JPH03211361A - Heat-pump hot water supplier - Google Patents
Heat-pump hot water supplierInfo
- Publication number
- JPH03211361A JPH03211361A JP2004708A JP470890A JPH03211361A JP H03211361 A JPH03211361 A JP H03211361A JP 2004708 A JP2004708 A JP 2004708A JP 470890 A JP470890 A JP 470890A JP H03211361 A JPH03211361 A JP H03211361A
- Authority
- JP
- Japan
- Prior art keywords
- condenser
- hot water
- compressor
- refrigerant gas
- discharge port
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 39
- 239000003507 refrigerant Substances 0.000 claims abstract description 51
- 230000006835 compression Effects 0.000 claims description 18
- 238000007906 compression Methods 0.000 claims description 18
- 208000028659 discharge Diseases 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 5
- 230000007423 decrease Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
Landscapes
- Heat-Pump Type And Storage Water Heaters (AREA)
- Domestic Hot-Water Supply Systems And Details Of Heating Systems (AREA)
Abstract
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明はヒートポンプ式給湯装置に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to a heat pump water heater.
(従来の技術及びその課題)
従来のヒートポンプ式給湯装置の1例が第4図に示され
ている。(Prior art and its problems) An example of a conventional heat pump water heater is shown in FIG.
圧縮8121から吐出された冷媒ガスは凝縮器22で給
湯水を加熱することによって凝縮液化した後、絞り装置
23で断熱膨張し、次いで、T発器24で蒸発気化した
後圧縮機21に戻る。The refrigerant gas discharged from the compressor 8121 is condensed and liquefied by heating hot water in the condenser 22, adiabatically expanded in the expansion device 23, then evaporated in the T generator 24, and then returned to the compressor 21.
このヒートポンプ式給湯装置は高温の湯を得るためには
圧縮機21における圧縮比を大きくしなければならず、
圧縮比を大きくすると、圧縮効率が低くなるので給湯性
能が低いという不具合があった。In order to obtain hot water in this heat pump water heater, the compression ratio in the compressor 21 must be increased.
When the compression ratio is increased, the compression efficiency decreases, resulting in a problem of low hot water supply performance.
そこで、これに対処するため第5図に示すヒトポンプ式
給湯装置が提案された。Therefore, in order to deal with this problem, a human pump water heater shown in FIG. 5 was proposed.
低段圧縮機31から吐出された冷媒ガスは中間地交換器
32で凝縮液化し、絞り装置33で断熱膨張し、蒸発器
34で蒸発気化して低段圧縮機31に戻る。The refrigerant gas discharged from the low stage compressor 31 is condensed and liquefied in the intermediate exchanger 32, adiabatically expanded in the expansion device 33, evaporated in the evaporator 34, and returned to the low stage compressor 31.
一方、高段圧縮機35から吐出された冷媒ガスは凝縮器
36で凝縮液化し、絞り装置37で断熱膨張し、中間熱
交換器32で蒸発気化した後、高段圧縮機35に戻る。On the other hand, the refrigerant gas discharged from the high stage compressor 35 is condensed and liquefied in the condenser 36, adiabatically expanded in the expansion device 37, evaporated in the intermediate heat exchanger 32, and then returned to the high stage compressor 35.
給湯水は中間熱交換器32で予熱された後、凝縮器36
で加熱されることにより熱湯となって取り出される。After the hot water is preheated in the intermediate heat exchanger 32, it passes through the condenser 36.
When heated, it becomes hot water and is taken out.
このヒートポンプ式給湯装置は2台の圧縮機31及び3
5を要するのみならず高段圧縮機35はその吸入圧力が
高いため特別仕様とする必要があるので、そのコストが
嵩むという不具合があった。This heat pump water heater has two compressors 31 and 3.
5, and the high-stage compressor 35 has a high suction pressure, so it needs to be specially designed, which increases the cost.
