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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, in m3, occupied by 2 kg of O2 at 30 bar, 200 K, using data from compressibility chart.
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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- 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.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_forwardRound everything to four decimal places. Provide solution in this format: Given, Required, Solution and Answer. 1. Using the Beattie-Bridgeman equation explicit in volume, calculate the density in grams per cubic centimetre of N2 at 0°C and 100 atm pressure. 2. Employing the Kamerlingh Omnes equation of state, find the compressibility factors of CO at −50°? and pressure of 1000 atm.arrow_forward
- Determine the properties of propane in gaseous state with the help of generalized compressibility charts according to the conditions given below. Compare the results obtained with the ideal gas equation of state. Specific volume at 7 MPa, 150 °Carrow_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_forwardA two phase liquid - vapor mixture of refridgerant aa is Contained in a ciosed tank at 10 bar. The quality is l60% and the mas of Saturated liquid is 25 kg. Calculate the volume of saturated vapor in m. use 5 signifigant figures.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_forwardDetermine 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_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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