JP2916381B2 - Separate heat pump - Google Patents
Separate heat pumpInfo
- Publication number
- JP2916381B2 JP2916381B2 JP6215764A JP21576494A JP2916381B2 JP 2916381 B2 JP2916381 B2 JP 2916381B2 JP 6215764 A JP6215764 A JP 6215764A JP 21576494 A JP21576494 A JP 21576494A JP 2916381 B2 JP2916381 B2 JP 2916381B2
- Authority
- JP
- Japan
- Prior art keywords
- flow path
- refrigerant
- expansion valve
- condenser
- compressor
- 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 - Fee Related
Links
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Air Conditioning Control Device (AREA)
Description
【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION
【0001】[0001]
【産業上の利用分野】本発明は、大型ビル空調設備とし
て好適なセパレート形ヒートポンプに関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a separate type heat pump suitable as a large building air conditioning system.
【0002】[0002]
【従来の技術】従来、図2に示すセパレート形ヒートポ
ンプが公知である。この図2では、暖房基調比例熱回収
運転時の状態を示しており、油冷式の圧縮機11、例え
ば油冷式スクリュ圧縮機、油分離回収器12、第1開閉
弁13、凝縮器14、第1膨張弁15、および蒸発器1
6を含む第1冷媒循環流路と、この冷媒循環流路の内の
凝縮器14と第1膨張弁15との間の流路の部分にて三
方切換弁17を介して分岐するとともに、蒸発器16と
圧縮機11の間の流路の部分にて合流し、圧縮機11、
油分離回収器12、第1開閉弁13、凝縮器14、第2
膨張弁18および空気熱交換器19を含む第2冷媒循環
流路とが形成されている。なお、このヒートポンプで
は、第1冷媒循環流路と第2冷媒循環流路とが合流する
箇所の各流路の上流側に流量調節弁20,第2開閉弁2
1が設けてある。この運転状態では、油分離回収器12
から凝縮器14に至る流路の内の、第1開閉弁13の上
流側の部分から分岐して、第2開閉弁21の上流側の部
分に合流する流路は閉じられている。2. Description of the Related Art Conventionally, a separate heat pump shown in FIG. 2 is known. FIG. 2 shows a state during a heating tone proportional heat recovery operation, in which an oil-cooled compressor 11, for example, an oil-cooled screw compressor, an oil separation and recovery unit 12, a first on-off valve 13, a condenser 14 , First expansion valve 15, and evaporator 1
6 and a portion of a flow path between the condenser 14 and the first expansion valve 15 in the refrigerant circulation flow path through the three-way switching valve 17, and evaporates. At the part of the flow path between the compressor 16 and the compressor 11, and the compressor 11,
Oil separation and recovery unit 12, first on-off valve 13, condenser 14, second
A second refrigerant circulation flow path including the expansion valve 18 and the air heat exchanger 19 is formed. In this heat pump, the flow control valve 20 and the second on-off valve 2 are provided upstream of each flow path at a location where the first refrigerant flow path and the second refrigerant flow path join.
1 is provided. In this operation state, the oil separation and recovery device 12
In the flow path from the flow path to the condenser 14, the flow path that branches off from the upstream portion of the first on-off valve 13 and joins the upstream portion of the second on-off valve 21 is closed.
【0003】また、このヒートポンプでは、冷媒流路の
蒸発器16の下流側側部分に温度検出器22および圧力
検出器23が設けてあり、この両検出器からの信号に基
づいて過熱度を算出して、この過熱度が適正な状態にな
るように第1膨張弁15の開度を調節する過熱度調節計
24が設けてある。さらに、冷媒流路の空気熱交換器1
9の下流側部分に温度検出器25および圧力検出器26
が設けてあり、この両検出器からの信号に基づいて過熱
度を算出して、この過熱度が適正な状態になるように第
2膨張弁18の開度を調節する過熱度調節計27が設け
てある。一方、蒸発器16から流出する冷水の流路に
は、この流路内の冷水の温度を検出して、この温度が設
定値になるように流量調節弁20の開度を調節する温度
調節器28が設けてある。In this heat pump, a temperature detector 22 and a pressure detector 23 are provided in a portion of the refrigerant flow passage on the downstream side of the evaporator 16, and the degree of superheat is calculated based on signals from the two detectors. Then, a superheat degree controller 24 for adjusting the opening degree of the first expansion valve 15 so that the superheat degree becomes an appropriate state is provided. Furthermore, the air heat exchanger 1 in the refrigerant flow path
9, a temperature detector 25 and a pressure detector 26
The superheat controller 27 that calculates the degree of superheat based on the signals from the two detectors and adjusts the degree of opening of the second expansion valve 18 so that the degree of superheat is in an appropriate state is provided. It is provided. On the other hand, in the flow path of the cold water flowing out of the evaporator 16, a temperature controller that detects the temperature of the cold water in the flow path and adjusts the opening of the flow control valve 20 so that the temperature becomes a set value. 28 are provided.
