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38results about How to "High split yield" patented technology

Aminobutanol resolution method

The invention relates to an aminobutanol resolution method, which comprises: 1) carrying out a reaction: dissolving L-tartaric acid in anhydrous methanol, heating to a temperature of 65-55 DEG C, adding DL-2-aminobutanol to the L-tartaric acid methanol solution in a dropwise manner, carrying out a reaction, and controlling the pH value of the reaction system at 5-7; 2) precipitating D-2-aminobutanol-tartrate: cooling the mixing liquid obtained in the step 1) to a temperature of 35-25 DEG C to precipitate the D-2-aminobutanol-tartrate; 3) precipitating L-2-aminobutanol-tartrate: evaporating the filtrate in the step 2) to remove the methanol, adding water, controlling the temperature at 55-45 DEG C to obtain a clarified liquid, and cooling to a temperature of 15-5 DEG C so as to precipitate the L-2-aminobutanol-tartrate; and 4) preparing D-2-aminobutanol and L-2-aminobutanol: respectively adding an alkali liquid to the D-2-aminobutanol-tartrate precipitated in the step 2) and the L-2-aminobutanol-tartrate precipitated in the step 3), carrying out alkali precipitation, and respectively rectifying the filtrates so as to obtain the D-2-aminobutanol having the specific rotation of more than or equal to + / -10 and the L-2-aminobutanol having the specific rotation of more than or equal to + / -10.
Owner:嘉兴润博化工科技有限公司 +1

Method for preparing L-2-aminopropanol by means of splitting DL-2-aminopropanol

The invention relates to a method for preparing L-2-aminopropanol by means of splitting DL-2-aminopropanol. The method includes steps of 1), dissolving L-tartaric acid in water to obtain L-tartaric acid aqueous solution; 2), dissolving the DL-2-aminopropanol in alcohol solvents at the room temperature, then stirring the DL-2-aminopropanol and the alcohol solvents under cooling conditions, simultaneously completely dropwise adding the L-tartaric acid aqueous solution into the DL-2-aminopropanol to obtain mixed solution, then cooling the mixed solution until the temperature of the mixed solution reaches 0-5 DEG C, and preserving heat to obtain cooled solution; 3), adding a small quantity of crystal seeds into the cooled solution, allowing the cooled solution to stand still at the temperatures ranging from -15 DEG C to +25 DEG C, crystallizing the cooled solution at the temperatures ranging from -15 DEG C to +25 DEG C for 16-24 hours and separating out L-tartaric acid-L-2-aminopropanol acid salt crystals; 4), dissolving the L-tartaric acid-L-2-aminopropanol acid salt crystals by the aid of alcohol solvents, adding inorganic bases into the L-tartaric acid-L-2-aminopropanol acid salt crystals in batches, stirring the inorganic bases and the L-tartaric acid-L-2-aminopropanol acid salt crystals until amino alcohol is completely free, carrying out suction filtration and carrying out reduced-pressure distillation on filter liquid to obtain the L-2-aminopropanol. The method has the advantages that processes are easy to implement, raw materials are high in utilization rate, and accordingly the method is suitable for large-scale production.
Owner:WUHAN INSTITUTE OF TECHNOLOGY

Method for preparing (S)-tetrahydro-1-naphthoic acid through high-efficiency resolution

The invention relates to a preparation method of a palonosetron hydrochloride key intermediate (S)-1,2,3,4-tetrahydro-1-naphthoic acid as shown in a formula (I). The method comprises the following steps of adding a resolution agent for resolution by adopting 1,2,3,4-tetrahydro-naphthalene acid racemate as a raw material to obtain a salt (III) formed by a (S)-1,2,3,4-tetrahydro naphthalene acid and the resolution agent, and a salt (IV) formed by (R)-1,2,3,4-tetrahydro naphthalene acid and the resolution agent; carrying out salt removing on a compound III and a compound IV separately to obtain compounds (I) and (II); and carrying out racemization on the compound (II) under an alkaline condition to obtain a starting material 1,2,3,4-tetrahydro-naphthalene acid racemate and further carrying out resolution according to the steps. Therefore, the overall yield can be greatly improved, the production cost is reduced and environmental protection is facilitated. The preparation technology of the palonosetron hydrochloride key intermediate provided by the invention is different from the prior art, is safe, environmentally friendly, simple in operation and high in yield, and has relatively great practical value. The formula is as shown in the specification.
Owner:HANGZHOU XINBOSI BIOMEDICAL CO LTD

A method for splitting dl-2-aminopropanol to prepare 1-2-aminopropanol

The invention relates to a method for preparing L-2-aminopropanol by means of splitting DL-2-aminopropanol. The method includes steps of 1), dissolving L-tartaric acid in water to obtain L-tartaric acid aqueous solution; 2), dissolving the DL-2-aminopropanol in alcohol solvents at the room temperature, then stirring the DL-2-aminopropanol and the alcohol solvents under cooling conditions, simultaneously completely dropwise adding the L-tartaric acid aqueous solution into the DL-2-aminopropanol to obtain mixed solution, then cooling the mixed solution until the temperature of the mixed solution reaches 0-5 DEG C, and preserving heat to obtain cooled solution; 3), adding a small quantity of crystal seeds into the cooled solution, allowing the cooled solution to stand still at the temperatures ranging from -15 DEG C to +25 DEG C, crystallizing the cooled solution at the temperatures ranging from -15 DEG C to +25 DEG C for 16-24 hours and separating out L-tartaric acid-L-2-aminopropanol acid salt crystals; 4), dissolving the L-tartaric acid-L-2-aminopropanol acid salt crystals by the aid of alcohol solvents, adding inorganic bases into the L-tartaric acid-L-2-aminopropanol acid salt crystals in batches, stirring the inorganic bases and the L-tartaric acid-L-2-aminopropanol acid salt crystals until amino alcohol is completely free, carrying out suction filtration and carrying out reduced-pressure distillation on filter liquid to obtain the L-2-aminopropanol. The method has the advantages that processes are easy to implement, raw materials are high in utilization rate, and accordingly the method is suitable for large-scale production.
Owner:WUHAN INSTITUTE OF TECHNOLOGY
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