THERMODYNAMICS (LL)-W/ACCESS >CUSTOM<
9th Edition
ISBN: 9781266657610
Author: CENGEL
Publisher: MCG CUSTOM
expand_more
expand_more
format_list_bulleted
Concept explainers
Videos
Textbook Question
Chapter 12.6, Problem 79P
Propane is compressed isothermally by a piston–cylinder device from 100°C and 1 MPa to 4 MPa. Using the generalized charts, determine the work done and the heat transfer per unit mass of propane.
Expert Solution & Answer
Want to see the full answer?
Check out a sample textbook solution
Students have asked these similar questions
850 g of a certain substance is heated at constant pressure from 40 ⁰C to 70 ⁰C. Specific heat capacity at constant pressure is given by the following expression:
8Cp² - 5Cp = 7
Where:
Cp = specific heat capacity at constant pressure in kJ/kg-K
Determine the change in entropy in J/K.
A piston-cylinder assembly contains 20 kg of ammonia, initially at 80 kPa and -10°C. The ammonia is compressed to a pressure of 550
kPa. During the process, the pressure and specific volume are related by po¹¹ = constant. Determine the work and the heat transfer,
in kJ.
Determine work
Work can be evaluated:
as equal to the pressure times (final specific volume minus initial specific volume).
O by integrating volume from the initial pressure to the final pressure.
O as equal to the pressure times (initial volume minus final volume).
as the integral of pdV from the initial volume to the final volume.
eTextbook and Media
Save for Later
Assistance Used
Attempts: 0 of 5 used
Determine specific internal energy
The parts of this question must be completed in order. This part will be available when you complete the part above.
Calculate heat transfer
The parts of this question must be completed in order. This part will be available when you complete the part above.
Calculate work
The parts of…
1. An ideal gas at a pressure of 4120 kPaa and a temperature of 25 °C is
contained in a cylinder with a volume of 20 m³. A certain amount of the gas
is released so that the pressure in the cylinder drops to 1730 kPaa.
Expansion of the gas is isentropic. The heat capacity ratio is 1.4 and the gas
constant is 0.286 kJ/kg-ºC. Determine the mass of gas remaining in the
cylinder, in kg.
Chapter 12 Solutions
THERMODYNAMICS (LL)-W/ACCESS >CUSTOM<
Ch. 12.6 - What is the difference between partial...Ch. 12.6 - Consider the function z(x, y). Plot a differential...Ch. 12.6 - Consider a function z(x, y) and its partial...Ch. 12.6 - Prob. 4PCh. 12.6 - Prob. 5PCh. 12.6 - Consider a function f(x) and its derivative df/dx....Ch. 12.6 - Conside the function z(x, y), its partial...Ch. 12.6 - Consider air at 350 K and 0.75 m3/kg. Using Eq....Ch. 12.6 - Consider air at 350 K and 0.75 m3/kg. Using Eq....Ch. 12.6 - Nitrogen gas at 800 R and 50 psia behaves as an...
Ch. 12.6 - Consider an ideal gas at 400 K and 100 kPa. As a...Ch. 12.6 - Using the equation of state P(v a) = RT, verify...Ch. 12.6 - Prove for an ideal gas that (a) the P = constant...Ch. 12.6 - Verify the validity of the last Maxwell relation...Ch. 12.6 - Verify the validity of the last Maxwell relation...Ch. 12.6 - Show how you would evaluate T, v, u, a, and g from...Ch. 12.6 - Prob. 18PCh. 12.6 - Prob. 19PCh. 12.6 - Prob. 20PCh. 12.6 - Prove that (PT)=kk1(PT)v.Ch. 12.6 - Prob. 22PCh. 12.6 - Prob. 23PCh. 12.6 - Using the Clapeyron equation, estimate the...Ch. 12.6 - Prob. 26PCh. 12.6 - Determine the hfg of refrigerant-134a at 10F on...Ch. 12.6 - Prob. 28PCh. 12.6 - Prob. 29PCh. 12.6 - Two grams of a saturated liquid are converted to a...Ch. 12.6 - Prob. 31PCh. 12.6 - Prob. 32PCh. 12.6 - Prob. 33PCh. 12.6 - Prob. 34PCh. 12.6 - Prob. 35PCh. 12.6 - Prob. 36PCh. 12.6 - Determine the change in the internal energy of...Ch. 12.6 - Prob. 38PCh. 12.6 - Determine the change in the entropy of helium, in...Ch. 12.6 - Prob. 40PCh. 12.6 - Estimate the specific heat difference cp cv for...Ch. 12.6 - Derive expressions for (a) u, (b) h, and (c) s for...Ch. 12.6 - Derive an expression for the specific heat...Ch. 12.6 - Derive