 Nano Express
 Open Access
 Published:
Enhancing surface heat transfer by carbon nanofins: towards an alternative to nanofluids?
Nanoscale Research Letters volume 6, Article number: 249 (2011)
Abstract
Background
Nanofluids are suspensions of nanoparticles and fibers which have recently attracted much attention because of their superior thermal properties. Nevertheless, it was proven that, due to modest dispersion of nanoparticles, such high expectations often remain unmet. In this article, by introducing the notion of nanofin, a possible solution is envisioned, where nanostructures with high aspectratio are sparsely attached to a solid surface (to avoid a significant disturbance on the fluid dynamic structures), and act as efficient thermal bridges within the boundary layer. As a result, particles are only needed in a small region of the fluid, while dispersion can be controlled in advance through design and manufacturing processes.
Results
Toward the end of implementing the above idea, we focus on single carbon nanotubes to enhance heat transfer between a surface and a fluid in contact with it. First, we investigate the thermal conductivity of the latter nanostructures by means of classical nonequilibrium molecular dynamics simulations. Next, thermal conductance at the interface between a single wall carbon nanotube (nanofin) and water molecules is assessed by means of both steadystate and transient numerical experiments.
Conclusions
Numerical evidences suggest a pretty favorable thermal boundary conductance (order of 10^{7} W·m^{2}·K^{1}) which makes carbon nanotubes potential candidates for constructing nanofinned surfaces.
Background and motivations
Nanofluids are suspensions of solid particles and/or fibers, which have recently become a subject of growing scientific interest because of reports of greatly enhanced thermal properties [1, 2]. Filler dispersed in a nanofluid is typically of nanometer size, and it has been shown that such nanoparticles are able to endow a base fluid with a much higher effective thermal conductivity than fluid alone [3, 4]: significantly higher than those of commercial coolants such as water and ethylene glycol. In addition, nanofluids show an enhanced thermal conductivity compared to theoretical predictions based on the Maxwell equation for a welldispersed particulate composite model. These features are highly favorable for applications, and nanofluids may be a strong candidate for new generation of coolants [2]. A review about experimental and theoretical results on the mechanism of heat transfer in nanofluids can be found in Ref. [5], where those authors discuss issues related to the technology of nanofluid production, experimental equipment, and features of measurement methods. A large degree of randomness and scatter has been observed in the experimental data published in the open literature. Given the inconsistency in these data, we are unable to develop a comprehensive physicalbased model that can predict all the experimental evidences. This also points out the need for a systematic approach in both experimental and theoretical studies [6].
In particular, carbon nanotubes (CNTs) have attracted great interest for nanofluid applications, because of the claims about their exceptionally high thermal conductivity [7]. However, recent experimental findings on CNTs report an anomalously wide range of enhancement values that continue to perplex the research community and remain unexplained [8]. For example, some experimental studies showed that there is a modest improvement in thermal conductivity of water at a high loading of multiwalled carbon nanotubes (MWCNTs), approximately of 35% increase for a 1 wt% MWNT nanofluid [9]. Those authors attribute the increase to the formation of a nanotube network with a higher thermal conductivity. On the contrary, at low nanotube content, <0.03 wt%, they observed a decrease in thermal conductivity with an increase of nanotube concentration. On the other hand, more recent experimental investigations showed that the enhancement of thermal conductivity as compared with water varied linearly when MWCNT weight content was increased from 0.01 to 3 wt%. For a MWNT weight content of 3 wt%, the enhancement of thermal conductivity reaches 64% of that of the base fluid (e.g., water). The average length of the nanotubes appears to be a very sensitive parameter. The enhancement of thermal conductivity compared with water alone is enhanced when nanotube average length is increased in the 0.55 μ m range [10].
