JPH01196458A - Separation type freezer - Google Patents

Separation type freezer

Info

Publication number
JPH01196458A
JPH01196458A JP2243188A JP2243188A JPH01196458A JP H01196458 A JPH01196458 A JP H01196458A JP 2243188 A JP2243188 A JP 2243188A JP 2243188 A JP2243188 A JP 2243188A JP H01196458 A JPH01196458 A JP H01196458A
Authority
JP
Japan
Prior art keywords
refrigerant
pipe
pressure
unit
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.)
Granted
Application number
JP2243188A
Other languages
Japanese (ja)
Other versions
JP2594087B2 (en
Inventor
Kiyoshi Tamura
清 田村
Masazumi Makino
正純 牧野
Kazuaki Sakaino
境野 一秋
Junichi Saito
順一 斉藤
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP63022431A priority Critical patent/JP2594087B2/en
Publication of JPH01196458A publication Critical patent/JPH01196458A/en
Application granted granted Critical
Publication of JP2594087B2 publication Critical patent/JP2594087B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To prevent the freezing ability of the freezer from lowering by providing a bypass pipe which leads a part of a coolant from a high-pressure liquid pipe to the suction side of a compressor when the temperature or pressure of a high-pressure coolant exceeds a predetermined value and making the diameter of each of unit pipelines connected to the high-pressure liquid pipe smaller than that of a coolant pipe. CONSTITUTION:During a space cooling (cooling) operation, since no liquid receiving apparatus is provided in a high-pressure liquid pipe 15, the over-cooling degree is suppressed. A high- pressure liquid coolant which has left a power source side heat exchange 2 flows along a unit pipeline 9. During this operation the high-pressure liquid coolant becomes like a flash gas and reaches a pressure reducing apparatus 7, and the diameter of the unit pipeline 9 is reduced and hence the quantity of the coolant occupying the unit pipeline 9 is reduced. Even if the unit pipelines 9 and 10 are long, the quantity of circulating coolant does not become a sort of shortage, and hence there is no need to fill the coolant at the time of supplying the coolant in the spot pipelines. Further, when due to a sort of the shortage of the coolant, the temperature of the discharged coolant in the compressor 1 rises up and becomes a set value of 100 deg.C or higher, a switching valve 13 and an auxiliary valve 18 are opened by a signal from a detector 12, and a part of a high-pressure liquid coolant is introduced into a low-pressure vessel 3, and hence the rise of the temperature of the discharged coolant is suppressed.

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は熱源側ユニットと利用側ユニットとを一対のユ
ニット間配管で接続した分離型冷房機や分離型冷暖房機
や分離型冷却機(食品冷却用)等の分離型冷凍装置に関
する。
DETAILED DESCRIPTION OF THE INVENTION (a) Industrial Application Field The present invention relates to a separate air conditioner, a separate air conditioner/heater, and a separate cooler ( related to separate type refrigeration equipment (for food cooling), etc.

(ロ)従来の技術 分離型冷凍装置において、熱源側ユニットと利用側ユニ
ットとを接続する一対のユニット間配管の長さは両ユニ
ットの設置場所によって例えば7mから50mと大きく
異なるため、冷凍装置の冷媒回路中に充填する冷媒量を
中間長さの30mに合わせて選定しても短配管時(7m
)及び長配管時(50m)に生じる約20mの配管長の
差が大き過ぎるため、短配管時には冷媒充填量が多過ぎ
、長配管時には冷媒充填量が少な過ぎてしまい、冷凍能
力が大きく低下してしまう欠点を有していた。
(b) Conventional technology In separate refrigeration systems, the length of the inter-unit piping that connects the heat source side unit and the user side unit varies greatly, for example from 7 m to 50 m, depending on the installation location of both units. Even if the amount of refrigerant to be filled into the refrigerant circuit is selected according to the intermediate length of 30 m, it will not work when the pipe is short (7 m).
) and the difference in pipe length (approximately 20 m) that occurs when using long pipes (50 m) is too large, so the amount of refrigerant charged is too large when using short pipes, and too little when using long pipes, resulting in a significant decrease in refrigeration capacity. It had the disadvantage of being

このため、高圧液管に余剰冷媒を貯溜する受液器を設け
たり、冷媒不足時には現地配管時に冷媒を補充するよう
にしていた。(例えば実公昭55−21016号公報参
照) (ハ)発明が解決しようとする課題 上述のように受液器を設ける場合、多量の余剰冷媒を貯
溜する大容量の受液器を必要とするため製造コストが高
くつくと共に熱源側ユニットが大型となる不具合さかあ
った。又、冷媒を現地配管時に補充する充填作業はうっ
かり忘れられてしまう虞れがあり、且つ適切な冷媒量を
充填するのは面倒な作業であり敬遠されていた。
For this reason, high-pressure liquid pipes are provided with liquid receivers to store excess refrigerant, and when refrigerant is insufficient, refrigerant is replenished during on-site piping. (For example, see Utility Model Publication No. 55-21016.) (c) Problems to be Solved by the Invention When a liquid receiver is provided as described above, a large capacity liquid receiver is required to store a large amount of surplus refrigerant. There were problems in that the manufacturing cost was high and the heat source side unit was large. In addition, there is a risk that the refilling work of replenishing refrigerant at the time of on-site piping may be accidentally forgotten, and filling the refrigerant with an appropriate amount is a troublesome work and has been avoided.

本発明はかかる課題を解決した分離型冷凍装置を提供す
ることを目的としたものである。
An object of the present invention is to provide a separate type refrigeration system that solves the above problems.

(ニ)課題を解決するための手段 上記目的を達成するために、本発明は圧縮機と熱源側熱
交換器と前記圧縮機に吸い込まれる冷媒を気液分離する
低圧容器とを冷媒管で接続した熱源側ユニットと、利用
側熱交換器とこの利用側熱交換器に流入する冷媒を減圧
する減圧器とを有する利用側ユニットとを一対のユニッ
ト間配管で接続した分離型冷凍装置、又は圧縮機と四方
弁と熱源側熱交換器と暖房用減圧器と前記圧縮機に吸い
込まれる冷媒を気液分離する低圧容器とを冷媒管で接続
した熱源側ユニットと、利用側熱交換器と冷房用減圧器
とを有する利用側ユニットとを一対のユニット間配管で
接続したヒートポンプ式の分離型冷凍装置において、熱
源側ユニット内に高圧冷媒の温度または圧力が設定値以
上になると高圧液管からの冷媒の一部を圧縮機の吸込側
へ導くバイパス管を設けると共に、前記高圧液管と接続
されるユニット間配管の管径を前記冷媒管の管径よりも
小さくするようにしたものである。
(d) Means for Solving the Problems In order to achieve the above objects, the present invention connects a compressor, a heat source side heat exchanger, and a low-pressure container that separates the refrigerant sucked into the compressor into gas and liquid through a refrigerant pipe. A separate type refrigeration system, or a compressor, in which a heat source side unit with a heat exchanger and a user side unit having a user side heat exchanger and a pressure reducer that reduces the pressure of the refrigerant flowing into the user side heat exchanger are connected by a pair of inter-unit piping. A heat source side unit that connects a four-way valve, a heat source side heat exchanger, a pressure reducer for heating, and a low pressure container that separates the refrigerant sucked into the compressor into gas and liquid by a refrigerant pipe, a user side heat exchanger, and a cooling side unit. In a heat pump-type separate refrigeration system in which a user unit with a pressure reducer is connected to a user unit by a pair of inter-unit piping, if the temperature or pressure of high-pressure refrigerant in the heat source unit exceeds a set value, the refrigerant is discharged from the high-pressure liquid pipe. A bypass pipe is provided to guide a part of the refrigerant to the suction side of the compressor, and the pipe diameter of the inter-unit pipe connected to the high-pressure liquid pipe is made smaller than the pipe diameter of the refrigerant pipe.

