Since VLE can also be expressed in terms of H-xy data, estimate the H-xy data for the mixture with component (A) - component (B) system at 1 atm total pressure. The required integral heat of solution...

Since VLE can also be expressed in terms of H-xy data, estimate the H-xy data<br>for the mixture with component (A) - component (B) system at 1 atm total<br>pressure. The required integral heat of solution (at 20°C) and x-y* data is given<br>below.<br>Cps<br>ΔΗ5<br>(kcal/kmol) (kcal/kg.K)<br>Temperature<br>| (°C)<br>57.2<br>0.93<br>0.959<br>0.55<br>59.1<br>0.72<br>0.851<br>-41.30<br>0.64<br>66.8<br>0.12<br>0.742<br>-161.7<br>0.93<br>kcal<br>Other specific heat of liquid for A: cpA<br>= 0.57<br>.K,<br>kg<br>kcal<br>Average specific heat of B, cpB<br>= 1.0<br>kg<br>0.252(t-50)kcal<br>Heat of vaporization of A, l4 = 125.8<br>(t in °C), and B, 1g =<br>kg<br>550 kcat<br>kg<br>Molecular Weight, A = 58, B = 18.<br>

Extracted text: Since VLE can also be expressed in terms of H-xy data, estimate the H-xy data for the mixture with component (A) - component (B) system at 1 atm total pressure. The required integral heat of solution (at 20°C) and x-y* data is given below. Cps ΔΗ5 (kcal/kmol) (kcal/kg.K) Temperature | (°C) 57.2 0.93 0.959 0.55 59.1 0.72 0.851 -41.30 0.64 66.8 0.12 0.742 -161.7 0.93 kcal Other specific heat of liquid for A: cpA = 0.57 .K, kg kcal Average specific heat of B, cpB = 1.0 kg 0.252(t-50)kcal Heat of vaporization of A, l4 = 125.8 (t in °C), and B, 1g = kg 550 kcat kg Molecular Weight, A = 58, B = 18.

Jun 10, 2022

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Since VLE can also be expressed in terms of H-xy data, estimate the H-xy data for the mixture with component (A) - component (B) system at 1 atm total pressure. The required integral heat of solution...

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