid valve 43 is opened during the heating operation of the vapor compression refrigerator X, and the solenoid valve 41 and the solenoid valve 45 are closed. It is configured.

従って、上記蒸気圧縮式冷凍機Xの冷房運転時と暖房運転時においてそれぞれ以下の作用効果が得られる。   Therefore, the following functions and effects can be obtained during the cooling operation and the heating operation of the vapor compression refrigerator X, respectively.

(c−1) 冷房運転時
上記蒸気圧縮式冷凍機Xの冷房運転時には、上記電磁弁45は上記蒸気圧縮式冷凍機Xの上記バイパス路75の入口の冷媒温度の設定温度により開閉されるが、上記電磁弁41が開弁され、上記電磁弁43は閉弁される。従って、その回路構成は、上記第1の発明に係る冷凍装置の冷房運転時における回路構成と同様となり、これと同様の作用効果(上記(a)参照)が得られるので、その該当説明を援用し、ここでの説明を省略する。
(C-1) During cooling operation During the cooling operation of the vapor compression refrigeration machine X, the electromagnetic valve 45 is opened and closed by the set temperature of the refrigerant temperature at the inlet of the bypass passage 75 of the vapor compression refrigeration machine X. The solenoid valve 41 is opened, and the solenoid valve 43 is closed. Accordingly, the circuit configuration is the same as the circuit configuration during the cooling operation of the refrigeration apparatus according to the first invention, and the same operational effects (see (a) above) can be obtained. The description here is omitted.

(c−2) 暖房運転時
上記蒸気圧縮式冷凍機Xの暖房運転時には、上記吸収式冷凍機Yにおいては、上記凝縮器14はその運転が停止され、上記溶液ポンプ17のみが運転される。また、上記発生器11への排熱の供給は継続される。そして、この状態で、上記電磁弁43は開弁され、上記電磁弁41と電磁弁45は閉弁される。
(C-2) During heating operation During the heating operation of the vapor compression refrigerator X, in the absorption refrigerator Y, the operation of the condenser 14 is stopped, and only the solution pump 17 is operated. Further, the supply of exhaust heat to the generator 11 is continued. In this state, the solenoid valve 43 is opened, and the solenoid valve 41 and the solenoid valve 45 are closed.

従って、上記吸収式冷凍機Yの上記蒸発器13には上記溶液ポンプ17によって上記吸収式冷凍機Y側の溶液が循環され、上記蒸気圧縮式冷凍機X側の上記利用側熱交換器3において凝縮した後の冷媒は、上記蒸発器13において上記吸収式冷凍機Y側の溶液との熱交換によって吸熱することで蒸発する。上記吸収式冷凍機Y側の溶液は蒸発器13内で冷却されるが、溶液ポンプ17により過冷却熱交換器15に送られ、外気より熱を奪って温度が上がり、蒸発器13に送液される。また、上記蒸発器13で蒸発した上記蒸気圧縮式冷凍機X側の冷媒は、上記発生器11内でエンジン等の排熱により加熱された溶液と熱交換器11bにより温度が上げられ、上記蒸気圧縮式冷凍機Xの上記圧縮機1側に吸入され、蒸気圧縮式冷凍機Xの冷媒の蒸発温度が上昇する。このため、例えば、上記発生器11に供給される排熱量が少なくても、上記蒸気圧縮式冷凍機Xの冷媒は外気より吸熱することで、蒸発温度が維持されることから、上記蒸気圧縮式冷凍機Xの暖房性能はそのままで、エンジン等の排熱により上記発生器11内の熱交換器11bでの加熱分が、上記蒸気圧縮式冷凍機Xの暖房性能の改善に寄与することになる。   Therefore, the solution on the absorption refrigeration machine Y side is circulated through the evaporator 13 of the absorption refrigeration machine Y by the solution pump 17, and in the use side heat exchanger 3 on the vapor compression refrigeration machine X side. The condensed refrigerant evaporates by absorbing heat in the evaporator 13 by heat exchange with the solution on the absorption refrigerator Y side. The solution on the absorption refrigeration machine Y side is cooled in the evaporator 13, but is sent to the supercooling heat exchanger 15 by the solution pump 17, deprived of heat from the outside air, rises in temperature, and is sent to the evaporator 13. Is done. The refrigerant on the vapor compression refrigerator X side evaporated by the evaporator 13 is heated by the heat exchanger 11b and the solution heated by exhaust heat from the engine or the like in the generator 11, and the vapor The refrigerant is sucked into the compressor 1 side of the compression refrigerator X, and the evaporation temperature of the refrigerant of the vapor compression refrigerator X increases. For this reason, for example, even when the amount of exhaust heat supplied to the generator 11 is small, the refrigerant of the vapor compression refrigerator X absorbs heat from the outside air, so that the evaporation temperature is maintained. Heating performance of the heat exchanger 11b in the generator 11 due to exhaust heat from the engine or the like contributes to improvement of the heating performance of the vapor compression refrigerator X while the heating performance of the refrigerator X remains unchanged. .

(c−3) 上記(c−1)と(c−2)に記載の効果の相乗効果として、冷房運転時と暖房運転時の双方において蒸気圧縮式冷凍機Xの性能改善効果が得られ、実用性に富む冷凍装置が得られることになる。   (C-3) As a synergistic effect of the effects described in the above (c-1) and (c-2), the performance improvement effect of the vapor compression refrigeration machine X is obtained both during the cooling operation and during the heating operation. A refrigeration apparatus rich in practicality can be obtained.

(d) 本願の第4の発明
本願の第4の発明では、上記(b)又は(c)に記載の効果に加えて以下のような特有の効果が得られる。即ち、この発明に係る冷凍装置では、図3に例示するように、上記第2又は第3の発明に係る冷凍装置において、上記吸収式冷凍機Yの上記吸収器12の入口側の管路66に電磁弁44を設け、上記蒸気圧縮式冷凍機Xの冷房運転時には上記電磁弁44を開弁し、暖房運転時には上記電磁弁44を閉弁するように構成している。
(D) 4th invention of this application In the 4th invention of this application, in addition to the effect as described in said (b) or (c), the following specific effects are acquired. That is, in the refrigeration apparatus according to the present invention, as illustrated in FIG. 3, in the refrigeration apparatus according to the second or third aspect of the invention, a pipe line 66 on the inlet side of the absorber 12 of the absorption refrigeration machine Y. The electromagnetic valve 44 is provided, and the electromagnetic valve 44 is opened during the cooling operation of the vapor compression refrigerator X, and the electromagnetic valve 44 is closed during the heating operation.

従って、上記蒸気圧縮式冷凍機Xの冷房運転時と暖房運転時においてそれぞれ以下の作用効果が得られる。   Therefore, the following functions and effects can be obtained during the cooling operation and the heating operation of the vapor compression refrigerator X, respectively.

(d−1) 冷房運転時
上記蒸気圧縮式冷凍機Xの冷房運転時には、上記電磁弁41と上記電磁弁44が開弁され、上記電磁弁45は上記蒸気圧縮式冷凍機Xの上記バイパス路75の入口の冷媒温度の設定温度により開閉されるが、上記電磁弁43が閉弁される。従って、その回路構成は、上記第1の発明に係る冷凍装置の冷房運転時における回路構成と同様となり、これと同様の作用効果(上記(a)参照)が得られるので、その該当説明を援用し、ここでの説明を省略する。
(D-1) During cooling operation During cooling operation of the vapor compression refrigeration machine X, the electromagnetic valve 41 and the electromagnetic valve 44 are opened, and the electromagnetic valve 45 is connected to the bypass path of the vapor compression refrigeration machine X. The solenoid valve 43 is closed although it is opened and closed by the set temperature of the refrigerant temperature at 75 inlets. Accordingly, the circuit configuration is the same as the circuit configuration during the cooling operation of the refrigeration apparatus according to the first invention, and the same operational effects (see (a) above) can be obtained. The description here is omitted.

(d−2) 暖房運転時
上記蒸気圧縮式冷凍機Xの暖房運転時には、上記吸収式冷凍機Yにおいては、上記凝縮器14はその運転が停止され、上記溶液ポンプ17のみが運転される。また、上記発生器11への排熱の供給は継続される。そして、この状態で、上記電磁弁43は開弁され、上記電磁弁41と電磁弁44と電磁弁45は閉弁される。
(D-2) During heating operation During the heating operation of the vapor compression refrigerator X, in the absorption refrigerator Y, the operation of the condenser 14 is stopped, and only the solution pump 17 is operated. Further, the supply of exhaust heat to the generator 11 is continued. In this state, the solenoid valve 43 is opened, and the solenoid valve 41, the solenoid valve 44, and the solenoid valve 45 are closed.

従って、上記吸収式冷凍機Yの上記蒸発器13には上記溶液ポンプ17によって上記吸収式冷凍機Y側の溶液が循環され、上記蒸気圧縮式冷凍機X側の上記利用側熱交換器3において凝縮した後の冷媒は、上記蒸発器13に流入する上記吸収式冷凍機Y側の溶液との間の熱交換によって吸熱することで蒸発する。上記吸収式冷凍機Y側の溶液は蒸発器13内で冷却されるが、溶液ポンプにより過冷却熱交換器15に送られ、外気より熱を奪って温度が上がり、蒸発器13に送液される。また、上記蒸発器13で蒸発した上記蒸気圧縮式冷凍機X側の冷媒は、上記発生器11内でエンジン等の排熱により加熱された溶液と熱交換器11bにより温度が上げられ、上記蒸気圧縮式冷凍機Xの上記圧縮機1側に吸入され、蒸気圧縮式冷凍機Xの冷媒の蒸発温度が上昇する。このため、例えば、上記発生器11に供給される排熱量が少なくても、上記蒸気圧縮式冷凍機Xの冷媒は外気より吸熱することで、蒸発温度が維持されることから、上記蒸気圧縮式冷凍機Xの暖房性能はそのままで、エンジン等の排熱により発生器11内の熱交換器11bでの加熱分が、上記蒸気圧縮式冷凍機Xの暖房性能の改善に寄与することになる。   Therefore, the solution on the absorption refrigeration machine Y side is circulated through the evaporator 13 of the absorption refrigeration machine Y by the solution pump 17, and in the use side heat exchanger 3 on the vapor compression refrigeration machine X side. The condensed refrigerant evaporates by absorbing heat by heat exchange with the solution on the absorption refrigerator Y side flowing into the evaporator 13. The solution on the absorption refrigerator Y side is cooled in the evaporator 13, but is sent to the supercooling heat exchanger 15 by the solution pump, takes heat from the outside air, rises in temperature, and is sent to the evaporator 13. The The refrigerant on the vapor compression refrigerator X side evaporated by the evaporator 13 is heated by the heat exchanger 11b and the solution heated by exhaust heat from the engine or the like in the generator 11, and the vapor The refrigerant is sucked into the compressor 1 side of the compression refrigerator X, and the evaporation temperature of the refrigerant of the vapor compression refrigerator X increases. For this reason, for example, even when the amount of exhaust heat supplied to the generator 11 is small, the refrigerant of the vapor compression refrigerator X absorbs heat from the outside air, so that the evaporation temperature is maintained. The heating performance of the heat exchanger 11b in the generator 11 due to exhaust heat from the engine or the like contributes to the improvement of the heating performance of the vapor compression refrigeration machine X while the heating performance of the refrigerator X remains unchanged.

