A washing method for genetically engineered inclusion bodies
A washing method and genetic engineering technology, applied in the field of biomedicine, can solve problems such as high cost, cumbersome operation, and easy pollution, and achieve the effects of improving production efficiency, simple process, and convenient operation
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Embodiment 1
[0018] Example 1 Washing of Inclusion Body (0.2 kg) of Escherichia coli Expressing Recombinant Human Proinsulin
[0019] The hollow fiber membrane (made of polyethersulfone, the inner diameter of the fiber tube is 1 mm, and the pore size of the filter membrane is 0.1 μm) is first rinsed with purified water to balance, and the water flow rate is adjusted so that the membrane pressure is 15 bar and the permeation flux is 30 LMH . Add 3 L of washing buffer Ⅰ (20 mM Tris-HCl, 1% Triton-X-100, pH 9.0) to 0.2 kg of Escherichia coli expressing recombinant human proinsulin inclusion body, stir to make a suspension, and remove the inclusion body The suspension was pumped into the hollow fiber membrane, so that the pressure across the membrane was 5 bar, and the permeation flux was 10 LMH. The inclusion body suspension was concentrated by 3 times and then stopped feeding.
[0020] Add 5 L of washing buffer II (100 mM Tris-HCl, 2 M urea, pH 9.0) into the above-mentioned inclusion body c...
Embodiment 2
[0022] Example 2 Washing of Escherichia coli expressing recombinant human proinsulin inclusion body (1 kg)
[0023] The hollow fiber membrane (made of polyethersulfone, the inner diameter of the fiber tube is 1.75 mm, and the pore size of the filter membrane is 0.2 μm) is first rinsed with purified water to balance, and the water flow rate is adjusted so that the membrane pressure is 5 bar and the permeation flux is 10 LMH . Add 15 L of washing buffer Ⅰ (20 mM Tris-HCl, 5% Tween-20, pH 9.0) into inclusion bodies expressing recombinant human proinsulin in Escherichia coli, stir to make a suspension, and pump the inclusion body suspension into the hollow For fibrous membranes, the membrane pressure is 5 bar, the permeation flux is 10 LMH, and the inclusion body suspension is concentrated 5 times before liquid feeding is stopped.
[0024] Add 45 L of washing buffer II (100 mM Tris-HCl, 3 M guanidine hydrochloride, pH 9.0) to the above inclusion body concentrate, stir to form a s...
Embodiment 3
[0026] Example 3 Washing of Escherichia coli expressing recombinant human proinsulin inclusion body (5 kg)
[0027] The hollow fiber membrane (made of polyethersulfone, the inner diameter of the fiber tube is 1 mm, and the pore size of the filter membrane is 0.2 μm) is first rinsed with purified water to balance, and the water flow rate is adjusted so that the membrane pressure is 10 bar and the permeation flux is 20 LMH . Add 75 L of washing buffer Ⅰ (100 mM Tris-HCl, 5% Triton-X-100, pH 9.0) into inclusion bodies expressing recombinant human proinsulin in Escherichia coli, stir to make a suspension, and dissolve the inclusion body suspension Pump into the hollow fiber membrane so that the pressure across the membrane is 15 bar, the permeation flux is 30 LMH, and the inclusion body suspension is concentrated 5 times before stopping the liquid feeding.
[0028] Add 45 L of washing buffer II (100 mM Tris-HCl, 4 M urea, pH 9.0) to the above-mentioned inclusion body concentrate, s...
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