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dax
Posted
how to reduce the HP gas pressure pulsation in a screw compressor
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
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You'll have re-design the silancer or install orifice plate in discharge line (energy loss).
 
Posts: 120 | Location: Baytown, TX | Registered: 17 March 2006Reply With QuoteEdit or Delete MessageReport This Post
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Run two compressors with a 180 degree phase difference in pulsations to cancel each other.
 
Posts: 45 | Location: Southeast GA | Registered: 02 March 2005Reply With QuoteEdit or Delete MessageReport This Post
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If you are talking of gas pressure pulsation itself and not vibration caused by it, then why worry at all? Pressure pulsations are practically not present in the receiver tank.
 
Posts: 980 | Location: Texas | Registered: 22 February 2005Reply With QuoteEdit or Delete MessageReport This Post
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Volumetric compressor always has pressure pulsation coming from trapped low-pressure air being released from the rotating element into the high-pressure side of the system. The momentary back flow causes shock pulse throughout the compressor. I don’t know of any system that can help other than good maintenance practice like filter cleaning, system design, load, air temperature, etc. It should not affect the reliability of the compressor.
Best regard, Marcel
 
Posts: 150 | Location: Varennes, Canada | Registered: 21 December 2005Reply With QuoteEdit or Delete MessageReport This Post
dax
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[QUOTE]Originally posted by David_G:
If you are talking of gas pressure pulsation itself and not vibration caused by it, then why worry at all? Pressure pulsations are practically not present in the receiver tank.[/QUOTE
]no that is causing a vibration of 25mm/sec pk in the initial time when taken on load,,,so some modification to be done!!
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
dax
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quote:
Originally posted by DavidM:
Run two compressors with a 180 degree phase difference in pulsations to cancel each other.

how to run with phase difference in pulsation 180 deg???system get loaded at 8 bar andunloaded at 9 bar
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
dax
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quote:
Originally posted by Alex J:
You'll have re-design the silancer or install orifice plate in discharge line (energy loss).

wat are the differnt ways of modificationthe silencer ???
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
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There are several companies I'm aware of specializing in these silencers. I know that even on new installations you can encounter a very high pulsation leading to piping vibration. As this is usually a high frequency phenomenon it's very damaging for the equipment and existing silencer if exposed to it can develop cracks. Some time silencer manufacturers are not too good and some consulting companies have to solve their design issues. I know that Engineering Dynamics from San Antonio has been working on this kind of issues.
http://www.engdyn.com/
 
Posts: 120 | Location: Baytown, TX | Registered: 17 March 2006Reply With QuoteEdit or Delete MessageReport This Post
dax
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quote:
Originally posted by Alex J:
There are several companies I'm aware of specializing in these silencers. I know that even on new installations you can encounter a very high pulsation leading to piping vibration. As this is usually a high frequency phenomenon it's very damaging for the equipment and existing silencer if exposed to it can develop cracks. Some time silencer manufacturers are not too good and some consulting companies have to solve their design issues. I know that Engineering Dynamics from San Antonio has been working on this kind of issues.
http://www.engdyn.com/

hey alex thanks for response.But suppose if i wanna modify the silencer in the site.wat are the things i shld consider?
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
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dax,

Likely you are experiencing such a high vibration on the pipes. If so, run a simple bump test and install braces if at resonance. Has it been confirmed that vibration occurs at the pressure pulsation frequency?

David
 
Posts: 980 | Location: Texas | Registered: 22 February 2005Reply With QuoteEdit or Delete MessageReport This Post
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Dax,
Changing silencer design is not such a simple thing. It depends on type of silencer (reactive, reactive/dissipative, dissipative or splitter type) and you have to understand this specific design. I would not recommend any changes to be done without good understanding or knowledge in this subject. You can create more damage.
 
Posts: 120 | Location: Baytown, TX | Registered: 17 March 2006Reply With QuoteEdit or Delete MessageReport This Post
dax
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quote:
Originally posted by Alex J:
Dax,
Changing silencer design is not such a simple thing. It depends on type of silencer (reactive, reactive/dissipative, dissipative or splitter type) and you have to understand this specific design. I would not recommend any changes to be done without good understanding or knowledge in this subject. You can create more damage.

do u have some material on the remedies of HP gas pulsation
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
dax
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quote:
Originally posted by David_G:
dax,

Likely you are experiencing such a high vibration on the pipes. If so, run a simple bump test and install braces if at resonance. Has it been confirmed that vibration occurs at the pressure pulsation frequency?

yeah this is congfirmed .Male rotor has 4 lobes and speed of 10025 rpm and peak at 40025 and 80050 rpm.

