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1 \documentclass[11pt]{article}
2 \usepackage{amsmath}
3 \usepackage{amssymb}
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14 \usepackage[version=3]{mhchem} % this is a great package for formatting chemical reactions
15 \usepackage[square, comma, sort&compress]{natbib}
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19 9.0in \textwidth 6.5in \brokenpenalty=10000
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21 % double space list of tables and figures
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26 \bibpunct{}{}{,}{s}{}{;}
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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 We report on simulations of heat conduction from Au(111) / hexane interfaces in which the surface has been protected by a mix of short and long chain alkanethiolate ligands. A variant of reverse non-equilibrium molecular dynamics (RNEMD) was used to create a thermal flux between the metal and solvent, and thermal conductance was computed using the resulting thermal profiles of the interface. We find a non-monotonic dependence of the interfacial thermal conductance on the fraction of long chains present at the interface, and correlate this behavior to solvent ordering and escape from the thiolate layer immediately in contact with the metal surface.
56 Our results suggest that a mixed vibrational transfer / convection model is
57 necessary to explain the features of heat transfer at this interface. The
58 alignment of the solvent chains with the ordered ligand allows rapid transfer
59 of energy to the trapped solvent (and this is the dominant feature for ordered
60 ligand layers). Diffusion of the vibrationally excited solvent into the bulk
61 also plays a significant role when the ligands are less tightly packed.
62
63 \end{abstract}
64
65 \newpage
66
67 %\narrowtext
68
69 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
70 % **INTRODUCTION**
71 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
72 \section{Introduction}
73
74 The structural details of the interfaces of metal nanoparticles
75 determines how energy flows between these particles and their
76 surroundings. Understanding this energy flow is essential in designing
77 and functionalizing metallic nanoparticles for plasmonic photothermal
78 therapies,\cite{Jain:2007ux,Petrova:2007ad,Gnyawali:2008lp,Mazzaglia:2008to,Huff:2007ye,Larson:2007hw}
79 which rely on the ability of metallic nanoparticles to absorb light in
80 the near-IR, a portion of the spectrum in which living tissue is very
81 nearly transparent. The relevant physical property controlling the
82 transfer of this energy as heat into the surrounding tissue is the
83 interfacial thermal conductance, $G$, which can be somewhat difficult
84 to determine experimentally.\cite{Wilson:2002uq,Plech:2005kx}
85
86 Metallic particles have also been proposed for use in highly efficient
87 thermal-transfer fluids, although careful experiments by Eapen {\it et
88 al.} have shown that metal-particle-based nanofluids have thermal
89 conductivities that match Maxwell predictions.\cite{Eapen:2007th} The
90 likely cause of previously reported non-Maxwell
91 behavior\cite{Eastman:2001wb,Keblinski:2002bx,Lee:1999ct,Xue:2003ya,Xue:2004oa}
92 is percolation networks of nanoparticles exchanging energy via the
93 solvent,\cite{Eapen:2007mw} so it is important to get a detailed
94 molecular picture of particle-ligand and ligand-solvent interactions
95 in order to understand the thermal behavior of complex fluids. To
96 date, there have been few reported values (either from theory or
97 experiment) for $G$ for ligand-protected nanoparticles embedded in
98 liquids, and there is a significant gap in knowledge about how
99 chemically distinct ligands or protecting groups will affect heat
100 transport from the particles.
101
102 Experimentally, the thermal properties of various nanostructured
103 interfaces have been investigated by a number of groups. Cahill and
104 coworkers studied thermal transport from metal nanoparticle/fluid
105 interfaces, epitaxial TiN/single crystal oxide interfaces, and
106 hydrophilic and hydrophobic interfaces between water and solids with
107 different self-assembled
108 monolayers.\cite{cahill:793,Wilson:2002uq,PhysRevB.67.054302,doi:10.1021/jp048375k,PhysRevLett.96.186101}
109 Wang {\it et al.} studied heat transport through long-chain
110 hydrocarbon monolayers on gold substrate at the individual molecular
111 level,\cite{Wang10082007} Schmidt {\it et al.} studied the role of
112 cetyltrimethylammonium bromide (CTAB) on the thermal transport between
113 gold nanorods and solvent,\cite{doi:10.1021/jp8051888} and Juv\'e {\it
114 et al.} studied the cooling dynamics, which is controlled by thermal
115 interface resistance of glass-embedded metal
116 nanoparticles.\cite{PhysRevB.80.195406} Although interfaces are
117 normally considered barriers for heat transport, Alper {\it et al.}
118 have suggested that specific ligands (capping agents) could completely
119 eliminate this barrier
120 ($G\rightarrow\infty$).\cite{doi:10.1021/la904855s}
121
122 In previous simulations, we applied a variant of reverse
123 non-equilibrium molecular dynamics (RNEMD) to calculate the
124 interfacial thermal conductance at a metal / organic solvent interface
125 that had been chemically protected by butanethiolate groups. Our
126 calculations suggested an explanation for the very large thermal
127 conductivity at alkanethiol-capped metal surfaces when compared with
128 bare metal/solvent interfaces. Specifically, the chemical bond
129 between the metal and the ligand introduces a vibrational overlap that
130 is not present without the protecting group, and the overlap between
131 the vibrational spectra (metal to ligand, ligand to solvent) provides
132 a mechanism for rapid thermal transport across the interface.
