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JP2765243B2 - Air conditioner - Google Patents
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JP2765243B2 - Air conditioner - Google Patents

Air conditioner

Info

Publication number
JP2765243B2
JP2765243B2 JP3014560A JP1456091A JP2765243B2 JP 2765243 B2 JP2765243 B2 JP 2765243B2 JP 3014560 A JP3014560 A JP 3014560A JP 1456091 A JP1456091 A JP 1456091A JP 2765243 B2 JP2765243 B2 JP 2765243B2
Authority
JP
Japan
Prior art keywords
refrigerant
pipe
liquid
air conditioner
branch
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
Application number
JP3014560A
Other languages
Japanese (ja)
Other versions
JPH04332356A (en
Inventor
真理 佐田
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.)
Daikin Industries Ltd
Original Assignee
Daikin Kogyo 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 Daikin Kogyo Co Ltd filed Critical Daikin Kogyo Co Ltd
Priority to JP3014560A priority Critical patent/JP2765243B2/en
Publication of JPH04332356A publication Critical patent/JPH04332356A/en
Application granted granted Critical
Publication of JP2765243B2 publication Critical patent/JP2765243B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00Evaporators; Condensers
    • F25B39/02Evaporators
    • F25B39/028Evaporators having distributing means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/40Fluid line arrangements
    • F25B41/42Arrangements for diverging or converging flows, e.g. branch lines or junctions
    • F25B41/48Arrangements for diverging or converging flows, e.g. branch lines or junctions for flow path resistance control on the downstream side of the diverging point, e.g. by an orifice

Landscapes

  • Compression-Type Refrigeration Machines With Reversible Cycles (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、一台の室外ユニットに
対して複数の室内ユニットを互いに並列に接続した空気
調和装置に係り、特に、冷媒充填量の低減対策に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air conditioner in which a plurality of indoor units are connected in parallel to one outdoor unit, and more particularly to a measure for reducing the amount of refrigerant charged.

【0002】[0002]

【従来の技術】従来より、例えば実開平1―10266
1号公報に開示される如く、一台の室外ユニットに対し
て複数台の室内ユニットを配置し、室外ユニットの各機
器を主管により接続する一方、室内ユニットの各機器を
分岐管により接続し、主管に対して各分岐管を並列に接
続することにより、閉回路の冷媒回路を形成するように
したいわゆるマルチ形空気調和装置は公知の技術であ
る。
2. Description of the Related Art Conventionally, for example, Japanese Utility Model Laid-Open No. 1-1266.
As disclosed in No. 1, a plurality of indoor units are arranged for one outdoor unit, and each device of the outdoor unit is connected by a main pipe, while each device of the indoor unit is connected by a branch pipe, A so-called multi-type air conditioner in which each branch pipe is connected in parallel to a main pipe to form a closed circuit refrigerant circuit is a known technique.

【0003】[0003]

【発明が解決しようとする課題】ところで、上記従来の
ようなマルチ形空気調和装置において、冷房運転時に各
室内ユニットにおける膨張弁直前の冷媒状態が均一であ
ることが望ましく、さらに、各利用側熱交換器が十分な
能力を発揮するためにはその冷媒状態がある一定の範囲
内に収まっている必要がある。このため、液管における
圧力損失をできるだけ小さくすべく、冷媒管を十分保温
シ―ルして、液冷媒単相で配管内を流通させる方式が一
般的に採られている。しかるに、近年、冷媒使用量を低
減させるべき要請が強いが、上記のように全ての配管内
を液単相流で流通させると、特にマルチ形空気調和装置
では配管長さが数10mにも及ぶために、冷媒充填量が
莫大になり、冷媒充填量を低減することが困難である。
By the way, in the above-mentioned conventional multi-type air conditioner, it is desirable that the state of the refrigerant immediately before the expansion valve in each indoor unit during the cooling operation is uniform, and furthermore, that each utilization side heat is used. In order for the exchanger to exhibit sufficient capacity, its refrigerant state needs to be within a certain range. For this reason, in order to minimize the pressure loss in the liquid pipe, a system is generally adopted in which the refrigerant pipe is sufficiently kept warm and the liquid refrigerant is circulated through the pipe in a single phase. However, in recent years, there has been a strong demand to reduce the amount of refrigerant used. However, when all the pipes are circulated in a liquid single-phase flow as described above, especially in a multi-type air conditioner, the pipe length reaches several tens of meters. Therefore, the amount of refrigerant charged becomes enormous, and it is difficult to reduce the amount of refrigerant charged.

【0004】一方、液側の主管内を気液二相流で流通さ
せることにより、冷媒充填量を低減することが考えられ
るが、上記のようなマルチ形空気調和装置の場合、主管
から分岐管に冷媒を分流させる際、二相流では気液比率
を一様に分配するつまりボイド率を一定に各分岐管に分
配するのは非常に困難であるため偏流を生じていた。特
殊な装置を必要とするという問題があった。
[0004] On the other hand, it is conceivable to reduce the amount of refrigerant by flowing a gas-liquid two-phase flow through the main pipe on the liquid side. However, in the case of the multi-type air conditioner as described above, the main pipe is connected to the branch pipe. When the refrigerant is diverted into the two-phase flow, it is very difficult to distribute the gas-liquid ratio uniformly in the two-phase flow, that is, it is very difficult to distribute the void ratio to each branch pipe. There was a problem that a special device was required.