又、圧縮機と利用側熱交換器とこの利用側熱交換器に流
入する冷媒を減圧する減圧器と前記圧縮機に吸い込まれ
る冷媒を気液分離する低圧容器とを冷媒管で接続した利
用側ユニットと、熱源側熱交換器を有する熱源側ユニッ
トとを一対のユニット間配管で接続した分離型冷凍装置
、又は圧縮機と四方弁と利用側熱交換器と冷房用減圧器
と前記圧縮機に吸い込まれる冷媒を気液分離する低圧容
器とを冷媒管で接続した利用側ユニットと、熱源側熱交
換器と暖房用減圧器とを有する熱源側ユニットとを一対
のユニット間配管で接続したヒートポンプ式の分離型冷
凍装置において、利用側ユニット内に高圧冷媒の温度ま
たは圧力が設定値以上になると高圧液管からの冷媒の一
部を圧縮機の吸込側へ導くバイパス管を設けると共に、
前記高圧液管と接続されるユニット間配管の管径を前記
冷媒管の管径よりも小さくするようにしたものである。
Further, there is a user side in which a compressor, a user side heat exchanger, a pressure reducer that reduces the pressure of the refrigerant flowing into the user side heat exchanger, and a low pressure container that separates the refrigerant sucked into the compressor into gas and liquid are connected by a refrigerant pipe. A separate refrigeration system in which a unit and a heat source side unit having a heat source side heat exchanger are connected by a pair of inter-unit piping, or a compressor, a four-way valve, a user side heat exchanger, a cooling pressure reducer, and the compressor. A heat pump type in which the user side unit is connected to a low-pressure container that separates the refrigerant sucked into gas and liquid through a refrigerant pipe, and the heat source side unit has a heat exchanger on the heat source side and a pressure reducer for heating, and is connected through a pair of inter-unit piping. In the separate type refrigeration system, a bypass pipe is provided in the user-side unit to guide a part of the refrigerant from the high-pressure liquid pipe to the suction side of the compressor when the temperature or pressure of the high-pressure refrigerant exceeds a set value, and
The pipe diameter of the inter-unit pipe connected to the high-pressure liquid pipe is made smaller than the pipe diameter of the refrigerant pipe.

前記バイパス管は圧縮機の吐出冷媒温度が設定値以上に
なると開く開閉弁を介在した管とし、又、このバイパス
管の冷媒出口端は低圧容器の冷媒入口管に接続した方が
好ましい。
The bypass pipe preferably has an on-off valve that opens when the temperature of the refrigerant discharged from the compressor exceeds a set value, and the refrigerant outlet end of the bypass pipe is preferably connected to the refrigerant inlet pipe of the low-pressure container.

更に、高圧液管の管径がこの液管と接続されるユニット
間配管の管径と同一とし、又、高圧液管に補助減圧器を
介在すると共にこの補助減圧器と並列に補助開閉弁を設
け、この補助開閉弁を好ましくは圧縮機の吐出冷媒温度
が設定値以上になると開くようにした方が良い。
Furthermore, the diameter of the high-pressure liquid pipe is the same as that of the inter-unit piping connected to this liquid pipe, and an auxiliary pressure reducer is interposed in the high-pressure liquid pipe, and an auxiliary on-off valve is installed in parallel with this auxiliary pressure reducer. Preferably, the auxiliary on-off valve is opened when the temperature of the refrigerant discharged from the compressor exceeds a set value.

(ネ)作用 上記のように構成された分離型冷凍装置ではユニット間
配管の長さが7mの時に低圧容器に約173冷媒が溜ま
り込むように冷媒充填量を設定しておき受液器は小容量
のものを用いるか、もしくは不要としている。従って冷
房時もしくは暖房時において、高圧液冷媒はユニット間
配管を流れていく際にフラッシュガス気味となって減圧
器に達すると共に、ユニット間配管の管径を小さくして
いるのでこのユニット間配管内に占められる高圧液冷媒
の量が少なくなり、ユニット間配管の長さが例えば50
mであってもそれほど循環冷媒量が不足気味にならず、
冷媒を現地配管時に充填する必要はない、しかし、この
冷媒不足気味により圧縮機の吐出冷媒温度が異常上昇す
ることは避けられず、この吐出冷媒温度が設定値100
°C以上になるとバイパス管の開閉弁が開いて高圧液冷
媒の一部が圧縮機に吸い込まれ、吐出冷媒温度の上昇が
抑えられる。
(f) Effect In the separate type refrigeration system configured as described above, the refrigerant filling amount is set so that approximately 173 refrigerant accumulates in the low-pressure container when the length of the pipe between units is 7 m, and the liquid receiver is small. Either use one with a large capacity or eliminate it. Therefore, during cooling or heating, the high-pressure liquid refrigerant becomes a bit of flash gas as it flows through the inter-unit piping and reaches the pressure reducer. The amount of high-pressure liquid refrigerant occupied by the
Even if it is m, the amount of circulating refrigerant does not seem to be insufficient,
There is no need to fill the refrigerant at the time of on-site piping, but it is inevitable that the refrigerant temperature discharged from the compressor will rise abnormally due to this refrigerant shortage, and this discharge refrigerant temperature will exceed the set value of 100.
When the temperature exceeds °C, the on-off valve of the bypass pipe opens and a portion of the high-pressure liquid refrigerant is sucked into the compressor, suppressing a rise in the temperature of the discharged refrigerant.

(へ)実施例 第1図は本発明の第1実施例を示す分離型冷凍装置の冷
媒回路図で、圧縮機(1)と熱源側熱交換器(2)と圧
縮機(1)に吸い込まれる冷媒を気液分離する低圧容器
(3)とを冷媒管(4)で接続した熱源側ユニット(5
)と、利用側熱交換器(6)とこの利用側熱交換器に流
入する冷媒を減圧する毛細管等の減圧器(7)とを有す
る利用側ユニット(8)とが一対のユニット間配管(9
)(1o)で接続されて冷房(冷却)サイクルが形成さ
れるようになっている。
(F) Embodiment Figure 1 is a refrigerant circuit diagram of a separate refrigeration system showing the first embodiment of the present invention. A heat source side unit (5) is connected to a low pressure container (3) for separating the refrigerant into gas and liquid through a refrigerant pipe (4).
) and a user-side unit (8) having a user-side heat exchanger (6) and a pressure reducer (7) such as a capillary tube that reduces the pressure of the refrigerant flowing into the user-side heat exchanger, and a pair of inter-unit piping ( 9
) (1o) to form a cooling cycle.

(11)は熱源側ユニット(5)内に設けられたバイパ
ス管で、吐出冷媒の温度が設定値100″C以上になる
と検出器(12)からの信号で開く開閉弁(13)と毛
細管(14)とが介在されており、このバイパス管り1
1)の冷媒出口端は高圧液管(15)からの冷媒の一部
が圧縮機(1)に直接、吸い込まれないように低圧容器
(3)の冷媒入口管(16)に接続されている。
(11) is a bypass pipe installed in the heat source side unit (5), which includes an on-off valve (13) and a capillary tube ( 14) is interposed, and this bypass pipe 1
The refrigerant outlet end of 1) is connected to the refrigerant inlet pipe (16) of the low pressure container (3) so that a part of the refrigerant from the high pressure liquid pipe (15) is not directly sucked into the compressor (1). .

(17)は高圧液管(15)に介在された毛細管等の補
助減圧器、(18)はこの補助減圧器と並列に接続され
、吐出冷媒の温度が設定値100″C以上になると検出
器り12)からの信号で開く補助開閉弁である。
(17) is an auxiliary pressure reducer such as a capillary tube interposed in the high-pressure liquid pipe (15), and (18) is connected in parallel with this auxiliary pressure reducer. This is an auxiliary on-off valve that opens with a signal from 12).

