23 |
|
\setlength{\belowcaptionskip}{30 pt} |
24 |
|
|
25 |
|
%\renewcommand\citemid{\ } % no comma in optional reference note |
26 |
< |
\bibpunct{[}{]}{,}{s}{}{;} |
27 |
< |
\bibliographystyle{aip} |
26 |
> |
\bibpunct{[}{]}{,}{n}{}{;} |
27 |
> |
\bibliographystyle{achemso} |
28 |
|
|
29 |
|
\begin{document} |
30 |
|
|
222 |
|
|
223 |
|
To compare the above definitions ($G$ and $G^\prime$), we have modeled |
224 |
|
a metal slab with its (111) surfaces perpendicular to the $z$-axis of |
225 |
< |
our simulation cells. Both with and withour capping agents on the |
225 |
> |
our simulation cells. Both with and without capping agents on the |
226 |
|
surfaces, the metal slab is solvated with simple organic solvents, as |
227 |
|
illustrated in Figure \ref{demoPic}. |
228 |
|
|
229 |
|
\begin{figure} |
230 |
< |
\includegraphics[width=\linewidth]{demoPic} |
231 |
< |
\caption{A sample showing how a metal slab has its (111) surface |
232 |
< |
covered by capping agent molecules and solvated by hexane.} |
230 |
> |
\includegraphics[width=\linewidth]{method} |
231 |
> |
\caption{Interfacial conductance can be calculated by applying an |
232 |
> |
(unphysical) kinetic energy flux between two slabs, one located |
233 |
> |
within the metal and another on the edge of the periodic box. The |
234 |
> |
system responds by forming a thermal response or a gradient. In |
235 |
> |
bulk liquids, this gradient typically has a single slope, but in |
236 |
> |
interfacial systems, there are distinct thermal conductivity |
237 |
> |
domains. The interfacial conductance, $G$ is found by measuring the |
238 |
> |
temperature gap at the Gibbs dividing surface, or by using second |
239 |
> |
derivatives of the thermal profile.} |
240 |
|
\label{demoPic} |
241 |
|
\end{figure} |
242 |
|
|
325 |
|
\end{equation} |
326 |
|
|
327 |
|
\subsection{Force Field Parameters} |
328 |
< |
Our simulations include various components. Therefore, force field |
329 |
< |
parameter descriptions are needed for interactions both between the |
330 |
< |
same type of particles and between particles of different species. |
328 |
> |
Our simulations include various components. Figure \ref{demoMol} |
329 |
> |
demonstrates the sites defined for both United-Atom and All-Atom |
330 |
> |
models of the organic solvent and capping agent molecules in our |
331 |
> |
simulations. Force field parameter descriptions are needed for |
332 |
> |
interactions both between the same type of particles and between |
333 |
> |
particles of different species. |
334 |
|
|
335 |
+ |
\begin{figure} |
336 |
+ |
\includegraphics[width=\linewidth]{structures} |
337 |
+ |
\caption{Structures of the capping agent and solvents utilized in |
338 |
+ |
these simulations. The chemically-distinct sites (a-e) are expanded |
339 |
+ |
in terms of constituent atoms for both United Atom (UA) and All Atom |
340 |
+ |
(AA) force fields. Most parameters are from |
341 |
+ |
Refs. \protect\cite{TraPPE-UA.alkanes,TraPPE-UA.alkylbenzenes} (UA) and |
342 |
+ |
\protect\cite{OPLSAA} (AA). Cross-interactions with the Au atoms are given |
343 |
+ |
in Table \ref{MnM}.} |
344 |
+ |
\label{demoMol} |
345 |
+ |
\end{figure} |
346 |
+ |
|
347 |
|
The Au-Au interactions in metal lattice slab is described by the |
348 |
|
quantum Sutton-Chen (QSC) formulation\cite{PhysRevB.59.3527}. The QSC |
349 |
|
potentials include zero-point quantum corrections and are |
350 |
|
reparametrized for accurate surface energies compared to the |
351 |
|
Sutton-Chen potentials\cite{Chen90}. |
330 |
– |
|
331 |
– |
Figure \ref{demoMol} demonstrates how we name our pseudo-atoms of the |
332 |
– |
organic solvent molecules in our simulations. |
333 |
– |
|
334 |
– |
\begin{figure} |
335 |
– |
\includegraphics[width=\linewidth]{demoMol} |
336 |
– |
\caption{Denomination of atoms or pseudo-atoms in our simulations: a) |
337 |
– |
UA-hexane; b) AA-hexane; c) UA-toluene; d) AA-toluene.} |
338 |
– |
\label{demoMol} |
339 |
– |
\end{figure} |
352 |
|
|
353 |
|
For both solvent molecules, straight chain {\it n}-hexane and aromatic |
354 |
|
toluene, United-Atom (UA) and All-Atom (AA) models are used |
355 |
|
respectively. The TraPPE-UA |
