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14 \usepackage[version=3]{mhchem} % this is a great package for formatting chemical reactions
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28 \citestyle{nature}
29 \bibliographystyle{achemso}
30
31 \begin{document}
32
33 \newcolumntype{A}{p{1.5in}}
34 \newcolumntype{B}{p{0.75in}}
35
36 \title{Simulations of heat conduction at thiolate-capped gold
37 surfaces: The role of chain length and solvent penetration}
38
39 \author{Kelsey M. Stocker and J. Daniel
40 Gezelter\footnote{Corresponding author. \ Electronic mail:
41 gezelter@nd.edu} \\
42 251 Nieuwland Science Hall, \\
43 Department of Chemistry and Biochemistry,\\
44 University of Notre Dame\\
45 Notre Dame, Indiana 46556}
46
47 \date{\today}
48
49 \maketitle
50
51 \begin{doublespace}
52
53 \begin{abstract}
54
55 \end{abstract}
56
57 \newpage
58
59 %\narrowtext
60
61 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
62 % **INTRODUCTION**
63 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
64 \section{Introduction}
65
66 The structural details of the interfaces of metal nanoparticles
67 determines how energy flows between these particles and their
68 surroundings. Understanding this energy flow is essential in designing
69 and functionalizing metallic nanoparticles for plasmonic photothermal
70 therapies,\cite{Jain:2007ux,Petrova:2007ad,Gnyawali:2008lp,Mazzaglia:2008to,Huff:2007ye,Larson:2007hw}
71 which rely on the ability of metallic nanoparticles to absorb light in
72 the near-IR, a portion of the spectrum in which living tissue is very
73 nearly transparent. The relevant physical property controlling the
74 transfer of this energy as heat into the surrounding tissue is the
75 interfacial thermal conductance, $G$, which can be somewhat difficult
76 to determine experimentally.\cite{Wilson:2002uq,Plech:2005kx}
77
78 Metallic particles have also been proposed for use in highly efficient
79 thermal-transfer fluids, although careful experiments by Eapen {\it et
80 al.} have shown that metal-particle-based ``nanofluids'' have
81 thermal conductivities that match Maxwell
82 predictions.\cite{Eapen:2007th} The likely cause of previously
83 reported non-Maxwell
84 behavior\cite{Eastman:2001wb,Keblinski:2002bx,Lee:1999ct,Xue:2003ya,Xue:2004oa}
85 is percolation networks of nanoparticles exchanging energy via the
86 solvent,\cite{Eapen:2007mw} so it is vital to get a detailed molecular
87 picture of particle-ligand and particle-solvent interactions in order
88 to understand the thermal behavior of complex fluids. To date, there
89 have been few reported values (either from theory or experiment) for
90 $G$ for ligand-protected nanoparticles embedded in liquids, and there
91 is a significant gap in knowledge about how chemically distinct
92 ligands or protecting groups will affect heat transport from the
93 particles.
94
95 Experimentally, the thermal properties of various nanostructured
96 interfaces have been investigated by a number of groups. Cahill and
97 coworkers studied nanoscale thermal transport from metal
98 nanoparticle/fluid interfaces, to epitaxial TiN/single crystal oxide
99 interfaces, and hydrophilic and hydrophobic interfaces between water
100 and solids with different self-assembled
101 monolayers.\cite{cahill:793,Wilson:2002uq,PhysRevB.67.054302,doi:10.1021/jp048375k,PhysRevLett.96.186101}
102 Wang {\it et al.} studied heat transport through long-chain
103 hydrocarbon monolayers on gold substrate at the individual molecular
104 level,\cite{Wang10082007} Schmidt {\it et al.} studied the role of
105 cetyltrimethylammonium bromide (CTAB) on the thermal transport between
106 gold nanorods and solvent,\cite{doi:10.1021/jp8051888} and Juv\'e {\it
107 et al.} studied the cooling dynamics, which is controlled by thermal
108 interface resistance of glass-embedded metal
109 nanoparticles.\cite{PhysRevB.80.195406} Although interfaces are
110 normally considered barriers for heat transport, Alper {\it et al.}
111 suggested that specific ligands (capping agents) could completely
112 eliminate this barrier
113 ($G\rightarrow\infty$).\cite{doi:10.1021/la904855s}
114
115 In previous simulations, we applied a variant of reverse
116 non-equilibrium molecular dynamics (RNEMD) to calculate the
117 interfacial thermal conductance at a metal / organic solvent interface
118 that had been chemically protected by butanethiolate groups. Our
119 calculations suggest an explanation for the very large thermal
120 conductivity at alkanethiol-capped metal surfaces when compared with
121 bare metal/solvent interfaces. Specifically, the chemical bond
122 between the metal and the ligand introduces a vibrational overlap that
123 is not present without the protecting group, and the overlap between
124 the vibrational spectra (metal to ligand, ligand to solvent) provides
125 a mechanism for rapid thermal transport across the interface.
