Daniel Massey1, Andrew Masters1, Jonathan Macdonald-Taylor2, David Woodhead3, Robin Taylor3. 1. Department of Chemical Engineering, The University of Manchester, Oxford Road, Manchester M13 9PL, U.K. 2. National Nuclear Laboratory, 5th Floor Chadwick House, Warrington Road, Birchwood Park, Warrington WA3 6AE, U.K. 3. National Nuclear Laboratory, Central Laboratory, Sellafield, Seascale CA20 1PG, U.K.
Abstract
Liquid-liquid extraction is a commonly used technique to separate metals and is a process that has particular relevance to the nuclear industry. There has been a drive to use environmentally friendly ligands composed only of carbon, hydrogen, nitrogen, and oxygen. One example is the i-SANEX process that has been developed to separate minor actinides from spent nuclear fuel. The underlying science of such processes, is, however, both complex and intriguing. Recent research indicates that the liquid phases involved are frequently structured fluids with a hierarchical organization of aggregates. Effective flow-sheet modeling of such processes is likely to benefit from the knowledge of the fundamental properties of these phases. As a stepping stone toward this, we have performed molecular dynamics simulations on a metal free i-SANEX system composed of the ligand N,N,N',N'-tetraoctyl diglycolamide (TODGA), diluent hydrogenated tetrapropylene (TPH), and polar species water and nitric acid. We have also studied the effects of adding n-octanol and swapping TPH for n-dodecane. It would seem sensible to understand this simpler system before introducing metal complexes. Such an understanding would ideally arise from studying the system's properties over a wide range of compositions. The large number of components, however, precludes a comprehensive scan of compositions, so we have chosen to study a fixed concentration of TODGA while varying the concentrations of water and nitric acid over a substantial range. Reverse aggregates are observed, with polar species in the interior in contact with the polar portions of the TODGA molecules and the organic diluent on the exterior in contact with the TODGA alkyl chains. These aggregates are irregular in shape and grow in size as the amount of water and nitric acid increases. At a sufficiently high polar content, a single extended cluster forms corresponding to the third phase formation. No well-defined bonding motifs were observed between the polar species and TODGA. The cluster size distribution fits an isodesmic model, where the Gibbs energy change of adding a TODGA molecule to a cluster ranges between 4.5 and 7.0 kJ mol-1, depending on the system composition. The addition of n-octanol was found to reduce the degree of aggregation, with n-octanol acting as a co-surfactant. Exchanging the diluent TPH for n-dodecane also decreased the aggregation. We present evidence that this is due to the greater penetration of n-dodecane into the reverse aggregates. It is known, however, that the propensity for the third phase formation is greater with n-dodecane as the diluent than is the case with TPH, but we argue that these two results are not contradictory. This research casts light on the driving forces for aggregation, informs process engineers as to what species are present, and indicates that flow-sheet liquid-liquid extraction modeling might benefit by incorporating an isodesmic aggregation approach.
Liquid-liquid extraction is a commonly used technique to separate metals and is a process that has particular relevance to the nuclear industry. There has been a drive to use environmentally friendly ligands composed only of carbon, hydrogen, nitrogen, and oxygen. One example is the i-SANEX process that has been developed to separate minor actinides from spent nuclear fuel. The underlying science of such processes, is, however, both complex and intriguing. Recent research indicates that the liquid phases involved are frequently structured fluids with a hierarchical organization of aggregates. Effective flow-sheet modeling of such processes is likely to benefit from the knowledge of the fundamental properties of these phases. As a stepping stone toward this, we have performed molecular dynamics simulations on a metal free i-SANEX system composed of the ligand N,N,N',N'-tetraoctyl diglycolamide (TODGA), diluent hydrogenated tetrapropylene (TPH), and polar species water and nitric acid. We have also studied the effects of adding n-octanol and swapping TPH for n-dodecane. It would seem sensible to understand this simpler system before introducing metal complexes. Such an understanding would ideally arise from studying the system's properties over a wide range of compositions. The large number of components, however, precludes a comprehensive scan of compositions, so we have chosen to study a fixed concentration of TODGA while varying the concentrations of water and nitric acid over a substantial range. Reverse aggregates are observed, with polar species in the interior in contact with the polar portions of the TODGA molecules and the organic diluent on the exterior in contact with the TODGA alkyl chains. These aggregates are irregular in shape and grow in size as the amount of water and nitric acid increases. At a sufficiently high polar content, a single extended cluster forms corresponding to the third phase formation. No well-defined bonding motifs were observed between the polar species and TODGA. The cluster size distribution fits an isodesmic model, where the Gibbs energy change of adding a TODGA molecule to a cluster ranges between 4.5 and 7.0 kJ mol-1, depending on the system composition. The addition of n-octanol was found to reduce the degree of aggregation, with n-octanol acting as a co-surfactant. Exchanging the diluent TPH for n-dodecane also decreased the aggregation. We present evidence that this is due to the greater penetration of n-dodecane into the reverse aggregates. It is known, however, that the propensity for the third phase formation is greater with n-dodecane as the diluent than is the case with TPH, but we argue that these two results are not contradictory. This research casts light on the driving forces for aggregation, informs process engineers as to what species are present, and indicates that flow-sheet liquid-liquid extraction modeling might benefit by incorporating an isodesmic aggregation approach.
