JPH0476358A - Device in refrigerating cycle - Google Patents
Device in refrigerating cycleInfo
- Publication number
- JPH0476358A JPH0476358A JP18796990A JP18796990A JPH0476358A JP H0476358 A JPH0476358 A JP H0476358A JP 18796990 A JP18796990 A JP 18796990A JP 18796990 A JP18796990 A JP 18796990A JP H0476358 A JPH0476358 A JP H0476358A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- pressure
- low
- refrigerant
- liquid
- 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
- 239000007788 liquid Substances 0.000 claims abstract description 42
- 238000005057 refrigeration Methods 0.000 claims description 13
- 239000003507 refrigerant Substances 0.000 abstract description 32
- 230000006835 compression Effects 0.000 abstract description 7
- 238000007906 compression Methods 0.000 abstract description 7
- 229920006395 saturated elastomer Polymers 0.000 abstract description 4
- 239000011555 saturated liquid Substances 0.000 abstract description 2
- 230000005494 condensation Effects 0.000 abstract 1
- 238000009833 condensation Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 5
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
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
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/13—Economisers
-
- 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
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/23—Separators
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明は単一の密閉形シェル内に高、低2段圧縮機部
を収納させた冷凍サイクル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 refrigeration cycle device in which high and low two-stage compressor sections are housed in a single closed shell.
[従来の技術〕
第3図は特開平2−10062号公報に示された従来の
冷凍サイクル装置の冷媒回路図であり、図において(1
)は圧縮機、 (la)はその密閉形シェル、(3)は
内装の低段圧縮機部、(4)は内装の高段圧縮機部、(
5)は凝縮器、(6a)は第1のキャピラリーチューブ
、(7)は気液分離器、(8a)は第2のキャピラリー
チューブ、(9)は蒸発器、 (10)はインジェクシ
ョン路、(11)は補助減圧装置、(12)は液冷媒導
入路である。[Prior Art] Figure 3 is a refrigerant circuit diagram of a conventional refrigeration cycle device disclosed in Japanese Patent Application Laid-Open No. 2-10062.
) is the compressor, (la) is its closed shell, (3) is the internal low stage compressor section, (4) is the internal high stage compressor section, (
5) is a condenser, (6a) is a first capillary tube, (7) is a gas-liquid separator, (8a) is a second capillary tube, (9) is an evaporator, (10) is an injection path, ( 11) is an auxiliary pressure reducing device, and (12) is a liquid refrigerant introduction path.
次に動作について説明する。低段圧縮機部(3)によっ
て圧縮された中圧中温のガス冷媒はインジェクション路
(10)を通ってきた中圧で飽和温度ガス、もしくは少
し湿り気味の冷媒と合流して高段圧縮機部(4)で高圧
、高温のガスに圧縮されて凝縮器(5)に至る。ここで
凝縮液化した高圧液冷媒のほとんどが第1のキャピラリ
ーチューブ(6a)で減圧されて中圧の二相冷媒となり
気液分離器(7)に流入する。ここで気液分離された中
圧飽和ガスおよび凝縮器(5)からの高圧液冷媒の一部
が補助減圧装置(11)で減圧された中圧の二相冷媒と
共にインジェクション路(io)を通り、上記高段圧縮
機部(4)に吸入される。また一方、気液分離器(7)
内の液は第2のキャピラリーチューブ(8a)で減圧さ
れ低圧二相冷媒となって蒸発器(9)でガス化し、再び
低段圧縮機部(3)に吸入されて冷媒回路が構成される
ことになる。Next, the operation will be explained. The medium-pressure medium-temperature gas refrigerant compressed by the low-stage compressor section (3) joins with the medium-pressure, saturated-temperature gas or slightly moist refrigerant that has passed through the injection path (10), and flows into the high-stage compressor section. At step (4), the gas is compressed into high-pressure, high-temperature gas and reaches the condenser (5). Most of the high-pressure liquid refrigerant condensed and liquefied here is depressurized in the first capillary tube (6a) to become a medium-pressure two-phase refrigerant and flows into the gas-liquid separator (7). Here, the intermediate pressure saturated gas separated into gas and liquid and a part of the high pressure liquid refrigerant from the condenser (5) pass through the injection path (io) together with the intermediate pressure two-phase refrigerant whose pressure has been reduced in the auxiliary pressure reducing device (11). , is sucked into the high stage compressor section (4). On the other hand, the gas-liquid separator (7)
The liquid inside is depressurized in the second capillary tube (8a), becomes a low-pressure two-phase refrigerant, is gasified in the evaporator (9), and is sucked into the low stage compressor section (3) again to form a refrigerant circuit. It turns out.