126
127 One notable result of our previous work was the observation of
128 non-monotonic dependence of the thermal conductance on the coverage of
129 a metal surface by a chemical protecting group. Our explanation for
130 this behavior was that gaps in surface coverage allowed solvent to
131 penetrate close to the capping molecules that had been heated by the
132 metal surface, to absorb thermal energy from these molecules, and then
133 diffuse away. The effect of surface coverage was relatively difficult
134 to study as the individual protecting groups have lateral mobility on
135 the surface and can aggregate to form domains on the timescale of the
136 simulation.
137
138 To prevent lateral mobility of the surface ligands, the current work
139 involves mixed-chain monolayers in which the length mismatch between
140 long and short chains is sufficient to accomodate solvent
141 molecules. These complete (but mixed-chain) surfaces are significantly
142 less prone to surface domain formation, and allow us to further
143 investigate the mechanism of heat transport to the solvent. A thermal
144 flux is created using velocity shearing and scaling reverse
145 non-equilibrium molecular dynamics (VSS-RNEMD), and the resulting
146 temperature profiles are analyzed to yield information about the
147 interfacial thermal conductance.
148
149
150 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
151 % **METHODOLOGY**
152 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
153 \section{Methodology}
154
155 There are many ways to compute bulk transport properties from
156 classical molecular dynamics simulations. Equilibrium Molecular
157 Dynamics (EMD) simulations can be used by computing relevant time
158 correlation functions and assuming that linear response theory
159 holds.\cite{PhysRevB.37.5677,MASSOBRIO:1984bl,PhysRev.119.1,Viscardy:2007rp,che:6888,kinaci:014106}
160 For some transport properties (notably thermal conductivity), EMD
161 approaches are subject to noise and poor convergence of the relevant
162 correlation functions. Traditional Non-equilibrium Molecular Dynamics
163 (NEMD) methods impose a gradient (e.g. thermal or momentum) on a
164 simulation.\cite{ASHURST:1975tg,Evans:1982zk,ERPENBECK:1984sp,MAGINN:1993hc,Berthier:2002ij,Evans:2002ai,Schelling:2002dp,PhysRevA.34.1449,JiangHao_jp802942v}
165 However, the resulting flux is often difficult to
166 measure. Furthermore, problems arise for NEMD simulations of
167 heterogeneous systems, such as phase-phase boundaries or interfaces,
168 where the type of gradient to enforce at the boundary between
169 materials is unclear.
170
171 {\it Reverse} Non-Equilibrium Molecular Dynamics (RNEMD) methods adopt
172 a different approach in that an unphysical {\it flux} is imposed
173 between different regions or ``slabs'' of the simulation
174 box.\cite{MullerPlathe:1997xw,ISI:000080382700030,Kuang:2010uq} The
175 system responds by developing a temperature or momentum {\it gradient}
176 between the two regions. Since the amount of the applied flux is known
177 exactly, and the measurement of a gradient is generally less
178 complicated, imposed-flux methods typically take shorter simulation
179 times to obtain converged results for transport properties. The
180 corresponding temperature or velocity gradients which develop in
181 response to the applied flux are then related (via linear response
182 theory) to the transport coefficient of interest. These methods are
183 quite efficient, in that they do not need many trajectories to provide
184 information about transport properties. To date, they have been
185 utilized in computing thermal and mechanical transfer of both
186 homogeneous
187 liquids~\cite{MullerPlathe:1997xw,ISI:000080382700030,Maginn:2010} as
188 well as heterogeneous
189 systems.\cite{garde:nl2005,garde:PhysRevLett2009,kuang:AuThl}
190
191 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
192 % VSS-RNEMD
193 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
194 \subsection{VSS-RNEMD}
195 The original ``swapping'' approaches by M\"{u}ller-Plathe {\it et
196 al.}\cite{ISI:000080382700030,MullerPlathe:1997xw} can be understood
197 as a sequence of imaginary elastic collisions between particles in
198 regions separated by half of the simulation cell. In each collision,
199 the entire momentum vectors of both particles may be exchanged to
200 generate a thermal flux. Alternatively, a single component of the
201 momentum vectors may be exchanged to generate a shear flux. This
202 algorithm turns out to be quite useful in many simulations of bulk
203 liquids. However, the M\"{u}ller-Plathe swapping approach perturbs the
204 system away from ideal Maxwell-Boltzmann distributions, and this has
205 undesirable side-effects when the applied flux becomes
206 large.\cite{Maginn:2010}
207
208 The most useful alternative RNEMD approach developed so far utilizes a
209 series of simultaneous velocity shearing and scaling exchanges between
210 the two slabs.\cite{2012MolPh.110..691K} This method provides a set of
211 conservation constraints while simultaneously creating a desired flux
212 between the two slabs. Satisfying the constraint equations ensures
213 that the new configurations are sampled from the same NVE ensemble.