The most common way to separate metals
is liquid–liquid
extraction.[1−8] Taking nuclear fuel recycling as an important example, spent nuclear
fuel is delay-stored to reduce the effects of short-lived radioactive
species and is then dissolved in nitric acid. This is contacted with
an organic diluent and an appropriate ligand. The ligand binds selectively
to the desired metal or metals to form a complex, and this complex
moves from the aqueous to the organic phase, thus achieving the separation.
The plutonium–uranium reduction extraction (PUREX) process
for extracting uranium and plutonium was patented in 1947 and is still
in common use.[9,10] The ligand is n-tributyl phosphate (TBP) and sophisticated flow-sheet models exist
for this process.[11−14] More recently, other extraction processes, based on more environmentally
friendly CHON ingredients, containing only C, H, O, and N, are coming
to the fore.[15,16] These can be decomposed, yielding
only gaseous products, thereby reducing the volume of radioactive
waste.What is becoming increasingly clear, however, is that
the organic
phase, containing the extracted metal, is far from a simple solution.
Both atomistic computer simulations, small-angle neutron (SANS) and
X-ray (SAXS) scattering experiments, indicate the presence of discrete
aggregated structures, resulting from a complex interplay between
the interactions between metal complexes and the reverse-emulsion-like
structures resulting from having an amphiphilic ligand in a non-polar
environment.[1,7,17−26] At sufficiently high metal loadings or at sufficiently high acidities,
these discrete aggregates within the organic phase fuse either to
form a precipitate or else to form what appears to be a continuous,
percolating structure containing connected regions of polar molecules,
such as water and nitric acid, and connected regions of non-polar
molecules, such as the hydrocarbon diluent. The metal complexes are
in the polar region, while unbound amphiphilic ligands are largely
at the interface. This is the so-called third phase, which, while
very interesting, is highly undesirable in any extraction process,
not least because high concentrations of uranium and plutonium may
risk nuclear criticality.[1,19,20,22,27−37]The detailed structures of these phases and the molecular
driving
forces for the phase transition to the third phase are still far from
clear. Molecular dynamics simulations struggle with achieving a large
enough system size to capture all the details of the aggregated structures,
with the third phase being an especially difficult challenge. SANS
and SAXS experiments require the use of models to interpret the scattering
profiles and simplifying assumptions concerning the shapes of the
aggregates have to be made. Arguably, a combination of atomistic computer
simulation and SANS/SAXS experiments is a powerful way to proceed,
with the experimental work providing at least partial validation of
the simulations and the simulations giving detailed information on
the molecular interactions and structures. What seems to emerge from
these studies is that the aggregates are not simple, ordered structures.
They are not mono-disperse and do not have a simple shape. Snapshots
from the simulation indicate very disordered, flexible structures
rather than the spheres, cylinders, and bi-layers that form the framework
for understanding amphiphiles in aqueous solution.[38,39]In this paper, we present results aimed at increasing our
understanding
of these structured organic phases. We consider, as a ligand, the
diglycolamide N,N,N′,N′-tetraoctyl diglycolamide, commonly
known as TODGA. Its chemical structure is given in Figure a[40] drawn using the software Marvin 18.3.0, 2018, ChemAxon.[41] TODGA is a key ingredient in the i-SANEX process,[42−47] which shows great promise for the separation of minor trivalent
actinides (e.g. americium and curium) from high-level waste (HLW)
solutions generated by PUREX or similar extraction processes. The
removal of actinides significantly reduces the time taken for nuclear
waste to be isolated from the environment before its radiotoxicity
falls below that of the uranium ore. Also, the minor actinides are
the main contributors to heat generation in the longer term (once
plutonium is separated from spent fuel), and their removal enables
a more compact arrangement of radioactive waste in the disposal facility,
thus reducing the size of the disposal facility. This is the so-called
partitioning and transmutation strategy for recycling actinides in
a fully closed fuel cycle.[48−52] In this strategy, after the PUREX process has been used to extract
uranium, plutonium, and possibly other metals such as neptunium and
technetium, the remaining HLW is contacted with a mixture of a diluent
hydrocarbon, TODGA, and n-octanol. A commonly used
diluent is hydrogenated tetrapropylene (TPH). This is a branched dodecane
and its structure is shown in Figure b.[53] Other diluents are
also used, for example, isane and odorless kerosene, of which n-dodecane is a major constituent. Furthermore, the addition
of n-octanol as a phase modifier has been shown to
reduce the propensity for third phase formation and/or precipitation.[8,23,33,54−56]
Figure 1
(a) Structure of a TODGA molecule. (b) Structure of TPH.
