Patent Number: 
Section: claims

1. A chemical decontamination method comprising a dissolution step in which a radioactive insoluble substance containing a metal oxide, the radioactive insoluble substance being adhered to a decontamination object including carbon steel, is dissolved in a decontamination solution and a metal-ion removal step in which the decontamination solution containing the metal ion, the decontamination solution being produced in the dissolution step, is brought into contact with a cation-exchange resin in order to remove the metal ion, the dissolution step including a reductive dissolution step conducted using a decontamination solution containing formic acid, ascorbic acid and/or erythorbic acid (hereinafter, referred to as “ascorbic acid, etc.”), and a corrosion inhibitor. 2. The chemical decontamination method according to claim 1, wherein the decontamination object includes carbon steel and stainless steel, and wherein the dissolution step includes an oxidative dissolution step conducted using a decontamination solution containing permanganic acid and/or a permanganic acid salt (hereinafter, referred to as “permanganic acid (salt)”) at a concentration of 100 to 2,000 mg/L, a reductive decomposition step in which a reducing agent is added to the decontamination solution treated in the oxidative dissolution step in order to perform reductive decomposition of the permanganic acid (salt), and the reductive dissolution step conducted subsequent to the reductive decomposition step. 3. The chemical decontamination method according to claim 2, wherein, in the reductive decomposition step, ascorbic acid, etc. is added to the decontamination solution in an amount 1.0 to 2.0 times the amount equivalent to the permanganic acid (salt) in order to perform the reductive decomposition of the permanganic acid (salt). 4. The chemical decontamination method according claim 1, wherein, in the reductive dissolution step, the metal oxide is dissolved in a decontamination solution containing formic acid at a concentration of 1,000 to 10,000 mg/L, ascorbic acid, etc. at a concentration of 400 to 4,000 mg/L, and a corrosion inhibitor at a concentration of 100 to 500 mg/L. 5. The chemical decontamination method according to claim 1, wherein the metal-ion removal step includes a first cation-exchange treatment step in which the decontamination solution containing the metal ion, the decontamination solution being produced in the reductive dissolution step, is passed through a cation-exchange resin column in order to produce first cation-exchange treatment water containing an Fe ion at a concentration of 300 mg/L or less. 6. The chemical decontamination method according to claim 5, wherein, subsequent to the first cation-exchange treatment step, a formic acid oxidative decomposition step in which a corrosion inhibitor is added to the first cation-exchange treatment water at a concentration of 200 to 300 mg/L and hydrogen peroxide is subsequently added to the first cation-exchange treatment water in an amount 1 to 3 times the amount equivalent to the formic acid in order to decompose the formic acid using the Fe ion as a catalyst is conducted. 7. The chemical decontamination method according to claim 6, wherein the metal-ion removal step includes a second cation-exchange treatment step in which water treated in the formic acid oxidative decomposition step is irradiated with ultraviolet radiation and subsequently passed through a cation-exchange resin column in order to remove the metal ion. 8. The chemical decontamination method according to claim 7, wherein an ascorbic acid, etc. oxidative decomposition step in which a corrosion inhibitor is added to water treated in the second cation-exchange treatment step at a concentration of 200 to 300 mg/L, hydrogen peroxide is subsequently added to the treated water, and the treated water is then irradiated with ultraviolet radiation in order to perform oxidative decomposition of the ascorbic acid, etc. is conducted. 9. The chemical decontamination method according to claim 8, wherein water treated in the ascorbic acid, etc. oxidative decomposition step is passed through a mixed-bed resin column in order to produce treated water having an electric conductivity of 2 μS/cm or less.