JPH0579896B2 - - Google Patents

Info

Publication number
JPH0579896B2
JPH0579896B2 JP59219764A JP21976484A JPH0579896B2 JP H0579896 B2 JPH0579896 B2 JP H0579896B2 JP 59219764 A JP59219764 A JP 59219764A JP 21976484 A JP21976484 A JP 21976484A JP H0579896 B2 JPH0579896 B2 JP H0579896B2
Authority
JP
Japan
Prior art keywords
rectifier
refrigerant
compressor
gas
low
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 - Lifetime
Application number
JP59219764A
Other languages
Japanese (ja)
Other versions
JPS6199062A (en
Inventor
Shigeo Suzuki
Juji Yoshida
Kazuo Nakatani
Juji Mukai
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP59219764A priority Critical patent/JPS6199062A/en
Publication of JPS6199062A publication Critical patent/JPS6199062A/en
Publication of JPH0579896B2 publication Critical patent/JPH0579896B2/ja
Granted legal-status Critical Current

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  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
  • Central Heating Systems (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は熱ポンプ装置に関するものである。[Detailed description of the invention] Industrial applications The present invention relates to a heat pump device.

従来例の構成とその問題点 従来、熱ポンプ装置の増熱手段として、ガスイ
ンジエクシヨン方式と呼ばれるものがあつた。こ
の方式は、凝縮器と蒸発器の中間圧力に設置され
た気液分離器において分離される冷媒のガス成分
を圧縮機シリンダ内に注入することにより、冷媒
循環量を増大させて増熱を図つたものである。し
かし、かかる従来の装置においては、注入される
ガス量分だけの増熱効果しかなく、中間圧力で発
生するガス量にも制約があるため能力調節範囲は
小さなものであつた。
Configuration of Conventional Example and Its Problems Conventionally, there has been a method called a gas injection system as a heat increasing means for a heat pump device. This method increases the amount of refrigerant circulated and increases heat by injecting the gas component of the refrigerant, which is separated in a gas-liquid separator installed at an intermediate pressure between the condenser and evaporator, into the compressor cylinder. It is ivy. However, in such a conventional device, the heating effect is only increased by the amount of gas injected, and the amount of gas generated at intermediate pressure is also limited, so the range of capacity adjustment is small.

発明の目的 本発明は熱ポンプ装置の能力調節範囲を拡大す
るとともに、その能力調節を確実にすることを目
的とするものであり、従来のガスインジエクシヨ
ン方式に加えて、圧縮機低圧吸入側での冷媒循環
量を大きく可変させるものである。
Purpose of the Invention The purpose of the present invention is to expand the capacity adjustment range of a heat pump device and to ensure the capacity adjustment. This allows the amount of refrigerant circulated in the system to be greatly varied.

発明の構成 本発明になる熱ポンプ装置は、冷媒回路に非共
沸混合冷媒を封入すると共に、中間圧で精留器下
部に分岐導入される一部冷媒を、加熱、冷却手段
を用いて精留貯留させ、精留器頂部のガス成分を
圧縮機シリンダ内に注入する如く構成してなるも
のである。
Structure of the Invention The heat pump device of the present invention seals a non-azeotropic mixed refrigerant in a refrigerant circuit, and refines a portion of the refrigerant branched into the lower part of the rectifier at intermediate pressure using a heating and cooling means. The gas component at the top of the rectifier is injected into the compressor cylinder.

実施例の説明 以下、本発明の熱ポンプ装置の一実施例を図を
もつて説明する。図において1は圧縮機、2は凝
縮器、3,4はそれぞれ第1及び第2の絞り装
置、5は蒸発器であり、これらの要素は一連に接
続配管されている。6は精留器であり第1及び第
2の絞り装置3,4は中間圧力において配管7を
介して、精留器6下部に一部冷媒が分岐導入され
る如く構成されている。精留器6の内部には充填
材8が充填され、下部には凝縮器2から第1絞り
装置3に至る高温配管9が、上部には第2絞り装
置4から蒸発器5に至る低温配管10がそれぞれ
熱交換器として配置されている。さらに精留器6
の頂部からは、ガス成分を圧縮機1のシリンダ内
に注入する第1流量制御弁11を介したインジエ
クシヨン配管12が接続され、精留器6の塔底貯
留器13下部からは第2流量制御弁14を介した
配管15を蒸発器5側へ接続している。
DESCRIPTION OF EMBODIMENTS Hereinafter, one embodiment of the heat pump device of the present invention will be described with reference to the drawings. In the figure, 1 is a compressor, 2 is a condenser, 3 and 4 are first and second throttle devices, respectively, and 5 is an evaporator, and these elements are connected in series with piping. Reference numeral 6 denotes a rectifier, and the first and second throttle devices 3 and 4 are constructed so that a portion of the refrigerant is branched into the lower part of the rectifier 6 through a pipe 7 at an intermediate pressure. The inside of the rectifier 6 is filled with a filler 8, and the lower part has a high-temperature pipe 9 leading from the condenser 2 to the first throttle device 3, and the upper part has a low-temperature pipe leading from the second throttle device 4 to the evaporator 5. 10 are each arranged as a heat exchanger. Furthermore, rectifier 6
An injection piping 12 is connected to the top of the column via a first flow control valve 11 for injecting gas components into the cylinder of the compressor 1, and a second flow control valve is connected from the bottom of the bottom reservoir 13 of the rectifier 6. A pipe 15 is connected to the evaporator 5 via a valve 14.

