Introduction

The appearance of 131Cs implants at the radiopharmaceutical market and its clinical use in brachytherapy has made a breakthrough in prostate cancer treatment. The repopulation rate of the prostate cancer cells is 1.5 % a day, and it doubles in 67 days. The absorption of 90 % of radiation doze by cancer cells will require three half-life periods of radionuclides. Therefore, the destruction rate of cancer cells by 131Cs (T 1/2 = 9.6 days) is essentially higher than repopulation rate, and practically does not give a chance for their survival, as opposed to 103Pd (17 days) and 125I (59.9 days) [1, 2].

To obtain 131Cs, the most useful nuclear reaction with thermal neutrons is [3]:

$$ ^{130}{\text{Ba }}(n,{{\upgamma}})^{131}{\text{Ba}} \to^{131}{\text{Cs}} $$
(1)

Parent radionuclide 131Ba with T 1/2 = 11.8 days decays to daughter radionuclide 131Cs which decays to stable 131Xe.

In Table 1, nuclear-physical characteristics and radioactivity values of radionuclides at the irradiation of 1 gram of natural barium by a thermal neutron flux of 3.5 × 1013 cm−2 s−1 for 5 days on (n, γ) reaction are shown [7, 8].

Table 1 Nuclear-physical characteristics of the Ba radionuclides produced by (n, γ) reaction [7, 8]

As shown in Table 1, radioactivity yield is only 4.38 × 108 Bq 131Ba, since the nuclear reaction is limited by the low-abundance isotope of the 130Ba (0.1 %). The discharge of 131Cs essentially leads to the separation of some tens of nanograms of 131Cs from very high amount of highly-active barium radionuclides [4, 5].

In scientific literature and patents, some radiochemical methods of extraction of 131Cs from irradiated BaCO3, Ba(NO3)2 are described [37]. And also there are the studies of mutual extraction of cesium and barium radionuclides from the radioactive wastes by calcium alginate beads [9].

In our case, barium oxide has been taken as a target material, since a percent share of natural barium in compounds consists of 89.5 % in BaO, 52 % in Ba(NO3)2, 69 % in BaCO3 and 65 % in BaCl2·2H2O. Therefore, irradiation of BaO yields a higher radioactivity of 131Ba than irradiation with identical mass of Ba compounds.

The reason why barium oxide has not been used as a target material is the long irradiation of large amounts of BaO at the nuclear reactor for 5–7 days which leads to some structural changes. As a result, the further process of solution becomes very difficult at heating and takes a long time in acid medium.

From this point of view, the process of dissolution of a sparingly-soluble radioactive samples under influence of microwave radiation represents scientific and practical interest.

The microwave chemistry was formed in 1980 at a joint of physics and chemistry. It studies chemical processes in solid and liquid materials, connected with the use of energy of the microwave radiation [10]. Therefore, different compounds convert microwave radiation to heat by different amounts.

The aim of this work was to study the solubility dependence of irradiated barium oxide on various concentration of a hydrochloric acid under influence of microwave radiation.

Experimental

As a source of MWR, a normal domestic MWR oven was used, with following technical parameters: model—NIKAI® NMO-517; voltage of 220-240 Volt at 50 Hz; MWR power of 120–700 W at operating frequency 2.450 GHz.

For dissolution of irradiated samples in a microwave oven, the special vessel and auxiliary accessories were made of Teflon material (a cup, a lid, a mixer and a holder). It is known that at the certain frequency and temperature the dielectric material and solution have different capacities of absorption of microwave radiation and various abilities to convert it in thermal energy, which is characterized by the concept of a dissipation coefficient. At frequency 2.450 GHz and temperature 25 °C, the value of dissipation coefficient varies 1,000 times depending of the compound material. For example, dissipation coefficient is equal to 157 for water, and it is ≪1 for Teflon [10].

In Fig. 1, the schematic view of experimental MWR oven for dissolution of the irradiated samples is shown.

Fig. 1
figure 1

Schematic view of MWR oven and Teflon accessories for dissolution of irradiated samples. 1 microwave oven, 2 rotary quarts plate, 3 cup for radioactive solution, 4 lid, 5 mixer, 6 mixer holder

As shown in Fig. 1, in MWR oven (1) on the center of a quartz plate (2) a cup with a solution of irradiated BaO in a hydrochloric acid (3) is fixed. The mixer (5) is installed into the solution and closed by a lid (4), the end of mixer is fastened to the motionless holder (6). The mixing process of baric solution is carried out by rotating the cup with quartz plate, while mixer is fixed.

The studied barium oxide (m Ba = 20 g) is sealed in quartz vessel and is located in aluminum block-containers. It is irradiated at a thermal neutron flux of 5 × 1013 cm−2 s−1 for 5 days, at the WWR SM reactor of INP AS RUz. The irradiated samples of BaO were aged for 10 days for the maximal accumulation of radioactivity of 131Cs and decay of radionuclides with T 1/2 < 1 days.

Results and discussions

To determine optimum power of MWR and necessary time for a full dissolution of the radioactive BaO, the sample of BaO, weighing 3 g, in stehiometric quantity (14 mL) 1 M HCl was taken, and its dissolution at five various power levels of MWR was carried out. In Fig. 2, the dependence of dissolution of irradiated BaO on the power of MWR oven was shown. At 120 and 230 W, 50 and 75 % dissolution of BaO in 1 M HCl were observed, respectively. The full dissolution of BaO was occurred at 385 W in 150 s, and the further increase in MWR power did not give desirable effect. The growth of power of MWR leads to change of color solution.

