9-1 solvent extraction based on separating aqueous phase from organic phase used in many separations...

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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 a multistage separation Can vary aqueous phase, organic phase, ligands Uncomplexed metal ions are not soluble in organic phase Metals complexed by organics can be extracted into organic phase Considered as liquid ion exchangers

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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

9-1

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

9-2

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

9-3

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

9-4

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

Page 6: 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

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

Page 7: 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

9-7

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

Page 8: 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

9-8

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

Page 9: 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

9-9

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

9-10

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

9-11

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

9-12

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

9-13

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

9-14

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

Page 15: 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

9-15

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

Page 16: 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

9-16

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!

Page 17: 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

9-17

Actinide Third Phases

Light Phase

Heavy Phase

Aqueous

Phase

U(VI)

Pu(IV)

Np(IV) Np(VI)

Pu(VI)

Page 18: 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

9-18

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

Page 19: 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

9-19

Phase Inverted Plutonium

Inverted Organic

Aqueous

Heavy Organic

Light Organic

Page 20: 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

9-20

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)

Page 21: 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

9-21

Reverse Micelle Theory

Classical StoichiometryPossible Reverse Micelle

UOUO222+2+ + 2NO + 2NO33

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

Page 22: 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

9-22

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

Page 23: 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

9-23

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-

Page 24: 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

9-24

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

Page 25: 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

9-25

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

Page 26: 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

9-26

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

Page 27: 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

9-27

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)

Page 28: 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

9-28

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

Page 29: 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

9-29

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

Page 30: 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

9-30

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

Page 31: 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

9-31

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

Page 32: 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

9-32

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

Page 33: 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

9-33

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

Page 34: 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

9-34

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

Page 35: 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

9-35

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

Page 36: 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

9-36

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)

Page 37: 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

9-37

Spectrum – Mixed Valence Phases

Page 38: 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

9-38

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

Page 39: 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

9-39

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

Page 40: 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

9-40

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

Page 41: 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

9-41

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 )(

Page 42: 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

9-42

• 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