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\begin{document} |
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\title{Simulating interfacial thermal conductance at metal-solvent |
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interfaces: the role of chemical capping agents} |
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\author{Shenyu Kuang and J. Daniel |
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Gezelter\footnote{Corresponding author. \ Electronic mail: gezelter@nd.edu} \\ |
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Department of Chemistry and Biochemistry,\\ |
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University of Notre Dame\\ |
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Notre Dame, Indiana 46556} |
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\date{\today} |
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\maketitle |
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\begin{doublespace} |
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\begin{abstract} |
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We have developed a Non-Isotropic Velocity Scaling algorithm for |
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setting up and maintaining stable thermal gradients in non-equilibrium |
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molecular dynamics simulations. This approach effectively imposes |
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unphysical thermal flux even between particles of different |
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identities, conserves linear momentum and kinetic energy, and |
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minimally perturbs the velocity profile of a system when compared with |
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previous RNEMD methods. We have used this method to simulate thermal |
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conductance at metal / organic solvent interfaces both with and |
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without the presence of thiol-based capping agents. We obtained |
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values comparable with experimental values, and observed significant |
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conductance enhancement with the presence of capping agents. Computed |
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power spectra indicate the acoustic impedance mismatch between metal |
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and liquid phase is greatly reduced by the capping agents and thus |
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leads to higher interfacial thermal transfer efficiency. |
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\end{abstract} |
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\newpage |
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%\narrowtext |
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%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
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% BODY OF TEXT |
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%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
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\section{Introduction} |
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[BACKGROUND FOR INTERFACIAL THERMAL CONDUCTANCE PROBLEM] |
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Interfacial thermal conductance is extensively studied both |
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experimentally and computationally, and systems with interfaces |
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present are generally heterogeneous. Although interfaces are commonly |
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barriers to heat transfer, it has been |
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reported\cite{doi:10.1021/la904855s} that under specific circustances, |
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e.g. with certain capping agents present on the surface, interfacial |
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conductance can be significantly enhanced. However, heat conductance |
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of molecular and nano-scale interfaces will be affected by the |
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chemical details of the surface and is challenging to |
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experimentalist. The lower thermal flux through interfaces is even |
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more difficult to measure with EMD and forward NEMD simulation |
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methods. Therefore, developing good simulation methods will be |
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desirable in order to investigate thermal transport across interfaces. |
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Recently, we have developed the Non-Isotropic Velocity Scaling (NIVS) |
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algorithm for RNEMD simulations\cite{kuang:164101}. This algorithm |
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retains the desirable features of RNEMD (conservation of linear |
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momentum and total energy, compatibility with periodic boundary |
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conditions) while establishing true thermal distributions in each of |
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the two slabs. Furthermore, it allows more effective thermal exchange |
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between particles of different identities, and thus enables extensive |
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study of interfacial conductance. |
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\section{Methodology} |
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\subsection{Algorithm} |
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[BACKGROUND FOR MD METHODS] |
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There have been many algorithms for computing thermal conductivity |
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using molecular dynamics simulations. However, interfacial conductance |
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is at least an order of magnitude smaller. This would make the |
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calculation even more difficult for those slowly-converging |
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equilibrium methods. Imposed-flux non-equilibrium |
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methods\cite{MullerPlathe:1997xw} have the flux set {\it a priori} and |