【0004】そして、凝縮器14を出た冷媒を第1膨張
弁15および第2膨張弁18に導き、第1,第2冷媒循
環流路内で循環させて、凝縮器14にて温水を、蒸発器
16にて冷水を作り出し、空気熱交換器19にて空気中
に放熱するようになっている。斯るヒートポンプの内
で、例えば病院等で使用される大型のものについては、
冬であっても冷水、温水を作り出すことが要求される。
凝縮器14で作り出される温水は、夏であっても冬であ
っても、常に要求されるのに対して、冷水は、特に冬に
おいて、使う時と使わない時がある。冷水を使わない時
は、温度調節計28からの信号により流量調節弁20の
開度は縮小されてゆき、これとともに過熱度調節計24
からの信号により第1膨張弁15の開度も縮小され、蒸
発器16からの冷媒の流量は減少してゆく。これに対し
て、凝縮器14から空気熱交換器19側に流れる冷媒は
増大し、過熱度調節計27からの信号によって第2膨張
弁18の開度は調節される。Then, the refrigerant that has exited the condenser 14 is guided to the first expansion valve 15 and the second expansion valve 18 and circulated in the first and second refrigerant circulation passages. The evaporator 16 produces cold water, and the air heat exchanger 19 radiates heat into the air. Among such heat pumps, for large ones used in hospitals, for example,
It is required to produce cold and hot water even in winter.
The hot water produced by the condenser 14 is always required, whether in summer or winter, whereas cold water is used or not used, especially in winter. When cold water is not used, the opening degree of the flow control valve 20 is reduced by a signal from the temperature controller 28, and the superheat degree controller 24
, The opening degree of the first expansion valve 15 is also reduced, and the flow rate of the refrigerant from the evaporator 16 is reduced. On the other hand, the amount of the refrigerant flowing from the condenser 14 to the air heat exchanger 19 increases, and the opening degree of the second expansion valve 18 is adjusted by a signal from the superheat degree controller 27.
【0005】[0005]
【発明が解決しようとする課題】上記従来のヒートポン
プでは、凝縮器14から蒸発器16或は空気熱交換器1
9へ流れる冷媒の量は、第1,第2膨張弁15,18に
より制御されている。一方、通常、凝縮器14、蒸発器
16は地下室に、また空気熱交換器19はビルの屋上に
設置されており、これらの高低差は100mにも達する
場合もある。第2膨張弁18の2次側は冷媒ガスと冷媒
液の2相流となるため、ある流速以下では、冷媒ガスと
冷媒液とが分離して、配管底部に液滞留が起こる。その
後、圧縮機11の容量変動および冷水負荷の変動が生じ
た場合、圧縮機11の吸込量の増大、冷媒の流速の増大
が生じる。この流速の増大により、圧縮機11に液体の
状態の冷媒が戻る、液バック現象が生じて、圧縮機11
にダメージを与えるという問題が生じる。本発明は、斯
る従来の問題点を課題としてなされたもので、空気熱交
換器への冷媒の流量が減少するような負荷条件下におい
ても圧縮機への液バックおよびこれに伴う圧縮機の損傷
事故の発生防止を可能としたセパレート形ヒートポンプ
を提供しようとするものである。In the above-described conventional heat pump, the condenser 14 is turned into the evaporator 16 or the air heat exchanger 1.