133
134 A notable result of the previous simulations was the non-monotonic
135 dependence of $G$ on the fractional coverage of the metal surface by
136 the chemical protecting group. Gaps in surface coverage allow the
137 solvent molecules come into direct contact with ligands that had been
138 heated by the metal surface, absorb thermal energy from the ligands,
139 and then diffuse away. Quantifying the role of surface coverage is
140 difficult as the ligands have lateral mobility on the surface and can
141 aggregate to form domains on the timescale of the simulation.
142
143 To isolate this effect without worrying about lateral mobility of the
144 surface ligands, the current work involves mixed-chain-length
145 monolayers in which the length mismatch between long and short chains
146 is sufficient to accommodate solvent molecules. These completely
147 covered (but mixed-chain) surfaces are significantly less prone to
148 surface domain formation, and allow us to further investigate the
149 mechanism of heat transport to the solvent. A thermal flux is created
150 using velocity shearing and scaling reverse non-equilibrium molecular
151 dynamics (VSS-RNEMD), and the resulting temperature profiles are
152 analyzed to yield information about the interfacial thermal
153 conductance.
154
155
156 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
157 % **METHODOLOGY**
158 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
159 \section{Methodology}
160
161 There are many ways to compute bulk transport properties from
162 classical molecular dynamics simulations. Equilibrium Molecular
163 Dynamics (EMD) simulations can be used by computing relevant time
164 correlation functions and assuming that linear response theory
165 holds.\cite{PhysRevB.37.5677,MASSOBRIO:1984bl,PhysRev.119.1,Viscardy:2007rp,che:6888,kinaci:014106}
166 For some transport properties (notably thermal conductivity), EMD
167 approaches are subject to noise and poor convergence of the relevant
168 correlation functions. Traditional Non-equilibrium Molecular Dynamics
169 (NEMD) methods impose a gradient (e.g. thermal or momentum) on a
170 simulation.\cite{ASHURST:1975tg,Evans:1982zk,ERPENBECK:1984sp,MAGINN:1993hc,Berthier:2002ij,Evans:2002ai,Schelling:2002dp,PhysRevA.34.1449,JiangHao_jp802942v}
171 However, the resulting flux is often difficult to
172 measure. Furthermore, problems arise for NEMD simulations of
173 heterogeneous systems, such as phase-phase boundaries or interfaces,
174 where the type of gradient to enforce at the boundary between
175 materials is unclear.
176
177 {\it Reverse} Non-Equilibrium Molecular Dynamics (RNEMD) methods adopt
178 a different approach in that an unphysical {\it flux} is imposed
179 between different regions or ``slabs'' of the simulation
180 box.\cite{MullerPlathe:1997xw,ISI:000080382700030,Kuang2010} The
181 system responds by developing a temperature or momentum {\it gradient}
182 between the two regions. Since the amount of the applied flux is known
183 exactly, and the measurement of a gradient is generally less
184 complicated, imposed-flux methods typically take shorter simulation
185 times to obtain converged results for transport properties. The
186 corresponding temperature or velocity gradients which develop in
187 response to the applied flux are then related (via linear response
188 theory) to the transport coefficient of interest. These methods are
189 quite efficient, in that they do not need many trajectories to provide
190 information about transport properties. To date, they have been
191 utilized in computing thermal and mechanical transfer of both
192 homogeneous
193 liquids~\cite{MullerPlathe:1997xw,ISI:000080382700030,Maginn:2010} as
194 well as heterogeneous
195 systems.\cite{garde:nl2005,garde:PhysRevLett2009,kuang:AuThl}
196
197 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
198 % VSS-RNEMD
199 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
200 \subsection{VSS-RNEMD}
201 The original ``swapping'' approaches by M\"{u}ller-Plathe {\it et
202 al.}\cite{ISI:000080382700030,MullerPlathe:1997xw} can be understood
203 as a sequence of imaginary elastic collisions between particles in
204 regions separated by half of the simulation cell. In each collision,
205 the entire momentum vectors of both particles may be exchanged to
206 generate a thermal flux. Alternatively, a single component of the
207 momentum vectors may be exchanged to generate a shear flux. This
208 algorithm turns out to be quite useful in many simulations of bulk
209 liquids. However, the M\"{u}ller-Plathe swapping approach perturbs the
210 system away from ideal Maxwell-Boltzmann distributions, and this has
211 undesirable side-effects when the applied flux becomes
212 large.\cite{Maginn:2010}
213
214 The most useful alternative RNEMD approach developed so far utilizes a
215 series of simultaneous velocity shearing and scaling exchanges between
216 the two slabs.\cite{Kuang2012} This method provides a set of
217 conservation constraints while simultaneously creating a desired flux
218 between the two slabs. Satisfying the constraint equations ensures
219 that the new configurations are sampled from the same NVE ensemble.
