Electrodes for electrolytic germane process
View Patent ↗The invention relates to the electrolysis of aqueous electrolyte solutions containing GeO 2 ; hydroxide and water with metal alloy electrodes, such as, copper or tin rich alloy electrodes with alloying elements such as Sn, Pb, Zn, Cu etc, to generate Germane (GeH 4 ). Cu-rich alloy electrodes have been demonstrated to increase the GeH 4 current efficiency by almost 20% compared to Cu metal electrodes. Germanium deposition has been found to be either absent or minimal by using Cu-rich alloy electrodes. Several different methods for maintaining the cell performance or restoring the cell performance after a reduction in current efficiency over time, have been identified. A titration-based method for the analysis of the electrolyte, to obtain the concentration of GeO 2 and the concentration of hydroxide has also been disclosed.
1. A method for generating germane in a divided tubular housing electrochemical cell; comprising the steps of:
providing a cathode chamber comprising a metal alloy cathode, and cathode gas outlet;
providing an anode chamber comprising an anode that is part of inner wall of the tubular housing comprising metal M 1 , and an anode gas outlet;
providing an aqueous electrolyte solution comprising Germanium dioxide (GeO 2 ), a hydroxide M 2 OH and an electrolyte solvent in the cathode chamber and the anode chamber; wherein the metal alloy cathode and the anode are at least partially immersed in the aqueous electrolyte solution;
providing a divider separating the cathode chamber from the anode chamber; wherein the divider is electrically insulated from anode and cathode circuits;
supplying an electric power to the divided electrochemical cell;
releasing gas generated in the cathode chamber through the cathode gas outlet as the hydride gas; and
releasing gas generated in the anode chamber through the anode gas outlet;
wherein the metal alloy is selected from the group consisting of copper alloy, tin alloy and combinations thereof.
2. The method of claim 1 , wherein M 1 is a metal or a metal alloy suitable for anodic oxygen generation selected from the group consisting of nickel, platinum, copper, and combinations thereof; and the M 2 OH is selected from the group consisting of KOH, NaOH, LiOH, CsOH, and combinations thereof.
3. The method of claim 1 , wherein the metal alloy is a copper alloy comprising >60% copper (Cu), and lead(Pb).
4. The method of claim 3 , wherein the copper alloy further comprising tin(Sn) and zinc (Zn); and Zn is <15%.
5. The method of claim 1 wherein the electrolyte solvent is selected from the group consisting of de-ionized(DI) water, deuterated water (D 2 O), and mixtures thereof.
6. The method of claim 1 , wherein GeO 2 in the aqueous electrolyte solution ranges about 30 to 150 g/l, and M 2 OH in the aqueous electrolyte solution ranges about 50 to 350 g/l.
7. The method of claim 6 , wherein concentration of GeO 2 is determined by weighing GeO 2 precipitation generated through adding acid to the aqueous electrolyte solution to decrease pH to between 9 and 10.
8. The method of claim 1 , wherein the divided tubular housing electrochemical cell is operated at a temperature ranging from 2 50 C to 9 00 C, and at a current density ranging from 250 mA/c m2 to 350 mA/c m2 .
9. The method of claim 1 , wherein the metal alloy cathode is a hollow cathode or a metal alloy cathode comprising a plurality of perforations.
10. The method of claim 1 , further comprising steps of:
suspending the cathode in gas phase over the aqueous electrolyte solution; and
reinserting the cathode back to the aqueous electrolyte solution.
11. A method for generating germane in a divided tubular housing electrochemical cell; comprising the steps of:
providing a cathode chamber comprising a copper alloy cathode, and a cathode gas outlet;
providing an anode chamber comprising an anode that is part of inner wall of the tubular housing comprising nickel, and an anode gas outlet;
providing an aqueous electrolyte solution comprising Germanium dioxide (GeO 2 ), KOH and DI water in the cathode chamber and the anode chamber; wherein the metal alloy cathode and the anode are at least partially immersed in the aqueous electrolyte solution;
providing a divider separating the cathode chamber from the anode chamber; wherein the divider is electrically insulated from anode and cathode circuits;
supplying an electric power to the divided electrochemical cell;
releasing gas generated in the cathode chamber through the cathode gas outlet as the hydride gas; and
releasing gas generated in the anode chamber through the anode gas outlet.
12. The method of claim 11 , wherein the copper alloy comprising >60% copper (Cu), and lead(Pb).
13. The method of claim 12 , wherein the copper alloy further comprising tin(Sn) and zinc (Zn); and Zn is <15%.
14. The method of claim 11 , wherein GeO 2 in the aqueous electrolyte solution ranges about 30 to 150 g/l, and KOH in the aqueous electrolyte solution ranges about 50 to 350 g/l.
15. The method of claim 14 , wherein concentrations of GeO 2 is determined by weighing GeO 2 precipitation generated through adding acid to the aqueous electrolyte solution to decrease pH to between 9 and 10.
16. The method of claim 11 , wherein the divided tubular housing electrochemical cell is operated at a temperature ranging from 25° C. to 90° C., and at a current density range of 250 mA/cm 2 to 350 mA/cm 2 .
17. The method of claim 11 , further comprising steps of :
suspending the cathode in gas phase over the aqueous electrolyte solution; and
reinserting the cathode back to the aqueous electrolyte solution.
18. A method for generating germane in a divided tubular housing electrochemical cell; comprising the steps of:
providing a cathode chamber comprising a copper alloy cathode, and the cathode gas outlet;
providing an anode chamber comprising an anode that is part of inner wall of the tubular housing comprising nickel, and an anode gas outlet;
providing an aqueous electrolyte solution comprising KOH ranging from 80 to 170 g/l, germanium dioxide (GeO 2 ) ranging from 60-150 g/l and DI water in the cathode chamber and the anode chamber; wherein the copper alloy cathode and the anode are at least partially immersed in the aqueous electrolyte solution;
providing a divider separating the cathode chamber from the anode chamber; wherein the divider is electrically insulated from anode and cathode circuits;
supplying an electric power to the divided electrochemical cell;
releasing gas generated in the cathode chamber through the cathode gas outlet as the hydride gas; and
releasing gas generated in the anode chamber through the anode gas outlet.
19. The method of claim l 8 , wherein
the copper alloy cathode comprising 81% Cu, 12% Pb and about 7% Sn;
the aqueous electrolyte solution comprising 145 g/l KOH, 100 g/l GeO2 and DI water; and the divided tubular housing electrochemical cell is operated at 30° C.; and at a current density of 330 mA/cm 2 .
20. The method of claim 18 , further comprising steps of:
suspending the cathode in gas phase over the aqueous electrolyte solution; and
reinserting the cathode back to the aqueous electrolyte solution.