また、上記電磁弁44が閉弁されることで、上記過冷却熱交換器15からの溶液の全量が上記蒸発器13側に流入するため、例えば、上記過冷却熱交換器15からの溶液の一部しか上記蒸発器13に流入しない場合に比して、該蒸発器13での上記蒸気圧縮式冷凍機X側の冷媒との熱交換作用が促進され、該冷媒の蒸発温度が高められ、その結果、上記蒸気圧縮式冷凍機Xの上記利用側熱交換器3での冷媒の凝縮に伴う放熱量が増加し、それだけ上記蒸気圧縮式冷凍機Xの暖房性能が改善されることになる。   Moreover, since the whole amount of the solution from the supercooling heat exchanger 15 flows into the evaporator 13 side by closing the electromagnetic valve 44, for example, the solution of the solution from the supercooling heat exchanger 15 is supplied. Compared to the case where only a part of the refrigerant flows into the evaporator 13, the heat exchange action with the refrigerant on the vapor compression refrigerator X side in the evaporator 13 is promoted, and the evaporation temperature of the refrigerant is increased. As a result, the amount of heat release accompanying the condensation of the refrigerant in the use side heat exchanger 3 of the vapor compression refrigerator X increases, and the heating performance of the vapor compression refrigerator X is improved accordingly.

(d−3) 上記(d−1)と(d−2)に記載の効果の相乗効果として、冷房運転時と暖房運転時の双方において蒸気圧縮式冷凍機Xの性能改善効果が得られ、実用性に富む冷凍装置が得られることになる。   (D-3) As a synergistic effect of the effects described in (d-1) and (d-2) above, the performance improvement effect of the vapor compression refrigeration machine X is obtained both during the cooling operation and during the heating operation. A refrigeration apparatus rich in practicality can be obtained.

(e) 本願の第5の発明
本願の第5の発明は、上記(a)、(b)、(c)又は(d)に記載の効果に加えて以下のような特有の効果が得られる。即ち、この発明に係る冷凍装置では、図4に例示するように、上記第1、第2、第3又は第4の発明に係る冷凍装置において、上記発生器11の排熱入口側の管路60に電磁弁46を設け、冷房運転時には上記電磁弁46を開弁する一方、暖房運転時には上記発生器11の溶液温度が設定温度以上のとき上記電磁弁46を閉弁し、該設定温度未満のとき上記電磁弁46を開弁させるように構成している。
(E) Fifth invention of the present application The fifth invention of the present application provides the following specific effects in addition to the effects described in (a), (b), (c) or (d) above. . That is, in the refrigeration apparatus according to the present invention, as illustrated in FIG. 4, in the refrigeration apparatus according to the first, second, third, or fourth invention, a pipe line on the exhaust heat inlet side of the generator 11. An electromagnetic valve 46 is provided at 60, and the electromagnetic valve 46 is opened during the cooling operation, while the electromagnetic valve 46 is closed when the solution temperature of the generator 11 is equal to or higher than the set temperature during the heating operation. At this time, the electromagnetic valve 46 is configured to open.

従って、上記蒸気圧縮式冷凍機Xの冷房運転時と暖房運転時においてそれぞれ以下の作用効果が得られる。   Therefore, the following functions and effects can be obtained during the cooling operation and the heating operation of the vapor compression refrigerator X, respectively.

(e−1) 冷房運転時
上記蒸気圧縮式冷凍機Xの冷房運転時には、上記電磁弁41と上記電磁弁44及び上記電磁弁46が開弁され、上記電磁弁45は上記蒸気圧縮式冷凍機Xの上記バイパス路75の入口の冷媒温度の設定温度により開閉されるが、上記電磁弁43が閉弁される。従って、その回路構成は、上記第1の発明に係る冷凍装置の冷房運転時における回路構成と同様となり、これと同様の作用効果(上記(a)参照)が得られるので、その該当説明を援用し、ここでの説明を省略する。
(E-1) During cooling operation During cooling operation of the vapor compression refrigerator X, the solenoid valve 41, the solenoid valve 44, and the solenoid valve 46 are opened, and the solenoid valve 45 is connected to the vapor compression refrigerator. The solenoid valve 43 is closed although it is opened and closed by the set temperature of the refrigerant temperature at the inlet of the bypass passage 75 of X. Accordingly, the circuit configuration is the same as the circuit configuration during the cooling operation of the refrigeration apparatus according to the first invention, and the same operational effects (see (a) above) can be obtained. The description here is omitted.

(e−2) 暖房運転時
上記蒸気圧縮式冷凍機Xの暖房運転時には、上記吸収式冷凍機Yにおいては、上記凝縮器14はその運転が停止され、上記溶液ポンプ17のみが運転される。そして、この状態で、上記電磁弁43は開弁され、上記電磁弁41と上記電磁弁44及び上記電磁弁45は閉弁される。また、上記電磁弁46は、上記発生器11の溶液温度が設定温度以上のときには閉弁され、該設定温度未満のときには開弁される。
(E-2) During heating operation During the heating operation of the vapor compression refrigeration machine X, in the absorption refrigeration machine Y, the operation of the condenser 14 is stopped and only the solution pump 17 is operated. In this state, the solenoid valve 43 is opened, and the solenoid valve 41, the solenoid valve 44, and the solenoid valve 45 are closed. The electromagnetic valve 46 is closed when the solution temperature of the generator 11 is equal to or higher than a set temperature, and is opened when the temperature is lower than the set temperature.

従って、上記吸収式冷凍機Yの上記蒸発器13には上記溶液ポンプ17によって上記吸収式冷凍機Y側の溶液が循環され、上記蒸気圧縮式冷凍機X側の上記利用側熱交換器3において凝縮した後の冷媒は、上記蒸発器13に流入する上記吸収式冷凍機Y側の溶液との間の熱交換によって吸熱することで蒸発する。上記吸収式冷凍機Y側の溶液は蒸発器13内で冷却されるが、溶液ポンプ17により過冷却熱交換器15に送られ、外気より熱を奪って温度が上がり、蒸発器13に送液される。また、上記蒸発器13で蒸発した上記蒸気圧縮式冷凍機X側の冷媒は、上記発生器11内でエンジン等の排熱により加熱された溶液と熱交換器11bにより温度が上げられ、上記蒸気圧縮式冷凍機Xの上記圧縮機1側に吸入され、蒸気圧縮式冷凍機Xの冷媒の蒸発温度が上昇する。このため、例えば、上記発生器11に供給される排熱量が少なくても、上記蒸気圧縮式冷凍機Xの冷媒は外気より吸熱することで、蒸発温度が維持されることから、上記蒸気圧縮式冷凍機Xの暖房性能はそのままで、エンジン等の排熱により発生器11内の熱交換器11bでの加熱分が、上記蒸気圧縮式冷凍機Xの暖房性能の改善に寄与することになる。   Therefore, the solution on the absorption refrigeration machine Y side is circulated through the evaporator 13 of the absorption refrigeration machine Y by the solution pump 17, and in the use side heat exchanger 3 on the vapor compression refrigeration machine X side. The condensed refrigerant evaporates by absorbing heat by heat exchange with the solution on the absorption refrigerator Y side flowing into the evaporator 13. The solution on the absorption refrigeration machine Y side is cooled in the evaporator 13, but is sent to the supercooling heat exchanger 15 by the solution pump 17, deprived of heat from the outside air, rises in temperature, and is sent to the evaporator 13. Is done. The refrigerant on the vapor compression refrigerator X side evaporated by the evaporator 13 is heated by the heat exchanger 11b and the solution heated by exhaust heat from the engine or the like in the generator 11, and the vapor The refrigerant is sucked into the compressor 1 side of the compression refrigerator X, and the evaporation temperature of the refrigerant of the vapor compression refrigerator X increases. For this reason, for example, even when the amount of exhaust heat supplied to the generator 11 is small, the refrigerant of the vapor compression refrigerator X absorbs heat from the outside air, so that the evaporation temperature is maintained. The heating performance of the heat exchanger 11b in the generator 11 due to exhaust heat from the engine or the like contributes to the improvement of the heating performance of the vapor compression refrigeration machine X while the heating performance of the refrigerator X remains unchanged.

また、上記発生器11内の溶液温度が設定温度以上のときには上記電磁弁46が閉弁されて上記発生器11への排熱の供給が中断され、該設定温度未満のときには上記電磁弁46が開弁されて該発生器11に排熱が供給されることで、上記発生器11内の溶液温度が常時適正に保たれる。   Further, when the solution temperature in the generator 11 is equal to or higher than the set temperature, the electromagnetic valve 46 is closed, and the supply of exhaust heat to the generator 11 is interrupted. When the temperature is lower than the set temperature, the electromagnetic valve 46 is When the valve 11 is opened and exhaust heat is supplied to the generator 11, the solution temperature in the generator 11 is always kept appropriate.

さらに、上記電磁弁44が閉弁されることで、上記過冷却熱交換器15からの溶液の全量が上記蒸発器13側に流入するため、例えば、上記過冷却熱交換器15からの溶液の一部しか上記蒸発器13に流入しない場合に比して、該蒸発器13での上記蒸気圧縮式冷凍機X側の冷媒との熱交換作用が促進され、該冷媒の蒸発温度が高められ、その結果、上記蒸気圧縮式冷凍機Xの上記利用側熱交換器3での冷媒の凝縮に伴う放熱量が増加し、それだけ上記蒸気圧縮式冷凍機Xの暖房性能が改善されることになる。   Further, since the entire amount of the solution from the supercooling heat exchanger 15 flows into the evaporator 13 side by closing the solenoid valve 44, for example, the solution of the solution from the supercooling heat exchanger 15 is supplied. Compared to the case where only a part of the refrigerant flows into the evaporator 13, the heat exchange action with the refrigerant on the vapor compression refrigerator X side in the evaporator 13 is promoted, and the evaporation temperature of the refrigerant is increased. As a result, the amount of heat release accompanying the condensation of the refrigerant in the use side heat exchanger 3 of the vapor compression refrigerator X increases, and the heating performance of the vapor compression refrigerator X is improved accordingly.

(e−3) 上記(e−1)と(e−2)に記載の効果の相乗効果として、冷房運転時と暖房運転時の双方において蒸気圧縮式冷凍機Xの性能改善効果が得られ、実用性に富む冷凍装置が得られることになる。   (E-3) As a synergistic effect of the effects described in the above (e-1) and (e-2), the performance improvement effect of the vapor compression refrigeration machine X is obtained both in the cooling operation and in the heating operation. A refrigeration apparatus rich in practicality can be obtained.

(f) 本願の第6の発明
本願の第6の発明では、上記(d)、又は(e)に記載の効果に加えて以下のような特有の効果が得られる。即ち、この発明に係る冷凍装置では、図3及び図4に例示するように、上記蒸発器13における溶液散布用の散布器18と冷媒液散布用の散布器19を、別体構成又は共用可能な一体構成としている。
(F) Sixth invention of the present application In the sixth invention of the present application, in addition to the effects described in (d) or (e) above, the following specific effects can be obtained. That is, in the refrigeration apparatus according to the present invention, as illustrated in FIGS. 3 and 4, the sprayer 18 for spraying the solution and the sprayer 19 for spraying the refrigerant liquid in the evaporator 13 can be configured separately or shared. It has a one-piece construction.

従って、上記溶液散布用の散布器18と冷媒液散布用の散布器19を別体構成とした場合には、本来的に設けられている冷媒散布用の上記散布器19における上記蒸発器13の熱交換器への冷媒の適正な散布状態を維持したまま、上記蒸発器13の熱交換器への溶液の散布が適正に行なわれるよう上記溶液散布用の散布器18の構造あるいは設置位置を設定することができる。   Therefore, in the case where the solution spraying device 18 and the coolant spraying device 19 are configured separately, the evaporator 13 of the coolant spraying device 19 that is originally provided for the coolant spraying is used. The structure or installation position of the solution spraying device 18 is set so that the solution is properly sprayed to the heat exchanger of the evaporator 13 while maintaining the proper spraying state of the refrigerant to the heat exchanger. can do.