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the response of temperature or momentum gradients are easier to |
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measure than the flux, if unknown, and thus, is a preferable way to |
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the forward NEMD methods. Although the momentum swapping approach for |
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flux-imposing can be used for exchanging energy between particles of |
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different identity, the kinetic energy transfer efficiency is affected |
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by the mass difference between the particles, which limits its |
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application on heterogeneous interfacial systems. |
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The non-isotropic velocity scaling (NIVS)\cite{kuang:164101} approach in |
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non-equilibrium MD simulations is able to impose relatively large |
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kinetic energy flux without obvious perturbation to the velocity |
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distribution of the simulated systems. Furthermore, this approach has |
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the advantage in heterogeneous interfaces in that kinetic energy flux |
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can be applied between regions of particles of arbitary identity, and |
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the flux quantity is not restricted by particle mass difference. |
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The NIVS algorithm scales the velocity vectors in two separate regions |
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of a simulation system with respective diagonal scaling matricies. To |
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determine these scaling factors in the matricies, a set of equations |
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including linear momentum conservation and kinetic energy conservation |
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constraints and target momentum/energy flux satisfaction is |
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solved. With the scaling operation applied to the system in a set |
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frequency, corresponding momentum/temperature gradients can be built, |
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which can be used for computing transportation properties and other |
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applications related to momentum/temperature gradients. The NIVS |
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algorithm conserves momenta and energy and does not depend on an |
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external thermostat. |
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\subsection{Defining Interfacial Thermal Conductivity $G$} |
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For interfaces with a relatively low interfacial conductance, the bulk |
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regions on either side of an interface rapidly come to a state in |
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which the two phases have relatively homogeneous (but distinct) |
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temperatures. The interfacial thermal conductivity $G$ can therefore |
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be approximated as: |
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\begin{equation} |
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G = \frac{E_{total}}{2 t L_x L_y \left( \langle T_\mathrm{hot}\rangle - |
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\langle T_\mathrm{cold}\rangle \right)} |
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\label{lowG} |
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\end{equation} |
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where ${E_{total}}$ is the imposed non-physical kinetic energy |
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transfer and ${\langle T_\mathrm{hot}\rangle}$ and ${\langle |
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T_\mathrm{cold}\rangle}$ are the average observed temperature of the |
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two separated phases. |
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When the interfacial conductance is {\it not} small, two ways can be |
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used to define $G$. |
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One way is to assume the temperature is discretely different on two |
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sides of the interface, $G$ can be calculated with the thermal flux |
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applied $J$ and the maximum temperature difference measured along the |
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thermal gradient max($\Delta T$), which occurs at the interface, as: |
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\begin{equation} |
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G=\frac{J}{\Delta T} |
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\label{discreteG} |
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\end{equation} |
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The other approach is to assume a continuous temperature profile along |
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the thermal gradient axis (e.g. $z$) and define $G$ at the point where |
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the magnitude of thermal conductivity $\lambda$ change reach its |
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maximum, given that $\lambda$ is well-defined throughout the space: |
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\begin{equation} |
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G^\prime = \Big|\frac{\partial\lambda}{\partial z}\Big| |
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= \Big|\frac{\partial}{\partial z}\left(-J_z\Big/ |
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\left(\frac{\partial T}{\partial z}\right)\right)\Big| |
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= |J_z|\Big|\frac{\partial^2 T}{\partial z^2}\Big| |
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\Big/\left(\frac{\partial T}{\partial z}\right)^2 |
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\label{derivativeG} |
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\end{equation} |
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With the temperature profile obtained from simulations, one is able to |
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approximate the first and second derivatives of $T$ with finite |