214
215 The VSS moves are applied periodically to scale and shift the particle
216 velocities ($\mathbf{v}_i$ and $\mathbf{v}_j$) in two slabs ($H$ and
217 $C$) which are separated by half of the simulation box,
218 \begin{displaymath}
219 \begin{array}{rclcl}
220
221 & \underline{\mathrm{shearing}} & &
222 \underline{~~~~~~~~~~~~\mathrm{scaling}~~~~~~~~~~~~} \\ \\
223 \mathbf{v}_i \leftarrow &
224 \mathbf{a}_c\ & + & c\cdot\left(\mathbf{v}_i - \langle\mathbf{v}_c
225 \rangle\right) + \langle\mathbf{v}_c\rangle \\
226 \mathbf{v}_j \leftarrow &
227 \mathbf{a}_h & + & h\cdot\left(\mathbf{v}_j - \langle\mathbf{v}_h
228 \rangle\right) + \langle\mathbf{v}_h\rangle .
229
230 \end{array}
231 \end{displaymath}
232 Here $\langle\mathbf{v}_c\rangle$ and $\langle\mathbf{v}_h\rangle$ are
233 the center of mass velocities in the $C$ and $H$ slabs, respectively.
234 Within the two slabs, particles receive incremental changes or a
235 ``shear'' to their velocities. The amount of shear is governed by the
236 imposed momentum flux, $j_z(\mathbf{p})$
237 \begin{eqnarray}
238 \mathbf{a}_c & = & - \mathbf{j}_z(\mathbf{p}) \Delta t / M_c \label{vss1}\\
239 \mathbf{a}_h & = & + \mathbf{j}_z(\mathbf{p}) \Delta t / M_h \label{vss2}
240 \end{eqnarray}
241 where $M_{\{c,h\}}$ is total mass of particles within each slab and $\Delta t$
242 is the interval between two separate operations.
243
244 To simultaneously impose a thermal flux ($J_z$) between the slabs we
245 use energy conservation constraints,
246 \begin{eqnarray}
247 K_c - J_z\Delta t & = & c^2 (K_c - \frac{1}{2}M_c \langle\mathbf{v}_c
248 \rangle^2) + \frac{1}{2}M_c (\langle \mathbf{v}_c \rangle + \mathbf{a}_c)^2 \label{vss3}\\
249 K_h + J_z\Delta t & = & h^2 (K_h - \frac{1}{2}M_h \langle\mathbf{v}_h
250 \rangle^2) + \frac{1}{2}M_h (\langle \mathbf{v}_h \rangle +
251 \mathbf{a}_h)^2 \label{vss4}.
252 \label{constraint}
253 \end{eqnarray}
254 Simultaneous solution of these quadratic formulae for the scaling
255 coefficients, $c$ and $h$, will ensure that the simulation samples from
256 the original microcanonical (NVE) ensemble. Here $K_{\{c,h\}}$ is the
257 instantaneous translational kinetic energy of each slab. At each time
258 interval, it is a simple matter to solve for $c$, $h$, $\mathbf{a}_c$,
259 and $\mathbf{a}_h$, subject to the imposed momentum flux,
260 $j_z(\mathbf{p})$, and thermal flux, $J_z$ values. Since the VSS
261 operations do not change the kinetic energy due to orientational
262 degrees of freedom or the potential energy of a system, configurations
263 after the VSS move have exactly the same energy ({\it and} linear
264 momentum) as before the move.
