USH137H - Process for reducing beta activity in uranium - Google Patents

Process for reducing beta activity in uranium Download PDF

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USH137H
USH137H US06/722,023 US72202385A USH137H US H137 H USH137 H US H137H US 72202385 A US72202385 A US 72202385A US H137 H USH137 H US H137H
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uranium
beta
radiation
salt
ingots
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Gifford G. Briggs
Takeo R. Kato
Edward Schonegg
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US Department of Energy
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US Department of Energy
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B60/00Obtaining metals of atomic number 87 or higher, i.e. radioactive metals
    • C22B60/02Obtaining thorium, uranium, or other actinides

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  • This invention relates to the reduction of beta activity in uranium, and more specifically to the reduction of beta emitters from depleted uranium derbies and ingots and from crucibles used in the uranium manufacturing process, and is a result of a contract with the United States Department of Energy.
  • a phenomenon associated with the casting of uranium is that the surfaces of the ingots, after stripping from the molds, exhibit high radiation levels which are many times greater than that emitted from a cut face of the same ingot.
  • This radiation contains alpha particle, beta particle, and gamma components, but it is the strong beta component that is of greatest concern.
  • This beta radiation penetrates several feet of air and constitutes a skin dose hazard.
  • Another phenomenon is the near absence of radiation in derbies newly prepared using magnesiothermic reduction processes. This phenomenon was also noticed and investigated by Spanish workers several years ago in connection with a similar calciothermic reduction of UF 4 to uranium metal, Travesi, et al., The Composition of Solids in the Smoke Released in the Calciothermic Process for the Manufacture of Uranium, Vol. 4, Peaceful Uses of Atomic Energy, 1958 (pp. 93-100). Although newly prepared derbies exhibit little initial radiation, the hazardous beta radiation appears in the derbies in less than a month. The inventors of the subject invention are not aware of methods previously developed to improve safety conditions by reduction of harmful beta activity in the work areas associated with melting and casting ingots.
  • the process of this invention comprises heating uranium containing beta emitters in the presence of a salt selected from the group magnesium fluoride (MgF 2 ), calcium fluoride (CaF 2 ) and mixtures of MgF 2 and CaF 2 to a temperature sufficient to melt all the solids; allowing the liquid salt phase (containing salts MgF 2 , CaF 2 or a mixture of the salts) to separate from and move above the heavier liquid uranium phase; and removing the uranium phase from the salt phase that contains a substantial amount of the beta emitters initially present in the uranium, thus reducing the beta activity in the uranium.
  • a salt selected from the group magnesium fluoride (MgF 2 ), calcium fluoride (CaF 2 ) and mixtures of MgF 2 and CaF 2
  • a mixture of CaF 2 and MgF 2 should be used, the best being a mixture containing between sixteen (16) and seventy-five (75) weight percent of CaF 2 .
  • Separation of the phases is best done by removing the molten uranium from the bottom of the container since most of the beta emitters remain in the upper salt phase.
  • This method of lowering beta emissions provides a considerable improvement in working conditions in the area of melting and casting uranium.
  • Employee exposure to harmful radiation is lessened significantly and administrative time required to rotate personnel at a location of high radiation is eased when radiation is lower making rotation less frequent.
  • a specific advantage of the process if UF 4 is reduced to U using magnesium, is the use of slag liner as a source of MgF 2 . If the reduction is done with calcium, then the CaF 2 slag liner can be used. This is advantageous because slag liner is abundant.
  • a first consideration is the nature of the radiation associated with the casting process.
  • a phenomenon associated with castings of uranium is that the surfaces of the ingots, after stripping from the molds, exhibit high radiation levels which are many times greater than that emitted from a cut face of the same ingot.
  • This radiation contains alpha particle, beta particle, and gamma components, but is the strong beta component that is of greatest concern.
  • This beta radiation penetrates several feet of air and constitutes a skin dose hazard.
  • a feature of the radiation problem encountered in the casting process is that the radioactive daughter product Th 234 largely separates from the bulk of the molten metal and becomes highly concentrated in a thin layer on the surface of the solidified ingot. It is this strong separation of the Th 234 out of uniform solution in the bulk of the metal that gives rise to the high beta field in the air surrounding the ingot. If the minute amount of Th234 had remained uniformly dissolved throughout the volume of the ingot, the radiation problem would not exist. In such a case the Th 234 decays to Pa 234 and this in turn ejects high energy beta particle electrons within the ingot, and the fast moving beta electrons will be stopped by a very thin thickness of the dense uranium. The rapid slowing down of the beta electrons will produce "braking" or bremsstrahlung x-rays which in turn will be largely absorbed before reaching the surface of the ingot.
  • the separated and concentrated Th 234 at the ingot surface constitutes what is called an "unsupported" daughter product activity. (It is "unsupported” because the ratio of daughter Th 234 to parent U 238 atoms in the thin surface layer is many times greater than that corresponding to secular equilibrium between parent and daughter).
  • the specific activity of the surface radiation is greatest immediately after casting at the time that the ingot is stripped from the mold and sawed to remove the top crop. The surface radiation will diminish with time as controlled by the half-life decay time of 24.1 days for Th 234 .
  • the cut faces of the ingot will be lowest in specific activity immediately after casting because the ratio of Th 234 to U 238 atoms within the metal is now less than that corresponding to secular equilibrium.
