1 Actinide stripping by a hydrophilic BTP ligand in aqueous HNO 3 from TODGA containing organic phase. L. Steczek 1 , J. Narbutt 1 , M. Rejnis 1 , P. Moisy 2 , M. Ch. Charbonnel 2 1 Institute of Nuclear Chemistry and Technology, 2 Alternative Energies and Atomic Energy Commission First SACSESS International Workshop: ‘Towards safe and optimised separation processes, a challenge for nuclear scientists’ 22-24.04.2015 Warsaw
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1
Actinide stripping by a hydrophilic BTP ligandin aqueous HNO3 from TODGA containingorganic phase.
L. Steczek1, J. Narbutt1, M. Rejnis1, P. Moisy2, M. Ch. Charbonnel2
1 Institute of Nuclear Chemistry and Technology, 2 Alternative Energies and Atomic Energy Commission
First SACSESS International Workshop: ‘Towards safe and optimised separation processes, a challenge for nuclear
scientists’ 22-24.04.2015 Warsaw
| PAGE 2
Bibliography ‐ Aromatic poly‐N‐dentate ligands
The simplest aromatic poly-N-dentate ligand is 2,2'-bipyridil
Affinity to protonate nitrogen atoms decreases in the order:
> >
| PAGE 3
The Choice of Selected ligand Lipophilic poly-N-nitrogen ligands are broadly studied asselective extractants for separation of long-lived actinides fromirradiated nuclear fuel. In the last years, the research wasfocused on the derivatives of bis-triazinyl pyridine (BTP) whichselectively extract actinides(III) from lanthanides(III) fromaqueous HNO3 solutions to organic solvents. Moreover, selectivestripping of minor actinides can be done also, using a hydrophilicligand, e.g. SO3-Ph-BTP delivered by Technocomm Ltd (UK).
NN
NN N
NN SO3H
SO3HHO
3S
HO3S
HSO3PhBTP
| PAGE 4
Bibliography Complexes of An(III), Ln(III) with HSO3PhBTP
β Cm Euβ1 5,4 5,2
β2 9,3 8
β3 12,2 10,2
Stability constant of An with SO3‐Ph‐BTP ligand ← TRLFS, An3+ forms more stable complexes than Ln3+. Complexes (1:1), (1:2) and (1:3) were observed
Stability constants of Cm and Eu with SO3‐Ph‐BTP ligand; at pH 3 (TRLFS)
Ch.M. Ruff, U. Müllich, A. Geist, P. J. Panak, Dalton Trans., 2012, 41, 14594
Distribution ratio of Am (0.5 M NH4NO3 + HNO3 (pH 1)/ 0.2 M TODGA in kerosene A. Geist et al., Solv. Extr. Ion Exch.,30: 433–444, 2012
0.01
0.1
1
10
100
0 0.002 0.004 0.006 0.008 0.01
DA
m
HSO3PhBTP mol · L-1
| PAGE 5
Liquid‐liquid Extraction of Actinides with TODGA
In certain separation schemes under study (innovative-SANEX)the f-block elements are extracted together from acidic PUREXraffinate to the organic phase using e.g. lipophlilic tri-O-dentateligand, TODGA.
TODGA-2
-1.5-1
-0.50
0.51
1.52
2.5
-1 -0.5 0 0.5 1log
D0
log [HNO3]
Th(IV)Pu(IV)UO2(VI)
0.2 M TODGA
Yuji Sasakia*, Yasuhiro Tsubataa, Yoshihiro Kitatsujia, Yumi, SolventExtraction and Ion Exchange Volume 31, Issue 4, 2013 401-415
| PAGE 6
Principle of the LLE Method
n221
0 ......1 Lβ+Lβ+Lβ=DD
n
An4+ + sTODGA + uNO3- = [An(TODGA)s(NO3)u]4-u
An4+ + uNO3- = [An(NO3)u]4-u
An4+ + kBTP = [An(hsBTP)k]4-4k
hsBTP4- + aH+ = [hsBTP(H+)a]4-a
where hsBTP = SO3PhBTP
u3
su3s
NOTODGAAnNOTODGAAn )(Kex=
kBTPk
k
i
u3unitrate
u
i
0
hsBTPK+NOK+
D
1,
1][1
u
u
u3l
uNOAnAn
NOTODGAAn
1
43 ])([][
])([D0=
D=
| PAGE 7
Method of the determination of the Distribution coefficient