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    • 1. 发明专利
    • METHOD FOR RECOVERING AND REFINING RHODIUM
    • JPH03285029A
    • 1991-12-16
    • JP8357090
    • 1990-03-30
    • TANAKA PRECIOUS METAL IND
    • ICHIISHI TOMOSHISHIBAZAKI TAKUO
    • C22B11/00
    • PURPOSE:To simply recover low concn. Rh at a high recovering rate and high purity by adding SnCl2 to a rhodium-hydrochloric acid soln. having specified hydrochloric acid concn. and adsorbing Rh by a dialkyl sulfide-impregnated porous resin. CONSTITUTION:Hydrochloric acid is added to a rhodium-hydrochloric acid soln. including large amounts of base metals and having low Rh concn. to regulate the hydrochloric acid concn. to 1 to 6N. Next, SnCl2 is added to this soln. The amt. of the SnCl2 to be added is preferably regulated to 10 to 50 times, by molar ratio, to Rh. After that, this soln. is brought into contact with a porous resin impregnated with preferably >=50wt.% dialkyl sulfide to absorb Rh. Then, the porous resin adsorbed with Rh is washed by dilute hydrochloric acid of 0.5 to 1 stipulation to remove Sn or the like and is thereafter baked at about 800 deg.C. The obtd. partially oxidized metallic Rh is reduced by a hydrogen gas and is perfectly metallized. After that, this Rh is mixed with NaCl, in which a Cl2 gas is blown, and chlorination is executed at 800 to 950 deg.C for >= one hr. In this way, Rh hardly including base metals can be recovered at approximately 100% recovering rate in the shape of soluble sodium salt of chlorhodic acid.
    • 4. 发明专利
    • PREPARATION OF PLATINUM NITRATE SOLUTION
    • JPH1192150A
    • 1999-04-06
    • JP25475497
    • 1997-09-19
    • TANAKA PRECIOUS METAL IND
    • SHIBAZAKI TAKUO
    • C01G55/00B01J23/42
    • PROBLEM TO BE SOLVED: To easily prepare a platinum nitrate soln. having stability over a long period of time by adding nitric acid having a specified concn. to hydroxyplatinic acid by the sum of the amt. required to dissolve the hydroxyplatinic acid and the amt. required to stabilize the resultant platinum nitrate and dissolving the hydroxyplatinic acid. SOLUTION: Acetic acid is added to a hexahydroxopotassium platinum soln. and a formed precipitate is separated by filtration and washed to prepare hydroxyplatinic acid. Nitric acid having ∞300 g/L concn. is added to the hydroxyplatinic acid by about 8 times (mol) the amt. of platinum as the sum of about 6 times (mol) the amt. of platinum as the amt. required to dissolve the hydroxyplatinic acid and about 2 times (mol) the amt. of platinum as the amt. required to stabilize the resultant platinum nitrate soln. They are heated to about 50-100 deg.C under atmospheric pressure and the hydroxyplatinic acid is perfectly dissolved by stirring. After cooling, nitric acid is properly added to attain a prescribed concn. and the objective platinum nitrate soln. causing no change in the state even after storage for >=1 month is obtd.
    • 7. 发明专利
    • PRODUCTION OF TETRAAMMINE PLATINUM (II) DICHLORIDE CRYSTAL
    • JPH10218625A
    • 1998-08-18
    • JP2259197
    • 1997-02-05
    • TANAKA PRECIOUS METAL IND
    • SHIBAZAKI TAKUO
    • C01G55/00B01J31/22
    • PROBLEM TO BE SOLVED: To obtain an impurity-free tetraammine platinum (II) dichloride crystal by adding aqueous ammonia to an aqueous solution of dichlorodiamine platinum (II), concentrating the solution, as its ammonia alkalinity is maintained, filtering and drying the precipitate. SOLUTION: Chloroplatinic acid or its salt is allowed to react with aqueous ammonia at 60-80 deg.C. Hydrochloric acid is added to the resultant tetraammine Pt(II) dichloride and they are heated under reflux to precipitate trans- dichlorodiammine Pt(II). This precipitate is filtered and washed with water to collect dichlorodiammine Pt(II) ammonia. Then, aqueous ammonia is added to this dichlorodiammine Pt(II) in an amount of about 5-fold equivalents needed for the reaction, the mixture is placed in a pressure tightly sealable reaction vessel, heated at 60-80 deg.C, then cooled down, the precipitate is filtered and dried. Thus, the objective tetraammine Pt(II) dichloride can be produced in the form of crystals, which has excellent operability and stability and is useful as a catalyst carrier.
    • 9. 发明专利
    • METHOD FOR RECOVERING AND REFINING RHODIUM
    • JPH03285030A
    • 1991-12-16
    • JP8357190
    • 1990-03-30
    • TANAKA PRECIOUS METAL IND
    • ICHIISHI TOMOSHISHIBAZAKI TAKUO
    • C22B11/00
    • PURPOSE:To simply recover low concn. Rh at a high recovering rate and high purity by adding SnCl2 and CuCl2 to a rhodium-hydrochloric acid soln. having specified hydrochloric acid concn. and absorbing Rh by dialkyl sulfide- impregnated resin. CONSTITUTION:Hydrochloric acid is added to a rhodium-hydrochloric acid soln. including base metals and having low Rh concn. to regulate the hydrochloric acid concn. to 1 to 6 N. Next, SnCl2 and CuCl2 are added to this soln. The amounts of the SnCl2 and CuCl2 to be added are preferably regulated to 10 to 50 times respectively, by molar ratio, to Rh. After that, this soln. is brought into contact with porous resin impregnated with preferably >=30wt.% dialkyl sulfide to adsorb Rh. Next, this porous resin adsorbed with Rh is washed by dilute hydrochloric acid of 0.5 to 3 N. to remove Sn, Cu or the like and is thereafter baked at about 800 deg.C. The obtd. rhodium oxide is reduced by a hydrogen gas, is thereafter mixed with NaCl, in which a Cl2 gas is blown, and chlorination is executed at 800 to 950 deg.C for >= one hr. In this way, high purity Rh can be obtd. at approximately 100% recovering rate in the shape of soluble sodium salt of chlorhodic acid.