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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

Active Publication Date: 2015-02-18
兰州鑫隆泰生物科技有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0015] It has been reported in the literature that methanol and ethanol are used as organic solvents to prepare L-(+)-tartaric acid, but the added calcium chloride reacts with the solvent to form CaCl2 ·4CH3OH, CaCL2·4C2H5OH and other complex impurities , even under strong acid catalysis and a certain temperature, impurities such as L-(+)-dimethyl tartrate and L-(+)-diethyl tartrate are formed. Then most of the impurities are always present in the L-(+)-tartaric acid, causing the quality of the recovered L-(+)-tartaric acid product to fail to meet the resolution requirements
[0016] In the reaction process of the above-mentioned water phase method and the alcohol solvent method, there are many difficult problems, if not handled properly, it will cause the recovered L-(+) - Unqualified quality of tartaric acid, HPLC content <98.0%, specific rotation [a] D20: <+12° (C=20, aqueous solution) (generally +9.0°~+11.5°), recovered L-(+) - The quality of tartaric acid products is poor, basically not up to the quality standard of L-(+)-tartaric acid raw materials, and cannot be directly applied to the production of D-ethyl ester

Method used

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  • Method for recycling and reusing L-(+)-tartaric acid in production of D-p-methyl sulfone phenyl ethyl serinate
  • Method for recycling and reusing L-(+)-tartaric acid in production of D-p-methyl sulfone phenyl ethyl serinate

Examples

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Effect test

Embodiment 1

[0046] Production of L-(+)-tartaric acid by recovering L-(+)-diammonium tartrate from D-ethyl ester mother liquor

[0047] In a 5000L glass-lined reaction kettle, add pure water, start stirring, add the split D-ethyl ester·L-(+)-tartrate, add ammonia water dropwise to adjust the pH to 7~8, and obtain D-ethyl ester product and a 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°C. Freeze and cool to 10°C to crystallize, centrifuge, wash with cold water, and dry to obtain white crystals of high-purity L-(+)-ammonium hydrogen tartrate.

[0049] In a 5000L glass-lined reaction kettle, add 3000~4000kg of organic solvent acetone, stir, cool down to ≤10°C, add about 500~1000kg of L-(+)-ammonium hydrogen tartrate solid, cool down, and control the temperature in the...

Embodiment 2

[0054] Recovery of L-(+)-calcium tartrate from L-ethyl ester mother liquor to produce L-(+)-tartaric acid

[0055] L-(-)-p-thymphenylphenylserine ethyl ester · L-(+)-tartrate methanol solution is concentrated under reduced pressure to recover methanol, and water is added to obtain L-(-)-p-thymphenylphenylserine ethyl ester · L -(+)-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, cooled, separated and washed to obtain L-(+)-calcium tartrate crystals.

[0056] In the 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% liquid level, start stirring; add high-purity calcium chloride solid in batches, and react Generate L-(+)-calcium tartrate crystals, cool to 10~25°C to crystallize, and centrifuge to obtain L-(+)-calcium tartrate.

[0057] In a 5000L glass-lined r...

Embodiment 3

[0062] Recovery of L-(+)-tartaric acid for application and separation

[0063] Add 2200~3000kg of anhydrous methanol into a 5000L split kettle, add 220Kg of L-(+)-tartaric acid recovered by the above process, heat up, and keep warm at 25~35°C for 30min~60min, until the L-(+)-tartaric acid is completely Dissolve and set aside; add the prepared 400Kg DL-(±)-p-thymphenylphenylserine ethyl ester methanol solution into the split kettle, stir for 40-60 minutes, heat up to 45-66°C and reflux, and keep warm for 30-60 minutes ;After the reaction is completed, cool down to 28-33°C and prepare for pressure filtration;

[0064] At the same time, preheat the diaphragm filter press to about 28-33°C and keep it warm. When the temperature of the split kettle is cooled to about 28-33°C, discharge the material to the filter press for filtration. After the discharge is completed, press, Drying with compressed nitrogen, unloading to obtain D-(+)-p-thymphenyl phenylserine ethyl ester L-(+)-tart...

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Abstract

The invention discloses a method for recycling and reusing L-(+)-tartaric acid in production of D-p-methyl sulfone phenyl ethyl serinate. The method comprises the following steps: (1), a L-(+)-calcium tartrate dihydrate crystal is recovered from L-ethyl ester mother liquor; (2), an L-(+)-tartaric acid double brine solution is recovered from D-p-methyl sulfone phenyl ethyl serinate mother liquor; (3), L-(+)-tartaric acid double hydrochlorination is performed; (4), L-(+)-tartaric acid is recovered through L-(+)-tartaric acid single hydrochlorination; and (5), processes of vacuum concentration, crystallization, separation, drying and the like are performed. An insert organic solvent is used for replacing a conventional water phase method to recover L-(+)-tartaric acid, the possibility of side reaction is avoided, the purity and specific rotation of a product can both reach the raw material quality standard, and L-(+)-tartaric acid can be directly and circularly applied to chiral resolution of D-p-methyl sulfone phenyl ethyl serinate. Different recovery processing technologies are adopted for different mother liquor of two components in the production process of D-p-methyl sulfone phenyl ethyl serinate, the product quality is improved remarkably, the whole recovery condition is mild, and the operation is simpler and easy to control.

Description

technical field [0001] The invention belongs to the technical field of chemistry and relates to a method for recovering and applying L-(+)-tartaric acid in the production of D-ethyl ester. Background technique [0002] D-(+)-p-thymphenylphenylserine ethyl ester (referred to as D-ethyl ester) is obtained from DL-(±)-p-thymphenylphenylserine ethyl ester through L-(+)-tartaric acid optical resolution Obtained, the intermediate is an important intermediate for the synthesis of thiamphenicol and florfenicol, especially florfenicol is an excellent broad-spectrum antibiotic for veterinary use, with low toxicity, no residue, and no drug resistance. Because the rapid growth of the amount of florfenicol has driven the growth of the demand for intermediates, therefore, a large amount of L-(+)-tartaric acid needs to be consumed in the D-(+)-ethyl ester generation process. [0003] The chiral substance L-(+)-tartaric acid was used to resolve DL-(±)-p-thiamphenicyl phenylserine ethyl est...

Claims

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Application Information

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IPC IPC(8): C07C59/255C07C51/02C07C317/48C07C315/06
CPCC07B57/00C07B2200/07C07C51/02C07C51/412C07C51/42C07C315/06C07C59/255C07C317/48
Inventor 欧阳建峰黄朝纲张晖孙衍辉孙静丽李明
Owner 兰州鑫隆泰生物科技有限公司
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