Heat_conduction

Heat conduction, or thermal conduction, is the spontaneous transfer of thermal energy through matter, from a region at higher temperature to a region at lower temperature. It thus acts to equalize temperature differences. It is also described as heat energy transferred from one material to another by direct contact.
Thermal energy, in the form of continuous random motion of particles of matter, is transferred by the same coulomb forces that act to support the structure of matter. For this reason, its transfer can be said to occur by physical contact between the particles.

Contents

1 Fourier's law

1.1 Differential form
1.2 Integral form


2 Conductance and resistance

2.1 Intensive-property representation


3 See also
4 References
5 External links
6 Credits



Besides conduction, heat can also be transferred by radiation and convection, and often more than one of these processes may occur in a given situation.

Fourier's law
The law of heat conduction, also known as Fourier's law, states that the time rate of heat transfer through a material is proportional to the negative gradient in the temperature and to the area at right angles, to that gradient, through which the heat is flowing. This law can be stated in two equivalent forms:

The integral form, in which one considers the amount of energy flowing into or out of a body as a whole.
The differential form, in which one considers the local flows or fluxes of energy.
Differential form
In the differential formulation of Fourier's law, the fundamental quantity is the local heat flux 






ϕ

q


→




{\displaystyle {\overrightarrow {\phi _{q}}}}

. This is the amount of energy flowing through an infinitesimal oriented surface per unit of time. The length of 






ϕ

q


→




{\displaystyle {\overrightarrow {\phi _{q}}}}

 is given by the amount of energy per unit of time, and the direction is given by the vector perpendicular to the surface. As a vector equation, this leads to:








ϕ

q


→


=
−
k


∇
→


T


{\displaystyle {\overrightarrow {\phi _{q}}}=-k{\overrightarrow {\nabla }}T}


where (showing the terms in SI units)








ϕ

q


→




{\displaystyle {\overrightarrow {\phi _{q}}}}

 is the local heat flux, in Watts per square meter (W•m−2),




k


{\displaystyle k}

 is the material's thermal conductivity, in Watts per meter per degree Kelvin (W•m−1•K−1),




∇
T


{\displaystyle \nabla T}

 is the temperature gradient, in degrees Kelvin per meter (K•m−1)
Note that the thermal conductivity of a material generally varies with temperature, but the variation can be small over a significant range of temperatures for some common materials. In anisotropic materials, the thermal conductivity typically varies with direction; in this case, 



k


{\displaystyle k}

 is a tensor.

Integral form
By integrating the differential form over the material's total surface 



S


{\displaystyle S}

, we arrive at the integral form of Fourier's law:








∂
Q


∂
t



=
−
k

∮

S





∇
→


T
⋅




d
S

→





{\displaystyle {\frac {\partial Q}{\partial t}}=-k\oint _{S}{{\overrightarrow {\nabla }}T\cdot \,{\overrightarrow {dS}}}}


where (showing the terms in SI units)








∂
 Q


∂
t





{\displaystyle {\frac {\partial Q}{\partial t}}}

 is the amount of heat transferred per unit time, in Watts (W) or Joules per second (J•s-1),




S


{\displaystyle S}

 is the surface through which the heat is flowing, in square meters (m2).
 Diagram of linear heat flow, from a hotter surface (red) to a cooler surface (blue).
Consider a simple linear situation (see diagram), where there is uniform temperature across equally sized end surfaces and the sides are perfectly insulated. In such a case, integration of the above differential equation gives the heat flow rate between the end surfaces as:








Δ
Q


Δ
t



=
−
k
A



Δ
T


Δ
x





{\displaystyle {\frac {\Delta Q}{\Delta t}}=-kA{\frac {\Delta T}{\Delta x}}}


where

A is the cross-sectional surface area,




Δ
T


{\displaystyle \Delta T}

 is the temperature difference between the ends,




Δ
x


{\displaystyle \Delta x}

 is the distance between the ends.
This law forms the basis for derivation of the heat equation.
The R-value is the unit for heat resistance, the reciprocal of heat conductance.
Ohm's law is the electrical analog of Fourier's law.

