At 1600°C, Fe– Cr melts exhibit Raoultian ideality, and the molar heat of melting of Cr, at its equilibrium melting temperature of 2173 K, is 21,000 J. Thus, for Cr_{(s)}=Cr_{(l)} ,
\Delta G^\circ _{m}=\Delta H^\circ _{m}-T\frac{\Delta H^\circ _{m}}{T_{m}}=21,000-9.66T J
and for Cr_{(l)}=\left[Cr\right]_{(1 wt\% in Fe)} ,
\Delta G=RT\ln \frac{55.85}{100\times 52.01}=-37.70T J
Therefore, for Cr_{(s)}- \left[Cr\right]_{(1 wt\% in Fe)} ,
\Delta G^\circ _{(iii)}=21,000-47.36T J (iii)
The standard Gibbs free energy change for the reaction
2\left[Cr\right]_{(1wt\%)} +3\left[O\right]_{(1wt\%)}=Cr_2O_{3(s)} (iv)
is thus
\Delta G^\circ _{(iv)} =\Delta G^\circ _{(i)}-3\Delta G^\circ _{(ii)}-2\Delta G^\circ _{(iii)}
= -829,090 + 372.13T J
=-RT\ln \frac{a_{Cr_2O_3}}{h^2_{Cr(1wt\%)}.h^3_{O(1wt\%)}}
or, at 1873 K,
\log \frac{h^2_{Cr(1 wt\%)}.h^3_{O(1 wt\%)}}{a_{Cr_2O_3}} =-3.68 (v)
Saturation of the melt with solid Cr_2O_3 occurs at {a_{Cr_2O_3}}=1 , and, if the interactions between Cr and O in solution are ignored, and it is assumed that oxygen obeys Henry’ s law, Equation (v) can be written as
\log \left[wt\% Cr\right] =-1.5\log \left[wt\% O\right] -1.84 (vi)
which is the variation of [wt% Cr] with [wt% O] in liquid iron required for equilibrium with solid Cr_2O_3 at 1600°C. Equation (vi) is drawn as line (vi) in Figure 13.35.
For
Fe_{(l)}+2Cr_{(S)}+2O_{2(g)}=FeO.Cr_2O_{3(S)}
\Delta G^\circ _{(vii)}=-1,409,420+318.07T J (vii)
and thus, for the reaction
Fe_{(l)}+22\left[Cr\right]_{(1 wt\%)}+4\left[O\right]_{(1 WT\%)} =FeO.Cr_2O_{3(S)}
\Delta G^\circ _{(viii)}=\Delta G^\circ _{(vii)}-2\Delta G^\circ _{(iii)}-4\Delta G^\circ _{(ii)}
= -1,007,140 + 436.27T J (viii)
=-RT\ln \frac{a_{FeO.Cr_2O_3}}{a_{Fe}.h^2_{Cr(1 wt\%)}.h^4_{O(1 wt\%)}}
or, at 1873 K,
\log \frac{a_{Fe}.h^2_{Cr(1wt\%)}.h^4_{O{(1wt\%)}} }{a_{FeO.Cr_2O_3}} =-5.30 (ix)
Saturation of the melt with FeO.Cr_2O_3 occurs at a_{FeO.Cr_2O_3} =1 and, with the same assumptions as before, and a_{Fe}=X_{Fe}=1-X_{Cr}, the variation of [wt% Cr] with [wt% O] required for equilibrium with solid FeO.Cr_2O_3 at 1600°C is
\log (1-X_{Cr})+2\log \left[wt\% Cr\right]+4\log \left[wt\% O\right]=-5.30 (x)
In solutions sufficiently dilute that X_{Fe}\sim 1 , Equation (x) can be simplified as
\log \left[wt\% Cr\right]=-2\log \left[wt\% O\right] -2.65 (xi)
Equation (xi) is drawn as line (x) in Figure 13.35. Lines (vi) and (x) intersect at the point A , log [wt% Cr] = 0.59, log [wt% O] = – 1.62 (wt% O = 0.024, wt% Cr = 3.89), which is the composition of the melt which is simultaneously saturated with solid Cr_2O_3 and FeO.Cr_2O_3 . From the phase rule, equilibrium in a three-component system (Fe– Cr– O) among four phases (liquid Fe– Cr– O, solid Cr_2O_3 , solid FeO.Cr_2O_3 , and a gas phase) has one degree of freedom, which, in the present case, has been used by specifying the temperature to be 1873 K. Thus, the activities of Fe, Cr, and O are uniquely fixed, and hence [wt% Cr] and [wt% O] are uniquely fixed. The equilibrium oxygen pressure in the gas phase is obtained from Equation (ii) as
\Delta G^\circ _{(ii),1873 K}=-122,065 J =-8.3144\times 1873\ln \frac{\left[WT\%O\right] }{p^{1/2}_{O_2}}
