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1 \documentclass[11pt]{article}
2 \usepackage{amsmath}
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23 \bibliographystyle{achemso}
24
25 \begin{document}
26
27 \title{Simulations of heat conduction at thiolate-capped gold
28 surfaces: The role of chain length and solvent penetration}
29
30 \author{Kelsey M. Stocker and J. Daniel
31 Gezelter\footnote{Corresponding author. \ Electronic mail:
32 gezelter@nd.edu} \\
33 251 Nieuwland Science Hall, \\
34 Department of Chemistry and Biochemistry,\\
35 University of Notre Dame\\
36 Notre Dame, Indiana 46556}
37
38 \date{\today}
39
40 \maketitle
41
42 \begin{doublespace}
43
44 \begin{abstract}
45
46 \end{abstract}
47
48 \newpage
49
50 %\narrowtext
51
52 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
53 % **INTRODUCTION**
54 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
55 \section{Introduction}
56
57 The structural and dynamical details of interfaces between metal
58 nanoparticles and solvents determines how energy flows between these
59 particles and their surroundings. Understanding this energy flow is
60 essential in designing and functionalizing metallic nanoparticles for
61 plasmonic photothermal
62 therapies,\cite{Jain:2007ux,Petrova:2007ad,Gnyawali:2008lp,Mazzaglia:2008to,Huff:2007ye,Larson:2007hw} which rely on the ability of metallic
63 nanoparticles to absorb light in the near-IR, a portion of the
64 spectrum in which living tissue is very nearly transparent. The
65 principle of this therapy is to pump the particles at high power at
66 the plasmon resonance and to allow heat dissipation to kill targeted
67 (e.g. cancerous) cells. The relevant physical property controlling
68 this transfer of energy is the interfacial thermal conductance, $G$,
69 which can be somewhat difficult to determine
70 experimentally.\cite{Wilson:2002uq,Plech:2005kx}
71
72 Metallic particles have also been proposed for use in highly efficient
73 thermal-transfer fluids, although careful experiments by Eapen {\it et al.}
74 have shown that metal-particle-based ``nanofluids'' have thermal
75 conductivities that match Maxwell predictions.\cite{Eapen:2007th} The
76 likely cause of previously reported non-Maxwell
77 behavior\cite{Eastman:2001wb,Keblinski:2002bx,Lee:1999ct,Xue:2003ya,Xue:2004oa}
78 is percolation networks of nanoparticles exchanging energy via the
79 solvent,\cite{Eapen:2007mw} so it is vital to get a detailed molecular
80 picture of particle-solvent interactions in order to understand the
81 thermal behavior of complex fluids. To date, there have been few
82 reported values (either from theory or experiment) for $G$ for
83 ligand-protected nanoparticles embedded in liquids, and there is a
84 significant gap in knowledge about how chemically distinct ligands or
85 protecting groups will affect heat transport from the particles.
86
87 The thermal properties of various nanostructured interfaces have been
88 investigated experimentally by a number of groups: Cahill and
89 coworkers studied nanoscale thermal transport from metal
90 nanoparticle/fluid interfaces, to epitaxial TiN/single crystal oxides
91 interfaces, and hydrophilic and hydrophobic interfaces between water
92 and solids with different self-assembled
93 monolayers.\cite{cahill:793,Wilson:2002uq,PhysRevB.67.054302,doi:10.1021/jp048375k,PhysRevLett.96.186101}
94 Wang {\it et al.} studied heat transport through long-chain
95 hydrocarbon monolayers on gold substrate at the individual molecular
96 level,\cite{Wang10082007} Schmidt {\it et al.} studied the role of
97 cetyltrimethylammonium bromide (CTAB) on the thermal transport between
98 gold nanorods and solvent,\cite{doi:10.1021/jp8051888} and Juv\'e {\it
99 et al.} studied the cooling dynamics, which is controlled by thermal
100 interface resistance of glass-embedded metal
101 nanoparticles.\cite{PhysRevB.80.195406} Although interfaces are
102 normally considered barriers for heat transport, Alper {\it et al.}
103 suggested that specific ligands (capping agents) could completely
104 eliminate this barrier
105 ($G\rightarrow\infty$).\cite{doi:10.1021/la904855s}
106
107 In previous simulations, we applied a variant of reverse
108 non-equilibrium molecular dynamics (RNEMD) to calculate the
109 interfacial thermal conductance at a metal / organic solvent interface
110 that had been chemically protected by butanethiolate groups. Our
111 calculations suggest an explanation for the very large thermal
112 conductivity at alkanethiol-capped metal surfaces when compared with
113 bare metal/solvent interfaces. Specifically, the chemical bond
114 between the metal and the ligand introduces a vibrational overlap that
115 is not present without the protecting group, and the overlap between
116 the vibrational spectra (metal to ligand, ligand to solvent) provides
117 a mechanism for rapid thermal transport across the interface.