(a) Structure of a TODGA molecule. (b) Structure of TPH.The i-SANEX organic phase is a complex mixture
of a metal complex,
TPH, TODGA, n-octanol, water, and nitric acid. In
order to study this system, it makes sense to build up complexity
in stages. We thus do not consider the metal in this article but focus
instead on the properties of the metal-free mixture, which is still
a complicated system. That said, the aggregates formed in the metal-free
system may be regarded as receptacles for metal complexes, so this
study also provides some useful background for the analysis of metal-containing
systems.[40] This metal-free system has been
studied experimentally using, among other techniques, SAXS and SANS
measurements, both in a normal organic phase and in the third phase.
These studies indicate that at low acidity and water concentrations,
TODGA in the organic phase will mainly be found in the form of monomers
and dimers, but at higher acid and water concentrations, small reverse-micelles
appear containing a small number of TODGA monomers, typically in the
range of 3–6, along with associated acid and water.[17,19,21,57]Our aim in this article is to study the metal-free i-SANEX
system,
exploring the link between molecular interactions and the aggregates
that result. Previous simulations of metal-free systems have shown
that diglycolamides form reverse structures in a non-polar diluent,
and there has been extensive analysis of the molecular organization
of these clusters and the distributions of cluster sizes and compositions.[19,21,58−63] A very recent article reports the results of large-scale simulations
of the TODGA/n-dodecane/water/nitric acid system
as well as providing a detailed description of the molecular structure
of the aggregates.[64]In this article,
we aim to add to this existing knowledge by looking
at the thermodynamics of aggregate formation and studying the effects
of changing the diluent and of adding n-octanol.
Yaita et al.[18] and Nave et al.[19] report experimental results on these systems,
including scattering experiments (SANS and SAXS) that provide information
on clustering. They also provide the full composition of the organic
phase, including the concentration of water. As shown in a recent
study, water plays an important role in tuning the lanthanide selectivity
of diglycolamides.[65] It is thus very likely
that it also plays a significant role in actinides. A knowledge of
its concentration can therefore be invaluable when comparing simulation
with experiment. Yaita et al.[18] studied
a metal-free organic phase where the TODGA and nitric acid concentrations
in the organic phase were 0.1 M and 0.05 M, respectively. Nave et
al.[19] focused on an organic phase with
the same TODGA concentration as above but a nitric acid concentration
of 0.01 M. In both cases, these organic phases were in equilibrium
with corresponding aqueous phases. These systems have been previously
simulated[63,64] and the clustering discussed. Bell et al.[61] studied nitric acid extraction into TODGA at
a higher nitric acid concentration. For 0.1 M TODGA, their data go
up to an organic nitric acid concentration of 0.132 M. They also present
modeling that suggests that four water molecules are extracted with
each nitric acid molecule. It is of interest to study these higher
concentrations where aggregation effects are more pronounced. This
is both because of the intrinsic scientific interest of such systems
and also because such studies may help inform the flow-sheet modeling
used in practical applications. Such simulation studies have been
reported previously[63,64] and one of our aims here is to
extend the composition space investigated. After looking briefly at
pure TODGA and TODGA/TPH mixtures, we investigate the effects of varying
the amount of water and nitric acid in the system on local structure
and aggregate formation. We then add n-octanol to
study its effect on cluster formation. We also briefly consider the
effects of changing the diluent from TPH to n-dodecane.
We finish up with a discussion.
Methodology
The OPLS-2005 all-atom forcefield and combining
rule[66] was used for TPH, n-dodecane,
and n-octanol and also for the non-bonded parameters
in TODGA. The TIP3P model was used for water for compatibility with
this forcefield. The TODGA atomic charges were those previously reported
by Singh et al.[63] The nitric acid parameters
came from Price et al.[67] (also using geometric
combining following the OPLS procedures) and are given explicitly
in the Supporting Information. This nitric
acid model was also used by Mu et al.[22] in their study of a TBP system. It should be noted that this forcefield
does not allow for the breakage and formation of bonds, which means
that there is no mechanism allowing nitric acid to dissociate into
hydronium and nitrate ions and no mechanism allowing for the protonation
of the carboxyl oxygens in TODGA. For this, one requires more sophisticated
simulation techniques, such as constant pH simulations. Recent examples
of such studies are given in refs (68) and (69). Experimental studies by Musikas and Hubert[70] on the related ligand N,N′-dimethyldioctyl malonamide indicate that in the
presence of nitric acid, the protonated ligand is extracted in relatively
low concentrations, estimated to be at a mole fraction of 0.075 of
the total ligand extracted under the conditions studied. Lefrançois
et al.[71] also discuss such effects based
on an analysis of NMR data, focusing on the extraction of a quaternary
malonamide. Their studies indicate that protonation is a significant