220
221 The VSS moves are applied periodically to scale and shift the particle
222 velocities ($\mathbf{v}_i$ and $\mathbf{v}_j$) in two slabs ($H$ and
223 $C$) which are separated by half of the simulation box,
224 \begin{displaymath}
225 \begin{array}{rclcl}
226
227 & \underline{\mathrm{shearing}} & &
228 \underline{~~~~~~~~~~~~\mathrm{scaling}~~~~~~~~~~~~} \\ \\
229 \mathbf{v}_i \leftarrow &
230 \mathbf{a}_c\ & + & c\cdot\left(\mathbf{v}_i - \langle\mathbf{v}_c
231 \rangle\right) + \langle\mathbf{v}_c\rangle \\
232 \mathbf{v}_j \leftarrow &
233 \mathbf{a}_h & + & h\cdot\left(\mathbf{v}_j - \langle\mathbf{v}_h
234 \rangle\right) + \langle\mathbf{v}_h\rangle .
235
236 \end{array}
237 \end{displaymath}
238 Here $\langle\mathbf{v}_c\rangle$ and $\langle\mathbf{v}_h\rangle$ are
239 the center of mass velocities in the $C$ and $H$ slabs, respectively.
240 Within the two slabs, particles receive incremental changes or a
241 ``shear'' to their velocities. The amount of shear is governed by the
242 imposed momentum flux, $j_z(\mathbf{p})$
243 \begin{eqnarray}
244 \mathbf{a}_c & = & - \mathbf{j}_z(\mathbf{p}) \Delta t / M_c \label{vss1}\\
245 \mathbf{a}_h & = & + \mathbf{j}_z(\mathbf{p}) \Delta t / M_h \label{vss2}
246 \end{eqnarray}
247 where $M_{\{c,h\}}$ is total mass of particles within each slab and $\Delta t$
248 is the interval between two separate operations.
249
250 To simultaneously impose a thermal flux ($J_z$) between the slabs we
251 use energy conservation constraints,
252 \begin{eqnarray}
253 K_c - J_z\Delta t & = & c^2 (K_c - \frac{1}{2}M_c \langle\mathbf{v}_c
254 \rangle^2) + \frac{1}{2}M_c (\langle \mathbf{v}_c \rangle + \mathbf{a}_c)^2 \label{vss3}\\
255 K_h + J_z\Delta t & = & h^2 (K_h - \frac{1}{2}M_h \langle\mathbf{v}_h
256 \rangle^2) + \frac{1}{2}M_h (\langle \mathbf{v}_h \rangle +
257 \mathbf{a}_h)^2 \label{vss4}.
258 \label{constraint}
259 \end{eqnarray}
260 Simultaneous solution of these quadratic formulae for the scaling
261 coefficients, $c$ and $h$, will ensure that the simulation samples from
262 the original microcanonical (NVE) ensemble. Here $K_{\{c,h\}}$ is the
263 instantaneous translational kinetic energy of each slab. At each time
264 interval, it is a simple matter to solve for $c$, $h$, $\mathbf{a}_c$,
265 and $\mathbf{a}_h$, subject to the imposed momentum flux,
266 $j_z(\mathbf{p})$, and thermal flux, $J_z$ values. Since the VSS
267 operations do not change the kinetic energy due to orientational
268 degrees of freedom or the potential energy of a system, configurations
269 after the VSS move have exactly the same energy ({\it and} linear
270 momentum) as before the move.
271
272 As the simulation progresses, the VSS moves are performed on a regular
273 basis, and the system develops a thermal or velocity gradient in
274 response to the applied flux. Using the slope of the temperature or
275 velocity gradient, it is quite simple to obtain of thermal
276 conductivity ($\lambda$),
277 \begin{equation}
278 J_z = -\lambda \frac{\partial T}{\partial z},
279 \end{equation}
280 and shear viscosity ($\eta$),
281 \begin{equation}
282 j_z(p_x) = -\eta \frac{\partial \langle v_x \rangle}{\partial z}.
