首页> 外国专利> PROCESS FOR PRODUCING ALUMINIUM TRIHYDRATE CONTAINING GRAINS SMALLER THAN 45 MICROMETERS UP TO 10 MASS PER CENT

PROCESS FOR PRODUCING ALUMINIUM TRIHYDRATE CONTAINING GRAINS SMALLER THAN 45 MICROMETERS UP TO 10 MASS PER CENT

机译:生产粒度小于45微米的三水合氧化铝的工艺,质量分数最高为10%

摘要

The invention concerns a process for the precipitation of aluminium hydroxide by seeding in two phases, which is intended to produce at a high level of productivity alumina with large grains, referred to as 'sandy coarse', by precipitation in a succession of tanks in cascade relationship of a supersaturated solution of sodium aluminate coming from alkaline attack on bauxite in accordance with the BAYER process. The process comprises three stages: in the first agglomeration stage, the supersaturated aluminate liquor is introduce into the tank, with an equivalent amount of terms of Na2O of between 110 and 175 g/liter, at a temperature of between 65 DEG and 80 DEG C., and seeding is effected with an amount of washed seed of between 20 and 120 g/l of aluminate, in the second stage, selective retention of the largest crystals of aluminium trihydrate formed is effected in the tanks, so as to produce a content of dry matter of between 300 and 800 g/liter of suspension, the whole of the aluminium trihydrate which is intended for the production of alumina is extracted in the course of or at the end of the second stage, in a third stage, referred to as a liquor depletion stage, an amount of seed of between 400 and 800 g/l of suspension, that is to say between 480 and 1200 g/liter of liquor, is introduced, at the end of the third stage, separation is effected on the one hand of a depleted aluminate liquor which is recycled in known fashion and on the other hand aluminium trihydrate with very fine grains, a small portion of which is recycled after washing as a seed for the agglomeration stage while the remainder is recycled as a seed to the liquor depletion stage.
机译:本发明涉及一种通过分两阶段播种来沉淀氢氧化铝的方法,该方法旨在通过在一系列级联的槽中沉淀来以高生产率生产具有大晶粒的氧化铝,称为“桑迪粗”。 BAYER方法根据碱浸蚀铝土矿得到的铝酸钠过饱和溶液的关系式。该过程包括三个阶段:在第一附聚阶段中,将过饱和的铝酸盐溶液以65至80摄氏度的等当量Na2O量在110至175克/升之间引入罐中。在第二阶段,在槽中进行形成的三水合铝最大晶体的选择性保留,以产生一定量的铝酸盐,然后用20到120 g / l铝酸盐之间的洗净种子进行播种。在300到800克/升悬浮液之间的干物质中,在第二阶段的过程中或在第三阶段结束时,提取了全部用于生产氧化铝的三水合铝。作为废液阶段,引入了400至800克/升悬浮液的种子,即480至1200克/升液体,在第三阶段结束时,进行了分离。铝酸锂的一只手以已知方式回收的铝,另一方面具有非常细的晶粒的三水合铝,洗涤后的一小部分作为结块阶段的种子被回收,而其余部分作为种子被回收到废液阶段。

著录项

  • 公开/公告号NO170074C

    专利类型

  • 公开/公告日1992-09-09

    原文格式PDF

  • 申请/专利权人 ALUMINIUM PECHINEY;

    申请/专利号NO19850004662

  • 发明设计人 VEYRIER MAURICE;

    申请日1985-11-21

  • 分类号C01F7/14;

  • 国家 NO

  • 入库时间 2022-08-22 05:34:51

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号