3.68 Consider o conduction in a plane com- posite wall. The outer surfaces are exposed to...
Consider the 1D plan composite wall shown in the figure made of three regions.Only in region B, there is a uniform thermal energy generation qB. The left side of wall A is insulated, and the right side of wall B is exposed to convection. There is thermal resistance between region B and region C. The numerical values are given below. Problem 1. Consider the 1D plan composite wall shown in the figure made of three regions. Only in region B,...
A plane wall of thickness 2L= 30 mm and thermal conductivity k= 3 W/m·K experiences uniform volumetric heat generation at a rate q˙, while convection heat transfer occurs at both of its surfaces (x=-L, +L), each of which is exposed to a fluid of temperature ∞T∞= 20°C. Under steady-state conditions, the temperature distribution in the wall is of the form T(x)=a+bx+cx2 where a= 82.0°C, b= -210°C/m, c= -2 × 104°C/m2, and x is in meters. The origin of the x-coordinate...
Problem 3. A plane wall of thickness 2L = 40 mm and thermal conductivity k = 5 W/m.K experiences uniform volumetric heat generation at a rate ġ, while convection heat transfer occurs at both of its surfaces (x = -1, + L), each of which is exposed to a fluid of temperature Too = 20 °C. Under steady-state conditions, the temperature distribution in the wall is of the form T(x) = a + bx + cx? where a = 82.0°C,...
A plane wall with thermal conductivity of k, is insulated on one side and is exposed to ambient air at To and convection coefficient of h, on the other side. A heat source in the 3) wall is generating a uniform heat rate per unit volume of For one-dimensional steady-state conduction in the wall, derive a proper differential equation for the temperature by either using the heat equations or doing the energy balance. Identify proper boundary conditions and find the...
The heat generation rate in a plane wall of 0.24 m thickness is 0.4 MW/m3 . The wall is exposed on both sides to convection at 30°C. (a) Determine and compare the maximum temperatures for k = 25, k = 50, k = 200 and k = 410 W/mK assuming h = 250 W/m2K. (b) Determine and compare the maximum temperature for h = 50, 250, 500 and 1000 W/m2K with k = 25 W/mK.
The schematic diagram of a chamber wall with the known properties is Plane A: kn -5 Wim K, uniform heat generation,4 2000 wim' shown below. Plane B: kn 20 W/m-K, no heat generation Inside air: 40 °C, h,-10 Wm2 K; Outside air: 20 °C, ho= 5 w/m2 K. A tape heater is placed on the outer wall to provide a uniform heat flux of q, to prevent any loss from the wall. Assuming steady-state, ID conduction along x-direction (a) Determine...
A planar wall is composed of two materials, wall 1 has a uniform heat generation of 1.5 x 106 W/m3 and a thermal conductivity of 60 Wm.Κ. Wall 2 has no heat generation and thermal resistance of 150 W/m.K. The inner surface of Wall 1 is well insulated, while the outer surface of Wall 2 is exposed to 30°C fluld. The temperature of the wall surface exposed to the fluid is most nearly 00 heat flow fluid at 30°C h...
Heat is uniformly generated at the rate of 2x 10W/m* in a wall of thermal conductivity 25 W/m-K and thickness 60 mm. The wall is exposed to convection on both sides, with different heat transfer coefficients and temperatures as shown. There are straight rectangular fins on the right-hand side of the wall, with dimensions as shown (L =20 mm) and thermal conductivity of 250 W/m-K. What is the maximum temperature that will occur in the wall? L tt-2 mm k=25...
The temperature distribution across a wall 0.2 m thick at a certain instant of time is T(x) = a + bx + cxº, where T is in degrees Celsius and x is in meters, a = 200°C, b = -190°c/m, and c = 30°C/m2. The wall has a thermal conductivity of 1 W/m.k. (a) On a unit surface area basis, determine the rate of heat transfer into and out of the wall and the rate of change of energy stored...
Problem Wall with Strip Heater The air inside a chamber is measured to be 50C and used to convectively heat a wall (h 20 w/m2 K). The wall (thermal conductivity of 4 W/m K) is 200 mm thick and has a uniform heat generation of 1000 W/m2. To prevent any heat generated within the wall from being lost to the outside of the chamber a very thin electrical strip heater is placed on the outer wall to provide a uniform...