Fundamentals Of Engineering Thermodynamics
9th Edition
ISBN: 9781119391388
Author: MORAN, Michael J., SHAPIRO, Howard N., Boettner, Daisie D., Bailey, Margaret B.
Publisher: Wiley,
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Question
Chapter 3, Problem 3.62P
a.
To determine
Volume using compressibility chart.
b.
To determine
Volume using steam table
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B) Calculate the volume of the vapor using (a) ideal gas law (b) steam
tables (c) the generalized compressibility chart.
R = 0.4615 kP.m3/kg.K
Ter 647.1 K
Per = 22.06 MPa
Q1. Determine the molar volume of n-buthane at 510 K and 25 bar by each of the following:
(a) the ideal-gas equation, (b) the generalized compressibility chart, and (c) The
Redlich/Kwong equation. Also determine the error involved in the first two cases.
Determine the volume for water vapor at 200 bar and 470 oc at 10kg, using
(a) ideal gas equation
(b) data from the compressibility chart.
(c) data from the steam tables. Also find the error percent.
Chapter 3 Solutions
Fundamentals Of Engineering Thermodynamics
Ch. 3 - Prob. 3.1ECh. 3 - Prob. 3.2ECh. 3 - Prob. 3.3ECh. 3 - Prob. 3.4ECh. 3 - Prob. 3.6ECh. 3 - Prob. 3.7ECh. 3 - Prob. 3.8ECh. 3 - Prob. 3.9ECh. 3 - Prob. 3.10ECh. 3 - Prob. 3.11E
Ch. 3 - Prob. 3.12ECh. 3 - Prob. 3.13ECh. 3 - Prob. 3.1CUCh. 3 - Prob. 3.2CUCh. 3 - Prob. 3.3CUCh. 3 - Prob. 3.4CUCh. 3 - Prob. 3.5CUCh. 3 - Prob. 3.6CUCh. 3 - Prob. 3.7CUCh. 3 - Prob. 3.8CUCh. 3 - Prob. 3.9CUCh. 3 - Prob. 3.10CUCh. 3 - Prob. 3.11CUCh. 3 - Prob. 3.12CUCh. 3 - Prob. 3.13CUCh. 3 - Prob. 3.14CUCh. 3 - Prob. 3.15CUCh. 3 - Prob. 3.16CUCh. 3 - Prob. 3.17CUCh. 3 - Prob. 3.18CUCh. 3 - Prob. 3.19CUCh. 3 - Prob. 3.20CUCh. 3 - Prob. 3.21CUCh. 3 - Prob. 3.22CUCh. 3 - Prob. 3.23CUCh. 3 - Prob. 3.24CUCh. 3 - Prob. 3.25CUCh. 3 - Prob. 3.26CUCh. 3 - Prob. 3.27CUCh. 3 - Prob. 3.28CUCh. 3 - Prob. 3.29CUCh. 3 - Prob. 3.30CUCh. 3 - Prob. 3.31CUCh. 3 - Prob. 3.32CUCh. 3 - Prob. 3.33CUCh. 3 - Prob. 3.34CUCh. 3 - Prob. 3.35CUCh. 3 - Prob. 3.36CUCh. 3 - Prob. 3.37CUCh. 3 - Prob. 3.38CUCh. 3 - Prob. 3.39CUCh. 3 - Prob. 3.40CUCh. 3 - Prob. 3.41CUCh. 3 - Prob. 3.42CUCh. 3 - Prob. 3.43CUCh. 3 - Prob. 3.44CUCh. 3 - Prob. 3.45CUCh. 3 - Prob. 3.46CUCh. 3 - Prob. 3.47CUCh. 3 - Prob. 3.48CUCh. 3 - Prob. 3.49CUCh. 3 - Prob. 3.50CUCh. 3 - Prob. 3.51CUCh. 3 - Prob. 3.52CUCh. 3 - Prob. 3.1PCh. 3 - Prob. 3.2PCh. 3 - Prob. 3.3PCh. 3 - Prob. 3.4PCh. 3 - Prob. 3.5PCh. 3 - Prob. 3.6PCh. 3 - Prob. 3.7PCh. 3 - Prob. 3.8PCh. 3 - Prob. 3.9PCh. 3 - Prob. 3.10PCh. 3 - Prob. 3.11PCh. 3 - Prob. 3.12PCh. 3 - Prob. 3.13PCh. 3 - Prob. 3.14PCh. 3 - Prob. 3.15PCh. 3 - Prob. 3.16PCh. 3 - Prob. 3.17PCh. 3 - Prob. 3.18PCh. 3 - Prob. 3.19PCh. 3 - Prob. 3.20PCh. 3 - Prob. 3.21PCh. 3 - Prob. 3.22PCh. 3 - Prob. 3.23PCh. 3 - Prob. 3.24PCh. 3 - Prob. 3.25PCh. 3 - Prob. 3.26PCh. 3 - Prob. 3.27PCh. 3 - Prob. 3.28PCh. 3 - Prob. 3.29PCh. 3 - Prob. 3.30PCh. 3 - Prob. 3.31PCh. 3 - Prob. 3.32PCh. 3 - Prob. 3.33PCh. 3 - Prob. 3.34PCh. 3 - Prob. 3.35PCh. 3 - Prob. 3.36PCh. 3 - Prob. 3.37PCh. 3 - Prob. 3.38PCh. 3 - Prob. 3.39PCh. 3 - Prob. 3.40PCh. 3 - Prob. 3.41PCh. 3 - Prob. 3.42PCh. 3 - Prob. 3.43PCh. 3 - Prob. 3.44PCh. 3 - Prob. 3.45PCh. 3 - Prob. 3.46PCh. 3 - Prob. 3.47PCh. 3 - Prob. 3.48PCh. 3 - Prob. 3.49PCh. 3 - Prob. 3.50PCh. 3 - Prob. 3.51PCh. 3 - Prob. 3.52PCh. 3 - Prob. 3.53PCh. 3 - Prob. 3.54PCh. 3 - Prob. 3.55PCh. 3 - Prob. 3.56PCh. 3 - Prob. 3.57PCh. 3 - Prob. 3.58PCh. 3 - Prob. 3.59PCh. 3 - Prob. 3.60PCh. 3 - Prob. 3.61PCh. 3 - Prob. 3.62PCh. 3 - Prob. 3.63PCh. 3 - Prob. 3.64PCh. 3 - Prob. 3.65PCh. 3 - Prob. 3.66PCh. 3 - Prob. 3.67PCh. 3 - Prob. 3.68PCh. 3 - Prob. 3.69PCh. 3 - Prob. 3.70PCh. 3 - Prob. 3.71PCh. 3 - Prob. 3.72PCh. 3 - Prob. 3.73PCh. 3 - Prob. 3.74PCh. 3 - Prob. 3.75PCh. 3 - Prob. 3.76PCh. 3 - Prob. 3.77PCh. 3 - Prob. 3.78PCh. 3 - Prob. 3.79PCh. 3 - Prob. 3.80PCh. 3 - Prob. 3.81PCh. 3 - Prob. 3.82PCh. 3 - Prob. 3.83PCh. 3 - Prob. 3.84PCh. 3 - Prob. 3.85PCh. 3 - Prob. 3.86PCh. 3 - Prob. 3.87PCh. 3 - Prob. 3.88PCh. 3 - Prob. 3.89PCh. 3 - Prob. 3.90PCh. 3 - Prob. 3.91PCh. 3 - Prob. 3.92PCh. 3 - Prob. 3.93PCh. 3 - Prob. 3.94PCh. 3 - Prob. 3.95PCh. 3 - Prob. 3.96PCh. 3 - Prob. 3.97PCh. 3 - Prob. 3.98PCh. 3 - Prob. 3.99P
