4) An infinite bar with thermal conductivity of k and thickness L is insulated on the...
3/5 25 pts.J A slab of thickness L, made of material with constant thermal conductivity k, is undergoing a 1-D, steady heat transfer. Its boundary surface at x 0 is insulated while the boundary surface at x= 1 is kept at constant temperature T= oc. Heat energy is generated within the slab at a rate of 2. qx)o cos(rx/2L) is the energy generation rate per unit volume (Wm) at x= 0. where qo a. Develop an expression for the steady-state...
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...
Problem 2: Consider a large plane slab of semi-thickness L = 0.3 m, thermal conductivity k = 2.5 W/m K and surface area A = 20.0 m². Both sides of the slab is maintained at a constant wall temperature of 358°K while it is subjected to a uniform but constant heat flux of 950.0 W/m2 Evaluate the temperature distribution/profile within the wall. Calculate the heat flux and temperature at location x = 0.1m. Problem 3: Consider a 10.0 m long...
Consider a rectangular bar of thermal conductivity k W/m-K and total length 2L, as shown in the figure, is connected to a hot surface that is at a temperature T1. The connection between the bar and the surface is imperfect and results in a thermal contact resistance of R’’ m2-K/W. The width of the rod into the depth of the paper is W meters and the thickness of the rod is t meters. The first section of the rod of...
ent material has the thermal conductivity k and thickness L. The temperature the material is of the form: distribution along the x-direction, T(x) in + Bx2 + C, where A, a, B, and C are constants. The irradiation is fully the material and can be characterized by a uniform volumetric heat generation, W/m3). Assuming 1D steady-state conduction and constant properties. xpressions for the conduction heat fluxes (alx) at the top and bottom surfaces; absorbed by (4 points) (b) Derive an...
Please show all work for review! 5) Consider problem 4. Instead of an insulated left surface, a known heat flux is imposed on it. Everything else remains the same. • Stating all the assumptions clearly, derive expression for temperature profile with the rod in the steady state. (25 points) • Bonus problem: If possible, draw temperature profile. (10 points) 9 gen air
A plane wall of thickness L has constant thermal conductivity, k, uniform generation throughout, q, and is insulated on one side, at x-0. Only the outer surface temperature (Ts) is known. (a) Derive an equation describing the steady-state wall temperature at any point (x), when given the outer wall surface temperature, Tsi. (b) If L-15 cm, k: 3.4 W/m"K, q-10 kW/m3, and Ts1-300 K, what is the steady-state temperature at x - 6 cm (in K)? S1
A very long rod of 5-mm diameter and uniform thermal conductivity k = 25 W/m-K is subjected to a heat treatment process. The center, 30-mm-long portion of the rod within the induction heating coil experiences uniform volumetric heat generation of 7.5 x 106 W/m3. The unheated portions of the rod, which protrude from the heating coil on either side, experience convection with the ambient air at T∞ = 20 °C and h = 10 W/m2K. Assume that there is no convection...
Reviewer Score 3. A plane wall of thickness 0.12m and thermal conductivity 40W/m K having uniform volumetric energy generation of 0.4MW/m3 is insulated on one side, while the other side is exposed to a fluid at 52 C. The convection heat transfer coefficient between the wall and the fluid is 400W/m2-K. Determine the (20 scores) maximum temperature in the wall. 4. r,rod OA rotates with uniform o o. At the moment, AB- 6r Signatory Score leration of block B at...
Problem 1. (75') This is a 1-D steady state problem. Only object A generates heat per unit volume of dA 2 x 106W/m3. The left surface of A is insulated and the right surface of B is exposed to a fluid. Temperature of the fluid is To 300 K. The convective heat transfer coefficient is h 1000 W/m2/K Thermal conductivity of A is kA 30 W/m/K, and B is k 20 W/m/K Thickness of each object is: IA-30 mm, 1':...