wouldn't an approach be to:
1)Create a balanced reaction for the decomp of this compond including gaseous and non-gaseous products
2)Calculate mMole of each gaseous product in your reaction
3)use patial pressures to develop your pressures at each increment of time over the reaction.
I think you...
Try checking with manufacturers of air bladders for semi-tractor air shocks, or call a few garages that service semi-tractors and maybe the mechanic can give you a suppliers name. As was mentioned in the above post, there are companies that supply them for the rescue and salvage/rigging industry
I found a table in "Perry's" a while ago. It has all the formulae for different head types. If you have a copy of the design prints, they sometimes have the areas listed. A final option would be to ask your vessel supplier. Are you calculating heat transfer coefficents?
Mike
IPA would be a better degreaser. It is intermediate in polarity vs. the polar acetone. Now you have to weigh vapor pressures IPA's is greater and less volatile relative to acetone and would require a longer drying cycle or N2/inert gas purge period. I would also implement a QC test to check that...
