Unsteady conduction: lumped capacitance and Heisler charts
Transient conduction: Biot and Fourier numbers, the lumped-capacitance model and time constant, when to use Heisler (one-term) solutions, and the semi-infinite solid, with quenching, thermocouple and erf examples.
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Why it matters
Most real thermal events are transient: a motor warming up after start, a power transistor during a current pulse, a quenched gear, a thermocouple following a changing gas temperature. Transient conduction tells you how fast a body heats or cools and how long a sensor takes to respond. The lumped model gives the answer in one line when it is valid; the Biot number tells you whether it is.
Key ideas
Unsteady (transient) conduction. Temperature changes with time as well as position. It ends in a new steady state, which is not the same as thermal equilibrium unless the body is isolated.
Biot number. Bi = h L_c / k compares the internal conduction resistance (L_c/k) with the external convection resistance (1/h). A small Bi means the inside of the body equalises much faster than heat can leave the surface, so the temperature is nearly uniform inside at every instant.
- For the lumped check use L_c = V/A_s: for a plane wall of thickness 2L cooled on both faces L_c = L (half-thickness); for a long cylinder L_c = r₀/2; for a sphere L_c = r₀/3.
- Do not confuse Bi with the Nusselt number: Bi uses the solid's k, Nu uses the fluid's k.
Lumped capacitance model (Bi < 0.1). An energy balance on the whole body, −hA_s(T − T∞) = ρVc dT/dt, gives an exponential approach to T∞ with time constant τ = ρVc/(hA_s). After one τ the body has covered 63.2 % of the change; after 4.6 τ it is within 1 %. The criterion Bi < 0.1 keeps the error in the lumped result to about 5 %.
Fourier number. Fo = αt/L_c² is dimensionless time: it compares the rate of heat conduction through the body with the rate of energy storage in it. α = k/(ρc) is the thermal diffusivity (m²/s): metals have high α and respond quickly; insulators, concrete and soil have low α. The lumped exponent can be written hA_s t/(ρVc) = Bi·Fo.
When Bi > 0.1: spatial effects. The centre lags the surface. For an infinite plane wall, a long cylinder and a sphere, with uniform initial temperature, constant h and T∞, constant properties and no generation, the exact series solution is plotted as the Heisler charts (centre temperature θ₀/θᵢ against Fo for curves of 1/Bi, plus position-correction and heat-ratio Q/Q₀ charts). Here Bi and Fo use the half-thickness L or the outer radius r₀, not V/A_s. For Fo > 0.2 the first term of the series alone is accurate to about 2 %; the one-term constants (λ₁, C₁) come from tables in your data book.
- Short bodies (finite cylinder, rectangular bar) are handled by multiplying the one-dimensional solutions (product solution).
Semi-infinite solid. For early times or very thick bodies (ground, thick concrete, a brake disc in a short stop), the heat has not yet reached the far side. With a sudden change of surface temperature, the solution uses the error function of η = x/(2√(αt)). The penetration depth grows as √(αt), not linearly with time.
Formulas
Bi = h L_c / k — h (W/m²·K), L_c (m), k of the solid (W/m·K); lumped valid if Bi < 0.1.
L_c = V / A_s — wall: half-thickness L; long cylinder: r₀/2; sphere: r₀/3 (m).
α = k / (ρ c) — thermal diffusivity (m²/s); ρ (kg/m³), c (J/kg·K).
Fo = α t / L_c² — t (s).
θ/θᵢ = (T − T∞)/(Tᵢ − T∞) = exp(−t/τ) = exp(−Bi·Fo) — lumped body.
τ = ρ V c / (h A_s) = ρ c L_c / h — time constant (s).
t = τ · ln[(Tᵢ − T∞)/(T − T∞)] — time to reach T.
Q(t) = ρ V c (Tᵢ − T∞) [1 − exp(−t/τ)] — heat lost (J) up to time t.
θ₀/θᵢ ≈ C₁ exp(−λ₁² Fo) — one-term centre solution, Fo > 0.2 (C₁, λ₁ from tables for the given Bi).
(T − T_s)/(Tᵢ − T_s) = erf[x / (2√(α t))] — semi-infinite solid, surface suddenly at T_s.
Worked examples
Example 1 (standard, quenching). A steel ball of diameter 10 mm (k = 40 W/m·K, ρ = 7800 kg/m³, c = 460 J/kg·K) at 900 °C is quenched in oil at 30 °C with h = 300 W/m²·K. Find the time to reach 100 °C.