Conductance and resistance
The conductance (



U


{\displaystyle U}

) can be defined as:





U
=


k

Δ
x



,



{\displaystyle U={\frac {k}{\Delta x}},\quad }


where the units for 



U


{\displaystyle U}

 are given in W/(m2 K).
Thus, Fourier's law can also be stated as:





Q
=
U
A

Δ
T
.


{\displaystyle Q=UA\,\Delta T.}


The reciprocal of conductance is resistance, R. It is given by:





R
=


1
U


=



A

Δ
T

Q


,



{\displaystyle R={\frac {1}{U}}={\frac {A\,\Delta T}{Q}},\quad }


Resistance is additive when several conducting layers lie between the hot and cool regions, because A and Q are the same for all layers. In a multilayer partition, the total conductance is related to the conductance of its layers by the following equation:







1
U


=


1

U

1




+


1

U

2




+


1

U

3




+
⋯


{\displaystyle {\frac {1}{U}}={\frac {1}{U_{1}}}+{\frac {1}{U_{2}}}+{\frac {1}{U_{3}}}+\cdots }


So, when dealing with a multilayer partition, the following formula is usually used:





Q
=



A

Δ
T






Δ

1


x


K

1




+




Δ

2


x


K

2




+




Δ

3


x


K

3




+
⋯



.


{\displaystyle Q={\frac {A\,\Delta T}{{\frac {\Delta _{1}x}{K_{1}}}+{\frac {\Delta _{2}x}{K_{2}}}+{\frac {\Delta _{3}x}{K_{3}}}+\cdots }}.}


When heat is being conducted from one fluid to another through a barrier, it is sometimes important to consider the conductance of the thin film of fluid which remains stationary next to the barrier. This thin film of fluid is difficult to quantify, its characteristics depending upon complex conditions of turbulence and viscosity, but when dealing with thin high-conductance barriers it can sometimes be quite significant.

Intensive-property representation
The previous conductance equations written in terms of extensive properties, can be reformulated in terms of intensive properties.
Ideally, the formulae for conductance should produce a quantity with dimensions independent of distance, like Ohm's Law for electrical resistance: 



R
=
V

/

I




{\displaystyle R=V/I\,\!}

, and conductance: 



G
=
I

/

V




{\displaystyle G=I/V\,\!}

.
From the electrical formula: 



R
=
ρ
x

/

A




{\displaystyle R=\rho x/A\,\!}

, where ρ is resistivity, x = length, A cross sectional area, we have 



G
=
k
A

/

x




{\displaystyle G=kA/x\,\!}

, where G is conductance, k is conductivity, x = length, A cross sectional area.
For Heat,





U
=



k
A


Δ
x



,



{\displaystyle U={\frac {kA}{\Delta x}},\quad }


where U is the conductance.
Fourier's law can also be stated as:





Q
=
U

Δ
T



{\displaystyle Q=U\,\Delta T\quad }


analogous to Ohm's law: 



I
=
V

/

R




{\displaystyle I=V/R\,\!}

 or 



I
=
V
G
.




{\displaystyle I=VG.\,\!}


The reciprocal of conductance is resistance, R, given by:





R
=




Δ
T

Q


,



{\displaystyle R={\frac {\,\Delta T}{Q}},\quad }


analogous to Ohm's law: 



R
=
V

/

I
.




{\displaystyle R=V/I.\,\!}


The sum of conductances in series is still correct.

See also
Heat
Thermal conductivity
Convection
Thermal radiation
ReferencesISBN links support NWE through referral fees
Baierlein, Ralph. 2003. Thermal Physics. Cambridge: Cambridge University Press. ISBN 0521658381
Halliday, David, Robert Resnick, and Jearl Walker. 1997. Fundamentals of Physics, 5th ed. New York: Wiley. ISBN 0471105589
Serway, Raymond A., and John W. Jewett. 2004. Physics for Scientists and Engineers. Belmont, CA: Thomson-Brooks/Cole. ISBN 0534408427
Srivastava, G.P. 1990. The Physics of Phonons. Bristol: A. Hilger. ISBN 0852741537
Young, Hugh D., and Roger A. Freedman. 2003. Physics for Scientists and Engineers. San Fransisco, CA: Pearson. ISBN 080538684X
External links
All links retrieved December 12, 2017.

Newton's Law of Cooling Wolfram Demonstrations Project.

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