く課題を解決するための手段)
本発明は上記課題を解決するために発明されたものであ
って、その要旨とするところは、圧縮機の吐出口から吐
出された冷媒ガスを凝縮器、絞り装置、蒸発器をこの順
に経て上記圧wi機の吸入口に循環させる冷媒配管と、
上記圧l1ii罐の中間吐出11から吐出された圧縮途
中の冷媒ガスを中間凝縮器及び絞り手段をこの順に経て
上記蒸発器の入口にi環さセる冷媒回路と、給湯水を上
記中間凝縮器及び上記凝縮器をこの順に流過させる給湯
配管とを配設したことを特徴とするヒートポンプ式給湯
装置にある。Means for Solving the Problems) The present invention was invented to solve the above problems, and its gist is that the refrigerant gas discharged from the discharge port of the compressor is refrigerant piping that circulates through the device and the evaporator in this order to the inlet of the pressure wi machine;
A refrigerant circuit in which the compressed refrigerant gas discharged from the intermediate discharge 11 of the pressure l1ii can passes through an intermediate condenser and a throttle means in this order and is connected to the inlet of the evaporator, and hot water is supplied to the intermediate condenser. and a heat pump type hot water supply system, characterized in that the hot water supply pipe is arranged to cause the hot water to flow through the condenser in this order.
(作用)
圧縮機の吐出口から吐出された高温・高圧の冷媒ガスは
冷媒配管を循環する過程で凝縮器で凝縮液化し、絞り装
置で断熱膨張し、1発器で蒸発気化した後、圧縮機の吸
入口に吸入される。(Function) The high-temperature, high-pressure refrigerant gas discharged from the discharge port of the compressor is condensed and liquefied in the condenser as it circulates through the refrigerant piping, adiabatically expanded in the expansion device, evaporated and vaporized in one generator, and then compressed. Inhaled into the machine's inlet.
圧縮機の中間吐出口から吐出された圧縮途中の中温 中
圧の冷媒ガスは冷媒回路を流過する過程で中間凝縮器で
凝縮液化し、絞り手段で断熱膨張した後、蒸発器の入口
で冷媒配管中を循環する冷媒と合流する。During compression, the medium temperature and medium pressure refrigerant gas discharged from the intermediate discharge port of the compressor is condensed and liquefied in the intermediate condenser as it flows through the refrigerant circuit, adiabatically expanded by the throttling means, and then refrigerated at the inlet of the evaporator. It joins the refrigerant circulating in the piping.
給湯水は中間凝縮器で中間吐出口から吐出された中温・
中圧の冷媒ガスと熱交換することによって予熱された後
、凝縮器で吐出口から吐出された高温・高圧の冷媒ガス
と熱交換することによって更に加熱されて熱湯水となる
。Hot water is a medium-temperature water discharged from an intermediate outlet in an intermediate condenser.
After being preheated by exchanging heat with medium-pressure refrigerant gas, it is further heated by exchanging heat with high-temperature, high-pressure refrigerant gas discharged from the discharge port in the condenser, and becomes hot water.
(実施例)
本発明の1実施例が第1図ないし第3図に示されている
。Embodiment One embodiment of the invention is shown in FIGS. 1-3.
第1図において、■は圧縮機で、圧縮途中の冷媒ガスを
吐出するための中間吐出口11と完全に圧縮された後の
冷媒ガスを吐出するための吐出口12と、吸入口13と
を持っている。この圧縮機」の吐出口12と、凝縮器2
と、絞り装置3と、蒸発器4と、圧縮機1の吸入口13
とはこの順に冷媒配管25により接続されている。圧縮
Illの中間吐出口11と、中間凝縮器5と、絞り手段
6と蒸発器4の入口とはこの順に冷媒回路7により接続
される。In FIG. 1, ■ is a compressor, which has an intermediate discharge port 11 for discharging refrigerant gas in the middle of compression, a discharge port 12 for discharging refrigerant gas after being completely compressed, and a suction port 13. have. The discharge port 12 of this compressor and the condenser 2
, the throttle device 3 , the evaporator 4 , and the suction port 13 of the compressor 1
and are connected in this order by refrigerant piping 25. The intermediate discharge port 11 of the compression Ill, the intermediate condenser 5, the throttle means 6, and the inlet of the evaporator 4 are connected in this order by a refrigerant circuit 7.
8は給湯水を中間凝縮器5及び凝縮器2をこの順に流過
させる給湯配管である。Reference numeral 8 denotes a hot water supply pipe that allows hot water to flow through the intermediate condenser 5 and the condenser 2 in this order.
第2図には圧w3機lの詳細が示されている。Figure 2 shows details of the pressure w3 machine.
