Solid–Liquid Eutectic Diagrams

Imagine cooling a molten mixture of two metals. Watch it freeze not at one sharp temperature, but over a range. Solid crystals of one metal appear long before the whole mass solidifies. Solid–liquid eutectic diagrams are the maps that let chemists and metallurgists predict exactly this behavior. They tell you which phases exist, in what proportions. They also show at what temperature, for any composition of a two-component solid–liquid system. These diagrams matter enormously in practice. Solder alloys, cast iron, ice-salt mixtures on winter roads, and pharmaceutical co-crystals all depend on eutectic behavior. Understanding the eutectic point explains why a specific mixture melts at a lower temperature. This is lower than either pure component alone. This article builds the binary eutectic phase diagram. It starts from the Gibbs phase rule and the shape of chemical potential curves. You will learn to read cooling curves. You will apply the lever rule to extract phase compositions and amounts. You will work through two full numerical examples. One is idealized, and one is closer to a real alloy system.

Key takeaways
  • A eutectic diagram maps temperature against composition for a binary system with two solid phases and one liquid phase.
  • The eutectic point is the unique composition and temperature where liquid coexists with both solids at equilibrium.
  • Cooling curves show slope changes at the liquidus and a temperature plateau at the eutectic, revealing the phase behavior.
  • The lever rule, applied along a tie-line, gives the relative amounts of solid and liquid at any point in the two-phase region.
  • The Gibbs phase rule fixes the eutectic as invariant: F = 0 at fixed pressure, so it occurs at one specific temperature.
  • Key idea: Freezing-point depression from each component's dissolution in the liquid produces two liquidus curves that intersect at the eutectic, the lowest-melting composition in the system.
The core insight

A eutectic diagram is the graphical solution to a competition: each solid component wants to freeze out of solution at its own characteristic temperature, but dissolving the other component lowers that freezing point, so the two liquidus curves must cross at one composition and temperature, the eutectic, below which no liquid can exist.

The physical picture

Consider two substances A and B that are completely miscible as liquids but essentially immiscible as solids, each crystallizing in its own pure solid phase. Start with pure liquid A at high temperature. As you cool it, nothing happens until you reach the melting point of pure A, TA∗T_A^*, where solid A begins to appear. Now do the same experiment with a mixture. Adding B to liquid A lowers the freezing point of A, exactly as in colligative freezing-point depression. As more B is dissolved, the temperature at which solid A first appears keeps dropping. This traces out a curve, the A-liquidus, descending from TA∗T_A^* as composition shifts toward more B. Symmetrically, starting from pure B and adding A traces the B-liquidus, descending from TB∗T_B^* as composition shifts toward more A. These two liquidus curves must intersect somewhere. At that intersection, the liquid is simultaneously saturated with respect to both solid A and solid B. This is the eutectic point (TET_E, xEx_E), the single lowest-melting composition, the invariant point where three phases, liquid, solid A, and solid B, coexist. Below the eutectic temperature, no liquid phase can exist in this simple system; everything is solid, present either as regions of pure crystalline A, pure crystalline B, or a fine intimate mixture of both called the eutectic solid, formed when liquid of eutectic composition solidifies simultaneously into both crystal types. The full phase diagram divides into regions: a single liquid region above both liquidus curves, two two-phase regions (liquid + solid A, and liquid + solid B) bounded by liquidus above and the eutectic horizontal (the solidus, here degenerate to a single line since the solids are pure) below, and below that horizontal line, a two-phase solid region everywhere except at pure A or pure B.

Figure
The binary eutectic phase diagram: two liquidus curves meeting at the eutectic point
composition, x(B) temperature eutectic E T*A T*B TE liquid + solid A liquid + solid B solid A + solid B pure A pure B

A second essential picture is the cooling curve: temperature versus time as a fixed-composition melt loses heat at constant rate. For a composition off the eutectic, the curve is smooth until it hits the liquidus, where a slope change (a "kink") appears as solid begins to form and releases latent heat. The slope stays shallower through the two-phase region, then the curve flattens into a plateau at TET_E while the remaining liquid freezes at constant temperature (a three-phase invariant), before dropping again once all liquid is gone. A melt of exactly the eutectic composition shows no kink at all, only a single plateau at TET_E, behaving thermally like a pure substance even though it is a mixture.

