Kp Calculator (Equilibrium Constant in Pressure)

Calculate the equilibrium constant Kp from partial pressures. Convert between Kp and Kc using the ideal gas law. Find Δn and reaction quotient Qp.

Reactant Partial Pressures (atm)

Product Partial Pressures (atm)

Kp (calculated)
0.000e+0
From partial pressures entered
Kc (calculated)
0.000e+0
Kc = Kp / (RT)^Δn
Δn (gas)
-2
Moles products − moles reactants (gas)
ΔG° (kJ/mol)
0.00
Non-spontaneous forward
Total Pressure
0.00 atm
Sum of all partial pressures
Reaction Direction
At equilibrium
Qp vs known Kp comparison

Le Chatelier: Pressure Effect (Δn = -2)

Since Δn = -2 (< 0), increasing total pressure shifts equilibrium toward products (fewer gas moles). High pressure is favorable for product yield.

Kp vs Temperature (van\'t Hoff Illustration)

T (K)1/T × 10³ln(Kp) approxKp factor
2005.000.001.000
3003.330.001.000
4002.500.001.000
5002.000.001.000
6001.670.001.000
8001.250.001.000
10001.000.001.000

Kp Values for Common Reactions

ReactionT (°C)KpΔn
N₂ + 3H₂ ⇌ 2NH₃256.0 × 10⁵-2
N₂ + 3H₂ ⇌ 2NH₃5006.0 × 10⁻²-2
2SO₂ + O₂ ⇌ 2SO₃253.4 × 10²⁴-1
H₂ + I₂ ⇌ 2HI425540
2NO₂ ⇌ N₂O₄256.7-1
CO + H₂O ⇌ CO₂ + H₂251.0 × 10⁵0
CaCO₃ ⇌ CaO + CO₂9001.041
Planning notes, formulas, and examples

About the Kp Calculator (Equilibrium Constant in Pressure)

The equilibrium constant Kp expresses the ratio of partial pressures of products to reactants at chemical equilibrium for gas-phase reactions. For a general reaction aA + bB ⇌ cC + dD, Kp = (P_C^c × P_D^d) / (P_A^a × P_B^b), where each P represents the partial pressure in atmospheres (or bar) and the exponents are stoichiometric coefficients.

Kp is related to the concentration-based equilibrium constant Kc through the equation Kp = Kc(RT)^Δn, where Δn is the change in moles of gas (products minus reactants), R is the gas constant, and T is the absolute temperature. When Δn = 0, Kp = Kc. This relationship is fundamental for converting between pressure and concentration expressions of equilibrium.

Understanding Kp is essential for predicting the direction of gas-phase reactions, calculating equilibrium compositions at different temperatures and pressures, and applying Le Chatelier's principle. Industrial processes like the Haber process (ammonia synthesis), sulfuric acid production, and methanol synthesis all depend on accurate Kp calculations for optimizing yield and operating conditions.

When This Page Helps

Essential for chemical engineering, gas-phase reaction design, and chemistry courses. Quickly calculate equilibrium constants, convert between Kp and Kc, predict reaction direction, and explore how conditions affect gas-phase equilibria.

How to Use the Inputs

  1. Select a reaction preset or enter custom stoichiometric coefficients.
  2. Input the partial pressures of each species at equilibrium.
  3. View the calculated Kp and the reaction quotient Qp.
  4. Enter temperature to convert between Kp and Kc.
  5. Use Δn to understand how pressure changes affect equilibrium.
  6. Compare Qp with Kp to predict reaction direction.
  7. Explore different temperatures to see how Kp changes.
Formula used
Kp = Π(P_products^coefficients) / Π(P_reactants^coefficients). Kp-Kc relationship: Kp = Kc × (RT)^Δn, where Δn = Σ(product moles) − Σ(reactant moles), R = 0.08206 L·atm/(mol·K), T in Kelvin. ΔG° = −RT ln Kp gives the standard Gibbs free energy.

Example Calculation

Result: Kp = 9.26 × 10⁻³

For N₂ + 3H₂ ⇌ 2NH₃: Kp = (0.5)² / (1 × 3³) = 0.25/27 = 9.26 × 10⁻³. Since Δn = 2 − 4 = −2, increasing pressure shifts equilibrium toward products (fewer moles of gas).

Tips & Best Practices

  • Always use consistent pressure units — Kp values differ if you use atm vs. bar vs. Pa.
  • Remember that pure solids and liquids are NOT included in Kp expressions.
  • For the Haber process (N₂ + 3H₂ ⇌ 2NH₃), Δn = −2, so high pressure favors ammonia.
  • ΔG° = −RT ln Kp relates the equilibrium constant to the Gibbs free energy change.
  • At very high or low temperatures, Kp can change by many orders of magnitude.
  • When Kp >> 1, the reaction goes essentially to completion; when Kp << 1, very little product forms.

Industrial Applications of Kp

The Haber-Bosch process for ammonia synthesis (N₂ + 3H₂ ⇌ 2NH₃) operates at 400-500°C and 150-300 atm. Despite the reaction being exothermic, high temperature is needed for kinetics while high pressure compensates for the unfavorable Kp at elevated temperatures. Understanding the interplay between Kp, temperature, and pressure is crucial for optimizing industrial processes. Similar considerations apply to sulfuric acid production (2SO₂ + O₂ ⇌ 2SO₃), methanol synthesis, and Fischer-Tropsch processes.

Van't Hoff Equation and Temperature Dependence

The van't Hoff equation relates Kp at two temperatures: ln(K₂/K₁) = −ΔH°/R × (1/T₂ − 1/T₁). Plotting ln(Kp) vs. 1/T gives a straight line with slope −ΔH°/R. This is a powerful tool for determining reaction enthalpies from equilibrium data and for extrapolating Kp to new temperatures. For reactions where ΔH° changes significantly with temperature, the integrated form with heat capacity corrections is needed.

Thermodynamic Equilibrium Constants

Strictly, the thermodynamic equilibrium constant K° is dimensionless and defined in terms of activities rather than pressures. For ideal gases, activity equals P/P° where P° = 1 bar (or 1 atm in older conventions). The distinction matters when calculating ΔG° = −RT ln K°, which requires a dimensionless K. In practice, Kp calculated with pressures in the standard unit (bar or atm) equals K° for ideal gas mixtures.

Sources & Methodology

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Frequently Asked Questions

  • Kp uses partial pressures (in atm or bar) while Kc uses molar concentrations (mol/L). They're related by Kp = Kc(RT)^Δn. When Δn = 0, they're equal.