Clearly, there are difficulties in the experimental measurements [11], but the previous results also reveal some underlaying technological problems. First of all, the CNTs show some bundling or the formation of aggregates originating from the fabrication step. Moreover, it seems reasonable that CNTs encounter poor dispersibility and suspension durability because of the aggregation and surface hydrophobicity of CNTs as a nanofluid filler. Therefore, the surface modification of CNTs or additional chemicals (surfactants) have been required for stable suspensions of CNTs, because of the polar characteristics of base fluid. In the case of surface modification of CNTs, waterdispersible CNTs have been extensively investigated for potential applications, such as biological uses, nanodevices, novel precursors for chemical reagents, and nanofluids [2]. From the above brief review, it is possible to conclude that, despite the great interest and intense research in this field, the results achieved so far cannot be considered really encouraging. Hence, toward the end of overcoming these problems, we introduce the notion of thermal nanofins, with an entirely different meaning with respect to standard terminology. By nanofins, we mean slender nanostructures, sparse enough not to interfere with the thermal boundary layer, but sufficiently rigid and conductive to allow for direct energy transfer between the wall and the bulk fluid, thus acting as thermal bridges. A macroscopic analogy is given by an eolic park, where wind towers are slim enough to avoid disturbing the planetary boundary layer, but high enough to reach the region where the wind is stronger (see Figure 1). In this way, nanoparticles are used only where they are needed, namely, in the thermal boundary layer (or in the thermal laminar sublayer, in case of turbulent flows, not discussed here), and this might finally unlock the enormous potential of the basic idea behind nanofluids.
This article investigates a possible implementation of the above idea using CNTs, because of their unique geometric features (slimness) and thermophysical properties (high thermal conductivity). CNTs have attracted the attention of scientific community, since their mechanical and transport (both electrical and thermal) properties were proven to be superior compared with traditional materials. This observation has motivated intensive theoretical and experimental efforts during the last decade, toward the full understanding/exploitation of these properties [12–16]. Despite these expectations, however, it is reasonable to say that these efforts are far from setting out a comprehensive theoretical framework that can clearly describe these phenomena. First of all, the vast majority of CNTs (mainly multiwalled) exhibits a metallic behavior, but the phonon mechanism (lattice vibrations) of heat transfer is considered the prevalent one close to room temperature [17, 18]. The phonon mean free path, however, is strongly affected by the existence of lattice defects, which is actually a very common phenomenon in nanotubes and closely linked to manufacturing methods. Second, there is the important issue of quantifying the interface thermal resistance between a nanostructure and the surrounding fluid, which affects the heat transfer and the maximum efficiency. It is noted that, according to the classical theory, there is an extremely low thermal resistance when one reduces the characteristic size of the thermal "antenna" promoting heat transfer [19], as confirmed by numerical investigations for CNTs [20–22].
This article investigates, by molecular mechanics based on force fields (MMFF), the thermal performance of nanofins made of single wall CNTs (SWCNTs). The SWCNTs were selected mainly because of time constraints of our parallel computational facilities. The following analysis can be split into two parts. First of all, the heat conductivity of SWCNTs is estimated numerically by both simplified model (section "Heat conductivity of singlewall carbon nanotubes: a simplified model", where this approach is proved to be inadequate) and a detailed threedimensional model (section "Heat conductivity of singlewall carbon nanotubes: detailed three dimensional models"). This allows one to appreciate the role of model dimensionality (and harmonicity/anharmonicity of interaction potentials) in recovering standard heat conduction (i.e., Fourier's law). This first step is used for validation purposes in a vacuum and for comparison with results from literature. Next, the thermal boundary conductance between SWCNT and water (for the sake of simplicity) is computed by two methods: the steadystate method (section "Steadystate simulations"), mimicking ideal cooling by a strong forced convection (thermostatted surrounding fluid), and the transient method (section "Transient simulations"), taking into account only atomistic interactions with the local fluid (defined by the simulation box). This strategy allows one to estimate a reasonable range for the thermal boundary conductance.