effect in the third phase but less so in the organic phase. Singh
et al.[63] ran simulations on the i-SANEX
system considered here, both with molecular and dissociated nitric
acid in the organic phase, finding little effect on the degree of
clustering. We are thus hopeful that our neglect of protonation will
not seriously affect our conclusions.The simulations were completed
using the GROMACS 2018.4 software
package.[72−79] All simulations used cubic periodic boundary conditions and a time
step of 1 fs. For van der Waals and short-range Coulomb interactions,
a 1.2 nm cut-off was implemented and potential shift functions were
applied from 0.9 to 1.2 nm to conserve energies at the cut-off. Particle-mesh
Ewald summation[80] was used for the long-range
electrostatic potential. The Fourier spacing was 0.12 nm–1, and cubic interpolation was employed. Bonds involving hydrogen
were constrained using LINCS. Simulations were all performed in the
isobaric isothermal NpT ensemble using a leapfrog
Verlet integrator at a pressure and a temperature of 1 bar and 298.15
K, respectively. For each system configuration, the molecules were
randomly inserted into a 6 nm cubic box. The systems were equilibrated
for 10 ns, first conducting a 5 ns run using the velocity-rescaling
thermostat and the Berendsen barostat with a time constant of 1 ps,
followed by a second run using the Nosé–Hoover thermostat
and the Parrinello–Rahman barostat with a time constant of
5 ps. The production runs were for 40 ns, again using the Nosé–Hoover
thermostat and the Parrinello–Rahman barostat.To help
analyze the local structure of the systems, we make use
of co-ordination numbers, CNαβ, defined byHere, ρβ is
the number density of atoms
of type β and gαβ(r) is the atom–atom radial distribution function
for atom types α and β. rmin is the position of the first minimum of gαβ(r). This co-ordination number gives an estimate
of the number of β atoms that are in the first co-ordination
shell of an α atom.In order to analyze
the degree of aggregation, we made use of cluster
analysis. This requires a criterion to decide whether two molecules
are connected. GROMACS provides an in-built cluster analyzer where
the connectivity criterion depends on the distance between two specified
atoms. We are also interested in analyzing hydrogen-bonded clusters.
For this, we used the algorithm of Sevick et al.,[81] as modified by Mu et al.,[22] to
estimate the number and sizes of clusters formed by TODGA, HNO3, and H2O. The criterion for a hydrogen bond was
a donor–acceptor distance of less than 0.36 nm and a bond angle
between the donor, the hydrogen atom, and the atom bonded to the hydrogen
of 150° or greater. We found that these criteria gave predictions
in reasonable agreement with an intuitive inspection of simulation
snapshots and that our general conclusions did not depend sensitively
upon the precise numbers chosen.
Results
Pure TODGA System
A pure TODGA system containing 800
molecules was simulated at 1 bar and 298.15 K as described previously,
except that a production run of 20 ns was found to be sufficient.
The average density was 0.9373 ± 0.0003 g cm–3 as opposed to experimental values for pure TODGA of 0.910 g cm–3.[82]The system size
dependence of this result was found to be negligible. No doubt, the
forcefield could be adjusted to give closer agreement with the experimental
density, but considerably more experimental data are required to do
such a fit reliably. As the purpose of this paper is to explore trends
rather than to obtain quantitative predict ions, we believed this
level of agreement to be acceptable.
TODGA/TPH
In the TODGA/TPH system, the composition
was chosen to give a TODGA molarity of approximately 0.1, which is
typically used in studies of this sort.[11,18,33,56,60,63,83−85] This system comprised 10 TODGA molecules and 400
TPH molecules. The co-ordination number from the carbonyl oxygen–carbonyl
oxygen distribution function was 0.8 while the ether oxygen–ether
oxygen co-ordination number was 0.7. These numbers indicate an attraction
between TODGA molecules. Visual inspection of simulation snapshots
showed the formation of small clusters. Typical examples are shown
in Figure . For a
more detailed analysis of the molecular organization within these
clusters, we refer elsewhere.[64] These clusters
are mobile, as witnessed by the very different molecular arrangements
shown in the two snapshots in Figure . This variation indicates that the interactions between
the polar groups are somewhat unspecific. We used the Gromacs[86] cluster analyzer, where the connection criterion
was a separation of less than 0.7 nm between two TODGA carbonyl oxygens.
This distance corresponds to the first minimum of the distribution
function. The analysis is an average over the 40 ns production run.
A graph showing the cluster distribution is shown in Figure , indicating that the TODGAs
exist mainly as monomers, dimers, or trimers. Here, W is the average mole fraction of TODGA
molecules to be found in a TODGA cluster with aggregation number n.
Figure 2
Snapshots of TODGA forming small clusters. Red—oxygen,
blue—nitrogen,
cyan—carbon, white—hydrogen.
Figure 3
Cluster size distribution of TODGA in the TODGA-TPH system,
defined
in Table . Here, n is the number of TODGAs in a cluster, while W is the average mole fraction of TODGA
in an n-cluster.
Snapshots of TODGA forming small clusters. Red—oxygen,
blue—nitrogen,
cyan—carbon, white—hydrogen.Cluster size distribution of TODGA in the TODGA-TPH system,
defined
in Table . Here, n is the number of TODGAs in a cluster, while W is the average mole fraction of TODGA
in an n-cluster.
