A polyimide membrane manufactured from a co-polymer of diaminophenylindane
with benzophenone tetracarboxylic dianhydride has been shown to have excell
ent chemical resistance and economically viable flux and rejection characte
ristics for the separation of light hydrocarbon solvents from lube oil filt
rates. This asymmetric membrane was subjected to a series of bench scale hy
perfiltration studies. After 2 months of continuous high pressure tests, th
e membrane demonstrated recovery of chilled solvent (a mixture of methyl et
hyl ketone and toluene at -10 degreesC) from the lube filtrates at a purity
of better than 99% with a steady permeate rate. When a membrane system is
combined with a conventional solvent lube dewaxing process, significant inc
reases in energy efficiency and solvent recovery capacity are realized. Sub
sequently, this work led to the installation of a commercial membrane plant
designed for a maximum feed rate of 11 500 cubic meters per day (72 000 ba
rrels per day) at Mobil's Beaumont, Texas refinery. This process, trademark
ed MAX-DEWAX(R), provides a low capital method for expansion of solvent dew
axing units and is available for licensing. (C) 2000 Elsevier Science B.V.
All rights reserved.