Method for refining beta-thymidine in fermentation broth through ultrafiltration and ion exchange technology
A technology of ion exchange and fermented liquid, applied in the field of β-thymidine production, which can solve the problems of reduced membrane filtration speed, affecting product yield, cumbersome operation steps, etc., to improve product yield, reduce extraction and separation steps, and simple process reasonable effect
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Embodiment 1
[0026] 100L of β-thymidine fermentation broth passed through a microfiltration membrane with a membrane pore size of 1000nm, the membrane entry pressure was 0.2MPa, the membrane exit pressure was 0.1MPa, and the operating temperature was 25°C. After the fermentation broth was concentrated 10 times, 20L of dialysis water was added. The filtrate passes through the 732-type cation-exchange resin column with a 2BV / H flow rate, and the positive column effluent is directly connected to the 717-type anion-exchange resin column with a 2BV / H flow rate. The ion exchange liquid passes through the ultrafiltration membrane with a molecular weight cut-off of 5000, the operating pressure is 1.4MPa, and the operating temperature is 30-35°C. After the ion exchange liquid is concentrated 15 times, 25L of dialysis water is added. The filtrate passes through 732-type cation exchange resin, 331-type anion-exchange resin, and HZ-818 resin in sequence. The resin chromatography effluent is concentrat...
Embodiment 2
[0029] 100L of β-thymidine fermentation broth passed through a microfiltration membrane with a membrane pore size of 200nm, the membrane entry pressure was 0.2MPa, the membrane exit pressure was 0.1MPa, and the operating temperature was 25°C. After the fermentation broth was concentrated 10 times, 30L of dialysis water was added. The filtrate passes through the 732-type cation-exchange resin column with a 2BV / H flow rate, and the positive column effluent is directly connected to the 717-type anion-exchange resin column with a 2BV / H flow rate. The ionotropic liquid passes through the ultrafiltration membrane with a molecular weight cut-off of 2000, the operating pressure is 1.4MPa, and the operating temperature is 30-35°C. After the ionotropic liquid is concentrated 15 times, 30L of dialysis water is added. According to the subsequent extraction method in Example 1, the β-thymidine crystals were vacuum-dried to obtain a total of 4.97 Kg of β-thymidine product. The purity of the...
Embodiment 3
[0032]100L of β-thymidine fermentation broth passed through a microfiltration membrane with a membrane pore size of 500nm, the membrane entry pressure was 0.2MPa, the membrane exit pressure was 0.1MPa, and the operating temperature was 25°C. After the fermentation broth was concentrated 10 times, 25L of dialysis water was added. The filtrate passes through an ultrafiltration membrane with a molecular weight cut-off of 2000, the operating pressure is 1.4MPa, and the operating temperature is 30-35°C. After the microfiltrate is concentrated by 15 times, 25 L of dialysis water is added. The ultrafiltrate passes through the 732-type cation exchange resin column with a 2BV / H flow rate, and the positive column effluent is directly connected to the 717-type anion-exchange resin column with a 2BV / H flow rate. According to the subsequent extraction method in Example 1, the β-thymidine crystals were vacuum-dried to obtain a total of 4.93 kg of β-thymidine product. The purity of the β-thy...
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