JPH01293115A - Separator - Google Patents

Separator

Info

Publication number
JPH01293115A
JPH01293115A JP12178888A JP12178888A JPH01293115A JP H01293115 A JPH01293115 A JP H01293115A JP 12178888 A JP12178888 A JP 12178888A JP 12178888 A JP12178888 A JP 12178888A JP H01293115 A JPH01293115 A JP H01293115A
Authority
JP
Japan
Prior art keywords
oil
gas
separator
filter
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
JP12178888A
Other languages
Japanese (ja)
Other versions
JPH06165B2 (en
Inventor
Norihide Saho
典英 佐保
Tadashi Takada
忠 高田
Susumu Harada
進 原田
Shintaro Sado
佐渡 慎太郎
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP12178888A priority Critical patent/JPH06165B2/en
Publication of JPH01293115A publication Critical patent/JPH01293115A/en
Priority to US07/657,269 priority patent/US5158585A/en
Publication of JPH06165B2 publication Critical patent/JPH06165B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component 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
    • F04B39/16Filtration; Moisture separation

Abstract

PURPOSE:To miniaturize the group of separators and to reduce the pressure loss and the gas leakage making the separator in such a structure that the main body is a pressure vessel having plural spaces partitioned with plural filter walls for removing liquid drops in the inner part of the separator. CONSTITUTION:The refrigerant, such as helium gas, used in a refrigerator 1, is compressed by a compressor 2 and introduced into the separator A after the compression heat is removed by a cooler 3. The gas is flowed into a 1st filter 6 in the separator A through an ejector 5, and the oil drops in the gas are separated and stored in a groove 9 and returned to the compressor 2 through an oil returning port 10 and a piping 11. As a 3rd and a 4th filters 12, 13 are concentrically disposed respectively, the gas is flowed from inner part to outer part through the filters, and the oil is caught and removed, and the remaining fine oil drops and the oil vapor contained in the gas having left the 4th filter 13 are introduced into an adsorber 4 to be adsorbed and removed by adsorbent 18, such as activated carbon.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、圧縮機用分離器に係り、特にガス圧縮機の気
液分離を行うものに好適な圧縮機用の分離器に関するも
のでおる。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a separator for a compressor, and particularly to a separator for a compressor that is suitable for separating gas and liquid in a gas compressor. .

〔従来の技術〕[Conventional technology]

従来の圧縮機ユニットの分離器1例えば、ヘリウムガス
の圧縮機ユニットの油分離器は、圧f1機内で圧縮され
るガスヘリウムが発生する圧縮熱を冷却する目的で、圧
縮機の吸入口又は、圧縮途中の油圧入口より、水冷また
は空冷式のオイルクー2によって冷却した油を注入する
。このため、圧縮機の高圧吐出ガスヘリウム中に含まれ
た高い濃度の油分を分離するため、冬濃度レベルに適し
た油分離器を個々に複数段シリーズに設け、各油分離器
間は配管で接続していた。
Conventional Compressor Unit Separator 1 For example, an oil separator in a helium gas compressor unit is used to cool down the heat of compression generated by the helium gas compressed in the pressure f1 machine. Oil cooled by a water-cooled or air-cooled oil cooler 2 is injected from the hydraulic inlet during compression. Therefore, in order to separate the high concentration of oil contained in the high-pressure helium gas discharged from the compressor, oil separators suitable for winter concentration levels are installed individually in a multi-stage series, and piping is connected between each oil separator. It was connected.

なお、この種の装置として関連するものには例えば特公
昭57−27992号公報等が挙げられる。
Note that related devices of this type include, for example, Japanese Patent Publication No. 57-27992.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上記従来技術は、油分離器の小型化の点について配慮さ
れておらず、分離濃度が異なる油分離器群及び吸着器を
各油分離器に分割しシリーズに連通していたため、各油
分離器を配管で接続する必要があシ、油分離器群が大形
化するとともに、配管が長尺化して圧力損失が増加し、
また、油分離器と配管継目とでガスリークを生じやすく
、かつ。
The above conventional technology does not take into consideration the miniaturization of oil separators, and separates oil separators and adsorbers with different separation concentrations into individual oil separators and communicates them in series. It is necessary to connect the oil separators with piping, and as the oil separator group becomes larger, the piping becomes longer and pressure loss increases.
In addition, gas leaks are likely to occur between the oil separator and piping joints.