L_c = r₀/3= 0.005/3 = 1.667 × 10⁻³ m.Bi = h L_c / k= 300 × 1.667 × 10⁻³ / 40 = 0.0125 < 0.1, so the lumped model holds.τ = ρ c L_c / h= 7800 × 460 × 1.667 × 10⁻³ / 300 = 19.93 s.t = τ ln[(Tᵢ − T∞)/(T − T∞)]= 19.93 × ln(870/70) = 19.93 × 2.520 = 50.2 s.
t ≈ 50 s
Example 2 (GATE level, thermocouple response). A spherical thermocouple bead of diameter 1 mm (k = 35 W/m·K, ρ = 8500 kg/m³, c = 320 J/kg·K) is placed suddenly in a gas stream with h = 210 W/m²·K. Find its time constant and the time to show 99 % of the step change.
L_c = D/6= 1.667 × 10⁻⁴ m;Bi= 210 × 1.667 × 10⁻⁴ / 35 = 0.001, so lumped.τ = ρ c D / (6h)= 8500 × 320 × 0.001 / (6 × 210) = 2.159 s.- 99 % response: θ/θᵢ = 0.01, so t = τ ln(100) = 2.159 × 4.605 = 9.94 s.
- Halving the bead diameter halves τ; doubling h (higher gas velocity) also halves τ.
τ ≈ 2.16 s, t₉₉ ≈ 9.9 s
Example 3 (semi-infinite solid). A thick concrete floor (α = 7 × 10⁻⁷ m²/s) initially at 20 °C has its surface suddenly raised to 80 °C. Find the temperature 50 mm below the surface after 1 h.
- η = x/(2√(αt)) = 0.05 / (2√(7 × 10⁻⁷ × 3600)) = 0.05 / (2 × 0.0502) = 0.498.
- erf(0.498) = 0.519 (from erf tables).
T = T_s + (Tᵢ − T_s) erf(η)= 80 + (20 − 80) × 0.519 = 48.9 °C.
T ≈ 49 °C
Common mistakes
- Using L_c = radius (or diameter) in the lumped Biot check instead of V/A_s; for a sphere it is r₀/3.
- Using the fluid's k in the Biot number. Bi uses the solid's conductivity.
- Applying the lumped exponential when Bi > 0.1, or using V/A_s in the Heisler charts, which are built on L or r₀.
- Writing the temperature ratio upside down: θ/θᵢ starts at 1 and decays to 0.
- Forgetting to convert hours to seconds, or mm to m, inside exponentials.
- Reading a Heisler chart for Fo < 0.2, where the one-term approximation and many chart curves become inaccurate.
For GATE ME
Questions here are mostly lumped-capacitance numericals: check Bi, find the time constant, the time to reach a temperature, or the temperature after a given time; thermocouple response time and the effect of bead diameter or h on it; and conceptual questions on the meaning of Bi and Fo. Practise writing τ = ρcV/(hA) for spheres, cylinders and plates quickly, and ratio problems where properties cancel.
Quick check
- What is the lumped characteristic length of a sphere of radius r₀?
- A body has τ = 10 s. What fraction of the temperature step remains after 10 s?
- Does a larger bead make a thermocouple faster or slower?
- What does a Biot number of 5 tell you?
- In the semi-infinite solid, how does the penetration depth scale with time?
Answers: 1. r₀/3. 2. e⁻¹ ≈ 0.368 (36.8 %). 3. Slower (τ ∝ D). 4. Internal resistance dominates; large temperature gradients inside, so the lumped model is invalid. 5. As √(αt).
Interview questions
All Thermal Engineering interview questionsTry answering each one aloud before you open it.
1.What is unsteady conduction in thermal engineering?Concept
Unsteady conduction, also known as transient conduction, refers to the process where the temperature within a material changes with time. Unlike steady-state conduction, where temperatures are constant over time, unsteady conduction involves time-dependent temperature variations. This occurs when a material is subjected to a sudden change in temperature at its boundary, causing heat to flow until a new equilibrium is reached.
2.Explain the lumped capacitance method in the context of unsteady conduction.Concept
The lumped capacitance method is an approach used to simplify the analysis of transient heat conduction problems. It assumes that the temperature within a solid body is uniform at any given time, meaning the temperature gradient within the body is negligible. This method is valid when the Biot number (Bi) is less than 0.1, indicating that the thermal resistance within the body is much smaller than the thermal resistance at the surface. This allows the entire body to be treated as a single 'lump' with a uniform temperature that changes over time.
