Subscriber access provided by UNIVERSITY OF ADELAIDE LIBRARIES
B: Liquids, Chemical and Dynamical Processes in Solution, Spectroscopy in Solution
Solvation Dynamics of HEHEHP Ligand at the Liquid-Liquid Interface An T. Ta, Govind A. Hegde, Brian D. Etz, Anna G. Baldwin, Yuan Yang, Jenifer C. Shafer, Mark Peter Jensen, C. Mark Maupin, and Shubham Vyas J. Phys. Chem. B, Just Accepted Manuscript • DOI: 10.1021/acs.jpcb.8b03165 • Publication Date (Web): 14 May 2018 Downloaded from http://pubs.acs.org on May 15, 2018
Just Accepted “Just Accepted” manuscripts have been peer-reviewed and accepted for publication. They are posted online prior to technical editing, formatting for publication and author proofing. The American Chemical Society provides “Just Accepted” as a service to the research community to expedite the dissemination of scientific material as soon as possible after acceptance. “Just Accepted” manuscripts appear in full in PDF format accompanied by an HTML abstract. “Just Accepted” manuscripts have been fully peer reviewed, but should not be considered the official version of record. They are citable by the Digital Object Identifier (DOI®). “Just Accepted” is an optional service offered to authors. Therefore, the “Just Accepted” Web site may not include all articles that will be published in the journal. After a manuscript is technically edited and formatted, it will be removed from the “Just Accepted” Web site and published as an ASAP article. Note that technical editing may introduce minor changes to the manuscript text and/or graphics which could affect content, and all legal disclaimers and ethical guidelines that apply to the journal pertain. ACS cannot be held responsible for errors or consequences arising from the use of information contained in these “Just Accepted” manuscripts.
is published by the American Chemical Society. 1155 Sixteenth Street N.W., Washington, DC 20036 Published by American Chemical Society. Copyright © American Chemical Society. However, no copyright claim is made to original U.S. Government works, or works produced by employees of any Commonwealth realm Crown government in the course of their duties.
Page 1 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
1
Solvation Dynamics of HEHEHP Ligand at the
2
Liquid-Liquid Interface
3
An T. Ta, Govind A. Hegde, Brian D. Etz, Anna G. Baldwin, Yuan Yang, Jenifer C. Shafer, Mark
4
P. Jensen, C. Mark Maupin, and Shubham Vyas*
5
Department of Chemistry, Colorado School of Mines, Golden, Colorado 80401, United States
6
*Corresponding author: phone +1-303-273-3632, E-mail:
[email protected] 7 8 9 10 11 12 13 14 15 16
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
17
Abstract. Actinide-Lanthanide Separation (ALSEP) has been a topic of interest in recent years as
18
it has been shown to selectively extract problematic metals from spent nuclear fuel. However, the
19
process suffers from slow kinetics prohibiting it from being applied to nuclear facilities. In effort
20
to improve the process, many fundamental studies have been performed, but the majority have
21
only focused on the thermodynamics of separation. Therefore, to understand the mechanism
22
behind the ALSEP process, molecular dynamics (MD) simulations were utilized to obtain the
23
dynamics and solvation characteristics for an organic extractant, 2-ethylhexylphosphonic acid
24
mono-2-ethylhexyl ester (HEHEHP). Simulations were conducted with both pure and biphasic
25
solvent systems to evaluate the complex solvent interactions within the ALSEP extraction method.
26
The MD simulations revealed solvation and dynamical behaviors that are consistent with
27
experimentally observed chemical properties of HEHEHP for the pure solvent systems (e.g.
28
hydrophobic/hydrophilic behaviors of the polar head group and alkyl chains and dimer formation
29
between the ligands within an organic solvent). When present in a biphasic solvent system,
30
interfacial behaviors of the ligand revealed that, at low concentrations, the alkyl side chains of
31
HEHEHP were parallel to the interfacial plane. Upon increasing the concentration to 0.75 M,
32
tendency for the parallel orientation decreased and a more perpendicular-like orientation was
33
observed. Analysis of ligand solvation energies in different solvents through the thermodynamic
34
integration method demonstrated favorability towards n-dodecane and biphasic solvents, which is
35
in agreement with the previous experimental findings.
36 37 38
ACS Paragon Plus Environment
Page 2 of 26
Page 3 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
39
The Journal of Physical Chemistry
I. Introduction
40
One of the major challenges faced by nuclear facilities is the management of spent nuclear
41
fuel. Approximately 2,500 tons of spent fuel is generated in the United States each year and, if left
42
untreated, the long-term radiotoxicity will pose a threat to the environment.1–4 Of the many isotopes
43
present within nuclear waste, transuranic actinides foster major concern due to their large
44
radiotoxicities. Such elements are primary contributors to long-term toxicity and, contribute major
45
strain on waste repositories.1–3 To simplify repository design and siting, recent efforts have been
46
dedicated to minimizing the transuranic content within spent nuclear fuel.4,5
47
Although separation processes such as PUREX have been successfully implemented at the
48
industrial6,7 scale for the extraction of plutonium and uranium, recovery of other prominent
49
actinides, such as americium (Am) and curium (Cm), remains difficult due to the presence of
50
fission product lanthanides. The separation of Am and Cm is crucial because the lanthanides
51
possess high neutron capture cross sections, which may inhibit the transmutation of the actinides
52
in advanced nuclear reactors.8 Different separation processes have been developed to address this
53
issue but solvent (liquid-liquid) extractions are most commonly used.4 This method utilizes two
54
immiscible solvents to partition the actinides from the lanthanides in solution. Some solvent
55
extraction separations that have shown to be capable of selectively separating Am and Cm are
56
SANEX, GANEX, advanced TALSPEAK, and ALSEP.4,5,9 However, implementation of these
57
processes often suffers from slow kinetics resulting in unsatisfactory throughput when
58
implemented at the industrial scale.