  • the radiation from a cut face will rise with time in accordance with a 24.1 day half-life as Th234 grows back in to reach the concentration corresponding to secular equilibrium. In about five months the radiation from the ingot surface should die down until it equals that from the cut face.
  • Uranium purified by various methods may exhibit very little initial radioactivity. However, as time passes following purification, the concentrations of daughter products Th 234 and Pa 234 will increase. Secular equilibrium will be essentially reestablished for these two isotopes in about five months. The equilibrium will be reestablished as determined by the half-life decay time of the Th 234 which is 24.1 days. After six half-lives or about 4.7 months, the Th 234 (and Pa 234 ) will have "grown in" to closely approach secular equilibrium. At secular equilibrium, the number of U 238 , Th 234 , and Pa 234 atoms undergoing decay per unit time will have become equal.
  • Th 234 and Pa 234 are very short compared to the half-life of U 238 , the actual concentrations of the two daughter products in the uranium or uranium compound will be very small.
  • the atomic ratios of the U 238 , Th 234 and Pa 234 will be proportional to the ratios of their half-lives. For example, 1400 pounds of uranium (the weight of uranium in what is referred to as a Mark 31B ingot) should contain 9.2 micrograms of Th 234 and 310 micro-micrograms of Pa 234 at secular equilibrium.
  • Th 234 is temporarily reduced in amount by contacting the molten metal with a molten salt phase
  • this general scheme is applied to the casting process.
  • Derbies prepared and stored for a few months before being consumed in casting contain the Th 234 grown back in.
  • the same is true of the recycled solid scrap and briquetted chips which may be included in the total charges going into the cylindrical ingots.
  • a relatively small addition of MgF 2 or a mixture of MgF 2 and CaF 2 to the melting charges in the crucibles is quite effective in scavenging the Th 234 from the molten metal into the molten salt phase, and a mixture of the two fluorides is more effective as a scavenging agent in the casting process than either MgF 2 , or CaF 2 alone.
  • the melting points of pure uranium, MgF 2 , and CaF 2 are respectively 1133° C., 1263° C., and 1380° C.
  • the salt phase probably cannot act as a very efficient scavenging agent until it has melted.
  • the binary system MgF2-CaF 2 contains a deep eutectic melting at about 940° C.
  • the eutectic composition is at 52 wt. % CaF 2 . Any mixture of the two fluorides lying between about 16 and 75 wt. % CaF 2 should begin to melt at 940° C. and be completely molten at the melting point of uranium metal.
  • Th 234 originally present as thorium metal atoms uniformly dissolved in essentially "clean" casting charges becomes largely extracted within a thin surface layer on cast ingots and (2) how a molten salt phase of MgF 2 - CaF 2 can act effectively to scavenge the Th 234 into the salt phase.
  • a possible explanation of (1) is as follows: In vacuum casting there exist low but significant partial pressures of oxygen and nitrogen in the furnace atmosphere. In general, the hot uranium (solid or molten) will react with all gas molecules of 0 2 and N 2 that strike the clean metal surface.
  • the inclusions are lower in density than molten uranium and will tend to liquate upwards to the surface of the melt under the influence of gravity. Probably more important are phase separating mechanisms brought about by interfacial tension forces. If the uranium melt does not strongly "wet" the inclusions, any inclusion that has reached the surface of the melt or which finds itself at the melt-crucible wall interface will tend to remain there and not re-enter the metal phase. In other words the inclusions which carry most of the Th 234 from the melt will form "skull" material floating on the molten metal or will be trapped at the crucible wall.
  • the skull material should consist of only a relatively small amount of the solid uranium oxynitrides (and some uranium carbide). If the small volume of skull material has extracted almost all of the Th 234 , the specific radioactivity (mr/gram or cc) of this material should be very high. Upon pouring, some amount of the skull material will enter the mold to be trapped as a thin layer between the metal and mold surface. The rest will remain on the walls of the crucible.
  • a total of four pounds of the fluorides containing 19 wt. % CaF 2 is added to 1400 pounds of uranium metal (derbies plus recycled scrap metal) in a Mark 31B charge.
  • the salt mixture On heating the charge in the crucible, the salt mixture begins to melt first at 940° C. and is completely melted at a temperature somewhat below the melting point of the uranium.
  • the molten fluorides float on top of the liquid metal. As the metal becomes molten under the vacuum conditions, it is agitated by bubbles of escaping hydrogen that is present in the uranium in minute amounts. This ebullition of the melt helps mix the molten metal and fluorides.
  • uranium oxynitrides As the solid inclusions of uranium oxynitrides form they are taken into the molten fluoride phase by processes involving increased surface tension wetting of the particles by the salt phase and also because the molten fluorides can dissolve the oxynitrides to some extent.
  • the Th 234 at this point is largely contained within the salt phase. Moreover, because the molten salts add considerably to the total volume of skull material, the specific radioactivity (or concentration of the activity) in the skull material is lowered. At pour, some of the skull may enter the mold and be trapped at the surfaces of the freezing ingot, but the Th 234 is far less concentrated in a surface layer on the ingot. Also most of the molten salt skull material remains in the drained crucible. Very little may flow out into the mold because of its relatively low density and because it may be rendered quite viscous by its content of undissolved uranium oxynitride particles.
