Macrocyclic amine complexes for ligand extraction and generation

• US 4,952,289 A
• Filed: 05/09/1988
• Issued: 08/28/1990
• Est. Priority Date: 05/09/1988
• Status: Expired due to Term

• Current Assignee: W R Grace & Company - CONN (Standard Industries Holdings, Inc.)
• Original Assignee: Aquanautics Corporation
• Inventors: DeCastro, Emory S., Kerr, John B., Ciccone, Joseph P.
• Primary Examiner(s): Niebling, John F.
• Assistant Examiner(s): Gorgos, Kathryn
• Application Number:
  US07/191,519
• Time in Patent Office: 841 Days
• Field of Search: 204/129, 204/130, 204/180.1, 204/182.3, 204/182.5, 204/233, 204/235, 204/252, 204/263, 204/266, 261/161, 261/DIG. 28, 422/48, 423/219, 423/579, 544/4, 544/66, 544/7, 544/64, 546/2, 548/101, 548/108, 548/109, 548/402, 556/13, 556/14, 556/16, 556/42, 556/44, 556/45, 556/49, 556/50, 556/110, 556/113, 556/146, 556/138
• US Class Current: 205/633
• CPC Class Codes: C01B 13/0251 by making use of membranes
• CPC Class Codes: C01B 13/0285 by absorption in liquids
• CPC Class Codes: C01B 2210/0046 Nitrogen
• CPC Class Codes: C01B 2210/0062 Water
• CPC Class Codes: C07D 257/02 not condensed with other rings
• CPC Class Codes: C07D 471/08 Bridged systems
• CPC Class Codes: C07F 15/065 without a metal-carbon linkage
• CPC Class Codes: H01M 8/06 Combination of fuel cells with means for production of reactants or for treatment of residues regenerative fuel cells H01M8/18
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

Methods and apparatus for electrochemical extraction of a ligand such as molecular oxygen from a first fluid environment and for release of a ligand such as molecular oxygen, as well as ligand carrier compounds therefor comprising macrocyclic amines having the general formulas: ##STR1## where: A, B, C, D, E, and F are each nitrogen, oxygen, sulfur, or phosphorous;

m, n, o, p, q, and r are each typically 2, 3, 4, 5, or 6;

the R substituents are each generally H or short chain (linear or branched) alkyl, although R₂ may represent ketyl (═o); and

M is a suitable transition metal ion.

Claims

1. A method for extracting a ligand from a first fluid environment, the method comprising the steps of:

contacting the first fluid environment containing ligand with a first surface of a first ligand permeable membrane having a first surface and a second surface wherein the membrane separates the environment from an interior space of a container;

contacting a carrier fluid with the second surface of the membrane wherein the carrier fluid is confined in the container and the carrier fluid contains a carrier compound, whereby at least a portion of a ligand which diffuses through the membrane binds to the carrier compound to give bound ligand complex;

transporting the carrier fluid containing the bound ligand complex to a first electrode compartment of an electrochemical cell which forms a second portion of the container;

electrochemically modulating the carrier compound to an oxidation state having a relatively less binding affinity for the ligand, thereby releasing free ligand into the carrier fluid and producing a non-binding state carrier compound;

removing ligand from the carrier fluid to give a ligand depleted carrier fluid;

transporting the ligand depleted carrier fluid containing the non-binding state carrier compound to a second electrode compartment of an electrochemical cell which forms a third portion of the container; and

electrochemically modifying the non-binding state carrier compound to reform the binding state carrier compound;

wherein the carrier compound comprises a metallic complex of a transition metal ion and a macrocyclic amine having the general formula;

##STR10## where;

A, B, C, D, E, and F are each nitrogen, oxygen, sulfur, or phosphorous;

m, n, o, p, q, and r are each 2, 3, 4, 5 or 6; and

each R is selected from the group consisting of hydrogen, short chain linear alkyl, and short chain branched alkyl, or R₂ is ketyl.

2. The method of claim 1 wherein the carrier compound comprises a metallic complex of a macrocyclic amine having the general formula:

##STR11## where;

at least three of A, B, C, and D are each nitrogen, the remaining one of A, B, C, and D being nitrogen, oxygen, sulfur, or phosphorous; and

m, n, o, and p are each 2, 3, or 4.

3. The method of claim 2 wherein A, B, C, and D are each nitrogen and wherein at least two of m, n, o, and p are equal to 3, the remaining ones of m, n, o, and p being equal to 2.

4. The method of claims 1, 2, 3, or 4 using an electrocatalyst to transfer electrons between the electrodes and the carrier compound, the electrocatalyst being mobile in the carrier fluid.

5. The method of claim 4 wherein the electrocatalyst is selected from the group consisting of substituted ferrocenes and substituted phenylenediamines.

