首页> 外国专利> Preparing salt of O-acetylsalicylic acid of basic amino acid, by contacting, in reactor, aqueous solution of basic amino acid and solution of O-acetylsalicylic acid dissolved in solvent, and introducing part of basic amino acid in reactor

Preparing salt of O-acetylsalicylic acid of basic amino acid, by contacting, in reactor, aqueous solution of basic amino acid and solution of O-acetylsalicylic acid dissolved in solvent, and introducing part of basic amino acid in reactor

机译:通过在反应器中使碱性氨基酸的水溶液与溶解在溶剂中的O-乙酰基水杨酸的溶液接触,并在反应器中引入部分碱性氨基酸,来制备碱性氨基酸的O-乙酰水杨酸的盐

摘要

Preparing a salt of O-acetylsalicylic acid of basic amino acid, comprises continuously contacting, in a reactor (4), an aqueous solution of basic amino acid and a solution of O-acetylsalicylic acid dissolved in a solvent, and introducing a part of basic amino acid in the reactor, where: a quantity of the basic amino acid is relative to a stoichiometry ratio; and a weight concentration of the solutions is less than a saturation and higher than 5 wt.% of O-acetylsalicylic acid and 20 wt.% of basic amino acid. Preparing a salt of O-acetylsalicylic acid of basic amino acid, comprises continuously contacting, in a reactor (4), an aqueous solution of basic amino acid and a solution of O-acetylsalicylic acid dissolved in a solvent, and introducing a part of basic amino acid in the reactor, where: a quantity of the basic amino acid is relative to a stoichiometry ratio; a weight concentration of the solutions is less than a saturation and higher than 5 wt.% of O-acetylsalicylic acid and 20 wt.% of basic amino acid; the reaction is carried out in suspension under an agitation effect with an expenditure of energy of 0.5-2 W/l of reactional medium; a temperature of the reactional medium in the reactor is constant and is 2-25[deg] C; a reactor volume and supply flow values are such that the reaction solutions are maintained in the reactor for 15-60 minutes; an output flow from the reactor is directly supplied to a device (12), which separates the liquid phase and solid phase from output flow; and the solid phase formed in the reactor is dried for obtaining the salt in the form of powder.
机译:制备碱性氨基酸的O-乙酰基水杨酸的盐,包括在反应器(4)中使碱性氨基酸的水溶液和溶解在溶剂中的O-乙酰基水杨酸的溶液连续接触,并引入一部分碱性反应器中的氨基酸,其中:碱性氨基酸的量相对于化学计量比;溶液的重量浓度小于饱和度且大于5重量%的O-乙酰基水杨酸和20重量%的碱性氨基酸。制备碱性氨基酸的O-乙酰基水杨酸的盐,包括在反应器(4)中使碱性氨基酸的水溶液和溶解在溶剂中的O-乙酰基水杨酸的溶液连续接触,并引入一部分碱性反应器中的氨基酸,其中:碱性氨基酸的量相对于化学计量比;溶液的重量浓度小于饱和且大于5重量%的O-乙酰基水杨酸和20重量%的碱性氨基酸;反应在搅拌作用下在悬浮液中进行,反应介质能量消耗为0.5-2W / l。反应器中反应介质的温度恒定,为2-25℃。反应器的体积和供应流量值使得反应溶液在反应器中保持15-60分钟。来自反应器的输出流直接提供给装置(12),该装置将液相和固相与输出流分开。干燥在反应器中形成的固相,以获得粉末形式的盐。

著录项

  • 公开/公告号FR2973370A1

    专利类型

  • 公开/公告日2012-10-05

    原文格式PDF

  • 申请/专利权人 HOLIS TECHNOLOGIES;

    申请/专利号FR20110000920

  • 发明设计人 LEBORGNE FABRICE;GUYOT DANIEL;

    申请日2011-03-29

  • 分类号C07C229/26;C07C63/08;C07C229/06;

  • 国家 FR

  • 入库时间 2022-08-21 17:03:57

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