Fig. 2
figure 2

Dependence of dissolution of irradiated BaO on power of MWR

At 540 W, the solution gets white-yellow coloration and then, at 700 W, becomes dark yellow. As it is shown in Fig. 2, for full dissolution of irradiated BaO, an optimal power of MWR is 385 W.

The study of influence of the hydrochloric acid concentration on solubility of irradiated BaO showed that the increase of HCl concentration from 1 to 5 M reduces the dissolution time from 150 to 60 s (Fig. 3). However, dissolution of BaO in strongly concentrated mediums is undesirable, since the release of radioactive solution from the cups to the MWR oven occurs.

Fig. 3
figure 3

Dependence of dissolution time of irradiated BaO on concentrations of HCl

The times of the full dissolution of the radioactive samples were established, as at the usual and MWR heating, the results are shown in Fig. 4.

Fig. 4
figure 4

Dependence of dissolution of an irradiated BaO on heating time for: 1 microwave and 2 electric ovens

It is established that at usual heating on the electric oven the full dissolution of BaO occurs in ≥20 min, and at MWR heating it occurs in ≤2.5 min. Besides, at dissolution under the influence of MWR, strictly a stoichiometric volume of hydrochloric acid is used, which leads to the decrease of the volumes of highly radioactive solutions and of the reprocessing time of irradiated samples. Therefore, the technological process of obtain 131Cs is simplified as well.

After a full dissolution of the BaO, 131Cs is extracted by adding of 1 M Na2CO3 solution to sedimentation ions of Ba2+, as a carbonate form, in the alkalescent medium according to reaction:

$$ {\text{BaCl}}_{ 2} + {\text{Na}}_{ 2} {\text{CO}}_{ 3} \to {\text{BaCO}}_{ 3} + {\text{ 2NaCl}} $$
(2)

The obtained solution of 131Cs was extracted from the precipitate of BaCO3 by filtration and was rinsed with 0.1 M ammonium hydrate solution. The traces of barium ions in the filtrate were removed with the addition of 3–5 mL 5 M H2SO4 solution for precipitation in barium sulfate form. Because the 131Cs (T 1/2 = 9.6 days) is daughter radionuclide of the 131Ba (T 1/2 = 11.8 days), the equilibrium radioactivity between 131Ba and 131Cs is established in 10–15 days. In our experiments, four cycles of branching of 131Cs from 131Ba or the “milking” process were held every 10 days by dissolution of the precipitate of BaCO3 in hydrochloric acid each time.

Radionuclidic purity

The radionuclidic purity of 131Cs product and its radiochemical yield were investigated by gamma-ray spectrometry using HPGe and Si(Li) detectors from CANBERRA (USA) after each cycle of separation of the 131Cs from barium solution. When analyzing at the X-ray Spectrometer (Si(Li) detector), only two lines of Cs → Xe transitions 29.67 and 33.61 keV were recognized. The measurements of the background and solution radioactivity were carried out on HPGe detector in 600–4000 s.

The activity value of the radionuclide was determined by the formula:

$$ A \, = \, s \cdot k_{1} \cdot k_{2} /t_{\text{ms}} \cdot \alpha_{\text{eff}} \cdot \eta_{\gamma } $$
(3)

where A radionuclide activity, Bq; s peak area, imp; k 1 correction on geometry of measurements; k 2 correction on aliquot; t ms measuring time activity, s; α eff registration efficiency of detectors for gamma and X-ray radiations, relative unit; η γ intensity of gamma and X-ray radiations, relative unit. The root-mean-square error of this method is no more than ± 10 %.

In Table 2, the results of radionuclide activity measurements are presented on four cycles of separation of the 131Cs at a rate per 1 g of barium.

Table 2 The radionuclidic purity of the 131Cs solutions

As shown in Table 2, the radionuclide 124Sb is presented in all cycles of separations. Apparently, it may be explained by the presence of natural antimony in basic samples of BaO. Its contents in cesium solutions were determined by relative method in an interval 2.5 × 10−8–8.7 × 10−7 g/g. The percent ratio of radioactivity of the 124Sb/131Cs in the 1th–4th cycles of extractions was 0.028, 0.023, 0.0064 and 0.0052 %, respectively. In all cesium solutions, 132Cs has been found only at the first cycle of extraction and its contribution to the 131Cs activity accounted to 0.012 %. The contribution of the parent radionuclide 131Ba to the 131Cs solutions was on the average 0.0067 %.

Conclusion

Thus, the use of the MWR accelerates the dissolution process of the radioactive sample, almost an order of magnitude compared to the heat of electric oven, and takes ≤2.5 min at 385 W and at concentration 1 M HCl, which considerably simplifies technological process. The increase of solution concentrations from 1 to 5 M HCl also leads to the reduction of dissolution time from 150 to 60 s of irradiated BaO.

Radiochemical purity of the 131Cs product was determined to be about 99.97 %. The percentage relations of impurity activities to 131Cs product were 124Sb/131Cs −0.015 %; 132Cs/131Cs −0.012 % and 131Ba/131Cs−0.0067 %.

This work was supported by A11-FA-F131 Grant of Committee for coordination of science and technology development under the Cabinet of Ministers of Uzbekistan.