초록 ▼

A process for the production of low benzene content gasoline is disclosed wherein a full boiling range naphtha is fractionated to produce a light naphtha, a medium naphtha and a heavy naphtha. The benzene is contained in the medium naphtha and this stream is subjected to hydrogenation to convert the

A process for the production of low benzene content gasoline is disclosed wherein a full boiling range naphtha is fractionated to produce a light naphtha, a medium naphtha and a heavy naphtha. The benzene is contained in the medium naphtha and this stream is subjected to hydrogenation to convert the benzene to cyclohexane which may be isomerized to improve the octane. The valuable olefins are removed in the light naphtha and the valuable heavier aromatics (toluene and xylenes) are removed in the heavy naphtha. In a preferred embodiment all of the reactions are carried out in distillation column reactors.

대표청구항 ▼

1. A process for producing low benzene content gasoline corn rising the steps of:(a) feeding a full boiling range naphtha containing benzene, olefins, diolefins, mercaptans, thiophenes and other organic sulfur compounds to a distillation column wherein a light naphtha fraction is taken as overheads,

1. A process for producing low benzene content gasoline corn rising the steps of:(a) feeding a full boiling range naphtha containing benzene, olefins, diolefins, mercaptans, thiophenes and other organic sulfur compounds to a distillation column wherein a light naphtha fraction is taken as overheads, a medium naphtha fraction containing said benzene is taken as a side draw and a heavy naphtha fraction is taken as a bottoms; (b) feeding said medium naphtha fraction containing said benzene and said thiophenes to a hydrogenation reactor containing a hydrogenation catalyst wherein a portion of said benzene is hydrogenated to cyclohexane and said thiophenes are converted to hydrogen sulfide; (c) combining said overheads, said bottoms and the effluent from said hydrogenation reactor to produce a gasoline lower in benzene content than said full boiling range naphtha feed; (d) feeding said overheads to a thioetherification react r containing a thioetherification catalyst wherein a portion of said diolefins are react d with a portion of said mercaptans to produce sulfides; (e) separating said sulfides from said overheads; (f) feeding said bottoms and hydrogen to a hydrodesulfurization reactor containing a hydrodesulfurization catalyst wherein a portion of said other organic sulfur compounds are reacted with hydrogen to produce hydrogen sulfide; and (g) separating said hydrogen sulfide from said bottoms. 2. The process according to claim 1 wherein the effluent from said hydrogenation reactor is fed to an isomerization reactor containing an isomerization catalyst wherein a portion of said cyclohexane is isomerized to methyl cyclo pentane.3. The process according to claim 2 wherein said distillation column contains said thioetherification catalyst and said sulfides are remove along with said bottoms.4. The process according to claim 2 wherein said hydrogenation catalyst is contained within a second distillation column and any material boiling at a temperature below that of benzene or cyclohexane is removed as a second overheads and any material boiling at or above the boiling point of benzene an cyclohexane is removed as a second bottoms.5. The process according to claim 2 wherein said hydrodesulfurization catalyst is contained within a third distillation column and the hydrodesulfurization reaction is carried out simultaneously with distillation.6. The process according to claim 2 wherein sa d isomerization catalyst is contained within a fourth distillation column and the isomerization reaction is carried out simultaneously with distillation.7. A process for the production of low sulfur, low benzene content gasoline comprising the steps of:(a) feeding hydrogen and a full boiling range naphtha containing olefins, benzene, diolefins, mercaptans, thiophenes and other organic sulfur compounds to a first distillation column reactor containing a thioetherification catalyst; (b) concurrently in said first distillation column reactor; (i) contacting said diolefins with said mercaptans in the presence of said thioetherification catalyst to react a portion of said diolefins with portion of said mercaptans to produce sulfides, and (ii) fractionating said full boiling range naphtha to produce a light naphtha, medium naphtha containing said benzene and said thiophene and heavy naphtha; (c) removing said light naphtha from said first distillation column reactor as a first overheads; (d) removing said medium naphtha from said first distillation column reactor as a side draw; (e) removing said heavy naphtha from said first distillation column reactor as a first bottoms; (f) feeding hydrogen and said medium naphtha to a second distillation column reactor containing a hydrogenation catalyst; (g) concurrently in said second distillation column reactor; (i) contacting the benzene and thiophene contained within said medium naphtha with hydrogen in the presence of said hydrogenation catalyst to hydrogenate a portion of said benzene to cyclohexane and to react a portion of said thiophene with said hydrogen to produce hydrogen sulfide, and (ii) fractionating said medium naphtha to separate said hydrogen sulfide and any material boiling at a temperature below that of benzene or cyclohexane from any material boiling at or above the boiling point of benzene and cyclohexane; (h) removing said hydrogen sulfide and the material boiling a temperature below that of benzene or cyclohexane as a second overheads; and (i) removing any material boiling at or above the boiling point of benzene and cyclohexane as a second bottoms. 8. The process according to claim 7 further comprising feeding said second bottoms to a third distillation column reactor containing an isomerization catalyst and concurrently in said third distillation column reactor:(a) isomerizing a portion of said cyclohexane to methyl cyclo pentane to form a reaction mixture; and (b) separating the isomerization product from the reaction mixture by fractional distillation. 9. The process according to claim 7 further comprising feeding hydrogen and said first bottoms to a fourth distillation column reactor containing a hydrodesulfurization catalyst and concurrently in said fourth distillation column reactor:(a) reacting a portion of said heavier organic sulfur compounds with hydrogen to form hydrogen sulfide; and (b) separating hydrogen sulfide from the heavy naphtha by distillation.