356 |
|
parameters\cite{TraPPE-UA.alkanes,TraPPE-UA.alkylbenzenes} are used |
357 |
< |
for our UA solvent molecules. In these models, pseudo-atoms are |
358 |
< |
located at the carbon centers for alkyl groups. By eliminating |
359 |
< |
explicit hydrogen atoms, these models are simple and computationally |
360 |
< |
efficient, while maintains good accuracy. However, the TraPPE-UA for |
361 |
< |
alkanes is known to predict a lower boiling point than experimental |
350 |
< |
values. Considering that after an unphysical thermal flux is applied |
351 |
< |
to a system, the temperature of ``hot'' area in the liquid phase would be |
352 |
< |
significantly higher than the average, to prevent over heating and |
353 |
< |
boiling of the liquid phase, the average temperature in our |
354 |
< |
simulations should be much lower than the liquid boiling point. [MORE DISCUSSION] |
355 |
< |
For UA-toluene model, rigid body constraints are applied, so that the |
356 |
< |
benzene ring and the methyl-CRar bond are kept rigid. This would save |
357 |
< |
computational time.[MORE DETAILS] |
357 |
> |
for our UA solvent molecules. In these models, sites are located at |
358 |
> |
the carbon centers for alkyl groups. Bonding interactions, including |
359 |
> |
bond stretches and bends and torsions, were used for intra-molecular |
360 |
> |
sites not separated by more than 3 bonds. Otherwise, for non-bonded |
361 |
> |
interactions, Lennard-Jones potentials are used. [MORE CITATION?] |
362 |
|
|
363 |
+ |
By eliminating explicit hydrogen atoms, these models are simple and |
364 |
+ |
computationally efficient, while maintains good accuracy. However, the |
365 |
+ |
TraPPE-UA for alkanes is known to predict a lower boiling point than |
366 |
+ |
experimental values. Considering that after an unphysical thermal flux |
367 |
+ |
is applied to a system, the temperature of ``hot'' area in the liquid |
368 |
+ |
phase would be significantly higher than the average, to prevent over |
369 |
+ |
heating and boiling of the liquid phase, the average temperature in |
370 |
+ |
our simulations should be much lower than the liquid boiling point. |
371 |
+ |
|
372 |
+ |
For UA-toluene model, the non-bonded potentials between |
373 |
+ |
inter-molecular sites have a similar Lennard-Jones formulation. For |
374 |
+ |
intra-molecular interactions, considering the stiffness of the benzene |
375 |
+ |
ring, rigid body constraints are applied for further computational |
376 |
+ |
efficiency. All bonds in the benzene ring and between the ring and the |
377 |
+ |
methyl group remain rigid during the progress of simulations. |
378 |
+ |
|
379 |
|
Besides the TraPPE-UA models, AA models for both organic solvents are |
380 |
|
included in our studies as well. For hexane, the OPLS-AA\cite{OPLSAA} |
381 |
< |
force field is used. [MORE DETAILS] |
382 |
< |
For toluene, the United Force Field developed by Rapp\'{e} {\it et |
383 |
< |
al.}\cite{doi:10.1021/ja00051a040} is adopted.[MORE DETAILS] |
381 |
> |
force field is used. Additional explicit hydrogen sites were |
382 |
> |
included. Besides bonding and non-bonded site-site interactions, |
383 |
> |
partial charges and the electrostatic interactions were added to each |
384 |
> |
CT and HC site. For toluene, the United Force Field developed by |
385 |
> |
Rapp\'{e} {\it et al.}\cite{doi:10.1021/ja00051a040} is |
386 |
> |
adopted. Without the rigid body constraints, bonding interactions were |
387 |
> |
included. For the aromatic ring, improper torsions (inversions) were |
388 |
> |
added as an extra potential for maintaining the planar shape. |
389 |
> |
[MORE CITATIONS?] |
390 |
|
|
391 |
|
The capping agent in our simulations, the butanethiol molecules can |
392 |
|
either use UA or AA model. The TraPPE-UA force fields includes |
403 |
|
interactions between capping agent and solvent can be derived using |
404 |
|
Lorentz-Berthelot Mixing Rule: |
405 |
|
\begin{eqnarray} |
406 |
< |
\sigma_{IJ} & = & \frac{1}{2} \left(\sigma_{II} + \sigma_{JJ}\right) \\ |
407 |
< |
\epsilon_{IJ} & = & \sqrt{\epsilon_{II}\epsilon_{JJ}} |
406 |
> |
\sigma_{ij} & = & \frac{1}{2} \left(\sigma_{ii} + \sigma_{jj}\right) \\ |