an expression for the specific heat...Ch. 12.6 - Derive an expression for the isothermal...Ch. 12.6 - Prob. 46PCh. 12.6 - Show that cpcv=T(PT)V(VT)P.Ch. 12.6 - Show that the enthalpy of an ideal gas is a...Ch. 12.6 - Prob. 49PCh. 12.6 - Show that = ( P/ T)v.Ch. 12.6 - Prob. 51PCh. 12.6 - Prob. 52PCh. 12.6 - Prob. 53PCh. 12.6 - Prob. 54PCh. 12.6 - Prob. 55PCh. 12.6 - Does the Joule-Thomson coefficient of a substance...Ch. 12.6 - The pressure of a fluid always decreases during an...Ch. 12.6 - Will the temperature of helium change if it is...Ch. 12.6 - Estimate the Joule-Thomson coefficient of...Ch. 12.6 - Estimate the Joule-Thomson coefficient of...Ch. 12.6 - Prob. 61PCh. 12.6 - Steam is throttled slightly from 1 MPa and 300C....Ch. 12.6 - What is the most general equation of state for...Ch. 12.6 - Prob. 64PCh. 12.6 - Consider a gas whose equation of state is P(v a)...Ch. 12.6 - Prob. 66PCh. 12.6 - What is the enthalpy departure?Ch. 12.6 - On the generalized enthalpy departure chart, the...Ch. 12.6 - Why is the generalized enthalpy departure chart...Ch. 12.6 - What is the error involved in the (a) enthalpy and...Ch. 12.6 - Prob. 71PCh. 12.6 - Saturated water vapor at 300C is expanded while...Ch. 12.6 - Determine the enthalpy change and the entropy...Ch. 12.6 - Prob. 74PCh. 12.6 - Prob. 75PCh. 12.6 - Prob. 77PCh. 12.6 - Propane is compressed isothermally by a...Ch. 12.6 - Prob. 81PCh. 12.6 - Prob. 82RPCh. 12.6 - Starting with the relation dh = T ds + vdP, show...Ch. 12.6 - Using the cyclic relation and the first Maxwell...Ch. 12.6 - For ideal gases, the development of the...Ch. 12.6 - Show that cv=T(vT)s(PT)vandcp=T(PT)s(vT)PCh. 12.6 - Temperature and pressure may be defined as...Ch. 12.6 - For a homogeneous (single-phase) simple pure...Ch. 12.6 - For a homogeneous (single-phase) simple pure...Ch. 12.6 - Prob. 90RPCh. 12.6 - Prob. 91RPCh. 12.6 - Estimate the cpof nitrogen at 300 kPa and 400 K,...Ch. 12.6 - Prob. 93RPCh. 12.6 - Prob. 94RPCh. 12.6 - Prob. 95RPCh. 12.6 - Methane is to be adiabatically and reversibly...Ch. 12.6 - Prob. 97RPCh. 12.6 - Prob. 98RPCh. 12.6 - Prob. 99RPCh. 12.6 - An adiabatic 0.2-m3 storage tank that is initially...Ch. 12.6 - Prob. 102FEPCh. 12.6 - Consider the liquidvapor saturation curve of a...Ch. 12.6 - For a gas whose equation of state is P(v b) = RT,...Ch. 12.6 - Prob. 105FEPCh. 12.6 - Prob. 106FEP
Knowledge Booster
Learn more about
Need a deep-dive on the concept behind this application? Look no further. Learn more about this topic, mechanical-engineering and related others by exploring similar questions and additional content below.Similar questions
- 1. A frictionless piston-cylinder device with cross-section area of 0.01 m² contains 0.5 m3 gaseous ammonia initially at 200 kPa and 135 °C. Now the gas is isothermally compressed until the pressure increases to 800 psig. The surrounding pressure is 100 kPa and the gravitational force is 9.8 m/s? a. What is the mass of the gas in kg b. What is the mass of the piston in kg c. Calculate the volume in m³ of the compressed gasarrow_forward0.25kg/s of Carbon Dioxide (R = 0.1889 kJ/kg-K, k = 1.289) undergo a certain process in a close system from initial volume and temperature of 268cm3 and 134K to a final volume and temperature of 840cm3 and 402K respectively. From the data given, perform necessary analysis in determining the type of process to further solve the following questions as follow: a. Work done by on the system (kJ/s) b. Change in Entropy (kW/K) c. Heat added/rejected by the system (kJ/s)arrow_forwardA rigid vessel contains 4.45lb,m of steam at 6.25 MPa and 350°K. Determine its enthalpy in kJ using steam tables only.arrow_forward
