Pyromellitic acid dianhydride production wastewater treatment by two-stage adsorption method and resource recovery method
A technology of pyromellitic acid and production wastewater, which is applied in the field of powder coating additives, can solve the problems of insufficient thoroughness and effectiveness in the adsorption, separation and recycling of pyromellitic acid, and achieves improvement of treatment and recovery efficiency, and saving of drug consumption and energy. consumption effect
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Embodiment 1
[0015] Put 20ml of composite functional resin (NDA-910) into two jacketed glass adsorption columns (Φ32×360mm). At room temperature (20°C), the pyromellitic acid production wastewater first passes through the first-stage composite functional resin bed at a flow rate of 2BV / h. The wastewater treatment capacity is 2BV / batch. Through the second-stage composite functional resin bed, the wastewater treatment capacity is 8BV / batch. The COD of the original wastewater is 28800mg / l, and the content of pyromellitic acid is about 18250mg / l. After continuous adsorption by two-stage resin, the COD is about 11200mg / L, and the content of pyromellitic acid is about 7mg / L.
[0016] Use 1BV 8% NaOH aqueous solution + 4BV water to desorb through the first-stage composite functional resin bed at 50°C at 1BV / h, use 2BV 3% NaOH + 2BV aqueous solution at 50°C at a flow rate of 4BV / h Desorption is carried out through the second-stage composite functional resin bed, and the desorption rate of pyromel...
Embodiment 2
[0018] Replace the composite functional resin NDA-910 used in Example 1 with NDA-900, and pass the pyromellitic acid production wastewater at a flow rate of 4BV / h through the first-stage composite functional resin bed at a temperature of 35°C, and the wastewater treatment capacity is 2BV / batch, the first-stage adsorption water is passed through the second-stage composite functional resin bed at a flow rate of 8BV / h, and the wastewater treatment capacity is 8BV / batch. Use 2BV 6% NaOH aqueous solution + 4BV water to desorb through the first-stage composite functional resin bed at a flow rate of 3BV / h at 40°C; The flow is desorbed through the second-stage composite functional resin bed.
[0019] Under the above operating conditions, the adsorption effect of the treated wastewater is slightly improved, the COD is about 11300mg / L, and the content of pyromellitic acid is lower than 5mg / L. The desorption rate of pyromellitic acid on the two-stage resin was >99%.
Embodiment 3
[0021] Replace the two glass adsorption columns in Example 1 with two polypropylene adsorption columns (Φ160 × 1000mm), and fill each column with 10 kilograms (about 13 L) of composite functional resin (NDA-910), according to 700 times the amount of the embodiment The wastewater treatment capacity in 1 is operated, and the adsorption temperature of the two-stage resin is controlled to be 10° C., and the effect of adsorption treatment and resource recovery consistent with that of Example 1 can be obtained.
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