Process for recovering alkali metals and sulfur from alkali metal sulfides and polysulfides
View Patent ↗Alkali metals and sulfur may be recovered from alkali monosulfide and polysulfides in an electrolytic process that utilizes an electrolytic cell having an alkali ion conductive membrane. An anolyte solution includes an alkali monosulfide, an alkali polysulfide, or a mixture thereof and a solvent that dissolves elemental sulfur. A catholyte includes molten alkali metal. Applying an electric current oxidizes sulfide and polysulfide in the anolyte compartment, causes alkali metal ions to pass through the alkali ion conductive membrane to the catholyte compartment, and reduces the alkali metal ions in the catholyte compartment. Liquid sulfur separates from the anolyte solution and may be recovered. The electrolytic cell is operated at a temperature where the formed alkali metal and sulfur are molten.
1. An electrolytic cell for oxidizing an alkali metal monosulfide or alkali metal polysulfides comprising:
an anolyte compartment configured with an anode and containing an anolyte solution comprising an alkali metal monosulfide, an alkali metal polysulfide, or a mixture thereof and an anolyte solvent that partially dissolves elemental sulfur, the anolyte compartment further comprising an anolyte solution inlet and an anolyte solution outlet;
a catholyte compartment configured with a cathode and containing a catholyte, wherein the catholyte comprises a molten alkali metal, the catholyte compartment further comprising a catholyte outlet;
an alkali ion conductive membrane configured to selectively transport alkali ions, wherein the alkali ion conductive membrane is substantially impermeable to anions, the anolyte solvent, and dissolved sulfur;
a source of electric potential electrically coupled to the anode and the cathode and configured to:
oxidize the alkali metal monosulfide or polysulfide in the anolyte compartment to form liquid elemental sulfur and alkali metal ions;
cause the alkali metal ions to pass through the alkali ion conductive membrane from the anolyte compartment to the catholyte compartment; and
reduce the alkali metal ions in the catholyte compartment to form liquid elemental alkali metal;
an elemental sulfur settling zone where the liquid elemental sulfur forms a second liquid phase and separates from the anolyte solution; and
a sulfur outlet for removal of the liquid elemental sulfur from the electrolytic cell disposed at a location lower than the anolyte solution outlet.
2. The electrolytic cell according to claim 1 , wherein the alkali ion conductive membrane comprises in part an alkali metal conductive ceramic or glass ceramic.
3. The electrolytic cell according to claim 1 , wherein the alkali ion conductive membrane comprises a solid MSICON (Metal Super Ion CONducting) material, where M is Na or Li.
4. The electrolytic cell according to claim 1 , wherein the anolyte solvent comprises one or more solvents selected from N,N-dimethylaniline, quinoline, tetrahydrofuran, 2-methyl tetrahydrofuran, benzene, cyclohexane, fluorobenzene, thrifluorobenzene, toluene, xylene, tetraethylene glycol dimethyl ether (tetraglyme), diglyme, isopropanol, ethyl propional, dimethyl carbonate, dimethoxy ether, dimethylpropyleneurea, formamide, methyl formamide, dimethyl formamide, acetamide, methyl acetamide, dimethyl acetamide, triethylamine, diethyl acetamide, ethanol and ethyl acetate, propylene carbonate, ethylene carbonate, and diethyl carbonate.
5. The electrolytic cell according to claim 1 , wherein the anolyte solvent comprises from about 60-100 vol. % polar solvent and 0-40 vol. % apolar solvent.
6. A plurality of coupled electrolytic cells comprising a first electrolytic cell according to claim 1 and a second electrolytic cell according to claim 1 , wherein the anolyte solution inlet of the second electrolytic cell is connected to the anolyte solution outlet of the first electrolytic cell.
7. A plurality of coupled electrolytic cells comprising a first electrolytic cell according to claim 1 , a second electrolytic cell according to claim 1 , a third electrolytic cell according to claim 1 , and a fourth electrolytic cell according to claim 1 , wherein the anolyte solution inlet of the fourth electrolytic cell is connected to the anolyte solution outlet of the third electrolytic cell, wherein the anolyte solution inlet of the third electrolytic cell is connected to the anolyte solution outlet of the second electrolytic cell, and wherein the anolyte solution inlet of the second electrolytic cell is connected to the anolyte solution outlet of the first electrolytic cell.