  • Th 234 which occurs in the manufacture of uranium using magnesio- or calciothermic reduction almost certainly proceeds by a mechanism similar to that discussed above for the casting operation. It is believed that the essential key is that a small content of oxygen must be present as an "impurity" in the reduction process. It must be present in sufficient concentration to react with the Th 234 to form the very stable thorium-oxygen bonds. In the reduction process the oxygen content ultimately ends up as the minor phases MgO and UO 2 in the slag MgF 2 . The derby interior metal contains very little of the oxygen in the form of oxygen in solution or inclusions of UO 2 . In the reduction process the Th 234 forms ThO 2 which is absorbed into the inclusions of UO 2 that are formed simultaneously. The inclusion material is then taken into the MgF 2 slag phase as previously discussed.
  • the magnesium fluoride for the test consisted of the depleted liner material (MgF 2 ) taken from the production supply of milled product.
  • MgF 2 depleted liner material
  • the slag liner was leached with nitric acid, washed and dried before use. This was done to remove most of the uranium which is present in the milled slag as either free metal or uranium oxides.
  • no obvious benefits were detected by leaching the slag liner material.
  • MgF 2 was added as coarser lumps produced by breaking up massive reduction slag with a hammer.
  • Casting with the fluoride addition differed in only one detail. Roughing evacuation of the furnace was done slowly over a period of up to five minutes. This was done to make sure that the mixture of the powdery fluorides would not be partially blown out of the crucibles by the sudden expansion of air entrapped in the powders but later work showed that this precaution was not necessary.
  • the radiation measurements were made on the ingots within a day after casting and usually immediately after stripping from the graphite molds.
  • the readings (mr/hr) are taken using two Ludlum Model Geiger-Muller survey meters. (Model 3 is used in the lower ranges and Model 5 is used for higher ranges).
  • Tables I and II are for similar charges (three derbies plus solid scrap) while Tables III and IV are for charges with three derbies, solid scrap and machine turnings (briquettes).
  • Table V shows the readings obtained on the inside top (2" down) and on the inside bottom of crucibles used in making fluoride additive melts (crucible S 8808 and S 8809). Similar readings were obtained on one crucible (S 8811) used in casting "control" charges.
  • the results show a reduction of 4.6 ⁇ in radiation from the top of the crucible and a 1.13 ⁇ reduction at the bottom of the crucible.
  • the overall reduction is about 2.9 ⁇ .

Abstract

This invention is a method for lowering the beta radiation hazards associated with the casting of uranium. The method reduces the beta radiation emitted from the as-cast surfaces of uranium ingots. The method also reduces the amount of beta radiation emitters retained on the interiors of the crucibles that have been used to melt the uranium charges and which have undergone cleaning in a remote handling facility. The lowering of the radioactivity is done by scavenging the beta emitters from the molten uranium with a molten mixture containing the fluorides of magnesium and calcium. The method provides a means of collection and disposal of the beta emitters in a manner that reduces radiation exposure to operating personnel in the work area where the ingots are cast and processed.

Description

BACKGROUND OF THE INVENTION
This invention relates to the reduction of beta activity in uranium, and more specifically to the reduction of beta emitters from depleted uranium derbies and ingots and from crucibles used in the uranium manufacturing process, and is a result of a contract with the United States Department of Energy.
In the manufacture of uranium a significant amount of radiation is emitted from the surface of newly cast uranium ingots as well as from the interiors of the graphite crucible in which the ingot charges are melted. This is a considerable problem because radiation levels in a casting area can be sufficiently severe to require frequent personnel rotation at work stations where tasks bring workers into proximity with the ingots and crucibles.
A phenomenon associated with the casting of uranium is that the surfaces of the ingots, after stripping from the molds, exhibit high radiation levels which are many times greater than that emitted from a cut face of the same ingot. This radiation contains alpha particle, beta particle, and gamma components, but it is the strong beta component that is of greatest concern. This beta radiation penetrates several feet of air and constitutes a skin dose hazard.
Another phenomenon is the near absence of radiation in derbies newly prepared using magnesiothermic reduction processes. This phenomenon was also noticed and investigated by Spanish workers several years ago in connection with a similar calciothermic reduction of UF4 to uranium metal, Travesi, et al., The Composition of Solids in the Smoke Released in the Calciothermic Process for the Manufacture of Uranium, Vol. 4, Peaceful Uses of Atomic Energy, 1958 (pp. 93-100). Although newly prepared derbies exhibit little initial radiation, the hazardous beta radiation appears in the derbies in less than a month. The inventors of the subject invention are not aware of methods previously developed to improve safety conditions by reduction of harmful beta activity in the work areas associated with melting and casting ingots.
SUMMARY OF THE INVENTION
In view of the above-mentioned problem in uranium manufacturing, it is an object of this invention to provide a process that reduces beta activity in newly cast uranium ingots and the crucibles in which the ingot charges are melted.
It is another object of this invention to improve safety conditions in the uranium manufacturing process.
It is a further object to remove beta emitters from the uranium before it is poured into ingots.
