JPS58210380A - Parallel compression system refrigerator - Google Patents
Parallel compression system refrigeratorInfo
- Publication number
- JPS58210380A JPS58210380A JP9424682A JP9424682A JPS58210380A JP S58210380 A JPS58210380 A JP S58210380A JP 9424682 A JP9424682 A JP 9424682A JP 9424682 A JP9424682 A JP 9424682A JP S58210380 A JPS58210380 A JP S58210380A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- compressor
- compression element
- chamber
- pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B39/00—Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
- F04B39/02—Lubrication
- F04B39/0207—Lubrication with lubrication control systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—Component parts or details not otherwise provided for in this subclass
- F25B2400/07—Details of compressors or related parts
- F25B2400/075—Details of compressors or related parts with parallel compressors
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
- Compressor (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は、互に並列に接続された圧縮機の並列運転時
、或は任意の圧縮機の単独運転時のいづれの場合でも圧
縮機の油面を適正に保つようにした並列圧縮式冷凍装置
に関するものである。[Detailed Description of the Invention] The present invention is designed to maintain the oil level of the compressor at an appropriate level whether the compressors connected in parallel are operating in parallel or any compressor is operating independently. The present invention relates to a parallel compression type refrigeration system.
従来の2台の圧縮機による並列圧縮式冷凍装置において
は、測圧縮機間に均圧均油配管が設けられ、これ等の配
管は並列運転、単独運転を問わず、運転中は常に連通し
た状態で運転していた。この結果、吸入室要素と圧縮室
要素に区分された半密閉形冷凍機lこおいては、単独運
転中、停止した圧縮機の吸入管、モータ室、圧縮要素室
、及び均圧管を通して、運転中の圧縮機の圧縮要素室に
圧力がかかるため運転中の圧縮機の均油逆止弁が閉とな
り、せっかく吸入室へ戻った油が圧縮要素室へ戻らず、
圧縮室の油面を正常に維持することは難しく、圧縮機の
慴動部への潤滑油の供給不良等による焼付や、運転中の
圧縮機の油上り量過大による冷凍能力の低下、及び油圧
縮による弁部分の損傷の恐れがあった。また部分運転時
の油上り過大を防止するため、圧縮機の吐出側に油分離
器を取付け、吐出ガス中に含まれている油を分離して圧
縮機へ直接返送する方法もあるが、高温の油がクランク
ケースに戻り、油温を上昇させること、及び長時間停止
後の再始動時には、温度の低い分離器内へ凝縮した液冷
媒が圧縮機に返送され、油を泡立たせ潤滑不良を発、生
すること等の危険性があった。また、微少な圧縮機の能
力の差、吸入配管抵抗の差により面圧縮機の圧縮要素室
に差圧が生じ、運転中の圧縮機の油面がアンバランスと
なりやすい傾向があり、保守に当り油窓からの油面位置
の確認が難しく保守業務がやり難い等の欠点があった。In conventional parallel compression type refrigeration equipment using two compressors, pressure equalization and oil piping is installed between the measuring compressors, and these piping are always in communication during operation, regardless of parallel operation or individual operation. I was driving in this condition. As a result, in a semi-hermetic refrigerator that is divided into a suction chamber element and a compression chamber element, during independent operation, the suction pipe, motor room, compression element chamber, and pressure equalization pipe of the stopped compressor are passed through the Because pressure is applied to the compression element chamber of the compressor inside, the oil equalizing check valve of the compressor during operation closes, and the oil that has returned to the suction chamber does not return to the compression element chamber.
It is difficult to maintain the oil level in the compression chamber at a normal level, which can cause seizures due to insufficient supply of lubricating oil to the moving parts of the compressor, decrease in refrigeration capacity due to excessive oil flow from the compressor during operation, and oil leakage. There was a risk of damage to the valve part due to compression. In addition, in order to prevent excessive oil rise during partial operation, there is a method of installing an oil separator on the discharge side of the compressor to separate the oil contained in the discharged gas and return it directly to the compressor. The oil returns to the crankcase and raises the oil temperature, and when restarting after a long stop, the liquid refrigerant that condensed in the low-temperature separator is returned to the compressor, causing the oil to bubble and cause lubrication failure. There was a risk that this could occur. In addition, due to slight differences in compressor capacity and suction piping resistance, a pressure difference occurs in the compression element chamber of a surface compressor, which tends to cause the oil level of the compressor to become unbalanced during operation. There were drawbacks such as difficulty in checking the oil level position through the oil window and maintenance work.
