Steady Conduction

Steady conduction is heat transfer through a solid (or stagnant fluid) with temperature field independent of time. Fourier’s law
q=kAdTdxq = -kA\frac{dT}{dx}
relates heat rate to the temperature gradient. Plane walls, cylinders, and spheres are solved with thermal resistances
RthR_{\mathrm{th}}
in series/parallel networks (RC Sachdeva / GATE HT).

Key formulas & points

Skim these first — then read the full notes below.

  • Fourier law (1-D): qx=kAdTdxq_x = -kA\frac{dT}{dx} — heat flows from hot to cold; kk in W/(mK)\mathrm{W/(m\cdot K)}.
  • Plane wall (constant kk): q=kA(T1T2)Lq = \frac{kA(T_1-T_2)}{L}, Rwall=LkAR_{\mathrm{wall}}=\frac{L}{kA}.
  • Cylinder (radial): q=2πkL(T1T2)ln(r2/r1)q = \frac{2\pi k L(T_1-T_2)}{\ln(r_2/r_1)}, Rcyl=ln(r2/r1)2πkLR_{\mathrm{cyl}}=\frac{\ln(r_2/r_1)}{2\pi k L}.
  • Sphere (radial): q=4πk(T1T2)1/r11/r2q = \frac{4\pi k(T_1-T_2)}{1/r_1-1/r_2}, Rsph=1/r11/r24πkR_{\mathrm{sph}}=\frac{1/r_1-1/r_2}{4\pi k}.
  • Composite series: q=ΔToverallRiq=\frac{\Delta T_{\mathrm{overall}}}{\sum R_i}; ΔTi=qRi\Delta T_i = q R_i.
  • Surface convection film: Rconv=1hAR_{\mathrm{conv}}=\frac{1}{hA}.
  • Critical insulation radius (cylinder): rcr=kinshr_{\mathrm{cr}}=\frac{k_{\mathrm{ins}}}{h}; insulation below rcrr_{\mathrm{cr}} can increase heat loss.

Topic details

Definition and physical meaning

Conduction is the transfer of thermal energy through a medium by molecular interaction (lattice vibration in solids; molecular collisions in fluids) without bulk motion of the medium.
Steady conduction means the temperature field T(r)T(\mathbf{r}) does not change with time:
Tt=0\frac{\partial T}{\partial t}=0

Consequently the heat flux field is divergence-free in the absence of generation:
q=0(no generation)\nabla\cdot\mathbf{q}=0\quad(\text{no generation})
Physical parameters
Symbol
Meaning
SI unit
TT
Temperature
K\mathrm{K} (or °C)
qq
Heat transfer rate
W\mathrm{W}
qq''
Heat flux
W/m2\mathrm{W/m^2}
kk
Thermal conductivity
W/(mK)\mathrm{W/(m\cdot K)}
AA
Area normal to heat flow
m2\mathrm{m^2}
LL, rr
Thickness / radius
m\mathrm{m}
hh
Convective coefficient
W/(m2K)\mathrm{W/(m^2\cdot K)}
RthR_{\mathrm{th}}
Thermal resistance
K/W\mathrm{K/W}
Typical kk (order of magnitude): metals 1010400400, building materials 0.10.122, insulation 0.020.020.10.1, air 0.026W/(mK)\sim 0.026\,\mathrm{W/(m\cdot K)} at room temperature.

Core assumptions (state these in exams)

Before applying textbook formulas, write the assumptions explicitly:
1. Steady stateT/t=0\partial T/\partial t = 0.
2. One-dimensional heat flow (plane wall: xx only; cylinder/sphere: rr only).
3. Constant thermal conductivity kk (or use average kk over the temperature range).
4. No internal heat generation unless the problem states generation (q˙\dot{q} or qgq_{g}).
5. Homogeneous isotropic material in each layer.
6. Perfect thermal contact between layers (contact resistance neglected unless given).
7. Constant cross-section for plane wall; for cylinder/sphere use the correct radial area A(r)A(r).
If generation is present, the governing equation becomes
ddx(kAdTdx)+E˙gen=0\frac{d}{dx}\left(kA\frac{dT}{dx}\right)+\dot{E}_{\mathrm{gen}}=0

and the simple q=kAΔT/Lq=kA\Delta T/L form no longer holds without integrating the ODE.

