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    • 5. 发明授权
    • Chlorination of impure magnesium chloride melt
    • 氯化不纯的氯化镁熔体
    • US4248839A
    • 1981-02-03
    • US61587
    • 1979-07-30
    • Robert D. ToomeyBrian R. DavisRamaswami NeelamegghamR. Keith Darlington
    • Robert D. ToomeyBrian R. DavisRamaswami NeelamegghamR. Keith Darlington
    • C01F5/32
    • C01F5/32
    • Magnesium oxide is chlorinated in molten impure magnesium chlorine with chlorine gas by adding ferrous chloride to magnesium chloride brine, drying the brine, adding a mixture of calcined petroleum coke and charcoal to the dried brine, melting the product and chlorinating the formed melt. Ferrous chloride is added in amounts sufficient to provide from about 1.0% to 2.2% by weight of iron in the dried product. A highly reactive carbon source is added in amounts of from about 0.8 to 2.3% by weight and a carbon source that is less reactive than the highly reactive carbon source is added in amounts ranging from about 0.8 to 2.3% by weight of dried brine. Iron levels in the magnesium chloride melt may be adjusted upwardly by addition of a mixture of iron oxide and charcoal.A melt cell characterized by side entry electrodes disposed at angles from 40.degree. to 50.degree., an arched roof configuration, and an improved electrode refractory and ceramic sleeve construction is used to chlorinate the magnesium.
    • 通过向氯化镁盐水中加入氯化亚铁,干燥盐水,将煅烧石油焦炭和木炭的混合物加入到干燥的盐水中,使产物熔化并对形成的熔体进行氯化,将氧化镁在熔融的不纯的氯化镁中用氯气氯化。 加入氯化亚铁的量足以在干燥产物中提供约1.0重量%至2.2重量%的铁。 高反应性碳源的添加量为约0.8-2.3重量%,反应性低于高反应性碳源的碳源的加入量为干燥盐水的约0.8-2.3重量%。 可以通过加入氧化铁和木炭的混合物向上调节氯化镁熔体中的铁含量。 一种熔融池,其特征在于以40°至50°的角度设置的侧入口电极,拱形屋顶结构以及改进的电极耐火材料和陶瓷套筒构造用于对镁进行氯化。
    • 7. 发明授权
    • Process for manufacturing titanium dioxide
    • 制造二氧化钛的方法
    • US4288418A
    • 1981-09-08
    • US202039
    • 1980-10-29
    • Brian R. DavisJoseph A. Rahm
    • Brian R. DavisJoseph A. Rahm
    • C01G23/053C22B34/12
    • C22B34/125C01G23/0532Y02P10/212
    • A process is provided for the manufacture of titanium dioxide pigment wherein excess ilmenite ore is reacted with dilute sulfuric acid having a concentration of between about 25% and about 60% by weight and in preferably at least two stages wherein the first stage is maintained at a temperature up to about 140.degree. C. and the second stage is conducted at a lower temperature (than the first stage) which is below about 100.degree. C. to provide a salt solution of titanium and iron. Thereafter, the titanium is hydrolyzed to provide titanium dioxide hydrate accompanied by recycling the spent acid from the hydrolysis for reaction with the ilmenite ore charged to the process. The titanium hydrate is calcined to provide titanium dioxide pigment.
    • 提供了一种用于制造二氧化钛颜料的方法,其中过量的钛铁矿矿石与浓硫酸的浓度在约25%至约60%之间,优选至少两级的稀硫酸反应,其中第一级保持在 温度高达约140℃,第二阶段在低于约100℃的较低温度(低于第一阶段)进行,以提供钛和铁的盐溶液。 此后,钛被水解以提供二氧化钛水合物,伴随着从水解中回收废酸与用于与该方法反应的钛铁矿的反应。 将钛水合物煅烧以提供二氧化钛颜料。