Method and apparatus for separating oxygen from a gaseous mixture

Claim 2

A process in which an electrochemical cell is used to separate oxygen from a mixture of gases, the process comprising the steps of: contacting the cathode of an electrochemical cell with a gaseous mixture comprising oxygen to thereby reduce such oxygen by a single electron to its superoxide ion; transporting such a superoxide ion across the cell from the cathode to the anode through an electrolyte contained therein; and oxidizing the superoxide ion to oxygen at the anode where said oxygen is discharged as oxygen gas.

Claim 3

The process according to claim 1 wherein the electrolyte is an aqueous solution having a pH greater than 7 and the cathode has a coating thereon, the coating being relatively impermeable to water and relatively permeable to the superoxide ion.

Claim 4

The process according to claim 2 wherein the coating comprises quinoline.

Claim 5

The process according to claim 2 wherein the electrolyte contains acetonitrile.

Claim 6

The process according to claim 2 wherein the coating is a polymer.

Claim 7

The process according to claim 5 wherein the polymer is selected from the group consisting of polyvinylpyridine, polyacrylonitrile, polyacrylamide and co-polymers thereof.

Claim 8

The process according to claim 2 wherein the aqueous solution has a pH greater than about 10.

Claim 9

The process according to claim 1 wherein the electrolyte is an aprotic, polar solvent containing a salt which is capable of dissolving in the solvent to provide at least a 0.1 molar solution.

Claim 10

The process according to claim 8 wherein the salt is selected from the group consisting of tetraalkylammonium salts and alkylpyridinium salts.

Claim 11

The process according to claim 1 wherein the electrolyte is a solid polymer.

Claim 12

The process according to claim 1 wherein the electrolyte contains a transition metal complex which is capable of stabilizing the superoxide ion against disproportionation.

Claim 13

The process according to claim 11 wherein the transition metal complex is a cobalt complex which is primarily in the II oxidation state at the oxygen/superoxide reversible potential.

Claim 14

The process according to claim 1 wherein the electrolyte contains a Lewis acid for stabilizing the superoxide ion against disproportionation.

Claim 15

The process according to claim 1 wherein the electrolyte contains a nitrile for stabilizing the superoxide ion against disproportionation.

Claim 16

The process according to claim 1 wherein the cathode is a gas diffusion electrode.

Claim 17

An electrochemical cell for use in separating oxygen from a mixture of gases comprising oxygen, the cell comprising: a cathode having a coating thereon and capable of reducing oxygen in the gaseous mixture to its superoxide ion, the coating being relatively impermeable to water and relatively permeable to superoxide ion; an anode at which such a superoxide ion is reoxidized to oxygen; and an aqueous electrolyte having a pH greater than about 7 the electrolyte providing the means for transporting such a superoxide ion across the cell from the cathode to the anode.

Claim 18

An electrochemical cell for use in separating oxygen from a mixture of gases comprising oxygen, the cell comprising: a cathode having a coating thereon and capable of reducing oxygen in the gaseous mixture to its superoxide ion, the coating being relatively impermeable to water and relatively permeable to superoxide ion; an anode at which such a superoxide ion is reoxidized to oxygen; and an aqueous electrolyte having a pH greater than about 7 the electrolyte providing the means for transporting such a superoxide ion across the cell from the cathode to the anode.

Claim 19

An electrochemical cell as claimed in claim 16 wherein the coating comprises quinoline.

Claim 20

An electrochemical cell as claimed in claim 16 wherein the cathode comprises mercury.

Claim 21

An electrochemical cell as claimed in claim 16 wherein the cathode comprises mercury and the coating comprises quinoline.

Claim 22

An electrochemical cell as claimed in claim 16 wherein the aqueous electrolyte has a pH greater than about 12.

Claim 23

An electrochemical cell as claimed in claim 16 wherein the coating comprises a polymer.

Claim 24

An electrochemical cell as is claimed in claim 21 wherein the polymer is selected from the group consisting of polyvinylpyridine, polyacrylonitrile, polyacrylamide and copolymers thereof.

Claim 25

An electrochemical cell as is claimed in claim 16 wherein the aqueous electrolyte contains a transition metal complex which is capable of stabilizing the superoxide ion against disproportionation.

Claim 26

An electrochemical cell as claimed in claim 16 wherein the electrolyte contains a Lewis acid for stabilizing the superoxide ion against disproportionation.

Claim 27

An electrochemical cell as claimed in claim 16 wherein the electrolyte contains a nitrile for stabilizing the superoxide ion against disproportionation.

Claim 28

An electrochemical cell for use in separating oxygen from a mixture of gases comprising oxygen, the cell comprising: a cathode capable of reducing oxygen in the gaseous mixture to its superoxide ion; an anode at which such superoxide ions are reoxidized to oxygen; and an electrolyte comprising an aprotic solvent containing a dissolved salt, the electrolyte providing the means for transporting such a superoxide ion across the cell from the cathode to the anode.

