JPH03211364A - refrigeration cycle - Google Patents
refrigeration cycleInfo
- Publication number
- JPH03211364A JPH03211364A JP611990A JP611990A JPH03211364A JP H03211364 A JPH03211364 A JP H03211364A JP 611990 A JP611990 A JP 611990A JP 611990 A JP611990 A JP 611990A JP H03211364 A JPH03211364 A JP H03211364A
- Authority
- JP
- Japan
- Prior art keywords
- refrigeration cycle
- refrigerant
- mixed refrigerant
- rectifier
- pressure
- 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
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (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、混合冷媒を用いた冷凍サイクルに関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a refrigeration cycle using a mixed refrigerant.
第3図は、特開昭62−237252号公報に記載の技
術で公知である。FIG. 3 is a known technique described in Japanese Unexamined Patent Publication No. 62-237252.
上記の公知技術は、冷凍サイクル内の貯留器31に低沸
点冷媒を溜めるために、圧縮機20の吐出して分離装置
35に入る混合冷媒を加熱器32で加熱し、加熱と分離
装置35で発生した低沸点冷媒を冷却液化し、貯留器3
1に溜めるために、室内熱交換器22または、空外熱交
換器23より出た混合冷媒の一部を、膨張弁24、また
は。The above-mentioned known technology heats the mixed refrigerant discharged from the compressor 20 and enters the separator 35 with the heater 32 in order to store the low-boiling point refrigerant in the reservoir 31 in the refrigeration cycle. The generated low boiling point refrigerant is cooled and liquefied, and stored in the reservoir 3.
1, a part of the mixed refrigerant discharged from the indoor heat exchanger 22 or the outdoor heat exchanger 23 is transferred to the expansion valve 24 or .
26で低圧にし、冷却器25で冷却する冷凍サイクルで
ある。This is a refrigeration cycle in which the pressure is lowered at 26 and cooled at a cooler 25.
上記従来技術は、冷凍サイクル内の貯溜器に低沸点冷媒
を溜めるものであった。The above conventional technology stores a low boiling point refrigerant in a reservoir within a refrigeration cycle.
本発明の目的は、冷凍サイクル内の分離装置の貯留部に
高沸点冷媒を溜める冷凍サイクルを提供することにある
。An object of the present invention is to provide a refrigeration cycle in which a high boiling point refrigerant is stored in a storage section of a separation device within the refrigeration cycle.
上記目的を達成するために1本発明では、分離装置の貯
留部は凝縮器出口からの混合冷媒で加熱する。In order to achieve the above object, in one aspect of the present invention, the storage section of the separator is heated with a mixed refrigerant from the condenser outlet.
また、分離装置で発生した低沸点冷媒は、冷凍サイクル
での低圧側に戻すようにした。Furthermore, the low boiling point refrigerant generated in the separator was returned to the low pressure side of the refrigeration cycle.
この構成により、分離装置の貯留部には低沸点冷媒を溜
めることができ、主回路の混合冷媒の組成を使用目的に
従って変化させることができる。With this configuration, the low boiling point refrigerant can be stored in the storage section of the separator, and the composition of the mixed refrigerant in the main circuit can be changed according to the purpose of use.
以下、本発明の実施例を第1図、第2図について説明す
る6
第1図の混合冷媒の分離時の説明をする。Hereinafter, embodiments of the present invention will be explained with reference to FIGS. 1 and 2. 6 The separation of the mixed refrigerant shown in FIG. 1 will be explained.
圧縮機1で高温、高圧にされた混合冷媒は、四方弁2を
通り、室外熱交換器5.または、室内熱交換器4で凝縮
されて液となり、整流装置6を通って二方向に分岐する
。一方はキャピラリチューブ8で流量調整をし分離装置
17の上部に入り。The mixed refrigerant made high temperature and high pressure by the compressor 1 passes through the four-way valve 2 and is transferred to the outdoor heat exchanger 5. Alternatively, it is condensed into a liquid in the indoor heat exchanger 4, passes through the rectifier 6, and branches into two directions. One side adjusts the flow rate with the capillary tube 8 and enters the upper part of the separation device 17.
整流装置6より分岐したもう一方は、二方弁9と加熱器
16を通り、膨張弁12で低圧となる、分離装置17は
、上部よりキャピラリチューブ8で流量調整した混合冷
媒が流下し、また、一方は分離装置17の下部の貯留部
に溜まった混合冷媒を、加熱器16で加熱し、低沸点冷
媒を蒸発させる。そして、流下する混合冷媒と上昇する
低沸点冷媒とを充填物18を介して、接触させることに
より熱と物質が移動して混合冷媒の分離を行う。The other branched from the rectifier 6 passes through a two-way valve 9 and a heater 16, and becomes low pressure at the expansion valve 12.The separator 17 has a mixed refrigerant flowing down from the upper part, whose flow rate is adjusted by a capillary tube 8, and On the other hand, the mixed refrigerant accumulated in the storage section at the lower part of the separator 17 is heated by the heater 16 to evaporate the low boiling point refrigerant. Then, by bringing the flowing down mixed refrigerant and the rising low boiling point refrigerant into contact with each other via the filling 18, heat and substances are transferred and the mixed refrigerant is separated.