Additional objects, advantages and novel features of the invention will be set forth in part in the description which follows, and in part will become apparent to those skilled in the art upon examination of the following or may be learned by practice of the invention. The objects and advantages of the invention may be realized and attained by means of the instrumentalities and combinations particularly pointed out in the appended claims.
To achieve the foregoing and other objects and in accordance with the purpose of the present invention, as embodied and broadly described herein, the process of this invention comprises heating uranium containing beta emitters in the presence of a salt selected from the group magnesium fluoride (MgF2), calcium fluoride (CaF2) and mixtures of MgF2 and CaF2 to a temperature sufficient to melt all the solids; allowing the liquid salt phase (containing salts MgF2, CaF2 or a mixture of the salts) to separate from and move above the heavier liquid uranium phase; and removing the uranium phase from the salt phase that contains a substantial amount of the beta emitters initially present in the uranium, thus reducing the beta activity in the uranium.
Preferably a mixture of CaF2 and MgF2 should be used, the best being a mixture containing between sixteen (16) and seventy-five (75) weight percent of CaF2. Separation of the phases is best done by removing the molten uranium from the bottom of the container since most of the beta emitters remain in the upper salt phase.
This method of lowering beta emissions provides a considerable improvement in working conditions in the area of melting and casting uranium. Employee exposure to harmful radiation is lessened significantly and administrative time required to rotate personnel at a location of high radiation is eased when radiation is lower making rotation less frequent. A specific advantage of the process, if UF4 is reduced to U using magnesium, is the use of slag liner as a source of MgF2. If the reduction is done with calcium, then the CaF2 slag liner can be used. This is advantageous because slag liner is abundant.
DETAILED DESCRIPTION OF THE INVENTION
A first consideration is the nature of the radiation associated with the casting process.
A phenomenon associated with castings of uranium is that the surfaces of the ingots, after stripping from the molds, exhibit high radiation levels which are many times greater than that emitted from a cut face of the same ingot. This radiation contains alpha particle, beta particle, and gamma components, but is the strong beta component that is of greatest concern. This beta radiation penetrates several feet of air and constitutes a skin dose hazard. We now recognize that the radioactivity stems from the decay daughters of U238 as outlined below: ##EQU1##
In this partial decay scheme, it is the decay of the Pa234 that yields very energetic beta particles (electrons) of 2.28 MEV maximum energy.
A feature of the radiation problem encountered in the casting process is that the radioactive daughter product Th234 largely separates from the bulk of the molten metal and becomes highly concentrated in a thin layer on the surface of the solidified ingot. It is this strong separation of the Th234 out of uniform solution in the bulk of the metal that gives rise to the high beta field in the air surrounding the ingot. If the minute amount of Th234 had remained uniformly dissolved throughout the volume of the ingot, the radiation problem would not exist. In such a case the Th234 decays to Pa234 and this in turn ejects high energy beta particle electrons within the ingot, and the fast moving beta electrons will be stopped by a very thin thickness of the dense uranium. The rapid slowing down of the beta electrons will produce "braking" or bremsstrahlung x-rays which in turn will be largely absorbed before reaching the surface of the ingot.
The separated and concentrated Th234 at the ingot surface constitutes what is called an "unsupported" daughter product activity. (It is "unsupported" because the ratio of daughter Th234 to parent U238 atoms in the thin surface layer is many times greater than that corresponding to secular equilibrium between parent and daughter). The specific activity of the surface radiation is greatest immediately after casting at the time that the ingot is stripped from the mold and sawed to remove the top crop. The surface radiation will diminish with time as controlled by the half-life decay time of 24.1 days for Th234. Conversely, the cut faces of the ingot will be lowest in specific activity immediately after casting because the ratio of Th234 to U238 atoms within the metal is now less than that corresponding to secular equilibrium. The radiation from a cut face will rise with time in accordance with a 24.1 day half-life as Th234 grows back in to reach the concentration corresponding to secular equilibrium. In about five months the radiation from the ingot surface should die down until it equals that from the cut face.
Perhaps the most curious and least well understood feature of the radiation from the ingots is its variation over the ingot surface. Invariably, the highest readings (β+γ) are found at the flat bottoms of the cylindrical ingots where the metal solidifies most rapidly against the mold cup. The readings generally taper off from the bottom to top of the cylindrical surface although this variation may be quite irregular. Radiation readings from the tops of the uncropped ingots tend to be higher than those from the uppermost side surface, but are also quite variable.
Uranium purified by various methods may exhibit very little initial radioactivity. However, as time passes following purification, the concentrations of daughter products Th234 and Pa234 will increase. Secular equilibrium will be essentially reestablished for these two isotopes in about five months. The equilibrium will be reestablished as determined by the half-life decay time of the Th234 which is 24.1 days. After six half-lives or about 4.7 months, the Th234 (and Pa234) will have "grown in" to closely approach secular equilibrium. At secular equilibrium, the number of U238, Th234, and Pa234 atoms undergoing decay per unit time will have become equal. Since the half-lives of Th234 and Pa234 are very short compared to the half-life of U238, the actual concentrations of the two daughter products in the uranium or uranium compound will be very small. The atomic ratios of the U238, Th234 and Pa234 will be proportional to the ratios of their half-lives. For example, 1400 pounds of uranium (the weight of uranium in what is referred to as a Mark 31B ingot) should contain 9.2 micrograms of Th234 and 310 micro-micrograms of Pa234 at secular equilibrium. Because the half-life decay of the uranium isotope U234 is very long, secular equilibrium between this isotope and U238 will not be reestablished for several hundred thousand years. Depleted UF4 that which has been in storage for several years will thus always contain highly radioactive Th234 and Pa234 in secular equilibrium, and these elements will be uniformly distributed throughout the UF4 in solid solution.