407 |
> |
\epsilon_{ij} & = & \sqrt{\epsilon_{ii}\epsilon_{jj}} |
408 |
|
\end{eqnarray} |
409 |
|
|
410 |
|
To describe the interactions between metal Au and non-metal capping |
421 |
|
|
422 |
|
Besides, the potentials developed from {\it ab initio} calculations by |
423 |
|
Leng {\it et al.}\cite{doi:10.1021/jp034405s} are adopted for the |
424 |
< |
interactions between Au and aromatic C/H atoms in toluene.[MORE DETAILS] |
424 |
> |
interactions between Au and aromatic C/H atoms in toluene. A set of |
425 |
> |
pseudo Lennard-Jones parameters were provided for Au in their force |
426 |
> |
fields. By using the Mixing Rule, this can be used to derive pair-wise |
427 |
> |
potentials for non-bonded interactions between Au and non-metal sites. |
428 |
|
|
429 |
|
However, the Lennard-Jones parameters between Au and other types of |
430 |
< |
particles in our simulations are not yet well-established. For these |
431 |
< |
interactions, we attempt to derive their parameters using the Mixing |
432 |
< |
Rule. To do this, the ``Metal-non-Metal'' (MnM) interaction parameters |
433 |
< |
for Au is first extracted from the Au-CH$_x$ parameters by applying |
434 |
< |
the Mixing Rule reversely. Table \ref{MnM} summarizes these ``MnM'' |
430 |
> |
particles, such as All-Atom normal alkanes in our simulations are not |
431 |
> |
yet well-established. For these interactions, we attempt to derive |
432 |
> |
their parameters using the Mixing Rule. To do this, Au pseudo |
433 |
> |
Lennard-Jones parameters for ``Metal-non-Metal'' (MnM) interactions |
434 |
> |
were first extracted from the Au-CH$_x$ parameters by applying the |
435 |
> |
Mixing Rule reversely. Table \ref{MnM} summarizes these ``MnM'' |
436 |
|
parameters in our simulations. |
437 |
|
|
438 |
|
\begin{table*} |
439 |
|
\begin{minipage}{\linewidth} |
440 |
|
\begin{center} |
441 |
< |
\caption{Non-bonded interaction paramters for non-metal |
442 |
< |
particles and metal-non-metal interactions in our |
443 |
< |
simulations.} |
444 |
< |
|
415 |
< |
\begin{tabular}{cccccc} |
441 |
> |
\caption{Non-bonded interaction parameters (including cross |
442 |
> |
interactions with Au atoms) for both force fields used in this |
443 |
> |
work.} |
444 |
> |
\begin{tabular}{lllllll} |
445 |
|
\hline\hline |
446 |
< |
Non-metal atom $I$ & $\sigma_{II}$ & $\epsilon_{II}$ & $q_I$ & |
447 |
< |
$\sigma_{AuI}$ & $\epsilon_{AuI}$ \\ |
448 |
< |
(or pseudo-atom) & \AA & kcal/mol & & \AA & kcal/mol \\ |
446 |
> |
& Site & $\sigma_{ii}$ & $\epsilon_{ii}$ & $q_i$ & |
447 |
> |
$\sigma_{Au-i}$ & $\epsilon_{Au-i}$ \\ |
448 |
> |
& & (\AA) & (kcal/mol) & ($e$) & (\AA) & (kcal/mol) \\ |
449 |
|
\hline |
450 |
< |
CH3 & 3.75 & 0.1947 & - & 3.54 & 0.2146 \\ |
451 |
< |
CH2 & 3.95 & 0.0914 & - & 3.54 & 0.1749 \\ |
452 |
< |
CHar & 3.695 & 0.1003 & - & 3.4625 & 0.1680 \\ |
453 |
< |
CRar & 3.88 & 0.04173 & - & 3.555 & 0.1604 \\ |
454 |
< |
S & 4.45 & 0.25 & - & 2.40 & 8.465 \\ |
455 |
< |
CT3 & 3.50 & 0.066 & -0.18 & 3.365 & 0.1373 \\ |
456 |
< |
CT2 & 3.50 & 0.066 & -0.12 & 3.365 & 0.1373 \\ |
457 |
< |
CTT & 3.50 & 0.066 & -0.065 & 3.365 & 0.1373 \\ |
458 |
< |
HC & 2.50 & 0.030 & 0.06 & 2.865 & 0.09256 \\ |
459 |
< |
CA & 3.55 & 0.070 & -0.115 & 3.173 & 0.0640 \\ |
460 |
< |
HA & 2.42 & 0.030 & 0.115 & 2.746 & 0.0414 \\ |
450 |
> |
United Atom (UA) |
451 |
> |
&CH3 & 3.75 & 0.1947 & - & 3.54 & 0.2146 \\ |
452 |
> |
&CH2 & 3.95 & 0.0914 & - & 3.54 & 0.1749 \\ |
453 |
> |
&CHar & 3.695 & 0.1003 & - & 3.4625 & 0.1680 \\ |
454 |
> |
&CRar & 3.88 & 0.04173 & - & 3.555 & 0.1604 \\ |
455 |
> |
\hline |
456 |
> |
All Atom (AA) |
457 |
> |
&CT3 & 3.50 & 0.066 & -0.18 & 3.365 & 0.1373 \\ |
458 |
> |
&CT2 & 3.50 & 0.066 & -0.12 & 3.365 & 0.1373 \\ |
459 |
> |
&CTT & 3.50 & 0.066 & -0.065 & 3.365 & 0.1373 \\ |
460 |
> |
&HC & 2.50 & 0.030 & 0.06 & 2.865 & 0.09256 \\ |
461 |
> |
&CA & 3.55 & 0.070 & -0.115 & 3.173 & 0.0640 \\ |
462 |
> |
&HA & 2.42 & 0.030 & 0.115 & 2.746 & 0.0414 \\ |
463 |
> |
\hline |
464 |
> |
Both UA and AA |
465 |
> |
& S & 4.45 & 0.25 & - & 2.40 & 8.465 \\ |
466 |
|
\hline\hline |
467 |
|
\end{tabular} |
468 |
|
\label{MnM} |
483 |
|
