Abstract in simplified Chinese:有机硝酸酯系借由以下步骤自一元醇、二元醇或多元醇制备(i)将以下物质同时馈入第一连续流动微型反应器单元中(a)浓硝酸,(b)乙酸酐,(c)视情况选用之催化量的并非硝酸之强无机酸,及(d)视情况选用之溶剂,从而获得乙酰硝酸酯溶液,及(ii)将步骤(i)中获得之乙酰硝酸酯溶液及呈液体形式或溶于溶剂中之该一元醇、二元醇或多元醇同时馈入第二连续流动微型反应器中,从而获得该有机硝酸酯溶液,及(iii)视情况,将该有机硝酸酯自步骤(ii)获得之该溶液中分离出来。本发明方法尤其适用于诸如1,4-丁二醇之二元醇的单硝化反应。
Abstract:
The present invention relates to a process for preparing hexanoic acid, 6-(nitrooxy)-, (1S,2E)-3-[(1R,2R,3S,5R)-2-[(2Z)-7-(ethylamino)-7-oxo-2-hepten-1-yl]-3,5-dihydroxycyclopentyl]-1-(2-phenylethyl)-2-propen-1-yl ester of formula (I).
In accordance with the present invention, the compound (I) can be efficiently prepared with high purity by coupling bimatoprost in a boronate protected form with 6-(nitrooxy)hexanoyl chloride and removing the boronate protecting group. The invention also relates to a process for the preparation of 6-(nitrooxy) hexanoic acid having a HPLC purity equal to or greater than 99% and containing an amount of 6-{[6-(nitrooxy)hexanoyl]oxy}hexanoic acid (compound (IXa) equal to or lower than 0.2%.
Abstract:
The invention relates to a safe and efficient process for the hydrolysis of α,ω-C3-10alkanediol mononitrate monoacylates. The process is safer to operators and allows to obtain advantageous yields on industrial scale.
Abstract:
The invention relates to a safe and efficient process for the nitrate ester formation of an α,ω-C3-10alkanediol monoacylate. The process is safer to operators and allows to obtain advantageous yields on industrial scale.
Abstract:
The present invention provides a method for producing alkyl nitrate. The centrifugal extraction equipment acts as the esterification separator; a mixed acid solution containing sulfuric acid and nitric acid enters from the heavy phase inlet of the centrifugal extraction equipment; alkyl alcohol enters from the light phase inlet of the centrifugal extraction equipment; the feeding molar ratio of alkyl alcohol and nitric acid equals to 1:1.0-3.0; esterification reaction occurs with the mixed acid and alkyl alcohol at a temperature of 10˜60° C. under the rotating speed of 800-2000 r/min; under the action of centrifugal force, the generated coarse ester as a light phase and the spent acid as a heavy phase are separated; coarse ester as a light phase is discharged through the light-phase outlet of the centrifugal extractor; the spent acid as a heavy phase is discharged through the heavy-phase outlet of the centrifugal extractor; after alkali washing and water washing conventionally, coarse ester is dehydrated for drying and purified, then the refining products of alkyl nitrate is obtained. In the method of the present invention, esterification reaction, the separation of reaction products and the spent acid are finished in the same reactor simultaneously, which reduces the contact time of reaction products with the spent acid greatly, avoids the side reaction effectively, and ensures the safety of esterification process.
Abstract:
A method producing a surfactant from glycerol by converting glycerol, in a first step, to glycidol, polymerizing glycidol to an aliphatic alcohol and finally substituting a hydroxyl group with a substitute anion.
Abstract:
Methods of forming a nitrate ester include combining at least one nitrate salt and sulfuric acid to form a nitrating solution and adding an aliphatic polyol to the nitrating solution. Nitrate esters formed by this method may be, for example, triethylene glycol dinitrate (TEGDN), pentaerythritol tetranitrate (PETN), diglycerol tetranitrate (DGTN), 1,1,1-tris(methylol)ethane trinitrate (TMETN), 1,2,4-butanetriol trinitrate (BTTN), nitroglycerin (NG), diethylene glycol dinitrate (DEGDN), ethylene glycol dinitrate (EGDN), metriol trinitrate (MTN), nitrocellulose (NC), or 1,2-propanediol dinitrate (PDDN).