Selective Precipitation Simulator: pH-Controlled Metal Separation

simulator intermediate ~10 min
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Fe: 99.9% removed — Cu, Zn, Ni remain in solution

At pH 3.5 and 40°C, iron precipitates as Fe(OH)₃ at 99.9% removal while copper (0.1%), zinc (0%), and nickel (0%) remain dissolved — achieving clean iron/copper separation.

Formula

Ksp = [M^n+] · [OH⁻]^n — solubility product expression
pH_precip = (1/n)·(pKsp - log[M^n+] - n·pKw) — onset of precipitation
[M^n+] = Ksp / [OH⁻]^n — residual metal in solution at given pH

Precipitation as Separation

Selective precipitation is one of the oldest and most reliable techniques in hydrometallurgy. By raising the pH of a multi-metal solution with lime or caustic soda, metals can be knocked out of solution one by one, exploiting the vast differences in their hydroxide solubility products. Iron, with its extremely insoluble Fe(OH)₃, falls out first at pH 3–4. Copper follows at pH 5–6, then zinc and nickel at pH 7–9. This pH staircase is the basis for purifying leach solutions before electrowinning.

Solubility Product Chemistry

The solubility product Ksp defines the equilibrium between a solid precipitate and its dissolved ions. For a metal hydroxide M(OH)n, Ksp = [M^n+][OH⁻]^n. This means the residual metal concentration in solution depends on [OH⁻] raised to the power n — trivalent metals like Fe³⁺ are far more sensitive to pH changes than divalent metals like Cu²⁺. The logarithmic relationship between pH and solubility creates the characteristic S-shaped precipitation curves shown in this simulation.

Industrial pH Windows

In zinc plant practice, the pregnant leach solution first passes through an iron precipitation stage at pH 3.5 using limestone, producing a jarosite or goethite residue. The iron-free solution then undergoes cementation (zinc dust purification) to remove Cu, Co, and Cd. Separate circuits use careful pH staging: copper at pH 2–3 with H₂S gas, cobalt at pH 4–5 with α-nitroso-β-naphthol. Each precipitation window must be precisely maintained to maximize selectivity and minimize co-precipitation losses.

Beyond Hydroxide Precipitation

While hydroxide precipitation is the most common method, sulfide precipitation offers superior selectivity. Metal sulfide Ksp values span an even wider range than hydroxides, enabling separation of metals with similar hydroxide precipitation pH values. Copper sulfide (Ksp ~10⁻³⁶) precipitates at pH as low as 1, far below zinc sulfide (Ksp ~10⁻²⁵). This simulator focuses on hydroxide chemistry but the principles extend directly to sulfide, carbonate, and phosphate precipitation systems.

FAQ

What is selective precipitation?

Selective precipitation exploits the different solubility products (Ksp) of metal hydroxides or sulfides. By carefully controlling pH, metals can be removed from solution in sequence — iron first (pH 3–4), then copper (pH 5–6), then zinc and nickel (pH 7–9). The technique is fundamental to hydrometallurgical purification and wastewater treatment.

Why does iron precipitate before copper?

Iron(III) hydroxide has an extremely low Ksp of 2.8×10⁻³⁹, meaning it becomes insoluble at much lower pH than copper hydroxide (Ksp = 2.2×10⁻²⁰). This 19 orders-of-magnitude difference provides a comfortable pH window for selective separation. Oxidizing Fe²⁺ to Fe³⁺ before precipitation dramatically improves this selectivity.

What reagents are used for pH adjustment?

Limestone (CaCO₃) is the cheapest option but limited to pH ~6. Lime (CaO/Ca(OH)₂) reaches higher pH and is widely used. Sodium hydroxide (NaOH) provides precise control but is expensive. Magnesia (MgO) is used where calcium contamination must be avoided, particularly in nickel circuits.

What is co-precipitation and why is it a problem?

Co-precipitation occurs when a non-target metal is trapped within, adsorbed onto, or occluded in the precipitate of another metal. For example, copper can co-precipitate with iron hydroxide, causing metal losses. Slow, controlled precipitation, staged pH adjustment, and re-pulping can minimize co-precipitation losses.

Sources

Embed

<iframe src="https://homo-deus.com/lab/hydrometallurgy/precipitation/embed" width="100%" height="400" frameborder="0"></iframe>
View source on GitHub