Processing method for resource recovery of acidic dye waste water
A technology for recovery and treatment of acid dyes, applied in chemical instruments and methods, multi-stage water/sewage treatment, adsorption water/sewage treatment, etc., can solve the problem of large area, difficult to purify thoroughly, chroma and COD concentration are difficult to reach the standard And other problems, to achieve high oxidation efficiency, improve recycling rate, and broad prospects
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Embodiment 1
[0021] At 25°C, filter 1000 mL of Disperse Orange 288# dye wastewater with a pH value less than 2 to remove suspended impurities. The waste water after filtering is added in the reactor, stir evenly, keep the constant speed of 20mL / hr and evenly add the NaClO solution 10mL (NaClO mass percentage concentration is 0.1% in waste water) and nano titanium dioxide catalyst 10g ( The mass percent concentration of nano-titanium dioxide in the waste water is 1%), and the rapid stirring is continued for 0.5 hr and then stopped, and a large amount of dark green oily matter appears in the solution. After standing still for 24 hours, the oily matter settled in the lower layer, and the supernatant was yellow. Get supernatant and cross the adsorption column that 50mL columnar activated carbon forms with the speed of 150mL / hr, collect effluent and be used for the production process of dispersing orange 288# as 100% reaction solvent, the yield of gained product is 95.13%, purity 91.35%, It ha...
Embodiment 2
[0023] The difference from Example 1 is: at 25°C, 25mL of oxidizing agent NaClO with a mass percentage concentration of 10% is evenly added dropwise (the mass percentage concentration of NaClO in wastewater is 0.25%). Matter increased compared with Example 1, and the yellow color of the supernatant was lighter than that of Example 1. After standing for 24 hours, the supernatant was passed through an adsorption column composed of 50 mL columnar activated carbon at a rate of 150 mL / hr, and the effluent was collected. The total organic carbon removal rate of the collected liquid can reach 70%, and the decolorization rate of the water sample is 55%. The collected effluent was used as 100% reaction solvent in the production process of Disperse Orange 288#. The yield of the product was 92.69%, and the purity was 90.53%, which completely reached the production standard of Disperse Orange 288#.
Embodiment 3
[0025] The difference from Example 1 is: 3mL of oxidizing agent NaClO (the mass percent concentration of NaClO in waste water is 0.03%) is uniformly added dropwise at 25° C., and the stirring is continued for 0.5 hr after the addition is completed. After standing, it is found that There is dark green oil in the upper layer of the solution, and the supernatant is slightly lighter than the wine red mother liquor. After standing for 24 hours, the supernatant was passed through an adsorption column composed of 50 mL columnar activated carbon at a rate of 150 mL / hr, and the effluent was collected. The total organic carbon removal rate of the collected liquid is about 30%, and the decolorization rate of the water sample is 25%. The collected effluent was used as 100% reaction solvent in the production process of Disperse Orange 288#. The yield of the product was 87.47%, and the purity was 80.05%, basically reaching the production standard of Disperse Orange 288#.
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