results. |
484 |
|
|
485 |
|
In some of our simulations, we allowed $L_x$ and $L_y$ to change |
486 |
< |
during equilibrating the liquid phase. Due to the stiffness of the Au |
487 |
< |
slab, $L_x$ and $L_y$ would not change noticeably after |
488 |
< |
equilibration. Although $L_z$ could fluctuate $\sim$1\% after a system |
489 |
< |
is fully equilibrated in the NPT ensemble, this fluctuation, as well |
490 |
< |
as those comparably smaller to $L_x$ and $L_y$, would not be magnified |
491 |
< |
on the calculated $G$'s, as shown in Table \ref{AuThiolHexaneUA}. This |
492 |
< |
insensivity to $L_i$ fluctuations allows reliable measurement of $G$'s |
493 |
< |
without the necessity of extremely cautious equilibration process. |
486 |
> |
during equilibrating the liquid phase. Due to the stiffness of the |
487 |
> |
crystalline Au structure, $L_x$ and $L_y$ would not change noticeably |
488 |
> |
after equilibration. Although $L_z$ could fluctuate $\sim$1\% after a |
489 |
> |
system is fully equilibrated in the NPT ensemble, this fluctuation, as |
490 |
> |
well as those of $L_x$ and $L_y$ (which is significantly smaller), |
491 |
> |
would not be magnified on the calculated $G$'s, as shown in Table |
492 |
> |
\ref{AuThiolHexaneUA}. This insensivity to $L_i$ fluctuations allows |
493 |
> |
reliable measurement of $G$'s without the necessity of extremely |
494 |
> |
cautious equilibration process. |
495 |
|
|
496 |
|
As stated in our computational details, the spacing filled with |
497 |
|
solvent molecules can be chosen within a range. This allows some |
518 |
|
the thermal flux across the interface. For our simulations, we denote |
519 |
|
$J_z$ to be positive when the physical thermal flux is from the liquid |
520 |
|
to metal, and negative vice versa. The $G$'s measured under different |
521 |
< |
$J_z$ is listed in Table \ref{AuThiolHexaneUA} and [REF]. These |
522 |
< |
results do not suggest that $G$ is dependent on $J_z$ within this flux |
523 |
< |
range. The linear response of flux to thermal gradient simplifies our |
524 |
< |
investigations in that we can rely on $G$ measurement with only a |
525 |
< |
couple $J_z$'s and do not need to test a large series of fluxes. |
521 |
> |
$J_z$ is listed in Table \ref{AuThiolHexaneUA} and |
522 |
> |
\ref{AuThiolToluene}. These results do not suggest that $G$ is |
523 |
> |
dependent on $J_z$ within this flux range. The linear response of flux |
524 |
> |
to thermal gradient simplifies our investigations in that we can rely |
525 |
> |
on $G$ measurement with only a couple $J_z$'s and do not need to test |
526 |
> |
a large series of fluxes. |
527 |
|
|
492 |
– |
%ADD MORE TO TABLE |
528 |
|
\begin{table*} |
529 |
|
\begin{minipage}{\linewidth} |
530 |
|
\begin{center} |
540 |
|
(K) & & $L_x$ \& $L_y$? & (g/cm$^3$) & (GW/m$^2$) & |
541 |
|
\multicolumn{2}{c}{(MW/m$^2$/K)} \\ |
542 |
|
\hline |
543 |
< |
200 & 266 & No & 0.672 & -0.96 & 102() & 80.0() \\ |
544 |
< |
& 200 & Yes & 0.694 & 1.92 & 129() & 87.3() \\ |
545 |
< |
& & Yes & 0.672 & 1.93 & 131() & 77.5() \\ |
546 |
< |
|
547 |
< |
& 166 & Yes & 0.679 & 0.97 & 115() & 69.3() \\ |
548 |
< |
& & Yes & 0.679 & 1.94 & 125() & 87.1() \\ |
549 |
< |
|
550 |
< |
250 & 200 & No & 0.560 & 0.96 & 81.8() & 67.0() \\ |
551 |
< |
|
552 |
< |
& 166 & Yes & 0.570 & 0.98 & 79.0() & 62.9() \\ |
553 |
< |
|
554 |
< |
& & No & 0.569 & 1.44 & 76.2() & 64.8() \\ |
555 |
< |
|
543 |
> |
200 & 266 & No & 0.672 & -0.96 & 102() & 80.0() \\ |
544 |
> |
& 200 & Yes & 0.694 & 1.92 & 129(11) & 87.3(0.3) \\ |
545 |
> |
& & Yes & 0.672 & 1.93 & 131(16) & 78(13) \\ |
546 |
> |
& & No & 0.688 & 0.96 & 125() & 90.2() \\ |
547 |
> |
& & & & 1.91 & 139(10) & 101(10) \\ |
548 |
> |
& & & & 2.83 & 141(6) & 89.9(9.8) \\ |
549 |
> |
& 166 & Yes & 0.679 & 0.97 & 115(19) & 69(18) \\ |
550 |
> |
& & & & 1.94 & 125(9) & 87.1(0.2) \\ |
551 |
> |
& & No & 0.681 & 0.97 & 141(30) & 78(22) \\ |
552 |
> |
& & & & 1.92 & 138(4) & 98.9(9.5) \\ |
553 |
> |
\hline |
554 |
> |
250 & 200 & No & 0.560 & 0.96 & 75(10) & 61.8(7.3) \\ |
555 |
> |
& & & & -0.95 & 49.4(0.3) & 45.7(2.1) \\ |
556 |
> |
& 166 & Yes & 0.570 & 0.98 & 79.0(3.5) & 62.9(3.0) \\ |
