In: Mechanical Engineering
Elementary Partial Differential Equations
Heat flow in a circular cylinder.
Consider a strand of heat-conducting material, homoge- neous with heat capacity c, thermal conductivity κ, and surface heat transfer coefficient μ. The strand is a right circular cylinder of radius R and height H. Unless otherwise indicated below, assume that no heat is being generated or destroyed inside the strand. For each of the following scenarios, set up the IBVP for the temperature distribution u in the strand. In each case, reduce the spatial dimension of the problem as far as possible, identify the independent variables (time t and a subset of the cylindrical coordinates r, θ, z), write all equations explicitly in terms of those variables, and indicate where exactly the equations are to hold. Also, whenever possible, set up the corresponding steady-state problem. If it reduces to an ODE, solve the steady-state problem and graph the solution.
(a) While the lateral surface and the top of the cylinder are
perfectly insulated, the bottom is maintained at a constant
temperature Tbot. The initial temperature distribution is a
function f(z).(b) Same as in (a), except that the temperature at
the bottom changes, at a constant rate and over a period of τ units
of time, from an initial constant temperature T0 to a final
constant temperature T∞, and is maintained at that final value ever
after.
(c) Same as in (a), except that heat is exchanged across the top
end, according to Newton’s law of cooling, with an external medium
at constant temperature Text.
(d) Same as in (c), except that Newton’s law applies also on the
lateral surface of the cylinder. (e) Same as in (d), except that
top and bottom are perfectly insulated and the initial
temperature
distribution is a function f(r).
(f) Same as in (e), except that the initial temperature
distribution is a function f(r,θ) and that heat is generated inside
the cylinder (for example, via Joule heating) at a constant rate G
(heat units per unit time and unit volume).
(g) Same as in (f), except that heat is added also through the
bottom of the cylinder, at a constant rate Q (heat units per unit
time and unit area).