265
266 As the simulation progresses, the VSS moves are performed on a regular
267 basis, and the system develops a thermal or velocity gradient in
268 response to the applied flux. Using the slope of the temperature or
269 velocity gradient, it is quite simple to obtain of thermal
270 conductivity ($\lambda$),
271 \begin{equation}
272 J_z = -\lambda \frac{\partial T}{\partial z},
273 \end{equation}
274 and shear viscosity ($\eta$),
275 \begin{equation}
276 j_z(p_x) = -\eta \frac{\partial \langle v_x \rangle}{\partial z}.
277 \end{equation}
278 Here, the quantities on the left hand side are the imposed flux
279 values, while the slopes are obtained from linear fits to the
280 gradients that develop in the simulated system.
281
282 The VSS-RNEMD approach is versatile in that it may be used to
283 implement both thermal and shear transport either separately or
284 simultaneously. Perturbations of velocities away from the ideal
285 Maxwell-Boltzmann distributions are minimal, and thermal anisotropy is
286 kept to a minimum. This ability to generate simultaneous thermal and
287 shear fluxes has been previously utilized to map out the shear
288 viscosity of SPC/E water over a wide range of temperatures (90~K) with
289 a single 1 ns simulation.\cite{2012MolPh.110..691K}
290
291 \begin{figure}
292 \includegraphics[width=\linewidth]{figures/rnemd}
293 \caption{The VSS-RNEMD approach imposes unphysical transfer of
294 linear momentum or kinetic energy between a ``hot'' slab and a
295 ``cold'' slab in the simulation box. The system responds to this
296 imposed flux by generating velocity or temperature gradients. The
297 slope of the gradients can then be used to compute transport
298 properties (e.g. shear viscosity or thermal conductivity).}
299 \label{fig:rnemd}
300 \end{figure}
301
302 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
303 % INTERFACIAL CONDUCTANCE
304 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
305 \subsection{Reverse Non-Equilibrium Molecular Dynamics approaches
306 to interfacial transport}
307
308 Interfaces between dissimilar materials have transport properties
309 which can be defined as derivatives of the standard transport
310 coefficients in a direction normal to the interface. For example, the
311 {\it interfacial} thermal conductance ($G$) can be thought of as the
312 change in the thermal conductivity ($\lambda$) across the boundary
313 between materials:
314 \begin{align}
315 G &= \left(\nabla\lambda \cdot \mathbf{\hat{n}}\right)_{z_0} \\
316 &= J_z\left(\frac{\partial^2 T}{\partial z^2}\right)_{z_0} \Big/
317 \left(\frac{\partial T}{\partial z}\right)_{z_0}^2.
318 \label{derivativeG}
319 \end{align}
320 where $z_0$ is the location of the interface between two materials and
321 $\mathbf{\hat{n}}$ is a unit vector normal to the interface (assumed
322 to be the $z$ direction from here on). RNEMD simulations, and
323 particularly the VSS-RNEMD approach, function by applying a momentum
324 or thermal flux and watching the gradient response of the
325 material. This means that the {\it interfacial} conductance is a
326 second derivative property which is subject to significant noise and
327 therefore requires extensive sampling. We have been able to
328 demonstrate the use of the second derivative approach to compute
329 interfacial conductance at chemically-modified metal / solvent
330 interfaces. However, a definition of the interfacial conductance in
331 terms of a temperature difference ($\Delta T$) measured at $z_0$,
332 \begin{displaymath}
333 G = \frac{J_z}{\Delta T_{z_0}},
334 \end{displaymath}
335 is useful once the RNEMD approach has generated a stable temperature
336 gap across the interface.
