JPS62142965A - Heat pump device - Google Patents
Heat pump deviceInfo
- Publication number
- JPS62142965A JPS62142965A JP28355485A JP28355485A JPS62142965A JP S62142965 A JPS62142965 A JP S62142965A JP 28355485 A JP28355485 A JP 28355485A JP 28355485 A JP28355485 A JP 28355485A JP S62142965 A JPS62142965 A JP S62142965A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- pipe
- accumulator
- liquid
- condenser
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2341/00—Details of ejectors not being used as compression device; Details of flow restrictors or expansion valves
- F25B2341/001—Ejectors not being used as compression device
- F25B2341/0014—Ejectors with a high pressure hot primary flow from a compressor discharge
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Central Heating Systems (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、空調用、冷凍用等の熱交換効率の向上を目的
としたヒートポンプ装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a heat pump device for improving heat exchange efficiency for air conditioning, refrigeration, and the like.
従来の技術
従来、熱交換効率を向上することを目的としたヒートポ
ンプ装置として、第4図に示すHi /Re/Li 回
路(ウェスチングハウス社開発)がある。2. Description of the Related Art Conventionally, as a heat pump device aimed at improving heat exchange efficiency, there is a Hi/Re/Li circuit (developed by Westinghouse) shown in FIG.
第4図において、圧縮機1、凝縮器2、絞り3、蒸発器
4、アキュムレータ5を主機能要素とし、凝縮器2と絞
り3とを連結する冷媒配管をアキュムレータ5と熱交換
関係に配設し、絞り3で凝縮器2の出口冷媒の過冷却度
を調整するように構成されておる。第5図のモリエル線
図に示すように、蒸発器4の出口を湿り状態8点にし、
圧縮機1への液バツク防止のために、アキュムレータ5
での凝縮器2出口の高温冷媒流B−C点の熱量と熱交換
させることで圧縮機1の吸入冷媒状態を飽和ガス状態に
なるように構成されている。以上のようにすることで、
蒸発器4での冷媒状態は全域にわたり気液2相域の状態
で、第6図に示すごとく、熱伝達率の高い点で蒸発器4
が作用するため、熱交換効率の向上がはかられ、サイク
ル全体としても効率の向上につながっている。In Fig. 4, the main functional elements are a compressor 1, a condenser 2, a throttle 3, an evaporator 4, and an accumulator 5, and a refrigerant pipe connecting the condenser 2 and the throttle 3 is arranged in a heat exchange relationship with the accumulator 5. However, the throttle 3 is configured to adjust the degree of subcooling of the refrigerant at the outlet of the condenser 2. As shown in the Mollier diagram of FIG. 5, the outlet of the evaporator 4 is set to eight wet points,
To prevent liquid back to the compressor 1, the accumulator 5
By exchanging heat with the amount of heat at point B-C of the high-temperature refrigerant flow at the outlet of the condenser 2, the state of the refrigerant sucked into the compressor 1 becomes a saturated gas state. By doing the above,
The state of the refrigerant in the evaporator 4 is in a gas-liquid two-phase region over the entire region, and as shown in FIG.
, which improves heat exchange efficiency and improves the efficiency of the cycle as a whole.
発明が解決しようとする問題点
しかしながら上記のような構成では、第5図のモリエル
線図で明らかなように、蒸発器4側のみでの効率向上で
あり、凝縮器2側では、熱伝達率の悪い過熱ガス域があ
り、凝縮器2側での効率向上がはかられていないので、
サイクル全体としての効率向上が十分でないという問題
点を有していた。Problems to be Solved by the Invention However, with the above configuration, as is clear from the Mollier diagram in FIG. There is a superheated gas region with poor performance, and no attempt has been made to improve efficiency on the condenser 2 side.
The problem was that the efficiency of the cycle as a whole was not sufficiently improved.
本発明はかかる従来の問題を解消するもので、蒸発器、
凝縮器ともに内部全域の冷媒が気液2相域の状態とする
ことで、サイクル全体としての効率向上をはかることを
目的とする。The present invention solves such conventional problems, and includes an evaporator,
The purpose is to improve the efficiency of the entire cycle by bringing the refrigerant throughout the entire interior of the condenser into a gas-liquid two-phase state.