118
119 One interesting result of our previous work was the observation of
120 {\it non-monotonic dependence} of the thermal conductance on the
121 coverage of a metal surface by a chemical protecting group. Our
122 explanation for this behavior was that gaps in surface coverage
123 allowed solvent to penetrate close to the capping molecules that had
124 been heated by the metal surface, to absorb thermal energy from these
125 molecules, and then diffuse away. The effect of surface coverage is
126 relatively difficult to study as the individual protecting groups have
127 lateral mobility on the surface and can aggregate to form domains on
128 the timescale of the simulation.
129
130 The work reported here involves the use of velocity shearing and
131 scaling reverse non-equilibrium molecular dynamics (VSS-RNEMD) to
132 study surfaces composed of mixed-length chains which collectively form
133 a complete monolayer on the surfaces. These complete (but
134 mixed-chain) surfaces are significantly less prone to surface domain
135 formation, and would allow us to further investigate the mechanism of
136 heat transport to the solvent.
137
138 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
139 % **METHODOLOGY**
140 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
141 \section{Methodology}
142
143 There are many ways to compute bulk transport properties from
144 classical molecular dynamics simulations. Equilibrium Molecular
145 Dynamics (EMD) simulations can be used by computing relevant time
146 correlation functions and assuming that linear response theory
147 holds.\cite{PhysRevB.37.5677,MASSOBRIO:1984bl,PhysRev.119.1,Viscardy:2007rp,che:6888,kinaci:014106}
148 For some transport properties (notably thermal conductivity), EMD
149 approaches are subject to noise and poor convergence of the relevant
150 correlation functions. Traditional Non-equilibrium Molecular Dynamics
151 (NEMD) methods impose a gradient (e.g. thermal or momentum) on a
152 simulation.\cite{ASHURST:1975tg,Evans:1982zk,ERPENBECK:1984sp,MAGINN:1993hc,Berthier:2002ij,Evans:2002ai,Schelling:2002dp,PhysRevA.34.1449,JiangHao_jp802942v}
153 However, the resulting flux is often difficult to
154 measure. Furthermore, problems arise for NEMD simulations of
155 heterogeneous systems, such as phase-phase boundaries or interfaces,
156 where the type of gradient to enforce at the boundary between
157 materials is unclear.