Fourier’s law — derivation summary

Statement (1-D Cartesian). The heat rate in the +x+x direction is proportional to area and to the negative temperature gradient:
qx=kAdTdxq_x=-kA\frac{dT}{dx}
Why the minus sign? Heat flows spontaneously from high TT to low TT. If dTdx<0\frac{dT}{dx}<0 (temperature decreases in +x+x), then qx>0q_{x}>0.
Heat flux form:
qx=kdTdx[W/m2]q_x''=-k\frac{dT}{dx}\qquad\left[\mathrm{W/m^2}\right]
Vector form (isotropic solid):
q=kT\mathbf{q}''=-k\nabla T
Derivation sketch (continuum). Consider a slab of thickness Δx\Delta x and area AA. Net energy into a control volume with no generation and steady state must be zero. Empirically, qAΔT/Δxq\propto A\,\Delta T/\Delta x. Taking the continuum limit Δx0\Delta x\to 0 and inserting the minus sign for direction yields Fourier’s law. The proportionality constant is k(T)k(T), measured experimentally.
Units check:
[k]=[q][L][A][ΔT]=Wmm2K=W/(mK)[k]=\frac{[q]\,[L]}{[A]\,[\Delta T]}=\frac{\mathrm{W}\cdot\mathrm{m}}{\mathrm{m^2}\cdot\mathrm{K}}=\mathrm{W/(m\cdot K)}
Wall (k)T₁T₂q →L
Fig — Plane wall (RC Sachdeva / GATE schematic)

Schematic diagram for study — aligned with standard B.Tech / GATE syllabus.

One-dimensional plane-wall conduction. Fourier law: heat flows from hot face T₁ through wall thickness L to cold face T₂.

Plane wall with constant k

Integrate Fourier’s law from x=0x = 0 (T=T1T = T_{1}) to x=Lx = L (T=T2T = T_{2}) with constant kk and AA:
q0Ldx=kAT1T2dTq\int_0^L dx=-kA\int_{T_1}^{T_2}dT

qL=kA(T1T2)qL = kA(T_{1}-T_{2})

q=kA(T1T2)Lq=\frac{kA(T_1-T_2)}{L}
Temperature distribution is linear:
T(x)=T1T1T2LxT(x)=T_1-\frac{T_1-T_2}{L}x
Thermal resistance of the wall:
Rwall=LkAq=T1T2RwallR_{\mathrm{wall}}=\frac{L}{kA}\qquad\Rightarrow\qquad q=\frac{T_1-T_2}{R_{\mathrm{wall}}}
This is the conduction analogue of Ohm’s law I=VRI = \frac{V}{R}.

Cylindrical and spherical walls

For a hollow cylinder (inner radius r1r_{1}, outer r2r_{2}, length LL), area grows as A(r)=2πrLA(r)=2\pi r L. Integrating Fourier’s law in radial coordinates:
qr=2πkL(T1T2)ln(r2/r1)q_r=\frac{2\pi k L(T_1-T_2)}{\ln(r_2/r_1)}

Rcyl=ln(r2/r1)2πkLR_{\mathrm{cyl}}=\frac{\ln(r_2/r_1)}{2\pi k L}
Temperature is logarithmic in rr:
T(r)=T1T1T2ln(r2/r1)ln(rr1)T(r)=T_1-\frac{T_1-T_2}{\ln(r_2/r_1)}\ln\left(\frac{r}{r_1}\right)
For a hollow sphere:
qr=4πk(T1T2)1r11r2q_r=\frac{4\pi k(T_1-T_2)}{\dfrac{1}{r_1}-\dfrac{1}{r_2}}

Rsph=1/r11/r24πkR_{\mathrm{sph}}=\frac{1/r_1-1/r_2}{4\pi k}
Exam trap: Never use q=kAΔT/Lq=kA\Delta T/L with a single “mean” area for a thick pipe unless the problem explicitly allows a thin-wall approximation (r2r1r_2\approx r_1).

