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Benzene (C(6)H(6), 78 g//mol) and tolue...

Benzene `(C_(6)H_(6), 78 g//mol)` and toluene `(C_(7)H_(8),92g//mol)` form an ideal solution. At `60^(@)C` the vapour pressure of pure benzene and pure toluene are `0.507` atm and `0.184` atm, respectively. The mole fraction of benezen in a solution of these two chemicals that has a vapour preesure of `0.350` atm at `60^(@)C`, will be :

A

`0.514`

B

`0.690`

C

`0.486`

D

`0.190`

Text Solution

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The correct Answer is:
To find the mole fraction of benzene in a solution of benzene and toluene that has a vapor pressure of 0.350 atm at 60°C, we can use Raoult's Law. Here’s a step-by-step solution: ### Step 1: Write down Raoult's Law Raoult's Law states that the total vapor pressure of a solution (P_total) is the sum of the partial pressures of each component: \[ P_{total} = P_{A0} \cdot X_A + P_{B0} \cdot X_B \] Where: - \( P_{A0} \) = vapor pressure of pure benzene = 0.507 atm - \( P_{B0} \) = vapor pressure of pure toluene = 0.184 atm - \( X_A \) = mole fraction of benzene - \( X_B \) = mole fraction of toluene ### Step 2: Express \( X_B \) in terms of \( X_A \) Since the sum of the mole fractions in a solution equals 1: \[ X_A + X_B = 1 \] Thus, we can express \( X_B \) as: \[ X_B = 1 - X_A \] ### Step 3: Substitute \( X_B \) into Raoult's Law Now, substitute \( X_B \) into the Raoult's Law equation: \[ P_{total} = P_{A0} \cdot X_A + P_{B0} \cdot (1 - X_A) \] Given that \( P_{total} = 0.350 \) atm, we can write: \[ 0.350 = 0.507 \cdot X_A + 0.184 \cdot (1 - X_A) \] ### Step 4: Simplify the equation Now, simplify the equation: \[ 0.350 = 0.507 \cdot X_A + 0.184 - 0.184 \cdot X_A \] Combine the terms involving \( X_A \): \[ 0.350 = (0.507 - 0.184) \cdot X_A + 0.184 \] \[ 0.350 - 0.184 = (0.507 - 0.184) \cdot X_A \] \[ 0.166 = 0.323 \cdot X_A \] ### Step 5: Solve for \( X_A \) Now, solve for \( X_A \): \[ X_A = \frac{0.166}{0.323} \] Calculating this gives: \[ X_A \approx 0.514 \] ### Final Answer The mole fraction of benzene in the solution is approximately \( 0.514 \). ---
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