Production method and application of special dietary protein
A construction method and technology of phenylalanine protein are applied in the production and application field of special dietary protein, which can solve the problems of limited yield, poor patient compliance with treatment, complicated production and purification process, etc.
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Embodiment 1
[0068] Example 1: Construction of Bacillus licheniformis strains expressing no / low phenylalanine content protein
[0069] The Bacillus licheniformis strain (B. licheniformis CICC 10266) used in the examples was purchased from China Industrial Microorganism Culture Collection and Management Center.
[0070] The pEBKan194-GFP plasmid used in the examples is pKGFP194ts in another patent application of the applicant (application number: 201610410811.8), and its construction information can be found in Example 1 of the specification of this application.
[0071] Unless otherwise specified, the reagents used in the experiment are all commercially available scientific research reagents or consumables. The ingredients and preparation methods of various reagents and media can refer to the operation in the routine experiment manual.
[0072] 1. Construction of phenylalanine-free protein expression strain BL01
[0073] 1. Knockout of the original gene in the expression strain
[0074] ...
Embodiment 2
[0122] Example 2: Fermentation production and purification preparation of no / low phenylalanine recombinant protein powder
[0123] This embodiment provides a production method of no / low phenylalanine recombinant protein powder, the specific steps are as follows:
[0124] 1) With the recombinant Bacillus licheniformis BL01 constructed in Example 1 as the starting strain, a 5L fermenter was used to carry out continuous feeding process fermentation, and the fermentation base medium was: 3% corn starch, 2% soybean protein isolate, and 0.5% yeast extract powder. %, K 2 HPO 4 0.45%, NaH 2 PO 4 0.7%, CaCl 2 0.04%, MgSO 4 ·7H 2 O 0.08%, MnSO 4 0.02%, defoamer 0.1%, α-high temperature amylase 0.01%, adjust pH to 7.5, base liquid volume is 50%, high temperature sterilization at 120°C for 20min; feeding medium: glucose, soybean hydrolyzed protein 10% , Yeast powder 10%, high temperature sterilization at 120°C. Fermentation inoculum amount is 5%, culture conditions: 37°C, aera...
Embodiment 3
[0127] Embodiment 3: the production of no / low phenylalanine recombinant protein powder
[0128] This embodiment provides a production method of no / low phenylalanine recombinant protein powder, the specific steps are as follows:
[0129] 1) Using the recombinant Bacillus licheniformis BL02 constructed in Example 1 as the starting strain, a 30L fermenter was used to carry out continuous feeding process fermentation, and the basic fermentation medium was: glucose 4%, soybean protein powder 3%, K 2 HPO 4 0.4%, NaH 2 PO 4 0.8%, CaCl 2 0.03%, MgSO 4 ·7H 2 O 0.06%, MnSO 4 0.03%, defoamer 0.2%, adjust the pH to 7.5, the basic liquid volume is 40%, 120 ℃ high-temperature sterilization for 20 minutes; feeding medium: glucose 40%, soybean hydrolyzed protein 15% + yeast powder 5%, Both were sterilized at high temperature at 120°C. Fermentation inoculum amount is 3%, culture conditions: 37°C, aeration rate 0.6-1.2vvm, DO control over 50% by adjusting the number of revolutions an...
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