この発明は、上記欠点を除去すべくなされたもので、以
下、この発明の一実施例を図によって説明する。すなわ
ち、図において、(1)、(2)は第1及び第2の半密
閉形圧縮機、(1a)(2a)はこの圧縮機(1) (
2)のクランクケースで、この中には隔壁(lb)(2
b)によりモータ室(1c)(2c)と圧縮要素室(l
d)(2d)として区画形成されている。(le)(2
e)、(If)(2f)は各各モータ室(lc)(2c
)、圧縮要素室(ld)(2d)に収容されたモータ及
び圧縮要素であるー (1g82g)は両要素(1eX
2e)、(1fX2f)をそれぞれ接続するクランク軸
、(xh)(2h)は隔壁(lb)(2b)の上部に設
けられた均圧用差圧弁で、起動時のようにモータ室(1
cX2c)の圧力が圧縮要素室(1d)(2d)の圧力
よりも著しく低くなるようなとき閉となる。This invention was made to eliminate the above-mentioned drawbacks, and one embodiment of the invention will be described below with reference to the drawings. That is, in the figure, (1) and (2) are the first and second semi-hermetic compressors, and (1a) and (2a) are the compressors (1) (
2) crankcase, inside which is the bulkhead (lb) (2).
b), the motor chambers (1c) (2c) and the compression element chamber (l
d) It is sectioned as (2d). (le) (2
e), (If) (2f) are each motor chamber (lc) (2c
), the motor and compression element housed in the compression element chamber (ld) (2d) - (1g82g) are both elements (1eX
2e), (1f
It closes when the pressure in cX2c) becomes significantly lower than the pressure in the compression element chambers (1d) (2d).
(li)(2i)は隔壁(lb ) (2b )の下部
に設けた均油用逆止弁で、モータ室(1cX2c)底部
の油溜(1jX2j)から圧縮室(1dX2d)底部の
油溜(1に02k)−”sのみ油の流入を許容するもの
である。(3)は面圧縮機(1) (2)の圧縮要素室
(ld ) (2d ’)を連通ずる均圧均油管、(4
)はこの均圧均油管(3)に設けられ、第1の圧縮機(
1)の圧縮要素室(1d)より第2の圧縮機Q)の圧縮
要素室(2d)−Sのガスの流れを塞化する逆止弁であ
る。(li) (2i) is a check valve for oil equalization installed at the bottom of the partition wall (lb) (2b), which allows the oil to flow from the oil sump (1jX2j) at the bottom of the motor chamber (1c Only 02k)-"s in 1 is allowed to inflow oil. (3) is a pressure equalizing oil pipe that communicates the compression element chambers (ld) (2d') of the surface compressor (1) (2), (4
) is provided in this pressure equalizing oil pipe (3), and the first compressor (
This is a check valve that blocks the flow of gas from the compression element chamber (1d) of 1) to the compression element chamber (2d)-S of the second compressor Q).
(5)は周知のアキュムレータ(9)を介して蒸発器(
図示せず)に接続された冷凍サイクルの吸入管、(6)
はこの吸入管(5)の上部と第1の圧縮機(1)のモー
タ室(1c)とを接続する第1の圧縮機(1)の吸入分
岐管、(7)は吸入管(5)の下部と第2の圧縮機(2
)のモー々室(2c)とを接続する第2の圧縮機(2)
の吸入分岐管で、吸入管(5)の分岐点から面圧縮機(
1) (2)のモータ室(ic)(2c)入口までの圧
力損失を(第1の圧縮機(1)の吸入分岐管(6)の圧
力損失)≧(第2の圧縮機(2)の吸入分岐管(7)の
圧力損失)の関係に設けている。(5) is connected to the evaporator (
refrigeration cycle suction pipe connected to (not shown), (6)
is a suction branch pipe of the first compressor (1) that connects the upper part of this suction pipe (5) and the motor chamber (1c) of the first compressor (1), and (7) is a suction pipe (5). and the second compressor (2
) and the second compressor (2) connected to the motor chamber (2c) of
The suction branch pipe (5) connects the surface compressor (
1) The pressure loss to the motor chamber (IC) (2c) inlet of (2) (pressure loss of the suction branch pipe (6) of the first compressor (1)) ≧ (second compressor (2) (pressure loss of the suction branch pipe (7)).
