Purification of acetic acid product streams
In one embodiment, the invention is to an ion exchange resin composition comprising a metal-functionalized exchange resin comprising from 3% to 94% metal-functionalized active sites; and a non-metal-functionalized exchange resin comprising non-metal-functionalized active sites.
1. A process for purifying a crude acetic acid composition comprising acetic acid, iodides, and corrosion metals, the process comprising:
contacting the crude acetic acid composition with an ion exchange resin composition comprising:
a mixture comprising:
(a) a metal ion-functionalized exchange resin comprising from 3% to 94% metal ion-functionalized active sites; and
(b) a non-metal ion-functionalized exchange resin comprising non-metal ion-functionalized active sites, wherein the percentages are based on the total number of sites of the metal ion-functionalized exchange resin and the non-metal ion-functionalized exchange resin;
wherein the non-metal ion-functionalized exchange resin does not contain any metal ion-functionalized active sites; and
wherein the non-metal ion-functionalized exchanged resin optionally comprises non-metal ion functionalization
to form a purified acetic acid product.
2. The process of claim 1 , wherein the amounts of (a) and (b) correspond, within a ±25% margin of error, to the iodide content and a corrosion metal content, respectively, in the crude acetic acid composition.
3. The process of claim 1 , wherein the ratio of metal ion-functionalized active sites to non-metal ion-functionalized active sites corresponds, within a ±25% margin of error, to the molar ratio of iodides to corrosion metals in the crude acetic acid composition.
4. The process of claim 1 , wherein the ratio of non-metal ion-functionalized active sites to metal ion-functionalized active sites ranges from 1:0.05 to 1:35.
5. The process of claim 1 , wherein the ion exchange resin composition comprises at least 3% metal ion-functionalized active sites, and at least 3% non-metal ion-functionalized active sites.
6. The process of claim 1 , wherein the ion exchange resin composition comprises at least 10% metal ion-functionalized active sites, and at least 10% non-metal ion-functionalized active sites.
7. The process of claim 1 , wherein the ion exchange resin composition comprises:
from 1 wt. % to 99 wt. % metal ion-functionalized exchange resin; and
from 1 wt. % to 99 wt. % non-metal ion-functionalized exchange resin.
8. The process of claim 1 , wherein the ion exchange resin composition comprises:
from 10 wt. % to 90 wt. % metal ion-functionalized exchange resin; and
from 10 wt. % to 90 wt. % non-metal ion-functionalized exchange resin.
9. The process of claim 1 , wherein the ion exchange resin composition comprises:
from 25 wt. % to 75 wt. % metal ion-functionalized exchange resin; and
from 25 wt. % to 75 wt. % non-metal ion-functionalized exchange resin.
10. The process of claim 1 , wherein the metal content of the ion exchange resin composition ranges from 1 wt. % to 35 wt. %.
11. The process of claim 1 , wherein the metal ion-functionalized exchange resin is functionalized with a metal ion selected from the group consisting of mercury, palladium, and rhodium.
12. The process of claim 1 , wherein the metal ion-functionalized exchange resin is functionalized with silver ion.
13. The process of claim 1 , wherein the ion exchange resin composition comprises a base resin selected from the group consisting of polystyrene, styrene/divinyl benzene polymer, polyvinyl pyrrolidone, polyvinyl pyridine, and macroreticulated strong acid cation exchange resins.
14. The process of claim 1 , wherein the ion exchange resin composition comprises a base resin comprising styrene/divinyl benzene polymer, and wherein the metal-functionalized exchange resin is functionalized with silver ion.
15. The process of claim 1 , wherein the metal ion-functionalized exchange resin comprises a first base resin and the non-metal ion-functionalized exchange resin comprises a second base resin, different from the first base resin.
16. The process of claim 1 , wherein the metal ion-functionalized exchange resin comprises a first base resin and the non-metal ion-functionalized exchange resin comprises a second base resin, and wherein the first and second base resins are the same material.
17. The process of claim 1 , wherein the contacting is conducted at a temperature ranging from 25° C. to 120° C.
18. The process of claim 1 , wherein the purified acetic acid product comprises:
less than 100 wppb iodides; and
less than 1,000 wppb corrosion metals and/or
wherein at least 25 wt. % of the iodides and at least 25 wt. % of the corrosion metals are removed from the crude acetic acid product.
19. The process of claim 1 , wherein the crude acetic acid product is produced via a carbonylation method in which the concentration of water maintained in a liquid reaction composition ranges from 0.1 wt. % to 10 wt. %.
20. A guard bed for purifying a crude acetic acid composition comprising acetic acid, iodides, and corrosion metals, the guard bed comprising an ion exchange resin composition comprising:
a mixture comprising:
(a) a metal ion-functionalized exchange resin comprising from 3% to 94% metal ion-functionalized active sites; and
(b) a non-metal ion-functionalized exchange resin comprising non-metal ion-functionalized active sites, wherein the percentages are based on the total number of sites of the metal ion-functionalized exchange resin and the non-metal ion-functionalized exchange resin;
wherein the non-metal ion-functionalized exchange resin does not contain any metal ion-functionalized active sites; and
wherein the non-metal ion-functionalized exchanged resin optionally comprises non-metal ion functionalization.