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US2870072A - Preparation of fused salt electrolytes - Google Patents

Preparation of fused salt electrolytes Download PDF

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US2870072A
US2870072A US522954A US52295455A US2870072A US 2870072 A US2870072 A US 2870072A US 522954 A US522954 A US 522954A US 52295455 A US52295455 A US 52295455A US 2870072 A US2870072 A US 2870072A
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chlorinated
molten
fused salt
chloride
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Merlub-Sobel Menahem
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Horizons Titanium Corp
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    • 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

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  • This invention relates to the production of anhydrous chlorides of various metals and to the subsequent recovery of the metal by a fused salt electrolysis of the chloride. More particularly, it relates to a novel procedure whereby an oxide containing compound of the metal to be recovered is converted into an oxygen-free chloride of the metal and the oxygen-free chloride is thereafter converted to the desired metal by electrolysis in a fused salt electrolyte.
  • chlorinating agents may be employed to effect the chlorination of the oxidic metal compound, among which may be mentioned anhydrous hydrogen chloride, carbon tetrachloride, phosgene and elemental chlorine.
  • anhydrous hydrogen chloride carbon tetrachloride, phosgene and elemental chlorine.
  • the reaction requires the presence ICC compound with which carbon may be admixed if desiredl and then the charge is chlorinated by means of the chlorinating gas.
  • the metal chloride formed is carried out of-the tube through the porous disc in the stream of excess chlorinating agent and other gaseous products formed by the reaction into the fused salt bath surrounding the porous portion of the charge containing reaction tube, wherein the metal chloride dissolves.
  • the hollow-non-reactive conductive tube serves merely as a reaction chamber in which the following reaction is caused to' take place between a suitably proportioned mixture of metal oxide withcarbon or graphite and a chlorinating agent, such as elemental chlorine (Equation 1)'or a metal oxide and a chlorinating agent -such as hydrogen chloride (Equa- Where x and y are integers and M is any metal whose oxide or readily decomposed oxygen containing compounds are adapted to be treated in the manner described.
  • a chlorinating agent such as elemental chlorine (Equation 1)'or a metal oxide and a chlorinating agent -such as hydrogen chloride (Equa- Where x and y are integers and M is any metal whose oxide or readily decomposed oxygen containing compounds are adapted to be treated in the manner described.
  • the metal chloride at the temperature of the reaction, is carried out of the reaction chamber along with any gaseous products produced and any excess or unreacted chlorinating gas.
  • the several products may be readily separated from one another in any convenient fashion.
  • various known techniques may be employed.
  • the metal chloride may be decomposed by electrolyzing the fused salt bath surrounding the reaction tube after the metal chloride has dissolved therein.
  • this fused bath is pumped to a conventional fused salt electrolytic cell and electrolyte is returned to surround the reaction chamber and to be replenished with metal chloride evolved in the continuing chlorination.
  • the reaction tube itself serves as the anode in an electrolysis which may be carried out during or subsequent to the chlorination reaction.
  • the reaction tube is immersed in a fused salt bath so that, as the metal oxide is chlorinated, the metal chloride formed passes out of the porous disc and directly into the fused salt bath as previously described.
  • the fused bath surrounding the hollow tube serves to protect the tube and its contents from the effect of air, oxygen, or any other undesirable reactive environment, and also functions to maintain the temperature of the reaction tube and its vcontents within close limits.
  • the resulting salt bath which comprises the original salt bath plus the metal chloride which has passed out of the reaction tube may be directlyelectrolyzed to recover the metal by suitably constructing the reaction apparatus.
  • an extraneous salt usually an alkali metal chloride, in which the metal chloride dissolves as it forms during the chlorination reaction so that the metal chloride dissolved in the alkali metal chloride passes on into the fused bath in the form of a molten mixture instead of as a vapor.
  • the reaction may be represented as follows:
  • the desired electrical ndutivity is provided ⁇ v by thehollow anode, and.as .a. result, instead of proportioning a mixture of oxide and carbon to produce the required conductivity, the mixture may;r beproportioned frouttthe standpoint :of: the optimum". chemicall conversion;- to;Vl metal chloride,- with little or; um excess of any of the reactants. By etectingicoutact ⁇ ber tweerrthe metal oxide and; the chlorinating agent; within the-contines of.
  • Reaction chamber 20 is formed of any suitable material, anclY is preferably-constructed of graphite.
  • Y it hasY been foundthat commercial graphite is suitable andfa cylindrical, elliptical, rectangular or other. shapedY hollow configurationA may be ⁇ employed.
