Process for preparing choline hydroxide from trimethylamine and ethylene oxide
View Patent ↗Processes for preparing N,N,N-trimethylethanolammonium hydroxide (choline hydroxide) and the choline hydroxide produced are described. These processes minimize the production of byproduct mono-ethoxylated and di-ethyoxylated choline in the product choline hydroxide. The processes generally include feeding ethylene oxide, trimethylamine, and water into a first reactor to create a first reactor product under temperature controlled conditions. The product of the first reactor is fed into a second reactor to form a second reactor product under uncontrolled, adiabatic, conditions. Finally, any unreacted trimethylamine in the second reactor product is removed to form a final product comprising choline hydroxide. Additional reactors can be used for the ethylene oxide and trimethylamine reaction.
1. A process for preparing choline hydroxide comprising: feeding ethylene oxide, trimethylamine, and water into a first reactor to create a first reactor product, wherein the first reactor temperature is maintained between 5° C. and 35° C. and the molar ratio of ethylene oxide to trimethylamine fed to the first reactor is equal to or less than one; feeding the first reactor product into a second reactor to form a second reactor product, wherein the second reactor is insulated; and removing any unreacted trimethylamine from the second reactor product to form a final product comprising choline hydroxide.
2. The process of claim 1 , wherein the choline hydroxide final product comprises less than 10 weight percent mono-ethoxylated choline and/or di-ethyoxylated choline.
3. The process of claim 1 , wherein the trimethylamine and water are fed into the first reactor as a mixture.
4. The process of claim 1 , wherein the residence time in the second reactor is sufficient for any unreacted ethylene oxide present in the first reactor product to react.
5. The process of claim 1 , wherein adiabatic heating in the second reactor raises the temperature of the second reactor product to between 15° and 45° C.
6. The process of claim 1 , wherein the first reactor is a continuously stirred tank reactor.
7. The process of claim 1 , wherein the first reactor is a loop reactor with a high internal recycle ratio provided by a pump.
8. The process of claim 1 , wherein the first reactor is maintained at 20° C.
9. The process of claim 1 , wherein the unreacted trimethylamine is added to the trimethylamine fed into the first reactor.
10. A process for preparing choline hydroxide comprising: feeding trimethylamine, water, and ethylene oxide into a first reactor to create a first reactor product, wherein the first reactor temperature is maintained between 5° and 35° C.; feeding the first reactor product and a second amount of ethylene oxide into a second reactor to form a second reactor product, wherein the second reactor temperature is maintained between 5° and 35° C.; feeding the second reactor product into a third reactor to form a third reactor product, wherein the third reactor is insulated; and removing any unreacted trimethylamine from the third reactor product to form a final product comprising choline hydroxide.
11. The process of claim 10 , wherein the choline hydroxide final product comprises less than 10 weight percent mono-ethoxylated choline and/or di-ethyoxylated choline.
12. The process of claim 10 , wherein the trimethylamine and water are fed into the first reactor as a mixture.
13. The process of claim 10 , wherein the residence time in the third reactor is sufficient for any unreacted ethylene oxide present in the second reactor product to react.
14. The process of claim 10 , wherein adiabatic heating in the third reactor raises the temperature of the third reactor product to between 15° and 45° C.
15. The process of claim 10 , wherein the second amount of ethylene oxide fed into the second reactor is split from the ethylene oxide fed into the first reactor.
16. The process of claim 10 , wherein the ratio of amount of ethylene oxide fed into the first reactor to the second amount of ethylene oxide fed into the second reactor is between 50:50 and 99:1.
17. The process of claim 10 , wherein the ratio of amount of ethylene oxide fed into the first reactor to the second amount of ethylene oxide fed into the second reactor is 90:10.
18. The process of claim 10 , wherein the first reactor and second reactor are continuously stirred tank reactors.
19. The process of claim 10 , wherein the first reactor and second reactor are loop reactors with high internal recycle ratios provided by a pump.
20. The process of claim 10 , wherein the first reactor and second reactor are maintained at 20° C.
21. The process of claim 10 , wherein the unreacted trimethylamine is added to the trimethylamine fed into the first reactor.
22. The method of claim 1 , wherein the second reactor allows for uncontrolled adiabatic heating.