59
The ALSEP process displays a fast solvent loading step where trivalent lanthanides and
60
actinides are extracted from molar concentrations of nitric acid but the selective stripping step
61
where actinides and lanthanides are actually separated from each other is too slow to implement
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Page 4 of 26
62
in conventional centrifugal contractors.5,10 The separation step in the ALSEP process is very
63
similar to that of the reverse TALSPEAK and advanced TALSPEAK processes, in which an
64
organophosphorus extractant such as di-(2-ethylhexyl)phosphoric acid (HDEHP) or 2-
65
ethylhexylphosphonic acid mono-2ethylhexyl ester (HEHEHP) is used to extract both trivalent
66
actinide and lanthanide cations into the organic phase. Then the actinides are selectively stripped
67
from the organic phase with aqueous diethylenetriaminepentaacetic acid (DTPA) or N-(2-
68
[bis(carboxymethyl)amino]ethyl)-N-(2-hydroxyethyl)glycine
69
conceptually simple, a detailed and quantitative understanding of the chemical process behind
70
ALSEP have yet to be uncovered.
(HEDTA).5,11
Although
71
Currently, most fundamental research of the ALSEP process has only considered
72
thermodynamics and little attention has been directed towards understanding mechanisms that
73
drive the kinetics of separation. Nevertheless, previous studies of extraction kinetics on
74
TALSPEAK have demonstrated that the rate of partitioning is dependent on chemical reactions at
75
or near the interface of the system.12–14 Due to the chemical similarities between the processes, it
76
is believed that such rate dependence will also be the same for the ALSEP method. Therefore,
77
understanding the various phenomena occurring at the interface and identification of important
78
interfacial reactions are essential to determining the origin of the kinetic barriers in ALSEP. Once
79
the critical interfacial reactions are identified, and their kinetics barriers are evaluated, the rate
80
limiting steps can be identified and possible improvements can be proposed. In an effort to deepen
81
our understanding of the events occurring at the interface, computational modeling through ab
82
initio calculations and molecular dynamics (MD) simulations were used to analyze dynamics and
83
solvation behaviors of HEHEHP (Figure 1) in n-dodecane, water, and a biphasic n-dodecane +
84
water solvents.
ACS Paragon Plus Environment
Page 5 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
85 86
Figure 1. Structure of HEHEHP. Oxygen atoms are depicted in red, phosphorous in orange, carbon
87
in grey, and hydrogen in white colored spheres. The labeling scheme is as follows: ester oxygen –
88
(O1), hydroxy oxygen – (O2), phosphonyl oxygen – (O3), ethyl carbon – (E1/2), and hexyl carbon
89
(H1/2).
90
In this study, new atomic charge force field parameters were developed for HEHEHP
91
through ab initio calculations and were used within MD simulations to model the ligand dynamics
92
within different solvents. These simulations were analyzed to determine solvation spheres, cluster
93
formations, interfacial orientations, and solvation energies in two scenarios (single and multi-
94
ligand systems). Investigations of these scenarios probed the impact of extractant concentration on
95
HEHEHP behavior within different solvents and provided critical insights that are useful to
96
developing a mechanistic understanding of the ALSEP process.
97
II. Computational Methods
98
A. Ab initio Calculations
99
Ab initio calculations were performed using the Gaussian09 software package.15 Geometry
100
optimizations of HEHEHP and n-dodecane were carried out using the Minnesota global hybrid
101
functional, M06-2X,16 with the CBSB7 basis sets (i.e. 6-311g(2d,d,p)).17 The nature of the
102
stationary state was confirmed to be a minimum by the absence of imaginary frequencies. Single
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
103
point calculation on the previously obtained geometries using Møller-Plesset second order
104
perturbation theory (MP2)18 and the cc-PVTZ basis sets19 were then utilized with the restrained
105
electrostatic potential (RESP) method to obtain the classical point charges.20 These charges and
106
the optimized geometry coordinates are reported in Table S1 and S2 of the supporting information.
107
Similar to previously published work21, charge calculations were employed in conjunction with
108
the General Amber Force Field (GAFF)22 using the antechamber program23 within the Amber14
109
software package24 to generate charge modified GAFF parameter sets. These modified GAFF
110
parameter sets were then used in subsequent MD simulations within n-dodecane, water, and a
111
biphasic (n-dodecane + water) solvent system.
112
B. Molecular Dynamics Simulations
113
All MD simulations were performed using the Amber14 package while analyses were
114
conducted with AmberTools14, Visual Molecular Dynamics (VMD)25, and in-house programs,
115
which are detailed in the respective results sections. Simulations within three different solvents
116
were conducted at two different scenarios, as shown in Table S3. Single-ligand systems represent
117
one molecule of HEHEHP in a box of solvent and multi-ligand systems contain a HEHEHP
118
concentration of 0.75 M, which was chosen to study the behavior of HEHEHP at typical ALSEP
119
concentrations.5 Water was modeled using the SPC/FW26 flexible water model whereas HEHEHP
120
and n-dodecane were described by the charge modified GAFF parameters obtained through
121
calculations done in Section II.A. The Packmol program27 was utilized to produce initial
122
coordinates for all systems, which consisted of a random distribution of the molecules across the
123
simulation box unless otherwise noted.
124
All systems were initially minimized for 2500 steps using the steepest descent algorithm,
125
followed by 2500 steps using the conjugate gradient algorithm. After minimization, an isobaric-
ACS Paragon Plus Environment
Page 6 of 26
Page 7 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
126
isothermal ensemble (NPT) simulation was performed at 298 K and 1 atm for 1 ns to ensure that
127
the densities of the systems had converged. To ascertain the accuracy of the force field and
128
sufficiency of the NPT simulation lengths, the density of a pure HEHEHP system (500 molecules)
129
was calculated to be of 0.941 ± 0.001 g/cm3, which is in good agreement with the experimental
130
value, 0.958 g/cm3. NPT simulations were followed by a production run using the canonical
131
ensemble (NVT) at 298 K for 20 ns and a microcanonical ensemble (NVE) simulation for 50 ns.
