Transalkylation of heavy aromatic hydrocarbon feedstocks

摘要

In a process for producing xylene by transalkylation of a C9+ aromatic hydrocarbon feedstock with a C6 and/or C7 aromatic hydrocarbon, the C9+ aromatic hydrocarbon feedstock, at least one C6 and/or C7 aromatic hydrocarbon and hydrogen are contacted with a first catalyst comprising (i) a first molecular sieve having a Constraint Index in the range of about 3 to about 12 and (ii) at least first and second different metals or compounds thereof of Groups 6 to 12 of the Periodic Table of the Elements. Contacting with the first catalyst is conducted under conditions effective to dealkylate aromatic hydrocarbons in the feedstock containing C2+ alkyl groups and to saturate C2+ olefins formed so as to produce a first effluent. At least a portion of the first effluent is then contacted with a second catalyst comprising a second molecular sieve having a Constraint Index less than 3 under conditions effective to transalkylate C9+ aromatic hydrocarbons with said at least one C6-C7 aromatic hydrocarbon to form a second effluent comprising xylene.

主权项

1. A catalyst system comprising:
(a) a first catalyst bed comprising (i) a first molecular sieve having a Constraint Index in the range of about 3 to about 12 and (ii) at least one metal selected from platinum, palladium, iridium, and rhenium, in an amount between about 0.001 and about 5 wt % of the first catalyst, and at least one metal selected from copper, silver, gold, ruthenium, iron, tungsten, molybdenum, cobalt, nickel, tin and zinc, in an amount between about 0.001 and about 10 wt % of the first catalyst; and (b) a second catalyst bed comprising (i) a second molecular sieve having a Constraint Index less than 3 and (ii) at least one metal selected from platinum, palladium, iridium, and rhenium, in an amount between about 0.001 and about 5 wt % of the second catalyst, and at least one metal selected from copper, silver, gold, ruthenium, iron, tungsten, molybdenum, cobalt, nickel, tin and zinc, in an amount between about 0.001 and about 10 wt % of the second catalyst; wherein the weight ratio of said first catalyst to said second catalyst is in the range of about 5:95 to about 75:25 and wherein said first catalyst bed is located upstream of said second catalyst bed when the catalyst system is brought into contact with said C9+ aromatic hydrocarbon feedstock and said C6-C7 aromatic hydrocarbon in the presence of hydrogen; (c) a third catalyst bed comprising a third molecular sieve having a Constraint Index in the range of about 3 to about 12, said catalyst system further characterized as comprising, in series, said first catalyst bed, then said second catalyst bed, then said third catalyst bed.