JPH03279683A - Multiple stage compressor - Google Patents
Multiple stage compressorInfo
- Publication number
- JPH03279683A JPH03279683A JP7691290A JP7691290A JPH03279683A JP H03279683 A JPH03279683 A JP H03279683A JP 7691290 A JP7691290 A JP 7691290A JP 7691290 A JP7691290 A JP 7691290A JP H03279683 A JPH03279683 A JP H03279683A
- Authority
- JP
- Japan
- Prior art keywords
- water
- gas
- drain
- flow
- cooler
- 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.)
- Pending
Links
- 239000000498 cooling water Substances 0.000 claims abstract description 15
- 238000001816 cooling Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 11
- 230000007797 corrosion Effects 0.000 abstract 1
- 238000005260 corrosion Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 4
- MBYLVOKEDDQJDY-UHFFFAOYSA-N tris(2-aminoethyl)amine Chemical compound NCCN(CCN)CCN MBYLVOKEDDQJDY-UHFFFAOYSA-N 0.000 description 3
- 238000010586 diagram Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
Landscapes
- Applications Or Details Of Rotary Compressors (AREA)
- Compressor (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、多段圧縮機における、各冷却器へ流す冷却水
の流し方に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method of flowing cooling water to each cooler in a multi-stage compressor.
従来の多段圧縮機における冷却水の流れは、圧縮機の吸
入温度を低くするために、まず、中間冷却器へ流し、そ
の後、後段冷却器へ流すか、あるいは、中間冷却器と後
段冷却器へ併行して流していた。In a conventional multi-stage compressor, cooling water flows first to an intercooler and then to a post-cooler, or to an intercooler and a post-cooler, in order to lower the compressor suction temperature. They were running concurrently.
上記従来技術は、より温度の低い冷却水を使用する場合
、ドレン発生量が増加する点について考慮されてからす
、中間冷却器の出口、すなわち、後段圧縮機の入口部で
、ドレンアタックによる腐食摩耗が大となるという問題
があった。The above conventional technology takes into consideration the fact that when lower temperature cooling water is used, the amount of condensate generated increases. There was a problem of increased wear.
本発明の目的は、中間段冷却器の出口でのドレンの発生
量をより少なくすることを目的としており、さらに冷却
後段冷却器のガス出口温度を低くし、より低温のガスを
提供することにある。The purpose of the present invention is to further reduce the amount of condensate generated at the outlet of the intermediate stage cooler, and further to lower the gas outlet temperature of the post-cooling stage cooler to provide lower temperature gas. be.
上記目的を達成するために、本発明の多段圧縮機の各冷
却部器へ流す冷却水を、まず、後段冷却器に流し、ここ
で熱交換され、より高温となった冷却水を中間冷却器へ
流すようにしたものである。In order to achieve the above object, the cooling water flowing to each cooling unit of the multistage compressor of the present invention is first flowed to the downstream cooler, where heat is exchanged, and the cooling water that has become higher temperature is transferred to the intercooler. It was designed to flow to
後段冷却器を通過した冷却水が中間冷却器へ流入する。 The cooling water that has passed through the post-cooler flows into the intercooler.
それによって、冷却水は、後段冷却器で熱交換され、よ
り高温となるので、中間冷却器出口のドレン発生量はよ
り少なくすることができ、トレンアタックによる後段圧
縮機の腐食摩耗をより少なくすることができる。As a result, the cooling water undergoes heat exchange in the post-cooler and reaches a higher temperature, so the amount of drain generated at the outlet of the intercooler can be reduced, which further reduces corrosive wear on the post-stage compressor due to train attack. be able to.
また、後段冷却器では、より低温の冷却水が流入するた
め、後段冷却器出口のガス温度をより低くすることがで
きる。Furthermore, since lower temperature cooling water flows into the second stage cooler, the gas temperature at the outlet of the second stage cooler can be lowered.
以下、本発明の一実施例を第1図により説明する。第1
図において、ガスは前段圧縮機1で圧縮され高温で、か
つ、高圧のガスとなり、中間段冷却器3へ流入し冷却さ
れるが、この時、ドレン、すなわち、凝縮水が発生する
のでドレン分離器5でトレンを分離排出する。しかし、
ドレン分離器ではトレンを完全に分離することは不可能
であり、トレンを含んだガスは、後段圧縮機2へ吸込ま
れる。An embodiment of the present invention will be described below with reference to FIG. 1st
In the figure, the gas is compressed by the pre-stage compressor 1 to become a high-temperature and high-pressure gas, which flows into the intermediate stage cooler 3 and is cooled. At this time, drain, that is, condensed water, is generated, so the drain is separated. The tren is separated and discharged in vessel 5. but,
It is impossible to completely separate the drain in the drain separator, and the gas containing the drain is sucked into the subsequent compressor 2.