しかも、高圧液管(15〉と接続されるユニット間配管
<9)の管径を冷媒管り4)の管径(例えば9.52〜
15.88ffll)よりも小さく(例えば6.35m
m)設定しである。
Moreover, the pipe diameter of the inter-unit pipe <9) connected to the high-pressure liquid pipe (15>) should be changed to the pipe diameter of the refrigerant pipe 4) (for example, 9.52~
15.88ffll) smaller (e.g. 6.35m
m) is set.

以上の如く構成された分離型冷凍装置ではユニット間配
管(9)(10)の長さが7m程度の短配管時に低圧容
器(3)に約173冷媒が溜まり込むように冷媒充填量
が設定されているため、短配管時に圧縮機(1)の吐出
冷媒温度が100℃以上に上昇することがないので開閉
弁(13)及び補助開閉弁(18)は閉じたままであり
、圧縮機り1)−熱源側熱交換器(2)−補助減圧器(
17)−ユニット間配管(9)−派圧器(7)−利用側
熱交換器(6)−ユニット間配管(10)−低圧容器(
3)−圧縮機(1)と順次冷媒が循環して、熱源側熱交
換器(2)が凝縮器として、利用側熱交換器(6)が蒸
発器として夫々作用する冷房(冷却)運転が行なわれる
In the separation type refrigeration system configured as described above, the refrigerant charging amount is set so that about 173 refrigerant accumulates in the low pressure container (3) when the inter-unit piping (9) (10) is short, about 7 m long. Therefore, when the piping is short, the temperature of the refrigerant discharged from the compressor (1) does not rise above 100°C, so the on-off valve (13) and the auxiliary on-off valve (18) remain closed, and the compressor (1) - Heat source side heat exchanger (2) - Auxiliary pressure reducer (
17) - Inter-unit piping (9) - Pressure divider (7) - Utilization side heat exchanger (6) - Inter-unit piping (10) - Low pressure vessel (
3) - Cooling operation in which the refrigerant circulates sequentially through the compressor (1), the heat source side heat exchanger (2) acts as a condenser, and the user side heat exchanger (6) acts as an evaporator. It is done.

かかる冷房(冷却)運転時、高圧液管(15)に受液器
を設けていないため過冷却度が抑えられており、熱源側
熱交換器(2)を出た高圧液冷媒はユニット間配管(9
)を流れていく際にフラッシュガス気味となって減圧器
(7)に達すると共に、このユニット間配管(9)の管
径は小さくなっているのでこのユニット間配管(9)内
に占められる冷媒の量が少なくなり、ユニット間配管(
9)(10)が長さ50m程度の長配管であってもそれ
ほど循環冷媒量が不足気味にならず、冷媒を現地配管時
に充填する必要はない。しかし、この冷媒不足気味によ
り圧縮機り1)の吐出冷媒温度が異常上昇することはさ
けられず、この吐出冷媒温度が設定値1o。
During such cooling operation, the degree of supercooling is suppressed because the high-pressure liquid pipe (15) is not provided with a liquid receiver, and the high-pressure liquid refrigerant that exits the heat source side heat exchanger (2) is transferred to the inter-unit pipe. (9
), it becomes a bit of flash gas and reaches the pressure reducer (7), and since the pipe diameter of this inter-unit piping (9) has become smaller, the refrigerant occupied in this inter-unit piping (9) The amount of piping between units (
9) Even if (10) is a long pipe with a length of about 50 m, the amount of circulating refrigerant will not be so insufficient, and there is no need to fill the refrigerant at the time of on-site piping. However, due to this refrigerant shortage, it is unavoidable that the temperature of the discharged refrigerant from the compressor 1) rises abnormally, and this discharged refrigerant temperature reaches the set value 1o.

℃以上になると検出器(12)からの信号で開閉弁(1
3)及び補助開閉弁(18)が開いて高圧液冷媒の一部
が低圧容器(3)に導かれるため吐出冷媒温度の上昇が
抑えられると共に補助減圧器(17)の抵抗値が減った
分だけ短配管時の配管抵抗値に近づき、長配管時と短配
管時におけるユニット間配管の抵抗差が少なくなる。
When the temperature exceeds ℃, a signal from the detector (12) turns on the on-off valve (1).
3) and the auxiliary on-off valve (18) opens and a portion of the high-pressure liquid refrigerant is guided to the low-pressure container (3), suppressing the rise in discharge refrigerant temperature and reducing the resistance value of the auxiliary pressure reducer (17). The difference in piping resistance between units between long piping and short piping becomes smaller.

尚、ユニット間配管(9)が長配管であれば、管径の小
さいこのユニット間配管(9)が冷媒減圧器として作用
することになるが、短配管時にはユニット間配管(9)
が冷媒減圧器としてあまり作用しないため、減圧器(7
)は必要である。
Furthermore, if the inter-unit piping (9) is a long piping, this inter-unit piping (9) with a small pipe diameter will act as a refrigerant pressure reducer, but when the piping is short, the inter-unit piping (9)
The pressure reducer (7) does not function very well as a refrigerant pressure reducer.
) is necessary.

又、熱源側ユニット(5)内の高圧液管(15)と利用
側ユニット(8)内の高圧液管(19〉とをユニット間
配管(9)の管径(例えば6.3511111)と同じ
管径にして高圧液冷媒の占める量を更に少なくすればユ
ニット間配管<9)(10)が長さ50m程度の長配管
であっても循環冷媒量の不足気味が更に緩和される。
Also, the high pressure liquid pipe (15) in the heat source side unit (5) and the high pressure liquid pipe (19> in the usage side unit (8)) are set to have the same pipe diameter (for example, 6.3511111) as the inter-unit pipe (9). If the amount occupied by the high-pressure liquid refrigerant in terms of pipe diameter is further reduced, even if the inter-unit piping <9) (10) is a long pipe with a length of about 50 m, the shortage of circulating refrigerant can be further alleviated.

又、開閉弁(13)及び補助開閉弁(18)は圧縮機(
1)の吐出冷媒圧力もしくは高圧液管(15)の冷媒圧
力を検出して開閉するようにしても良いが、ユニット間
配管(9)(10)が長配管であるために循環冷媒量が
不足気味となった場合、圧縮機(1)の吐出冷媒温度が
速やかに上昇するので、第1の実施例で上述したように
圧縮機(1)の吐出冷媒温度を検出した方が好ましい。
In addition, the on-off valve (13) and the auxiliary on-off valve (18) are connected to the compressor (
It may be possible to open and close by detecting the discharge refrigerant pressure in 1) or the refrigerant pressure in the high-pressure liquid pipe (15), but since the inter-unit piping (9) and (10) are long piping, the amount of circulating refrigerant is insufficient. If the temperature becomes slightly low, the temperature of the refrigerant discharged from the compressor (1) will quickly rise, so it is preferable to detect the temperature of the refrigerant discharged from the compressor (1) as described above in the first embodiment.

第2図は本発明の第2実施例を示すヒートポンプ式の分
離型冷凍装置の冷媒回路図で、第1実施例と異なるのは
熱源側ユニット(20)内において、冷暖流路切換用の
四方弁(21)と、受液器(22)と、熱源側熱交換器
(2)の下部に一体に設けられた結氷防止コイル(23
)と、暖房用減圧器(24)(25)と、冷房用逆止弁
(26)とを図示の如く冷媒管(4)で接続すると共に
、利用側ユニット(27)内において冷房用減圧器(2
8)と暖房用逆上弁(29)とを図示の如く並列接続し
た点であり、第1実施例と同一のものは同一符号で付記
して説明は省略する。
FIG. 2 is a refrigerant circuit diagram of a heat pump type separate refrigeration system showing a second embodiment of the present invention. What differs from the first embodiment is that in the heat source side unit (20), four directions for switching between cooling and heating channels are provided. An anti-icing coil (23) integrally provided at the bottom of the valve (21), the liquid receiver (22), and the heat source side heat exchanger (2).
), the heating pressure reducer (24), (25), and the cooling check valve (26) are connected with the refrigerant pipe (4) as shown in the figure, and the cooling pressure reducer (27) is connected in the user side unit (27). (2
8) and a heating reversal valve (29) are connected in parallel as shown in the figure, and the same parts as in the first embodiment are given the same reference numerals and their explanation will be omitted.

