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Processes for selectively removing sulfur-containing compounds from a gas are described herein. The processes generally include contacting a first gas including carbon dioxide and hydrogen sulfide with a scrub solution including ammonium bisulfite and ammonium sulfite in a first contact zone to prod

Processes for selectively removing sulfur-containing compounds from a gas are described herein. The processes generally include contacting a first gas including carbon dioxide and hydrogen sulfide with a scrub solution including ammonium bisulfite and ammonium sulfite in a first contact zone to produce a first contact zone effluent liquid including ammonium thiosulfate and a first contact zone overhead gas including carbon dioxide.

대표청구항 ▼

The invention claimed is: 1. A process for selectively removing sulfur-containing compounds from a gas comprising: producing a scrub solution by contacting ammonia and sulfur dioxide with an aqueous solution in a second contact zone; contacting a first gas comprising carbon dioxide and hydrogen sul

The invention claimed is: 1. A process for selectively removing sulfur-containing compounds from a gas comprising: producing a scrub solution by contacting ammonia and sulfur dioxide with an aqueous solution in a second contact zone; contacting a first gas comprising carbon dioxide and hydrogen sulfide with the scrub solution comprising ammonium bisulfite and ammonium sulfite in the first contact zone to produce a first contact zone effluent liquid comprising ammonium thiosulfate and a first contact zone overhead gas comprising carbon dioxide; and controlling the pH in the second contact zone by modulating the amount of ammonia supplied to the second contact zone. 2. The process of claim 1 comprising controlling the amount of sulfur dioxide supplied to the second contact zone in response to the oxidation potential of the first contact zone effluent. 3. A process for selectively removing sulfur-containing compounds from a gas comprising: (a) contacting a first gas comprising carbon dioxide and hydrogen sulfide with a scrub solution comprising ammonium bisulfite and ammonium sulfite in a first contact zone to produce ammonium thiosulfate, the first contact zone producing a first contact zone overhead gas comprising carbon dioxide and a first contact zone effluent liquid comprising ammonium thiosulfate; (b) contacting a second gas comprising sulfur dioxide with a third gas, the third gas comprising ammonia, and a feed liquid, the feed liquid comprising at least a portion of the first contact zone effluent liquid, in a second contact zone to produce ammonium bisulfite and ammonium sulfite, the second contact zone producing a second contact zone effluent liquid comprising ammonium bisulfite and ammonium sulfite; (c) controlling the sulfite concentration of the feed liquid; and (d) feeding at least a portion of the second contact zone effluent liquid to the first contact zone as the scrub solution. 4. The process of claim 3 comprising: measuring the oxidation potential of the first contact zone effluent liquid; and modulating the amount of sulfur dioxide supplied to second contact zone in response to the oxidation potential to control the sulfite concentration of the first contact zone effluent liquid. 5. The process of claim 3 comprising: measuring the sulfite concentration of first contact zone effluent liquid with an infrared analyzer; and modulating the amount of sulfur dioxide supplied to the second contact zone in response to the measured sulfite concentration of the first contact zone effluent liquid. 6. The process of claim 3 comprising: contacting the first contact zone overhead gas with a solvent in a first solvent scrubber to remove carbon dioxide from the first contact zone overhead gas, the first solvent scrubber producing a first solvent scrubber overhead gas and a first solvent scrubber effluent liquid; and regenerating the first solvent scrubber effluent liquid to produce a regeneration overhead gas comprising carbon dioxide. 7. The process of claim 6 comprising: contacting the regeneration overhead gas comprising hydrogen sulfide and carbon dioxide with at least a portion of the second contact zone effluent liquid in a third contact zone to produce a third contact zone overhead gas comprising carbon dioxide and a third contact zone effluent liquid comprising ammonium thiosulfate. 8. The process of claim 7 comprising: combining the third contact zone effluent liquid with at least a portion of the first contact zone effluent liquid to form the feed liquid supplied to the second contact zone. 9. The process of claim 8 comprising: measuring the oxidation potential of the feed liquid; and modulating the amount of sulfur dioxide supplied to the second contact zone in response to the oxidation potential. 