間原点を解決するための手段
上記間置点を解決するために、本発明のヒートポンプ装
置は、凝縮器と絞り装置とを結ぶ冷媒管路をアキュムレ
ータと熱交換関係に配設し、アキュムレータと熱交換し
た後の絞り装置入口の冷媒管路の液冷媒の一部を圧縮機
吐出配管へ再循環させるための冷媒分岐管と再循環手段
を設けるという構成を備えたものである。Means for Solving the Intermediate Point In order to solve the above-mentioned interstitial point, the heat pump device of the present invention arranges the refrigerant pipe line connecting the condenser and the expansion device in a heat exchange relationship with the accumulator. This system includes a refrigerant branch pipe and recirculation means for recirculating a portion of the liquid refrigerant in the refrigerant pipe at the inlet of the throttling device to the compressor discharge pipe after replacement.
作 用
本発明は上記した構成によって、アキュムレータで蒸発
器より出た低温冷媒と凝縮器を出た高温冷媒を熱交換さ
せることにより、蒸発器出口の冷媒状態を気液2相域に
、凝縮器出口の冷媒状態を気液2相域に設定でき、また
、アキュムレータで熱交換され過冷却状態となった絞り
装置入口冷媒管路の液冷媒の一部を圧縮機吐出配管へ再
循環させることにより、凝縮器入口の冷媒状態も気液2
相域となり、蒸発器、凝縮器ともに内部全域の冷媒が熱
伝達率の高い気液2相の状態となり、サイクル全体の効
率向上がはかれるものである。Effect of the Invention With the above-described configuration, the present invention exchanges heat between the low-temperature refrigerant discharged from the evaporator and the high-temperature refrigerant discharged from the condenser in the accumulator, thereby changing the refrigerant state at the evaporator outlet into a gas-liquid two-phase region. By setting the refrigerant state at the outlet to a gas-liquid two-phase region, and by recirculating a portion of the liquid refrigerant in the throttle device inlet refrigerant pipe, which has become supercooled through heat exchange in the accumulator, to the compressor discharge pipe. , the refrigerant state at the condenser inlet is also gas-liquid 2
The refrigerant in both the evaporator and the condenser is in a gas-liquid two-phase state with a high heat transfer coefficient, improving the efficiency of the entire cycle.
実施例
以下、本発明の実施例を添付図面にもとづいて説明する
。第1図において、1は圧縮機、2は凝縮器、3は絞り
装置、4は蒸発器、5はアキュムレータで、これらを環
状の冷媒配管で結合し、凝縮器2と絞り装置3とを結ぶ
冷媒配管6をアキュムレータ5と熱交換関係に配設する
。冷媒配管6がアキュムレータ5と熱交換した後の冷媒
管路6から冷媒分岐管7を設け、圧縮機1の吐出管8に
設けたエジェクタ9の吸引側へ連結されている。Embodiments Hereinafter, embodiments of the present invention will be described based on the accompanying drawings. In Fig. 1, 1 is a compressor, 2 is a condenser, 3 is a throttle device, 4 is an evaporator, and 5 is an accumulator, which are connected by an annular refrigerant pipe to connect the condenser 2 and the throttle device 3. The refrigerant pipe 6 is arranged in a heat exchange relationship with the accumulator 5. A refrigerant branch pipe 7 is provided from the refrigerant pipe 6 after the refrigerant pipe 6 has exchanged heat with the accumulator 5, and is connected to the suction side of an ejector 9 provided in a discharge pipe 8 of the compressor 1.
エジェクタ9は圧縮機1の吐出ガスを駆動流とし、冷媒
管路6の過冷却液冷媒の一部を冷媒分岐管7を介して吸
引し、吐出ガスと吸引した過冷却液冷媒の混合した冷媒
を凝縮器2へ送る。The ejector 9 uses the discharge gas of the compressor 1 as a driving flow, sucks a part of the supercooled liquid refrigerant in the refrigerant pipe line 6 through the refrigerant branch pipe 7, and produces a refrigerant mixture of the discharge gas and the suctioned supercooled liquid refrigerant. is sent to condenser 2.
