Double aqueous phase solid-liquid separation method for yeast origin recombinant protein fermentation liquor
A recombinant protein and solid-liquid separation technology, which is applied in the field of bioengineering, can solve the problems of high cost of solid-liquid separation and difficult removal of bacteria, and achieve the effect of simple and easy recovery method, good bacteria removal rate and good separation effect
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Embodiment 1
[0013] The recombinant human serum albumin fermentation broth was obtained by applying the genetically engineered bacteria and production method constructed by our own patent application technology (CN1854301A and CN1854306A), the bacterial concentration was 37g / 100ml fermentation broth, and the protein concentration was 9.5g / L.
[0014] At 4°C, take 200ml of the above-mentioned recombinant human serum albumin fermentation broth, add 63.5g of dipotassium hydrogen phosphate, after the salt is dissolved, add 68.8ml of absolute ethanol, stir well, pH 11, stand at 4°C for 3 hours, extract Phase 160ml, raffinate phase 120ml, the extract phase is clear and transparent, cell removal rate is 99.95%, using Bradford method to measure the protein concentration of the extract phase is 7.6mg / ml, and the protein concentration of the raffinate phase is 0.2mg / ml. The protein recovery rate was 98.0%, and the partition coefficient reached 50.6. SDS-PAGE electrophoresis analysis showed that reco...
Embodiment 2
[0017] Use 200ml of the fermented broth in Example 1, add 40g of sodium carbonate and 65ml of ethanol in sequence at 25°C, mix, and the pH is 13. After stirring and mixing, the two-phase separation operation was carried out according to the operation of Example 1, the protein recovery rate was 86.2%, and the cell removal rate was 99.96%.
Embodiment 3
[0019] Using 200ml of the fermented broth in Example 1, add 15g of sodium chloride, 42g of potassium phosphate, and 68.5ml of ethanol in order at 4°C, stir well, and the pH is 13. After stirring and mixing, the two-phase separation operation was carried out according to the operation of Example 1, the protein recovery rate was 85.2%, and the cell removal rate was 99.96%.
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