Method of preparing ammonium metatungstate solution based on bipolar membrane electrodialysis
A technology of bipolar membrane electrodialysis and ammonium metatungstate, applied in the direction of electrodialysis, preparation of tungsten compounds, chemical instruments and methods, etc., can solve problems such as low direct yield and insufficient product purity, and achieve low and high tungsten High yield, guaranteed high efficiency, and low equipment investment
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Embodiment 1
[0063] Using a basic structure such as figure 2 In the electrodialysis system shown, the membrane stack of the electrodialyzer includes 20 two-chamber units, and the effective area of a single membrane is 0.02m 2 , the bipolar membrane is NEOSEPTA BP-1, the cation exchange membrane is NEOSEPTA CMB, the anode and cathode are both titanium-plated nickel-plated electrodes, and the membrane stack structure is as follows figure 1 shown. Ammonium tungstate solution containing WO 3 250g / L. The solution initially filled into the circulation tank of the acidification chamber is ammonium metatungstate solution, where WO 3 300.0g / L, pH value around 3.0, volume 6.0L. The solution initially filled into the circulation tank of the alkali chamber is NH 4 HCO 3 solution with a concentration of 1.0 mol / L and a volume of 5 L. The solution continuously added to the alkali chamber is 1.0mol / L NH 4 HCO 3 solution. The solution initially filled into the circulation tank of the electr...
Embodiment 2
[0065] Using a basic structure such as figure 2 The electrodialysis system shown, wherein the membrane stack of the electrodialyzer is the same as that of embodiment 1. Ammonium tungstate solution containing WO 3 151.2g / L,. The solution initially filled into the circulation tank of the acidification chamber is obtained by diluting the ammonium metatungstate solution prepared in Example 1 with deionized water, wherein WO 3 150.0g / L, pH value around 2.0, volume 6.0L.
[0066] The solution initially filled into the circulation tank of the alkali chamber is (NH 4 ) 2 CO 3 solution with a concentration of 0.1mol / L and a volume of 5L. The solution that is going to be continuously added to the alkali chamber is also a concentration of 0.1mol / L (NH 4 ) 2 CO 3 solution. The solution initially filled into the circulation tank of the electrode chamber is NH 4 OH solution with a concentration of 1.0mol / L and a volume of 5L. After the power-on operation starts, the ammonium ...
Embodiment 3
[0068] The equipment used is the same as that of Example 1, except that the cathode and anode are platinum-plated titanium plate electrodes. Ammonium tungstate solution containing WO 3 100.0g / L. The solution initially filled into the circulation tank of the acidification chamber is obtained by diluting the ammonium metatungstate solution prepared in Example 2 with deionized water, wherein WO 3 50.0g / L, pH value around 4.0, volume 6.0L. The solution initially filled into the circulation tank of the alkali chamber is NH 4 NO 3 solution with a concentration of 0.5mol / L and a volume of 5L. The solution to be continuously added to the alkali chamber is NH with a concentration of 0.5mol / L 4 NO 3 solution. The solution initially filled into the circulation tank of the electrode chamber is NH 4 NO 3 solution with a concentration of 1.0 mol / L and a volume of 5 L. After the electrodialysis operation starts, the ammonium tungstate solution is continuously added to the inlet p...
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