Claim 29

An electrochemical cell for use in separating oxygen from a mixture of gases comprising oxygen, the cell comprising: a cathode capable of reducing oxygen in the gaseous mixture to its superoxide ion; an anode at which such superoxide ions are reoxidized to oxygen; and an electrolyte comprising an aprotic solvent containing a dissolved salt, the electrolyte providing the means for transporting such a superoxide ion across the cell from the cathode to the anode.

Claim 30

An electrochemical cell as claimed in claim 26 wherein the salt is selected from the group consisting of tetraalkylammonium salts and alkylpyridinium salts.

Claim 31

An electrochemical cell as claimed in claim 26 wherein the dissolved salt forms at least a 0.1 molar solution with the aprotic solvent.

Claim 32

An electrochemical cell for use in separating oxygen from a mixture of gases comprising oxygen, the cell comprising: a cathode capable of reducing oxygen in the gaseous mixture to its superoxide ion: an anode at which such a superoxide ion is reoxidized to oxygen; and a solid polymer electrolyte, the polymer electrolyte providing the means for transporting such a superoxide ion across the cell from the cathode to the anode.

Claim 33

An electrochemical cell for use in separating oxygen from a mixture of gases comprising oxygen, the cell comprising: a cathode capable of reducing oxygen in the gaseous mixture to its superoxide ion: an anode at which such a superoxide ion is reoxidized to oxygen; and a solid polymer electrolyte, the polymer electrolyte providing the means for transporting such a superoxide ion across the cell from the cathode to the anode.

Claim 34

A process in which an electrochemical cell is used to separate oxygen from a mixture of gases, the process comprising the steps of: adding a transition metal complex to the electrolyte contained in the cell, such a transition metal complex capable of being reduced at a potential more positive than oxygen reduction; providing a potential across the cell to reduce the transition metal complex at the cathode to form a complex capable of reversibly binding oxygen; introducing a gaseous mixture comprising oxygen into the electrochemical cell to contact the reduced transition metal complex so that oxygen is bound to said complex; and transporting the oxygen-containing complex to the anode where the complex is reoxidized at which time said complex releases the bound oxygen for recovery.

Claim 35

A process in which an electrochemical cell is used to separate oxygen from a mixture of gases, the process comprising the steps of: adding a transition metal complex to the electrolyte contained in the cell, such a transition metal complex capable of being reduced at a potential more positive than oxygen reduction; providing a potential across the cell to reduce the transition metal complex at the cathode to form a complex capable of reversibly binding oxygen; introducing a gaseous mixture comprising oxygen into the electrochemical cell to contact the reduced transition metal complex so that oxygen is bound to said complex; and transporting the oxygen-containing complex to the anode where the complex is reoxidized at which time said complex releases the bound oxygen for recovery.

Claim 36

A process in which an electrochemical cell is used to separate oxygen from a mixture of gases, the process comprising the steps of: adding a transition metal complex of the formula L x Co(III).sup.(n-1)+ to the electrolyte of the electrochemical cell, where L designates a ligand, x designates the number of such ligands associated with the Co ion, III represents the Co ion valence and n is the total charge of the complex, the ligand selected to provide that Co(III) is reduced to Co(II) at potentials more positive than oxygen reduction; providing a potential across the cell to thereby reduce the Co(III) to Co(II) at the cathode to provide a complex of the formula L x Co(II) n+ ; introducing a gaseous mixture comprising oxygen into the electrochemical cell to contact the L x Co(II) n+ complex so that such oxygen is bound to the complex; and transporting the oxygen containing complex to the anode where the Co(II) comprising the complex is oxidized to Co(III), at which time the complex releases the bound oxygen for recovery.

Claim 37

A process in which an electrochemical cell is used to separate oxygen from a mixture of gases, the process comprising the steps of: adding a transition metal complex of the formula L x Co(III).sup.(n-1)+ to the electrolyte of the electrochemical cell, where L designates a ligand, x designates the number of such ligands associated with the Co ion, III represents the Co ion valence and n is the total charge of the complex, the ligand selected to provide that Co(III) is reduced to Co(II) at potentials more positive than oxygen reduction; providing a potential across the cell to thereby reduce the Co(III) to Co(II) at the cathode to provide a complex of the formula L x Co(II) n+ ; introducing a gaseous mixture comprising oxygen into the electrochemical cell to contact the L x Co(II) n+ complex so that such oxygen is bound to the complex; and transporting the oxygen containing complex to the anode where the Co(II) comprising the complex is oxidized to Co(III), at which time the complex releases the bound oxygen for recovery.