  • the lower-end of ⁇ tube 20 is closed with av porous plug 22 of graphite, carbon or ceramic composition.
  • the upper end offtube ⁇ 20 is closed by a plug 2,4 provided with inlet means 26 for admitting a halogenating agent. such as chlorine gas and means 28 schematically showing an arrangement for replenishing the solid portion of the reaction mixture inl the element.20.
  • briquettes of the. oxide or decomposable oxygen containing compound of the metal toV be produced with or without a carbonaceous reducingv agent.
  • the briquettes are p reterablyformedA by mixing together finely divided carbon such ⁇ as ⁇ -325 meshI (Tyler Standard) lampblack with -200 meshmetaloxide in substantially stoichiometric proportions.
  • These ingredients may be formed into ⁇ briquettesor pellets with any suitable binder, methyl cellulose, molasses, and water each having been found suitable.
  • T o facilitate the. removal of the metal chloride formed by. the reaction conducted in chamberv 20Y asv a; liquid rather than in, vapor form, ⁇ it; has been found advantageous in some cases, to include a small amount of at least one alkali metal halide or alkaline earth metal halide in the charge.
  • the additional halide is chosen from those halides in which the metal chloride, formed by chlorination of themetaloxide, dissolves; Y
  • one or more cathodes 32 arev suspendedin fused bath 22 whichv is4 comprised of one or more alkali halides or ⁇ alkaline earth halides" or mixtures of same.
  • V alkali halides or ⁇ alkaline earth halides
  • Both the electrolytic and nou-electrolytic processes constituting my invention are based on the same reactions and hence are both generally applicable to the recovery of the same metals and metalloids.
  • the processes are particularly suited to the recovery of the halides; of?y metals, which cannotbe recovered. from aqueous solutions by ordnary methods.
  • aqueous solutions containing zirconium chloride are evaporated to recover the chloride, the product obtained is largely an oxychloride.
  • the desired chlorides areobtained, dissolved in an anhydrous fused salt menstruum, from which many of the halides may be recovered by heating the fused bath to a temperature sufiicient to volatilize the metal halide.
  • The'elements which form chlorides may beV considered asfalling into three more or less clearly defined groups.
  • a ii'rstgroup composed of the elements which are highly metallic is characterizedA by the formation of chlorides whichV are. completely or substantially completely stable in water solutionsantl which can therefore be recovered substantially undecomposed from an aqueous medium.
  • Exemplary of this group are the alkali metals, the alkaline earthy metals and such metals as silver, lead and copper.
  • Asecond' groupingoffthe elements comprises those which are considered completely or. partially nonmetallic, such as.sulphur,phosphorus, vboron and silicon. On contact with water,rthe, chlorides of these elementsI hydrolize, completely and. thereforeA cannot be recovered ⁇ from. aqueous solutions..
  • the ⁇ chlorides; of v this second, group of elements when formed in nonaqueousk systems are substantiallyv insoluble: in and/or. immiscible withfused melts; of alkali metal or alkalineearth metal halides.
  • the remaining elements Which-form chloridesconstitute atransitiongroup. These elements: form chlorideswhich unlike the rst group cannot. be recovered: from aqueous solutions without complete or 4at least substantial decomposition.
  • these elements form chlorides which will dissolvel or which will react withV alkali metal orlalkaline earth metals fused halide. melts to form at elevated temperatures a continuous phase of electricity-conducting properties.
  • halides particularlyy the chlorides,- including-the chloridesof the elements fallingzin thethird group-above described.
  • These comprise aluminum, beryllium, cerium, chromium, hafnium, molybdenum, zirconium, tantalum; titanium (as a chloride lowerinzvalence-zthan-4), thorium, tungsten, uranium; vanadium, and the other rare earth (atomic number $7- 7l)1'or-refr ⁇ actorymetals:
  • the chloridesV so produced may'be electrolyzed inra-*manner Well known in the art to obtain the desired metal;
  • Example I An intimate mixture of carbon, sodium chloride and basic zirconium carbonate was formed by grinding the three ingredients together in the proportion of about 4 parts by weight of lampblack, 13 parts by weight of sodium chloride and 40 parts by weight of basic zirconium carbonate, containing about 23.4% Zr02. The mixture was formed into small briquettes about one-half inchl in diameter and one-half inch in length by means of a hand arbor press.
  • a reaction chamber was constructed in accordance with the drawing by providing a graphite tube about 18 inches long, 2 inches external diameter, and 1% inches internal diameter.