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difference method and thus calculate $G^\prime$. |
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In what follows, both definitions are used for calculation and comparison. |
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[IMPOSE G DEFINITION INTO OUR SYSTEMS] |
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To facilitate the use of the above definitions in calculating $G$ and |
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$G^\prime$, we have a metal slab with its (111) surfaces perpendicular |
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to the $z$-axis of our simulation cells. With or withour capping |
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agents on the surfaces, the metal slab is solvated with organic |
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solvents, as illustrated in Figure \ref{demoPic}. |
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\begin{figure} |
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\includegraphics[width=\linewidth]{demoPic} |
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\caption{A sample showing how a metal slab has its (111) surface |
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covered by capping agent molecules and solvated by hexane.} |
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\label{demoPic} |
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\end{figure} |
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With a simulation cell setup following the above manner, one is able |
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to equilibrate the system and impose an unphysical thermal flux |
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between the liquid and the metal phase with the NIVS algorithm. Under |
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a stablized thermal gradient induced by periodically applying the |
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unphysical flux, one is able to obtain a temperature profile and the |
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physical thermal flux corresponding to it, which equals to the |
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unphysical flux applied by NIVS. These data enables the evaluation of |
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the interfacial thermal conductance of a surface. Figure \ref{gradT} |
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is an example how those stablized thermal gradient can be used to |
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obtain the 1st and 2nd derivatives of the temperature profile. |
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\begin{figure} |
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\includegraphics[width=\linewidth]{gradT} |
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\caption{The 1st and 2nd derivatives of temperature profile can be |
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obtained with finite difference approximation.} |
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\label{gradT} |
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\end{figure} |
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\section{Computational Details} |
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\subsection{System Geometry} |
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In our simulations, Au is used to construct a metal slab with bare |
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(111) surface perpendicular to the $z$-axis. Different slab thickness |
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(layer numbers of Au) are simulated. This metal slab is first |
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equilibrated under normal pressure (1 atm) and a desired |
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temperature. After equilibration, butanethiol is used as the capping |
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agent molecule to cover the bare Au (111) surfaces evenly. The sulfur |
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atoms in the butanethiol molecules would occupy the three-fold sites |
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of the surfaces, and the maximal butanethiol capacity on Au surface is |
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$1/3$ of the total number of surface Au atoms[CITATION]. A series of |
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different coverage surfaces is investigated in order to study the |
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relation between coverage and conductance. |
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[COVERAGE DISCRIPTION] However, since the interactions between surface |
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Au and butanethiol is non-bonded, the capping agent molecules are |
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allowed to migrate to an empty neighbor three-fold site during a |
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simulation. Therefore, the initial configuration would not severely |
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affect the sampling of a variety of configurations of the same |
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coverage, and the final conductance measurement would be an average |
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effect of these configurations explored in the simulations. [MAY NEED FIGURES] |
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After the modified Au-butanethiol surface systems are equilibrated |
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under canonical ensemble, Packmol\cite{packmol} is used to pack |
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organic solvent molecules in the previously vacuum part of the |
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simulation cells, which guarantees that short range repulsive |
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interactions do not disrupt the simulations. Two solvents are |
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investigated, one which has little vibrational overlap with the |
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alkanethiol and plane-like shape (toluene), and one which has similar |
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vibrational frequencies and chain-like shape ({\it n}-hexane). The |
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initial configurations generated by Packmol are further equilibrated |
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with the $x$ and $y$ dimensions fixed, only allowing length scale |
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change in $z$ dimension. This is to ensure that the equilibration of |
