System and process for removal of organic carboxylates from mono ethylene glycol (MEG) water streams by acidification and vaporization under vacuum
A system and method for removing organic carboxylates from a mono ethylene glycol (“MEG”) stream includes a reaction vessel; means for cooling and diluting the MEG stream being routed to the reaction vessel; means for acidifying the cooled and diluted MEG stream during its residence time within the reaction vessel; and means for removing an acetic-rich overhead stream from the reaction vessel. The acidification of the cooled and diluted MEG stream occurs under a vacuum. The reaction vessel may be located downstream of a calcium removal vessel and receive a filtered bottom stream from that vessel, or it may be a single reaction vessel that cycles between a calcium removal mode and an acetate removal mode, with the pressure of the single vessel being greater during the calcium removal mode than during the acetate removal mode.
1. A process for removal of organic carboxylates from a mono ethylene glycol (“MEG”) stream, the system comprising:
routing a MEG stream having organic carboxylates in solution to a reaction vessel;
cooling and diluting the MEG stream being routed to the reaction vessel to a lower % wt MEG and a lower temperature than an upstream % wt MEG and temperature of the MEG stream;
acidifying the cooled and diluted MEG stream during its residence time within the reaction vessel to a pH no less than 3.5, the organic carboxylates remaining in solution as carboxylic acid; and
removing in a vapor phase a carboxylic acid-rich overhead stream from the reaction vessel.
2. The process according to claim 1 wherein the reaction vessel is located downstream of a calcium removal vessel within a MEG recycle loop, the process further comprising a step of routing a bottom stream from the calcium removal vessel to the reaction vessel.
3. The process according to claim 1 further comprising a step of raising the alkalinity of the MEG stream prior to its residence time within the reaction vessel.
4. The process according to claim 3 wherein the raising alkalinity step includes adding at least one of sodium carbonate, potassium carbonate, sodium hydroxide, and potassium hydroxide of said MEG stream.
5. The process according to claim 1 wherein the reaction vessel is at a pressure in a range of 0.1 to 0.3 bar.
6. The process according to claim 1 wherein the pH is not greater than 5.5.
7. The process according to claim 1 wherein the acidifying step includes hydrochloric acid.
8. The process according to claim 1 wherein the lower % wt MEG is below 80 wt % MEG.
9. The process according to claim 8 wherein the lower % wt MEG is about 50 wt % MEG.
10. The process according to claim 1 wherein the lower temperature is a temperature in a range of 80° to 100° C.
11. The process according to claim 1 wherein the cooling and diluting the MEG stream step includes water.
12. The process according to claim 1 wherein the acidification of the cooled and diluted MEG stream occurs under a vacuum.
13. A process for removal of organic carboxylates from a mono ethylene glycol (“MEG”) stream, the process comprising:
acidifying the MEG stream during its residence time within a reaction vessel, the MEG stream having organic carboxylates including at least organic acetates in solution and a lower wt % MEG and a lower temperature within the reaction vessel than upstream of the reaction vessel, the organic acetates remaining in solution during the residence time as acetic acid, the acidifying step resulting in the MEG stream having a pH in a range of 3.5 to 5.5; and
removing when in vapor phase said acetic acid in an acetate-rich overhead stream from the reaction vessel;
wherein the acidification of the MEG stream occurs under a vacuum.
14. The process according to claim 13 wherein the vacuum is a pressure in a range of 0.1 to 0.3 bar.
15. The process according to claim 13 wherein the acidifying step includes hydrochloric acid.
16. The process according to claim 13 wherein the lower wt % MEG is below 80 wt % MEG.
17. The process according to claim 13 wherein the lower wt % MEG is about 50 wt % MEG.
18. The process according to claim 13 wherein the lower temperature is in a range of 80° to 100° C.
19. A process for removal of organic acetates from a mono ethylene glycol (“MEG”) stream, the system comprising:
raising the alkalinity of the MEG stream to convert said organic acetates to acetate salt in solution;
routing said MEG stream having acetate salt in solution to a reaction vessel;
cooling and diluting said MEG stream being routed to the reaction vessel to a lower % wt MEG and a lower temperature than an upstream % wt MEG and temperature of the MEG stream;
acidifying the cooled and diluted MEG stream at sub-ambient pressure during its residence time within the reaction vessel to a pH no less than 3.5, the acetate salt being converted to acetic acid; and,
removing a vapor phase overhead stream including said acetic acid from the reaction vessel.
20. The process according to claim 19 wherein the reaction vessel is at a pressure in a range of 0.1 to 0.3 bar.