JPH0353032Y2 - - Google Patents
Info
- Publication number
- JPH0353032Y2 JPH0353032Y2 JP1985024352U JP2435285U JPH0353032Y2 JP H0353032 Y2 JPH0353032 Y2 JP H0353032Y2 JP 1985024352 U JP1985024352 U JP 1985024352U JP 2435285 U JP2435285 U JP 2435285U JP H0353032 Y2 JPH0353032 Y2 JP H0353032Y2
- Authority
- JP
- Japan
- Prior art keywords
- stage
- oil
- compressor
- gas
- lubricating oil
- 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
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Description
【考案の詳細な説明】
(産業上の利用分野)
本考案は、多段スクリユ圧縮機等の多段回転容
積形圧縮機(以下、単に多段圧縮機という)に関
するものである。[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to a multistage rotary positive displacement compressor (hereinafter simply referred to as a multistage compressor) such as a multistage screw compressor.
(従来の技術)
従来、この種の多段圧縮機において、多段の圧
縮機は無給油式又は給油式のどちらかのみの組合
わせが用いられている。(Prior Art) Conventionally, in this type of multi-stage compressor, a combination of either a non-lubricated type or an oil-filled type of multi-stage compressor has been used.
すなわち、無給油式のみの組合わせによる多段
圧縮機は、例えば第2図に示すように、共通の駆
動機Mを有する各無給油式圧縮機1a,1b,1
cと、その吐出側に設けた中間冷却器2a,2b
(最終段にあつては後方冷却器3)とから構成さ
れ、前段からの吐出ガスを中間冷却器2a,2b
で冷却して次段の吸込側に導き、最終段より後方
冷却器3を通して所定の消費温度に冷却した後、
図示しない消費箇所に送るようになつている。 That is, a multi-stage compressor that is a combination of only oil-free compressors is, for example, as shown in FIG.
c, and intercoolers 2a and 2b provided on the discharge side thereof.
(rear cooler 3 in the case of the final stage), and the discharge gas from the previous stage is transferred to intercoolers 2a and 2b.
After being cooled and guided to the suction side of the next stage, and cooled to a predetermined consumption temperature through the rear cooler 3 from the final stage,
It is designed to be sent to a consumption point (not shown).
給油式のみの組合わせによる多段圧縮機は、例
えば第3図に示すように、共通の駆動機Mを有す
る各給油式圧縮機4a,4bと、その吐出側に設
けた油分離器5a,5bおよび中間冷却器2c
(最終段にあつては後方冷却器3)とから構成さ
れている。そして、前段からの吐出ガスを油分離
器5aにて潤滑油と分離するとともに、中間冷却
器2cで冷却して次段の吸込側に導き、最終段か
らの吐出ガスを油分離器5bにて潤滑油と分離
し、後方冷却器3を通して所定の消費温度に冷却
した後、図示しない消費箇所に送るようになつて
いる。 For example, as shown in FIG. 3, a multi-stage compressor that is a combination of only oil-fed compressors includes oil-fed compressors 4a and 4b having a common drive M, and oil separators 5a and 5b provided on the discharge side thereof. and intercooler 2c
(In the case of the final stage, a rear cooler 3). Then, the discharged gas from the previous stage is separated from the lubricating oil in an oil separator 5a, cooled in an intercooler 2c, and guided to the suction side of the next stage, and the discharged gas from the final stage is passed to an oil separator 5b. After being separated from the lubricating oil and cooled to a predetermined consumption temperature through a rear cooler 3, it is sent to a consumption point (not shown).
また、油分離器5a,5bにて分離された潤滑
油は、直前の給油式圧縮機4a,4bに戻され循
環使用される。 Furthermore, the lubricating oil separated by the oil separators 5a and 5b is returned to the immediately preceding oil-supplied compressors 4a and 4b for circulation.
(考案が解決しようとする問題点)
ところで、前記両形式の圧縮機本体(以下、単
に本体という。)は、それぞれ一長一短があり、
それぞれの特徴に適した分野で利用されている。(Problems to be solved by the invention) By the way, both types of compressor main bodies (hereinafter simply referred to as main bodies) have their own advantages and disadvantages.
They are used in fields suited to their respective characteristics.
このうち、無給油式圧緒機の長所は、圧縮ガス
中に注油による不純物質が混入することがないこ
とである。しかし、反面、この形式のものは、例
えばスクリユ圧縮機では雌雄ロータ間等に一定の
〓間が存在するため、ガス圧縮過程において高圧
部分より低圧部分へのガスの逆流が生じ、それだ
け圧縮効率が低下するという短所を有している。 Among these, the advantage of the oilless cord press is that impurities caused by oiling do not get mixed into the compressed gas. However, on the other hand, in this type of compressor, for example, there is a certain gap between the male and female rotors, so gas backflows from the high-pressure part to the low-pressure part during the gas compression process, which reduces the compression efficiency. It has the disadvantage that it decreases.
