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US2739934A - Electrolytic purification of uranium - Google Patents

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US2739934A
US2739934A US423401A US42340154A US2739934A US 2739934 A US2739934 A US 2739934A US 423401 A US423401 A US 423401A US 42340154 A US42340154 A US 42340154A US 2739934 A US2739934 A US 2739934A
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uranium
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leach liquor
anode
sulfuric acid
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Kunin Robert
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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
    • C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/22—Electrolytic production, recovery or refining of metals by electrolysis of solutions of metals not provided for in groups C25C1/02 - C25C1/20

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  • This invention relates to the recovery of uranium. It relates to a method of concentrating'and purifying uranium values. More particularly, it relates to an electrolytic process wherein uranium, in the form of the uranyl sulfate anionic complex, is separated from other metallic ions present in sulfuric acid leach liquors.
  • the process of this invention comprises passing a direct electric current through an electrolysis cell which is divided by means of two anionic permselective membranes into three compartments; viz., a cathode compartment, an anode compartment, and a center compartment.
  • the cathode compartment contains an aqueous solution of a soluble sulfate salt, such as sodium, potassium or ammonium sulfatepreferably, sodium sulfateand
  • the anode compartment contains an aqueous mineral acidpreferably sulfuric acidand
  • the center compartment contains a sulfuric acid leach liquor in which are dissolved the uranium values together with ions of other metals such as iron, magnesium, or aluminum.
  • the leach liquor can be the unfiltered acid slurry (ore pulp) obtained from the acid digestion of uranium-bearing ore as well as the filtered leach liquor.
  • the uranyl sulfate anionic complex migrates into the anode compartment while the cations of the other metals, present in the leach liquor, remain in the center compartment, as is described in greater detail below. In this way there is effected a separation of the uranium values from the metallic contaminants in leach liquors.
  • the electrolysis cell which is employed can best be understood by a reference to the attached drawing wherein the single figure is a diagrammatical representation of a typical cell which is divided into three compartments by means of two anionic permselective membranes.
  • 1 represents a container which is divided into three compartments, 5, 6, and 7, by two anionic permselective membranes, 2a and 2c, which are described in greater detail below.
  • Compartment 5 is an anode compartment by virtue of the presence there of anode 3, while compartment 6 is a cathode compartment because it contains the cathode 4.
  • the electrodes are connected to a source of electric power not shown.
  • Between the anode compartment 5 and the cathode compartment 6 is the so-called center compartment 7.
  • the cell which is employed in this invention can be varied as to size, shape, volumes of the individual compartments, vents, ports, exits, construction materials, controls, embellishments, means for admitting and removing the contents of the compartments, et cetera, without departing from the spirit of this invention. What is essential is that the cell have three compartments, one a cathode compartment, another an anode compartment, and a center compartment, the anode and cathode compartments being separated from the center compartment by means of the two anionic permselective membranes or diaphragms which contain an anion exchange resin.
  • the permselective membranes which divide the elec- 2,739,934 Patented Mar. 27, 1956 trolysis cellinto the three compartments are essential to the success of this process. They function by allowing anions to pass through them while at the same time preventing the passage through them of cations.
  • the membranes contain anion exchange resins; and it is the presence of the anion exchange resin which imparts the property of permselectivity to the membrane. While the composition of the permselective membranes can vary within reasonable limits, it is important that they contain enough anion exchange resin as to have suitably high conductance when employed in the electrolysis cell.
  • the permselective diaphragms, membranes, or films which have proven to be most suitable for use in this process are those tough and relatively flexible products made by incorporating particles of an anion exchange resin in a film-forming matrix such as polyethylene or a vinyl resin.
  • Such membranes are available commercially and are described in U. S. patent application Serial No. 205,413, now U. S.
  • Patent No. 2,681,319 and the corresponding Canadian patent, No. 493,563, of June 9, 1953.
  • a uranium-bearing, sulfuric acid leach liquor which contains metallic ions in addition to the complex uranium anions is placed in the center compartment of an electrolysis cell such as that one described above.
