PTT
Mechanical
- Dec 12, 2006
- 7
Dear all,
We use a gear pump on a polymer transfer line. The suction pressure on this pumps is 8 PSIg and the discharge pressure is 110 PSIg. We use a John Crane double mechanical seal with a barrier fluid. The pressure of the barrier fluid is 80 PSIg. We experienced a failure of this seal and the polymer has leaked into the barrier fluid system. It's obvious that the barrier fluid pressure is not enough to keep the polymer inside the pump in case of seal failure. To calculate the stuffing box pressure on a centrifugal pump we generaly use this equation:
Stuffing Box press.= Suction press. + 10% differential press. (25% for non-API pump)
Is there any equation to calculate or evaluate the stuffing box pressure for a gear pump stuffing box???
Thanks a lot!
PTT
We use a gear pump on a polymer transfer line. The suction pressure on this pumps is 8 PSIg and the discharge pressure is 110 PSIg. We use a John Crane double mechanical seal with a barrier fluid. The pressure of the barrier fluid is 80 PSIg. We experienced a failure of this seal and the polymer has leaked into the barrier fluid system. It's obvious that the barrier fluid pressure is not enough to keep the polymer inside the pump in case of seal failure. To calculate the stuffing box pressure on a centrifugal pump we generaly use this equation:
Stuffing Box press.= Suction press. + 10% differential press. (25% for non-API pump)
Is there any equation to calculate or evaluate the stuffing box pressure for a gear pump stuffing box???
Thanks a lot!
PTT