[発明が解決しようとする課題〕
従来の冷凍サイクル装置は以上のように構成されている
ので、圧縮機の起動時にインジェクション路を冷媒が逆
流して、起動時における圧力の立ち上りスピードが遅く
なったり、あるいはまた補助減圧装置より液インジェク
ションされる冷媒量が不適正の時は高段圧縮機部が液圧
縮を起すという不具合があった。[Problem to be solved by the invention] Since the conventional refrigeration cycle device is configured as described above, the refrigerant flows backward through the injection path when the compressor is started, and the pressure rise speed at the time of startup is slow. Alternatively, when the amount of refrigerant injected from the auxiliary pressure reducing device is inappropriate, there is a problem in that the high stage compressor section causes liquid compression.
この発明は上記のような問題点を解消するためになされ
たもので、低段圧縮機部の吐出口から気液分離器へ冷媒
が逆流して流れ込むことなく、また常に高段圧縮機部が
液圧縮を起すこともない冷凍サイクル装置を得ることを
目的とする。This invention was made to solve the above-mentioned problems, and it prevents the refrigerant from flowing backwards from the discharge port of the low-stage compressor section to the gas-liquid separator, and also prevents the high-stage compressor section from flowing back into the gas-liquid separator. The object is to obtain a refrigeration cycle device that does not cause liquid compression.
[課題を解決するための手段]
この発明に係る冷凍サイクル装置は、低段圧縮機部の吐
出口と高段圧縮機部の吸入口とを接続する連絡配管の途
中に、中圧飽和ガスとなっている気液分離器のガス部か
らのバイパス管を逆止弁を介して接続している。[Means for Solving the Problems] The refrigeration cycle device according to the present invention includes a medium-pressure saturated gas and The bypass pipe from the gas section of the gas-liquid separator is connected via a check valve.
[作 用]
この発明における冷凍サイクル装置は、圧縮機の起動時
に低段圧縮機部から吐出された中圧ガスが、逆止弁があ
るため気液分離器に逆流することなく、高段圧縮機部に
吸入されるので、起動時の圧力の立ち上り時間が短くな
る。さらに高段圧縮機部への吸入ガスは、低段圧縮機部
からの吐出過熱ガスと気液分離器内の中圧飽和ガスのみ
の混合冷媒なので、液圧縮は発生しない8
[実施例]
以下この発明の一実施例について説明する。すなわち第
1図において(1)は圧縮機、(1a)はその密閉形シ
ェル、(2)は内装の電動機、(3)はこれによって駆
動される内装の低段圧縮機部、(4)は同じく高段圧縮
機部、(5)は上v2密閉形シェル内に連通された凝縮
器、(6)はこれに接続された高段側膨張弁、(7)は
この膨張弁にガス部(7a)が接続された気液分離器、
(8)はこの気液分離器の液部(7b)に接続された低
段側膨張弁、(9)はこの膨張弁に接続された蒸発器、
(13)は上記低段圧縮機部の吐出口、(14)は高段
圧縮機部の吸入口で、これらは連絡配管(15)で連通
されている。(16)は上記気液分離器(7)のガス部
(7a)から引出されたバイパス管で、逆止弁(17)
を介して上記連絡配管(15)の途中に接続されている
。[Function] In the refrigeration cycle device of the present invention, the intermediate pressure gas discharged from the low stage compressor section when the compressor is started does not flow back to the gas-liquid separator due to the check valve, and is transferred to the high stage compressor. Since it is sucked into the machine part, the pressure rise time at startup is shortened. Furthermore, the suction gas to the high-stage compressor section is a mixed refrigerant consisting only of the superheated gas discharged from the low-stage compressor section and the medium-pressure saturated gas in the gas-liquid separator, so no liquid compression occurs8 [Example] Below An embodiment of this invention will be described. That is, in Fig. 1, (1) is the compressor, (1a) is its closed shell, (2) is the internal electric motor, (3) is the internal low stage compressor section driven by this, and (4) is the internal low stage compressor section. Similarly, the high-stage compressor section, (5) is a condenser communicated in the upper v2 closed shell, (6) is the high-stage expansion valve connected to this, and (7) is the gas section ( 7a) a gas-liquid separator connected to
(8) is a low-stage expansion valve connected to the liquid part (7b) of this gas-liquid separator; (9) is an evaporator connected to this expansion valve;
(13) is the discharge port of the low-stage compressor section, and (14) is the suction port of the high-stage compressor section, which are communicated by a connecting pipe (15). (16) is a bypass pipe drawn out from the gas section (7a) of the gas-liquid separator (7), and a check valve (17)
It is connected to the middle of the connecting pipe (15) via the connecting pipe (15).
