Method for recovering cobalt in cobalt chloride wastewater based on two-stage resin separation
A resin separation and recovery method technology, applied in chemical instruments and methods, water pollutants, water/sewage treatment, etc., can solve the problems of long dark spots on the surface of cobalt-based materials, adverse effects of deep purification of cobalt solution, and high operating costs , to extend the hydraulic retention time, improve the efficiency of wastewater treatment, and reduce operating costs.
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Embodiment 1
[0031] The cobalt chloride wastewater in this example is cobalt chloride production wastewater from a company in Taizhou. The wastewater TOC is about 202 mg / L, the Cd concentration is 1.9 mg / L, and the Co concentration is 1.6×10 5 mg / L, solution pH 4.5, the treatment steps for this waste water are:
[0032] (1) Filtration: waste water with 4m 3 The flow rate of / h flows through the bag filter to remove suspended solids in the wastewater.
[0033] (2) Primary resin adsorption: Send the filtered wastewater to the lower end of the adsorption device filled with macroporous non-polar special adsorption resin, and perform countercurrent adsorption to remove organic matter in the wastewater. The aspect ratio of macroporous non-polar special adsorption resin is 3:1, and 50BV wastewater is adsorbed at a flow rate of 3.5BV / h, and the resin effluent TOC is reduced to 26.79mg / L.
[0034] (3) Secondary resin adsorption: Send the effluent of the primary resin to the secondary adsorption d...
Embodiment 2
[0040] The cobalt chloride wastewater in this example is cobalt chloride production wastewater from a new energy material company in Tianjin. The wastewater TOC is about 147 mg / L, the Cd concentration is 2.316 mg / L, and the Co concentration is 1.95×10 5 mg / L, solution pH 3.9, the treatment steps for this waste water are:
[0041] (1) Filtration: waste water with 5 m 3 The flow rate of / h flows through the bag filter to remove suspended solids in the wastewater.
[0042] (2) Primary resin adsorption: Send the filtered wastewater to the lower end of the adsorption device filled with macroporous non-polar special adsorption resin, and perform countercurrent adsorption to remove organic matter in the wastewater. The macroporous non-polar special adsorption resin is loaded with a height-to-diameter ratio of 3:1, and absorbs 65 BV of wastewater at a flow rate of 4 BV / h, and the TOC of the resin effluent is reduced to 9.4 mg / L.
[0043] (3) Secondary resin adsorption: Send the efflue...
Embodiment 3
[0046] The waste water in this example is cobalt chloride waste water produced by an ultrafine powder material production company in Hubei. The waste water TOC is about 317 mg / L, the Cd concentration is 1.739 mg / L, and the Co concentration is 2.01×10 5 mg / L, solution pH 4.8, the treatment steps for this waste water are:
[0047] (1) Filtration: waste water with 5 m 3 The flow rate of / h flows through the bag filter to remove suspended solids in the wastewater.
[0048] (2) Primary resin adsorption: Send the filtered wastewater to the lower end of the adsorption device filled with macroporous non-polar special adsorption resin, and perform countercurrent adsorption to remove organic matter in the wastewater. The aspect ratio of macroporous non-polar special adsorption resin is 3.5:1, and 45 BV wastewater is adsorbed at a flow rate of 3 BV / h. The resin effluent TOC is reduced to 43.7 mg / L, and 80% of the primary resin effluent is refluxed to At the water inlet, repeat the firs...
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