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    • 7. 发明授权
    • Electrochemical process for the production of chromic acid
    • 电化学工艺生产氯酸
    • US5068015A
    • 1991-11-26
    • US393733
    • 1989-08-15
    • Hans-Dieter BlockNorbert LonhoffBernd MakowkaHelmut KlotzRainer WeberBernhard Spreckelmeyer
    • Hans-Dieter BlockNorbert LonhoffBernd MakowkaHelmut KlotzRainer WeberBernhard Spreckelmeyer
    • C25B1/00C25B1/22C25B15/08
    • C25B1/22
    • A process for the production of chromic acid by the multistage electrolysis of dichromate and/or monochromate solutions in two-compartment electrolysis cells, of which the anode and cathode compartments are separated by cation exchanger membranes, at temperatures in the range from 50.degree. to 90.degree. C., the dichromate and/or monochromate solutions being obtained by the digestion of chrome ores and leaching, the improvement wherein, optionally after the removal of aluminum, vanadium and other impurities, the monochromate solution obtained after leaching is adjusted at 20.degree. to 110.degree. C. to a pH value of from 8 to 12 by the addition and/or in situ formation of carbonate in a quantity of from 0.01 to 0.18 mol/l (for 300 to 500 g/l Na.sub.2 CrO.sub.4, converted with CO.sub.2 under pressure into a dichromate-containing solution, the dichromate-containing solution is introduced into the anode compartment of the electrolysis cell, a solution containing chromic acid, in which the molar ratio of Na ions to chromic acid is from 0.45:0.55 to 0.30:0.70, is electrolytically produced and the chromic acid is worked up by crystallization, washing and drying.
    • 通过在两室电解池中的重铬酸盐和/或单色溶液的多级电解生产铬酸的方法,其中阳极和阴极室由阳离子交换膜分离,温度范围为50至90℃ ℃,通过铬矿和沥滤的消解获得的重铬酸盐和/或单色溶液,其中任选地在除去铝,钒和其它杂质之后,将浸出后获得的单色溶液调节至20℃至 通过加入和/或原位形成量为0.01至0.18mol / l的碳酸盐(对于300至500g / l的Na 2 CrO 4,在压力下用CO 2转化),将pH值为8至12 将含有重铬酸盐的溶液引入电解槽的阳极室中,将含有铬酸的溶液与Na离子的摩尔比 欧米酸为0.45:0.55-0.30:0.70,经电解生产,铬酸通过结晶,洗涤和干燥处理。
    • 10. 发明授权
    • Process for the preparation of chromic acid
    • 制备色素的方法
    • US5096548A
    • 1992-03-17
    • US626076
    • 1990-12-11
    • Norbert LonhoffLudwig SchmidtHans-Dieter BlockRainer Weber
    • Norbert LonhoffLudwig SchmidtHans-Dieter BlockRainer Weber
    • C25B1/00B01J47/12C01G37/033C25B1/22C25B15/08C25C1/10
    • C01G37/033C25B1/22C25C1/10
    • A process for the production of chromic acid, comprising(a) dissolving ferrochrome in sulphuric acid and mother liquor from the subsequent crystallization of ammonium chrome alum, optionally with the addition of at least one of catholyte and anolyte overflow from the subsequent electrolysis,(b) removing undissolved constituents by filtration,(c) removing dissolved iron by the addition of at least one of ammonia and ammonium sulphate to the filtrate obtained, crystallizing iron ammonium sulphate and filtering,(d) crystallizing and filtering ammonium chrome alum from the remaining solution and returning the filtrate for dissolving ferrochrome in step (a),(e) dissolving the ammonium chrome alum in water,(f) precipitating and separating chromium-(III) hydroxide from the resulting solution by adding a base, optionally under reducing conditions,(g) dissolving the separated chromium hydroxide in chromic acid and optionally sulphuric acid so that either a single solution in chromic acid is obtained or two solutions are obtained, one in chromic acid and another in sulphuric acid,(h) separating the solution(s) from undissolved constituents, and(i) utilizing the solution of chromium hydroxide in chromic acid as anolyte in the electrolytic production of chromic acid in an electrolytic cell divided by a membrane, and either utilizing the same solution as catholyte in the above mentioned electrolytic cell divided by a membrane or utilizing the solution of chromium hydroxide in sulphuric acid as catholyte in the above mentioned electrolytic cell divided by a membrane, hydrogen and metallic chromium being deposited electrolytically at the cathode and/or chromium (II) ions being produced electrolytically at the cathode.
    • 一种生产铬酸的方法,包括(a)将铬铁铬酸盐和母液从随后的铵铬明矾结晶中溶解,任选地从随后的电解中加入至少一种阴极电解液和阳极电解液溢出物(b )通过过滤除去未溶解的组分,(c)通过向所得滤液中加入至少一种氨和硫酸铵除去溶解的铁,结晶硫酸铁铵并过滤,(d)从剩余溶液中结晶并过滤铵铬明矾 并在步骤(a)中返回用于溶解铬铁的滤液,(e)将铵铬明矾溶解在水中,(f)通过加入碱(任选在还原条件下)将所得溶液中的铬 - (III) (g)将分离的氢氧化铬溶解在铬酸和任选的硫酸中,使得单一的铬酸溶液 得到两种溶液,一种在铬酸中,另一种在硫酸中,(h)将溶液与未溶解的组分分离,和(i)在电解生产中利用铬酸中的铬酸溶液作为阳极电解液 在由电解槽中分离的膜中的铬酸,或者利用与上述电解槽中的阴极电解液相同的溶液,或者利用氢氧化铬溶液作为阴极电解液,除去上述电解槽 在阴极处电解沉积的阴极和/或铬(II)离子沉积的膜,氢和金属铬。