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Transcript
Proceedings of the 7th IASME / WSEAS International Conference on HEAT TRANSFER, THERMAL ENGINEERING and ENVIRONMENT (HTE '09)
Effect of Nanoconvection due to Brownian Motion on Thermal Conductivity of
Nanofluids
M. REZA AZIZIANa, HIKMET Ş. AYBARa, TUBA OKUTUCUb
Department of Mechanical Engineering, Eastern Mediterranean University, Gazimagusa, Mersin10, TURKEY
b
Department of Mechanical Engineering, Middle East Technical University, Ankara, 06530, TURKEY
[email protected]
http://me.emu.edu.tr
a
Abstract: - A nanofluid is a new class of heat transfer fluids that contain a base fluid and nanoparticles. The use of
additives is a technique applied to enhance the heat transfer performance of base fluids. The thermal conductivity of the
ordinary heat transfer fluids is not adequate to meet today’s cooling rate requirements. Nanofluids have been shown to
increase the thermal conductivity and convective heat transfer performance of the base liquids. One of the possible
mechanisms for anomalous increase in the thermal conductivity of nanofluids is the Brownian motions of the
nanoparticles inside the base fluids. It is shown in this study that the heat diffusion assumption that has been used in the
macro- and micro- composite systems is not valid in the nanofluid systems. Apart from heat diffusion the nanoconvection
diffusion that it is due to the indirect effect of Brownian motion is responsible of enhancement in thermal conductivity of
nanofluid systems.
Key-Words: - Heat Transfer, Thermal Conductivity, Nanofluids, Nanoconvection, Brownian Motion
1
low volume concentrations, a significant increase occurs
in thermal performance. Research results from nanofluid
research groups all around the world show that nanofluids
have thermal properties that are very different from those
of ordinary heat transfer fluids [5].
The apparent thermal conductivity is the most
important parameter demonstrating the enhancement
potential of heat transfer in nanofluids.
Understanding of the effective thermal conductivity
of mixtures originates from continuum models where it is
assumed that diffusive heat transfer occurs in both fluid
and solid phases. The models with this assumption give
good results for the large particles suspended in base fluid
systems [6]. Nevertheless, they could not predict the
anomalous heat transfer characteristics of nanofluids. In
addition, the important disadvantage of the macroscopic
approach based on the diffusive heat transport is that the
particle size does not affect the thermal conductivity. On
the other hand, the experimental data for the thermal
conductivity of different types of nanofluids show that in
the same volume fraction the effective thermal
conductivity is greater for suspensions of smaller
particles. Indicating that there exist some other
parameters affecting the thermal characteristics of
nanofluids.
Four possible explanations for the cause of an
anomalous increase in the thermal conductivity are the
effects of interfacial layer, Brownian motion,
nanoparticles clustering, and the nature of heat transport
Introduction
The thermal conductivity of ordinary heat transfer fluids
is not adequate to meet today’s industrial requirements.
They are about two orders of magnitude less efficient in
conducting heat compared to metals. Therefore the use of
solid particles as an additive suspended into the base fluid
is a technique for increasing the heat transfer rate.
Enhancment of the thermal conductivity is the main idea
for improving the heat transfer characteristics of ordinary
fluids [1].
Dispersing solid particles in liquids to improve the
physical properties of liquids is hardly new as it has been
well known for 100 years. The idea can be traced back to
James Clerk Maxwell’s theoretical work (Maxwell, 1873)
[2]. In conventional cases, the suspended particles are of
micrometer or even mm dimension. Such large particles
may cause such severe problems as abrasion and
clogging. Therefore, fluids with suspended large particles
have little application in heat transfer enhancement [3].
Nanofluids have a potential to reduce such problems.
Nanofluids, a name conceived by Choi [4], in Argonne
National Laboratory, to describe a fluid consisting of
solid nanoparticles of size less than 100nm suspended on
it with solid volume fractions typically less than 4%.
Nanofluids consisting of such particles have been shown
to increase the thermal conductivity and convective heat
transfer performance of the base liquids. Because of the
higher thermal conductivity of particle materials, even at
ISSN: 1790-5095
53
ISBN: 978-960-474-105-2
Proceedings of the 7th IASME / WSEAS International Conference on HEAT TRANSFER, THERMAL ENGINEERING and ENVIRONMENT (HTE '09)
nanoparticles in a nanofluid produces convection like
effects at the nanoscale (nanoconvection).
The last two modes are related to the Brownian
motion effect that is being considered in this work.
in nanoparticles [10]. This study focuses on the Brownian
motion effect of the nanoparticles on the thermal
conductivity of the nanofluids.
