Acesulfame potassium compositions and processes for producing same
US-10590096-B2 · Mar 17, 2020 · US
US10975047B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10975047-B2 |
| Application number | US-202016984356-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 4, 2020 |
| Priority date | Sep 21, 2016 |
| Publication date | Apr 13, 2021 |
| Grant date | Apr 13, 2021 |
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Improved processes for producing high purity acesulfame potassium. In one embodiment, the process comprises the steps of contacting a solvent, e.g., dichloromethane, and a cyclizing agent, e.g., sulfur trioxide, to form a cyclizing agent composition and reacting an acetoacetamide salt with the cyclizing agent in the composition to form a cyclic sulfur trioxide adduct. The contact time is less than 60 minutes. The process also comprises forming from the cyclic sulfur trioxide adduct composition a finished acesulfame potassium composition comprising non-chlorinated, e.g., non-chlorinated, acesulfame potassium and less than 35 wppm 5-halo acesulfame potassium, preferably less than 5 wppm.
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We claim: 1. A process for producing a finished acesulfame potassium composition, the process comprising: (a) providing a solvent at an initial temperature and a cyclizing agent at an initial temperature, wherein the cyclizing agent includes sulfur trioxide; (b) contacting the solvent and the cyclizing agent to form a cyclizing agent composition; (c) reacting an acetoacetamide salt with the cyclizing agent composition to form a cyclic sulfur trioxide adduct, wherein prior to being reacted with the acetoacetamide salt, the cyclizing agent composition has a temperature that is lower than the initial temperature of the cyclizing agent and/or the initial temperature of the solvent; and (d) hydrolyzing the cyclic sulfur trioxide adduct to form an acesulfame-H composition comprising acesulfame-H, neutralizing the acesulfame-H in the acesulfame-H composition to form a crude acesulfame potassium composition comprising non-chlorinated acesulfame potassium, forming a finished acesulfame potassium composition from the crude acesulfame potassium composition comprising non-chlorinated acesulfame potassium and less than 35 wppm 5-chloro-acesulfame potassium; wherein the contact time from the beginning of step (b) to the beginning of step (c) is less than 60 minutes. 2. The process of claim 1 , wherein the finished acesulfame potassium composition comprises from 0.001 wppm to 5 wppm 5-chloro-acesulfame potassium. 3. The process of claim 1 , wherein the hydrolyzing comprises adding water to the cyclic sulfur trioxide adduct to form a hydrolysis reaction mixture, and wherein the temperature of the hydrolysis reaction mixture is maintained at a temperature ranging from −35° C. to 0° C. 4. The process of claim 3 , wherein the finished acesulfame potassium composition comprises from 0.001 wppm to 5 wppm organic impurities. 5. The process of claim 1 , further comprising: reacting sulfamic acid and an amine to form an amidosulfamic acid salt; and reacting the amidosulfamic acid salt and acetoacetylating agent to form the acetoacetamide salt. 6. The process of claim 1 , wherein the finished acesulfame potassium composition comprises from 0.001 wppm to 2.7 wppm 5-chloro-acesulfame potassium. 7. The process of claim 1 , wherein the finished acesulfame potassium composition comprises from 0.001 wppm to 5 wppm organic impurities. 8. The process of claim 1 , wherein the finished acesulfame potassium composition comprises from 0.001 wppm to 5 wppm heavy metals. 9. The process of claim 1 , wherein the cyclizing agent composition comprises less than 1 wt % of compounds selected from chloromethyl chlorosulfate, methyl-bis-chlorosulfate, and mixtures thereof. 10. The process of claim 1 , wherein the reacting is conducted for a cyclization reaction time, from the start of a reactant feed to the end of the reactant feed, of less than 35 minutes. 11. The process of claim 1 , wherein the weight ratio of solvent to cyclizing agent in the cyclizing agent composition is at least 1:1. 12. The process of claim 1 , wherein the solvent comprises dichloromethane. 13. A finished acesulfame potassium composition produced from the process of claim 1 . 14. The finished acesulfame potassium composition of claim 13 , comprising: non-chlorinated acesulfame potassium; from 0.001 wppm to 2.7 wppm 5-chloro acesulfame potassium; and from 0.001 wppm to 5 wppm heavy metals. 15. The finished acesulfame potassium composition of claim 13 , wherein the finished composition contains less than 37 wppm acetoacetamide-N-sulfonic acid. 16. The finished acesulfame potassium composition of claim 13 , wherein the finished composition contains from 0.001 wppm to 5 wppm organic impurities and from 0.001 wppm to 5 wppm of at least one heavy metal. 17. The finished acesulfame potassium composition of claim 16 , wherein the heavy metal is selected from the group consisting of mercury, lead and mixtures thereof. 18. The finished acesulfame potassium composition of claim 17 , wherein mercury is present in the finished composition in an amount of 1 wppb to 20 wppm. 19. The finished acesulfame potassium composition of claim 17 , wherein lead is present in the finished composition in an amount of 1 wppb to 25 wppm. 20. The process of claim 1 , wherein the temperature of the cyclizing agent composition is at least 2° C. lower than the initial temperature of the solvent and/or the initial temperature of the cyclizing agent. 21. The process of claim 1 , further comprising cooling the cyclizing agent composition. 22. The process of claim 21 , wherein the cyclizing agent composition is cooled to a temperature of less than 35° C. 23. The process of claim 21 , wherein the cyclizing agent composition is cooled to a temperature of less than 15° C. 24. The process of claim 1 , further comprising cooling the solvent prior to contact with the cyclizing agent. 25. The process of claim 24 , wherein the solvent is cooled to a temperature that is at least 2° C. less than the initial temperature of the solvent. 26. The process of claim 24 , wherein the solvent is cooled to a temperature of less than 35° C. 27. The process of claim 24 , wherein the solvent is cooled to a temperature of less than 15° C. 28. The process of claim 1 , further comprising cooling the cyclizing agent prior to contact with the solvent. 29. The process of claim 28 , wherein the cyclizing agent is cooled to a temperature that is at least 2° C. less than the initial temperature of the cyclizing agent. 30. The process of claim 28 , wherein the cyclizing agent is cooled to a temperature of less than 35° C. 31. The process of claim 28 , wherein the cyclizing agent is cooled to a temperature of less than 15° C. 32. The process of claim 1 , wherein the temperature of the cyclizing agent composition is less than 35° C. prior to reacting with the acetoacetamide salt. 33. The process of claim 1 , wherein the temperature of the cyclizing agent composition is less than 15° C. prior to reacting with the acetoacetamide salt. 34. The process of claim 1 , wherein the contact time is less than 15 minutes. 35. The process of claim 34 , wherein the temperature of the cyclizing agent composition is less than 35° C. prior to reacting with the acetoacetamide salt. 36. The process of claim 35 , wherein the finished acesulfame potassium composition comprises from 1 wppb to 5 wppm 5-chloro-acesulfame potassium. 37. The process of claim 1 , wherein the contact time is less than 5 minutes. 38. The process of claim 37 , wherein the temperature of the cyclizing agent composition is less than 35° C. prior to reacting with the acetoacetamide salt. 39. The process of claim 38 , wherein the finished acesulfame potassium composition comprises from 1 wppb to 5 wppm 5-chloro-acesulfame potassium. 40. The process of claim 1 , further comprising forming the acetoacetamide salt by a process that comprises reacting sulfamic acid and triethylamine to form an amidosulfamic acid salt, and reacting the amidosulfamic acid salt and a diketene to the form acetoacetamide salt.
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