Heat conductivity of SWCNTs: a simplified model
In order to significantly downgrade the difficulty of studying energy transport processes within a CNT, some authors often resort to simplified lowdimensional systems such as onedimensional lattices [23–28]. In particular, heat transfer in a lattice is typically modeled by the vibrations of lattice particles interacting with the nearest neighbors and by a coupling with thermostats at different temperatures. The latter are the popular numerical experiments based on nonequilibrium molecular dynamics (NEMD). In this respect, to the end of measuring the thermal conductivity of a single wall nanotube (SWNT), we set up a model for solving the equations of motion of the particle chain pictorially reported in Figure 2 where each particle represents a ring of several atoms in the real nanotube (see also the lefthand side of Figure 3). In the present model, carboncarbonbonded interactions between first neighbors (i.e., atoms of the i th particles and atoms of the particles i ± 1) separated by a distance r are taken into account by a Morsetype potential (shown on the righthand side of Figure 3) [29] expressed in terms of deviations x = r  r_{0} from the bond length r_{0}:
where V_{0} is the bond energy, while a is assumed as a = r_{0}/2. Following [30], the bond energy V_{0} = 4.93 eV, while the distance between two consecutive particles at equilibrium is assumed as r_{0} = 0.123 nm. At any arbitrary configuration, the total force, F_{ i } , acting on the i th particle is computed as
with dx_{ij}= x_{ i }  x_{ij}, dx_{i+j}= x_{i+j} x_{ i } , and N_{bon} denoting the number of carboncarbon bonds between two particles, whereas a penalization factor sin ϑ may be included to account for bonds not aligned with the tube axis (see Figure 3). In the present case, we use freeend boundary condition, and hence, forces experienced by particles at the ends of the chain read:
Let p_{ i } and m_{ i } be the momentum and mass of the i th particle, respectively; the equations of motion for the inner particles take the form:
whereas the outermost particles (i = 1, N ) are coupled to NoséHoover thermostats and are governed by the equations:
with k_{b}, T_{0}, N_{f}, and τ_{T} denoting the Boltzmann constant, the thermostat temperature, number of degrees of freedom, and relaxation time, respectively, while the auxiliary variable ξ is typically referred to as friction coefficient[31]. NoséHoover thermostatting is preferred since it is deterministic and it typically preserves canonical ensemble. However, we notice that (5) represent the equations of motions with a single thermostat. In this case, it is known that the latter scheme may run into ergodicity problems and thus fail to generate a canonical distribution. Although stochastic thermostats (see, e.g., Andersen [32]) are purposely devised to generate a canonical distribution, they are characterized by a less realistic dynamics. Hence, to the end of overcoming the above issues, using deterministic approaches, Martyna et al. have introduced the idea of NoséHoover chain [33] (see also [34, 35] for the equation of motion of NoséHoover chains and further details on thermostats in molecular dynamics simulations). Simulations presented below were carried out using both a single thermostat and a NoséHoover chain (with two thermostats), and no differences were noticed.
Local temperature T_{ i } (t) at a time instant t is computed for each particle i using energy equipartition:
where 〈〉 denotes time averaging. On the other hand, local heat flux J_{ i } , transferred between particle i and i + 1, can be linked to mechanical quantities by the following relationship [25, 27]:
The above simplified model has been tested in a range of low temperature (300 K < T < 1000 K), where we notice that it is not suitable to predict normal heat conduction (Fourier's law). In other words, at steady state (i.e., when heat flux is uniform along the chain and constant in time) is observed a finite heat flux although no meaningful temperature gradient could be established along the chain (see Figure 2). Thus, the above results predict a divergent heat conductivity. In this context, it is worth stressing that onedimensional lattices with harmonic potentials are known to violate Fourier's law, and they exhibit a flat temperature profile (and divergent heat conductivity). On the one hand, the results of the simplified model in Figure 2 are likely due to a nonsufficiently strong anharmonicity. Indeed, as reported on the righthand side of Figure 3, the Morse function (1) can be safely approximated by an harmonic potential in the range of maximal deviation x observed at low temperature (T < 1000 K), namely, V_{b} (x) ≈ V_{0} (x^{2}/a^{2}  1).
