Delayed coking process

C - Chemistry – Metallurgy – 10 – B

Patent

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196/74

C10B 55/02 (2006.01)

Patent

CA 1284962

Abstract of the Disclosure A delayed coking process having more liquid yield and less coke yield is characterized by the absence of heavy recycle and the presence of a solvent. The feed is heated in a coker furnace and led to the coker drums where coking takes place and the vaporous effluents are passed to a fractionator from which a heavy gas oil product is removed. Process heat is conserved by indirect heat exchange of the feed with the coking products upstream of the coking furnace. A solvent or diluent is added to the feed downstream of the coking furnace. This may be either a hydrocarbon fraction such as a coker distillate, a light gas oil or another fraction having an end point below 450°C. A reactive or nonreactive gas such as nitrogen, steam, hydrogen or hydrogen sulfide, may also be added.

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