Composite walls and the resistance network

Series layers (heat flows through layer 1, then 2, …): the heat rate qq is the same through each layer; temperature drops add:
q=ThotTcoldiRiq=\frac{T_{\mathrm{hot}}-T_{\mathrm{cold}}}{\sum_i R_i}

ΔTi=qRi\Delta T_i=q R_i
Parallel paths (side-by-side materials spanning the same ΔT\Delta T): conductances add:
1Req=i1Ri\frac{1}{R_{\mathrm{eq}}}=\sum_i\frac{1}{R_i}
Including convection at a surface exposed to fluid at TT_\infty:
Rconv=1hAR_{\mathrm{conv}}=\frac{1}{hA}

Example plane wall with convection on both sides:
q=T,1T,21h1A+LkA+1h2Aq=\frac{T_{\infty,1}-T_{\infty,2}}{\dfrac{1}{h_1A}+\dfrac{L}{kA}+\dfrac{1}{h_2A}}
Overall heat-transfer coefficient UU is defined by q=UAΔToverallq=UA\Delta T_{\mathrm{overall}}, so
1UA=Ri\frac{1}{UA}=\sum R_i

Critical radius of insulation

For an insulated cylinder (pipe) of outer insulation radius rr, heat loss to ambient involves
Rtotal=ln(r/ri)2πkinsL+1h(2πrL)R_{\mathrm{total}}=\frac{\ln(r/r_i)}{2\pi k_{\mathrm{ins}}L}+\frac{1}{h(2\pi r L)}

Differentiating q(r)q(r) (or RtotalR_{\mathrm{total}}) with respect to rr and setting dqdr=0\frac{dq}{dr} = 0 gives the critical radius
rcr=kinshr_{\mathrm{cr}}=\frac{k_{\mathrm{ins}}}{h}
Physical meaning
- If bare outer radius ro<rcrr_o < r_{\mathrm{cr}}, adding a thin layer of insulation can increase heat loss (area increase dominates).
- If ro>rcrr_o > r_{\mathrm{cr}}, adding insulation decreases heat loss.
For a sphere, rcr=2kins/hr_{\mathrm{cr}}=2k_{\mathrm{ins}}/h.
This is a favourite GATE conceptual question — always compare ror_{o} with rcrr_{\mathrm{cr}} before concluding that “more insulation is better.”

Step-by-step problem approach

1. Sketch geometry; mark known temperatures (surface or fluid) and materials.
2. Decide plane / cylinder / sphere; write assumptions (steady, 1-D, constant kk, …).
3. Draw the thermal resistance circuit including convection films if fluid temperatures are given.
4. Compute each RiR_{i} with consistent SI units (convert mm → m).
5. Find q=ΔToverall/Rq=\Delta T_{\mathrm{overall}}/\sum R.
6. Recover interface temperatures via ΔTi=qRi\Delta T_i=qR_i if asked.
7. For insulation problems, compute rcr=k/hr_{\mathrm{cr}}=k/h and interpret.
8. Check units and order of magnitude (qq should be sensible for the area and ΔT\Delta T).

Common mistakes in exams

• Using Celsius in formulas that need absolute temperature — not required for conduction ΔT\Delta T, but required for radiation T4T^4.
• Mixing mm and m in LL, AA, rr (factor-of-10310^3 errors).
• Applying plane-wall formula to a thick cylindrical pipe.
• Omitting 1(hA)\frac{1}{(hA)} when only fluid temperatures are known.
• Adding series resistances incorrectly as parallel (or vice versa).
• Assuming insulation always reduces heat loss without checking rcrr_{\mathrm{cr}}.
• Forgetting that AA for a cylinder wall is 2πrL2\pi r L (varies with rr), not a constant plane area.

