Patent classifications
C07C203/06
Method for preparing nitrate ester
A method for preparing a nitrate ester is provided. The method includes providing a first solution including a compound (which has at least one hydroxyl group) and a carboxylic acid having 2-5 carbon atoms; providing a second solution including nitric acid, acetic anhydride, and acetic acid; and transferring the first solution and the second solution to a microreactor, obtaining a nitrate ester after a residence time. In particular, the ratio of the weight of nitric acid to the total volume of the acetic anhydride and acetic acid is 1:1 to 1:3.5. The ratio of the molar amount of nitric acid to the hydroxyl group equivalent of the compound is from 1:1 to 15:1.
Method for preparing nitrate ester
A method for preparing a nitrate ester is provided. The method includes providing a first solution including a compound (which has at least one hydroxyl group) and a carboxylic acid having 2-5 carbon atoms; providing a second solution including nitric acid, acetic anhydride, and acetic acid; and transferring the first solution and the second solution to a microreactor, obtaining a nitrate ester after a residence time. In particular, the ratio of the weight of nitric acid to the total volume of the acetic anhydride and acetic acid is 1:1 to 1:3.5. The ratio of the molar amount of nitric acid to the hydroxyl group equivalent of the compound is from 1:1 to 15:1.
METHOD FOR PREPARING NITRATE ESTER
A method for preparing a nitrate ester is provided. The method includes providing a first solution including a compound (which has at least one hydroxyl group) and a carboxylic acid having 2-5 carbon atoms; providing a second solution including nitric acid, acetic anhydride, and acetic acid; and transferring the first solution and the second solution to a microreactor, obtaining a nitrate ester after a residence time. In particular, the ratio of the weight of nitric acid to the total volume of the acetic anhydride and acetic acid is 1:1 to 1:3.5. The ratio of the molar amount of nitric acid to the hydroxyl group equivalent of the compound is from 1:1 to 15:1.
METHOD FOR PREPARING NITRATE ESTER
A method for preparing a nitrate ester is provided. The method includes providing a first solution including a compound (which has at least one hydroxyl group) and a carboxylic acid having 2-5 carbon atoms; providing a second solution including nitric acid, acetic anhydride, and acetic acid; and transferring the first solution and the second solution to a microreactor, obtaining a nitrate ester after a residence time. In particular, the ratio of the weight of nitric acid to the total volume of the acetic anhydride and acetic acid is 1:1 to 1:3.5. The ratio of the molar amount of nitric acid to the hydroxyl group equivalent of the compound is from 1:1 to 15:1.
Electrochemical Alcohol Nitration Systems and Methods
Electrochemistry is used to generate active nitrating species from nitrate salt in situ in an aprotic solvent to eliminate acidic and/or toxic waste streams associated with the production of energetic materials. The systems/methods perform alcohol nitration without using nitric acid and/or sulfuric acid. As a result, the systems/methods may be operated under milder conditions (e.g., room temperature and ambient pressure). In addition, the disclosed systems/methods offer high product selectivity via controlling electrolysis potential. The electrochemical synthetic method is scalable, highly amenable to continuous processing and can make use of inexpensive feedstocks, making the systems/methods well-suited to large-scale manufacture.
Electrochemical Alcohol Nitration Systems and Methods
Electrochemistry is used to generate active nitrating species from nitrate salt in situ in an aprotic solvent to eliminate acidic and/or toxic waste streams associated with the production of energetic materials. The systems/methods perform alcohol nitration without using nitric acid and/or sulfuric acid. As a result, the systems/methods may be operated under milder conditions (e.g., room temperature and ambient pressure). In addition, the disclosed systems/methods offer high product selectivity via controlling electrolysis potential. The electrochemical synthetic method is scalable, highly amenable to continuous processing and can make use of inexpensive feedstocks, making the systems/methods well-suited to large-scale manufacture.