A method for continuously extracting transglutaminase from fermentation broth
A technology of glutamine and fermentation broth, applied in the field of bioengineering, can solve problems such as large loss of enzyme activity, high equipment requirements, complicated operation, etc., and achieve the effects of small loss of enzyme activity, small personnel requirements, and simple equipment
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Embodiment 1
[0032] The fermentation broth of the present embodiment is obtained by the following methods:
[0033] The fermentation strain used in this example is Streptomyces hygroscopicus NYU-70 (CCTCC M 2014121). The strain was cultured and enriched in the seed liquid medium and then inoculated into the fermentation medium with 1 / 3 of the inoculum amount. The fermenter was set to rotate at 220 rpm, temperature at 30° C., pH 7.2, and the fermentation period was 64 hours.
[0034] At the end of the fermentation, the enzyme activity in the transglutaminase fermentation broth was 15.9 U / ml. The fermentation broth was introduced into the ceramic composite membrane device at a flow rate of 80 L / h to remove bacteria and impurities. The membrane separation accuracy of the ceramic composite membrane device was 50 nm. The separation liquid obtained by the ceramic composite membrane was introduced into the membrane separation equipment at a flow rate of 80L / h, and concentrated by ultrafiltration....
Embodiment 2
[0039] The fermentation broth of this example was obtained by the same method as in Example 1.
[0040]At the end of the fermentation, the enzyme activity in the transglutaminase fermentation broth was 15.9 U / ml. The fermentation broth was introduced into the ceramic composite membrane device at a flow rate of 80 L / h to remove bacteria and impurities. The membrane separation accuracy of the ceramic composite membrane device was 50 nm. The separation liquid obtained by the ceramic composite membrane was introduced into the membrane separation equipment at a flow rate of 80L / h, and concentrated by ultrafiltration. The molecular weight cut off of the membrane was 6000, and the temperature of the enzyme liquid was controlled by circulating water to 6±2℃. Add 1% soy protein (w / w) to the ultrafiltration concentrate obtained by ultrafiltration, stir at a speed of 120rpm for 5min with electric stirring, continue stirring at a speed of 80rpm and add 1.5 times (V / V) at a flux of 500mL / mi...
Embodiment 3
[0042] The fermentation broth of this example was obtained by the same method as in Example 1.
[0043] At the end of the fermentation, the enzyme activity in the transglutaminase fermentation broth was 15.9 U / ml. The fermentation broth was introduced into the ceramic composite membrane device at a flow rate of 80 L / h to remove bacteria and impurities. The membrane separation accuracy of the ceramic composite membrane device was 50 nm. The separation liquid obtained by the ceramic composite membrane was introduced into the membrane separation equipment at a flow rate of 80L / h, and concentrated by ultrafiltration. The molecular weight cut off of the membrane was 6000, and the temperature of the enzyme liquid was controlled by circulating water to 6±2℃. Add 1% β-cyclodextrin (w / w) to the ultrafiltration concentrate obtained by ultrafiltration, stir with electric stirring for 5 min at a speed of 120 rpm, continue stirring at a speed of 80 rpm and add 1.5 times ( V / V) precipitated...
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