また吸入分岐管(6) (7)は吸入管(5)に対し、
上述したように上下部より分lすることにより吸入管(
5)内を流通する冷媒ガスが潤滑油とガスとに分離する
分離手段(5a)を構成している。(8)は面圧縮機(
1) (2)の共通吐出管で、油分離器OQを介して凝
縮器(イ)、膨張弁(図示せず)を介して蒸発器(図示
せず)に接続されている。油分離器a0の中には油面を
検知するフロート(1oa)とフロート(10a)の動
きにより開閉する針弁(10b)が設けられ、返送油は
返油管(ロ)を介して吸入側のアキュムレータ(9)内
へ接続されている。返油管(ロ)には、凝縮器μsから
吸入管(5)の温度によって制御される弁及び膨張装置
を介して液冷媒を吸入側のアキュムレータ(9)内へ噴
射する配管装置α壕が接続されている。In addition, the suction branch pipes (6) and (7) are connected to the suction pipe (5),
As mentioned above, the suction pipe (
5) It constitutes a separation means (5a) that separates the refrigerant gas flowing therein into lubricating oil and gas. (8) is a surface compressor (
1) The common discharge pipe of (2) is connected to the condenser (A) via the oil separator OQ, and to the evaporator (not shown) via the expansion valve (not shown). The oil separator a0 is equipped with a float (1oa) that detects the oil level and a needle valve (10b) that opens and closes according to the movement of the float (10a), and the return oil is sent to the suction side through the oil return pipe (b). Connected into the accumulator (9). The oil return pipe (b) is connected to a piping device α trench that injects liquid refrigerant from the condenser μs into the accumulator (9) on the suction side via a valve and expansion device controlled by the temperature of the suction pipe (5). has been done.
次に動作について説明する。面圧縮機CI) (2)が
運転されているときは、面圧縮機(1) (2)の吸入
分岐管(6) (7)の配管抵抗の差により第1の圧縮
機(1)と第2の圧縮機(2)の運転圧力の関係は、(
第2の圧縮機(2)のモータ室(2c狂力)−(第1の
圧縮機(1)のモータ室(IC)圧力)=約100〜4
00 mmAqとなっている。また、通常、冷媒循環量
の0,5%程度含まれた油は冷媒サイクルの吸入管(5
)内を蒸発した冷媒ガスと共に圧縮機(1) (2)側
へ戻ってくる。この時、分離手段(5a)によって冷媒
ガスは潤滑油とガスとに分離され、この油の大部分は重
力の影響で第2の圧縮機(2)の吸入分岐管(7)へ流
入し、第2の圧縮機(2)のモータ室(2c)、均油逆
止弁(21)を通り、圧縮要素室(2dト供給される。Next, the operation will be explained. When the plane compressor CI) (2) is in operation, due to the difference in piping resistance between the suction branch pipes (6) and (7) of the plane compressors (1) and (2), The relationship between the operating pressure of the second compressor (2) is (
Second compressor (2) motor chamber (2c madness) - (first compressor (1) motor chamber (IC) pressure) = approximately 100 to 4
00 mmAq. In addition, oil containing about 0.5% of the refrigerant circulation amount is normally contained in the refrigerant cycle suction pipe (5.
) returns to the compressor (1) and (2) side together with the evaporated refrigerant gas. At this time, the refrigerant gas is separated into lubricating oil and gas by the separation means (5a), and most of this oil flows into the suction branch pipe (7) of the second compressor (2) under the influence of gravity. The oil is supplied to the compression element chamber (2d) through the motor chamber (2c) and oil equalizing check valve (21) of the second compressor (2).