557 |
> |
& & No & 0.569 & 0.97 & 80.3(0.6) & 67(11) \\ |
558 |
> |
& & & & 1.44 & 76.2(5.0) & 64.8(3.8) \\ |
559 |
> |
& & & & -0.95 & 56.4(2.5) & 54.4(1.1) \\ |
560 |
> |
& & & & -1.85 & 47.8(1.1) & 53.5(1.5) \\ |
561 |
|
\hline\hline |
562 |
|
\end{tabular} |
563 |
|
\label{AuThiolHexaneUA} |
573 |
|
temperature is higher than 250K. Additionally, the equilibrated liquid |
574 |
|
hexane density under 250K becomes lower than experimental value. This |
575 |
|
expanded liquid phase leads to lower contact between hexane and |
576 |
< |
butanethiol as well.[MAY NEED FIGURE] And this reduced contact would |
576 |
> |
butanethiol as well.[MAY NEED SLAB DENSITY FIGURE] |
577 |
> |
And this reduced contact would |
578 |
|
probably be accountable for a lower interfacial thermal conductance, |
579 |
|
as shown in Table \ref{AuThiolHexaneUA}. |
580 |
|
|
640 |
|
|
641 |
|
However, when the surface is not completely covered by butanethiols, |
642 |
|
the simulated system is more resistent to the reconstruction |
643 |
< |
above. Our Au-butanethiol/toluene system did not see this phenomena |
644 |
< |
even at $\langle T\rangle\sim$300K. The Au(111) surfaces have a 90\% |
645 |
< |
coverage of butanethiols and have empty three-fold sites. These empty |
646 |
< |
sites could help prevent surface reconstruction in that they provide |
647 |
< |
other means of capping agent relaxation. It is observed that |
643 |
> |
above. Our Au-butanethiol/toluene system had the Au(111) surfaces 90\% |
644 |
> |
covered by butanethiols, but did not see this above phenomena even at |
645 |
> |
$\langle T\rangle\sim$300K. The empty three-fold sites not occupied by |
646 |
> |
capping agents could help prevent surface reconstruction in that they |
647 |
> |
provide other means of capping agent relaxation. It is observed that |
648 |
|
butanethiols can migrate to their neighbor empty sites during a |
649 |
|
simulation. Therefore, we were able to obtain $G$'s for these |
650 |
|
interfaces even at a relatively high temperature without being |
655 |
|
thermal conductance, a series of different coverage Au-butanethiol |
656 |
|
surfaces is prepared and solvated with various organic |
657 |
|
molecules. These systems are then equilibrated and their interfacial |
658 |
< |
thermal conductivity are measured with our NIVS algorithm. Table |
659 |
< |
\ref{tlnUhxnUhxnD} lists these results for direct comparison between |
660 |
< |
different coverages of butanethiol. To study the isotope effect in |
661 |
< |
interfacial thermal conductance, deuterated UA-hexane is included as |
662 |
< |
well. |
658 |
> |
thermal conductivity are measured with our NIVS algorithm. Figure |
659 |
> |
\ref{coverage} demonstrates the trend of conductance change with |
660 |
> |
respect to different coverages of butanethiol. To study the isotope |
661 |
> |
effect in interfacial thermal conductance, deuterated UA-hexane is |
662 |
> |
included as well. |
663 |
|
|
664 |
|
It turned out that with partial covered butanethiol on the Au(111) |
665 |
< |
surface, the derivative definition for $G$ (Eq. \ref{derivativeG}) has |
666 |
< |
difficulty to apply, due to the difficulty in locating the maximum of |
667 |
< |
change of $\lambda$. Instead, the discrete definition |
668 |
< |
(Eq. \ref{discreteG}) is easier to apply, as max($\Delta T$) can still |
669 |
< |
be well-defined. Therefore, $G$'s (not $G^\prime$) are used for this |
670 |
< |
section. |
665 |
> |
surface, the derivative definition for $G^\prime$ |
666 |
> |
(Eq. \ref{derivativeG}) was difficult to apply, due to the difficulty |
667 |
> |
in locating the maximum of change of $\lambda$. Instead, the discrete |
668 |
> |
definition (Eq. \ref{discreteG}) is easier to apply, as the Gibbs |
669 |
> |
deviding surface can still be well-defined. Therefore, $G$ (not |
670 |
> |
$G^\prime$) was used for this section. |
671 |
|
|
672 |
< |
From Table \ref{tlnUhxnUhxnD}, one can see the significance of the |
672 |
> |
From Figure \ref{coverage}, one can see the significance of the |
673 |
|
presence of capping agents. Even when a fraction of the Au(111) |
674 |
|
surface sites are covered with butanethiols, the conductivity would |