次に動作について説明する。低段圧縮機部(3)によっ
て圧縮された中圧中温のガス冷媒は、バイパス管(16
)より流入する中圧飽和ガス冷媒と合流した後、高段圧
縮機部(4)に吸入されて高温高圧のガス冷媒となり吐
出されて凝縮器(5)に至る。Next, the operation will be explained. The medium-pressure medium-temperature gas refrigerant compressed by the low-stage compressor section (3) passes through the bypass pipe (16
), it is sucked into the high-stage compressor section (4), becomes a high-temperature, high-pressure gas refrigerant, and is discharged to the condenser (5).
ここで凝縮液化した高圧液冷媒は高段側膨張弁(6)で
中圧まで減圧されて二相冷媒となり気液分離器(7)に
流入する。気液分離器(7)内のガス部(7a)におけ
るガス冷媒はバイパス管(16)により逆止弁(17)
を経由して再び高段圧縮機部(4)に吸入される。−勇
気液分離器(7)内の液部(7b)における中圧飽和液
は低段側膨張弁(8)で低圧二相冷媒となり、蒸発器(
9)で蒸発ガス化して再び低段圧縮機部(3)に吸入さ
れ、このようにして二段圧縮方式の冷凍サイクルが構成
されている。また第1図に示す冷凍サイクルの各ポイン
ト(a) (b) (c) (d) (e)(f) (
g) (h) (i)個所は第2図のモリエル線図上で
同一符号で示す通りになっている。The high-pressure liquid refrigerant condensed and liquefied here is depressurized to intermediate pressure by the high-stage expansion valve (6), becomes a two-phase refrigerant, and flows into the gas-liquid separator (7). The gas refrigerant in the gas section (7a) in the gas-liquid separator (7) is passed through the check valve (17) by the bypass pipe (16).
is sucked into the high-stage compressor section (4) again. - The medium-pressure saturated liquid in the liquid part (7b) in the liquid separator (7) becomes a low-pressure two-phase refrigerant in the low-stage expansion valve (8), and becomes a low-pressure two-phase refrigerant in the evaporator (
In step 9), it is evaporated into gas and sucked into the low-stage compressor section (3) again, thus configuring a two-stage compression type refrigeration cycle. In addition, each point (a) (b) (c) (d) (e) (f) (
g) (h) (i) The locations are as indicated by the same reference numerals on the Mollier diagram in FIG.
なお上記実施例では低段側膨張弁と高段側膨張弁を使用
したが、これらはキャピラリーチューブでも、あるいは
電子膨張弁であってもよい。In the above embodiment, a low-stage expansion valve and a high-stage expansion valve are used, but these may be capillary tubes or electronic expansion valves.
[発明の効果コ
この発明の冷凍サイクル装置は以上のように構成してい
るので、低段圧縮機部の吐出口から気液分離器内への冷
媒の逆流がなく、また高段圧縮機部での液圧縮のおそれ
もなく、しかも起動時の圧力の立ち上りの早い冷凍サイ
クル装置が得られるという効果がある。[Effects of the Invention] Since the refrigeration cycle device of the present invention is configured as described above, there is no backflow of refrigerant from the discharge port of the low stage compressor section into the gas-liquid separator, and This has the effect of providing a refrigeration cycle device in which there is no fear of liquid compression during startup, and the pressure rises quickly at startup.