また、上記溶液散布用の散布器18と冷媒液散布用の散布器19を一体構成とした場合には、散布器の配置スペースの狭小化によって、上記蒸発器13のコンパクト化及び低コスト化が図れる。   Further, in the case where the solution spraying device 18 and the refrigerant solution spraying device 19 are integrated, the evaporator 13 can be made compact and low in cost by narrowing the space for the spraying device. I can plan.

(g) 本願の第7の発明
本願の第7の発明では、上記(a)、(b)、(c)、(d)、(e)又は(f)に記載の効果に加えて以下のような特有の効果が得られる。即ち、この発明に係る冷凍装置では、上記蒸発器13を、冷媒液が一過性で該蒸発器熱交換器13aの伝熱面を流れ、未蒸発の冷媒液が上記吸収器12側へ移動して該吸収器12側の溶液に吸収されるように構成しているので、例えば、上記蒸発器13を循環式とする場合に比して、該蒸発器13及びこれに隣接設置される上記吸収器12の低コスト化が図れ、延いては蒸気圧縮式冷凍機Xと吸収式冷凍機Yを組み合わせて構成される冷凍装置の低コスト化が図られる。
(G) 7th invention of this application In 7th invention of this application, in addition to the effect as described in said (a), (b), (c), (d), (e) or (f), the following Such unique effects can be obtained. That is, in the refrigeration apparatus according to the present invention, the refrigerant liquid passes through the heat transfer surface of the evaporator heat exchanger 13a while the refrigerant liquid is transient, and the non-evaporated refrigerant liquid moves to the absorber 12 side. Therefore, for example, as compared with the case where the evaporator 13 is a circulation type, the evaporator 13 and the above-mentioned installed adjacent to the evaporator 13 are absorbed in the solution on the absorber 12 side. The cost of the absorber 12 can be reduced, and as a result, the cost of a refrigeration apparatus configured by combining the vapor compression refrigerator X and the absorption refrigerator Y can be reduced.

(h) 本願の第8の発明
本願の第8の発明では、上記(a)、(b)、(c)、(d)、(e)、(f)又は(g)に記載の効果に加えて以下のような特有の効果が得られる。即ち、この発明に係る冷凍装置では、図5に例示するように、上記蒸気圧縮式冷凍機Xを複数台設置するとともに該各蒸気圧縮式冷凍機Xのそれぞれに上記熱回収熱交換器6を設けて該各蒸気圧縮式冷凍機Xの冷媒の排熱をそれぞれ回収し、該各熱回収熱交換器6で回収された排熱を一台の吸収式冷凍機Yの上記発生器11に供給するように構成しているので、上記蒸気圧縮式冷凍機Xの冷媒側から上記吸収式冷凍機Yの発生器11側への回収熱量が大きくなることから、エンジン等の排熱が少ない場合でも上記吸収式冷凍機Yを適正に運転させることができ、その結果、該吸収式冷凍機Yの蒸発器13での熱交換によって蒸気圧縮式冷凍機Xの冷媒を十分に過冷却することが可能となり、延いては上記冷凍装置全体としての性能改善効果を得ることができる。
(H) Eighth Invention of the Present Application In the eighth invention of the present application, the effect described in (a), (b), (c), (d), (e), (f) or (g) is achieved. In addition, the following specific effects can be obtained. That is, in the refrigeration apparatus according to the present invention, as illustrated in FIG. 5, a plurality of the vapor compression refrigeration machines X are installed, and the heat recovery heat exchanger 6 is installed in each of the vapor compression refrigeration machines X. Provided to recover the exhaust heat of the refrigerant of each vapor compression refrigerator X and supply the exhaust heat recovered by each heat recovery heat exchanger 6 to the generator 11 of one absorption refrigerator Y Since the amount of recovered heat from the refrigerant side of the vapor compression refrigeration machine X to the generator 11 side of the absorption refrigeration machine Y increases, even when there is little exhaust heat from the engine, etc. The absorption refrigerator Y can be properly operated, and as a result, the refrigerant of the vapor compression refrigerator X can be sufficiently subcooled by heat exchange in the evaporator 13 of the absorption refrigerator Y. As a result, the performance improvement effect of the entire refrigeration system Rukoto can.

本願発明の第1の実施の形態に係る冷凍装置の全体回路図である。1 is an overall circuit diagram of a refrigeration apparatus according to a first embodiment of the present invention. 本願発明の第2の実施の形態に係る冷凍装置の全体回路図である。It is a whole circuit diagram of the freezing apparatus which concerns on 2nd Embodiment of this invention. 本願発明の第3の実施の形態に係る冷凍装置の全体回路図である。It is a whole circuit diagram of the freezing apparatus which concerns on 3rd Embodiment of this invention. 本願発明の第4の実施の形態に係る冷凍装置の全体回路図である。It is a whole circuit diagram of the freezing apparatus which concerns on 4th Embodiment of this invention. 本願発明の第5の実施の形態に係る冷凍装置の全体回路図である。It is a whole circuit diagram of the freezing apparatus which concerns on 5th Embodiment of this invention. 従来の冷凍装置の全体回路図である。It is a whole circuit diagram of the conventional freezing apparatus.

以下、本願発明を好適な実施形態に基づいて具体的に説明する。   Hereinafter, the present invention will be specifically described based on preferred embodiments.

I:第1の実施形態
図1には、本願発明の第1の実施形態に係る冷凍装置Zの回路構成を示している。この冷凍装置Zは、次述の蒸気圧縮式冷凍機Xと吸収式冷凍機Yを組み合わせて構成され、室内の冷暖房に供せられる。
I: First Embodiment FIG. 1 shows a circuit configuration of a refrigeration apparatus Z according to a first embodiment of the present invention. This refrigeration apparatus Z is configured by combining a vapor compression refrigeration machine X and an absorption refrigeration machine Y described below, and is used for indoor air conditioning.

I−1:蒸気圧縮式冷凍機Xの構成
上記蒸気圧縮式冷凍機Xは、圧縮機1と四路切換弁2と利用側熱交換器3(即ち、室内機)と膨張弁4及びアキュームレーター5を、管路51〜管路57によって接続して構成され、上記四路切換弁2の切換操作によって冷房運転と暖房運転を選択的に実現するようになっている。即ち、上記圧縮機1の吐出側の管路51には上記四路切換弁2が備えられており、該四路切換弁2の切換えによって上記管路51は上記利用側熱交換器3に至る管路52(暖房運転時)とアキムレーター5に至る管路56(冷房運転時)に選択的に切り換えられ、上記利用側熱交換器3は冷房運転時には冷媒の蒸発作用をなし、暖房運転時には冷媒の凝縮作用を為す。
I-1: Configuration of Vapor Compression Refrigerator X The vapor compression chiller X includes a compressor 1, a four-way switching valve 2, a use-side heat exchanger 3 (that is, an indoor unit), an expansion valve 4, and an accumulator. 5 are connected by a pipe 51 to a pipe 57, and a cooling operation and a heating operation are selectively realized by a switching operation of the four-way switching valve 2. That is, the four-way switching valve 2 is provided in the discharge-side pipe 51 of the compressor 1, and the pipe 51 reaches the use-side heat exchanger 3 by switching the four-way switching valve 2. It is selectively switched between a pipeline 52 (during heating operation) and a pipeline 56 (during cooling operation) leading to the accumulator 5, and the use side heat exchanger 3 performs refrigerant evaporation during cooling operation, and during heating operation. The refrigerant condenses.

I−2:吸収式冷凍機Yの構成
上記吸収式冷凍機Yは、例えば、臭化リチュム(LiBr)を吸収液、水を冷媒として該吸収液への冷媒の吸収及び放出(再生)作用を利用して冷凍作用を為すものであって、発生器11と、空冷式の凝縮器14と、隣接配置された吸収器12及び蒸発器13と、空冷式の過冷却熱交換器15と、溶液熱交換器16と溶液ポンプ17を備え、これら各要素を管路61〜管路67によって接続して構成される。
I-2: Configuration of Absorption Refrigerator Y The absorption chiller Y has, for example, a function of absorbing and releasing (regenerating) refrigerant into the absorbing liquid using lithum bromide (LiBr) as an absorbing liquid and water as a refrigerant. Refrigeration is performed by using a generator 11, an air-cooled condenser 14, an adjacently disposed absorber 12 and evaporator 13, an air-cooled supercooling heat exchanger 15, and a solution. A heat exchanger 16 and a solution pump 17 are provided, and these components are connected by a pipeline 61 to a pipeline 67.

上記発生器11は、基本的にはエンジン等の排熱を駆動熱源として駆動されるものであって、排熱と溶液との間で熱交換を行なうために排熱用の熱交換器11aを内蔵している。   The generator 11 is basically driven by using exhaust heat from an engine or the like as a drive heat source, and a heat exchanger 11a for exhaust heat is provided to exchange heat between the exhaust heat and the solution. Built-in.

さらに、上記発生器11の上部と上記凝縮器14は管路61によって接続され、上記発生器11で発生した冷媒蒸気(水蒸気)を上記凝縮器14に流入させて凝縮するようになっている。   Furthermore, the upper part of the generator 11 and the condenser 14 are connected by a pipe 61 so that the refrigerant vapor (water vapor) generated by the generator 11 flows into the condenser 14 and condenses.

また、上記発生器11には上記溶液ポンプ17からの管路67と後述の吸収器12の出口側に接続される管路63が備えられており、該発生器11には上記吸収器12から希溶液が流入されるとともに、該発生器11内で濃縮された濃溶液は上記管路63から上記吸収器12の出口側へ送られるようになっている。   Further, the generator 11 is provided with a pipe line 67 from the solution pump 17 and a pipe line 63 connected to an outlet side of the absorber 12 which will be described later. As the dilute solution is introduced, the concentrated solution concentrated in the generator 11 is sent from the pipe 63 to the outlet side of the absorber 12.

上記吸収器12の出口側から上記発生器11へ向かう上記管路67と、該発生器11から上記吸収器12の出口側へ向かう上記管路63の間には、上記溶液熱交換器16が備えられ、該溶液熱交換器16においては上記管路63を流れる濃溶液と上記管路67を流れる希溶液の間で熱交換が行なわれ、該濃溶液側から希溶液側へ熱回収される。   The solution heat exchanger 16 is interposed between the pipe line 67 from the outlet side of the absorber 12 toward the generator 11 and the pipe line 63 from the generator 11 toward the outlet side of the absorber 12. In the solution heat exchanger 16, heat exchange is performed between the concentrated solution flowing through the pipe line 63 and the dilute solution flowing through the pipe line 67, and heat is recovered from the concentrated solution side to the diluted solution side. .

上記吸収器12は、上記発生器11からの濃溶液に、次述の蒸発器13で発生した冷媒蒸気を吸収させて希溶液とするものであって、該吸収器12には管路66から過冷却熱交換器15によって過冷却された後の溶液が流入される。   The absorber 12 absorbs the refrigerant vapor generated in the evaporator 13 described below into the concentrated solution from the generator 11 to form a dilute solution. The solution after being supercooled by the supercooling heat exchanger 15 is introduced.