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liquid phase does not affect the metal crystal structure in $x$ and |
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$y$ dimensions. Further equilibration are run under NVT and then NVE ensembles. |
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After the systems reach equilibrium, NIVS is implemented to impose a |
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periodic unphysical thermal flux between the metal and the liquid |
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phase. Most of our simulations have this flux from the metal to the |
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liquid so that the liquid has a higher temperature and would not |
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freeze due to excessively low temperature. This induced temperature |
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gradient is stablized and the simulation cell is devided evenly into |
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N slabs along the $z$-axis and the temperatures of each slab are |
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recorded. When the slab width $d$ of each slab is the same, the |
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derivatives of $T$ with respect to slab number $n$ can be directly |
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used for $G^\prime$ calculations: |
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\begin{equation} |
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G^\prime = |J_z|\Big|\frac{\partial^2 T}{\partial z^2}\Big| |
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\Big/\left(\frac{\partial T}{\partial z}\right)^2 |
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= |J_z|\Big|\frac{1}{d^2}\frac{\partial^2 T}{\partial n^2}\Big| |
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\Big/\left(\frac{1}{d}\frac{\partial T}{\partial n}\right)^2 |
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= |J_z|\Big|\frac{\partial^2 T}{\partial n^2}\Big| |
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\Big/\left(\frac{\partial T}{\partial n}\right)^2 |
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\label{derivativeG2} |
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\end{equation} |
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\subsection{Force Field Parameters} |
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The Au-Au interactions in metal lattice slab is described by the |
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quantum Sutton-Chen (QSC) formulation.\cite{PhysRevB.59.3527} The QSC |
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potentials include zero-point quantum corrections and are |
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reparametrized for accurate surface energies compared to the |
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Sutton-Chen potentials\cite{Chen90}. |
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Straight chain {\it n}-hexane and aromatic toluene are respectively |
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used as solvents. For hexane, both United-Atom\cite{TraPPE-UA.alkanes} |
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and All-Atom\cite{OPLSAA} force fields are used for comparison; for |
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toluene, United-Atom\cite{TraPPE-UA.alkylbenzenes} force fields are |
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used with rigid body constraints applied. (maybe needs more details |
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about rigid body) |
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Buatnethiol molecules are used as capping agent for some of our |
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simulations. United-Atom\cite{TraPPE-UA.thiols} and All-Atom models |
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are respectively used corresponding to the force field type of |
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solvent. |
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To describe the interactions between metal Au and non-metal capping |
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agent and solvent, we refer to Vlugt\cite{vlugt:cpc2007154} and derive |
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other interactions which are not parametrized in their work. (can add |
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hautman and klein's paper here and more discussion; need to put |
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aromatic-metal interaction approximation here) |
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[TABULATED FORCE FIELD PARAMETERS NEEDED] |
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\section{Results} |
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\subsection{Toluene Solvent} |
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The results (Table \ref{AuThiolToluene}) show a |
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significant conductance enhancement compared to the gold/water |
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interface without capping agent and agree with available experimental |
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data. This indicates that the metal-metal potential, though not |
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predicting an accurate bulk metal thermal conductivity, does not |
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greatly interfere with the simulation of the thermal conductance |
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behavior across a non-metal interface. The solvent model is not |
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particularly volatile, so the simulation cell does not expand |
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significantly under higher temperature. We did not observe a |
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significant conductance decrease when the temperature was increased to |
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300K. The results show that the two definitions used for $G$ yield |
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comparable values, though $G^\prime$ tends to be smaller. |
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\begin{table*} |
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\begin{minipage}{\linewidth} |
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\begin{center} |
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\caption{Computed interfacial thermal conductivity ($G$ and |
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$G^\prime$) values for the Au/butanethiol/toluene interface at |
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different temperatures using a range of energy fluxes.} |