油は、面圧縮機(1) (2)の圧縮要素室=(ld)
(2d殖;均圧均油管(3)により均圧され、かつ、面
圧縮機(1) (2)のモータ室(lc)(2c)間は
前述の如く差圧があるので、第2の圧縮機(2)の圧縮
要素室(2d)より、第1の圧縮機(1)の圧縮要素室
(1d)へ流れたガスと共に流れるため均圧均油管(3
)及び逆止弁(4)を通り第1の圧縮機(1)の圧縮要
素室(1dト供給され正常に潤滑機能をはだすことが出
来る。The oil is in the compression element chamber of the surface compressor (1) (2) = (ld)
(2d reproduction: The pressure is equalized by the pressure equalization oil pipe (3), and there is a pressure difference between the motor chambers (lc) and (2c) of the surface compressors (1) and (2) as described above, so the second The pressure equalizing pipe (3) flows together with the gas flowing from the compression element chamber (2d) of the compressor (2) to the compression element chamber (1d) of the first compressor (1).
) and the check valve (4), the compression element chamber (1d) of the first compressor (1) is supplied to the compression element chamber (1d), so that the lubricating function can be performed normally.
次に、第1の圧縮機(1)だけが運転する場合、吸入管
(5)より冷媒ガスは第1の圧縮機(1)の吸入分岐管
(6)よりモータ室(1cト流入する。この間の配管の
圧力損失により約600rrmAQ程度圧力低下する。Next, when only the first compressor (1) is operated, refrigerant gas flows into the motor chamber (1c) from the suction pipe (5) through the suction branch pipe (6) of the first compressor (1). During this time, the pressure decreases by about 600 rrmAQ due to pressure loss in the piping.
また、圧縮要素室(1d)の圧力も均圧差圧弁(1h)
の作用で低下する。一方、油は吸入管(5)より、第2
の圧縮機(2)の吸入分岐管(7)、モータ室(2c)
、均油逆止弁(21)を介して圧縮要素室(2d外流入
するが、第2の圧縮機(2)は運転していないため吸入
分岐管(7)の圧力損失は極めて少ないため第1の圧縮
機(1)の圧縮要素室(1d)の圧力Pldと第2の圧
縮機(2)の圧縮要素室(2d)の圧力PgdはPld
<P!6となり、第2の圧縮機(2)の圧縮要素室(2
d)に溜った油の一部は圧力差により第1の圧縮機(1
)の圧縮要素室(1d)へ供給され、正常に運転を続け
ることが可能である。In addition, the pressure in the compression element chamber (1d) is also controlled by the equalization differential pressure valve (1h).
It decreases due to the action of On the other hand, oil is supplied from the suction pipe (5) to the second
Suction branch pipe (7) of compressor (2), motor room (2c)
, flows out of the compression element chamber (2d) through the oil equalizing check valve (21), but since the second compressor (2) is not operating, the pressure loss in the suction branch pipe (7) is extremely small. The pressure Pld in the compression element chamber (1d) of the first compressor (1) and the pressure Pgd in the compression element chamber (2d) of the second compressor (2) are Pld
<P! 6, and the compression element chamber (2) of the second compressor (2)
d) Some of the oil accumulated in the first compressor (1
) is supplied to the compression element chamber (1d), allowing normal operation to continue.