10. The process of claim 3 wherein the second gas supplied to the second contact zone is a Claus unit tail gas. 11. The process of claim 10 wherein the Claus unit tail gas is oxidized prior to entering the second contact zone. 12. The process of claim 10 wherein the second gas is treated with a sulfur dioxide-removal solvent in a second solvent scrubber prior to the second contact zone. 13. The process of claim 12 comprising bypassing the second solvent scrubber with a portion of the second gas to form a bypass gas. 14. The process of claim 13 comprising controlling the oxidation potential of the portion of the feed liquid to the second contact zone by modulating the flow rate of the bypass gas. 15. The process of claim 13 comprising: measuring the concentration of sulfite in the feed liquid with an infrared analyzer; and controlling the concentration of sulfite in the feed liquid by modulating the flow rate of the bypass gas. 16. The process of claim 12 comprising: regenerating the sulfur dioxide-removal solvent in a second solvent regenerator; and controlling the amount of sulfur dioxide removed from the second gas by adjusting the amount of sulfur dioxide released from the sulfur dioxide-removal solvent during regeneration. 17. The process of claim 16 wherein the amount of sulfur dioxide released from the sulfur dioxide-removal solvent is adjusted by modulating the amount of heat added to the second solvent regenerator. 18. The process of claim 16 wherein the amount of sulfur dioxide released from the sulfur dioxide-removal solvent is adjusted by modulating the flow rate of the sulfur dioxide-removal solvent. 19. The process of claim 16 comprising: measuring the oxidation potential of the feed liquid to the second contact zone; and modulating the amount of heat added to a second solvent regenerator reboiler in response to the oxidation potential. 20. The process of claim 16 comprising: measuring the sulfite concentration of the feed liquid to the second contact zone with an infrared analyzer; and controlling the amount of heat added to the second solvent regenerator reboiler in response to the sulfite concentration. 21. The process of claim 3 comprising distilling sour water in a second fractionator to produce the ammonia supplied to the second contact zone in the third gas. 22. The process of claim 21 comprising fractionating the sour water in a first fractionator prior to entering the second fractionator to produce a top gas comprising hydrogen sulfide. 23. The process of claim 3 comprising controlling the pH in the second contact zone by modulating the amount of ammonia supplied to the second contact zone. 24. A process for selectively removing sulfur-containing compounds from a gas comprising: (a) contacting a first gas comprising carbon dioxide and hydrogen sulfide with a scrub solution comprising ammonium bisulfite and ammonium sulfite in a first contact zone to produce ammonium thiosulfate, the first contact zone producing a first contact zone overhead gas comprising carbon dioxide and a first contact zone effluent liquid comprising ammonium thiosulfate; (b) contacting a second gas comprising sulfur dioxide with a third gas, the third gas comprising ammonia, and a feed liquid in a second contact zone to produce ammonium bisulfite and ammonium sulfite, the second contact zone producing a second contact zone overhead gas and a second contact zone effluent liquid comprising ammonium bisulfite and ammonium sulfite; (c) feeding at least a portion of the second contact zone effluent liquid to the first contact zone as the scrub solution; (d) contacting the first contact zone overhead gas with a first solvent in a first solvent scrubber to remove carbon dioxide and hydrogen sulfide from the first contact zone overhead gas, the first solvent scrubber producing a first solvent scrubber overhead gas and a first solvent scrubber effluent liquid; (e) regenerating the first solvent scrubber effluent liquid to produce a regeneration overhead gas comprising carbon dioxide and hydrogen sulfide; (f) contacting the regeneration overhead gas with a second portion of the second contact zone effluent liquid in a third contact zone to produce a third contact zone overhead gas comprising carbon dioxide and a third contact zone effluent liquid comprising ammonium thiosulfate; (g) combining the third contact zone effluent liquid with the first contact zone effluent liquid to form the feed liquid to the second contact zone; and (h) removing a portion of the feed liquid as product. 25. The process of claim 24 comprising: measuring the oxidation potential of the feed liquid; and controlling the oxidation potential of the feed liquid by modulating the amount of sulfur dioxide supplied to the second contact zone. 26. The process of claim 24 comprising: treating the second gas with a sulfur-removal solvent in a second solvent scrubber prior to the second contact zone; bypassing the second solvent scrubber with a portion of the second gas; and controlling the oxidation potential of the feed solution by modulating the flow rate of the bypassed portion of the second gas.