158
159 {\it Reverse} Non-Equilibrium Molecular Dynamics (RNEMD) methods adopt
160 a different approach in that an unphysical {\it flux} is imposed
161 between different regions or ``slabs'' of the simulation
162 box.\cite{MullerPlathe:1997xw,ISI:000080382700030,Kuang:2010uq} The
163 system responds by developing a temperature or momentum {\it gradient}
164 between the two regions. Since the amount of the applied flux is known
165 exactly, and the measurement of a gradient is generally less
166 complicated, imposed-flux methods typically take shorter simulation
167 times to obtain converged results for transport properties. The
168 corresponding temperature or velocity gradients which develop in
169 response to the applied flux are then related (via linear response
170 theory) to the transport coefficient of interest. These methods are
171 quite efficient, in that they do not need many trajectories to provide
172 information about transport properties. To date, they have been
173 utilized in computing thermal and mechanical transfer of both
174 homogeneous
175 liquids~\cite{MullerPlathe:1997xw,ISI:000080382700030,Maginn:2010} as
176 well as heterogeneous
177 systems.\cite{garde:nl2005,garde:PhysRevLett2009,kuang:AuThl}
178
179 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
180 % VSS-RNEMD
181 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
182 \subsection{VSS-RNEMD}
183 The original ``swapping'' approaches by M\"{u}ller-Plathe {\it et
184 al.}\cite{ISI:000080382700030,MullerPlathe:1997xw} can be understood
185 as a sequence of imaginary elastic collisions between particles in
186 regions separated by half of the simulation cell. In each collision,
187 the entire momentum vectors of both particles may be exchanged to
188 generate a thermal flux. Alternatively, a single component of the
189 momentum vectors may be exchanged to generate a shear flux. This
190 algorithm turns out to be quite useful in many simulations of bulk
191 liquids. However, the M\"{u}ller-Plathe swapping approach perturbs the
192 system away from ideal Maxwell-Boltzmann distributions, and this has
193 undesirable side-effects when the applied flux becomes
194 large.\cite{Maginn:2010}
195
196 Instead of having momentum exchange between {\it individual particles}
197 in each slab, the NIVS algorithm applies velocity scaling to all of
198 the selected particles in both slabs.\cite{Kuang:2010uq} A combination
199 of linear momentum, kinetic energy, and flux constraint equations
200 governs the amount of velocity scaling performed at each step. NIVS
201 has been shown to be very effective at producing thermal gradients and
202 for computing thermal conductivities, particularly for heterogeneous
203 interfaces. Although the NIVS algorithm can also be applied to impose
204 a directional momentum flux, thermal anisotropy was observed in
205 relatively high flux simulations, and the method is not suitable for
206 imposing a shear flux or for computing shear viscosities.
207
208 The most useful RNEMD
209 approach developed so far utilizes a series of simultaneous velocity
210 shearing and scaling exchanges between the two
211 slabs.\cite{2012MolPh.110..691K} This method provides a set of
212 conservation constraints while simultaneously creating a desired flux
213 between the two slabs. Satisfying the constraint equations ensures
214 that the new configurations are sampled from the same NVE ensemble.
215
216 The VSS moves are applied periodically to scale and shift the particle
217 velocities ($\mathbf{v}_i$ and $\mathbf{v}_j$) in two slabs ($H$ and
218 $C$) which are separated by half of the simulation box,
219 \begin{displaymath}
220 \begin{array}{rclcl}
221
222 & \underline{\mathrm{shearing}} & &
223 \underline{~~~~~~~~~~~~\mathrm{scaling}~~~~~~~~~~~~} \\ \\
224 \mathbf{v}_i \leftarrow &
225 \mathbf{a}_c\ & + & c\cdot\left(\mathbf{v}_i - \langle\mathbf{v}_c
226 \rangle\right) + \langle\mathbf{v}_c\rangle \\
227 \mathbf{v}_j \leftarrow &
228 \mathbf{a}_h & + & h\cdot\left(\mathbf{v}_j - \langle\mathbf{v}_h
229 \rangle\right) + \langle\mathbf{v}_h\rangle .
230
231 \end{array}
232 \end{displaymath}
233 Here $\langle\mathbf{v}_c\rangle$ and $\langle\mathbf{v}_h\rangle$ are
234 the center of mass velocities in the $C$ and $H$ slabs, respectively.
235 Within the two slabs, particles receive incremental changes or a
236 ``shear'' to their velocities. The amount of shear is governed by the
237 imposed momentum flux, $j_z(\mathbf{p})$
238 \begin{eqnarray}
239 \mathbf{a}_c & = & - \mathbf{j}_z(\mathbf{p}) \Delta t / M_c \label{vss1}\\
240 \mathbf{a}_h & = & + \mathbf{j}_z(\mathbf{p}) \Delta t / M_h \label{vss2}
241 \end{eqnarray}
242 where $M_{\{c,h\}}$ is total mass of particles within each slab and $\Delta t$
243 is the interval between two separate operations.
