Abstract A process for producing high octane low lead content or unleaded gasoline from a hydrocarbon feedstock by hydrocracking the hydrocarbon feedstock; fractionating the hydrocracking effluent in a fractionation zone, thereby obtaining a stream rich in singly branched hexanes; isomerizing the singly branched hexanes to doubly branched hexanes in an isomerization zone operated at a reaction temperature below 300°F.; and combining the doubly branched hexanes with C 7 + hydrocarbons derived from the hydrocracking effluent, thereby obtaining a high octane gasoline or gasoline blending stock. In a preferred embodiment, the isomerization zone effluent is fractionated to give a cyclohexane-rich stream which stream is catalytically reformed and then the reformate is combined with the doubly branched hexanes from the isomerization zone.
A process for producing high octane low lead content or unleaded gasoline from a hydrocarbon feedstock which comprises hydrocracking the hydrocarbon feedstock, thereby obtaining a hydrocracking effluent comprising singly branched hexanes and C 7 + hydrocarbons; fractionating the hydrocracking effluent in a fractionation zone, thereby obtaining a stream rich in singly branched hexanes; isomerizing the singly branched hexanes to doubly branched hexanes in an isomerization zone operated at a reaction temperature below 300°F.; and combining the doubly branched hexanes with C 7 + hydrocarbons derived from the hydrocracking effluent, thereby obtaining a high octane gasoline or gasoline blending stock.
Claim 2
Dependent Claim
99 words
A process for producing high octane low lead content or unleaded gasoline from a hydrocarbon feedstock which comprises hydrocracking the hydrocarbon feedstock, thereby obtaining a hydrocracking effluent comprising singly branched hexanes and C 7 + hydrocarbons; fractionating the hydrocracking effluent in a fractionation zone, thereby obtaining a stream rich in singly branched hexanes; isomerizing the singly branched hexanes to doubly branched hexanes in an isomerization zone operated at a reaction temperature below 300°F.; and combining the doubly branched hexanes with C 7 + hydrocarbons derived from the hydrocracking effluent, thereby obtaining a high octane gasoline or gasoline blending stock.
Claim 3
Dependent Claim
38 words
The process in accordance with claim 1 wherein the fractionating is carried out to obtain a butane fraction, a pentane-hexane fraction and a C 7 + fraction, and wherein the pentane-hexane fraction is fed to the isomerizing step.
Claim 4
Dependent Claim
28 words
The process in accordance with claim 2 wherein the fractionating is carried out to obtain an isopentane-rich fraction and wherein the pentane-hexane fraction is a normal pentane-hexane fraction.
Claim 5
Dependent Claim
54 words
The process in accordance with claim 1 wherein the fractionating is carried out to obtain a cyclohexane-rich fraction and wherein the process further comprises feeding the cyclohexane-rich fraction to catalytic reforming, thereby obtaining a C 5 + hydrocarbon effluent from catalytic reforming; and combining the C 5 + hydrocarbons with said doubly branched hexanes.
Claim 6
Dependent Claim
32 words
The process in accordance with claim 1 wherein the isomerization is carried out by contacting the singly branched hexanes with a catalyst comprising HF.sup.. antimony pentafluoride supported on a porous solid carrier.