283 \end{equation}
284 Here, the quantities on the left hand side are the imposed flux
285 values, while the slopes are obtained from linear fits to the
286 gradients that develop in the simulated system.
287
288 The VSS-RNEMD approach is versatile in that it may be used to
289 implement both thermal and shear transport either separately or
290 simultaneously. Perturbations of velocities away from the ideal
291 Maxwell-Boltzmann distributions are minimal, and thermal anisotropy is
292 kept to a minimum. This ability to generate simultaneous thermal and
293 shear fluxes has been previously utilized to map out the shear
294 viscosity of SPC/E water over a wide range of temperatures (90~K) with
295 a single 1 ns simulation.\cite{Kuang2012}
296
297 \begin{figure}
298 \includegraphics[width=\linewidth]{figures/rnemd}
299 \caption{The VSS-RNEMD approach imposes unphysical transfer of
300 linear momentum or kinetic energy between a ``hot'' slab and a
301 ``cold'' slab in the simulation box. The system responds to this
302 imposed flux by generating velocity or temperature gradients. The
303 slope of the gradients can then be used to compute transport
304 properties (e.g. shear viscosity or thermal conductivity).}
305 \label{fig:rnemd}
306 \end{figure}
307
308 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
309 % INTERFACIAL CONDUCTANCE
310 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
311 \subsection{Reverse Non-Equilibrium Molecular Dynamics approaches
312 to interfacial transport}
313
314 Interfaces between dissimilar materials have transport properties
315 which can be defined as derivatives of the standard transport
316 coefficients in a direction normal to the interface. For example, the
317 {\it interfacial} thermal conductance ($G$) can be thought of as the
318 change in the thermal conductivity ($\lambda$) across the boundary
319 between materials:
320 \begin{align}
321 G &= \left(\nabla\lambda \cdot \mathbf{\hat{n}}\right)_{z_0} \\
322 &= J_z\left(\frac{\partial^2 T}{\partial z^2}\right)_{z_0} \Big/
323 \left(\frac{\partial T}{\partial z}\right)_{z_0}^2.
324 \label{derivativeG}
325 \end{align}
326 where $z_0$ is the location of the interface between two materials and
327 $\mathbf{\hat{n}}$ is a unit vector normal to the interface (assumed
328 to be the $z$ direction from here on). RNEMD simulations, and
329 particularly the VSS-RNEMD approach, function by applying a momentum
330 or thermal flux and watching the gradient response of the
331 material. This means that the {\it interfacial} conductance is a
332 second derivative property which is subject to significant noise and
333 therefore requires extensive sampling. We have been able to
334 demonstrate the use of the second derivative approach to compute
335 interfacial conductance at chemically-modified metal / solvent
336 interfaces. However, a definition of the interfacial conductance in
337 terms of a temperature difference ($\Delta T$) measured at $z_0$,
338 \begin{displaymath}
339 G = \frac{J_z}{\Delta T_{z_0}},
340 \end{displaymath}
341 is useful once the RNEMD approach has generated a stable temperature
342 gap across the interface.
343
344 \begin{figure}
345 \includegraphics[width=\linewidth]{figures/resistor_series}
346 \caption{The inverse of the interfacial thermal conductance, $G$, is
347 the Kapitza resistance, $R_K$. Because the gold / thiolate/
348 solvent interface extends a significant distance from the metal
349 surface, the interfacial resistance $R_K$ can be computed by
350 summing a series of temperature drops between adjacent temperature
351 bins along the $z$ axis.}
352 \label{fig:resistor_series}
353 \end{figure}
354
355 In the particular case we are studying here, there are two interfaces
356 involved in the transfer of heat from the gold slab to the solvent:
357 the metal/thiolate interface and the thiolate/solvent interface. We
358 could treat the temperature on each side of an interface as discrete,
359 making the interfacial conductance the inverse of the Kaptiza
360 resistance, or $G = \frac{1}{R_k}$. To model the total conductance
361 across multiple interfaces, it is useful to think of the interfaces as
362 a set of resistors wired in series. The total resistance is then
363 additive, $R_{total} = \sum_i R_{i}$ and the interfacial conductance
364 is the inverse of the total resistance, or $G = \frac{1}{\sum_i
365 R_i}$). In the interfacial region, we treat each bin in the
366 VSS-RNEMD temperature profile as a resistor with resistance
367 $\frac{T_{2}-T_{1}}{J_z}$, $\frac{T_{3}-T_{2}}{J_z}$, etc. The sum of
368 the set of resistors which spans the gold/thiolate interface, thiolate
369 chains, and thiolate/solvent interface simplifies to
370 \begin{equation}
371 R_{K} = \frac{T_{n}-T_{1}}{J_z},
372 \label{eq:finalG}
373 \end{equation}
374 or the temperature difference between the gold side of the
375 gold/thiolate interface and the solvent side of the thiolate/solvent
376 interface over the applied flux.