次に、第2の圧縮機(2)だけが運転した場合、冷媒ガ
スと油は吸入管(5)より第2の圧縮機(2)の吸入分
岐管(7)を経てモータ室(2cト流入する。この間に
配管の圧力損失により第2の圧縮機(2)のモータ室(
2c)の圧力は約400mnAq程度圧力低下する。一
方、均圧均油管(3)に逆止弁(4)がない場合、停止
中の第1の圧縮機(1)の吸入分岐管(6)より第1の
圧縮機(1)のモータ室(1c)、均油逆止弁(li
)、圧縮要素室(ld)、均油管(3)を介して、運転
中の第2の圧縮機(2)の圧縮要素室(2のへガスが流
入し、圧力を高め第2の圧縮機(2)の均油逆止弁(2
1)を閉とし、せっかくモータ室(2c)まで戻った油
を圧縮要素室(20へ移動することが不可能であり、短
時間に油不足による潤滑不良を発生する可能性があった
が、この発明では10ormIAq程度で作用する逆止
弁(4)を均油管(3)に設けているため第1の圧縮機
(1)から第2の圧縮機(2)の圧縮要素室(20への
ガスの流入が阻止され、圧縮要素室(2d)の圧力は均
圧差圧弁(2h)の作用でほぼモータ室(2c)と同一
レベルに維持される。従って、モータ室(2υへ戻った
油を圧縮要素室(20へ送り込むことが可能となり、第
2の圧縮機(2)の連続運転を行っても、油面を比較的
安定させた運転を行うことが出来る。Next, when only the second compressor (2) is operating, the refrigerant gas and oil are passed from the suction pipe (5) to the motor room (2c) through the suction branch pipe (7) of the second compressor (2). During this time, due to pressure loss in the piping, the motor chamber of the second compressor (2) (
The pressure in 2c) decreases by about 400 mnAq. On the other hand, if the pressure equalizing oil pipe (3) does not have a check valve (4), the suction branch pipe (6) of the stopped first compressor (1) is connected to the motor chamber of the first compressor (1). (1c), oil equalizing check valve (li
), the compression element chamber (ld), and the oil equalizing pipe (3), gas flows into the compression element chamber (2) of the second compressor (2) in operation, increasing the pressure and increasing the pressure in the second compressor. (2) Oil equalizing check valve (2
1), it was impossible to move the oil that had returned to the motor chamber (2c) to the compression element chamber (20), and there was a possibility that lubrication failure would occur due to lack of oil in a short period of time. In this invention, a check valve (4) that operates at about 10 ormIAq is provided in the oil equalizing pipe (3), so that there is no flow from the first compressor (1) to the compression element chamber (20) of the second compressor (2). The inflow of gas is blocked, and the pressure in the compression element chamber (2d) is maintained at approximately the same level as the motor chamber (2c) by the action of the equalizing differential pressure valve (2h).Therefore, the oil returned to the motor chamber (2υ) is It becomes possible to feed the oil into the compression element chamber (20), and even if the second compressor (2) is operated continuously, the oil level can be kept relatively stable.
ところが、両圧縮機(1) (2>が運転している時に
は両圧縮機(1)(2)の吸入配管(6) (7)の吸
入抵抗の差により1又、第1の圧縮機(1)だけが運転
している時は第2の圧縮機(2)の吸入管(7)を介し
て、吸入管(5)の圧力が第1の圧縮機(1)の圧縮要
素室(1d)にかかり、第1の圧縮機(1)の圧縮要素
室(1d)とモータ室(1c)の間の均圧逆止弁(1h
)の前後に通常より大きな差圧〃)発生し、圧縮要素室
(1d)内の潤滑油の飛沫がより多く、圧力の低いモー
タ室(1c)内へ流出し、そのまま吸入ガスと共に圧縮
要素に吸入され、ガスと共に吐出管(8)へ吐出され油
上り量が増大する傾向がある。この油上り量の増大は冷
媒サイクル中の冷媒中の油含有量の増加となり吸入管(
5)中の油滞溜量の増加、負荷変動による圧縮機油面の
変動に大きく影響し、特に食品店舗のショーケース冷却
設備等の負荷変動の大きな冷凍設備では油面の大巾な変
動となり、運転上重大な問題となっているが、この発明
では圧縮機(1) (2)の吐出管(8)に油分離器四
を設け、上記条件において過大な油を分離し、返送する
ことにより、常に安定した油面で、圧縮機(1) (2
>を運転することができる。また、一般にはこの油返送
管(ロ)は圧縮機(1) (2)クランクケースの圧縮
要素室(昆)(2d)[へ返送されるのが常であるが上
記条件の如く、通常の圧縮機(1) (2)運転状態よ
りも油上り量の多い条件では高温返送油量が多く、圧縮
機(1) (2)の油温か上昇し、圧縮機(1) (2
)運転上大きな問題となるが本発明では吸入側に戻すこ
とにより吸入ガスと混合するとともに、吸入ガス温度を
検知しながら、吸入ガス温度によって制御される弁及び
全冷媒循環量に対する液噴射冷媒量の割合と液噴射配管
装置(2)なしに油分離器顛より油を返油した場合の吸
入ガス温度上昇による冷凍能力の損失割合がほぼ等しく
なるように選定された膨張装置を介して、液冷媒が吸入
ガスと混合されるようになっているので冷凍能力の損失
なしに吸入ガス温度がほぼ一定に保たれ、吸入ガス温度
とほぼ同一温度で圧縮機へ返送するため上記の如き条件
でも常に安定した油温を維持して充分に潤滑作用を発揮
し、信頼性を確保することが可能である。さらに図に示
す如く、油分離器onの返送管Q])をアキュムレータ
(9)に接続すると、万一、長期間停止後の再起動時に
おいて、冷却された油分離器QOに凝縮した液冷媒が返
送されることがあったとしてもアキュムレータ(9)内
へ液冷媒が戻るため安全である。However, when both compressors (1) (2>) are in operation, the first compressor ( 1) is in operation, the pressure in the suction pipe (5) is transferred to the compression element chamber (1d) of the first compressor (1) via the suction pipe (7) of the second compressor (2). ) and a pressure equalizing check valve (1h) between the compression element chamber (1d) and the motor chamber (1c) of the first compressor (1).