上記蒸発器13は、一過性の蒸発機能をもつもので、熱交換器13aを内蔵している。そして、上記凝縮器14で凝縮された液冷媒を管路62から流入させ、該冷媒を上記熱交換器13aの表面を伝って流下させることで、該熱交換器13a内を流れる流体(この実施形態では、後述するように上記蒸気圧縮式冷凍機X側の冷媒)によってこれを加熱蒸発させて冷媒蒸気を発生させる。   The evaporator 13 has a temporary evaporation function and includes a heat exchanger 13a. Then, the liquid refrigerant condensed in the condenser 14 is introduced from the pipe 62, and the refrigerant flows down the surface of the heat exchanger 13a, whereby the fluid flowing in the heat exchanger 13a (this embodiment) In the embodiment, as will be described later, the refrigerant is heated and evaporated by the vapor compression refrigerator X side refrigerant) to generate refrigerant vapor.

上記蒸発器13において発生した冷媒蒸気は、上記吸収器12へ流入し、該吸収器12において上記過冷却熱交換器15側から流入する溶液に吸収される。また、上記蒸発器13での未蒸発冷媒も、上記吸収器12側へ流入し、該吸収器12内の溶液に吸収される。   The refrigerant vapor generated in the evaporator 13 flows into the absorber 12, and is absorbed by the solution flowing in from the supercooling heat exchanger 15 side in the absorber 12. Further, the non-evaporated refrigerant in the evaporator 13 also flows into the absorber 12 side and is absorbed by the solution in the absorber 12.

また、上記吸収器12の出口側の溶液(希溶液)は、上記溶液ポンプ17によって、上記過冷却熱交換器15と上記発生器11及び上記冷媒熱回収熱交換器6にそれぞれ送られる。   The solution (dilute solution) on the outlet side of the absorber 12 is sent to the supercooling heat exchanger 15, the generator 11, and the refrigerant heat recovery heat exchanger 6 by the solution pump 17.

I−3:特有の構成
ここで、この冷凍装置Zに特有の構成を説明する。
I-3: Specific Configuration Here, a configuration specific to the refrigeration apparatus Z will be described.

第1の構成は、上記蒸気圧縮式冷凍機Xの管路53、54を上記吸収式冷凍機Yの上記蒸発器13の熱交換器13aの両端に接続し、上記蒸気圧縮式冷凍機Xの冷房運転時には、上記圧縮機1で圧縮された後の冷媒を上記蒸発器13で過冷却する構成である。   In the first configuration, pipes 53 and 54 of the vapor compression refrigerator X are connected to both ends of the heat exchanger 13a of the evaporator 13 of the absorption refrigerator Y, and the vapor compression refrigerator X of the vapor compression refrigerator X is connected. In the cooling operation, the refrigerant after being compressed by the compressor 1 is supercooled by the evaporator 13.

第2の構成は、上記発生器11内に熱交換器11bを配置し、該熱交換器11bの両端を上記蒸気圧縮式冷凍機Xの冷媒管路54、55にそれぞれ接続している。そして、上記蒸気圧縮式冷凍機Xの冷房運転時には、上記圧縮機1において圧縮された冷媒を導入して冷媒熱を上記発生器11の溶液側に回収する。また、上記蒸気圧縮式冷凍機Xの暖房運転時には、上記吸収式冷凍機Yの上記蒸発器13での熱交換によって蒸発した上記蒸気圧縮式冷凍機X側の冷媒を導入してその蒸発温度を高めるようにした構成である。   In the second configuration, the heat exchanger 11b is arranged in the generator 11, and both ends of the heat exchanger 11b are connected to the refrigerant pipes 54 and 55 of the vapor compression refrigerator X, respectively. During the cooling operation of the vapor compression refrigerator X, the refrigerant compressed in the compressor 1 is introduced to recover the refrigerant heat to the solution side of the generator 11. Further, during the heating operation of the vapor compression refrigerator X, the refrigerant on the vapor compression refrigerator X side evaporated by heat exchange in the evaporator 13 of the absorption refrigerator Y is introduced and the evaporation temperature thereof is set. It is the structure made to raise.

第3の構成は、上記発生器11内に配置された上記熱交換器11bをバイパスするように上記管路54と管路55の間をバイパス路75で接続するとともに、該バイパス路75に電磁弁45を設けた構成である。そして、この電磁弁45を、上記蒸気圧縮式冷凍機Xの冷房運転時には上記蒸気圧縮式冷凍機X側の冷媒温度によって開閉弁する一方、上記蒸気圧縮式冷凍機Xの暖房運転時には上記電磁弁45を閉弁するようにしている。   In the third configuration, the pipe 54 and the pipe 55 are connected by a bypass 75 so as to bypass the heat exchanger 11b disposed in the generator 11, and the bypass 75 is electromagnetically coupled. The valve 45 is provided. The electromagnetic valve 45 is opened / closed by the refrigerant temperature on the vapor compression refrigerator X side during the cooling operation of the vapor compression refrigerator X, while the electromagnetic valve 45 is operated during the heating operation of the vapor compression refrigerator X. 45 is closed.

尚、上記蒸気圧縮式冷凍機Xの冷房運転時における上記電磁弁45の作動は、上記蒸気圧縮式冷凍機X側の上記バイパス路75の入口の冷媒の温度が設定温度未満である場合には上記電磁弁45を開弁し、冷媒の温度が設定温度以上である場合には上記電磁弁45を閉弁するように設定されている。   The operation of the solenoid valve 45 during the cooling operation of the vapor compression refrigerator X is performed when the temperature of the refrigerant at the inlet of the bypass passage 75 on the vapor compression refrigerator X side is lower than a set temperature. The solenoid valve 45 is opened, and the solenoid valve 45 is set to be closed when the temperature of the refrigerant is equal to or higher than a set temperature.

I−4:冷凍装置Zの作動説明
I−4−a:冷房運転時
上記蒸気圧縮式冷凍機Xの冷房運転時には、上記吸収式冷凍機Yも同時に運転される。そして、この冷房運転時には上記電磁弁45が上記蒸気圧縮式冷凍機X側の上記バイパス路75の入口の冷媒温度によって開閉弁される。
I-4: Explanation of Operation of Refrigeration Apparatus Z I-4-a: During Cooling Operation During the cooling operation of the vapor compression refrigeration machine X, the absorption chiller Y is also operated simultaneously. During the cooling operation, the solenoid valve 45 is opened and closed by the refrigerant temperature at the inlet of the bypass passage 75 on the vapor compression refrigerator X side.

上記バイパス路75の入口の冷媒温度が設定温度以上である場合には、上記電磁弁45が閉弁されるので、上記蒸気圧縮式冷凍機Xの上記圧縮機1において圧縮された後の高温の冷媒(ガス冷媒)は、上記四路切換弁2を経て上記吸収式冷凍機Y側の上記発生器11の熱交換器11bに流入し、ここで該熱交換器11bの外側に存在する溶液との間で熱交換を行なうことで、該冷媒の排熱が上記発生器11の溶液側へ回収され、該発生器11においてはこの回収熱が上記吸収式冷凍機Yの駆動熱源の一部として利用される。   When the refrigerant temperature at the inlet of the bypass passage 75 is equal to or higher than the set temperature, the solenoid valve 45 is closed, so that the high temperature after being compressed in the compressor 1 of the vapor compression refrigerator X is high. The refrigerant (gas refrigerant) flows into the heat exchanger 11b of the generator 11 on the absorption refrigeration machine Y side through the four-way switching valve 2, where the solution present outside the heat exchanger 11b and By exchanging heat between them, the exhaust heat of the refrigerant is recovered to the solution side of the generator 11, and this recovered heat is part of the drive heat source of the absorption refrigeration machine Y in the generator 11. Used.

従って、上記発生器11側への回収熱量が、管路60を通して供給されるエンジン等の排熱による熱量に加算され、この合算熱量を駆動熱源として上記発生器11が駆動される。この結果、上記蒸気圧縮式冷凍機X側の冷媒排熱の利用分だけ、上記発生器11をエンジン等の排熱のみで駆動する場合に比して、排熱の有効利用が促進され、例えば、エンジン等の排熱量が減少した場合でも、上記吸収式冷凍機Yを運転することができる。   Therefore, the amount of heat recovered toward the generator 11 is added to the amount of heat generated by exhaust heat from the engine or the like supplied through the pipe 60, and the generator 11 is driven using this combined amount of heat as a driving heat source. As a result, compared with the case where the generator 11 is driven only by exhaust heat from the engine or the like, the effective use of exhaust heat is promoted by the amount of use of refrigerant exhaust heat on the vapor compression refrigerator X side, for example, Even when the amount of exhaust heat from the engine or the like is reduced, the absorption refrigerator Y can be operated.

これに対して、上記バイパス路75の入口の冷媒温度が設定温度未満である場合には、上記電磁弁45が開弁されるので、上記蒸気圧縮式冷凍機Xの上記圧縮機1において圧縮された後の高温の冷媒は、上記四路切換弁2及び上記電磁弁45を経て、即ち、上記発生器11側への熱回収を行なうことなく、そのまま上記吸収式冷凍機Yの上記蒸発器13の熱交換器13a側に流入する。   On the other hand, when the refrigerant temperature at the inlet of the bypass passage 75 is lower than the set temperature, the solenoid valve 45 is opened, so that the compressor 1 of the vapor compression refrigerator X is compressed. After that, the high-temperature refrigerant passes through the four-way switching valve 2 and the electromagnetic valve 45, that is, without performing heat recovery to the generator 11 side, and the evaporator 13 of the absorption refrigerator Y as it is. Into the heat exchanger 13a side.

そして、冷媒が上記発生器11側の上記熱交換器11bに流入した場合(即ち、冷媒温度が設定温度以上である場合)には、この冷媒は該熱交換器11bでの熱交換によって凝縮されたのち、さらに上記蒸発器13において、上記吸収式冷凍機Y側の冷媒との間での熱交換によって冷却、または過冷却される。この過冷却冷媒が上記利用側熱交換器3に流入し、ここで蒸発するが、この場合、上記蒸発器13での過冷却によって冷媒温度が低下しているため、上記利用側熱交換器3における入口冷媒の比エンタルピーが低下し、該利用側熱交換器3で放熱される冷熱量が増加し、それだけ上記蒸気圧縮式冷凍機Xの冷房性能が改善される。   When the refrigerant flows into the heat exchanger 11b on the generator 11 side (that is, when the refrigerant temperature is equal to or higher than the set temperature), the refrigerant is condensed by heat exchange in the heat exchanger 11b. After that, the evaporator 13 is further cooled or supercooled by heat exchange with the refrigerant on the absorption refrigerator Y side. The supercooled refrigerant flows into the use side heat exchanger 3 and evaporates here. In this case, since the refrigerant temperature is lowered by the supercooling in the evaporator 13, the use side heat exchanger 3 is used. The specific enthalpy of the refrigerant at the inlet is reduced, the amount of cooling heat dissipated in the use side heat exchanger 3 is increased, and the cooling performance of the vapor compression refrigerator X is improved accordingly.

これに対して、冷媒が上記発生器11側の上記熱交換器11bに流入せずに、そのまま上記蒸発器13に流入した場合においても、該冷媒は上記蒸発器13において上記吸収式冷凍機Y側の冷媒との間での熱交換によって冷却、または過冷却される熱量は減少するが、上記利用側熱交換器3において蒸発し、冷房機能は発揮されることになる。   On the other hand, even when the refrigerant does not flow into the heat exchanger 11b on the generator 11 side, but flows into the evaporator 13 as it is, the refrigerant is absorbed by the absorption refrigerator Y in the evaporator 13. Although the amount of heat that is cooled or supercooled by heat exchange with the refrigerant on the side decreases, it evaporates in the use side heat exchanger 3 and the cooling function is exhibited.

