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Question: At \(353K\), the vapour pressure of pure ethylene bromide and propylene bromide are \(22.93\) and \(...

At 353K353K, the vapour pressure of pure ethylene bromide and propylene bromide are 22.9322.93 and 16.93kNm216.93kN{m^{ - 2}} respectively, and these compounds form a nearly ideal solution. 3mol3mol of ethylene bromide and 2mol2mol of propylene bromide are equilibrated at 553K553K and a total pressure of 20.4kNm220.4kN{m^{ - 2}}
(a) what is the composition of the liquid phase?
(b) what amount of each compound is present in the vapour phase?
A. (a) 0.578,0.4220.578,0.422 (b) 0.9967mol,0.5374mol0.9967mol,0.5374mol
B. (a) 0.345,0.4220.345,0.422 (b) 0.9967mol,0.434mol0.9967mol,0.434mol
C. (a) 0.578,0.2120.578,0.212 (b) 0.9967mol,0.5374mol0.9967mol,0.5374mol
D. (a) 0.578,0.2120.578,0.212 (b) 0.497mol,0.5374mol0.497mol,0.5374mol

Explanation

Solution

We can use Raoult's Law to find the composition of the liquid phase. With this, we can then find the partial pressure of each component and use that to find the composition in the vapour phase. As we are given the number of moles initially present, if we can find the total number of moles present in the vapour phase at equilibrium, we can also find the amount of each component.
Formula used: pA=xAPAS,pB=xBPBS{p_A} = {x_A}P_A^S,{p_B} = {x_B}P_B^S
Where pA{p_A} and pB{p_B} are the partial pressures of component A (ethylene bromide) and component B (propylene bromide) respectively, xA{x_A} and xB{x_B} are the mole fractions of each component in the liquid phase and PAS,PBSP_A^S,P_B^S are the vapour pressures of components A and B.
pA=yAP,pB=yBP{p_A} = {y_A}P,{p_B} = {y_B}P
Where yA{y_A} and yB{y_B} are the mole fractions of respective components in the vapour phase and PP is the total pressure.
yA=nAVnAV+nBV{y_A} = \dfrac{{n_A^V}}{{n_A^V + n_B^V}} and xA=nALnAL+nBL{x_A} = \dfrac{{n_A^L}}{{n_A^L + n_B^L}}
Where nAVn_A^V and nBVn_B^V are the moles of A and B that are present in the vapour phase, and nALn_A^L and nBLn_B^L are the moles of A and B present in the liquid phase.