  • An aqueous solution of a mineral acid preferably sulfuric acidis employed as the anolyte while an aqueous solution of a water-soluble sulfate saltpreferably a sulfate of an alkali metal-is used as the catholyte.
  • the ions in solution tend to migrate to the electrode of opposite sign, but only the anions have complete freedom of migration because of the presence in the cell of the cation-restraining permselective membranes.
  • the negatively charged uranyl sulfate complex ions migrate from the center compartment through the anionic membrane and become concentrated in the anode compartment.
  • Sulfate ions which are free to pass through the two permselective membranes, migrate to the anode compartment also.
  • Oxygen is liberated at the anode.
  • hydrogen is liberated at the cathode and hydroxyl ions are formed in the catho lyte.
  • the uranium values in the resultant anolyte are then recovered. This is done by electrolytic precipitation according to the process described in another of my patent applications, Serial No. 421,667, filed April 7, 1954. Or, the alkaline catholyte is used to neutralize the uraniumbearing acidic anolyte and to precipitate the uranium as an oxide. Then, the precipitated uranium oxide is separated by conventional means such as filtration, decantation, or centrifuging and is ignited to UaOa.
  • the liquid from which the precipitated uranium oxide is removed is essentally a solution of alkali metal sulfate which is then transferred to a cathode compartment of an eleotrolysis cell and is used as the catholyte in subsequent electrolytic separations.
  • the method as described above, is a batch process.
  • the instant invention can be run on LCOIltlllllOllS scale.
  • leach liquor s passed through the center compartment and the uranium alues are removed electrolytically therefrom in a coninuous manner and appear in the anolyte.
  • the uranium-bearing anolyte and the alkaline cathoyte are removed and are mixed.
  • the resultant :olution is fed continuously to the cathode compartment.
  • iulfuric acid is also fed to the anode compartment to -eplace the uranium-bearing anolyte which is removed.
  • Example An electrolysis cell was constructed of polymethyl nethacryl'ate (Plexiglas). It had a cross-sectional area at ten square inches (2" x 5"). The cell had an anode :ompartment and a cathode compartment separated from a. center compartment by means of two anionic permselective membranes (Amberplex A-l) known to contain about 70% anion exchange resin in a matrix of polyethylene and known to have been made according to the process of U. S. patent application Serial No. 205,413, new U. S. Patent No. 2,681,319, and the corresponding Canadian Patent No. 493,563 of June 9, 1953.
  • Amberplex A-l anionic permselective membranes
  • the membrane contained a quaternary ammonium anion exchange resin made by aminating with a tertiary amine an insoluble, cross-linked chloromethylated copolymer of styrene and divinylbenzene.
  • the cell was generally similar to that shown in the drawing with the exception that every one of the three compartments had means for admitting and removing the contents continuously.
  • the electrodes were platinum.
  • Dilute sulfuric acid was employed as the anolyte while a 1.0 N solution of ammonium sulfate was used as the catholyte.
  • a filtered, low-grade Belgian Congo sulfuric acid leach liquor was passed through the center compartment while a direct current of 2-3 amperes was passed through the cell at a potential of 5.5 volts.
  • the ratio of uranium to iron in the leach liquor was 0.85 gram to 1 gram at the outset.
  • the catholyte meanwhile had become very alkaline. This was added to some of the uranium-bearing anolyte and uranium was precipitated as an oxide which was then ignited to UaOs.
  • a process for the separation of uranium values from metallic cations in a sulfuric acid leach liquor of a uranium ore which comprises passing a direct electric current through an electrolysis cell comprising a cathode compartment containing an aqueous solution of a sulfate salt. an anode compartment containing aqueous sulfuric acid, and a center compartment containing said sulfuric acid leach liquor, said cathode and anode compartments being separated from said center compartment by anionic permselective membranes which contain an anion exchange resin, whereby said uranium values migrate into said anode compartment and said metallic cations remain in said center compartment.
