JPS6158745B2 - - Google Patents
Info
- Publication number
- JPS6158745B2 JPS6158745B2 JP9883778A JP9883778A JPS6158745B2 JP S6158745 B2 JPS6158745 B2 JP S6158745B2 JP 9883778 A JP9883778 A JP 9883778A JP 9883778 A JP9883778 A JP 9883778A JP S6158745 B2 JPS6158745 B2 JP S6158745B2
- Authority
- JP
- Japan
- Prior art keywords
- heating
- evaporator
- refrigerator
- heat
- absorption
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000010438 heat treatment Methods 0.000 claims description 34
- 238000010521 absorption reaction Methods 0.000 claims description 23
- 238000001816 cooling Methods 0.000 claims description 19
- 238000004378 air conditioning Methods 0.000 claims description 8
- 238000005057 refrigeration Methods 0.000 claims description 5
- 230000006835 compression Effects 0.000 claims description 3
- 238000007906 compression Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000003507 refrigerant Substances 0.000 description 5
- 239000012530 fluid Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000003350 kerosene Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は、ガス又は灯油を燃焼させて冷房用冷
水又は暖房用温水を生成できる直焚式の吸収冷凍
機と、電動機によつて駆動される往復動圧縮機、
スクリユー圧縮機等を冷凍サイクルの構成要素と
する加圧式冷凍機とを熱媒配管によつて組み合わ
せた冷暖房装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a direct-fired absorption refrigerator capable of producing cold water for cooling or hot water for heating by burning gas or kerosene, a reciprocating compressor driven by an electric motor,
The present invention relates to a heating and cooling system in which a pressurized refrigerator having a screw compressor or the like as a component of the refrigeration cycle is combined through heat medium piping.
従来より、冷房用と暖房用とに共用できる冷凍
機は各種のものが実用に供されている。例えば、
往復動圧縮機やスクリユー圧縮機等を電動機で駆
動してフレオン等の冷媒を加圧し、この冷媒の凝
縮潜熱をもつて暖房、気化潜熱をもつて冷房に利
用する加圧式冷凍機は、冷房時の温度が0℃以下
の任意の低温が得られる反面、暖房時の温度は45
〜50℃を実用上の限界温度とする。一方、ガスや
灯油を燃焼させて吸収液と冷媒とを加熱分離し、
この冷媒の気化潜熱をもつて冷房、吸収液又は冷
房の顕熱および潜熱をもつて暖房に利用する吸収
式冷凍機は、暖房時の温度が70℃以上の高温を得
られる反面、冷房時の温度は6℃迄の冷却を実用
上の限界温度としている。 Conventionally, various types of refrigerators that can be used for both cooling and heating have been put into practical use. for example,
A pressurized refrigerator drives a reciprocating compressor or screw compressor with an electric motor to pressurize a refrigerant such as Freon, and uses the latent heat of condensation of this refrigerant for heating and the latent heat of vaporization for cooling. While the temperature can be any low temperature below 0℃, the temperature during heating is 45℃.
The practical limit temperature is ~50℃. On the other hand, the absorption liquid and refrigerant are separated by heating by burning gas or kerosene.
Absorption refrigerators use the latent heat of vaporization of the refrigerant for cooling, and the absorption liquid or the sensible heat and latent heat of the cooling for heating. The practical limit temperature is 6°C.
このため、特開昭51−3039号公報に吸収冷凍機
と圧縮式冷凍機とを組み合わせて冷房時に充分に
低温の熱媒を得るようにしたシステムが提示され
ているが、暖房時には余り温度の高い熱媒を得る
ことができない問題点を有していた。 For this reason, Japanese Patent Application Laid-Open No. 51-3039 proposes a system that combines an absorption refrigerator and a compression refrigerator to obtain a sufficiently low temperature heat medium during cooling, but the temperature is too low during heating. The problem was that it was not possible to obtain a high heat medium.