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\begin{tabular}{cccc} |
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\hline\hline |
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$\langle T\rangle$ & $J_z$ & $G$ & $G^\prime$ \\ |
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(K) & (GW/m$^2$) & \multicolumn{2}{c}{(MW/m$^2$/K)} \\ |
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\hline |
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200 & 1.86 & 180 & 135 \\ |
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& 2.15 & 204 & 113 \\ |
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& 3.93 & 175 & 114 \\ |
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300 & 1.91 & 143 & 125 \\ |
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& 4.19 & 134 & 113 \\ |
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\hline\hline |
| 333 |
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\end{tabular} |
| 334 |
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\label{AuThiolToluene} |
| 335 |
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\end{center} |
| 336 |
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\end{minipage} |
| 337 |
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\end{table*} |
| 338 |
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|
| 339 |
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\subsection{Hexane Solvent} |
| 340 |
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|
| 341 |
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Using the united-atom model, different coverages of capping agent, |
| 342 |
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temperatures of simulations and numbers of solvent molecules were all |
| 343 |
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investigated and Table \ref{AuThiolHexaneUA} shows the results of |
| 344 |
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these computations. The number of hexane molecules in our simulations |
| 345 |
|
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does not affect the calculations significantly. However, a very long |
| 346 |
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length scale for the thermal gradient axis ($z$) may cause excessively |
| 347 |
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hot or cold temperatures in the middle of the solvent region and lead |
| 348 |
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to undesired phenomena such as solvent boiling or freezing, while too |
| 349 |
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few solvent molecules would change the normal behavior of the liquid |
| 350 |
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phase. Our $N_{hexane}$ values were chosen to ensure that these |
| 351 |
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extreme cases did not happen to our simulations. |
| 352 |
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|
| 353 |
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Table \ref{AuThiolHexaneUA} enables direct comparison between |
| 354 |
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different coverages of capping agent, when other system parameters are |
| 355 |
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held constant. With high coverage of butanethiol on the gold surface, |
| 356 |
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the interfacial thermal conductance is enhanced |
| 357 |
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significantly. Interestingly, a slightly lower butanethiol coverage |
| 358 |
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leads to a moderately higher conductivity. This is probably due to |
| 359 |
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more solvent/capping agent contact when butanethiol molecules are |
| 360 |
|
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not densely packed, which enhances the interactions between the two |
| 361 |
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phases and lowers the thermal transfer barrier of this interface. |
| 362 |
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% [COMPARE TO AU/WATER IN PAPER] |
| 363 |
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|
| 364 |
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It is also noted that the overall simulation temperature is another |
| 365 |
|
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factor that affects the interfacial thermal conductance. One |
| 366 |
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possibility of this effect may be rooted in the decrease in density of |
| 367 |
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the liquid phase. We observed that when the average temperature |
| 368 |
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|
increases from 200K to 250K, the bulk hexane density becomes lower |
| 369 |
|
|
than experimental value, as the system is equilibrated under NPT |
| 370 |
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ensemble. This leads to lower contact between solvent and capping |
| 371 |
|
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agent, and thus lower conductivity. |
| 372 |
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|
| 373 |
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Conductivity values are more difficult to obtain under higher |
| 374 |
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temperatures. This is because the Au surface tends to undergo |
| 375 |
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reconstructions in relatively high temperatures. Surface Au atoms can |
| 376 |
|
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migrate outward to reach higher Au-S contact; and capping agent |
| 377 |
|
|
molecules can be embedded into the surface Au layer due to the same |
| 378 |
|
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driving force. This phenomenon agrees with experimental |
| 379 |
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|
results\cite{doi:10.1021/j100035a033,doi:10.1021/la026493y}. A surface |
| 380 |
|
|
fully covered in capping agent is more susceptible to reconstruction, |
| 381 |
|
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possibly because fully coverage prevents other means of capping agent |
| 382 |
|
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relaxation, such as migration to an empty neighbor three-fold site. |
| 383 |
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|
| 384 |
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%MAY ADD MORE DATA TO TABLE |
| 385 |
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\begin{table*} |
| 386 |
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\begin{minipage}{\linewidth} |
| 387 |