Worked examples

Try the problem first — open the solution when you are ready to check.

Plane-wall conduction rate

Problem

A plane wall has k=40W/(mK)k=40\,\mathrm{W/(m\cdot K)}, A=0.2m2A=0.2\,\mathrm{m^2}, L=0.05mL=0.05\,\mathrm{m}, and face temperatures T1=120CT_1=120^\circ\mathrm{C}, T2=60CT_2=60^\circ\mathrm{C}. Find the steady heat rate qq.

Solution

Formulas (Indian textbook notation)

  • ΔT=T1T2=60K\Delta T=T_1-T_2=60\,\mathrm{K}

Formulas (Indian textbook notation)

  • q=kAΔTL=40×0.2×600.05=4800.05=9600W=9.6kWq=\frac{kA\Delta T}{L}=\frac{40\times 0.2\times 60}{0.05}=\frac{480}{0.05}=9600\,\mathrm{W}=9.6\,\mathrm{kW}
Also Rwall=L/(kA)=0.05/(40×0.2)=0.00625K/WR_{\mathrm{wall}}=L/(kA)=0.05/(40\times 0.2)=0.00625\,\mathrm{K/W}, so q=ΔT/R=60/0.00625=9600Wq=\Delta T/R=60/0.00625=9600\,\mathrm{W}.

Composite wall with convection

Problem

A furnace wall: firebrick L1=0.2mL_1=0.2\,\mathrm{m}, k1=1.0W/(mK)k_1=1.0\,\mathrm{W/(m\cdot K)}; steel shell L2=0.01mL_2=0.01\,\mathrm{m}, k2=40W/(mK)k_2=40\,\mathrm{W/(m\cdot K)}. Inside gas T,i=800CT_{\infty,i}=800^\circ\mathrm{C}, hi=50W/(m2K)h_i=50\,\mathrm{W/(m^2\cdot K)}; outside air T,o=30CT_{\infty,o}=30^\circ\mathrm{C}, ho=20W/(m2K)h_o=20\,\mathrm{W/(m^2\cdot K)}. Area A=1m2A=1\,\mathrm{m^2}. Find qq.

Critical radius check

Problem

A wire of outer radius ro=1mmr_o=1\,\mathrm{mm} is to be insulated with material k=0.05W/(mK)k=0.05\,\mathrm{W/(m\cdot K)}. Ambient convection h=10W/(m2K)h=10\,\mathrm{W/(m^2\cdot K)}. Will a thin insulation layer reduce heat loss?

Practice questions

Most-asked interview and GATE questions for this topic — expand any item for a model answer.

  1. 1
    What is Fourier’s law of heat conduction? State its assumptions.

    Model answer

    Fourier’s law: qx=kAdTdxq_x=-kA\dfrac{dT}{dx}. Heat flows from high to low temperature. Assumptions for the simple form: steady state, one-dimensional flow, constant kk, no generation, homogeneous isotropic material.
  2. 2
    Define thermal resistance and write RthR_{\mathrm{th}} for a plane wall.

    Model answer

    Thermal resistance relates temperature difference to heat rate: q=ΔT/Rthq=\Delta T/R_{\mathrm{th}}. For a plane wall, Rwall=LkAR_{\mathrm{wall}}=\dfrac{L}{kA} with unit K/W\mathrm{K/W}.
  3. 3
    Why is temperature distribution linear in a plane wall with constant kk?

    Model answer

    From Fourier’s law with constant qq and kk, dTdx=qkA=constant\dfrac{dT}{dx}=-\dfrac{q}{kA}=\text{constant}, so T(x)T(x) is linear between the two face temperatures.
  4. 4
    Write the radial conduction formula for a hollow cylinder.

    Model answer

    q=2πkL(T1T2)ln(r2/r1)q=\dfrac{2\pi k L(T_1-T_2)}{\ln(r_2/r_1)} and Rcyl=ln(r2/r1)2πkLR_{\mathrm{cyl}}=\dfrac{\ln(r_2/r_1)}{2\pi k L}. Area grows with radius, so the log form appears.
  5. 5
    Explain the electrical analogy for conduction.

