relentlessratt
Mechanical
- Mar 1, 2010
- 31
can someone provide advice about this service?
i am having frequent seal failures with large amounts of coke buildup in all areas of a double seal. the plans are plans 41/52. coke was found in the primary and the backup seal bellows,faces, pumping ring, gland ports etc.
the product is cooled from 620 F in the heat exchanger to the outlet temperature of about 300 F. is this flush temperature too high? maybe the product is coking with increased temperature generated by seal faces. the seal components are designed for high temperature service with solids - graphalloy packings, hard faces, inconel 718 bellows assembly.
the product has coke chips - the reason for the cyclone separator. other than the coke, faces seem to be in okay condition when disassembled.
i am thinking to go to a plan 32/52. The flush material is compatible but very expensive.
i am having frequent seal failures with large amounts of coke buildup in all areas of a double seal. the plans are plans 41/52. coke was found in the primary and the backup seal bellows,faces, pumping ring, gland ports etc.
the product is cooled from 620 F in the heat exchanger to the outlet temperature of about 300 F. is this flush temperature too high? maybe the product is coking with increased temperature generated by seal faces. the seal components are designed for high temperature service with solids - graphalloy packings, hard faces, inconel 718 bellows assembly.
the product has coke chips - the reason for the cyclone separator. other than the coke, faces seem to be in okay condition when disassembled.
i am thinking to go to a plan 32/52. The flush material is compatible but very expensive.