377
378
379 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
380 % **COMPUTATIONAL DETAILS**
381 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
382 \section{Computational Details}
383
384 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
385 % FORCE-FIELD PARAMETERS
386 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
387 \subsection{Force-Field Parameters}
388
389 Our simulations include a number of chemically distinct components.
390 Figure \ref{fig:structures} demonstrates the sites defined for both
391 the {\it n}-hexane and alkanethiolate ligands present in our
392 simulations.
393
394 \begin{figure}
395 \includegraphics[width=\linewidth]{figures/structures}
396 \caption{Topologies of the thiolate capping agents and solvent
397 utilized in the simulations. The chemically-distinct sites (S,
398 \ce{CH2}, and \ce{CH3}) are treated as united atoms. Most
399 parameters are taken from references \bibpunct{}{}{,}{n}{}{,}
400 \protect\cite{TraPPE-UA.alkanes} and
401 \protect\cite{TraPPE-UA.thiols}. Cross-interactions with the Au
402 atoms were adapted from references
403 \protect\cite{landman:1998},~\protect\cite{vlugt:cpc2007154},~and
404 \protect\cite{hautman:4994}.}
405 \label{fig:structures}
406 \end{figure}
407
408 The Au-Au interactions in the metal lattice slab are described by the
409 quantum Sutton-Chen (QSC) formulation.\cite{PhysRevB.59.3527} The QSC
410 potentials include zero-point quantum corrections and are
411 reparametrized for accurate surface energies compared to the
412 Sutton-Chen potentials.\cite{Chen90}
413
414 For the {\it n}-hexane solvent molecules, the TraPPE-UA
415 parameters\cite{TraPPE-UA.alkanes} were utilized. In this model,
416 sites are located at the carbon centers for alkyl groups. Bonding
417 interactions, including bond stretches and bends and torsions, were
418 used for intra-molecular sites closer than 3 bonds. For non-bonded
419 interactions, Lennard-Jones potentials were used. We have previously
420 utilized both united atom (UA) and all-atom (AA) force fields for
421 thermal conductivity,\cite{kuang:AuThl,Kuang2012} and since the united
422 atom force fields cannot populate the high-frequency modes that are
423 present in AA force fields, they appear to work better for modeling
424 thermal conductivity. The TraPPE-UA model for alkanes is known to
425 predict a slightly lower boiling point than experimental values. This
426 is one of the reasons we used a lower average temperature (200K) for
427 our simulations.
428
429 The TraPPE-UA force field includes parameters for thiol
430 molecules\cite{TraPPE-UA.thiols} which were used for the
431 alkanethiolate molecules in our simulations. To derive suitable
432 parameters for butanethiol adsorbed on Au(111) surfaces, we adopted
433 the S parameters from Luedtke and Landman\cite{landman:1998} and
434 modified the parameters for the CTS atom to maintain charge neutrality
435 in the molecule.
436
437 To describe the interactions between metal (Au) and non-metal atoms,
438 we refer to an adsorption study of alkyl thiols on gold surfaces by
439 Vlugt {\it et al.}\cite{vlugt:cpc2007154} They fitted an effective
440 Lennard-Jones form of potential parameters for the interaction between
441 Au and pseudo-atoms CH$_x$ and S based on a well-established and
442 widely-used effective potential of Hautman and Klein for the Au(111)
443 surface.\cite{hautman:4994} As our simulations require the gold slab
444 to be flexible to accommodate thermal excitation, the pair-wise form
445 of potentials they developed was used for our study.
446
447 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
448 % SIMULATION PROTOCOL
449 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
450 \subsection{Simulation Protocol}
451
452 We have implemented the VSS-RNEMD algorithm in OpenMD, our group
453 molecular dynamics code.\cite{openmd} An 1188 atom gold slab was
454 equilibrated at 1 atm and 200 K. The periodic box was then expanded
455 in the $z$-direction to expose two Au(111) faces on either side of the
456 11-atom thick slab.
457
458 A full monolayer of thiolates (1/3 the number of surface gold atoms)
459 was placed on three-fold hollow sites on the gold interfaces. The
460 effect of thiolate binding sites on the thermal conductance was tested
461 by placing thiolates at both fcc and hcp hollow sites. No appreciable
462 difference in the temperature profile was noted due to the location of
463 thiolate binding.
