Electrochemical method for separation of zirconium and hafnium

Patent metadata

Field	Value
Publication number	US-2024240343-A1
Application number	US-202218289708-A
Country	US
Kind code	A1
Filing date	Apr 21, 2022
Priority date	May 8, 2021
Publication date	Jul 18, 2024
Grant date	—

Abstract

The present disclosure provides an electrochemical method for the separation of zirconium and hafnium, using an electrolytic cell equipped with an anode chamber and a cathode chamber, wherein the anode chamber and the cathode chamber are separated by a liquid alloy. In particular, the liquid alloy comprises a crude zirconium and a matrix metal with the metal activity lower than zirconium. After the electrolysis reaction is started, since the metal activity series in the liquid alloy is: hafnium>zirconium>>matrix metal, the hafnium in the liquid alloy is oxidized prior to the zirconium, the hafnium in ionic form migrates into the cathode electrolyte in the cathode chamber, leading to a continuous decrease of hafnium content in the liquid alloy, whereas the zirconium remains in the liquid alloy. Accordingly, deep separation of zirconium from hafnium is achieved, and therefore, nuclear-grade zirconium products can be prepared.

First claim

1 . An electrochemical method for the separation of zirconium and hafnium, the method comprises:
An electrolytic cell equipped with an anode chamber and a cathode chamber is used, wherein there is an anode electrolyte in the anode chamber and there is a cathode electrolyte in the cathode chamber, an anode is inserted into the anode electrolyte, a cathode is inserted into the cathode electrolyte: the anode chamber and the cathode chamber are separated by a liquid alloy, and both the anode and the cathode are not in contact with the liquid alloy; the liquid alloy comprises solute metal and matrix metal, the solute metal is crude zirconium, the crude zirconium contains hafnium element: the metal activity of the matrix metal is lower than the metal activity of zirconium; applying electrical current for electrolysis, the hafnium content in the liquid alloy continuously decreases, whereas the zirconium remains in the liquid alloy, therefore the separation of zirconium from hafnium is achieved.

2 . An electrochemical method for the separation of zirconium and hafnium according to claim 1 , the material of the anode is selected from one of graphite, copper, and zirconium.

3 . An electrochemical method for the separation of zirconium and hafnium according to claim 2 , when the material of the anode is graphite, a zirconium-containing material is added into the anode chamber, the zirconium-containing material is a halide of zirconium or an oxide of zirconium.

4 . An electrochemical method for the separation of zirconium and hafnium according to claim 3 , the zirconium-containing material is selected from one or several of Na 2 ZrCl 6 , K 2 ZrCl 6 , Na 2 ZrF 6 , K 2 ZrF 6 , ZrO 2 , ZrCl 2 , ZrCl 3 , ZrCl 4 .

5 . An electrochemical method for the separation of zirconium and hafnium according to claim 2 , when the material of the anode is copper or crude zirconium, there is no need to add a zirconium-containing material into the anode chamber.

6 . An electrochemical method for the separation of zirconium and hafnium according to claim 1 , the matrix metal is selected from one or several of copper, lead, zinc, tin, bismuth, and the melting point of the liquid alloy formed by the solute metal and the matrix metal is lower than 1100° C.

7 . An electrochemical method for the separation of zirconium and hafnium according to claim 2 , when the material of the anode is copper, the anode electrolyte is selected from one or several of CuCl 2 and LiF, NaF, KF, LiCl, NaCl, KCl, CaCl 2 ; when the material of the anode is graphite or zirconium, the anode electrolyte is selected from one or several of ZrCl 4 , ZrCl 2 , ZrCl 3 , Na 2 ZrF 6 , K 2 ZrF 6 or one or several of LiF, NaF, KF, LiCl, NaCl, KCl, CaCl 2 ;
the cathode electrolyte is selected from one or several of LiF, NaF, KF, LiCl, NaCl, KCl, CuCl 2 , there are a zirconium halide and/or a hafnium halide dissolved in the cathode electrolyte, and the zirconium halide and/or the hafnium halide are selected from one or several of ZrCl 4 , ZrCl 2 , ZrCl 3 , HfCl 4 , HfCl 2 , HfCl 3 , Na 2 ZrCl 6 , K 2 ZrCl 6 , Na 2 HfCl 6 , K 2 HfCl 6 , Na 2 ZrF 6 , K 2 ZrF 6 , Na 2 HfF 6 , K 2 HfF 6 .

8 . An electrochemical method for the separation of zirconium and hafnium according to claim 7 , the zirconium halide and/or the hafnium halide are dissolved in the cathode electrolyte.

9 . An electrochemical method for the separation of zirconium and hafnium according to claim 1 , the material of the cathode is stainless steel, zirconium, titanium or tungsten.

10 . An electrochemical method for the separation of zirconium and hafnium according to claim 1 , the electrolysis reaction is carried out under the protection of the argon gas, the electrolysis reaction temperature is 400-1100° C., the anode current density is controlled at 0.002-0.5 A·cm −2 .

Assignees

• Univ Zhengzhou

Inventors

• Zhao Zhongwei

Classifications

• C25C3/34

  of metals not provided for in groups C25C3/02 - C25C3/32 · CPC title

• C25C3/00

  Electrolytic production, recovery or refining of metals by electrolysis of melts (C25C5/00 takes precedence) · CPC title

• C25C3/26 Primary

  of titanium, zirconium, hafnium, tantalum or vanadium · CPC title

• C25C1/22

  of metals not provided for in groups C25C1/02 - C25C1/20 · CPC title

• C25C7/06

  Operating or servicing · CPC title