Method for performing ion exchange on molecular sieve containing exchangeable ions
A technology of ion exchange and ion exchange, applied in chemical instruments and methods, semi-permeable membrane separation, membrane technology, etc., can solve problems such as high cost, complicated operation, and high energy consumption of the process, so as to reduce usage and improve economic benefits , the effect of reducing pollution
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Embodiment 1
[0064] 100g of NH 4 NaY molecular sieve (Na 2 The O content is 4.3% by weight, the silicon-alumina ratio is 5, and the relative crystallinity is 90.3%) and 1000 g of water are stirred evenly, and the temperature is raised to 95°C. 20 g of an aqueous solution of 90% by weight of ammonium hexafluorosilicate was added, and the mixture was treated at 95° C. for 2 hours to obtain a molecular sieve slurry with a high silicon-to-aluminum ratio. The SiO of the molecular sieve with high silicon-aluminum ratio 2 and Al 2 O 3 The molar ratio was 12, and the relative crystallinity was 95%.
[0065] The above-mentioned high silicon-aluminum ratio molecular sieve slurry was filtered to obtain 300 g of solid phase (the weight ratio of molecular sieve to water was 1:2) and 800 g of liquid phase containing high silicon-aluminum ratio molecular sieve. Add 4 g of Na to the liquid phase 2 SO 4 , and fill the liquid phase into the acid chamber storage tank of the bipolar membrane electrodia...
Embodiment 2
[0067] Put 200g of NH 4 NaY molecular sieve (Na 2 O content is 3.5 wt%, silicon-aluminum ratio is 5, relative crystallinity is 90%) and 15 g of rare earth chloride, treated at 90 °C for 1 hour, and calcined at 550 °C for 2 hours to obtain a high silicon-aluminum ratio. Molecular Sieve. The SiO of the molecular sieve with high silicon-aluminum ratio 2 and Al 2 O 3 The molar ratio was 11, and the relative crystallinity was 56.0%.
[0068] Weigh 100g of the molecular sieve with the above-mentioned high silicon-aluminum ratio and stir well with 1000g of deionized water to obtain the slurry of the molecular sieve, filter, and obtain 400g of the solid phase containing the high-silicon-aluminum ratio molecular sieve (the weight ratio of molecular sieve and water is 1:3) and 700g of liquid phase. 3.8 g of Na were added to the liquid phase 2 SO 4 , and fill the liquid phase into the acid chamber storage tank of the bipolar membrane electrodialyzer, and at the same time add 1000...
Embodiment 3
[0070] 200g of NaX (Na 2 The O content is 11.6 wt%, the silicon-aluminum ratio is 1.26, and the relative crystallinity is 81.3%) and 15 g of rare earth chloride were treated at 90 °C for 1 hour, and calcined at 550 °C for 2 hours to obtain a high silicon-aluminum ratio molecular sieve . The Si / Al ratio of the high silicon-aluminum ratio molecular sieve is 10, and the relative crystallinity is 76.2%.
[0071] Weigh 100g of the molecular sieve with the high silicon-aluminum ratio and 1000g of deionized water and stir to obtain the slurry of the molecular sieve, filter, and obtain 300g of the solid phase of the molecular sieve containing the high silicon-to-aluminum ratio (the weight ratio of molecular sieve and water is 1:2) and 800g of liquid phase. Add 5 g of Na to the liquid phase 2 SO 4 , and fill the liquid phase into the acid chamber storage tank of the bipolar membrane electrodialyzer, and at the same time add 1000 g of deionized water to the alkali chamber storage ta...
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