II:第2の実施形態
図2には、本願発明の第2の実施形態に係る冷凍装置Zの回路構成を示している。この冷凍装置Zは、上記第1の実施形態に係る冷凍装置Zの回路構成を基本とし、この基本回路において、上記吸収式冷凍機Yの上記発生器11をバイパスするバイパス路75に設けられた上記電磁弁45第1電磁弁41の他に、上記吸収式冷凍機Yの上記吸収器12の出口から上記溶液ポンプ17を経て上記溶液熱交換器16に至る管路67に電磁弁41を設けるとともに、上記吸収式冷凍機Yの上記吸収器12の入口側の管路66と上記蒸発器13の冷媒入口側の管路62を、電磁弁43を備えた管路76によって接続して構成される。
II: Second Embodiment FIG. 2 shows a circuit configuration of a refrigeration apparatus Z according to a second embodiment of the present invention. This refrigeration apparatus Z is based on the circuit configuration of the refrigeration apparatus Z according to the first embodiment, and is provided in a bypass path 75 that bypasses the generator 11 of the absorption refrigeration machine Y in this basic circuit. In addition to the electromagnetic valve 45 and the first electromagnetic valve 41, the electromagnetic valve 41 is provided in a pipe 67 extending from the absorber 12 of the absorption refrigerator Y to the solution heat exchanger 16 through the solution pump 17. In addition, a pipe line 66 on the inlet side of the absorber 12 of the absorption refrigerator Y and a pipe line 62 on the refrigerant inlet side of the evaporator 13 are connected by a pipe 76 having an electromagnetic valve 43. The

そして、これら各電磁弁41,43,45の作動を以下のように設定している。即ち、上記電磁弁45は、上記蒸気圧縮式冷凍機Xの冷房運転時には上記蒸気圧縮式冷凍機X側の上記バイパス路75の入口の冷媒温度によって開閉弁され、暖房運転時には閉弁される。上記電磁弁41は、上記蒸気圧縮式冷凍機Xの冷房運転時には開弁され、暖房運転時には閉弁される。上記電磁弁43は、上記蒸気圧縮式冷凍機Xの冷房運転時には閉弁され、暖房運転時には開弁される。   The operation of each of the electromagnetic valves 41, 43, 45 is set as follows. That is, the electromagnetic valve 45 is opened and closed by the refrigerant temperature at the inlet of the bypass passage 75 on the vapor compression refrigerator X side during the cooling operation of the vapor compression refrigerator X, and is closed during the heating operation. The electromagnetic valve 41 is opened during the cooling operation of the vapor compression refrigerator X, and is closed during the heating operation. The electromagnetic valve 43 is closed during the cooling operation of the vapor compression refrigerator X, and is opened during the heating operation.

従って、この実施形態の冷凍装置Zでは、上記蒸気圧縮式冷凍機Xの冷房運転時と暖房運転時においてそれぞれ以下の作用効果が得られる。   Therefore, in the refrigeration apparatus Z of this embodiment, the following functions and effects can be obtained during the cooling operation and the heating operation of the vapor compression refrigerator X, respectively.

II−1:冷房運転時
上記蒸気圧縮式冷凍機Xの冷房運転時には、上記電磁弁45は上記蒸気圧縮式冷凍機X側の上記バイパス路75の入口の冷媒温度によって開閉弁され、上記電磁弁41は開弁され、上記電磁弁43は閉弁される。従って、その回路構成は、上記第1の発明に係る冷凍装置の冷房運転時における回路構成と同様となり、これと同様の作用効果が得られるので、その該当説明を援用し、ここでの説明を省略する。
II-1: During cooling operation During the cooling operation of the vapor compression refrigerator X, the solenoid valve 45 is opened and closed by the refrigerant temperature at the inlet of the bypass passage 75 on the vapor compression refrigerator X side. 41 is opened, and the solenoid valve 43 is closed. Accordingly, the circuit configuration is the same as the circuit configuration during the cooling operation of the refrigeration apparatus according to the first aspect of the invention, and the same operation and effect as this can be obtained. Omitted.

II−2:暖房運転時
上記蒸気圧縮式冷凍機Xの暖房運転時には、上記吸収式冷凍機Yの上記凝縮器14の運転を停止し、上記溶液ポンプ17のみを運転し、上記過冷却器15と上記蒸発器13の間で溶液を循環させる。なお、上記凝縮器14は運転停止されているため、上記吸収器12側へも溶液が流入するが、該吸収器12での吸収作用は行なわれない。また、上記発生器11への排熱の供給は継続される。
II-2: During heating operation During the heating operation of the vapor compression refrigerator X, the operation of the condenser 14 of the absorption refrigerator Y is stopped, only the solution pump 17 is operated, and the supercooler 15 is operated. And circulating the solution between the evaporator 13. In addition, since the condenser 14 is stopped, the solution also flows into the absorber 12 side, but the absorbing action in the absorber 12 is not performed. Further, the supply of exhaust heat to the generator 11 is continued.

そして、この状態において、上記電磁弁45と上記電磁弁43が開弁され、上記電磁弁41が閉弁される。   In this state, the solenoid valve 45 and the solenoid valve 43 are opened, and the solenoid valve 41 is closed.

従って、上記吸収式冷凍機Yの上記蒸発器13には上記溶液ポンプ17によって上記吸収式冷凍機Y側の溶液が循環され、上記蒸気圧縮式冷凍機X側の上記利用側熱交換器3において凝縮した後の冷媒は、上記蒸発器13において上記吸収式冷凍機Y側の溶液との熱交換によって吸熱することで蒸発する。   Therefore, the solution on the absorption refrigeration machine Y side is circulated through the evaporator 13 of the absorption refrigeration machine Y by the solution pump 17, and in the use side heat exchanger 3 on the vapor compression refrigeration machine X side. The condensed refrigerant evaporates by absorbing heat in the evaporator 13 by heat exchange with the solution on the absorption refrigerator Y side.

上記吸収式冷凍機Y側の溶液は蒸発器13内で冷却されるが、溶液ポンプにより過冷却熱交換器15に送られ、外気より熱を奪って温度が上がり、蒸発器13に送液される。また上記蒸発器13で蒸発した上記蒸気圧縮式冷凍機X側の冷媒は、上記発生器11内でエンジン等の排熱により加熱された溶液と熱交換器11bにより温度が上げられ、上記蒸気圧縮式冷凍機Xの上記圧縮機1側に吸入され、蒸気圧縮式冷凍機Xの冷媒の蒸発温度が上昇する。このため、例えば、上記発生器11に供給される排熱量が少なくても、上記蒸気圧縮式冷凍機Xの冷媒は外気より吸熱することで、蒸発温度が維持されることから、上記蒸気圧縮式冷凍機Xの暖房性能はそのままで、エンジン等の排熱により上記発生器11内の熱交換器11bでの加熱分が上記蒸気圧縮式冷凍機Xの暖房性能の改善に寄与することになる。   The solution on the absorption refrigerator Y side is cooled in the evaporator 13, but is sent to the supercooling heat exchanger 15 by the solution pump, takes heat from the outside air, rises in temperature, and is sent to the evaporator 13. The The refrigerant on the vapor compression refrigeration machine X side evaporated by the evaporator 13 is heated by the heat exchanger 11b and the solution heated by exhaust heat from the engine or the like in the generator 11, and the vapor compression The refrigerant is sucked into the compressor 1 side of the refrigerator 10 and the evaporation temperature of the refrigerant of the vapor compression refrigerator X is increased. For this reason, for example, even when the amount of exhaust heat supplied to the generator 11 is small, the refrigerant of the vapor compression refrigerator X absorbs heat from the outside air, so that the evaporation temperature is maintained. Heating performance of the heat exchanger 11b in the generator 11 contributes to improvement of the heating performance of the vapor compression refrigeration machine X due to exhaust heat from the engine or the like while the heating performance of the refrigerator X remains unchanged.

II−3: 以上のように、この実施形態の冷凍装置Zでは、冷房運転時と暖房運転時の双方において蒸気圧縮式冷凍機Xの性能改善効果が得られ、実用性に富む冷凍装置とされる。   II-3: As described above, in the refrigeration apparatus Z of this embodiment, the performance improvement effect of the vapor compression refrigeration machine X can be obtained both during the cooling operation and during the heating operation, and the refrigeration apparatus is highly practical. The

尚、上記以外の構成及び作用効果は上記第1の実施形態の冷凍装置Zと同様であるので、その該当説明を援用し、ここでの説明を省略する。   In addition, since the structure and effect other than the above are the same as that of the refrigerating apparatus Z of the said 1st Embodiment, the corresponding description is used and description here is abbreviate | omitted.

III:第3の実施形態
図3には、本願発明の第3の実施形態に係る冷凍装置Zの回路構成を示している。この冷凍装置Zは、上記第2の実施形態に係る冷凍装置Zの変形例として位置付けられるものである。即ち、上記第2の実施形態では、上記吸収式冷凍機Yの上記吸収器12の出口側と上記過冷却熱交換器15を接続する管路66に電磁弁41を設けていたのに対して、この第3の実施形態では、上記吸収式冷凍機Yの上記吸収器12の入口側の管路66を、電磁弁43を備えた管路77を介して上記蒸発器13に接続するとともに、上記吸収式冷凍機Yの上記吸収器12の入口側の管路66に電磁弁44を設けたものである。尚、上記発生器11をバイパスするバイパス路75に電磁弁45を、上記吸収器12の出口側から上記溶液ポンプ17を経て上記溶液熱交換器16に至る管路67に電磁弁41を設ける点は、上記第2実施形態の場合と同様である。
III: Third Embodiment FIG. 3 shows a circuit configuration of a refrigeration apparatus Z according to a third embodiment of the present invention. This refrigeration apparatus Z is positioned as a modified example of the refrigeration apparatus Z according to the second embodiment. That is, in the second embodiment, the electromagnetic valve 41 is provided in the conduit 66 connecting the outlet side of the absorber 12 of the absorption refrigerator Y and the supercooling heat exchanger 15. In this third embodiment, the inlet line 66 of the absorber 12 of the absorption refrigeration machine Y is connected to the evaporator 13 via a line 77 provided with an electromagnetic valve 43, and In the absorption refrigerator Y, an electromagnetic valve 44 is provided in a pipe line 66 on the inlet side of the absorber 12. A solenoid valve 45 is provided in a bypass passage 75 that bypasses the generator 11, and a solenoid valve 41 is provided in a pipeline 67 that leads from the outlet side of the absorber 12 to the solution heat exchanger 16 through the solution pump 17. Is the same as in the case of the second embodiment.

そして、この実施形態では、上記蒸気圧縮式冷凍機Xの冷房運転時には、上記電磁弁45は上記蒸気圧縮式冷凍機X側の上記バイパス路75の入口の冷媒温度によって開閉し、上記電磁弁43を閉弁し、上記電磁弁41と上記電磁弁43を開弁するようにしている。また、上記蒸気圧縮式冷凍機Xの暖房運転時には、上記電磁弁41と電磁弁44及び電磁弁45を閉弁し、上記電磁弁43を開弁するようにしている。   In this embodiment, during the cooling operation of the vapor compression refrigeration machine X, the electromagnetic valve 45 opens and closes depending on the refrigerant temperature at the inlet of the bypass passage 75 on the vapor compression refrigeration machine X side, and the electromagnetic valve 43 Is closed, and the solenoid valve 41 and the solenoid valve 43 are opened. Further, during the heating operation of the vapor compression refrigerator X, the solenoid valve 41, the solenoid valve 44, and the solenoid valve 45 are closed, and the solenoid valve 43 is opened.

