Synergistic extraction agent and method for separating zirconium from hafnium
An extraction agent, the technology of zirconium and hafnium, applied in the field of chemical substances, can solve the problems of large dosage, high cost, and difficult control of the operation process, and achieve the effect of high hafnium extraction rate
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Embodiment 1
[0131] This embodiment provides a synergistic extractant for preferentially extracting hafnium and an extraction and separation method for zirconium and hafnium.
[0132] The co-extractant is composed of 12vol% secondary carboamine N1923, 12vol% tributyl phosphate and 76vol% n-hexane diluent.
[0133] Zirconium hafnium extraction separation method, the specific steps are as follows:
[0134] (1) The above-mentioned extractant was mixed with an equal volume of a presaturated solution containing 2.5 mol / L ammonium thiocyanate and 3.0 mol / L hydrochloric acid and stirred for 15 minutes, and the presaturated extractant was obtained after phase separation.
[0135] (2) preparation zirconium ion concentration is 1.2mol / L, hafnium ion concentration is the zirconium hafnium aqueous phase material liquid of 0.020mol / L, and the ammonium thiocyanate concentration is 3.0mol / L in the zirconium hafnium aqueous phase material liquid, and hydrochloric acid concentration is 3.0mol / L, ammonium ...
Embodiment 2
[0140] A method similar to that of Example 1 was used to prepare the extractant and the zirconium and hafnium aqueous phase feed solution.
[0141] Containing 15vol% 1,8-octanediamine, 15vol% dimethylheptyl methylphosphonate and 70vol% diisobutyl ketone diluent in the extractant, the presaturated solution contains 2.5mol / L sodium thiocyanate and 3.0 mol / L hydrochloric acid, the zirconium and hafnium aqueous phase feed solution contains 1.1mol / L zirconium ions, 0.014mol / L hafnium ions, 2.8mol / L sodium thiocyanate, 1.4mol / L sulfuric acid, and 0.8mol / L ammonium chloride.
[0142] The specific operation method is the same as that of Example 1, and the extraction rate of hafnium and zirconium by the extractant is calculated to be 77.9%, and the extraction rate of zirconium is 19.0%, and the separation coefficient of hafnium and zirconium is 15.1.
Embodiment 3
[0144] A method similar to that of Example 1 was used to prepare the extractant and the zirconium and hafnium aqueous phase feed solution.
[0145] The extractant contains 15vol% diisooctylamine, 15vol% trioctylphosphine oxide and 70vol% sulfonated kerosene diluent, the presaturated solution contains 2.5mol / L ammonium thiocyanate and 4.0mol / L hydrochloric acid, zirconium hafnium The aqueous phase feed solution contains 1.0mol / L zirconium ion, 0.018mol / L hafnium ion, 3.0mol / L ammonium thiocyanate, 3.0mol / L hydrochloric acid, 0.4mol / L sulfuric acid, and 0.8mol / L ammonium chloride.
[0146] The specific operation method is the same as that in Example 1, and the extraction rate of hafnium and zirconium by the extractant is calculated to be 88.4%, and the extraction rate of zirconium is 41.1%, and the separation coefficient of hafnium and zirconium is 10.9.
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