冷媒回路動作を説明すると、ユニット間配管(9)(1
0)の長さが7m程度の短配管時において、冷房運転時
は四方弁(21)を実線状態に設定することにより、圧
縮機り1)−四方弁(21)−熱源側熱交換器(2)−
冷房用逆止弁(26)−結氷防止コイルく23)−受液
器(22)−補助減圧器(17)−ユニット間配管(9
)−冷房用減圧器(28)−利用側熱交換器(6〉−ユ
ニット間配管(10)−四方弁(21)−低圧容器(3
)−圧縮機(1)と順次冷媒が循環して、熱源側熱交換
器(2)及び結氷防止コイル(23)が凝縮器として、
利用側熱交換器(6)が蒸発器として夫々作用し、室内
が冷房される。
To explain the refrigerant circuit operation, the inter-unit piping (9) (1
0) with a short piping length of about 7 m, by setting the four-way valve (21) to the solid line state during cooling operation, the compressor 1) - four-way valve (21) - heat source side heat exchanger ( 2)-
Cooling check valve (26) - Anti-icing coil 23) - Liquid receiver (22) - Auxiliary pressure reducer (17) - Inter-unit piping (9)
) - Cooling pressure reducer (28) - User side heat exchanger (6> - Inter-unit piping (10) - Four-way valve (21) - Low pressure vessel (3)
) - The refrigerant circulates sequentially with the compressor (1), and the heat source side heat exchanger (2) and anti-icing coil (23) act as a condenser,
The user-side heat exchangers (6) each act as an evaporator to cool the room.

一方、暖房運転時は四方弁(21)を破線状態に切り換
えることにより、圧縮機(1)−四方弁(21)−ユニ
ット間配管(10)−利用側熱交換器(6)−暖房用逆
止弁(29)−ユニット間配管(9)−補助減圧器(1
7)−受液器(22)の下部より過冷却コイル(23)
−暖房用減圧器(24)及び受液器(22)の上部より
暖房用減圧器(25)−熱源側熱交換器(2)−四方弁
り21)−低圧容器(3)−圧縮機(1)と順次冷媒が
循環して、利用側熱交換器(6)及び結氷貼止コイル(
23)が凝縮器として、熱源側熱交換器(2)が蒸発器
として夫々作用し、室内が暖房される。
On the other hand, during heating operation, by switching the four-way valve (21) to the broken line state, the Stop valve (29) - Inter-unit piping (9) - Auxiliary pressure reducer (1)
7) - Supercooling coil (23) from the bottom of the liquid receiver (22)
- Heating pressure reducer (25) - Heat source side heat exchanger (2) - Four-way valve 21) - Low pressure vessel (3) - Compressor ( 1), the refrigerant is sequentially circulated through the user-side heat exchanger (6) and the ice-forming coil (
23) acts as a condenser, and the heat source side heat exchanger (2) acts as an evaporator, thereby heating the room.

かかる暖房運転時、結氷防止コイル(23)で熱源側熱
交換器(2)の下部が加熱されるため、この熱交換器(
2)の下部が凍結することはなく、且っ受液器(22)
内に液冷媒が一杯溜まり込まなくなると暖房用減圧器(
25)を流れる液冷媒がガス冷媒となってこの減圧器(
25)をほとんど冷媒が流れなくなり、暖房用減圧器(
24)のみで冷媒が減圧されるという具合に減圧度合が
調節される。しかも、この受液器(22)は小容量のも
のを用いているため、暖房運転時と同様に冷房運転時も
過冷却度が抑えられており、冷房運転時には結氷防止コ
イルク23)を、又、暖房運転時には暖房用逆止弁(2
9)を夫々用た高圧液冷媒はユニット間配管(9)を流
れていく際にフラッシュガス気味となると共にこのユニ
ット間配管(9)の管径は小さくなっているので、この
ユニット間配管(9)内に占められる冷媒の量が少なく
なり、ユニット間配管(9)(10)が長さ50m程度
の長足管であってもそれほど循環冷媒量が不足気味にな
らず、冷媒を現地配管時に充填する必要はない、しかし
、この冷媒不足気味により圧縮機(1)の吐出冷媒温度
が異常上昇することは避けられず、この吐出冷媒温度が
設定値1゜O″C0以上ると検出器(12)からの信号
で開閉弁(13)及び補助開閉弁(18)が開いて高圧
液冷媒の一部が低圧容器り3)に導かれると共に補助減
圧器(17)の抵抗値が減った分だけ過冷却度が上がる
ため吐出冷媒温度の上昇が抑えられる。
During such heating operation, the lower part of the heat source side heat exchanger (2) is heated by the anti-icing coil (23), so this heat exchanger (
2) The lower part of the liquid receiver (22) will not freeze.
When the liquid refrigerant no longer accumulates inside, the heating pressure reducer (
The liquid refrigerant flowing through 25) becomes gas refrigerant and passes through this pressure reducer (
25), almost no refrigerant flows through the heating pressure reducer (
The degree of pressure reduction is adjusted such that the refrigerant is depressurized only by step 24). Moreover, since this liquid receiver (22) is of a small capacity, the degree of supercooling is suppressed during cooling operation as well as during heating operation, and the anti-icing coil 23) is used during cooling operation. , during heating operation, the heating check valve (2
The high-pressure liquid refrigerant using each of 9) becomes a bit of flash gas as it flows through the inter-unit piping (9), and the pipe diameter of this inter-unit piping (9) is small. 9) The amount of refrigerant occupied by the unit is reduced, and even if the pipes (9) and (10) between the units are long pipes with a length of about 50 m, the amount of circulating refrigerant will not be so short, and the refrigerant can be transferred to the pipes at the site. There is no need to charge the refrigerant, but it is inevitable that the refrigerant temperature discharged from the compressor (1) will rise abnormally due to this refrigerant shortage. The on-off valve (13) and the auxiliary on-off valve (18) are opened by the signal from 12), and part of the high-pressure liquid refrigerant is guided to the low-pressure container 3), and the resistance value of the auxiliary pressure reducer (17) is reduced. Since the degree of supercooling increases by this amount, the rise in discharge refrigerant temperature is suppressed.

尚、ユニット間配管(9)が長足管であれば、管径の小
さいこのユニット間配管(9)が冷媒減圧器として作用
することになるが、短配管時にはユニット間配管(9)
が冷媒減圧器としてあまり作用しないため、冷房用減圧
器(28)及び暖房用減圧器(24)(25)は必要で
ある。
In addition, if the inter-unit piping (9) is a long leg pipe, this inter-unit piping (9) with a small pipe diameter will act as a refrigerant pressure reducer, but when the pipe is short, the inter-unit piping (9)
The cooling pressure reducer (28) and the heating pressure reducer (24) and (25) are necessary because the refrigerant does not function much as a refrigerant pressure reducer.

