Lactylate purification process
A method for separation of fatty acid from a mixture having fatty acid, the corresponding acyl lactylate and lactic acid, method having steps of: a) providing dispersion of mixture in polar carrier; b) adjusting dispersion mixture to pH from 5-9; and, c) extracting fatty acid from dispersion carrier mixture into solvent immiscible with polar carrier, obtaining fatty acid solution and aqueous raffinate having lactic acid and fatty acid lactylate. Polar carrier has from 70-100 wt. % of water and from 0-30 wt. % of one or more miscible, polar co-solvents. Aqueous raffinate may be further processed by: i) acidifying raffinate to pH from 0-3; and, either ii)a) allowing acidified raffinate to separate into two layers and separating lower, aqueous layer from residual layer of acyl lactylate, or ii)b) extracting fatty acid lactylate from acidified raffinate into second solvent which is immiscible with aqueous raffinate, obtaining an acyl lactylate solution.
1. A method for separation of fatty acid from a mixture comprising fatty acid, the corresponding acyl lactylate and lactic acid, said method comprising the steps of:
a) providing a dispersion of said mixture in a polar carrier;
b) adjusting the dispersion mixture to a pH of from 5 to 9; and,
c) extracting the fatty acid from the dispersion carrier mixture into a solvent immiscible with said polar carrier, thereby obtaining a fatty acid solution,
wherein said polar carrier comprises, by weight of said carrier, from 70 to 100 wt. % of water and from 0 to 30 wt. % of one or more miscible, polar co-solvents.
2. The method according to claim 1 , wherein the immiscible solvent has a boiling point less than 120° C. at atmospheric pressure.
3. The method according to claim 1 , wherein the immiscible solvent should be capable of dissolving said fatty acid in an amount of at least 5 wt. % based on the weight of the solvent.
4. The method according to claim 1 , wherein at least a portion of the immiscible solvent is distilled from said fatty acid solution and recycled to extraction step c).
5. The method according to claim 1 , wherein step c) is a multi-stage extraction.
6. A method for separating acyl lactylate from a mixture comprising said lactylate, the corresponding fatty acid and lactic acid, said method comprising the steps of:
a) providing a dispersion of said mixture in a polar carrier;
b) adjusting the dispersion mixture to a pH of from 5 to 9;
c) extracting the fatty acid from the dispersion carrier mixture into a first solvent which is immiscible with said polar carrier, thereby obtaining a fatty acid solution and an aqueous raffinate comprising lactic acid and fatty acid lactylate;
d) acidifying said raffinate to a pH of from 0 to 3; and,
e) allowing said acidified raffinate to separate into two layers and separating the lower, aqueous layer from the residual layer of acyl lactylate
wherein said polar carrier comprises, by weight of said carrier, from 70 to 100 wt. % of water and from 0 to 30 wt. % of one or more miscible, polar co-solvents.
7. A method for separating acyl lactylate from a mixture comprising said lactylate, the corresponding fatty acid and lactic acid, said method comprising the steps of:
a) providing a dispersion of said mixture in a polar carrier;
b) adjusting the dispersion mixture to a pH of from 5 to 9;
c) extracting the fatty acid from the dispersion carrier mixture into a first solvent immiscible with said polar carrier, thereby obtaining a fatty acid solution and an aqueous raffinate comprising lactic acid and fatty acid lactylate;
d) acidifying said raffinate to a pH of from 0 to 3; and,
f) extracting the fatty acid lactylate from the acidified raffinate into a second solvent which is immiscible with said aqueous raffinate, thereby obtaining an acyl lactylate solution,
wherein said polar carrier comprises, by weight of said carrier, from 70 to 100 wt. % of water and from 0 to 30 wt. % of one or more miscible, polar co-solvents.
8. The method according to claim 6 , wherein said first solvent has a boiling point of less than 120° C. at atmospheric pressure.
9. The method according to claim 6 , wherein at least a portion of said first solvent is distilled from the said fatty acid solution and recycled to extraction step c).
10. The method according to claim 7 , wherein said second solvent has a boiling point of less than 120° C. at atmospheric pressure.
11. The method according to claim 7 , wherein the first and second solvents are the same.
12. The method according to claim 7 , wherein at least a portion of said second solvent is distilled from the acyl lactylate solution and recycled to step f).
13. The method according to claim 7 , wherein at least one of step c) and step f) is a multi-stage extraction.
14. The method according to claim 1 , wherein the fatty acid chain of the acyl lactylate has an acyl group with 8-18 carbon atoms.
15. The method according to claim 1 , wherein said polar carrier comprises, by weight of said carrier:
from 80 to 100 wt. % of water; and,
from 0 to 20 wt. % of one or more miscible, polar co-solvents.