초록 ▼

The present invention provides a process for removing ammonia as an aqueous salt solution from an acid gas comprising ammonia and hydrogen sulfide. A strong acid, such as sulfuric acid, is used as a scrubbing agent to convert ammonia to an ammonium salt. Control of pH and stripping in combination wi

The present invention provides a process for removing ammonia as an aqueous salt solution from an acid gas comprising ammonia and hydrogen sulfide. A strong acid, such as sulfuric acid, is used as a scrubbing agent to convert ammonia to an ammonium salt. Control of pH and stripping in combination with reboiler or evaporators reduces hydrogen sulfide concentration. The ammonium salt is produced as an aqueous solution, which may crystallized to form a solid product. The ammonium salt solution or solid may be used as a fertilizer.

대표청구항 ▼

What is claimed is: 1. A process for removing ammonia from an acid gas comprising ammonia and hydrogen sulfide comprising: (a) contacting the acid gas with a strong acid, selected from the group consisting of sulfuric acid, phosphoric acid and nitric acid and with recycle solution at a pH less than

What is claimed is: 1. A process for removing ammonia from an acid gas comprising ammonia and hydrogen sulfide comprising: (a) contacting the acid gas with a strong acid, selected from the group consisting of sulfuric acid, phosphoric acid and nitric acid and with recycle solution at a pH less than 7, wherein recycle solution is a portion of the product ammonium salt solution, to produce a gas phase and an ammonium salt solution; (b) separating the gas phase from the solution; (c) feeding the solution from step (b) to a stripper to remove hydrogen sulfide, water, and hydrocarbons, if present in said acid gas to provide a purified concentrated ammonium salt solution and a gas component, wherein heat and driving force to remove said hydrogen sulfide, water, and hydrocarbons is supplied to said stripper by a reboiler, which circulates purified concentrated ammonium salt solution; and (d) contacting the purified ammonium salt solution exiting the stripper with a base to provide an ammonium salt solution having a pH between 6 and 8. 2. A process for removing ammonia from an acid gas comprising ammonia and hydrogen sulfide comprising: (a) contacting the acid gas with a strong acid, selected from the group consisting of sulfuric acid, phosphoric acid and nitric acid and with recycle solution at a pH less than 7, wherein recycle solution is a portion of the product ammonium salt solution, to produce a gas phase and an ammonium salt solution; (b) separating the gas phase from the solution; (c) feeding the solution from step (b) to an evaporator, to provide a gas phase and a concentrated ammonium salt solution; (d) feeding the concentrated ammonium salt solution to a steam stripper to remove residual hydrogen sulfide, water and hydrocarbons, if present, wherein steam provides driving force to remove said hydrogen sulfide, water and hydrocarbons from said concentrated salt solution to provide a purified concentrated ammonium salt solution and a gas component; and (e) contacting the purified ammonium salt solution exiting the stripper with a base to provide an ammonium salt solution having a pH between 6 and 8. 3. A process for removing ammonia from an acid gas comprising ammonia and hydrogen sulfide comprising: (a) contacting the acid gas with a strong acid, selected from the group consisting of sulfuric acid, phosphoric acid and nitric acid and with recycle solution at a pH less than 7, wherein recycle solution is a portion of the product ammonium salt solution, to produce a gas phase and an ammonium salt solution; (b) separating the gas phase from the solution; (c) feeding the solution from step (b) to an evaporator, to provide a gas phase and a concentrated ammonium salt solution; (d) feeding the concentrated ammonium salt solution to a gas stripper to remove residual hydrogen sulfide, water and hydrocarbons, if present, wherein carrier gas provides driving force to remove said hydrogen sulfide, water and hydrocarbons from said concentrated salt solution to provide a purified concentrated ammonium salt solution and a gas component; and (e) contacting the purified ammonium salt solution exiting the stripper with a base to provide an ammonium salt solution having a pH between 6 and 8. 4. A process according to claim 1, 2, or 3 further comprising feeding the ammonium salt solution having a pH between 6 and 8 to a crystallizer to produce a solid ammonium salt product. 5. A process according to claim 1, 2, or 3 wherein the strong acid is sulfuric acid. 6. A process according to claim 1, 2, or 3 wherein the strong acid is phosphoric acid. 7. A process according to claim 1, 2, or 3 wherein the strong acid is nitric acid. 8. A process according to claim 1, 2, or 3 wherein the base is ammonia or ammonium hydroxide. 9. A process according to claim 1, 2, or 3 wherein the base is potassium hydroxide. 10. A process according to claim 1, 2, or 3 wherein the ammonium salt solution produced in step (a) has a pH of 2 to 4. 11. A process according to claim 1, 2, or 3 wherein the gas phase produced in step (b) is further processed in a sulfur recovery unit furnace or in a spent acid recovery furnace. 12. A process according to claim 1 further comprising condensing the gas component produced in step (c) to provide a liquid comprising hydrogen sulfide and feeding the liquid to a sour water storage tank or a spent acid recovery furnace for further processing. 13. A process according to claim 2 or 3 further comprising condensing the gas component produced in step (d) to provide a liquid comprising hydrogen sulfide and feeding the liquid to a sour water storage tank or a spent acid recovery furnace for further processing. 14. A process according to claim 3 further comprising feeding the gas component produced in step (d) to a sulfur recovery unit furnace or a spent acid recovery furnace for further processing. 15. A process according to claim 3 wherein the carrier gas is air or nitrogen. 16. A process according to claim 15 wherein the carrier gas is air.