一方、給油式圧縮機の長所は、例えばスクリユ
圧縮機ではガス圧縮過程で歯形間および歯形とロ
ータ室の壁面との間に潤滑油が充填されることに
より、ガスの洩れ量が小さいため、圧縮効率がよ
いことである。また、潤滑油の温度を低くして、
冷却剤として使用することにより、圧縮ガスの温
度を下げて圧縮効率を改善することができる。 On the other hand, the advantage of an oil-filled compressor is that, for example, in a screw compressor, lubricating oil is filled between the teeth and between the teeth and the wall of the rotor chamber during the gas compression process, so the amount of gas leakage is small. It is efficient. Also, by lowering the temperature of the lubricating oil,
By using it as a coolant, it is possible to lower the temperature of the compressed gas and improve compression efficiency.
これに対して、この給油式圧縮機の短所は、本
体からの吐出ガス中に前記潤滑油が混入するの
で、この潤滑油を分離する油分離器等の分離装置
が必要となることである。また、潤滑油がガス圧
縮過程において、以下のような悪影響を及ぼすこ
とがある。 On the other hand, the disadvantage of this oil-fed compressor is that the lubricating oil is mixed into the gas discharged from the main body, so a separation device such as an oil separator is required to separate this lubricating oil. Additionally, lubricating oil may have the following adverse effects on the gas compression process.
その第1は、本体の吸込圧力が比較的低い場
合、潤滑油の蒸発量も多くなり、これが実際に圧
縮した吸込ガス中に混入して、実質的にこの吸込
ガスの吸込量を減少させて、本体の性能低下を招
く。また、ガス圧縮時の温度上昇によつても潤滑
油の蒸発量が増えるので、これによつても上記同
様に本体の性能が低下する。 The first is that when the suction pressure of the main body is relatively low, the amount of lubricating oil that evaporates increases, which actually mixes into the compressed suction gas and substantially reduces the suction amount of this suction gas. , leading to a decrease in the performance of the main unit. Further, the amount of evaporation of lubricating oil also increases due to the temperature rise during gas compression, and this also causes the performance of the main body to deteriorate in the same manner as described above.
第2は、通常本体への吸込ガス温度が潤滑油温
度より低いため、本体に吸込まれる前に潤滑油に
より吸込ガスの加熱、膨張が生じ、吸込ガス量が
減少して本体の性能が低下する。 Second, since the temperature of the suction gas to the main body is usually lower than the lubricating oil temperature, the lubricating oil causes the suction gas to heat and expand before it is sucked into the main body, reducing the amount of suction gas and deteriorating the performance of the main body. do.
第3は、給油式のものでは、潤滑油と吸込ガス
とを本体にて圧縮した後吐出し、分離装置にて圧
縮ガスから潤滑油を分離して、これを圧縮機の低
圧部すなわち吸込口あるいはその近傍に再度供給
して循環使用している。ところが、通常潤滑油へ
のガス溶解量は高圧力、低温度である程、増大す
る傾向にあるため、上記のように高圧力下で分離
した潤滑油を低圧部に供給したとき、潤滑油中の
溶解ガスのボイルオフが起こり、吸込ガスの量が
減少して、本体の性能が低下する。 Thirdly, in the oil supply type, the lubricating oil and suction gas are compressed in the main body and then discharged, the lubricating oil is separated from the compressed gas in the separator, and the lubricating oil is transferred to the low pressure part of the compressor, that is, the suction port. Alternatively, it can be resupplied to nearby areas for cyclical use. However, the amount of gas dissolved in lubricating oil tends to increase as the pressure and temperature decrease, so when lubricating oil separated under high pressure is supplied to a low pressure section as described above, Boil-off of dissolved gas occurs, reducing the amount of suction gas and reducing the performance of the main body.
さらに、前記無給油式のみの組合わせによる多
段圧縮機では、特に、圧力比が比較的高い場合
(圧力比10以上)において、段数が多くシステム
が複雑で高価になるとともに、高段での動力性能
が悪くなるという問題点を有している。 Furthermore, in a multi-stage compressor that is a combination of oil-free type only, the number of stages is large, making the system complex and expensive, especially when the pressure ratio is relatively high (pressure ratio 10 or more), and the power consumption at the high stages is also high. This has the problem of poor performance.
