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Production of heavier hydrocarbons from light olefins in multistage catalytic reactors

Patent ·
OSTI ID:6385234
This patent describes a continuous multistage catalytic process for conversion of light olefins to distillate range of hydrocarbons rich in C/sub 10/ + aliphatics, comprising the steps of: maintaining a fluidized bed of medium pore acid zeolite catalyst particles in a primary reaction stage in a turbulent reactor bed maintained under reaction severity conditions effective to convert a primary ethene-containing olefinic feedstream by passing hot feedstock vapor upwardly through the fluidized catalyst bed at reaction severity conditions sufficient to convert ethene substantially to intermediate range olefins and aromatics in the C/sub 5/-C/sub 9/ range; recovering primary stage effluent, including a liquid stream containing a major amount of aromatics-rich C/sub 5/ + hydrocarbons; contacting a secondary olefinic feedstream comprising C/sub 3/-C-/sub 4/ olefins in a secondary catalytic reactor stage with a series of fixed catalyst bed reactors containing shape selective medium pore acid zeolite oligomerization catalyst at high pressure under distillate mode oligomerization conditions; mixing at least a portion of liquid primary stage effluent containing aromatic hydrocarbon with at least one hot inter-reactor stream containing partially upgraded olefins in the secondary stage, thereby quenching the inter-reactor stream.
Assignee:
Mobil Oil Corp., New York, NY
Patent Number(s):
US 4788366
OSTI ID:
6385234
Country of Publication:
United States
Language:
English