Method for producing fermentation product
A technology for fermentation products and manufacturing methods, applied in the direction of fermentation, biochemical equipment and methods, separation methods, etc., which can solve the problem that fermentation products are rarely reused
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0141] (1) Construction of Bacillus subtilis mutant strain (168_protease strain) introduced into protease gene expression mutation
[0142] Introduction of protease gene expression mutations was carried out. Using the genomic DNA of the Bacillus subtilis mutant strain RIK1140 (trpB'A'::PrrnOcatpt1 erm hisC101) (Japanese Patent No. 5847458) as a template, use the primers trpB-F and PrrnO-catsd-R described in Table 1 to amplify by PCR Contains the Shine-Dalgarno (SD) sequence in the upstream region of the chloramphenicol resistance gene from the trpB gene (Shine, J., Dalgarno, L., Proc. Natl. Acad. Sci. USA., 1974, 71: 1342 -1346) fragment (A). In addition, using the primers PrrnO-cat-erm-F and hisC-R2 described in Table 1, a fragment (B) containing the erythromycin resistance gene and the hisC gene was amplified by PCR.
[0143] Next, with reference to the records in JP-A-2002-218989, JP-A-2002-306176, JP-A-2004-122, JP-A-2004-305176, and JP-A-2006-129865, KP43 protease muta...
Embodiment 2
[0178] In the first culture of Example 1, the same operation was performed except that the culture was performed for 97 hours. In the first culture, the cell concentration (OD600 value) after 97 hours of culture was 30, in addition, the amount of residual sugar in the culture solution was 13 (g / L), and the production amount of alkaline protease was 0.27 (g / L) ). In the second culture, the cell concentration (OD600 value) after 76 hours of culture was 73, and the production amount of alkaline protease was 0.53 (g / L).
[0179] In addition, the carbon source conversion rate of alkaline protease was 0.71% with respect to the total sugar input amount in the first culture and the second culture.
Embodiment 3
[0181] In the first culture of Example 1, the same operation was performed except that the culture was performed for 122 hours. In the first culture, the cell concentration (OD600 value) after 122 hours of culture was 29, in addition, the amount of residual sugar in the culture solution was 10 (g / L), and the production amount of alkaline protease was 0.27 (g / L) ). In the second culture, the cell concentration (OD600 value) after 76 hours of culture was 68, and the production amount of alkaline protease was 0.59 (g / L).
[0182] In addition, the carbon source conversion rate of alkaline protease was 0.77% with respect to the total amount of sugar input in the first culture and the second culture.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 