132
The NVE simulations were then used to calculate diffusion coefficients through an in-house
133
program. All MD simulations utilized a 1 fs time step.
134
C. Solvation Energy Calculations
135
Solvation energies of HEHEHP in different solvents were calculated using
136
Thermodynamic Integration (TI) as implemented in the AMBER14 software package.28 The TI
137
procedure involves defining a thermodynamic cycle to probe the free energy difference between
138
two states and running a separate simulation to represent each discrete segment in the
139
thermodynamic cycle. In this case, the cycle involves a pathway with an initial state corresponding
140
to the ligand having no interactions with the solvent (𝜆 = 0) and a final state corresponding to the
141
ligand having complete interactions with the solvent (𝜆 = 1), which represents the fully solvated
142
state of the ligand. The free energy is calculated using:
143
1
Δ𝐸 = ∫0 𝑑𝜆
(1)
144
where Δ𝐸 is the free energy difference of solvation, U is the potential energy of the system, and 𝜆
145
is a parameter that varies the potential from the initial state where 𝜆 = 0 to the final state where 𝜆
146
= 1. Solvation free energy was obtained with simulations ran at discrete values of 𝜆 from the initial
147
to final state at intervals of 0.1 and numerical integration of Equation 1 by an in-house program.
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
148
The procedure used in this study utilizes the new and more efficient implementation of TI in
149
Amber28, wherein the transformation of both the charges and the van der Waals parameters from
150
the initial state to the final state are done in the same step. Earlier implementations of TI required
151
the electrostatic and van der Waals transformations to be done separately in two separate
152
simulations. Furthermore, the new implementation allows for the calculation of free energies at
153
both the initial and final states, which reduces error compared to previous implementations
154
wherein the potential energy calculation became unstable at values of 𝜆 close to the initial and
155
final states.
156
D. NMR Measurements
157
The average diffusion coefficient of a 0.2 M sample of HDEHP in n-dodecane was
158
measured with a 500 MHz JEOL NMR spectrometer at 21ºC by implementing a pulsed field
159
gradient stimulated echo experiment as described in previous works of Tanner and Baldwin et
160
al.29,30 To achieve 90% attenuation (or greater) of the HDEHP peak at 4 ppm, 16 gradients of 16
161
scans at a magnetic field gradient strength of 270 mT/m was utilized. A gradient pulse width of 2
162
ms and a diffusion time of 200 ms was used in conjunction with a 5 s relaxation delay. The self
163
diffusion coefficient was then calculated from the Stejskal-Tanner equation that relates decay of
164
NMR signal intensity with increasing applied magnetic field gradient strength to the displacement
165
of NMR-active nuclei. These results were used to compare with and validate the accuracy of the
166
computational protocol used to find diffusion coefficients of HEHEHP.
167 168 169
ACS Paragon Plus Environment
Page 8 of 26
Page 9 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
170
III. Results and Discussion
171
A. Solvation of HEHEHP
172
Interactions of HEHEHP in solution were investigated by computing radial distribution
173
functions (RDFs) for seven atoms (labelled in Figure 1) with respect to solvent molecules and each
174
other (when applicable) from the NVT simulation. To examine the immediate solution
175
environment around the ligand (i.e. first solvation sphere), coordination numbers (CNs) were
176
calculated by integrating the first peak of the respective atom’s RDF. Analyses in which a distinct
177
peak was absent were interpreted as the atom having an asymptotic relationship with the solvent
178
and the coordination number was deemed to be zero. Specific values of the cutoff distances for all
179
RDFs can be found in Table S4 in the supporting information.
180
RDFs of HEHEHP within pure n-dodecane and water solvents are reported within the
181
supporting information as Figure S1 and S2 respectively. Both single- and multi-ligand systems
182
displayed expected hydrophobic/hydrophilic behavior towards solvent molecules as the alkyl
183
chains coordinated with n-dodecane within the pure organic system while the oxygen atoms
184
exhibited interactions with water within the pure aqueous system. In n-dodecane, analysis of the
185
ethyl carbons revealed a coordination number of 0.0 for both single- and multi-ligand systems.
186
Although the carbon is hydrophobic and should favor interaction with n-dodecane, this can be
187
attributed to the relatively large size of the solvent molecules and the solute’s polar head group,
188
which restricts interaction between the chains and solvent. Analyses of ligand-ligand interactions
189
also showed expected behaviors with coordination primarily occurring between the head group in
190
n-dodecane and interactions largely found to be between alkyl chains in water. In depth analyses
191
of these expected behaviors within pure solvent systems can be found within the supporting
192
information.
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
193 194
Figure 2. Cluster distribution of HEHEHP (0.75M) in water (blue), n-dodecane (red), and biphasic
195
water + n-dodecane (green) solvent.