464
465 To test the role of thiolate chain length on interfacial thermal
466 conductance, full coverages of each of five chain lengths were tested:
467 butanethiolate (C$_4$), hexanethiolate (C$_6$), octanethiolate
468 (C$_8$), decanethiolate (C$_{10}$), and dodecanethiolate
469 (C$_{12}$). To test the effect of mixed chain lengths, full coverages
470 of C$_4$ / C$_{10}$ and C$_4$ / C$_{12}$ mixtures were created in
471 short/long chain percentages of 25/75, 50/50, 62.5/37.5, 75/25, and
472 87.5/12.5. The short and long chains were placed on the surface hollow
473 sites in a random configuration.
474
475 The simulation box $z$-dimension was set to roughly double the length
476 of the gold/thiolate block. Hexane solvent molecules were placed in
477 the vacant portion of the box using the packmol algorithm. Figure \ref{fig:timelapse} shows two of the mixed chain length systems both before and after the RNEMD simulation.
478
479 \begin{figure}
480 \includegraphics[width=\linewidth]{figures/timelapse}
481 \caption{Images of 25\%~C$_4$~/~75\%~C$_{12}$ (top panel) and 75\%~C$_4$~/~25\%~C$_{12}$ (bottom panel) interfaces at the beginning and end of 3 ns simulations. Solvent molecules that were initially present in the thiolate layer are colored light blue. Diffusion of the initially-trapped solvent into the bulk is apparent in the interface with fewer long chains. Trapped solvent is orientationally locked to the orientation of the ligand (and is less able to diffuse into the bulk) when the fraction of long chains increases.}
482 \label{fig:timelapse}
483 \end{figure}
484
485 The system was equilibrated to 220 K in the canonical (NVT) ensemble,
486 allowing the thiolates and solvent to warm gradually. Pressure
487 correction to 1 atm was done using an isobaric-isothermal (NPT)
488 integrator that allowed expansion or contraction only in the $z$
489 direction, maintaining the crystalline structure of the gold as close
490 to the bulk result as possible. The diagonal elements of the pressure
491 tensor were monitored during the pressure equilibration stage. If the
492 $xx$ and/or $yy$ elements had a mean above zero throughout the
493 simulation -- indicating residual surface tension in the plane of the
494 gold slab -- an additional short NPT equilibration step was performed
495 allowing all box dimensions to change. Once the pressure was stable
496 at 1 atm, a final equilibration stage was performed at constant
497 temperature. All systems were equilibrated in the microcanonical (NVE)
498 ensemble before proceeding with the VSS-RNEMD and data collection
499 stages.
500
501 A kinetic energy flux was applied using VSS-RNEMD. The total
502 simulation time was 3 nanoseconds, with velocity scaling occurring
503 every 10 femtoseconds. The hot slab was centered in the gold and the
504 cold slab was placed in the center of the solvent region. The entire
505 system has a (time-averaged) temperature of 220 K, with a temperature
506 difference between the hot and cold slabs of approximately 30 K. The
507 average temperature and kinetic energy flux were selected to prevent
508 solvent freezing (or glass formation) and to not allow the thiolates
509 to bury in the gold slab. The Au-S interaction has a deep potential
510 energy well, which allows sulfur atoms to embed into the gold slab at
511 temperatures above 250 K. Simulation conditions were chosen to avoid
512 both of these undesirable situations.
513
514 Temperature profiles of the system were created by dividing the box
515 into $\sim$ 3 \AA \, bins along the $z$ axis and recording the average
516 temperature of each bin.
517
518
519
520 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
521 % **RESULTS**
522 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
523 \section{Results}
524
525 The solvent, hexane, is a straight chain flexible alkane that is structurally
526 similar to the thiolate alkane tails. Previous work has shown that UA models
527 of hexane and butanethiolate have a high degree of vibrational
528 overlap.\cite{kuang:AuThl} This overlap provides a mechanism for thermal
529 energy conduction from the thiolates to the solvent. Indeed, we observe that
530 the interfacial conductance is twice as large with the thiolate monolayers (of
531 all chain lengths) than with the bare metal surface.
532
533 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
534 % CHAIN LENGTH
535 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
536 \subsection{Effect of Chain Length}
537
538 We examined full coverages of five chain lengths, n = 4, 6, 8, 10, and 12. As shown in table \ref{table:chainlengthG}, the interfacial conductance is roughly 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.