The key to the development of successful methods of reducing the radiation associated with the casting process came with the realization that the troublesome daughter product Th234 (and hence also the Pa234) is largely removed temporarily from uranium metal during the bomb reduction process in which the UF4 is reduced to metal by reaction with magnesium. This phenomenon was noticed and investigated by Spanish workers several years ago in connection with the similar calciothermic reduction of UF4 to metal as previously mentioned. In the reduction process, a two-phase liquid-liquid system is produced in which the radioactive daughter products are largely transferred from the liquid uranium phase to the molten MgF2 slag phase. The separation process is quite similar in effect to a single-stage liquid-liquid solvent extraction process. With the realization that Th234 is temporarily reduced in amount by contacting the molten metal with a molten salt phase, this general scheme is applied to the casting process. Derbies prepared and stored for a few months before being consumed in casting contain the Th234 grown back in. The same is true of the recycled solid scrap and briquetted chips which may be included in the total charges going into the cylindrical ingots. A relatively small addition of MgF2 or a mixture of MgF2 and CaF2 to the melting charges in the crucibles is quite effective in scavenging the Th234 from the molten metal into the molten salt phase, and a mixture of the two fluorides is more effective as a scavenging agent in the casting process than either MgF2, or CaF2 alone. The melting points of pure uranium, MgF2, and CaF2 are respectively 1133° C., 1263° C., and 1380° C. Thus, on heating a uranium metal charge with either of the pure fluorides, the fluoride phase will not melt until the uranium metal has been superheated to temperatures well above its melting point. The salt phase probably cannot act as a very efficient scavenging agent until it has melted. However, the binary system MgF2-CaF2 contains a deep eutectic melting at about 940° C. The eutectic composition is at 52 wt. % CaF2. Any mixture of the two fluorides lying between about 16 and 75 wt. % CaF2 should begin to melt at 940° C. and be completely molten at the melting point of uranium metal.
Thought has been given to possible mechanisms to explain in greater detail (1) how Th234 originally present as thorium metal atoms uniformly dissolved in essentially "clean" casting charges becomes largely extracted within a thin surface layer on cast ingots and (2) how a molten salt phase of MgF2 - CaF2 can act effectively to scavenge the Th234 into the salt phase. A possible explanation of (1) is as follows: In vacuum casting there exist low but significant partial pressures of oxygen and nitrogen in the furnace atmosphere. In general, the hot uranium (solid or molten) will react with all gas molecules of 02 and N2 that strike the clean metal surface. As the molecules of air are removed from the furnace atmosphere by reaction with the metal, they will be replenished by back-streaming of air through the pumps since the furnace pressure must remain essentially constant at whatever low pressure the pumps are capable of producing. Neither nitrogen nor oxygen has appreciable solubility in uranium with the result that minute inclusions of solid oxynitride must nucleate and grow within the molten metal. Since thorium forms even more stable chemical bonds with oxygen and nitrogen than does uranium, it is to be expected that a large fraction of the Th234 atoms will form such bonds and be incorporated into the inclusions of the uranium oxynitrides. As the inclusions nucleate and grow in size, they will develop a tendency to leave the metal phase. The inclusions are lower in density than molten uranium and will tend to liquate upwards to the surface of the melt under the influence of gravity. Probably more important are phase separating mechanisms brought about by interfacial tension forces. If the uranium melt does not strongly "wet" the inclusions, any inclusion that has reached the surface of the melt or which finds itself at the melt-crucible wall interface will tend to remain there and not re-enter the metal phase. In other words the inclusions which carry most of the Th234 from the melt will form "skull" material floating on the molten metal or will be trapped at the crucible wall. If the casting charges consist of essentially "clean" metal containing very little slag MgF2 on the derbies, the skull material should consist of only a relatively small amount of the solid uranium oxynitrides (and some uranium carbide). If the small volume of skull material has extracted almost all of the Th234, the specific radioactivity (mr/gram or cc) of this material should be very high. Upon pouring, some amount of the skull material will enter the mold to be trapped as a thin layer between the metal and mold surface. The rest will remain on the walls of the crucible.
A total of four pounds of the fluorides containing 19 wt. % CaF2 is added to 1400 pounds of uranium metal (derbies plus recycled scrap metal) in a Mark 31B charge. On heating the charge in the crucible, the salt mixture begins to melt first at 940° C. and is completely melted at a temperature somewhat below the melting point of the uranium. As the metal begins to melt, the molten fluorides float on top of the liquid metal. As the metal becomes molten under the vacuum conditions, it is agitated by bubbles of escaping hydrogen that is present in the uranium in minute amounts. This ebullition of the melt helps mix the molten metal and fluorides. As the solid inclusions of uranium oxynitrides form they are taken into the molten fluoride phase by processes involving increased surface tension wetting of the particles by the salt phase and also because the molten fluorides can dissolve the oxynitrides to some extent. The Th234 at this point is largely contained within the salt phase. Moreover, because the molten salts add considerably to the total volume of skull material, the specific radioactivity (or concentration of the activity) in the skull material is lowered. At pour, some of the skull may enter the mold and be trapped at the surfaces of the freezing ingot, but the Th234 is far less concentrated in a surface layer on the ingot. Also most of the molten salt skull material remains in the drained crucible. Very little may flow out into the mold because of its relatively low density and because it may be rendered quite viscous by its content of undissolved uranium oxynitride particles.