A larger pressure difference than usual occurs before and after ), and more lubricating oil droplets in the compression element chamber (1d) flow into the motor chamber (1c), where the pressure is lower, and flow directly into the compression element along with the suction gas. The oil is inhaled and discharged together with the gas into the discharge pipe (8), which tends to increase the amount of oil coming up. This increase in oil flow increases the oil content in the refrigerant during the refrigerant cycle, and the suction pipe (
5) Increase in the amount of oil accumulated in the compressor, and fluctuations in the compressor oil level due to load fluctuations, especially in refrigeration equipment with large load fluctuations such as showcase cooling equipment in food stores, the oil level will fluctuate widely. This is a serious problem in operation, but in this invention, an oil separator 4 is installed in the discharge pipe (8) of the compressor (1) (2) to separate and return excess oil under the above conditions. , the compressor (1) (2
> can drive. Generally, this oil return pipe (b) is returned to the compressor (1) (2) compression element chamber (k) (2d) of the crankcase, but under the above conditions, the oil is returned to the compressor (1) (2). Compressor (1) (2) When the amount of oil coming up is higher than the operating condition, the amount of high temperature return oil is large, the oil temperature of compressor (1) (2) rises, and compressor (1) (2)
) Although this poses a major operational problem, in the present invention, the liquid is mixed with the suction gas by returning it to the suction side, and while the suction gas temperature is being detected, the valve is controlled by the suction gas temperature and the amount of liquid injected refrigerant is determined relative to the total refrigerant circulation amount. The liquid is pumped through an expansion device that is selected so that the ratio of the loss of refrigerating capacity due to the rise in suction gas temperature when oil is returned from the oil separator without the liquid injection piping device (2) is approximately equal. Since the refrigerant is mixed with the suction gas, the suction gas temperature is kept almost constant without loss of refrigeration capacity, and the refrigerant is returned to the compressor at almost the same temperature as the suction gas temperature, so even under the above conditions, the suction gas temperature is kept almost constant. It is possible to maintain a stable oil temperature, provide sufficient lubrication, and ensure reliability. Furthermore, as shown in the figure, if the return pipe Q]) of the oil separator ON is connected to the accumulator (9), in the event of a restart after a long-term shutdown, liquid refrigerant may condense in the cooled oil separator QO. Even if the liquid refrigerant is returned, it is safe because the liquid refrigerant returns to the accumulator (9).
以上のようにこの発明によれば、一方の圧縮機に対し積
極的に冷凍9サイクル中の油をもどしながら、両圧縮機
による全運転、及び何れ応)の圧縮機による部分運転と
全ての条件において両圧縮機の油面を適正に維持するこ
とが可能であり、従来のように摺動部の焼付、油上り量
過大による冷凍能力の低下、弁部分損傷を防止すること
が出来る。As described above, according to the present invention, while actively returning oil during 9 refrigeration cycles to one compressor, full operation of both compressors, partial operation of both compressors, and all conditions. It is possible to maintain an appropriate oil level in both compressors, and it is possible to prevent seizure of sliding parts, reduction in refrigeration capacity due to excessive oil flow, and damage to valve parts as in the conventional case.