337
338 \begin{figure}
339 \includegraphics[width=\linewidth]{figures/resistor_series}
340 \caption{The inverse of the interfacial thermal conductance, $G$, is
341 the Kapitza resistance, $R_K$. Because the gold / thiolate/
342 solvent interface extends a significant distance from the metal
343 surface, the interfacial resistance $R_K$ can be computed by
344 summing a series of temperature drops between adjacent temperature
345 bins along the $z$ axis.}
346 \label{fig:resistor_series}
347 \end{figure}
348
349 In the particular case we are studying here, there are two interfaces
350 involved in the transfer of heat from the gold slab to the solvent:
351 the gold/thiolate interface and the thiolate/solvent interface. We
352 could treat the temperature on each side of an interface as discrete,
353 making the interfacial conductance the inverse of the Kaptiza
354 resistance, or $G = \frac{1}{R_k}$. To model the total conductance
355 across multiple interfaces, it is useful to think of the interfaces as
356 a set of resistors wired in series. The total resistance is then
357 additive, $R_{total} = \sum_i R_{i}$ and the interfacial conductance
358 is the inverse of the total resistance, or $G = \frac{1}{\sum_i
359 R_i}$). In the interfacial region, we treat each bin in the
360 VSS-RNEMD temperature profile as a resistor with resistance
361 $\frac{T_{2}-T_{1}}{J_z}$, $\frac{T_{3}-T_{2}}{J_z}$, etc. The sum of
362 the set of resistors which spans the gold/thiolate interface, thiolate
363 chains, and thiolate/solvent interface simplifies to
364 \begin{equation}
365 R_{K} = \frac{T_{n}-T_{1}}{J_z},
366 \label{eq:finalG}
367 \end{equation}
368 or the temperature difference between the gold side of the
369 gold/thiolate interface and the solvent side of the thiolate/solvent
370 interface over the applied flux.
371
372
373 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
374 % **COMPUTATIONAL DETAILS**
375 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
376 \section{Computational Details}
377
378 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
379 % FORCE-FIELD PARAMETERS
380 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
381 \subsection{Force-Field Parameters}
382
383 Our simulations include a number of chemically distinct components.
384 Figure \ref{fig:structures} demonstrates the sites defined for both
385 the {\it n}-hexane and alkanethiolate ligands present in our
386 simulations. Force field parameters are needed for interactions both
387 between the same type of particles and between particles of different
388 species.
389
390 \begin{figure}
391 \includegraphics[width=\linewidth]{figures/structures}
392 \caption{Topologies of the thiolate capping agents and solvent
393 utilized in the simulations. The chemically-distinct sites (S,
394 \ce{CH2}, and \ce{CH3}) are treated as united atoms. Most
395 parameters are taken from references \bibpunct{}{}{,}{n}{}{,}
396 \protect\cite{TraPPE-UA.alkanes} and
397 \protect\cite{TraPPE-UA.thiols}. Cross-interactions with the Au
398 atoms were adapted from references
399 \protect\cite{landman:1998},~\protect\cite{vlugt:cpc2007154},~and
400 \protect\cite{hautman:4994}.}
401 \label{fig:structures}
402 \end{figure}
403
404 The Au-Au interactions in the metal lattice slab are described by the
405 quantum Sutton-Chen (QSC) formulation.\cite{PhysRevB.59.3527} The QSC
406 potentials include zero-point quantum corrections and are
407 reparametrized for accurate surface energies compared to the
408 Sutton-Chen potentials.\cite{Chen90}
409
410 For the {\it n}-hexane solvent molecules, the TraPPE-UA
411 parameters\cite{TraPPE-UA.alkanes} were utilized. In this model,
412 sites are located at the carbon centers for alkyl groups. Bonding
413 interactions, including bond stretches and bends and torsions, were
414 used for intra-molecular sites closer than 3 bonds. For non-bonded
415 interactions, Lennard-Jones potentials are used. We have previously
416 utilized both united atom (UA) and all-atom (AA) force fields for
417 thermal conductivity in previous work,\cite{} and since the united
418 atom force fields cannot populate the high-frequency modes that are
419 present in AA force fields, they appear to work better for modeling
420 thermal conductivity. The TraPPE-UA model for alkanes is known to
421 predict a slightly lower boiling point than experimental values. This
422 is one of the reasons we used a lower average temperature (200K) for
423 our simulations.
424
425 The TraPPE-UA force field includes parameters for thiol
426 molecules\cite{TraPPE-UA.thiols} which were used for the
427 alkanethiolate molecules in our simulations. To derive suitable
428 parameters for butanethiol adsorbed on Au(111) surfaces, we adopted
429 the S parameters from Luedtke and Landman\cite{landman:1998} and
430 modified the parameters for the CTS atom to maintain charge neutrality
431 in the molecule.