上記構成において、第3図のモリエル線図と合せて作用
効果を説明する。圧縮機1の吐出管8における吐出ガス
は第3図モリエル線図上の入点で過熱ガス域である。エ
ジェクタ9で上記吐出ガスを駆動流として、冷媒管路6
′の過冷却液冷媒C点の一部を冷媒分岐管7を介して吸
引し、エジェクタ9出口では、吐出ガス八点と過冷却液
冷媒C点の一部とが混合して、気液2相域G点となり凝
縮器2へ送られる。凝縮器2で冷媒は放熱し、凝縮器2
出口では気液2相域C点となりアキュムレータ5と熱交
換関係に配設された冷媒配管6へ送られ、アキュムレー
タ5内の低温の未蒸発冷媒と熱交換し、過冷却液状態C
点となる。絞り装置3により、C点の過冷却液冷媒は減
圧され気液2相域り点となり蒸発器4へ入り、ここで吸
熱し、気液2相域状態E点で蒸発器4からアキュムレー
タ5へ送られる。アキュムレータ5内では冷媒配管6の
高温冷媒と熱交換され、F点の状態となり圧縮機1へ吸
入される。The effects of the above configuration will be explained in conjunction with the Mollier diagram shown in FIG. The discharge gas in the discharge pipe 8 of the compressor 1 is in the superheated gas region at the entry point on the Mollier diagram in FIG. The ejector 9 uses the discharged gas as a driving flow to
A part of the supercooled liquid refrigerant at point C is sucked through the refrigerant branch pipe 7, and at the outlet of the ejector 9, the eight discharged gas points and a part of the supercooled liquid refrigerant at point C are mixed to form gas-liquid 2. It becomes the phase region G point and is sent to the condenser 2. The refrigerant radiates heat in condenser 2, and
At the outlet, the gas-liquid two-phase region becomes point C, and the refrigerant is sent to the refrigerant pipe 6 arranged in a heat exchange relationship with the accumulator 5, where it exchanges heat with the low-temperature unevaporated refrigerant in the accumulator 5, resulting in a supercooled liquid state C.
It becomes a point. The supercooled liquid refrigerant at point C is depressurized by the throttling device 3, becomes a gas-liquid two-phase region, enters the evaporator 4, absorbs heat there, and flows from the evaporator 4 to the accumulator 5 at point E, which is in a gas-liquid two-phase region. Sent. Inside the accumulator 5, heat is exchanged with the high-temperature refrigerant in the refrigerant pipe 6, and the refrigerant reaches point F and is sucked into the compressor 1.
上記のように、凝縮器2と絞り装置3とを結ぶ冷媒管路
6をアキュムレータ5と熱交換関係に配設することで、
凝縮器2の出口冷媒状態と、・蒸発器4の出口状態を気
液2相域状態にできる。また、アキュムレータ5と熱交
換した後の冷媒管路6′より分岐された冷媒分岐管7を
設け、過冷却液冷媒の一部を圧縮機1の吐出配管8へ再
循環させる手段として圧縮機吐出ガスを駆動流とするエ
ジェクタ9を設けたことにより、エジェクタ9は圧縮機
吐出ガスを駆動流として冷媒管路6′の過冷却液冷媒の
一部を冷媒分岐管7を介して吸引し、過熱ガス域状態の
圧縮機吐出ガスと混合させることで、凝縮器2の入口状
態を気液2相域状態にてきる。As mentioned above, by arranging the refrigerant pipe line 6 connecting the condenser 2 and the expansion device 3 in a heat exchange relationship with the accumulator 5,
The refrigerant state at the exit of the condenser 2 and the exit state of the evaporator 4 can be made into a gas-liquid two-phase region state. In addition, a refrigerant branch pipe 7 is provided which branches off from the refrigerant pipe 6' after heat exchange with the accumulator 5, and serves as a means for recirculating a part of the supercooled liquid refrigerant to the discharge pipe 8 of the compressor 1. By providing the ejector 9 that uses gas as the driving flow, the ejector 9 uses the compressor discharge gas as the driving flow to suck a part of the supercooled liquid refrigerant in the refrigerant pipe line 6' through the refrigerant branch pipe 7, and superheat it. By mixing it with the compressor discharge gas in the gas region, the inlet state of the condenser 2 is brought into the gas-liquid two-phase region.
上記作用の説明のごとく、本発明の構成をとることで、
凝縮器2、蒸発器4ともに内部全域の冷媒が熱伝達率の
高い気液2相域状態となるため、サイクル全体の効率向
上がはかれるという効果がある。また、冷媒管路6の過
冷却液冷媒の一部を圧縮機1の吐出管8へ再循環させる
再循環手段として、圧縮機吐出ガスを駆動流とするエジ
ェクタ9で構成することζこより、外部動力を必要とし
ないため、構造が簡単で、省エネルギーな再循環構成が
可能となる効果がある。As explained above, by adopting the configuration of the present invention,
Since the refrigerant throughout the interior of both the condenser 2 and the evaporator 4 is in a gas-liquid two-phase state with a high heat transfer coefficient, the efficiency of the entire cycle is improved. Further, as a recirculation means for recirculating a part of the supercooled liquid refrigerant in the refrigerant pipe line 6 to the discharge pipe 8 of the compressor 1, an ejector 9 using the compressor discharge gas as a driving flow is used. Since no power is required, the structure is simple and an energy-saving recirculation configuration is possible.
