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Wet-process phosphoric acid: electrochemical removal of copper and cadmium

Phosphoric acidElectrochemistryElectrowinningPurificationCadmium removalFertilizer
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Wet-process phosphoric acid (about 42 wt% H3PO4, 10 kg/s) carries the metals its phosphate rock brought in: iron, zinc, nickel, copper and the cadmium that limits how the acid may be used in fertilizer. Two flow-through electrochemical cells remove the two noble enough to plate from strong acid. The first holds its cathode at -0.05 V vs SHE: copper's Nernst potential sits far above that, so copper plates at its mass-transfer limit (plug-flow law, 99% removed) while zinc, nickel, iron and cadmium, whose potentials lie below the cathode, stay dissolved. The second cell runs at -0.55 V and is told that only cadmium plates: mass transfer alone would take 99.4% of it, but at that potential and 323 K the Nernst floor holds about 2.6e-5 mol/L in solution, so the solver reports the equilibrium-limited 91% instead. Each cell's current comes from the metal's partial current and the current efficiency you give it; the copper and cadmium currents regenerate phosphoric acid (one proton per dihydrogen-phosphate counter-ion), and the rest of the charge evolves hydrogen beside the anode's oxygen, which the cell gas reports, with a flammability warning. Honesty notes: (1) the impurity levels are illustrative inputs, not a measured acid analysis; (2) iron-group metals (Fe, Ni) are thermodynamically able to plate at -0.55 V but deposit from strong acid only with large kinetic overpotentials that a thermodynamic ordering cannot see, so the second cell is restricted to cadmium by the user, not by the model; (3) the mass-transfer coefficient, cathode area, current efficiencies and cell voltages are illustrative inputs for a three-dimensional flow-through cathode, to be replaced with measured cell data; (4) real wet-process acid holds its iron mostly as Fe(III), whose reduction to Fe(II) at the cathode consumes current, and that shuttle is represented only through the low current efficiencies given; and (5) activity coefficients are taken as one, so the Nernst potentials order the metals rather than fix their electrode potentials.

The flowsheet

The solved topology — every unit op's real duty, conversion, or split, read straight off a genuine converged solve.

WPA
electrolyte
spent
cathode
gas
EW CU
Copper Cathode
CU CELL GAS
electrolyte
spent
cathode
gas
EW CD
Cadmium Cathode
CD CELL GAS
Purified ACID

The stream table

Every stream's flow, temperature, pressure, and composition — real converged numbers, not placeholders.

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