又、補助減圧器(17)と補助開閉弁(18)は設けた
方が好ましいこと、高圧液管(15)(19)の管径を
ユニット間配管(9)の管径(例えば6.35mm)と
同じ管径にした方が好ましいこと、検出器(12)で圧
縮機(1)の吐出冷媒温度を検出した方が好ましいこと
は上記第1実施例と同様である。
Also, it is preferable to provide an auxiliary pressure reducer (17) and an auxiliary on-off valve (18), and the diameter of the high-pressure liquid pipes (15) and (19) should be set to the diameter of the inter-unit pipe (9) (for example, 6.35 mm). ), and that it is preferable to use the detector (12) to detect the refrigerant temperature discharged from the compressor (1) are the same as in the first embodiment.

第3図は本発明の第3実施例を示す分離型冷凍装置の冷
媒回路図で、第1実施例と異なるのは熱源側ユニット(
30)に熱源側熱交換器り2)のみを内蔵し、利用側ユ
ニット(31)に利用側熱交換器(6)と減圧器(7)
の他に圧縮機(1)と低圧容器(3)とバイパス管(1
1)等を内蔵した点であり、第1実施例と同一のものは
同一符号で付記して説明は省略する。
FIG. 3 is a refrigerant circuit diagram of a separate refrigeration system showing a third embodiment of the present invention, which differs from the first embodiment in the heat source side unit (
30) has only the heat source side heat exchanger 2) built in, and the user side unit (31) has the user side heat exchanger (6) and pressure reducer (7) built-in.
In addition, there is a compressor (1), a low pressure vessel (3) and a bypass pipe (1).
1), etc., and the same parts as in the first embodiment are denoted by the same reference numerals and the explanation thereof will be omitted.

冷媒回路動作を説明すると、ユニット間配管(9)(1
0)の長さが7m程度の短配管時において、圧縮機(1
)−ユニット間配管(10)−熱源側熱交換器(2)−
ユニット間配管(9)−補助減圧器り17)−減圧器(
7)−利用側熱交換器(6)−低圧容器(3)−圧縮機
(1)と順次冷媒が循環して熱源側熱交換器(2)が凝
縮器として、利用側熱交換器(6)が蒸発器として夫々
作用する冷房(冷却)運転が行なわれる。
To explain the refrigerant circuit operation, the inter-unit piping (9) (1
When the compressor (1
) - Inter-unit piping (10) - Heat source side heat exchanger (2) -
Inter-unit piping (9) - Auxiliary pressure reducer 17) - Pressure reducer (
7) - Utilization side heat exchanger (6) - Low pressure container (3) - Compressor (1) The refrigerant is circulated in order, and the heat source side heat exchanger (2) serves as a condenser, and the utilization side heat exchanger (6) ) acts as an evaporator in a cooling operation.

かかる冷房(冷却)運転時、高圧液管(15)に受液器
を設けていないため過冷却度が抑えられており、熱源側
熱交換器(2)を出た高圧液冷媒はユニット間配管(9
)を流れていく際にフラッシュガス気味となって補助減
圧器(17)に達すると共に、このユニット間配管(9
)の管径は小さくなっているのでこのユニット間配管(
9)内に占められる冷媒の量が少なくなり、ユニット間
配管(9)(10)が長さ50m程度の長足管であって
もそれほど循環冷媒量が不足気味にならず、冷媒を現地
配管時に充填する必要はない、しかし、この冷媒不足気
味により圧縮機(1)の吐出冷媒温度が異常上昇するこ
とは避けられず、この吐出冷媒温度が設定値100°C
以上になると検出器(12)からの信号で開閉弁(13
〉及び補助開閉弁(18)が開いて高圧液冷媒の一部が
低圧容器(3)に導かれると共に補助減圧器<17)の
抵抗値が減った分だけ過冷却度が上がるため吐出冷媒温
度の上昇が抑えられる。
During such cooling operation, the degree of supercooling is suppressed because the high-pressure liquid pipe (15) is not provided with a liquid receiver, and the high-pressure liquid refrigerant that exits the heat source side heat exchanger (2) is transferred to the inter-unit pipe. (9
), it becomes a bit of flash gas and reaches the auxiliary pressure reducer (17), and this inter-unit piping (9
) is smaller, so this inter-unit piping (
9) The amount of refrigerant occupied by the unit is reduced, and even if the pipes (9) and (10) between the units are long pipes with a length of about 50 m, the amount of circulating refrigerant will not be so short, and the refrigerant can be transferred to the pipes at the site. There is no need to charge the refrigerant, but due to this refrigerant shortage, it is inevitable that the discharge refrigerant temperature of the compressor (1) will rise abnormally, and this discharge refrigerant temperature will exceed the set value of 100°C.
When the temperature exceeds the limit, a signal from the detector (12) is sent to the on-off valve (13).
〉 and the auxiliary on-off valve (18) open and a part of the high-pressure liquid refrigerant is guided to the low-pressure container (3), and the degree of supercooling increases by the amount that the resistance value of the auxiliary pressure reducer <17) decreases, so the discharge refrigerant temperature decreases. The increase in

尚、ユニット間配管(9)が長足管であれば、管径の小
さいこのユニット間配管(9)が冷媒減圧器として作用
することになるが、短配管時にはユニット間配管(9〉
が冷媒減圧器としてあまり作用しないため、減圧器(7
)は必要である。
In addition, if the inter-unit piping (9) is a long leg pipe, this inter-unit piping (9) with a small pipe diameter will act as a refrigerant pressure reducer, but when the pipe is short, the inter-unit piping (9)
The pressure reducer (7) does not function very well as a refrigerant pressure reducer.
) is necessary.

又、補助減圧器(17)と補助開閉弁(18)は設けた
方が好ましいこと、高圧液管(15)(19)の管径を
ユニット間配管(9)の管径(例えば6.35m1ll
)と同じ管径にした方が好ましいこと、検出器(12)
で圧縮機(1)の吐出冷媒温度を検出した方が好ましい
ことは上記第1実施例と同様である。
Also, it is preferable to provide an auxiliary pressure reducer (17) and an auxiliary on-off valve (18), and the diameters of the high-pressure liquid pipes (15) and (19) should be adjusted to the diameter of the inter-unit piping (9) (for example, 6.35ml).
), it is preferable to use the same pipe diameter as the detector (12).
As in the first embodiment, it is preferable to detect the temperature of the refrigerant discharged from the compressor (1).

第4図は本発明の第4実施例を示すヒートポンプ式の分
離型冷凍装置の冷媒回路図で、第3実施例と異なるのは
利用側ユニット(32〉に冷暖流路切換用の四方弁(2
1)と冷房用減圧器(28)と暖房用逆止弁(29)と
を図示の如く設けると共に熱源側ユニット(33)内に
暖房用減圧器(24)と冷房用逆止弁り26)とを図示
の如ぐ設けた点であり、第3実施例と同一のものは同一
符号で付記して説明は省略する。
FIG. 4 is a refrigerant circuit diagram of a heat pump type separate refrigeration system showing a fourth embodiment of the present invention. What differs from the third embodiment is that the user side unit (32) has a four-way valve for switching between cooling and heating channels. 2
1), a cooling pressure reducer (28), and a heating check valve (29) are installed as shown in the figure, and a heating pressure reducer (24) and a cooling check valve 26) are installed in the heat source side unit (33). Components that are the same as those in the third embodiment are designated by the same reference numerals, and a description thereof will be omitted.

冷媒回路動作を説明すると、ユニット間配管(9)(1
0)の長さが7m程度の短配管時において、冷房運転時
は四方弁(21)を実線状態に設定することにより、圧
縮機(1)−四方弁(21)−ユニット間配−管(10
)−熱源側熱交換器(21)−冷房用逆上弁(26)−
ユニット間配管(9)−補助減圧器(17)−冷房用減
圧器(28〉−利用側熱交換器(6)−四方弁(21)
−低圧容器(3)−圧縮機(1)と順次冷媒が循環して
、熱源側熱交換器(2)が凝縮器として、利用側熱交換
器(6)が蒸発器として夫々作用し、室内が冷房される
To explain the refrigerant circuit operation, the inter-unit piping (9) (1
0) with a short piping length of about 7 m, by setting the four-way valve (21) to the solid line state during cooling operation, the piping between the compressor (1), the four-way valve (21), and the unit ( 10
) - Heat source side heat exchanger (21) - Cooling reverse valve (26) -
Inter-unit piping (9) - Auxiliary pressure reducer (17) - Cooling pressure reducer (28> - User side heat exchanger (6) - Four-way valve (21)
- Low pressure container (3) - Compressor (1), the refrigerant circulates in order, the heat source side heat exchanger (2) acts as a condenser, the user side heat exchanger (6) acts as an evaporator, and the indoor is cooled.