このような熱ポンプ装置において、特に増熱時
を中心に能力調節の作用を説明する。通常運転時
は第1及び第2の流量制御弁11,14を閉止し
ておくと精留器6は単なる液溜めとして機能し、
配管7を通じて流入する冷媒は一定量液として貯
溜されている。ここで増熱を必要とする場合には
第1の流量制御弁11を開放することにより、精
留器6頂部に溜つたガス成分は配管12を通じて
徐々に圧縮機1のシリンダ内に注入され、これに
つれて配管7を通じて気液共存状態の冷媒が新た
に分岐導入される。この精留器6に導入される冷
媒は非共沸混合冷媒であるため、低沸点成分を多
く含むガス成分は上方に、また高沸点成分を多く
含む液成分は下部の塔底貯溜器13に溜まるが、
塔底貯溜器13では高温配管9により加熱される
ために、液成分中の低沸点成分が沸騰上昇し、上
部では低温配管10によりガス成分中の高沸点成
分が凝縮滴下する。すなわち精留器6内では沸騰
上昇する低沸点成分と凝縮滴下する高沸点成分と
が向流的に気液接触して精留器6の塔底貯溜器1
3には高沸点成分が徐々に精留貯溜される。従つ
て蒸発器5を経て圧縮機1の低圧吸入側に循環す
る冷媒は低沸点成分が多くなり、低沸点成分はガ
ス比容積が小さいため圧縮機1による冷媒循環量
が増加し、更にインジエクシヨン配管12を通じ
て注入される冷媒が付加されて、凝縮器2では従
来以上に能力が増大する。この時、本実施例では
第1及び第2の絞り装置3,4の中間から精留器
6への配管7を精留器6の下部に設けているため
に精留器6内でのいわゆる濃縮部が長くなり、低
沸点成分の濃縮が効率良く行なわれ、精留器6上
部の冷媒濃度が非常に効率良く迅速に低沸点成分
になり、それ故、増熱作用も短時間で出来るもの
である。
In such a heat pump device, the effect of capacity adjustment will be explained, particularly when heating is increased. During normal operation, if the first and second flow control valves 11 and 14 are closed, the rectifier 6 functions as a mere liquid reservoir.
A fixed amount of the refrigerant flowing through the pipe 7 is stored as a liquid. If heating is required here, by opening the first flow control valve 11, the gas component accumulated at the top of the rectifier 6 is gradually injected into the cylinder of the compressor 1 through the pipe 12. At the same time, a new refrigerant in a gas-liquid coexistence state is branched into the pipe 7. Since the refrigerant introduced into the rectifier 6 is a non-azeotropic mixed refrigerant, the gas component containing many low boiling point components flows upward, and the liquid component containing many high boiling point components flows into the bottom reservoir 13 at the bottom. It accumulates, but
In the tower bottom reservoir 13, since it is heated by the high-temperature pipe 9, the low-boiling point component in the liquid component boils up, and in the upper part, the high-boiling point component in the gas component is condensed and dripped by the low-temperature pipe 10. That is, in the rectifier 6, the low boiling point component that boils up and the high boiling point component that condenses and drops come into contact with gas and liquid in a countercurrent manner to the bottom reservoir 1 of the rectifier 6.
3, high boiling point components are gradually rectified and stored. Therefore, the refrigerant that circulates through the evaporator 5 to the low-pressure suction side of the compressor 1 has a large amount of low-boiling point components, and since the low-boiling point components have a small gas specific volume, the amount of refrigerant circulated by the compressor 1 increases. By adding the refrigerant injected through 12, the capacity of the condenser 2 is increased more than before. At this time, in this embodiment, since the piping 7 from between the first and second throttle devices 3 and 4 to the rectifier 6 is provided at the lower part of the rectifier 6, so-called The condensing section is longer, and the concentration of low-boiling components is performed efficiently, and the refrigerant concentration at the top of the rectifier 6 is very efficiently and quickly reduced to low-boiling components.Therefore, the heat-increasing effect can be achieved in a short time. It is.

