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Production of synthesis gas and related products via the cracking of heavy oil feeds

Patent ·
OSTI ID:6961634
In a process for cracking a heavy oil feed having a Conradson carbon number above 2 wt. % and being a member selected from the group consisting of topped crudes, reduced crudes, vacuum bottoms, heavy asphaltic crudes, coal crude oils, shale oils, and tar sands oil products, which process comprises contacting in a riser cracking zone the heavy oil feed with a fluid hydrocarbon cracking catalyst to form products comprising gasoline and coke on catalyst, the coke containing hydrogen, and thereafter regenerating the catalyst in a regeneration zone by removing at least a portion of the coke to provide as regenerated catalyst, and passing the regenerated catalyst to the cracking zone, the improvement is described which comprises: A. cracking of the heavy oil feed in a progressive flow riser cracking zone at an outlet temperature of about 950/sup 0/F to 1150F in the substantial absence of added molecular hydrogen and for a period of time within the range of 0.5 second to 4 seconds and in the presence of the catalyst; B. separating the coked catalyst from the gasiform effluent and regenerating the coked catalyst in a regeneration zone consisting of a first regeneration stage and a second regeneration stage; C. separating the gasiform efficient into the hydrocarbon products, the hydrogen-rich gaseous product, and the second water condensation product; and D. treating the hydrogen-rich gaseous product to remove the ammonia and the acidic components therefrom and to provide a purified hydrogen-rich gaseous product.
Assignee:
Ashland Oil, Inc., Ashland, KY
Patent Number(s):
US 4744883
OSTI ID:
6961634
Country of Publication:
United States
Language:
English