quote:
Originally posted by Sushil:
Thanks for the reply. The compressor 2nd stg discharge temperature ranges from 135 to 155 degree C. We foudn hitish deposits choking the tips of lube oil ports, which in turn causes premature wear out of rider, piston rings & rod packing, due to dry run. These deposits were analysed to be Zn additives from the mineral oil. Moreover viscosity thins down at this temperature adding to the problem. I can still live with the probem, if I can stop the compressor once in 4 months. But that proves to be costly, due to flaring of gases during PM checks. I am also looking for some blended oil, i.e in between Synth & Mineral Oil. I think Diester should be selected, but Compressor OEM & Oil companies talk of PAG. We had a bad experience with PAG earlier in a similar application. Made lot of sludge, within a short span of time.
If you are looking for very high VI and good thermal stability then a water insoluble double end capped PAG meets these needs. It may not need an anti-wear package to lubricate the compressor, but if needed you could investigate phosphate anti-wear additives. The PAG should resist acidic impurities in the hydrocarbon stream much better than diester.
You don't describe the type of PAG that failed before, but it not have been built for thermal and hydrolytic stability.
PAO and alkylbenzenes are also possibilities, and may be able to be formulated with more thermally stable antiwear additives than ZDDP. The phosphates are commonly used in jet tubine engine lubricants with POE basestocks for very high thermal stability.
It seems your simplest solution may be to try a mineral oil with a more stable additive package, since most of your problems seem to be related to the ZDDP deposits.