675 |
|
see an enhancement by at least a factor of 3. This indicates the |
676 |
|
important role cappping agent is playing for thermal transport |
677 |
< |
phenomena on metal/organic solvent surfaces. |
677 |
> |
phenomena on metal / organic solvent surfaces. |
678 |
|
|
679 |
|
Interestingly, as one could observe from our results, the maximum |
680 |
|
conductance enhancement (largest $G$) happens while the surfaces are |
693 |
|
would not offset this effect. Eventually, when butanethiol coverage |
694 |
|
continues to decrease, solvent-capping agent contact actually |
695 |
|
decreases with the disappearing of butanethiol molecules. In this |
696 |
< |
case, $G$ decrease could not be offset but instead accelerated. |
696 |
> |
case, $G$ decrease could not be offset but instead accelerated. [NEED |
697 |
> |
SNAPSHOT SHOWING THE PHENOMENA] |
698 |
|
|
699 |
|
A comparison of the results obtained from differenet organic solvents |
700 |
|
can also provide useful information of the interfacial thermal |
704 |
|
studies, even though eliminating C-H vibration samplings, still have |
705 |
|
C-C vibrational frequencies different from each other. However, these |
706 |
|
differences in the infrared range do not seem to produce an observable |
707 |
< |
difference for the results of $G$. [MAY NEED FIGURE] |
707 |
> |
difference for the results of $G$. [MAY NEED SPECTRA FIGURE] |
708 |
|
|
709 |
|
Furthermore, results for rigid body toluene solvent, as well as other |
710 |
|
UA-hexane solvents, are reasonable within the general experimental |
713 |
|
such as Au-thiol/organic solvent. |
714 |
|
|
715 |
|
However, results for Au-butanethiol/toluene do not show an identical |
716 |
< |
trend with those for Au-butanethiol/hexane in that $G$'s remain at |
716 |
> |
trend with those for Au-butanethiol/hexane in that $G$ remains at |
717 |
|
approximately the same magnitue when butanethiol coverage differs from |
718 |
|
25\% to 75\%. This might be rooted in the molecule shape difference |
719 |
< |
for plane-like toluene and chain-like {\it n}-hexane. Due to this |
719 |
> |
for planar toluene and chain-like {\it n}-hexane. Due to this |
720 |
|
difference, toluene molecules have more difficulty in occupying |
721 |
|
relatively small gaps among capping agents when their coverage is not |
722 |
|
too low. Therefore, the solvent-capping agent contact may keep |
725 |
|
its effect to the process of interfacial thermal transport. Thus, one |
726 |
|
can see a plateau of $G$ vs. butanethiol coverage in our results. |
727 |
|
|
728 |
< |
[NEED ERROR ESTIMATE, CONVERT TO FIGURE] |
729 |
< |
\begin{table*} |
730 |
< |
\begin{minipage}{\linewidth} |
731 |
< |
\begin{center} |
732 |
< |
\caption{Computed interfacial thermal conductivity ($G$) values |
733 |
< |
for the Au-butanethiol/solvent interface with various UA |
734 |
< |
models and different capping agent coverages at $\langle |
735 |
< |
T\rangle\sim$200K using certain energy flux respectively.} |
694 |
< |
|
695 |
< |
\begin{tabular}{cccc} |
696 |
< |
\hline\hline |
697 |
< |
Thiol & \multicolumn{3}{c}{$G$(MW/m$^2$/K)} \\ |
698 |
< |
coverage (\%) & hexane & hexane(D) & toluene \\ |
699 |
< |
\hline |
700 |
< |
0.0 & 46.5() & 43.9() & 70.1() \\ |
701 |
< |
25.0 & 151() & 153() & 249() \\ |
702 |
< |
50.0 & 172() & 182() & 214() \\ |
703 |
< |
75.0 & 242() & 229() & 244() \\ |
704 |
< |
88.9 & 178() & - & - \\ |
705 |
< |
100.0 & 137() & 153() & 187() \\ |
706 |
< |
\hline\hline |
707 |
< |
\end{tabular} |
708 |
< |
\label{tlnUhxnUhxnD} |
709 |
< |
\end{center} |
710 |
< |
\end{minipage} |
711 |
< |
\end{table*} |
728 |
> |
\begin{figure} |
729 |
> |
\includegraphics[width=\linewidth]{coverage} |
730 |
> |
\caption{Comparison of interfacial thermal conductivity ($G$) values |
731 |
> |
for the Au-butanethiol/solvent interface with various UA models and |
732 |
> |
different capping agent coverages at $\langle T\rangle\sim$200K |
733 |
> |
using certain energy flux respectively.} |
734 |
> |
\label{coverage} |
735 |
> |
\end{figure} |
736 |
|
|
737 |
|
\subsection{Influence of Chosen Molecule Model on $G$} |
738 |
|
[MAY COMBINE W MECHANISM STUDY] |