【0005】本発明は斯かる点に鑑みてなされたもので
あり、その目的は、主管では液冷媒のみの単相流とする
一方、分岐管では気液二相流とし、さらに各室内ユニッ
トにおける冷媒状態を均一化させることにより、空調機
能を良好に維持しながら、冷媒充填量の低減を図ること
にある。
[0005] The present invention has been made in view of such a point, and an object thereof is to make a single-phase flow of only a liquid refrigerant in a main pipe, a gas-liquid two-phase flow in a branch pipe, and furthermore, in each indoor unit. An object of the present invention is to reduce the amount of charged refrigerant while maintaining a good air conditioning function by making the refrigerant state uniform.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するた
め、請求項1の発明が講じた手段は、図1に示すよう
に、圧縮機(1)、熱源側熱交換器(3)及び室外減圧
弁(4)が配設された室外ユニット(X)に対して、室
内減圧弁(6a)及び利用側熱交換器(7a)を有する
複数台の室内ユニット(A),…を配置し、上記室外ユ
ニット(X)の各機器(1),(3),(4)を冷媒配
管の主管(9)により順次接続する一方、上記各室内ユ
ニット(A),…の各機器(6a)及び(7a),…を
それぞれ冷媒配管の分岐管(9a),…により接続し、
該各分岐管(9a),…を上記主管(9)に対して互い
に並列に接続してなる冷媒回路(10)を備えた空気調
和装置を前提とする。
In order to achieve the above object, the means of the present invention is, as shown in FIG. 1, composed of a compressor (1), a heat source side heat exchanger (3) and an outdoor unit. A plurality of indoor units (A) having an indoor pressure reducing valve (6a) and a use-side heat exchanger (7a) are arranged with respect to the outdoor unit (X) provided with the pressure reducing valve (4), The devices (1), (3), (4) of the outdoor unit (X) are sequentially connected by the main pipe (9) of the refrigerant pipe, while the devices (6a) of the indoor units (A),. (7a),... Are connected by branch pipes (9a),.
It is assumed that the air conditioner includes a refrigerant circuit (10) in which the branch pipes (9a) are connected in parallel to the main pipe (9).

【0007】そして、上記各分岐管(9a),…の上記
主管(9)の液管部から分岐している液側分岐部付近に
は、冷房運転時に冷媒を減圧して気液二相流で各分岐管
(9a),…に流すように、かつ当該分岐管(9a),
…の長さが長いほど冷媒の減圧度を低くするように構成
された減圧機構(20a),…がそれぞれ介設されてい
構成としたものである。
The branch pipes (9a),.
In the vicinity of the liquid side branch that branches off from the liquid pipe of the main pipe (9)
During the cooling operation, the refrigerant is depressurized and each branch pipe is
(9a), ... and the branch pipe (9a),
… Composed so that the longer the length, the lower the degree of decompression of the refrigerant
, The decompression mechanisms (20a),.
The configuration is as follows.

【0008】請求項2の発明の講じた手段は、上記請求
項1の発明において、各減圧機構(20a),…の減圧
度を当該室内ユニット(A),…の利用側熱交換器(7
a),…の容量が大きいほど低く設定したものである。
[0008] The means adopted by the invention of claim 2 is that, in the invention of claim 1, the degree of decompression of each decompression mechanism (20a),... Is determined by the use side heat exchanger (7) of the indoor unit (A),.
a),... are set lower as the capacity is larger.

【0009】請求項3の発明の講じた手段は、上記請求
項1又は2に発明において、各減圧機構(20a),…
の減圧度を当該分岐管(9a),…の径が大きいほど高
く設定したものである。
The means adopted by the invention of claim 3 is the same as that of claim 1 or 2 except that each of the pressure reducing mechanisms (20a),.
Are set higher as the diameter of the branch pipes (9a),... Is larger.

【0010】[0010]

【作用】以上の構成により、請求項1の発明では、空気
調和装置の冷房運転時、熱源側熱交換器(3)で凝縮液
化された冷媒が主管(9)内を液単相流で流れた後、各
分岐管(9a),…に分岐して、各室内ユニット
(A),…に流れる。そのとき、各分岐管(9a)〜
(9c)と主管(9)との分岐部に、冷媒を減圧して気
液二相流で各分岐管(9a),…に流すための減圧機構
(20a),…が設けられているので、液冷媒の一部が
蒸発液化し、その後気液二相流で流れる。したがって、
空気調和装置全体の冷媒充填量が低減することになる。
According to the first aspect of the present invention, during the cooling operation of the air conditioner, the refrigerant condensed and liquefied by the heat source side heat exchanger (3) flows through the main pipe (9) as a liquid single-phase flow. After that, it branches into each branch pipe (9a),... And flows into each indoor unit (A),. At that time, each branch pipe (9a) ~
The refrigerant is decompressed at the branch between (9c) and the main pipe (9),
Since the pressure reducing mechanisms (20a),... For flowing the liquid two-phase flow to the branch pipes (9a),... Are provided, a part of the liquid refrigerant is evaporated and liquefied, and then flows in a gas-liquid two-phase flow. Therefore,
The amount of refrigerant charged in the entire air conditioner is reduced.