第1図はこの発明の冷凍サイクル装置の一実施例を示す
冷媒回路図、第2図はそのモリエル線図、第3図は従来
の冷凍サイクル装置の冷媒回路図である。
なお図中(1)は圧縮機、(la)は密閉形シェル、(
2)は電動機、(3)は低段圧縮機部、(4)は高段圧
縮機部、(5)は凝縮器、(6)は高段側膨張弁、(7
)は気液分離器、(7a)はガス部、(7b)は液部、
(13)は吐出口、(14)は吸入口、(15)は連絡
配管、(16)はバイパス管、 (17)は逆止弁であ
る。
圧縮機
口止出口
5、凝縮器
6 : KF?tfAlfll’yl井7゛気液OI
!器
7a カス艶
7b ’7部
第
図FIG. 1 is a refrigerant circuit diagram showing one embodiment of the refrigeration cycle apparatus of the present invention, FIG. 2 is a Mollier diagram thereof, and FIG. 3 is a refrigerant circuit diagram of a conventional refrigeration cycle apparatus. In the figure, (1) is the compressor, (la) is the closed shell, (
2) is an electric motor, (3) is a low-stage compressor section, (4) is a high-stage compressor section, (5) is a condenser, (6) is a high-stage expansion valve, and (7) is a high-stage compressor section.
) is a gas-liquid separator, (7a) is a gas part, (7b) is a liquid part,
(13) is a discharge port, (14) is an inlet, (15) is a connecting pipe, (16) is a bypass pipe, and (17) is a check valve. Compressor port 5, condenser 6: KF? tfAlfll'yl Well 7゛Gas-Liquid OI
! Vessel 7a Kasu Gloss 7b 'Part 7 Figure
Claims (1)
と高段圧縮機部とを密閉形シェル内に有する圧縮機、上
記シェル内に連通された凝縮器、これに高段側膨張弁を
介してそのガス部が接続された気液分離器、これの液部
に低段側膨張弁を介して接続され上記低段圧縮器部に連
通する蒸発器とから構成された冷凍サイクルにおいて、
上記低段圧縮機部の吐出口と高段圧縮機部の吸入口を接
続する連絡配管の途中に、上記気液分離器のガス部から
のバイパス配管を逆止弁を介して接続したことを特徴と
する冷凍サイクル装置。A compressor having a single electric motor, a low-stage compressor section and a high-stage compressor section driven by the motor in a closed shell, a condenser communicated with the shell, and a high-stage expansion valve. In a refrigeration cycle comprising a gas-liquid separator whose gas section is connected through a gas-liquid separator, and an evaporator that is connected to the liquid section of the separator through a low-stage expansion valve and communicates with the low-stage compressor section,
A bypass pipe from the gas section of the gas-liquid separator is connected via a check valve in the middle of the connecting pipe connecting the discharge port of the low-stage compressor section and the suction port of the high-stage compressor section. Features of refrigeration cycle equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18796990A JPH0476358A (en) | 1990-07-18 | 1990-07-18 | Device in refrigerating cycle |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18796990A JPH0476358A (en) | 1990-07-18 | 1990-07-18 | Device in refrigerating cycle |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0476358A true JPH0476358A (en) | 1992-03-11 |
Family
ID=16215318
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18796990A Pending JPH0476358A (en) | 1990-07-18 | 1990-07-18 | Device in refrigerating cycle |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0476358A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100452347B1 (en) * | 2001-08-02 | 2004-10-12 | 엘지전자 주식회사 | A evaporator using micro channel heat exchanger |
KR100488532B1 (en) * | 2003-07-08 | 2005-05-11 | 삼성전자주식회사 | Cooling system |
JP2006207974A (en) * | 2005-01-31 | 2006-08-10 | Sanyo Electric Co Ltd | Refrigerating apparatus and refrigerator |
-
1990
- 1990-07-18 JP JP18796990A patent/JPH0476358A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100452347B1 (en) * | 2001-08-02 | 2004-10-12 | 엘지전자 주식회사 | A evaporator using micro channel heat exchanger |
KR100488532B1 (en) * | 2003-07-08 | 2005-05-11 | 삼성전자주식회사 | Cooling system |
JP2006207974A (en) * | 2005-01-31 | 2006-08-10 | Sanyo Electric Co Ltd | Refrigerating apparatus and refrigerator |
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