The crude product purification method of 1,2,4-triazole-3-carboxylic acid methyl ester
A technology of methyl carboxylate and purification method, applied in the field of crude product purification of 1,2,4-triazole-3-carboxylate methyl ester, can solve the problem of uneven particle size, affecting product application, poor transparency, etc. problem, to achieve the effect of white crystal appearance, improved drug yield, and uniform crystal appearance
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Embodiment 1
[0020] (1) Re-dissolution of the wet crude product: In the current production process of 1,2,4-triazole-3-carboxylate methyl ester, after the wet crude product crystallized by nitrogen release and suction filtration, methanol with 15 times the volume of the wet crude product was used Solvent, re-dissolve the obtained wet crude crystals at 70°C;
[0021] (2) Activated carbon decolorization: Add activated carbon accounting for 10% of the volume of methanol solvent to the solvent, and keep it for 15 minutes for decolorization;
[0022] (3) Temperature-controlled recrystallization: Control the temperature of the solvent to drop slowly to 50°C, add seed crystals accounting for 1% of the weight of the wet crude product, and then control the temperature to slowly drop to 35°C to re-form white crystals with uniform particles;
[0023] (4) Dry the crystals to obtain the finished product, and the purity of the product is 99.6%.
Embodiment 2
[0025] (1) Redissolution of the wet crude product: In the current production process of methyl 1,2,4-triazole-3-carboxylate, after the crystallization of the wet crude product obtained by nitrogen release and suction filtration, methanol with 13 times the volume of the wet crude product is used Solvent, re-dissolve the obtained wet crude crystals at 70°C;
[0026] (2) Activated carbon decolorization: Add activated carbon accounting for 7% of the volume of methanol solvent to the solvent, and keep it for 20 minutes for decolorization;
[0027] (3) Temperature-controlled recrystallization: Control the temperature of the solvent to drop slowly to 50°C, add seed crystals accounting for 1% of the weight of the wet crude product, and then control the temperature to slowly drop to 35°C to re-form white crystals with uniform particles;
[0028] (4) Dry the crystals to obtain the finished product, and the purity of the product is 99.8%.
Embodiment 3
[0030] (1) Redissolution of the wet crude product: In the current production process of methyl 1,2,4-triazole-3-carboxylate, after the crystallization of the wet crude product obtained by nitrogen release and suction filtration, methanol with 10 times the volume of the wet crude product is used Solvent, re-dissolve the obtained wet crude crystals at 70°C;
[0031] (2) Activated carbon decolorization: Add activated carbon accounting for 5% of the volume of methanol solvent to the solvent, and keep it for 24 minutes for decolorization;
[0032] (3) Temperature-controlled recrystallization: Control the temperature of the solvent to drop slowly to 50°C, add a seed crystal accounting for 0.5% of the weight of the wet crude product, and then control the temperature to slowly drop to 35°C to re-form white crystals with uniform particles;
[0033] (4) Dry the crystals to obtain the finished product, and the purity of the product is 99.7%.
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