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{{Language_sel|LANG=ger|ARTIKEL=Thermische Leitfähigkeit}}
{{PSM_Infobox}}
Thermal conductivity; Thermal diffusivity
__FORCETOC__

==Definition==

From the physical point of view, a fundamental differentiation must be made between heat conductivity, which describes the transport of energy in a material, and temperature conductivity or thermal diffusivity.

The temperature conductivity ''a'' is that velocity at which temperature fields change in a material, and so describes the non-stationary thermal conduction. It is determined by the thermal conductivity ''λ'', the specific thermal capacity ''c''p and by the mass [[Density | density]] ''ϱ''. The temperature conductivity is defined by

{|
|-
|width="20px"|
|width="500px" | <math> a = \frac {\lambda} { \varrho ~ c_p} </math>
|(1)
|}

==Derivation==

Given are two containers with the temperatures ''T''1 and ''T''2 and between them a transition medium in which the temperature gradient is present ('''Fig. 1'''). The heat flow thereby goes in the direction indicated by the arrow in the picture. The heat quantity ''Q''1 with the temperature ''T''1 flows in the transition medium to the container with the heat quantity ''Q''2 of the lower temperature ''T''2. This means that heat is transported through the transition medium. The heat flow has the form

{|
|-
|width="20px"|
|width="500px" | <math> \dot Q = m \cdot c_p \cdot \frac{\partial T}{\partial t} </math>
|(2)
|}

Considering now the property of the thermal conductivity of the transition medium, then (''A'' is the heat transfer area) also applies:

{|
|-
|width="20px"|
|width="500px" | <math> \dot{Q} = - \lambda \cdot A ~ \frac{\partial T}{\partial x} </math>
|(3)
|}

[[file:Thermische_Leitfaehigkeit1.JPG|400px]]
{|
|- valign="top"
|width="80px"|'''Figure 1''':
|width="600px" |Schematic illustration of the temperature gradient between the containers with temperatures ''T''1 and ''T''2 with the transition medium
|}

The equation of Eq. (2) and Eq. (3) does not yet yield the temperature conductivity. For this, the general form of these equations must be used:

Instead of the heat flow, the heat flow density vector '''''j''''' is considered, which is the heat flow through a cross-sectional area that can be calculated with the 1st Fourier's law according to Eq. (4).

{|
|-
|width="20px"|
|width="500px" | <math>{\boldsymbol{j} = -\lambda \cdot \mathrm{grad}~T}</math>.
|(4)
|}

The heat flow per volume which the container loses with ''T''1 is according to Eq. (2)

{|
|-
|width="20px"|
|width="500px" | <math>{\dot{q} = \varrho \cdot c_{p} \cdot \frac{\partial T}{\partial t}}</math>.
|(5)
|}

According to the continuity equation, the following applies to heat transport

{|
|-
|width="20px"|
|width="500px" | <math>{\frac{\partial q} {\partial t} = - \mathrm{div} \ \boldsymbol{j}}</math>.
|(6)
|}

After entering Eq. (4) and Eq. (5) into Eq. (6), the continuity equation obtains the form

{|
|-
|width="20px"|
|width="500px" | <math>{\frac{\partial T} {\partial t} = \frac{\lambda} {\rho \cdot c_{p}} \cdot \frac{\partial^{2} T} {\partial x^{2}}}</math>.
|(7)
|}

with which again Eq. (1) is obtained (2nd Fourier's law).

==Practical Aspects==

The temperature conductivity is a property of the respective material and is listed here in '''Table 1''' for a selection of [[Thermoplastic Material | thermoplastics]]. This characteristic value describes the non-stationary heat transport. For example, it is important that the handles of the vessels containing the hot liquid have a lower thermal conductivity in order to reduce the risk of injury when handling them. Furthermore, this parameter is used for the fire safety of materials and the assessment of heat storage.

'''Table 1''': Temperature conductivity of some selected thermoplastics
{| border="1px" style="border-collapse:collapse"
!! style="width:200px; background:#DCDCDC" | Material
!! style="width:200px; background:#DCDCDC" | Temperature conductivity α (mm2/s)
|-
|style="text-align:center" |PVC-U
|style="text-align:center" | 0.122
|-
|style="text-align:center" |PVC-P
|style="text-align:center" | 0.145
|-
|style="text-align:center" |PE-HD
|style="text-align:center" | 0.227
|-
|style="text-align:center" |PP
|style="text-align:center" | 0.145
|-
|style="text-align:center" |PS
|style="text-align:center" | 0.115
|-
|style="text-align:center" |POM
|style="text-align:center" | 0.161
|}

==Importance==

Since the temperature conductivity indicates the velocity at which a temperature spreads through a medium, it is fundamental for studies on heat transport in media. This characteristic value is used in the building's industry, e.g. for the thermal insulation of buildings. Moreover, temperature conductivity is easier and more accurate to measure than thermal conductivity, therefore thermal conductivity is often determined indirectly via temperature conductivity.

'''References'''

{|
|-valign="top"
|[1]
|Landau, L. D., Lifschitz, E. M.: Hydrodynamik – Lehrbuch der theoretischen Physik. Akademie-Verlag, Berlin (1991)
|-valign="top"
|[2]
|https://www.linseis.com: Wärmeleitfähigkeit/Temperaturleitfähigkeit (access: 01.04.2025)
|-valign="top"
|[3]
|Marek, R., Nitsche, K.: Praxis der Wärmeübertragung. Grundlagen – Anwendungen – Übungsaufgaben. 2., aktualisierte und erweiterte Auflage, Fachbuchverlag Leipzig im Carl Hanser Verlag, München (2010) (ISBN 978-3-446-42510-1; see [[AMK-Büchersammlung|AMK-Library]] under I 43)
|-valign="top"
|[4]
|Paus, H.: Physik in Experimenten und Beispielen. Carl Hanser Munich Vienna (1995), p. 580 f. (ISBN 3-446-17371-4; see [[AMK-Büchersammlung|AMK-Library]] under I 4)
|-valign="top"
|[5]
|Domininghaus, H., Elsner, P., Eyerer, P., Hirth, T.: Kunststoffe. Eigenschaften und Anwendungen. 8. Auflage, Springer, Heidelberg (2012), p. 304 (ISBN 978-3-642-16172-8 ; see [[AMK-Büchersammlung|AMK-Library]] under G 41)
|}

'''Standards Reference'''

• ISO 22007-2 (2022-06): Plastics — Determination of Thermal Conductivity and Thermal Diffusivity — Part 2: Transient Plane Heat Source (Hot Disc) Method

[[Category:Thermoanalytical Methods]]

Temperature Conductivity - Revision history