Method for producing medical and commercial grade poly-gamma-glutamic acid of high molecular weight
Methods for producing high molecular weight poly-gamma-glutamic acid (PGA). The PGA is produced by fermentation, and purified by use of tangential flow filtration, followed by diafiltration, as necessary, to yield a product of the desired purity. Product obtained may be of very high purity using all the prescribed purification steps. Product of this purity is suitable for in vivo medical applications. Other applications, such as food or agricultural, may utilize lower purity levels, and hence do not require all the purification steps specified.
1. A method for producing poly-gamma-glutamic acid (PGA), comprising:
fermenting a Bacillus in a fermentation broth to allow production by the Bacillus of PGA, wherein the fermentation increases the broth viscosity;
terminating the fermentation when the broth viscosity ceases to substantially increase;
buffer exchanging the fermentation broth via diafiltration using a filter having a molecular weight cutoff of at least 30 kDA and less than 100 kDa;
lowering pH of the buffer exchanged solution to about 2 or less;
removing-the Bacillus cells from the buffer exchanged fermented broth comprising filtering the Bacillus cells from the buffer exchanged fermented broth using a filter with a pore opening of about 0.22 microns or less; and
neutralizing the pH of the resulting cell free, buffer exchanged fermentation broth.
2. The method of claim 1 , wherein the Bacillus is a Bacillus licheniformis.
3. The method of claim 2 , wherein the Bacillus is Bacillus licheniformis ATCC 9945a.
4. The method of claim 1 , wherein the fermentation broth comprises glutamic acid, citric acid, glycerol, ammonium sulfate, dipotassium phosphate, magnesium sulfate, manganese sulfate, and calcium chloride.
5. The method of claim 1 , wherein the fermentation is carried out at a temperature of about 37 C.
6. The method of claim 5 , wherein the fermentation is carried out with agitation using air at a flow of about 1 reactor volume per minute.
7. The method of claim 6 , wherein the fermentation is carried out in a pressurized vessel.
8. The method of claim 1 , wherein the fermentation is carried out for about three to five days.
9. The method of claim 1 , wherein the fermentation is terminated by decreasing the pH to about 2 or less.
10. The method of claim 1 , wherein the fermentation is terminated by beginning the buffer exchange step.
11. The method of claim 1 , wherein the step of adjusting the pH comprises buffering with citric acid.
12. The method of claim 1 , further comprising buffer exchanging the neutralized filtrate via diafiltration using a filter with a molecular weight cutoff of less than 100 kDa.
13. The method of claim 12 , wherein the diafiltration is carried out using a filter with a molecular weight cutoff of at least-30 kDa.
14. A method for producing poly-gamma-glutamic acid (PGA), comprising:
fermenting a Bacillus in a fermentation broth for sufficient time to allow production by the Bacillus of PGA;
terminating the fermentation when the broth viscosity ceases to substantially increase;
buffer exchanging the fermentation broth via diafiltration using a filter with a molecular weight cutoff of at least 30 kDa and less than 100 kDa;
lowering the pH of the buffer exchanged fermentation broth to about 2 or less;
removing the Bacillus cells from the lowered-pH, buffer exchanged fermented broth comprising filtering the Bacillus cells from the buffer exchanged fermented broth using a filter with a pore opening of about 0.22 microns or less;
neutralizing the pH of the cell-free buffer exchanged broth; and
buffer exchanging the cell-free fermentation broth via diafiltration using a filter with a molecular weight cutoff of at least 30 kDa and less than 100 kDa to concentrate the solution.
15. The method of claim 14 , wherein the fermentation is carried out in a pressurized vessel.
16. A method for producing poly-gamma-glutamic acid (PGA), comprising:
fermenting a Bacillus licheniformis ATCC 9945 a in a fermentation broth to allow production of by the Bacillus of PGA, wherein the fermentation is carried out in a pressurized vessel and the fermentation increases the broth viscosity;
terminating the fermentation when the broth viscosity ceases to substantially increase;
buffer exchanging the fermentation broth via diafiltration using a filter with a molecular weight cutoff of at least 30 kDa and less than 100 kDa;
lowering the pH of the buffer exchanged fermentation broth to about 2 or less;
filtering the Bacillus cells from the buffer exchanged fermented broth using a filter with a pore opening of about 0.22 microns or less; and
neutralizing the pH of the resulting filtrate.
17. The method of claim 16 , wherein the fermentation is carried out with agitation using air at a flow of about 1 reactor volume per minute.
18. The method of claim 16 , further comprising buffer exchanging the cell-free solution via diafiltration using a filter with a molecular weight cutoff of at least 30 kDa and less than 100 kDa to concentrate the solution.
19. The method of claim 1 , further comprising sterile filtering the resulting solution.
20. The method of claim 1 , further comprising freeze drying the resulting PGA.