+++ title = "Heat Transfer" author = ["Dehaeze Thomas"] draft = false +++ Tags : ## Conduction (diffusion) {#conduction--diffusion} The _conduction_ corresponds to the heat transfer \\(P\\) (in watt) through molecular agitation within a material and is specified with: \\[ P = \frac{\lambda \cdot A \cdot \Delta T}{L} \quad [W] \\] with: - \\(\lambda\\) the thermal conductivity in \\([W/m \cdot K]\\) - \\(A\\) the surface area in \\([m^2]\\) - \\(\Delta T\\) the temperature difference in \\([K]\\) - \\(L\\) the length of the barrier in \\([m]\\) ## Convection {#convection} The convection corresponds to the heat transfer through flow of a fluid. It can be either _natural_ or _forced_. The _forced convection_ \\(P\\) (in watt) can be described with: \\[ P = h A (T\_0 - T\_f) \quad [W] \\] with: - \\(h\\) the convection heat transfer coefficient in \\([W/m^2 \cdot K]\\). \\(h \approx 10.5 - v + 10\sqrt{v}\\) with \\(v\\) the velocity of the object through the fluid in \\([m/s]\\) - \\(A\\) the surface area in \\([m^2]\\) - \\(T\_0\\) the temperature of the object in \\([K]\\) - \\(T\_f\\) the temperature of the convecting fluid in \\([K]\\) Note that clean-room air flow should be considered as forced convection. ## Radiation {#radiation} _Radiation_ corresponds to the heat transfer \\(P\\) (in watt) through the emission of electromagnetic waves from the emitter to its surroundings is: \\[ P = \epsilon \cdot \sigma \cdot A \cdot (T\_r^4 - T\_s^4) \\] with: - \\(\epsilon\\) the emissivity which corresponds to the ability of a surface to emit energy through radiation relative to a black body surface at equal temperature. It is between 0 (no emissivity) and 1 (maximum emissivity) - \\(\sigma\\) the Stefan-Boltzmann constant: \\(\sigma = 5.67 \cdot 10^{-8} \\, \frac{W}{m^2 K^4}\\) - \\(A\\) the surface in \\([m^2]\\) - \\(T\_r\\) the temperature of the emitter in \\([K]\\) - \\(T\_s\\) the temperature of the surrounding in \\([K]\\) The emissivity of materials highly depend on the surface finish (the more polished, the lower the emissivity). Some examples are given in .
Table 1: Some examples of emissivity (specified at 25 degrees)
| Substance | Emissivity | |----------------------------|------------| | Silver (polished) | 0.005 | | Silver (oxidized) | 0.04 | | Stainless Steel (polished) | 0.02 | | Aluminium (polished) | 0.02 | | Aluminium (oxidized) | 0.2 | | Aluminium (anodized) | 0.9 | | Copper (polished) | 0.03 | | Copper (oxidized) | 0.87 |
Let's take a polished aluminum plate (20 by 20 cm) at 125K (temperature of zero thermal expansion coefficient of silicon) surrounded by elements are 25 degrees (300 K): \\[ P = \epsilon \cdot \sigma \cdot A \cdot (T\_r^4 - T\_s^4) = 0.36\\, J \\]
## Heat {#heat} The _heat_ \\(Q\\) (in Joules) corresponds to the energy necessary to change the temperature of the mass with a certain material specific heat capacity: \\[ Q = m \cdot c \cdot \Delta T \\] with: - \\(m\\) the mass in \\([kg]\\) - \\(c\\) the specific heat capacity in \\([J/kg \cdot K]\\) - \\(\Delta T\\) the temperature different \\([K]\\)
Let's compute the heat (i.e. energy) necessary to increase a 1kg granite by 1 degree. The specific heat capacity of granite is \\(c = 790\\,[J/kg\cdot K]\\). The required heat is then: \\[ Q = m\cdot c \cdot \Delta T = 790 \\,J \\]
Table 2: Some examples of specific heat capacity
| Substance | Specific heat capacity [J/kg.K] | |---------------------|---------------------------------| | Air | 1012 | | Aluminium | 897 | | Copper | 385 | | Granite | 790 | | Steel | 466 | | Water at 25 degrees | 4182 | ## Heat flow {#heat-flow} The heat flow \\(P\\) (in watt) is the derivative of the heat: \\[ P = \cdot{Q} = \frac{dQ}{dt} = \frac{dT}{R\_T} = C\_T \cdot dT \\] with: - \\(Q\\) the heat in [W] - \\(R\_T\\) the thermal resistance in \\([K/W]\\) - \\(C\_T\\) the thermal conductance in \\([W/K]\\) ## Bibliography {#bibliography}