6. The method of claim 1 wherein at least one of A, B, C, D, and E is nitrogen from a heterocyclic aromatic amine.

7. The method of claim 1 wherein the transition metal ion is selected from the group consisting of manganese, ion, cobalt, copper, and nickel.

8. The method of claim 7 wherein the metal is cobalt.

9. A method for extracting a ligand from a first fluid environment and releasing the ligand to a second fluid environment, the method comprising the steps of:

providing an electrochemical cell including an anode, a cathode and an electrolyte comprising a transition metal carrier compound having the general formula;

##STR12## where;

A, B, C, D, E, and F are each nitrogen, oxygen, sulfur, or phosphorous,

m, n, o, p, q and r are each 2, 3, 4, 5 or 6,

each R is selected from the group consisting of hydrogen, short chain linear alkyl, and short chain branched alkyl, or R₂ taken together is ketyl, and

M is a transition metal ion;

providing a potential across the cell sufficient to convert the metal of the carrier compound to a binding valence state at the cathode and convert, at the anode, the metal of a carrier compound ligand complex to a non-binding valence state;

communicating the ligand from the first fluid environment to the electrolyte in the region of the cathode so that the carrier compound ligand complex is formed between the ligand and the binding valence state carrier compound; and

transporting the carrier compound ligand complex to the anode for release of the ligand.

10. The method of claim 9 further comprising the step of electrochemically releasing the ligand from the carrier compound ligand complex to the second fluid environment.

11. The method of claim 9 wherein the metal is selected from the group consisting of manganese, iron, cobalt, copper, and nickel.

12. The method of claim 9 using an electrocatalyst to transfer electrons between the electrodes and the carrier compound the electrocatalyst being mobile in the carrier fluid, covalently linked to the carrier compound, immobilized on at least one of the electrodes, or immobilized on a substrate other than an electrode and circulated between the electrodes.

13. The method of claim 12 wherein the electrocatalyst is mobile in the carrier fluid and is selected from the group consisting of substituted ferrocenes and substituted phenylenediamines.

14. A method as in claim 12, wherein a voltage is applied across the electrodes, said voltage being from about 0.1 to 0.5 volts less than that applied under the conditions of the cell in the absence of the electrocatalyst.

15. An electrochemical system for extracting molecular oxygen from a fluid mixture feedstock, said system comprising:

an oxygen loading station;

an electrochemical cell including a pair of electrodes;

a voltage source connected to the electrodes;

a carrier fluid which circulates between the electrodes of the electrochemical cell and the oxygen loading station, said carrier fluid including a carrier compound capable in a first oxidation state of binding molecular oxygen and in a second oxidation state of releasing bound oxygen; and

an electrocatalyst in proximity to at least one of the electrodes, said electrocatalyst selected to promote electron transfer between the electrode and the carrier compound;

wherein the carrier compound is a transition metal complex having the general formula;

##STR13## where;

A, B, C, D, E, and F are each nitrogen, oxygen, sulfur, or phosphorous;

m, n, o, p, q, and r are each 2, 3, 4, 5 or 6;

each R is selected from the group consisting of hydrogen, short chain linear alkyl, and short chain branched alkyl or R₂ taken together is ketyl; and

M is a transition metal ion.

16. The system of claim 15 wherein the carrier compound is a transition metal complex having the general formula:

##STR14## where;

at least two of A, B, C, and D are nitrogen, the remaining ones of A, B, C, and D being nitrogen, oxygen, sulfur, or phosphorous;

m, n, o, and p are each 2, 3, or 4; and

M is a transition metal ion selected from the group consisting of manganese, iron, cobalt, nickel, and copper ions.

17. A composition of matter for use in electrochemical ligand extraction and generation processes comprising:

an aqueous solution of greater than about 10 millimoles per liter of a metallic complex of a transition metal ion and a macrocyclic amine having the general formula;

##STR15## where;

A, B, C, D, E, and F are each nitrogen, oxygen, sulfur, or phosphorous;

m, n, o, p, q, and r are each 2, 3, 4, 5 and 6;

each R is selected from the group consisting of hydrogen, short chain linear alkyl, and short chain branched alkyl, or R₂ is ketyl; and

the transition metal ion is selected from the group consisting of manganese, iron, cobalt, nickel, and copper ions.

18. The composition of matter according to claim 17 further comprising a supporting electrolyte including a salt selected from the group consisting of sodium chloride, potassium chloride, sodium nitrate, and potassium nitrate, the salt having a concentration between about 0.1 and about 3.0 molar.

19. The composition of matter according to claim 17, titrated to a pH of about 1 pH unit above the pH at which greater than about 50% of the metallic complex, when exposed to an oxygen containing environment, is present as an oxygen complex.

20. The composition of matter as in claim 17, wherein the carrier fluid is at a pH in the range from about 5 to 9 and further comprising an electrocatalyst, present at a concentration from about 0.01 mM to 1 M, selected from the group consisting of substituted ferrocenes and substituted phenylenediamines.