Preparation method of high-purity glycine methyl ester hydrochloride
A technology of hydrochloride and amino acid ester is applied in the fields of low temperature, the preparation of similar glycine ester hydrochloride, and the preparation of high-purity amino acid methyl ester hydrochloride, which can solve problems that are not conducive to industrialization promotion, personal safety and environmental friendliness. , increase the production cost of products, etc., to achieve the effect of easy industrial production, good crystal form, and easy control of crystallization
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Embodiment 1
[0017] (1) At room temperature, add 150g of glycine and 640g of anhydrous methanol (among them: the molar ratio of glycine to anhydrous methanol is 1:10) into the reactor with stirring, start stirring to mix evenly;
[0018] (2) Infuse hydrogen chloride gas at a flow rate of 40L / h for 20 minutes until the system is completely dissolved, and at the same time raise the reaction temperature of the system to 45±1°C;
[0019] (3) When the heat preservation reaction lasts for 0.75 hours until crystals are precipitated in the system, continue to feed hydrogen chloride gas at a flow rate of 30L / h;
[0020] (4) Control the stirring rate to 120r / min, and the system drops to ≤10°C according to the gradient of 4°C / h;
[0021] (5) After suction filtration and drying at 100±5°C for 2 hours, a total of 241.58g of white crystal fine granular glycine methyl ester hydrochloride was obtained, and the yield was 95.64% based on the amount of glycine fed; the NMR purity of the product was 99.37% af...
Embodiment 2
[0023] (1) At room temperature, add 150g of glycine and 512g of anhydrous methanol (among them: the molar ratio of glycine to anhydrous methanol is 1:8) into the reactor with stirring, and start stirring to mix evenly;
[0024] (2) Infuse hydrogen chloride gas at a flow rate of 30L / h for about 30 minutes until the system is completely dissolved, and at the same time raise the reaction temperature of the system to 55±1°C;
[0025] (3) Insulate and react for 0.5 hours, and continue to feed hydrogen chloride gas at a flow rate of 20L / h until crystals are precipitated in the system;
[0026] (4) Control the stirring rate to 240r / min, and the system drops to ≤10°C according to the gradient of 4°C / h;
[0027] (5) After suction filtration and drying at 100±5°C for 2 hours, a total of 238.02g of glycine methyl ester hydrochloride in the form of white crystals and fine particles was obtained, and the yield was 93.90% based on the amount of glycine fed; the purity of the product was tes...
Embodiment 3
[0029] Control the agitation rate of late crystallization to 180r / min, the system drops to room temperature according to the gradient of 6°C / h, and other process conditions and operating procedures are the same as in Example 1.
[0030] After suction filtration and drying, a total of 241.30g of white crystal fine granular glycine methyl ester hydrochloride was obtained, and the product yield was 95.29%; the purity of the product was tested to be 99.12%, the melting point of the product was 173.1-173.3°C, and the content of glycine hydrochloride was 0.64%. After filtration, the methanol-containing mother liquor is recycled for the synthesis reaction of glycine methyl ester hydrochloride.
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