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Title: Extraction systems for the study of dubnium

Conference ·
OSTI ID:939487

The chemistry of transactinide elements (Z {ge} 104) is a topic of great interest in current nuclear chemistry research. The chemical systems that can be used in these studies are limited by the short half-lives of the isotopes and the small production rates of atoms per minute or even atoms per week. In the initial investigations, the chemistry used had to be very selective to the periodic group of interest to separate the transactinide atom from all the other unwanted nuclear reaction products, e.g., transfer products. By using the Berkeley Gas-filled Separator (BGS) as a physical pre-separator, we are able concentrate on systems that are selective between the members of the group of interest, because all other interfering products and the beam are being suppressed by the BGS [1]. We are developing suitable extraction systems for the study of element 105, dubnium. For this purpose we have studied the extraction of niobium and tantalum, the lighter homologs of dubnium, from mineral acids with different organophosphorus compounds. All studies were performed online, using short-lived niobium and tantalum produced in the {sup 124}Sn({sup 51}V,5n){sup 170}Ta and {sup 74}Se({sup 18}O,p3n){sup 88}Nb reactions. This allowed for the study of the lighter homologues at metal concentrations of 10{sup -16} M. At these low metal concentrations, the formation of polymeric species is largely prohibited. As seen in Fig. 1, by varying the extractant and the hydrochloric acid concentration from 1 to 11 M, we are able to see a difference in extraction behavior between niobium and tantalum. While the system is suitable for determining chemical differences between the lighter homologues, the extraction of tantalum from hydrochloric acid shows slow kinetics. Figure 2 shows that after 90 seconds of mixing, the system is not in equilibrium. However, experiments indicate that equilibrium is reached faster at higher acid concentrations. We have studied the influence of hydrogen ion concentration on the extraction kinetics. By varying the chloride concentration while holding the hydrogen ion concentration at a low, fixed value, equilibrium can be reached in less than 10 s. Results for different extractants and various aqueous phase compositions will be presented and discussed.

Research Organization:
Lawrence Berkeley National Lab. (LBNL), Berkeley, CA (United States)
Sponsoring Organization:
Nuclear Science Division
DOE Contract Number:
DE-AC02-05CH11231
OSTI ID:
939487
Report Number(s):
LBNL-229E-Ext.-Abs; TRN: US0806798
Resource Relation:
Conference: 3rd International Conference on the Chemistry and Physics of the Transactinide Elements, Davos, Switzerland, September 23-28, 2007
Country of Publication:
United States
Language:
English