Table 1
Compositions of Simulated Systems
in Terms of Both Molarity, mol dm–3, and below the
Number of Molecules Simulateda
system
1
2
3
4
5
6
third phase
TODGA
0.09
0.09
0.09
0.09
0.09
0.09
0.15
10
10
10
10
10
10
200
H2O
0.07
0.15
0.23
0.15
0.30
0.45
0.07
8
16
24
16
32
48
90
HNO3
0.04
0.08
0.11
0.04
0.07
0.11
0.77
4
8
12
4
8
12
1000
TPH
400
400
400
400
400
400
5000
Thus, for example, in system 1,
the TODGA molarity was 0.09 mol dm–3 and 10 TODGA
molecules were simulated.
Effects of Acid and Water
We have systematically varied
the amount of water and nitric acid in the organic phase to study
how these polar molecules affect the liquid structure. Systems 1–3
have a water/nitric acid ratio of 2, while systems 4–6 have
a water/nitric acid ratio of 4. For both compositions, we vary the
amount of polar material, with details given in Table . The maximum nitric acid concentration studied was 0.11 M,
while the largest organic nitric acid concentration reported by Bell
et al.[61] for a TODGA concentration of 0.1
M was 0.132 M. We thus believe our chosen compositions to be physically
reasonable and not prone to phase separation. We carefully checked
all our simulation runs for any signs of liquid–liquid demixing,
and no such trends were observed. On the timescale of the simulation,
extensive visual inspection indicated that molecules entered and left
clusters on a timescale of approximately 1 ns, while the timescale
for the formation or break-up of a whole cluster was approximately
3–5 ns. In Figure S6 in the Supporting Information, we show a plot of the TODGA cluster distribution
over time for system 6, which has the highest content of water and
nitric acid simulated. The plot shows no sign of cluster growth with
time. These plots were similar for all systems studied. We thus believe
that all the results reported here are for thermodynamically stable
phases. Clustering is observed in all these systems. These clusters
are irregular in shape and are dynamic in nature. It would be of interest
to quantitatively compare this dynamics with experimental observations.
Such studies have been conducted on micelles in aqueous phases, for
example, as done by Aniansson et al.[87] and
would be an interesting future line of study.Thus, for example, in system 1,
the TODGA molarity was 0.09 mol dm–3 and 10 TODGA
molecules were simulated.We begin by looking at the interactions between the
polar species
and TODGA by making use of a co-ordination number analysis. A sub-set
of results is shown in Table .
Table 2
Co-ordination Numbers for Certain
Atoms in the Systems Simulateda
pair (first
atom reference)
system 1
system 2
system 3
system 4
system 5
system 6
rmin/nm
TODGA(O)–TODGA(O)
0.96
0.70
0.67
0.88
0.73
0.60
0.61
TODGA(O)–HNO3(H)
0.12
0.30
0.44
0.13
0.29
0.44
0.36
TODGA(O)–H2O(H)
0.21
0.28
0.31
0.37
0.48
0.46
0.25
HNO3(N)–HNO3(N)
0.04
0.11
0.19
0.06
0.12
0.20
0.68
HNO3(N)–H2O(O)
0.09
0.21
0.36
0.18
0.44
0.80
0.60
H2O(O)–H2O(O)
0.34
0.77
1.16
0.74
1.88
3.85
0.65
TODGA(O) refers to a carbonyl oxygen
atom in TODGA.
TODGA(O) refers to a carbonyl oxygen
atom in TODGA.The polar region of TODGA corresponds to the two amide
groups connected
by an ether oxygen. Many of these atoms have significant partial charges
(see the Supporting Information). It is
therefore likely that all these atoms are involved, to a greater or
lesser extent, in the formation of clusters via polar interactions.
Analysis of the co-ordination numbers and the radial distribution
functions indicate, however, that the prime binding site is the carbonyl
oxygen. We thus begin by looking at which species bind to these carbonyl
oxygens. The obvious candidates are hydrogen in nitric acid, hydrogens
in water, and the positively charged atoms in TODGA, such as the carbonyl
carbon. As noted previously, however, there only appear to be rather
unspecific TODGA–TODGA interactions, so we focus here on the
water and nitric acid interactions.The data indicate that as
the amount of polar material increases
at a fixed water/nitric acid ratio, the nitric acid tends to displace
water as the main co-ordinator to the carbonyl oxygen, implying that
nitric acid has a stronger interaction than does water. This is the
same trend as observed in TBP systems, but there the effects are much
more pronounced.[22,88]There are, however, no
clear hydrogen bonding motifs to be observed
in the clusters. We show snapshots of how the polar molecules interact
with TODGAs in Figure but, unlike, for example, TBP systems where there are clearly defined
bridging molecules and strings of molecules connecting TBPs,[22] this is not so clearly defined in this system.
In Figure b, we can
see hydrogen of nitric acid clearly being attracted to a carbonyl
oxygen. In Figure c,d, we can see that water also acts as a bridging molecule with
its two hydrogen atoms being used to form a hydrogen bonding network.
