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Question

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, $Q=142 kJ/mol$

yerf(y)
0.850.7707
0.900.7970
0.950.8209

What is the depth (in $µm$) from the surface of the specimen at which a composition of 0.4 wt.% C is obtained after carburizing at $870^\circ C$ for 10 h?

The correct answer is
875

Understanding Carbon Diffusion in Steel

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) $
  • $C_s = 1.2$ wt.% C (Surface concentration)
  • $C_0 = 0.2$ wt.% C (Initial concentration)
  • $C(x,t) = 0.4$ wt.% C (Target concentration at depth $x$, time $t$)
  • $t = 10 \text{ h} = 10 \times 3600 \text{ s} = 36000 \text{ s}$ (Carburizing time)

Calculating Diffusion Coefficient (D)

The diffusion coefficient ($D$) depends on temperature ($T$) and is given by the Arrhenius equation:

$ D = D_0 \exp\left(-\frac{Q}{RT}\right) $
  • $D_0 = 2.0 \times 10^{-5} m^2/s$
  • $Q = 142 \text{ kJ/mol} = 142000 \text{ J/mol}$
  • $R = 8.314 \text{ J/(mol·K)}$ (Gas constant)
  • $T = 870^\circ C = 870 + 273.15 = 1143.15 \text{ K}$

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 $

Applying Fick's Second Law

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 $

Determining Diffusion Depth (x)

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.

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Important Questions from Diffusion Fick's Second Law Concentration Profile

  1. 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.

    zerf (z)
    0.30.3268
    0.40.4284
    0.50.5205
  2. 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

  3. The concentration $C$ of a solute (in units of atoms$\cdot\text{mm}^{-3}$) in a solid along $x$direction (for $x > 0$) follows the expression
    $C = a_1x^2 + a_2x$
    where $x$ is in mm, $a_1$ and $a_2$ are in units of atoms$\cdot\text{mm}^{-5}$ and atoms$\cdot\text{mm}^{-4}$,respectively. Assuming $a_1= a_2= 1$, the magnitude of flux at $x = 2 \text{ mm}$ is________ $\times 10^{-3} \text{ atoms} \cdot \text{mm}^{-2} \cdot \text{s}^{-1}$ (answer rounded off to the nearest integer).
    Given: diffusion coefficient of the solute in the solid is $3 \times 10^{-3} \text{ mm}^2 \cdot \text{s}^{-1}$.
  4. Determine the correctness or otherwise of the following Assertion [a] and the Reason [r]
    Assertion [a]: The rate of homogenization in a dilute substitutional solid solution of B in A is controlled by the diffusivity of B.
    Reason [r]: Atomic migration cannot occur along dislocations and grain boundaries.
  5. A species can diffuse through the lattice (diffusion coefficient, $D_L$), along grain boundaries (diffusion coefficient, $D_{GB}$), and along free surfaces (diffusion coefficient, $D_S$). Which of the following relations is CORRECT?
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