Method and cell for the electrolytic production of a polyvalent metal

• US 5,015,342 A
• Filed: 04/19/1989
• Issued: 05/14/1991
• Est. Priority Date: 04/19/1988
• Status: Expired due to Fees

• Current Assignee: Ginatta Torno Titanium SPA An Italian Joint Stock Company
• Original Assignee: Ginatta Torno Titanium SPA
• Inventors: Orsello, Gianmichele, Berruti, Riccardo, Ginatta, Marco V.
• Primary Examiner(s): Valentine, Donald R.
• Application Number:
  US07/340,356
• Time in Patent Office: 755 Days
• Field of Search: 204/243 R-247, 204/260, 204/272, 204/64 T, 204/268, 204/280, 204/284, 204/283, 204/282, 204/287
• US Class Current: 205/397
• CPC Class Codes: C25C 3/26 of titanium, zirconium, hafnium, tantalum or vanadium
• CPC Class Codes: C25C 7/005 of cells for the electrolysis of melts C25C7/02 - C25C7/06 take precedence

Abstract

In a method for the production of a polyvalent metal, particularly titanium, by the cathodic dissolution of a halide of the metal in an electrolyte of alkali or alaline earth metal halides and the electro-extraction of the dissolved metal ions, the electro-extraction stage is carried out with the use of a composite electrode including an anode and a framework surrounding the anode and provided with metal partitions capable of anodic dissolution for confining within the framework a bath of alkali or alkaline earth metal halides which does not contain ions of the metal to be produced, and then applying a potential between the anode and the framework to cause the formation of an accumulation of alkali metal or alkaline earth metal by cathodic reduction, after which a potential is applied between the anode and the cathode to cause the deposition of the metal to be produced at the cathode and the simultaneous anodic dissolution of the partitions.

The stage of cathodic dissolution of the halide is carried out separately from the extraction stage with the use of composite electrode similar to that used in the extraction stage.

Claims

1. An electrolytic cell for use in combination with at least one cathode for the electrolytic production of a polyvalent metal in an electrolyte of fused halides including:

at least one anode provided with a terminal for its electrical connection,

a conductive framework, which is electrically insulated from the anode and provided with a terminal for its electrical connection, the framework surrounding the anode like a basket and having wall portions facing the anode which are permeable to the electrolyte and are adapted to support a cathodic metal deposit, and having support means (19,20) associated with the walls (4,5) of the framework (3) for supporting partition-like sealing elements (18) adjacent the electrolyte-permeable wall portions in order to confine within the framework, an electrolytic bath which does not contain the metal to be produced, and to prevent the infiltration of the electrolyte into the framework through the permeable wall portions, the partition-like sealing elements being constituted by a metal capable of anodic dissolution under the operating conditions of the electrode.

2. An electrolytic cell according to claim 1, wherein the electrolyte-permeable wall portions are constituted by grating members (13) formed by a plurality of tile-shaped elements (14) arranged in horizontal rows and defining passages (15) for the electrolyte.

3. An electrolytic cell according to claim 2, wherein each of the tile-shaped elements has a V-shaped cross section.

4. An electrolytic cell according to claim 1, wherein the anode is formed by an anodic cross member (1) and a plurality of anodic bars (2) extending substantially perpendicular to the cross member and wherein the cross member is supported at its ends by a first concave support terminal (12) which is electrically connected to the cross member and by a second concave support terminal (11) which is electrically connected to the framework.

5. An electrolytic cell according to claim 1, wherein the walls of the framework support a plurality of deflector elements (21) on their surfaces which face towards the interior of the framework.

6. A method for the production of a polyvalent metal selected from the group consisting of titanium, zirconium and hafnium, by means of:

the cathodic dissolution of a halide of the metal in an electrolyte of alkali metal of alkaline earth metal halides in the fused state and

the electro-extraction of the metal carried out in a cell including at least one anode and one cathode and a conductive framework which acts as an intermediate electrode and surrounds the anode so as to define an anodic compartment and a cathodic compartment, the framework having walls which are permeable to the electrolyte and are adapted to support a deposit of the metal to be produced in the form of a panel, so as to allow ion transfer between the anodic and cathodic compartments but to limit the transfer of ions of the metal to be produced from the cathodic compartment to the anodic compartment, comprising the steps of;

(a) supplying the extraction cell with the electrolyte containing ions of the metal to be produced in solution,

