A method for purifying and removing rhenium from ammonium paratungstate
A technology of ammonium paratungstate and ammonium tungstate, applied in the field of purification and removal of rhenium, can solve the problems of inability to separate and remove, and achieve good adsorption effect.
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Embodiment 1
[0027] The method for purifying and removing rhenium from ammonium paratungstate whose rhenium content is 18ppm is:
[0028] Step 1. Dissolution: Dissolve 57g of sodium hydroxide (analytical pure) in 4.425L of water to obtain a sodium hydroxide solution, then dissolve 100g of ammonium paratungstate with a rhenium content of 18ppm in the sodium hydroxide solution, and react with the sodium hydroxide , finally obtain the alkaline solution of sodium tungstate; the mass concentration of NaOH in the alkaline solution of sodium tungstate is 6g / L, WO 3 The mass concentration is 20g / L;
[0029] Step 2, adsorption: pass the alkaline solution of sodium tungstate described in step 1 through the - The ion exchange column of type 201×7 resin performs dynamic ion exchange, when the effluent of the ion exchange column contains WO 3 The mass concentration and WO in the influent 3 At the same mass concentration, Cl - Type 201 × 7 resin adsorption saturation, then stop the ion exchange; the e...
Embodiment 2
[0033] The method for purifying and removing rhenium from ammonium paratungstate with a rhenium content of 15ppm is:
[0034] Step 1. Dissolving: Dissolve 44.6g of sodium hydroxide (analytically pure) in 3.54L of water to obtain a sodium hydroxide solution, then dissolve 100g of ammonium paratungstate with a rhenium content of 15ppm in the sodium hydroxide solution, and react with sodium hydroxide reaction, finally obtain the alkaline solution of sodium tungstate; the mass concentration of NaOH in the alkaline solution of sodium tungstate is 4g / L, WO 3 The mass concentration is 25g / L;
[0035] Step 2, adsorption: pass the alkaline solution of sodium tungstate described in step 1 through the - The ion exchange column of type 201×7 resin performs dynamic ion exchange, when the effluent of the ion exchange column contains WO 3 The mass concentration and WO in the influent 3 At the same mass concentration, Cl - Type 201 × 7 resin adsorption saturation, then stop the ion exchan...
Embodiment 3
[0039] The method for purifying and removing rhenium from ammonium paratungstate whose rhenium content is 22ppm is:
[0040] Step 1. Dissolution: Dissolve 58.8g of sodium hydroxide (analytically pure) in 3.54L of water to obtain a sodium hydroxide solution, then dissolve 100g of ammonium paratungstate with a rhenium content of 22ppm in the sodium hydroxide solution, and react with sodium hydroxide reaction, finally obtain the alkaline solution of sodium tungstate; the mass concentration of NaOH in the alkaline solution of sodium tungstate is 8g / L, WO 3 The mass concentration is 25g / L;
[0041] Step 2, adsorption: pass the alkaline solution of sodium tungstate described in step 1 through the - The ion exchange column of type 201×7 resin performs dynamic ion exchange, when the effluent of the ion exchange column contains WO 3 The mass concentration and WO in the influent 3 At the same mass concentration, Cl - Type 201 × 7 resin adsorption saturation, then stop the ion exchan...
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