次に本発明の他の実施例を第2図を用いて説明する。第
2図において前記実施例と相違する点は、冷媒管路6の
過冷却液冷媒の一部を圧縮機1の吐出管8へ再循環させ
る再循環手段として、冷媒液循環ポンプ10を冷媒分岐
管7中に設ける構成としたことにあり、この構成によれ
ば、冷媒液循環ポンプ10の動力源が外部にあるため、
流量調整が容易であり、サイクル状態の変動に合せて、
再循環量を最適に調整可能であるという効果がある。Next, another embodiment of the present invention will be described using FIG. 2. The difference in FIG. 2 from the above embodiment is that a refrigerant liquid circulation pump 10 is used as a refrigerant branch for recirculating a part of the supercooled liquid refrigerant in the refrigerant pipe line 6 to the discharge pipe 8 of the compressor 1. According to this structure, since the power source of the refrigerant liquid circulation pump 10 is external,
Flow rate adjustment is easy, and according to fluctuations in cycle conditions,
This has the effect that the amount of recirculation can be adjusted optimally.
発明の効果
以上のように本発明のヒートポンプ装置によれば次の効
果が得られる。Effects of the Invention As described above, the heat pump device of the present invention provides the following effects.
(1)圧縮機、凝縮器、絞り装置、蒸発器、アキュムレ
ータを環状の冷媒配管で結合し、前記凝縮器と絞り装置
を結ぶ冷媒管路を前記アキュムレータと熱交換関係に配
設し、上記アキュムレータと熱交換した後の冷媒管路の
液冷媒の一部を圧縮機吐出配管へ再循環させるための冷
媒分岐管と再循環手段を設けているので、凝縮器、蒸発
器ともに内部全域の冷媒を熱伝達率の高い気液2相域状
態に形成できるため、サイクル全体の効率が向上すると
いう効果がある。(1) A compressor, a condenser, a throttling device, an evaporator, and an accumulator are connected by an annular refrigerant pipe, and a refrigerant pipe connecting the condenser and the throttling device is arranged in a heat exchange relationship with the accumulator, and the accumulator A refrigerant branch pipe and recirculation means are provided to recirculate part of the liquid refrigerant in the refrigerant pipe to the compressor discharge pipe after heat exchange with the refrigerant, so the refrigerant in the entire internal area of both the condenser and evaporator is Since it can be formed in a gas-liquid two-phase state with a high heat transfer coefficient, it has the effect of improving the efficiency of the entire cycle.
(= アキュムレータと熱交換した後の冷媒管路の液冷
媒の一部を圧縮機吐出配管へ再循環させる手段として、
圧縮機吐出ガスを駆動流とするエジェクタで構成するこ
とにより、外部動力を必要としないため、構造が簡単で
あり、省エネルギーであるという効果がある。(= As a means of recirculating a part of the liquid refrigerant in the refrigerant pipe after heat exchange with the accumulator to the compressor discharge pipe,
By configuring the ejector using the compressor discharge gas as a driving flow, no external power is required, resulting in a simple structure and energy saving.
(3)アキュムレータと熱交換した後の冷媒管路の液冷
媒の一部を圧縮機吐出配管へ再循環させる手段として、
冷媒液循環ポンプを冷媒分岐管中に設けた構成とするこ
とにより、冷媒液循環ポンプの動力源が外部にあるため
、流量調整が容易であり、サイクル状態の変動ζこ合せ
て、再循環量を最適に調整可能であるという効果がある
。(3) As a means for recirculating a part of the liquid refrigerant in the refrigerant pipe line after heat exchange with the accumulator to the compressor discharge pipe,
By configuring the refrigerant liquid circulation pump in a refrigerant branch pipe, the power source for the refrigerant liquid circulation pump is external, making it easy to adjust the flow rate. This has the effect that it can be adjusted optimally.
