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    • 1. 发明授权
    • Process for the preparation of titanium dioxide
    • 二氧化钛的制备方法
    • US5229087A
    • 1993-07-20
    • US523107
    • 1990-05-14
    • Karl-Heinz SchultzGunter LailachRudolf Gerken
    • Karl-Heinz SchultzGunter LailachRudolf Gerken
    • C01B17/90C01G23/053C22B34/12
    • C01B17/901C01G23/0532C22B34/125C22B34/1259
    • A process for the preparation of titanium dioxide by the sulphate process in which titanium raw materials are decomposed with sulphuric acid, the resulting titanyl sulphate is hydrolyzed, the waste acid is separated from the hydrolyzate and evaporated to a concentration of 60 to 70%, sulphuric acid is separated from the solid metal sulphates, and the sulphuric acid which has been concentrated by evaporation is used again for the decomposition of the titanium raw material, the improvement wherein the 60 to 70% sulphuric acid is concentrated to 70 to 80% H.sub.2 SO.sub.4 in a further evaporation stage and the concentration of a part of this sulphuric acid is raised to a concentration of 98 to 99% H.sub.2 SO.sub.4 by the absorption of SO.sub.3 and then used together with the remainder of the above-mentioned 70 to 80% sulphuric acid for the decomposition of titanium raw materials.
    • 通过硫酸盐工艺制备二氧化钛的方法,其中钛原料用硫酸分解,得到的硫酸氧钛被水解,废酸与水解产物分离并蒸发至60至70%的浓度,硫酸 酸与固体金属硫酸盐分离,通过蒸发浓缩的硫酸再次用于钛原料的分解,其中将60-70%硫酸浓缩至70-80%H 2 SO 4的改进 进一步蒸发阶段,通过吸收SO 3将该硫酸的一部分浓度提高至98至99%H 2 SO 4的浓度,然后与剩余的上述70-80%硫酸一起用于 分解钛原料。
    • 2. 发明授权
    • Process for the purification and reheating of exhaust gases
    • 废气净化和再加热的方法
    • US4931269A
    • 1990-06-05
    • US262144
    • 1988-10-21
    • Gunter LailachRudolf Gerken
    • Gunter LailachRudolf Gerken
    • B01D53/34B01D53/50B01D53/77C01B17/60C01B17/74C01B17/775
    • C01B17/60B01D53/507C01B17/74
    • A process for the removal of dust and sulphur dioxide from hot exhaust gases which have a low hydrogen halide content and the reheating of the purified exhaust gases, wherein(a) the hot exhaust gases are cooled to temperatures below 135.degree. C. by scrubbing with sulphuric acid,(b) sulphuric acid containing solids and dissolved metal sulphates is then separated from the exhaust gases from (a),(c) the exhaust gases from (b) are cooled to temperatures of 50.degree. to 70.degree. C. by scrubbing with 15 to 50% sulphuric acid,(d) and desulphurized with the formation of sulphuric acid,(e) and reheated to temperatures of 70.degree. to 90.degree. C. by scrubbing with 50 to 65% sulphuric acid while the sulphuric acid discharged from (c) is concentrated and(f) the sulphuric acid from stage (a) together with the solid particles contained therein is cooled with the pure sulphuric acid from (e) in heat exchangers.The process according to the invention is particularly suitable for the purification of hot exhaust gases which are at a temperature of 170.degree. to 500.degree. C.
    • 一种从具有低卤化物含量和纯化废气再热的热废气中去除灰尘和二氧化硫的方法,其中(a)将热废气通过以下方式洗涤而被冷却至低于135℃的温度: 硫酸,(b)含硫固体和溶解的金属硫酸盐然后从(a),(c)的废气中分离,(b)的废气通过洗涤被冷却至50至70℃的温度 用15〜50%的硫酸,(d),硫酸形成硫酸脱硫,(e),再用50〜65%的硫酸洗涤再次加热至70〜90℃, (c)浓缩,(f)来自步骤(a)的硫酸与其中所含的固体颗粒一起用(e)在热交换器中的纯硫酸冷却。 根据本发明的方法特别适合于在170℃至500℃的温度下净化热废气。
    • 9. 发明授权
    • Process for desulphurizing flue gases
    • 烟气脱硫工艺
    • US4670235A
    • 1987-06-02
    • US775201
    • 1985-09-12
    • Gunter LailachRudolf GerkenKarl-Heinz Schultz
    • Gunter LailachRudolf GerkenKarl-Heinz Schultz
    • B01D53/50B01D53/68B01D53/77B01D53/86C01B17/775B01D53/14C01B17/90
    • B01D53/68B01D53/8609C01B17/775
    • In the desulphurizing of SO.sub.2 - and hydrogen halide-containing flue gases by catalytically oxidizing the sulphur dioxide on moist active carbon at a temperature of from 45.degree. to 70.degree. C. with the formation of 3 to 20% dilute sulphuric acid, the improvement which comprises contacting the dilute sulphuric acid with the hot flue gases to be desulphurized so as to evaporate water resulting sulphuric acid of a concentration of from 60 to 85%, and removing by evaporation the hydrogen chloride and hydrogen fluoride dissolved in the dilute sulphuric acid. Advantageously evaporation is carried out in two scrubbing stages, the hydrogen chloride and hydrogen fluoride being removed, by vacuum evaporation or by stripping with air or flue gas, from a mixture of the dilute sulphuric acid from the second scrubbing stage with the concentrated sulphuric acid from the first scrubbing stage, the mixture having the H.sub.2 SO.sub.4 concentration of from 40 to 70%.
    • 在SO2-和含卤化氢的烟道气的脱硫中,通过在温度为45〜70℃的温度下在湿活性炭上催化氧化二氧化硫,形成3〜20%的稀硫酸, 包括使稀硫酸与待脱硫的热烟道气接触,以使水蒸发得到浓度为60至85%的硫酸,并通过蒸发除去溶解在稀硫酸中的氯化氢和氟化氢。 有利地,在两个洗涤阶段进行蒸发,通过真空蒸发或通过空气或烟道气从第二洗涤阶段的稀硫酸的混合物中除去氯化氢和氟化氢,使浓硫酸从 第一次洗涤阶段,该混合物的H 2 SO 4浓度为40-70%。