Method for producing EDTA ferric sodium salt by recovering Fe<II>EDTA wet-process complexed denitrated waste-liquid
A technology for denitrification and waste liquid, which is applied to the preparation of alkali metal nitrates, chemical instruments and methods, and organic compounds. It can solve the problems of high recycling costs, achieve low investment and operating costs, high economic value, and realize resource utilization. Effect
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Embodiment 1
[0023] Using Fe II EDTA and Na 2 SO 3 The absorption liquid is denitrified, and the waste liquid after denitrification is discharged into the oxidation tank, and hydrogen peroxide is used as the oxidant. At a reaction temperature of 15°C, the concentration of hydrogen peroxide is 0.1 M, the pH value is 4, and the oxidation time is 24 hours. The yield of FeNaEDTA is 60- 70%.
Embodiment 2
[0025] Using Fe II EDTA and Na 2 SO 3 The absorption liquid is denitrified, and the waste liquid after denitrification is discharged into the oxidation tank, and hydrogen peroxide is used as the oxidant. At a reaction temperature of 20 ° C, the concentration of hydrogen peroxide is 0.3 M, the pH value is 5, and the oxidation time is 36 hours. The yield of FeNaEDTA is 60- 78%.
Embodiment 3
[0027] Using Fe II EDTA and Na 2 SO 3 The absorption liquid is denitrified, and the waste liquid after denitrification is discharged into the oxidation tank, and hydrogen peroxide is used as the oxidant. At a reaction temperature of 25°C, the concentration of hydrogen peroxide is 0.5 M, the pH value is 3, and the oxidation time is 48 hours. The yield of FeNaEDTA is 60- 80%.
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