The addition of the fluorides results in less of the total radioactivity being retained on the interior crucible wall after burnout of the crucibles since the daughter product activity is now diluted in a larger bulk of skull material. Most of this material drops out of the inverted crucible during the burnout to leave less activity on the crucible walls. Thus a greater fraction of the total activity is removed and captured at a separate location where it no longer poses a radiation hazard to operating personnel. Less of the total activity reaches the station where the crucibles are further cleaned manually and, of course, even less remains in the crucibles at the charging station.
The separation of the daughter product Th234 which occurs in the manufacture of uranium using magnesio- or calciothermic reduction almost certainly proceeds by a mechanism similar to that discussed above for the casting operation. It is believed that the essential key is that a small content of oxygen must be present as an "impurity" in the reduction process. It must be present in sufficient concentration to react with the Th234 to form the very stable thorium-oxygen bonds. In the reduction process the oxygen content ultimately ends up as the minor phases MgO and UO2 in the slag MgF2. The derby interior metal contains very little of the oxygen in the form of oxygen in solution or inclusions of UO2. In the reduction process the Th234 forms ThO2 which is absorbed into the inclusions of UO2 that are formed simultaneously. The inclusion material is then taken into the MgF2 slag phase as previously discussed.
EXAMPLE
The magnesium fluoride for the test consisted of the depleted liner material (MgF2) taken from the production supply of milled product. For some tests, the slag liner was leached with nitric acid, washed and dried before use. This was done to remove most of the uranium which is present in the milled slag as either free metal or uranium oxides. In the test work no obvious benefits were detected by leaching the slag liner material. In two test castings, MgF2 was added as coarser lumps produced by breaking up massive reduction slag with a hammer.
About 25 pounds of calcium fluoride from a supply of pure precipitated material was combined with a further quantity of 70 pounds of pure CaF2 was prepared in the laboratory. The laboratory material was precipitated by slurrying technical-grade, bagged, calcium hydroxide in dilute (36%) HF. The precipitated CaF2 was filtered, washed and tray-dried in ovens. The soft cake was pulverized and passed through a 25-mesh screen before use.
The general procedure followed throughout the test program of MgF2 -CaF2 addition was to cast consecutive groups of three ingots, two of which contained the fluoride additions and one of which contained no fluorides. The three ingots thus all would be similar in charge makeup (number of derbies and same type of recycle scrap). The ingot cast without fluoride addition differed in no way from regular production ingots and was considered to be a "control".
Casting with the fluoride addition differed in only one detail. Roughing evacuation of the furnace was done slowly over a period of up to five minutes. This was done to make sure that the mixture of the powdery fluorides would not be partially blown out of the crucibles by the sudden expansion of air entrapped in the powders but later work showed that this precaution was not necessary.
The radiation measurements were made on the ingots within a day after casting and usually immediately after stripping from the graphite molds. The readings (mr/hr) are taken using two Ludlum Model Geiger-Muller survey meters. (Model 3 is used in the lower ranges and Model 5 is used for higher ranges).
During the test work, an effort was made to retain the same two crucibles for repeated use in casting those test ingots containing the added fluorides. Similarly the same crucible was repeatedly used for casting of the "control" ingots. After each use the crucibles (test and control), following burnout, were set out and measured for radioactivity on their interior surfaces.
Some of the results of the tests on 30" long ingots with 10" diameter for both "control" and fluoride added charges are shown in Tables I-IV.
Tables I and II are for similar charges (three derbies plus solid scrap) while Tables III and IV are for charges with three derbies, solid scrap and machine turnings (briquettes).