製作工数が増加してしまうという問題があった。There is a problem in that the number of manufacturing steps increases.

また、この分離器の問題は、ガス中の油除去のみならず
、ヘリウム以外のガス中の水分、固形分の除去および液
中の固形分の除去に関しても同様に生じていた。
Furthermore, problems with this separator occur not only in the removal of oil from gases, but also in the removal of moisture and solid content from gases other than helium, and the removal of solid content from liquids.

本発明の目的は2分離器群を小形化して圧縮機ユニット
を小形化しユニット製作工数を低減させるとともに、ガ
ス圧力損失を小さく、かつ、ガスの大気へのリークを無
くすことのできる圧縮機用分離器及び吸着器を提供する
ことにある。
The purpose of the present invention is to provide a compressor separator that can miniaturize the separator group to miniaturize the compressor unit, reduce the unit manufacturing time, reduce gas pressure loss, and eliminate gas leakage to the atmosphere. The purpose of this invention is to provide a container and an adsorption device.

〔課題を解決するための手段〕[Means to solve the problem]

上記目的は1分離機器を内部に複数の液滴除去用フィル
タ壁で仕切られた複数の空間を有する圧力容器と、該フ
ィルタ群の一端に流体を導入し、他端より流体を搬出す
る手段、又は、これらに液滴及び液蒸気除去用のフィル
タ又は吸着剤等の除去手段とから構成することにより、
達成される。
The above objects include: (1) a pressure vessel having a separation device therein and a plurality of spaces partitioned by a plurality of droplet removal filter walls; a means for introducing fluid into one end of the filter group and carrying out the fluid from the other end; Or, by configuring these with a removal means such as a filter or adsorbent for removing droplets and liquid vapor,
achieved.

即ち本発明の分離器は、内部にフィルタを有し。That is, the separator of the present invention has a filter inside.

一連につながる複数個の圧力容器と、前記フィルタの一
方にガスを導入する手段と該圧力容器内に設けられ前記
フィルタを介して出たガスを前記他の圧力容器内のフィ
ルタの一方に導く手段と、このフィルタで分離した分離
物を該圧力容器外に導く手段とから成る分離手段を有す
ることを特徴とする。
A plurality of pressure vessels connected in series, means for introducing gas into one of the filters, and means provided in the pressure vessel for guiding the gas exiting through the filter to one of the filters in the other pressure vessel. and a means for guiding the separated substance separated by the filter to the outside of the pressure vessel.

尚、このフィルタ内又はフィルタ後段側に不純物を吸着
する吸着層を単段又は多段に配置することが好ましく、
また吸着層内に、不純物の移動防止用保持手段を有する
ことが望ましい。
In addition, it is preferable to arrange an adsorption layer for adsorbing impurities in a single stage or in multiple stages within this filter or on the downstream side of the filter.
Further, it is desirable to have a holding means for preventing movement of impurities in the adsorption layer.

更に同一圧力容器内において、フィルタ間にガス流路断
面の縮小部を設けないことも望ましい。
Furthermore, it is also desirable not to provide a section with a reduced cross section of the gas flow path between the filters in the same pressure vessel.

〔作用〕[Effect]

圧力容器A内に一連につながったフィルタの一方から導
入された流体は、複数のフィルタを通ジ。
Fluid introduced into pressure vessel A from one of the series of filters passes through multiple filters.

除去物を分離したのち、圧力容器A外に出て他の圧力容
器B外の分離器に流入するか、又は、前記同一圧力容器
Aの一連のフィルタの後に配設した吸着剤等を通シ、蒸
気状の除去物を除去した後。
After the removed material is separated, it exits the pressure vessel A and flows into a separator outside another pressure vessel B, or it is passed through an adsorbent or the like placed after a series of filters in the same pressure vessel A. , after removing the vaporous waste.

圧力容器A外に排出する。これによって、油分離器群を
継ぐ配管又は、これに加えて油吸着器への配管を省略で
きるので、油分離器群を小形化して。
Discharge outside pressure vessel A. This allows the piping connecting the oil separator group or the piping to the oil absorber to be omitted, making the oil separator group more compact.