従って、この実施形態の冷凍装置Zでは、上記蒸気圧縮式冷凍機Xの冷房運転時と暖房運転時においてそれぞれ以下の作用効果が得られる。   Therefore, in the refrigeration apparatus Z of this embodiment, the following functions and effects can be obtained during the cooling operation and the heating operation of the vapor compression refrigerator X, respectively.

III−1: 冷房運転時
上記蒸気圧縮式冷凍機Xの冷房運転時には、上記電磁弁45は上記蒸気圧縮式冷凍機X側の上記バイパス路75の入口の冷媒温度によって開閉し、上記電磁弁43が閉弁され、上記電磁弁41と電磁弁44が開弁されることから、その回路構成は、上記第1の発明に係る冷凍装置の冷房運転時における回路構成と同様となり、これと同様の作用効果が得られるので、その該当説明を援用し、ここでの説明を省略する。
III-1: During cooling operation During cooling operation of the vapor compression refrigerator X, the electromagnetic valve 45 opens and closes depending on the refrigerant temperature at the inlet of the bypass passage 75 on the vapor compression refrigerator X side, and the electromagnetic valve 43 Is closed and the solenoid valve 41 and the solenoid valve 44 are opened. Therefore, the circuit configuration is the same as the circuit configuration during the cooling operation of the refrigeration apparatus according to the first aspect of the invention. Since the effect is obtained, the corresponding explanation is cited and the explanation here is omitted.

III−2: 暖房運転時
上記蒸気圧縮式冷凍機Xの暖房運転時には、上記吸収式冷凍機Yにおいては、上記凝縮器14はその運転が停止され、上記溶液ポンプ17のみが運転される。また、上記発生器11への排熱の供給は継続される。そして、この状態で、上記電磁弁43は開弁され、上記電磁弁41と電磁弁45は閉弁される。
III-2: During heating operation During the heating operation of the vapor compression refrigerator X, in the absorption refrigerator Y, the operation of the condenser 14 is stopped and only the solution pump 17 is operated. Further, the supply of exhaust heat to the generator 11 is continued. In this state, the solenoid valve 43 is opened, and the solenoid valve 41 and the solenoid valve 45 are closed.

従って、上記吸収式冷凍機Yの上記蒸発器13には上記溶液ポンプ17によって上記吸収式冷凍機Y側の溶液が循環され、上記蒸気圧縮式冷凍機X側の上記利用側熱交換器3において凝縮した後の冷媒は、上記蒸発器13において上記吸収式冷凍機Y側の溶液との熱交換によって吸熱することで蒸発する。   Therefore, the solution on the absorption refrigeration machine Y side is circulated through the evaporator 13 of the absorption refrigeration machine Y by the solution pump 17, and in the use side heat exchanger 3 on the vapor compression refrigeration machine X side. The condensed refrigerant evaporates by absorbing heat in the evaporator 13 by heat exchange with the solution on the absorption refrigerator Y side.

上記吸収式冷凍機Y側の溶液は蒸発器13内で冷却されるが、溶液ポンプ17により過冷却熱交換器15に送られ、外気より熱を奪って温度が上がり、蒸発器13に送液される。また、上記蒸発器13で蒸発した上記蒸気圧縮式冷凍機X側の冷媒は、上記発生器11内でエンジン等の排熱により加熱された溶液と熱交換器11bにより温度が上げられ、上記蒸気圧縮式冷凍機Xの上記圧縮機1側に吸入され、蒸気圧縮式冷凍機Xの冷媒の蒸発温度が上昇する。このため、例えば、上記発生器11に供給される排熱量が少なくても、これに影響されることなく、上記蒸気圧縮式冷凍機Xの冷媒は外気より吸熱することで、蒸発温度が維持されることから、上記蒸気圧縮式冷凍機Xの暖房性能はそのままで、エンジン等の排熱により上記発生器11内の熱交換器11bでの加熱分が上記蒸気圧縮式冷凍機Xの暖房性能の改善に寄与することになる。   The solution on the absorption refrigeration machine Y side is cooled in the evaporator 13, but is sent to the supercooling heat exchanger 15 by the solution pump 17, deprived of heat from the outside air, rises in temperature, and is sent to the evaporator 13. Is done. The refrigerant on the vapor compression refrigerator X side evaporated by the evaporator 13 is heated by the heat exchanger 11b and the solution heated by exhaust heat from the engine or the like in the generator 11, and the vapor The refrigerant is sucked into the compressor 1 side of the compression refrigerator X, and the evaporation temperature of the refrigerant of the vapor compression refrigerator X increases. For this reason, for example, even if the amount of exhaust heat supplied to the generator 11 is small, the refrigerant of the vapor compression refrigeration machine X absorbs heat from the outside air without being affected by this, and the evaporation temperature is maintained. Therefore, the heating performance of the vapor compression refrigeration machine X is the same as that of the steam compression refrigeration machine X. It will contribute to improvement.

また、この実施形態では、上記蒸発器13における溶液散布用の散布器18を、冷媒液散布用の散布器として共用できるように一体に構成しているので、散布器の配置スペースの狭小化によって、上記蒸発器13のコンパクト化及び低コスト化が図れる。   Further, in this embodiment, the solution spraying device 18 in the evaporator 13 is integrally configured so that it can be shared as a refrigerant liquid spraying device. Thus, the evaporator 13 can be made compact and low in cost.

III−3: 以上のように、この実施形態の冷凍装置Zでは、冷房運転時と暖房運転時の双方において蒸気圧縮式冷凍機Xの性能改善効果が得られ、実用性に富む冷凍装置とされる。   III-3: As described above, in the refrigeration apparatus Z of this embodiment, the performance improvement effect of the vapor compression refrigeration machine X can be obtained both during the cooling operation and during the heating operation, and the refrigeration apparatus is highly practical. The

尚、上記以外の構成及び作用効果は上記第1の実施形態の冷凍装置Zと同様であるので、その該当説明を援用し、ここでの説明を省略する。   In addition, since the structure and effect other than the above are the same as that of the refrigerating apparatus Z of the said 1st Embodiment, the corresponding description is used and description here is abbreviate | omitted.

IV:第4の実施形態
図4には、本願発明の第4の実施形態に係る冷凍装置Zの回路構成を示している。この冷凍装置Zは、上記第3の実施形態に係る冷凍装置Zの回路構成を基本とし、この基本回路において、上記吸収式冷凍機Yの上記発生器11の排熱入口側の管路60に電磁弁46を設け、該電磁弁46を、上記蒸気圧縮式冷凍機Xの冷房運転時には開弁する一方、暖房運転時には上記発生器11の溶液温度が設定温度以上のときには閉弁し、該設定温度未満のときには開弁させるように構成したものである。
IV: Fourth Embodiment FIG. 4 shows a circuit configuration of a refrigeration apparatus Z according to a fourth embodiment of the present invention. This refrigeration apparatus Z is based on the circuit configuration of the refrigeration apparatus Z according to the third embodiment. In this basic circuit, the refrigeration apparatus Z is connected to a pipe 60 on the exhaust heat inlet side of the generator 11 of the absorption refrigeration machine Y. An electromagnetic valve 46 is provided. The electromagnetic valve 46 is opened during the cooling operation of the vapor compression refrigerator X, and is closed when the solution temperature of the generator 11 is equal to or higher than a set temperature during the heating operation. The valve is configured to open when the temperature is lower.

なお、上記発生器11をバイパスするバイパス路75に電磁弁45を、上記吸収器12の出口側から上記溶液ポンプ17を経て上記溶液熱交換器16に至る管路67に電磁弁41を、上記吸収器12の入口側の管路66と上記蒸発器13を接続する管路69に電磁弁43を、さらに上記吸収式冷凍機Yの上記吸収器12の入口側の管路66に電磁弁44を設けた点は、上記第3実施形態の場合と同様である。   The electromagnetic valve 45 is connected to the bypass passage 75 that bypasses the generator 11, the electromagnetic valve 41 is connected to the conduit 67 that leads from the outlet side of the absorber 12 to the solution heat exchanger 16 via the solution pump 17, The electromagnetic valve 43 is connected to a pipe line 69 connecting the inlet 66 of the absorber 12 and the evaporator 13, and the electromagnetic valve 44 is further connected to the pipe line 66 of the absorption refrigerator Y on the inlet side of the absorber 12. The point provided with is the same as in the case of the third embodiment.

従って、この実施形態の冷凍装置Zでは、上記蒸気圧縮式冷凍機Xの冷房運転時と暖房運転時においてそれぞれ以下の作用効果が得られる。   Therefore, in the refrigeration apparatus Z of this embodiment, the following functions and effects can be obtained during the cooling operation and the heating operation of the vapor compression refrigerator X, respectively.

IV−1: 冷房運転時
上記蒸気圧縮式冷凍機Xの冷房運転時には、上記電磁弁41と電磁弁44が開弁され、上記電磁弁45は上記蒸気圧縮式冷凍機X側の上記バイパス路75の入口の冷媒温度によって開閉し、上記電磁弁43が閉弁される。また上記発生器11内の溶液温度が設定温度以上のときには上記電磁弁46が閉弁されて、該設定温度未満のときには開弁される。従って、その回路構成は、上記第1の発明に係る冷凍装置の冷房運転時における回路構成と同様となり、これと同様の作用効果が得られるので、その該当説明を援用し、ここでの説明を省略する。
IV-1: During cooling operation During the cooling operation of the vapor compression refrigerator X, the solenoid valve 41 and the solenoid valve 44 are opened, and the solenoid valve 45 is connected to the bypass passage 75 on the vapor compression refrigerator X side. The solenoid valve 43 is closed by opening and closing according to the refrigerant temperature at the inlet. The electromagnetic valve 46 is closed when the solution temperature in the generator 11 is equal to or higher than the set temperature, and is opened when the temperature is lower than the set temperature. Accordingly, the circuit configuration is the same as the circuit configuration during the cooling operation of the refrigeration apparatus according to the first aspect of the invention, and the same operation and effect as this can be obtained. Omitted.

IV−2: 暖房運転時
上記蒸気圧縮式冷凍機Xの暖房運転時には、上記吸収式冷凍機Yにおいては、上記凝縮器14はその運転が停止され、上記溶液ポンプ17のみが運転される。そして、この状態で、上記電磁弁43は開弁され、上記電磁弁41と電磁弁44及び電磁弁45は閉弁される。また、上記電磁弁46は、上記発生器11の溶液温度が設定温度以上のときには閉弁され、該設定温度未満のときには開弁される。
IV-2: During heating operation During the heating operation of the vapor compression refrigerator X, in the absorption refrigerator Y, the operation of the condenser 14 is stopped, and only the solution pump 17 is operated. In this state, the solenoid valve 43 is opened, and the solenoid valve 41, the solenoid valve 44, and the solenoid valve 45 are closed. The electromagnetic valve 46 is closed when the solution temperature of the generator 11 is equal to or higher than a set temperature, and is opened when the temperature is lower than the set temperature.

従って、上記吸収式冷凍機Yの上記蒸発器13には上記溶液ポンプ17によって上記吸収式冷凍機Y側の溶液が循環され、上記蒸気圧縮式冷凍機X側の上記利用側熱交換器3において凝縮した後の冷媒は、上記蒸発器13に流入する上記吸収式冷凍機Y側の溶液との間の熱交換によって吸熱することで蒸発する。   Therefore, the solution on the absorption refrigeration machine Y side is circulated through the evaporator 13 of the absorption refrigeration machine Y by the solution pump 17, and in the use side heat exchanger 3 on the vapor compression refrigeration machine X side. The condensed refrigerant evaporates by absorbing heat by heat exchange with the solution on the absorption refrigerator Y side flowing into the evaporator 13.