244
245 To simultaneously impose a thermal flux ($J_z$) between the slabs we
246 use energy conservation constraints,
247 \begin{eqnarray}
248 K_c - J_z\Delta t & = & c^2 (K_c - \frac{1}{2}M_c \langle\mathbf{v}_c
249 \rangle^2) + \frac{1}{2}M_c (\langle \mathbf{v}_c \rangle + \mathbf{a}_c)^2 \label{vss3}\\
250 K_h + J_z\Delta t & = & h^2 (K_h - \frac{1}{2}M_h \langle\mathbf{v}_h
251 \rangle^2) + \frac{1}{2}M_h (\langle \mathbf{v}_h \rangle +
252 \mathbf{a}_h)^2 \label{vss4}.
253 \label{constraint}
254 \end{eqnarray}
255 Simultaneous solution of these quadratic formulae for the scaling
256 coefficients, $c$ and $h$, will ensure that the simulation samples from
257 the original microcanonical (NVE) ensemble. Here $K_{\{c,h\}}$ is the
258 instantaneous translational kinetic energy of each slab. At each time
259 interval, it is a simple matter to solve for $c$, $h$, $\mathbf{a}_c$,
260 and $\mathbf{a}_h$, subject to the imposed momentum flux,
261 $j_z(\mathbf{p})$, and thermal flux, $J_z$ values. Since the VSS
262 operations do not change the kinetic energy due to orientational
263 degrees of freedom or the potential energy of a system, configurations
264 after the VSS move have exactly the same energy ({\it and} linear
265 momentum) as before the move.
266
267 As the simulation progresses, the VSS moves are performed on a regular
268 basis, and the system develops a thermal or velocity gradient in
269 response to the applied flux. Using the slope of the temperature or
270 velocity gradient, it is quite simple to obtain of thermal
271 conductivity ($\lambda$),
272 \begin{equation}
273 J_z = -\lambda \frac{\partial T}{\partial z},
274 \end{equation}
275 and shear viscosity ($\eta$),
276 \begin{equation}
277 j_z(p_x) = -\eta \frac{\partial \langle v_x \rangle}{\partial z}.
278 \end{equation}
279 Here, the quantities on the left hand side are the imposed flux
280 values, while the slopes are obtained from linear fits to the
281 gradients that develop in the simulated system.
282
283 The VSS-RNEMD approach is versatile in that it may be used to
284 implement both thermal and shear transport either separately or
285 simultaneously. Perturbations of velocities away from the ideal
286 Maxwell-Boltzmann distributions are minimal, and thermal anisotropy is
287 kept to a minimum. This ability to generate simultaneous thermal and
288 shear fluxes has been previously utilized to map out the shear
289 viscosity of SPC/E water over a wide range of temperatures (90~K) with
290 a {\it single 1 ns simulation}.\cite{2012MolPh.110..691K}
291
292 \begin{figure}
293 \includegraphics[width=\linewidth]{figures/rnemd}
294 \caption{VSS-RNEMD}
295 \label{fig:rnemd}
296 \end{figure}
297
298
299
300 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
301 % INTERFACIAL CONDUCTANCE
302 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
303 \subsection{Reverse Non-Equilibrium Molecular Dynamics approaches
304 to interfacial transport}
305
306 Interfaces between dissimilar materials have transport properties
307 which can be defined as derivatives of the standard transport
308 coefficients in a direction normal to the interface. For example, the
309 {\it interfacial} thermal conductance ($G$) can be thought of as the
310 change in the thermal conductivity ($\lambda$) across the boundary
311 between materials:
312 \begin{align}
313 G &= \left(\nabla\lambda \cdot \mathbf{\hat{n}}\right)_{z_0} \\
314 &= J_z\left(\frac{\partial^2 T}{\partial z^2}\right)_{z_0} \Big/
315 \left(\frac{\partial T}{\partial z}\right)_{z_0}^2.
