Method of producing chemical by continuous fermentation and continuous fermentation apparatus

Patent metadata

Field	Value
Publication number	US-9644221-B2
Application number	US-201314388306-A
Country	US
Kind code	B2
Filing date	Mar 27, 2013
Priority date	Mar 30, 2012
Publication date	May 9, 2017
Grant date	May 9, 2017

Abstract

A method of producing a chemical includes culturing cells in a culture solution in a fermentor to ferment a feedstock to produce a chemical; supplying the culture solution containing the chemical produced in the culturing to a plurality of separation membrane units arranged in parallel; filtering the culture solution supplied in the supplying to separate a permeate containing the chemical; refluxing a retentate that is not filtered in the filtering to the fermentor; and supplying a gas containing oxygen to the plurality of separation membrane units while a supply amount is changed to at least two different values to perform scrubbing, wherein the supply amount and supply time of the gas containing oxygen supplied in the culturing and the supplying the gas are set so that a kLa value is within a predetermined range from an optimal kLa value for the cells cultured in the culturing.

First claim

The invention claimed is:

1. A method of producing a chemical comprising:
a chemical production step of culturing cells in a culture solution in a fermentor to ferment a feedstock to produce a chemical;
a culture solution supply step of supplying the culture solution containing the chemical produced in the chemical production step to a plurality of separation membrane units arranged in parallel;
a filtration step of filtering the culture solution supplied in the culture solution supply step to separate a permeate containing the chemical;
a reflux step of refluxing a retentate not filtered in the filtration step to the fermentor; and
a washing step of washing the plurality of separation membrane units by scrubbing with a gas containing oxygen and having at least two different flow rates for the plurality of separation membrane units while supplying the culture solution to the plurality of separation membrane units, wherein
the supply amount and supply time of the gas containing oxygen supplied in the chemical production step and the washing step are set so that a kLa value is within a predetermined range from an optimal kLa value for the cells cultured in the chemical production step.

2. The method according to claim 1 , wherein, in the washing step, a flow rate of the gas supplied to the plurality of separation membrane units is changed to two or more levels and the separation membrane units are sequentially switched for supply of a largest flow rate of the gas.

3. The method according to claim 2 , wherein, in the filtration step, a filtration operation is intermittently performed.

4. The method according to claim 2 , wherein the cells are bacteria.

5. The method according to claim 2 , wherein the cells are yeast.

6. The method according to claim 2 , wherein the chemical is an amino acid.

7. The method according to claim 2 , wherein the chemical is an organic acid.

8. The method according to claim 1 , wherein the cells are bacteria.

9. The method according to claim 8 , wherein the bacteria are bacteria belonging to any of a genus Escherichia , a genus Providencia , a genus Corynebacterium , a genus Brevibacterium , and a genus Serratia.

10. The method according to claim 8 , wherein the bacteria are any of Escherichia coli, Providencia rettgeri, Corynebacterium glutamicum, Brevibacterium flavum, Brevibacterium lactofermentum , and Serratia marcescens.

11. The method according to claim 1 , wherein the cells are yeast.

12. The method according to claim 1 , wherein the chemical is an amino acid.

13. The method according to claim 12 , wherein the amino acid is L-threonine, L-lysine, L-glutamic acid, L-tryptophan, L-isoleucine, L-glutamine, L-arginine, L-alanine, L-histidine, L-proline, L-phenylalanine, L-aspartic acid, L-tyrosine, L-methionine, L-serine, L-valine, or L-leucine.

14. The method according to claim 1 , wherein the chemical is an organic acid.

15. The method according to claim 14 , wherein the chemical is lactic acid.

16. The method according to claim 1 , wherein the chemical is cadaverine.

Assignees

• Toray Industries

Inventors

• Kanamori Satoko
• Sawai Hideki
• Takeuchi Norihiro

Classifications

• C12P13/001

  Amines; Imines · CPC title

• C12P13/06

  Alanine; Leucine; Isoleucine; Serine; Homoserine · CPC title

• C12P13/222

  Phenylalanine · CPC title

• C12P13/20

  Aspartic acid; Asparagine · CPC title

• C12M33/14

  with filters, sieves or membranes · CPC title