Aliphatic gasoline component and process to prepare said gasoline component
AssigneeShell Oil Company
InventorJan Lodewijk Maria DIERICKX
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AssigneeShell Oil Company
InventorJan Lodewijk Maria DIERICKX
Estimating the term…
A process to prepare an aliphatic gasoline component comprising more than 90 wt % of a mixture of trimethyl substituted compounds and monomethyl substituted compounds in a weight ratio of trimethyl to monomethyl compounds of at least 0.03 and wherein the compounds may be paraffins and olefins. The invention is also directed to a process to prepare an aliphatic gasoline component by (a) contacting a Fischer-Tropsch synthesis product with a catalyst system comprising a catalyst, which catalyst comprises an acidic matrix and a large pore molecular sieve in a riser reactor at a temperature of between 450 and 650° C. at a contact time of between 1 and 10 seconds and at a catalyst to oil ratio of between 2 and 20 kg/kg, (b) isolating from the product of step (a) a gasoline fraction and a fraction comprising iso-butane and iso-butylene; (c) subjecting the iso-butane and the iso-butylene obtained in step (b) to an alkylation step to prepare a trimethyl substituted pentane, and (d) combining the gasoline fraction obtained in step (b) with the product rich in trimethyl substituted pentane as obtained in step (c).
A process to prepare an aliphatic gasoline component comprising
A process to prepare an aliphatic gasoline component comprising more than 90 wt % of a mixture of trimethyl substituted compounds and monomethyl substituted compounds in a weight ratio of trimethyl to monomethyl compounds of at least 0.03 and wherein the compounds may be paraffins and olefins, the process comprising (a) cracking a Fischer-Tropsch synthesis product which comprises at least 30 wt % of compounds having at least 30 carbon atoms wherein the weight ratio of compounds having at least 60 or more carbon atoms to compounds having at least 30 carbon atoms is at least 0.2 to form a gasoline fraction boiling for more than 90 wt % between 25 and 215° C. and (b) mixing a trimethyl substituted aliphatic compound with the gasoline fraction.
Dependencies are inferred from the claim text.