  • Aprocess for the isolation of uranium values from a sulfuric acid leach liquor containing said uranium values and metallic cations which comprises electrolyzing said leach liquor while it is contained in the center compartment of an electrolysis cell which has acathode compartment containing a catholyte comprising an aqueous solution of a sulfate salt and separated from said center compartment by an anionic permselective membrane containing an anion-exchange resin, and an anode compartment containing an anolyte comprising aqueous sulfuric acid and separated from said center compartment by an anionic permselective membrane containing an anion exchange resin, whereby said uranium values migrate to said anode compartment while said metallic cations remain in said center compartment, removing the resultant catholyte and the resultant anolyte from said cell and mixing them, thereby precipitating said uranium values, separating said precipitated uranium values and employing the resultant solution as thecatholyte in

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)

Description

March 27, 1956 KUNlN ELECTROLYTIC PURIFICATION OF URANIUM Filed April 15, 1954 Anionic Permselecfive Membrane INVENTOR. ROBERT KUNIN BY m ATTORNE ELECTROLYTIC PURIFICATION OF URANIUM Robert Kunin, Trenton, N. J., assignor, by mesne assignments, to the United States of America as represented by the United States Atomic Energy Commission Application April 15, 1954, Serial No. 423,401
6 Claims. (Cl. 204-96) This invention relates to the recovery of uranium. It relates to a method of concentrating'and purifying uranium values. More particularly, it relates to an electrolytic process wherein uranium, in the form of the uranyl sulfate anionic complex, is separated from other metallic ions present in sulfuric acid leach liquors.
The process of this invention comprises passing a direct electric current through an electrolysis cell which is divided by means of two anionic permselective membranes into three compartments; viz., a cathode compartment, an anode compartment, and a center compartment. At the beginning of the operation of the cell, the cathode compartment contains an aqueous solution of a soluble sulfate salt, such as sodium, potassium or ammonium sulfatepreferably, sodium sulfateand the anode compartment contains an aqueous mineral acidpreferably sulfuric acidand the center compartment contains a sulfuric acid leach liquor in which are dissolved the uranium values together with ions of other metals such as iron, magnesium, or aluminum. The leach liquor can be the unfiltered acid slurry (ore pulp) obtained from the acid digestion of uranium-bearing ore as well as the filtered leach liquor. During electrolysis the uranyl sulfate anionic complex migrates into the anode compartment while the cations of the other metals, present in the leach liquor, remain in the center compartment, as is described in greater detail below. In this way there is effected a separation of the uranium values from the metallic contaminants in leach liquors.
The electrolysis cell which is employed can best be understood by a reference to the attached drawing wherein the single figure is a diagrammatical representation of a typical cell which is divided into three compartments by means of two anionic permselective membranes. In said figure, 1 represents a container which is divided into three compartments, 5, 6, and 7, by two anionic permselective membranes, 2a and 2c, which are described in greater detail below. Compartment 5 is an anode compartment by virtue of the presence there of anode 3, while compartment 6 is a cathode compartment because it contains the cathode 4. When the cell is in operation, the electrodes are connected to a source of electric power not shown. Between the anode compartment 5 and the cathode compartment 6 is the so-called center compartment 7.
The cell which is employed in this invention can be varied as to size, shape, volumes of the individual compartments, vents, ports, exits, construction materials, controls, embellishments, means for admitting and removing the contents of the compartments, et cetera, without departing from the spirit of this invention. What is essential is that the cell have three compartments, one a cathode compartment, another an anode compartment, and a center compartment, the anode and cathode compartments being separated from the center compartment by means of the two anionic permselective membranes or diaphragms which contain an anion exchange resin.
The permselective membranes which divide the elec- 2,739,934 Patented Mar. 27, 1956 trolysis cellinto the three compartments are essential to the success of this process. They function by allowing anions to pass through them while at the same time preventing the passage through them of cations. The membranes contain anion exchange resins; and it is the presence of the anion exchange resin which imparts the property of permselectivity to the membrane. While the composition of the permselective membranes can vary within reasonable limits, it is important that they contain enough anion exchange resin as to have suitably high conductance when employed in the electrolysis cell. The permselective diaphragms, membranes, or films which have proven to be most suitable for use in this process are those tough and relatively flexible products made by incorporating particles of an anion exchange resin in a film-forming matrix such as polyethylene or a vinyl resin. Such membranes are available commercially and are described in U. S. patent application Serial No. 205,413, now U. S.
