By Gurevich B. M., Tempelman A. A.
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Integrating DCC technology into existing refineries as either a grassroots or revamp application can offer an attractive opportunity to produce large quantities of light olefins. In a market requiring both proplylene and ethylene, use of both thermal and catalytic processes is essential, due to the fundamental differences in the reaction mechanisms involved. The combination of thermal and catalytic cracking mechanisms is the only way to increase total olefins from heavier feeds while meeting the need for a increased propylene to ethylene ratio.
Deasphalted oil separator recovers solvent at supercritical conditions (2) and asphalt flash (3) recovers solvent. Products are steam stripped (4, 5). Operating conditions: Typical ranges are: solvent, various blends back to main menu of C2–C7 hydrocarbons including light naphthas. Pressure, 300 to 600 psig. , 120°F to 450°F. Solvent/oil ratio, 4/1 to 13/1. S. 8 Steam, 150 psig, lb 116 11 Water, cooling (25°F rise), gal 15 nil Installation: 42 units. , McGraw-Hill, 1997, pp. 44. Licensor: Foster Wheeler USA Corp.
Description: Catalytic and selective cracking in a short-contact-time riser (1) where oil feed is effectively dispersed and vaporized through a proprietary feed injection system. Operation is carried out at a temperature consistent with targeted yields. Reaction products exit the riser-reactor through a high-efficiency, proprietary riser termination device (2). Spent catalyst that has not been cooled is pre-stripped and back to main menu flows through a rapid preliminary stripping section, followed by a high-efficiency baffled stripper prior to regeneration.