Figure
Cooling curves: off-eutectic composition shows a kink and a plateau; eutectic composition shows only a plateau
time T x(B) = 0.30, kink then plateau x(B) = x_E, plateau only liquidus T TE

The core relations

F=C−P+1(condensed phase rule, Ptotal fixed)F = C - P + 1 \quad \text{(condensed phase rule, } P_{\text{total}} \text{ fixed)}

where: FF = degrees of freedom, C=2C = 2 components, PP = number of phases present; pressure is fixed so the "+2" phase rule loses one degree of freedom.

ln⁡xA=−ΔfusHAR(1T−1TA∗)\ln x_A = -\frac{\Delta_{\text{fus}}H_A}{R}\left(\frac{1}{T} - \frac{1}{T_A^*}\right)

where: xAx_A = mole fraction of A in the liquid on the A-liquidus, ΔfusHA\Delta_{\text{fus}}H_A = molar enthalpy of fusion of pure A, TA∗T_A^* = melting point of pure A, TT = liquidus temperature.

nα=ntotal×x−xβxα−xβn_{\alpha} = n_{\text{total}}\times\frac{x - x_{\beta}}{x_{\alpha} - x_{\beta}}

where: lever rule giving moles of phase α\alpha at overall composition xx, with the tie-line endpoints at xαx_\alpha and xβx_\beta.

TE:xAliq(TE)∣A-liquidus=xAliq(TE)∣B-liquidusT_E: \quad x_A^{\text{liq}}(T_E)\big|_{\text{A-liquidus}} = x_A^{\text{liq}}(T_E)\big|_{\text{B-liquidus}}

where: the eutectic point is defined as the unique intersection of the two liquidus curves computed from each component's freezing-point-depression law.

Derivation ALocating the eutectic point from ideal-solution liquidus curves

Goal. Starting from the condition that solid A (or solid B) is in equilibrium with an ideal liquid solution, derive the liquidus curve for each component, then find their intersection, the eutectic.

Step 1. For solid A in equilibrium with liquid, equate chemical potentials:

μA∗(s)=μA∗(l)+RTln⁡xA\mu_A^{*}(\text{s}) = \mu_A^{*}(\text{l}) + RT\ln x_A

Here xAx_A is the mole fraction of A in the liquid (solid A is pure, so its activity is 1), and μA∗(l)\mu_A^{*}(\text{l}), μA∗(s)\mu_A^{*}(\text{s}) are the pure-component chemical potentials of liquid and solid A at temperature TT.

Step 2. Rearranging,

ln⁡xA=μA∗(s)−μA∗(l)RT=−ΔfusGA(T)RT\ln x_A = \frac{\mu_A^{*}(\text{s}) - \mu_A^{*}(\text{l})}{RT} = -\frac{\Delta_{\text{fus}}G_A(T)}{RT}

since μA∗(l)−μA∗(s)=ΔfusGA(T)\mu_A^{*}(\text{l}) - \mu_A^{*}(\text{s}) = \Delta_{\text{fus}}G_A(T), the molar Gibbs energy of fusion of pure A at temperature TT.

Step 3. Use the Gibbs–Helmholtz relation to convert ΔfusGA(T)\Delta_{\text{fus}}G_A(T), known exactly only at TA∗T_A^* where it is zero, into a temperature-dependent form, assuming ΔfusHA\Delta_{\text{fus}}H_A is constant over the small range considered:

ln⁡xA=−ΔfusHAR(1T−1TA∗)\ln x_A = -\frac{\Delta_{\text{fus}}H_A}{R}\left(\frac{1}{T} - \frac{1}{T_A^*}\right)

This is the A-liquidus: for any T<TA∗T < T_A^*, it gives the maximum mole fraction of A the liquid can hold while staying saturated with solid A. Equivalently it is the freezing-point-depression law applied all the way from dilute B to concentrated B.

Step 4. By identical reasoning for solid B, define xB=1−xAx_B = 1 - x_A on the B-liquidus:

ln⁡(1−xA)=−ΔfusHBR(1T−1TB∗)\ln(1-x_A) = -\frac{\Delta_{\text{fus}}H_B}{R}\left(\frac{1}{T} - \frac{1}{T_B^*}\right)

Step 5. The two curves are computed independently and both plotted against the same xAx_A axis. Physically only the lower branch of each is real — cooling a liquid rich in A follows the A-liquidus down; cooling a liquid rich in B follows the B-liquidus down. The point where the two expressions give the same TT for the same xAx_A is the point at which liquid is saturated in both solids simultaneously.

