Affinity micro-filtration separation purification method for producing zytase
A xylanase, separation and purification technology, applied in the field of affinity microfiltration separation and purification of xylanase, can solve the problems of complex process and low efficiency, and achieve simple separation process, high separation efficiency and high recovery rate of enzyme activity Effect
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Embodiment 1
[0010] Use 0.05mol / L citric acid solution to adjust the pH value of 1L xylanase crude enzyme solution to pH3.0, place it in a jacketed reactor, cool the xylanase crude enzyme solution to 4°C, add An appropriate amount of oat xylan, so that the xylan content is 10g / L, is stirred (250r / min) at 4°C for 3 hours for adsorption.
[0011] With a pressure of 30kPa and a feed rate of 200mL / min, an effective membrane area of 140cm 2 The 0.2 μm microfiltration membrane intermittently diafiltration (diafiltration) the suspension in the reactor. During diafiltration, the suspension was first concentrated 4 times, and then the citric acid-sodium citrate buffer solution of pH 3.0 was added to make the reactor The volume of the material in the reactor was restored to the original volume (1 L). This was done 3 times, and the replacement volume was 2.0 L. At the end of the washing, the volume of the suspension in the reactor was about 200 mL.
[0012] Use sodium dihydrogen phosphate-disodium...
Embodiment 2
[0015] Use 0.05mol / L citric acid solution to adjust the pH value of 1L xylanase crude enzyme solution to pH3.0, place it in a jacketed reactor, cool the xylanase crude enzyme solution to 4°C, add An appropriate amount of oat xylan, so that the xylan content is 100g / L, is stirred (250r / min) at 4°C for 3 hours for adsorption.
[0016] Under the condition that the pressure is 30kPa and the feed rate is 200mL / min, the suspension in the reactor is intermittently diafiltration (diafiltration) with a 0.2 μm microfiltration membrane with an effective membrane area of 140cm2. During diafiltration, the suspension is first concentrated 5 times, then replenish the citric acid-sodium citrate buffer solution of pH3.0, make the material volume in the reactor return to original volume (1L), carry out like this 3 times, replacement volume is 2.5L, when washing finishes, reactor The inner suspension volume is about 250 mL.
[0017] Use sodium dihydrogen phosphate-disodium hydrogen phosphate ...
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