The Heat Equation — Question 1

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Question 1

A stationary rod has cross-sectional area A(x)>0A(x)>0, conductivity k(x)>0k(x)>0 and volumetric heat capacity C(x)>0C(x)>0. Temperature u(x,t)u(x,t) is uniform across each section; the lateral surface is insulated. A volumetric source s(x,t)s(x,t) has units W/m3\mathrm{W/m^3}. Define signed heat power toward increasing xx by Q=−kAuxQ=-kA u_x, in watts. All coefficients are independent of time.

Tasks

  1. Apply energy conservation to an arbitrary interval [a,b][a,b] and derive the local heat equation. State the units of every term in the balance.

  2. Expand the spatial derivative and identify the diffusivity. Explain when the equation reduces to ut=αuxxu_t=\alpha u_{xx}.

  3. After nondimensionalization, take 0<x<10<x<1, A=exA=e^x, k=C=1k=C=1, s=0s=0 and an instantaneous profile u=xu=x. Find QQ, the storage rate AutAu_t and utu_t. Sketch the first two quantities.

  4. Explain why this linear temperature profile need not be steady, even though its curvature is zero. Distinguish heat flux per area from total heat power.

Original worksheet page 1: question and worked solution for 9-1-001
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Question 1 – Solution

Strategy. Balance total heat power before dividing by the local cross-sectional area.

Step 1: Derive the conservation law. The stored thermal energy relative to a fixed reference has time derivative ∫abCAutdx\int_a^b CAu_t\,dx. Inflow minus outflow plus generation gives ∫abCAutdx=Q(a,t)−Q(b,t)+∫abAsdx.\int_a^b CAu_t\,dx=Q(a,t)-Q(b,t)+\int_a^b As\,dx. Since this holds on every interval, with Fourier’s law it yields CAut=−Qx+As=(kAux)x+As.\boxed{CAu_t=-Q_x+As=(kAu_x)_x+As.} Each local term has units W/m\mathrm{W/m}: CC is J/(m3K)\mathrm{J/(m^3K)}, AA is m2\mathrm{m^2} and utu_t is K/s\mathrm{K/s}. Each integrated term, including Q(a)−Q(b)Q(a)-Q(b), is in watts.

Step 2: Identify the geometric contribution. Dividing by CACA gives ut=kCuxx+(kA)′CAux+sC.\boxed{u_t=\frac{k}{C}u_{xx}+\frac{(kA)'}{CA}u_x+\frac{s}{C}.} The diffusivity k/Ck/C has units m2/s\mathrm{m^2/s}. For a homogeneous constant-area rod without a source, this is ut=αuxxu_t=\alpha u_{xx} with constant α=k/C\alpha=k/C. More generally, the first-derivative term vanishes when kAkA is constant; constant diffusivity additionally requires k/Ck/C constant.

Step 3: Evaluate the nondimensional example. Here ux=1u_x=1 and uxx=0u_{xx}=0, but Q(x)=−ex,Aut=−Qx=ex,ut=1.\boxed{Q(x)=-e^x,\qquad Au_t=-Q_x=e^x,\qquad u_t=1.} The signed power is negative because heat moves toward decreasing temperature, which here is the negative xx direction. Its magnitude increases toward the larger cross section.

Step 4: Interpret the nonzero storage. Flux per unit area is q=−kux=−1q=-ku_x=-1, constant in this example. Total power is Q=Aq=−exQ=Aq=-e^x, which is not constant. More heat enters a small interval through its larger right face than leaves through its smaller left face, so energy accumulates. Zero curvature alone is a steady-state test only under the coefficient and geometry assumptions that remove the extra term.

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Original worksheet page 2: question and worked solution for 9-1-001

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