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# Line 56 | Line 56 | the simulation cell.\cite{MullerPlathe:1997xw,Muller-P
56   (RNEMD) obtains transport coefficients (thermal conductivity and shear
57   viscosity) in a fluid by imposing an artificial momentum flux between
58   two thin parallel slabs of material that are spatially separated in
59 < the simulation cell.\cite{MullerPlathe:1997xw,Muller-Plathe:1999ek} The
59 > the simulation cell.\cite{MullerPlathe:1997xw,ISI:000080382700030} The
60   artificial flux is typically created by periodically ``swapping'' either
61   the entire momentum vector $\vec{p}$ or single components of this
62   vector ($p_x$) between molecules in each of the two slabs.  If the two
# Line 201 | Line 201 | given simply by the decrease in kinetic energy of the
201   hot and cold slabs are separated along the z-axis, the energy flux is
202   given simply by the decrease in kinetic energy of the cold bin:
203   \begin{equation}
204 < (1-x^2) K_c^x  + (1-y^2) K_c^y + (1-z^2) K_c^z = J_z
204 > (1-x^2) K_c^x  + (1-y^2) K_c^y + (1-z^2) K_c^z = J_z\Delta t
205   \end{equation}
206   The expression for the energy flux can be re-written as another
207   ellipsoid centered on $(x,y,z) = 0$:
208   \begin{equation}
209 < x^2 K_c^x + y^2 K_c^y + z^2 K_c^z = (K_c^x + K_c^y + K_c^z - J_z)
209 > x^2 K_c^x + y^2 K_c^y + z^2 K_c^z = K_c^x + K_c^y + K_c^z - J_z\Delta t
210   \label{eq:fluxEllipsoid}
211   \end{equation}
212   The spatial extent of the {\it flux ellipsoid equation} is governed
# Line 221 | Line 221 | One may also define momentum flux (say along the x-dir
221  
222   One may also define momentum flux (say along the x-direction) as:
223   \begin{equation}
224 < (1-x) P_c^x  = j_z(p_x)
224 > (1-x) P_c^x  = j_z(p_x)\Delta t
225   \label{eq:fluxPlane}
226   \end{equation}
227   The above {\it flux equation} is essentially a plane which is
# Line 273 | Line 273 | Our simulation consists of a series of systems.
273   an approach similar to the above would be sufficient for this as well.
274  
275   \section{Computational Details}
276 < Our simulation consists of a series of systems.
276 > Our simulation consists of a series of systems. All of these
277 > simulations were run with the OOPSE simulation software
278 > package\cite{Meineke:2005gd} integrated with RNEMD methods.
279  
280   A Lennard-Jones fluid system was built and tested first. In order to
281   compare our method with swapping RNEMD, a series of simulations were
282   performed to calculate the shear viscosity and thermal conductivity of
283 < argon. 2592 atoms were in a orthorhombic cell, which was ${10.06 \sigma
284 <  \times 10.06 \sigma \times 30.18 \sigma}$ by size. The reduced density
285 < ${\rho^* = \rho\sigma^3}$ was thus 0.849, which enabled direct
286 < comparison between our results and others.
283 > argon. 2592 atoms were in a orthorhombic cell, which was ${10.06\sigma
284 >  \times 10.06\sigma \times 30.18\sigma}$ by size. The reduced density
285 > ${\rho^* = \rho\sigma^3}$ was thus 0.85, which enabled direct
286 > comparison between our results and others. These simulations used
287 > Verlet time-stepping algorithm with reduced timestep ${\tau^* =
288 >  4.6\times10^{-4}}$.