圧縮機ユニットを小形化でき、ユニット製作工数を低減
させるとともに、ガス圧力損失を小さく。
The compressor unit can be made smaller, reducing unit manufacturing time and reducing gas pressure loss.

かつ、ガスの大気へのリークを無くすことができる。ま
た、この時、フィルタで分離した油等は。
Moreover, leakage of gas into the atmosphere can be eliminated. Also, at this time, the oil etc. separated by the filter.

フィルタ壁で仕切られた複数の空間に溜り2別々に、又
は21ケ所に捕集され、圧力容器A外に排出され、圧縮
機に戻すことも可能である。
It is also possible to collect the stagnation 2 separately in a plurality of spaces partitioned by filter walls or at 21 locations, discharge it outside the pressure vessel A, and return it to the compressor.

〔実施例〕〔Example〕

以下、本発明の一実施例を第1図により説明する。 An embodiment of the present invention will be described below with reference to FIG.

冷凍機1で使用する冷媒例えばガスヘリウムは、圧縮機
2で加圧され、クーラ3で圧縮熱を排除した後、圧縮@
2の入口又は内部で混入した液状不純物1例えば5水や
油等を除去する分離器3に流入する。ヘリウムガスは分
離器3で滴状の不純物を分離した後、吸着器4で蒸気状
の油等を吸着し。
The refrigerant used in the refrigerator 1, such as gas helium, is pressurized by the compressor 2, and after removing the heat of compression by the cooler 3, it is compressed @
It flows into a separator 3 which removes liquid impurities 1, such as water and oil, mixed in at the inlet or inside of 2. After separating droplet-like impurities from the helium gas in a separator 3, an absorber 4 adsorbs vaporized oil and the like.

高圧の不純度ガスヘリウムとして冷凍機1に供給され、
冷凍機1内で断熱膨張等により寒冷を発生した後、低圧
ガスヘリウムは、圧縮機2に戻る。
It is supplied to the refrigerator 1 as high-pressure impure gas helium,
After generating cold in the refrigerator 1 by adiabatic expansion or the like, the low pressure gas helium returns to the compressor 2.

油分離器3内においてガスは、エジェクタ5を通り、第
1フイルタ6に流入する。ガス中の油滴は例エバクラス
ファイバ製の円筒状の第1フイルタ6を通過する過程で
ガスから分離され、油8は。
In the oil separator 3 , the gas passes through the ejector 5 and flows into the first filter 6 . The oil droplets in the gas are separated from the gas in the process of passing through a cylindrical first filter 6 made of Eva class fiber, for example, and the oil 8 is.

第2フイルタ7との間下部に設けた溝9内に溜まり、油
戻り口10を通シ、配管11により圧縮機2内に戻る。
The oil collects in a groove 9 provided in the lower part between the oil and the second filter 7, passes through the oil return port 10, and returns to the compressor 2 through the pipe 11.

分離器3内には、第3フイルタ12及び第4フイルタ1
3を内蔵し、各々、同心円状  ′に配置している。フ
ィルタの下部は、フランジ14で固定支持し、上部は、
ホルダ15.16で支持しており、ホルダ16はホルダ
15と一体化している。各々のフィルタ間は、フランジ
及びホルダで端部をシールしており、ガスは、内から外
に向ってフィルタを通過する過程で油滴はフィルタに捕
捉され、フィルタ外側下部に溜り、油接き管17,18
.18’を通じて、フィルタ外に排出される。本実施例
では1分離善人口部に設けたエジェクタ背圧12に油接
き管17,18.18’を連通し、ガスの流れによって
生じる吸引作用を利用し、第1フイルタ入口部に分離し
た油を戻している。これは各油接き管を圧縮機2の吸込
側に連結しても良い。第4フイルタを出たガス中には。
Inside the separator 3, a third filter 12 and a fourth filter 1 are installed.
3 built-in, each arranged in a concentric circle. The lower part of the filter is fixedly supported by a flange 14, and the upper part is
It is supported by holders 15 and 16, and holder 16 is integrated with holder 15. The ends between each filter are sealed with flanges and holders, and as the gas passes through the filters from the inside to the outside, oil droplets are captured by the filters and accumulate at the bottom of the outside of the filters, causing oil droplets to flow through the filters. tubes 17, 18
.. It is discharged out of the filter through 18'. In this embodiment, the oil-wetted pipes 17, 18, and 18' are connected to the ejector back pressure 12 provided in the 1-minute good port section, and by utilizing the suction effect generated by the gas flow, the ejector back pressure 12 is separated into the first filter inlet section. Returning oil. This may be done by connecting each oil wetting pipe to the suction side of the compressor 2. In the gas leaving the 4th filter.

