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JPH03279683A - Multiple stage compressor - Google Patents

Multiple stage compressor

Info

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
Application number
JP7691290A
Other languages
Japanese (ja)
Inventor
Junji Okita
沖田 純二
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 JP7691290A priority Critical patent/JPH03279683A/en
Publication of JPH03279683A publication Critical patent/JPH03279683A/en
Pending legal-status Critical Current

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  • Applications Or Details Of Rotary Compressors (AREA)
  • Compressor (AREA)

Abstract

PURPOSE:To prevent corrosion wear due to drain attack by letting flow cooling water for respective coolers at first to a post cooler, exchanging heat there, and letting flow the cooling water raised to high temperature to an intercooler. CONSTITUTION:Gas is compressed in a pre-stage compressor 1 to become gas of high temperature and high pressure and let flow into an intercooler 3 to be cooled. At this time, condensed water is generated and drain water is separated with a drain separator 5 and drained. But the drain water cannot be completely separated with the drain separator 5, and the gas containing drain water is sucked into a post stage compressor 2. Hereat, gas of further high pressure and high temperature is generated, and let flow into a post cooler 4 to be cooled. Drain water generated here is separated with a drain separator 6, and gas is let flow into a dryer 7. Meanwhile, cooling water to cool gas is let flow into the post cooler 4, heat is exchanged between gas and water in the post cooler 4, and after rise of water temperature the water is let flow into the intercooler 3.

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.

〔従来の技術〕[Conventional technology]

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.

〔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、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.

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

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

〔作用〕[Effect]

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.

〔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。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.

〔発明の効果〕〔Effect of the invention〕

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.

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

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)

【特許請求の範囲】[Claims] 1、中間段冷却器と後段冷却器を含む多段圧縮機におい
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.
JP7691290A 1990-03-28 1990-03-28 Multiple stage compressor Pending JPH03279683A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (9)

* Cited by examiner, † Cited by third party
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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