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- B) Calculate the volume of the vapor using (a) ideal gas law (b) steam tables (c) the generalized compressibility chart. R = 0.4615 kP.m3/kg.K Ter = 647.1 K Per = 22.06 MPa %3D (40 Manlu)arrow_forwardQ5/ Determine the molar volume of butane at 510 K and 25 bar by each of the following : a- Ideal gas law. b- Compressibility factor.arrow_forwardNote: Use values from the Steam Tables by Keenan, Keyes, Hill and Moore.arrow_forward
- Steam at 160 bars and 440 °C expands isothermally until its volume is doubled. Determine the final pressure with; a) İdeal-gas equation of state. b) Compressibility charts. c) Steam tables.arrow_forwardQuestion 2 (a) Please complete the following table for water as pure substance. Show your analysis clearly. State T, °C P, kPa i 300 ii 200 400 iii 120 500 iv 300 v, m³/kg 0.100 Phase of substance Saturated vapor (b) Please plot all states below on the same T-v diagram with respect to saturation lines. Saturated mixture at pressure of 250 kPa and with quality of 0.50. (i) (ii) Saturated liquid at pressure of 400 kPa. (iii) Saturated vapor at pressure of 450 kPa. (iv) Superheated water at pressure of 400 kPa and temperature of 500°C. (c) A piston-cylinder device initially contained 0.5 kg of water at pressure of 650 kPa and temperature of 150 °C. During a process, the pressure of the water is reduced to 200 kPa in an isothermal manner. Determine the change in volume, m³. (i) (ii) Sketch the process on pressure versus specific volume (P-v) diagram with respect to saturation lines. Question 3 (a) An ideal gas expands from State 1 to State 2 according to PV = constant law. Derive the…arrow_forwardUsing the steam tables, given a 0.085-m3 drum contains with wet steam at 371.5oC, (a) find the respective masses of the saturated vapor and saturated liquid in the mixture if they occupy equal volume. (b) find the respective volumes of the saturated liquid and saturated vapor in the mixture if their masses are equal.arrow_forward
- Exercise 1 1: The specific volume of superheated water vapor at 0.6 MPa and 900°C is 0.90179 m³/kg in the steam tables, determine the specific volume also using: (a) The ideal-gas equation. :s) (b) The generalized compressibility chart. 'I (c) Can we consider the superheated vapor to behave as an ideal gas under the given temperature and pressure? Why?arrow_forwardParts ,g,h,i,jarrow_forward1. Complete the following table. Show the states on the T-v diagram Substance T°C P, KPa Internal Energy. Enthalpy, Specific volume, Quality, X Phase description u, kj/kg h, kj/kg v, m'/kg Pg 98 pa H,0 200 10000 H,O 600 2000 R-134a 900 180arrow_forward
- 5arrow_forward● Determine the missing properties and the phase descriptions in the following table for water: T, °C 125 75 P, KPa 200 1000 500 800 u, kJ/kg 1600 2950 X 0.6 0.0 Phase Descriptionarrow_forwardQuestion 1: Derive the thermodynamic equation of state (dH/dP)_T = V-T(dV/dT)_P Derive an expression for (dH/dP)_T for an ideal gas and for a van der Waals gas. For the van der waals gas, estimate its value for 1.0 mol of Ar(g) at 298K and 10 atm. Question 2: Show that the slope of compressibility factor Z as a function of pressure as P ---> 0; at isothermal conditions is related to the van der waals parameters by: Limit (P-->0) dz/dP = (b-a/RT)/RTarrow_forward
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