On the other hand, it is worth stressing that it has been demonstrated that anharmonicity alone is insufficient to ensure normal heat conduction [23], in onedimensional lattice chains.
Heat conductivity of SWCNTs: detailed threedimensional models
In all simulations below, we have adopted the opensource molecular dynamics (MD) simulation package GROningen MAchine for Chemical Simulations (GROMACS) [36–38] to investigate the energy transport phenomena in threedimensional SWNT obtained by a freely available structure generator (Tubegen) [39]. Three harmonic terms are used to describe the carboncarbonbonded interactions within the SWNT. That is, a bond stretching potential (between two covalently bonded carbon atoms i and j at a distance r_{ ij } ):
a bending angle potential (between the two pairs of covalently bonded carbon atoms (i, j) and (j, k))
and the RyckaertBellemans potential for proper dihedral angles (for carbon atoms i, j, k and l)
are considered in the following MD simulations. In this case, θ_{ ijk } and ϕ_{ ijkl } represent all the possible bending and torsion angles, respectively, while = 0.142 and = 120° are the reference geometry parameters for graphene. Nonbonded van der Waals interaction between two individual atoms i and j at a distance r_{ ij } can be also included in the model by a LennardJones potential:
where the force constants , and in (8), (9), and (10) and the parameters (σ_{CC}, ϵ_{CC}) in (11) are chosen according to the Table 1 (see also [40, 41]). In reversible processes, differentials of heat dQ_{rev} are linked to differentials of a state function, entropy, ds through temperature: dQ_{rev} = T ds. Moreover, following Hoover [31, 42], entropy production of a NoséHoover thermostat is proportional to the time average of the friction coefficient 〈ξ〉 through the Boltzmann constant k_{b}, and hence, once a steadystate temperature profile is established along the nanotube, the heat flux per unit area within the SWNT can be computed as
where the cross section S_{A} is defined as S_{A} = 2πrb, with b = 0.34 nm denoting the van der Waals thickness (see also [43]). In this case, the use of formula (12) is particularly convenient since the quantity 〈ξ〉 can be readily extracted from the output files in GROMACS.
The measure of both the slopes of temperature profiles along the inner rings of SWNT in Figures 4 and 5 and the heat flux by (12) enables us to evaluate heat conductivity λ according to Fourier's law. It is worth stressing that, as shown in the latter figures, unlike onedimensional chains such as the one discussed above, fully threedimensional models do predict normal heat conduction even when using harmonic potentials such as (8), (9), and (10). Nevertheless, we notice that in the above threedimensional model, anharmonicity (necessary condition for standard heat conduction in onedimensional lattice chains [23]), despite the potential form itself, intervenes due to a more complicated geometry and the presence of angular and dihedral potentials (9), and (10). Interestingly, in our simulations we can omit at will some of the interaction terms V_{b}, V_{a}, V_{rb}, and V_{nb}, and investigate how temperature profile and thermal conductivity λ are affected. It was found that potentials V_{b} and V_{a} are strictly needed to avoid a collapse of the nanotube. Results corresponding to several setups are reported in Figure 5 and Table 2. It is worth stressing that, for all simulations in a vacuum, nonbonded interactions V_{nb} proven to have a negligible effect on both the slope of temperature profile and heat flux at steady state. On the contrary, the torsion potential V_{rb} does have impact on the temperature profile while no significant effect on the heat flux was noticed: as a consequence, in the latter case, thermal conductivity shows a significant dependence on V_{rb}. More specifically, the higher the torsion rigidity the flatter the temperature profile. Depending on the CNT length (and total number of atoms), computations were carried out for 4 ns up to 6 ns to reach a steady state of the above NEMD simulations. Finally, temperature values of the endpoints of CNTs (see Figures 4, 5) were chosen following others [16, 18].
