Alkylation process startup procedure

Claim 2

A start-up method for a liquid phase hydrofluoric acid-catalyzed alkylation process wherein a quantity of liquid hydrofluoric acid catalyst containing less than 5 wt.% water is retained within an alkylation zone which comprises the steps of: a. forming a first stream of hydrofluoric acid by removing a stream of the hydrofluoric acid catalyst retained in the alkylation zone; b. passing a hydrocarbon stream comprising olefinic normal hydrocarbons having from 2 to about 12 carbon atoms per molecule into an environment in which there are substantially no isoparaffins present and which is maintained at a pressure of from 20 psig. to about 500 psig. and a temperature of from about 50°F. to about 140°F.; c. admixing the hydrocarbon stream with the first hydrofluoric acid stream and effecting a polymerization of substantially all of the hydrocarbon stream and the formation of a polymeric diluent comprising hydrocarbons having a carbon number ranging from 12 to about 40; d. admixing the polymeric diluent with the first hydrofluoric acid stream and effecting the formation of a second hydrofluoric acid stream containing a lower weight percentage of hydrofluoric acid than the first hydrofluoric acid stream; e. admixing the second hydrofluoric acid stream with the hydrofluoric acid catalyst retained in the alkylation zone, and effecting a reduction in the weight percentage of hydrofluoric acid in the hydrofluoric acid catalyst retained in the alkylation zone; and f. continuing the polymerization of the hydrocarbon stream in step (c) until the average acid strength in the hydrofluoric acid retained in the alkylation zone is reduced to about 86 to 90 wt.% .

Claim 3

A hydrofluoric acid-catalyzed alkylation process which comprises the steps of: a. admixing a first olefinic hydrocarbon stream comprising mono-olefins having from 2 to about 6 carbon atoms per molecule with an alkylatable hydrocarbon stream comprising isoparaffins having from 4 to 7 carbon atoms per molecule and effecting the formation of a reactant mixture which is substantially free of hydrofluoric acid; b. passing the reactant mixture into a reaction zone which contains a quantity of liquid phase hydrofluoric acid catalyst comprising less than 5 wt.% water and which is maintained under alkylation conditions, effecting the reaction of the mono-olefins with the isoparaffins and the production of high-octane gasoline blending components; c. effecting the formation of a second olefinic hydrocarbon stream by diverting a portion of the first olefinic hydrocarbon stream, and passing the second olefinic hydrocarbon stream into a polymerization zone maintained under conditions including a temperature of from 0°F. to about 200°F. and a pressure of from about 20 psig. to about 500 psig. and in which there are substantially no isoparaffins present; d. contacting the second olefinic hydrocarbon stream with liquid hydrofluoric acid and effecting a polymerization of essentially all of the second olefinic hydrocarbon stream and the formation of a polymeric diluent; e. admixing the polymeric diluent with the hydrofluoric acid catalyst contained with in the reaction zone and effecting a reduction in the weight percentage of hydrofluoric acid in the hydrofluoric acid catalyst contained in the reaction zone; and, f. continuing the polymerization of the hydrocarbon stream in step (d) until the average acid strength in the hydrofluoric acid retained in the alkylation zone is reduced to about 86 to 90 weight percent.

Claim 4

A hydrofluoric acid-catalyzed alkylation process which comprises the steps of: a. admixing a first olefinic hydrocarbon stream comprising mono-olefins having from 2 to about 6 carbon atoms per molecule with an alkylatable hydrocarbon stream comprising isoparaffins having from 4 to 7 carbon atoms per molecule and effecting the formation of a reactant mixture which is substantially free of hydrofluoric acid; b. passing the reactant mixture into a reaction zone which contains a quantity of liquid phase hydrofluoric acid catalyst comprising less than 5 wt.% water and which is maintained under alkylation conditions, effecting the reaction of the mono-olefins with the isoparaffins and the production of high-octane gasoline blending components; c. effecting the formation of a second olefinic hydrocarbon stream by diverting a portion of the first olefinic hydrocarbon stream, and passing the second olefinic hydrocarbon stream into a polymerization zone maintained under conditions including a temperature of from 0°F. to about 200°F. and a pressure of from about 20 psig. to about 500 psig. and in which there are substantially no isoparaffins present; d. contacting the second olefinic hydrocarbon stream with liquid hydrofluoric acid and effecting a polymerization of essentially all of the second olefinic hydrocarbon stream and the formation of a polymeric diluent; e. admixing the polymeric diluent with the hydrofluoric acid catalyst contained with in the reaction zone and effecting a reduction in the weight percentage of hydrofluoric acid in the hydrofluoric acid catalyst contained in the reaction zone; and, f. continuing the polymerization of the hydrocarbon stream in step (d) until the average acid strength in the hydrofluoric acid retained in the alkylation zone is reduced to about 86 to 90 weight percent.