432
433 To describe the interactions between metal (Au) and non-metal atoms,
434 we refer to an adsorption study of alkyl thiols on gold surfaces by
435 Vlugt {\it et al.}\cite{vlugt:cpc2007154} They fitted an effective
436 Lennard-Jones form of potential parameters for the interaction between
437 Au and pseudo-atoms CH$_x$ and S based on a well-established and
438 widely-used effective potential of Hautman and Klein for the Au(111)
439 surface.\cite{hautman:4994} As our simulations require the gold slab
440 to be flexible to accommodate thermal excitation, the pair-wise form
441 of potentials they developed was used for our study.
442
443 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
444 % SIMULATION PROTOCOL
445 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
446 \subsection{Simulation Protocol}
447
448 We have implemented the VSS-RNEMD algorithm in OpenMD, our
449 group molecular dynamics code. A 1188 atom gold slab was
450 equilibrated at 1 atm and 200 K. The periodic box was then expanded
451 in the $z$-direction to expose two Au(111) faces on either side of the 11-atom thick slab.
452
453 A full monolayer of thiolates (1/3 the number of surface gold atoms) was placed on three-fold hollow sites on the gold interfaces. To efficiently test the effect of thiolate binding sites on the thermal conductance, all systems had one gold interface with thiolates placed only on fcc hollow sites and the other interface with thiolates only on hcp hollow sites. To test the effect of thiolate chain length on interfacial thermal conductance, full coverages of five chain lengths were tested: butanethiolate, hexanethiolate, octanethiolate, decanethiolate, and dodecanethiolate. To test the effect of mixed chain lengths, full coverages of butanethiolate/decanethiolate and butanethiolate/dodecanethiolate mixtures were created in short/long chain percentages of 25/75, 50/50, 62.5/37.5, 75/25, and 87.5/12.5. The short and long chains were placed on the surface hollow sites in a random configuration.
454
455 The simulation box $z$-dimension was set to roughly double the length of the gold/thiolate block. Hexane solvent molecules were placed in the vacant portion of the box using the packmol algorithm. Hexane, a straight chain flexible alkane, is very structurally similar to the thiolate alkane tails; previous work has shown that UA models of hexane and butanethiolate have a high degree of vibrational overlap.\cite{Kuang2011} This overlap should provide a mechanism for thermal energy transfer from the thiolates to the solvent.
456
457 The system was equilibrated to 220 K in the NVT ensemble, allowing the thiolates and solvent to warm gradually. Pressure correction to 1 atm was done in an NPT ensemble that allowed expansion or contraction only in the z direction, so as not to disrupt the crystalline structure of the gold. The diagonal elements of the pressure tensor were monitored during the pressure correction step. If the xx and/or yy elements had a mean above zero throughout the simulation -- indicating residual pressure in the plane of the gold slab -- an additional short NPT equilibration step was performed allowing all box dimensions to change. Once the pressure was stable at 1 atm, a final NVT simulation was performed. All systems were equilibrated in the microcanonical (NVE) ensemble before proceeding with the VSS-RNEMD step.
458
459 A kinetic energy flux was applied using VSS-RNEMD in the NVE ensemble. The total simulation time was 3 nanoseconds, with velocity scaling occurring every 10 femtoseconds. The hot slab was centered in the gold and the cold slab was placed in the center of the solvent region. The average temperature was 220 K, with a temperature difference between the hot and cold slabs of approximately 30 K. The average temperature and kinetic energy flux were carefully selected with two considerations in mind: 1) if the cold bin gets too cold (below ~180 K) the solvent may freeze or undergo a glassy transition, and 2) due to the deep sulfur-gold potential well, sulfur atoms routinely embed into the gold slab, particularly at temperatures above 250 K. Simulation conditions were chosen to avoid both of these undesirable situations. A reversed flux direction resulted in frozen long chain thiolates and solvent too near its boiling point.
460
461 A temperature profile of the system was created by dividing the box into $\sim$ 3 \AA \, bins along the z axis and recording the average temperature of each bin.
462
463
464
465 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
466 % **RESULTS**
467 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
468 \section{Results}
469
470
471 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
472 % CHAIN LENGTH
473 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
474 \subsection{Effect of Chain Length}
475
476 We examined full coverages of five chain lengths, n = 4, 6, 8, 10, 12. As shown in table \ref{table:chainlengthG}, the interfacial conductance is constant as a function of chain length, indicating that the length of the thiolate alkyl chains does not play a significant role in the transport of heat across the gold/thiolate and thiolate/solvent interfaces. In all cases, the hexane solvent was unable to penetrate into the thiolate layer, leading to a persistent 2-4 \AA \, gap between the solvent region and the thiolates. However, while the identity of the alkyl thiolate capping agent has little effect on the interfacial thermal conductance, the presence of a full monolayer of capping agent provides a two-fold increase in the G value relative to a bare gold surface.
