Transcript
Page 1: 9-1 Solvent Extraction Based on separating aqueous phase from organic phase Used in many separations U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, Ni Can be

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Solvent Extraction

• Based on separating aqueous phase from organic phase• Used in many separations

U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, NiCan be a multistage separationCan vary aqueous phase, organic phase, ligandsUncomplexed metal ions are not soluble in organic phaseMetals complexed by organics can be extracted into organic phaseConsidered as liquid ion exchangers

Page 2: 9-1 Solvent Extraction Based on separating aqueous phase from organic phase Used in many separations U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, Ni Can be

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Extraction Reaction• Phases are mixed• Ligand in organic phase complexes metal ion in

aqueous phaseConditions can select specific metal ions oxidation state ionic radius stability with extracting ligands

• Phase are separated• Metal ion removed from organic phase

EvaporationBack Extraction

Page 3: 9-1 Solvent Extraction Based on separating aqueous phase from organic phase Used in many separations U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, Ni Can be

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Solvent extraction• Influence of chemical conditions

Solvent Overall extraction, phase splitting

Metal ion and acid concentration Phase splitting

• Distribution coefficient

[M]org/[M]aq=Kd

Used to determine separation factors for a given metal ion Ratio of Kd for different metal ions

Distribution can be used to evaluate stoichiometry Evaluation distribution against change in solution

parameter* Plot log Kd versus log [X], slope is stoichiometry

• Extraction can be explained by complexationUsed to determine complexation constantsConsider all speciation in aqueous and organic phase

Page 4: 9-1 Solvent Extraction Based on separating aqueous phase from organic phase Used in many separations U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, Ni Can be

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Mechanism

• Solvation Extraction of neutral complex UO2(NO3)2 forms with TBP

* Equilibrium shifts with nitrate, back extraction into aqueous at low nitric acid

• Ion exchangeMetal ion exchanged into organic phase, ion transfer in aqueous phaseUse of organic soluble acid i.e., alkyl phosphinic acid (R2PO2H)

• Ion pair extractionCharged metal complex with extractant of opposite charge i.e., Quaternary ammonium salt with anionic actinide

nitrate

Page 5: 9-1 Solvent Extraction Based on separating aqueous phase from organic phase Used in many separations U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, Ni Can be

9-5(CH3CH2)2O Diethyl ether

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9-6Effect of nitric acid concentration on extraction of uranyl nitrate with TBP

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Reactions

• Tributyl Phosphate (TBP)

(C4H9O)3P=O

Resonance of double bond between P and O

UO22+

(aq) + 2NO3-(aq) + 2TBP(org) <--

>UO2(NO3)2.2TBP(org)

Consider Pu4+

• Thenoyltrifluoroacetone (TTA)

Keto Enol Hydrate

aa

S

O O

CF3S

O OH

CF3S

OOH

CF3

HO

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TTA

• General Reaction

Mz+(aq)

+ zHTTA(org) <-->M(TTA)z(org) + H+

(aq)

What is the equilibrium constant?

Problems with solvent extraction• Waste• Degradation of ligands• Ternary phase formation• Solubility

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Page 10: 9-1 Solvent Extraction Based on separating aqueous phase from organic phase Used in many separations U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, Ni Can be

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Page 11: 9-1 Solvent Extraction Based on separating aqueous phase from organic phase Used in many separations U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, Ni Can be

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Page 12: 9-1 Solvent Extraction Based on separating aqueous phase from organic phase Used in many separations U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, Ni Can be

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Page 13: 9-1 Solvent Extraction Based on separating aqueous phase from organic phase Used in many separations U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, Ni Can be

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Page 14: 9-1 Solvent Extraction Based on separating aqueous phase from organic phase Used in many separations U, Zr, Hf, Th, Lanthanides, Ta, Nb, Co, Ni Can be

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Non-ideal behavior

• Variation in chemical condition during extraction

Change in acidity• Extractant saturation

Metal or competing ion• Phase dissolution

Solubility into other phase• Degradation• Third phase formation

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Third phase formation

• Brief review of third phase formation• Related prior research• Laboratory methods• Np third phase behavior• Comparison with U and Pu• Spectroscopic observations

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Third Phase Formation

• In liquid-liquid solvent extraction certain conditions cause the organic phase to splitPUREX separations using tributyl phosphate (TBP)Possible with future advanced separations

• Limiting Organic Concentration (LOC) – highest metal content in phase prior to split

• Light phase – mostly diluent• Heavy phase – extractant and metal rich

Problematic to safety!