シリンダ14内にはロータ15が偏心した状態で配設さ
れ、このロータ15は駆動軸16によって駆動されるこ
とにより矢印方向に偏心回転してその外周面がシリンダ
14の内周面に摺接する。シリンダ14にはヘーン17
が出没自在に支持され、このヘー717はスプリング1
日によって押推されることにより前進してその先端はロ
ータ15の外周面に摺接する。A rotor 15 is disposed eccentrically within the cylinder 14 , and the rotor 15 is driven by a drive shaft 16 to eccentrically rotate in the direction of the arrow, so that its outer circumferential surface slides against the inner circumferential surface of the cylinder 14 . Höhn 17 for cylinder 14
is supported so that it can appear and retract freely, and this hee 717 is supported by the spring 1
It moves forward by being pushed and pushed by the sun, and its tip comes into sliding contact with the outer peripheral surface of the rotor 15.
シリンダ14にはヘーン17に隣接して回転方向側に吸
入口13が配設され、また、その反回転方向側には吐出
口12が配設され、これら吸入口13と吐出口12との
中間に中間吐出口11が配設されている。19は吐出口
12を開閉する吐出弁、20は中間吐出口11を開閉す
る中間吐出弁である。The cylinder 14 is provided with an inlet 13 on the rotational direction side adjacent to the hone 17, and a discharge port 12 is provided on the opposite side of the rotational direction. An intermediate discharge port 11 is disposed at. 19 is a discharge valve that opens and closes the discharge port 12, and 20 is an intermediate discharge valve that opens and closes the intermediate discharge port 11.
じかして、ロータ15を矢印方向に回転駆動すると、冷
媒ガスが吸入口13から吸入室Sに吸入される。そして
、ロータ15が吸入口13を通過すると、吸入室Sは圧
縮室Cとなり、圧縮室Cの容積が次第に減少するのに伴
って圧縮室C内の冷媒ガスが次第に圧縮される。冷媒ガ
スの圧力が所定の中間圧力に上昇すると、中間吐出弁2
0を押し開いて中間吐出口11から吐出される。ロータ
15が中間吐出口11を通過すると、圧縮室C内の冷媒
ガスの圧力は更に上昇し、この圧力が所定の吐出圧力に
上昇すると、吐出弁19を押し開いて吐出口12から吐
出される。When the rotor 15 is rotated in the direction of the arrow, refrigerant gas is sucked into the suction chamber S from the suction port 13. When the rotor 15 passes through the suction port 13, the suction chamber S becomes a compression chamber C, and as the volume of the compression chamber C gradually decreases, the refrigerant gas in the compression chamber C is gradually compressed. When the pressure of the refrigerant gas rises to a predetermined intermediate pressure, the intermediate discharge valve 2
0 is pushed open and discharged from the intermediate discharge port 11. When the rotor 15 passes through the intermediate discharge port 11, the pressure of the refrigerant gas in the compression chamber C further increases, and when this pressure rises to a predetermined discharge pressure, the discharge valve 19 is pushed open and the refrigerant gas is discharged from the discharge port 12. .
第3図にはモリエル線図が示され、圧縮機1の吸入口1
3から吸入された状Maの冷媒ガスは圧縮機1によって
圧縮された後吐出口12から状態す状態で吐出され、凝
縮器2で凝縮することによりb状態からC状態となり、
次いで、絞り装置3で断熱膨張することによりC状態か
らd状態となり、次いで、蒸発器4で蒸発することによ
ってd状態からC状態となる。FIG. 3 shows a Mollier diagram, in which the suction port 1 of the compressor 1
After being compressed by the compressor 1, the refrigerant gas in the state Ma drawn from the refrigerant gas 3 is discharged from the discharge port 12 in the state shown in FIG.
Next, the C state changes to the d state by adiabatic expansion in the expansion device 3, and then the d state changes to the C state by evaporation in the evaporator 4.
一方、中間吐出口11からC状態で吐出された冷媒ガス
は中間凝縮器5で凝縮することによりe状態からra′
態となり、次いで、絞り手段6で断熱膨張することによ
りra’gからg状態となり、次いで、蒸発器4で蒸発
することによりg状態からa状態となる。On the other hand, the refrigerant gas discharged from the intermediate discharge port 11 in the C state is condensed in the intermediate condenser 5 and changed from the e state to ra'
Then, by adiabatic expansion in the throttle means 6, the state changes from ra'g to the state g, and then, by evaporation in the evaporator 4, the state changes from the state g to the state a.
給湯配管8から供給される低温・低圧の水は中間凝縮器
5に入り、ここで中間吐出口11から吐出された中温・
中圧の冷媒ガスと熱交換することにより予熱された後、
凝縮器2に入り、ここで吐出口12から吐出された高温
・高圧の冷媒ガスと熱交換することによって昇温しで熱
湯水となって取り出される。The low-temperature, low-pressure water supplied from the hot water supply piping 8 enters the intermediate condenser 5, where the medium-temperature and low-pressure water discharged from the intermediate discharge port 11 enters the intermediate condenser 5.
