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A process and reactor for the preparation of a concentrated ammonium nitrate solution.

机译:用于制备浓硝酸铵溶液的方法和反应器。

摘要

Ammonium nitrate solutions of concentrations up to 99.8% NH4NO3 are prepared by reacting aqueous nitric acid with anhydrous ammonia at a temperature and pressure which cause the solution to boil, and recirculating this solution by means of the steam produced in it. As shown, the apparatus consists of three superposed chambers 2, 3 and 4, the upper and lower communicating by a reaction tube 5 which extends well into the lower chamber 4 and is flush with the base of the top chamber 2 and by other tubes 6a and 6b which extend into the top and bottom chambers but not as far down into the bottom chamber as the first tube 5. The middle section contains an inlet 13 and an PICT:1105466/C1/1 outlet pipe 14 for a fluid (steam or water) and acts as a heat exchanger. The apparatus is filled with ammonia solution and nitric acid is passed into the second set of tubes 6 through diffusers. Reaction occurs in these tubes, and the heat of reaction generates steam which circulates the solution up these tubes and down the reaction tube 5. If nitric acid of less than 62.5% concentration is used heat must be externally supplied by steam through the central vessel 3, if above 62.5% concentration the system is water cooled. Concentrated ammonium nitrate solution is removed from the base of the top chamber 2 and steam from the very top 18, a set of baffles 17 preventing the removal of the nitrate solution through this outlet. The process may be carried out at atmospheric pressure or above or below. The partial pressure of the steam in the reaction vessel may be decreased by the addition of air, gaseous ammonia or a mixture of the two.
机译:通过使硝酸水溶液与无水氨在导致溶液沸腾的温度和压力下反应,并利用其中产生的蒸汽将该溶液再循环,来制备浓度高达99.8%NH4NO3的硝酸铵溶液。如图所示,该装置由三个叠置的腔室2、3和4组成,上部和下部通过反应管5连通,该反应管5很好地延伸到下部室4中并与顶室2的底部齐平,并且通过其他管6a和6b延伸到顶部和底部腔室,但不像第一管5向下延伸到底部腔室。中间部分包含用于流体的入口13和出口管14(蒸汽或水),并充当热交换器。该设备充满氨溶液,硝酸通过扩散器进入第二组管6。在这些管中发生反应,并且反应热产生蒸汽,使溶液沿这些管向上和向下向反应管5循环。如果使用浓度低于62.5%的硝酸,则必须通过中央容器3通过蒸汽从外部提供热量,如果浓度高于62.5%,则将系统水冷。从顶部腔室2的底部除去浓硝酸铵溶液,并从最顶部18除去蒸汽,一组挡板17阻止硝酸铵溶液通过该出口除去。该方法可以在大气压或高于或低于大气压下进行。可以通过添加空气,气态氨或两者的混合物来降低反应容器中蒸汽的分压。

著录项

  • 公开/公告号DK115837B

    专利类型

  • 公开/公告日1969-11-17

    原文格式PDF

  • 申请/专利权人 ROGER MAX KALTENBACH;

    申请/专利号DK19660002312

  • 发明设计人 ROGER MAX KALTENBACH;

    申请日1966-05-05

  • 分类号C01C1/18;

  • 国家 DK

  • 入库时间 2022-08-23 11:35:55

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