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1
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arbainmahmood
Mechanical
- Apr 21, 2008
- 4
Hello, anybody out there has any experience in expander - compressor failure?
Ours is Rotoflow, 4 stage expander - compressor configuration, H2 service in ethylene plant. In July 2008 we experienced a catastrophic failure in Unit-A, both expander & compressor wheel broken into pieces. Normal speed 44,000 rpm for unit A~C & D is 28,000-30,000 rpm. Pressure drop across unit A ~ D normally from 30 barg to 4 barg, temp from -90 deg C to - 160 eg C. It failed during routine start up & during manual loading of unit C just after unit D was in auto mode. Unit A went overspeed to > 61,000 rpm, it did not trip on overspeed, but tripped on high vibration, apart from inadequacy of intrumentation to detect impending overspeed tripping, the IGV was later checked & confirmed OK. What caused it to overspeed? Any comment/input very much appreciated. TQ
Ours is Rotoflow, 4 stage expander - compressor configuration, H2 service in ethylene plant. In July 2008 we experienced a catastrophic failure in Unit-A, both expander & compressor wheel broken into pieces. Normal speed 44,000 rpm for unit A~C & D is 28,000-30,000 rpm. Pressure drop across unit A ~ D normally from 30 barg to 4 barg, temp from -90 deg C to - 160 eg C. It failed during routine start up & during manual loading of unit C just after unit D was in auto mode. Unit A went overspeed to > 61,000 rpm, it did not trip on overspeed, but tripped on high vibration, apart from inadequacy of intrumentation to detect impending overspeed tripping, the IGV was later checked & confirmed OK. What caused it to overspeed? Any comment/input very much appreciated. TQ