Patent No. 2,681,319, and the corresponding Canadian patent, No. 493,563, of June 9, 1953.
In the process of this invention a uranium-bearing, sulfuric acid leach liquor which contains metallic ions in addition to the complex uranium anions is placed in the center compartment of an electrolysis cell such as that one described above. An aqueous solution of a mineral acidpreferably sulfuric acidis employed as the anolyte while an aqueous solution of a water-soluble sulfate saltpreferably a sulfate of an alkali metal-is used as the catholyte.
As electrolysis proceeds, the ions in solution tend to migrate to the electrode of opposite sign, but only the anions have complete freedom of migration because of the presence in the cell of the cation-restraining permselective membranes. Thus, the negatively charged uranyl sulfate complex ions migrate from the center compartment through the anionic membrane and become concentrated in the anode compartment. Sulfate ions, which are free to pass through the two permselective membranes, migrate to the anode compartment also. Oxygen is liberated at the anode. At the same time, hydrogen is liberated at the cathode and hydroxyl ions are formed in the catho lyte. While the cations of the other metals which are present as undesirable impurities in the leach liquor tend to migrate from the center compartment into the cathode compartment, they are constrained by the anionic perms selective barrier. The net result is that the catholyte is progressively changed from a solution of an alkali metal sulfate to a solution of an alkali metal hydroxide while the anolyte becomes more concentrated as to sulfuric are liberated and the uranium values are separated from the other contaminating metals and are concentrated in the anolyte.
The uranium values in the resultant anolyte are then recovered. This is done by electrolytic precipitation according to the process described in another of my patent applications, Serial No. 421,667, filed April 7, 1954. Or, the alkaline catholyte is used to neutralize the uraniumbearing acidic anolyte and to precipitate the uranium as an oxide. Then, the precipitated uranium oxide is separated by conventional means such as filtration, decantation, or centrifuging and is ignited to UaOa. The liquid from which the precipitated uranium oxide is removed is essentally a solution of alkali metal sulfate which is then transferred to a cathode compartment of an eleotrolysis cell and is used as the catholyte in subsequent electrolytic separations.
It is, therefore, apparent that by means of this electrolytic process uranium values are separated from contaminated leach liquors in a very efi'icient manner.
The method, as described above, is a batch process.
kctually, however, the instant invention can be run on LCOIltlllllOllS scale. In the continuous process, leach liquor s passed through the center compartment and the uranium alues are removed electrolytically therefrom in a coninuous manner and appear in the anolyte. At the same ime the uranium-bearing anolyte and the alkaline cathoyte are removed and are mixed. After the precipitated .lranium oxide is removed from the mixture, the resultant :olution is fed continuously to the cathode compartment. iulfuric acid is also fed to the anode compartment to -eplace the uranium-bearing anolyte which is removed.
The following example further illustrates the process )f this invention.
Example An electrolysis cell was constructed of polymethyl nethacryl'ate (Plexiglas). It had a cross-sectional area at ten square inches (2" x 5"). The cell had an anode :ompartment and a cathode compartment separated from a. center compartment by means of two anionic permselective membranes (Amberplex A-l) known to contain about 70% anion exchange resin in a matrix of polyethylene and known to have been made according to the process of U. S. patent application Serial No. 205,413, new U. S. Patent No. 2,681,319, and the corresponding Canadian Patent No. 493,563 of June 9, 1953. The membrane contained a quaternary ammonium anion exchange resin made by aminating with a tertiary amine an insoluble, cross-linked chloromethylated copolymer of styrene and divinylbenzene. The cell was generally similar to that shown in the drawing with the exception that every one of the three compartments had means for admitting and removing the contents continuously. The electrodes were platinum. Dilute sulfuric acid was employed as the anolyte while a 1.0 N solution of ammonium sulfate was used as the catholyte. A filtered, low-grade Belgian Congo sulfuric acid leach liquor was passed through the center compartment while a direct current of 2-3 amperes was passed through the cell at a potential of 5.5 volts. The ratio of uranium to iron in the leach liquor was 0.85 gram to 1 gram at the outset. The electrolysis was continued for four hours after which the anolyte was analyzed. It was found that a small amount of iron, presumably as a complex anion, had migrated to the anode compartment together with the uranium values. But, whereas the leach liquor at the outset had contained more iron than uranium (ratio U:Fe=.85 :1), the ratio of the amount of uranium to iron in the anolyte at .the end of the electrolysis was 296 grams to 1 gram. During the period of electrolysis 71% of the uranium was removed from the leach liquor and was concentrated in the anolyte.