一方、暖房運転時は四方弁(21)を破線状態に切り換
えることにより、圧縮機(1)−四方弁(21)−利用
側熱交換器(6〉−暖房用逆止弁(29)−補助減圧器
(17)−ユニット間配管(9)−暖房用減圧器(25
)−熱源側熱交換器(2)−ユニット間配管(10)−
四方弁(21)−低圧容器(3)−圧縮機(1)と順次
冷媒が循環して、利用側熱交換器(6)が凝縮器として
、熱源側熱交換器(2)が蒸発器として夫々作用し、室
内が暖房される。
On the other hand, during heating operation, by switching the four-way valve (21) to the broken line state, compressor (1) - four-way valve (21) - user side heat exchanger (6> - heating check valve (29) - auxiliary Pressure reducer (17) - Inter-unit piping (9) - Heating pressure reducer (25)
) - Heat source side heat exchanger (2) - Inter-unit piping (10) -
The refrigerant circulates in sequence through the four-way valve (21) - low pressure container (3) - compressor (1), with the user side heat exchanger (6) acting as a condenser and the heat source side heat exchanger (2) acting as an evaporator. Each acts to heat the room.

かかる冷暖房運転時、高圧液管(15)(19)に受液
器を設けていないため過冷却度が抑えられており、冷房
運転時には冷房用逆上弁(26〉を、暖房運転時には補
助減圧器(17)を夫々出た高圧液冷媒はユニット間配
管(9)を流れていく際にフラッシュガス気味となると
共にこのユニット間配管(9)の管径は小さくなってい
るので、このユニット間配管(9)内に占められる冷媒
の量が少なくなり、ユニット間配管(9)Do)が長さ
50m程度の長配管であってもそれほど循環冷媒量が不
足気味にならず、冷媒を現地配管時に充填する必要はな
い、しかし、この冷媒不足気味により圧縮機(1)の吐
出冷媒温度が異常上昇することは避けられず、この吐出
冷媒温度が設定値100″C以上になると検出器(12
)からの信号で開閉弁(13)及び補助開閉弁(18)
が開いて高圧液冷媒の一部が低圧容器(3)に導かれる
と共に補助減圧器(17)の抵抗値が減った分だけ過冷
却度が上がるため吐出冷媒温度の上昇が抑えられる。
During such cooling/heating operation, the degree of supercooling is suppressed because the high-pressure liquid pipes (15) and (19) are not provided with liquid receivers. The high-pressure liquid refrigerant that has exited the respective units (17) becomes a bit of flash gas as it flows through the inter-unit piping (9), and the pipe diameter of this inter-unit piping (9) is small. The amount of refrigerant occupied in the pipe (9) is reduced, and even if the inter-unit pipe (9) Do) is a long pipe with a length of about 50 m, the amount of circulating refrigerant will not be so short, and the refrigerant can be transferred to the local pipe. However, due to this refrigerant shortage, it is inevitable that the discharge refrigerant temperature of the compressor (1) will rise abnormally, and if the discharge refrigerant temperature exceeds the set value of 100"C, the detector (12)
) The on-off valve (13) and the auxiliary on-off valve (18)
opens and a portion of the high-pressure liquid refrigerant is guided to the low-pressure container (3), and the degree of supercooling increases by the amount that the resistance value of the auxiliary pressure reducer (17) is reduced, thereby suppressing a rise in the temperature of the discharged refrigerant.

尚、ユニット間配管(9)が長配管であれば、管径の小
さいこのユニット間配管(9)が冷媒減圧器として作用
することになるが、短配管時にはユニット間配管(9)
が冷媒減圧器としてあまり作用しないため、冷房用減圧
器(28)及び暖房用減圧器(24)は必要である。
Furthermore, if the inter-unit piping (9) is a long piping, this inter-unit piping (9) with a small pipe diameter will act as a refrigerant pressure reducer, but when the piping is short, the inter-unit piping (9)
The cooling pressure reducer (28) and the heating pressure reducer (24) are necessary because the refrigerant does not function much as a refrigerant pressure reducer.

又、補助減圧器(17)と補助開閉弁(18)は設けた
方が好ましいこと、高圧液管(15>(19)の管径を
ユニット間配管(9)の管径(例えば6.35nll)
と同じ管径にした方が好ましいこと、検出器(12)で
圧縮機(1)の吐出冷媒温度を検出した方が好ましいこ
とは上記第1実施例と同様である。
Also, it is preferable to provide an auxiliary pressure reducer (17) and an auxiliary on-off valve (18), and the diameter of the high-pressure liquid pipe (15>(19)) should be set to the diameter of the inter-unit pipe (9) (for example, 6.35nll). )
As in the first embodiment, it is preferable that the tube diameter is the same as that of the first embodiment, and that it is preferable that the temperature of the refrigerant discharged from the compressor (1) be detected by the detector (12).

(ト)発明の効果 本発明は、以上説明したように構成されているので、次
に記載する効果を奏する。
(G) Effects of the Invention Since the present invention is configured as described above, it produces the following effects.

■請求項1,2.3又は4の分離型冷凍装置においては
、熱源側゛ユニット又は利用側ユニット内に高圧冷媒の
温度または圧力が設定値以上になると高圧液管からの冷
媒の一部を圧縮機の吸込側へ導くバイパス管を設けると
共に、前記高圧液管と接続されるユニット間配管の管径
を他の冷媒管の管径よりも小さくしたので、ユニット間
配管内に占められる高圧液冷媒の量が少なくなり、この
ユニット間配管が例えば50mの長配管であってもそれ
ほど循環冷媒量が不足気味にならず、冷媒を現地配管時
に充填する必要がないと共に、この冷媒不足気味により
高圧冷媒の温度又は圧力が上昇するとバイパス管を経て
高圧液管より高圧液冷媒の一部が圧縮機に吸い込まれる
ため、圧縮機の吐出冷媒温度が異常上昇するのを防止す
ることができる。
■In the separate refrigeration system of Claims 1, 2.3, or 4, when the temperature or pressure of the high-pressure refrigerant in the heat source side unit or the user side unit exceeds a set value, a part of the refrigerant from the high-pressure liquid pipe is removed. In addition to providing a bypass pipe that leads to the suction side of the compressor, the pipe diameter of the inter-unit pipe connected to the high-pressure liquid pipe is made smaller than the pipe diameter of other refrigerant pipes, so that the high-pressure liquid occupied in the inter-unit pipe is The amount of refrigerant decreases, and even if the piping between units is long, for example, 50 m, the amount of circulating refrigerant does not become insufficient, and there is no need to refill the refrigerant at the time of on-site piping. When the temperature or pressure of the refrigerant increases, a portion of the high-pressure liquid refrigerant is sucked into the compressor from the high-pressure liquid pipe via the bypass pipe, so it is possible to prevent the temperature of the refrigerant discharged from the compressor from increasing abnormally.

