首页> 外国专利> PRODUCTION OF HIGH-PURITY ANTIMONY TRIOXIDE WITH LOW-LEVEL ALPHA-DOSE

PRODUCTION OF HIGH-PURITY ANTIMONY TRIOXIDE WITH LOW-LEVEL ALPHA-DOSE

机译:低水平α-剂量生产高纯三氧化二锑

摘要

PURPOSE: To obtain antimony trioxide improved in both purity and dispersibility at low cost, by dissolving in an alcohol a fraction obtained by vacuum distillation of a specified solution of crude antimony trioxide followed by adding water to the resultant alcoholic solution and then conducting solid-liquid separation and then by bringing the resultant solid into contact with an alkali to carry out a further solid-liquid separation. ;CONSTITUTION: Firstly, a liquid A is obtained in the 1st process where crude antimony trioxide is dissolved with hydrochloric acid and a solid-liquid separation is conducted. Second, a high-temperature fraction B is obtained in the 2nd process where a low- temperature fraction (100°C) is removed from the liquid A followed by vacuum distillation at ≥100°C. Third, a solid C such as antimony oxychloride is obtained in the 3rd process where the component B is dissolved in an alcohol followed by adding water to the resultant alcoholic solution to effect hydrolyzing the component B followed by carrying out a solid-liquid separation. Finally, the objective high-purity antimony trioxide ≤0.005 counts/cm2.hr in α-ray radiation and ≤10ppm in impurity content is obtained through the 4th process where the component C is brought into contact with an alkali such as ammonia water to form antimony trioxide followed by conducting a solid-liquid separation.;COPYRIGHT: (C)1994,JPO&Japio
机译:用途:为了以低成本获得纯度和分散性均得到改善的三氧化二锑,方法是将馏出的三氧化二锑的特定溶液真空蒸馏,然后将水加到所得的乙醇溶液中,然后进行固液混合,将馏分溶于醇中。分离,然后使所得的固体与碱接触以进行进一步的固液分离。 ;组成:首先,在第一步骤中获得液体A,其中将粗制三氧化二锑用盐酸溶解,并进行固液分离。第二,在第二步骤中获得高温馏分B,其中从液体A中除去低温馏分(100℃),然后在≥100℃下进行真空蒸馏。第三,在第三步骤中获得固体C,例如三氯氧化锑,其中将组分B溶解在醇中,然后将水加到所得的醇溶液中以水解组分B,然后进行固液分离。最后,通过第四步使组分C与金属C接触,得到目标高纯三氧化二锑在α射线辐射中≤0.005counts / cm 2 .hr,杂质含量≤10ppm。碱液,例如氨水,形成三氧化二锑,然后进行固液分离。;版权所有:(C)1994,日本特许厅

著录项

  • 公开/公告号JPH06256019A

    专利类型

  • 公开/公告日1994-09-13

    原文格式PDF

  • 申请/专利权人 DOWA CHEM KK;DOWA MINING CO LTD;

    申请/专利号JP19910284257

  • 发明设计人 NAGAO JUNICHI;NOGAMI TOKUAKI;

    申请日1991-08-06

  • 分类号C01G30/00;

  • 国家 JP

  • 入库时间 2022-08-22 04:54:43

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