【0011】その場合、分岐管(9a),…の長さが長
いほど圧力損失が大きくなり、特に気液二相流の場合、
圧力損失の差によって各室内減圧弁(6a),…直前に
おける圧力等の冷媒状態が大きく変化するが、本発明で
は、当該分岐管(9a),…の長さが長いほど各減圧機
構(20a),…の減圧度が小さくなるように設定され
ているので、各分岐管(9a),…における圧力損失の
差が補償され、各室内減圧弁(6a),…直前の冷媒圧
力が略均一化されて、各利用側熱交換器(7a),…の
能力が適正に確保される。したがって、分岐管(9
a),…の配管長に差がある場合にも、配管径を微細に
変更することなく、減圧機構(9a),…の減圧度の設
定により、各室内ユニット(A),…における空調機能
を良好に維持しながら、冷媒充填量の低減が可能とな
る。
In this case, the longer the length of the branch pipes (9a),..., The greater the pressure loss, and especially in the case of a gas-liquid two-phase flow,
The refrigerant state such as the pressure immediately before each indoor pressure reducing valve (6a),... Greatly changes due to the difference in pressure loss. In the present invention, the longer the length of the branch pipes (9a),.
Are set so as to reduce the degree of pressure reduction in the structures (20a),..., The difference in pressure loss in each branch pipe (9a),. Are made substantially uniform, and the capacity of each use-side heat exchanger (7a),. Therefore, the branch pipe (9
a), even if there is a difference in the piping length, the air conditioning function in each indoor unit (A),... by setting the degree of decompression of the pressure reducing mechanisms (9a),. , And the amount of refrigerant charged can be reduced.

【0012】請求項2の発明では、各室内ユニット
(A),…の利用側熱交換器(7a),…の容量に差が
ある場合、容量が大きいほど多くの冷媒循環量が必要と
なるが、当該利用側熱交換器(7a),…の容量が大き
いほど各減圧機構(9a),…の減圧度が低く設定され
ているので、利用側熱交換器(7a),…の能力が適正
に確保され、各室内ユニット(A),…における空調能
力が良好に維持されることになる。
According to the second aspect of the present invention, when there is a difference between the capacities of the use side heat exchangers (7a),... Of the indoor units (A),. However, the larger the capacity of the use side heat exchangers (7a),..., The lower the degree of decompression of each decompression mechanism (9a),. The air-conditioning capacity of each of the indoor units (A),... Is properly maintained.

【0013】請求項3の発明では、分岐管(9a),…
の径が大きくなるほど減圧機構(20a),…の減圧度
が高く設定されているので、径の増大に応じて低下する
各分岐管(9a),…の圧力損失の差が補償され、径の
変更による圧力損失の調整と相俟って、室内減圧弁(6
a),…直前の冷媒圧力がより微細に均一化され、円滑
な運転が確保されることになる。
According to the third aspect of the present invention, the branch pipes (9a),.
Are set higher as the diameter of the pressure reducing mechanisms (20a),... Is increased, the difference in pressure loss between the branch pipes (9a),. In conjunction with the adjustment of the pressure loss by the change, the indoor pressure reducing valve (6
a),... The refrigerant pressure immediately before is more finely equalized, and a smooth operation is ensured.

【0014】[0014]

【実施例】以下、本発明の実施例について、図1〜図4
に基づき説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to FIGS.
It will be described based on.

【0015】図1は実施例に係る空気調和装置の冷媒配
管系統を示し、一台の室外ユニット(X)に対して三台
の室内ユニット(A)〜(C)が並列に接続されたマル
チ形に構成されている。上記室外ユニット(X)には、
吸入した冷媒を圧縮して吐出する圧縮機(1)と、冷房
運転時には図中実線のごとく、暖房運転時には図中破線
のごとく接続が切換わる四路切換弁(2)と、冷房運転
時には凝縮器として、暖房運転時には蒸発器として機能
する熱源側熱交換器(3)と、暖房運転時に冷媒を減圧
する室外減圧弁として機能する室外電動膨張弁(4)
と、液冷媒を貯溜するためのレシ―バ(5)と、上記圧
縮機(1)に吸入される冷媒中の液冷媒を除去するアキ
ュムレ―タ(8)とが主要機器として配置されており、
上記各機器は冷媒配管の主管(9)により順次直列に接
続されている。
FIG. 1 shows a refrigerant piping system of an air conditioner according to an embodiment. A multi-unit in which three indoor units (A) to (C) are connected in parallel to one outdoor unit (X). It is configured in shape. In the outdoor unit (X),
A compressor (1) that compresses and discharges the sucked refrigerant, a four-way switching valve (2) whose connection switches as shown by the solid line in the cooling operation and a broken line in the heating operation as shown by the solid line in the cooling operation, and a condensate in the cooling operation A heat source side heat exchanger (3) that functions as an evaporator during the heating operation, and an outdoor electric expansion valve (4) that functions as an outdoor pressure reducing valve that reduces the pressure of the refrigerant during the heating operation.
And a receiver (5) for storing the liquid refrigerant and an accumulator (8) for removing the liquid refrigerant in the refrigerant sucked into the compressor (1). ,
The above devices are connected in series by a main pipe (9) of a refrigerant pipe.

