Liquid-liquid exchangers and process of using

Claim 2

A liquid-liquid exchanger containing a dispersed phase circulating in a counterflow manner relative to a continuous phase, which comprises: a column; a dispersed phase inlet and outlet and a continuous phase inlet and outlet connected to said column said that said dispersed phase and said continous phase flow in a counterflow manner, said dispersed phase inlet being connectable to a source of a dispersed phase; and a perforated electrocoalescer which comprises at least two electrodes, one of which is connected to ground while another is live, said electrodes being positioned in said column perpendicularly to the axis of said column such that when said dispersed phase is flowing in counterflow manner relative to a continuous phase, substantially all of said continuous phase passes through said electrocoalescer and small droplets of the dispersed phase are coalesced to form larger droplets and the volume of said larger droplets increases to a point where they are able to move in a direction away from said continuous phase outlet and then reach a part of said exchanger positioned between the dispersed phase inlet and the continuous phase inlet, thereby diminishing entrainment of said dispersed phase by said continuous phase.

Claim 3

A liquid-liquid exchanger according to claim 1, wherein the electrocoalescer comprises two electrodes connected to ground, surrounding a live electrode.

Claim 4

A liquid-liquid exchanger according to claim 1, wherein it comprises a retention level measuring means attached to that part of the exchanger between the dispersed phase inlet and the electrocoalescer.

Claim 5

A liquid-liquid exchanger according to claim 3, wherein the measuring means determines the pressure.

Claim 6

A liquid-liquid exchanger according to claim 3, wherein the measuring means determines the conductivity of the dispersed phase and continuous phase.

Claim 7

A liquid-liquid exchanger according to claim 1, wherein it is constituted by at least one pulsed column.

Claim 8

A liquid-liquid exchanger according to claim 1, wherein it is constituted by at least one spraying column.

Claim 9

A liquid-liquid exchanger according to claim 1, wherein it is constituted by at least one Kuhni column.

Claim 10

A process for removal of entrained droplets of a dispersed phase in a continuous phase, which comprises: providing a column; said column having connected thereto a dispersed phase inlet and outlet and a continous phase inlet and outlet; connecting said dispersed phase inlet to a source of a dispersed phase; said column having a perforated electrocoalescer which comprises at least two electrodes, one of which is connected to ground while another is live, said electrodes being positioned perpendicularly to the axis of said column such that when said dispersed phase is flowing in counterflow manner relative to said continuous phase, small droplets of the dispersed phase are coalesced to form larger droplets which are able to move in a direction away from said continuous phase outlet and then reach a part of said exchanger positioned between the dispersed phase inlet and the continuous phase inlet, thereby diminishing entrainment of said dispersed phase by said continous phase; introducing a continuous phase into said column by way of said continous phase inlet; introducing a dispersed phase into said column in a counterflow manner to said continuous phase by way of said dispersed phase inlet; drawing off said dispersed phase by way of said dispersed phase outlet; passing substantially all of said continuous phase through said electrocoalescer with removal of entrained droplets of said dispersed phase; and drawing off by way of said continuous phase outlet a coalesced phase.

Claim 11

A process for removal of entrained droplets of a dispersed phase in a continuous phase, which comprises: providing a column; said column having connected thereto a dispersed phase inlet and outlet and a continous phase inlet and outlet; connecting said dispersed phase inlet to a source of a dispersed phase; said column having a perforated electrocoalescer which comprises at least two electrodes, one of which is connected to ground while another is live, said electrodes being positioned perpendicularly to the axis of said column such that when said dispersed phase is flowing in counterflow manner relative to said continuous phase, small droplets of the dispersed phase are coalesced to form larger droplets which are able to move in a direction away from said continuous phase outlet and then reach a part of said exchanger positioned between the dispersed phase inlet and the continuous phase inlet, thereby diminishing entrainment of said dispersed phase by said continous phase; introducing a continuous phase into said column by way of said continous phase inlet; introducing a dispersed phase into said column in a counterflow manner to said continuous phase by way of said dispersed phase inlet; drawing off said dispersed phase by way of said dispersed phase outlet; passing substantially all of said continuous phase through said electrocoalescer with removal of entrained droplets of said dispersed phase; and drawing off by way of said continuous phase outlet a coalesced phase.

Claim 12

The process of claim 9, wherein said dispersed phase comprises uranium and isotopes thereof.