I am in the process of checking the adequacy of seal flush plan for BB5 pump pumping condensate hydrocarbon.The pump will also pump produced water at times. The current selection of seal plan is API 11/52. The Pump has a limited NPSH margin of 1.3m. Is API 11/52 the optimal plan for the selected application or should a pressurized seal plan API 11/53B be required?
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API 11/52 Seal Plan selection
- Thread starter Selva1111
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