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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Chapter 3, Problem 3.44CU
To determine
The quality of a liquid-vapor two-phase mixture with equivalent volumes of saturated liquid and saturated vapor is 0.5. Indicate true or false.
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3. An ideal gas mixture that contains (% volume) 21% Hydrogen, 34% Octane, 5% Oxygen and 40% methane undergo a certain process inside a closed rigid container increasing the temperature by 1000F. Let the specific heat ratio for the mixture be 1.35, determine the change in specific enthalpy (Btu/lb-°R). Draw a figure or FBD that will support the problem. Explain each step by step formula.
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.
Determine the state of water if P= 130 bar
and T= 288 C.
Select one:
a. Superheated Vapor
b. Compressed liquid
c. Mixture
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 state of water if T= 15 C and P = 0.01705 bar %3D Select one: a. Compressed liquid b. Superheated Vapor c. Mixturearrow_forward4) A liquid-vapor water mixture of 50% quality and equilibrium pressure of 1 bar (initial state) is heated to 280 °C (final state) in a rigid closed container. Calculate the following:arrow_forwardProvide clear and complete solution as well as a diagram for below given problem. 1 kg of mixture at 250oC and with enthalpy of 1861 KJ/kg and s = 4.275 KJ/kg-K undergoesisothermal process. Heat is applied until the steam becomes saturated. Determine the heatadded. At 250oC: sf = 2.7927, hf = 1085.36, hfg = 1716.20 A. 940.25 KJ B. 1715.32 KJ C. 863.45 KJ D. 634.34 KJ Answer: Aarrow_forward
- a) Properties of pure substance changes with phase, temperature and pressure. It is important to understand specific properties of a substance to evaluate its thermodynamics properties. Given a situation where 500g of water in saturated vapor state at 200 °C is being cooled under an isobaric condition until the enthalpy reaches 1500 kJ/kg. i. Sketch the state and process pathway on a P-v diagram with respect to saturation lines and label all relevant information Determine the pressure where the process take place Determine the quality of water at the end of process Determine the changes in volume during the cooling process Determine the heat loss during the cooling process ii. ii. iv. V.arrow_forward7. Two vessels 1 and 2, of different sizes are connected by a pipe with a valve .Vessel contains 142 L of air at 2,767.92 kPa, 93.33°C. Vessel 2 of unknown volume contains air at 68.95 kPa, 4.44C. The valve is opened and when the have been determined it is found that the pressure of the mixture is P3 = 1378.96 kPa and the temperature of the mixture is T3= 43.33°C. How many liters of air are contained in vessel 2?arrow_forwardShow the critical point, superheated vapor region, compressed liquid region, saturated mixture region, saturated liquid line, and saturated vapor line on a h-s phase diagram for a pure substance.arrow_forward
- A pipe with a valve connects two vessels A&B of different sizes. Vessel A contains 142L of air at 27.7 bar, 93.33 deg C. Vessel B, of unknown volume contains air at 68.95 kPa, 4.44 deg C. The valve is opened and when the properties have been determined, it is found that the pressure of mixture is 200 psi and the temperature is 43.33 deg F. What is the volume of vessel B?arrow_forwardDetermine the state of water if P= 25 bar and T= 150 C. Select one: O a. Superheated Vapor O b. Mixture O c. Compressed liquidarrow_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 MPaarrow_forward
- A. Draw a P-v diagram of a typical pure-substance and clearly indicate the following: i. Critical point ii. Critical temperature Ter, iii. Critical pressure Per, iv. Critical specific volume Ver. v. Superheated vapor region vi. Compressed liquid region vii. Liquid-vapor region viii. Constant temperature line ix. Saturated liquid line x. Saturated vapour linearrow_forwardEquation of state when 6. Principle of corresponding states "all gases follow the expressed in terms of variables"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
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