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    • 2. 发明专利
    • TREATMENT OF DRAINAGE CONTAINING HYDROGEN PEROXIDE AND CHROMIUM ION
    • JPH0824897A
    • 1996-01-30
    • JP16776094
    • 1994-07-20
    • NIPPON DENKO
    • KASHIWAGI RYOICHIHAYAKAWA SATOSHI
    • C02F1/42C02F1/58C02F1/62C02F9/00
    • PURPOSE:To recover chromium portion from a drainage effectively and make it possible to recycle a treated water by passing drainage containing hydrogen peroxide and chromium ion through a hydrogen peroxide decomposition tower filled with a catalyst, then passing the drainage in which hydrogen peroxide is decomposed through an ion exchange resin tower, and thereby removing chromium ion. CONSTITUTION:Drained water containing hydrogen peroxide and chromium ion generated in a decoloring step is collected into a raw water tank 2 through effluent piping 1, and then is circulated to a hydrogen peroxide decomposition tower 5 filled with granular manganese oxide (IV) using a raw water pump 3. Hydrogen peroxide contained in the drainage is decomposed by a catalytic action of granular manganese oxide, and the concentration of hydrogen peroxide is made to be 100mg/l or less. Next, the drainage is circulated flowing down in ion-exchange resin towers 6, 7, and in this process, chromium ion and other ions are adsorbed and removed. After that, the treated water is collected into a treated water tank 8, then is sent to an original process, using a treated water pump 9 and feed piping 10, and is recycled.
    • 3. 发明专利
    • PRODUCTION OF HIGHLY PURE CHROMIUM HYDROXIDE
    • JPH0292828A
    • 1990-04-03
    • JP24478188
    • 1988-09-29
    • NIPPON DENKO
    • KASHIWAGI RYOICHI
    • C01G37/02
    • PURPOSE:To readily prepare highly pure chromium hydroxide by separating precipitates from a chromium hydroxide slurry using a trivalent chromium salt aqueous solution as a raw material, from a slurry of the precipitates and passing the slurry through an ion exchange resin column. CONSTITUTION:In a method for preparing a highly pure chromium hydroxide from a trivalent chromium salt as a raw material, the following processes are performed. The aqueous solution of the trivalent chromium salt is neutralized with caustic soda or ammonia water and the resultant precipitates are filtered off from the prepared slurry of the chromium hydroxide. The separated precipitated are suspended in water to give a slurry, which is passed through an ion exchange resin column to adsorb water-soluble impurities, thereby providing the objective highly pure chromium hydroxide. The final pH of the reaction for preparing the chromium hydroxide by neutralizing the trivalent chromium salt aqueous solution with the caustic soda or ammonia water is preferably 9.0-11.0, because a too high pH value causes the re-dissolution of the chromium hydroxide with the excess alkali to produce a chromite salt.