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Actinide Third Phases

Light Phase

Heavy Phase

Aqueous

Phase

U(VI)

Pu(IV)

Np(IV) Np(VI)

Pu(VI)

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Importance to Safety

• Increased risk of criticality• Phase inversion• Difficulty in process fluid separations• Carry-over of high concentration TBP to

heated process units

Possible contribution to Red Oil event at Tomsk, Russia

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Phase Inverted Plutonium

Inverted Organic

Aqueous

Heavy Organic

Light Organic

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Prior Research

Majority of work focused on defining LOC boundary (reviewed by Rao and Kolarik)

-Effects of temp., concs., acid, diluent, etc.

Recent work on possible mechanisms

-Reverse micelle evidence from neutron scattering (Osseo-Asare; Chiarizia)

-Spectroscopic studies -UV, IR, EXAFS (Jensen)

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Reverse Micelle Theory

Classical StoichiometryPossible Reverse Micelle

UOUO222+2+ + 2NO + 2NO33

-- + 2TBP + 2TBP UO UO22(NO(NO33))22 ▪ ▪ 2TBP2TBP

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Role of the Metal

• LOC behavior well known for U(VI), U(IV), Pu(IV), and Th(IV)

• Little data available on Pu(VI) • No data on any Np systems• Mixed valence systems not understood

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Mixed Systems

• Observed effect of Pu(VI) in HPT vs. C12

• Large impact of presence of Pu(VI) in HPT

-Indications heavy phase enriched in Pu(VI)• Opposite found with U(VI) inhibiting phase

separation in U(IV) system (Zilberman 2001)

Suggests possible role of trinitrato species

AnO2(NO3)3-

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Neptunium Study

• Unique opportunity to examine trends in the actinides [LOC curve for U(IV) vs Pu(IV)]

- Effective ionic charge

- Ionic radii

- Stability constants for trinitrato species• Never been investigated• Ease of preparing both tetravalent and

hexavalent nitrate solutions

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Neptunium Methods

• Worked performed at Argonne National Laboratory, Argonne, IL

• Stock prepared from nitric acid dissolution of 237Np oxide stock

• Anion exchange purification

-Reillex HPQ resin, hydroquinone (Pu reductant), hydrazine (nitrous scavenger)

• Np(IV) reduction with hydrogen peroxide reduction

• Np(VI) oxidation with concentrated HNO3 under reflux

Np(VI) nitrate salt

Np(IV) nitrate

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LOC Behavior

• Np(VI) near linear• Np(IV) slight parabolic

Appears between linear U(IV) and parabolic Pu(IV)

• Both curves similar resemblance to distribution values Purex systems

Suggests possible link with metal-nitrate speciation

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Np Third Phase Boundaries

4 5 6 7 8 9 100.05

0.10

0.15

0.20

0.25

0.30

L

OC

, M

HNO3, M

Np(IV) Np(VI)

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Comparison with Other Actinides

U Np Pu

An (IV) 0.08

(Wilson 1987)

0.15 0.27

(Kolarik 1979)

An (VI) No 3Φ

(Chiarizia 2003)

0.17 0.10

LOC in 7M HNO3 / 1.1M TBP/dodecane 20-25 °C, M

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Organic Nitric Acid

• Balance available TBP and organic H+

• Np(IV) = mixture of the monosolvate (TBP · HNO3) and hemisolvate (TBP · 2HNO3) species

• Np(VI) = hemisolvate

Agrees with literature data on U(VI) and Th(IV) acid speciations

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Valence Trends – An (IV)

