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A macroscopic and molecular study for a complete description of technetium (VII) and uranium (VI) co-extraction mechanism with monoamides

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HAL Id: cea-02442334

https://hal-cea.archives-ouvertes.fr/cea-02442334

Submitted on 16 Jan 2020

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A macroscopic and molecular study for a complete

description of technetium (VII) and uranium (VI)

co-extraction mechanism with monoamides

P. Moeyaert, C. Sorel, T. Dumas, D. Guillaumont, M. Miguirditchian, P. Moisy, Jean-François Dufrêche

To cite this version:

P. Moeyaert, C. Sorel, T. Dumas, D. Guillaumont, M. Miguirditchian, et al.. A macroscopic and molecular study for a complete description of technetium (VII) and uranium (VI) co-extraction mech-anism with monoamides. RANC 2016 - The 1st International Conference on Radioanalytical and Nuclear Chemistry, Apr 2016, Budapest, Hungary. �cea-02442334�

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| PAGE 1

RANC 2016

Budapest, April 12th 2016

A MACROSCOPIC AND MOLECULAR

STUDY FOR A COMPLETE DESCRIPTION

OF TECHNETIUM (VII) AND URANIUM (VI)

CO-EXTRACTION MECHANISM WITH

MONOAMIDES

P. Moeyaerta, C. Sorela, T. Dumasa , D. Guillaumonta, M.

Miguirditchiana, Ph. Moisya, J.-F. Dufrêcheb

a CEA Marcoule, DEN / DRCP / SMCS BP 17171

30207 Bagnols sur Cèze, France.

b ICSM BP 17171 30207 Bagnols sur Cèze, France

(3)

CONTEXT

Uox & MOX fuel fabrication Extraction cycles Storage Pu Fuel (Uox, MOX) Enriched U Reprocessed U Irradiated fuel

Irradiated fuel (MOX, URE) Reactors Conversion Enrichment TBP Monoamide

Monoamides for U & Pu extraction …

→ Innovative liquid-liquid extraction processes for the reprocessing of spent nuclear fuels

→ Good stability towards radiolysis and hydrolysis

… But what about fission products extraction?

TBP Natural U

(4)

CONTEXT

Technetium in the PUREX process

99Tc = Long-lived β emitting radionuclide (with a radioactive half-life of 2.1×105 y)

Radionuclide potentially mobile in the environment Present as HTcO4 in nitric acid dissolution solutions

Can cause some issues in the PUREX process if not correctly scrubbed (hydrazine destruction, U & Pu contamination)

Measurements implemented in La Hague plant

Zr, PF SCRUB MAIN EXTRACTION Solvent TBP 30% Tc SCRUB SECONDARY EXTRACTION Solvent TBP 30% U, Pu, Tc Load U, Pu, Zr, Tc HNO33 M HNO32 M HNO31,5 M HNO310 M Tc U, Pu Zr, PF

(5)

CONTEXT

DEHiBA

Towards a new process …

DEHiBA (N,N-di-2-ethylhexyl-isobutyramide) = promising extractant for future processes

Technetium in the PUREX process

99Tc = Long-lived β emitting radionuclide (with a radioactive half-life of 2.1×105 y)

Radionuclide potentially mobile in the environment Present as HTcO4 in nitric acid dissolution solutions

Can cause some issues in the PUREX process if not correctly scrubbed (hydrazine destruction, U & Pu contamination)

(6)

OBJECTIVES & METHODOLOGY

Objectives:

Understanding the mechanisms involved in the extraction of technetium with DEHiBA Modeling technetium extraction

Integrating the model into the CEA PAREX code to improve the modeling of extraction processes and help flowsheets design

Liquid liquid extraction:

Batch experiments, γspectrometry, UV-vis, etc Objectives : D, SF, recovery % Molecular scale Physico-chemical modeling Process modeling Charge M1+ M2 Solution de désextraction Solution de désextraction M1 Raffinat M2 Extractant(s) Diluant RÉGÉNÉRATION EXTRACTION DÉSEXTRACTION Charge M1+ M2 Solution de désextraction Solution de désextraction M1 Raffinat M2 Extractant(s) Diluant RÉGÉNÉRATION EXTRACTION DÉSEXTRACTION Macroscopic scale Modeling:

Solving the mass balance by taking into account deviation from ideal behaviour

Process simulation:

Models integrated into the CEA PAREX code

Speciation of organic complexes:

(7)

Organic phase:

DEHiBA / TPH

Aqueous phase:

H2O HNO3 0.1-6 M UO2(NO3)2 0-120 g.L-1 HTcO4 10-3 M + 99mTc as γ spiker Contact

TECHNETIUM EXTRACTION

EXPERIMENTAL PROTOCOLE

Settling Vortexing 1h at 25°C

- Acid base titration - γ spectrometry

- UV-vis spectrophotometry

- Acid base titration - γ spectrometry

- UV-vis spectrophotometry

99mTc = short-lived γ

emitter (T1/2≈ 6 h) Used as spiker for Tc

(8)