  • One end of tube 20 was plugged with a rubber stopper 24 having a connection 26 for admitting chlorine and the other end was provided with a porous carbon plug 22.
  • Plug 22 was about 4 inches in length.
  • a hole /s inch in diameter was drilled through about 31/2 inches of the plug so that the end of the hole inside was about liush vwith the end of the graphite tube.
  • the graphite tube 20. was partially filled with briquettes and then was placed in a fused salt bath 12 formed of sodium chloride, in a vertical electrically heated furnace.
  • Chlorine gas was admitted through the inlet and the entire assembly was heated (by means not shown) gradually to the melting point of sodium chloride and, as chlorination proceeded, to a temperature of almost 900 C. Thereafter the assembly was cooled and the salt bath surrounding the tube was an analyzed for zirconium. It was found that about 6.4% ZrCl4 was present in the sodium chloride.
  • the complex fused salt was melted in a conventional electrolytic cell and electrolyzed therein under a controlled atmosphere at about 750 C. with a cell voltage of between about 2.2 and 2.4 volts and a current density of about 100 amps/square decimeter, whereby the zirconium was recovered as a cathode deposit on a steel cathode.
  • transition group element to include the elements characterized as neither highly metallic nor completely nonmetallic on the basis of the manner in which the chlorides behave in aqueous and fused media.
  • a process of preparing a fused salt composition adapted to be electrolyzed which comprises: providing a refractory vessel; establishing a fused salt bath consisting essentially of at -least one halide from the group consisting of alkali metal halides and alkaline earth metal halides; providing a container adapted to contain material to be chlorinated and consisting of a tubular element confining the material to be chlorinated within a solid tubular upper portion and a porous lower portion; charging into said container an oxygen-containing compound of an element other than the alkali metals and alkaline earth metals and selected from the group of elements forming chlorides which cannot be recovered from aqueous solutions in substantially undecomposed and unhydrolyzed fornr and whose chlorides are miscible in fused alkali halide melts, alkaline earth halide melts and molten mixtures of alkali halide and alkaline earth halides; immersing said container in said fused salt bath so
  • An electrolytic apparatus comprising a refractory vessel adapted to contain a molten salt electrolyte and having a cover to enclose the contents of the vessel; means for heating the contents so as to maintain it in molten form; a hollow tubular anode element adapted to contain solid material to be chlorinated, said element being mounted so as to pass through said cover and having an upper end extending above said cover and a lower end adapted to extend into the molten contents of the vessel; a plug in the upper end of said tube; a rst means extending through said plug Vfor admitting a chlorinating gas into said tubular element; a second means extending through said plug for introducing a charge of solid material to be chlorinated into said tubular element; a porous plu'gdisposed within the lower end ofsaid tubular element so as to support a charge of material to be chlorinated in said tubular element and to permit the egress of chlorinated reaction products from said tubular element directly into the molten contents of the vessel;

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  • Chemical Kinetics & Catalysis (AREA)
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Description

Jan. 20, 1959 M. MERLUB-SOBEL PREPARATION OF FUSED SALT ELECTROLYTES Filed July 19, 195,5
UnitedStates Patent O.
PREPARAnoN oF FUsnn SALT ELEcrRoLYrEs Menahem Merlub=Sobel, Cleveland, Ohio, assignor, by mesne assignments, to Horizons Titanium Corporation, Princeton, N. I., a corporation of New Jersey Application July 19, 1955, Serial No. 522,954-
2 Claims. (Cl. 2014-564) This invention relates to the production of anhydrous chlorides of various metals and to the subsequent recovery of the metal by a fused salt electrolysis of the chloride. More particularly, it relates to a novel procedure whereby an oxide containing compound of the metal to be recovered is converted into an oxygen-free chloride of the metal and the oxygen-free chloride is thereafter converted to the desired metal by electrolysis in a fused salt electrolyte.
