<p>A side by side hydrocarbon conversion-two staged stacked catalyst regeneration arrangement is provided wherein the first stage of catalyst regeneration is temperature restricted to achieve incomplete removal of carbon deposits and a second higher temperature regeneration is accomplished in an upflowing catalyst contact system under conditions to accomplish removal of residual carbon on the catalyst and produce a CO2 rich flue gas. A special external cyclone separator arrangement may be attached to either of the second stage regeneration operationor the riser hydrocarbon conversion operation to effect separation of catalyst particles from gasiform material.</p>
申请公布号
CA1156591(A)
申请公布日期
1983.11.08
申请号
CA19800357965
申请日期
1980.08.11
申请人
DEAN, ROBERT R.;MAULEON, JEAN-LOUIS;PFEIFFER, ROBERT W.
发明人
DEAN, ROBERT R.;MAULEON, JEAN-LOUIS;PFEIFFER, ROBERT W.