The catholyte meanwhile had become very alkaline. This was added to some of the uranium-bearing anolyte and uranium was precipitated as an oxide which was then ignited to UaOs.
It is evident from the above that uranium values in leach liquors are readily separated and concentrated by this process. Essentially the same results are obtained when an unfiltered leach liquor is electrolyzed in the same way. As might be expected, the cost of carrying out the electrolytic process varies inversely with the concentration of the uranium in the leach liquors being electrolyzed. Thus, at an initial concentration of 10.4 grams of uranium per liter, 79% of the uranium is removed from the center compartment to the anode compartment at a cost of 1 kilowatt of electricity per pound of uranium. The cost of removing the next 19% rises to about 4 kilowatts per pound of transported uranium. Nevertheless, the instant process is very efficient and provides a particularly convenient method of separating uranium values from other contaminating metals and of concentrating the uranium values.
I claim:
1. A process for the separation of uranium values from metallic cations in a sulfuric acid leach liquor of a uranium ore which comprises passing a direct electric current through an electrolysis cell comprising a cathode compartment containing an aqueous solution of a sulfate salt. an anode compartment containing aqueous sulfuric acid, and a center compartment containing said sulfuric acid leach liquor, said cathode and anode compartments being separated from said center compartment by anionic permselective membranes which contain an anion exchange resin, whereby said uranium values migrate into said anode compartment and said metallic cations remain in said center compartment.
2. The process of claim 1 in which said aqueous solution of a sulfate salt is a solution of sodium sulfate.
3. The process of claim 1 in which said aqueous solution of a sulfate salt is a solution of ammonium sulfate.
4. Aprocess for the isolation of uranium values from a sulfuric acid leach liquor containing said uranium values and metallic cations which comprises electrolyzing said leach liquor while it is contained in the center compartment of an electrolysis cell which has acathode compartment containing a catholyte comprising an aqueous solution of a sulfate salt and separated from said center compartment by an anionic permselective membrane containing an anion-exchange resin, and an anode compartment containing an anolyte comprising aqueous sulfuric acid and separated from said center compartment by an anionic permselective membrane containing an anion exchange resin, whereby said uranium values migrate to said anode compartment while said metallic cations remain in said center compartment, removing the resultant catholyte and the resultant anolyte from said cell and mixing them, thereby precipitating said uranium values, separating said precipitated uranium values and employing the resultant solution as thecatholyte in subsequent electrolysis of.additional uranium-bearing leach liquor.
5. The process of claim 4 in which the said catholyte comprising an aqueous solution of a sulfate salt is an aqueous solution of sodium sulfate.
6. The process of claim 4 in which the said catholyte comprising an aqueous solution of a sulfate salt. is an aqueous solution of ammonium sulfate.
No references cited.