Complete answer:
Raoult’s Law states that partial pressure of a component is the product of its mole fraction in liquid phase and vapour pressure at a particular temperature. Thus,
pA=xAPAS,pB=xBPBS{p_A} = {x_A}P_A^S,{p_B} = {x_B}P_B^S
Where pA{p_A} and pB{p_B} are the partial pressures of component A (ethylene bromide) and component B (propylene bromide) respectively, xA{x_A} and xB{x_B} are the mole fractions of each component in the liquid phase and PAS,PBSP_A^S,P_B^S are the vapour pressures of components A and B.
The sum of both partial pressures is the total pressure. Thus, by adding, we get:
pA+pB=xAPAS+xBPBS=P{p_A} + {p_B} = {x_A}P_A^S + {x_B}P_B^S = P
As we know, sum of mole fractions is 1. Therefore,
xA+xB=1xB=1xA{x_A} + {x_B} = 1 \Rightarrow {x_B} = 1 - {x_A}
Substituting this in our previous equation, we get:
P=xAPAS+(1xA)PBS=xAPAS+PBSxAPBSP = {x_A}P_A^S + (1 - {x_A})P_B^S = {x_A}P_A^S + P_B^S - {x_A}P_B^S
Rearranging this, we get:
PPBS=xAPASxAPBSPPBS=xA(PASPBS)P - P_B^S = {x_A}P_A^S - {x_A}P_B^S \Rightarrow P - P_B^S = {x_A}(P_A^S - P_B^S)
Therefore, mole fraction of component A in liquid phase,
xA=PPBS(PASPBS){x_A} = \dfrac{{P - P_B^S}}{{(P_A^S - P_B^S)}}
From the data given, P=20.4kNm2,PAS=22.93kNm2,PBS=16.93kNm2P = 20.4kN{m^{ - 2}},P_A^S = 22.93kN{m^{ - 2}},P_B^S = 16.93kN{m^{ - 2}}
Substituting our values into this equation, we get:
xA=20.416.9322.9316.93{x_A} = \dfrac{{20.4 - 16.93}}{{22.93 - 16.93}}
On solving, we get: xA=0.578{x_A} = 0.578
xB=1xA=10.578=0.422\Rightarrow {x_B} = 1 - {x_A} = 1 - 0.578 = 0.422
Thus, we have now obtained the liquid phase compositions
The Dalton’s Law states that the partial pressure of a component in a gaseous mixture is equal to the product of its mole fraction in vapour phase and the total pressure. That is,
pA=yAP,pB=yBP{p_A} = {y_A}P,{p_B} = {y_B}P
Therefore, mole fraction in vapour phase,
yA=pAP,yB=pBP{y_A} = \dfrac{{{p_A}}}{P},{y_B} = \dfrac{{{p_B}}}{P}
Where yA{y_A} and yB{y_B} are the mole fractions of respective components in the vapour phase and PP is the total pressure
But we know pA=xAPAS,pB=xBPBS{p_A} = {x_A}P_A^S,{p_B} = {x_B}P_B^S
Substituting this in our previous equation, we get:
yA=xAPASP{y_A} = \dfrac{{{x_A}P_A^S}}{P}
As we have obtained earlier, xA=0.578,PAS=22.93kNm2,P=20.4kNm2{x_A} = 0.578,P_A^S = 22.93kN{m^{ - 2}},P = 20.4kN{m^{ - 2}}
Substituting our values, we get:
yA=0.578×22.9320.4=0.6497{y_A} = \dfrac{{0.578 \times 22.93}}{{20.4}} = 0.6497
Now, let us take nAVn_A^V and nBVn_B^V as the moles of A and B that are present in the vapour phase, and nALn_A^L and nBLn_B^L as the moles of A and B present in the liquid phase.
Hence, by the definition of mole fraction, yA=nAVnAV+nBV=0.6497{y_A} = \dfrac{{n_A^V}}{{n_A^V + n_B^V}} = 0.6497
On rearrangement, we get:
nAV0.6497=nAV+nBV\dfrac{{n_A^V}}{{0.6497}} = n_A^V + n_B^V
As initially 3mol3mol of ethylene bromide and 2mol2mol of propylene bromide are present, sum of moles in liquid and vapour phase for A and B will be equal to 3mol3mol and 2mol2mol respectively. Hence,
3mol=nAL+nAV,2mol=nBL+nBV3mol = n_A^L + n_A^V,2mol = n_B^L + n_B^V
Therefore, since xA=nALnAL+nBL{x_A} = \dfrac{{n_A^L}}{{n_A^L + n_B^L}}
xA=3nAV(3nAV)+(2nBV)=0.578\Rightarrow {x_A} = \dfrac{{3 - n_A^V}}{{(3 - n_A^V) + (2 - n_B^V)}} = 0.578
Rearranging this, we get:
3nAV(3+2)(nAV+nBV)=0.5783nAV=0.578[5(nAV+nBV)]\dfrac{{3 - n_A^V}}{{(3 + 2) - (n_A^V + n_B^V)}} = 0.578 \Rightarrow 3 - n_A^V = 0.578\left[ {5 - (n_A^V + n_B^V)} \right]
Substituting the value we got earlier, nAV+nBV=nAV0.6497n_A^V + n_B^V = \dfrac{{n_A^V}}{{0.6497}}
3nAV=0.578[5nAV0.6497]\Rightarrow 3 - n_A^V = 0.578\left[ {5 - \dfrac{{n_A^V}}{{0.6497}}} \right]
On solving this, we get:
3nAV=2.890.8896nAV3 - n_A^V = 2.89 - 0.8896n_A^V
Hence, nAV=0.9967moln_A^V = 0.9967mol
Substituting this into our equation for mole fraction in vapour phase, nAV0.6497=nAV+nBV\dfrac{{n_A^V}}{{0.6497}} = n_A^V + n_B^V, we get:
0.99670.6497=0.9967+nBVnBV=1.534090.9967\dfrac{{0.9967}}{{0.6497}} = 0.9967 + n_B^V \Rightarrow n_B^V = 1.53409 - 0.9967
On solving this, we get:
nBV=0.5374moln_B^V = 0.5374mol
Therefore, the values we have obtained are: liquid phase composition =0.578,0.422 = 0.578,0.422 and amount of each compound present in vapour phase nAV=0.9967mol,nBV=0.5374moln_A^V = 0.9967mol,n_B^V = 0.5374mol
Hence, the correct set of options is A.

Note:
While the Raoult’s Law can be applied only when the binary mixture of components forms an ideal solution, the Dalton’s Law of partial pressures is applicable to all gaseous mixtures. Note that the vapour pressure of a compound is a direct function of the temperature. That is, these experiments are thought to be carried out in isothermal conditions, so that the vapour pressures don’t change. Also note that the sum of individual mole fractions of all the components in any mixture will always be equal to 1.