    Model answer

    Temperature difference ↔ voltage, heat rate qq ↔ current, thermal resistance ↔ electrical resistance. Series layers add RR; parallel paths add conductances 1R\frac{1}{R}.
  6. 6
    What is critical radius of insulation for a cylinder?

    Model answer

    rcr=kinshr_{\mathrm{cr}}=\dfrac{k_{\mathrm{ins}}}{h}. If bare radius ro<rcrr_o<r_{\mathrm{cr}}, adding thin insulation can increase heat loss because surface area grows faster than conduction resistance.
  7. 7
    When do you include convective film resistance 1(hA)\frac{1}{(hA)}?

    Model answer

    Whenever fluid temperatures (not surface temperatures) are given. Then Rconv=1/(hA)R_{\mathrm{conv}}=1/(hA) is placed at the fluid–solid interface in the thermal circuit.
  8. 8
    How do you find interface temperature in a composite wall?

    Model answer

    First find q=ΔToverall/Rq=\Delta T_{\mathrm{overall}}/\sum R. Then for each layer ΔTi=qRi\Delta T_i=qR_i. Interface temperature follows by subtracting successive drops from the hot side.
  9. 9
    Differentiate conduction, convection, and radiation in one line each.

    Model answer

    Conduction: molecular energy transfer in a continuum without bulk motion. Convection: energy transport by fluid motion plus conduction near the wall. Radiation: electromagnetic emission, needs no medium, T4\propto T^4.
  10. 10
    What is overall heat transfer coefficient UU?

    Model answer

    Defined by q=UAΔToverallq=UA\Delta T_{\mathrm{overall}} so 1UA=Ri\dfrac{1}{UA}=\sum R_i. UU lumps wall conduction and surface convection into one coefficient.
  11. 11
    Why can’t you use q=kAΔT/Lq=kA\Delta T/L for a thick pipe?

    Model answer

    In a cylinder, heat-flow area A(r)=2πrLA(r)=2\pi r L varies with radius. Integration of Fourier’s law gives the logarithmic formula, not the plane-wall form.
  12. 12
    State SI units of kk, hh, qq, and RthR_{\mathrm{th}}.

    Model answer

    kk: W/(mK)\mathrm{W/(m\cdot K)}; hh: W/(m2K)\mathrm{W/(m^2\cdot K)}; qq: W\mathrm{W}; RthR_{\mathrm{th}}: K/W\mathrm{K/W}.
  13. 13
    What happens to heat flux if wall thickness doubles at fixed ΔT\Delta T and kk?

    Model answer

    For a plane wall q1/Lq\propto 1/L, so heat rate (and average flux) halves when LL doubles, all else equal.
  14. 14
    Explain series vs parallel thermal resistances with an example.

    Model answer

    Series: multilayer furnace wall — same qq, ΔT\Delta T splits by RiR_{i}. Parallel: two materials side-by-side spanning the same ΔT\Delta T — conductances add.
  15. 15
    How would you reduce heat loss from a steam pipe in practice?

    Model answer

    Use insulation with low kk and outer radius well above rcrr_{\mathrm{cr}}; reduce outer hh with cladding/weather shield; minimize bare fittings; ensure good joint sealing to avoid thermal bridges.

Exams & GATE

  • 1
    Textbook: RC Sachdeva Ch. 2–3 / Incropera Ch. 3.
  • 2
    Always draw the thermal circuit before writing equations.
  • 3
    State SI units: kk in W/(m·K), hh in W/(m²·K), qq in W, TT in K or °C (ΔT\Delta T identical).
  • 4
    GATE favourites: composite walls, insulated pipes, and critical-radius conceptual MCQs.

📖 Standard books (India)

  • Fundamentals of Engineering Heat & Mass TransferRC Sachdeva

    Read: Syllabus unit

    Heat transfer and heat exchangers