上記吸収式冷凍機Y側の溶液は蒸発器13内で冷却されるが、溶液ポンプにより過冷却熱交換器15に送られ、外気より熱を奪って温度が上がり、蒸発器13に送液される。また、上記蒸発器13で蒸発した上記蒸気圧縮式冷凍機X側の冷媒は、上記発生器11内でエンジン等の排熱により加熱された溶液と熱交換器11bにより温度が上げられ、上記蒸気圧縮式冷凍機Xの上記圧縮機1側に吸入され、蒸気圧縮式冷凍機Xの冷媒の蒸発温度が上昇する。上記発生器11での熱の授受はない。このため、例えば、上記発生器11に供給される排熱量が少なくても、これに影響されることなく、上記蒸気圧縮式冷凍機Xの冷媒は外気より吸熱することで、蒸発温度が維持されることから、上記蒸気圧縮式冷凍機Xの暖房性能はそのままで、エンジン等の排熱により上記発生器11内の熱交換器11bでの加熱分が上記蒸気圧縮式冷凍機Xの暖房性能の改善に寄与することになる。   The solution on the absorption refrigerator Y side is cooled in the evaporator 13, but is sent to the supercooling heat exchanger 15 by the solution pump, takes heat from the outside air, rises in temperature, and is sent to the evaporator 13. The The refrigerant on the vapor compression refrigerator X side evaporated by the evaporator 13 is heated by the heat exchanger 11b and the solution heated by exhaust heat from the engine or the like in the generator 11, and the vapor The refrigerant is sucked into the compressor 1 side of the compression refrigerator X, and the evaporation temperature of the refrigerant of the vapor compression refrigerator X increases. There is no heat exchange in the generator 11. For this reason, for example, even if the amount of exhaust heat supplied to the generator 11 is small, the refrigerant of the vapor compression refrigeration machine X absorbs heat from the outside air without being affected by this, and the evaporation temperature is maintained. Therefore, the heating performance of the vapor compression refrigeration machine X is the same as that of the steam compression refrigeration machine X. It will contribute to improvement.

また、上記発生器11内の溶液温度が設定温度以上のときには上記電磁弁46が閉弁されて上記発生器11への排熱の供給が中断され、該設定温度未満のときには上記電磁弁46が開弁されて該発生器11に排熱が供給されることで、上記発生器11内の溶液温度が常時適正に保たれる。   Further, when the solution temperature in the generator 11 is equal to or higher than the set temperature, the electromagnetic valve 46 is closed, and the supply of exhaust heat to the generator 11 is interrupted. When the temperature is lower than the set temperature, the electromagnetic valve 46 is When the valve 11 is opened and exhaust heat is supplied to the generator 11, the solution temperature in the generator 11 is always kept appropriate.

さらに、上記電磁弁44が閉弁されることで、上記過冷却熱交換器15からの溶液の全量が上記蒸発器13側に流入するため、例えば、上記過冷却熱交換器15からの溶液の一部しか上記蒸発器13に流入しない場合に比して、該蒸発器13での上記蒸気圧縮式冷凍機X側の冷媒の熱交換作用が促進され、該冷媒の蒸発温度が高められ、その結果、上記蒸気圧縮式冷凍機Xの上記利用側熱交換器3での冷媒の凝縮に伴う放熱量が増加し、それだけ上記蒸気圧縮式冷凍機Xの暖房性能が改善されることになる。   Further, since the entire amount of the solution from the supercooling heat exchanger 15 flows into the evaporator 13 side by closing the solenoid valve 44, for example, the solution of the solution from the supercooling heat exchanger 15 is supplied. Compared to the case where only a part of the refrigerant flows into the evaporator 13, the heat exchange action of the refrigerant on the vapor compression refrigerator X side in the evaporator 13 is promoted, and the evaporation temperature of the refrigerant is increased. As a result, the heat radiation amount accompanying the condensation of the refrigerant in the use side heat exchanger 3 of the vapor compression refrigerator X increases, and the heating performance of the vapor compression refrigerator X is improved accordingly.

また、この実施形態では、上記蒸発器13における溶液散布用の散布器18と冷媒液散布用の散布器19を別体構成としているので、本来的に設けられている冷媒散布用の上記散布器19における上記蒸発器13のコイルへの冷媒の適正な散布状態を維持したまま、上記蒸発器13のコイルへの溶液の散布が適正に行なわれるよう上記溶液散布用の散布器18の構造あるいは設置位置を設定することができる。   Further, in this embodiment, the sprayer 18 for spraying the solution and the sprayer 19 for spraying the refrigerant liquid in the evaporator 13 are configured separately, so that the above-mentioned sprayer for spraying the refrigerant originally provided. The structure or installation of the sprayer 18 for spraying the solution so that the solution can be sprayed properly to the coil of the evaporator 13 while maintaining the proper spraying state of the refrigerant to the coil of the evaporator 13 in 19. The position can be set.

V:第5の実施形態
図5には、本願発明の第5の実施形態に係る冷凍装置Zの回路構成を示している。この冷凍装置Zは、上記第3の実施形態に係る冷凍装置Zの変形例として位置付けられるものである。即ち、上記第3の実施形態に係る冷凍装置Zでは一台の蒸気圧縮式冷凍機Xと一台の吸収式冷凍機Yで上記冷凍装置Zを構成していたのに対して、この第5の実施形態に係る冷凍装置Zでは、これを二台の蒸気圧縮式冷凍機Xと一台の吸収式冷凍機Yで構成するとともに、該蒸気圧縮式冷凍機Xの設置数の増加に対応して、上記吸収式冷凍機Yの上記発生器11に二つの熱交換11b,11bを配置し、これら各熱交換器11b、11bの両端をそれぞれ上記二台の蒸気圧縮式冷凍機Xの冷媒の管路54,55に接続し、該各蒸気圧縮式冷凍機Xの冷媒の排熱をそれぞれ対応する熱交換器11b,11bを介して上記吸収式冷凍機Yの溶液側へ回収し、この回収された排熱を一台の上記吸収式冷凍機Yの上記発生器11に供給するように構成したものである。
V: Fifth Embodiment FIG. 5 shows a circuit configuration of a refrigeration apparatus Z according to a fifth embodiment of the present invention. This refrigeration apparatus Z is positioned as a modified example of the refrigeration apparatus Z according to the third embodiment. That is, in the refrigerating apparatus Z according to the third embodiment, the refrigerating apparatus Z is configured by one vapor compression refrigerating machine X and one absorption refrigerating machine Y. In the refrigeration apparatus Z according to the embodiment, this is constituted by two vapor compression refrigeration machines X and one absorption refrigeration machine Y, and the increase in the number of installed vapor compression refrigeration machines X is supported. Then, two heat exchanges 11b, 11b are arranged in the generator 11 of the absorption refrigeration machine Y, and both ends of the heat exchangers 11b, 11b are respectively connected to the refrigerant of the two vapor compression refrigeration machines X. Connected to the pipes 54 and 55, the exhaust heat of the refrigerant of each vapor compression refrigerator X is recovered to the solution side of the absorption refrigerator Y via the corresponding heat exchangers 11b and 11b. Configured to supply the exhausted heat to the generator 11 of the single absorption refrigerator Y Those were.

係る構成によれば、上記蒸気圧縮式冷凍機Xの冷媒側から上記吸収式冷凍機Yの発生器11側への回収熱量が大きくなることから、例えば、エンジン等の排熱が少ない場合でも、回収した冷媒排熱を有効に使って上記吸収式冷凍機Yを適正に運転させることができ、その結果、該吸収式冷凍機Yの蒸発器13での熱交換によって上記各蒸気圧縮式冷凍機Xの冷媒を十分に過冷却することが可能となり、延いては上記冷凍装置Z全体の性能改善効果を得ることができる。   According to such a configuration, since the amount of recovered heat from the refrigerant side of the vapor compression refrigeration machine X to the generator 11 side of the absorption refrigeration machine Y increases, for example, even when there is little exhaust heat from the engine or the like, The absorption refrigeration machine Y can be appropriately operated by effectively using the recovered refrigerant exhaust heat, and as a result, each of the vapor compression refrigeration machines by heat exchange in the evaporator 13 of the absorption refrigeration machine Y. The refrigerant of X can be sufficiently subcooled, and as a result, the performance improvement effect of the entire refrigeration apparatus Z can be obtained.

また、上記蒸気圧縮式冷凍機Xの並置台数には制約は無く、必要に応じて並置台数を設定すれば良い。   Moreover, there is no restriction | limiting in the juxtaposition number of the said vapor compression type refrigerator X, What is necessary is just to set the juxtaposition number as needed.

1 ・・圧縮機
2 ・・四路切換弁
3 ・・利用側熱交換器
4 ・・膨張弁
5 ・・アキュームレーター
7 ・・熱源側熱交換器
11 ・・発生器
12 ・・吸収器
13 ・・蒸発器
14 ・・凝縮器
15 ・・過冷却熱交換器
16 ・・溶液熱交換器
17 ・・溶液ポンプ
18、19・・散布器
41 ・・電磁弁
43 ・・電磁弁
44 ・・電磁弁
45 ・・電磁弁
51〜57 ・・管路
61〜67 ・・管路
75〜77 ・・管路
X ・・蒸気圧縮式冷凍機
Y ・・吸収式冷凍機
Z ・・冷凍装置
1 ·· Compressor 2 ·· Four-way switching valve 3 ·· Use side heat exchanger 4 ·· Expansion valve 5 ·· Accumulator 7 ·· Heat source side heat exchanger 11 ·· Generator 12 ·· Absorber 13 ·・ Evaporator 14 ・ ・ Condenser 15 ・ ・ Supercooling heat exchanger 16 ・ ・ Solution heat exchanger 17 ・ ・ Solution pump 18, 19 ・ ・ Sprayer 41 ・ ・ Solenoid valve 43 ・ ・ Solenoid valve 44 ・ ・ Solenoid valve 45 .. Solenoid valves 51 to 57 .. Pipe lines 61 to 67 .. Pipe lines 75 to 77 .. Pipe lines X .. Vapor compression type refrigerator Y .. Absorption type refrigerator Z.