745 |
|
the previous section. Table \ref{modelTest} summarizes the results of |
746 |
|
these studies. |
747 |
|
|
724 |
– |
[MORE DATA; ERROR ESTIMATE] |
748 |
|
\begin{table*} |
749 |
|
\begin{minipage}{\linewidth} |
750 |
|
\begin{center} |
752 |
|
\caption{Computed interfacial thermal conductivity ($G$ and |
753 |
|
$G^\prime$) values for interfaces using various models for |
754 |
|
solvent and capping agent (or without capping agent) at |
755 |
< |
$\langle T\rangle\sim$200K.} |
755 |
> |
$\langle T\rangle\sim$200K. (D stands for deuterated solvent |
756 |
> |
or capping agent molecules; ``Avg.'' denotes results that are |
757 |
> |
averages of simulations under different $J_z$'s. Error |
758 |
> |
estimates indicated in parenthesis.)} |
759 |
|
|
760 |
< |
\begin{tabular}{ccccc} |
760 |
> |
\begin{tabular}{llccc} |
761 |
|
\hline\hline |
762 |
|
Butanethiol model & Solvent & $J_z$ & $G$ & $G^\prime$ \\ |
763 |
|
(or bare surface) & model & (GW/m$^2$) & |
764 |
|
\multicolumn{2}{c}{(MW/m$^2$/K)} \\ |
765 |
|
\hline |
766 |
< |
UA & AA hexane & 1.94 & 135() & 129() \\ |
767 |
< |
& & 2.86 & 126() & 115() \\ |
768 |
< |
& AA toluene & 1.89 & 200() & 149() \\ |
769 |
< |
AA & UA hexane & 1.94 & 116() & 129() \\ |
770 |
< |
& AA hexane & 3.76 & 451() & 378() \\ |
771 |
< |
& & 4.71 & 432() & 334() \\ |
772 |
< |
& AA toluene & 3.79 & 487() & 290() \\ |
773 |
< |
AA(D) & UA hexane & 1.94 & 158() & 172() \\ |
774 |
< |
bare & AA hexane & 0.96 & 31.0() & 29.4() \\ |
766 |
> |
UA & UA hexane & Avg. & 131(9) & 87(10) \\ |
767 |
> |
& UA hexane(D) & 1.95 & 153(5) & 136(13) \\ |
768 |
> |
& AA hexane & Avg. & 131(6) & 122(10) \\ |
769 |
> |
& UA toluene & 1.96 & 187(16) & 151(11) \\ |
770 |
> |
& AA toluene & 1.89 & 200(36) & 149(53) \\ |
771 |
> |
\hline |
772 |
> |
AA & UA hexane & 1.94 & 116(9) & 129(8) \\ |
773 |
> |
& AA hexane & Avg. & 442(14) & 356(31) \\ |
774 |
> |
& AA hexane(D) & 1.93 & 222(12) & 234(54) \\ |
775 |
> |
& UA toluene & 1.98 & 125(25) & 97(60) \\ |
776 |
> |
& AA toluene & 3.79 & 487(56) & 290(42) \\ |
777 |
> |
\hline |
778 |
> |
AA(D) & UA hexane & 1.94 & 158(25) & 172(4) \\ |
779 |
> |
& AA hexane & 1.92 & 243(29) & 191(11) \\ |
780 |
> |
& AA toluene & 1.93 & 364(36) & 322(67) \\ |
781 |
> |
\hline |
782 |
> |
bare & UA hexane & Avg. & 46.5(3.2) & 49.4(4.5) \\ |
783 |
> |
& UA hexane(D) & 0.98 & 43.9(4.6) & 43.0(2.0) \\ |
784 |
> |
& AA hexane & 0.96 & 31.0(1.4) & 29.4(1.3) \\ |
785 |
> |
& UA toluene & 1.99 & 70.1(1.3) & 65.8(0.5) \\ |
786 |
|
\hline\hline |
787 |
|
\end{tabular} |
788 |
|
\label{modelTest} |
805 |
|
interfaces, using AA model for both butanethiol and hexane yields |
806 |
|
substantially higher conductivity values than using UA model for at |
807 |
|
least one component of the solvent and capping agent, which exceeds |
808 |
< |
the upper bond of experimental value range. This is probably due to |
809 |
< |
the classically treated C-H vibrations in the AA model, which should |
810 |
< |
not be appreciably populated at normal temperatures. In comparison, |
811 |
< |
once either the hexanes or the butanethiols are deuterated, one can |
812 |
< |
see a significantly lower $G$ and $G^\prime$. In either of these |
813 |
< |
cases, the C-H(D) vibrational overlap between the solvent and the |
814 |
< |
capping agent is removed. [MAY NEED FIGURE] Conclusively, the |
808 |
> |
the general range of experimental measurement results. This is |
809 |
> |
probably due to the classically treated C-H vibrations in the AA |
810 |
> |
model, which should not be appreciably populated at normal |
811 |
> |
temperatures. In comparison, once either the hexanes or the |
812 |
> |
butanethiols are deuterated, one can see a significantly lower $G$ and |
813 |
> |
$G^\prime$. In either of these cases, the C-H(D) vibrational overlap |
814 |
> |
between the solvent and the capping agent is removed. |
815 |
> |
[MAY NEED SPECTRA FIGURE] Conclusively, the |
816 |
|
improperly treated C-H vibration in the AA model produced |
817 |
|
over-predicted results accordingly. Compared to the AA model, the UA |
818 |
|
model yields more reasonable results with higher computational |
