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Methods and systems for the production of linear alkylbenzenes are described herein. The methods and systems incorporate the novel use of a high shear device to promote dispersion and mixing of one or more olefins (e.g. propylene) with an aromatic. The high shear device may allow for lower reaction

Methods and systems for the production of linear alkylbenzenes are described herein. The methods and systems incorporate the novel use of a high shear device to promote dispersion and mixing of one or more olefins (e.g. propylene) with an aromatic. The high shear device may allow for lower reaction temperatures and pressures and may also reduce reaction time with existing catalysts.

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1. A system for producing a linear alkylbenzene, the system comprising: a high shear device comprising an inlet for an aqueous liquid-liquid stream comprising an olefin and an aromatic, and an outlet for a liquid product dispersion, wherein the outlet of the high shear device is fluidly connected to

1. A system for producing a linear alkylbenzene, the system comprising: a high shear device comprising an inlet for an aqueous liquid-liquid stream comprising an olefin and an aromatic, and an outlet for a liquid product dispersion, wherein the outlet of the high shear device is fluidly connected to an inlet of a vessel, and wherein the high shear device is capable of producing the liquid product dispersion comprising an olefin dispersed in an aromatic liquid phase, wherein the dispersed olefin has an average bubble diameter of less than about 5 μm;a pump configured for delivering the aqueous liquid-liquid stream to the high shear device via a conduit; anda vessel downstream the high shear device and configured for maintaining a predetermined pressure and temperature for a catalytic alkylation reaction and comprising an inlet for a stream comprising catalyst and an outlet for a product comprising the linear alkylbenzene produced by reaction of the olefin and the aromatic in the vessel. 2. The system of claim 1, wherein said high shear device comprises at least one rotor and at least one stator separated by a shear gap in the range of from about 0.02 mm to about 5 mm, wherein the shear gap is the minimum distance between the at least one rotor and the at least stator, and wherein the high shear device is capable of producing a tip speed of the at least one rotor in the range of greater than about 23 m/s. 3. The system of claim 1 wherein said high shear device is configured to produce a shear rate of greater than about 20,000 s−1. 4. The system of claim 1, wherein the vessel comprises a fixed bed alkylation reactor containing a fixed bed of alkylation catalyst. 5. The system of claim 1 wherein the high shear device comprises at least two generators. 6. The system of claim 5 wherein the shear rate provided by one generator is greater than the shear rate provided by another generator. 7. The system of claim 1 further comprising one or more strippers coupled to said vessel and configured for purifying the alkylbenzene. 8. The system of claim 1 wherein the dispersed olefin has an average bubble or droplet size of less than 100 nm. 9. The system of claim 8 wherein the dispersion comprises particles having a submicrometer average diameter. 10. The system of claim 1 wherein the linear alkylbenzene has the formula: wherein R is a branched or unbranched alkyl group having from 1 to 20 carbon atoms. 11. The system of claim 10 wherein the alkylbenzene comprises dodecylbenzene. 12. The system of claim 10 wherein the olefin comprises from 1 to 10 carbon atoms. 13. The system of claim 1 further comprising an inlet for alkylation catalyst, the inlet for alkylation catalyst configured for introduction of alkylation catalyst into at least one component of the system selected from the group consisting of the conduit, the high shear device and the vessel. 14. The system of claim 13 wherein the catalyst is selected from the group consisting of hydrofluoric acid and aluminum chloride. 15. The system of claim 13 wherein the catalyst is selected from the group consisting of aluminum halides, titanium halides, zirconium halides, iron halides, vanadium halides, chromium halides and combinations thereof. 16. The system of claim 1 wherein the aromatic is selected from the group consisting of benzene, toluene, phenol, aniline, xylene and ethylbenzene. 17. The system of claim 1 further comprising a recycle line for recycling unreacted aromatic from the vessel to the high shear device. 18. A system for producing a linear alkylbenzene, the system comprising: a high shear device comprising an inlet for a fluid stream comprising an olefin and an aromatic, and an outlet for a product dispersion, wherein the outlet of the high shear device is fluidly connected to an inlet of a vessel, wherein the high shear device is configured to produce a dispersion comprising the olefin dispersed in an aromatic liquid phase, and wherein the dispersed olefin has an average bubble diameter of less than about 5 μm;a pump configured for delivering the fluid stream to the high shear device via a conduit;a vessel downstream the high shear device and configured to provide a catalytic alkylation reaction of the olefin and the aromatic, the vessel comprising an inlet and an outlet for a product of the catalytic alkylation reaction comprising the linear alkylbenzene; andan alkylation catalyst. 19. The system of claim 18 wherein the system comprises an inlet for the alkylation catalyst, the inlet configured for introduction of the alkylation catalyst into at least one component of the system selected from the group consisting of the conduit, the high shear device and the vessel; wherein the vessel comprises a fixed bed alkylation reactor containing a fixed bed of additional alkylation catalyst; or both. 20. The system of claim 18 wherein the alkylation catalyst is selected from the group consisting of hydrofluoric acid, aluminum halides, titanium halides, zirconium halides, iron halides, vanadium halides, chromium halides and combinations thereof.