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\begin{center} |
| 388 |
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\caption{Computed interfacial thermal conductivity ($G$ and |
| 389 |
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|
$G^\prime$) values for the Au/butanethiol/hexane interface |
| 390 |
|
|
with united-atom model and different capping agent coverage |
| 391 |
|
|
and solvent molecule numbers at different temperatures using a |
| 392 |
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|
range of energy fluxes.} |
| 393 |
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|
| 394 |
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\begin{tabular}{cccccc} |
| 395 |
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\hline\hline |
| 396 |
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|
Thiol & $\langle T\rangle$ & & $J_z$ & $G$ & $G^\prime$ \\ |
| 397 |
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coverage (\%) & (K) & $N_{hexane}$ & (GW/m$^2$) & |
| 398 |
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\multicolumn{2}{c}{(MW/m$^2$/K)} \\ |
| 399 |
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|
\hline |
| 400 |
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|
0.0 & 200 & 200 & 0.96 & 43.3 & 42.7 \\ |
| 401 |
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& & & 1.91 & 45.7 & 42.9 \\ |
| 402 |
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|
& & 166 & 0.96 & 43.1 & 53.4 \\ |
| 403 |
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|
88.9 & 200 & 166 & 1.94 & 172 & 108 \\ |
| 404 |
|
|
100.0 & 250 & 200 & 0.96 & 81.8 & 67.0 \\ |
| 405 |
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& & 166 & 0.98 & 79.0 & 62.9 \\ |
| 406 |
|
|
& & & 1.44 & 76.2 & 64.8 \\ |
| 407 |
|
|
& 200 & 200 & 1.92 & 129 & 87.3 \\ |
| 408 |
|
|
& & & 1.93 & 131 & 77.5 \\ |
| 409 |
|
|
& & 166 & 0.97 & 115 & 69.3 \\ |
| 410 |
|
|
& & & 1.94 & 125 & 87.1 \\ |
| 411 |
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|
\hline\hline |
| 412 |
|
|
\end{tabular} |
| 413 |
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\label{AuThiolHexaneUA} |
| 414 |
|
|
\end{center} |
| 415 |
|
|
\end{minipage} |
| 416 |
|
|
\end{table*} |
| 417 |
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|
| 418 |
|
|
For the all-atom model, the liquid hexane phase was not stable under NPT |
| 419 |
|
|
conditions. Therefore, the simulation length scale parameters are |
| 420 |
|
|
adopted from previous equilibration results of the united-atom model |
| 421 |
|
|
at 200K. Table \ref{AuThiolHexaneAA} shows the results of these |
| 422 |
|
|
simulations. The conductivity values calculated with full capping |
| 423 |
|
|
agent coverage are substantially larger than observed in the |
| 424 |
|
|
united-atom model, and is even higher than predicted by |
| 425 |
|
|
experiments. It is possible that our parameters for metal-non-metal |
| 426 |
|
|
particle interactions lead to an overestimate of the interfacial |
| 427 |
|
|
thermal conductivity, although the active C-H vibrations in the |
| 428 |
|
|
all-atom model (which should not be appreciably populated at normal |
| 429 |
|
|
temperatures) could also account for this high conductivity. The major |
| 430 |
|
|
thermal transfer barrier of Au/butanethiol/hexane interface is between |
| 431 |
|
|
the liquid phase and the capping agent, so extra degrees of freedom |
| 432 |
|
|
such as the C-H vibrations could enhance heat exchange between these |
| 433 |
|
|
two phases and result in a much higher conductivity. |
| 434 |
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|
|
| 435 |
|
|
\begin{table*} |
| 436 |
|
|
\begin{minipage}{\linewidth} |
| 437 |
|
|
\begin{center} |
| 438 |
|
|
|
| 439 |
|
|
\caption{Computed interfacial thermal conductivity ($G$ and |
| 440 |
|
|
$G^\prime$) values for the Au/butanethiol/hexane interface |
| 441 |
|
|
with all-atom model and different capping agent coverage at |
| 442 |
|
|
200K using a range of energy fluxes.} |
| 443 |
|
|
|
| 444 |
|
|
\begin{tabular}{cccc} |
| 445 |
|
|
\hline\hline |
| 446 |
|
|
Thiol & $J_z$ & $G$ & $G^\prime$ \\ |
| 447 |
|
|
coverage (\%) & (GW/m$^2$) & \multicolumn{2}{c}{(MW/m$^2$/K)} \\ |
| 448 |
|
|
\hline |
| 449 |
|
|
0.0 & 0.95 & 28.5 & 27.2 \\ |
| 450 |
|
|
& 1.88 & 30.3 & 28.9 \\ |
| 451 |
|
|
100.0 & 2.87 & 551 & 294 \\ |
| 452 |
|
|
& 3.81 & 494 & 193 \\ |
| 453 |
|
|
\hline\hline |
| 454 |
|
|
\end{tabular} |
| 455 |
|
|
\label{AuThiolHexaneAA} |
| 456 |
|
|
\end{center} |
| 457 |
|
|
\end{minipage} |
| 458 |
|
|
\end{table*} |
| 459 |
|
|
|
| 460 |
|
|
%subsubsection{Vibrational spectrum study on conductance mechanism} |
| 461 |
|
|
To investigate the mechanism of this interfacial thermal conductance, |
| 462 |
|
|
the vibrational spectra of various gold systems were obtained and are |
| 463 |
|
|
shown as in the upper panel of Fig. \ref{vibration}. To obtain these |
| 464 |
|
|
spectra, one first runs a simulation in the NVE ensemble and collects |
| 465 |
|
|
snapshots of configurations; these configurations are used to compute |
| 466 |
|
|
the velocity auto-correlation functions, which is used to construct a |
| 467 |
|
|
power spectrum via a Fourier transform. The gold surfaces covered by |
| 468 |
|
|
butanethiol molecules exhibit an additional peak observed at a |
| 469 |
|
|
frequency of $\sim$170cm$^{-1}$, which is attributed to the vibration |
| 470 |
|
|
of the S-Au bond. This vibration enables efficient thermal transport |
| 471 |
|
|
from surface Au atoms to the capping agents. Simultaneously, as shown |
| 472 |
|
|
in the lower panel of Fig. \ref{vibration}, the large overlap of the |
| 473 |
|
|
vibration spectra of butanethiol and hexane in the all-atom model, |
| 474 |
|
|
including the C-H vibration, also suggests high thermal exchange |
| 475 |
|
|
efficiency. The combination of these two effects produces the drastic |
| 476 |
|
|
interfacial thermal conductance enhancement in the all-atom model. |
| 477 |
|
|
|
| 478 |
|
|
\begin{figure} |
| 479 |
|
|
\includegraphics[width=\linewidth]{vibration} |
| 480 |
|
|
\caption{Vibrational spectra obtained for gold in different |
| 481 |
|
|
environments (upper panel) and for Au/thiol/hexane simulation in |
| 482 |
|
|
all-atom model (lower panel).} |
| 483 |
|
|
\label{vibration} |
| 484 |
|
|
\end{figure} |
| 485 |
|
|
% 600dpi, letter size. too large? |
| 486 |
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|
|
| 487 |
|
|
|
| 488 |
gezelter |
3717 |
\section{Acknowledgments} |
| 489 |
|
|
Support for this project was provided by the National Science |
| 490 |
|
|
Foundation under grant CHE-0848243. Computational time was provided by |
| 491 |
|
|
the Center for Research Computing (CRC) at the University of Notre |
| 492 |
|
|
Dame. \newpage |
| 493 |
|
|
|
| 494 |
|
|
\bibliography{interfacial} |
| 495 |
|
|
|
| 496 |
|
|
\end{doublespace} |
| 497 |
|
|
\end{document} |
| 498 |
|
|
|