EBK INTRODUCTION TO CHEMICAL ENGINEERIN
EBK INTRODUCTION TO CHEMICAL ENGINEERIN
8th Edition
ISBN: 9781259878091
Author: SMITH
Publisher: MCGRAW HILL BOOK COMPANY
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Chapter 6, Problem 6.22P
Interpretation Introduction

Interpretation:

The steam quality, enthalpy and entropy of wet steam at a temperature of 230C0 should be deduced.

Concept Introduction:

  • For a two-phase liquid-vapor equilibrium mixture the specific volume (V), enthalpy (H) and entropy (S) are given as:
  • V = Vf + x(Vg-Vf) -----(1)H = Hf + x(Hg-Hf)-----(2)S = Sf + x(Sg-Sf)--------(3)where, Vg and Vf are the specific volumes in the vapor and liquid phases respectively Hg and Hf are the specific enthalpies in the vapor and liquid phases respectivelySg and Sf are the specific entropies in the vapor and liquid phases respectivelyx = steam quality 

Steam quality, x = 0.867

Enthalpy, H = 2572.9 kJ/kg

Entropy, S = 5.636 kJ/kg-K

Given:

Density of wet steam, D = 0.025 g/cm3

Temperature = 230C0

Explanation:

Based on the steam tables at Temperature = 230C0 we have:

Specific volume of liquid, vf = 0.001252 m3/kg

Specific volume of vapor, vg = 0.045941 m3/kg

Specific enthalpy of liquid, Hf = 1085.7 kJ/kg

Specific enthalpy of vapor, Hg = 2801.0 kJ/kg

Specific entropy of liquid, Sf = 2.7933 kJ/kg-K

Specific entropy of liquid, Sg = 6.0721 kJ/kg-K

Calculation:

Step 1:

Calculate the steam quality x

It is given that:

Density of steam, D = 0.025 g/cm3 = 25 kg/m3

The specific volume V is given as:V = 1D = 125 = 0.04 m3/kgBased on equation (1), the steam quality x is:-x = V - VfVg - Vf=0.04 - 0.0012520.045941 - 0.001252=0.867

Step 2:

Calculate H and S based on equations 2 and 3

H = Hf + x (Hg-Hf)    = 1085.7 + 0.867(2801.0-1085.7) = 2572.9 kJ/kg

S = Sf + x (Sg-Sf)   = 2.7933 + 0.867(6.0721-2.7933) = 5.636 kJ/kg-K

Thus the quality, total enthalpy and entropy values are:

x = 0.867

Enthalpy, H = 2572.9 kJ/kg

Entropy, S = 5.636 kJ/kg-K

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Chapter 6 Solutions

EBK INTRODUCTION TO CHEMICAL ENGINEERIN

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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