A steel specimen containing 0.2 wt.% C is carburized in an atmosphere that maintains a carbon content of 1.2 wt.% C at the surface of the specimen. Given:
For carbon diffusion in austenite: $D_0=2.0\times10^{-5} m^2/s$
Activation energy for diffusion, $Q=142 kJ/mol$y erf(y) 0.85 0.7707 0.90 0.7970 0.95 0.8209
The problem involves calculating the depth ($x$) in a steel specimen where a specific carbon concentration ($C(x,t)$) is reached after carburizing. We are given the initial carbon concentration ($C_0$), the surface carbon concentration ($C_s$), the carburizing temperature ($T$), time ($t$), and diffusion parameters ($D_0$, $Q$).
The relevant formula for diffusion under constant surface concentration in a semi-infinite solid is derived from Fick's second law:
$ \frac{C_s - C(x,t)}{C_s - C_0} = \text{erfc}\left(\frac{x}{2\sqrt{Dt}}\right) $The diffusion coefficient ($D$) depends on temperature ($T$) and is given by the Arrhenius equation:
$ D = D_0 \exp\left(-\frac{Q}{RT}\right) $First, calculate the term $Q/(RT)$:
$ \frac{Q}{RT} = \frac{142000 \text{ J/mol}}{8.314 \text{ J/(mol·K)} \times 1143.15 \text{ K}} \approx 14.938 $Now, calculate $D$:
$ D = (2.0 \times 10^{-5} m^2/s) \times \exp(-14.938) $ $ D \approx (2.0 \times 10^{-5} m^2/s) \times (2.186 \times 10^{-7}) $ $ D \approx 4.372 \times 10^{-12} m^2/s $Calculate the concentration ratio term:
$ \frac{C_s - C(x,t)}{C_s - C_0} = \frac{1.2 - 0.4}{1.2 - 0.2} = \frac{0.8}{1.0} = 0.8 $We need to find the argument $z = \frac{x}{2\sqrt{Dt}}$ such that $\text{erfc}(z) = 0.8$.
Using the provided table data, which seems to represent $z$ vs $\text{erfc}(z)$:
| z | erfc(z) |
| 0.85 | 0.7707 |
| 0.90 | 0.7970 |
| 0.95 | 0.8209 |
Our target value $\text{erfc}(z) = 0.8$ lies between $0.7970$ (at $z=0.90$) and $0.8209$ (at $z=0.95$). We interpolate to find $z$:
$ z = 0.90 + \frac{0.8 - 0.7970}{0.8209 - 0.7970} \times (0.95 - 0.90) $ $ z = 0.90 + \frac{0.0030}{0.0239} \times 0.05 \approx 0.90 + 0.0063 = 0.9063 $Now we can calculate the depth $x$ using $z = \frac{x}{2\sqrt{Dt}}$.
First, calculate $2\sqrt{Dt}$:
$ 2\sqrt{Dt} = 2\sqrt{(4.372 \times 10^{-12} m^2/s) \times (36000 s)} $ $ 2\sqrt{Dt} = 2\sqrt{1.5739 \times 10^{-7} m^2} \approx 2 \times (3.967 \times 10^{-4} m) $ $ 2\sqrt{Dt} \approx 7.934 \times 10^{-4} m $Calculate the depth $x$:
$ x = z \times (2\sqrt{Dt}) $ $ x \approx 0.9063 \times (7.934 \times 10^{-4} m) $ $ x \approx 7.187 \times 10^{-4} m $Convert the depth to micrometers ($µm$):
$ x \approx 7.187 \times 10^{-4} m \times \frac{10^6 µm}{1 m} \approx 718.7 µm $Note: Based on standard calculations and interpolation from the provided table, the depth is approximately $719 µm$. The provided options might imply a different interpretation or data set. Proceeding with the calculated value based on the given information.
During carburizing of a steel, the surface concentration is kept constant at 1.4 wt.% carbon. Diffusivity of carbon for the steel at 950 $^\circ$C is $6.25 \times 10^{-11}$ m$^2$/s. At 950 $^\circ$C, the time required to carburize the steel with an initial composition of 0.2 wt.% carbon to 0.8859 wt.% carbon at a depth of 0.2 mm is ______________ seconds (approximate to the nearest integer).
Use the nearest value of the error function from the table given below for your calculation.
| z | erf (z) |
|---|---|
| 0.3 | 0.3268 |
| 0.4 | 0.4284 |
| 0.5 | 0.5205 |
For self-diffusion in polycrystalline copper with a lattice diffusion coefficient $D_L$, grain boundary diffusion coefficient $D_{GB}$, and surface diffusion coefficient $D_S$, the correct relationship is