However, it must be stressed that these are not recurring motifs.
There is a large variability in these structures and no well-defined
molecular strings or bridges. The clusters are irregular and mobile,
and while there are correlations between the various polar groups,
as evidenced by the radial distribution functions and the co-ordination
numbers given in Table , the picture is much more that of a rather disorganized polar glue
holding the clusters together. For a more detailed analysis of the
molecular organization, we refer to Sadhu and Clark.[64]
Figure 4
Snapshots of polar molecules interacting with TODGA (hydrocarbon
chains hidden for clarity). Red—oxygen, cyan—carbon,
blue—nitrogen, white—hydrogen.
Snapshots of polar molecules interacting with TODGA (hydrocarbon
chains hidden for clarity). Red—oxygen, cyan—carbon,
blue—nitrogen, white—hydrogen.
Cluster Analysis
As shown in the snapshots in Figure , the system forms
TODGA clusters. At a fixed water/nitric acid ratio, the greater the
polar content, the greater the degree of clustering. Further discussion
is provided by Sadhu and Clark.[64]
Figure 5
Snapshots of
systems with increasing polar contents and TPH hidden
for clarity. Red—oxygen, cyan—carbon, blue—nitrogen,
white—hydrogen. (a) TODGA-TPH system. (b) System 1. (c) System
3. (d) Third phase.
Snapshots of
systems with increasing polar contents and TPH hidden
for clarity. Red—oxygen, cyan—carbon, blue—nitrogen,
white—hydrogen. (a) TODGA-TPH system. (b) System 1. (c) System
3. (d) Third phase.At very high polar contents, the system forms an
infinitely connected
polar aggregate, which corresponds to the third phase formation. The
composition of the simulated system is given in the Third
Phase column of Table . This composition is again not chosen to correspond to systems
that have been studied experimentally. It does, however, give an indication
of the structure of such phases.As noted previously, these
clusters are irregular in shape and
are dynamic in nature. The polar groups are, by and large, in the
interior of the aggregate. Such structures are often called reverse
micelles in the literature, but it must be noted that the shapes are
not simple spheres, rods, or ellipsoids, which are images often conjured
up when discussing micelles. Extensive viewing of movies of the simulations
show that these aggregates form and break up on a timescale similar
to that already reported.The cluster distribution was analyzed
using the hydrogen-bonding
criterion discussed earlier, and the results are averages over a 40
ns period. These clusters contain TODGA, nitric acid, and water molecules,
and there is a distribution of all three species. To simplify the
analysis, we first classify clusters according to the TODGA content
alone and later go on to consider the number of polar species, here
water and nitric acid, which are also associated with them.We always observe a distribution of cluster sizes rather than a
single cluster size. A simple model for this is the isodesmic model,[38,60,89] where we assume that the Gibbs
energy change of adding a single TODGA molecule to an n-cluster, TODGA, is independent of n. This is tantamount to saying that the chemical equilibrium
constant, K, foris independent of n. This
approximation yieldsHere, a is the activity
of TODGAn. We assume Henry’s law applies, so we
havewhere we have divided the cluster concentration
by the standard concentration of 1 M so as to obtain a dimensionless
activity. In Figure , we plot against (n – 1)
which, if the isodesmic approximation holds, should yield a straight
line of slope ln K. The graphs indicate that this
is a reasonably good approximation and yield equilibrium constants
in the range 4–6, the values increasing with increasing polar
content of the system. There are, however, discrepancies from the
straight line behavior at a large n. This is first
due to statistical error, for large clusters have smaller concentrations
than small ones. The other reason is that eq is only valid for a large system. In our
system of 10 TODGA molecules, system size effects will come into play
for large clusters. Our estimates for K are typically
based on cluster sizes up to n = 5, where there is
good straight line behavior.
Figure 6
against n – 1 for
system 3.
against n – 1 for
system 3.These K values may be related
to the Gibbs energies
of aggregation, ΔGagg, given bywhere R is the gas constant
and T is the absolute temperature. Estimates for K and ΔGagg are given
in Table .
Table 3
Equilibrium Constants and Gibbs Energies
of Aggregation for Systems 1–6a
system
K
ΔGagg/(kJ mol–1)
1
6.2 (1.0)
4.52 (0.06)
2
7.2 (1.0)
4.88
(0.06)
3
10.1 (1.0)
5.73 (0.09)
4
8.6 (1.0)
5.33 (0.06)
5
10.8 (1.0)
5.91
(0.06)
6
159 (1.0)
6.85 (0.06)
Errors are given in brackets.
Errors are given in brackets.As noted by Špadina and Bohinc,[1] the Gibbs energies of aggregation are comparable with thermal
energies
and the values increase with the amount of polar material present.
