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)
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.
Quantity
Value
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.
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 $t$.
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 $c_x=0.005(7850)=39.25$.
Invert the error function. $\mathrm{erf}(\eta)=0.721\Rightarrow\eta=0.765$ (by bisection / erf tables).
Solve for the time. $$t=\frac{1}{D}\left(\frac{x}{2\eta}\right)^2=\frac{1}{2.0\times10^{-11}}\left(\frac{4\times10^{-4}}{2(0.765)}\right)^2=3.42\times10^{3}\ \text{s}=\boxed{0.95\ \text{h}}.$$
Quantity
Result
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.