これに対し、給油式のみの組合わせによる多段
圧縮機では、段数が少なくなるものの、低段の給
油式圧縮機4a及び油分離器5a等が非常に大型
となつて高価であり、場合によつては、無給油式
のみの組合わせによるものに比べて低段動力性能
が悪くなるという問題点を有している。 On the other hand, in a multi-stage compressor that is a combination of only oil-fed compressors, the number of stages is reduced, but the low-stage oil-fed compressor 4a, oil separator 5a, etc. are very large and expensive, and in some cases However, there is a problem in that the low-stage power performance is worse than that of a combination of only non-lubricated types.
本考案は、斯る問題点に鑑みてなされたもの
で、無給油式と給油式の圧縮機を組合わせること
により、両者の短所による圧縮性能低下への影響
を小さくするとともに、両者の長所を兼ね備えた
多段圧縮機を提供することを目的とする。 The present invention was developed in view of these problems, and by combining a non-lubricated type compressor and a lubricated type compressor, it is possible to reduce the influence of the deterioration of compression performance due to the disadvantages of both, and to take advantage of the advantages of both. The purpose is to provide a multi-stage compressor with the following functions.
(問題点を解決するための手段)
前記問題点を解決するため、本考案に係る多段
圧縮機は、低段側に無給油式圧縮機を、高段側に
給油式圧縮機を設けたものである。(Means for Solving the Problems) In order to solve the above-mentioned problems, the multi-stage compressor according to the present invention is provided with an oil-free compressor on the lower stage side and an oil-filled compressor on the higher stage side. It is.
(実施例)
次に、本考案の一実施例を第1図に基づいて説
明する。(Example) Next, an example of the present invention will be described based on FIG.
第1図は、2段スクリユ圧縮機を示し、共通の
駆動機Mを有する第1段の無給油式スクリユ圧縮
機1及び第2段の給油式スクリユ圧縮機4と、第
1段の吐出側に設けた中間冷却器2と、第2段の
吐出側に設けた油分離器5及び後方冷却器3とか
ら構成されている。そして、第1段からのオイル
フリー吐出ガスを中間冷却器2で冷却して第2段
の吸込側に導き、第2段からの吐出ガスを油分離
器5にて潤滑油と分離するとともに、後方冷却器
3を通して所定の消費温度に冷却した後、図示し
ない消費箇所に送るようになつている。また、油
分離器5にて分離された潤滑油は、第2段の給油
式スクリユ圧縮機4に戻され循環使用可能になつ
ている。 FIG. 1 shows a two-stage screw compressor, including a first-stage oil-free screw compressor 1 and a second-stage oil-filled screw compressor 4 having a common drive machine M, and a first-stage discharge side. It consists of an intercooler 2 provided on the second stage, an oil separator 5 and a back cooler 3 provided on the discharge side of the second stage. Then, the oil-free discharge gas from the first stage is cooled by an intercooler 2 and guided to the suction side of the second stage, and the discharge gas from the second stage is separated from lubricating oil by an oil separator 5. After being cooled to a predetermined consumption temperature through the rear cooler 3, it is sent to a consumption location (not shown). Furthermore, the lubricating oil separated by the oil separator 5 is returned to the second stage oil supply type screw compressor 4 so that it can be used for circulation.
このように、第1段に無給油式圧縮機1を採用
することにより、潤滑油により生じる圧縮工程で
の性能低下がなくなる。また、この第1段での圧
力差は小さいので、無給油式の欠点である歯形間
隙間からのガス洩れによる性能低下が小さく、さ
らに通常、第1段の吸込ガス温度は低いので吐出
ガス温度の上昇は小さく第2段にとつても好まし
い状態となる。 In this way, by employing the oilless compressor 1 in the first stage, performance degradation in the compression process caused by lubricating oil is eliminated. In addition, since the pressure difference in the first stage is small, there is little performance deterioration due to gas leakage from the gap between tooth profiles, which is a disadvantage of non-lubricated types.Furthermore, since the suction gas temperature in the first stage is usually low, the discharge gas temperature The rise in the temperature is small, which is a favorable condition for the second stage.
また、第2段に給油式圧縮機4を採用すること
により、この給油式圧縮機4での吸込圧力、温度
が第1段に比べて高くなつており、潤滑油による
悪影響が小さくなる一方、大きな圧力差に対して
は潤滑油のシール効果により、高性能が維持され
る。さらに、第2段は第1段より高温の吸込ガス
の供給を受けるが、潤滑油の冷却効果により、圧
縮工程でのガス温度の上昇を抑制することがで
き、給油式の長所が生かされる。 In addition, by employing the oil-fed compressor 4 in the second stage, the suction pressure and temperature in the lubricant-fed compressor 4 are higher than those in the first stage, and the negative effects of lubricating oil are reduced. High performance is maintained due to the sealing effect of lubricating oil against large pressure differences. Furthermore, although the second stage is supplied with higher temperature suction gas than the first stage, the cooling effect of the lubricating oil makes it possible to suppress the rise in gas temperature during the compression process, making the best use of the advantages of the oil supply type.