316 \label{derivativeG}
317 \end{align}
318 where $z_0$ is the location of the interface between two materials and
319 $\mathbf{\hat{n}}$ is a unit vector normal to the interface (assumed
320 to be the $z$ direction from here on). RNEMD simulations, and
321 particularly the VSS-RNEMD approach, function by applying a momentum
322 or thermal flux and watching the gradient response of the
323 material. This means that the {\it interfacial} conductance is a
324 second derivative property which is subject to significant noise and
325 therefore requires extensive sampling. We have been able to
326 demonstrate the use of the second derivative approach to compute
327 interfacial conductance at chemically-modified metal / solvent
328 interfaces. However, a definition of the interfacial conductance in
329 terms of a temperature difference ($\Delta T$) measured at $z_0$,
330 \begin{displaymath}
331 G = \frac{J_z}{\Delta T_{z_0}},
332 \end{displaymath}
333 is useful once the RNEMD approach has generated a stable temperature
334 gap across the interface.
335
336 \begin{figure}
337 \includegraphics[width=\linewidth]{figures/resistor_series}
338 \caption{RESISTOR SERIES}
339 \label{fig:resistor_series}
340 \end{figure}
341
342 In the particular case we are studying here, there are two interfaces
343 involved in the transfer of heat from the gold slab to the solvent:
344 the gold/thiolate interface and the thiolate/solvent interface. We
345 could treat the temperature on each side of an interface as discrete,
346 making the interfacial conductance the inverse of the Kaptiza
347 resistance, or $G = \frac{1}{R_k}$. To model the total conductance
348 across multiple interfaces, it is useful to think of the interfaces as
349 a set of resistors wired in series. The total resistance is then
350 additive, $R_{total} = \sum_i R_{i}$ and the interfacial conductance
351 is the inverse of the total resistance, or $G = \frac{1}{\sum_i
352 R_i}$). In the interfacial region, we treat each bin in the
353 VSS-RNEMD temperature profile as a resistor with resistance
354 $\frac{T_{2}-T_{1}}{J_z}$, $\frac{T_{3}-T_{2}}{J_z}$, etc. The sum of
355 the set of resistors which spans the gold/thiolate interface, thiolate
356 chains, and thiolate/solvent interface simplifies to
357 \begin{equation}
358 \frac{T_{n}-T_{1}}{J_z},
359 \label{eq:finalG}
360 \end{equation}
361 or the temperature difference between the gold side of the
362 gold/thiolate interface and the solvent side of the thiolate/solvent
363 interface over the applied flux.
364
365
366 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
367 % **COMPUTATIONAL DETAILS**
368 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
369 \section{Computational Details}
370
371 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
372 % SIMULATION PROTOCOL
373 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
374 \subsection{Simulation Protocol}
375
376 We have implemented the VSS-RNEMD algorithm in OpenMD, our
377 group molecular dynamics code. A gold slab 11 atoms thick was
378 equilibrated at 1 atm and 200 K. The periodic box was expanded
379 in the z direction to expose two Au(111) faces.
380
381 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.
382
383 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.
384
385 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.
386
387 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.
388
389 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.
390
391 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
392 % FORCE-FIELD PARAMETERS
393 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
394 \subsection{Force-Field Parameters}
395
396 Our simulations include a number of chemically distinct components.
397 Figure \ref{fig:structures} demonstrates the sites defined for both
398 the {\it n}-hexane and alkanethiolate ligands present in our
399 simulations. Force field parameters are needed for interactions both
400 between the same type of particles and between particles of different
401 species.
402
403 \begin{figure}
404 \includegraphics[width=\linewidth]{figures/structures}
405 \caption{STRUCTURES}
406 \label{fig:structures}
407 \end{figure}
408
409 The Au-Au interactions in metal lattice slab is described by the
410 quantum Sutton-Chen (QSC) formulation.\cite{PhysRevB.59.3527} The QSC
411 potentials include zero-point quantum corrections and are
412 reparametrized for accurate surface energies compared to the
413 Sutton-Chen potentials.\cite{Chen90}
414
415 For the {\it n}-hexane solvent molecules, the TraPPE-UA
416 parameters\cite{TraPPE-UA.alkanes} were utilized. In this model,
417 sites are located at the carbon centers for alkyl groups. Bonding
418 interactions, including bond stretches and bends and torsions, were
419 used for intra-molecular sites closer than 3 bonds. For non-bonded
420 interactions, Lennard-Jones potentials are used. We have previously
421 utilized both united atom (UA) and all-atom (AA) force fields for
422 thermal conductivity in previous work,\cite{} and since the united
423 atom force fields cannot populate the high-frequency modes that are
424 present in AA force fields, they appear to work better for modeling
425 thermal conductivity. The TraPPE-UA model for alkanes is known to
426 predict a slightly lower boiling point than experimental values. This
427 is one of the reasons we used a lower average temperature (200K) for
428 our simulations.
