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A method for the production of propyl, nitrate, or isopropyl nitrate

机译:一种生产硝酸丙酯,硝酸酯或异丙基硝酸酯的方法

摘要

A process for the continuous production of a propyl nitrate comprises keeping an aqueous reaction solution containing per 100 parts thereof between 30 and 45 parts nitric acid, at least 3 parts urea, and between 10 and 31.5 parts ammonium nitrate, all by weight, at a temperature between 105 DEG and 112 DEG C. (preferably 107-110 DEG C.) at atmospheric pressure, while maintaining this composition and the bulk by continuously introducing under the surface of the reaction solution nitric acid, the appropriate propyl alcohol, water and urea, at least the continuously added nitric acid and said propyl alcohol being introduced in separate streams, if desired already diluted with at least part of the continuously added water, at rates such that the molar ratio of added nitric acid to said propyl alcohol exceeds unity, and the continuously added urea being introduced in solution in at least one of the liquids streaming into the solution, continuously distilling away and condensing the resulting vapour mixture containing the propyl nitrate formed, continuously bleeding off a portion of the aqueous reaction solution of said composition, and separating the propyl nitrate rich layer of the condensate from the water rich layer. The aqueous reaction solution may be progressively formed by heating a solution containing per 100 parts between 30 and 45 parts nitric acid and at least 9 parts urea or less than 9 parts but greater than 3 parts urea together with between 5.3 and 2.3 parts ammonium nitrate for each part of urea short of 9 parts. Preferred nitric acid, urea and ammonium nitrate concentrations in the aqueous reaction solution are 45 per cent, 3 per cent and 22 per cent at 110 DEG C.; 40 per cent, 3 per cent and 14 per cent at 110 DEG C.; 40 per cent, 4 per cent and 18 per cent at 108 DEG C.; 32 per cent, 6 per cent and 13 per cent at 105 DEG C. The examples describe the preparation of n-propyl and isopropyl nitrate. Specifications 379,312, 540,050, 696,489 and 743,141 are referred to.
机译:连续生产硝酸丙酯的方法包括使反应溶液的每100重量份含有30-45重量份的硝酸,至少3重量份的尿素和10-31.5重量份的硝酸铵,按重量计为通过在反应溶液的表面下连续引入硝酸,适当的丙醇,水和尿素来保持该组成和体积,同时在大气压下在105-112℃(优选107-110℃)的温度下保持该组成和体积。 ,将至少连续加入的硝酸和所述丙醇以分开的物流引入,如果需要,已经用至少一部分连续加入的水稀释,其速率应使加入的硝酸与所述丙醇的摩尔比超过1,并且将连续添加的尿素以至少一种流入溶液中的液体的形式引入溶液中,不断蒸馏除去并冷凝结果形成的含有硝酸丙酯的蒸气混合物,连续渗出一部分所述组合物的水性反应溶液,并将冷凝液的富含硝酸丙酯的层与富含水的层分离。反应水溶液可以通过加热每100份包含30至45份硝酸和至少9份尿素或少于9份但大于3份尿素以及5.3至2.3份硝酸铵的溶液逐渐形成。每份尿素不足9份。反应水溶液中优选的硝酸,尿素和硝酸铵的浓度在110℃为45%,3%和22%; 110℃时分别为40%,3%和14%; 108℃时分别为40%,4%和18%;在105℃下分别为32%,6%和13%。这些实施例描述了硝酸正丙基酯和硝酸异丙酯的制备。参考规格379,312、540,050、696,489和743,141。

著录项

  • 公开/公告号DE1059426B

    专利类型

  • 公开/公告日1959-06-18

    原文格式PDF

  • 申请/专利权人 ICI LTD;

    申请/专利号DE1954I009419

  • 申请日1954-11-26

  • 分类号B01J23/94;B01J27/28;B01J38/00;C07C51/31;C07C203/04;

  • 国家 DE

  • 入库时间 2022-08-23 19:59:22

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