After being preheated by heat exchange with medium pressure refrigerant gas,
It enters the condenser 2, where it exchanges heat with the high-temperature, high-pressure refrigerant gas discharged from the discharge port 12, thereby increasing its temperature and being taken out as hot water.
上記実施例においては、圧縮機1として回転圧縮機を用
いているが、圧縮途中のガスを取り出し得るものであれ
ば任意の形式、構造の圧縮機を用いうろことは勿論であ
る。In the above embodiment, a rotary compressor is used as the compressor 1, but it goes without saying that any type and structure of the compressor can be used as long as it can extract the gas during compression.
(発明の効果)
本発明においては、圧縮機の吐出口から吐出された冷媒
ガスを凝縮器、絞り装置、蒸発器をこの順に経て上記圧
縮機の吸入口に循環させる冷媒配管と、上記圧縮機の中
間吐出口から吐出された圧縮途中の冷媒ガスを中間凝縮
器及び絞り手段をこの順に経て上記蒸発器の入口に循環
させる冷媒回路と、給湯水を上記中間凝縮器及び上記凝
縮器をこの順に流過させる給湯配管とを配設したため、
給湯水は中間凝縮器で中間吐出口から吐出された中温・
中圧の冷媒ガスと熱交換することによって予熱された後
、凝縮器で吐出口から吐出された高温・高圧の冷媒ガス
と熱交換することによって更に加熱されて熱湯水となる
。(Effects of the Invention) The present invention includes a refrigerant pipe that circulates refrigerant gas discharged from a discharge port of a compressor to a suction port of the compressor through a condenser, a throttle device, and an evaporator in this order; a refrigerant circuit that circulates refrigerant gas discharged from an intermediate discharge port in the middle of compression to the inlet of the evaporator via an intermediate condenser and a throttle means in this order; and a refrigerant circuit that circulates hot water through the intermediate condenser and the condenser in this order. Because hot water supply piping was installed to allow water to flow through,
Hot water is a medium-temperature water discharged from an intermediate outlet in an intermediate condenser.
After being preheated by exchanging heat with medium-pressure refrigerant gas, it is further heated by exchanging heat with high-temperature, high-pressure refrigerant gas discharged from the discharge port in the condenser, and becomes hot water.
この結果、−台の圧縮機しか有しないのにも拘らず第5
図に示す2段圧縮式と同程度の高い給湯性能を奏するこ
とができ、しかも、従来の2段圧縮式に比し装置を構成
する機器の数が減少するので設備費が低減する。また、
圧縮機の吸入圧力は低くて足り、従って、従来の2段圧
縮式の高段圧縮機と異なり比重量の大きい冷媒ガスを圧
縮する必要がないので機械的トラブルを回避できる。As a result, despite having only -1 compressors, the 5th
It is possible to achieve the same high hot water supply performance as the two-stage compression type shown in the figure, and the equipment cost is reduced because the number of devices constituting the device is reduced compared to the conventional two-stage compression type. Also,
The suction pressure of the compressor only needs to be low, and therefore, unlike conventional two-stage compression type high-stage compressors, there is no need to compress refrigerant gas having a large specific weight, thereby avoiding mechanical troubles.
第1図ないし第3図は本発明の1実施例を示し、第1図
は系統図、第2図は圧縮機の縦断面図、第3図はモリエ
ル線図である。第4図は従来の華段圧縮弐の系統図、第
5図は従来の2段圧縮式の系統図である。1 to 3 show one embodiment of the present invention, in which FIG. 1 is a system diagram, FIG. 2 is a vertical sectional view of the compressor, and FIG. 3 is a Mollier diagram. FIG. 4 is a system diagram of a conventional two-stage compression system, and FIG. 5 is a system diagram of a conventional two-stage compression system.