【0016】一方、上記各室内ユニット(A)〜(C)
には、互いに異なる容量を有し、冷房運転時には蒸発器
として、暖房運転時には凝縮器として機能する利用側熱
交換器(7a)〜(7c)と、冷房運転時には冷媒を減
圧し、暖房運転時には冷媒流量を調節する室内減圧弁と
しての室内電動膨張弁(6a)〜(6c)とが設けられ
ており、上記各室内ユニット(A)〜(C)の各機器
(6a)〜(6c),(7a)〜(7c)は、それぞれ
冷媒配管の分岐管(9a)〜(9c)により接続されて
おり、さらに、各分岐管(9a)〜(9c)は、上記主
管(9)の両端に設けられた液分流器(14)及びガス
分流器(15)間に互いに並列に接続されている。すな
わち、上記空気調和装置の各主要機器(1)〜(8)
は、主管(9)及び分岐管(9a)〜(9c)により、
閉回路を形成するように順次接続され、熱移動を生じさ
せるように冷媒が循環する主冷媒回路(10)が構成さ
れている。
On the other hand, each of the indoor units (A) to (C)
Have heat exchangers (7a) to (7c) having different capacities and functioning as an evaporator during the cooling operation and as a condenser during the heating operation, depressurizing the refrigerant during the cooling operation, and performing the heating operation during the heating operation. There are provided indoor electric expansion valves (6a) to (6c) as indoor pressure reducing valves for adjusting the flow rate of the refrigerant, and each device (6a) to (6c) of each of the indoor units (A) to (C) is provided. (7a) to (7c) are connected by branch pipes (9a) to (9c) of the refrigerant pipe, respectively. Further, the branch pipes (9a) to (9c) are connected to both ends of the main pipe (9). The liquid distributor (14) and the gas distributor (15) are connected in parallel with each other. That is, each of the main devices (1) to (8) of the air conditioner.
Is composed of a main pipe (9) and branch pipes (9a) to (9c).
A main refrigerant circuit (10) is sequentially connected to form a closed circuit and circulates refrigerant to generate heat transfer.

【0017】ここで、本発明の特徴として、上記各分岐
管(9a)〜(9c)の液分流器(14)からの分岐部
(冷房運転時における液冷媒の入口部)には、各々各分
岐管(9a)〜(9c)の長さ,径及び各利用側熱交換
器(7a)〜(7c)の容量に対応した減圧度を有する
減圧機構としてのキャピラリチュ―ブ(20a)〜(2
0c)が設けられている。該各キャピラリチュ―ブ(2
0a),(20b),(20c)は、冷媒配管の主管
(9)の液側端部に設けられた液分流器(14)から分
岐する分岐管(9a),(9b),(9c)の液冷媒の
冷房運転時における入口部に設けられていて、各キャピ
ラリチュ―ブ(20a),(20b),(20c)の内
径に応じて、その減圧度が各室内ユニット(A),
(B),(C)の利用側熱交換器(7a),(7b),
(7c)の容量、各分岐管(9a),(9b),(9
c)の径及び長さに対し、下記表1のように設定されて
いる。
Here, as a characteristic of the present invention, each of the branch pipes (9a) to (9c) has a branch portion from the liquid distributor (14) (the inlet portion of the liquid refrigerant during the cooling operation). Capillary tubes (20a) to (20a) to (9a) to (9a) to (9a) to (9a) to (9a) to (9a) to (9a) to (7a) to (7a) to (7c). 2
0c) is provided. Each of the capillary tubes (2
0a), (20b) and (20c) are branch pipes (9a), (9b) and (9c) branching from a liquid flow divider (14) provided at the liquid side end of the main pipe (9) of the refrigerant pipe. Is provided at the inlet portion of the liquid refrigerant during the cooling operation, and the degree of decompression is set according to the inner diameter of each of the capillary tubes (20a), (20b), and (20c).
(B), (C) utilization side heat exchangers (7a), (7b),
(7c), each branch pipe (9a), (9b), (9
Table 1 below sets the diameter and length of c).

【0018】[0018]

【表1】 ただし、上記表1において、L,LM,M,HM,Hは
減圧度を示し、低い側から順に記載されている。すなわ
ち、上記表1に示すように、各キャピラリチュ―ブ(2
0a),(20b),(20c)の減圧度は、分岐管
(9a)〜(9c)の長さが長いほど低く、利用側熱交
換器(7a)〜(7c)の容量が大きいほど低く、かつ
分岐管(9a)〜(9c)の径が大きいほど高く設定さ
れている。
[Table 1] However, in Table 1 above, L, LM, M, HM, and H indicate the degree of pressure reduction, and are described in order from the lower side. That is, as shown in Table 1 above, each capillary tube (2
0a), (20b), and (20c), the degree of decompression decreases as the length of the branch pipes (9a) to (9c) increases, and decreases as the capacity of the use-side heat exchangers (7a) to (7c) increases. The higher the diameter of the branch pipes (9a) to (9c), the higher the setting.

【0019】したがって、上記実施例では、空気調和装
置の冷房運転時、圧縮機(1)から吐出された冷媒が冷
媒配管の主管(9)を流れ、熱源側熱交換器(3)で凝
縮液化され、レシ―バ(5)に貯溜された後、液分流器
(14)から各分岐管(9a)〜(9c)に分岐して各
室内ユニット(A)〜(C)に流れる。そして、各電動
膨張弁(6a)〜(6c)で絞られて各利用側熱交換器
(7a)〜(7c)で蒸発した後、ガス分流器(15)
で合流して室外ユニット(X)に流入し、アキュムレ―
タ(8)を経て圧縮機(1)に戻る。この循環を繰り返
すことにより、各利用側熱交換器(7a)〜(7c)で
室内空気との熱交換により吸収した熱を熱源側熱交換器
(3)で室外空気に放出して、各室内の冷房を行う。
Therefore, in the above embodiment, during the cooling operation of the air conditioner, the refrigerant discharged from the compressor (1) flows through the main pipe (9) of the refrigerant pipe and condenses and liquefies in the heat source side heat exchanger (3). After being stored in the receiver (5), the liquid branches from the liquid distributor (14) to the branch pipes (9a) to (9c) and flows to the indoor units (A) to (C). After being throttled by each of the electric expansion valves (6a) to (6c) and evaporated by each of the use-side heat exchangers (7a) to (7c), the gas diverter (15)
, Flow into the outdoor unit (X), and accumulate
Return to the compressor (1) via the compressor (8). By repeating this circulation, the heat absorbed by the heat exchange with the indoor air in each of the use-side heat exchangers (7a) to (7c) is released to the outdoor air by the heat-source-side heat exchanger (3), and each of the indoor heat exchangers (7a) to (7c) is released. Perform air conditioning.

