5h-furan-2-one derivatives stabilization of organic material
US-2016362535-A1 · Dec 15, 2016 · US
US9988574B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9988574-B2 |
| Application number | US-201314387501-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 27, 2013 |
| Priority date | Mar 30, 2012 |
| Publication date | Jun 5, 2018 |
| Grant date | Jun 5, 2018 |
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Process and station for stabilizing an aqueous solution of an iron salt of an organic acid with a ferric component and a ferrous component of less solubility than the ferric component, such as the aqueous solution based on the Fe 3+ salt of meso-tartaric acid. To stabilize the content of the dissolved ferric salt, the solution is at least partly subjected to electrolytic oxidation.
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The invention claimed is: 1. A process for stabilizing an aqueous solution comprising an iron complex of an organic acid with a ferric component and a ferrous component of less solubility than the ferric component, the process comprising at least partly subjecting the aqueous solution to electrolytic oxidation, wherein the aqueous solution has a pH between 3 and 5. 2. The process according to claim 1 , wherein the aqueous solution comprises an Fe3+ complex of meso-tartaric acid. 3. The process according to claim 2 , wherein the electrolytic oxidation is carried out in at least one electrolytic cell, with a separated anode and cathode. 4. The process according to claim 3 , wherein the aqueous solution comprises FeMTA and is circulated along the anode of one or more of the at least one electrolytic cells. 5. The process according to claim 3 , wherein the anode and cathode are separated by a porous or a non-porous separator. 6. The process according to claim 5 , wherein the anode and cathode are separated by a non-porous separator comprising at least one of an anion exchange membrane or a cationic exchange membrane. 7. The process according to claim 6 , wherein the aqueous solution comprises FeMTA and is circulated along the anode of one or more of the at least one electrolytic cells. 8. The process according to claim 6 , wherein the aqueous solution comprises FeMTA and has an iron content below 5 wt. % by weight of the total solution, and wherein the electrolytic oxidation is carried out to maintain the Fe2+ content below 3 wt. % by weight of the total iron content. 9. The process according to claim 6 , wherein the electrolytic cell comprises a catholyte of 1-3 M HCl aqueous solution. 10. The process according to claim 9 , wherein the aqueous solution comprises FeMTA and is circulated along the anode of one or more of the at least one electrolytic cells. 11. The process according to claim 1 , wherein the aqueous solution comprises FeMTA and has an iron content below 5 wt. % by weight of the total solution, and wherein the electrolytic oxidation is carried out to maintain the Fe2+ content below 3 wt. % by weight of the total iron content. 12. The process according to claim 1 , wherein at least 50 wt. % of the Fe2+ in the aqueous solution is oxidized to Fe3+. 13. The process according to claim 1 , wherein at least 90 wt. % of the Fe2+ in the aqueous solution is oxidized to Fe3+. 14. A station for preparing an aqueous solution, wherein the station comprises at least one electrolytic cell comprising the aqueous solution for the oxidation of Fe2+, and wherein the solution comprises an iron complex of an organic acid with a ferric component and a ferrous component of less solubility than the ferric component, and the aqueous solution has pH between 3 and 5. 15. The station according to claim 14 , wherein the at least one electrolytic cell comprises an anode, a cathode, and a separator separating the anode from the cathode. 16. The station according to claim 15 , wherein the separator is a non-porous anionic or cationic exchange membrane. 17. The station according to claim 16 , wherein the anode comprises a porous structure forming part of a circulation loop, and wherein the anode is at least partly positioned against the separator. 18. The station according to claim 16 , wherein an anolyte space between the anode and the separator is part of a circulation loop. 19. The station according to claim 18 , wherein the anode comprises a porous structure forming part of a circulation loop, and wherein the anode is at least partly positioned against the separator. 20. A dispensing station for dosing an aqueous solution of an iron complex of an organic acid with a ferric component on salt, wherein the dispensing station for dosing comprises at least one electrolytic cell comprising a aqueous solution for the oxidation of Fe2+, and wherein the solution comprises an iron complex of an organic acid with a ferric component and a ferrous component of less solubility than the ferric component, and the aqueous solution has a pH between 3 and 5.
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