Comprehensive Guide to Electrolysis and Faraday's Laws
Electrolysis is a fundamental electrochemical process in which non-spontaneous chemical reactions are driven by the passage of a direct electric current through an electrolyte. In contrast to galvanic cells where spontaneous redox reactions produce electricity, an electrolytic cell uses an external electrical power supply to induce chemical change. The process is used in industrial applications such as aluminum smelting (Hall-Héroult process), electroplating of protective metal coatings, chlorine and sodium hydroxide synthesis (chlor-alkali industry), and high-purity hydrogen gas production for clean energy storage.
The quantitative relationship governing electrolytic deposition was discovered experimentally by the English scientist Michael Faraday in 1834. Known as Faraday's Laws of Electrolysis, these principles established the first direct link between macroscopic electric charge and microscopic chemical stoichiometry, anticipating the discovery of the electron by more than six decades. Understanding these laws allows electrochemists to accurately predict the mass of metal plated, the total coulombs required, and the volumetric output of evolved gases, topics closely aligned with our Cell EMF Calculator – Electromotive Force of a Cell.
Mathematical Formulations of Faraday's Laws
1. Faraday's First Law of Electrolysis
Faraday's First Law states that the mass of a substance liberated or deposited at an electrode during electrolysis is directly proportional to the total quantity of electric charge passed through the solution:
Where:
- m: Mass of the substance deposited or liberated at the electrode (grams).
- Q: Total electric charge passed through the electrolyte, measured in Coulombs (C), where
Q = I * t. - I: Direct electric current flowing through the circuit (Amperes).
- t: Total electrolysis time (seconds).
- Z: The electrochemical equivalent (ECE) of the substance, defined as the mass in grams deposited by one Coulomb of charge (g/C).
2. Faraday's Second Law and the Combined Formulation
Faraday's Second Law states that when the same quantity of electric charge passes through different electrolytes, the masses of the elements deposited are directly proportional to their equivalent weights (molar mass divided by valency):
Combining both laws into a single equation relates mass directly to electric current, time, molar mass, and electron stoichiometry:
Where:
- M: Molar mass of the liberated substance in grams per mole (g/mol), verified with our Molar Mass Calculator.
- z: Valency number or number of electrons transferred per ion (for example, z = 2 for Cu²⁺ + 2e⁻ → Cu, and z = 1 for Ag⁺ + e⁻ → Ag).
- F: Faraday's Constant = 96,485.3321 C/mol of electrons. This constant represents the total electric charge carried by one mole of elementary electrons, derived from Avogadro's number multiplied by elementary charge ($F = N_A \cdot e$).
- η: Faradaic current efficiency (expressed as a fraction between 0.0 and 1.0, or 0% to 100%). In real industrial cells, side reactions (such as simultaneous hydrogen evolution during metal plating) consume a fraction of the current, reducing actual yield below 100%.
3. Molar Quantity and Gas Volume at STP
By dividing the deposited mass by its molar mass, we obtain the chemical moles ($n$) of substance produced, an operation explored in our Grams to Moles Calculator:
For gaseous products liberated at electrodes (such as hydrogen gas, H₂, at the cathode, or oxygen, O₂, and chlorine, Cl₂, at the anode), the volume produced under Standard Temperature and Pressure (STP, defined as 0 °C and 1.000 atm where one mole of ideal gas occupies 22.414 L) is computed using our STP Calculator (Standard Temperature and Pressure):
Step-by-Step Practical Calculation Examples
Worked Example 1: Industrial Electroplating of Copper
A decorative copper electroplating bath processes automotive parts using a current of 5.00 Amperes for 45.0 minutes. The plating solution contains copper(II) sulfate (CuSO₄, providing Cu²⁺ ions with $z = 2$). The bath operates at a Faradaic current efficiency of 95.0%. Determine the total mass of pure copper deposited onto the cathode.
- Convert Time into Seconds:
t = 45.0 minutes * 60 seconds/minute = 2,700 seconds - Calculate Total Charge Passed (Q):
Q = I * t = 5.00 A * 2,700 s = 13,500 Coulombs - Identify Substance Constants:
Molar mass of Copper ($M$) = 63.546 g/mol
Electrons transferred ($z$) = 2
Faraday's Constant ($F$) = 96,485.33 C/mol
Efficiency ($\eta$) = 95.0% = 0.950 - Apply the Electrolysis Formula:
m = (13,500 C * 63.546 g/mol * 0.950) / (2 * 96,485.33 C/mol)
m = 814,977.45 / 192,970.66 = 4.223 grams
Conclusion: Approximately 4.22 grams of copper plates out onto the cathode. The remaining 5% of electric charge is consumed by parasitic reactions, primarily minor proton reduction to hydrogen gas.
Worked Example 2: Water Electrolysis for Green Hydrogen Generation
An alkaline water electrolyzer operates at a current of 100.0 Amperes for 3.00 hours at 98.0% current efficiency. Determine the volume of pure hydrogen gas ($H_2$) liberated at the cathode at STP.
- Cathode Half-Reaction: 2H₂O + 2e⁻ → H₂(g) + 2OH⁻ (Thus, $z = 2$ electrons per mole of H₂ gas).
