GTBL042-06 GTBL042-Callister-v3 September 28, 2007 21:46
2nd Revise Page6.4 Nonsteady-State Diffusion • 169Distance from interface, xConcentration,CCx – C 0
C 0CxCsCs – C 0Figure 6.6 Concentration profile for
nonsteady-state diffusion; concentration
parameters relate to Equation 6.5.relationship between concentration, position, and time—namely, thatCx, being a
function of the dimensionless parameterx/√
Dt, may be determined at any time and
position if the parametersC 0 ,Cs, andDare known.
Suppose that it is desired to achieve some specific concentration of solute,C 1 ,in
an alloy; the left-hand side of Equation 6.5 now becomesC 1 −C 0
Cs−C 0=constantThis being the case, the right-hand side of this same expression is also a constant,
and subsequently
x
2√
Dt=constant (6.6a)or
x^2
Dt=constant (6.6b)Some diffusion computations are thus facilitated on the basis of this relationship,
as demonstrated in Example Problem 6.3.EXAMPLE PROBLEM 6.2Nonsteady-State Diffusion Time Computation I
For some applications, it is necessary to harden the surface of a steel (or iron-
carbon alloy) above the hardness of its interior. One way this may be accom-
plished is by increasing the surface concentration of carbon in a process termed
carburizing carburizing;the steel piece is exposed, at an elevated temperature, to an atmo-
sphere rich in a hydrocarbon gas, such as methane (CH 4 ).
Consider one such alloy that initially has a uniform carbon concentration of
0.25 wt% and is to be treated at 950◦C (1750◦F). If the concentration of carbon
at the surface is suddenly brought to and maintained at 1.20 wt%, how long
will it take to achieve a carbon content of 0.80 wt% at a position 0.5 mm below
the surface? The diffusion coefficient for carbon in iron at this temperature is
1.6× 10 −^11 m^2 /s; assume that the steel piece is semi-infinite.