Fermentation process

Patent metadata

Field	Value
Publication number	US-11136602-B2
Application number	US-201716462978-A
Country	US
Kind code	B2
Filing date	Nov 29, 2017
Priority date	Nov 29, 2016
Publication date	Oct 5, 2021
Grant date	Oct 5, 2021

Abstract

A fermentation product manufacturing process includes fermenting under fermentation conditions in an aqueous fermentation medium in a fermentation reactor a carbohydrate source with a microorganism capable of converting the carbohydrate into a fermentation product which is a salt or a product with a boiling point above the boiling point of water, during the process withdrawing part of the medium including biomass from the reactor in the form of a recycle stream, providing the stream including biomass to a pressure vessel wherein the pressure is such that the temperature of the stream decreases 1-8° C., as compared to the temperature of the medium in the reactor, by the evaporation of water, and recycling the cooled recycle stream to the reactor. The process makes it possible to obtain a homogeneous temperature profile of the fermentation medium with limited occurrence of hot or cool spots within the reactor which results in improved fermentation performance.

First claim

The invention claimed is:

1. Process for manufacturing a fermentation product comprising the following steps:
fermenting under fermentation conditions in an aqueous fermentation medium in a fermentation reactor with a carbohydrate source and a microorganism capable of converting the carbohydrate into a fermentation product, wherein the fermentation product is a salt or a product with a boiling point above the boiling point of water,
during the fermentation process withdrawing part of a fermentation medium comprising the aqueous fermentation medium, fermentation product, and microbial biomass from the fermentation reactor in the form of a recycle stream,
providing at least part of the recycle stream to a pressure vessel wherein the pressure is selected such that the temperature of the recycle stream decreases with a value of 1-8° C., as compared to the temperature of the fermentation medium in the fermentation reactor, by the evaporation of water to form a cooled recycle stream, and
recycling the cooled recycle stream to the fermentation reactor.

2. Process according to claim 1 , wherein the temperature of the recycle stream decreases with a value of 2-5° C., as compared to the temperature of the fermentation medium in the fermentation reactor.

3. Process according to claim 1 , wherein the volume of the pressure vessel is between 0.1 and 10 percent of the volume of the fermentation reactor.

4. Process according to claim 1 , wherein the recycle time, defined as the time between withdrawal of a fraction of fermentation medium from the fermentation reactor and reintroduction of the fraction into the reactor is at most 10 minutes.

5. Process according to claim 1 , wherein solid fermentation product is present in the fermentation medium in the fermentation reactor during at least part of the fermentation.

6. Process according to claim 1 , wherein the volume of fermentation medium in the fermentation reactor is at least 100 m 3 .

7. Process according to claim 1 , wherein the difference between the highest temperature of the fermentation medium in the fermentation reactor and the lowest temperature of the fermentation medium in the fermentation reactor is at most 8° C.

8. Process according to claim 1 , wherein
a first part of the recycle stream is provided to the pressure vessel, and
a second part of the recycle stream is not provided to the pressure vessel.

9. Process according to claim 1 , wherein the fermentation product is a salt of a carboxylic acid selected from the group consisting of mono-, di-, and tricarboxylic acids having 2-8 carbon atoms.

10. Process for manufacturing a fermentation product comprising the following steps:
fermenting under fermentation conditions in an aqueous fermentation medium in a fermentation reactor with a carbohydrate source and a microorganism capable of converting the carbohydrate into an intermediate fermentation product, wherein the intermediate fermentation product is a salt of a carboxylic acid, wherein the intermediate fermentation product has a boiling point above the boiling point of water,
during the fermentation process, withdrawing part of a fermentation medium comprising the aqueous fermentation medium and intermediate fermentation product, from the fermentation reactor in the form of a recycle stream,
providing at least part of the recycle stream to a pressure vessel wherein the pressure is selected such that the temperature of the recycle stream decreases with a value of 1-8° C., as compared to the temperature of the fermentation medium in the fermentation reactor, by the evaporation of water to form a cooled recycle stream,
recycling the cooled recycle stream to the fermentation reactor, and subjecting the intermediate fermentation product to an acidification step, to convert the salt of the carboxylic acid into the carboxylic acid under the formation of a aqueous mixture of a carboxylic acid and an inorganic salt.

11. Process according to claim 10 , wherein the carboxylic acid is separated from the inorganic salt.

12. Process according to claim 11 , wherein after separation of the carboxylic acid from the salt, the carboxylic acid is subjected to a purification step.

13. Process according to claim 12 , wherein the purification step is selected from the group of consisting of washing, active carbon treatment, recrystallization, distillation, and filtration.

14. Process according to claim 10 , wherein a microbial biomass removal step is carried out between the fermentation step and the acidification step.

15. Process according to claim 10 , wherein the carboxylic acid is lactic acid, which is subsequently converted into lactide or polylactide.

Assignees

• Purac Biochem Bv

Inventors

• De Haan Andre Banier
• Bokhove Jeroen

Classifications

• C12P7/40 Primary

  containing a carboxyl group {including Peroxycarboxylic acids} · CPC title

• C12P7/56 Primary

  Lactic acid · CPC title

• C12P7/58

  Aldonic, ketoaldonic or saccharic acids (uronic acids C12P19/00) · CPC title

• C12M47/12

  Purification (C12M47/04 takes precedence) · CPC title

• C12P7/52

  Propionic acid; Butyric acids · CPC title