Method for recycling and reusing L-(+)-tartaric acid in production of D-p-methyl sulfone phenyl ethyl serinate
A technology of tartaric acid and calcium tartrate, which is applied in the chemical field, can solve the problems that the product quality of L-(+)-tartaric acid cannot meet the split requirements, fail to meet the quality standard, and the product quality is poor, so as to achieve easy control and avoid side effects. Response, the effect of reducing production costs
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[0045] Example 1
[0046] Production of L-(+)-tartaric acid from L-(+)-diammonium tartrate from mother liquor of D-ethyl ester
[0047] In a 5000L glass-lined reactor, add pure water, turn on the stirring, add the separated D-ethyl ester·L-(+)-tartrate, add dropwise ammonia to adjust PH=7~8 to obtain D-ethyl ester product And the mother liquor containing L-(+)-diammonium tartrate.
[0048] In a 5000L glass-lined reactor, add L-(+)-diammonium tartrate aqueous solution, stir, add hydrochloric acid dropwise to adjust pH=3.4 (control pH=3.3-3.6), cool, and control the temperature not to exceed 10-30℃. Freeze cooling to 10°C for crystallization, centrifugation, cold water washing, and drying to obtain high-purity L-(+)-ammonium hydrogen tartrate white crystals.
[0049] In a 5000L glass-lined reactor, add 3000~4000kg organic solvent acetone, stir, cool down to ≤10℃, add 500~1000kg of L-(+)-ammonium hydrogen tartrate solid, cool down, and control the temperature in the kettle to ≤10 ℃, ...
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[0053] Example 2
[0054] Production of L-(+)-tartaric acid from L-(+)-calcium tartrate from mother liquor of L-ethyl ester
[0055] L-(-)-p-methylsulfonyl phenylserine ethyl ester·L-(+)-tartrate methanol solution was concentrated under reduced pressure to recover methanol, and water was added to obtain L-(-)-p-methylsulfonyl phenylserine ethyl ester·L The -(+)-tartaric acid aqueous solution is neutralized and freed by alkaline substances, and calcium chloride solid is added to react to form L-(+)-calcium tartrate crystals, which are cooled, separated and washed to obtain L-(+)-calcium tartrate crystals.
[0056] In a 5000L calcium tartrate recovery kettle, add D-ethyl ester free mother liquor or L-ethyl ester free mother liquor into the recovery kettle, inject 70-80% of the liquid level, turn on the stirring; add high-purity calcium chloride solids in batches to react Generate L-(+)-calcium tartrate crystals, cool to 10~25°C to crystallize and centrifuge to obtain L-(+)-calcium t...
Example Embodiment
[0061] Example 3
[0062] Application and separation of recovered L-(+)-tartaric acid
[0063] Add 2200~3000kg of anhydrous methanol to the 5000L separation kettle, add 220Kg of L-(+)-tartaric acid recovered by the above process, heat it up, keep it at 25~35℃ for 30min~60min, wait until the L-(+)-tartaric acid is complete Dissolve and prepare for later use; add the prepared 400Kg DL-(±)-p-methylsulfonylphenylserine ethyl ester methanol solution into the separation kettle, stir for 40-60min, heat up to 45~66℃, reflux, keep for 30~60min ; After the reaction is completed, cool down to 28~33℃, ready to press filter;
[0064] At the same time, the diaphragm filter press is preheated in advance to about 28~33℃ and kept warm. When the separation kettle is cooled to about 28~33℃, the material is discharged to the filter press for pressure filtration. After discharging, it is pressed, D-(+)-p-methylsulfonylphenylserine ethyl ester·L-(+)-tartaric acid crude salt was obtained by compressed...
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