National Physical Laboratory

Modelling Heat Transfer in Polymer Processing

 


Analysis for heat transfer coefficients across polymer-steel interfaces

Modelling Heat Transfer in Polymer Processing

Figure 3: Single layer structure
Modelling Heat Transfer in Polymer Processing



Figure 4: Three layer sandwich structure

 

For a single specimen between plates, Figure 3, the thermal resistance R1is given as the sum of thermal resistances of the two interfaces and the sandwiched layer plus a contribution due to the instrument construction itself rinst:

Modelling Heat Transfer in Polymer ProcessingEquation 8

whereModelling Heat Transfer in Polymer Processing is the thermal resistance of the interface (denoted by the superscript h) between the metal and polymer (denoted by the subscript m-p) and Modelling Heat Transfer in Polymer Processing is the thermal resistance of the polymer specimen (denoted by the subscript p1) due to its thermal conductivity and thickness (denoted by the superscript΢΢). The term rinst is a factor for the thermal resistance of the instrument due to the interfaces and layers within the instrument itself.

Similarly for a polymer specimen of a different thickness, indicated by the use of the subscript p2:

Modelling Heat Transfer in Polymer ProcessingEquation 9

For the three-layer system, Figure 4, the total thermal resistance is similarly given by:

Modelling Heat Transfer in Polymer ProcessingEquation 10

whereModelling Heat Transfer in Polymer Processing is the resistance of the metal layer. In order to express the thermal resistances of the component layers and interfaces in terms of measurable or determinable quantities, taking the difference of Equations 8 and 9 yields:

Modelling Heat Transfer in Polymer ProcessingEquation 11

or, using Equation 4:

Modelling Heat Transfer in Polymer ProcessingEquation 12

Assuming equal thermal conductivities of the two specimens, i.e. p = p1 = p2, as they were made of the same material, then:

Modelling Heat Transfer in Polymer ProcessingEquation 13

Thus the thermal resistances of the polymer layers are given by:

Modelling Heat Transfer in Polymer ProcessingEquation 14

and:

Modelling Heat Transfer in Polymer ProcessingEquation 15

Similarly, the thermal resistance of the metal layers is given by:

Modelling Heat Transfer in Polymer ProcessingEquation 16

Rearranging equation 10 yields:

Modelling Heat Transfer in Polymer ProcessingEquation 17

The thermal resistance of the instrument, rinst, without specimen and without the plate-plate interface, Modelling Heat Transfer in Polymer Processingcan be determined from measurements of the metal plate specimen. For no specimen:

Modelling Heat Transfer in Polymer ProcessingEquation 18

For the metal plate specimen:

Modelling Heat Transfer in Polymer ProcessingEquation 19

Thus from the difference in equations 18 and 19 the thermal resistance of the metal-metal interface is given by:

Modelling Heat Transfer in Polymer ProcessingEquation 20

and can be determined, given values for the thickness and thermal conductivity of the metal plate. Thus using Equations 18 and 20 the thermal resistance correction factor rinstcan be determined:

Modelling Heat Transfer in Polymer ProcessingEquation 21

Thus by substituting using the above, Equation 17 becomes:

Modelling Heat Transfer in Polymer ProcessingEquation 22 

thereby enabling the heat transfer coefficient of the polymer-metal interface to be determined.


For more information, please contact Angela Dawson

Last Updated: 25 Feb 2013
Created: 23 Aug 2007