第1図は本発明の一実施例を示すヒートポンプ装置の構
成図、第2図は本発明の他の実施例を示すヒートポンプ
蓼1の構成図、第3図は本発明の作用を示すモリエル線
図、第4図は従来例を示す回路構成図、第5図は従来例
の作用を示すモリエル線図、第6図は冷媒の相変化伝熱
特性図である。
1・・・・・・圧縮機、2・・・・・・凝縮器、3・・
・・・・絞り装置、4・・・・・・蒸発器、5・・・・
・・アキュムレータ、7・・・・・・冷媒分岐管、8・
・・・・・圧縮機吐出管、9・・・・・・エジェクタ、
10・・・・・・冷媒液ポンプ。
代理人の氏名 弁理士 中 尾 赦 男 ほか1名第2
図
第3図
−−エンタルビ−
第4図
第6図
図面のl′γ弓C(内容にニー)f−’=L)第5図
/62アヤエ4し一タルロ
手続補正書げ戎)
昭和61年3月 72日Fig. 1 is a block diagram of a heat pump device showing one embodiment of the present invention, Fig. 2 is a block diagram of a heat pump unit 1 showing another embodiment of the present invention, and Fig. 3 is a Mollier wire diagram showing the action of the present invention. 4 is a circuit configuration diagram showing a conventional example, FIG. 5 is a Mollier diagram showing the operation of the conventional example, and FIG. 6 is a phase change heat transfer characteristic diagram of a refrigerant. 1... Compressor, 2... Condenser, 3...
... Throttle device, 4... Evaporator, 5...
...Accumulator, 7...Refrigerant branch pipe, 8.
... Compressor discharge pipe, 9 ... Ejector,
10...Refrigerant liquid pump. Name of agent: Patent attorney Masao Nakao and 1 other person 2nd
Figure 3 - Enthalby Figure 4 Figure 6 of the drawing l'γ bow C (knee to the content) f-' = L) Figure 5/62 Ayae 4 Shii Taruro procedure amendment writing) 1986 March 72nd
Claims (3)
ータを環状の冷媒配管で結合し、前記凝縮器と絞り装置
を結ぶ冷媒管路を前記アキュムレータと熱交換関係に配
設し、上記アキュムレータと熱交換した後の冷媒管路の
液冷媒の一部を圧縮機吐出配管へ再循環させる冷媒分岐
管と再循環手段を設けたヒートポンプ装置。(1) A compressor, a condenser, a throttling device, an evaporator, and an accumulator are connected by an annular refrigerant pipe, and a refrigerant pipe connecting the condenser and the throttling device is arranged in a heat exchange relationship with the accumulator, and the accumulator A heat pump device equipped with a refrigerant branch pipe and recirculation means for recirculating part of the liquid refrigerant in the refrigerant pipe line to the compressor discharge pipe after heat exchange with the refrigerant pipe.
エジェクタで構成した特許請求の範囲第1項記載のヒー
トポンプ装置。(2) The heat pump device according to claim 1, wherein the recirculation means is an ejector that uses compressor discharge gas as a driving flow.
管中に設けた特許請求の範囲第1項記載のヒートポンプ
装置。(3) The heat pump device according to claim 1, wherein a refrigerant liquid circulation pump is provided in the refrigerant branch pipe as the recirculation means.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28355485A JPS62142965A (en) | 1985-12-17 | 1985-12-17 | Heat pump device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28355485A JPS62142965A (en) | 1985-12-17 | 1985-12-17 | Heat pump device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62142965A true JPS62142965A (en) | 1987-06-26 |
Family
ID=17667026
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28355485A Pending JPS62142965A (en) | 1985-12-17 | 1985-12-17 | Heat pump device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62142965A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008267691A (en) * | 2007-04-20 | 2008-11-06 | Mitsubishi Electric Corp | Air conditioner |
JP2011133132A (en) * | 2009-12-22 | 2011-07-07 | Daikin Industries Ltd | Refrigerating device |
JP2014526667A (en) * | 2011-09-09 | 2014-10-06 | ヨーロピアン オーガナイゼーション フォー ニュークリア リサーチ | Mini cooling system and method for accurate temperature control |
-
1985
- 1985-12-17 JP JP28355485A patent/JPS62142965A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008267691A (en) * | 2007-04-20 | 2008-11-06 | Mitsubishi Electric Corp | Air conditioner |
JP2011133132A (en) * | 2009-12-22 | 2011-07-07 | Daikin Industries Ltd | Refrigerating device |
JP2014526667A (en) * | 2011-09-09 | 2014-10-06 | ヨーロピアン オーガナイゼーション フォー ニュークリア リサーチ | Mini cooling system and method for accurate temperature control |
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