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17-Phys-B6 Applied Thermodynamics and Heat Transfer · December 2013

Question 7 of 8: Radiation Error in a Thermocouple Reading

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

Paper format. 98-Phys-B6 Applied Thermodynamics and Heat Transfer, National Examination December 2013 — a three-hour open-book examination; candidates are expected to bring both a thermodynamics text and a heat-transfer text to make use of the property tables. A complete examination is five questions — either three from Part A (Thermodynamics, Q1–Q4) and two from Part B (Heat Transfer, Q5–Q8), or two from Part A and three from Part B — every question carrying equal value; all eight are solved below as a complete study set. Candidates are invited to state any assumptions where a question is open to interpretation; this licence is used explicitly in Question 1(b) (standard air properties, not printed directly) and Question 7 (a printed convective "rate" read as a heat-transfer coefficient with a temperature unit omitted in print — the same omission the paper shows in Question 6's specific-heat units).

Reference texts. Y. A. Çengel and M. A. Boles, Thermodynamics: An Engineering Approach, 8th ed. (ideal-gas processes, vapour power cycles, gas-turbine/Brayton cycles, vapour-compression refrigeration); F. P. Incropera and D. P. DeWitt, Fundamentals of Heat and Mass Transfer, 7th ed. (conduction, natural convection, lumped-capacitance transient conduction, radiation exchange between surfaces, heat-exchanger LMTD analysis).

Question 7: Radiation Error in a Thermocouple Reading

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Given. Bead reading (its own equilibrium temperature) $T_{th}=179\,{}^{\circ}\text{C}$; duct wall temperature $T_w=65\,{}^{\circ}\text{C}$; bead emissivity $\varepsilon_b=0.7$; duct emissivity $\varepsilon_d=0.9$; duct 0.92 m long, no duct diameter $D$ printed anywhere in the source. Convective "rate of 790 W/m$^2$" — read, per the exam's own licence to state assumptions, as the convective heat-transfer coefficient $h_c=790\text{ W/m}^2\cdot\text{K}$ with its temperature-unit suffix dropped in print, as the paper also does in Question 6's "J/k C" specific heat, since a bare heat flux value alone cannot be combined with $F_{b-d}$, $\varepsilon_b$, $\varepsilon_d$ to solve for anything — only a coefficient can.

Given data
QuantitySymbolValue
Indicated (bead) temperature$T_{th}$$179\,{}^{\circ}\text{C}$ (452.15 K)
Duct wall temperature$T_w$$65\,{}^{\circ}\text{C}$ (338.15 K)
Bead emissivity$\varepsilon_b$0.7
Duct emissivity$\varepsilon_d$0.9
Convection coefficient (read)$h_c$790 W/m²·K
Duct length$L$0.92 m

Find. The error in the thermocouple reading, $T_{gas}-T_{th}$.

Approach. At steady state the bead's convective heat gain from the (hotter) gas balances its radiative heat loss to the (cooler) duct wall. The bead is a very small sphere compared with the duct's inner surface for any physically sensible duct diameter, so in the two-gray-surface radiation network the duct-emissivity term vanishes; with no duct diameter printed, the configuration factor $F_{b-d}=L/\sqrt{D^2+L^2}$ is taken as unity (its limit for $D\ll L$); compute the radiative loss from the KNOWN bead and wall temperatures, then back out the true gas temperature from the convective balance using $h_c$.

  1. Radiative loss from the bead to the duct wall. For a small sphere (area $A_b$) radiating to a much larger surrounding surface (area $A_d\gg A_b$) with view factor $F_{b-d}\to1$ (assumed above), the two-surface gray-enclosure network reduces to $$q''_{rad} = \varepsilon_b\,\sigma\left(T_{th}^4-T_w^4\right)$$ — independent of the duct's own emissivity $\varepsilon_d$, since the $(1-\varepsilon_d)/(\varepsilon_d A_d)$ term is negligible whenever $A_b\ll A_d$ (true for a 3 mm bead in any real duct, regardless of the unprinted diameter $D$). Numerically, $$q''_{rad} = 0.7\times5.670\times10^{-8}\times\left(452.15^4-338.15^4\right) = 1140.0\text{ W/m}^2$$
  2. True gas temperature from the convective balance. At steady state the convective heat gained from the gas equals the radiative heat lost to the wall, $$h_c\left(T_{gas}-T_{th}\right) = q''_{rad}$$ $$T_{gas}-T_{th} = \frac{q''_{rad}}{h_c} = \frac{1140.0}{790}$$ $$\boxed{\text{Error} = T_{gas}-T_{th} = 1.44\,{}^{\circ}\text{C}, \qquad T_{gas}=180.4\,{}^{\circ}\text{C}}$$

Check: No duct diameter $D$ is printed anywhere in the source, so the given $F_{b-d}$ formula cannot be evaluated numerically; $F_{b-d}=1$ is adopted, per the exam's own instruction to state assumptions. The duct-emissivity term is negligible for ANY diameter ($A_b\ll A_d$), but the view factor is not: if a diameter were specified and $F_{b-d}$ applied to the bead–wall exchange (the open ends contributing nothing), the error scales with $F_{b-d}$ — $D=0.1$ m gives $F=0.994$ and 1.43°C, $D=0.3$ m gives $F=0.951$ and 1.37°C, $D=0.5$ m gives $F=0.879$ and 1.27°C. The 1.44°C found here is therefore the upper (slender-duct) bound.

Question 7 — results
QuantityValue
Radiative heat loss from bead1140.0 W/m²
Error in reading ($T_{gas}-T_{th}$)$1.44\,{}^{\circ}\text{C}$
True gas temperature$180.4\,{}^{\circ}\text{C}$