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Use of a high shear mechanical device incorporated into a process for the production of chloral as a reactor device is capable of decreasing mass transfer limitations, thereby enhancing the chloral production process. A system for the production of chloral from acetaldehyde and chlorine, the system

Use of a high shear mechanical device incorporated into a process for the production of chloral as a reactor device is capable of decreasing mass transfer limitations, thereby enhancing the chloral production process. A system for the production of chloral from acetaldehyde and chlorine, the system comprising a reactor and an external high shear device the outlet of which is fluidly connected to the inlet of the reactor; the high shear device capable of providing a dispersion of chlorine gas bubbles within a liquid, the bubbles having an average bubble diameter of less than about 100 μm.

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We claim: 1. A method for producing choral, the method comprising: forming a mixture by combining a dispersable gas stream comprising chlorine and a reactant stream comprising liquid aldehyde; forming a dispersion from the mixture comprising liquid aldehyde and chlorine gas by introducing the mixtu

We claim: 1. A method for producing choral, the method comprising: forming a mixture by combining a dispersable gas stream comprising chlorine and a reactant stream comprising liquid aldehyde; forming a dispersion from the mixture comprising liquid aldehyde and chlorine gas by introducing the mixture into a high shear device, wherein the dispersion comprises chlorine gas bubbles with a mean diameter of less than about 5 μm, and wherein the high shear device comprises at least one rotor and at least one stator; and introducing the dispersion into a reactor from which a product comprising chloral is removed, wherein the operating temperature within the reactor is maintained at a temperature of less than about 40° C. 2. The method of claim 1 further comprising pumping an aqueous stream comprising the liquid aldehyde to a pressure of at least about 203 kPa to produce a pressurized aqueous stream. 3. The method of claim 1 wherein the chlorine gas bubbles in the dispersion have an average diameter of less than about 1.5 μm. 4. The method of claim 1 wherein forming the dispersion comprises rotating the at least one rotor at a tip speed of at least 5 m/s. 5. The method of claim 1 wherein forming the dispersion comprises rotating the at least one rotor at a tip speed of at least about 20 m/s. 6. The method of claim 4 wherein forming the dispersion comprises producing a localized pressure of about 1000 MPa at the tip of the at least one rotor. 7. The method of claim 1 wherein forming the dispersion comprises subjecting the chlorine gas and liquid aldehyde to a shear rate of greater than about 20,000 s−1. 8. The method of claim 1 wherein forming the dispersion comprises an energy expenditure of at least 1000 W/m3. 9. The method of claim 1 wherein the dispersion comprises a micro-foam. 10. The method of claim 1 further comprising treating the product with sulfuric acid. 11. The method of claim 1 wherein the liquid aldehyde comprises acetaldehyde, paraldehyde, or a combination thereof. 12. A method for producing chloral, the method comprising: providing a mixture of chlorine gas in aqueous solution comprising aldehyde; and forming a dispersion of chlorine gas bubbles in the aqueous solution comprising aldehyde by introducing the mixture into a high shear device and subjecting the mixture of liquid aldehyde and chlorine gas to a shear rate of at least 20,000 s−1. 13. The method of claim 12 wherein the high shear device comprises at least one rotor and at least one stator.