Recently, while studying the concept of chemical equilibrium, I came across the following statement in my textbook:

An increase in pressure favours the side of an equilibrium reaction that has the smaller number of gas molecules.

While there’s a simple explanation for why this statement holds true using Le Chatelier’s principle, I thought it’d be a fun exercise to convince myself of the statement via a different, more convoluted route: deducing the expected direction of the shift via comparing the equilibrium constant KcK_c with the reaction quotient QQ.

Idea

In general, the reaction quotient QQ tends toward the equilibrium constant KcK_c. Concretely, if Q<KcQ < K_c then the products are favored and conversely if Q>KcQ > K_c the reactants are favored. Thus, if we can somehow show that, in the event of an increase in pressure, QQ is greater than KcK_c if and only if there are fewer moles of gas on the reactant side (and similar for the case where QQ is smaller), then we’ll have proven the claim. Let’s try that!

Analysis

Consider the general reaction

aAX(g)+bBX(g)+rRX(g)+sSX(g)+ \ce{aA_{(g)} + bB_{(g)} + \dots <=> rR_{(g)} + sS_{(g)} + \dots}

where AA, BB, \dots denote the reactants and RR, SS, \dots the products.

Suppose the system is currently in equilibrium. Then the initial reaction quotient Q0Q_0 and the equilibrium constant KcK_c must be equal, so

Q0=Kc=[R]r[S]s[A]a[B]b.(1) Q_0 = K_c = \frac{[R]^r[S]^s\cdots}{[A]^a[B]^b\cdots}. \tag{1}

Our goal is to express the reaction quotient as a function of the total pressure of the system, say P0P_0. Recall that concentration c=n/Vc = n/V where nn is the number of moles and VV is the volume. Rearranging the ideal gas law PV=nRTPV = nRT for n/Vn/V yields

nV=PRT=c.(2) \frac{n}{V} = \frac{P}{RT} = c. \tag{2}

We cannot directly substitute this back into Equation 1 yet as each gas has its own partial pressure —that is, the PP for each gas is different. To account for this, we use

pX=ptotnXntot p_X = p_{\mathrm{tot}} \frac{n_X}{n_{\mathrm{tot}}}

that is, the partial pressure is the total pressure scaled by the mole fraction. Combining this with Equation 2 yields an expression for the concentration of any gas (say XX) participating in the reaction in terms of the total pressure of the system:

cX=[X]=pXRT=P0ntotRTnX(3) c_X = [X] = \frac{p_X}{RT} = \frac{P_0n_{\mathrm{tot}}}{RTn_X} \tag{3}

Substituting the final expression for concentration into Equation 1 and factoring out the part dependent on pressure, we get

Q0=Kc=(P0ntotRTnR)r(P0ntotRTnS)s(P0ntotRTnA)a(P0ntotRTnB)b=P0r+s+P0a+b+(ntotRTnR)r(ntotRTnS)s(ntotRTnA)a(ntotRTnB)b. \begin{align*} Q_0 = K_c &= \cfrac{\left(\cfrac{P_0n_{\mathrm{tot}}}{RTn_R}\right)^r\left(\cfrac{P_0n_{\mathrm{tot}}}{RTn_S}\right)^s\cdots}{\left(\cfrac{P_0n_{\mathrm{tot}}}{RTn_A}\right)^a\left(\cfrac{P_0n_{\mathrm{tot}}}{RTn_B}\right)^b\cdots} \\\\ &= \cfrac{{P_0}^{r + s + \dots}}{{P_0}^{a + b + \dots}} \cfrac{\left(\cfrac{n_{\mathrm{tot}}}{RTn_R}\right)^r\left(\cfrac{n_{\mathrm{tot}}}{RTn_S}\right)^s\cdots}{\left(\cfrac{n_{\mathrm{tot}}}{RTn_A}\right)^a\left(\cfrac{n_{\mathrm{tot}}}{RTn_B}\right)^b\cdots}. \tag{4} \end{align*}

(As an aside: Substituting the expression for concentration in terms of partial pressure instead gives us a rather interesting link to the equilibrium constant using partial pressures.)