Numerous processes have been described in the prior art for producing metals from4 oxygen-containing metal compounds such as the oxides, carbonates, nitrates, and various salts of organic acids such as oxylates and the like, since the metal oxides are relatively inexpensive and are generally easy to prepare in relatively pure form from such oxygen containing compounds. These processes include thermal as well as electrochemical procedures. One electrochemical approach which has been extensively attempted has been an electrolysis in a suitable fused salt electrolyte employing an anode formed of a mixture of the metal oxide and carbon. Such electrolytes have been formed of one or more alkali metal chlorides or one or more alkaline earth chlorides or mixtures of one or more alkali metal chlorides and one or more alkaline earth metal chlorides. Invariably, these attempts have failed when attempted on a commercial scale because most of the chlorine formed by electrolysis at the anode escapes as a gas instead of reacting with the metal oxide constituent of the mixture to form the metal chloride necessary for the success of the operation. A further disadvantage of this prior art method arises from the necessity for obtaining the required electrical conductivity in the anode. This is met by providing a large excess of carbon in the mixture, with the resulting decrease in the amount of metal oxide in the mixture available for reaction with the chlorine evolved, as well as later contamination of the bath by the excess carbon. Since this prior art appreach employs materials which are relatively inexpensive, and which are readily prepared, the method remains economically attractive in spite of the technical difficulties previously encountered in adapting it to commercial production.
I have discovered a method which is free from the disadvantages of the prior art methods and a novel means for carrying out my method whereby the advantages of a reactive oxide anode can be retained. Instead of relying on a self supporting electrically conductive mixture of metal oxide and carbon to serve as the anode, I provide a charge container in the form of a hollow non-reactive conductive reaction tube one end of which is adapted to be closed by a porous disc and the other end of which is adapted to be connected to a source of a chlorinating gas.
Various chlorinating agents may be employed to effect the chlorination of the oxidic metal compound, among which may be mentioned anhydrous hydrogen chloride, carbon tetrachloride, phosgene and elemental chlorine. In the case of chlorine, the reaction requires the presence ICC compound with which carbon may be admixed if desiredl and then the charge is chlorinated by means of the chlorinating gas. The metal chloride formed is carried out of-the tube through the porous disc in the stream of excess chlorinating agent and other gaseous products formed by the reaction into the fused salt bath surrounding the porous portion of the charge containing reaction tube, wherein the metal chloride dissolves.
In this aspect of my invention, the hollow-non-reactive conductive tube serves merely as a reaction chamber in which the following reaction is caused to' take place between a suitably proportioned mixture of metal oxide withcarbon or graphite and a chlorinating agent, such as elemental chlorine (Equation 1)'or a metal oxide and a chlorinating agent -such as hydrogen chloride (Equa- Where x and y are integers and M is any metal whose oxide or readily decomposed oxygen containing compounds are adapted to be treated in the manner described.
The metal chloride,at the temperature of the reaction, is carried out of the reaction chamber along with any gaseous products produced and any excess or unreacted chlorinating gas. The several products may be readily separated from one another in any convenient fashion. To recover the desired metal from the metal chloride so produced, various known techniques may be employed. For instance, the metal chloride may be decomposed by electrolyzing the fused salt bath surrounding the reaction tube after the metal chloride has dissolved therein. Preferably this fused bath is pumped to a conventional fused salt electrolytic cell and electrolyte is returned to surround the reaction chamber and to be replenished with metal chloride evolved in the continuing chlorination.
In another aspect of my invention, the reaction tube itself serves as the anode in an electrolysis which may be carried out during or subsequent to the chlorination reaction. In this embodiment, the reaction tube is immersed in a fused salt bath so that, as the metal oxide is chlorinated, the metal chloride formed passes out of the porous disc and directly into the fused salt bath as previously described. The fused bath surrounding the hollow tube serves to protect the tube and its contents from the effect of air, oxygen, or any other undesirable reactive environment, and also functions to maintain the temperature of the reaction tube and its vcontents within close limits. The resulting salt bath, which comprises the original salt bath plus the metal chloride which has passed out of the reaction tube may be directlyelectrolyzed to recover the metal by suitably constructing the reaction apparatus. Y
In a preferred aspect of my invention, there may be added to the charge in the hollow tube a small amount of an extraneous salt, usually an alkali metal chloride, in which the metal chloride dissolves as it forms during the chlorination reaction so that the metal chloride dissolved in the alkali metal chloride passes on into the fused bath in the form of a molten mixture instead of as a vapor. The reaction may be represented as follows:
described are at once evident. First, the desired electrical ndutivity is provided`v by thehollow anode, and.as .a. result, instead of proportioning a mixture of oxide and carbon to produce the required conductivity, the mixture may;r beproportioned frouttthe standpoint :of: the optimum". chemicall conversion;- to;Vl metal chloride,- with little or; um excess of any of the reactants. By etectingicoutact` ber tweerrthe metal oxide and; the chlorinating agent; within the-contines of. thehollow anode, instead of; ortA the ex terior-,surface-of theY anode, asinitheprionart, the chlorinatingagent isafiordedample opportunity to4 react with metal-oxide-in, an efficient manner. Other advantages will becomeapparent fromthe following description.