この時、分離装置17、貯留部の液面のオーバーフロー
分は配管15で低圧側に戻し、液面調整を行う。また、
分離装置17の下部の貯留部に高沸点冷媒とともに、油
も溜まる可能性があるため、これはキャピラリチューブ
14を通り低圧側に戻すことにより油を循環させる。At this time, the overflow of the liquid level in the separator 17 and the storage section is returned to the low pressure side through the pipe 15 to adjust the liquid level. Also,
Since oil may also accumulate together with the high boiling point refrigerant in the lower reservoir of the separation device 17, the oil is circulated by passing through the capillary tube 14 and returning to the low pressure side.
分離装置17の上部より出た低沸点ガス冷媒は、キャピ
ラリチューブ10を通り配管工5より出てくる分離装置
17の貯留部のオーバーフロー分と、キャピラリチュー
ブ14より出てくる油を含む高沸点冷媒と合流し、二方
弁13を通り、さらに。The low boiling point gas refrigerant discharged from the upper part of the separator 17 is composed of an overflow portion of the storage section of the separator 17 which passes through the capillary tube 10 and comes out from the plumber 5, and a high boiling point refrigerant containing oil which comes out from the capillary tube 14. , passes through two-way valve 13, and continues.
膨張弁12を通って低圧となった混合冷媒と合流し、整
流装置6を通り、室内熱交換器4.または、室外熱交換
器5で蒸発され、四方弁2とアキュムレータ3を通り、
圧縮機へ吸い込まれる冷凍サイクルを構成する。It passes through the expansion valve 12, joins with the low-pressure mixed refrigerant, passes through the rectifier 6, and enters the indoor heat exchanger 4. Or, it is evaporated in the outdoor heat exchanger 5, passes through the four-way valve 2 and the accumulator 3,
It constitutes a refrigeration cycle that is sucked into the compressor.
次に、混合冷媒の混合時について説明する。Next, the time of mixing the mixed refrigerant will be explained.
主回路についての動作は、冷凍サイクルと同じなので相
違箇所のみについて説明する。The operation of the main circuit is the same as that of the refrigeration cycle, so only the differences will be explained.
凝縮された高圧の混合冷媒は、整流装置6を通り二方向
に分岐されるが、一方は二方弁9を閉じ、もう一方のみ
に流す。このときキャピラリチューブをバイパスする二
方弁7を開ける。分離装置17に入り、下部より出て、
逆止弁11を通り膨張弁12で低圧になり整流装置に入
る。このとき二方弁13を閉じ分離装置17より低圧側
へ流れるのを防ぐ冷凍サイクルを構成する。The condensed high-pressure mixed refrigerant passes through the rectifier 6 and is branched into two directions, one of which closes the two-way valve 9 and flows only into the other direction. At this time, open the two-way valve 7 that bypasses the capillary tube. Enters the separation device 17, exits from the bottom,
It passes through the check valve 11, becomes low pressure at the expansion valve 12, and enters the rectifier. At this time, the two-way valve 13 is closed to form a refrigeration cycle that prevents the fluid from flowing to the lower pressure side from the separator 17.
第2図の冷凍サイクルの主回路は第1図の冷凍サイクル
と同じなので相違箇所のみについて説明する。The main circuit of the refrigeration cycle shown in FIG. 2 is the same as the refrigeration cycle shown in FIG. 1, so only the differences will be explained.
まず、混合冷媒の分離時について説明する。First, the separation of the mixed refrigerant will be explained.
整流装置6から出た高圧の混合冷媒は三方向に分岐する
が、一つは二方弁9を閉じるので二方向のみに流れる。The high-pressure mixed refrigerant coming out of the rectifier 6 branches into three directions, but one of them closes the two-way valve 9, so it flows only in two directions.
一方は二方弁7を通り、キャピラリチューブ8で流量調
整して、分離装置17に入り、整流装置6から分岐した
もう一方は、加熱器16と二方弁11を通り、膨張弁1
2で低圧となる。One side passes through the two-way valve 7, the flow rate is adjusted with a capillary tube 8, and enters the separation device 17.
At 2, the pressure is low.
分離装置17の上部より出た低沸点冷媒は、キャピラリ
チューブ10を通り配管15より出てくる分離装置17
の貯留部のオーバーフロー分と、キャピラリチューブ1
4より出てくる油を含む高沸点冷媒と合流し、逆止弁1
9を通り、さらに、膨張弁12を通り低圧となった混合
冷媒と合流し、整流装置6に入る冷凍サイクルを構成す
る6次に、混合冷媒の混合時について説明する。The low boiling point refrigerant coming out from the upper part of the separation device 17 passes through the capillary tube 10 and comes out from the piping 15 to the separation device 17.
