Method used for purifying methyl 1, 2, 4-triazole-3-carboxylate coarse product
A technology of methyl carboxylate and purification method, which is applied in the field of crude product purification of methyl 1,2,4-triazole-3-carboxylate, 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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