又、特開昭53−43266号公報には圧縮式ヒート
ポンプの圧縮機吐出温度で吸収式ヒートポンプの
蒸発器内の水を蒸発させることにより吸収式ヒー
トポンプの吸収器から高温度の温水を、又、特開
昭48−2428号公報には吸収式冷凍機で冷却された
冷却水でスクリユー圧縮機の凝縮器を冷却するこ
とによりこの圧縮機の蒸発器から低温度の冷水を
得るようにしたシステムが提示されているが、こ
の何れも一方の冷凍機を他方の冷凍機の熱源機と
して利用するため両冷凍機の熱媒同志が熱交換す
る分だけ熱交換効率が低下する問題点を有してい
た。 Furthermore, Japanese Patent Application Laid-Open No. 53-43266 discloses that high-temperature hot water can be extracted from the absorber of an absorption heat pump by evaporating the water in the evaporator of the absorption heat pump at the discharge temperature of the compressor of the compression heat pump. Japanese Unexamined Patent Publication No. 48-2428 discloses a system in which low-temperature cold water is obtained from the evaporator of a screw compressor by cooling the condenser of the screw compressor with cooling water cooled by an absorption refrigerator. However, in both of these methods, one of the refrigerators is used as a heat source for the other refrigerator, so there is a problem that the heat exchange efficiency decreases due to the heat exchange between the heat medium of both refrigerators. Ta.
本発明はかかる問題点に鑑み、冷暖房する室に
配置する調温器の熱媒を、暖房時には加圧式冷凍
機の凝縮器から吸収冷凍機の熱媒加熱装置へ、且
つ冷房時には吸収冷凍機の蒸発器から加圧式冷凍
機の蒸発器へ、夫々切替弁で切替えて流すことに
より、暖房時には充分に高温の熱媒を、又、冷房
時には充分に低温の熱媒を効率的に生成すること
により成積係数を向上させるようにした冷暖房装
置を提供したものである。 In view of this problem, the present invention transfers the heat medium of the temperature controller installed in the room to be cooled or heated from the condenser of the pressure refrigerator to the heat medium heating device of the absorption refrigerator during heating, and from the absorption refrigerator during cooling. By switching the flow from the evaporator to the evaporator of the pressurized refrigerator using a switching valve, it is possible to efficiently generate a sufficiently high temperature heat medium during heating and a sufficiently low temperature heat medium during cooling. The present invention provides an air-conditioning device that improves the build-up coefficient.
以下、本発明の実施例を図面に従い説明する。 Embodiments of the present invention will be described below with reference to the drawings.
図において1は、先に説明した往復動圧縮機、
スクリユー圧縮機等を冷凍サイクルの構成要素と
する加圧式冷凍機、2は冷水および温水を生成で
きる直焚式の吸収冷凍機、3は冷房又は暖房する
室に設置された調温器、4は熱媒の循環ポンプ、
5,5′は切替弁であり、これらの機器と、加圧
式冷凍機の熱交換部(凝縮器又は蒸発器等)6お
よび吸収冷凍機の熱交換部(熱媒加熱装置又は蒸
発器等)7とは、熱媒配管8によつて接続されて
いる。 In the figure, 1 is the reciprocating compressor described earlier;
2 is a direct-fired absorption refrigerator that can generate cold water and hot water; 3 is a temperature controller installed in the room to be cooled or heated; 4 is a pressure refrigerator with a screw compressor as a component of the refrigeration cycle; heat medium circulation pump,
5 and 5' are switching valves, and these devices are connected to the heat exchange section (condenser or evaporator, etc.) 6 of the pressure refrigerator and the heat exchange section (heat medium heating device, evaporator, etc.) of the absorption refrigerator. 7 is connected by a heat medium pipe 8.
尚、9は吸収冷凍機2と加圧式冷凍機1とを、
必要に応じ、後述するように熱的に接続する補助
配管である。 In addition, 9 indicates the absorption refrigerator 2 and the pressure refrigerator 1,
This is an auxiliary pipe that is thermally connected as required, as will be described later.