しかも圧縮機に吸い込まれる冷媒を気液分離する低圧容
器と、利用側熱交換器もしくは熱源側熱交換器に流入す
る冷媒を減圧する減圧器とを備えたので、ユニット間配
管が例えば7mの短配管の場合は余剰冷媒が低圧容器に
溜まり込むと共にユニット間配管ではそれほど減圧きれ
ない冷媒を減圧器で充分に減圧でき、適正な循環冷媒量
と冷媒減圧度合で冷房(冷却)及び暖房運転を行なうこ
とができる。
Furthermore, since it is equipped with a low-pressure container that separates the refrigerant sucked into the compressor into gas and liquid, and a pressure reducer that reduces the pressure of the refrigerant flowing into the user-side heat exchanger or heat source-side heat exchanger, the piping between the units can be as short as, for example, 7 m. In the case of piping, excess refrigerant accumulates in a low-pressure container, and the pressure of the refrigerant that cannot be reduced so much in the piping between units can be sufficiently reduced in pressure with a pressure reducer, allowing air conditioning (cooling) and heating operations to be performed with an appropriate amount of circulating refrigerant and degree of refrigerant pressure reduction. be able to.

■請求項5の分離型冷凍装置においては、ユニット間配
管が長配管であるために循環冷媒量が不足気味となった
場合、圧縮機の吐出冷媒温度が速やかに上昇するのに着
目し、この吐出冷媒温度を検出してバイパス管の開閉弁
を開閉するようにしたので、圧縮機の温度が異常上昇す
るのを確実に助士することができる。
■ In the separated refrigeration system of claim 5, when the amount of circulating refrigerant becomes insufficient because the piping between the units is long, the temperature of the refrigerant discharged from the compressor quickly rises. Since the temperature of the discharged refrigerant is detected and the on-off valve of the bypass pipe is opened and closed, it is possible to reliably prevent the temperature of the compressor from rising abnormally.

■請求項6の分離型冷凍装置においては、高圧液冷媒の
一部がバイパス管より低圧容器に導かれて気液分離きれ
た後、圧縮機に吸い込まれるので、圧縮機が液圧縮する
のを防止することができる。
- In the separation type refrigeration system of claim 6, a part of the high-pressure liquid refrigerant is guided from the bypass pipe to the low-pressure container and separated into gas and liquid, and then sucked into the compressor, thereby preventing the compressor from compressing the liquid. It can be prevented.

■請求項7の分離型冷凍装置においては、ユニット間配
管内と高圧液管内とに占められる高圧液冷媒の量が少な
くなるので、長配管による循環冷媒量の不足気味を更に
緩和することができる。
■In the separate refrigeration system of claim 7, the amount of high-pressure liquid refrigerant occupied in the inter-unit piping and the high-pressure liquid pipe is reduced, so it is possible to further alleviate the shortage of circulating refrigerant due to long piping. .

■請求項8の分離型冷凍装置においては、補助減圧器が
ユニット間配管の短い時に作用し、長い時に作用しない
ため、短配管時と長配管時におけるユニット間配管の抵
抗差が少なくなり、短配−管と長配管の何れの場合でも
略適正な循環冷媒量で冷暖房運転を行なうことができる
■In the separate type refrigeration system of claim 8, the auxiliary pressure reducer acts when the inter-unit piping is short and does not act when it is long, so the difference in resistance between the inter-unit piping between short piping and long piping is reduced. Cooling/heating operation can be performed with a substantially appropriate amount of circulating refrigerant in both pipes and long pipes.

■請求項9の分離型冷凍装置においては、補助減圧器の
制御をユニット間配管の長さによって変化する圧縮機の
吐出冷媒温度により行なうため、上記■の効果を更に高
めることができる。
(2) In the separate refrigeration system of the ninth aspect, the auxiliary pressure reducer is controlled by the compressor discharge refrigerant temperature, which changes depending on the length of the inter-unit piping, so that the effect (2) can be further enhanced.

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

第1図は本発明の第1実施例を示す分離型冷凍装置の冷
媒回路図、第2図は本発明の第2実施例を示すヒートポ
ンプ式の分離型冷凍装置の冷媒回路図、第3図は本発明
の第3実施例を示す分離型冷凍装置の冷媒回路図、第4
図は本発明の第4実施例を示すヒートポンプ式の分離型
冷凍装置の冷媒回路図である。 (1)・・・圧縮機、 (2)・・・熱源側熱交換器、
 (3)・・・低圧容器、 (4)・・・冷媒管、 (
5)(20)(30)(33)・・・熱源側ユニット、
 (6)・・・利用側熱交換器、(7)・・・減圧器、
 (8)(27)(31)(32)・・・利用側ユニッ
ト、  (9)(10)・・・ユニット間配管、 (1
1)・・・バイパス管、 (13)・・・開閉弁、 (
15)・・・高圧液管、(16)・・・低圧容器の冷媒
入口管、 (17)・・・補助減圧器、 (18)・・
・補助開閉弁、 (24)(25)・・・暖房用減圧器
、 (28)・・・冷房用減圧器。
FIG. 1 is a refrigerant circuit diagram of a separate type refrigeration system showing a first embodiment of the present invention, FIG. 2 is a refrigerant circuit diagram of a heat pump type separate type refrigeration system showing a second embodiment of the present invention, and FIG. 4 is a refrigerant circuit diagram of a separate refrigeration system showing a third embodiment of the present invention.
The figure is a refrigerant circuit diagram of a heat pump type separation type refrigeration apparatus showing a fourth embodiment of the present invention. (1)...Compressor, (2)...Heat source side heat exchanger,
(3)...Low pressure container, (4)...Refrigerant pipe, (
5) (20) (30) (33)...Heat source side unit,
(6)...user-side heat exchanger, (7)...pressure reducer,
(8) (27) (31) (32)... User side unit, (9) (10)... Inter-unit piping, (1
1)...Bypass pipe, (13)...On-off valve, (
15)...High pressure liquid pipe, (16)...Refrigerant inlet pipe of low pressure container, (17)...Auxiliary pressure reducer, (18)...
- Auxiliary on-off valve, (24) (25)... Heating pressure reducer, (28)... Cooling pressure reducer.

Claims (1)