539 \begin{longtable}{p{4cm} p{3cm}}
540 \caption{Computed interfacial thermal conductance ($G$) values for bare gold and 100\% coverages of various thiolate alkyl chain lengths.}
541 \\
542 \centering {\bf Chain Length (n)} & \centering\arraybackslash {\bf G (MW/m$^2$/K)} \\ \hline
543 \endhead
544 \hline
545 \endfoot
546 \centering bare metal & \centering\arraybackslash 30.2 \\
547 \centering 4 & \centering\arraybackslash 59.4 \\
548 \centering 6 & \centering\arraybackslash 60.2 \\
549 \centering 8 & \centering\arraybackslash 61.0 \\
550 \centering 10 & \centering\arraybackslash 58.2 \\
551 \centering 12 & \centering\arraybackslash 58.8
552 \label{table:chainlengthG}
553 \end{longtable}
554
555 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
556 % MIXED CHAINS
557 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
558 \subsection{Effect of Mixed Chain Lengths}
559
560 Previous simulations have demonstrated a non-monotonic behavior for $G$ as a function of the surface coverage. One difficulty with the previous study was the ability of butanethiolate ligands to migrate on the Au(111) surface and to form segregated domains. To simulate the effect of low coverages while preventing thiolate domain formation, we maintain 100\% thiolate coverage while varying the proportions of short (butanethiolate, C$_4$ and long (decanethiolate, C$_{10}$, or dodecanethiolate, C$_{12}$) alkyl chains. Data on the conductance as the fraction of long chains was varied is shown in figure \ref{fig:Gstacks}. Note that as in the previous study, $G$ is depends on solvent accessibility to thermally excited ligands. Our simulations indicate a similar (but not as dramatic) non-monotonic dependence on the fraction of long chains.
561 \begin{figure}
562 \includegraphics[width=\linewidth]{figures/Gstacks}
563 \caption{Interfacial thermal conductivity of mixed-chains has a non-monotonic dependence on the fraction of long chains (lower panels). At low fractions of long chains, the solvent escape rate ($k_{escape}$) dominates the heat transfer process, while the solvent-thiolate orientational ordering dominates in systems with higher fractions of long chains (upper panels).}
564 \label{fig:Gstacks}
565 \end{figure}
566
567 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
568 % **DISCUSSION**
569 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
570 \section{Discussion}
571 In the mixed chain-length simulations, solvent molecules can become
572 temporarily trapped or entangled with the thiolate chains. Their
573 residence in close proximity to the higher temperature environment
574 close to the surface allows them to carry heat away from the surface
575 quite efficiently. There are two aspects of this behavior that are
576 relevant to thermal conductance of the interface: the residence time
577 of solvent molecules in the thiolate layer, and the alignment
578 of the C-C chains as a mechanism for transferring vibrational
579 energy to these entrapped solvent molecules. To quantify these competing effects, we have computed solvent escape rates from the ligand layer as well as a joint orientational order parameter between the trapped solvent and the thiolate ligands.
580
581 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
582 % RESIDENCE TIME
583 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
584 \subsection{Mobility of solvent in the interfacial layer}
585
586 We use a simple survival correlation function, $C(t)$, to measure the
587 residence time of a solvent molecule in the thiolate
588 layer. This function correlates the identity of all hexane molecules
589 within the $z$-coordinate range of the thiolate layer at two separate
590 times. If the solvent molecule is present at both times, the
591 configuration contributes a $1$, while the absence of the molecule at
592 the later time indicates that the solvent molecule has migrated into
593 the bulk, and this configuration contributes a $0$. A steep decay in
594 $C(t)$ indicates a high turnover rate of solvent molecules from the
595 chain region to the bulk. We define the escape rate for trapped solvent molecules at the interface as
596 \begin{equation}
597 k_{escape} = \left( \int_0^T C(t) dt \right)^{-1}
598 \label{eq:mobility}
599 \end{equation}
600 where T is the length of the simulation. This is a direct measure of
601 the rate at which solvent molecules initially entangled in the thiolate layer
602 can escape into the bulk. As $k_{escape} \rightarrow 0$, the
603 solvent has become permanently trapped in the thiolate layer. In
604 figure \ref{fig:Gstacks} we show that interfacial solvent mobility
605 decreases as the percentage of long thiolate chains increases.
606
607 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
608 % ORDER PARAMETER
609 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
610
611 \subsection{Vibrational coupling via orientational ordering}
612
613 As the fraction of long-chain thiolates increases, the entrapped
614 solvent molecules must find specific orientations relative to the mean
615 orientation of the thiolate chains. This alignment allows for
616 efficient thermal energy exchange between the thiolate alkyl chain and
617 the solvent molecules.