The amount of the refrigerant flowing to 9 is controlled by the first and second expansion valves 15 and 18. On the other hand, the condenser 14 and the evaporator 16 are usually installed in a basement, and the air heat exchanger 19 is installed on the roof of a building, and the height difference between them may reach 100 m. Since the secondary side of the second expansion valve 18 has a two-phase flow of the refrigerant gas and the refrigerant liquid, the refrigerant gas and the refrigerant liquid are separated at a certain flow rate or less, and liquid stays at the bottom of the pipe. Thereafter, when a change in the capacity of the compressor 11 and a change in the chilled water load occur, the suction amount of the compressor 11 and the flow velocity of the refrigerant increase. Due to the increase in the flow velocity, the refrigerant in a liquid state returns to the compressor 11, and a liquid back phenomenon occurs, and the compressor 11
The problem of damaging the device. SUMMARY OF THE INVENTION The present invention has been made to solve the above-described conventional problems. Even under a load condition in which the flow rate of the refrigerant to the air heat exchanger is reduced, the liquid back to the compressor and the accompanying An object of the present invention is to provide a separate heat pump that can prevent the occurrence of a damage accident.
【0006】[0006]
【課題を解決するための手段】上記課題を解決するため
に、本発明は、少なくとも圧縮機,凝縮器,第1膨張
弁,蒸発器を含む第1冷媒循環流路と、この冷媒循環流
路の内の上記凝縮器と上記第1膨張弁との間の流路の部
分から分岐するとともに、上記蒸発器と上記圧縮機の間
の流路の部分にて合流し、少なくとも上記圧縮機,上記
凝縮器,第2膨張弁,空気熱交換器を含む第2冷媒流路
とを形成できるセパレート形ヒートポンプにおいて、上
記凝縮器の入側の冷媒流路の部分にて分岐し、上記第2
膨張弁の出側の流路の部分にて合流するホットガス流路
を設けるとともに、このホットガス流路に、ここを流れ
る冷媒の量が少なくなった場合には、開度が大きくなる
流量調節弁を設けて形成した。In order to solve the above-mentioned problems, the present invention provides a first refrigerant circulating flow path including at least a compressor, a condenser, a first expansion valve, and an evaporator; And branches off from a part of a flow path between the condenser and the first expansion valve, and joins at a part of a flow path between the evaporator and the compressor to form at least the compressor and the compressor. In a separate type heat pump capable of forming a second refrigerant flow path including a condenser, a second expansion valve, and an air heat exchanger, a branch is made at a part of the refrigerant flow path on the inlet side of the condenser, and
In addition to providing a hot gas flow path that merges at the flow path portion on the outlet side of the expansion valve, the flow rate adjustment increases the degree of opening when the amount of refrigerant flowing through the hot gas flow path decreases. It was formed with a valve.
【0007】[0007]
【作用】上記発明のように構成することにより、凝縮器
を出て、空気熱交換器側に流れる冷媒の量が減少する負
荷条件下においても、空気熱交換器への冷媒の必要最低
流速が確保されるようになる。With the construction as described above, the required minimum flow rate of the refrigerant to the air heat exchanger can be reduced even under load conditions in which the amount of the refrigerant flowing out of the condenser and flowing to the air heat exchanger side is reduced. Will be secured.
【0008】[0008]
【実施例】次に、本発明の一実施例を図面にしたがって
説明する。図1は、本発明に係るセパレート形ヒートポ
ンプを示し、図2に示すセパレート形ヒートポンプと互
いに共通する部分については、同一番号を付して説明を
省略する。本実施例では、凝縮器14の入側の冷媒流路
の部分にて分岐し、第2膨張弁18の出側の流路の部分
にて合流するホットガス流路1を設けるとともに、この
ホットガス流路1に、過熱度調節計27により開度制御
される流量調節弁2を設けて形成してある。また、本実
施例では、図2に示すヒートポンプにおける三方切換弁
17に代えて、開閉弁3,4を設けて、三方切換弁17
と同様の働きをさせている。Next, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows a separate heat pump according to the present invention. Portions common to those of the separate heat pump shown in FIG. In the present embodiment, the hot gas flow path 1 which branches at the refrigerant flow path on the inlet side of the condenser 14 and joins at the flow path on the output side of the second expansion valve 18 is provided. The gas flow path 1 is provided with a flow control valve 2 whose opening is controlled by a superheat controller 27. In the present embodiment, on-off valves 3 and 4 are provided instead of the three-way switching valve 17 in the heat pump shown in FIG.
