4th International Nuclear Chemistry Congress, Maresias, San Paulo-Brazil, September 14 - 19, 2014 Recovery of Actinium-225 and Radium-223 from Natural Thorium Irradiated with Protons Elena.V. LAPSHINA, Stanislav V. ERMOLAEV, Boris L. ZHUIKOV, Aleksandr N. VASILIEV, Valentina S. OSTAPENKO, Ramiz A. ALIEV, Stepan N. KALMYKOV Institute for Nuclear Research of Russian Academy of Sciences (Moscow, Russia) Lomonosov Moscow State University, Chemistry Department (Moscow, Russia) 225Ac and 223Ra Properties Attractive for Nuclear Medicine q α-Particles have high linear energy transfer (up to 100 keV/µm) and a short pathlength (about 50-100 µm) in comparison with particles q 225Ac and 223Ra emit four α-particles each in the decay chains providing a higher impact to tumor cells q Intermediate half-lives of 225Ac and 223Ra (10.0 d and 11.4 d, respectively) are suitable for manufacturing and therapeutic treatment q 225Ac and 223Ra may be also used as generators of the short-lived isotopes: 225Ac→213Bi (T1/2=46 min) and 223Ra→211Pb (T1/2=36 min) providing α-particles Slide 2 High intensity linear accelerator Isotope production facility Slide 3 Main Nuclear Reactions Resulting in 225Ac and 227Ac 226Pa 227Pa 228Pa 229Pa 230Pa 231Pa 232Pa 233Pa 225Th 226Th 227Th 228Th 229Th 230Th 231Th 232Th 224Ac 225Ac 226Ac 227Ac 228Ac 229Ac 230Ac 231Ac Proton Energy up to 141 MeV INR Accelerator Capacity for One 10-day Irradiation Run : 223Ra 224Ra 225Ra 226Ra 227Ra 228Ra 225Ac 229Ra 230Ra 225Ac Activity 2.6 Ci Impurity 0.2 % Decay after EOB 10 days (225Ac) 227Ac 227Ac (chemically inseparable impurity) 232Th (p, x) 225Ac 232Th (p, p7n) 225Th (8 min, EC, 10%) → 225Ac 232Th (p, 4n) 229Pa (1.4 d, α, 0.48%) → 225Ac 232Th (p, x) 225Ra (14.8 d, β-, 100%) → 225Ac 232Th (p, x) 227Ac Slide 4 Main Nuclear Reactions Resulting in 223Ra and 224Ra 226Pa 227Pa 228Pa 229Pa 230Pa 231Pa 232Pa 233Pa 225Th 226Th 227Th 228Th 229Th 230Th 231Th 232Th 224Ac 225Ac 226Ac 227Ac 228Ac 229Ac 230Ac 231Ac Proton Energy up to 141 MeV INR Accelerator Capacity for One 10-day Irradiation Run : 223Ra 223Ra 224Ra 225Ra 226Ra 227Ra 223Ra 232Th (p, p5n) 227Th 232Th (p, 6n) 227Pa 227Th 228Ra 229Ra 230Ra Activity 4.5 Ci 224Ra Impurity 16 % Decay after EOB 16 days (223Ra) 224Ra (chemically inseparable impurity) 232Th (38 min, EC, 15%) → 227Th (18.7 d, α, 100%) → 223Ra (p, p4n) 228Th 232Th (p, 5n) 228Pa (22 h, EC, 98%) → 228Th 232Th (p, x) 228Ac (6.1 h, β-, 100%) → 228Th 228Th (1.91 a, α, 100%) → 224Ra (3.7 d) Slide 5 Scheme of 223Ra Production via 227Th 10 Irradiation Decay Activity, Ci 8 Optimal decay time 227Th 6 223Ra 4 2 228Th 224Ra 0 0 5 10 15 20 25 30 35 40 45 50 Time, days Slide 6 225Ac and 223Ra separation from irradiated 232Th Irradiated thorium target Organic phase Th, Pa, Ru, Zr, Nb… Accumulation 223Ra from 227Th DGA Thorium Separation by extraction with tributyl phosphate (TBP), or di(2-ethylhexyl)orthophosphoric acid (HDEHP) dissolved in toluene Water phase Ac, Ra, Ba, Sb, Ce… Dissolution in 6 М HNO3 with addition of 4*10-3 M HF Radionuclide separation on DGA Resin (N,N,N,,N,-tetroctyldiglicol amide) Eluate 4 M HNO3, Ra, Ba, Cs… Purification of Ra fraction Ra - II Ra - I Desorbate 0,01 M HNO3 Ac, La, Ce Ac purification on TRU