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    • 6. 发明专利
    • THERMOCHEMICAL PREPARATION OF HYDROGEN FROM WATER
    • JPS62148301A
    • 1987-07-02
    • JP28722385
    • 1985-12-20
    • AGENCY IND SCIENCE TECHN
    • MIZUTA SUSUMUKUMAGAI TOSHIYA
    • C01F5/06C01B3/02C01B3/04C01B7/13
    • PURPOSE:To provide a process for prepg. hydrogen from water requiring low reaction temp. even for the maximum reaction temp., mitigating requirements for the material of the preparation apparatus remarkably, thus elevating the practicality of the process by utilizing a mechanism wherein the hydrogen is separated by the specified thermochemical decomposition process of water. CONSTITUTION:(A) Gaseous mixture consisting of NO and O2 is introduced into aq. slurry contg. MgO and I2 to react with and absorb NO alone, and precipitate of Mg(NO3)2 and aq. slurry of MgI2 are formed, and separated O2 is taken out of the reaction system. (B) The solid in the slurry is separated from liquid, and (C) MgI2 is separated and HI is generated by heating the obtd. aq. soln. obtd. MgO residue is recycled simultaneously to the stage (A). (D) Mg(MO3)2 in the solid phase obtd. in the stage (B) is decomposed thermally to generate NO and O2, and MgO residue is formed. These products are recycled to the stage (A), and HI produced in the stage (C) is decomposed to I2 and H2, and produced I2 is recycled to the stage (A), and H2 is taken out of the reaction system. Thus, H2 is prepd. All these reactions can be carried out at
    • 9. 发明专利
    • THERMOCHEMICAL PRODUCTION OF HYDROGEN FROM WATER
    • JPS6265901A
    • 1987-03-25
    • JP20131785
    • 1985-09-11
    • AGENCY IND SCIENCE TECHN
    • MIZUTA SUSUMUKUMAGAI TOSHIYA
    • C01B3/02C01B3/12C01B3/14
    • PURPOSE:To produce hydrogen at an excellent reaction rate, with high heat efficiency and in high yield by improving the process when gaseous hydrogen is thermochemically produced from water by an Mg-S-I cycle method. CONSTITUTION:A gaseous mixture of SO2 and O2 is blown into an aq. slurry at 0-120 deg.C wherein MgO and I2 are suspended in water to form a slurry consisting of an aq. soln. of MgSO4 and MgI2. The slurry is separated by filtration, centrifugation, etc., into an MgSO4 crystal and a concd. soln, of MgI2. The concd. soln. of MgI2 is heated, concentrated and evaporated to dryness. The residue is further heated at 400 deg.C to generate HI and the residue of MgO is returned to the first stage. The MgSO4 obtained by the preceding stage is brought into contact with an aq. soln. and the soln. is heated at 900-1,200 deg.C to generate SO2 and O2 and the residue of MgO is returned to the first stage. Then the HI is brought into contact with an aq. soln. and the soln. is thermochemically decomposed by electrical energy into a gaseous mixture of H2 and I2. The I2 is condensed with use of a separation membrane or by cooling and high-purity gaseous H2 is separated from the I2 and recovered in high yield.
    • 10. 发明专利
    • METHOD OF STORING HIGHLY EFFICIENT POWER
    • JPS6261277A
    • 1987-03-17
    • JP20131685
    • 1985-09-11
    • AGENCY IND SCIENCE TECHN
    • MIZUTA SUSUMUKONDO WAKICHIKUMAGAI TOSHIYA
    • H01M8/18H01M8/22
    • PURPOSE:To make it possible to efficiently perform the charging and discharging processes by using a water solution containing hydrogen chloride, ferrochloride and ferrichloride while regulating its hydrogen chloride concentration within a specific range. CONSTITUTION:A charging process in which ferrochloride in a water solution containing hydrogen chloride, ferrochloride and ferrichloride is partly oxidized into ferrichloride at an anode electrode to generate hydrogen at a cathode electrode and a discharging process in which generated hydrogen is oxidized at the anode electrode while reducing a water solution containing generated ferrichloride at the cathode electrode to generate ferrochloride and hydrogen chloride constitute the captioned method. Thereby, the respective water solutions containing chlorinated iron have hydrogen chloride concentration, desirably 2-7mol/kg-H2O and the total iron concentration of the primary iron and the secondary iron, desirably 1-4mol/kg-H2O, while a mol ratio of the primary iron to the secondary iron is desirably in the range of 1/3-3/1.