- Convert Time into Seconds:
t = 3.00 hours * 3,600 seconds/hour = 10,800 seconds - Compute Moles of Hydrogen Produced:
n = (I * t * η) / (z * F)
n = (100.0 A * 10,800 s * 0.980) / (2 * 96,485.33 C/mol)
n = 1,058,400 / 192,970.66 = 5.4848 moles of H₂ - Calculate Volume at STP:
V = n * 22.414 L/mol = 5.4848 mol * 22.414 L/mol = 122.94 Liters
Conclusion: The electrolyzer yields approximately 122.9 liters of clean hydrogen gas. Simultaneously, the anode liberates exactly half that volume of oxygen gas (61.47 L), because oxygen evolution requires 4 electrons ($z = 4$).
Electrochemical Equivalents Reference Data
The table below presents molar masses, electron requirements, and electrochemical equivalents ($Z$) for common elements during electrolysis:
| Chemical Species | Half-Reaction at Electrode | Molar Mass (g/mol) | Valency (z) | ECE Z (mg/C) | Deposition Rate (g/A-hr) |
|---|---|---|---|---|---|
| Silver (Ag) | Ag⁺ + e⁻ → Ag | 107.87 | 1 | 1.1180 | 4.0247 |
| Gold (Au) | Au³⁺ + 3e⁻ → Au | 196.97 | 3 | 0.6805 | 2.4497 |
| Copper (Cu) | Cu²⁺ + 2e⁻ → Cu | 63.55 | 2 | 0.3293 | 1.1855 |
| Nickel (Ni) | Ni²⁺ + 2e⁻ → Ni | 58.69 | 2 | 0.3041 | 1.0949 |
| Zinc (Zn) | Zn²⁺ + 2e⁻ → Zn | 65.38 | 2 | 0.3388 | 1.2197 |
| Tin (Sn) | Sn²⁺ + 2e⁻ → Sn | 118.71 | 2 | 0.6152 | 2.2146 |
| Chromium (Cr) | Cr³⁺ + 3e⁻ → Cr | 52.00 | 3 | 0.1796 | 0.6467 |
| Aluminum (Al) | Al³⁺ + 3e⁻ → Al | 26.98 | 3 | 0.0932 | 0.3356 |
| Hydrogen (H₂) | 2H⁺ + 2e⁻ → H₂ | 2.016 | 2 | 0.0104 | 0.0376 |
| Oxygen (O₂) | 2H₂O → O₂ + 4H⁺ + 4e⁻ | 32.00 | 4 | 0.0829 | 0.2985 |
| Chlorine (Cl₂) | 2Cl⁻ → Cl₂ + 2e⁻ | 70.91 | 2 | 0.3674 | 1.3228 |
Electrolytic Cell Mechanics vs. Galvanic Cells
While both galvanic and electrolytic cells rely on redox processes, their operational principles and electrical polarities are distinct:
- Energy Flow: Galvanic cells convert spontaneous chemical free energy into electricity ($\Delta G < 0$). Electrolytic cells use external electrical work to drive non-spontaneous transformations ($\Delta G > 0$).
- Anode Polarity: Oxidation occurs at the anode in both systems. However, in an electrolytic cell, the anode connects to the positive terminal (+) of the DC power supply, which pulls electrons away from chemical species in solution.
- Cathode Polarity: Reduction occurs at the cathode in both systems. In an electrolytic cell, the cathode connects to the negative terminal (-) of the DC supply, which pumps electrons into the electrode to reduce cations.
- Overpotential: The actual cell voltage required for electrolysis always exceeds the theoretical thermodynamic cell potential due to kinetic resistance, bubble polarization, and solution ohmic drop, parameters related to reaction barriers evaluated in our Activation Energy Calculator.
Industrial Applications of Electrolysis
Modern chemical synthesis and metallurgy rely on large-scale electrolysis systems:
- Electrowinning and Electrorefining: Impure copper anodes dissolve in acidic sulfate baths and re-deposit on cathodes with purities exceeding 99.99%, removing impurities like silver and gold.
- Molten Salt Electrolysis: Highly reactive metals with standard reduction potentials more negative than water (like sodium, potassium, and aluminum) cannot be plated from aqueous solutions because water reduces first. They are isolated by electrolyzing molten salts, such as molten cryolite-alumina mixtures.
- Electroplating: Thin layers of noble or corrosion-resistant metals (gold, silver, nickel, chrome) deposit onto base substrates (steel, brass, plastics) to enhance wear resistance and appearance.
- Water Splitting: Using renewable electricity to split water into hydrogen and oxygen provides emission-free fuel, analyzed alongside kinetic rates in our Arrhenius Equation Calculator.
Frequently Asked Questions (FAQ)
F = e * N_A = 96,485.3321 C/mol.V = (n * R * T) / P, accounting for the vapor pressure of water if the gas is collected over an aqueous solution.Z = M / (z * F) and is typically expressed in milligrams per Coulomb (mg/C) or grams per Coulomb (g/C).d = m / (A * \rho). Controlling the current, time, and bath efficiency allows precise deposit thickness from nanometers to hundreds of micrometers.