Thermal boundary conductance of a carbon nanofin in water
Steadystate simulations
In this section, we investigate on the heat transfer between a carbon nanotube and a surrounding fluid (water). The latter represents a first step toward a detailed study of a batch of single CNTs (or small bundles) utilized as carbon nanofins to enhance the heat transfer of a surface when transversally attached to it. To this end, and limited by the power of our current computational facilities, we consider a (5, 5) SWNT (with a length L ≤ 14 nm) placed in a box filled with water (typical setup is shown in Figure 6). SWNT end temperatures are set at a fixed temperature T_{hot} = 360 K, while the solvent is kept at T_{w} = 300 K. The carbonwater interaction is taken into account by means of a LennardJones potential between the carbon and oxygen atoms with a parameterization (ϵ_{CO}, σ_{CO}) reported in Table 1. Moreover, nonbonded interactions between the water molecules consist of both a LennardJones term between oxygen atoms (with ϵ_{OO}, σ_{OO} from Table 1) and a Coulomb potential:
where ε_{0} is the permittivity in a vacuum, while q_{ i } and q_{ j } are the partial charges with q_{O} = 0.82 e and q_{H} = 0.41 e (see also [41]).
We notice that, the latter is a classical problem of heat transfer (pictorially shown in Figure 7), where a single fin (heated at the ends) is immersed in a fluid maintained at a fixed temperature. This system can be conveniently treated using a continuous approach under the assumptions of homogeneous material, constant cross section S, and onedimensionality (no temperature gradients within a given cross section) [44]. In this case, both temperature field and heat flux only depend on the spatial coordinate x, and the analytic solution of the energy conservation equation yields, at the steady state, the following relationship:
where denotes the difference between the local temperature at an arbitrary position x and the fixed temperature T_{w} of a surrounding fluid. Let α and C be the thermal boundary conductance and the perimeter of the fin cross sections, respectively, m be linked to geometry, and material properties as follows:
whereas the two parameters M and N are dictated by the boundary conditions, T (0) = T (L) = T_{hot} (or equivalently, due to symmetry, zero flux condition: dT/ dx (L/ 2) = 0), namely:
Thus, the analytic solution (14) takes a more explicit form:
whereas the heat flux at one end of the fin reads:
In the setup illustrated in Figures 7 and 6, periodic boundary conditions are applied in the x, y, and z directions, and all the simulations are carried out with a fixed time step dt = 1 fs upon energy minimization. First of all, the whole system is led to thermal equilibrium at T = 300 by NoséHoover thermostatting implemented for 0.8 ns with a relaxation time τ_{T} = 0.1 ns. Next, the simulation is continued for 15 ns where NoséHoover temperature coupling is applied only at the tips of the nanofin (here, the outermost 16 carbon atom rings at each end) with T_{hot} = 360 K, and in water with T_{w} = 300 K until, at the steady state, the temperature profile in Figure 8 is developed. Moreover, pressure is set to 1 bar by ParrinelloRahman barostat during both thermal equilibration and subsequent nonequilibrium computation. We notice that the above MD results are in a good agreement with the continuous model for single fins if mL/2 = 0.28 (see also Figure 8). Hence, this enables us to estimate the thermal boundary conductance α_{st} between SWNT and water with the help of Equation (15):
The thermal conductivity λ has been independently computed by means of the technique illustrated in the sections above for the SWNT alone in a vacuum. Results for a nanofin with L = 14 nm are reported in Table 2. We stress that heat flux computed by time averaging of the NoséHoover parameter ξ (see Equation (12)) is also in excellent agreement with the value predicted by the continuous model through Equation (18). For instance, with the above choice mL/2 = 0.28, for (5, 5) SWNT with L = 10 nm, L_{NH} = 2 nm in a box 5 × 5 × 14 nm^{3} we have:  〈ξ〉 N_{f}k_{b}T = 3.11 × 10^{8} W while