618
619 To measure this cooperative ordering, we computed the orientational order
620 parameters and director axes for both the thiolate chains and for the
621 entrapped solvent. The director axis can be easily obtained by diagonalization
622 of the order parameter tensor,
623 \begin{equation}
624 \mathsf{Q}_{\alpha \beta} = \frac{1}{2 N} \sum_{i=1}^{N} \left( 3 \mathbf{e}_{i
625 \alpha} \mathbf{e}_{i \beta} - \delta_{\alpha \beta} \right)
626 \end{equation}
627 where $\mathbf{e}_{i \alpha}$ was the $\alpha = x,y,z$ component of
628 the unit vector $\mathbf{e}_{i}$ along the long axis of molecule $i$.
629 For both kinds of molecules, the $\mathbf{e}$ vector is defined using
630 the terminal atoms of the chains.
631
632 The largest eigenvalue of $\overleftrightarrow{\mathsf{Q}}$ is
633 traditionally used to obtain orientational order parameter, while the
634 eigenvector corresponding to the order parameter yields the director
635 axis ($\mathbf{d}(t)$) which defines the average direction of
636 molecular alignment at any time $t$. The overlap between the director
637 axes of the thiolates and the entrapped solvent is time-averaged,
638 \begin{equation}
639 \langle d \rangle = \langle \mathbf{d}_{thiolates} \left( t \right) \cdot
640 \mathbf{d}_{solvent} \left( t \right) \rangle_t
641 \label{eq:orientation}
642 \end{equation}
643 and reported in figure \ref{fig:Gstacks}.
644
645 Once the solvent molecules have picked up thermal energy from the
646 thiolates, they carry heat away from the gold as they diffuse back
647 into the bulk solvent. When the percentage of long chains decreases,
648 the tails of the long chains are much more disordered and do not
649 provide structured channels for the solvent to fill.
650
651 C$_4$ / C$_{10}$ mixed monolayers have a peak interfacial conductance with 75\% long chains. At this fraction of long chains, the cooperative orientational ordering of the solvent molecules and chains becomes the dominant effect while the solvent escape rate sharply decreases. C$_4$ / C$_{12}$ mixtures have a peak interfacial conductance for 87.5\% long chains. The solvent-thiolate orientational ordering reaches its maximum value at this long chain fraction. Long chain fractions of over $0.5$ for the n = 4, 12 system are well ordered, but this effect is tempered by the exceptionally slow solvent escape rate.
652
653 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
654 % **CONCLUSIONS**
655 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
656 \section{Conclusions}
657 Our results suggest that a mixed vibrational transfer / convection model is necessary to explain the features of heat transfer at this interface. The alignment of the solvent chains with the ordered ligand allows rapid transfer of energy to the trapped solvent (and this is the dominant feature for ordered ligand layers). Diffusion of the vibrationally excited solvent into the bulk also plays a significant role when the ligands are less tightly packed.
658
659 In the language of earlier continuum approaches to interfacial
660 conductance,\cite{RevModPhys.61.605} the alignment of the chains is an
661 important factor in the transfer of phonons from the thiolate layer to the
662 trapped solvent. The aligned solvent and thiolate chains have nearly identical
663 acoustic impedances and the phonons can scatter directly into a solvent
664 molecule that has been forced into alignment. When the entrapped solvent has
665 more configurations available, the likelihood of an impedance mismatch is
666 higher, and the phonon scatters into the solvent with lower
667 efficiency. The fractional coverage of the long chains is therefore a simple
668 way of tuning the acoustic mismatch between the thiolate layer and the hexane
669 solvent.
670
671 Efficient heat transfer also can be accomplished via convective or diffusive motion of vibrationally excited solvent back into the bulk. Once the entrapped solvent becomes too tightly aligned with the ligands, however, the convective avenue of heat transfer is cut off.
672
673 Our simulations suggest a number of routes to make interfaces with high thermal conductance. If it is possible to create an interface which forces the solvent into alignment with a ligand that shares many of the solvent's vibrational modes, while simultaneously preserving solvent mobility back to the bulk, we would expect a significant jump in the interfacial conductance. One possible way to do this is to use polyene ligands with alternating unsaturated bonds. These are significantly more rigid than long alkanes, and could force solvent alignment (even at low relative coverages) while preserving mobility into the bulk.
674
675 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
676 % **ACKNOWLEDGMENTS**
677 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
678 \section*{Acknowledgments}
679
680 We gratefully acknowledge conversations with Dr. Shenyu Kuang. Support for
681 this project was provided by the National Science Foundation under grant
682 CHE-0848243. Computational time was provided by the Center for Research
683 Computing (CRC) at the University of Notre Dame.
684
685 \newpage
686
687 \bibliography{thiolsRNEMD}
688
689 \end{doublespace}
690 \end{document}
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