196
To quantify ligand-ligand aggregation in the MD simulations, cluster analysis was
197
performed on HEHEHP within the different solvents. It is well known that HEHEHP, when
198
coordinating with a metal cation, forms dimer clusters between the head groups in an organic
199
phase.31–36 Therefore, to investigate whether the MD simulations can reproduce the same behavior,
200
cluster analysis was conducted in the absence of metal cations. A cluster was considered to be
201
formed if phosphorous atoms of different ligand molecules came within a cut-off distance of 4.9
202
Å. This distance was selected based on the ligand-ligand RDF from Figure S1C of the supporting
203
information. The presence of clusters was determined throughout the entire simulation using an
204
in-house hierarchical clustering algorithm. A distribution of various multimeric complexes is
205
shown in Figure 2 and a table of these values are reported in Table S5 of the supporting
206
information. Multiple clusters were observed within the pure n-dodecane solvent with dimers
207
primarily present throughout the simulation at ~54%. This illustrates HEHEHP’s tendency to form
208
dimers, however, other multimeric complexes (e.g. trimers, tetramers, pentamers, and even
209
hexamers), were also present, which demonstrates a more aggregative behavior in the absence of
ACS Paragon Plus Environment
Page 10 of 26
Page 11 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
210
cations. Such behavior was suggested previously for HDEHP based on isopiestic measurements37
211
and hints at the impact of the metal cation acting as a driver for dimer formation. Based off the
212
criteria used, extractant clustering within the water solvent was observed to result primarily in
213
monomers (~96%) with little dimer formation. This is in agreement with the RDF analyses of the
214
aqueous solution, which showed that the polar P(=O)OH group of HEHEHP primarily hydrogen
215
bonds to water molecules with ligand-ligand interactions mainly occurring between alkyl chains. (A)
(C)
(B)
(D)
216 217
Figure 3. Radial distribution functions for (A) single-ligand HEHEHP to n-dodecane molecules,
218
(B) multi-ligand HEHEHP to n-dodecane molecules, (C) single-ligand HEHEHP to water
219
molecules, and (D) multi-ligand HEHEHP to water molecules in n-dodecane + water solvent.
220
RDF assessment of HEHEHP in the biphasic solvent (Figure 3) revealed that the ester
221
oxygen (O1) had an unexpectedly larger coordination number with water than the other oxygen
222
atoms at the interface. This larger coordination number suggests that the orientation of the alkyl
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
223
chains is parallel to the interface. Such orientation may be due to the hydrophobic n-dodecane
224
molecules being parallel at the interface (vide infra, Section III.C) and, in turn, drive parallelization
225
of the alkyl chains, which has been previously hypothesized.38 In addition, the single-ligand system
226
revealed that the ethyl carbon (E1/2) had little interaction with n-dodecane molecules while they
227
had a coordination number of ~2 in the multi-ligand system. This difference in interaction between
228
ethyl carbon and n-dodecane implies that the paralleled orientation of HEHEHP may be more
229
prominent at low concentrations. Under ALSEP concentrations, coordination between ligands was
230
observed to be primarily between alkyl chains (Figure 4), which may help facilitate a more
231
perpendicular conformation to the interfacial plane as conventional thought would suggest.31,32
232
This was also seen within the cluster analysis (Figure 2) which showed monomers being primarily
233
present from the perspective of the polar head groups.
234 235
Figure 4. Radial distribution function of HEHEHP to HEHEHP in n-dodecane + water system.
236
Note: "H" represents the head group and "T" represents the alkyl chains of the ligand.
237 238
ACS Paragon Plus Environment
Page 12 of 26
Page 13 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
239
The Journal of Physical Chemistry
B. Diffusivity of HEHEHP
240
To investigate the dynamical behavior of HEHEHP in various solvation environments,
241
diffusion coefficients were calculated from the NVE simulation using Einstein’s relationship
242
between the mean square displacement and diffusion coefficient as shown in equation 2,
243
𝐷=
𝜕 6(𝜕𝑡)
(2)
244
where D is the diffusion coefficient, is the mean squared displacement, and t is time. The
245
accuracy of the protocol used to determine diffusivity for HEHEHP was evaluated by comparing
246
experimental values available for the 0.2 M HDEHP in n-dodecane to values found from the MD
247
simulations. The MD simulations on HDEHP were performed with the same procedure as
248
described in the section II.A and II.B. The diffusion coefficient for the steric bulk of HDEHP (alkyl
249
side chain) was 0.22 x 10-5 ± 0.07 cm2/s as determined from NMR measurements, while the MD
250
simulations yielded 0.09 x 10-5 ± 0.02 cm2/s. Considering experimental and theoretical error, these
251
values are of acceptable agreement and demonstrate that the protocol used to capture the diffusion
252
of HDEHP in solution is of reasonable accuracy. HDEHP is quite similar to HEHEHP with the
253
only structural difference being the head group is a phosphoric and not a phosphonic acid (i.e.
254
HEHEHP contains one less ester oxygen than HDEHP). Separately calculated diffusivities of the
255
alkyl chains in HEHEHP revealed that the ester oxygen has little effect on the diffusion of the
256
steric bulk with a value of 0.04 ± 0.04 x 10-5 cm2/s and 0.04 ± 0.02 x 10-5 cm2/s for ester containing
257
and non-ester containing chains, respectively. Keeping in mind structural similarity and the little
258
effect from the ester oxygen, it is concluded that the diffusion of HEHEHP is captured accurately
259
within this study.
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
260
To evaluate the dynamics of various parts of HEHEHP in solution, diffusion coefficients
261
for the polar head group (represented by the phosphorous atom), alkyl chains (represented by the
262
average of the two hexyl-terminal carbons), and the entire molecule on average were calculated at
263
25 °C as shown in Table 1. Within the single-ligand system, it was observed that the diffusion of
264
the head group was lower in a water system than in n-dodecane while the opposite was observed
265
for the alkyl chain. This trend may be attributed to favorable interactions (aqueous solvent
266
molecules interacting with the polar head group, etc.) causing the first solvation sphere to be tightly
267
bound. When such spheres are formed, the effective size will become larger and a slower
268
diffusivity is observed. A mixture of both n-dodecane and water solvents allows for both the polar
269
head group and alkyl chains to achieve favorable interactions at the interface and, thus, all diffusion
270
coefficients found within the biphasic solvent was observed to be smaller than that in pure solvents.
271
However, this was not observed within the multi-ligand system.
272
Table 1. Diffusion coefficients of different molecular subunits of HEHEHP and average diffusion
273
coefficients of HEHEHP for single- and multi-ligand systems in different solvents.
