Chromatographic separation of ammonium sulfate and 2-hydroxy-2-methylpropionic acid
The invention relates to a process for the chromatographic purification of a starting stream containing ammonium sulfate and 2-hydroxy-2-methylpropionic acid, comprising: passage of the starting stream through a bed of stationary phase; elution of a raffinate enriched in ammonium sulfate and depleted in 2-hydroxy-2-methylpropionic acid; and elution of an extract enriched in 2-hydroxy-2-methylpropionic acid and depleted in ammonium sulfate.
1. A process for the chromatographic purification of a starting stream containing ammonium sulfate and 2-hydroxy-2-methylpropionic acid, comprising:
passing said starting stream through a bed of stationary phase;
elution of a raffinate enriched in ammonium sulphate and depleted in 2-hydroxy-2-methylpropionic acid; and
elution of an extract enriched in 2-hydroxy-2-methylpropionic acid and depleted in ammonium sulphate.
2. The process as claimed in claim 1 , wherein the purification is performed by ion-exclusion chromatography.
3. The process as claimed in claim 1 , wherein the stationary phase is a cationic resin.
4. The process as claimed in claim 1 , wherein the stationary phase consists of particles with a size Dv50 of between 200 and 350 μm.
5. The process as claimed in claim 1 , wherein the stationary phase is pre-equilibrated with a solution containing ammonium ions.
6. The process as claimed in claim 1 , wherein the starting stream is at a pH of from 1 to 4 during its passage through the bed of stationary phase.
7. The process as claimed in claim 1 , wherein an eluent is passed through the bed of stationary phase for the elution of the raffinate and the elution of the extract, said eluent being demineralized water or acidified demineralized water, at a pH of from 3 to 5, the acidified demineralized water having an acid content of 0.0005 to 5 g/L.
8. The process as claimed in claim 1 , which is performed at a temperature of from 20 to 85° C.
9. The process as claimed in claim 1 , performed on a multi- column chromatographic system.
10. The process as claimed in claim 9 , wherein the chromatographic system comprises a zone 4 located between a raffinate collection line and an eluent injection line, zone 4 being traversed by a volume of mobile phase of between 0.3 and 0.55 BV.
11. The process as claimed in claim 9 , wherein the multi-column chromatographic system comprises less than 12 columns.
12. The process as claimed in claim 9 , wherein the multi-column chromatographic system comprises columns with a diameter of greater than or equal to 2 meters.
13. The process as claimed in claim 9 , wherein the multi-column chromatographic system comprises columns having a length of between 1 and 2.5 meters.
14. The process as claimed in claim 1 , which is performed with a mean elution operating speed of greater than 1 m/h.
15. The process as claimed in claim 1 , wherein the starting stream is derived from a methyl methacrylate production process, said methyl methacrylate production process comprising the steps of:
reacting acetone cyanohydrin with sulfuric acid to prepare methacrylamide sulfate;
reacting said methacrylamide sulfate with a mixture of water and methanol to prepare methyl methacrylate;
collecting an acidic effluent;
neutralizing the acidic effluent with ammonia; and
crystallizing the neutralized acid effluent to obtain ammonium sulfate crystals and a crystallization purge, this crystallization purge providing said starting stream.
16. The process as claimed in claim 3 , wherein the stationary phase is a strong cationic resin in NH 4 + counterion form.
17. The process as claimed in claim 1 , wherein the stationary phase is pre-equilibrated with the starting stream.
18. The process as claimed in claim 8 , which is performed at a temperature of from 50 to 80° C.
19. The process as claimed in claim 9 , performed on a multi-column chromatography system selected from the group consisting of a simulated moving bed system, and a sequential simulated moving bed system.