289  
290   For shear viscosity calculation, the reduced temperature was ${T^* =
291 <  k_B T / \epsilon = 0.72}$. Simulations were run in microcanonical
291 >  k_B T/\varepsilon = 0.72}$. Simulations were run in microcanonical
292   ensemble (NVE). For the swapping part, Muller-Plathe's algorithm was
293   adopted.\cite{ISI:000080382700030} The simulation box was under
294 < periodic boundary condition, and devided into 20 slabs. In each swap,
295 < the top slab ${(n = 0)}$ exchange the most negative $x$ momentum with the
296 < most positive $x$ momentum in the center slab ${(n = N/2)}$. Referring
294 > periodic boundary condition, and devided into ${N = 20}$ slabs. In each swap,
295 > the top slab ${(n = 1)}$ exchange the most negative $x$ momentum with the
296 > most positive $x$ momentum in the center slab ${(n = N/2 + 1)}$. Referred
297   to Tenney {\it et al.}\cite{tenneyANDmaginn}, a series of swapping
298 < frequency were chosen. Corresponding to each result from swapping
298 > frequency were chosen. According to each result from swapping
299   RNEMD, scaling RNEMD simulations were run with the target momentum
300 < flux parameter set to produce a similar momentum flux and shear
301 < rate. Furthermore, various scaling frequencies and corresponding flux
302 < can be tested for one swapping rate.
300 > flux set to produce a similar momentum flux and shear
301 > rate. Furthermore, various scaling frequencies can be tested for one
302 > single swapping rate. To compare the performance between swapping and
303 > scaling method, temperatures of different dimensions in all the slabs
304 > were observed.
305  
306 < After each simulation, the shear viscosities were calculated in
307 < reduced unit.
306 > After each simulation, the shear viscosity was calculated in reduced
307 > unit. The momentum flux was calculated with total unphysical
308 > transferred momentum ${P_x}$ and simulation time $t$:
309 > \begin{equation}
310 > j_z(p_x) = \frac{P_x}{2 t L_x L_y}
311 > \end{equation}
312 > And the velocity gradient ${\langle \partial v_x /\partial z \rangle}$
313 > can be obtained by a linear regression of the velocity profile. From
314 > the shear viscosity $\eta$ calculated with the above parameters, one
315 > can further convert it into reduced unit ${\eta^* = \eta \sigma^2
316 >  (\varepsilon  m)^{-1/2}}$.
317  
318 + For thermal conductivity calculation, simulations were first run under
319 + reduced temperature ${T^* = 0.72}$ in NVE ensemble. Muller-Plathe's
320 + algorithm was adopted in the swapping method. Under identical
321 + simulation box, in each swap, the top slab exchange the molecule with
322 + least kinetic energy with the molecule in the center slab with most
323 + kinetic energy, unless this ``coldest'' molecule in the ``hot'' slab
324 + is still ``hotter'' than the ``hottest'' molecule in the ``cold''
325 + slab. According to swapping RNEMD results, target energy flux for
326 + scaling RNEMD simulations can be set. Also, various scaling
327 + frequencies can be tested for one target energy flux. To compare the
328 + performance between swapping and scaling method, distributions of
329 + velocity and speed in different slabs were observed.
330 +
331 + For each swapping rate, thermal conductivity was calculated in reduced
332 + unit. The energy flux was calculated similarly to the momentum flux,
333 + with total unphysical transferred energy ${E_{total}}$ and simulation
334 + time $t$:
335 + \begin{equation}
336 + J_z = \frac{E_{total}}{2 t L_x L_y}
337 + \end{equation}
338 + And the temperature gradient ${\langle\partial T/\partial z\rangle}$
339 + can be obtained by a linear regression of the temperature
340 + profile. From the thermal conductivity $\lambda$ calculated, one can
341 + further convert it into reduced unit ${\lambda^*=\lambda \sigma^2
342 +  m^{1/2} k_B^{-1}\varepsilon^{-1/2}}$.
343 +
344 + \section{Results And Discussion}
345 + \subsection{Shear Viscosity}
346 +
347   \section{Acknowledgments}
348   Support for this project was provided by the National Science
349   Foundation under grant CHE-0848243. Computational time was provided by

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