Apparatus and process for electrically resolving emulsions

Claim 2

Apparatus for electrically resolving an emulsion having immiscible aqueous and organic liquid phases, the aqueous phase being internal, comprising: (a) a metallic vessel having an emulsion inlet, an aqueous material outlet and organic material outlet means, said aqueous material outlet being at the bottom portion of said vessel and said organic material outlet means being in the upper portion of said vessel; (b) distributor means positioned in the lower portion of said vessel above said aqueous material outlet and connected by conduit means to said emulsion inlet; (c) planar, permeable electrode means adapted to be energized, horizontally positioned in said vessel spaced apart from the vessel walls and intermediate said distributor means and said organic material outlet means, said electrode means being the only electrode means positioned in said vessel; (d) conductive means adapted to connect said electrode means with an electrical power source outside of said vessel; (e) insulating means for maintaining said conductive means electrically isolated from said vessel; and (f) means for controlling the level of aqueous material which collects in the bottom portion of said vessel, said means adapted to maintain the level of said aqueous material at a position intermediate said distributor means and said electrode means.

Claim 3

The apparatus of claim 1 comprising also an electrical power source means for applying electrical potential to said electrode means (c) for establishing an electric field between said electrode means and the aqueous material surface, said electrical potential being of sufficient intensity to resolve said emulsion at said aqueous material surface.

Claim 4

The apparatus of claim 2 wherein said electrical power source means is adjustable as to electrical potential supplied by it.

Claim 5

The apparatus of claim 2 wherein said electrical power source means is adapted to supply an electrical potential producing an emulsion treating gradient of between about 0.5 and about 4 kilovolts per inch between the electrode means (c) and the aqueous material surface.

Claim 6

The apparatus of claim 4 wherein said treating gradient is between about 0.75 and about 1.5 kilovolts per inch.

Claim 7

The apparatus of claim 4 wherein said treating gradient is about 1.5 kilovolts per inch.

Claim 8

The apparatus of claim 2 wherein said electrical power source means is adapted to supply an electrical potential producing an emulsion treating gradient between the electrode means (c) and the aqueous material surface sufficient to make the emulsion conductive to current flow, but which potential is insufficient to ionize substances in the emulsion whereby small increases in the supplied potential produce disproportionately larger increases in current flow through the emulsion.

Claim 9

The apparatus of claim 1 comprising also means for adjusting the vertical spacing between the electrode means (c) and the aqueous material surface.

Claim 10

The apparatus of claim 1 wherein said metallic vessel is horizontally elongated and said organic material outlet means includes collector means positioned in the upper part of said vessel.

Claim 11

The apparatus of claim 1 wherein said metallic vessel is vertically elongated.

Claim 12

The apparatus of claim 1 wherein said distributor means comprises a trough or pan distributor.

Claim 13

A process for electrically resolving an emulsion having immiscible aqueous and organic liquid phases, the aqueous phase being internal, comprising: (a) maintaining a body of aqueous material in a treating vessel, said aqueous material serving as an electrical ground; (b) establishing an electric field between an energized horizontal planar permeable electrode and the surface of said body of aqueous material, said electrode being positioned above said aqueous material surface; (c) introducing the emulsion into said body of aqueous material; (d) allowing said emulsion to rise to the surface of said body of aqueous material; (e) supplying sufficient potential to said energized electrode to provide an emulsion treating gradient in the electric field of sufficient magnitude so that the aqueous phase content of said emulsion coalesces instantaneously at said aqueous material surface, thus resolving the emulsion, and the coalesced drops become part of the aqueous material surface with no settling required; said potential being insufficient to ionize substances in the emulsion whereby small increases in the applied potential produce disproportionately larger increases in current flows through the emulsion; (f) allowing the organic liquid phase to rise; and (g) withdrawing said organic liquid from the upper part of said treating vessel and said aqueous material from the lower part of said treating vessel.

Claim 14

A process for electrically resolving an emulsion having immiscible aqueous and organic liquid phases, the aqueous phase being internal, comprising: (a) maintaining a body of aqueous material in a treating vessel, said aqueous material serving as an electrical ground; (b) establishing an electric field between an energized horizontal planar permeable electrode and the surface of said body of aqueous material, said electrode being positioned above said aqueous material surface; (c) introducing the emulsion into said body of aqueous material; (d) allowing said emulsion to rise to the surface of said body of aqueous material; (e) supplying sufficient potential to said energized electrode to provide an emulsion treating gradient in the electric field of sufficient magnitude so that the aqueous phase content of said emulsion coalesces instantaneously at said aqueous material surface, thus resolving the emulsion, and the coalesced drops become part of the aqueous material surface with no settling required; said potential being insufficient to ionize substances in the emulsion whereby small increases in the applied potential produce disproportionately larger increases in current flows through the emulsion; (f) allowing the organic liquid phase to rise; and (g) withdrawing said organic liquid from the upper part of said treating vessel and said aqueous material from the lower part of said treating vessel.

Claim 15

The process of claim 12, wherein said emulsion treating gradient is between about 0.5 and about 4 kilovolts per inch.

Claim 16

The process of claim 12, wherein said emulsion treating gradient is between about 0.75 and about 1.5 kilovolts per inch.

Claim 17

The process of claim 12, wherein said emulsion treating gradient is about 1.5 kilovolts per inch.