Claims (1)

1. A PROCESS FOR THE SEPARATION OF URANIUM VALUES FROM METALLIC CATIONS IN A SULFURIC ACID LEACH LIQUOR OF A URANIUM ORE WHICH COMPRISES PASSING A DIRECT ELECTRIC CURRENT THROUGH AN ELECTROLYSIS CELL COMPRISING A CATHODE COMPARTMENT CONTAINING AN AQUEOUS SOLUTION OF A SULFATE SALT, AN ANODE COMPARTMENT CONTAINING AQUEOUS SULFURIC ACID, AND A CENTER COMPARTMENT CONTAINING SAID SULFURIC ACID LEACH LIQUOR, SAID CATHODE AND ANODE COMPARTMENTS BEING
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Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2832727A (en) * 1954-04-07 1958-04-29 Kunin Robert Electrolytic precipitation of uranium from the ion exchange eluates
US3143483A (en) * 1955-06-20 1964-08-04 Commissariat Energie Atomique Methods of extracting uranium from ores containing it
US3265607A (en) * 1960-10-04 1966-08-09 American Mach & Foundry Apparatus for improving the taste of fruit juice by dialysis
US3357823A (en) * 1964-05-08 1967-12-12 Treadwell Corp Recovery of gold, silver, copper and zinc by alkaline cyaniding with electrodialysis
US3433726A (en) * 1962-06-08 1969-03-18 Ionics Method and apparatus for treating liquid milk products
US3450630A (en) * 1963-02-07 1969-06-17 Yeda Res & Dev Method of separating metal ions
US3766038A (en) * 1971-12-15 1973-10-16 Basf Ag Production of cycloalkanone oximes
US4105532A (en) * 1975-01-09 1978-08-08 Parel Societe Anonyme Improvements in or relating to the electrowinning of metals
US4152215A (en) * 1976-11-12 1979-05-01 Matsushita Electric Industrial Co., Ltd. Apparatus for controlling pH of culture solution for a living organism
US4234393A (en) * 1979-04-18 1980-11-18 Amax Inc. Membrane process for separating contaminant anions from aqueous solutions of valuable metal anions
EP0078017A3 (en) * 1981-10-22 1984-04-25 Olympus Optical Co., Ltd. Endoscope apparatus with motor-driven bending mechanism
WO1991001392A1 (en) * 1989-07-21 1991-02-07 Ionex Method of removing ions
US5405509A (en) * 1989-05-08 1995-04-11 Ionex Remediation of a bulk source by electropotential ion transport using a host receptor matrix
US5489370A (en) * 1989-05-08 1996-02-06 Ionex Removal of ions from a bulk source by electropotential ion transport using a host receptor matrix

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2832727A (en) * 1954-04-07 1958-04-29 Kunin Robert Electrolytic precipitation of uranium from the ion exchange eluates
US3143483A (en) * 1955-06-20 1964-08-04 Commissariat Energie Atomique Methods of extracting uranium from ores containing it
US3265607A (en) * 1960-10-04 1966-08-09 American Mach & Foundry Apparatus for improving the taste of fruit juice by dialysis
US3433726A (en) * 1962-06-08 1969-03-18 Ionics Method and apparatus for treating liquid milk products
US3450630A (en) * 1963-02-07 1969-06-17 Yeda Res & Dev Method of separating metal ions
US3357823A (en) * 1964-05-08 1967-12-12 Treadwell Corp Recovery of gold, silver, copper and zinc by alkaline cyaniding with electrodialysis
US3766038A (en) * 1971-12-15 1973-10-16 Basf Ag Production of cycloalkanone oximes
US4105532A (en) * 1975-01-09 1978-08-08 Parel Societe Anonyme Improvements in or relating to the electrowinning of metals
US4152215A (en) * 1976-11-12 1979-05-01 Matsushita Electric Industrial Co., Ltd. Apparatus for controlling pH of culture solution for a living organism
US4234393A (en) * 1979-04-18 1980-11-18 Amax Inc. Membrane process for separating contaminant anions from aqueous solutions of valuable metal anions
EP0078017A3 (en) * 1981-10-22 1984-04-25 Olympus Optical Co., Ltd. Endoscope apparatus with motor-driven bending mechanism
US5405509A (en) * 1989-05-08 1995-04-11 Ionex Remediation of a bulk source by electropotential ion transport using a host receptor matrix
US5489370A (en) * 1989-05-08 1996-02-06 Ionex Removal of ions from a bulk source by electropotential ion transport using a host receptor matrix
WO1991001392A1 (en) * 1989-07-21 1991-02-07 Ionex Method of removing ions

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