477 \begin{longtable}{p{4cm} p{3cm}}
478 \caption{Computed interfacial thermal conductance (G) values for bare gold and 100\% coverages of various thiolate alkyl chain lengths.}
479 \\
480 \centering {\bf Chain Length (n)} & \centering\arraybackslash {\bf G (MW/m$^2$/K)} \\ \hline
481 \endhead
482 \hline
483 \endfoot
484 \centering bare gold & \centering\arraybackslash 30.2 \\
485 \centering 4 & \centering\arraybackslash 59.4 \\
486 \centering 6 & \centering\arraybackslash 60.2 \\
487 \centering 8 & \centering\arraybackslash 61.0 \\
488 \centering 10 & \centering\arraybackslash 58.2 \\
489 \centering 12 & \centering\arraybackslash 58.8
490 \label{table:chainlengthG}
491 \end{longtable}
492
493 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
494 % MIXED CHAINS
495 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
496 \subsection{Effect of Mixed Chain Lengths}
497
498 Previous work demonstrated that for butanethiolate monolayers on a Au(111) surface, the interfacial conductance was a non-monotonic function of the percent coverage. This is believed to be due to enhanced solvent-thiolate coupling through greater penetration of solvent molecules into the thiolate layer. At lower coverages, hexane solvent can more penetrate into the interfacial layer by fitting into gaps between the thiolates. However, a side effect of low coverages is surface aggregation of the thiolates. To simulate the effect of low coverages while preventing thiolate domain formation, we maintain 100\% thiolate coverage while varying the proportions of short (butanethiolate, n = 4) and long (decanethiolate, n = 10 or dodecanethiolate, n = 12) thiolate alkyl chains. We show in figure \ref{fig:Gstacks} that the interfacial conductance of full coverage mixed-chain systems is a non-monotonic function of the fraction of long chains.
499 \begin{figure}
500 \includegraphics[width=\linewidth]{figures/Gstacks}
501 \caption{Interfacial thermal conductivity of mixed-chains has a non-monotonic dependence on the fraction of long chains (lower panels). At low long chain coverage, the solvent escape rate dominates the heat transfer process, while the solvent-thiolate orientational order dominates at high long chain coverage (upper panels).}
502 \label{fig:Gstacks}
503 \end{figure}
504 Mixtures of butanethiolate/decanethiolate (n = 4, 10) have a peak interfacial conductance for 25\%/75\% short/long chains. At this short/long chain fraction, the orientational ordering of the solvent molecules and chains becomes a dominant effect while the solvent escape rate sharply decreases. Mixtures of butanethiolate/dodecanethiolate (n = 4, 12) have a peak interfacial conductance for 12.5\%/87.5\% short/long chains. The solvent-thiolate orientational ordering reaches its maximum value at this short/long chain ratio. Long chain fractions of over $0.5$ for the n = 4, 12 system are very well ordered, but this effect is tempered by the exceptionally slow solvent escape rate.
505
506 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
507 % **DISCUSSION**
508 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
509 \section{Discussion}
510
511 In the mixed chain-length simulations, solvent molecules can become
512 temporarily trapped or entangled with the thiolate chains. Their
513 residence in close proximity to the higher temperature environment
514 close to the surface allows them to carry heat away from the surface
515 quite efficiently. There are two aspects of this behavior that are
516 relevant to thermal conductance of the interface: the residence time
517 of solvent molecules in the thiolate layer, and the orientational
518 ordering of the C-C chains as a mechanism for transferring vibrational
519 energy to these entrapped solvent molecules. These competing effects are responsible for the non-monotonic dependence of the interfacial thermal conductance on the fraction of long chain capping agents.