粒径0.1μm以下程度の細粒と油蒸気のみが残留する
。これらの油分は1分離器用口17と連通した吸着器4
中の例えば活性炭18等の吸着材に工って吸着除去され
る。これら吸着剤からは微粉末が発生し易いので、グラ
スファイバ等のフィルタ19を設けることにより、ガス
中に該微粉末が同伴しない様にしている。
Only fine particles with a particle size of about 0.1 μm or less and oil vapor remain. These oils are transferred to the adsorber 4 which communicates with the separator port 17.
The particles are adsorbed and removed by an adsorbent such as activated carbon 18 inside. Since these adsorbents tend to generate fine powder, a filter 19 made of glass fiber or the like is provided to prevent the fine powder from being entrained in the gas.

油分離器内のガスの流れは1円筒状フィルタを通過する
のみで、フィルタから次のフィルタには。
The gas flow in the oil separator only passes through one cylindrical filter and from one filter to the next.

従来の様な、流路面積の大巾な縮小、拡大が無くガス流
動による圧力損失が、非常に小さい。
Unlike conventional methods, there is no large reduction or expansion of the flow path area, and pressure loss due to gas flow is extremely small.

本実施例によれば、多段のフィルタを円心状に同一油分
離容器内に配置でき、かつ、フィルタ間下部に溜った油
を圧縮機まで戻すことができるので、低圧力損失の小形
分離器を小形に、すなわち。
According to this embodiment, multi-stage filters can be arranged in a circular manner in the same oil separation container, and the oil accumulated in the lower part between the filters can be returned to the compressor, resulting in a small separator with low pressure loss. into a smaller size, ie.

これを内蔵する圧縮機ユニットを小形にできるとともに
、分離器内におけるガスの圧力損失を小さくでき、かつ
、同一容器内に複数段フィルタ収納容器を有しているの
で、従来の複数フィルタ収納容器部が無く、これらの容
器間を連絡する配管も不要となり、ガスの大気へリーク
を低減するとともに、当然、製作工数も低減できる効果
がある。
The compressor unit that incorporates this can be made smaller, the pressure loss of the gas in the separator can be reduced, and since multiple filter storage containers are included in the same container, it is possible to reduce the size of the compressor unit that incorporates this. This eliminates the need for piping to communicate between these containers, which reduces leakage of gas into the atmosphere, and naturally reduces manufacturing man-hours.

第2図は本発明になる他の実施例を示すもので。FIG. 2 shows another embodiment of the present invention.

第1図と異なる点は、油分離器に収めるフィルタを平板
状にした点にある。すなわち、平板状のフィルタ20,
21,22.23は、スペーサ24を介して、入口側7
ランジ25及びボルト26で。
The difference from FIG. 1 is that the filter housed in the oil separator is shaped like a flat plate. That is, the flat filter 20,
21, 22, and 23 are connected to the inlet side 7 via the spacer 24.
With lunge 25 and bolt 26.

出口側7ランジ27に固定されている。各々フィルタ間
に形成された空間下部に、油抜き孔27゜28.29.
30を設け、油抜き孔27は1分離器3の内側空間31
に連通、2段目以降の油抜き孔28,29.30は、イ
ンジェクタ5の背圧孔32と配管33で連通している。
It is fixed to the outlet side 7 flange 27. At the bottom of the space formed between each filter, there are oil drain holes 27°, 28°, 29°.
30, and the oil drain hole 27 is connected to the inner space 31 of the separator 3.
The oil drain holes 28, 29, and 30 of the second and subsequent stages communicate with the back pressure hole 32 of the injector 5 through a pipe 33.

多量に油を含んだガスは、インジェクタ5より分離器3
に流入し。
Gas containing a large amount of oil is transferred from the injector 5 to the separator 3.
flowed into.