なお、前記実施例では、第1段と第2段のスク
リユ圧縮機に共通の駆動機Mを用いたが、これに
限るものではなく、第4図から第7図に示すよう
な各種の方法を用いてもよい。すなわち、第4図
に示すものは、各圧縮機1,4にそれぞれ独立の
駆動機を用いたものであり、第5図は、第1段の
低圧側と第2段の高圧側を連結して共通の駆動機
Mで駆動するものであり、第6図は、両軸駆動機
Mにて第1段と第2段のそれぞれの高圧側を駆動
するものであり、第7図は、共通の駆動機Mによ
り3軸ギア6を介して第1段と第2段の高圧側を
駆動するものである。 In addition, in the above embodiment, a common drive machine M was used for the first and second stage screw compressors, but the invention is not limited to this, and various methods as shown in FIGS. 4 to 7 may be used. may also be used. In other words, the one shown in Fig. 4 uses an independent drive machine for each compressor 1, 4, and the one shown in Fig. 5 uses an independent drive machine for each compressor 1, 4, and Fig. 5 shows one in which the low-pressure side of the first stage and the high-pressure side of the second stage are connected. Fig. 6 shows a double-shaft drive machine M that drives the high pressure side of each of the first and second stages, and Fig. 7 shows a common drive machine M. The high-pressure side of the first stage and the second stage are driven by a drive machine M via a three-axis gear 6.
(考案の効果)
以上の説明から明らかなように、本考案によれ
ば、多段圧縮機の低段側を無給油式とすることに
より、低段において高性能化が図られ、大形の油
分離器が不要となり、装置が小形化する。また、
高段側を給油式とすることにより、高段において
高性能化が図られ、段数が減少して装置が簡素化
される。そして、総合的に動力性能の改善と設備
費の低減を図ることができるという効果を有して
いる。(Effects of the invention) As is clear from the above explanation, according to the invention, by making the lower stage side of the multistage compressor non-lubricated, performance can be improved in the lower stage, and large oil A separator is no longer required, making the device more compact. Also,
By making the high stage side oil-supplied, high performance can be achieved at the high stage, the number of stages can be reduced, and the device can be simplified. This has the effect of comprehensively improving power performance and reducing equipment costs.
第1図は、本考案に係る多段スクリユ圧縮機の
系統図を示し、第2図及び第3図は、従来の多段
スクリユ圧縮機の系統図を示し、第4図から第7
図は、圧縮機と駆動機の組合わせ例を示す図であ
る。
1……無給油式スクリユ圧縮機、4……給油式
スクリユ圧縮機。
FIG. 1 shows a system diagram of a multi-stage screw compressor according to the present invention, FIGS. 2 and 3 show system diagrams of a conventional multi-stage screw compressor, and FIGS.
The figure is a diagram showing an example of a combination of a compressor and a drive machine. 1...Oil-free screw compressor, 4...Oil-filled screw compressor.
Claims (1)
に給油式回転容積形圧縮機を設けたことを特徴と
する多段回転容積形圧縮機。 A multi-stage rotary positive displacement compressor, characterized in that an oil-free rotary positive displacement compressor is provided on the low stage side and an oil-filled rotary positive displacement compressor is provided on the high stage side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1985024352U JPH0353032Y2 (en) | 1985-02-21 | 1985-02-21 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1985024352U JPH0353032Y2 (en) | 1985-02-21 | 1985-02-21 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61140191U JPS61140191U (en) | 1986-08-30 |
| JPH0353032Y2 true JPH0353032Y2 (en) | 1991-11-19 |
Family
ID=30518420
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1985024352U Expired JPH0353032Y2 (en) | 1985-02-21 | 1985-02-21 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0353032Y2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2966575B2 (en) * | 1991-05-29 | 1999-10-25 | 株式会社日立製作所 | Oil-free scroll compressor |
| US20150211539A1 (en) * | 2014-01-24 | 2015-07-30 | Air Products And Chemicals, Inc. | Systems and methods for compressing air |
| JP6889058B2 (en) * | 2017-07-14 | 2021-06-18 | 株式会社神戸製鋼所 | Hydrogen boosting system |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS585114U (en) * | 1981-06-29 | 1983-01-13 | 小島プレス工業株式会社 | Actuation control device |
-
1985
- 1985-02-21 JP JP1985024352U patent/JPH0353032Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61140191U (en) | 1986-08-30 |
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