Ethylene production by steam cracking of normal paraffins
AssigneeUop LLC
InventorsStephen W. Sohn, Lynn H. Rice, Santi Kulprathipanja
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AssigneeUop LLC
InventorsStephen W. Sohn, Lynn H. Rice, Santi Kulprathipanja
Estimating the term…
A simulated moving bed adsorptive separation process for preparing the separate feed streams charged to naphtha reforming unit and a steam cracking unit has been developed. The feed stream to the overall unit is passed into the adsorptive separation unit. The desorbent in the adsorptive separation is C12 hydrocarbons. The simulated moving bed adsorptive separation separates the components of the feed stream into a normal paraffin stream, which is charged to the steam cracking process, and non-normal hydrocarbons which are passed into a reforming zone. The desorbent is readily separated from the normal paraffin stream and from the non-normal paraffin stream and the simulated moving bed adsorption zone is operated at an A/Fn ratio of from about 0.90 to about 0.92.
A process for preparing a feedstream to be charged to a steam cracking unit producing ethylene, the process comprising:
A hydrocarbon conversion process for producing ethylene which process comprises:
A process for preparing the feedstreams to a catalytic reforming zone and to a steam cracking unit producing ethylene, which process comprises:
Dependencies are inferred from the claim text.