Claims (8)

蒸気圧縮式冷凍機(X)とエンジン等の排熱で駆動される吸収式冷凍機(Y)とを備えて構成される冷凍装置であって、
上記吸収式冷凍機(Y)の吸収器(12)に流入する溶液を空冷式の過冷却熱交換器(15)によって過冷却して上記吸収器(12)へ流入させるとともに、上記蒸気圧縮式冷凍機(X)の冷媒と上記吸収式冷凍機(Y)の発生器(11)内の溶液との間で熱交換可能に構成する一方、
上記蒸気圧縮式冷凍機(X)の冷媒回路に、上記吸収式冷凍機(Y)の上記発生器(11)をバイパスして該吸収式冷凍機(Y)の上記蒸発器(13)に接続されるバイパス路(70)を設けるとともに該バイパス路(75)に電磁弁(45)を備え、
上記蒸気圧縮式冷凍機(X)の冷房運転時で且つ上記バイパス路75の入口の冷媒の温度が設定温度未満である場合には上記電磁弁(45)を開弁し、冷媒の温度が設定温度以上である場合には上記電磁弁(45)を閉弁する一方、
上記蒸気圧縮式冷凍機(X)の暖房運転時には上記電磁弁(45)を閉弁することを特徴とする冷凍装置。
A refrigerating apparatus comprising a vapor compression refrigerator (X) and an absorption refrigerator (Y) driven by exhaust heat from an engine or the like,
The solution flowing into the absorber (12) of the absorption refrigerator (Y) is supercooled by the air-cooled supercooling heat exchanger (15) and flows into the absorber (12), and the vapor compression type While configured to be able to exchange heat between the refrigerant of the refrigerator (X) and the solution in the generator (11) of the absorption refrigerator (Y),
The refrigerant circuit of the vapor compression refrigerator (X) is connected to the evaporator (13) of the absorption refrigerator (Y) by bypassing the generator (11) of the absorption refrigerator (Y). A bypass path (70) to be provided and a solenoid valve (45) provided in the bypass path (75),
During the cooling operation of the vapor compression refrigerator (X) and when the refrigerant temperature at the inlet of the bypass passage 75 is lower than the set temperature, the electromagnetic valve (45) is opened to set the refrigerant temperature. When the temperature is higher than the temperature, the solenoid valve (45) is closed,
The refrigerating apparatus characterized in that the electromagnetic valve (45) is closed during heating operation of the vapor compression refrigerator (X).
請求項1において、
上記吸収式冷凍機(Y)の上記吸収器(12)の出口から溶液ポンプ(17)を経て溶液熱交換器(16)に至る管路(67)に電磁弁(41)を設けるとともに、上記吸収式冷凍機(Y)の上記吸収器(12)の入口側の管路(66)と上記蒸発器(13)の冷媒入口側の管路(62)を、電磁弁(43)を備えた管路(76)によって接続し、
上記蒸気圧縮式冷凍機(X)の冷房運転時には上記電磁弁(45)は上記蒸気圧縮式冷凍機X側の上記バイパス路75の入口の冷媒温度によって開閉し、上記電磁弁(43)を閉弁し、電磁弁(41)を開弁する一方、
上記蒸気圧縮式冷凍機(X)の暖房運転時には上記電磁弁(43)を開弁し、上記電磁弁(41)と電磁弁(45)を閉弁するように構成したことを特徴とする冷凍装置。
In claim 1,
A solenoid valve (41) is provided in a pipe line (67) from the outlet of the absorber (12) of the absorption refrigerator (Y) to the solution heat exchanger (16) through the solution pump (17), and The absorption-type refrigerator (Y) has an electromagnetic valve (43), the pipe (66) on the inlet side of the absorber (12) and the pipe (62) on the refrigerant inlet side of the evaporator (13). Connected by conduit (76),
During the cooling operation of the vapor compression refrigeration machine (X), the electromagnetic valve (45) is opened and closed by the refrigerant temperature at the inlet of the bypass passage 75 on the vapor compression refrigeration machine X side, and the electromagnetic valve (43) is closed. While opening the solenoid valve (41),
In the heating operation of the vapor compression refrigerator (X), the solenoid valve (43) is opened, and the solenoid valve (41) and the solenoid valve (45) are closed. apparatus.
請求項1において、
上記吸収式冷凍機(Y)の上記吸収器(12)の出口から溶液ポンプ(17)を経て溶液熱交換器(16)に至る管路(67)に電磁弁(41)を設けるとともに、上記吸収式冷凍機(Y)の上記吸収器(12)の入口側の管路(66)を、上記電磁弁(43)を備えた管路(77)を介して上記蒸発器(13)に接続し、
上記蒸気圧縮式冷凍機(X)の冷房運転時には上記電磁弁(45)は上記蒸気圧縮式冷凍機X側の上記バイパス路75の入口の冷媒温度によって開閉し、上記電磁弁(43)を閉弁し、電磁弁41を開弁する一方、
上記蒸気圧縮式冷凍機(X)の暖房運転時には上記電磁弁(43)を開弁し、上記電磁弁(41)と電磁弁(45)を閉弁するように構成したことを特徴とする冷凍装置。
In claim 1,
A solenoid valve (41) is provided in a pipe line (67) from the outlet of the absorber (12) of the absorption refrigerator (Y) to the solution heat exchanger (16) through the solution pump (17), and The pipe (66) on the inlet side of the absorber (12) of the absorption refrigerator (Y) is connected to the evaporator (13) through a pipe (77) provided with the electromagnetic valve (43). And
During the cooling operation of the vapor compression refrigeration machine (X), the electromagnetic valve (45) is opened and closed by the refrigerant temperature at the inlet of the bypass passage 75 on the vapor compression refrigeration machine X side, and the electromagnetic valve (43) is closed. While opening the solenoid valve 41,
In the heating operation of the vapor compression refrigerator (X), the solenoid valve (43) is opened, and the solenoid valve (41) and the solenoid valve (45) are closed. apparatus.
請求項2又は3において、
上記吸収式冷凍機(Y)の上記吸収器(12)の入口側の管路(66)に電磁弁(44)を設け、
上記蒸気圧縮式冷凍機(X)の冷房運転時には上記電磁弁(44)を開弁し、暖房運転時には上記電磁弁(44)を閉弁するように構成したことを特徴とする冷凍装置。
In claim 2 or 3,
An electromagnetic valve (44) is provided on the inlet line (66) of the absorber (12) of the absorption refrigerator (Y),
A refrigerating apparatus configured to open the solenoid valve (44) during cooling operation of the vapor compression refrigerator (X) and close the solenoid valve (44) during heating operation.
請求項1,2,3又は4において、
上記発生器(11)の排熱入口側の管路(60)に電磁弁(46)を設け、上記発生器(11)の溶液温度が設定温度以上のとき上記電磁弁(46)を閉弁し、該設定温度未満のとき上記電磁弁(46)を開弁させるように構成したことを特徴とする冷凍装置。
In claim 1, 2, 3 or 4,
A solenoid valve (46) is provided in the pipe (60) on the exhaust heat inlet side of the generator (11), and the solenoid valve (46) is closed when the solution temperature of the generator (11) is equal to or higher than a set temperature. The refrigeration apparatus is configured to open the solenoid valve (46) when the temperature is lower than the set temperature.
請求項3又は4において、
上記蒸発器(13)における溶液散布用の散布器と冷媒液散布用の散布器を、別体構成又は共用可能な一体構成としたことを特徴とする冷凍装置。
In claim 3 or 4,
The refrigeration apparatus characterized in that the sprayer for spraying the solution and the sprayer for spraying the refrigerant liquid in the evaporator (13) have a separate structure or an integrated structure that can be shared.
請求項1,2,3,4,5又は6において、
上記蒸発器(13)は、冷媒液が一過性で該蒸発器(13)の伝熱面を流れ、未蒸発の冷媒液は上記吸収器(12)側へ移動して該吸収器(12)側の溶液に吸収されるように構成したことを特徴とする冷凍装置。
In claim 1, 2, 3, 4, 5 or 6,
In the evaporator (13), the refrigerant liquid is transient and flows on the heat transfer surface of the evaporator (13), and the non-evaporated refrigerant liquid moves to the absorber (12) side and moves to the absorber (12). The refrigeration apparatus is configured to be absorbed by the solution on the side.
請求項1,2,3,4,5,6又は7において、
上記蒸気圧縮式冷凍機(X)を複数台設置して該各蒸気圧縮式冷凍機(X)の冷媒の排熱を上記吸収式冷凍機(Y)の上記発生器(11)で回収するように構成したことを特徴とする冷凍装置。
In claim 1, 2, 3, 4, 5, 6 or 7,
A plurality of the vapor compression refrigerators (X) are installed, and the exhaust heat of the refrigerant of each vapor compression refrigerator (X) is recovered by the generator (11) of the absorption refrigerator (Y). A refrigeration apparatus characterized by comprising the above.
JP2009093124A 2009-04-07 2009-04-07 Refrigeration equipment Expired - Fee Related JP5434208B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2009093124A JP5434208B2 (en) 2009-04-07 2009-04-07 Refrigeration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009093124A JP5434208B2 (en) 2009-04-07 2009-04-07 Refrigeration equipment

Publications (2)

Publication Number Publication Date
JP2010243085A true JP2010243085A (en) 2010-10-28
JP5434208B2 JP5434208B2 (en) 2014-03-05

Family

ID=43096267

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2009093124A Expired - Fee Related JP5434208B2 (en) 2009-04-07 2009-04-07 Refrigeration equipment

Country Status (1)

Country Link
JP (1) JP5434208B2 (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0894202A (en) * 1994-09-22 1996-04-12 Saburo Kubo Air conditioner
JPH1123092A (en) * 1997-06-30 1999-01-26 Daikin Ind Ltd Heat storage device
JPH11281193A (en) * 1998-03-27 1999-10-15 Sanyo Electric Co Ltd Air conditioner
JP2000018762A (en) * 1998-07-06 2000-01-18 Daikin Ind Ltd Absorption refrigeration equipment
JP2003004334A (en) * 2001-06-25 2003-01-08 Ebara Corp Waste heat recovery air conditioner
JP2003121025A (en) * 2001-10-10 2003-04-23 Tokyo Gas Co Ltd Combined cooling and heating system
JP2006017350A (en) * 2004-06-04 2006-01-19 Sanyo Electric Co Ltd Refrigeration device
JP2009058181A (en) * 2007-08-31 2009-03-19 Daikin Ind Ltd Absorption refrigeration system

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0894202A (en) * 1994-09-22 1996-04-12 Saburo Kubo Air conditioner
JPH1123092A (en) * 1997-06-30 1999-01-26 Daikin Ind Ltd Heat storage device
JPH11281193A (en) * 1998-03-27 1999-10-15 Sanyo Electric Co Ltd Air conditioner
JP2000018762A (en) * 1998-07-06 2000-01-18 Daikin Ind Ltd Absorption refrigeration equipment
JP2003004334A (en) * 2001-06-25 2003-01-08 Ebara Corp Waste heat recovery air conditioner
JP2003121025A (en) * 2001-10-10 2003-04-23 Tokyo Gas Co Ltd Combined cooling and heating system
JP2006017350A (en) * 2004-06-04 2006-01-19 Sanyo Electric Co Ltd Refrigeration device
JP2009058181A (en) * 2007-08-31 2009-03-19 Daikin Ind Ltd Absorption refrigeration system

Also Published As

Publication number Publication date
JP5434208B2 (en) 2014-03-05

Similar Documents

Publication Publication Date Title
JP2011133123A (en) Refrigerating cycle device
JP2008202853A (en) Absorption type heat pump system
JP5375283B2 (en) Refrigeration equipment
JP4909245B2 (en) Absorption system operation method and absorption system
JP5240040B2 (en) Refrigeration equipment
JP5229076B2 (en) Refrigeration equipment
KR100983092B1 (en) Apparatus for saving cooling and heating energy using heat pump
JP5402186B2 (en) Refrigeration equipment
JP5434206B2 (en) Refrigeration equipment
JP5434207B2 (en) Refrigeration equipment
CN114111110A (en) Heat pump system with plate for exchanging supercooling
JP6613404B2 (en) Refrigeration system
JP5434208B2 (en) Refrigeration equipment
JP5375284B2 (en) Refrigeration equipment
JP3664587B2 (en) Air conditioner
JP5310224B2 (en) Refrigeration equipment
JP2009236440A (en) Gas heat pump type air conditioning device or refrigerating device
JP4273727B2 (en) Refrigeration system
CN210070284U (en) A heat pump unit containing multiple cold and heat source heat exchangers
JP5402187B2 (en) Refrigeration equipment
KR100827569B1 (en) Absorption refrigerating apparatus with heat pump
JP3892689B2 (en) Combined cooling device and cooling operation method thereof
CN119178251B (en) A low ambient temperature air source heat pump system and method for constant temperature hot water supply
JP3780643B2 (en) Absorption refrigeration system
KR101076923B1 (en) An absorption type chiller-heater respondable to the heating load conditions

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20111207

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20120104

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20130228

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20130305

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20130502

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20131112

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20131125

LAPS Cancellation because of no payment of annual fees