Method for recovering and mechanically applying L-(+)-tartrate in D-ethyl ester production

A technology of tartaric acid and calcium tartrate, applied in the field of chemistry, can solve the problems of L-(+)-tartaric acid product quality failing to meet the requirements of separation, failing to meet quality standards, unqualified quality, etc., achieving easy control and improving quality , to avoid the effect of side effects

Active Publication Date: 2015-02-04
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

[0016] 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 CaCl 2 ·4CH 3 OH, CaCl 2 ·4C 2 h 5 OH and other complex impurities, and even react under strong acid catalysis and a certain temperature to form impurities such as L-(+)-dimethyl tartrate, L-(+)-diethyl tartrate, etc., without special purification and separation, Concentrate under reduced pressure directly, most of the impurities are always present in the L-(+)-tartaric acid, resulting in the quality of the recovered L-(+)-tartaric acid not meeting the resolution requirements
[0017] In above-mentioned aqueous phase method and described alcohol solvent method reaction process, there are many difficult problems, if handle badly, will cause the L-(+)-tartaric acid quality of reclaiming to be unqualified, HPLC content<98.0%, specific rotation [a] D20: <+12° (C=20, aqueous solution) (generally +9.0°~+11.5°), the quality of recovered L-(+)-tartaric acid product is poor, and basically cannot reach L-( +)-tartaric acid raw material quality standards, can not be directly applied to the production of D-ethyl ester

Method used

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  • Method for recovering and mechanically applying L-(+)-tartrate in D-ethyl ester production

Examples

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Effect test

Embodiment 1

[0041] Production of L-(+)-Tartrate from L-(+)-Calcium Tartrate

[0042] 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, centrifuge, wash, and spin dry to obtain L-(+)-calcium tartrate.

[0043] In a 5000L glass-lined reaction kettle, add 2000~3500kg of organic solvent acetone, stir, cool down to ≤10℃, add about 500~1000kg of L-(+)-calcium tartrate solid, cool down, and control the temperature in the kettle to ≤10℃ , slowly add 98% H2SO4 dropwise at 0°C~25°C, and stir at 10~30°C for 1~2hr after the dropwise addition. Suction filtration to remove impurities such as insoluble inorganic salt calcium sulfate, ammonium salt, sodium salt and calcium chloride complexes, and collect the acetone mother liquor o...

Embodiment 2

[0048] Production of L-(+)-Tartrate from L-(+)-Calcium Tartrate

[0049] In a 5000L glass-lined reaction kettle, add 2000~3500kg of organic solvent cyclohexane, freeze and cool, stir, add about 500~1000kg of L-(+)-calcium tartrate solid, stir, cool down, and control the temperature in the kettle to ≤10℃ , slowly add 98% H2SO4 dropwise at 0°C-25°C, and stir at 10-25°C for 1 hr after the dropwise addition. Suction filtration removes impurities such as insoluble inorganic salt calcium sulfate, and collects the cyclohexane mother liquor of L-(+)-tartaric acid to a storage tank, or directly transfers it to a concentration kettle.

[0050] Put the L-(+)-tartrate acetone mother liquor into a 5O00L glass-lined concentration kettle, inject the liquid level to about 70~85%, distill and recover the solvent under normal pressure or reduced pressure, and control the final vacuum degree -0.085~-0.098Mpa, T≤60°C, the volume of the filtrate is concentrated to 1 / 3, the material is viscous, ...

Embodiment 3

[0055] Recovery of L-(+)-tartaric acid for application and separation

[0056] 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;

[0057] 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 recovering and mechanically applying L-(+)-tartrate in D-ethyl ester production, which comprises the following steps: 1)obtaining a L-(+)-tartrate solution; 2)recovering L-(+)-calcium tartrate dehydrate; 3)acidifying; 4)performing pressure reduction and condensation; and 5)crystallizing, separating and drying. The method of the invention employs an inertia organic solvent, takes a solvent method to replace a water phase method to recover L-(+)-tartrate, key points of control temperature, time, centrifugation and vacuum degree are realized, the product yield is high, the purity and specific rotation of the recovered L-(+)-tartrate product accord with quality requirement, quality standard of the L-(+)-tartrate raw material can be reached, and the method can be used for chiral resolution of D-ethyl ester, recovery and mechanical application of L-(+)-tartrate can be realized, production cost is reduced, and the method is suitable for industrial production.

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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Patent Type & Authority Applications(China)
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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