We stress that L_{NH} is the axial length of the outermost carbon atom rings coupled to a thermostat at each end of a nanotube. Finally, a useful parameter when studying fins is the thermal efficiency Ω, expressing the ratio between the exchanged heat flux q and the ideal heat flux q_{id} corresponding to an isothermal fin with T (x) = T(0), ∀x ∈ [0, L] [44]. In our case, we find highly efficient nanofins:
Transient simulations
The value of thermal boundary conductance between water and a SWCNT has been assessed by transient simulations as well. Results by the latter methodology are denoted as α_{tr} to distinguish them from the same quantities (α_{st} ) in the above section. In this study, the nanotube was initially heated to a predetermined temperature T_{hot} while water was kept at T_{w}< T_{hot} (using in both cases NoséHoover thermostatting for 0.6 ns). Next, an NVE MD (ensemble where number of particle N, system volume V and energy E are conserved) were performed, where the entire system (SWNT plus water) was allowed to relax without any temperature and pressure coupling. Under the assumption of a uniform temperature field T_{CNT} (t) within the nanotube at any time instant t (i.e., Biot number Bi < 0.1), the above phenomenon can be modeled by an exponential decay of the temperature difference (T_{CNT}  T_{w} ) in time, where the time constant τ_{d} depends on the nanotube heat capacity c_{T} and the thermal heat conductance α_{tr} at the nanotubewater interface as follows (see Figure 9):
In our computations, based on [20], we considered the heat capacity per unit area of an atomic layer of graphite c_{T} = 5.6 × 10^{4} (J·m^{2}·K^{1}).
The values of τ_{d} and α_{tr} have been evaluated in different setups, and results are reported in the Table 2. Numerical computations do predict pretty high thermal conductance at the interface (order of 10^{7} W·m^{2}·K^{1}) with a slight tendency to increase with both the tube length and diameter. It is worth stressing that values for thermal boundary conductance obtained in this study are consistent with both experimental and numerical results found by others for SWCNTs within liquids [20, 45]. However, since the order of magnitude of these results is extremely higher than that involved in macroscopic applications, it may appear as an artifact. Actually, it is quite simple to realize that continuumbased models diverge in case of nanometer dimensions, because of the effects of singularity. Hence, continuumbased predictions may lead to even higher thermal conductances, and they are not even upper bounded, which is clearly unphysical. For example, let us consider the ideal case of a circular cylinder (with diameter D and length L) centered in a square solid of equal length, as reported in Table 3.12 of [19]. The value of thermal boundary conductance can be put into relation with the heat conduction shape factor (CSF) S_{f} as follows:
where
and λ_{w} is the thermal conductivity of the medium, while the square box has dimensions w × w × L. Let us consider the following example, corresponding to the row '(5, 5), BADLJ (sol)' in Table 2. Assuming λ_{w} = 0.58 (W·m^{1}·K^{1}), D = 0.68 nm, w = 4 nm, it yields α_{csf} = 9.2 × 10^{8} W m^{2} K^{1}. The analytic results are even larger than those obtained by the steadystate simulation (usually larger than those obtained by the transient method). Moreover, the continuumbased formula prescribes that thermal conductance (weakly) diverges by reducing the cylinder diameter. On the contrary, MD simulations is in line with the expectation of a bounded thermal boundary conductance. In fact, in agreement with others [45], we even observe a slight decrease with the tube diameter.
We point out that neither the steadystate method nor the transient method fully reproduce the setup described by the analytic formula (23). In fact, in the steadystate method, the entire water bath is thermostatted (while in the analytic formula, only the water boundaries are thermostatted) and, in the transient method, the water temperature changes in time (while the analytic formula is derived under steadystate condition). Nevertheless, from the technological point of view, the above results are in line with the basic idea that high aspectratio nanostructures (such as CNTs) are suitable candidates for implementing the above idea of nanofin, and thus can be utilized for exploiting advantageous heat boundary conductances.
