Method for treating degradation-resistant organic wastewater by using Fenton oxidation intensified supercritical water oxidation method
A technology of organic wastewater and Fenton oxidation, applied in the direction of oxidized water/sewage treatment, chemical instruments and methods, water/sludge/sewage treatment, etc., can solve problems such as unreachable effects, reduce reaction conditions, and improve degradation effects Effect
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Embodiment 1
[0027] The initial TOC concentration of the used phenol waste water of the present invention and p-nitrophenol waste water is 1000mg / L; FeSO 4 ·7H 2 O(AR,≥98%) formulated as Fe 2+ The aqueous solution with a concentration of 1.5mg / L is used as a catalyst; 30wt% hydrogen peroxide is used as an oxidant; the pressure is set to 23MPa, and 98% concentrated sulfuric acid solution is prepared into a 0.01mol / L solution to adjust the pH, and the pH is adjusted to 3.0; the temperature is set separately 380°C, 400°C, 420°C, 440°C, 460°C, 480°C; the injection flow rate is 2mL / min, and the corresponding residence time is 217.3s.
[0028] Phenol wastewater, p-nitrophenol wastewater, oxidant, and ferrous ion solution were respectively passed through a low-pressure gradient mixer in a volume ratio of 9:5:10, and then mixed by a high-pressure constant-flow pump into a stainless steel pipe (outer diameter 1 / 8 ", with an inner diameter of 1.5mm), the tubular reactor is placed in a box-type res...
Embodiment 2
[0034] The initial TOC concentration of 2-naphthol wastewater and p-aminonaphthalenesulfonic acid wastewater is 1000mg / L; FeSO 4 ·7H 2 O(AR,≥98%) formulated as Fe 2+ A solution with a concentration of 1.5mg / L is used as a catalyst; 30wt% hydrogen peroxide is used as an oxidant; the pressure is set to 23MPa, and 98% concentrated sulfuric acid solution is prepared into a 0.01mol / L solution to adjust the pH, and the pH is adjusted to 3.0; the temperature is set separately 380°C, 400°C, 420°C, 440°C, 460°C, 480°C; the injection flow rate is 2mL / min, and the corresponding residence time is 217.3s.
[0035] Naphthol wastewater, p-aminonaphthalenesulfonic acid wastewater, oxidant, and ferrous ion solution were respectively passed through a low-pressure gradient mixer at a volume ratio of 9:5:10, and then mixed by a high-pressure constant-flow pump into a stainless steel pipe (outer diameter 1 / 8", inner diameter 1.5mm), the tubular reactor is placed in a box-type resistance furnace...
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