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),
ΔGm∘=ΔHm∘−TTmΔHm∘=21,000−9.66T J
and for Cr(l)=[Cr](1 wt% in Fe),
ΔG=RTln100×52.0155.85=−37.70T J
Therefore, for Cr(s)−[Cr](1 wt% in Fe),
ΔG(iii)∘=21,000−47.36T J (iii)
The standard Gibbs free energy change for the reaction
2[Cr](1wt%)+3[O](1wt%)=Cr2O3(s) (iv)
is thus
ΔG(iv)∘=ΔG(i)∘−3ΔG(ii)∘−2ΔG(iii)∘
= -829,090 + 372.13T J
=−RTlnhCr(1wt%)2.hO(1wt%)3aCr2O3
or, at 1873 K,
logaCr2O3hCr(1 wt%)2.hO(1 wt%)3=−3.68 (v)
Saturation of the melt with solid Cr2O3 occurs at aCr2O3=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[wt% Cr]=−1.5log[wt% O]−1.84 (vi)
which is the variation of [wt% Cr] with [wt% O] in liquid iron required for equilibrium with solid Cr2O3 at 1600°C. Equation (vi) is drawn as line (vi) in Figure 13.35.
For
Fe(l)+2Cr(S)+2O2(g)=FeO.Cr2O3(S)
ΔG(vii)∘=−1,409,420+318.07T J (vii)
and thus, for the reaction
Fe(l)+22[Cr](1 wt%)+4[O](1 WT%)=FeO.Cr2O3(S)
ΔG(viii)∘=ΔG(vii)∘−2ΔG(iii)∘−4ΔG(ii)∘
= -1,007,140 + 436.27T J (viii)
=−RTlnaFe.hCr(1 wt%)2.hO(1 wt%)4aFeO.Cr2O3
or, at 1873 K,
logaFeO.Cr2O3aFe.hCr(1wt%)2.hO(1wt%)4=−5.30 (ix)
Saturation of the melt with FeO.Cr2O3 occurs at aFeO.Cr2O3=1 and, with the same assumptions as before, and aFe=XFe=1−XCr, the variation of [wt% Cr] with [wt% O] required for equilibrium with solid FeO.Cr2O3 at 1600°C is
log(1−XCr)+2log[wt% Cr]+4log[wt% O]=−5.30 (x)
In solutions sufficiently dilute that XFe∼1, Equation (x) can be simplified as
log[wt% Cr]=−2log[wt% O]−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 Cr2O3 and FeO.Cr2O3. From the phase rule, equilibrium in a three-component system (Fe– Cr– O) among four phases (liquid Fe– Cr– O, solid Cr2O3, solid FeO.Cr2O3, 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
ΔG(ii),1873 K∘=−122,065 J=−8.3144×1873lnpO21/2[WT%O]
which, with [wt% O] = 0.024, gives pO2(eq)=8.96×10−11 atm. The positions of the lines in Figure 13.35 are such that, in melts of [wt% Cr] > 3.89, Cr2O3 is the stable phase in equilibrium with saturated melts along the line AB and, in melts in which [wt% Cr] < 3.89, FeO.Cr2O3 is the stable phase in equilibrium with saturated meltsalong the line AC . Alternatively Cr2O3 is the stable phase in equilibrium with saturated melts of [wt% O] < 0.024, and FeO.Cr2O3 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 Cr2O3 (at the point B in Figure 13.35) is 5.93×10−3 wt%, or log [wt% O] = – 2.25. From Equation (v), the activity of Cr2O3 in this melt with respect to solid Cr2O3 is unity, and hence the melt is saturated with respect to solid Cr2O3. However, from Equation (ix), in the same melt (i.e., XFe=0.668, [wt% Cr] = 31.6, [wt% O] = 0.00593), the activity of FeO.Cr2O3 with respect to solid FeO.Cr2O3 is only 0.2. Thus, the melt is saturated with respect to Cr2O3 and is undersaturated with respect to FeO.Cr2O3. Moving along the line BA from B toward A, aCr2O3=1 , and aFeO.Cr2O3=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.Cr2O3 is 0.084 wt% (log [wt% O] = – 1.075 at the point C in Figure 13.35). From Equation (ix), the activity of FeO.Cr2O3 in this melt is unity. However, from Equation (v), the activity of Cr2O3 in the melt, with respect to solid Cr2O3, is only 0.285. Thus, this melt is saturated with FeO.Cr2O3 and is undersaturated with Cr2O3 On moving along the line CA from C toward A ,aFeO.Cr2O3 is unity and aCr2O3 increases from 0.285 at C to unity at A . If the various solute– solute interactions had been considered, Equation (v), with aCr2O3=1, would be written as
2 loghCr(1wt%)+3 loghO(1wt%)=−3.68
or
2 logfCr(1 wt%)+2 log[wt% Cr]+3 logfO(1wt%)+3 log[wt% O]=−3.68
or
2eCrCr.[wt%Cr]+2eCrO.[wt%O]+2log[wt%Cr]+3eOO.[wt%O]+3eOCr[wt%Cr]+3log[wt%O]=−3.68
With
eCr0=O eOO=−0.2 eOCr=−0.041 and eCrO=−0.13
this gives
−0.43[wt% O]+0.0615[wt% Cr]+log[wt%Cr]+1.5log[wt% O]=−1.84 (xii)
which is drawn as line (xii) in Figure 13.36.
Similarly, with aFeO.Cr2O3=1 , Equation (ix) would be written as
logXFe+2 loghCr(1 wt%)+4loghO(1wt%)=−5.30
or
logXFe+2eCrCr.[wt%Cr]+2eCrO.[wt%O]+2log[wt%Cr]+4eOO.[wt%O]+4eOCr.[wt%Cr]+4log[wt%Cr]=−5.30
or
logXFe−1.06[wt% O]−0.164[wt% Cr]+2log[wt% Cr]+4log[wt% O]=−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.