各フィルタで油を分離した後、高純度なガスとなって出
口17より分離器3を出る。空間31は。
After the oil is separated by each filter, it becomes a highly pure gas and exits the separator 3 through the outlet 17. Space 31 is.

油戻し孔34を圧縮機の低圧又は中圧部と連結すること
に:す、フィルタ間の圧力よりも低く調整されている。
The oil return hole 34 is connected to the low pressure or intermediate pressure part of the compressor, and is adjusted to be lower than the pressure between the filters.

したがって1分離した油は、油抜き孔27より、空間3
1底部に溜り、油戻し孔34より圧縮機に戻る。
Therefore, the oil that has separated by
1 and returns to the compressor through the oil return hole 34.

本実施例によれば、平板状のフィルタで多段の油分離器
を構成できるので、より小形となり、かつ、同一サイズ
のフィルタで構成できるので、製造コストがより低減で
きる。また、分離油の横置きできる効果がある。なお1
本実施例では、油抜き孔28,29,30を空間31に
直接連通させてもよい。
According to this embodiment, since a multi-stage oil separator can be constructed using flat filters, the oil separator can be made smaller, and can be constructed using filters of the same size, so that manufacturing costs can be further reduced. It also has the effect of allowing separated oil to be placed horizontally. Note 1
In this embodiment, the oil drain holes 28, 29, and 30 may be directly communicated with the space 31.

第3図は1本発明になる他の実施例を示すもので、第2
図と異なる点は、中央部が球面の平板状フィルタ35,
36,37.38を配置、かつ。
FIG. 3 shows another embodiment of the present invention.
The difference from the figure is that the flat filter 35 has a spherical center portion,
Place 36, 37, and 38, and.

油戻し孔34の開閉をフロート39付きのニードル弁体
40″”r調節するフロート弁を設けた点にある。本実
施例では、フィルタに球面設けたことにより1本分離器
を縦置きで使用しても分離した油は、外周側に移動でき
、フィルタ中央部に停溜せず、通過するガスに油滴が同
伴することが無く。
A float valve is provided to adjust the opening and closing of the oil return hole 34 using a needle valve body 40''r with a float 39. In this example, by providing a spherical surface on the filter, even if one separator is used vertically, the separated oil can move to the outer periphery and not accumulate in the center of the filter, causing oil droplets to drop onto the gas passing through. without being accompanied.

安定し九分離性能を確保できる効果がある。また。It has the effect of ensuring stable and nine-separation performance. Also.

フロート弁を設けることにより、空間31の下部に一定
量の油が溜った後、油のみ圧縮機に戻すことが出来、ガ
スのバイパス量を無くすことにより。
By providing a float valve, after a certain amount of oil has accumulated in the lower part of the space 31, only the oil can be returned to the compressor, thereby eliminating the amount of gas bypass.

圧縮機吐出ガスをすべて冷凍機側に供給できる効果があ
る。
This has the effect of supplying all the compressor discharge gas to the refrigerator side.

第4図は、本発明による他の実施例を示すもので、第1
図と異なる点は、油回収機能を有した分離器3と、吸着
器4を一体化し、同一圧力容器   ′41内に収納し
た点にある。すなわち、フィルタ9の外周部に、吸着剤
18の微粉末混入防止用フィルタ42及び、ガス出口4
3側に、吸着剤18の微粉末飛散防止用フィルタ44を
設けた点にある。本実施例によれば1分離器と吸着器を
同一容器で構成できるので、圧縮機ユニットをより小形
に、かつ、製作コストを低減でき、かつ1分離器と吸着
器間の配管を無くすことができるので、圧力損失の低減
とガスリークを低減できる効果がある。
FIG. 4 shows another embodiment according to the present invention.
The difference from the figure is that the separator 3 with an oil recovery function and the adsorber 4 are integrated and housed in the same pressure vessel '41. That is, a filter 42 for preventing fine powder of the adsorbent 18 from being mixed in, and a gas outlet 4 are provided on the outer periphery of the filter 9.
A filter 44 for preventing scattering of fine powder of the adsorbent 18 is provided on the third side. According to this embodiment, the 1st separator and the adsorber can be configured in the same container, so the compressor unit can be made smaller and the manufacturing cost can be reduced, and piping between the 1st separator and the adsorber can be eliminated. This has the effect of reducing pressure loss and gas leaks.

