Method for preparing crude paromomycin with membrane separation technology
A paromomycin and membrane separation technology, applied in the preparation of sugar derivatives, chemical instruments and methods, sugar derivatives, etc., can solve the problems of unformed filter cake, high labor intensity, low filtration yield, etc. Resin bleaching, reducing secondary pollution, low energy and material consumption
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Embodiment 1
[0020] Using 260L of fermentation broth containing paromomycin with a concentration of 3.5g / L as raw material, a ceramic microfiltration membrane with a molecular weight cut-off of 50,000 is used. The flux is 35L / h·㎡, the operating pressure is 2.5bar, and the operating temperature is 35°C Remove bacteria and residues from the fermentation broth under certain operating conditions. The permeate adopts a composite ultrafiltration membrane with a molecular weight cut-off of 5000. Under the operating conditions of a membrane flux of 30L / h·㎡, an operating pressure of 5.0bar, and an operating temperature of 30°C, impurities are removed through the ultrafiltration membrane, and proteins and polysaccharides are removed. and colored substances, etc. The ultrafiltration permeate is treated by nanofiltration with a composite membrane with a molecular weight cut-off of 500. Under the operating conditions of the nanofiltration membrane flux of 30L / h·㎡, the operating pressure of 10.0bar, and...
Embodiment 2
[0022] Using 350L of fermentation broth containing paromomycin with a concentration of 3.3g / L as raw material, a ceramic microfiltration membrane with a molecular weight cut-off of 50,000 is used. The flux is 40L / h·㎡, the operating pressure is 3.0bar, and the operating temperature is 30°C Remove bacteria and residues from the fermentation broth under certain operating conditions. The permeate adopts a composite ultrafiltration membrane with a molecular weight cut-off of 5000. Under the operating conditions of a membrane flux of 30L / h·㎡, an operating pressure of 5.0bar, and an operating temperature of 30°C, impurities are removed through the ultrafiltration membrane, and proteins and polysaccharides are removed. and colored substances, etc. The ultrafiltration permeate is treated by nanofiltration with a composite membrane with a molecular weight cut-off of 500. Under the operating conditions of the nanofiltration membrane flux of 30L / h·㎡, the operating pressure of 8.0bar, and ...
Embodiment 3
[0024] Using 350L of fermentation broth containing paromomycin with a concentration of 3.8g / L as raw material, a ceramic microfiltration membrane with a molecular weight cut-off of 50,000 is used. The flux is 40L / h·㎡, the operating pressure is 3.0bar, and the operating temperature is 30°C Remove bacteria and residues from the fermentation broth under certain operating conditions. The permeate adopts a composite ultrafiltration membrane with a molecular weight cut-off of 5000. Under the operating conditions of a membrane flux of 30L / h·㎡, an operating pressure of 5.0bar, and an operating temperature of 30°C, impurities are removed through the ultrafiltration membrane, and proteins and polysaccharides are removed. and colored substances, etc. The ultrafiltration permeate is treated by nanofiltration with a composite membrane with a molecular weight cut-off of 500. Under the operating conditions of the nanofiltration membrane flux of 30L / h·㎡, the operating pressure of 8.0bar, and ...
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