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[Natural Convection]
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Concentric Cylinders — Natural Convection

Heat transfer across the annular gap between two concentric cylinders via effective conductivity.

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Inputs
Fluid Properties
ρkg/m³
CₚJ/(kg·K)
kW/(m·K)
μPa·s
νm²/s
Pr—
β1/K
Results
Modified Rayleigh Ra*c
——
k_eff / k
——
Effective conductivity
—W/m·K
Heat rate
—W
Concentric Cylinders — Natural Convection — schematic
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Results are indicative

Figures assume typical conditions and the stated method. For measured, guaranteed numbers on your plant, our engineers run site surveys, heat loss audits, and full process models.

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Concentric Cylinders — Natural Convection

Calculates the natural-convection heat transfer across the annular gap between two long concentric cylinders held at constant temperatures Ti​ (inner) and To​ (outer). The Raithby–Hollands method represents the buoyant flow in the gap as an enhanced conduction: heat is conducted through a stationary fluid of effective conductivity keff​>k.

Gap Rayleigh Number

Properties are evaluated at the mean temperature Tf​=(Ti​+To​)/2. The characteristic length is the radial gap b=(Do​−Di​)/2:

Rad​=ν2gβ(Ti​−To​)b3Pr​

Modified Rayleigh Number and Effective Conductivity

Rac∗​=b3(Di−3/5​+Do−3/5​)5[ln(Do​/Di​)]4​Rad​ kkeff​​=0.386(0.861+PrPr​)1/4(Rac∗​)1/4

The correlation is valid for 102≤Rac∗​≤107; below Rac∗​=100 buoyancy is negligible and keff​=k (pure conduction).

Heat Rate

Q=ln(Do​/Di​)2πkeff​L(Ti​−To​)​

References

  • Raithby, G. D. and Hollands, K. G. T., A General Method of Obtaining Approximate Solutions to Laminar and Turbulent Free Convection Problems, Advances in Heat Transfer, Vol. 11, Academic Press, pp. 265–315, 1975.
  • Incropera, F. P. and DeWitt, D. P., Fundamentals of Heat and Mass Transfer, eqs. 9.58–9.60.
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Frequently asked questions

Heat transfer across the annular gap between two concentric cylinders via effective conductivity. Enter your inputs and press Calculate — the worked solution shows every step of the method with your numbers substituted in.

When there is no fan, pump or significant draught — enclosures, outdoor surfaces on still days, passive heat sinks. If there is any imposed flow, compare the two mechanisms: when Gr/Re² is well below one, forced convection dominates and the forced-convection calculators are the right tools.

No — it computes the convective part only. At typical natural-convection coefficients of 2–10 W/m²·K, radiation from a painted or oxidised surface is often the same order of magnitude, so total heat loss should add a radiative term from the Radiation calculators.