Internal gas separation assembly for high current density electrolytic cells

Claim 2

In the process of electrolyzing a brine in an electrolytic cell, having at least one anode, at a total cell current above 2500 amperes per square foot of internal cell horizontal area whereby a froth of chlorine and electrolyte would otherwise be generated, the improvement comprising:

Claim 3

(a) partially separating said froth into liquid and gas fractions within said anode; and (b) completing the substantial separation of said froth into liquid and gas fractions within said cell in a disengaging zone having a horizontal cross-section area of less than 0.13 square feet per kiloampere of total cell current.

Claim 4

(a) partially separating said froth into liquid and gas fractions within said anode; and (b) completing the substantial separation of said froth into liquid and gas fractions within said cell in a disengaging zone having a horizontal cross-section area of less than 0.13 square feet per kiloampere of total cell current.

Claim 5

The improvement of claim 1 wherein said step a) involves changing the momentum of said froth within a plurality of separation zones within said anodes.

Claim 6

A gas separation assembly for an electrolytic cell having a cell body having a side wall and containing a liquid electrolyte and a hollow gas evolving electrode in said liquid electrolyte and a total cell current density above 2500 amperes per square foot of horizontal, cross-sectional, internal cell area, which system comprises: (a) a plurality of gas collector means within said gas evolving electrode extending across the interior space of said electrode and having portions defining an open end adjacent said side wall, for blocking upward flow of gas through said electrode and for vertically dividing said interior space into a plurality of separation zones and for collecting gas evolved by said electrode and for partially separating said evolved gas from said liquid electrolyte and for emitting said partially separated evolved gas through said open end; and (b) disengager means, located above said open end of said gas collector means and having less than 0.13 square feet of internal, horizontal, cross-sectional, disengaging area per kiloampere of total cell current, for receiving said partially separated, collected, evolved gas from said open end of said gas collector means and completing the separation of said gas.

Claim 7

A gas separation assembly for an electrolytic cell having a cell body having a side wall and containing a liquid electrolyte and a hollow gas evolving electrode in said liquid electrolyte and a total cell current density above 2500 amperes per square foot of horizontal, cross-sectional, internal cell area, which system comprises: (a) a plurality of gas collector means within said gas evolving electrode extending across the interior space of said electrode and having portions defining an open end adjacent said side wall, for blocking upward flow of gas through said electrode and for vertically dividing said interior space into a plurality of separation zones and for collecting gas evolved by said electrode and for partially separating said evolved gas from said liquid electrolyte and for emitting said partially separated evolved gas through said open end; and (b) disengager means, located above said open end of said gas collector means and having less than 0.13 square feet of internal, horizontal, cross-sectional, disengaging area per kiloampere of total cell current, for receiving said partially separated, collected, evolved gas from said open end of said gas collector means and completing the separation of said gas.

Claim 8

The assembly of claim 3 wherein said disengager means is located entirely within said cell body.

Claim 9

The assembly of claim 3 or 4 wherein said disengager means has less than 0.10 square feet of horizontal, internal, cross-sectional area per kiloampere of total cell current.

Claim 10

The assembly of claim 5 wherein said disengager means has less than 0.01 square feet of horizontal, internal, cross-sectional area per kiloampere of total cell current.

Claim 11

The assembly of claim 3 or 4 wherein said disengager means has a horizontal cross-sectional area equal to less than 50 percent of said internal horizontal cross-sectional area of said cell.

Claim 12

The assembly of claim 7 wherein said disengager means has a horizontal cross-sectional area equal to less than 10 percent of said internal horizontal cross-sectional area of said cell.

Claim 13

The assembly of claim 3 wherein said gas collector means comprises downwardly opening inclined channel sloped upwardly toward said open end whereby gases movement toward said open end is promoted.

Claim 14

The assembly of claim 3 wherein said gas collector means comprises downwardly opening horizontal channel, and the end of said gas collecting means opposite said open end is closed so that gas is emitted from said open end.

Claim 15

The assembly of claim 9 or 10 wherein said downwardly opening channel includes: (a) a center section having said open end and also having an opposite end away from said open end; (b) a first end means closing said opposite end and having a bottom; (c) a second end means partially closing said open end and having a bottom; and (d) said bottom of said second end means being located higher than said bottom of said first end so that gas bubbles tend to escape at said open end and flow upwardly therefrom into said disengager means.