Conclusions
In this study, we first investigated the thermal conductivity of SWCNTs by means of classical nonequilibrium MD using both simplified onedimensional and fully threedimensional models. Next, based on the latter results, we have focused on the boundary conductance and thermal efficiency of SWCNTs used as nanofins within water. More specifically, toward the end of computing the boundary conductance α, two different approaches have been implemented. First, α = α_{st} was estimated through a fitting procedure of results by steadystate MD simulations and a simple onedimensional continuous model. Second, cooling of SWNT (at T_{CNT} ) within water (at T_{w}) was accomplished by NVE simulations. In the latter case, the time constant τ_{d} of the temperature difference (T_{CNT}  T_{w}) dynamics enables us to compute α = α_{tr}. Numerical computations do predict pretty high thermal conductance at the interface (order of 10^{7} W·m^{2}·K^{1}), which indeed makes CNTs ideal candidates for constructing nanofins. We should stress that, consistently with our results α_{st}> α_{tr}, it is reasonable to expect that α_{st} represents the upper limit for the thermal boundary conductance, because (in steadystate simulations) water is forced by the thermostat to the lowest temperature at any time and any position in the computational box. Finally, it is worthwhile stressing that, following the suggestion in [46], all the results of this study can be generalized to different fluids using standard nondimensionalization techniques, upon a substitution of the parameterization (ϵ_{CO}, σ_{CO}) representing a different LennardJones interaction between SWNT and fluid molecules.
Methods
The CNTs geometries simulated in this article were generated using the program Tubegen [39], while water molecules were introduced using the SPC/E model implemented by the genbox package available in GROMACS [38]. Numerical results in this study are based on nonequilibrium MD where the allatom forcefields OPLSAA is adopted for modeling atom interactions. Visualization of simulation trajectories is accomplished using VEGA ZZ [47].
Abbreviations
 CNTs:

carbon nanotubes
 GROMACS:

GROningen MAchine for Chemical Simulations
 MD:

molecular dynamics
 MMFF:

molecular mechanics based on force fields
 MWCNTs:

multiwalled carbon nanotubes
 NEMD:

nonequilibrium molecular dynamics
 SWCNTs:

single wall CNTs
 SWNT:

single wall nanotube.
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Acknowledgements
The above research has received funding from the European Community Seventh Framework Program (FP7 20072013) under grant agreement N. 227407Thermonano. The authors owe their appreciation to Mr. Marco Giardino for his kind assistance whenever the authors had difficulites with computational facilities. The authors also thank Dr. Andrea Minoia and Dr. Thomas Moore for the fruitful discussions with them on the usage of GROMACS in simulating carbon nanotubes. The authors acknowledge also the inspiring discussions with Dr. JeanAntoine Gruss (CEA DTS/LETH, France) about CNTbased nanofluids.
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Motivation for investigating the nanofin idea was initially provided by PA, and thereafter refined by an active interaction between both authors. All onedimensional atomistic simulations and numerical experiments for assessing thermal boundary conductances α were performed by EC. Measurements of thermal boundary conductance through steady state (α_{st}) and transient simulations (α_{st}) were thought by PA, and EC, respectively. Computations of thermal conductivity with different combinations of interaction potentials, as reported in Figure 5, were performed by PA. Authors contributed equally in writing the present manuscript.
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Chiavazzo, E., Asinari, P. Enhancing surface heat transfer by carbon nanofins: towards an alternative to nanofluids?. Nanoscale Res Lett 6, 249 (2011). https://doi.org/10.1186/1556276X6249
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DOI: https://doi.org/10.1186/1556276X6249
Keywords
 Heat Flux
 Base Fluid
 Transient Method
 Carbon Atom Ring
 Thermal Boundary Conductance