Quality test for polymerizable lactic acid and method for producing same

1. A process for separation and purification of polymerizable lactic acid from fermentation liquors, comprising:

a) separating biomass and any solids from the fermentation liquor, in at least two successive stages;

b) separating lactic acid solution from the biomass-free fermentation liquor by use of simulated moving bed chromatography (SMB);

c) purifying the separated lactic acid solution by a first ion exchange step;

d) subjecting the first-ion-exchange purified lactic acid solution to at least one of a first single or multistage partial evaporation step to obtain a lactic acid solution having less than a 100% concentration by weight of lactic acid;

e) purifying the lactic acid solution further by a second ion exchange step;

f) subjecting the second-ion-exchange purified lactic acid solution to at least one of a second single or multistage evaporation step.

2. The process of claim 1 , wherein the process exhibits a dilactide yield of >90% and a racemization of <5%.

3. The process of claim 2 , wherein the step of purifying the separated lactic acid solution by a first ion exchange step includes nanofiltering the lactic acid solution.

4. The process of claim 2 , wherein the step of separating biomass and any solids from the fermentation liquor is effected in a first stage by at least one of a precoat, a microfiltration, and a centrifugation.

5. The process of claim 4 , wherein the step of separating the biomass from the fermentation liquor is effected without decreasing the pH and without thermal inactivation.

6. The process of claim 4 , wherein during the step of separating biomass and any solids from the fermentation liquor, the time between ending of the fermentation and the separation of the biomass is less than 2 hours.

7. The process of claim 4 , wherein during the step of separating biomass and any solids from the fermentation liquor, the biomass concentration in the filtrate is not higher than 1 g/l.

8. The process of claim 2 , wherein a second stage in the step of separating biomass and any solids from the fermentation liquor includes ultrafiltering the fermentation liquor by at least one of a single-stage or a two-stage ultrafiltration having filtration membranes with a separation limit of 10 kDa.

9. The process of claim 8 , further comprising:

recirculating a retentate from the second stage ultrafiltration back to the first stage in the step of separating biomass and any solids; and

passing a permeate from the second stage ultrafiltration to subsequent process steps.

10. The process of claim 2 , further comprising:

adding concentrated sulfuric acid to the fermentation liquor from the first stage in the step of separating biomass and any solids, to create an acidified fermentation liquor having a pH of 4.4 to 4.6; and

adding concentrated sulfuric acid to an ultrafiltration permeate from the second stage in the step of separating biomass and any solids, to create an acidified ultra permeate having a pH of 2.0 to 2.4, so that a salt of lactic acid contained in the purified fermentation solution is converted to lactic acid and salt is formed in the stoichiometric proportion, wherein the temperature of the acidified ultrafiltration permeate is kept in a range between 30° C. to 60° C.

11. The process of claim 8 , wherein the step of separating lactic acid solution from the biomass-free fermentation liquor includes separating the ultrafiltration permeate in a simulated moving bed chromatography (SMB) into (a) an extract containing the major part of the lactic acid and (b) a raffinate containing the major part of ammonium sulfate and small quantities of accompanying salts, such as phosphates, nitrates and chlorides, wherein

(i) the addition of the ultrafiltration permeate and an eluent is effected continuously in a permeate:eluent ratio of 1:1.5 to 1:2.5,

(ii) the extract containing the lactic acid, having a content of lactic acid >1 g/l, and the raffinate are collected separately from one another, and

(iii) the efficacy of the recovery of lactic acid from the ultrafiltration permeate is >95%.

12. The process of claim 2 , wherein in the two steps of purifying lactic acid solution by each of the first ion exchange step and the second ion exchange step, a purification from anionic and cationic impurities is produced by cation exchangers and/or anion exchangers.

13. The process of claim 2 , wherein in the step of subjecting the first-ion-exchange purified lactic acid solution to the at least one of the first single or multistage partial evaporation step, a single or multistage partial evaporation to a lactic acid concentration of 45 to 55 wt. % is achieved.

14. The process of claim 2 , wherein in the step of subjecting the second-ion-exchange purified lactic acid solution to at least one of a second single or multistage evaporation step a single or multistage evaporation to a lactic acid concentration of 80 wt. % is achieved.

15. The process of claim 2 further comprising producing polylactides based on the purified lactic acid solution after subjecting the second-ion-exchange purified lactic acid solution to the at least one of the second single or multistage evaporation step.

16. The use process of claim 15 , wherein producing the polylactides comprises:

concentrating the lactic acid to 98 wt. %;

performing precondensation on the concentrated lactic acid to achieve an average molecular mass of 500 to 2000 g/mol;

performing cyclizing depolymerization on the precondensated lactic acid, wherein lactide is generated;

purifying the lactide;

conducting ring opening polymerization on the lactide to create polylactide;

performing demonomerization on the polylactide;

converting the polylactide to polylactide granules; and

crystalizing the polylactide granules.