              TABLE I                                                     
______________________________________                                    
Control Ingots - No Fluorides Added                                       
Charge = 3 Derbies + Solid Scrap                                          
Readings (β + γ), mr/hr                                        
             DISTANCE FROM BOTTOM                                         
                                 TOP                                      
BOTTOM       (Circular Surface)  SUR-                                     
INGOT  SURFACE   3"      12"   20"   27"   FACE                           
______________________________________                                    
3762   1800      1400    1400  1300  650   400                            
3800   1850      1000     700  1400  900   125                            
3827   1800      1200     800  1000   70   600                            
3907   1800      1500    1500  1100   75   500                            
3940   1600      1350    1000   800  200   550                            
4165   1850       350    1150  1100  450   400                            
4207   1500      1200    1100   900   80   150                            
4238    900       600     120   400   60   600                            
4251   1300      1050     650  --    --    600                            
4321   1200       775     725   800   55   250                            
Avg.   1560      1043     915   978  282   418                            
______________________________________                                    
              TABLE II                                                    
______________________________________                                    
Test Ingots - Fluorides Added                                             
19 wt. % CaF.sub.2 /81 wt. % MgF.sub.2 added                              
(4 lbs/1400 lb charge)                                                    
CHARGE = 3 Derbies + Solid Scrap                                          
Readings (β + γ), mr/hr                                        
             DISTANCE FROM BOTTOM                                         
                                 TOP                                      
BOTTOM       (Circular Surface)  SUR-                                     
INGOT  SURFACE   3"      12"   20"   27"   FACE                           
______________________________________                                    
4208   1600      700     500   600   170   400                            
4209   1550      400     850   75    500   750                            
4252   1300      450      90   70    120   500                            
4253   1050      150      40   35    500   140                            
4319   1300       70      50   28     20   400                            
4320   1150       80      30   28     20   400                            
4344    700      500     200   110    80    50                            
Avg.   1236      336     251   135   201   377                            
______________________________________                                    
              TABLE III                                                   
______________________________________                                    
Control Ingots - No Fluorides Added                                       
CHARGE = 3 Derbies, Solid Scrap, Machining Chips                          
Readings (β + γ), mr/hr                                        
                DISTANCE FROM BOTTOM                                      
                                    TOP                                   
IN-   BOTTOM    (Circular Surface)  SUR-                                  
GOT   SURFACE   3"      12"   20"   27"   FACE                            
______________________________________                                    
3468  1200      600     700   --    160   1300                            
3718  1700      1100    750   700   500    60                             
3728  1750      1150    800   700   500   1500                            
3741  1850      1400    1200  1000  150   200                             
4346  1200      800     900   700   120   800                             
4535  1000      600     350   300   150    15*                            
4558  2000      950     750   350   125   250                             
Avg.  1529      943     779   625   244    685**                          
______________________________________                                    
 *Cropped Face                                                            
 **w/o Cropped Face                                                       
              TABLE IV                                                    
______________________________________                                    
Test Ingots - Fluorides Added                                             
19 wt. % CaF.sub.2 /81 wt. % MgF.sub.2 added                              
CHARGE = 3 Derbies, Solid Scrap, Machining Chips                          
Readings (β + γ), mr/hr                                        
             DISTANCE FROM BOTTOM                                         
                                 TOP                                      
BOTTOM       (Circular Surface)  SUR-                                     
INGOT  SURFACE   3"      12"   20"   27"   FACE                           
______________________________________                                    
4221   800       15      14    45    50    50                             
4222   750       75      50    130   400   50                             
4345   600       450     65    55    100   60                             
4533   1000      55      55    30    20     15*                           
4534   850       40      42    30    20     15*                           
4557   550       45      47    20    17    500                            
4624   400       100     50    65    25    500                            
Avg.   707       111     46    54    90     232**                         
______________________________________                                    
 *Cropped Face                                                            
 **w/o Cropped Face                                                       
Most of the radiation measurements were made with the ingot lying horizontally. Readings were taken at the top of the uncropped ingot, in most cases, at four positions along the exposed topside sides, and on the flat bottom. The readings are somewhat subjective and tend to be the values indicated by the maximum deflections of the meter needle.
Comparing the controls with the fluoride additives the following reductions in radiation were observed.
______________________________________                                    
               DISTANCE                                                   
       BOTTOM  FROM BOTTOM     TOP                                        
CHARGE   SURFACE   3"     12"  20"  27"  SURFACE                          
______________________________________                                    
3D, SS   1.3       3.1    3.6  7.2  1.4  1.1                              
3D, SS   2.2       8.5    17   12   2.7  3                                
brix                                                                      
______________________________________                                    
The highest levels of radiation from the Mark 31B ingots are found at the flat bottoms of the ingots where the metal solidifies against the mold cup. There is still no very cogent explanation of this phenomenon. The addition of the fluorides to the melts has not reduced the radiation from these ingot bottoms to a satisfactory degree. At one time it was thought that some of the daughter product activity gathered in the skull material was being spewed out of the crucible during the period of the vigorous metal "boil", and that some of this material was dropping down to the bottoms of the molds where it eventually became trapped against the mold cup by the rapidly freezing metal.
Table V shows the readings obtained on the inside top (2" down) and on the inside bottom of crucibles used in making fluoride additive melts (crucible S 8808 and S 8809). Similar readings were obtained on one crucible (S 8811) used in casting "control" charges.
The results show a reduction of 4.6× in radiation from the top of the crucible and a 1.13× reduction at the bottom of the crucible. The overall reduction is about 2.9×.
              TABLE V                                                     
______________________________________                                    
Radiation Measurements Performed on Crucibles                             
Used for Melting of Mk 31B Charges                                        
Radiation (β + γ) in mr/hr. (After Burnout and Cleaning)       
Crucibles Used with Fluoride Additions                                    
S 8808                     Control                                        
       BOT-  S 8809        S 8811                                         
TOP      TOM     TOP     BOTTOM  TOP   BOTTOM                             
______________________________________                                    
150      600      70      90     800   190                                
140      400     130     170     900   600                                
 300*    700     200     450     700   500                                
110      400     300     700     1000  800                                
 80      500      95     500     900   700                                
250      850     150     550     900   650                                
110      900      600*   700     900   800                                
 95      400     150     500     1200  1000                               
110      650     140     500     750   800                                
140      600     300     800     900   800                                
 90      700     120     700     500   500                                
150      700      90     500     600   500                                
200      750     110     600     850   750                                
                 150     500     800   650                                
                 190     500     700   725                                
                                       600                                
                 150     700     650   1000                               
                 150     700     ?     ?                                  
