Method for synchronously removing and stepwise recovering sulfoacid dye and heavy metal ion through resin
A technology of heavy metal ions and resins, applied in chemical instruments and methods, ion exchange water/sewage treatment, water pollutants, etc., can solve the problems of inability to recycle valuable resources, high cost, complicated procedures, etc., and achieve no secondary pollution Less pollution, stable performance, and low material cost
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Embodiment 1
[0028] A method utilizing resin to simultaneously remove and recover sulfonic acid dyes and heavy metal ions step by step, the steps are:
[0029] (1) Simultaneous adsorption: put 10 mL of adsorption resin (NDA-150) into a jacketed glass adsorption column (Φ32×360 mm), keep the column temperature at 30°C, add sulfonic acid dye (acid black 1, CAS : 1064-48-8) and copper salt (the initial concentration of the dye is 1000 mg / L, the initial concentration of copper ions is 30 mg / L) to adjust the pH to 5, and the flow rate is 5 BV / h. adsorption column. The processing capacity is 50 BV / batch. The average concentration of dye in the adsorbed water was 190 mg / L, and the average concentration of copper ions was 9.5 mg / L.
[0030] (2) Recovery of heavy metals: keep the column temperature at 30°C, use 15 BV of hydrochloric acid solution (concentration of 4% by mass percentage, the concentration of hydrochloric acid, sulfuric acid and sodium hydroxide in the following examples refers to ...
Embodiment 2
[0033] Same as Example 1, the difference is that NDA-99 is used to replace the adsorption resin NDA-150 in Example 1, and in step (2), 18 BV15% hydrochloric acid solution is used to carry out the first adsorption to the adsorbed resin at 6 BV / h. The column temperature in step (3) was 30°C. Under the same adsorption and desorption operating conditions, the average concentration of dye in the adsorbed water was 220 mg / L, and the average concentration of copper ions was 8.2 mg / L. In the first round of desorption, the copper ion desorption rate reached 100%, and the dye was not detected; in the second round of desorption, the dye desorption rate reached 98%.
Embodiment 3
[0035] Same as Example 1, the difference is that the adsorption resin NDA-150 in Example 1 is replaced by XAD-4 produced by U.S. Rohm & Haas Company. Under the same adsorption and desorption operating conditions, the average concentration of the adsorbed water dye is 310 mg / L, the average concentration of copper ions is about 18 mg / L. In the first round of desorption, the copper ion desorption rate reached 100%, and the dye was not detected; in the second round of desorption, the dye desorption rate reached 100%.
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