Step 6. At that intersection the phase rule confirms the physics: with C=2C = 2 and P=3P = 3 (liquid, solid A, solid B) at fixed pressure,

F=2−3+1=0F = 2 - 3 + 1 = 0

Zero degrees of freedom means temperature and composition are both pinned; this is the eutectic, an invariant point, not a line.

TE, xE solve simultaneously: Step 3 equation=Step 4 equation, at common (T,xA)\boxed{T_E,\ x_E \ \text{solve simultaneously: Step 3 equation} = \text{Step 4 equation, at common } (T,x_A)}

Worked examples

Example 1 — Foundational: locating a eutectic with ideal liquidus curves. Consider a simplified binary system of two organic solids, A and B, forming an ideal liquid solution with no solid solubility. Data: TA∗=400 KT_A^* = 400\ \text{K}, ΔfusHA=18.0 kJ mol−1\Delta_{\text{fus}}H_A = 18.0\ \text{kJ mol}^{-1}; TB∗=350 KT_B^* = 350\ \text{K}, ΔfusHB=12.0 kJ mol−1\Delta_{\text{fus}}H_B = 12.0\ \text{kJ mol}^{-1}. Find the eutectic temperature and composition. Step 1: write both liquidus equations.

ln⁡xA=−180008.314(1T−1400)\ln x_A = -\frac{18000}{8.314}\left(\frac{1}{T} - \frac{1}{400}\right)
ln⁡(1−xA)=−120008.314(1T−1350)\ln(1-x_A) = -\frac{12000}{8.314}\left(\frac{1}{T} - \frac{1}{350}\right)

Step 2: scan temperature to find where both give consistent, complementary mole fractions. Try T=320 KT = 320\ \text{K}: A-liquidus:

ln⁡xA=−2164.5(1320−1400)=−2164.5(0.003125−0.002500)=−1.353\ln x_A = -2164.5\left(\frac{1}{320}-\frac{1}{400}\right) = -2164.5(0.003125 - 0.002500) = -1.353
xA=e−1.353=0.259x_A = e^{-1.353} = 0.259

B-liquidus:

ln⁡(1−xA)=−1443.4(1320−1350)=−1443.4(0.003125−0.002857)=−0.387\ln(1-x_A) = -1443.4\left(\frac{1}{320}-\frac{1}{350}\right) = -1443.4(0.003125-0.002857) = -0.387
1−xA=e−0.387=0.679 ⇒ xA=0.3211-x_A = e^{-0.387} = 0.679 \ \Rightarrow\ x_A = 0.321

The two values (0.259 vs 0.321) don't yet agree; at T=320T=320 K the A-liquidus xAx_A is below the B-liquidus xAx_A, meaning we've gone slightly too cold. Try T=324 KT = 324\ \text{K}: A-liquidus: ln⁡xA=−2164.5(0.003086−0.002500)=−1.269\ln x_A = -2164.5(0.003086-0.002500) = -1.269, so xA=0.281x_A = 0.281. B-liquidus: ln⁡(1−xA)=−1443.4(0.003086−0.002857)=−0.330\ln(1-x_A) = -1443.4(0.003086-0.002857) = -0.330, so 1−xA=0.7191-x_A = 0.719, xA=0.281x_A = 0.281. The two agree to three significant figures at T≈324 KT \approx 324\ \text{K}. Result: TE≈324 K (51∘C)T_E \approx 324\ \text{K}\ (51^{\circ}\text{C}), xE(A)≈0.28x_E(\text{A}) \approx 0.28, xE(B)≈0.72x_E(\text{B}) \approx 0.72. Sanity check: TET_E lies below both TB∗T_B^* (350 K) and TA∗T_A^* (400 K), as required — the eutectic must be the lowest-melting point in the system. The eutectic composition sits closer to pure B, consistent with B's smaller ΔfusHB\Delta_{\text{fus}}H_B, which makes B's freezing point depress less steeply, pulling the crossing point toward higher xBx_B.

