In heat transfer, if we neglect the lumped capacity system approach and use the heat diffusion equation to solve transient conduction problems, why do they consider infinite and semi infinite geometries?
and what are the differences between infinite and semi infinite for spheres/plates or cylinders?
Infinite Body: A plate whose thickness is small relative to the other dimensions can be modeled as an infinitely large plate, except very near the outer edges. But the edge effects on large bodies are usually negligible.
Thus, a large plane wall such as the wall of a house can be modeled as an infinitely large wall for heat transfer purposes.
A long cylinder whose diameter is small relative to its length can be analyzed as an infinitely long cylinder.
Semi Infinite Body: This idealized body is used to indicate that the temperature change in the part of the body in which we are interested (the region close to the surface) is due to the thermal conditions on a single surface.
The earth, for example, can be considered to be a semi-infinite medium in determining the variation of temperature near its surface.
Also, a thick wall can be modeled as a semi-infinite medium if all we are interested in is the variation of temperature in the region near one of the surfaces, and the other surface is too far to have any impact on the region of interest during the time of observation.
In heat transfer, if we neglect the lumped capacity system approach and use the heat diffusion eq...
please show work
Transient heat transfer in a lumped system is a linear function as showing in equation below: In 7 ) =- kt • • t is the time recorded (column A) in the excel data sheet attached T is the temperature of Rod1 in the cooling process as shown in the Temp 01 column (column B) of the excel data sheet attached Ti is the initial temperature at time t = 0. Ti=60°C To is the average room...
roblem 5: When can we neglect axial conduction? Consider steady, fully developed, laminar flow inside a round tube, with the energy equation: The two terms on the right hand side represent conduction effects in the radial and axial directions, respectively. In convection analysis we usually neglect the axial conduction term, resulting in Eq. 8.48. Let's investigate the suitability of this approximation, by comparing the relative magnitudes of those two terms for a tube flow with constant wall temperature The full...
For this problem we consider a radiant heat transfer system commonly found in space/room heaters. The input to the plant is (heat) energy q(Watts) and the output of the system is its temperature (K). The ODE that describes the system is given below Where, 8a is the ambient temperature (27°C), b-91.6 is an input constant, m 0.1 kg is the mass, C 420 J/Kg.K is the specific heat of the heater and a-AEo. A0.25 m2 is the surface area of...
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For this problem we consider a radiant heat transfer system commonly found in space/room hoaters. Ihe ipu io the plani is (hcat) eey q(Wais) and he ouipui of the sysiem is is temperature (K). The ODE that describes the system is given below where, ền is the ambient temperature (27°C), b:91.6 is an input constant, m 0.1 kg is the mass, C-420 J/Kg. K is the specific heat of the heater and a-Acơ. A-0.25 m2 is the surface area of...
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