Extraction and purification method of nicotinamide ribose phosphate transferase
A purification method and phosphoribose technology, applied in the field of bioengineering, can solve problems such as the difficulty of effectively separating and purifying genetic recombinant proteins, and achieve the effect of improving yield and purity
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Embodiment 1
[0034] Example 1: Production of fermented broth containing NAMPT enzyme
[0035] (1) Strain activation: Streak the low-temperature-preserved NAMPT enzyme production strain on an LB plate containing 100 μg / ml KAN and 100 μg / ml AMP, and culture at 33°C for 24 hours; 100μg / ml KAN and 100μg / ml AMP on LB plates, cultured at 33°C for 24h, set aside.
[0036] The medium formula of LB plate: peptone 10.0g, yeast powder 5.0g, NaCl 10.0g, agar 15.0g, water 1.0L.
[0037] (2) Preparation of primary seed liquid: use the inoculation loop to scrape the lawn of the production strain activated in the second step (1), inoculate it in LB liquid medium, 33°C, 200r / min, shake the flask for 12h to obtain the primary seed liquid.
[0038] LB liquid medium formula: peptone 10.0g, yeast powder 5.0g, NaCl 10.0g, water 1.0L.
[0039] (3) Preparation of secondary seed liquid: the primary seed liquid prepared in step (2) is inoculated into the seed tank for fermentation and cultivation according to th...
Embodiment 2
[0046] Embodiment 2: Extraction and purification of NAMPT enzyme
[0047] (1) The fermented liquid produced in Example 1 is centrifuged at 4000r / min for 15min, and the thallus in the fermented liquid is collected;
[0048] (2) Add pure water to the cells (999g of water per 1g of cells), adjust the pH to 7.2-7.4 with ammonia water, and centrifuge after passing through a homogenizer (homogeneous pressure 15,000PSI, homogeneous flow rate 400L / Hr) , centrifuged at 10000r / min, centrifuged for 20min, and separated to obtain the supernatant;
[0049] (3) The supernatant is decolorized by activated carbon and filtered through a ceramic membrane (the aperture of the ceramic membrane is 100nm, and the filtration pressure is 0.5MPa) to process the supernatant to obtain the filtrate;
[0050] (4) add nonionic detergent Triton X-100 and sodium chloride in filtrate, make the final mass concentration of Triton X-100 be 2%, the final concentration of sodium chloride is 500mM, remove inclusio...
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