斯る構成を有する本発明の冷暖房装置を冷房に
用いる場合は、ポンプ4によつて、図の実線矢視
のように熱媒が循環され、吸収冷凍機の熱交換部
7で予冷された熱媒が加圧式冷凍機の熱交換部6
に流入して空調に充分な低温に冷却され、調温器
3に供給される。この運転時に同時に吸収冷凍機
の熱交換部7で予冷された別の流体を補助配管9
を経て加圧式冷凍機6の凝縮器の冷却に用いた
後、この冷却で逆に温度上昇した流体の熱を吸収
冷凍機2で回収するようにすれば成積係数が更に
向上する。こうして、空調に充分な低温(例え
ば、−2℃〜−4℃)に熱媒を冷却し、冷房を行
なう。 When the air-conditioning device of the present invention having such a configuration is used for cooling, the heat medium is circulated by the pump 4 as shown by the solid line arrow in the figure, and the heat pre-cooled in the heat exchange section 7 of the absorption refrigerator is transferred. The medium is a heat exchange section 6 of a pressurized refrigerator.
The air flows into the air conditioner, is cooled to a temperature sufficient for air conditioning, and is supplied to the temperature controller 3. During this operation, another fluid pre-cooled in the heat exchange section 7 of the absorption refrigerator is supplied to the auxiliary pipe 9.
After cooling the condenser of the pressurized refrigerator 6, the heat of the fluid whose temperature has risen due to this cooling is recovered by the absorption refrigerator 2, thereby further improving the build-up coefficient. In this way, the heating medium is cooled to a low temperature sufficient for air conditioning (for example, -2°C to -4°C), and air conditioning is performed.
この場合において、加圧式冷凍機では凝縮圧力
と蒸発圧力との差が小さくなり、単体運転のとき
より高い成績係数が得られる。 In this case, in the pressurized refrigerator, the difference between the condensing pressure and the evaporating pressure becomes smaller, and a higher coefficient of performance can be obtained than when operating alone.
一方、本発明装置を暖房に用いる場合は、切替
弁5,5′を破線のように切替え、熱媒を破線矢
視のポンプ4で循環すると、吸収冷凍機の熱交換
部7からは、通常の加圧式冷凍機では得られない
程の高温度(70℃以上)に加温された熱媒が調温
器3に供給される。この運転時に同時に加圧式冷
凍機の熱交換部6で加熱された別の流体を補助配
管9を経て吸収冷凍機2の蒸発器の加熱に用いた
後、この加熱で逆に温度が下がつた流体の熱を加
圧式冷凍機1で回収するようにすれば、成積係数
が更に向上する。 On the other hand, when the device of the present invention is used for heating, the switching valves 5 and 5' are switched as shown by the broken line, and the heat medium is circulated by the pump 4 shown by the broken line. A heating medium heated to a high temperature (70° C. or higher) that cannot be obtained with the pressure refrigerator is supplied to the temperature controller 3. At the same time during this operation, another fluid heated in the heat exchange section 6 of the pressure refrigerator was used to heat the evaporator of the absorption refrigerator 2 via the auxiliary pipe 9, and the temperature conversely decreased due to this heating. If the heat of the fluid is recovered by the pressurized refrigerator 1, the build-up coefficient will be further improved.
この場合において、加圧式冷凍機1での熱媒の
加熱温度は僅かで良く、従来のように熱交換部の
形状を大きくしたり、冷媒の加圧度を極度に大き
くする必要はなく、単体運転時と比較して高い成
績係数での運転が可能である。 In this case, the heating temperature of the heat medium in the pressurized refrigerator 1 only needs to be small, and there is no need to enlarge the shape of the heat exchange part or to extremely increase the degree of pressurization of the refrigerant, as in the case of the conventional method. It is possible to operate with a higher coefficient of performance than when driving.
更に又、本発明の冷暖房装置においては、冷房
時、暖房時のいずれの場合でも、冷暖房される室
の温度と調温器との温度差を大きくすることがで
きるので、熱交換器が小さい小型の調温器でも従
来と同様な冷暖房機能を有する等、冷暖房運転費
用の低減と併せ設備機器の費用低減の効果も有す
るものである。 Furthermore, in the air conditioning system of the present invention, the temperature difference between the temperature of the room being cooled and heated and the temperature controller can be increased both during cooling and heating, so the heat exchanger is small and compact. This temperature controller also has the same heating and cooling functions as conventional ones, and has the effect of reducing heating and cooling operation costs as well as equipment costs.
