Aspergillus niger seed continuous culture and method for producing citric acid therefrom

Patent metadata

Field	Value
Publication number	US-11434467-B2
Application number	US-201816467990-A
Country	US
Kind code	B2
Filing date	Dec 24, 2018
Priority date	Aug 28, 2018
Publication date	Sep 6, 2022
Grant date	Sep 6, 2022

Abstract

Disclosed is an Aspergillus niger seed continuous culture method, comprising the steps of: (1) at a startup stage, Aspergillus niger spores are inoculated into a seed culture medium to obtain a seed liquid; (2) at a seed continuous culture stage, continuous dispersion treatment is performed on the seed liquid obtained in step (1), continuous culture is performed on the seed liquid obtained by dispersion, and meanwhile, a fresh seed feed medium is replenished; and (3) at a stop stage, the replenishment of the fresh seed feed medium and the dispersion treatment are stopped, continuous culture is performed to obtain a seed liquid, and then the seed liquid is transferred into the fermentation medium for fermentation culture. The method according to the present invention makes breakthrough to solve problems that multi-cellular filamentous bacteria grow slowly and mycelium pellets are easy to lose in continuous culture, thus fully achieving seed continuous culture.

First claim

What is claimed is:

1. An Aspergillus Niger seed continuous culture method, comprising the steps of:
(1) inoculating Aspergillus Niger spores into a seed culture medium in a seed tank, and culturing for 16-36 hours to obtain a seed liquid;
(2) dispersing continuously the seed liquid obtained in step (1), culturing continuously the seed liquid obtained by dispersion, fermenting the seed liquid that flows out continuously into a fermentation medium in a fermentation tank, and replenishing a fresh seed feed medium to the seed tank at the same rate with the outflow seed liquid, wherein the total sugar of the fresh seed feed medium replenished in step (2) is 150-200 g/L, carbon to nitrogen ratio (C/N) is 15-30, and wherein the continuous seed culture conditions in step (2) are as follows: the temperature is 35-37° C., the ratio of volume of air under standard conditions per volume of liquid per minute (VVM) is 0.3-0.6, the tank pressure is 0.05-0.07 Mpa, and the agitation rate is 150-200 rpm, wherein the replenishing rate of the fresh seed feed medium and the outflow rate of the seed liquid in step (2) are F=V/t, wherein V is the volume of the seed liquid in the seed tank, and wherein t is the residence time of the seed liquid and is 6-24 hours; and
(3) stopping the replenishment of the fresh seed feed medium and the dispersion, maintaining continuous culture to obtain seed liquid, and transferring the seed liquid into the fermentation medium for fermentation culture.

2. The method according to claim 1 , wherein the final concentration of the Aspergillus Niger spores after step (1) incubation is 1×10 5 to 9×10 5 spores/mL, and wherein the seed culture conditions in step (1) are as follows: the total sugar of the seed culture medium is 100-180 g/L, the C/N is 20-40; the temperature is 35-39° C., the VVM is 0.2-0.4, the tank pressure is 0.05-0.1 Mpa, and the agitation rate is 100-200 rpm.

3. The method according to claim 1 , wherein the continuous culture conditions in step (3) are as follows: the temperature is 35-39° C., the VVM is 0.3-0.6, the tank pressure is 0.05-0.1 Mpa, and the agitation rate is 150-200 rpm.

4. The method according to claim 1 , wherein mycelium pellets in the seed liquid are dispersed in step (2) into 10-80 μm of flocculent hyphae using a disperser.

5. The method according to claim 1 , wherein the fermentation inoculation proportion in step (2) and step (3) is 5-25% v/v.

6. The method according to claim 1 , wherein the total sugar of the fermentation medium in step (2) and step (3) is 160-200 g/L, C/N is 50-90, and wherein the fermentation culture conditions in step (2) and step (3) are as follows: the temperature is 35-39° C., the VVM is 0.1-0.4, the tank pressure is 0.05-0.1 Mpa, the agitation rate is 100-200 rpm, and fermentation ends when a concentration of a reducing sugar is less than 5 g/L.

7. The method according to claim 1 , wherein the seed culture medium, the fresh seed feed medium, and the fermentation medium are formulated with a liquid starchy raw material, and a nitrogen source, wherein the starchy raw material comprises at least one of corn flour, cassava flour, sorghum flour, and wheat starch, and wherein the nitrogen source comprises at least one of ammonium sulfate, urea, soybean meal powder, and corn steep liquor.

Assignees

• Jiangsu Guoxin Union Energy Co Ltd
• Univ Jiangnan

Inventors

• Shi Guiyang
• Hu Zhijie
• Li youran
• Jiang Xiaodong
• Jin Sai
• Sun Fuxin
• Zhang Cheng
• Zhou Dongjiao
• Lu Jiawei
• Miao Maodong
• Fan Zihao

Classifications

• C12N1/14 Primary

  Fungi (culture of mushrooms A01G18/00; as new plants A01H15/00); Culture media therefor · CPC title

• C12P7/48 Primary

  Tricarboxylic acids, e.g. citric acid · CPC title

• C12N1/04

  Preserving or maintaining viable microorganisms (immobilised microorganisms C12N11/00) · CPC title

• C12N1/145

  Fungi isolates · CPC title

• C12R2001/685

  Aspergillus niger · CPC title