520
521 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
522 % RESIDENCE TIME
523 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
524 \subsection{Mobility of solvent in the interfacial layer}
525
526 We use a simple survival correlation function, $C(t)$, to quantify the
527 residence time of a solvent molecule in the long thiolate chain
528 layer. This function correlates the identity of all hexane molecules
529 within the $z$-coordinate range of the thiolate layer at two separate
530 times. If the solvent molecule is present at both times, the
531 configuration contributes a $1$, while the absence of the molecule at
532 the later time indicates that the solvent molecule has migrated into
533 the bulk, and this configuration contributes a $0$. A steep decay in
534 $C(t)$ indicates a high turnover rate of solvent molecules from the
535 chain region to the bulk. We define the escape rate for trapped solvent molecules at the interface as
536 \begin{equation}
537 k_{escape} = \left( \int_0^T C(t) dt \right)^{-1}
538 \label{eq:mobility}
539 \end{equation}
540 where T is the length of the simulation. This is a direct measure of
541 the rate at which solvent molecules entangled in the thiolate layer
542 can escape into the bulk. As $k_{escape} \rightarrow 0$, the
543 solvent has become permanently trapped in the thiolate layer. In
544 figure \ref{fig:Gstacks} we show that interfacial solvent mobility
545 decreases as the percentage of long thiolate chains increases.
546
547 \begin{figure}
548 \includegraphics[width=\linewidth]{figures/timelapse}
549 \caption{Images of 25\%/75\% C$_4$/C$_{12}$ (top panel) and 75\%/25\% C$_4$/C$_{12}$ (bottom panel) systems at the beginning and end of a 3 ns simulation. Initial interfacial solvent molecules are colored light blue. The solvent-thiolate disorder and interfacial solvent turnover of the 25\%/75\% short/long system stand in stark contrast to the highly ordered but entrapped interfacial solvent of the 75\%/25\% system.}
550 \label{fig:timelapse}
551 \end{figure}
552
553 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
554 % ORDER PARAMETER
555 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
556
557 \subsection{Vibrational coupling via orientational ordering}
558
559 As the fraction of long-chain thiolates becomes large, the entrapped
560 solvent molecules must find specific orientations relative to the mean
561 orientation of the thiolate chains. This configuration allows for
562 efficient thermal energy exchange between the thiolate alkyl chain and
563 the solvent molecules.
564
565 To quantify this cooperative
566 ordering, we computed the orientational order parameters and director
567 axes for both the thiolate chains and for the entrapped solvent. The
568 director axis can be easily obtained by diagonalization of the order
569 parameter tensor,
570 \begin{equation}
571 \mathsf{Q}_{\alpha \beta} = \frac{1}{2 N} \sum_{i=1}^{N} \left( 3 \mathbf{e}_{i
572 \alpha} \mathbf{e}_{i \beta} - \delta_{\alpha \beta} \right)
573 \end{equation}
574 where $\mathbf{e}_{i \alpha}$ was the $\alpha = x,y,z$ component of
575 the unit vector $\mathbf{e}_{i}$ along the long axis of molecule $i$.
576 For both kinds of molecules, the $\mathbf{e}$ vector is defined using
577 the terminal atoms of the chains.
578
579 The largest eigenvalue of $\overleftrightarrow{\mathsf{Q}}$ is
580 traditionally used to obtain orientational order parameter, while the
581 eigenvector corresponding to the order parameter yields the director
582 axis ($\mathbf{d}(t)$) which defines the average direction of
583 molecular alignment at any time $t$. The overlap between the director
584 axes of the thiolates and the entrapped solvent is time-averaged,
585 \begin{equation}
586 \bar{d} = \langle \mathbf{d}_{thiolates} \left( t \right) \cdot
587 \mathbf{d}_{solvent} \left( t \right) \rangle_t
588 \label{eq:orientation}
589 \end{equation}
590 and reported in figure \ref{fig:Gstacks}.
591
592 Once the solvent molecules have picked up thermal energy from the
593 thiolates, they carry heat away from the gold as they diffuse back
594 into the bulk solvent. When the percentage of long chains decreases,
595 the tails of the long chains are much more disordered and do not
596 provide structured channels for the solvent to fill.
597
598 Although the alignment of the chains with the entrapped solvent is one
599 possible mechanism for the non-monotonic increase in the conductance
600 as a function
601
602
603 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
604 % **CONCLUSIONS**
605 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
606 \section{Conclusions}
607
608
609
610 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
611 % **ACKNOWLEDGMENTS**
612 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
613 \section*{Acknowledgments}
614 Support for this project was provided by the
615 National Science Foundation under grant CHE-0848243. Computational
616 time was provided by the Center for Research Computing (CRC) at the
617 University of Notre Dame.
618
619 \newpage
620
621 \bibliography{thiolsRNEMD}
622
623 \end{doublespace}
624 \end{document}
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