|
Return to ion beam page | Return to top index |
|
| The following information is taken from Oak Ridge National Laboratory publication, ORNL-3301," PREPARATION OF CHARGE MATERIALS FOR ORNL ELECTROMAGNETIC ISOTOPE SEPARATORS " C. W. Sheridan, H. R. Gwinn, and L. O. Love, issued July 19, 1962, by Oak Ridge National Laboratory, then operated by Union Carbide Corporation for the U.S. Atomic Energy Commission. Some of the information below is useful in the preparation of charge materials for the Colutron ion sources. The sole intent of its publication is to provide our customers with a database of possible charge materials and techniques to prepare charges for the Colutron ion source. Numerous papers have been published in scientific journals since the 1960's using Colutron ion sources and should also be consulted concerning charge preparation techniques. Colutron Research assumes no liability in the accuracy of this information or to damage to equipment or injury to personnel concerning the use of these materials. | |
| note: |
The ORNL isotope separators used Calutron
beam sources.
These are not to be confused with the Colutron ion source. |
| [A] [B] [C] [D] [E] [G] [H] [I] [L] [M] [N] [O] [P] [R] [S] [T] [V] [Y] [Z] |
| PALLADIUM [Pd] |
|
|
Natural Abundance, Stable Isobars
Pd102, 0.96%, Ru102 Pd104, 10.97%, Ru106 Pd105, 22.2%, Cd106 Pd106, 27.3%, Cd108 Pd108, 26.7%, Cd110 Pd110, 11.8% Powdered palladium metal is the only charge material which has been used in the separation of palladium isotopes. The metal is used in a special graphite source block which is heated by electron bombardment. Because of the high cost of Pd, unresolved charge material is recycled and recovered. The source, receiver, and liner are washed in nitric acid and the solution is filtered and evaporated to a small volume. Concentrated hydrochloric acid is added in sufficient quantity to combine with the nitric acid present to form aqua regia, and the solution is evaporated to dryness forming palladium dichloride. Solids removed in the filtration are combined with the graphite salvage and ignited in oxygen. The ash produced is leached with aqua regia until all the Pd is dissolved. Combined leach solutions are evaporated to dryness yielding palladium dichloride. The palladium dichloride solids are combined and treated with concentrated ammonium hydroxide until they are completely dissolved. This forms a solution of tetramminepolladous chloride which, when acidified with hydrochloric acid, precipitates the yellow dichlorodiammine palladium. The precipitate is removed by filtering, and the filtrate is treated with an alcoholic solution of dimethylglyoxime to recover traces of palladium not precipitated as the dichlorodiammine. The dimethylglyoxime precipitate is filtered, washed with alcohol, and transferred to a beaker where it is digested with nitric acid. When the precipitate is dissolved, ammonium hydroxide is added until the solution is basic. The solution is then acidified with formic acid and digested to precipitate elemental Pd. The yellow dichlorodiammine palladium from the first precipitation is transferred to a crucible and thermally decomposed to the element, which will contain a small amount of blue palladium oxide. This mixture is combined with the metal from the formic acid reduction and digested with formic acid to insure that all the palladium is in the elemental form. The product is dried at 110° C and stored for future use. Palladium and its compounds are not considered toxic. |
|
| PLATINUM [Pt] |
|
|
Natural Abundance, Stable Isobars
aPt190, 0.0127%, Os190 Pt192, 0.78%, Os192 Pt194, 32.9%, Hg196 Pt195, 33.8%, Hg198 Pt196, 25.2% Pt198, 7.19% Platinum metal and platinum dicarbonyl dichloride have been used as charge material in the separation of platinum isotopes. It was found that platinum dicarbonyl dichloride decomposes under operating conditions of the calutron making it unsatisfactory for use as a feed material. Platinum metal is used in a special graphite source block which is heated by electron bombardment. Due to the high cost of Pt, the unresolved charge material is recycled and recovered. Approximately 90% of the un-ionized feed can be recovered from the charge container by mechanical means. The remainder is recovered by washing calutron components and by igniting graphite salvage. The source, receiver, and liner are washed with nitric acid. After filtering, the wash solution is evaporated to dryness and analyzed for Pt. Usually no Pt is detected in the filtrate and it is discarded. The solids are dried, ignited at 800° C and combined with the ash remaining after all graphite salvage has been burned. Solids from the ignitions are repeatedly leached with aqua regia until no additional Pt is recovered. The remaining solids are dried, reduced with hydrogen at 600° C, and again leached with aqua regia, which yields some additional Pt. The combined aqua regia leach solutions are repeatedly evaporated with hydrochloric acid to remove nitric acid and finally evaporated to dryness yielding chloroplatinic acid. These crystals are dissolved in 1 N hydrochloric acid, filtered, and treated with an excess of ammonium chloride and an equal volume of ethanol, producing the bright yellow salt ammonium chloroplatinate. The insoluble salt is filtered, washed with 20% ammonium chloride, and reduced to metal with hydrogen at 600° C. Spectrographic analysis of the recovered Pt metal indicates only traces of impurity. Unlike salts of the other platinum metals, platinum salts have been known to cause intoxication, wheezing, coughing, irritation of the nose, tightness in the chest, shortness of breath, and cyanosis. To avoid these symptoms, skin contact with these compounds should be minimized, and a chemical respirator should be employed when dusting may be encountered. aPt190, is radioactive with a half-life of 1012 years. |
|
| POTASSIUM [K] |
|
|
Natural Abundance, Stable Isobars