429
430 The TraPPE-UA force field includes parameters for thiol
431 molecules\cite{TraPPE-UA.thiols} which were used for the
432 alkanethiolate molecules in our simulations. To derive suitable
433 parameters for butanethiol adsorbed on Au(111) surfaces, we adopted
434 the S parameters from Luedtke and Landman\cite{landman:1998} and
435 modified the parameters for the CTS atom to maintain charge neutrality
436 in the molecule.
437
438 To describe the interactions between metal (Au) and non-metal atoms,
439 we refer to an adsorption study of alkyl thiols on gold surfaces by
440 Vlugt {\it et al.}\cite{vlugt:cpc2007154} They fitted an effective
441 Lennard-Jones form of potential parameters for the interaction between
442 Au and pseudo-atoms CH$_x$ and S based on a well-established and
443 widely-used effective potential of Hautman and Klein for the Au(111)
444 surface.\cite{hautman:4994} As our simulations require the gold slab
445 to be flexible to accommodate thermal excitation, the pair-wise form
446 of potentials they developed was used for our study. Table
447 \ref{table:pars} in the supporting information summarizes the
448 ``metal/non-metal'' parameters utilized in our simulations.
449
450 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
451 % **RESULTS**
452 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
453 \section{Results}
454
455
456 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
457 % CHAIN LENGTH
458 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
459 \subsection{Effect of Chain Length}
460
461 We examined full coverages of five chain lengths, n = 4, 6, 8, 10, 12. 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. The trend of interfacial conductance is mostly flat 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. There is, however, a peak in conductance for a chain length of 6 (hexanethiolate). This may be due to the equivalent chain lengths of the hexane solvent and the alkyl chain of the capping agent, leading to an especially high degree of vibrational overlap between the thiolate and solvent. Strong vibrational overlap would allow for efficient thermal energy transfer across the thiolate/solvent interface.
462
463 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
464 % MIXED CHAINS
465 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
466 \subsection{Effect of Mixed Chain Lengths}
467
468 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 easily line up lengthwise with the thiolate tails 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 aggregation we maintain 100\% thiolate coverage while varying the proportions of short (butanethiolate, n = 4) and long (decanethiolate, n = 10 or dodecanethiolate, n = 12). In systems where there is a mix of short and long chain thiolates, interfacial conductance is a non-monotonic function of the percent of long chains. The depth of the gaps between the long chains is $n_{long} - n_{short}$, which has implications for the ability of the hexane solvent to fill in the gaps between the long chains.
469
470 \subsubsection{Butanethiolate/Decanethiolate}
471 Mixtures of butanethiolate/decanethiolate (n = 4, 10) have a peak interfacial condutance for 25\%/75\% short/long chains.
472
473 \subsubsection{Butanethiolate/Dodecanethiolate}
474 Mixtures of butanethiolate/dodecanethiolate (n = 4, 12) have a peak interfacial condutance for 12.5\%/87.5\% short/long chains.
475
476
477
478
479 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
480 % **DISCUSSION**
481 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
482 \section{Discussion}
483
484 In the mixed chain-length simulations, solvent molecules can become
485 temporarily trapped or entangled with the thiolate chains. Their
486 residence in close proximity to the higher temperature environment
487 close to the surface allows them to carry heat away from the surface
488 quite efficiently. There are two aspects of this behavior that are
489 relevant to thermal conductance of the interface: the residence time
490 of solvent molecules in the thiolate layer, and the orientational
491 ordering of the C-C chains as a mechanism for transferring vibrational
492 energy to these entrapped solvent molecules.