The overflow of the reservoir and the capillary tube 1
It joins with the high boiling point refrigerant containing oil coming out from check valve 1.
9, further passes through the expansion valve 12, joins with the low-pressure mixed refrigerant, and enters the rectifier 6, forming a refrigeration cycle.Next, the mixing of the mixed refrigerant will be described.
整流装置6から出た高圧の冷媒ガスは三方向に分岐する
が、二方弁7と二方弁11を閉じるので一方向のみ流れ
る6流れる方向は、二方弁9と貯留器を通り膨張弁12
で低圧となり整流装置6に入る。このとき分離装置17
には逆止弁19を介しているので流れることはない冷凍
サイクルを構成する。The high-pressure refrigerant gas that comes out of the rectifier 6 branches into three directions, but since the two-way valves 7 and 11 are closed, only one direction flows 6. The flow direction is through the two-way valve 9 and the reservoir, and then to the expansion valve. 12
The pressure becomes low and enters the rectifier 6. At this time, the separation device 17
A refrigeration cycle is constructed in which no flow occurs because the flow is via the check valve 19.
整流装置6について説明する。The rectifier 6 will be explained.
第1図、第2図に示す整流装置6は逆止弁四つの組み合
わせである。室内熱交換器4から高圧の混合冷媒が流れ
てきた場合は一方向のみ決まり、分離装置17へ流れ込
む。膨張弁12で低圧となつた混合冷媒は、整流装置6
に入り流れる。方向は二方向あるが、一方は高圧である
ために流れる方向が一つだけが決まり室外熱交換器5へ
流れ込む。The rectifying device 6 shown in FIGS. 1 and 2 is a combination of four check valves. When the high-pressure mixed refrigerant flows from the indoor heat exchanger 4, only one direction is determined and it flows into the separation device 17. The mixed refrigerant that has become low pressure at the expansion valve 12 is transferred to the rectifier 6.
It enters and flows. There are two directions, but since one is at high pressure, only one flow direction is determined, and it flows into the outdoor heat exchanger 5.
室外熱交換器5から高圧の混合冷媒が流れてきた場合も
、上記と同しような動作をし、混合冷媒の流れる方向が
決まり、分離装置17には、常に、同じ方向から流し込
むことができる。When a high-pressure mixed refrigerant flows from the outdoor heat exchanger 5, the same operation as described above is performed, the direction in which the mixed refrigerant flows is determined, and it can always flow into the separation device 17 from the same direction.
本発明によれば、冬期暖房起動運動時の立上りがはやく
、また、圧縮機の油戻しが確実に行われる。According to the present invention, the start-up during the winter heating start-up movement is quick, and the oil return to the compressor is reliably performed.
第1図、第2図は本発明の冷凍サイクルの実施例の系統
図、第3図は従来例の系統図である。
1・・圧縮機、4・・・室内熱交換器、5 室外熱交換
器、6・・整流装置、12・膨張弁、16・・加熱器。
第
図
g、IO,淳
キャヒ1ラッチユーフ1 and 2 are system diagrams of an embodiment of the refrigeration cycle of the present invention, and FIG. 3 is a system diagram of a conventional example. 1. Compressor, 4. Indoor heat exchanger, 5. Outdoor heat exchanger, 6. Rectifier, 12. Expansion valve, 16. Heater. Figure g, IO, Atsushi 1 latch yuf
Claims (1)
した主回路に、複数の冷媒を封入し、前記冷媒の組成を
変えるための冷媒分離装置を設けた冷凍サイクルにおい
て、 主回路と前記冷媒分離装置との接続を、整流装置を用い
ることにより前記冷媒分離装置への前記冷媒の流れの方
向が一定となることを特徴とする冷凍サイクル。[Claims] 1. A main circuit connecting each element of a compressor, a condenser, a throttle device, and an evaporator is filled with a plurality of refrigerants, and a refrigerant separation device is provided for changing the composition of the refrigerants. A refrigeration cycle, characterized in that a flow direction of the refrigerant to the refrigerant separator becomes constant by using a rectifier to connect the main circuit and the refrigerant separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP611990A JPH03211364A (en) | 1990-01-17 | 1990-01-17 | refrigeration cycle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP611990A JPH03211364A (en) | 1990-01-17 | 1990-01-17 | refrigeration cycle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03211364A true JPH03211364A (en) | 1991-09-17 |
Family
ID=11629622
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP611990A Pending JPH03211364A (en) | 1990-01-17 | 1990-01-17 | refrigeration cycle |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03211364A (en) |
-
1990
- 1990-01-17 JP JP611990A patent/JPH03211364A/en active Pending
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