For brevity write

Δn=(r+s+)tot. num of product moles(a+b+)_tot. num of reactant moles(5) \Delta n = \overbrace{(r + s + \cdots)}^{\text{tot. num of product moles}} - \underbrace{(a + b + \cdots)}\_{\text{tot. num of reactant moles}} \tag{5}

such that the pressure factor in front is just P0Δn{P_0}^{\Delta n}. Also abbreviate the constant factor as kk,

k=(ntotRTnR)r(ntotRTnS)s(ntotRTnA)a(ntotRTnB)b k = \cfrac{\left(\cfrac{n_{\mathrm{tot}}}{RTn_R}\right)^r\left(\cfrac{n_{\mathrm{tot}}}{RTn_S}\right)^s\cdots}{\left(\cfrac{n_{\mathrm{tot}}}{RTn_A}\right)^a\left(\cfrac{n_{\mathrm{tot}}}{RTn_B}\right)^b\cdots}

so that Equation 4 simplifies to just

Q0=Kc=kP0Δn.(6) Q_0 = K_c = k{P_0}^{\Delta n}. \tag{6}

Now consider what happens when the pressure is increased to P1P_1. The equilibrium constant KcK_c does not change since it is only affected by temperature. What about the reaction quotient, Q1Q_1? The factor kk from Equation 6 remains the same, so the only change is replacing P0P_0 with P1P_1:

Q1=kP1Δn. Q_1 = k{P_1}^{\Delta n}.

Evidently the reaction quotient Q1Q_1 is no longer equal to the equilibrium constant, so the equilibrium position will shift to restore equilibrium. To determine whether the forward or reverse reaction will be favored, we need to compare Q1Q_1 to KcK_c. Let us examine the case where Q1<KcQ_1 < K_c:

Q1<KckP1Δn<kP0ΔnP1Δn<P0Δn. \begin{align*} Q_1 &< K_c \\\\ kP_1^{\Delta n} &< kP_0^{\Delta n} \\\\ P_1^{\Delta n} &< P_0^{\Delta n}. \end{align*}

Since P1>P0P_1 > P_0, this can only be the case if Δn<0\Delta n < 0. But we defined Δn\Delta n as the difference between the total moles of gas on the product side and the total moles of gas on the reactant side, so

Δn<0nproductsnreactants<0nproducts<nreactants. \begin{align*} \Delta n &< 0 \\\\ \sum n_{\rm{products}} - \sum n_{\rm{reactants}} &< 0 \\\\ \sum n_{\rm{products}} &< \sum n_{\rm{reactants}}. \end{align*}

In other words, Q1<KcQ_1 < K_c if and only if there are fewer moles of gas on the product side. But Q1<KcQ_1 < K_c also implies that the equilibrium position should shift rightward (favoring products). The analysis for the case in which there are fewer moles of gas on the reactant side is similar— the equilibrium position shifts leftward favoring reactants, which is what we wanted to show.

A connection to the equilibrium constant using partial pressures

As part of our proof, we encountered the following relationship (Equation 3):

cX=[X]=pXRT=P0ntotRTnX. c_X = [X] = \frac{p_X}{RT} = \frac{P_0n_{\mathrm{tot}}}{RTn_X}.

Recall that we originally substituted the final expression,

P0ntotRTnX \frac{P_0n_{\mathrm{tot}}}{RTn_X}

back into the equilibrium constant expression (leading to Equation 4). However, if instead we substitute the expression

pXRT \frac{p_X}{RT}

then we get something rather intriguing:

Kc=(pRRT)r(pSRT)s(pART)a(pBRT)b=pRrpSspAapBb(RT)(a+b+)(r+s+). \begin{align*} K_c &= \cfrac{\left(\cfrac{p_R}{RT}\right)^r\left(\cfrac{p_S}{RT}\right)^s\cdots}{\left(\cfrac{p_A}{RT}\right)^a\left(\cfrac{p_B}{RT}\right)^b\cdots} \\\\ &= \frac{{p_R}^r{p_S}^s\cdots}{{p_A}^a{p_B}^b\cdots} (RT)^{(a + b + \dots) - (r + s + \dots)}. \end{align*}

Indeed, observe that at constant temperature, the factor

(RT)(a+b+)(r+s+) (RT)^{(a + b + \dots) - (r + s + \dots)}

is constant. But if the temperature is constant KcK_c must, too, be constant, so that means the expression

pRrpSspAapBb \frac{{p_R}^r{p_S}^s\cdots}{{p_A}^a{p_B}^b\cdots}

is a constant as well! This expression may thus be viewed as a kind of equlibrium constant, the difference being that it is calculated using partial pressures instead of concentration. For this reason, it is often referred to as the equilibrium constant using partial pressures, denoted KpK_p. The relationship between KcK_c and KpK_p is readily given by isolating KpK_p in Equation 7:

Kc=Kp(RT)(a+b+)(r+s+)Kp=Kc(RT)(r+s+)(a+b+)Kp=Kc(RT)Δn \begin{align*} K_c &= K_p (RT)^{(a + b + \dots) - (r + s + \dots)} \\\\ K_p &= K_c (RT)^{(r + s + \dots) - (a + b + \dots)} \\\\ K_p &= K_c (RT)^{\Delta n} \end{align*}

where Δn\Delta n is as defined in Equation 5.