493
494 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
495 % RESIDENCE TIME
496 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
497 \subsection{Residence times for solvent in the interfacial layer}
498
499 We use a simple survival correlation function, $C(t)$, to quantify the
500 residence time of a solvent molecule in the long thiolate chain
501 layer. This function correlates the identity of all hexane molecules
502 within the $z$-coordinate range of the thiolate layer at two separate
503 times. If the solvent molecule is present at both times, the
504 configuration contributes a $1$, while the absence of the molecule at
505 the later time indicates that the solvent molecule has migrated into
506 the bulk, and this configuration contributes a $0$. A steep decay in
507 $C(t)$ indicates a high turnover rate of solvent molecules from the
508 chain region to the bulk. The correlation function is easily fit
509 using a biexponential,
510 \begin{equation}
511 C(t) = A \, e^{-t/\tau_{short}} + (1-A) e^{-t/\tau_{long}}
512 \label{eq:biexponential}
513 \end{equation}
514 to determine short and long residence timescales and the relative
515 populations of solvent molecules that can escape rapidly. In table
516 \ref{table:res} we show that the timescales...
517
518
519 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
520 % ORDER PARAMETER
521 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
522
523 \subsection{Vibrational coupling via orientational ordering}
524
525 As the fraction of long-chain thiolates becomes large, the entrapped
526 solvent molecules must find specific orientations relative to the mean
527 orientation of the thiolate chains. This configuration allows for
528 efficient thermal energy exchange between the thiolate alkyl chain and
529 the solvent molecules.
530
531 To quantify this cooperative
532 ordering, we computed the orientational order parameters and director
533 axes for both the thiolate chains and for the entrapped solvent. The
534 director axis can be easily obtained by diagonalization of the order
535 parameter tensor,
536 \begin{equation}
537 \mathsf{Q}_{\alpha \beta} = \frac{1}{2 N} \sum_{i=1}^{N} \left( 3 \mathbf{e}_{i
538 \alpha} \mathbf{e}_{i \beta} - \delta_{\alpha \beta} \right)
539 \end{equation}
540 where $\mathbf{e}_{i \alpha}$ was the $\alpha = x,y,z$ component of
541 the unit vector $\mathbf{e}_{i}$ along the long axis of molecule $i$.
542 For both kinds of molecules, the $\mathbf{e}$ vector is defined using
543 the terminal atoms of the chains.
544
545 The largest eigenvalue of $\overleftrightarrow{\mathsf{Q}}$ is
546 traditionally used to obtain orientational order parameter, while the
547 eigenvector corresponding to the order parameter yields the director
548 axis ($\mathbf{d}(t)$) which defines the average direction of
549 molecular alignment at any time $t$. The overlap between the director
550 axes of the thiolates and the entrapped solvent is time-averaged,
551 \begin{equation}
552 \left \langle \mathbf{d}_{thiolates} \left( t \right) \cdot
553 \mathbf{d}_{solvent} \left( t \right) \right \rangle,
554 \label{eq:orientation}
555 \end{equation}
556 and reported in table \ref{table:ordering}.
557
558 Once the solvent molecules have picked up thermal energy from the
559 thiolates, they carry heat away from the gold as they diffuse back
560 into the bulk solvent. When the percentage of long chains decreases,
561 the tails of the long chains are much more disordered and do not
562 provide structured channels for the solvent to fill.
563
564 Although the alignment of the chains with the entrapped solvent is one
565 possible mechanism for the non-monotonic increase in the conductance
566 as a function
567
568
569 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
570 % **ACKNOWLEDGMENTS**
571 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
572 \section*{Acknowledgments}
573 Support for this project was provided by the
574 National Science Foundation under grant CHE-0848243. Computational
575 time was provided by the Center for Research Computing (CRC) at the
576 University of Notre Dame.
577
578 \newpage
579
580 \bibliography{thiolsRNEMD}
581
582 \end{doublespace}
583 \end{document}
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