Ben,
Thanks for your response...
The comp seal water flow back to the ocmpressor is being supplied by head pressure from a 2 phase sep...
The spongy I refered to is the amount of HC in the water, mainly C3 and C4...The comp seal provides additional energy to the water on the final rotation of compression, less than 30 degrees of rotation...if the water is "spongy" the machine cannot develop the head and cannot get into the amine contactor system...we do not believe the issues is with the compressor, the issue is with the anncillary system that supports the machines.
We are operating the LR compressors on the edge of of available technology as far as pressure ratio, in my opinion.
My team is preparing a KT analysis of the system next week, using the failure and trip data from the last three months.
We feel the problem is with the 2 phase sep on the discharge of the compressor, inadquate design as far as retention time....
Hence the initial posting, looking for an expert on LR system design and trouble shooting the system.
We are all real close to the fire right now and third eye looking at the system, not knowing the past history of the system, project and operating issues would have been good.
I did not mean to offend anyone here, but it appears I have done so, even accused of poor writing skills. Interesting!!!