I-nthe. accompanying drawiug,.the figure represents a sectional view of a preferred apparatus, for: carrying out mylrnethod.
As. shownin the; drawing,Y az refractory crucible 10 sevesiasthe, container foi-fa. fused.- salt'bath 12. The crucible is provided-.With az cover 14 having an inlet 16 and*A anoutlet^18- throughfwhich gases may be admittedi toor vented from the space above the fused bath ingsr through which one or more reaction chambers` or '7' electrodes may be inserted. In the figure, one such chamber and one-such electrode are-shown identiiied as 2.0.and 32 respectively.
Reaction chamber 20 is formed of any suitable material, anclY is preferably-constructed of graphite. When the=tube 20 isf to serve asa reaction chamber in which the-chlorination is effected, itis merely required* to pos-v sess1the, necessary structural strength and chemical inertness to,` the; materialsin contact with it. When thetube Ztl-also vfunctions as an electrode, in an electrolytic cell, it -is=required to possessfaasufficient conductivity to satisfy the electricalV conditions imposed on it. In either instanceY it hasY been foundthat commercial graphite is suitable andfa cylindrical, elliptical, rectangular or other. shapedY hollow configurationA may be` employed. The lower-end of `tube 20 is closed with av porous plug 22 of graphite, carbon or ceramic composition. The upper end offtube` 20 is closed bya plug 2,4 provided with inlet means 26 for admitting a halogenating agent. such as chlorine gas and means 28 schematically showing an arrangement for replenishing the solid portion of the reaction mixture inl the element.20.
Within element 20'there is shown a charge consisting ol." briquettes of the. oxide or decomposable oxygen containing compound of the metal toV be produced with or without a carbonaceous reducingv agent. The briquettes are p reterablyformedA by mixing together finely divided carbon such` as` -325 meshI (Tyler Standard) lampblack with -200 meshmetaloxide in substantially stoichiometric proportions. These ingredients may be formed into` briquettesor pellets with any suitable binder, methyl cellulose, molasses, and water each having been found suitable.
T o facilitate the. removal of the metal chloride formed by. the reaction conducted in chamberv 20Y asv a; liquid rather than in, vapor form,` it; has been found advantageous in some cases, to include a small amount of at least one alkali metal halide or alkaline earth metal halide in the charge. The additional halide is chosen from those halides in which the metal chloride, formed by chlorination of themetaloxide, dissolves; Y
When: the apparatuss ,employed for carrying out'thev electrolytic; aspect zofmyprocess, one or more cathodes 32 arev suspendedin fused bath 22 whichv is4 comprised of one or more alkali halides or` alkaline earth halides" or mixtures of same. With most of the metals amenable to the practice of my invention, I prefer to form the bath of :sodium chloride or eutectic mixtures of Vsodium Chloride: andzother chlorides of the alkali vor alkaline earth 4' metals, sincesuch bathsareeeonomicalauderect-imposed of materials readily commercially available in the desired purity. i
Both the electrolytic and nou-electrolytic processes constituting my invention are based on the same reactions and hence are both generally applicable to the recovery of the same metals and metalloids. The processes are particularly suited to the recovery of the halides; of?y metals, which cannotbe recovered. from aqueous solutions by ordnary methods. For example, when aqueous solutions containing zirconium chloride are evaporated to recover the chloride, the product obtained is largely an oxychloride. By the practice ofF my invention, the desired chlorides areobtained, dissolved in an anhydrous fused salt menstruum, from which many of the halides may be recovered by heating the fused bath to a temperature sufiicient to volatilize the metal halide.
The'elements which form chlorides may beV considered asfalling into three more or less clearly defined groups.- A ii'rstgroup composed of the elements which are highly metallic is characterizedA by the formation of chlorides whichV are. completely or substantially completely stable in water solutionsantl which can therefore be recovered substantially undecomposed from an aqueous medium. Exemplary of this group are the alkali metals, the alkaline earthy metals and such metals as silver, lead and copper. Asecond' groupingoffthe elements comprises those which are considered completely or. partially nonmetallic, such as.sulphur,phosphorus, vboron and silicon. On contact with water,rthe, chlorides of these elementsI hydrolize, completely and. thereforeA cannot be recovered` from. aqueous solutions.. Furthermore, the` chlorides; of v this second, group of elements when formed in nonaqueousk systems are substantiallyv insoluble: in and/or. immiscible withfused melts; of alkali metal or alkalineearth metal halides. The remaining elements Which-form chloridesconstitute atransitiongroup. These elements: form chlorideswhich unlike the rst group cannot. be recovered: from aqueous solutions without complete or 4at least substantial decomposition. Unlike the. secondi group, these elements form chlorides which will dissolvel or which will react withV alkali metal orlalkaline earth metals fused halide. melts to form at elevated temperatures a continuous phase of electricity-conducting properties.