System
Group
Single-Ligand System
Head Group Alkyl Chains Average Head Group Alkyl Chains Average
Multi-Ligand System
Diffusion Coefficient (x 10-5 cm2/s) n-dodecane water n-dodecane + water 0.20 ± 0.08 0.11 ± 0.09 0.10 ± 0.03 0.15 ± 0.01 0.16 ± 0.09 0.13 ± 0.05 0.14 ± 0.07 0.17 ± 0.09 0.10 ± 0.03 0.02 ± 0.01 0.02 ± 0.02 0.10 ± 0.01 0.02 ± 0.01 0.07 ± 0.02 0.09 ± 0.02 0.02 ± 0.01 0.03 ± 0.02 0.10 ± 0.01
274 275
Dynamics of HEHEHP in the multi-ligand system showed diffusion coefficients being smaller
276
within the pure solvents. This may be due to the increased concentration of HEHEHP resulting in
277
the introduction of ligand-ligand interactions and the formation of clusters. These interactions and
ACS Paragon Plus Environment
Page 14 of 26
Page 15 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
278
clusters help accentuate added favorable contacts that were not possible with a single ligand. As
279
mentioned previously, HEHEHP formed clusters between hydrogen bonds of the hydrophilic head
280
groups in n-dodecane while clusters were formed between dispersion of the hydrophobic alkyl
281
chains in water. Ligands of a biphasic system reside at the interface, which prevents the formations
282
of such clusters and, thus, a larger diffusion constant is observed. Comparison of the single- and
283
multi-ligand systems also support this as the diffusion of HEHEHP did not change significantly in
284
a biphasic solvent. In addition, ligand clusters may explain why the diffusivity of HEHEHP is
285
similar in both n-dodecane and water for the head group and overall average. Conversely, alkyl
286
chains were observed to diffuse much faster in water (0.07x10-5cm2/s) than in n-dodecane
287
(0.02x10-5cm2/s). This exception is presumably a result of unfavorable interactions occurring
288
between the alkyl chains and water molecules. From the structure of HEHEHP, it was believed
289
that the ligand would form micelle-like structures in the aqueous phase as this is observed with n-
290
alkane phosphonic acids.39 However, unlike n-alkane phosphonic acids, HEHEHP contains a
291
mono-ester group, which may hinder the ligand’s ability to form complete micellar structures and,
292
instead, only aggregate towards one another incapable of fully avoiding unfavorable interactions.
293
C. Interfacial Analysis of HEHEHP
294
To fully understand the interfacial orientation of HEHEHP, a separate set of NVT
295
simulations was performed, in which the ligand was initially placed at the interface. By setting the
296
original coordinates of n-dodecane and water to be separated from each other, these systems
297
contained a well-defined interfacial plane. The conformation of n-dodecane molecules and
298
HEHEHP alkyl chains were analyzed with an in-house code, in which vectors were defined as the
299
starting atom to the terminal carbon of the relevant chain. For example, with the ester containing
300
ligand chain, the vector was defined from the starting oxygen atom (O1, Figure 1) to the terminal
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
301
hexyl-carbon (H2, Figure 1). Vectors with an angle of 0-20o with respect to the interface were
302
considered to be parallel while those with an angle of 70-90o were deemed to be perpendicular.
303 304
Figure 5. Average angle of n-dodecane molecules with respect to the distance of the MD box in
305
(A) single-ligand and (B) multi-ligand systems throughout the simulation. Blue region indicates
306
the aqueous phase while orange region represents the organic phase. The dashed line represents
307
the interface.
308
As mentioned in section III.A., it has been hypothesized that immiscible solvent molecules
309
are parallel to the interface near the interfacial plane and, in turn, orientation of any solute near or
310
at the interface is driven to also be parallel.38 Testing this hypothesis, orientation angles of n-
311
dodecane molecules were analyzed as a function of the simulation box distance (Figure 5). Both
312
single- and multi-ligand systems supported the hypothesis made by Vandegrift et al.38 with the
313
angles of the organic solvent being < 15o at the interface. In addition, it was observed that the n-
314
dodecane molecules exhibited much larger angles (~30o to ~48o) at increased distances from the
315
interface, which represents a random orientation and, hence, a bulk organic phase. This indicates
316
a distinct connection between the parallel configuration and proximity to the interfacial plane.
ACS Paragon Plus Environment
Page 16 of 26
Page 17 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
317
Noticeably, the highest angle observed within the multi-ligand system was not of the expected
318
bulk distribution with an angle ~30° and not 45°. This can be attributed to the smaller box size
319
preventing the solvent molecules from attaining bulk configuration. Analysis of the HEHEHP
320
alkyl chains revealed that parallelization was present regardless of concentration (Figure 6A) with
321
the steric bulk primarily possessing an orientation that is 10o with respect to the interface.
322
Moreover, such configuration was observed to be more prominent within the alkyl chain
323
containing the ester oxygen. These results support the findings from RDF analyses shown earlier
324
in Figure 2 with the ester oxygen of HEHEHP coordinating more with the aqueous phase than the
325
other oxygen atoms.
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
(A)
(B)
(C)
326
ACS Paragon Plus Environment
Page 18 of 26
Page 19 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
327
Figure 6. Occurrence of different interfacial angles analyzed (A) statistically for alkyl chains of
328
single-/multi-ligand systems and with respect to time for (B) the O-chain of the multi-ligand
329
system and (C) the C-chain of the multi-ligand system within n-dodecane + water solvent. Note:
330
O-chain and C-chain represent the alkyl chain with and without the ester oxygen, respectively.
331 332
Notably, due to steric hindrance, not all HEHEHP ligands were capable of being initially
333
placed at the interface within the multi-ligand simulation. Visual tracking by VMD revealed that
334
ligands began to partition to the interface and did not completely reside at the binary boundary till
335
later timeframes in the NVT simulation (Figure S3, supporting information).
