Extraction method of streptomycin sulfate
The technology of streptomycin sulfate and extraction method, which is applied in the field of preparation of pharmaceutical raw materials, can solve the problems of poor color grade of streptomycin sulfate finished products, low product qualification rate, low production efficiency, etc., and achieves good product color grade and high yield. , the effect of high pass rate
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Embodiment 1
[0036] A. Filtration: 60L of streptomycin fermented broth, titer 28550U / ml, product weight 1.713kg. Adjust the pH to 3.5 with oxalic acid, add 60 g of polyaluminum and polyacrylamide (1:1) and stir for 1 hour, then filter through a ceramic membrane;
[0037] B. Resin adsorption: the filtrate is adjusted to pH 7.0 with sodium hydroxide, and then injected into the resin column of D303 resin with a peristaltic pump, the flow rate is 1.5BV / h, and the adsorption capacity is 220g / L;
[0038] C, desorption: carry out desorption with 6% sulfuric acid aqueous solution, flow rate is 0.4BV / h, and volume is 3.5 times of resin volume;
[0039] D. Desalination and neutralization: Desalting and neutralizing the desorption solution with a mixed bed composed of 1×25 resin and 703 resin (1:1) to obtain a refined solution;
[0040] E, decolorization: add the refined solution to 370g activated carbon and stir to decolorize;
[0041] F. Concentration: Concentrate the decolorization solution with...
Embodiment 2
[0045] A. Filtration: 50L of streptomycin fermented broth, titer 28000U / ml, product weight 1.4kg. Adjust the pH to 4.0 with oxalic acid, add 75 g of polyaluminum and polyacrylamide (1:1.5) and stir for 1 hour, then filter through a ceramic membrane;
[0046] B. Resin adsorption: the filtrate is adjusted to pH 6.5 with sodium hydroxide, and then injected into the resin column of D308 resin with a peristaltic pump, the flow rate is 1.0BV / h, and the adsorption capacity is 212g / L;
[0047] C, desorption: carry out desorption with 7% sulfuric acid aqueous solution, flow velocity is 0.2BV / h, and volume is 3.0 times resin volume;
[0048] D. Desalination and neutralization: Desalting and neutralizing the desorption liquid with a mixed bed composed of 1×25 resin and 703 resin (1:1.5) to obtain a refined liquid;
[0049] E, decolorization: add 567g activated carbon to the refined solution and stir to decolorize;
[0050] F. Concentration: Concentrate the decolorization solution with ...
Embodiment 3
[0054] A. Filtration: 52L of streptomycin fermented broth, titer 28600U / ml, product weight 1.487kg. Adjust the pH to 2.0 with oxalic acid, add 78 g of polyaluminum and polyacrylamide (1:2.5) and stir for 1 hour, then filter through a ceramic membrane;
[0055] B. Resin adsorption: the filtrate is adjusted to pH 6.1 with sodium hydroxide, and then injected into the resin column of D303 resin with a peristaltic pump, the flow rate is 1.6BV / h, and the adsorption capacity is 235g / L;
[0056] C, desorption: carry out desorption with 7.8% sulfuric acid aqueous solution, flow velocity is 0.3BV / h, and volume is 3.2 times resin volume;
[0057] D. Desalination and neutralization: desalting and neutralizing the stripped solution with a mixed bed composed of 1×25 resin and 703 resin (1:2) to obtain a refined solution;
[0058] E, decolorization: add the refined solution to 500g activated carbon and stir to decolorize;
[0059] F. Concentration: Concentrate the decolorization solution w...
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