第5図は1本発明による他の実施例を示すもので、第4
図と異なる点は、フィルタの代pに、ファイバー単体を
充てんした点で1分離善人口5から流入したガスは、中
央部の通気孔45から充てんファイバ46内に流れ込み
、半径方向に流動して行く過程で油が分離し油はファイ
バを伝って下部方向に移動し、溝付きの油抜き孔47,
48゜49.50より分離外に排出され、それぞれ圧縮
機に回収される。油濃度が低減したガスは、バッフル5
1の外周部より。吸着材18の充てん層に流入し、さら
に油濃度を低減する。
FIG. 5 shows another embodiment according to the present invention.
The difference from the diagram is that the filter section p is filled with a single fiber, so that the gas flowing from the 1 minute good population 5 flows into the filled fiber 46 from the central ventilation hole 45 and flows in the radial direction. During the process, the oil separates and moves downward along the fiber, forming a grooved oil drain hole 47,
48°49.50 are discharged to the outside of the separation, and each is recovered by a compressor. The gas with reduced oil concentration is transferred to baffle 5.
From the outer periphery of 1. It flows into the packed layer of adsorbent 18 and further reduces the oil concentration.

本実施例では、フィルタの代りにクラスファイバ単体を
高密度に充てんして油分離器を構成できるので、フィル
タ間の空間部がなく、さらに小形化できる効果がある。
In this embodiment, since the oil separator can be configured by densely packing single class fibers instead of filters, there is no space between the filters, which has the effect of further downsizing.

第6図は1本発明による他の実施例を示すもので、第4
図と異なるのは、吸着剤18をファイバー等の保水性材
料52で多段に分離した点にあり。
FIG. 6 shows another embodiment according to the present invention.
The difference from the diagram is that the adsorbent 18 is separated in multiple stages using a water-retaining material 52 such as fiber.

吸着した油が、低濃度の吸着剤に油の重量等で移動する
のを防止できる効果がある。また、微粉末を分散してト
ラップできるので、フィルタの目づまりの集中を防止で
きる効果が生じる。なお、本効果は、第1図中に示した
吸着器単体に適用しても同等の効果を生じる。
This has the effect of preventing the adsorbed oil from moving to the low-concentration adsorbent due to the weight of the oil. Furthermore, since fine powder can be dispersed and trapped, there is an effect of preventing the concentration of clogging of the filter. Note that the same effect is produced even when this effect is applied to the adsorber shown in FIG. 1 alone.

〔発明の効果〕〔Effect of the invention〕

本発明によれば1分離器自にコンパクトに複数段の分離
用フィルタを内蔵でき、かつ、フィルタ間で分離した不
純物を回収でき、かつ、圧縮機と分難器間の油戻し管全
通してのバイパスガス流量を低減できるので、分離器自
体及び圧縮機ユニット内の器類及び配管のコンパクト化
、圧縮機ユニット吐出流量の低減を防止できる効率の向
上、及び1分離器自体及び圧縮機ユニットの製作コスト
を低減できる効果がある。
According to the present invention, it is possible to compactly incorporate multiple stages of separation filters in one separator itself, to recover impurities separated between the filters, and to completely pass the oil return pipe between the compressor and the separator. This reduces the bypass gas flow rate of the separator itself and the compressor unit, making the equipment and piping in the separator itself and the compressor unit more compact, improving efficiency by preventing a reduction in the discharge flow rate of the compressor unit, and increasing the efficiency of the separator itself and the compressor unit. This has the effect of reducing production costs.