Works in the same way as
【0009】そして、第2膨張弁18の開度が小さくな
って、空気熱交換器19へ流れる冷媒の量が少なくなっ
てくると、流量調節弁2の開度が大きくなって、油分離
回収器12を出た、ホットガスの一部を空気熱交換器1
9に至る配管の途中に導き、この配管内での冷媒の流速
を増大させるようにしてある。具体的には、例えば第2
膨張弁18の開度が小さくなってきて、ある設定値、例
えば50%に達すると、流量調節弁2を開き始め、第2
膨張弁18の開度がさらに小さくなっていくと、この開
度に反比例して流量調節弁2の開度を増大させるように
なっている。さらに、第2膨張弁18の開度が小さくな
って、設定値、例えば20%に達すると、流量調節弁2
は全開の状態となる。When the degree of opening of the second expansion valve 18 decreases and the amount of refrigerant flowing to the air heat exchanger 19 decreases, the degree of opening of the flow control valve 2 increases, and oil separation and recovery occurs. A part of the hot gas exiting the heat exchanger 12 is transferred to the air heat exchanger 1
9 is introduced in the middle of the pipe to increase the flow rate of the refrigerant in this pipe. Specifically, for example, the second
When the opening degree of the expansion valve 18 decreases and reaches a certain set value, for example, 50%, the flow control valve 2 starts to be opened,
As the opening of the expansion valve 18 further decreases, the opening of the flow control valve 2 increases in inverse proportion to this opening. Further, when the opening of the second expansion valve 18 decreases and reaches a set value, for example, 20%, the flow control valve 2
Becomes fully open.
【0010】また、このヒートポンプでは、冷水負荷に
対して優先的に対応させるようになっており、冷水負荷
に対応させている間は、空気熱交換器19側へはできる
だけ冷媒を流すことを避けるため、第2膨張弁18の開
度が10%以下では、これを全閉にするようになってい
る。このように、第2膨張弁18を通る冷媒の量が減少
すると、空気熱交換器19への配管に送るホットガスの
量を増大させて、冷媒液と冷媒ガスの2相流が空気熱交
換器19へ安定して流れるようにして、圧縮機11への
液バック現象の発生およびこれに伴う圧縮機11の損傷
事故の発生を防止している。さらに、冷水負荷に対応し
て、蒸発器16側への追従を行い、かつ凝縮器14での
温水負荷対応もでき、特に、温水を安定供給しつつ、冷
水の負荷が0〜100%変動しても、安定したヒートポ
ンプの運転が可能となっている。[0010] In this heat pump, the chilled water load is preferentially dealt with.
When the opening degree of the second expansion valve 18 is 10% or less, the second expansion valve 18 is fully closed in order to avoid flowing the refrigerant to the air heat exchanger 19 as much as possible. . As described above, when the amount of the refrigerant passing through the second expansion valve 18 decreases, the amount of the hot gas sent to the pipe to the air heat exchanger 19 increases, and the two-phase flow of the refrigerant liquid and the refrigerant gas exchanges the air heat. By causing the liquid to flow stably to the compressor 19, the occurrence of a liquid back phenomenon to the compressor 11 and the occurrence of a damage accident of the compressor 11 due to this phenomenon are prevented. Further, in response to the cold water load, it can follow the evaporator 16 side, and can also respond to the hot water load in the condenser 14. In particular, while the hot water is supplied stably, the load of the cold water fluctuates by 0 to 100%. However, stable operation of the heat pump is possible.
【0011】[0011]
【発明の効果】以上の説明より明らかなように、本発明
によれば、少なくとも圧縮機,凝縮器,第1膨張弁,蒸
発器を含む第1冷媒循環流路と、この冷媒循環流路の内
の上記凝縮器と上記第1膨張弁との間の流路の部分から
分岐するとともに、上記蒸発器と上記圧縮機の間の流路
の部分にて合流し、少なくとも上記圧縮機,上記凝縮
器,第2膨張弁,空気熱交換器を含む第2冷媒流路とを
形成できるセパレート形ヒートポンプにおいて、上記凝
縮器の入側の冷媒流路の部分にて分岐し、上記第2膨張
弁の出側の流路の部分にて合流するホットガス流路を設
けるとともに、このホットガス流路に、ここを流れる冷
媒の量が少なくなった場合には、開度が大きくなる流量
調節弁を設けて形成してある。As is apparent from the above description, according to the present invention, the first refrigerant circulation channel including at least the compressor, the condenser, the first expansion valve, and the evaporator, and the refrigerant circulation channel. In the flow path between the condenser and the first expansion valve, and merges in the flow path between the evaporator and the compressor, and at least the compressor and the condenser. In a separate type heat pump capable of forming a heat exchanger, a second expansion valve, and a second refrigerant flow path including an air heat exchanger, a branch is made at a part of the refrigerant flow path on the inlet side of the condenser, and In addition to providing a hot gas flow path that merges at the outlet side flow path part, a flow control valve that increases the degree of opening is provided in this hot gas flow path when the amount of refrigerant flowing here decreases. It is formed.