ここでさらに高圧で、かつ、高温のガスとなり、後段冷
却器4へ流入して、冷却される。ここで発生するドレン
はトレン分離器6で分離され、ガスはドライヤ7へ流入
する。一方、ガスを冷却する冷却水は、後段冷却器4へ
流入し、後段冷却器4でガスと熱交換され、水温が上昇
した後、中間冷却器3へ流入する。本実施例によれば、
冷却水は、まず、後段冷却器4へ流入するため、後段冷
却器4のガス出口温度をより低くする効果がある。また
、中間冷却器3へ流入する冷却水は、後段冷却器4で熱
交換され水温が上昇しているため、過冷却によるドレン
の発生量をより低くする効果がある。Here, the gas becomes even more high-pressure and high-temperature gas, flows into the post-cooler 4, and is cooled. The drain generated here is separated by a drain separator 6, and the gas flows into a dryer 7. On the other hand, the cooling water that cools the gas flows into the post-cooler 4, where it exchanges heat with the gas, and after the water temperature rises, it flows into the intercooler 3. According to this embodiment,
Since the cooling water first flows into the second stage cooler 4, it has the effect of lowering the gas outlet temperature of the second stage cooler 4. In addition, since the cooling water flowing into the intercooler 3 undergoes heat exchange in the post-cooler 4 and its water temperature increases, there is an effect of lowering the amount of drain generated due to supercooling.
本発明によれば、中間冷却器のトレンの発生量をより低
くおさえることができるので、後段圧縮機のトレンアタ
ックによる腐食摩耗を防ぐことができる。また、後段冷
却器出口のガス温度はより低くおさえることができるの
で、後方に取付けられるドライヤの能力をより軽減する
ことができる。According to the present invention, since the amount of tren generated in the intercooler can be suppressed to a lower level, corrosive wear due to tren attack in the rear-stage compressor can be prevented. Furthermore, since the gas temperature at the outlet of the rear cooler can be kept lower, the capacity of the dryer installed at the rear can be further reduced.
第1図は本発明の一実施例の系統図である。
1・前段圧縮機、2・後段圧縮機、3・・・中間冷却−
4〜FIG. 1 is a system diagram of an embodiment of the present invention. 1. Pre-stage compressor, 2. Post-stage compressor, 3...Intermediate cooling-
4~
Claims (1)
て、圧縮ガスを冷却する冷却水の流れを、前記後段冷却
器から流入させ、その後、前記中間冷却器へ流すことを
特徴とする多段圧縮機。1. A multi-stage compressor including an intermediate cooler and a post-cooler, characterized in that a flow of cooling water for cooling compressed gas is introduced from the post-cooler and then flows to the intercooler. compressor.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7691290A JPH03279683A (en) | 1990-03-28 | 1990-03-28 | Multiple stage compressor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7691290A JPH03279683A (en) | 1990-03-28 | 1990-03-28 | Multiple stage compressor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03279683A true JPH03279683A (en) | 1991-12-10 |
Family
ID=13618896
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7691290A Pending JPH03279683A (en) | 1990-03-28 | 1990-03-28 | Multiple stage compressor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03279683A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009133318A (en) * | 2009-02-26 | 2009-06-18 | Hitachi Ltd | System having compressor equipped with multiple middle coolers, and cooling method |
US8240122B2 (en) | 2006-06-26 | 2012-08-14 | Hitachi, Ltd. | Cooling apparatus of a gas turbine system |
US20120291434A1 (en) * | 2010-01-25 | 2012-11-22 | Stijn Jozef Rita Johanna Janssens | Method for recovering energy |
KR20170018835A (en) * | 2014-05-16 | 2017-02-20 | 아틀라스 캅코 에어파워, 남로체 벤누트삽 | Compressor device and cooler thereby used |
CN106438373A (en) * | 2016-10-28 | 2017-02-22 | 上海英正辉环保设备有限公司 | Air atomization cooling pot and air atomization cooling technology thereof |
CN109630381A (en) * | 2019-01-09 | 2019-04-16 | 苏州佳世达电通有限公司 | Heat recovery system |
-
1990
- 1990-03-28 JP JP7691290A patent/JPH03279683A/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8240122B2 (en) | 2006-06-26 | 2012-08-14 | Hitachi, Ltd. | Cooling apparatus of a gas turbine system |
US8402735B2 (en) | 2006-06-26 | 2013-03-26 | Hitachi, Ltd. | Cooling apparatus, gas turbine system using cooling apparatus, heat pump system using cooling system, cooling method, and method for operating cooling apparatus |
JP2009133318A (en) * | 2009-02-26 | 2009-06-18 | Hitachi Ltd | System having compressor equipped with multiple middle coolers, and cooling method |
US20120291434A1 (en) * | 2010-01-25 | 2012-11-22 | Stijn Jozef Rita Johanna Janssens | Method for recovering energy |
US9976569B2 (en) * | 2010-01-25 | 2018-05-22 | Atlas Copco Airpower, Naamloze Vennootschap | Method for recovering energy |
KR20170018835A (en) * | 2014-05-16 | 2017-02-20 | 아틀라스 캅코 에어파워, 남로체 벤누트삽 | Compressor device and cooler thereby used |
CN106438373A (en) * | 2016-10-28 | 2017-02-22 | 上海英正辉环保设备有限公司 | Air atomization cooling pot and air atomization cooling technology thereof |
CN109630381A (en) * | 2019-01-09 | 2019-04-16 | 苏州佳世达电通有限公司 | Heat recovery system |
CN109630381B (en) * | 2019-01-09 | 2021-01-05 | 苏州佳世达电通有限公司 | Heat recovery system |
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