A kind of method that reclaims articaine hydrochloride or its intermediate product from synthetic mother liquor
A technology for synthesizing articaine hydrochloride and mother liquor, applied to medical preparations containing active ingredients, pharmaceutical formulas, drug combinations, etc., can solve problems such as waste, high cost, and difficult processing, and achieve the effect of reducing waste
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Embodiment 1
[0038] Produce a batch of intermediate product 1 (4-methyl-3[[1-oxo-2-(chloro)propyl]amino]-2-thiophene carboxylate methyl ester) according to the flow process and production requirements: wherein raw materials (3 -Amino-4-methyl-thiophene-2-carboxylic acid methyl ester) input amount is 29kg, the theoretical output intermediate product 1 is 44.3kg, the actual production obtains the qualified intermediate product 1 is 29.2kg, and the yield is 65.9%. Collect 115kg of the mother liquor produced in the production of intermediate product 1 in this step, set the water bath temperature at 75°C and concentrate in vacuum until no obvious fraction appears to obtain 56kg of viscous feed solution, add 50kg of methanol and heat to reflux for dissolution, then cool down to 2°C and discharge to obtain Viscous material liquid (black in color, no obvious crystallization). The above viscous feed liquid was reworked and re-concentrated in vacuum until there was no obvious fraction, and 110 kg of...
Embodiment 2
[0040]Produce a batch of intermediate product 1 (4-methyl-3[[1-oxo-2-(chloro)propyl]amino]-2-thiophene carboxylate methyl ester) according to the flow process and production requirements: wherein raw materials (3 -Amino-4-methyl-thiophene-2-carboxylic acid methyl ester) input amount is 29kg, the theoretical output intermediate product 1 is 44.3kg, the actual production obtains the qualified intermediate product 1 is 30.1kg yield 67.9%. Collect 112kg of mother liquor produced in the production of intermediate product 1 in this step, set the water bath temperature at 71°C and concentrate in vacuum until no obvious fraction appears to obtain 52.5kg of viscous feed solution, add 50kg of methanol and heat to reflux to dissolve, then cool down to 2°C and discharge Viscous feed liquid (black in color, no obvious crystallization) was obtained. The above viscous feed liquid was reworked and re-concentrated in vacuum until there was no obvious fraction, and 110 kg of dichloromethane and...
Embodiment 3
[0042] Produce a batch of intermediate product 1 (4-methyl-3[[1-oxo-2-(chloro)propyl]amino]-2-thiophene carboxylate methyl ester) according to the flow process and production requirements: wherein raw materials (3 -Amino-4-methyl-thiophene-2-carboxylic acid methyl ester) input amount was 29kg, the theoretical output of compound 3 was 44.3kg, and the actual production obtained qualified intermediate product 1 was 27.2kg with a yield of 61.4%. Collect 117kg of mother liquor produced by the production of intermediate product 1 in this step, set the water bath temperature at 73°C and concentrate in vacuum until no obvious fraction appears to obtain 58kg of viscous feed solution, add 110kg of dichloromethane and 100kg of saturated saline, stir for 20 minutes, and let stand for 30 Minute layering. The organic layer was collected and the aqueous layer was discarded. Control the temperature of the water bath at 60-65°C and concentrate in vacuum until no obvious fraction appears to ob...
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