3.What are Heisler charts and how are they used in thermal engineering?Concept
Heisler charts plot the exact one-dimensional transient solution for an infinite plane wall, a long cylinder and a sphere suddenly exposed to convection at constant h and T∞, with uniform initial temperature and constant properties. The main chart gives the centre temperature ratio θ₀/θᵢ against the Fourier number Fo = αt/L² for curves of 1/Bi, where L is the half-thickness or outer radius; further charts correct for position and give the fraction of heat lost Q/Q₀. They are used when Bi > 0.1, so the lumped model fails, and they are accurate for Fo > 0.2, where the one-term series solution applies. Short cylinders and bars are handled by multiplying the one-dimensional results.
4.Why is the Biot number important in the lumped capacitance method?Application
The Biot number Bi = hL_c/k_solid compares the internal conduction resistance L_c/k with the external convection resistance 1/h. When Bi < 0.1, heat equalises inside the body much faster than it leaves the surface, so temperature is practically uniform and the lumped model's error stays within about 5 %. For the lumped check use L_c = V/A_s (r₀/3 for a sphere, r₀/2 for a long cylinder, half-thickness for a wall). Note that k here is the solid's conductivity, unlike the Nusselt number which uses the fluid's.
5.What happens if the Biot number is greater than 0.1 in a transient conduction problem?Application
If the Biot number is greater than 0.1, the assumption of uniform temperature within the body (as used in the lumped capacitance method) is no longer valid. This indicates that there is a significant temperature gradient within the body, and the internal thermal resistance cannot be neglected. In such cases, more complex methods, such as using Heisler charts or solving the heat conduction equation, are necessary to accurately predict the temperature distribution.
6.How would you use Heisler charts to find the centre temperature of a sphere after a given time?Application
First compute Bi = hr₀/k and Fo = αt/r₀², using the outer radius r₀ (not V/A as in the lumped check), and confirm Fo > 0.2. On the sphere centre-temperature chart, pick the curve for 1/Bi and read θ₀/θᵢ = (T₀ − T∞)/(Tᵢ − T∞) at your Fo. Then T₀ = T∞ + (θ₀/θᵢ)(Tᵢ − T∞). Equivalently, use the one-term solution θ₀/θᵢ = C₁exp(−λ₁²Fo) with C₁ and λ₁ from tables for that Bi.
7.A metal sphere of radius 0.05 m (k = 50 W/m·K) at 100 °C is suddenly exposed to air at 25 °C with h = 10 W/m²·K. Can the lumped capacitance method be used?Numerical
For the lumped check use L_c = V/A_s = r₀/3 = 0.05/3 = 0.0167 m. Then Bi = hL_c/k = 10 × 0.0167 / 50 = 0.0033, far below 0.1. So the lumped method applies and the sphere's temperature can be taken as uniform at every instant. (Even with L_c = r₀ the Biot number would be only 0.01, so the conclusion is robust.)
8.A long aluminium rod of radius 10 mm (k = 200 W/m·K, ρ = 2700 kg/m³, c = 900 J/kg·K) at 150 °C cools in air at 25 °C with h = 50 W/m²·K. How long does it take to reach 50 °C?Numerical
For a long cylinder L_c = V/A_s = r₀/2 = 0.005 m, so Bi = 50 × 0.005 / 200 = 0.00125 < 0.1 and the lumped model applies. The time constant is τ = ρcL_c/h = 2700 × 900 × 0.005 / 50 = 243 s. Then t = τ·ln[(Tᵢ − T∞)/(T − T∞)] = 243 × ln(125/25) = 243 × 1.609 ≈ 391 s, about 6.5 minutes.
9.Explain how the Fourier number is used in analyzing transient heat conduction problems.Concept
The Fourier number (Fo) is a dimensionless parameter used in transient heat conduction analysis. It is defined as Fo = αt/L², where α is the thermal diffusivity, t is the time, and L is the characteristic length. The Fourier number represents the ratio of heat conduction rate to the rate of thermal energy storage. A higher Fourier number indicates that heat has penetrated deeper into the material, and it is used to determine how quickly a material reaches thermal equilibrium.
10.What are the limitations of using Heisler charts for solving transient conduction problems?Application
They cover only one-dimensional plane walls, long cylinders and spheres (multi-dimensional shapes need product solutions). They assume uniform initial temperature, constant properties, no heat generation, and a sudden step to a constant ambient temperature with constant h. They are based on the one-term solution, so they are inaccurate at short times (Fo < 0.2), and reading log-scale charts adds error. Varying ambient conditions, time-dependent h or complex shapes need numerical methods such as finite differences.
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