Example 2 — Applied: cooling curve, phase amounts, and the lever rule. A 100 g melt of composition xB=0.55x_B = 0.55 (using the same system as Example 1, with eutectic at xE=0.72x_E = 0.72 in B, TE=324 KT_E = 324\ \text{K}) is cooled slowly from 380 K to 300 K. Suppose at T=340 KT = 340\ \text{K} the B-liquidus gives the liquid composition as xBliq=0.60x_B^{\text{liq}} = 0.60 (solid B is the phase precipitating, since overall composition xB=0.55x_B=0.55 is less rich in B than the liquid, meaning we're on the B-liquidus side — reread: overall xB=0.55<xE=0.72x_B = 0.55 < x_E = 0.72 places this melt in the "A-rich" partition, so solid A crystallizes first as the melt cools below the A-liquidus). Correcting the setup for internal consistency: overall composition xB=0.55x_B = 0.55 lies between pure A (xB=0x_B=0) and the eutectic (xB=0.72x_B = 0.72), so this is on the A-liquidus side. As the melt cools, solid A begins to separate once TT drops to the A-liquidus temperature for xB=0.55x_B = 0.55 (i.e., xA=0.45x_A = 0.45). Step 1: find the temperature at which solid A first appears. Using the A-liquidus equation from Example 1 with xA=0.45x_A = 0.45:

ln⁡(0.45)=−2164.5(1T−1400)\ln(0.45) = -2164.5\left(\frac{1}{T}-\frac{1}{400}\right)
−0.799=−2164.5(1T−0.002500)-0.799 = -2164.5\left(\frac{1}{T}-0.002500\right)
1T−0.002500=3.69×10−4\frac{1}{T} - 0.002500 = 3.69\times10^{-4}
1T=0.002869 ⇒ T=348.6 K\frac{1}{T} = 0.002869 \ \Rightarrow\ T = 348.6\ \text{K}

So the cooling curve shows a kink at T=348.6 KT = 348.6\ \text{K}; above this, pure liquid; below, liquid + solid A. Step 2: find phase compositions and amounts at T=330 KT = 330\ \text{K}, using the lever rule. At 330 K, evaluate the A-liquidus to find the liquid composition:

ln⁡xA=−2164.5(1330−1400)=−2164.5(0.003030−0.002500)=−1.148\ln x_A = -2164.5\left(\frac{1}{330}-\frac{1}{400}\right) = -2164.5(0.003030-0.002500) = -1.148
xAliq=e−1.148=0.317,xBliq=0.683x_A^{\text{liq}} = e^{-1.148} = 0.317, \quad x_B^{\text{liq}} = 0.683

The tie-line at 330 K runs from pure solid A (xB=0x_B = 0) to liquid at xBliq=0.683x_B^{\text{liq}} = 0.683. Overall composition is xB=0.55x_B = 0.55. By the lever rule, the mole fraction of material that is liquid is:

fliq=xBoverall−xBsolid AxBliq−xBsolid A=0.55−00.683−0=0.805f_{\text{liq}} = \frac{x_B^{\text{overall}} - x_B^{\text{solid A}}}{x_B^{\text{liq}} - x_B^{\text{solid A}}} = \frac{0.55 - 0}{0.683 - 0} = 0.805

So 80.5% of the total moles remain liquid, and 19.5% have solidified as pure solid A. Step 3: convert to mass. Take molar masses MA=120 g mol−1M_A = 120\ \text{g mol}^{-1}, MB=140 g mol−1M_B = 140\ \text{g mol}^{-1}. Overall moles in 100 g at xB=0.55x_B=0.55: average molar mass =0.45(120)+0.55(140)=54+77=131 g mol−1= 0.45(120)+0.55(140) = 54+77=131\ \text{g mol}^{-1}, so ntotal=100/131=0.763 moln_{\text{total}} = 100/131 = 0.763\ \text{mol}. Moles solid A =0.195×0.763=0.1489 mol= 0.195 \times 0.763 = 0.1489\ \text{mol}, mass =0.1489×120=17.9 g= 0.1489\times120 = 17.9\ \text{g}. Moles liquid =0.805×0.763=0.614 mol= 0.805\times0.763 = 0.614\ \text{mol}, mass =100−17.9=82.1 g= 100 - 17.9 = 82.1\ \text{g} (by mass balance). Sanity check: As cooling continues toward TE=324 KT_E = 324\ \text{K}, more solid A must form and the liquid composition slides down the A-liquidus toward xEx_E; at exactly TET_E the remaining liquid (whatever fraction is left) has composition xE=0.72x_E = 0.72 and then freezes isothermally into eutectic solid, producing the plateau on the cooling curve. The amount of eutectic solid finally formed can be found the same way, by the lever rule at TE−T_E^-.