Experimental results

D Tc ⁄ Tc ↗ when Utot

Assumption of the following extraction equilibria:

HTcO iL HTcO L UO NO L jHTcO

UO NO TcO L jHNO

Mass balance equations

Equilibrium constants:

K L! HTcO HTcO L " #$%&' ()

"#$%&'"(̅)

K UO NOL! UO NOTcO L HNOHTcO "+&, -&. ,/0 $%&' 0(,"#-&. 0 "+&, -&. ,"#$%&'0"(̅,

Method:

Free extractant concentration determined by an iterative method based on dichotomy resolution

Calculation of U, Tc, H, H2O concentrations in organic phase

Optimization of the unkown parameter K by an iterative method based on least-squares analysis corresponding to the minimization of:

min 3 4X6 4X67 8 4X69:; 9:;

TECHNETIUM EXTRACTION MODELING

MODELING SPECIES DISTRIBUTION

Mass balance equations

Equilibrium constants:

K L! HTcO HTcO L γ = >? @A

γ= >?γ@B

K UO NOL! UO NOTcO L HNOHTcO γC>γC>D E>F D/G >? G@Dγ=E>F

D E>F Dγ= >? γ@B

Method:

Free extractant concentration determined by an iterative method based on dichotomy resolution

Calculation of U, Tc, H, H2O concentrations in organic phase

Optimization of the unkown parameter K by an iterative method based on least-squares analysis corresponding to the minimization of:

min 3 4X6 4X67 8 4X69:; 9:;

(9)

In aqueous phase: the simple solutions theory

Simple behaviour of isopiestic solutions (Zdanovskii-Stokes-Robinson)

Mikulin equation to calculate activity coefficients

Procedure for binary data acquisition = triplet (Φ, γ, m)

Measurements of water activity aI Osmotic coefficient calculation ϕ 8υmMln aI = >

Activity coefficient of the electrolyte by integrating Gibbs-Duhem equation

lnγ ϕ 8 1 OPϕ 8 1m

Q dm

Fitting according to a semi-empirical equation (ex: NIST, Pitzer, …)

ϕ=f(m)

γ

= >?

υ

= >?

γ

= >S ?

m

= >S ?

υ

= >?

m

= >?

υ

=E>F

m

=E>F

υ

C>D E>F D

m

C>D E>F D

HTcO4

in H2O

TECHNETIUM EXTRACTION MODELING

DEVIATION FROM IDEAL BEHAVIOUR

γ

= >?

υ

= >?

"

#$%&T) '

U

#$%&T) '

υ

= >?

m

= >?

υ

=E>F

m

=E>F

υ

C>D E>F D

m

C>D E>F D

Binary mixture data =f(aw) Real mixture composition

(10)

Procedure for binary data acquisition = triplet (Φ, γ, m) mother solution

n n+2 water n+1

TECHNETIUM EXTRACTION MODELING

DEVIATION FROM IDEAL BEHAVIOUR

In aqueous phase: the simple solutions theory

Simple behaviour of isopiestic solutions (Zdanovskii-Stokes-Robinson)

Mikulin equation to calculate activity coefficients

γ

= >?

υ

= >?

"

#$%&T) '

U

#$%&T) '

υ

= >?

m

= >?

υ

=E>F

m

=E>F

υ

C>D E>F D

m

C>D E>F D

Binary mixture data =f(aw) Real mixture composition

(11)

Boyd, G.E., Inorganic Chemistry, 1978. 17(7): p. 1808-1810.

Moeyaert, P., et al. The Journal of Chem. Therm., 2015. 85(0): p. 61-67.

Pertechnetic acid HTcO

4

binary data = triplet (

Φ

HTcO4

, γ

HTcO4

, m

HTcO4

)

New variation of

γγγγ

= f(m)

Boyd’s data available in the

literrature

New a

w

measurements

New variation implemented in the

models

γ= >?

υ= >? "#$%&T) ' U#$%&T) '

υ= >?m= >? υ=E>Fm=E>F υC>DE>F DmC>DE>F D ϕ= > 8 ln aI

υm= > M= >

Pink coloration of the most concentrated solutions Hypothesis: Tc2O7 formation 2 HTcO ↔ H O Tc OX lnγ ϕ 8 1 OPϕ 8 1m Q dm ϕ m

TECHNETIUM EXTRACTION MODELING

(12)

An explicative model able to simulate the U-Tc co-extraction phenomena

A predictive model able to calculate DTc for a given aqueous composition (Uaq, Haq , Tcaq)

Modeling is based on hypothesis on the complexes stoechiometries …

… that have to be confirmed by speciation studies

Main extraction mechanisms:

#$%&' '( Y #$%&' (' HTcO 3L HNO HTcO HNO L HTcO 2L HNO HTcO HNO L

+&, -&. ,(, #$%&' ' +&, -&. $%&' (, #-&. UO NO HNO L HTcO [ UO NO TcO L HNO

TECHNETIUM EXTRACTION MODELING

(13)

IR and XAS spectroscopies investigations

IR spectroscopy: influence of the Tc/U ratio

XAS spectroscopy: influence of the Tc/U ratio and data processing

Organic phase:

DEHiBA 1 M / TPH

Aqueous phase:

HNO3 1 M, H2O, UO2(NO3)2 0-30 g.L-1 HTcO4 0-0.1 M

DEHiBA-HNO

3

-H+ UO22+ NO3 -TcO4 -UO22+ NO3 -NO3 -TcO4 -NO3 -NO3 -UO22+ TcO4 -H+ Contact Vortexing 1h at 25°C Settling

DEHiBA-HNO

3

-UO

2

(NO

3

)

2

DEHiBA-HNO

3

-HTcO

4

TECHNETIUM SPECIATION IN ORGANIC PHASE

(14)

IR spectroscopy

TECHNETIUM SPECIATION IN ORGANIC PHASE

Tc/U

ratio

0

Bonded C=O and UO2 stretch shifted to lower frequencies when [Tc] ↗

Changes in the intensity and in the shape of the nitrate ν1 N=O stretch when [Tc] ↗ → Changes are occuring in the U(VI) inner

coordination sphere when uranium and technetium are co-extracted

1.2

(15)

TECHNETIUM SPECIATION IN ORGANIC PHASE

0

Optimisation of the UO2(NO3)(TcO4)L2 complex structure Vibrational frequencies calculation for UO2(NO3)2L2 and UO2(NO3)(TcO4)L2 complexes

Confirmation that changes are occuring in the U(VI) inner coordination sphere when uranium and

technetium are co-extracted

Calculated UO2(NO3)(TcO4)L2 structure is used as support for XAS data processing

1.2 0.6

ν / cm-1

Type of vibration Bonded ν

C=O νas UO2

2+

exp UO2(NO3)2L2 1573 935

ν / cm-1

Type of vibration Bonded ν

C=O νas UO22+

calc UO2(NO3)2L2 1587 933

ν / cm-1

Type of vibration Bonded ν

C=O νasUO22+

calc UO2(NO3)2L2 1587 933 Tc/U

ratio

D. Guillaumont

(16)

Nuclear Energy Division, Marcoule

XAS spectroscopy

Fourier transform of the k3-weighted EXAFS spectra at uranium L3edge for U-Tc complexes

k3-weighted EXAFS spectra at uranium L edge for U-Tc T. Dumas

TECHNETIUM SPECIATION IN ORGANIC PHASE

0 2.4 0.6 Ratio Tc/U CNU-Oeq dU-Oeq / Å 1 6 2.48 2 5.7 2.47 3 5.3 2.45

Substitution of an anion TcO4- in the

place of a nitrate NO3

-→ TcO4- coordinnates the uranyl in a

monodentate fashion

CNU-Oeq dU-Oeq / Å

1 6 2.48

(UO2)(NO3)(TcO4)L2

Confirmation of the suggested co-extraction mechanism of U(VI) and Tc(VII)

Tc/U ↗: CNU-Oeq ↘ dU-Oeq

(UO2)(NO3)2L2

(17)

CONCLUSION & OUTLOOK

Objectives : D, SF, recovery % Liquid liquid extraction:

Batch experiments, γspectrometry, UV-vis, etc

Molecular scale Physico-chemical modeling Process modeling Macroscopic scale Modeling:

Solving the mass balance by taking into account deviation from ideal behaviour

Process simulation :

Models integrated into the CEA PAREX code

Speciation of organic complexes:

UV-vis, IR, ESI-MS, EXAFS etc.

Charge M1+ M2 Solution de désextraction Solution de désextraction M1 Raffinat M2 Extractant(s) Diluant RÉGÉNÉRATION EXTRACTION DÉSEXTRACTION Charge M1+ M2 Solution de désextraction Solution de désextraction M1 Raffinat M2 Extractant(s) Diluant RÉGÉNÉRATION EXTRACTION DÉSEXTRACTION

(18)

Commissariat à l’énergie atomique et aux énergies alternatives Centre de Marcoule| BP17171| 30207 Bagnols-sur-Cèze Cedex T. +33 (0)4 66 39 78 66 |F. +33 (0)4 66 79 63 25

Etablissement public à caractère industriel et commercial |RCS Paris B 775 685 019

THANK YOU FOR

YOUR ATTENTION

Aknowledgements

Laurence Chareyre

Dr. Christian Sorel

Dr. Manuel Miguirditchian

Dr. Thomas Dumas

Dr. Dominique Guillaumont

Dr. Kristina Kvashnina

Pr. Philippe Moisy

Pr. Jean-François Dufrêche

| PAGE 17

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