Claims (1)
り装置、蒸発器をこの順に経て上記圧縮機の吸入口に循
環させる冷媒配管と、上記圧縮機の中間吐出口から吐出
された圧縮途中の冷媒ガスを中間凝縮器及び絞り手段を
この順に経て上記蒸発器の入口に循環させる冷媒回路と
、給湯水を上記中間層凝縮器及び上記凝縮器をこの順に
流過させる給湯配管とを配設したことを特徴とするヒー
トポンプ式給湯装置。A refrigerant pipe that circulates the refrigerant gas discharged from the discharge port of the compressor through a condenser, a throttle device, and an evaporator in this order to the suction port of the compressor, and a refrigerant gas discharged from the intermediate discharge port of the compressor during compression. A refrigerant circuit that circulates refrigerant gas to the inlet of the evaporator through an intermediate condenser and a throttle means in this order, and hot water supply piping that allows hot water to flow through the intermediate condenser and the condenser in this order. A heat pump water heater that is characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP470890A JP2617596B2 (en) | 1990-01-12 | 1990-01-12 | Heat pump water heater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP470890A JP2617596B2 (en) | 1990-01-12 | 1990-01-12 | Heat pump water heater |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03211361A true JPH03211361A (en) | 1991-09-17 |
JP2617596B2 JP2617596B2 (en) | 1997-06-04 |
Family
ID=11591384
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP470890A Expired - Lifetime JP2617596B2 (en) | 1990-01-12 | 1990-01-12 | Heat pump water heater |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2617596B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5531630A (en) * | 1993-03-04 | 1996-07-02 | Crosta; Emanuele | Seam protecting device for drum grinding or raising machines |
WO2009001535A1 (en) * | 2007-06-22 | 2008-12-31 | Panasonic Corporation | Refrigeration cycle device |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61107058A (en) * | 1984-10-31 | 1986-05-24 | 株式会社東芝 | Compressor for superheating pump |
-
1990
- 1990-01-12 JP JP470890A patent/JP2617596B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61107058A (en) * | 1984-10-31 | 1986-05-24 | 株式会社東芝 | Compressor for superheating pump |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5531630A (en) * | 1993-03-04 | 1996-07-02 | Crosta; Emanuele | Seam protecting device for drum grinding or raising machines |
WO2009001535A1 (en) * | 2007-06-22 | 2008-12-31 | Panasonic Corporation | Refrigeration cycle device |
EP2096378A1 (en) * | 2007-06-22 | 2009-09-02 | Panasonic Corporation | Refrigeration cycle device |
EP2096378A4 (en) * | 2007-06-22 | 2013-06-12 | Panasonic Corp | Refrigeration cycle device |
US8549868B2 (en) | 2007-06-22 | 2013-10-08 | Panasonic Corporation | Refrigeration cycle apparatus |
US9618234B2 (en) | 2007-06-22 | 2017-04-11 | Panasonic Intellectual Property Management Co., Ltd. | Refrigerant circuit |
Also Published As
Publication number | Publication date |
---|---|
JP2617596B2 (en) | 1997-06-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US8079229B2 (en) | Economized refrigerant vapor compression system for water heating | |
CN102414522B (en) | Transcritical thermally activated cooling, heating and refrigerating system | |
GB2037965A (en) | Refrigeration or heat pump system | |
CN108759138B (en) | Operation method and system of secondary throttling middle incomplete cooling refrigerating system | |
CN109869940A (en) | Injecting type critical-cross carbon dioxide double-stage compressive refrigerating system | |
CN106568225B (en) | Compressor and refrigerating plant who has it | |
CN100507401C (en) | Capacity adjustable vortex compressor refrigeration system with mediate loop installed with ejector | |
CN109855323A (en) | Refrigeration system is subcooled in injecting type | |
CN110822755A (en) | Heat pump system using non-azeotropic refrigerant mixture | |
CN108709333B (en) | Operation method and system of secondary throttling middle complete cooling refrigerating system | |
CN108759139B (en) | Primary throttling intermediate incomplete cooling refrigeration system with intermediate temperature evaporator | |
CN100507400C (en) | Capacity adjustable vortex compressor refrigeration system with main return loop installed with ejector | |
CN109869944A (en) | Absorption supercooling refrigeration system | |
CN101140111A (en) | Capacity adjustable cyclone compressor refrigeration system | |
JP3915538B2 (en) | Water heater | |
JPH03211361A (en) | Heat-pump hot water supplier | |
CN110345636A (en) | The heat reclamation type air source hot pump water heater circulatory system and working method | |
CN205448417U (en) | Heat exchange system | |
CN108489129A (en) | A kind of double-stage compressive refrigerating system | |
CN110476024A (en) | Freezing cycle device | |
KR20190005645A (en) | Air conditioner | |
CN210089176U (en) | Injection type supercooling refrigerating system | |
KR100526105B1 (en) | Heat pump air-conditioner | |
JP2615496B2 (en) | Two-stage compression refrigeration cycle | |
JP2808899B2 (en) | Two-stage compression refrigeration cycle device |