*Enlace a Spanish version
Materials: [ Cód.: HeatExchModelEDPsimulayOrdenRedENGLISH.mlx ] [ PDF ]
This video compares the exact solution of the partial differential equation of a
tubular heater (details of the PDE modelling in video [
Erratum: there is an error in the video at line 5 of code where a power unit conversion factor from W to kW is wrongly propagated. The MLX and PDF have been corrected, changing the heat transfer constant so that the numerical results of the video remain correct.
Once the typo has been clarified, let’s continue with the description.
Actually, an approximation of the exponential in the Laplace transfer functions via a certain
parameter ,
first order models are derived, which, luckily, are identical to those obtained based
on physical insight with a non-uniform longitudinal temperature profile in video [
A particular case
renders the perfectly-stirred first-order approximation in video [
Additionally, Pade approximations of the delay are compared to the above models (first and third order Pade approximations, via Matlab’s pade).
Comparisons are made in both steady state (DC gain) and transient response to steps (in inlet temperature and in resistor heating power).
A few of these low-order approximations may be cascade-connected to
yield finite-element setups, discussed in other materials, such as the video
[
*Link to my [ whole collection] of videos in English. Link to larger [ Colección completa] in Spanish.