336
quantifiably monitor the effects of interfacial ligand concentration, time resolved analyses were
337
performed on the orientation angles of alkyl side chains with respect to the interface. From Figure
338
6B and 6C, it was observed that ligand-ligand interactions cause the orientation to shift towards
339
larger angles. Most notably, results from the 15-20 ns timeframe revealed that angles ≥ 50o were
340
significantly more present than at earlier times. This escalation in the occurrence of higher angles
341
suggests that increasing the concentration instigates ligand configuration to shift towards a more
342
perpendicular-like orientation presumably due to the increased dispersion interaction of the alkyl
343
chains, which is supported by the previous RDF analyses (Figure 3). When present in the single-
344
ligand system, majority of the interfacial plane is occupied by n-dodecane molecules, which helps
345
facilitate the parallel alignment of HEHEHP’s steric bulk. On the contrary, in the multi-ligand
346
system, dispersion interactions between the alkyl chains of HEHEHP facilitate an increase in
347
perpendicular arrangement, despite the parallel alignment of the solvent molecules. Moreover, this
348
relationship indicates the critical role of ligand concentration in the extraction mechanism. It is
349
known that the extraction of metal cations by HEHEHP occurs between a dimer formation of the
ACS Paragon Plus Environment
Hence, to
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
350
head group coordinating with metal cation.31,32 Such an extraction would be greatly hindered if the
351
ligand was parallel to the interface, limiting aqueous participation of the hydroxyl and phosphoryl
352
oxygen.
353
D. Solvation Energy of HEHEHP in Different Solvents
354
To understand and devise a mechanism for the ALSEP process, it is critical to be able to
355
quantitatively analyze the solvation of HEHEHP. TI method as implemented in AMBER14
356
software package was used to obtain the free energies of HEHEHP in multi-ligand systems
357
containing n-dodecane, water and biphasic n-dodecane + water solvent. The TI method was
358
applied in this study for reasons explained within the supporting information. In these calculations,
359
the presence of the ligand is gradually removed in solution, and the energetics of the nonphysical
360
disappearance is monitored. Therefore, to account for ligand-ligand interactions in solution, the
361
method was implemented such that only one ligand was disappearing within the solvent.
362
Normalizing to the water solution, the relative free energies of n-dodecane and biphasic solvents
363
were found to be favored with a value of -9 ±5 kcal/mol and -8.6 ±0.6 kcal/mol. In addition, it was
364
observed that the free energies between n-dodecane and biphasic solvent were similar (difference
365
of 0.4 kcal/mol) which was expected as it is well known that HEHEHP is soluble in both n-
366
dodecane and biphasic solvent.31–33,38–40 As the experimental observations of favorable and
367
unfavorable interactions of HEHEHP with the organic and aqueous phase respectively are
368
reflected, it is believed that the energies calculated through TI are quantitatively representative of
369
the HEHEHP ligand.
370
IV. Conclusion
ACS Paragon Plus Environment
Page 20 of 26
Page 21 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
371
Within this study, force field parameters were developed for the organic HEHEHP
372
extractant and were used to investigate the solvation and dynamical behavior of the ligand in n-
373
dodecane, water, and biphasic n-dodecane + water solvents. Solvation behavior of HEHEHP
374
demonstrated expected hydrophilic and hydrophobic behavior of the ligand within the pure organic
375
and aqueous phases respectively. Within n-dodecane, ligand-ligand interactions were found to be
376
primarily between the head groups while such interactions were primarily between alkyl chains
377
within the water and biphasic n-dodecane + water solvents. Contrary to what is observed when
378
HEHEHP coordinates with metals, cluster analyses showed that the ligand exhibited a more
379
aggregative behavior than dimer formation in the absence of metal cations. The calculated thermal
380
diffusivities were in good agreement with the experimental data. Calculated diffusion coefficients
381
of HEHEHP within different solvents for a single- and multi-ligand system showed that favored
382
non-covalent interactions were found to primarily dictate the diffusivity within the single-ligand
383
system while cluster formation was observed to be the major influence within the multi-ligand
384
system. It is worth noting that the alkyl chains of the multi-ligand system exhibited a larger
385
diffusion coefficient in water than n-dodecane presumably due to the mono-ester functional group
386
prohibiting a complete micellar structure.
387
Conformational analysis of the orientation of the molecules revealed that n-dodecane and
388
HEHEHP possessed a parallel orientation at the interface, which confirms the hypothesis of
389
Vandegrift et al.38 Moreover, it was observed that increased concentration of the ligand instigated
390
a more perpendicular orientation at the interface, which suggests that concentration plays a critical
391
role in the extraction mechanism of HEHEHP since the ligand is known to extract metals by
392
coordinating with metal cations through their polar head groups. Solvation energies obtained by
393
the TI method were observed to describe expected solution behavior of HEHEHP by
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
394
demonstrating relative favorability towards n-dodecane and biphasic solvent when compared to
395
water.
396
Solvation and dynamical analyses carried out in this study shows that the protocol used to
397
generate charge modified GAFF parameters is of reasonable accuracy and, thus, can be used for
398
future parameterization of extractant ligands. Additionally, interfacial analyses suggest that
399
concentration is key for HEHEHP to obtain optimal configuration for the extraction of metals.
400
These effects will be studied in future work along with systems that fully mimic an ALSEP process
401
such as the inclusion of TEHDGA, nitric acid, and ultimately heavy metals.
402
V. Acknowledgements
403
Authors gratefully acknowledge the allocated computational resources from the High
404
Performance Computing Facility by the Computing, Communications, and Information
405
Technologies (CCIT) center at the Colorado School of Mines. This research was financially
406
supported by the U.S. Department of Energy, Office of Nuclear Energy, and Nuclear Energy
407
University Program (NEUP).
408
VI. Supporting Information
409
Values of calculated relativistic charges and coordinates of optimized structures used within this
410
investigation, RDF cut-off distances, cluster distribution of HEHEHP (0.75M) within three
411
solvents, RDF plots for pure solvent (n-dodecane/water) systems, in depth analysis of expected
412
HEHEHP behavior within pure solvent systems, time stamps of the canonical simulation used for
413
interfacial analyses of HEHEHP within a multi-ligand system, and reasons for using the TI method
414
are provided within the supporting information along with this manuscript.
