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A method for hydrodesulfurization by forming a dispersion comprising hydrogen-containing gas bubbles with a mean diameter of less than 1 micron dispersed in a liquid phase comprising sulfur-containing compounds. Desulfurizing a liquid stream comprising sulfur-containing compounds by subjecting a flu

A method for hydrodesulfurization by forming a dispersion comprising hydrogen-containing gas bubbles with a mean diameter of less than 1 micron dispersed in a liquid phase comprising sulfur-containing compounds. Desulfurizing a liquid stream comprising sulfur-containing compounds by subjecting a fluid mixture comprising hydrogen-containing gas and the liquid to a shear rate greater than 20,000 s−1 to produce a dispersion of hydrogen in a continuous phase of the liquid and introducing the dispersion into a fixed bed hydrodesulfurization reactor from which a reactor product is removed. Systems of apparatus for hydrodesulfurization are also presented.

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1. A system for a hydrodesulfurization, hydrodenitrogenation, or hydrofinishing catalytic reaction comprising: at least one high shear mixing device comprising 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

1. A system for a hydrodesulfurization, hydrodenitrogenation, or hydrofinishing catalytic reaction comprising: at least one high shear mixing device comprising 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 mixing device is configured to produce a dispersion of hydrogen-containing gas bubbles in a liquid phase;a pump configured for delivering a liquid stream comprising liquid phase to the high shear mixing device; anda vessel configured for receiving the dispersion from the high shear device and for maintaining a predetermined bulk pressure and temperature for the hydrodesulfurization, hydrodenitrogenation, or hydrofinishing catalytic reaction. 2. The system of claim 1, wherein the predetermined bulk pressure is in the range of about 600 kPa to about 6.1 MPa, and wherein the predetermined bulk temperature is in the range of about 260° C. to about 427° C. 3. The system of claim 2, the system further comprising: a gas separator for receiving a product stream comprising from the vessel; andan absorber configured to receive and clean a gas separator outlet stream, resulting in a cleaned gas stream. 4. The system of claim 3, the system further comprising a reboiled stripper distillation tower, wherein the product stream comprises hydrogen sulfide. 5. The system of claim 1 wherein the liquid phase is selected from liquid phases comprising sulfur-containing species and hydrocarbons; liquid phases comprising nitrogen-containing species and hydrocarbons; and liquid phases comprising unsaturated hydrocarbons; wherein the dispersion has a mean bubble diameter of less than 400 nm. 6. The system of claim 1 wherein the at least one high shear mixing device is capable of producing a tip speed of the at least one rotor of at least 40.1 m/s (7,900 ft/min). 7. The system of claim 1 comprising at least two high shear mixing devices. 8. A system for a hydrodesulfurization, hydrodenitrogenation, or hydrofinishing catalytic reaction, the system comprising: a high shear device comprising an inlet for a fluid stream comprising a liquid and hydrogen gas, and an outlet for a product dispersion, wherein the high shear device is configured to produce a dispersion of hydrogen gas bubbles having an average bubble diameter of less than about 5 μm in the liquid; anda reactor selected from hydrodesulfurization, hydrodenitrogenation, and hydrofinishing reactors, wherein the reactor comprises catalyst, wherein the outlet of the high shear device is fluidly connected to an inlet of the reactor, and wherein the reactor is configured for receiving the dispersion from the high shear device and for maintaining a predetermined bulk pressure and temperature for the catalytic hydrodesulfurization, hydrodenitrogenation, or hydrofinishing reaction. 9. The system of claim 8 wherein the high shear device comprises a high shear mill having a tip speed of greater than 5.08 m/s (1000 ft/min). 10. The system of claim 8 wherein the high shear device has a tip speed of greater than 20.3 m/s (4000 ft/min). 11. The system of claim 8, the system further comprising: a gas separator for receiving a product stream comprising from the reactor; andan absorber configured to receive and clean a gas separator outlet stream, resulting in a cleaned gas stream. 12. The system of claim 11, the system further comprising a reboiled stripper distillation tower, wherein the product stream comprises hydrogen sulfide. 13. In a system for hydrodesulfurization, hydrodenitrogenation, or hydrofinishing catalytic reaction, or a combination thereof, the system comprising: an external high shear device comprising at least one generator comprising a rotor and a stator having a shear gap therebetween, and an inlet for a fluid stream comprising hydrogen gas and a liquid phase selected from liquid phases comprising sulfur-containing species and hydrocarbons; liquid phases comprising nitrogen-containing species and hydrocarbons; and liquid phases comprising unsaturated hydrocarbons; wherein the high shear device produces a dispersion of the hydrogen gas and the liquid phase; anda fixed bed reactor comprising catalyst, wherein the fixed bed reactor is configured to receive the dispersion from the high shear device and to maintain a predetermined bulk pressure and temperature for the catalytic hydrodesulfurization, hydrodenitrogenation, or hydrofinishing reaction. 14. The system of claim 13 wherein the high shear device comprises at least two generators. 15. The system of claim 14 wherein the shear rate provided by one generator is greater than the shear rate provided by another generator. 16. The system of claim 13, the system further comprising: a gas separator for receiving a product stream comprising from the fixed bed reactor; andan absorber configured to receive and clean a gas separator outlet stream, resulting in a cleaned gas stream. 17. The system of claim 16, the system further comprising a reboiled stripper distillation tower, wherein the product stream comprises hydrogen sulfide.