Method for splitting pinocembrin enantiomers through simulated moving bed chromatography
A technique of simulating moving bed and pinocerine, which is applied in the field of separation of chiral drugs, can solve problems such as no public reports, and achieve the effect of simple process and stable product quality
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example 1
[0028] 1. Sample preparation: The sample is dissolved in methanol to a concentration of 5g / L, filtered through a 0.45um organic filter membrane for use;
[0029] 2. Selection of simulated moving bed parameters: The parameters are determined as follows: injection flow rate 0.3mL / min, elution flow rate 2.0mL / min, extract flow rate 1.2mL / min, raffinate flow rate 1.1mL / min, switching time 13min, The temperature is controlled at 20-30℃;
[0030] 3. Product collection: After the simulated moving bed system is operating stably, collect the products from the two outlets respectively, and obtain the final product after concentration under reduced pressure and recrystallization;
[0031] 4. Finished product inspection: After the obtained product is dissolved in the mobile phase, the purity of the two export products R-pinocerin and S-pinocerin are 97.3% and 98.1%, respectively;
[0032] Each kilogram of stationary phase can produce 0.55kg of R-pinoselin and S-pinoselin each day, the consumption...
example 2
[0035] 1. Sample preparation: the sample is dissolved in methanol to a concentration of 10g / L, filtered through a 0.45um organic filter membrane for use;
[0036] 2. Selection of simulated moving bed parameters: Determine the parameters as follows: injection flow rate 0.6mL / min, elution flow rate 4.2mL / min, extract flow rate 2.6mL / min, raffinate flow rate 2.2mL / min, switching time 12min, The temperature is controlled at 20-30℃;
[0037] 3. Product collection: After the simulated moving bed system runs stably, collect the products from the two outlets respectively, and obtain the final product after concentration under reduced pressure and recrystallization;
[0038] 4. Finished product inspection: After the obtained product is dissolved in the mobile phase, the purity of the two export products R-pinocerin and S-pinocerin is 97.3% and 97.9%, respectively;
[0039] Each kilogram of stationary phase can produce 1.26kg of R-pinocerin and S-pinocerin each day, the mobile phase consumption...
example 3
[0042] 1. Sample preparation: the sample is dissolved in methanol to a concentration of 20g / L, filtered through a 0.45um organic filter membrane for use;
[0043] 2. Selection of simulated moving bed parameters: Determine the parameters as follows: injection flow rate 1.2mL / min, elution flow rate 6.8mL / min, extract flow rate 4.2mL / min, raffinate flow rate 3.8mL / min, switching time 11min, The temperature is controlled at 20-30℃;
[0044] 3. Product collection: After the simulated moving bed system runs stably, collect the products from the two outlets respectively, and obtain the final product after concentration under reduced pressure and recrystallization;
[0045] 4. Finished product inspection: After the obtained product is dissolved in the mobile phase, the purity of the two export products R-pinoselin and S-pinoseline are 97.3% and 98.3% respectively;
[0046] Each kilogram of stationary phase can produce 2.32kg of R-pinocerin and S-pinocerin each day, the mobile phase consumptio...
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