• General trend = decreasing LOC as ionic radii increases

Lowest charge density = lowest LOC• Np intermediate between U and Pu• Literature Th(IV) data consistent with trend

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Valence Trends – An(VI)

• An(VI) = LOC increases as ionic radii decreases

Opposite trend for An(IV), including Th(IV)• Charge density using effective cationic charge and 6-

coordinate radii

No evidence of correlation with charge density within error of effective charge data

• Oxo group interactions not fully considered

Future work required

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Spectral Study Methods

• Look for spectral trends in Np(VI) system• Examined trends for:

-LOC

-Metal loading

-Nitrate loading (using NaNO3)

• 5 mm quartz cuvette with Cary 5 Spectrometer

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LOC Spectra

900 1000 1100 1200 13000.0

0.2

0.4

0.6

0.8

1.0

[HNO3], M

4 6 7 8 10

A

bso

rba

nce

Wavelength, nm

Np(VI) 30% TBP / dodecane at LOC

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Metal Loading

900 1000 1100 1200 13000.0

0.2

0.4

0.6

0.8 [Np(VI)]org, M

LOC = 0.27 0.18 0.09 0.03

Abs

orba

nce

Wavelength, nm

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Nitrate Effects

Aqueous Organic

1000 1100 1200 13000.0

0.3

0.6

0.9

Abs

orba

nce

Wavelength, nm

[NO-

3], M

4 5 6 saturated

1000 1100 1200 13000.00

0.05

0.10

0.15

0.20

Abs

orba

nce

Wavelength, nm

[H+] = 4M, [Np(VI)] = 0.03M

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Valence Scoping Experiments

• Examined various mixes of Pu(IV)/Pu(VI)• Solutions prepared by method of slow addition

of concentrated HNO3 to heated syrupy Pu nitrate solution

• Use UV-Vis peak analysis for determination of initial aqueous composition

• Perform mole balance on aqueous phase before and after contact for organic content of each valence species (some samples)

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Spectrum – Mixed Valence Phases

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Third phase conclusions

• Third phase behavior measured in Np• LOC trends consistent with U and Pu• Np(IV) LOC trends with charge density• No clear correlation for Np(VI)• Spectroscopic evidence suggests possible role of

trinitrato species in third phase

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Basic decay equations

• The radioactive process is a subatomic change within the atom

• The probability of disintegration of a particular atom of a radioactive element in a specific time interval is independent of its past history and present circumstances

• The probability of disintegration depends only on the length of the time interval.

Probability of decay: p=t

Probability of not decaying: 1-p=1- t

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1-p=1-t=probability that atom will survive t

(1- t)n=probability that atom will survive n intervals of t

nt=t, therefore (1- t)n =(1- t/n)n

Since limn∞(1+x/n)n=ex, (1- t/n)n=e-t, the limiting value.

Considering No atoms, the fraction remaining unchanged after time t is N/No= e-t

Statistics of Radioactive Decay

N=Noe-t

where is the decay constant

Statistics of Radioactive Decay

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Radioactivity as Statistical Phenomenon

• Binomial Distribution for Radioactive Disintegrations

probability W(m) of obtaining m disintegrations in time t from No original radioactive atoms

probability of atom not decaying in time t, 1-p, is (N/No)=e-t, where N is number of atoms that survive in time interval t and No is initial number of atoms

• Time Intervals between Disintegrations

probability of time interval having value between t and t+d:

mNm

o

o oppmmN

NmW

)(

!)!(

!)( 1

dteNdttP tNo

o )(

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• Average Disintegration Rate

for radioactive disintegration--if n=No and p=1-e-t--average number M of atoms disintegrating in time t is M=No(1-e-t); for small t, M=Not and disintegration R=M/t=No , which corresponds to -dN/dt=N

• Expected Standard Deviation

• M is number of counts• Relative error = -1

nr

r

rnr

rrrWnp

qprrn

nrW

0)(

!)!(

!)(

where 1-p=q

MsmallgenerallyistpracticecountinginSince

MeeeN ttto

,

)(1