また逆に減熱を必要とする場合には、第1の流
量制御弁11を閉止し、第2の流量制御弁14を
開放する事により、本熱ポンプ装置の運転中に、
精留器6内に設けられた高温配管9と低温配管1
0との加熱、冷却によつて精留器6内でなされた
全環流型の精留作用によつて塔底貯溜器13に貯
えられた純度の高い高沸点成分を蒸発器5に注入
する。これによつて循環量が減少し能力を減少さ
せることができるものである。
On the other hand, when heat reduction is required, the first flow control valve 11 is closed and the second flow control valve 14 is opened.
High temperature piping 9 and low temperature piping 1 provided in the rectifier 6
The high boiling point components with high purity stored in the tower bottom reservoir 13 are injected into the evaporator 5 by the total reflux type rectification effect performed in the rectifier 6 by heating and cooling with 0.0. This reduces the amount of circulation and reduces capacity.

発明の効果 以上説明した如く、本発明の熱ポンプ装置は、
非共沸混合冷媒を封入し、中間圧で精留器内に分
岐導入される一部冷媒を精溜貯留せしめる如く構
成し、特に中間圧から精留器の下部に分岐導入す
る構成とし、従来以上の増減熱と能力調節範囲が
拡大されるとともに、特に増熱時の精留作用が効
果的迅速に行なわれるものである。
Effects of the Invention As explained above, the heat pump device of the present invention has the following features:
A non-azeotropic mixed refrigerant is enclosed, and a part of the refrigerant branched into the rectifier at intermediate pressure is rectified and stored.In particular, the structure is such that the refrigerant is branched into the lower part of the rectifier from the intermediate pressure. The above-mentioned heat increase/decrease and capacity adjustment ranges are expanded, and the rectification action, especially when increasing heat, is effectively and quickly carried out.

【図面の簡単な説明】[Brief explanation of the drawing]

図は本発明の一実施例の熱ポンプ装置の構成図
である。 1……圧縮機、2……凝縮器、5……蒸発器、
6……精留器、9……高温配管、10……低温配
管、12……インジエクシヨン配管。
The figure is a configuration diagram of a heat pump device according to an embodiment of the present invention. 1... Compressor, 2... Condenser, 5... Evaporator,
6... Rectifier, 9... High temperature piping, 10... Low temperature piping, 12... Injection piping.

Claims (1)

【特許請求の範囲】[Claims] 1 圧縮機、凝縮器、第1及び第2の絞り装置、
蒸発器等を一連に接続配管し、非共沸混合冷媒を
封入した冷媒回路と、下部が加熱され、上部が冷
却される精留器とを有し、前記冷媒回路の第1及
び第2絞り装置の中間と、前記精留器の下部とを
連通すると共に、前記精留器の頂部と前記圧縮機
のシリンダ内とを連通した熱ポンプ装置。
1 Compressor, condenser, first and second throttling devices,
It has a refrigerant circuit in which an evaporator and the like are connected in series and a non-azeotropic mixed refrigerant is sealed, and a rectifier whose lower part is heated and whose upper part is cooled, and the first and second apertures of the refrigerant circuit A heat pump device in which an intermediate portion of the device is communicated with a lower portion of the rectifier, and a top portion of the rectifier is communicated with the inside of the cylinder of the compressor.
JP59219764A 1984-10-18 1984-10-18 heat pump equipment Granted JPS6199062A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59219764A JPS6199062A (en) 1984-10-18 1984-10-18 heat pump equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59219764A JPS6199062A (en) 1984-10-18 1984-10-18 heat pump equipment

Publications (2)

Publication Number Publication Date
JPS6199062A JPS6199062A (en) 1986-05-17
JPH0579896B2 true JPH0579896B2 (en) 1993-11-05

Family

ID=16740633

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59219764A Granted JPS6199062A (en) 1984-10-18 1984-10-18 heat pump equipment

Country Status (1)

Country Link
JP (1) JPS6199062A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6438568A (en) * 1987-07-31 1989-02-08 Matsushita Electric Industrial Co Ltd Heat pump device
TW262529B (en) * 1993-03-29 1995-11-11 Toshiba Co Ltd Refrigerating apparatus
CN114087811A (en) * 2021-12-24 2022-02-25 珠海格力电器股份有限公司 Gas-liquid separation device and self-cascade refrigeration system comprising same

Also Published As

Publication number Publication date
JPS6199062A (en) 1986-05-17

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