A kind of separation and purification method of gamma cyclodextrin
A gamma cyclodextrin, separation and purification technology, applied in the field of drug separation and purification, can solve the problems of inability to achieve secondary purification, large solvent consumption, and high purification cost, and achieve environmental protection, instrument cost saving, and separation efficiency that are beneficial to the solvent. high effect
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Embodiment 1
[0074] Separation and purification of gamma cyclodextrin: take gamma cyclodextrin and add methanol / water (v / v, 1 / 1) to prepare a solution with a concentration of 2 g / mL, and adjust the pH to 1-2 with 5% trifluoroacetic acid aqueous solution. After the solution was clarified, it was filtered through a filter membrane with a pore size of 0.45 μm, and the filtrate was collected for later use. A self-assembled column is used, and the column packing model is SiliaSphere series ODS, with a particle size of 50 μm and a pore size of 0.1% trifluoroacetic acid aqueous solution was used as mobile phase A, methanol was used as mobile phase B, and the flow rate was 80 mL / min. Such as figure 1 As shown, the equilibration time of the first column and the second column is about 15min, and the crude product loading is carried out by the first pump ( figure 1 Marked by solid line), at 25min (that is, when the detector detects the target peak), switch valve 1, valve 2 and valve 3 sequentially...
Embodiment 2
[0076] Separation and purification of gamma cyclodextrin: take gamma cyclodextrin and add methanol / water (v / v, 1 / 1) to prepare a solution with a concentration of 2 g / mL, and adjust the pH to 1-2 with 5% trifluoroacetic acid aqueous solution. After the solution was clarified, it was filtered through a filter membrane with a pore size of 0.45 μm, and the filtrate was collected for later use. A self-assembled column is used, and the column packing model is SiliaSphere series ODS, with a particle size of 50 μm and a pore size of 0.1% trifluoroacetic acid aqueous solution was used as mobile phase A, methanol was used as mobile phase B, and the flow rate was 80 mL / min. Such as figure 1 As shown, the equilibration time of the first column and the second column is about 15min, and the crude product loading is carried out by the first pump ( figure 1 Marked by the solid line), at 45min (the detector detects the target peak), switch valve 1, valve 2 and valve 3 sequentially and press...
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