Nomenclature
d
Greek Symbols
μ
ρ
α
τ
2
Dynamic viscosity (kg/m.s)
Density (kg/m3)
Thermal diffusivity (m2/s)
Time scale (s)
Fluid
Brownian motion diffusion
Convection diffusion
Heat diffusion
Particle Collisions
force ∝ fV
(1)
where f is the drag coefficient and according to the
Stokes’ law it is equal to 6πμr, and V is the drift velocity.
After simplifications and according to the StokesEinstein formula particle diffusion constant takes the
form [10]
Brownian Motion Effect
In nanofluid systems, due to the size of the nanoparticles
Brownian motion takes place which can affect the heat
transfer properties. In a conventional approach for
calculating thermal conductivity of nanofluids such as
Maxwell [7] and Hamilton-Crosser model [8], the effect
of the particle Brownian motion is neglected due to the
large particle size. As the particle size scale approaches to
the nano-meter scale, the particle Brownian motion and
its effect on the surrounding liquids play an important
role in heat transfer. Jang and Choi in 2004 [9] conducted
a study that takes into account the Brownian motion
behavior of nanoparticles. Their model consists of the
four modes of energy transport in nanofluids. The first
mode is collision of the base fluid molecules showing the
heat conductivity at micro-scale, the second mode is the
thermal diffusion in nanoparticles inside the base fluids,
the third one is the collision between nanoparticles due to
Brownian motion, and the last one is the thermal
interactions of dynamic or dancing nanoparticles with the
base fluid molecules due to the Brownian motion.
Therefore, they postulate that Brownian motion of
ISSN: 1790-5095
3.1
The first mechanism that is expected to increase the
thermal conductivity is the nanoparticle collisions inside
the base fluid that could increase the solid-solid heat
transport from one particle to another one [10]. For
calculating this effect, a single sphere nanoparticle was
considered that moves slowly through the continuum of
the base fluid. In this case the net velocity of the particle
is proportional to the force acting on it
Subscripts
f
BD
CD
HD
Comparing the Time Scales
The Brownian motion of nanoparticles could contribute to
the thermal conduction enhancement through two ways: a
direct contribution due to the motion of the nanoparticles
that transport heat i.e. solid-solid transport of heat from
one to another, and an indirect contribution due to nanoconvection of the fluid surrounding individual
nanoparticles.
In order to prove the inadequacy of the heat diffusion
approach in nanofluid systems, the time scales involved
in the two Brownian motion effects, and in heat diffusion
approach are compared in this section.
Diameter (m)
Diffusion constant (m2/s)
Drag coefficient (kg/s)
Thermal conductivity (W/m.K)
Radius (m)
Temperature (K)
Drift velocity (m/s)
Kinematic viscosity (m2/s)
Specific heat (kJ/kg.K)
Boltzmann constant (J/K)
D
f
k
r
T
V
v
cp
kB
3
D=
k BT
6πμ r
(2)
where kB is the Boltzmann constant (1.3805 × 10-23 J/K), μ
is the fluid viscosity, and r is the particle radius.
Equation 2 shows that the effect of particle collisions
on thermal conductivity could be estimated by calculating
the time scale of the particle motion. Time required for a
particle to move by the distance equal to its size τBD, is
given by [10]
τ BD
54
d 2 24πμ r 3
=
=
6D
6 k BT
(3)
ISBN: 978-960-474-105-2
Proceedings of the 7th IASME / WSEAS International Conference on HEAT TRANSFER, THERMAL ENGINEERING and ENVIRONMENT (HTE '09)
3.2
Nanoconvection
4
The energy transport due to the convection of the
nanoparticles caused by the Brownian motion is called
nanoconvection. Nanoconvection is the second
mechanism that could be responsible of the energy
transport in nanofluid systems. The rate of heat transfer
due to convection could be calculated by convection
diffusivity. Convection diffusivity is the kinematic
diffusivity (v) of the liquid, which is also known as the
momentum diffusivity [11].
μ
ρf
ν=
Table 1. Comparison of the different diffusion time scales
for water base nanofluids containing 5nm nanoparticles
Diffusion time
Value
Formula
scale
(s)
(4)
where μ is the viscosity of the base liquid, and ρf is the
liquid density.
Hence, the time required for the transfer of the heat
due to the convection effect at a distance equal to the
nanoparticle size is given by [11]
τ CD =
3.2
d2
ν
=
4r 2
ν
Brownian motion
Diffusion
Nanoconvection
Diffusion
(5)
Heat
Diffusion
Heat Diffusion
k
ρc p
(6)
Where k is the thermal conductivity of the medium, and
ρcp is a volumetric heat capacity.