415
VII. References
ACS Paragon Plus Environment
Page 22 of 26
Page 23 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
416
(1)
Nuclear Energy Agency. Nuclear Energy Today; 2012.
417 418 419
(2)
Salvatores, M.; Palmiotti, G. Radioactive Waste Partitioning and Transmutation within Advanced Fuel Cycles: Achievements and Challenges. Prog. Part. Nucl. Phys. 2011, 66, 144–166.
420 421 422
(3)
Muller, J. M.; Galley, S. S.; Albrecht-Schmitt, T. E.; Nash, K. L. Characterization of Lanthanide Complexes with Bis-1,2,3-Triazole- Bipyridine Ligands Involved in Actinide/Lanthanide Separation. Inorg. Chem. 2016, 55, 11454–11461.
423 424
(4)
Aneheim, E. H. K. Development of a Solvent Extraction Process for Group Actinide Recovery from Used Nuclear Fuel, 2012.
425 426
(5)
Gelis, A. V; Lumetta, G. J. Actinide Lanthanide Separation Process-ALSEP. Ind. Eng. Chem. Res. 2014, 53, 1624–1631.
427 428
(6)
Glatz, J. P. Spent Fuel Dissolution and Reprocessing Processes; Elsevier Inc., 2012; Vol. 5.
429 430
(7)
Peppard, D. F.; Mason, G. W.; Lewey, S. Di N-Octyl Phosphonic Acid as a Selective Extractant for Metallic Cations. J. Inorg. Nucl. Chem. 1964, 27, 2065–2073.
431 432
(8)
Herbst, R. S.; Baron, P.; Nilsson, M. Standard and Advanced Separation: PUREX Processes for Nuclear Fuel Reprocessing; Woodhead Publishing Limited, 2011.
433 434 435
(9)
Braley, J. C.; Carter, J. C.; Sinkov, S. I.; Nash, K. L.; Lumetta, G. J. The Role of Carboxylic Acids in TALSQuEAK Separations. J. Coord. Chem. 2012, 65 (16), 2862– 2876.
436 437 438
(10)
Brown, M. A.; Wardle, K. E.; Lumetta, G.; Gelis, A. V. Accomplishing Equilibrium in ALSEP: Demonstrations of Modified Process Chemistry on 3-D Printed Enhanced Annular Centrifugal Contactors. Procedia Chem. 2016, 21, 167–173.
439 440 441 442
(11)
Weaver, B.; Kappelmann, F. A. TALSPEAK: A New Method of Separating Americium and Curium from the Lanthanides by Extraction from an Aqueous Solution of an Aminopolyacetic Organophosphate or Phosphonate. U.S. At. Energy Comm. 1964, ORNL (3559), 1–67.
443 444 445
(12)
Danesi, P. R.; Cianetti, C. Kinetics and Mechanism of the Interfacial Mass Transfer of Eu(III) in the System: Bis(2-Ethylhexyl)phosphoric Acid, N -Dodecane-NaCl, Lactic Acid, Polyaminocarboxylic Acid, Water. Sep. Sci. Technol. 1982, 17 (7), 969–984.
446 447 448
(13)
Matsuyama, H.; Okamoto, T.; Teramoto, M. Kinetic Studies of Exchange Reactions Between Rare Earth Metal Ions and Their Diethylene-Triaminepentaacetic Acid Complexes. J. Chem. Eng. Japan 1989, 459–468.
449 450 451
(14)
Kolařík, Z.; Koch, G.; Kuhn, W. Acidic Organophosphorus Extractants-XVIII. The Rate of lanthanide(III) Extraction by di(2-Ethylhexyl) Phosphoric Acid from Complexing Media. J. Inorg. Nucl. Chem. 1974, 36 (4), 905–909.
452 453
(15)
Frisch, M. J.; Trucks, G. W.; Schlegel, H. B.; Scuseria, G. E.; Robb, M. A.; Cheeseman, J. R.; Scalmani, G.; Barone, V.; Mennucci, B.; Petersson, G. A.; et al. Gaussian 09, Revision
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
454
C.01.
455 456 457 458
(16)
Zhao, Y.; Truhlar, D. G. The M06 Suite of Density Functionals for Main Group Thermochemistry, Thermochemical Kinetics, Noncovalent Interactions, Excited States, and Transition Elements: Two New Functionals and Systematic Testing of Four M06Class Functionals and 12 Other Function. Theor. Chem. Acc. 2008, 120, 215–241.
459 460 461
(17)
Montgomery, J. A.; Frisch, M. J.; Ochterski, J. W.; Petersson, G. A. A Complete Basis Set Model Chemistry. VI. Use of Density Functional Geometries and Frequencies. J. Chem. Phys. 1999, 110 (6), 2822–2598.
462 463
(18)
Singh, U. C.; Kollman, P. A. An Approach to Computing Electrostatic Charges for Molecules. J. Comput. Chem. 1984, 5 (2), 129–145.
464 465 466
(19)
Kendall, R. A.; Dunning, T. H.; Harrison, R. J.; Dunning, T. H. Electron Affinities of the First-Row Atoms Revisited. Systematic Basis Sets and Wave Functions. J. Chem. Phys. 1992, 96 (9), 6796–6806.
467 468
(20)
Besler, B. H.; Merz, K. M.; Kollman, P. A. Atomic Charges Derived from Semiempirical Methods. J. Comput. Chem. 1990, 11 (4), 431–439.
469 470 471 472
(21)
Schutt, T. C.; Bharadwaj, V. S.; Hegde, G. A.; Johns, A. J.; Maupin, C. M. In Silico Insights into the Solvation Characteristics of the Ionic Liquid 1-Methyltriethoxy-3Ethylimidazolium Acetate for Cellulosic Biomass. Phys. Chem. Chem. Phys. 2016, 18, 23715–23726.
