This compressor oil flow case study by Kevin D. Yates, a rotating equipment specialist at The Dow Chemical Company in Freeport, Texas, was presented at the 42nd Turbomachinery Symposium in Texas. The case study is about a new motor-gear-compressor train installation in which the lube oil pressure became an issue during commissioning and startup.
Installation: Field installation supervised by owner and general contractor. Lube oil console inspected for cleanliness and debris. Piping installed after inspections. All deficiencies were corrected. No known issues prior to commissioning.
Commissioning: Oil pressure design target on compressor deck is 1.2 bar / 17.5 psig. Upstream pressure control valve adjusted to its maximum travel to achieve only ~16.5-17 psig on the deck. Excessive oil return flow observed in return sight glasses. Was the LOC undersized? Was the oil supply short circuiting the machine?
Troubleshooting: Thorough field inspection vs. the P&ID’s was conducted. The LOC valve sizes were compared to design. The LOC witness test run reports were reviewed. Rundown tank check valve was inspected and verified. The lube oil pumps were inspected with rotation checks and pressure confirmation. No issues found in any of these.
Additional testing was needed. Ultrasonic oil flow tests were conducted on lube oil piping. Individual flows were measured at all available supply and return lines. Data results suggested excessive flow to the compressor thrust bearing. Oil flow to the thrust bearing was 2-3 x design.
Reviewed ultrasonic oil flow data with the compressor OEM. Thrust bearing oil flow = 2-3 x design flow Other supply flows were within expected ranges. Reviewed oil flow requirements and P&ID’s vs. test stand report. Compressor test run at the OEM factory was based on an oil supply pressure of 0.4 bar / 6.09 psig. Actual lube oil system design was based on 17.5 psig bearing supply pressure.
Resolution: Compressor OEM recommended an external orifice plate be added upstream of the thrust bearing. Dow agreed with the recommended solution and installed the orifice plate. Lube oil system restarted and pressures were found to be within the expected design parameters. The pressure control valve range was back within expected target. Compressor was successfully commissioned and started up. No oil leaks were observed. Vibration and bearing temperatures were acceptable.
Lessons learned: Internal OEM communication gap existed due to multiple team player involvement (Auxiliary System Team Vs. Compressor Design Team, Geographical Distance, Etc.). Need to verify that the test stand lube oil pressure is in agreement with the train design during document reviews. Need to shop verify test stand conditions vs. job order as another check and balance.
SATORP Awards Ebara Elliott Energy Equipment Supply Contract for Petrochemical Complex
December 6th 2024Ebara Elliott Energy will deliver 22 units across its compressor, pump, and turbine product lines to the AMIRAL project—a refinery equipped with a mixed-feed cracker and petrochemical units.