David
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
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Dax,
Could you describe some more about your issue? What compressor, what silencer, silencer location vs. discharge flange, why do you think there is a problem with pulsation, what's the frequuency vs. running speed etc?
 
Posts: 120 | Location: Baytown, TX | Registered: 17 March 2006Reply With QuoteEdit or Delete MessageReport This Post
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Dax, first of all, what Alex is trying to get at is that these problems are often not simple, and require some pretty high tech engineering analysis to fix.

Having said that I am assuming you are talking about a process gas compressor of some kind at a fairly high power, and not a little bitty air compressor sitting on a receiver.

The OEMs have some solutions, but my best experience has been with EDI as Alex recommended. There are also papers on their site on the subject.

David_G, perhaps you are not understanding the issue? The primary problem with screw compressors is high frequency pulsation and damaging levels can certainly be present in the receiver. I was recently involved with a refrig compressor that was tearing up the receiver causing ammonia release.

It is also typically much easier to reduce pulsation levels than it is to go out and bump test and detune every piece of piping, instrument line etc in the plant.


e-mail me at steven dot schultheis at gmail dot com
 
Posts: 346 | Location: Kuala Lumpur, Malaysia | Registered: 21 February 2005Reply With QuoteEdit or Delete MessageReport This Post
dax
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quote:
steven.schultheis at sbcglobal dot net

Thank u steve and alex
My compressor is a air compressor with 355kw motor.the running speed and the spectrum attached.if u see this is having a peak 40.5kcpm and at higher feqauencies 80.5kcpm(see HP female spectrum on load condition)The male rotor speed is 10098 rpm.thats y i doubt HP pulsation (see attachment given hp pulsation at 673 HZ).I also attach the schemetic wer u can see the location of the silencer .It is after the HP stage before after cooler(see attachment).So now can u help

Word DocDoc1.doc (166 Kb, 22 downloads)
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
dax
Posted Hide Post
quote:
Originally posted by Steve Schultheis:
Dax, first of all, what Alex is trying to get at is that these problems are often not simple, and require some pretty high tech engineering analysis to fix.

Having said that I am assuming you are talking about a process gas compressor of some kind at a fairly high power, and not a little bitty air compressor sitting on a receiver.

The OEMs have some solutions, but my best experience has been with EDI as Alex recommended. There are also papers on their site on the subject.

David_G, perhaps you are not understanding the issue? The primary problem with screw compressors is high frequency pulsation and damaging levels can certainly be present in the receiver. I was recently involved with a refrig compressor that was tearing up the receiver causing ammonia release.

It is also typically much easier to reduce pulsation levels than it is to go out and bump test and detune every piece of piping, instrument line etc in the plant.

see spectrum

Word Dochp_stage_pressure_pulsasion.doc (125 Kb, 20 downloads)
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
dax
Posted Hide Post
quote:
Originally posted by dax:
quote:
Originally posted by Steve Schultheis:
Dax, first of all, what Alex is trying to get at is that these problems are often not simple, and require some pretty high tech engineering analysis to fix.

Having said that I am assuming you are talking about a process gas compressor of some kind at a fairly high power, and not a little bitty air compressor sitting on a receiver.

The OEMs have some solutions, but my best experience has been with EDI as Alex recommended. There are also papers on their site on the subject.

David_G, perhaps you are not understanding the issue? The primary problem with screw compressors is high frequency pulsation and damaging levels can certainly be present in the receiver. I was recently involved with a refrig compressor that was tearing up the receiver causing ammonia release.

It is also typically much easier to reduce pulsation levels than it is to go out and bump test and detune every piece of piping, instrument line etc in the plant.

see spectrum


Word DocDoc111.doc (177 Kb, 20 downloads)
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
dax
Posted Hide Post
quote:
Originally posted by Steve Schultheis:
Dax, first of all, what Alex is trying to get at is that these problems are often not simple, and require some pretty high tech engineering analysis to fix.

Having said that I am assuming you are talking about a process gas compressor of some kind at a fairly high power, and not a little bitty air compressor sitting on a receiver.

The OEMs have some solutions, but my best experience has been with EDI as Alex recommended. There are also papers on their site on the subject.

David_G, perhaps you are not understanding the issue? The primary problem with screw compressors is high frequency pulsation and damaging levels can certainly be present in the receiver. I was recently involved with a refrig compressor that was tearing up the receiver causing ammonia release.

It is also typically much easier to reduce pulsation levels than it is to go out and bump test and detune every piece of piping, instrument line etc in the plant.
see attachmenrt

Word DocDoc111.doc (164 Kb, 18 downloads)
 
Posts: 18 | Location: delhi | Registered: 05 April 2008Reply With QuoteEdit or Delete MessageReport This Post
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