bk19702
Mechanical
- Oct 2, 2007
- 149
Hello,
I'm currently conducting a cost evaluation of some existing centrifugal compressor seal oil systems in plant. I am curious as to the amount of usable process gas that is lost across the inner labyrinth seal on either end to the sour seal oil trap. Two machines in particular have no external buffer gas injected in this area; it would be strictly the process gas leakage across the inner laby (laby between the oil film seal and process). Would a simple bushing flow calculation using the inner laby dimensions/clearances suffice? Has anyone used a different method to approximate a leakage rate in these circumstances? Thanks for your help.
I'm currently conducting a cost evaluation of some existing centrifugal compressor seal oil systems in plant. I am curious as to the amount of usable process gas that is lost across the inner labyrinth seal on either end to the sour seal oil trap. Two machines in particular have no external buffer gas injected in this area; it would be strictly the process gas leakage across the inner laby (laby between the oil film seal and process). Would a simple bushing flow calculation using the inner laby dimensions/clearances suffice? Has anyone used a different method to approximate a leakage rate in these circumstances? Thanks for your help.