Classifications

• • C—CHEMISTRY; METALLURGY
  • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
  • C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
  • C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
  • C25C3/02—Electrolytic production, recovery or refining of metals by electrolysis of melts of alkali or alkaline earth metals
• • C—CHEMISTRY; METALLURGY
  • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
  • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
  • C25B1/00—Electrolytic production of inorganic compounds or non-metals
• • C—CHEMISTRY; METALLURGY
  • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
  • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
  • C25B1/00—Electrolytic production of inorganic compounds or non-metals
  • C25B1/01—Products
  • C25B1/33—Silicon
• • C—CHEMISTRY; METALLURGY
  • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
  • C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
  • C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
  • C25C3/36—Alloys obtained by cathodic reduction of all their ions

Definitions

• the present invention relates to a process for the production of high purity calcium or calcium alloys, by electrolysis of a calcium derivative in a bath of molten salts, the derivative being in solution in the bath in ionic form.
• liquid cathode the process consisting in using as a cathode a liquid or molten metal, generally deposited at the bottom of the electrolysis tank.
• the invention aims precisely to obtain high purities, both for calcium and for its partner in the derivative. It consists in causing the deposition of calcium or of the alloy on a cathode by electrolysis of a calcium derivative in a bath of molten salts based on calcium halides, the calcium derivative being in solution in the salt bath. fused in ionic form.
• the metal constituting the liquid cathode one can choose for example aluminum, tin, copper, lead, bismuth, nickel, etc.
• the metal constituting the cathode is for example in the molten state. These metals can be used pure or as a mixture. To lower their melting point, they can also be pre ⁇ combined with calcium.
• the metal cathode is liquid proper, that is to say that the cathode is liquid from the start, even before the start of electrolysis.
• the cathode can be solid at the start and gradually change to the liquid state during the electrolysis process, as the Ca / Ni alloy is formed. .
• calcium derivative in ionic solution in molten calcium halides there may be mentioned calcium nitride, calcium hydride, calcium carbide, calcium silicide or if 1 ico-ca 1 cium, calcium boride , calcium cyanide and calcium cyanamide.
• CaC2 which make it possible to produce, at the anode, silicon, respectively, graphite carbon of high purity, alongside of course calcium or calcium alloys of high purity at the cathode.
• the calcium halides are chosen from the group comprising chloride, calcium fluoride and their mixtures.
• eutectic mixtures are preferably chosen.
• the bath may contain other halides, for example alkali halides, chlorides or fluorides in particular.
• the process is carried out at molten salt bath temperatures of between 650 and 1100 ° C., depending on the electrolysis conditions and on the calcium derivative treated.
• concentrations of these derivatives in the bath obviously depend on the nature of this derivative and on its solubility in the molten halide.
• the concentration of CaC2 in the bath is generally between 5 and 14% by weight, at the aforementioned temperatures.
• the concentration of CaS.i2 (ico-calcium silica is a relatively common metallurgical product) is generally between 1 and 2% by weight, also at the aforementioned temperatures.
• the calcium alloy obtained as a liquid cathode, is characterized by a high degree of purity and gives easy access to calcium which is also of high purity.
• distillation in fact, in particular under vacuum, it is easy to decompose the alloy and recover the calcium and the metal.
• reduced pressure 5 x 10 "2 to 10 HPa
• the silicon being obtained in an anodic manner is characterized by a high degree of purity and it is impossible to detect there by the traditional analytical means traces of conventional metallic contaminants, such as Fe, Al, Ca, Cu, Mg.
• the bath is regenerated to remove CaO (notably from technical CaC2) and the other impurities which have accumulated there.
• CaO notably from technical CaC2
• Cl 2 gas optionally in the presence of C in suspension or a reducing gas such as methane.
• the cell After fusion (772 ° C) the cell is closed and pumping is carried out using a vacuum line comprising a liquid nitrogen trap and one. primary pump.
• the calcium chloride is brought to 950 ° C. under a vacuum of 10 "" * HPa for 2 hours. After this treatment, the chloride is completely anhydrous (% H2O ⁇ 0.01 *).
• the cathodic current density is between 0.6 and 1.2 A / m 2 , ie electrolysis conditions corresponding on average to 120 A and 1 V.
• the electrolysis time is 5 hours.
• the metal alloy located at the bottom of the crucible is drawn off and analyzed.
• the alloy has a 10.8% calcium content and its melting point measured by thermal analysis is located at 625 ° C., that is to say very close to the compound CaSn3 "
• the anode was covered with a relatively dense graphite sponge of about 400 cm ⁇ containing about 210 g of graphite.
• the calcium alloy is then distilled in vacuo at 1000 ° C under ÎO- * HPa with a condenser temperature of 500 ° C.
• the metal obtained counts 99.2% calcium.
• the salt bath maintained in the graphite crucible has about 3% CaO or equivalent which are eliminated by adding to the bath about 200 g of anodic carbon sponge powder, finely ground and redispersed in the bath by stirring and by injection. and cladding of 300 g of chlorine gas diluted in argon.
• the bath also regenerated, is filtered on a porous nickel filter and reused for subsequent productions. .
• Example 2 The same procedure as that of Example 1 is used, except that only 310 g of technical C C2 is dissolved and that the electrolysis is carried out only at 700 ° C.
• the electrolysis was conducted in the same way, that is to say on average under 1 V practical and 120 A.
• the metal is recovered by vacuum distillation at 700 ° C under 10 ⁇ 2 HPa with a condenser at 500 ° C.
• the calcium obtained is of quality comparable to that of Example 1: 99.3% purity.
• the bath containing approximately 1% of CaO is regenerated by chlorination after dispersion of 100 g of sponge powder and passage of 150 g of chlorine gas, the titration of the bath is carried out by adding approximately 25 g of
• the calcium is then extracted by vacuum distillation of the calcium / tin alloy.
• the silicon formed a compact deposit on the anode. At the interface between the anode and the deposit, the presence of silicon carbide can be detected.
• the deposit of silicon is recovered on the anode and it is found that this metal is in a state of high purity. Indeed, no metal impurity is detectable with the analysis means available.

Landscapes

• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
• Materials Engineering (AREA)
• Metallurgy (AREA)
• Organic Chemistry (AREA)
• Inorganic Chemistry (AREA)
• Electrolytic Production Of Metals (AREA)
• Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
• Carbon And Carbon Compounds (AREA)

Applications Claiming Priority (4)

Publications (1)

Family

ID=26224194

Family Applications (1)

Country Status (9)

Families Citing this family (19)

Family Cites Families (5)

• 1985
  • 1985-09-27 BR BR8507254A patent/BR8507254A/pt unknown
  • 1985-09-27 WO PCT/FR1985/000266 patent/WO1986002108A1/fr not_active Application Discontinuation
  • 1985-09-27 EP EP85904824A patent/EP0230411A1/fr not_active Withdrawn
  • 1985-09-27 US US06/876,857 patent/US4738759A/en not_active Expired - Fee Related
  • 1985-09-27 AU AU50110/85A patent/AU5011085A/en not_active Abandoned
  • 1985-10-02 PT PT81241A patent/PT81241B/pt unknown
  • 1985-10-03 ES ES547525A patent/ES8608449A1/es not_active Expired
• 1986
  • 1986-06-04 NO NO862234A patent/NO862234L/no unknown
• 1987
  • 1987-04-01 FI FI871421A patent/FI871421A/fi not_active IP Right Cessation

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events