Method for removing ions in nano-level zirconium dioxide hydrate particle-water system
A hydrate and nano-scale technology, applied in the field of membrane separation, can solve problems such as no specific reports on the operation method, and achieve the effects of reducing agglomeration, high membrane flux, and reducing membrane clogging
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Embodiment 1
[0024] Referring to Fig. 1, at room temperature, the polyethersulfone (PES) ultrafiltration flat membrane device (membrane module) with a molecular weight cut-off of 50K is adopted to treat nanometer ZrO 2 The hydrated feed solution (Cl-concentration is 0.55mol / L, solid content is 5g / L) is concentrated and desalted. Operate the high-pressure pump so that the pressure displayed by the pressure gauge is 0.4MPa, the amount of feed liquid added to the material tank is 3.0L, and the reflux ratio is 20. The experiment is carried out according to the above steps. When the feed liquid is concentrated to 1.5L, add 1.5L of distilled water for dilution and sleeve washing, and the water addition ratio is 0.5. When the feed liquid volume is concentrated to 1.5L again, add 1.5L distilled water again and carry out dilution cover washing, through multiple cover washing, the Cl of concentrated solution - The concentration is 1.17×10 -5 mol / L, the average membrane flux is maintained at 295L / m...
Embodiment 2
[0026] Using polyethersulfone (PES) ultrafiltration flat membrane equipment with a molecular weight cut-off of 30K, the 2 Hydrated material liquid (Cl - The concentration is 0.55mol / L, and the solid content is 15g / L) for concentration and desalination. The operating pressure is 0.21MPa, the feed liquid volume is 3.0L, and the reflux ratio is 25. The experiment is carried out according to the above steps. When the feed liquid is concentrated to 2.5L, distilled water is added for dilution and top washing, and the water addition ratio is 0.17. After several washes, the Cl of the concentrate - The concentration is 8.78×10 -5 mol / L, the average membrane flux is maintained at 50L / m 2 .h and above. During the experiment, samples were taken every 10 minutes for testing.
Embodiment 3
[0028] Using polyethersulfone (PES) ultrafiltration flat membrane equipment with a molecular weight cut-off of 100K, the 2 Hydrated material liquid (Cl - The concentration is 0.55mol / L, and the solid content is 5g / L) for concentration and desalination. The operating pressure is 0.35MPa, the feed liquid volume is 3.0L, and the reflux ratio is 20. The experiment is carried out according to the above steps. When the feed liquid is concentrated to 1.2L, add 1.0L distilled water for dilution and sleeve washing, and the water addition ratio is 0.55. After several washes, the Cl of the concentrate - The concentration is 7.74×10 -5 mol / L, the average membrane flux is maintained at 85L / m 2 .h and above. During the experiment, samples were taken every 15 minutes for testing.
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