Resin (octylphenyl-N,N-diisobutylcarbomoylphoshine oxide) Ac-225 Slide 7 225Ac: Isolation and Purification by Extraction Chromatography DGA Resin TRU Resin Ac Sorption – 6 М HNO3 90 Sorption and Desorption – 2 М HNO3 Desorption – 0,01 М HNO3 80 70 La Аctivity, % 60 Ce 50 40 30 Column: d=0.35cm, h=8 cm V(TRU Resin)= 0.17 ml/min 20 10 0 25 65 105 115 125 127 129 131 133 135 137 V, ml Slide 8 223Ra (I): Re-extraction from Organic Phase and Purification TBP n, % Re-extractio 100 100 HCl 90 HNO3 90 80 80 70 70 60 60 50 50 40 40 30 30 20 20 10 10 0 9 Ce Th Pa 7 I Ru 0 9 Ce 5 Zr Nb Water fraction Ra > 99% Ru, I < 1% - may be removed by evaporation with HClO4 HDEHP Th Pa 7 I Ru 5 Zr Nb Acidity, mole/L Organic fraction Ce, Nb, Zr, Pa, Th, Ru > 99% Slide 9 223Ra (II): Isolation of Ra from DGA eluate on Dowex-50x8 Column: d=0.8cm, h=7 cm V= 0.5 ml/min 70% H 2O 0,5 M H2SO4 H 2O 2 M HNO3 4 M HNO3 60% Ra 223 50% Cs 136 Cs, Be Ba 140 40% Ru 103 Activity Ra, Ba La 140 Ru, Sb, Te 30% Te 123m Te Be 7 20% Sb 124 La 10% 0% 0 5 10 15 20 25 30 35 40 45 Volume, mL Slide 10 223Ra (II): Distribution Coefficients of Radium and Barium on Sr Resin (dicyclohexano 18-crown-6 derivative in octanol) E. P. Horwitz, R. Chiarizia and M. L. Dietz, Solvent Extr. Ion Exch. 1992, Vol. 10, pp. 313-‐336. Slide 11 223Ra (II): Isolation of Radium on Sr Resin 60% 3 M HNO3 La 50% Ru 40% Activity Column: d=0.8cm, h=7 cm V= 0.6 ml/min Ba 30% Ra 223 20% La 140 Ra Ru 103 10% Ba 140 0% 0 10 Volume, ml15 0,5 М HClO4 60% 20 25 2 М HNO3 La, Ru 50% Activity 5 Ra Ra 223 40% La 140 30% Ru 103 20% 10% 0% 0 5 10 15 20 25 Slide 12 Scheme of 223Ra I. Solu(on HDEHP in toluene (1:1) a6er liquid-‐liquid extrac(on separation II. Solu(on from DGA Resin, 0,01 M HNO3: 223,224Ra, Cs, Ba, La, Sb, Te, Nb, Ag 223,224Ra, Th, Pa, Zr, Nb, Ru Ca(on exchange resin Dowex 50 х 8 Re-‐extrac(on ( a6er 20 days) 223,224Ra, Ru, I 223,224Ra, Ba Sorbent Sr-‐resin Separa(on Ru, I by HClO4 Ra Slide 13 Conclusions q INR accelerator can provide 2.6 Ci of 225Ac and 4.5 Ci of 223Ra during a 10-day irradiation. q Radiochemical procedures for separation 225Ac and 223Ra from spallation and fission products generated in the irradiated thorium target have been developed. q This procedures provide a good chemical yield 80-90% and high radionuclidic purity (99.9%) suitable for medical applications. Slide 14 Acknowledgement The authors are grateful to: q Dr. Steffen Happel and TrisKem International company for providing the samples of extraction chromatography resins q Karpov Institute of Physical Chemistry located in Obninsk for the help in processing thorium targets in hot cells. Slide 15 Thank you for attention! J 16 mg/l Li Be B Al V Cr Mn Co Ni Cu Zn As Sr Ag Cd Sb Cs Ba Tl Pb Bi Th U Вода Water <2 <0,01 6,9 0,68 0,02 <0,1 0,25 <0.02 <0.02 0,15 1,0 <0,2 <0,05 0,045 <0,01 0,023 <0,01 0,14 <0,005 0,12 <0,02 <0,02 <0,002 Acфракция Ac-‐frac(on <2 0,033 5,6 20 0,20 10 3,7 0,15 10 12 53 <0,2 1,7 0,23 0,16 0,11 0,026 3,3 <0,005 18 <0,02 2,0 0,30 17 • Ln Resin M3+ + 3 HY MY3 + 3H+ • TRU Resin M3+ + 3(NO3)- + 3 E M(NO3)3 * E3 • DGA Resin M3+ + 3(NO3)- +3DGA = M(DGA)3 (NO3)3 M4+ + 4(NO3)- +2DGA = M(DGA)2 (NO3) 4 18
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