【0020】そのとき、上記各分岐管(9a)〜(9
c)の液分流器(14)との分岐部付近に、それぞれ各
分岐管(9a)〜(9c)への冷媒を減圧するための減
圧機構として機能するキャピラリチュ―ブ(20a)〜
(20c)が設けられているので、液分流器(14)ま
で液単相流で流れてきた液冷媒の一部が蒸発液化して、
その後気液二相流で流れる。ここで、例えばビル等の建
物内では、各室に至る冷媒配管の分岐管(9a)〜(9
c)の長さは数10mにも至るので、従来のようにこの
分岐管(9a)〜(9c)内に液冷媒を充填すると、そ
の冷媒量は莫大なものになり、冷媒使用量低減の要請に
応えることはできない。それに対して、上記実施例のよ
うに、各分岐管(9a)〜(9c)内を気液二相流で流
通させることにより、空気調和装置全体の冷媒充填量を
低減することができる。
At this time, each of the branch pipes (9a) to (9)
Capillary tubes (20a) to (c) functioning as decompression mechanisms for decompressing the refrigerant to the branch pipes (9a) to (9c) respectively near the branching point with the liquid flow divider (14).
Since the liquid refrigerant (20c) is provided, part of the liquid refrigerant flowing in the liquid single-phase flow to the liquid flow divider (14) evaporates and liquefies,
Thereafter, it flows in a gas-liquid two-phase flow. Here, for example, in a building such as a building, branch pipes (9a) to (9a) of refrigerant pipes reaching each room.
Since the length of c) reaches several tens of meters, if the branch pipes (9a) to (9c) are filled with the liquid refrigerant as in the prior art, the amount of the refrigerant becomes enormous, and the amount of refrigerant used is reduced. We cannot respond to requests. On the other hand, as in the above-described embodiment, by flowing the gas through the branch pipes (9a) to (9c) in a gas-liquid two-phase flow, the refrigerant charging amount of the entire air conditioner can be reduced.

【0021】その場合、液分流器(14)までの主管
(9)内を気液二相流で流通させると、各分岐管(9
a)〜(9c)への分配が困難となるが、上記実施例の
ように液側の主管(9)内では液単相流であるので、そ
のような問題は生じない。
In this case, when the main pipe (9) up to the liquid distributor (14) is circulated in a gas-liquid two-phase flow, each branch pipe (9)
Although the distribution to a) to (9c) becomes difficult, such a problem does not occur because the liquid is a single-phase flow in the main pipe (9) on the liquid side as in the above embodiment.

【0022】そして、上記各キャピラリチュ―ブ(20
a)〜(20c)の減圧度が配置される分岐管(9a)
〜(9c)の長さが長いほど低く設定されているので、
各分岐管(9a)〜(9c)における圧力損失の差が緩
和される。すなわち、分岐管(9a)〜(9c)の長さ
が長いほど圧力損失が大きくなり、特に気液二相流の場
合、圧力損失の差によって各室内電動膨張弁(6a)〜
(6b)直前における冷媒状態(冷媒圧力)が大きく変
化する。例えば、分岐管(9a)〜(9c)の長さは長
いものでは50m以上にも及ぶため、配管長が長いと圧
力損失により電動膨張弁(6a)直前の冷媒圧力が極め
て低くなり、他の利用側熱交換器(9a)〜(9c)直
前の冷媒圧力が高いと、冷媒流量が激減する。したがっ
て、利用側熱交換器(7a)〜(7c)の能力が十分発
揮できないことになる。それに対して、分岐管(9a)
〜(9c)の長さに応じて上述のように減圧度を調節す
ることにより、圧力損失の差が補償され、各室内電動膨
張弁(6a)〜(6c)の冷媒圧力が略均一化されて、
各利用側熱交換器(7a)〜(7c)の能力が適正に発
揮される。よって、各室内ユニット(A)〜(C)にお
ける空調機能を良好に維持しながら、冷媒充填量の低減
を図ることができるのである。
Then, each of the above capillary tubes (20
a) A branch pipe (9a) in which the degree of reduced pressure of (20c) is arranged
The longer the length of ~ (9c) is, the lower it is set,
The difference in pressure loss in each of the branch pipes (9a) to (9c) is reduced. That is, the longer the length of the branch pipes (9a) to (9c), the greater the pressure loss. Particularly, in the case of a gas-liquid two-phase flow, the difference between the pressure losses causes the pressure in each of the indoor electric expansion valves (6a) to (6a) to
(6b) The refrigerant state (refrigerant pressure) immediately before changes greatly. For example, if the length of the branch pipes (9a) to (9c) is as long as 50 m or more, if the pipe length is long, the refrigerant pressure immediately before the electric expansion valve (6a) becomes extremely low due to pressure loss, and If the refrigerant pressure immediately before the use-side heat exchangers (9a) to (9c) is high, the flow rate of the refrigerant will drastically decrease. Therefore, the capacity of the use side heat exchangers (7a) to (7c) cannot be sufficiently exhibited. On the other hand, the branch pipe (9a)
By adjusting the degree of pressure reduction as described above according to the length of (9c) to (9c), the difference in pressure loss is compensated, and the refrigerant pressure of each indoor electric expansion valve (6a) to (6c) is made substantially uniform. hand,
The capacity of each use side heat exchanger (7a) to (7c) is properly exhibited. Therefore, the refrigerant charging amount can be reduced while maintaining the air conditioning function in each of the indoor units (A) to (C) satisfactorily.