                 250     500     250   450                                
           250   500       Crucible cracked                               
Avg. 148     627     189   537     782   660                              
______________________________________                                    
 *Note highest "top" radiation readings obtained with additions of 6 lb   
 MgF.sub.2 containing no CaF.sub.2.                                       
As can be seen by these results the beta activity in these cast ingots and crucibles is significantly reduced using the process described. This reduction provides employees involved in melting and casting ingots a much safer work environment and those skilled in the art will become aware of further applications of the process upon study of the claims and specifications.
The foregoing description of a preferred embodiment of the invention has been presented for purposes of illustration and description. It is not intended to be exhaustive or to limit the invention to the precise form disclosed, and obviously many modifications and variations are possible in light of the above teaching. The embodiment was chosen and described in order to best explain the principles of the invention and its practical application to thereby enable others skilled in the art to best utilize the invention in various embodiments and with various modifications as are suited to the particular use contemplated. It is intended that the scope of the invention be defined by the claims appended hereto.

Claims (4)

We claim:
1. A process for reducing beta activity in uranium comprising:
placing uranium containing beta emitters and a salt selected from the group CaF2, MgF2 and mixtures of CaF2 and MgF2 in a container suitable for holding said uranium and said salt in a molten state in a vacuum;
in a vacuum, heating said uranium and said salt to a temperature sufficient to melt said uranium and said salt;
in a vacuum, maintaining said temperature for a time sufficient for a uranium phase and a salt phase containing said beta emitters to separate; and
separating said salt phase containing said beta emitters from said uranium phase yielding uranium having reduced beta activity.
2. The process of claim 1 wherein said salt is a mixture of CaF2 and MgF2 having a composition of from 16 to 75 weight percent CaF2.
3. The process of claim 2 wherein said temperature sufficient to melt said mixture is about 1133° C.
4. The process of claim 2 wherein said salt mixture is intially present in the amount of about 0.29 pounds per 100 pounds of said uranium.
US06/722,023 1985-04-11 1985-04-11 Process for reducing beta activity in uranium Abandoned USH137H (en)

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US6169756B1 (en) * 1997-12-23 2001-01-02 Lucent Technologies Inc. Vertical cavity surface-emitting laser with optical guide and current aperture
US6208680B1 (en) * 1997-12-23 2001-03-27 Lucent Technologies Inc. Optical devices having ZNS/CA-MG-fluoride multi-layered mirrors
US20100073231A1 (en) * 2004-07-12 2010-03-25 Nec Corp. Null-fill antenna, omni antenna, and radio communication equipment
US20140238198A1 (en) * 2013-02-25 2014-08-28 United States Department Of Energy Apparatus and Methods For Purifying Lead

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US2754347A (en) 1944-04-28 1956-07-10 Wroughton Donald Apparatus for refining rare refractory metals
US2758023A (en) 1953-04-24 1956-08-07 David W Bareis Method of purifying liquid fuels of nuclear reactors
US2766110A (en) 1944-03-08 1956-10-09 Meister George Method of refining uranium
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US2766110A (en) 1944-03-08 1956-10-09 Meister George Method of refining uranium
US2754347A (en) 1944-04-28 1956-07-10 Wroughton Donald Apparatus for refining rare refractory metals
US3000726A (en) 1945-11-14 1961-09-19 Frank H Speeding Production of metals
US2758023A (en) 1953-04-24 1956-08-07 David W Bareis Method of purifying liquid fuels of nuclear reactors
US2840464A (en) 1955-05-27 1958-06-24 Richard H Wiswall Method of separating fission products from fused bismuth-containing uranium
US2918366A (en) 1957-04-17 1959-12-22 Archie G Buyers Decontamination of neutron-irradiated reactor fuel

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Title
Travesi, et al. "The Composition of the Solids in the Smoke Released in the Calciothermic Process for the Manufacture of Uranium", in Proceedings of the Second United National International Conference on the Peaceful Uses of Atomic Energy, vol. 4, United Nations Publication, Geneva, 1958, pp. 93-101.

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6169756B1 (en) * 1997-12-23 2001-01-02 Lucent Technologies Inc. Vertical cavity surface-emitting laser with optical guide and current aperture
US6208680B1 (en) * 1997-12-23 2001-03-27 Lucent Technologies Inc. Optical devices having ZNS/CA-MG-fluoride multi-layered mirrors
US20100073231A1 (en) * 2004-07-12 2010-03-25 Nec Corp. Null-fill antenna, omni antenna, and radio communication equipment
US7768452B2 (en) * 2004-07-12 2010-08-03 Nec Corporation Null-fill antenna, omni antenna, and radio communication equipment
US8063821B1 (en) * 2004-07-12 2011-11-22 Nec Corporation Null-fill antenna, omni antenna, and radio communication equipment
US20140238198A1 (en) * 2013-02-25 2014-08-28 United States Department Of Energy Apparatus and Methods For Purifying Lead
US9234258B2 (en) * 2013-02-25 2016-01-12 U.S. Department Of Energy Apparatus and methods for purifying lead

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