また、油分離器からの潤滑油は吸入管で冷却されたのち
、圧縮機に戻るので、充分な潤滑作用を発揮させること
ができる。Furthermore, since the lubricating oil from the oil separator is cooled in the suction pipe and then returned to the compressor, it can exert sufficient lubricating action.
図はこの発明の一実施例を示す配管図である。
図中、(1) (2)は第1及び第2の半密閉形圧縮機
、(1cX2c)はモータ室、(1dX2d)は圧縮要
素室、(3)は均圧均油配管、(4)は逆止弁、(5)
は吸入管、(5a)は分離手段、’ (6) (7)は
吸入分岐管、(10は油分離器、(2)は凝縮器である
。
代理人 葛野信−The figure is a piping diagram showing an embodiment of the present invention. In the figure, (1) and (2) are the first and second semi-hermetic compressors, (1cX2c) is the motor room, (1dX2d) is the compression element chamber, (3) is the pressure equalization oil piping, and (4) is a check valve, (5)
(5a) is the suction pipe, (5a) is the separation means, (6) (7) is the suction branch pipe, (10 is the oil separator, and (2) is the condenser. Agent: Makoto Kazuno)
Claims (1)
る隔壁の所定位置に均圧孔及び上記モータ室側から゛圧
縮要素室側へのみ油流通を許容する均油用逆止弁を有す
る第1及び第2の圧縮機を互lこ並列に配管接続したも
のにおいて、冷凍サイクルの吸入管端部にこの吸入管内
を流通する冷媒ガスを潤滑油とガスとに分離する分離手
段を配設すると共に、この分離手段で分離されたガスの
一部を上記第1の圧縮機に供給する第1の配管装置と、
上記分離された残りのガス及び潤滑油を上記第2の圧縮
機に供給する第2の配管装置と、上記両圧縮機の圧縮要
素室間を連通ずる均圧均油配管に設けられ、上記第2の
圧縮機から上記第1の圧縮機へのみ流通を許容する弁と
、上記両圧縮機の吐出配管に設けられた油分1雅器およ
び、この油分]1器で分離された潤滑油を上記吸入管に
送る返油管を設けたごとを特徴とする。並列圧縮式冷凍
装置。A partition wall that divides the inside of the crankcase into the motor chamber side and the compression element chamber side has a pressure equalization hole at a predetermined position and an oil equalization check valve that allows oil to flow only from the motor chamber side to the compression element chamber side. In a system in which the first and second compressors are connected by piping in parallel, a separation means is provided at the end of the suction pipe of the refrigeration cycle to separate the refrigerant gas flowing through the suction pipe into lubricating oil and gas. and a first piping device that supplies a part of the gas separated by the separation means to the first compressor;
A second piping device that supplies the separated remaining gas and lubricating oil to the second compressor, and a pressure-equalizing oil piping that communicates between the compression element chambers of both compressors; A valve that allows flow only from the second compressor to the first compressor, an oil component installed in the discharge piping of both compressors, and a lubricating oil separated by the oil component It is characterized by the provision of a return pipe that sends oil to the suction pipe. Parallel compression refrigeration equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9424682A JPS58210380A (en) | 1982-05-31 | 1982-05-31 | Parallel compression system refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9424682A JPS58210380A (en) | 1982-05-31 | 1982-05-31 | Parallel compression system refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58210380A true JPS58210380A (en) | 1983-12-07 |
| JPH0137598B2 JPH0137598B2 (en) | 1989-08-08 |
Family
ID=14104946
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9424682A Granted JPS58210380A (en) | 1982-05-31 | 1982-05-31 | Parallel compression system refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58210380A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02192556A (en) * | 1989-01-18 | 1990-07-30 | Mitsubishi Electric Corp | Parallel compression refrigerating plant |
-
1982
- 1982-05-31 JP JP9424682A patent/JPS58210380A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02192556A (en) * | 1989-01-18 | 1990-07-30 | Mitsubishi Electric Corp | Parallel compression refrigerating plant |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0137598B2 (en) | 1989-08-08 |
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