【0023】特に、このような冷媒配管長の差に起因す
る圧力損失の差は、配管径の変更によっても可能である
が、多くの種類の口径を有する冷媒配管を準備すること
はコストアップにつながる。それに対して、キャピラリ
チュ―ブ(20a)〜(20c)の内径及び長さの差で
容易に調節しうる減圧度で圧力損失の差を補償すること
により、コストアップが抑制されることになる。
In particular, such a difference in pressure loss due to the difference in refrigerant pipe length can be achieved by changing the pipe diameter. However, preparing refrigerant pipes having various types of diameters increases costs. Connect. On the other hand, by compensating for the difference in pressure loss with the degree of reduced pressure that can be easily adjusted by the difference in inner diameter and length of the capillary tubes (20a) to (20c), cost increase is suppressed. .

【0024】また、各室内ユニット(A)〜(C)の各
利用側熱交換器(7a)〜(7cに容量差がある場合、
各利用側熱交換器(7a)〜(7c)の能力が大きいほ
ど、同じ冷媒状態を維持するのに必要な冷媒循環量は多
くなる。したがって、各利用側熱交換器(7a)〜(7
c)の容量が大きいほど減圧度を低くすることにより、
各利用側熱交換器(7a)〜(7c)に必要な冷媒循環
量が確保され、その能力が良好に発揮されることにな
る。
When there is a difference in capacity between the use side heat exchangers (7a) to (7c) of the indoor units (A) to (C),
The greater the capacity of each of the utilization side heat exchangers (7a) to (7c), the greater the amount of refrigerant circulation required to maintain the same refrigerant state. Therefore, each use side heat exchanger (7a) to (7a)
By reducing the degree of decompression as the volume of c) increases,
The required amount of the refrigerant circulating in each of the use-side heat exchangers (7a) to (7c) is ensured, and the capacity is sufficiently exhibited.

【0025】さらに、各分岐管(9a)〜(9c)の径
が大きくなるほど圧力損失は小さくなるので、分岐管
(9a)〜(9a)の径が大きくなるほどキャピラリチ
ュ―ブ(20a)〜(20c)の減圧度を高くすること
により、各分岐管(9a)〜(9c)間の圧力損失差を
補償することができる。特に分岐管(9a)〜(9c)
の長さに応じてその配管径を変更することにより、圧力
損失を調節することができるが、上述のように口径が少
しずつ異なる多くの種類の配管を準備することはコスト
アップを招くので、上記表1に示すように、数種の配管
径で圧力損失を大まかに調節する一方、各キャピラリチ
ュ―ブ(20a)〜(20c)の減圧度の設定により、
配管径による調節と相俟って圧力損失の差を微細に補償
することができる。よって、室内電動膨張弁(6a)〜
(6c)直前の冷媒圧力をより均一化でき、円滑な運転
を確保することができるのである。
Further, as the diameter of each of the branch pipes (9a) to (9c) increases, the pressure loss decreases. Therefore, as the diameter of each of the branch pipes (9a) to (9a) increases, the capillary tubes (20a) to (9a). By increasing the degree of pressure reduction in 20c), it is possible to compensate for the pressure loss difference between the branch pipes (9a) to (9c). In particular, branch pipes (9a) to (9c)
The pressure loss can be adjusted by changing the pipe diameter in accordance with the length of the pipe, but as described above, preparing many types of pipes whose diameters are slightly different from each other increases the cost, As shown in Table 1 above, while the pressure loss is roughly adjusted with several types of pipe diameters, the degree of decompression of each of the capillary tubes (20a) to (20c) is set.
Along with the adjustment by the pipe diameter, the difference in pressure loss can be finely compensated. Therefore, the indoor electric expansion valve (6a)-
(6c) The refrigerant pressure immediately before can be made more uniform, and smooth operation can be ensured.

【0026】なお、上記実施例では、本発明を主管
(9)の両端に分流器(14),(15)を配置したい
わゆるヘッダ―分岐方式による空気調和装置に適用した
例を説明したが、本発明はかかる実施例に限定されるも
のではない。図3は上記実施例の変形例を示し、主管
(9)の途中から各分岐管(9a)〜(9c)が分岐す
るいわゆるライン方式の空気調和装置に適用した例を示
し、各分流器(14),(15)が設けられていない点
以外は上記実施例と同様である。
In the above embodiment, an example was described in which the present invention was applied to an air conditioner of a so-called header-branch system in which flow splitters (14) and (15) were arranged at both ends of a main pipe (9). The present invention is not limited to such an embodiment. FIG. 3 shows a modification of the above embodiment, in which the present invention is applied to a so-called line type air conditioner in which each of the branch pipes (9a) to (9c) branches from the middle of the main pipe (9). It is the same as the above embodiment except that the points 14) and 15) are not provided.

【0027】この変形例においても、上記実施例と同様
に、各分岐管(9a)〜(9b)の長さ,径及び利用側
熱交換器(7a)〜(7c)の容量に応じて各キャピラ
リチュ―ブ(20a)〜(20c)の減圧度を設定する
ことにより、上記実施例と同様の効果を得ることができ
る。
Also in this modified example, as in the above embodiment, each of the branch pipes (9a) to (9b) depends on the length and diameter and the capacity of the use-side heat exchangers (7a) to (7c). By setting the degree of pressure reduction of the capillary tubes (20a) to (20c), the same effect as in the above embodiment can be obtained.