- Consider a piston-cylinder device that contains argon gas. The gas is initially at 140 kPa, 10 °C, and a volume of 0.1 m³. The gas is compressed in a polytropic process to 0.70 MPa and 280 °C. Argon can be assumed an ideal gas. Use the following Data for Argon gas: R=0.20813 kJ/kg.K, Cv=0.3122 kJ/kg.K, Cp=0.52033 kJ/kg.Karrow_forwardDetermine the internal energy change for carbon monoxide, in kJ/kg, as it is heated from 312° K to 1456° K, using the ideal gas properties tablearrow_forwardA 2.80-mol sample of helium gas initially at 300 K, and 0.400 atm is compressed isothermally to 1.40 atm. Note that the helium behaves as an ideal gas. (a) Find the final volume of the gas. m³ (b) Find the work done on the gas. kJ (c) Find the energy transferred by heat. kJarrow_forward
- 1. 10 kg of R – 134a at 300kPa fills a rigid container whose volume is 14 L. The container is now heated until the pressure is 600kPa. Sketch the process on a P – v diagram with respect to saturation lines and give reasons. Vf@300kPa = 7.7 × 10−4 m³/kg, vg@300kPa = 0.068 m³/kg; Vf@600kPa = 8.2 x 10 m³/kg, vg@600kPa = 0.034 m³/kg.arrow_forwardQUICKLY AND CORRECTLY PLEASE For a certain ideal gas (R = 25.8 ft.bf/lbm.R and k = 1.09 ) occupy a volume of 15 ft3 at 75 psia and 80o F undergoes a constant volume process, until the final pressure becomes 80 psia. Determine the heat transfer in Btu.arrow_forwardIn the first case, there is 5 kg of water at 300 kPa (3 bar) pressure and 60% dryness in a closed container whose volume does not change. Heat transfer is performed until the closed container water reaches a pressure value of 1 MPa. The limit temperature of the closed container is 300 Cwill be taken.Note: Changes in kinetic and potential energies are negligible.(P0 = 100 kPa, T0 = 25 ◦C and T (K) = 273.15 + ◦C)a) Find the heat transfer to the sealed container.b) Find the exergy that disappears during the process.arrow_forward
- 1arrow_forwardA mass of 0.1 kg of helium fills a 0.2 m³ rigid vessel at 350 kPa. The vessel is heated until the pressure is 710 kPa. Calculate the temperature change of helium (in K) as a result of this heating. The gas constant of helium is R= 2.0769 kPa-m3/kg-K. Helium 0.1 kg 0.2 m 350 kPa The temperature change is K.arrow_forwardone kg of water at 47.8°C is heated unde Constant pressure at 13.7 bar until it is Converted into Staam with 111 of Super-heated. Determine the quantety of heat Supplied during Superheating and the total heat .arrow_forward
arrow_back_ios
SEE MORE QUESTIONS
arrow_forward_ios
Recommended textbooks for you
Elements Of ElectromagneticsMechanical EngineeringISBN:9780190698614Author:Sadiku, Matthew N. O.Publisher:Oxford University Press
Mechanics of Materials (10th Edition)Mechanical EngineeringISBN:9780134319650Author:Russell C. HibbelerPublisher:PEARSON
Thermodynamics: An Engineering ApproachMechanical EngineeringISBN:9781259822674Author:Yunus A. Cengel Dr., Michael A. BolesPublisher:McGraw-Hill Education
Control Systems EngineeringMechanical EngineeringISBN:9781118170519Author:Norman S. NisePublisher:WILEY
Mechanics of Materials (MindTap Course List)Mechanical EngineeringISBN:9781337093347Author:Barry J. Goodno, James M. GerePublisher:Cengage Learning
Engineering Mechanics: StaticsMechanical EngineeringISBN:9781118807330Author:James L. Meriam, L. G. Kraige, J. N. BoltonPublisher:WILEY
Elements Of Electromagnetics
Mechanical Engineering
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Oxford University Press
Mechanics of Materials (10th Edition)
Mechanical Engineering
ISBN:9780134319650
Author:Russell C. Hibbeler
Publisher:PEARSON
Thermodynamics: An Engineering Approach
Mechanical Engineering
ISBN:9781259822674
Author:Yunus A. Cengel Dr., Michael A. Boles
Publisher:McGraw-Hill Education
Control Systems Engineering
Mechanical Engineering
ISBN:9781118170519
Author:Norman S. Nise
Publisher:WILEY
Mechanics of Materials (MindTap Course List)
Mechanical Engineering
ISBN:9781337093347
Author:Barry J. Goodno, James M. Gere
Publisher:Cengage Learning
Engineering Mechanics: Statics
Mechanical Engineering
ISBN:9781118807330
Author:James L. Meriam, L. G. Kraige, J. N. Bolton
Publisher:WILEY
First Law of Thermodynamics, Basic Introduction - Internal Energy, Heat and Work - Chemistry; Author: The Organic Chemistry Tutor;https://www.youtube.com/watch?v=NyOYW07-L5g;License: Standard youtube license