Loose Leaf For Introduction To Chemical Engineering Thermodynamics
Loose Leaf For Introduction To Chemical Engineering Thermodynamics
8th Edition
ISBN: 9781259878084
Author: Smith Termodinamica En Ingenieria Quimica, J.m.; Van Ness, Hendrick C; Abbott, Michael; Swihart, Mark
Publisher: McGraw-Hill Education
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Chapter 6, Problem 6.51P
Interpretation Introduction

Interpretation:

For n-butane, the molar volume, enthalpy and entropy as a saturated vapor as well as saturated liquid at 370 K needs to be calculated.

Concept Introduction:

The equation used to calculate the molar volume of vapor is:

  Vvap=ZRTP .......(1)

Here, P is the pressure, V is the volume, T is the temperature of the system, and R is the universal gas constant. Z is the compressibility factor and is defined as:

  Z=Z0+ωZ1 .......(2)

Here, ω is an acentric factor given in table B.1 and Z0 and Z1 are given in table D.1 and D.2.

The formula to calculate enthalpy of vapor (Hvap) is:

  Hvap=H0ig+T0TCpigdT+HR .......(3)

Here, H0ig is ideal-gas state enthalpy at initial temperature. Value of Cpig is taken from table C.1. HR is defined as:

  HR=(HR)0+ω(HR)1 .......(4)

Here, (HR)0 and (HR)1 are given in table D.5 and D.6.

The formula to calculate entropy of vapor (Svap) is:

  Svap=S0ig+T0TCpigdTTRlnPP0+SR .......(5)

Here, S0ig is ideal-gas state entropy at initial temperature. Value of Cpig is taken from table C.1. SR is defined as:

  SR=(SR)0+ω(SR)1 .......(6)

Here, (SR)0 and (SR)1 are given in table D.9 and D.10.

To calculate molar volume of saturated liquid, the formula to be used is:

  Vliq=VcZc( 1 T r )2/7 .......(7)

Equation to calculate enthalpy of liquid (Hliq) is:

  Hliq=HvapΔH .......(8)

Here, ΔH is heat of vaporization at the required temperature.

Equation by Reidel to calculate heat of vaporization at normal boiling point (Tn) is:

  ΔHn=RTn1.092(lnPc1.013)0.930Trn .......(9)

Watson equation to calculate heat of vaporization at any temperature using known heat of vaporization at another temperature is:

  ΔH2ΔH1=( 1 T r2 1 T r1 )0.38 .......(10)

Equation to calculate entropy of liquid (Sliq) is:

  Sliq=SvapΔHT .......(11)

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Chapter 6 Solutions

Loose Leaf For Introduction To Chemical Engineering Thermodynamics

Ch. 6 - Prob. 6.11PCh. 6 - Prob. 6.12PCh. 6 - Prob. 6.13PCh. 6 - Prob. 6.14PCh. 6 - Prob. 6.15PCh. 6 - Prob. 6.16PCh. 6 - Prob. 6.17PCh. 6 - Prob. 6.18PCh. 6 - Prob. 6.19PCh. 6 - Prob. 6.20PCh. 6 - Prob. 6.21PCh. 6 - Prob. 6.22PCh. 6 - Prob. 6.23PCh. 6 - Prob. 6.24PCh. 6 - Prob. 6.25PCh. 6 - Prob. 6.26PCh. 6 - Prob. 6.27PCh. 6 - What is the mole fraction of water vapor in air...Ch. 6 - Prob. 6.29PCh. 6 - Prob. 6.30PCh. 6 - Prob. 6.31PCh. 6 - Prob. 6.32PCh. 6 - Prob. 6.33PCh. 6 - Prob. 6.34PCh. 6 - Prob. 6.35PCh. 6 - Prob. 6.36PCh. 6 - Prob. 6.37PCh. 6 - Prob. 6.38PCh. 6 - Prob. 6.39PCh. 6 - Prob. 6.40PCh. 6 - Prob. 6.41PCh. 6 - Prob. 6.42PCh. 6 - Prob. 6.43PCh. 6 - Prob. 6.44PCh. 6 - Prob. 6.45PCh. 6 - Prob. 6.46PCh. 6 - Prob. 6.47PCh. 6 - Prob. 6.48PCh. 6 - Prob. 6.49PCh. 6 - Prob. 6.50PCh. 6 - Prob. 6.51PCh. 6 - Prob. 6.52PCh. 6 - Prob. 6.53PCh. 6 - Prob. 6.54PCh. 6 - Prob. 6.55PCh. 6 - Prob. 6.56PCh. 6 - Prob. 6.57PCh. 6 - Prob. 6.58PCh. 6 - Prob. 6.59PCh. 6 - Prob. 6.60PCh. 6 - Prob. 6.61PCh. 6 - Prob. 6.62PCh. 6 - Prob. 6.63PCh. 6 - Prob. 6.64PCh. 6 - Prob. 6.65PCh. 6 - Prob. 6.66PCh. 6 - Prob. 6.67PCh. 6 - Prob. 6.68PCh. 6 - Prob. 6.69PCh. 6 - Prob. 6.71PCh. 6 - Prob. 6.72PCh. 6 - Prob. 6.73PCh. 6 - Prob. 6.74PCh. 6 - Prob. 6.75PCh. 6 - Prob. 6.76PCh. 6 - Prob. 6.77PCh. 6 - Prob. 6.78PCh. 6 - Prob. 6.79PCh. 6 - Prob. 6.80PCh. 6 - Prob. 6.81PCh. 6 - The temperature dependence of the second virial...Ch. 6 - Prob. 6.83PCh. 6 - Prob. 6.84PCh. 6 - Prob. 6.85PCh. 6 - Prob. 6.86PCh. 6 - Prob. 6.87PCh. 6 - Prob. 6.88PCh. 6 - Prob. 6.89PCh. 6 - Prob. 6.90PCh. 6 - Prob. 6.91PCh. 6 - Prob. 6.92PCh. 6 - Prob. 6.93PCh. 6 - Prob. 6.94PCh. 6 - Prob. 6.95PCh. 6 - Prob. 6.96PCh. 6 - Prob. 6.97PCh. 6 - Prob. 6.98PCh. 6 - Prob. 6.99PCh. 6 - Prob. 6.100P
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