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Method for oxidizing trivalent titanium in solid titanium oxide-containing materials

机译:固体含钛氧化物材料中三价钛的氧化方法

摘要

An oxidic titanium-containing material comprising trivalent titanium oxide is agglomerated and then partly oxidised by means of an oxidising gas containing free oxygen in the presence of water and an electrolyte below 100 DEG C. and thereafter oxidising with a similar gas at a temperature, preferably gradually increasing, in the range 250-400 DEG C. such that autoxidation and consequent glowing is avoided. The process is particularly applicable to titanium oxide concentrates produced by thermal reduction in a rotary furnace, which have a particle size of 1-5 microns and are pyrophoric at 150 DEG C. and above. The agglomeration preferably consists of pelleting to a particle diameter of 3-15 mm. using, e.g. dilute sulphuric acid. The first oxidation stage may be conducted as described and claimed in Specification 809,753, to which reference is made. It is preferred in the second oxidation step to pass a hot gas through a layer of the material at such a velocity that the heat of reaction is substantially immediately removed, but the temperature may be controlled, e.g. in a rotary furnace, multiple-hearth furnace or tunnel kiln, by restricting the access of air. The oxidising gas may also be passed counter-currently through a moving layer of pellets. Where air is used to cool the oxidised material, the warmed air may be used in an oil burner and/or in admixture with the oxidising gases. In the examples, the first oxidation is performed by supporting a layer of pellets on an open wire screen and exposing to the air: in the second oxidation a stationary grate in an oil-fired chamber is employed and a preheated mixture of air and combustion gases passed therethrough. Specifications 754,453 and 791,366 also are referred to.
机译:将包含三价氧化钛的含氧化钛的材料团聚,然后在水和低于100℃的电解质的存在下,通过含有游离氧的氧化气体将其部分氧化,然后在相同温度下,优选用类似气体氧化,优选在250-400℃的范围内逐渐增加,从而避免了自氧化和随之而来的发光。该方法特别适用于通过在旋转炉中热还原而生产的氧化钛浓缩物,其粒度为1-5微米,并且在150℃及以上具有自燃性。附聚优选由造粒至3-15mm的粒径组成。使用,例如稀硫酸。第一氧化阶段可以如参考说明书809753中所述和要求的那样进行。在第二氧化步骤中,优选使热气体以基本上立即除去反应热的速度通过材料的层,但是可以控制温度,例如控制温度。在回转炉,多炉膛炉或隧道窑中,通过限制空气的进入。氧化气体也可以逆流通过小球的运动层。在使用空气冷却氧化材料的情况下,加热的空气可用于燃油燃烧器和/或与氧化气体混合。在示例中,第一次氧化是通过在开放式金属丝网筛上支撑一层小球并暴露于空气中来进行的:第二次氧化中,使用燃油室中的固定炉排,并预热了空气和燃烧气体的混合物通过。规格754,453和791,366也可参考。

著录项

  • 公开/公告号GB858785A

    专利类型

  • 公开/公告日1961-01-18

    原文格式PDF

  • 申请/专利权人 TITAN CO. A/S;

    申请/专利号GB19580029053

  • 发明设计人

    申请日1958-09-10

  • 分类号C22B34/12;

  • 国家 GB

  • 入库时间 2022-08-23 18:23:02

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