FUND OF ENG THERMODYN-WILEYPLUS NEXT GEN
9th Edition
ISBN: 9781119840589
Author: MORAN
Publisher: WILEY
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Chapter 3, Problem 3.62P
a.
To determine
Volume using compressibility chart.
b.
To determine
Volume using steam table
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Determine the volume, in m3, occupied by 3 kg of H2O at 80 bar, 380°C, using (a) data from the compressibility chart, (b) data from the steam tables (Need to mention the table number). Compare the results of parts (a) and (b).
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.
Chapter 3 Solutions
FUND OF ENG THERMODYN-WILEYPLUS NEXT GEN
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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- Determine the volume, in m3, occupied by 2 kg of O2 at 30 bar, 200 K, using data from compressibility chart.arrow_forwardDetermine 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.arrow_forwardB) 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_forward
- Q5/ 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_forwardSteam 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_forward
- Determine the temperature, in °C, of Butane at 30 bar and a specific volume of 0.026 m³/kg. Hint - you need to use compressibility charts since Butane is non-ideal under the specified conditions. Answer: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_forwardDetermine the specific volume, in m3/kg, of ammonia at 50°C, 2 bar, using (a) Table A-15. (b) Figure A-1. (c) the ideal gas equation of state.arrow_forward
- Using 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_forwardConsider a saturated water vapor isobarically heated from 400°C until itsvolume is triple. Determine the final temperature with:a) Steam tables b) The compressibility chart. c) Present a comparative analysis between the answers to "a" and "b".arrow_forwardExercise 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_forward
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