Limiting cases & common traps

SituationWhat actually happens
Overall composition exactly at xEx_ENo liquidus kink; cooling curve shows only the eutectic plateau, like a pure substance
Overall composition = pure A or pure BSharp single freezing point, no two-phase region at all
Partial solid solubility existsSolidus is no longer a flat line; a lens-shaped two-phase solid region appears, more like liquid–liquid diagrams
Congruent-melting compound presentDiagram splits into two eutectic sub-systems, each treated independently
Very slow cooling vs. rapid quenchRapid cooling can trap metastable, non-equilibrium (supercooled or amorphous) phases not shown on the equilibrium diagram

The chemist behind it

The term "eutectic," from the Greek eutektos meaning "easily melted," was coined in the 1880s by the British chemist Frederick Guthrie, who systematically studied freezing-point curves of salt mixtures. The theoretical grounding of the whole diagram, however, rests on the chemical potential and phase-rule framework developed by Josiah Willard Gibbs a decade earlier, later popularized and applied to metallurgy by scientists such as Gustav Tammann, whose triangulation method for constructing binary phase diagrams from cooling-curve data became standard practice in twentieth-century metallurgy.

Origins · 1 minJosiah Willard Gibbs and how this was discovered
JW
Josiah Willard Gibbs
1839–1903 · American mathematical physicist whose phase rule and chemical potential concept underlie every point on the eutectic diagram

Ask the tutor: How does this eutectic picture change once partial solid solubility or a peritectic reaction is introduced?

Why does the eutectic mixture melt at a lower temperature than either pure component

Dissolving component B into liquid A lowers A's chemical potential in the liquid phase relative to solid A, the same colligative effect behind ordinary freezing-point depression. The same happens in reverse for A dissolved in B. Because both liquidus curves descend from their respective pure melting points as the other component is added, they must cross somewhere below both TA∗T_A^* and TB∗T_B^*. That crossing, the eutectic, is therefore always the lowest-melting composition, exactly the same physics used to explain why salted ice melts below 0 degrees Celsius.

Is the eutectic solid a new phase or compound

No. It is a fine-grained, intimately mixed solid consisting of two separate, pure crystalline phases, solid A and solid B, that solidify simultaneously from the eutectic liquid. Under a microscope it often shows a lamellar or dendritic microstructure, but chemically it is just two phases in close contact, not one homogeneous phase. This distinguishes it from a true intermetallic compound, which would appear as its own distinct region on the phase diagram with its own melting point.

How do you read the overall composition and phase amounts off a eutectic diagram at some temperature inside a two-phase region

Draw a horizontal tie-line at that temperature across the two-phase region. Its two endpoints give the compositions of the two coexisting phases, read directly off the liquidus and the solid boundary (pure A or pure B, or the solidus if solid solubility exists). Then apply the lever rule: the fraction of each phase equals the length of the tie-line segment on the opposite side of the overall composition, divided by the total tie-line length.

What happens thermally if you cool a melt that is exactly at the eutectic composition

It behaves thermally like a pure substance, showing a single sharp arrest, a flat plateau, on its cooling curve at TET_E, with no preceding kink. Physically the liquid remains a single phase until TET_E, at which point solid A and solid B nucleate and grow together, releasing latent heat fast enough to hold temperature constant until all liquid is consumed. Only after the liquid is entirely gone does the temperature resume falling, now through the solid A + solid B two-phase field.

Can more than two solids and one eutectic point appear in a single binary phase diagram

Yes, if intermediate compounds form. A compound that melts congruently (retaining its own composition on melting) creates its own local maximum on the liquidus, effectively splitting the diagram into two separate simple eutectic systems side by side, each with its own eutectic point. Incongruent melting compounds produce a different feature, called a peritectic, which is governed by the same phase rule but has a different three-phase reaction (liquid + solid one to solid two) rather than freezing directly to two solids.

Before this