820 |
|
|
821 |
|
However, for Au-butanethiol/toluene interfaces, having the AA |
822 |
|
butanethiol deuterated did not yield a significant change in the |
823 |
< |
measurement results. |
824 |
< |
. , so extra degrees of freedom |
825 |
< |
such as the C-H vibrations could enhance heat exchange between these |
826 |
< |
two phases and result in a much higher conductivity. |
823 |
> |
measurement results. Compared to the C-H vibrational overlap between |
824 |
> |
hexane and butanethiol, both of which have alkyl chains, that overlap |
825 |
> |
between toluene and butanethiol is not so significant and thus does |
826 |
> |
not have as much contribution to the ``Intramolecular Vibration |
827 |
> |
Redistribution''[CITE HASE]. Conversely, extra degrees of freedom such |
828 |
> |
as the C-H vibrations could yield higher heat exchange rate between |
829 |
> |
these two phases and result in a much higher conductivity. |
830 |
|
|
790 |
– |
|
831 |
|
Although the QSC model for Au is known to predict an overly low value |
832 |
|
for bulk metal gold conductivity\cite{kuang:164101}, our computational |
833 |
|
results for $G$ and $G^\prime$ do not seem to be affected by this |
834 |
< |
drawback of the model for metal. Instead, the modeling of interfacial |
835 |
< |
thermal transport behavior relies mainly on an accurate description of |
836 |
< |
the interactions between components occupying the interfaces. |
834 |
> |
drawback of the model for metal. Instead, our results suggest that the |
835 |
> |
modeling of interfacial thermal transport behavior relies mainly on |
836 |
> |
the accuracy of the interaction descriptions between components |
837 |
> |
occupying the interfaces. |
838 |
|
|
839 |
|
\subsection{Mechanism of Interfacial Thermal Conductance Enhancement |
840 |
|
by Capping Agent} |
841 |
< |
%OR\subsection{Vibrational spectrum study on conductance mechanism} |
841 |
> |
[OR: Vibrational Spectrum Study on Conductance Mechanism] |
842 |
|
|
843 |
|
[MAY INTRODUCE PROTOCOL IN METHODOLOGY/COMPUTATIONAL DETAIL, EQN'S] |
844 |
|
|
850 |
|
the velocity auto-correlation functions, which is used to construct a |
851 |
|
power spectrum via a Fourier transform. |
852 |
|
|
853 |
+ |
[MAY RELATE TO HASE'S] |
854 |
|
The gold surfaces covered by |
855 |
|
butanethiol molecules, compared to bare gold surfaces, exhibit an |
856 |
|
additional peak observed at a frequency of $\sim$170cm$^{-1}$, which |
857 |
< |
is attributed to the vibration of the S-Au bond. This vibration |
857 |
> |
is attributed to the vibration of the S-Au bonding. This vibration |
858 |
|
enables efficient thermal transport from surface Au atoms to the |
859 |
|
capping agents. Simultaneously, as shown in the lower panel of |
860 |
|
Fig. \ref{vibration}, the large overlap of the vibration spectra of |
863 |
|
combination of these two effects produces the drastic interfacial |
864 |
|
thermal conductance enhancement in the all-atom model. |
865 |
|
|
866 |
< |
[MAY NEED TO CONVERT TO JPEG] |
866 |
> |
[REDO. MAY NEED TO CONVERT TO JPEG] |
867 |
|
\begin{figure} |
868 |
|
\includegraphics[width=\linewidth]{vibration} |
869 |
|
\caption{Vibrational spectra obtained for gold in different |
872 |
|
\label{vibration} |
873 |
|
\end{figure} |
874 |
|
|
875 |
< |
[COMPARISON OF TWO G'S; AU SLAB WIDTHS; ETC] |
875 |
> |
[MAY ADD COMPARISON OF G AND G', AU SLAB WIDTHS, ETC] |
876 |
|
% The results show that the two definitions used for $G$ yield |
877 |
|
% comparable values, though $G^\prime$ tends to be smaller. |
878 |
|
|
884 |
|
corresponding thermal gradient and to obtain interfacial thermal |
885 |
|
conductivities. Our simulations have seen significant conductance |
886 |
|
enhancement with the presence of capping agent, compared to the bare |
887 |
< |
gold/liquid interfaces. The acoustic impedance mismatch between the |
887 |
> |
gold / liquid interfaces. The acoustic impedance mismatch between the |
888 |
|
metal and the liquid phase is effectively eliminated by proper capping |
889 |
|
agent. Furthermore, the coverage precentage of the capping agent plays |
890 |
|
an important role in the interfacial thermal transport process. |