Restoration method for removing iron pollution of anion exchange resin and restoration drug formula
An exchange resin and anion technology, applied in ion exchange, ion exchange regeneration, chemical instruments and methods, etc., can solve the problems of corrosion of anion exchange resin tanks and poor recovery effect, and achieve the effect of improving iron removal efficiency.
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specific Embodiment approach 1
[0011] Specific embodiment one: a kind of recovery method that removes anion exchange resin iron pollution in this embodiment is carried out according to the following steps:
[0012] 1. Transformation of anion exchange resin: Circular soaking of anion exchange resin with salt water with a concentration of 8% to 10% by weight at a temperature of 18 to 22°C and a circulation velocity of 2 to 3m / h, adopting the method of top in and bottom out Circulation, after 6-10 hours of circulation soaking, the transformation is completed. 2. Flushing: After the transformation is completed, the waste liquid is drained, and the anion exchange resin is reversely flushed with desalted water. The flushing time is 1.5-2.5 hours, and the flushing flow rate is 18-22m / h. 3. Remove the iron contamination of the anion exchange resin and resuscitate it: set up a medicine box and a circulating pump, inject the resuscitating agent into the anion exchange resin tank for circular elution. The total volum...
specific Embodiment approach 2
[0017] Specific embodiment 2: The difference between this embodiment and specific embodiment 1 is that in step 1, the anion exchange resin is transformed into an anion exchange resin with a concentration of 8.5% to 9.5% by weight. ℃, the circulation flow rate is 2.2-2.8m / h, and the circulation is adopted in the way of top-in and bottom-out, and the cycle soaking time is 7-9 hours. Other steps and parameters are the same as in the first embodiment.
specific Embodiment approach 3
[0018] Specific embodiment three: the difference between this embodiment and specific embodiment one is that in step one, the anion exchange resin is transformed into an anion exchange resin with a weight percent concentration of 9% saline to circulate and soak the anion exchange resin at a temperature of 20°C and a circulation flow rate of 2.5m / h, using the top-in and bottom-out circulation, and the cycle soaking time is 8 hours. Other steps and parameters are the same as in the first embodiment.
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