K39, 93.08%, Ar40 aK40, 0.0119%, Ca40 K41, 6.91% Potassium chloride, potassium bromide, potassium iodide, and massive potassium metal have been used as charge material in the separation of the isotopes of potassium. In earlier separations using a low temperature source unit, heat limitations confined the choice of charge material to potassium iodide and potassium metal. Since development of the medium temperature source unit, M-16, any of the above materials can be used satisfactorily; however, experience has established fused KCl as the best charge material. The usual charge consists of 120 g KCl in a style S-16 stainless steel charge bottle. Potassium chloride usually is obtained from commercial sources and requires no special processing prior to use. One special charge, which had been enriched in K40 by reactor irradiation, was received as a KCl solution containing 0.19% K40 and was prepared for the calutron by precipitating the perchlorate and carefully decomposing it to KCl at 650° C. Although unresolved potassium charge material is not usually recycled and recovered, this procedure is used with enriched feed materials. The calutron components are washed with dilute hydrochloric acid. The wash solution is filtered to remove solids, and these solids are washed and discarded. Hydrogen sulfide is then passed through the filtered wash solution for 30 min. After settling, the precipitate is separated by decanting and washed with three portions of dilute hydrochloric acid saturated with hydrogen sulfide. The precipitate is filtered on paper, washed, and discarded. The combined filtrates and wash solutions are adjusted with ammonium hydroxide to a pH of 9.0 and saturated with hydrogen sulfide. Again the precipitate is washed by decantation, filtered, and discarded. The solution is then acidified with hydrochloric acid and boiled to agglomerate sulfur, which is removed by filtration, washed, and discarded. Dilute barium chloride solution is added to remove any sulfate which forms by air oxidation of the sulfide. Excess barium is removed by the addition of ammonium carbonate. Both barium sulfate and barium carbonate precipitates are removed by filtration, washed, and discarded. The solution is then evaporated to incipient dryness, and the ammonium salts destroyed by digestion with aqua regia. It is imperative to destroy all ammonium salts in order to prevent the formation of potentially explosive ammonium perchlorate later in the process. After removal of ammonium salts, the solution is evaporated to dryness. The potassium salt is dissolved in water and filtered to remove any insolubles, and these insolubles are washed and discarded. The filtered solution is concentrated by evaporation and cooled before adding an excess of perchloric acid. The mixture is chilled in a refrigerator and, while still cold, is filtered through a sintered glass funnel. The potassium perchlorate precipitate is transferred to a quartz dish, covered with a platinum lid, and slowly heated to 650° C. Decomposition begins in the 400° to 450° C range at which time the potassium perchlorate liquefies and has a tendency to spatter and creep. After ignition, the KCl is cooled, dissolved in water, and filtered to remove a small amount of silica leached from the quartz dish. The filtered solution of KCl is then evaporated to dryness in a Pyrex beaker, heated to 300° C, cooled, and stored in sealed bottles. Although the industrial hazards pertaining to potassium and its compounds are few, the oxide and hydroxide are extremely caustic and will cause burns on the skin. Since potassium metal is pyrophoric, heat and all oxidizing conditions should be avoided. The greatest potential hazard in the above method of potassium recovery is the use of perchloric acid. This acid, plus heat and in the presence of ammonium salts or readily oxidizable substances such as organics, can cause violent explosive conditions. Safety precautions for the handling of potassium and its compounds include the use of safety glasses or face shields, rubber gloves, and respirators, particularly if dusting occurs. aK40 is radioactive with a half-life of 1.3 x 109 years. |
|
| RHENIUM [Re] |
|
|
Natural Abundance, Stable Isobars
Re185, 37.07%, Os187 Re187, 62.93% Rhenium heptoxide and rhenium pentachloride have been used as charge material in the separation of the isotopes of rhenium. Both compounds can be used; however, Re2O7 is preferred since the charge consumption rate is lower. The usual charge consists of 150 g Re2O7 in a style S-12 stainless steel charge bottle. Rhenium heptoxide is prepared by burning the powdered metal in oxygen. The metal ignites at about 400° C and burns violently until conversion to rhenium trioxide is complete. Additional heat and oxygen serves to complete the oxidation to the yellow Re2O7. All equipment used for the conversion must be extremely clean and dry since any organic matter will reduce Re2O7 to a lower oxide, and moisture will hydrolyze the oxide to perrhenic acid. The flow rate of oxygen must be carefully controlled since too rapid a flow will carry Re2O7 through the exhaust traps in the form of a white smoke. Too low a flow rate, combined with the rapid burning of rhenium metal, may create a partial vacuum within the reactor causing the exhaust trap solution to flow into the reactor. The reactor used for the preparation of Re2O7 consists of a Pyrex tube 7.6 cm in diameter by 50 cm in length having a large ball joint on each end. A gas-washing bottle containing concentrated sulfuric acid is attached to the inlet end of the reactor. The exhaust end of the reactor is attached to a U-trop with the lower two-thirds of the trap immersed in a cold-bath of carbon tetrachloride and dry ice. Following the cold trap and connected by ball-and-socket joints are, in order, an empty trap, a sulfuric acid trap, another empty trap, and an ammonium hydroxide trap. The entire apparatus is fabricated of glass and is held together with clamps. An electric tube furnace 45 cm in length is used to heat the reactor. Approximately 125 g powdered rhenium metal contained in a Pyrex boat is inserted into the reactor. | |