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process for the production of industrial ceramics raw materials from alkalihaltiger alumina

机译:碱卤化铝矾土生产工业陶瓷原料的方法

摘要

Preparation of ceramic raw material on the basis of purified aluminum oxide from alumina comprises preparing an alumina raw material by Bayer process; calcinating the material to obtain a crystalline, alkali containing alumina consisting of gamma -alumina with an alpha -alumina (maximum 30%); subsequently thermally treating the alumina and processing in an intensive agitator to obtain an aqueous, alkaline suspension of alumina; contacting a bubble-forming carbon dioxide; separating dealklylated alumina from the liquid phase; and drying the dealkylated alumina to obtain purified alpha -aluminum oxide. Preparation of ceramic raw material on the basis of purified aluminum oxide from alumina comprises: (a) preparing an alumina raw material by Bayer process; (b) calcinating the material to obtain a crystalline, alkali containing alumina consisting of gamma -alumina with an alpha -alumina (maximum 30%), at 800-1200[deg]C for 0.5-3 hours; (c) subsequently thermally treating the obtained alumina; (d) processing the alumina exhibiting a Brunauer, Emmett and Teller surface of at least 30 m 2/g, and a specific particle size distribution with fine particles (less than 45 mu m) and coarse particles (less than 150 mu m) of less than 10%, in an intensive agitator with number of revolutions of 50-250 rpm to obtain an aqueous, alkaline suspension of alumina with a solid content of 60-1000 g/l; (e) contacting a bubble-forming carbon dioxide (4-10 g/kg of alumina) with a bubble diameter of 8 mu m with the aqueous, alkaline suspension of alumina at 2-10 bar; (f) continuously adjusting the retention time (10-100 seconds) of the suspension with a pressure difference of at least 2 bar; (g) separating the dealklylated alumina from the liquid phase; and (h) drying the dealkylated alumina at greater than 1200[deg]C for 4 hours to obtain purified alpha -aluminum oxide with at least 80% of alpha -aluminum oxide. Independent claims are included for: (1) a device for executing the preparation of ceramic raw material comprising an assembly for purifying and calcinating the alumina raw materials, a first assembly unit (1) for preparing the suspension, a second assembly unit (2) for carbon dioxide treatment of the suspension in the gas-tube, a third assembly unit (3) for separating dealkylated alumina and a fourth assembly unit (4) for drying the dealkylated alumina; and (2) the dealkylated aluminum oxide comprising at least 80% of alpha -oxide, remaining of transition alumina, sodium oxide (0.1 wt.%), silica (0.02 wt.%), boron oxide (0.001 wt.%), fluorine (0.01 wt.%) and chlorine (0.002 wt.%), where the Brunauer, Emmett and Teller surface of the dealkylated aluminum oxide is 0.5-10 m 2/g.
机译:基于由氧化铝提纯的氧化铝制备陶瓷原料的方法包括:通过拜耳法制备氧化铝原料。煅烧该材料以获得由γ-氧化铝和α-氧化铝(最大30%)组成的结晶的含碱氧化铝。随后对氧化铝进行热处理并在强力搅拌器中进行处理以获得氧化铝的碱性水悬浮液;接触形成气泡的二氧化碳;从液相中分离脱铝的氧化铝;干燥脱烷基氧化铝得到纯化的α-氧化铝。基于由氧化铝提纯的氧化铝制备陶瓷原料包括:(a)通过拜耳法制备氧化铝原料; (b)在800-1200℃下煅烧该材料以获得由γ-氧化铝和α-氧化铝(最大30%)组成的结晶的含碱氧化铝,历时0.5-3小时; (c)随后热处理所得的氧化铝; (d)处理具有至少30m 2> / g的Brunauer,Emmett和Teller表面并且具有细颗粒(小于45μm)和粗颗粒(小于150μm)的特定粒度分布的氧化铝在转速为50-250 rpm的强力搅拌器中,获得小于10%的固体含量为60-1000 g / l的氧化铝水成碱性悬浮液; (e)使气泡直径为8μm的气泡形成二氧化碳(4-10g / kg氧化铝)与氧化铝的碱性水悬浮液在2-10bar下接触; (f)以至少2 bar的压差连续调节悬浮液的停留时间(10-100秒); (g)将脱铝的氧化铝与液相分离; (h)将脱烷基的氧化铝在高于1200℃的温度下干燥4小时以获得具有至少80%的α-氧化铝的纯化的α-氧化铝。包括以下独立权利要求:(1)一种用于执行陶瓷原料制备的设备,该设备包括用于纯化和煅烧氧化铝原料的组件,用于制备悬浮液的第一组装单元(1),第二组装单元(2)为了对气管中的悬浮液进行二氧化碳处理,用于分离脱烷基氧化铝的第三组装单元(3)和用于干燥脱烷基氧化铝的第四组装单元(4); (2)包含至少80%的α-氧化物,剩余的过渡氧化铝,氧化钠(0.1重量%),二氧化硅(0.02重量%),氧化硼(0.001重量%),氟的脱烷基氧化铝。 (0.01 wt。%)和氯(0.002 wt。%),其中脱烷基氧化铝的Brunauer,Emmett和Teller表面为0.5-10 m 2> / g。

著录项

  • 公开/公告号DE502007005925D1

    专利类型

  • 公开/公告日2011-01-27

    原文格式PDF

  • 申请/专利权人 NABALTEC AG;

    申请/专利号DE20075005925T

  • 发明设计人 PRESCHER DIETER;KUPFER JAN;

    申请日2007-02-16

  • 分类号C01F7/02;C01F7/46;C04B14/30;C04B35/10;

  • 国家 DE

  • 入库时间 2022-08-21 17:46:49

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