System parameters
Advanced (ΔHfus, liquid non-ideality)
Click anywhere inside a shaded two-phase field on the diagram to drop a tie-line and read off the lever-rule phase fractions. Click a single-phase field to clear it.
Liquid (L)
Solid solution (α)
Solid + Liquid
Solid + Solid (miscibility gap)
Click inside a two-phase field to compute a tie-line.
What this is actually computing. Both phases are modeled as regular solutions,
G(x,T) = Ω·x(1−x) + RT[x ln x + (1−x) ln(1−x)], with the liquid anchored to the
solid reference state through each pure component's melting point (ΔGfus(T) = ΔHfus(1 − T/Tm),
i.e. ΔCp = 0 is assumed). At every temperature the two curves are sampled on a fine composition grid and the
equilibrium phases are read off the lower convex hull of the combined points, the same
minimize-the-Gibbs-energy principle a full CALPHAD solver uses, just without sublattices, multicomponent
systems, or an assessed database behind it. No diagram topology (eutectic, isomorphous, miscibility gap) is
hard-coded; whatever shape the hull finds for the chosen Ω/Tm values is what renders.
teaching-scale model