Itzwillbe seen that some metals form chlorides'which places them on the border line of more than one of the above groups; For example, by theuse of specialized techniques involving hydrogen chloride gas or ammonium chloride, the chlorides of'magnesium and cerium may be recovered from aqueous solutions and hence these elementsare properly Classifiable either in the first orl third group. As a practical matter, they should be-treated as' belonging tothe transitiony group. Other metalsisuch as titanium will fall inv more than: one group depending' upon thevalence state'ofthe chloride. Thus tetravalent titaniumwould be classed in the'non-metallic group since titanium tetrachloridetis substantially insoluble in fused halide melts, while as atrivalentelement it would fall inI thetransition group'.
Thereactions previously set forthare applicable-,to the production of a widevariety of halides, particularlyy the chlorides,- including-the chloridesof the elements fallingzin thethird group-above described. These comprise aluminum, beryllium, cerium, chromium, hafnium, molybdenum, zirconium, tantalum; titanium (as a chloride lowerinzvalence-zthan-4), thorium, tungsten, uranium; vanadium, and the other rare earth (atomic number $7- 7l)1'or-refr`actorymetals: The chloridesV so produced may'be electrolyzed inra-*manner Well known in the art to obtain the desired metal;
The following, example. will serve. to.. further.A illustrate the practice of my invention.
. Example I An intimate mixture of carbon, sodium chloride and basic zirconium carbonate Was formed by grinding the three ingredients together in the proportion of about 4 parts by weight of lampblack, 13 parts by weight of sodium chloride and 40 parts by weight of basic zirconium carbonate, containing about 23.4% Zr02. The mixture was formed into small briquettes about one-half inchl in diameter and one-half inch in length by means of a hand arbor press.
A reaction chamber was constructed in accordance with the drawing by providing a graphite tube about 18 inches long, 2 inches external diameter, and 1% inches internal diameter. One end of tube 20 was plugged with a rubber stopper 24 having a connection 26 for admitting chlorine and the other end was provided with a porous carbon plug 22. Plug 22 was about 4 inches in length. A hole /s inch in diameter was drilled through about 31/2 inches of the plug so that the end of the hole inside was about liush vwith the end of the graphite tube. The graphite tube 20. was partially filled with briquettes and then was placed in a fused salt bath 12 formed of sodium chloride, in a vertical electrically heated furnace.
Chlorine gas was admitted through the inlet and the entire assembly was heated (by means not shown) gradually to the melting point of sodium chloride and, as chlorination proceeded, to a temperature of almost 900 C. Thereafter the assembly was cooled and the salt bath surrounding the tube was an analyzed for zirconium. It was found that about 6.4% ZrCl4 was present in the sodium chloride.
The complex fused salt was melted in a conventional electrolytic cell and electrolyzed therein under a controlled atmosphere at about 750 C. with a cell voltage of between about 2.2 and 2.4 volts and a current density of about 100 amps/square decimeter, whereby the zirconium was recovered as a cathode deposit on a steel cathode.
Instead of permitting the fused bath to solidify, and transferring the salt to an electrolytic cell, for remelting, it will be obvious that the electrolysis could have been conducted in the original cell by providing a cathode and impressing a potential across the hollow anode and the cathode. Indeed the crucible itself may serve as the cathode in many cases.
While I have disclosed the process as applied to the recovery of zirconium, it will be appreciated by those skilled in the art that it is equally applicable to many other oxidic metal compounds, and even to oxygencontaminated metal scrap which may be thereby converted to a chloride in an anhydrous fused salt bath and subsequently recovered therefrom by known electrolytic procedures.
In the following claims I have employed the term transition group element to include the elements characterized as neither highly metallic nor completely nonmetallic on the basis of the manner in which the chlorides behave in aqueous and fused media.
