Method for removing mercury in exhaust gas

1. A method for removing mercury in exhaust gas, in which mercury is removed from exhaust gas of a boiler, characterized in that

said mercury removing method comprises an NH 3 decomposition process for decomposing excess NH 3 flowing down from a denitrification process and a mercury oxidation process for oxidizing mercury into mercury chloride on the downstream side of said NH 3 decomposition process, which are provided between said denitrification process and a wet desulfurization process, and mercury having been oxidized into mercury chloride is removed in said wet desulfurization process, said NH 3 decomposition process is separate from said denitrification process.

2. The method for removing mercury in exhaust gas according to claim 1 , characterized in that

in the mercury removing method comprising a heating process and a heat recovery process, which are provided between said denitrification process and wet desulfurization process,

said NH 3 decomposition process is carried out in a temperature zone of 300 to 450° C. on the downstream side of said denitrification process, and

said mercury oxidation process is carried out at least in one location of a temperature zone of 300 to 450°C. on the downstream side of said NH 3 decomposition process, a temperature zone of 120 to 200° C. on the downstream side of said heating process, or a temperature zone of 60 to 120° C. on the downstream side of said heat recovery process.

3. The method for removing mercury in exhaust gas according to claim 1 , characterized in that when said mercury oxidation process is carried out on the downstream side of said heating process, the temperature is controlled to a predetermined temperature in the range of 60 to 200° C.

4. The method for removing mercury in exhaust gas according to claim 1 or 2 , characterized in that the temperature in said mercury oxidation process is controlled by measuring the concentration of metallic mercury or mercury chloride in an oxidation catalyst outlet gas in said mercury oxidation process.

5. The method for removing mercury in exhaust gas according to claim 1 or 2 , characterized in that in said NH 3 decomposition process, NH 3 is treated so that the concentration of NH 3 at the outlet is 1 ppm or lower, and then mercury is oxidized in said mercury oxidation process.

6. The method for removing mercury in exhaust gas according to claims 1 or 2 , further comprising a NH 3 decomposition catalyst, said NH 3 decomposition catalyst comprises a carrier and an active component, said carrier is selected from the group consisting of TiO 2 , SiO 2 , ZrO 2 , Al 2 O 3 , and zeolite, and said active component is selected from the group consisting of Pt, Ru, Rh, Pd, Ir, V, W, Mo, Ni, Co, Fe, Cr, Cu, and Mn.

7. The method for removing mercury in exhaust gas according to claims 1 or 2 , further comprising a mercury oxidation catalyst, said mercury oxidation catalyst comprising a carrier and an active component, said carrier is selected from the group consisting of TiO 2 , SiO 2 , ZrO 2 , Al 2 O 3 , and zeolite, and said active component is selected from the group consisting of Pt, Ru, Rh, Pd, Ir, V, W, Mo, Ni, Co, Fe, Cr, Cu, and Mn.

8. A method for removing mercury in exhaust gas, in which mercury is removed from exhaust gas of a boiler, characterized in that

said mercury removing method comprises a NH 3 decomposition process for decomposing excess NH 3 flowing down from a denitrification process and a mercury oxidation process for oxidizing mercury into mercury chloride on the downstream side of said NH 3 decomposition process, which are provided between said denitrification process and a wet desulfurization process, and mercury having been oxidized into mercury chloride is removed in said wet desulfurization process, said NH 3 decomposition process is separate from said denitrification process, and

wherein said NH 3 decomposition occurs over a catalyst comprising a carrier and an active component, said carrier is selected from the group consisting of TiO 2 , SiO 2 , ZrO 2 , Al 2 O 3 , and zeolite, and said active component is selected from the group consisting of Pt, Ru, Rh, Pd, Ir, V, W, Mo, Ni, Co, Fe, Cr, Cu, and Mn.

9. The method for removing mercury in exhaust gas according to claim 8 , further comprising a mercury oxidation catalyst, said mercury oxidation catalyst comprising a carrier and an active component, said carrier is selected from the group consisting of TiO2, SiO2, ZrO2, Al2O3, and zeolite, and said active component is selected from the group consisting of Pt, Ru, Rh, Pd, Ir, V, W, Mo, Ni, Co, Fe, Cr, Cu, and Mn.

10. A method for removing mercury in exhaust gas, in which mercury is removed from exhaust gas of a boiler, characterized in that

said mercury removing method comprises an NH 3 decomposition process for decomposing excess NH 3 flowing down from a denitrification process and a mercury oxidation process for oxidizing mercury into mercury chloride on the downstream side of said NH 3 decomposition process, which are provided between said denitrification process and a wet desulfurization process, and mercury having been oxidized into mercury chloride is removed in said wet desulfurization process, said NH 3 decomposition process is separate from said denitrification process,

wherein said mercury oxidation occurs over a catalyst comprising a carrier and an active component, said carrier is selected from the group consisting of TiO 2 , SiO 2 , ZrO 2 , Al 2 O 3 , and zeolite, and said active component is selected from the group consisting of Pt, Ru, Rh, Pd, Ir, V, W, Mo, Ni, Co, Fe, Cr, Cu, and Mn.

11. The method for removing mercury in exhaust gas according to claim 10 , further comprising a NH 3 decomposition catalyst, said NH 3 decomposition catalyst comprises a carrier and an active component, said carrier is selected from the group consisting of TiO 2 , SiO 2 , ZrO 2 , Al 2 O 3 , and zeolite, and said active component is selected from the group consisting of Pt, Ru, Rh, Pd, Ir, V, W, Mo, Ni, Co, Fe, Cr, Cu, and Mn.