【0012】このため、第2膨張弁を通る冷媒の量が減
少しても、ホットガス流路からのホットガスにより、空
気熱交換器への配管内での冷媒液と冷媒ガスとの2相流
に必要な最低流速は常時維持され、圧縮機への液バッ
ク、およびこれに伴う圧縮機の破損事故を起こすことな
く、冷水負荷対応および温水の安定供給が可能になると
いう効果を奏する。For this reason, even if the amount of the refrigerant passing through the second expansion valve is reduced, the hot gas from the hot gas flow path causes the two-phase of the refrigerant liquid and the refrigerant gas in the pipe to the air heat exchanger. The minimum flow rate required for the flow is always maintained, and there is an effect that it is possible to cope with the cold water load and to supply the hot water stably without causing the liquid back to the compressor and the accident of breakage of the compressor accompanying the liquid back.
【図1】 本発明に係るセパレート形ヒートポンプの全
体構成を示す図である。FIG. 1 is a diagram showing an entire configuration of a separate heat pump according to the present invention.
【図2】 従来のセパレート形ヒートポンプの全体構成
を示す図である。FIG. 2 is a diagram showing the entire configuration of a conventional separate heat pump.
1 ホットガス流路 2 流量調節弁 11 圧縮機 14 凝縮器 15 第1膨張弁 16 蒸発器 18 第2膨張弁 19 空気熱交換器 DESCRIPTION OF SYMBOLS 1 Hot gas flow path 2 Flow control valve 11 Compressor 14 Condenser 15 First expansion valve 16 Evaporator 18 Second expansion valve 19 Air heat exchanger
Claims (1)
弁,蒸発器を含む第1冷媒循環流路と、この冷媒循環流
路の内の上記凝縮器と上記第1膨張弁との間の流路の部
分から分岐するとともに、上記蒸発器と上記圧縮機の間
の流路の部分にて合流し、少なくとも上記圧縮機,上記
凝縮器,第2膨張弁,空気熱交換器を含む第2冷媒流路
とを形成できるセパレート形ヒートポンプにおいて、上
記凝縮器の入側の冷媒流路の部分にて分岐し、上記第2
膨張弁の出側の流路の部分にて合流するホットガス流路
を設けるとともに、このホットガス流路に、ここを流れ
る冷媒の量が少なくなった場合には、開度が大きくなる
流量調節弁を設けて形成したことを特徴とするセパレー
ト形ヒートポンプ。1. A first refrigerant circulation channel including at least a compressor, a condenser, a first expansion valve, and an evaporator, and a portion of the refrigerant circulation channel between the condenser and the first expansion valve. A second branch including at least the compressor, the condenser, the second expansion valve, and the air heat exchanger is formed while branching off from the flow path and joining at the flow path between the evaporator and the compressor. In a separate type heat pump capable of forming a refrigerant flow path, a branch is made at a part of the refrigerant flow path on the inlet side of the condenser, and
In addition to providing a hot gas flow path that merges at the flow path portion on the outlet side of the expansion valve, the flow rate adjustment increases the degree of opening when the amount of refrigerant flowing through the hot gas flow path decreases. A separate heat pump characterized by being provided with a valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6215764A JP2916381B2 (en) | 1994-09-09 | 1994-09-09 | Separate heat pump |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6215764A JP2916381B2 (en) | 1994-09-09 | 1994-09-09 | Separate heat pump |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0875282A JPH0875282A (en) | 1996-03-19 |
JP2916381B2 true JP2916381B2 (en) | 1999-07-05 |
Family
ID=16677846
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6215764A Expired - Fee Related JP2916381B2 (en) | 1994-09-09 | 1994-09-09 | Separate heat pump |
Country Status (1)
Country | Link |
---|---|
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CN111141541B (en) * | 2020-01-20 | 2021-09-24 | 上海交通大学 | Movable oil-containing refrigerant testing device and method |
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JPS63123962A (en) * | 1986-11-11 | 1988-05-27 | 三菱電機株式会社 | Heat pump device |
JPH0534027A (en) * | 1991-07-25 | 1993-02-09 | Nippondenso Co Ltd | Freezer |
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