I claim:
l. A process of preparing a fused salt composition adapted to be electrolyzed which comprises: providing a refractory vessel; establishing a fused salt bath consisting essentially of at -least one halide from the group consisting of alkali metal halides and alkaline earth metal halides; providing a container adapted to contain material to be chlorinated and consisting of a tubular element confining the material to be chlorinated within a solid tubular upper portion and a porous lower portion; charging into said container an oxygen-containing compound of an element other than the alkali metals and alkaline earth metals and selected from the group of elements forming chlorides which cannot be recovered from aqueous solutions in substantially undecomposed and unhydrolyzed fornr and whose chlorides are miscible in fused alkali halide melts, alkaline earth halide melts and molten mixtures of alkali halide and alkaline earth halides; immersing said container in said fused salt bath so that the porous portion of the container is beneath the surface of the bath; passing a chlorinating gas into the upper portion of said charge-filled container, thereby forming a chloride of the element whose oxygen-con taining compound constituted the charge; and recoverving said chloride in said molten bath by passage of said chloride through the pores of said porous portion of the charge-confining container and directly into the surrounding molten bath.
2. An electrolytic apparatus comprising a refractory vessel adapted to contain a molten salt electrolyte and having a cover to enclose the contents of the vessel; means for heating the contents so as to maintain it in molten form; a hollow tubular anode element adapted to contain solid material to be chlorinated, said element being mounted so as to pass through said cover and having an upper end extending above said cover and a lower end adapted to extend into the molten contents of the vessel; a plug in the upper end of said tube; a rst means extending through said plug Vfor admitting a chlorinating gas into said tubular element; a second means extending through said plug for introducing a charge of solid material to be chlorinated into said tubular element; a porous plu'gdisposed within the lower end ofsaid tubular element so as to support a charge of material to be chlorinated in said tubular element and to permit the egress of chlorinated reaction products from said tubular element directly into the molten contents of the vessel; whereby a fused salt composition may be formed from' which the element which is chlorinated may be recovered by a fused salt electrolysis.
References Cited in the le of this patent UNITED STA'I'ES PATENTS OTHER REFERENCES Hackhs chemical Dictionary, 3rd edition (1944), pp. 863 and 864, delinition of transition elements.

Claims (2)

1. A PROCESS OF PREPARING A FUSED SALT COMPOSITION ADAPTED TO BE ELECTROLYZED WHICH COMPRISES: PROVIDING A REFRACTORY VESSEL; ESTABLISHING A FUSED SALT BATH CONSISTING ESSENTIALLY OF AT LEAST ONE HALIDE FROM THE GROUP CONSISTING OF ALKALI METAL HALIDES AND ALKALINE EARTH METAL HALIDES; PROVIDING A CONTAINER ADAPTED TO CONTAIN MATERIAL TO BE CHLORINATED AND CONSISTING OF A TUBULAR ELEMENT CONFINING THE MATERIAL TO BE CHLORINATED WITHIN A SOLID TUBULAR UPPER PORTION AND A POROUS LOWER PORTION; CHARGING INTO SAID CONTAINER AN OXYGEN-CONTAINING COMPOUND OF AN ELEMENT OTHER THAN THE ALKALI METALS AND ALKALINE EARTH METALS AND SELECTED FROM THE GROUP OF ELEMENTS FORMING CHLORIDES WHICH CANNOT BE RECOVERED FROM AQUEOUS SOLUTIONS IN SUBSTANTIALLY UNDECOMPOSED AND UNHYDROLYZED FORM AND WHOSE CHLORIDES ARE MISCIBLE IN FUSED ALKALI HALIDE MELTS, ALKALINE EARTH HALIDE MELTS AND MOLTEN MIXTURES OF ALKALI HALIDE AND ALKALINE EARTH HALIDES; IMMERSING SAID CONTAINER IN SAID FUSED SALT BATH SO THAT THE POROUS PORTION OF CONTAINER IS BENEATH THE SURFACE OF THE BATH; PASSING A CHLORINATING GAS INTO THE UPPER PORTION OF SAID CHARGE-FILLED CONTAINER, THEREBY FORMING A CHLORIDE OF THE ELEMENT WHOSE OXYGEN-CONTAINING COMPOUND CONSTITUTED THE CHARGE; AND RECOVERING SAID CHLORIDE IN SAID MOLTEN BATH BY PASSAGE OF SAID CHLORIDE THROUGH THE PORES OF SAID POROUS PORTION OF THE CHARGE-CONFINING CONTAINER AND DIRECTLY INTO THE SURROUNDING MOLTEN BATH.
