초록 ▼

Systems and methods of removing sulfur from a gas stream comprising hydrogen sulfide (H2S) are provided. The systems and methods may utilize iodine to remove sulfur from the gas stream. In certain systems and methods, the iodine may be regenerated. In particular, the present systems and methods may

Systems and methods of removing sulfur from a gas stream comprising hydrogen sulfide (H2S) are provided. The systems and methods may utilize iodine to remove sulfur from the gas stream. In certain systems and methods, the iodine may be regenerated. In particular, the present systems and methods may be capable of reducing sulfur content in a gas stream comprising hydrogen sulfide H2S gas to levels that are undetectable.

대표청구항 ▼

1. A method for treating hydrogen sulfide gas, comprising: reacting hydrogen sulfide gas with iodine to produce a stream comprising iodide and sulfur;removing sulfur from the stream to produce a separated stream comprising iodide; andreacting the separated stream comprising iodide with a source of o

1. A method for treating hydrogen sulfide gas, comprising: reacting hydrogen sulfide gas with iodine to produce a stream comprising iodide and sulfur;removing sulfur from the stream to produce a separated stream comprising iodide; andreacting the separated stream comprising iodide with a source of oxygen under aqueous conditions and at a predetermined temperature and a predetermined pressure to produce a stream comprising iodine. 2. The method of claim 1, further comprising recovering at least a portion of the iodine from the stream comprising iodine. 3. The method of claim 2, further comprising introducing at least a portion of the regenerated iodine to the hydrogen sulfide gas. 4. The method of claim 1, further comprising recovering elemental sulfur from the stream comprising iodide and sulfur. 5. The method of claim 1, wherein the source of oxygen is air. 6. The method of claim 1, wherein the predetermined temperature is in a range of from about 75° C. to about 260° C. 7. The method of claim 6, wherein the predetermined temperature is in a range of from about 120° C. to about 175° C. 8. The method of claim 1, wherein the predetermined pressure is in a range of from about 25 psi to about 2000 psi. 9. The method of claim 8, wherein the predetermined pressure is in a range of from about 100 psi to about 400 psi. 10. The method of claim 1, further comprising reacting the separated stream comprising iodide with a source of oxygen under aqueous conditions for a time period in a range of from about 15 minutes to about 120 minutes. 11. The method of claim 10, wherein the time period is less than about 15 minutes. 12. The method of claim 1, further comprising recovering thermal energy from the stream comprising iodine. 13. A system for treating hydrogen sulfide gas, comprising: a contactor fluidly connected to a source of hydrogen sulfide gas and a source of iodine;a separator fluidly connected downstream from the contactor and configured to separate elemental sulfur and iodide; anda wet air oxidation reactor fluidly connected downstream from the separator and the separated iodide and fluidly connected to a source of oxygen. 14. The system of claim 13, further comprising a control system configured to regulate a predetermined temperature and predetermined pressure of the wet air oxidation reactor. 15. The system of claim 13, further comprising at least one scrubber fluidly connected downstream from the wet air oxidation reactor and upstream from the source of iodine. 16. The system of claim 13, further comprising at least one energy recovery device fluidly connected downstream from the wet air oxidation reactor and upstream from the contactor and configured to recover thermal energy from the wet air oxidation reactor. 17. The system of claim 13, further comprising a wet air oxidation reactor outlet fluidly connected upstream from the contactor and configured to transfer at least a portion of regenerated iodine from the wet air oxidation reactor to the contactor. 18. The system of claim 17, wherein the rate of regeneration from iodide to regenerated iodine from the wet air oxidation reactor is at least 50%. 19. The system of claim 13, further comprising a scrubber fluidly connected downstream from the wet air oxidation reactor and configured to transfer at least a portion of regenerated iodine from the wet air oxidation reactor to the contactor. 20. The system of claim 13, further comprising at least one energy recovery device fluidly connected downstream from the separator and upstream from the wet air oxidation reactor.