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23-Chem-A3 Heat and Mass Transfer · May 2015

Question 6 of 7: Carburizing a steel roller — semi-infinite diffusion

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

Notes on this paper

National Exams — May 2015 — 04-Chem-A3 Mass Transfer Operations. Three-hour, open-book exam; any non-communicating calculator permitted. Format: seven questions in three parts — answer one of Q1–Q2 (Part A), one of Q3–Q4 (Part B) and two of Q5–Q7 (Part C); four questions of equal value constitute a complete paper. All seven are solved below for completeness. Every property datum (diffusivities, vapour pressures, solubilities, humid-air heat capacities) is stated in the question, so each answer is self-contained.

Reference texts: Geankoplis, Transport Processes and Separation Process Principles (4th ed., Prentice Hall) — molecular diffusion, convective mass transfer, gas absorption and drying; Welty, Wicks, Wilson & Rorrer, Fundamentals of Momentum, Heat and Mass Transfer (6th ed., Wiley) — boundary-layer and transient diffusion; Incropera & DeWitt, Fundamentals of Heat and Mass Transfer — transient conduction/diffusion charts and the sphere in a stagnant medium; Treybal, Mass-Transfer Operations (3rd ed.) — packed-tower design; Crank, The Mathematics of Diffusion (2nd ed.) — series solutions for the sphere; supporting data from Perry's Chemical Engineers' Handbook (9th ed.).

Question 6: Carburizing a steel roller — semi-infinite diffusion (Part C — equal value)

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. Carbon diffuses from a carbon-rich surface into steel. Over the short depth of interest (0.4 mm $\ll$ 5-mm radius) the roller behaves as a semi-infinite solid with a fixed surface concentration; the error-function solution applies.

QuantityValue
Depth of interest $x$0.4 mm $=4\times10^{-4}$ m
Surface carbon $c_s$$\rho_\text{gas}=100$ kg/m³
Initial carbon $c_0$0.2%$\times7850=15.7$ kg/m³
Target carbon $c_x$0.5%$\times7850=39.25$ kg/m³
Diffusivity $D$$2.0\times10^{-11}$ m²/s

Find. The carburizing time to reach 0.5% C at 0.4-mm depth.

surface c_s = 100 steel (c₀ = 15.7 kg/m³) x = 0.4 mm: c = 39.25 (0.5% C) c(x,t)
Figure 6 — Carbon penetrates the steel from a carbon-rich surface. Because the target depth (0.4 mm) is small compared with the 5-mm radius, the roller is treated as a semi-infinite medium and the concentration follows the complementary-error-function profile.

Approach. Apply the semi-infinite constant-surface-concentration solution $\dfrac{c_s-c_x}{c_s-c_0}=\mathrm{erf}\!\left(\dfrac{x}{2\sqrt{Dt}}\right)$, invert the error function for the similarity variable $\eta$, then solve for $t$.

  1. Concentrations on a consistent basis. Working in kg/m³ (the ratio is identical in mass-%): surface $c_s=100$, initial $c_0=0.002(7850)=15.7$, target $c_x=0.005(7850)=39.25$.
  2. Error-function argument. $$\frac{c_s-c_x}{c_s-c_0}=\frac{100-39.25}{100-15.7}=0.721=\mathrm{erf}(\eta),\qquad \eta=\frac{x}{2\sqrt{Dt}}.$$
  3. Invert the error function. $\mathrm{erf}(\eta)=0.721\Rightarrow\eta=0.765$ (by bisection / erf tables).
  4. Solve for the time. $$t=\frac{1}{D}\left(\frac{x}{2\eta}\right)^2=\frac{1}{2.0\times10^{-11}}\left(\frac{4\times10^{-4}}{2(0.765)}\right)^2=3.42\times10^{3}\ \text{s}=\boxed{0.95\ \text{h}}.$$
QuantityResult
erf argument (concentration ratio)0.721
Similarity variable $\eta$0.765
Carburizing time $t$$3.4\times10^{3}$ s ≈ 0.95 h
Check
The two densities are not distractors: the surface carbon concentration is set by the carbon gas ($c_s=100$ kg/m³) while the initial and target carbon contents are mass fractions of the steel density. Because the ratio $(c_s-c_x)/(c_s-c_0)$ is dimensionless, it is unchanged whether concentrations are in kg/m³ or in mass-%, confirming the setup is self-consistent.