Mineral oils: processes and products – Chemical conversion of hydrocarbons – Cracking
Patent
1992-05-04
1995-02-14
Myers, Helane
Mineral oils: processes and products
Chemical conversion of hydrocarbons
Cracking
208113, 208 48Q, C10G 1302
Patent
active
053892321
ABSTRACT:
A process for catalytically cracking a heavy feed in a single riser reactor FCC unit, with delayed riser quench and large amounts of shape selective cracking additive is disclosed. The feed is preferably quenched after at least 1 second of riser cracking. The catalyst inventory preferably contains over 3.0 wt % ZSM-5 cystal, in the form of an additive of 12-40% ZSM-5 on an amorphous support. Quenching with recycled LCO is preferred. Delayed quenching, with this catalyst system, produces unexpectedly large amounts of C3/C4 olefins, with little or no increase in coke make.
REFERENCES:
patent: 3758403 (1973-09-01), Rosinski et al.
patent: 4764268 (1988-08-01), Lane
patent: 4818372 (1989-04-01), Mauleon et al.
patent: 5019239 (1991-05-01), Owen
patent: 5043058 (1991-08-01), Forgac et al.
patent: 5087349 (1992-02-01), Goelzer et al.
Adewuyi Yusuf G.
Adornato Peter M.
Johnson David L.
Teitman Gerald L.
Keen Malcolm D.
McKillop Alexander J.
Mobil Oil Corporation
Myers Helane
Stone Richard D.
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