Regenerable solvent mixtures for acid-gas separation
US-9707510-B2 · Jul 18, 2017 · US
US12427471B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12427471-B2 |
| Application number | US-202218087359-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 22, 2022 |
| Priority date | Mar 2, 2012 |
| Publication date | Sep 30, 2025 |
| Grant date | Sep 30, 2025 |
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A solvent system for the removal of acid gases from mixed gas streams is provided. Also provided is a process for removing acid gases from mixed gas streams using the disclosed solvent systems. The solvent systems may be utilized within a gas processing system.
Opening claim text (preview).
The invention claimed is: 1. A solvent system for the removal of SO 2 from gas stream, consisting of: a nucleophilic amine, wherein the nucleophilic amine has a structure such that it reacts with SO 2 to form a Zwitterionic sulfamic acid; one or more Zwitterionic sulfamic acid reaction; optionally, water in an amount of less than about 10 weight percent; and optionally, one or more unreacted components of the gas stream. 2. The solvent system of claim 1 , wherein the nucleophilic amine is 3-fluoro-N-methylbenzylamine. 3. The solvent system of claim 1 , wherein the nucleophilic amine is hydrophobic. 4. The solvent system of claim 1 , wherein the solvent system is substantially immiscible with water. 5. The solvent system of claim 1 , wherein the solvent system has a solubility with water of less than about 20 g of solvent per 100 mL of water. 6. A process for the removal of SO 2 from a gas stream, comprising contacting the gas stream with the solvent system of claim 1 . 7. The process of claim 6 , wherein the solvent system tolerates water up to or equal to about 20% water by volume with no degradation of solvent performance. 8. The process of claim 6 , further comprising withdrawing a reaction product-rich solvent and a reaction component-lean gas stream. 9. The process of claim 8 , further comprising regenerating the reaction product-rich solvent by applying heat to form a regenerated solvent comprising a lower content of the one or more reaction products than present in the reaction product-rich solvent. 10. The process of claim 9 , wherein the applied heat is derived from a source selected from the group consisting of low-pressure steam, hot flue gas, or a combination thereof. 11. A solvent system for the removal of CO 2 and/or SO 2 from a gas stream, consisting of: 3-fluoro-N-methylbenzylamine; one or more reaction products of the 3-fluoro-N-methylbenzylamine and the CO 2 and/or SO 2 ; optionally, water in an amount of less than about 10 weight percent; and optionally, one or more unreacted components of the gas stream. 12. A process for the removal of CO 2 and/or SO 2 from a gas stream, comprising contacting the gas stream with the solvent system of claim 11 . 13. The process of claim 12 , wherein the solvent system tolerates water up to or equal to about 20% water by volume with no degradation of solvent performance.
Flue gases · CPC title
Carbon dioxide · CPC title
Nitrogen oxides other than dinitrogen oxide · CPC title
Carbonoxysulfide COS · CPC title
Sulfur oxides · CPC title
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