2. AN ELECTROLYTIC APPARATUS COMPRISING A REFRACTORY VESSEL ADAPTED TO CONTAIN A MOLTEN SALT ELECTROLYTE AND HAVING A COVER TO ENCLOSE THE CONTENTS OF THE VESSEL; MEANS FOR HEATING THE CONTENTS SO AS TO MAINTAIN IT IN MOLTEN FORM; A HOLLOW TUBULAR ANODE ELEMENT ADAPTED TO CONTAIN SOLID MATERIAL TO BE CHLORINATED, SAID ELEMENT BEING MOUNTED SO AS TO PASS THROUGH SAID COVER AND HAVING AN UPPER END EXTENDING ABOVE SAID COVER AND A LOWER END ADAPTED TO EXTEND INTO THE MOLTEN CONTENTS OF THE VESSEL; A PLUG IN THE UPPER END OF SAID TUBE; A FIRST MEANS EXTENDING THROUGH SAID PLUG FOR ADMITTING A CHLORINATING GAS INTO SAID TUBULAR ELEMENT; A SECOND MEANS EXTENDING THROUGH SAID PLUG FOR INTRODUCING A CHARGE OF SOLID MATERIAL TO BE CHLORINATED INTO SAID TUBULAR ELEMENT; A POROUS PLUG DISPOSED WITHIN THE LOWER END OF SAID TUBULAR ELEMENT SO AS TO SUPPORT A CHARGE OF MATERIAL TO BE CHLORINATED IN SAID TUBULAR ELEMENT AND TO PERMIT THE EGRESS OF CHLORINATED REACTION PRODUCTS FROM SAID TUBULAR ELEMENT DIRECTLY INTO THE MOLTEN CONTENTS OF THE VESSEL; WHEREBY A FUSED SALT COMPOSITION MAY BE FORMED FROM WHICH THE ELEMENT WHICH IS CHLORINATED MAY BE RECOVERED BY A FUSED SALT ELECTROLYSIS.
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3021268A (en) * 1956-06-29 1962-02-13 Ichiro Egami Electrolytic production of ticl4 and mg by means of a special anode
US3523884A (en) * 1968-05-10 1970-08-11 Systron Donner Corp Method and apparatus for making wall structure impervious to moisture
US4597839A (en) * 1983-12-14 1986-07-01 Atlantic Richfield Company Method and apparatus for production of a metal from metallic oxide ore
US20190211460A1 (en) * 2018-01-11 2019-07-11 Consolidated Nuclear Security, LLC Methods and systems for producing a metal chloride or the like
KR20200130526A (en) * 2019-05-08 2020-11-19 한국생산기술연구원 Method of controlling impurity of indium metal by electrolytic refining of molten salt

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1646734A (en) * 1922-08-21 1927-10-25 Westinghouse Lamp Co Metallurgical method
GB452269A (en) * 1935-03-13 1936-08-19 Magall Ag Improvements in and relating to the production of magnesium and alkali earth metals by electrolysis of fused starting materials
GB561651A (en) * 1941-11-24 1944-05-30 Motrac Motormaher & Traktoren Process and apparatus for the manufacture of metals of the alkaline earth series

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1646734A (en) * 1922-08-21 1927-10-25 Westinghouse Lamp Co Metallurgical method
GB452269A (en) * 1935-03-13 1936-08-19 Magall Ag Improvements in and relating to the production of magnesium and alkali earth metals by electrolysis of fused starting materials
GB561651A (en) * 1941-11-24 1944-05-30 Motrac Motormaher & Traktoren Process and apparatus for the manufacture of metals of the alkaline earth series

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3021268A (en) * 1956-06-29 1962-02-13 Ichiro Egami Electrolytic production of ticl4 and mg by means of a special anode
US3523884A (en) * 1968-05-10 1970-08-11 Systron Donner Corp Method and apparatus for making wall structure impervious to moisture
US4597839A (en) * 1983-12-14 1986-07-01 Atlantic Richfield Company Method and apparatus for production of a metal from metallic oxide ore
US20190211460A1 (en) * 2018-01-11 2019-07-11 Consolidated Nuclear Security, LLC Methods and systems for producing a metal chloride or the like
US10704152B2 (en) * 2018-01-11 2020-07-07 Consolidated Nuclear Security, LLC Methods and systems for producing a metal chloride or the like
KR20200130526A (en) * 2019-05-08 2020-11-19 한국생산기술연구원 Method of controlling impurity of indium metal by electrolytic refining of molten salt

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