Experiments with zeolite Beta and zeolite Y demonstrate that adamantan
e and methyl adamantanes can be isolated very effectively from modem r
efinery streams by mild hydrocracking over Pt- and Pd-containing large
pore zeolites. Yield depends importantly on individual refinery crude
source and process configuration. Heavy crudes and refineries with co
nventional hydrocracking and FCC feed hydrotreater facilities are part
icularly desirable, and an ideal feed for adamantane isolation in such
a situation is the 150-250 degrees C fraction of the hydrocracker (HD
C) recycle stream. When Pt- or Pd-containing zeolite Beta was used wit
h such a stream, temperatures of some 250 degrees C and pressures belo
w 3.5 mPa (500 psig) sufficed to remove selectively well over 90% of t
he non-adamantane hydrocarbon, with little conversion of adamantanes.
High selectivity for adamantanes is attributed in large part to size-s
elective exclusion of these molecules from the pores of zeolite Beta.