(b) confining a bath of alkali metal halides or alkaline earth metal halides, which is substantially without ions of the metal to be produced, within the framework by means of electrolyte-tight sealing of the permeable walls of the framework by metal partitions which are capable of anodic dissolution,

(c) feeding an electric current between the anode and the framework so as to cause the cathodic deposition of the alkali metal or alkaline earth metal on the permeable walls of the framework for a sufficient period of time to cause an accumulation of this metal,

(d) feeding an electric current between the anode and the cathode so as to cause the deposition of the metal to be produced at the cathode and the simultaneous anodic dissolution of the partitions so as to cause the diffusion of ions of the metal to be produced from the cathodic compartment towards the anodic compartment with the formation of the deposit of the metal to be produced on the permeable walls of the framework as a result of the reduction of the metal ions by the alkali metal or the alkaline earth metal,

(e) maintaining the electric current feed between the anode and the cathode to achieve the deposition of the metal at the cathode and simultaneously

(f) regulating the current between the anode and the cathode and the framework so as to keep the characteristics of permeability of the deposit substantially constant.

7. A method according to claim 6, wherein during step (f) the intensity of the current between the anode and the framework is regulated to a magnitude such as to cause the alkali metal or alkaline earth metal to be deposited by cathodic reduction at the interface of the framework which faces the anodic compartment at a deposition rate sufficient to reduce to the metallic state the ions of the metal to be produced which diffuse from the cathodic compartment, and such as to establish a state of substantial equilibrium between the depositing flow of ions of the metal to be produced and the flow of anodic dissolution of the metal being deposited at the interface of the framework which faces the cathodic compartment.

8. A method according to claim 6 in which the cathodic dissolution of the halide of the metal to be produced is carried out in a cell which is separate from the extraction cell and which communicates therewith through valve means, and in which the cathodic dissolution of the halide of the metal to be produced to enrich the electrolyte to be supplied to the extraction cell with ions of the metal to be produced, comprises the steps of:

(g) providing in the dissolution cell a dissolution cathode and a composite electrode comprised of said anode and said framework which confines within its framework, provided with the partitions, a bath of alkali metal or alkaline earth metal halides free from ions of the metal to be produced,

(h) applying a potential between the anode and the framework of the composite electrode to cause the deposition of the alkali metal or alkaline earth metal on the permeable walls of the framework for a sufficient period of time to cause an accumulation of the metal,

(i) applying a potential between the anode and the dissolution cathode so as to cause the anodic dissolution of the partitions and the formation of the deposit of the metal to be produced on the permeable walls of the framework and

(1) supplying the tetrachloride of the metal to be produced to the dissolution cathode at a rate substantially in the stoichiometric ration with the electrical current supplied to the dissolution cathode in order to cause enrichment of the electrolyte to the desired value.

9. A method according to claim 8 in which the stage of enrichment of the electrolyte with dissolved ions of the metal to be produced is followed by a stage of reduction of the average valence of the ions of the metal dissolved in the electrolyte, carried out without the supply of tetrachloride to the dissolution cell and with a supply of current to the composite electrode and of an intensity such as to maintain the production of the alkali metal or the alkaline earth metal at the anodic interface of the framework and the reduction of the trivalent titanium to the divalent state at the cathodic interface of the framework.

10. A method according to claim 6, in which the cathodic dissolution of the halide of the metal to be produced is carried out in a cell separate from the extraction cell and which communicates therewith through valve means, and in which the cathodic dissolution of the halide of the metal to be produced to enrich the electrolyte to be supplied to the extraction cell with the dissolved metal ions is carried out with the use of a composite electrode comprised of said anode and said framework by providing for the formation of the deposit of the metal to be produced on the walls of the framework of the electrode and by injecting the tetrachloride of the metal to be produced into the electrolytic bath in the absence of a cathodic current and supplying a current to the composite electrode between the anode and the framework, the current having an intensity substantially equal to the sum of a first current which corresponds to the stoichiometric ratio with the flow of tetrachloride injected into the bath, according to the reaction 2Ti³⁺ →

2e^- →

2Ti²⁺ and of the current necessary to maintain sufficient production of the alkali metal of the alkaline earth metal on the framework of the composite electrode to precipitate the divalent metal ion.

11. A method according to claim 6, in which the dissolution and extraction steps are carried out in an environment at sub-atmospheric pressure.

12. A method according to claim 6 in which the electrolyte is constituted by a bath of sodium chloride.