Many more data points would be needed, however, to establish a quantitative
relationship between ΔGagg and system
composition.The cluster algorithm can also tell us how many
water and nitric
acid molecules may be found in an n-cluster of TODGA,
and again there is a distribution. We provide such data in the Supporting Information. To study how the cluster
composition varies with TODGA aggregation number, n, we divide the average number of waters and nitric acid molecules
in such a cluster by n, so as to get the number of
polar species per TODGA molecule. In Figures and 8 we plot these
quantities against n for systems 3 and 6, respectively.
For system 3, the lines are approximately horizontal within the statistic
error, indicating a roughly constant composition. For system 6, there
is also not a great deal of variation, though longer runs on larger
systems would be needed to check, for example, whether the maximum
at n = 3 is statistically significant.
Figure 7
Average number
of polar molecules per TODGA vs the TODGA aggregation
number, n. Black—HNO3, red—H2O, green—total polar. Data for system 3.
Figure 8
Average number of polar molecules per TODGA vs the TODGA
aggregation
number, n. Black—HNO3, red—H2O, green—total polar. Data for system 6.
Average number
of polar molecules per TODGA vs the TODGA aggregation
number, n. Black—HNO3, red—H2O, green—total polar. Data for system 3.Average number of polar molecules per TODGA vs the TODGA
aggregation
number, n. Black—HNO3, red—H2O, green—total polar. Data for system 6.These observations are consistent with the observed
isodesmic behavior,
which would also suggest that the cluster composition is likely to
depend only weakly on aggregation number.It should be re-iterated,
though, that the cluster algorithm used
only includes molecules engaged in hydrogen bonding. Thus, there will
be water and nitric acid molecules that may well be associated with
these clusters but not counted by the algorithm.
Effects of n-Octanol on Cluster Formation
As noted in the Introduction, n-octanol is also
a standard ingredient in the i-SANEX process as it seems to reduce
the propensity for forming the unwanted third phase.[55,56] It also plays a significant role in nitric acid extraction into
the organic phase.[11,90] Abécassis et al. and Lu
et al. discuss the various roles that n-octanol can
play in these systems.[1,55,91] First, it can act as a co-surfactant and be present in the reverse
aggregates. Second, it can act as a co-solvent, affecting the interactions
between aggregates. This latter effect is argued to be dominant at
high n-octanol concentrations.[91] We have therefore conducted a limited number of simulations
for the systems listed earlier but with 20 n-octanol
molecules added to each. This corresponds to an n-octanol concentration of approximately 0.2 M. At this level of concentration,
we primarily study the co-surfactant behavior. As may be seen from
the snapshots, shown in Figure , for the modified system 1 and, more formally, from a co-ordination
number analysis, n-octanol is incorporated into the
clusters and the hydroxyl group interacts with the other polar species
present, that is, water, nitric acid, the polar regions of TODGA,
and other n-octanols. A few n-octanols
are observed to form small, independent aggregates, typically containing
a little water and nitric acid. The full list of co-ordination numbers
concerning n-octanol are given in the Supporting Information, but, taking system 3
as an example, the co-ordination numbers for the n-octanol OH group interacting with the TODGA carbonyl oxygen, water,
nitric acid, and a second n-octanol OH group are
all approximately 0.2. If we look at the TODGA cluster distribution,
we see that the degree of clustering is reduced by the addition of n-octanol. Taking system 3 as an example, Figure shows how the cluster distribution
alters upon the addition of n-octanol. The equilibrium
constant falls from 10.1 to 7.7. It would appear that n-octanol competes with TODGA, to some extent, for binding polar molecules
which, in turn, reduces the driving force for TODGA clustering.
Figure 9
Snapshots of
system 1 with added n-octanol. Purple—octanol,
cyan—TODGA, red—H2O, green—HNO3.
Figure 10
Weighted TODGA distribution in system 3 both without (black)
and
with (red) n-octanol.
Snapshots of
system 1 with added n-octanol. Purple—octanol,
cyan—TODGA, red—H2O, green—HNO3.Weighted TODGA distribution in system 3 both without (black)
and
with (red) n-octanol.The concentrations of n-octanol
are too small
in these cases to observe possible co-solvent effects. Further study
is needed on very large systems, however, to investigate the effects
of this on aggregate–aggregate interactions.
Effects of Organic Diluent—n-Dodecane
vs TPH
It has been observed that changing the organic diluent
to less branched alkanes tends to increase the propensity for third
phase formation.[27,56,92,93] While third phase properties are not the
focus of this article, this does suggest that a change of diluent
could affect clustering in the organic phase containing finite-sized
aggregates. We have therefore carried out a simulation where we replaced
the branched TPH by linear n-dodecane. This was observed
to reduce the degree of TODGA aggregation, with, for example, K changing from 10.1 to 6.1 in system 3. To help understand
why this happens, in Figure we present radial distribution functions of the diluent carbon
atoms around the amide nitrogen atom of TODGA. As seen from Figure a, this nitrogen
is the atom to which the TODGA alkyl chains are attached. The distribution
functions show that n-dodecane has a small, but significantly
greater penetration into the TODGA molecules than does TPH. One might
imagine that a straight chain can better worm its way into the interior
of a reverse aggregate than can TPH, which has a passing resemblance
to barbed wire.[94] As noted in standard
text-books,[23] in an oil/water/surfactant
system, a greater penetration of the oil into the surfactant film
leads to a greater curvature of the film toward the water. Our hypothesis
is that something similar is happening here. The greater penetration
of n-dodecane encourages greater curvature of the
aggregate, which corresponds to smaller aggregates and a reduced equilibrium
constant, K.
