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PROCESS FOR EXTRACTION OF ALUMINA FROM ORES BY SOLUTION OF CAUSTIC SODA AND SODIUM ALUMINATE

机译:苛性钠和铝酸钠溶液从矿石中提取氧化铝的方法

摘要

Bauxite is treated (to achieve a dissolution of the alumina content of the bauxite) with an aqueous solution of caustic soda and sodium aluminate in suspension in a series of pressure stages of increasing temperature, the final pressure stage being heated by live steam. The suspension is then passed through a series of expansion stages in which the suspension is cooled by partial vaporization. The first and each intermediate pressure stage comprises a mixing exchanger 44 and reservoir 45, suspension passing from the preceding stage into mixing exchanger 44 where it is heated to near its boiling point by direct injection of steam from a corresponding expansion stage 41. The reheated suspension remains in reservoir 45 until the solubility equilibria are reached, when an amount of suspension equal to that received from the preceding stage is passed via 46 to the next pressure stage, the excess being pumped via 47 to evaporator 42 wherein it is partially vaporized by the steam from 41, the remaining unvaporized suspension returning to the reservoir by gravity. In a modification of the process only the aqueous solution of NaOH and NaAlO 2 is passed through the initial pressure stage or stages and the bauxite is added in a later stage.
机译:在一系列升高温度的压力阶段中,用悬浮的苛性钠和铝酸钠水溶液处理铝土矿(以实现铝土矿中氧化铝含量的溶解),最终压力阶段由新鲜蒸汽加热。然后使悬浮液通过一系列的膨胀阶段,在其中通过部分汽化冷却悬浮液。第一中间压力级和每个中间压力级包括混合交换器44和储存器45,悬浮液从前一阶段进入混合交换器44,在此处通过直接从相应的膨胀级41注入蒸汽将其加热到接近其沸点。残留物保留在储液器45中直到达到溶解度平衡为止,当等于从前一级接收的悬浮液的量通过46进入下一压力级时,多余的悬浮液通过47泵送到蒸发器42,在此蒸发器将其部分蒸发。蒸汽从41排出,剩余的未蒸发悬浮液通过重力返回储层。在该方法的改进中,仅使NaOH和NaAlO 2的水溶液通过一个或多个初始压力阶段,并且在随后的阶段中添加铝土矿。

著录项

  • 公开/公告号ES351740A1

    专利类型

  • 公开/公告日1969-12-01

    原文格式PDF

  • 申请/专利权人 PECHINEY COMPAGNIE DE PRODUITS CHIMIQUES ET;

    申请/专利号ES19680351740

  • 发明设计人

    申请日1968-03-18

  • 分类号C01F;

  • 国家 ES

  • 入库时间 2022-08-23 11:28:00

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