【0028】また、本考案の減圧機構はキャピラリチュ
―ブに限定されるものではなく、図2は減圧機構として
ノズルを使用した例である。図4はその変形例を示し、
分岐管(9a)を途中の大径部で分割し、分割された各
端部にキャピラリチュ―ブ(20a)の外径部を嵌合さ
せた例である。この場合にも、液単相流の区間を極めて
短く限定することができ、上記実施例と同様の冷媒充填
量低減効果を発揮しうることはいうまでもない。
The pressure reducing mechanism of the present invention is not limited to the capillary tube, and FIG. 2 shows an example in which a nozzle is used as the pressure reducing mechanism. FIG. 4 shows a modified example thereof,
This is an example in which a branch pipe (9a) is divided at a large diameter part in the middle, and an outer diameter part of a capillary tube (20a) is fitted to each divided end. Also in this case, it is needless to say that the section of the liquid single-phase flow can be extremely short and the same effect of reducing the refrigerant charge as in the above embodiment can be exhibited.

【0029】[0029]

【発明の効果】以上説明したように、請求項1の発明に
よれば、空気調和装置の室外ユニットの各機器を主管で
接続する一方、室内ユニットの各機器を分岐管で接続
し、主管に対して各分岐管を互いに並列に接続して冷媒
回路を形成するとともに、各分岐管の主管からの液側分
岐部付近に、冷房運転時に冷媒を減圧して気液二相流で
各分岐管に流すための減圧機構を設け、この各減圧機構
の減圧度を当該分岐管の長さが長いほど低く設定するよ
うにしたので、液冷媒の一部を蒸発液化させて分岐管内
を気液二相流で流すことにより冷媒充填量を低減させる
ことができるとともに、配管径を微細に変更することな
く配管長差に基づく圧力損失の差を補償して各室内減圧
弁直前の冷媒状態を略均一化することができ、よって、
各室内ユニットにおける空調機能を良好に維持しなが
ら、冷媒充填量の低減を図ることができる。
As described above, according to the first aspect of the present invention, each device of the outdoor unit of the air conditioner is connected to the main pipe while each device of the indoor unit is connected to the main pipe. On the other hand, the branch pipes are connected in parallel with each other to form a refrigerant circuit, and in the vicinity of the liquid side branch from the main pipe of each branch pipe , the refrigerant is depressurized during the cooling operation to form a gas-liquid two-phase flow.
A decompression mechanism for flowing into each branch pipe is provided, and the degree of decompression of each decompression mechanism is set to be lower as the length of the branch pipe is longer. Refrigerant charge can be reduced by flowing in a gas-liquid two-phase flow, and the refrigerant state immediately before each indoor pressure reducing valve is compensated by compensating for the difference in pressure loss based on the pipe length difference without finely changing the pipe diameter. Can be made substantially uniform, so that
The refrigerant charging amount can be reduced while maintaining the air-conditioning function of each indoor unit satisfactorily.

【0030】請求項2の発明によれば、上記請求項1の
発明において、当該利用側熱交換器の容量が大きいほど
各減圧機構の減圧度を低く設定するようにしたので、各
室内ユニット利用側熱交換器の容量に差がある場合に
も、各利用側熱交換器の冷媒状態が適正に維持すること
ができ、よって、各室内ユニットにおける空調能力を良
好に維持することができる。
According to the second aspect of the present invention, in the first aspect of the present invention, the degree of decompression of each decompression mechanism is set to be lower as the capacity of the use side heat exchanger is larger. Even when there is a difference between the capacities of the side heat exchangers, the refrigerant state of each use side heat exchanger can be properly maintained, so that the air conditioning capacity of each indoor unit can be maintained well.

【0031】請求項3の発明によれば、上記請求項1又
は2の発明において、分岐管の径が大きくなるほど減圧
機構の減圧度を高く設定するようにしたので、径の増大
に応じて低下する各分岐管の圧力損失の差が補償され、
径の変更による圧力損失の調節と相俟って、室内減圧弁
直前の冷媒圧力をより微細に均一化させることができ、
よって、著効を発揮することができる。
According to the third aspect of the present invention, in the first or second aspect of the present invention, the degree of pressure reduction of the pressure reducing mechanism is set to be higher as the diameter of the branch pipe becomes larger, so that the pressure is reduced as the diameter increases. The difference in pressure loss between each branch pipe is compensated,
Together with the adjustment of the pressure loss by changing the diameter, the refrigerant pressure immediately before the indoor pressure reducing valve can be more finely uniformed,
Therefore, a remarkable effect can be exhibited.

【図面の簡単な説明】[Brief description of the drawings]

【図1】実施例に係る空気調和装置の冷媒配管系統図で
ある。
FIG. 1 is a refrigerant piping system diagram of an air conditioner according to an embodiment.

【図2】減圧機構にノズルを使用したときの構造を示す
縦断面図である。
FIG. 2 is a longitudinal sectional view showing a structure when a nozzle is used for a pressure reducing mechanism.

【図3】実施例の変形例に係る空気調和装置の冷媒配管
系統図である。
FIG. 3 is a refrigerant piping system diagram of an air conditioner according to a modification of the embodiment.

【図4】減圧機構にノズルを使用したときの変形例の構
造を示す縦断面図である。
FIG. 4 is a longitudinal sectional view showing a structure of a modified example when a nozzle is used for a pressure reducing mechanism.

