Process for separating monochloroacetic acid and dichloroacetic acid via extractive distillation
View Patent ↗The present invention pertains to a process for separating monochloroacetic acid and dichloroacetic acid from one another via extractive distillation, comprising the steps of (i) contacting a mixture comprising monochloroacetic acid and dichloroacetic acid with an extractive agent which is chemically stable and which has a BF 3 affinity of between 65 kJ/mole and 110 kJ/mole, (ii) distilling the mixture to obtain a monochloroacetic acid stream and a stream comprising dichloroacetic acid and the extractive agent, and (iii) regenerating the extractive agent.
1. A process for separating monochloroacetic acid and dichloroacetic acid from one another via extractive distillation, comprising the steps of
(i) contacting a mixture comprising monochloroacetic acid and dichloroacetic acid with an extractive agent which is chemically stable and which has a BF 3 affinity of between 65 kJ/mole and 110 kJ/mole, wherein the extractive agent is less volatile than the monochloroacetic acid and the dichloroacetic acid,
(ii) distilling the mixture to obtain a monochloroacetic acid stream and a stream comprising dichloroacetic acid and the extractive agent, and
(iii) regenerating the extractive agent.
2. The process according to claim 1 , wherein the extractive agent is selected from the group consisting of phosphine oxides, aldehydes, ketones, ethers, and amides.
3. The process according to claim 1 , wherein the extractive agent has a BF 3 affinity of between 75 kJ/mole and 90 kJ/mole.
4. The process according to claim 1 , wherein dichloroacetic acid is present in the mixture comprising monochloroacetic acid and dichloroacetic acid in an amount of at least 50 ppm, and wherein the mixture further comprises acetic acid.
5. The process according to claim 1 , wherein the mixture comprising monochloroacetic acid and dichloroacetic acid is contacted with the extractive agent at least one of prior to and during step (ii).
6. The process according to claim 1 , wherein the extractive agent is selected from the group consisting of tetraglyme, diethylene glycol dibutyl ether, dihexyl ether, diethylene glycol dipentyl ether, and dihexyl ketone.
7. The process according to claim 1 , wherein regenerated extractive agent is recycled to step (i).
8. The process according to claim 1 , wherein step (ii) is carried out in a distillation column, comprising a reboiler and a condenser.
9. The process according to claim 8 , wherein step (ii) is carried out at a pressure below 500 mbar and with a temperature at the bottom of said distillation column of below 453 K.
10. The process according to claim 1 , wherein in step (iii) the extractive agent is regenerated by stripping or distillation of the stream comprising dichloroacetic acid and the extractive agent.
11. The process according to claim 10 , wherein recovered dichloroacetic acid is subsequently subjected to a hydrogenation step to produce MCA.
12. The process according to claim 8 , wherein step (iii) is carried out in a distillation column at a pressure below 250 mbar and with a temperature at the bottom of said distillation column of below 493 K.
13. The process according to claim 1 , wherein the ratio between the extractive agent and dichloroacetic acid in step (i) is between 0.5 and 50, on a mole basis.
14. The process according to claim 1 , wherein at least steps (ii) and (iii) are carried out in a Petlyuk column or a divided wall column.
15. The process according to claim 1 , wherein dichloroacetic acid is present in the mixture comprising monochloroacetic acid and dichloroacetic acid in an amount of at least 500 ppm, and wherein the mixture further comprises acetic acid.
16. The process according to claim 2 , wherein the extractive agent is selected from the group consisting of tetraglyme, diethylene glycol dibutyl ether, dihexyl ether, diethylene glycol dipentyl ether, and dihexyl ketone.
17. The process according to claim 4 , wherein regenerated extractive agent is recycled to step (i).
18. The process according to claim 10 , wherein step (iii) is carried out in a distillation column at a pressure below 250 mbar and with a temperature at the bottom of said distillation column of below 493 K.
19. The process according to claim 6 , wherein the ratio between the extractive agent and dichloroacetic acid in step (i) is between 0.5 and 50, on a mole basis.
20. The process according to claim 13 , wherein at least steps (ii) and (iii) are carried out in a Petlyuk column or a divided wall column.