Process for direct preparation of amoxicillin by liquid 6-APA (amino penicillanic acid)
A technology of 6-APA and amoxicillin, which is applied in the field of drug preparation, can solve problems such as not being suitable for expanding production, increasing 6-APA degradation, and affecting yield, so as to improve drug safety, reduce investment, Effect of reducing energy loss
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Embodiment 1
[0022] Example 1 Liquid 6-APA straight-through amoxicillin
[0023] (1) in the reactor that immobilized penicillin G acylase (I type) 1kg is housed, add penicillin concentration and be 20kg of penicillin degreasing liquid of 10wt%, control cleavage reaction pH to be 8.0, temperature 30 ± 1 ℃, when pH has no When fluctuating, detect the content of penicillin, calculate when the conversion rate of penicillin is 98.8%, discharge, obtain the mixed cracking solution of 6-APA and phenylacetic acid;
[0024] (2) Add 50% dichloromethane of the volume of the lysate to the lysate, and adjust the pH value to 1.0 with 30wt% hydrochloric acid, stir, leave to separate phases, and separate to obtain an aqueous phase containing 6-APA;
[0025] (3) Chromatographically separate the aqueous phase through a LXT-080 macroporous adsorption resin column, control the flow rate to 4BV / h, and the temperature at 5-10°C. After passing through the resin column, it is detected that the residual phenylaceti...
Embodiment 2
[0029] Example 2 Liquid 6-APA straight-through amoxicillin
[0030] (1) in the reactor that immobilized penicillin G acylase (I type) 2.4kg is housed, add penicillin concentration and be 15wt% penicillin degreasing liquid 20kg, control cleavage reaction pH to be 7.8, temperature 28 ± 1 ℃, when pH When there is no fluctuation, the content of penicillin is detected, and when the conversion rate of penicillin is calculated to be 98.2%, the material is discharged to obtain a mixed lysis solution of 6-APA and phenylacetic acid;
[0031] (2) Add dichloromethane with 100% volume of the lysate to the lysate, and adjust the pH value to 1.0 with 30wt% hydrochloric acid, stir, leave to separate phases, and separate to obtain an aqueous phase containing 6-APA;
[0032] (3) Chromatographically separate the aqueous phase through a LXT-080 macroporous adsorption resin column, control the flow rate to 3BV / h, and the temperature at 5-10°C. After passing through the resin column, it is detected...
Embodiment 3
[0036] Example 3 Liquid 6-APA straight-through amoxicillin
[0037] (1) in the reactor that immobilized penicillin G acylase (I type) 22kg is housed, adding penicillin concentration is 20kg of penicillin degreasing liquid of 18wt%, and the control cleavage reaction pH is 8.2, and temperature 32 ± 1 ℃, when pH has no When fluctuating, detect the content of penicillin, calculate when the conversion rate of penicillin is 98.3%, discharge, obtain the mixed lysis solution of 6-APA and phenylacetic acid;
[0038] (2) Add dichloromethane of 1 / 3 of the volume of the lysate to the lysate, and adjust the pH value to 1.0 with 30wt% hydrochloric acid, stir, stand still and separate phases, and separate to obtain an aqueous phase containing 6-APA;
[0039](3) Chromatographically separate the aqueous phase through a LXT-081 macroporous adsorption resin column, control the flow rate to 5BV / h, and the temperature at 5-10°C. After passing through the resin column, it is detected that the resid...
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