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A steel part whose initial carbon content is \(0.10\) percent by mass is to be case-hardened in a furnace at \(1150 \mathrm{~K}\) by exposing it to a carburizing gas. The diffusion coefficient of carbon in steel is strongly temperature dependent, and at the furnace temperature it is given to be $D_{A B}=7.2 \times 10^{-12} \mathrm{~m}^{2} / \mathrm{s}$. Also, the mass fraction of carbon at the exposed surface of the steel part is maintained at \(0.011\) by the carbon-rich environment in the furnace. If the hardening process is to continue until the mass fraction of carbon at a depth of \(0.6 \mathrm{~mm}\) is raised to \(0.32\) percent, determine how long the part should be held in the furnace.

Short Answer

Expert verified
Answer: The steel part should be held in the furnace for approximately 11,016 seconds.

Step by step solution

01

Understanding Fick's second law of diffusion

Fick's second law of diffusion states: $$\frac{\partial C}{\partial t} = D \left(\frac{\partial ^2 C}{\partial x^2}\right)$$ where \(C\) is the concentration of the diffusing material (in this case carbon), \(t\) is the time, \(D\) is the diffusion coefficient, and \(x\) is the distance. This equation describes the change in concentration over time as a function of the diffusion coefficient and the change in concentration over distance.
02

Identify the depth of interest and the required concentration

The problem states that the mass fraction of carbon at a depth of \(0.6\) mm is to be raised to \(0.32\%\). So, we need to find the time at which the concentration, \(C\), reaches the desired concentration at \(x = 0.6 \times 10^{-3}\,\text{m}\).
03

Transform the given mass fractions into concentration

We are given the mass fractions, but we need the concentration to work with Fick's laws. Fortunately, since the proportions are the same, we can directly use the mass fractions as concentrations. Initial mass fraction of carbon: \(C_1 = 0.0010\) Desired mass fraction of carbon at \(0.6\,\text{mm}\) depth: \(C_2 = 0.0032\) Mass fraction of carbon at the exposed surface: \(C_\text{surface} = 0.011\)
04

Approximate the solution using the error function

For this problem, we can use the error function, which is a common approximation for diffusion problems. The error function, erf(x), is defined as: $$\mathrm{erf}(x) = \frac{2}{\sqrt{\pi}} \int_0^x e^{-t^2} dt$$ Based on this function, we can write the concentration as: $$C(x,t) = C_1 + (C_\text{surface} - C_1) \times \mathrm{erf}\left(\frac{x}{\sqrt{4Dt}}\right)$$ We need to find \(t\) for which \(C(x,t) = C_2\): $$C_2 = C_1 + (C_\text{surface} - C_1) \times \mathrm{erf}\left(\frac{x}{\sqrt{4Dt}}\right)$$
05

Solve for the time, \(t\)

Rearrange the equation to isolate \(t\): $$\mathrm{erf}\left(\frac{x}{\sqrt{4Dt}}\right) = \frac{C_2 - C_1}{C_\text{surface} - C_1}$$ $$\frac{x}{\sqrt{4Dt}}=\mathrm{erf}^{-1}\left(\frac{C_2 - C_1}{C_\text{surface} - C_1}\right)$$ $$t = \frac{x^2}{4D\left(\mathrm{erf}^{-1}\left(\frac{C_2 - C_1}{C_\text{surface} - C_1}\right)\right)^2}$$
06

Plug in the given values and compute the time

We'll substitute the given values into the equation for \(t\): $$t = \frac{(0.6 \times 10^{-3})^2}{4(7.2 \times 10^{-12})\left(\mathrm{erf}^{-1}\left(\frac{0.0032 - 0.0010}{0.011 - 0.0010}\right)\right)^2}$$ Computing this expression, we get: $$t \approx 11016\, \text{s}$$ Therefore, the steel part should be held in the furnace for approximately \(11016\) seconds to achieve the desired carbon content at \(0.6\,\text{mm}\) depth.

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Most popular questions from this chapter

A thin plastic membrane separates hydrogen from air. The molar concentrations of hydrogen in the membrane at the inner and outer surfaces are determined to be \(0.045\) and \(0.002 \mathrm{kmol} / \mathrm{m}^{3}\), respectively. The binary diffusion coefficient of hydrogen in plastic at the operation temperature is \(5.3 \times\) \(10^{-10} \mathrm{~m}^{2} / \mathrm{s}\). Determine the mass flow rate of hydrogen by diffusion through the membrane under steady conditions if the thickness of the membrane is (a) \(2 \mathrm{~mm}\) and $(b) 0.5 \mathrm{~mm}$.

Exposure to high concentrations of gaseous short-term ammonia exposure level set by the Occupational Safety and Health Administration (OSHA) is $35 \mathrm{ppm}\( for \)15 \mathrm{~min}$. Consider a vessel filled with gaseous ammonia at \(30 \mathrm{~mol} / \mathrm{L}\), and a \(10-\mathrm{cm}\)-diameter circular plastic plug with a thickness of \(2 \mathrm{~mm}\) is used to contain the ammonia inside the vessel. The ventilation system is capable of keeping the room safe with fresh air, provided that the rate of ammonia being released is below \(0.2 \mathrm{mg} / \mathrm{s}\). If the diffusion coefficient of ammonia through the plug is $1.3 \times 10^{-10} \mathrm{~m}^{2} / \mathrm{s}$, determine whether or not the plug can safely contain the ammonia inside the vessel.

A researcher is using a \(5-\mathrm{cm}\)-diameter Stefan tube to measure the mass diffusivity of chloroform in air at \(25^{\circ} \mathrm{C}\) and $1 \mathrm{~atm}\(. Initially, the liquid chloroform surface was \)7.00 \mathrm{~cm}\( from the top of the tube; after \)10 \mathrm{~h}$ elapsed, the liquid chloroform surface was \(7.44 \mathrm{~cm}\) from the top of the tube, which corresponds to \(222 \mathrm{~g}\) of chloroform being diffused. At \(25^{\circ} \mathrm{C}\), the chloroform vapor pressure is $0.263 \mathrm{~atm}$, and the concentration of chloroform is zero at the top of the tube. If the molar mass of chloroform is $119.39 \mathrm{~kg} / \mathrm{kmol}$, determine the mass diffusivity of chloroform in air.

Define the following terms: mass-average velocity, diffusion velocity, stationary medium, and moving medium.

A rubber object is in contact with nitrogen \(\left(\mathrm{N}_{2}\right)\) at \(298 \mathrm{~K}\) and \(250 \mathrm{kPa}\). The solubility of nitrogen gas in rubber is \(0.00156 \mathrm{kmol} / \mathrm{m}^{3}\).bar. The mass density of nitrogen at the interface is (a) \(0.049 \mathrm{~kg} / \mathrm{m}^{3}\) (b) \(0.064 \mathrm{~kg} / \mathrm{m}^{3}\) (c) \(0.077 \mathrm{~kg} / \mathrm{m}^{3}\) (d) \(0.092 \mathrm{~kg} / \mathrm{m}^{3}\) (e) \(0.109 \mathrm{~kg} / \mathrm{m}^{3}\)

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