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Calculate change in enthalpy when 2 mole...

Calculate change in enthalpy when 2 moles of liquid water at 1 bar and `100^(@)` C is coverted into steam at 2 bar and `300^(@)`. Assume `H_(2)O` vapoures to behave ideally.
[Latent heat of vaporisation of `H_(2)O(l)` at 1 bar and `100^(@)` C id=s 10.8 kcal per mole]
[R=`2cal//"mol" K`]

A

21.6 kcal

B

11.8 kcal

C

24.8 kcal

D

23.6 kcal

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The correct Answer is:
To calculate the change in enthalpy when 2 moles of liquid water at 1 bar and 100°C is converted into steam at 2 bar and 300°C, we will follow these steps: ### Step 1: Calculate the enthalpy change for vaporization (ΔH1) The latent heat of vaporization of water at 1 bar and 100°C is given as 10.8 kcal per mole. Since we have 2 moles of water, we can calculate ΔH1 as follows: \[ \Delta H_1 = \text{Latent heat of vaporization} \times \text{Number of moles} \] \[ \Delta H_1 = 10.8 \, \text{kcal/mol} \times 2 \, \text{moles} = 21.6 \, \text{kcal} \] ### Step 2: Calculate the enthalpy change for heating the steam (ΔH2) Next, we need to calculate the enthalpy change when the steam is heated from 100°C to 300°C at a pressure of 2 bar. The formula for this is: \[ \Delta H_2 = N C_p \Delta T \] Where: - \(N\) = number of moles = 2 - \(C_p\) = molar heat capacity of water vapor = 2 cal/mol K (given) - \(\Delta T\) = change in temperature = \(300°C - 100°C = 200°C\) Now substituting the values: \[ \Delta H_2 = 2 \, \text{moles} \times 2 \, \text{cal/mol K} \times 200 \, \text{K} \] \[ \Delta H_2 = 800 \, \text{cal} \] Since we need this in kcal, we convert it: \[ \Delta H_2 = \frac{800 \, \text{cal}}{1000} = 0.8 \, \text{kcal} \] ### Step 3: Calculate the total change in enthalpy (ΔH) Now, we can find the total change in enthalpy by adding ΔH1 and ΔH2: \[ \Delta H = \Delta H_1 + \Delta H_2 \] \[ \Delta H = 21.6 \, \text{kcal} + 0.8 \, \text{kcal} = 22.4 \, \text{kcal} \] ### Final Answer The change in enthalpy when 2 moles of liquid water at 1 bar and 100°C is converted into steam at 2 bar and 300°C is **22.4 kcal**. ---
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