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

第1図は本発明の実施例に係る圧縮機ユニットの構成を
示す系統図、第2図、第3図は夫々本発明の他の実施例
に係る圧縮機ユニットに用いる分離器の断面図、第4図
、第5図、第6図は夫々本発明の他の実施例に係る圧縮
機ユニットに用いる分離器及び吸着器の断面図である。 1・・・冷凍増、2・・・圧縮機、3・・・ターラ、4
・・・吸着器、5・・・エジェクタ、6・・・第1フイ
ルタ、7・・・第2フイルタ、8・・・油、9・・・溝
、10・・・油戻90711・・・配管、12・・・第
3フイルタ、13・・・第4フイルタ、14,25・・
・フランジ、15.16・・・ホルダ、17,18.1
8’・・・油抜き管、19゜20、 21. 22. 
23. 35,36,37゜38.42.44・・・フ
ィルタ、24・・・スペーサ。 26・・・ボルト、27,28,29,30,47゜4
8.49.50・・・油抜き孔、31・・・内側空間、
32・・・背圧孔、34・・・油戻し孔、39・・・フ
ロート。 40・・・ニードル弁体、41・・・圧力容器、51・
・・バッフル。
FIG. 1 is a system diagram showing the configuration of a compressor unit according to an embodiment of the present invention, FIGS. 2 and 3 are sectional views of a separator used in a compressor unit according to other embodiments of the present invention, respectively. FIG. 4, FIG. 5, and FIG. 6 are sectional views of a separator and an adsorber used in a compressor unit according to other embodiments of the present invention, respectively. 1... Refrigeration increase, 2... Compressor, 3... Tara, 4
...Adsorber, 5...Ejector, 6...First filter, 7...Second filter, 8...Oil, 9...Groove, 10...Oil return 90711... Piping, 12...Third filter, 13...Fourth filter, 14, 25...
・Flange, 15.16...Holder, 17, 18.1
8'...Oil drain pipe, 19°20, 21. 22.
23. 35, 36, 37° 38.42.44... Filter, 24... Spacer. 26...Volt, 27, 28, 29, 30, 47°4
8.49.50...Oil drain hole, 31...Inner space,
32... Back pressure hole, 34... Oil return hole, 39... Float. 40... Needle valve body, 41... Pressure vessel, 51...
...baffle.

Claims (1)

【特許請求の範囲】[Claims] 1、内部にフィルタを有し、一連につながる複数個の圧
力容器と、前記フィルタの一方にガスを導入する手段と
、前記圧力容器内に設けられ前記フィルタを介して出た
ガスを前記他の圧力容器内のフィルタの一方に導く手段
と、該フィルタで分離した分離物を該圧力容器外に導く
手段とから成る分離手段を有した分離器。
1. A plurality of pressure vessels each having a filter therein and connected in series; a means for introducing gas into one of the filters; and a means for introducing gas into one of the filters; 1. A separator having a separating means comprising means for guiding a substance separated by the filter to one side of a filter in a pressure vessel, and means for guiding a separated substance separated by the filter to the outside of the pressure vessel.
JP12178888A 1988-04-13 1988-05-20 Separator for compressor Expired - Lifetime JPH06165B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP12178888A JPH06165B2 (en) 1988-05-20 1988-05-20 Separator for compressor
US07/657,269 US5158585A (en) 1988-04-13 1991-02-19 Compressor unit and separator therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12178888A JPH06165B2 (en) 1988-05-20 1988-05-20 Separator for compressor

Publications (2)

Publication Number Publication Date
JPH01293115A true JPH01293115A (en) 1989-11-27
JPH06165B2 JPH06165B2 (en) 1994-01-05

Family

ID=14819909

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12178888A Expired - Lifetime JPH06165B2 (en) 1988-04-13 1988-05-20 Separator for compressor

Country Status (1)

Country Link
JP (1) JPH06165B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010516991A (en) * 2007-01-18 2010-05-20 アース トゥ エア システムズ,エルエルシー Multi-surface direct exchange geothermal heating / cooling system
JP2012531305A (en) * 2009-07-02 2012-12-10 オーリコン レイボルド バキューム ゲーエムベーハー Multistage oil separator
JP2014037333A (en) * 2012-08-16 2014-02-27 Japan Pionics Co Ltd Ammonia purification method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010516991A (en) * 2007-01-18 2010-05-20 アース トゥ エア システムズ,エルエルシー Multi-surface direct exchange geothermal heating / cooling system
JP2012531305A (en) * 2009-07-02 2012-12-10 オーリコン レイボルド バキューム ゲーエムベーハー Multistage oil separator
JP2014037333A (en) * 2012-08-16 2014-02-27 Japan Pionics Co Ltd Ammonia purification method

Also Published As

Publication number Publication date
JPH06165B2 (en) 1994-01-05

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