Based on the thermal diffusivity the time required for
the heat to diffuse into a liquid by a distance equal to the
size of the particle is
τ HD =
2
d 2 4r c p ρ
=
6α
6k f
ISSN: 1790-5095
τ BD =
24πμ r 3
6 k BT
τ CD =
τ HD =
4r 2
ν
4r 2c p ρ
6k f
3.8 × 10-8
3.11 × 10-11
2.83 × 10-11
Keblinski et al. [10] in 2002, showed that the
movement of nanoparticles due to the Brownian motion is
too slow compared to heat diffusion which is apparent
from Table 1 as well. However, another effect that is not
considered in their study is the nanoconvection diffusion
due to indirect effect of Brownian motion.
Comparing the time scales of the different diffusion
mechanism, it can be concluded that the effect of
nanoconvection diffusion is comparable to that of heat
diffusion. This simple comparison shows why the effect
of Brownian motion is important in the nanofluid systems
for thermal transport. The comparison also shows that the
assumption of heat diffusion by itself is not sufficient in
nanofluid systems. In order to calculate the heat transfer
enhancement rate the effect of nanoconvection due to the
indirect effect of Brownian motion should also
considered.
Diffusion of heat occurs by the net transport of heat from
a higher temperature region to a lower temperature one by
random molecular motion. The result of diffusion is a
progressive equilibrium temperature. Conduction is the
transfer of heat by direct contact of molecules. Heat is
transferred by conduction when adjacent atoms vibrates
against each other. Heat conduction in a stationary fluid
could be simulated as the diffusion of particles into a
fluid.
Normally one can estimate the rate of heat diffusion
in a solid or stationary fluid by the thermal diffusivity as
α=
Result and Disscusion
Three time scales for different mechanism of heat transfer
in nanofluids are evaluated by comparing them for a
nanofluid system with a base fluid of water and
nanoparticles of a 5nm diameter. For water at 300K,
specifications are as follows: kf = 0.613 W/m.K, cp =
4.179 kJ/kg.K, μ = 0.798 x 10-3 kg/m.s, ρ = 995.7 kg/m3.
This comparison has shown in Table 1.
References:
[1] V. Trisaksri, S. Wongwises, Critical review of heat
transfer characteristics of nanofluids, Journal of
Renewable and Sustainable Energy Review, 11
(2007) 512-523.
[2] W.Yu, S.U.S. Choi, The role of interfacial layers in
the enhanced thermal conductivity of nanofluids: A
(7)
55
ISBN: 978-960-474-105-2
Proceedings of the 7th IASME / WSEAS International Conference on HEAT TRANSFER, THERMAL ENGINEERING and ENVIRONMENT (HTE '09)
renovated Maxwell model, Journal of Nanoparticle
Research. 5 (2003) 167-171.
[3] Y. Xuan, Q. Li, Heat transfer enhancement of
nanofluids, International Journal of Heat and Fluid
Flow 21 (2000) 58-64.
[4] S.U.S. Choi, Enhancing thermal conductivity of
fluids with nanoparticles. In: Siginer, D.A. and
Wang, H.P.eds. Developments and Applications of
Non-Newtonian Flows, ASME, 66 (1995) 99-105.
[5] W. Yu, D.M. France, J.L. Routbort, S.U.S. Choi,
Review and Comparison of Nanofluid Thermal
Conductivity and Heat Transfer Enhancements,
Heat Transfer Engineering, 29:5 (2008) 432-460.
[6] X.Q. Wang, A.S. Mujumdar, Heat Transfer
Characteristics of Nanofluids: review, International
Journal of Thermal Science, 46 (2007) 1-19.
[7] J.C. Maxwell, Treatise on Electricity and
Magnetism, Oxford: Clarendon Press (1873).
[8] R.L. Hamilton, O.K. Crosser, Thermal
Conductivity of Heterogeneous Two-Component
Systems, Industrial & Engineering Chemistry
Fundamentals, 1 (1962) 187-191.
[9] S.P. Jang, S.U.S. Choi, Role of Brownian motion
in the enhanced thermal conductivity of nanofluids,
Applied Physics Letters, 84:21 (2004) 4316-4318.
[10] P. Keblinski, S.R. Phillpot, S.U.S. Choi, J.A.
Eastman, Mechanisms of heat flow in suspentions
of nano-sized particles (nanofluids), International
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[11] R. Prasher, P. Bhattacharya, P.E. Phelan,
Brownian-Motion-Based Convective-Conductive
Model for the Effective Thermal Conductivity of
Nanofluids, ASME Transactions, 128 (2006) 588595.
ISSN: 1790-5095
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ISBN: 978-960-474-105-2