【特許請求の範囲】 1、圧縮機と熱源側熱交換器と前記圧縮機に吸い込まれ
る冷媒を気液分離する低圧容器とを冷媒管で接続した熱
源側ユニットと、利用側熱交換器とこの利用側熱交換器
に流入する冷媒を減圧する減圧器とを有する利用側ユニ
ットとを一対のユニット間配管で接続した分離型冷凍装
置において、熱源側ユニット内に高圧冷媒の温度または
圧力が設置値以上になると高圧液管からの冷媒の一部を
圧縮機の吸込側へ導くバイパス管を設けると共に、前記
高圧液管と接続されるユニット間配管の管径を前記冷媒
管の管径よりも小さくしたことを特徴とする分離型冷凍
装置。 2、圧縮機と四方弁と熱源側熱交換器と暖房用減圧器と
前記圧縮機に吸い込まれる冷媒を気液分離する低圧容器
とを冷媒管で接続した熱源側ユニットと、利用側熱交換
器と冷房用減圧器とを有する利用側ユニットとを一対の
ユニット間配管で接続したヒートポンプ式の分離型冷凍
装置において、熱源側ユニット内に高圧冷媒の温度また
は圧力が設定値以上になると高圧液管からの冷媒の一部
を圧縮機の吸込側へ導くバイパス管を設けると共に、前
記高圧液管と接続されるユニット間配管の管径を前記冷
媒管の管径よりも小さくしたことを特徴とするヒートポ
ンプ式の分離型冷凍装置。 3、圧縮機と利用側熱交換器とこの利用側熱交換器に流
入する冷媒を減圧する減圧器と前記圧縮機に吸い込まれ
る冷媒を気液分離する低圧容器とを冷媒管で接続した利
用側ユニットと、熱源側熱交換器を有する熱源側ユニッ
トとを一対のユニット間配管で接続した分離型冷凍装置
において、利用側ユニット内に高圧冷媒の温度または圧
力が設定値以上になると高圧液管からの冷媒の一部を圧
縮機の吸込側へ導くバイパス管を設けると共に、前記高
圧液管と接続されるユニット間配管の管径を前記冷媒管
の管径よりも小さくしたことを特徴とする分離型冷凍装
置。 4、圧縮機と四方弁と利用側熱交換器と冷房用減圧器と
前記圧縮機に吸い込まれる冷媒を気液分離する低圧容器
とを冷媒管で接続した利用側ユニットと、熱源側熱交換
器と暖房用減圧器とを有する熱源側ユニットとを一対の
ユニット間配管で接続したヒートポンプ式の分離型冷凍
装置において、利用側ユニット内に高圧冷媒の温度また
は圧力が設定値以上になると高圧液管からの冷媒の一部
を圧縮機の吸込側へ導くバイパス管を設けると共に、前
記高圧液管と接続されるユニット間配管の管径を前記冷
媒管の管径よりも小さくしたことを特徴とするヒートポ
ンプ式の分離型冷凍装置。 5、バイパス管は圧縮機の吐出冷媒温度が設定値以上に
なると開く開閉弁を介在した管である請求項1、2、3
又は4に記載の分離型冷凍装置。 6、バイパス管の冷媒出口端を低圧容器の冷媒入口管に
接続した請求項1、2、3又は4に記載の分離型冷凍装
置。 7、高圧液管の管径がこの液管と接続されるユニット間
配管の管径と同一である請求項1、2、3又は4に記載
の分離型冷凍装置。 8、高圧液管に補助減圧器を介在すると共にこの補助減
圧器と並列に補助開閉弁を設けた請求項1、2、3又は
4に記載の分離型冷凍装置。 9、補助開閉弁は圧縮機の吐出冷媒温度が設定値以上に
なると開く弁である請求項8に記載の分離型冷凍装置。
[Scope of Claims] 1. A heat source side unit in which a compressor, a heat source side heat exchanger, and a low-pressure container that separates the refrigerant sucked into the compressor into gas and liquid are connected by a refrigerant pipe, and a user side heat exchanger and this In a separate refrigeration system in which a user unit is connected to a user unit that has a pressure reducer that reduces the pressure of the refrigerant flowing into the user heat exchanger through a pair of inter-unit piping, the temperature or pressure of the high-pressure refrigerant in the heat source unit is set to the installed value. In this case, a bypass pipe is installed to guide part of the refrigerant from the high-pressure liquid pipe to the suction side of the compressor, and the pipe diameter of the inter-unit pipe connected to the high-pressure liquid pipe is made smaller than the pipe diameter of the refrigerant pipe. Separate type refrigeration equipment characterized by the following. 2. A heat source side unit in which a compressor, a four-way valve, a heat source side heat exchanger, a heating pressure reducer, and a low pressure container that separates the refrigerant sucked into the compressor into gas and liquid are connected by refrigerant pipes, and a user side heat exchanger. In a heat pump type separate type refrigeration system in which a user unit with a cooling pressure reducer and a cooling pressure reducer are connected by a pair of inter-unit piping, when the temperature or pressure of high-pressure refrigerant in the heat source side unit exceeds a set value, the high-pressure liquid pipe A bypass pipe is provided to guide a part of the refrigerant from the compressor to the suction side of the compressor, and the pipe diameter of the inter-unit pipe connected to the high-pressure liquid pipe is made smaller than the pipe diameter of the refrigerant pipe. Separate heat pump type refrigeration equipment. 3. A user side in which a compressor, a user-side heat exchanger, a pressure reducer that reduces the pressure of the refrigerant flowing into the user-side heat exchanger, and a low-pressure container that separates the refrigerant sucked into the compressor into gas and liquid are connected by refrigerant pipes. In a separate refrigeration system in which a unit and a heat source side unit having a heat source side heat exchanger are connected by a pair of inter-unit piping, if the temperature or pressure of high pressure refrigerant in the user side unit exceeds a set value, the high pressure liquid pipe will A separation characterized in that a bypass pipe is provided to guide a part of the refrigerant to the suction side of the compressor, and the pipe diameter of the inter-unit pipe connected to the high-pressure liquid pipe is smaller than the pipe diameter of the refrigerant pipe. mold refrigeration equipment. 4. A user-side unit in which a compressor, a four-way valve, a user-side heat exchanger, a cooling pressure reducer, and a low-pressure container that separates the refrigerant sucked into the compressor into gas and liquid are connected by refrigerant pipes, and a heat source-side heat exchanger. In a heat pump type separate type refrigeration system in which a heat source side unit having a heating pressure reducer and a heat source side unit are connected by a pair of inter-unit piping, if the temperature or pressure of high pressure refrigerant in the user side unit exceeds a set value, the high pressure liquid pipe A bypass pipe is provided to guide a part of the refrigerant from the compressor to the suction side of the compressor, and the pipe diameter of the inter-unit pipe connected to the high-pressure liquid pipe is made smaller than the pipe diameter of the refrigerant pipe. Separate heat pump type refrigeration equipment. 5. Claims 1, 2, and 3, wherein the bypass pipe is a pipe with an on-off valve that opens when the temperature of the refrigerant discharged from the compressor exceeds a set value.
Or the separate type refrigeration device according to 4. 6. A separate refrigeration system according to claim 1, wherein the refrigerant outlet end of the bypass pipe is connected to the refrigerant inlet pipe of the low pressure container. 7. The separation type refrigeration system according to claim 1, 2, 3, or 4, wherein the diameter of the high-pressure liquid pipe is the same as that of the inter-unit piping connected to the liquid pipe. 8. The separate refrigeration system according to claim 1, 2, 3, or 4, wherein an auxiliary pressure reducer is interposed in the high-pressure liquid pipe and an auxiliary on-off valve is provided in parallel with the auxiliary pressure reducer. 9. The separate refrigeration system according to claim 8, wherein the auxiliary on-off valve is a valve that opens when the temperature of the refrigerant discharged from the compressor exceeds a set value.
JP63022431A 1988-02-01 1988-02-01 Separate refrigeration system Expired - Fee Related JP2594087B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63022431A JP2594087B2 (en) 1988-02-01 1988-02-01 Separate refrigeration system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63022431A JP2594087B2 (en) 1988-02-01 1988-02-01 Separate refrigeration system

Publications (2)

Publication Number Publication Date
JPH01196458A true JPH01196458A (en) 1989-08-08
JP2594087B2 JP2594087B2 (en) 1997-03-26

Family

ID=12082506

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63022431A Expired - Fee Related JP2594087B2 (en) 1988-02-01 1988-02-01 Separate refrigeration system

Country Status (1)

Country Link
JP (1) JP2594087B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0468967U (en) * 1990-10-25 1992-06-18
JP2007271181A (en) * 2006-03-31 2007-10-18 Fujitsu General Ltd Air conditioner
JP2007271180A (en) * 2006-03-31 2007-10-18 Fujitsu General Ltd Air conditioner

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54156266U (en) * 1978-04-24 1979-10-30
JPS6176852A (en) * 1984-08-20 1986-04-19 株式会社富士通ゼネラル Separate air conditioner
JPS62112065U (en) * 1986-01-07 1987-07-16

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54156266U (en) * 1978-04-24 1979-10-30
JPS6176852A (en) * 1984-08-20 1986-04-19 株式会社富士通ゼネラル Separate air conditioner
JPS62112065U (en) * 1986-01-07 1987-07-16

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0468967U (en) * 1990-10-25 1992-06-18
JP2007271181A (en) * 2006-03-31 2007-10-18 Fujitsu General Ltd Air conditioner
JP2007271180A (en) * 2006-03-31 2007-10-18 Fujitsu General Ltd Air conditioner

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