which, with [wt% O] = 0.024, gives p_{O_2(eq)}=8.96\times 10^{-11} atm . The positions of the lines in Figure 13.35 are such that, in melts of [wt% Cr] > 3.89, Cr_2O_3 is the stable phase in equilibrium with saturated melts along the line AB and, in melts in which [wt% Cr] < 3.89, FeO.Cr_2O_3 is the stable phase in equilibrium with saturated meltsalong the line AC . Alternatively Cr_2O_3 is the stable phase in equilibrium with saturated melts of [wt% O] < 0.024, and FeO.Cr_2O_3 is the stable phase in equilibrium with saturated melts of [wt% O] > 0.024. Consider a melt in which log [wt% Cr] = 1.5. From Figure 13.35, or Equation (vi), the oxygen content at this chromium level required for equilibrium with Cr_2O_3 (at the point B in Figure 13.35) is 5.93\times 10^{-3} wt%, or log [wt% O] = – 2.25. From Equation (v), the activity of Cr_2O_3 in this melt with respect to solid Cr_2O_3 is unity, and hence the melt is saturated with respect to solid Cr_2O_3 . However, from Equation (ix), in the same melt (i.e., X_{Fe}=0.668, [wt% Cr] = 31.6, [wt% O] = 0.00593), the activity of FeO.Cr_2O_3 with respect to solid FeO.Cr_2O_3 is only 0.2. Thus, the melt is saturated with respect to Cr_2O_3 and is undersaturated with respect to FeO.Cr_2O_3 . Moving along the line BA from B toward A, a_{Cr_2O_3}=1 , and a_{FeO.Cr_2O_3}=1 increases from 0.2 at B to unity at A in the doubly saturated melt. Consider a melt in which log [wt% Cr] = – 0.5. From Figure 13.35, the oxygen content required for saturation with FeO.Cr_2O_3 is 0.084 wt% (log [wt% O] = – 1.075 at the point C in Figure 13.35). From Equation (ix), the activity of FeO.Cr_2O_3 in this melt is unity. However, from Equation (v), the activity of Cr_2O_3 in the melt, with respect to solid Cr_2O_3 , is only 0.285. Thus, this melt is saturated with FeO.Cr_2O_3 and is undersaturated with Cr_2O_3 On moving along the line CA from C toward A ,a_{FeO.Cr_2O_3} is unity and a_{Cr_2O_3} increases from 0.285 at C to unity at A . If the various solute– solute interactions had been considered, Equation (v), with a_{Cr_2O_3}=1, would be written as
2 \log h_{Cr(1wt\%)}+3 \log h_{O(1wt\%)}=-3.68
or
2 \log f_{Cr(1 wt\%)}+2 \log\left[wt\% Cr\right]+3 \log f_{O(1wt\%)}+3 \log \left[wt\% O\right] =-3.68
or
2e^{Cr}_{Cr}.\left[wt\% Cr\right]+2e^{O}_{Cr}.\left[wt\% O\right]+2\log \left[wt\% Cr\right]+3e^{O}_{O}.\left[wt\% O\right]+3e^{Cr}_{O}\left[wt\% Cr\right]+3\log \left[wt\% O\right]=-3.68
With
e^{0}_{Cr}=O e^{O}_{O}=-0.2 e^{Cr}_{O}=-0.041 and e^{O}_{Cr}=-0.13
this gives
-0.43\left[wt\% O\right]+0.0615\left[wt\% Cr\right] +\log \left[wt\%Cr\right]+1.5\log \left[wt\% O\right] =-1.84 (xii)
which is drawn as line (xii) in Figure 13.36.
Similarly, with a_{FeO.Cr_2O_3} =1 , Equation (ix) would be written as
\log X_{Fe} +2 \log h_{Cr(1 wt\%)}+4\log h_{O(1wt\%)}=-5.30
or
\log X_{Fe} +2e^{Cr}_{Cr}.\left[wt\%Cr\right]+2e^{O}_{Cr}.\left[wt\%O\right]+2\log \left[wt\%Cr\right]+4e^{O}_{O}.\left[wt\%O\right]+4e^{Cr}_{O}.\left[wt\%Cr\right]+4\log \left[wt\%Cr\right]=-5.30
or
\log X_{Fe}-1.06\left[wt\% O\right]-0.164\left[wt\% Cr\right]+2\log \left[wt\% Cr\right]+4\log \left[wt\% O\right]=-5.30
which is drawn as line (xiii) in Figure 13.36. Lines (xii) and (xiii) intersect at log [wt% Cr] = 0.615, log [wt% O] = – 1.455 ([wt% Cr] = 4.12, [wt% O] = 0.035). When the interactions among the solute were ignored, the point of intersection, A , was obtained as [wt% Cr] = 3.89, [wt% O] = 0.024.