第1図は本発明による冷暖房装置の一実施例を
示す配管構成図、第2図は同じく他の実施例を示
す配管構成図である。
1〜加圧式冷凍機、2〜直焚式吸収冷凍機、3
〜調温器、8〜熱媒配管。
FIG. 1 is a piping configuration diagram showing one embodiment of the air conditioning system according to the present invention, and FIG. 2 is a piping configuration diagram showing another embodiment. 1 - Pressure refrigerator, 2 - Direct-fire absorption refrigerator, 3
~ Temperature controller, 8 ~ Heat medium piping.
Claims (1)
と凝縮器と蒸発器とで冷凍サイクルを構成して暖
房時に凝縮器で熱媒を加熱し冷房時に蒸発器で熱
媒を冷却する加圧式冷凍機と、熱媒加熱装置と蒸
発器とで冷凍サイクルを構成して暖房時に熱媒加
熱装置で熱媒を加熱し冷房時に蒸発器で熱媒を冷
却する吸収式冷凍機と、加圧式冷凍機の凝縮器と
蒸発器及び吸収式冷凍機の熱媒加熱装置と蒸発器
とに熱媒配管で接続され冷暖房する室に設置され
る調温器とを備え、この熱媒配管には暖房時に加
圧式冷凍機の凝縮器と吸収式冷凍機の熱媒加熱装
置と調温器とを順次環状に連結して暖房回路を形
成し、かつ、冷房時に吸収冷凍機の蒸発器と加圧
式冷凍機の蒸発器と調温器とを順次環状に連結し
て冷房回路を形成する切替弁を設けたことを特徴
とする冷暖房装置。1. Pressurized refrigeration, in which a refrigeration cycle is composed of a compressor such as a reciprocating compressor or screw compressor, a condenser, and an evaporator, and the condenser heats the heat medium during heating, and the evaporator cools the heat medium during cooling. There are two types of absorption refrigerators: absorption refrigerators, which form a refrigeration cycle with a heating medium heating device, a heating medium heating device, and an evaporator, and heat the heating medium with the heating medium heating device during heating, and cool the heating medium with an evaporator during cooling, and pressure refrigerators. The condenser, the evaporator, the heat medium heating device of the absorption chiller, and the evaporator are connected to the heat medium piping and installed in the room to be cooled and heated. The condenser of the compression refrigerator, the heat medium heating device of the absorption refrigerator, and the temperature controller are sequentially connected in an annular manner to form a heating circuit, and the evaporator of the absorption refrigerator and the pressure An air-conditioning/heating device characterized by being provided with a switching valve that sequentially connects an evaporator and a temperature controller in an annular manner to form a cooling circuit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9883778A JPS5525756A (en) | 1978-08-11 | 1978-08-11 | Coolerrheater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9883778A JPS5525756A (en) | 1978-08-11 | 1978-08-11 | Coolerrheater |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5525756A JPS5525756A (en) | 1980-02-23 |
JPS6158745B2 true JPS6158745B2 (en) | 1986-12-12 |
Family
ID=14230373
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9883778A Granted JPS5525756A (en) | 1978-08-11 | 1978-08-11 | Coolerrheater |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5525756A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02159431A (en) * | 1988-12-10 | 1990-06-19 | Toyota Motor Corp | Water cooling type disc brake |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60232466A (en) * | 1984-04-27 | 1985-11-19 | 株式会社クボタ | Air-conditioning facility utilizing engine heat pump |
JPS60232465A (en) * | 1984-04-27 | 1985-11-19 | 株式会社クボタ | Air-conditioning facility utilizing engine heat pump |
-
1978
- 1978-08-11 JP JP9883778A patent/JPS5525756A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02159431A (en) * | 1988-12-10 | 1990-06-19 | Toyota Motor Corp | Water cooling type disc brake |
Also Published As
Publication number | Publication date |
---|---|
JPS5525756A (en) | 1980-02-23 |
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