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Library / Foundations: Chemistry / FCH-27

Foundations: Chemistry

Equilibrium constant Kp from partial pressures

Equilibrium constant of a gas reaction written with partial pressures, in the common school convention.

Ref
FCH-27
Rev
v1
Field
Foundations: Chemistry
Result
Kp

For a gas-phase reaction aA + bB ⇌ cC + dD at equilibrium, Kp = (pCc pDd)/(pAa pBb), where each p is the equilibrium partial pressure and each exponent is the coefficient in the balanced equation. Here the pressures are taken in bar relative to a 1 bar standard state, so Kp has no unit; with other pressure units its unit depends on Δn = (c + d) − (a + b). It depends only on temperature. Put 0 for the exponent of a species that is not in the reaction.

Equilibrium constant of a gas reaction written with partial pressures, in the common school convention. Its units follow from the powers; use only gases, since pure solids and liquids are left out.

Calculator

Solve for
bar
0.01100
bar
0.01100
bar
0.01100
bar
0.01100
06
06
06
06
  • Change in moles of gas, Δn = (c + d) − (a + b)−2
  • ln Kp−5.257
  • Standard Gibbs energy change at 298 K, −RT ln Kp13.03 kJ/mol

What drives the result

Each variable is moved across its typical range while the others stay at the values above. The longest bar is the key driver.

Equilibrium constant Kp () current value 0.005208
pBPartial pressure of BKey driver
1.13e-61,120,000
pCPartial pressure of C
2.31e-723.1
bCoefficient of B
2.41e-51.13
pAPartial pressure of A
1.04e-41.04
cCoefficient of C
0.002310.0264
aCoefficient of A
1.63e-40.0104
pDPartial pressure of D
dCoefficient of D (0 if there is no D)
  • With these pressures Kp = 0.005208. A value well below 1 means the mixture is mostly reactants; well above 1, mostly products. The standard Gibbs energy change at 298 K is 13 kJ/mol.
  • The equilibrium constant depends only on temperature: changing the total pressure shifts the pressures, but they shift together so that the same Kp is restored.
Chart data as tables

Ranked variables

VariableTypical rangeLowest resultHighest resultSwing ()Local stepChange in result
pB Partial pressure of B0.01 to 100 bar1.125e-61,125,0001,125,000+10%−24.9 %
pC Partial pressure of C0.01 to 100 bar2.315e-723.1523.15+10%+21 %
b Coefficient of B0 to 6 2.411e-51.1251.125+1 −83.3 %
pA Partial pressure of A0.01 to 100 bar1.042e-41.0421.042+10%−9.09 %
c Coefficient of C0 to 6 0.0023150.026370.02405+1 +50 %
a Coefficient of A0 to 6 1.628e-40.010420.01025+1 −50 %
pD Partial pressure of D0.01 to 100 bar0.0052080.0052080+10%0 %
d Coefficient of D (0 if there is no D)0 to 6 0.0052080.0052080+1 0 %

Sweep of Partial pressure of C

Partial pressure of C (bar)Equilibrium constant Kp
0.012.315e-7
0.031622.315e-6
0.12.315e-5
0.31622.315e-4
10.002315
3.1620.02315
100.2315
31.622.315
10023.15

Sweep one variable

Equilibrium constant Kp ()Hover, touch, or use the arrow keys on the chart
05101520 0.010.1110100 Partial pressure of C (bar), log scale now 0.005208

Variables and how each one contributes

Kp

Equilibrium constant Kp

Result ·

What the equation gives you. Everything else feeds it.

pA

Partial pressure of A

bar · typical 0.01 to 100

Equilibrium partial pressure of reactant A, in bar. Lowers Kp, because pAa is in the denominator; the larger the exponent a, the stronger the effect. Raising it by 0.5 bar (to 2.5 bar) moves the result by −20 %, from 0.005208 to 0.004167.

pB

Partial pressure of B

bar · typical 0.01 to 100

Equilibrium partial pressure of reactant B, in bar. Lowers Kp, because pBb is in the denominator; with a coefficient of 3 on B the effect is strong. Raising it by 0.5 bar (to 6.5 bar) moves the result by −21.3 %, from 0.005208 to 0.004096.

pC

Partial pressure of C

bar · typical 0.01 to 100

Equilibrium partial pressure of product C, in bar. Raises Kp, because pCc is in the numerator; the larger the exponent c, the stronger the effect. Raising it by 0.25 bar (to 1.75 bar) moves the result by +36.1 %, from 0.005208 to 0.007089.

pD

Partial pressure of D

bar · typical 0.01 to 100

Equilibrium partial pressure of product D, in bar. It has no effect while its exponent d is 0. Has no effect while d = 0, and raises Kp with the power d when d is above 0. Raising it by 0.25 bar (to 1.25 bar) moves the result by +0 %, from 0.005208 to 0.005208.

a

Coefficient of A

· typical 0 to 6

Stoichiometric coefficient of A, a whole number (0 if absent). Lowers Kp when pA is above 1 bar and raises it when below, because pAa grows or shrinks with the exponent. Raising it by 1 (to 2) moves the result by −50 %, from 0.005208 to 0.002604.

b

Coefficient of B

· typical 0 to 6

Stoichiometric coefficient of B, a whole number (0 if absent). Lowers Kp when pB is above 1 bar and raises it when below. Raising it by 1 (to 4) moves the result by −83.3 %, from 0.005208 to 8.681×10−4.

c

Coefficient of C

· typical 0 to 6

Stoichiometric coefficient of C, a whole number (0 if absent). Raises Kp when pC is above 1 bar and lowers it when below. Raising it by 1 (to 3) moves the result by +50 %, from 0.005208 to 0.007813.

d

Coefficient of D (0 if there is no D)

· typical 0 to 6

Stoichiometric coefficient of D, a whole number (0 if absent). Has no effect when pD is 1 bar, raises Kp when pD is above 1 bar and lowers it when below. Raising it by 1 (to 1) moves the result by +0 %, from 0.005208 to 0.005208.

Worked example with the values above

  1. Products: pC2 × pD0 = 2.25 × 1 = 2.25.
  2. Reactants: pA1 × pB3 = 2 × 216 = 432.
  3. Kp = 2.25 / 432 = 0.005208.

Assumptions and limits

  • Ideal gases at equilibrium, with partial pressures in bar against a 1 bar standard state.
  • Exponents equal to the stoichiometric coefficients of the balanced equation, and a single temperature.

Common mistakes

  • Including solids or pure liquids in the expression: they are left out.
  • Using initial rather than equilibrium pressures.
  • Mixing pressure units and then quoting Kp as dimensionless.

Statistics and uncertainty

Equilibrium pressures are measured to a few per cent, and each is raised to its coefficient, so the relative error in Kp is the sum of the coefficient-weighted relative errors: with a coefficient of 3 on B, a 2 % error in pB becomes a 6 % error in Kp.

Where it is used

  • Predicting the composition of a gas mixture at equilibrium.
  • Finding the equilibrium constant from measured partial pressures, for example in a synthesis or combustion product mix.

Maths you need

  • Partial pressure: the share of the total pressure from one gas
  • Balanced equation: the coefficients give the exponents

Related formulas

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