Figure 11
Radial distribution functions in system
3 for the TODGA amide nitrogen/diluent
carbon. Red—n-dodecane, black—TPH.
Radial distribution functions in system
3 for the TODGA amide nitrogen/diluent
carbon. Red—n-dodecane, black—TPH.At first sight, this result might seem to be at
odds with the fact
that third phase formation occurs more readily with n-dodecane as the diluent as compared to TPH. If n-dodecane tends to reduce aggregation, then one might imagine that
its use would also discourage the formation of the extended clusters
present in the third phase and thus decrease, rather than increase,
the propensity for third phase formation. As is the case with n-octanol, however, there are solvent effects which will
influence the interactions between aggregates and the change of diluent
is likely to affect this. Further studies of the third phase and third
phase/organic phase equilibrium will be needed to investigate this
question. What the results do show, however, is that there is a definite
effect of the diluent on clustering (Figure ).
Figure 12
Weighted TODGA distribution in system 3 using
TPH (black) and n-dodecane (red).
Weighted TODGA distribution in system 3 using
TPH (black) and n-dodecane (red).
Conclusions
We have conducted a series of molecular
dynamics simulations of
the organic phase of the metal-free i-SANEX system. The majority of
these simulations were for a system of TPH/TODGA/water/nitric acid,
though we did more limited studies on the effects of adding n-octanol and on the effects of changing the branched TPH
diluent to straight chain n-dodecane. We studied
a range of water/nitric acid compositions to determine the general
trends.The main result is that the TODGA molecules form irregular
clusters,
with the average cluster size increasing with the polar content of
the mixture. This is in qualitative agreement with the results of
SANS/SAXS experiments. We also note the distinct roles of nitric acid
and water in driving aggregation, and we refer to Sadhu and Clark[64] for a comprehensive discussion. We studied the
bonding that took place within these clusters and found that the carbonyl
oxygen was the main site for hydrogen bonding in a TODGA molecule.
Typically, nitric acid bound more strongly than water and water more
strongly than another TODGA, but all three interactions are present
in our simulated structures. These clusters are flexible and mobile,
and there is little evidence of dominant hydrogen-bonded bridging
structures, though examples of many kinds of linkages may be found.
Indeed, it would seem that the interiors of these clusters are somewhat
disorganized and that they are held together largely by non-directional
polar interactions. A detailed account of the molecular organization
within these clusters is given by Sadhu and Clark.[64]A cluster analysis, based on hydrogen-bonding criteria,
predicted
a distribution of clusters, which accorded reasonably well with visual
inspection of simulation snapshots. The cluster-size distribution
appeared to fit an isodesmic model, with the equilibrium constant
for aggregation increasing with the polar content. Typically, this
equilibrium constant, based on molar concentrations, was in the range
of 4–6.The addition of n-octanol was
observed to decrease
the amount of TODGA clustering, reducing the aggregation equilibrium
constant. A structural analysis showed that at the relatively low
concentrations studied, the majority of the n-octanol
molecules were incorporated into the TODGA clusters. Our hypothesis
is that competition between n-octanol and TODGA for
favorable polar interactions is responsible for this decrease.Replacing the branched TPH diluent with straight chain n-dodecane also had the effect of decreasing the degree
of clustering. We argue that this is because n-dodecane
penetrates a reverse aggregate to a greater extent than TPH, probably
due to the fact that TPH has a branched structure and so there is
additional steric hindrance. Such penetration is known to increase
the curvature of a surfactant film in an oil/water system and, as
a small aggregate is move curved than a large one, this effect is
expected to reduce aggregate size.It would, of course, be useful
if simulation work, such as this,
could be used to inform the flow-sheeting modeling that is used at
the process level. In these flow-sheet models, it is common practice
to represent the organic and aqueous phases as containing well-defined
clusters, with a specific chemical formula, and thereby model cluster–cluster
equilibrium. Simulation, however, suggests a much more disordered
state of affairs, with loose aggregates comprising a wide range of
possible compositions. Process modeling studies also hint at this,[11] with the model requiring a range of nitric acid/TODGA
complexes. How best to represent such a system in practical flow-sheet
terms is far from obvious, but if the isodesmic behavior reported
here is general to many systems, this may prove to be a possible way
of incorporating aggregation effects into a practical model.
Authors: David Van Der Spoel; Erik Lindahl; Berk Hess; Gerrit Groenhof; Alan E Mark; Herman J C Berendsen Journal: J Comput Chem Date: 2005-12 Impact factor: 3.376
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