【符号の説明】[Explanation of symbols]

1 圧縮機 3 熱源側熱交換器 4 室外電動膨張弁(室外減圧弁) 6 室内電動膨張弁(室内減圧弁) 9 主管 9a〜9c 分岐管 10 冷媒回路 20a〜20c キャピラリチュ―ブ(減圧機構) DESCRIPTION OF SYMBOLS 1 Compressor 3 Heat source side heat exchanger 4 Outdoor electric expansion valve (outdoor decompression valve) 6 Indoor electric expansion valve (indoor decompression valve) 9 Main pipe 9a-9c Branch pipe 10 Refrigerant circuit 20a-20c Capillary tube (decompression mechanism)

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 圧縮機(1)、熱源側熱交換器(3)及
び室外減圧弁(4)が配設された室外ユニット(X)に
対して、室内減圧弁(6a)及び利用側熱交換器(7
a)を有する複数台の室内ユニット(A),…を配置
し、上記室外ユニット(X)の各機器(1),(3),
(4)を冷媒配管の主管(9)により順次接続する一
方、上記各室内ユニット(A),…の各機器(6a)及
び(7a),…をそれぞれ冷媒配管の分岐管(9a),
…により接続し、該各分岐管(9a),…を上記主管
(9)に対して互いに並列に接続してなる冷媒回路(1
0)を備えた空気調和装置において、上記各分岐管(9a),…の上記主管(9)の液管部か
ら分岐している液側分岐部付近には、冷房運転時に冷媒
を減圧して気液二相流で各分岐管(9a),…に流すよ
うに、かつ当該分岐管(9a),…の長さが長いほど冷
媒の減圧度を低くするように構成された減圧機構(20
a),…がそれぞれ介設されている ことを特徴とする空
気調和装置。
1. An indoor pressure reducing valve (6a) and a use side heat are supplied to an outdoor unit (X) provided with a compressor (1), a heat source side heat exchanger (3) and an outdoor pressure reducing valve (4). Exchanger (7
a), a plurality of indoor units (A),... having the respective units (1), (3),
(4) are sequentially connected by the main pipe (9) of the refrigerant pipe, while the devices (6a) and (7a),... Of the indoor units (A),.
, And each of the branch pipes (9a),... Is connected to the main pipe (9) in parallel with each other.
0), the branch pipes (9a),... Of the liquid pipe section of the main pipe (9).
In the vicinity of the liquid side branch that branches from the
Is decompressed and flowed to each branch pipe (9a), ... in a gas-liquid two-phase flow.
And the longer the length of the branch pipe (9a),.
A pressure reducing mechanism (20) configured to reduce the degree of pressure reduction of the medium.
An air conditioner , wherein a),... are interposed .
【請求項2】 請求項1記載の空気調和装置において、 各減圧機構(20a),…の減圧度は当該室内ユニット
(A),…の利用側熱交換器(7a),…の容量が大き
いほど低く設定されていることを特徴とする空気調和装
置。
2. The air conditioner according to claim 1, wherein the degree of pressure reduction of each of the pressure reducing mechanisms (20a),... Is such that the capacity of the use side heat exchangers (7a),. An air conditioner characterized by being set as low as possible.
【請求項3】 請求項1又は2記載の空気調和装置にお
いて、 各減圧機構(20a),…の減圧度は当該分岐管(9
a),…の径が大きいほど高く設定されていることを特
徴とする空気調和装置。
3. The air conditioner according to claim 1, wherein the degree of pressure reduction of each pressure reducing mechanism (20a),.
a) An air conditioner characterized by being set higher as the diameter of... increases.
JP3014560A 1991-02-05 1991-02-05 Air conditioner Expired - Fee Related JP2765243B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3014560A JP2765243B2 (en) 1991-02-05 1991-02-05 Air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3014560A JP2765243B2 (en) 1991-02-05 1991-02-05 Air conditioner

Publications (2)

Publication Number Publication Date
JPH04332356A JPH04332356A (en) 1992-11-19
JP2765243B2 true JP2765243B2 (en) 1998-06-11

Family

ID=11864544

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3014560A Expired - Fee Related JP2765243B2 (en) 1991-02-05 1991-02-05 Air conditioner

Country Status (1)

Country Link
JP (1) JP2765243B2 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10170104A (en) * 1996-12-05 1998-06-26 Daikin Ind Ltd Flow divider and air conditioner
CN1324280C (en) * 2002-11-26 2007-07-04 乐金电子(天津)电器有限公司 Refrigeration circulation and control method thereof
JP4739883B2 (en) * 2005-09-22 2011-08-03 三洋電機株式会社 Air conditioner
JP4901851B2 (en) * 2008-12-15 2012-03-21 三菱電機株式会社 Expansion valve mechanism and air conditioner equipped with the same
JP5544311B2 (en) * 2011-01-06 2014-07-09 日立アプライアンス株式会社 Air conditioner
CN103162476A (en) * 2011-12-15 2013-06-19 同方人工环境有限公司 Structure with double thermostatic expansion valves
CN102798256B (en) * 2012-04-20 2015-06-17 广东美的暖通设备限公司 Device for regulating capacity output of outdoor unit heat exchanger of multi-connected machine set
JP6766084B2 (en) * 2018-01-22 2020-10-07 ダイキン工業株式会社 How to install the refrigeration equipment

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5222116Y2 (en) * 1973-07-11 1977-05-20
JPS59110871U (en) * 1983-01-17 1984-07-26 株式会社東芝 air conditioner
JPS6229057U (en) * 1985-08-06 1987-02-21

Also Published As

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