473 474
(22)
Wang, J. M.; Wolf, R. M.; Caldwell, J. W.; Kollman, P. a; Case, D. a. Development and Testing of a General Amber Force Field. J. Comput. Chem. 2004, 25 (9), 1157–1174.
475 476 477
(23)
Wang, J.; Wang, W.; Kollman, P. A.; Case, D. A. Automatic Atom Type and Bond Type Perception in Molecular Mechanical Calculations. J. Mol. Graph. Model. 2006, 25, 247– 260.
478 479 480
(24)
Case, D. A.; Babin, J. T.; Berryman, R. M.; Betz, R. M.; Cai, Q.; Cerutti, D. S.; Chetham III, T. E.; Darden, T. A.; Duke, R. E.; Gohlke, H.; et al. Amber 14. University of California: San Francisco 2014.
481 482
(25)
Humphrey, W.; Dalke, A.; Schulten, K. VMD: Visual Molecular Dynamics. J. Mol. Graph. 1996, 14, 33–38.
483 484
(26)
Wu, Y.; Tepper, H. L.; Voth, G. A. Flexible Simple Point-Charge Water Model with Improved Liquid-State Properties. J. Chem. Phys. 2006, 124, 24503–234505.
485 486 487
(27)
Martinez, L.; Andrade, R.; Birgin, R. A.; Martinez, J. M. PACKMOL: A Package for Binding Initial Configurations for Molecular Dynamics Simulations. J. Comput. Chem. 2009, 30 (13), 2158–2164.
488 489 490
(28)
Kaus, J. W.; Pierce, L. T.; Walker, R. C.; Andrew McCammon, J. Improving the Efficiency of Free Energy Calculations in the Amber Molecular Dynamics Package. J. Chem. Theory Comput. 2013, 9, 4131–4139.
491
(29)
Tanner, J. E. Use of the Stimulated Echo in NMR Diffusion Studies. J. Chem. Phys. 1970,
ACS Paragon Plus Environment
Page 24 of 26
Page 25 of 26 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
The Journal of Physical Chemistry
492
52 (5), 2523–1768.
493 494 495
(30)
Baldwin, A. G.; Yang, Y.; Bridges, N. J.; Braley, J. C. Tributyl Phosphate Aggregation in the Presence of Metals: An Assessment Using Diffusion NMR Spectroscopy. J. Phys. Chem. B 2016, 120, 12184–12192.
496 497 498
(31)
Aguilar, M.; Liem, D. H. Studies on the Solvent Exctraction of Europium(III) by Di-(2Ethylhexyl)phosphoric Acid (HDEHP) in Toluene. Acta Chem. Scand. A 1976, 30, 313– 321.
499 500 501
(32)
Peppard, D. F.; Mason, G. W.; Hucher, I. Acidic Esters of Phosphonic Acid as Selective Extractants for Metallic Cations-Selected M(III) Tracer Studies. J. Inorg. Nucl. Chem. 1961, 18, 245–258.
502 503 504
(33)
Mason, G. W.; Metta, D. N.; Peppard, D. F. The Extraction of Selected M(III) Metals by Bis 2-Ethylhexyl Phosphoric Acid in N-Heptane. J. Inorg. Nucl. Chem. 1976, 38 (11), 2077–2079.
505 506 507
(34)
Comba, P.; Gloe, K.; Inoue, K.; Krüger, T.; Stephan, H.; Yoshizuka, K. Molecular Mechanics Calculations and the Metal Ion Selective Extraction of Lanthanoids. Inorg. Chem. 1998, 37 (13), 3310–3315.
508 509 510
(35)
Sella, C.; Nortier, P.; Bauer, D. A Molecular Modelling Study About the Influence of the Structure of Alkyl Chains of Dialkyl Phosphoric Acids on Liquid-Liquid Lanthanide (III) Extraction. Solvent Extr. Ion Exch. 1997, 15 (6), 931–960.
511 512 513
(36)
Yoshizuka, K.; Kosaka, H.; Shinohara, T.; Ohto, K.; Inoue, K. Structural Effect of Phosphonic Esters Having Bulky Substituents on the Extraction of Rare Earth Elements. Bull. Chem. Soc. Jpn. 1996, 69, 589–596.
514 515 516
(37)
Baes Jr., C. F. An Isopiestic Investigation of Di-(2-Ethylhexyl)-Phosphoric Acid (DPA) and Tri-N-Octylphosphine Oxide (TPO) in N-Octane. J. Phys. Chem. 1962, 66 (11), 1629–1634.
517 518
(38)
Vandegrift, G. F.; Horwitz, E. P. Interfacial Activity of Liquid-Liquid Extraction Reagents-I. Dialkyl Phosphorous Based Acids. J. Inorg. Nucl. Chem. 1980, 42, 119–125.
519 520 521 522
(39)
Di Anibal, C. V; Moroni, M. A.; Verdinelli, V.; Rodríguez, J. L.; Minardi, R.; Schulz, P. C.; Vuano, B. Critical Micelle Concentration of Tridecane, Tetradecane and Hexadecane Phosphonic Acids and Their Mono-and Disodium Salts. Coll. Surf.: A Physico. Eng. Aspects 2009, 348, 276–281.
523 524 525 526
(40)
Bauduin, P.; Testard, F.; Berthon, L.; Zemb, T. Relation between the Hydrophile/hydrophobe Ratio of Malonamide Extractants and the Stability of the Organic Phase: Investigation at High Extractant Concentrationsw. Phys. Chem. Chem. Phys. 2007, 9, 3776–3785.
527 528
ACS Paragon Plus Environment
The Journal of Physical Chemistry 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
529
TOC
530
ACS Paragon Plus Environment
Page 26 of 26