Recycling agent for hydrogen peroxide solution
A technology of working fluid and regeneration agent, applied in the direction of peroxide/peroxy hydrate/peroxyacid/superoxide/ozonide, inorganic chemistry, non-metallic elements, etc., which can solve the lack of comprehensive understanding of degraded molecules Mathematical model, active alumina regenerant dust is easy to fall off, increase the burden of post-treatment alkali separation, etc., to achieve the effect of reducing anthraquinone consumption, good hydrogenation environment, and light post-treatment burden
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Embodiment 1
[0026] A regeneration agent with a CaO content of 1% and a silicon dioxide content of 99% is used.
[0027] The total anthraquinone in the working solution before entering the clay bed is 132g / L, the total degradation products in the working solution are 46g / L, and the surface tension is 20 millinewtons / M.
[0028] Regeneration conditions: working fluid flow rate is 70M 3 / H, the clay bed is filled with 10T of regeneration agent.
[0029] The total anthraquinone was 135g / L, the total degraded product was 43g / L, and the surface tension of the working fluid was 22 millinewtons / M after regeneration with the above-mentioned working fluid regenerant.
Embodiment 2
[0031] A regeneration agent with a CaO content of 30% and a silicon dioxide content of 70% is used.
[0032] The total anthraquinone of the working solution before entering the clay bed is 132g / L, the total degradation product is 46g / L, and the surface tension is 20 millinewtons / M.
[0033] Regeneration conditions: working fluid flow rate is 70M 3 / H, the clay bed is filled with 10T of regeneration agent.
[0034] The total anthraquinone was 140g / L, the total degradation product was 33g / L, and the surface tension was 24 millinewtons / M after being regenerated with the above-mentioned working solution regenerator.
Embodiment 3
[0036] A regeneration agent with a CaO content of 50% and a silica content of 50% was used.
[0037] The total anthraquinone of the working solution before entering the clay bed is 132g / L, the total degradation product is 46g / L, and the surface tension is 20 millinewtons / M.
[0038] Regeneration conditions: working fluid flow rate is 70M 3 / H, the clay bed is filled with 10T of regeneration agent.
[0039] The total anthraquinone at the outlet of the clay bed is 143g / L and the total degradation products are 23g / L after regeneration with the above-mentioned working fluid regenerant. The surface tension is 24 millinewtons / M.
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