Enviar búsqueda
Cargar
Ch.12
•
8 recomendaciones
•
11,740 vistas
R G Sanjay Prakash
Seguir
Tecnología
Empresariales
Denunciar
Compartir
Denunciar
Compartir
1 de 92
Descargar ahora
Descargar para leer sin conexión
Recomendados
Ch.3
Ch.3
R G Sanjay Prakash
Ch.15
Ch.15
R G Sanjay Prakash
Ch.14
Ch.14
R G Sanjay Prakash
Ch.4
Ch.4
R G Sanjay Prakash
Fluid mechanic white (cap2.1)
Fluid mechanic white (cap2.1)
Raul Garcia
Ch.10
Ch.10
R G Sanjay Prakash
Sheet 1 pressure measurments
Sheet 1 pressure measurments
asomah
Thermodynamics problems
Thermodynamics problems
Yuri Melliza
Recomendados
Ch.3
Ch.3
R G Sanjay Prakash
Ch.15
Ch.15
R G Sanjay Prakash
Ch.14
Ch.14
R G Sanjay Prakash
Ch.4
Ch.4
R G Sanjay Prakash
Fluid mechanic white (cap2.1)
Fluid mechanic white (cap2.1)
Raul Garcia
Ch.10
Ch.10
R G Sanjay Prakash
Sheet 1 pressure measurments
Sheet 1 pressure measurments
asomah
Thermodynamics problems
Thermodynamics problems
Yuri Melliza
Mcconkey Chapter 9 solution
Mcconkey Chapter 9 solution
Azeem Waqar
004 ideal gas_law
004 ideal gas_law
physics101
Ch.1
Ch.1
R G Sanjay Prakash
Thermodynamics Problems Chapter 1
Thermodynamics Problems Chapter 1
VJTI Production
Ch.5
Ch.5
R G Sanjay Prakash
110 fluid mechanics
110 fluid mechanics
Zakaria Masud
Thermodynamics Chapter 3- Heat Transfer
Thermodynamics Chapter 3- Heat Transfer
VJTI Production
Design coaching22
Design coaching22
Neil Ian Lago
Termo 7 ca 17 1
Termo 7 ca 17 1
sebastian rodriguez romero
First Law of Thermodynamics: Energy Conservation For Mechanical and Industria...
First Law of Thermodynamics: Energy Conservation For Mechanical and Industria...
Kum Visal
EES Functions and Procedures for Forced convection heat transfer
EES Functions and Procedures for Forced convection heat transfer
tmuliya
Thermodynamics Hw #1
Thermodynamics Hw #1
littlepine13
Thermo problem set no. 2
Thermo problem set no. 2
Yuri Melliza
Mc conkey 13-pb
Mc conkey 13-pb
Azeem Waqar
EES for Thermodynamics
EES for Thermodynamics
Naveed Rehman
Dalton's Law of Partial Pressures
Dalton's Law of Partial Pressures
Ed Erhardt
Engineering Fluid Mechanics 11th Edition Elger Solutions Manual
Engineering Fluid Mechanics 11th Edition Elger Solutions Manual
VeronicaIngramss
Physics Formula list (1)
Physics Formula list (1)
WAYNE FERNANDES
Chemistry notes ideal gas laws
Chemistry notes ideal gas laws
hega coc
Ideal gas law firs tthis one
Ideal gas law firs tthis one
Dr Robert Craig PhD
Ch06b entropy
Ch06b entropy
suresh301
Topic 2 kft 131
Topic 2 kft 131
Nor Qurratu'aini Abdullah
Más contenido relacionado
La actualidad más candente
Mcconkey Chapter 9 solution
Mcconkey Chapter 9 solution
Azeem Waqar
004 ideal gas_law
004 ideal gas_law
physics101
Ch.1
Ch.1
R G Sanjay Prakash
Thermodynamics Problems Chapter 1
Thermodynamics Problems Chapter 1
VJTI Production
Ch.5
Ch.5
R G Sanjay Prakash
110 fluid mechanics
110 fluid mechanics
Zakaria Masud
Thermodynamics Chapter 3- Heat Transfer
Thermodynamics Chapter 3- Heat Transfer
VJTI Production
Design coaching22
Design coaching22
Neil Ian Lago
Termo 7 ca 17 1
Termo 7 ca 17 1
sebastian rodriguez romero
First Law of Thermodynamics: Energy Conservation For Mechanical and Industria...
First Law of Thermodynamics: Energy Conservation For Mechanical and Industria...
Kum Visal
EES Functions and Procedures for Forced convection heat transfer
EES Functions and Procedures for Forced convection heat transfer
tmuliya
Thermodynamics Hw #1
Thermodynamics Hw #1
littlepine13
Thermo problem set no. 2
Thermo problem set no. 2
Yuri Melliza
Mc conkey 13-pb
Mc conkey 13-pb
Azeem Waqar
EES for Thermodynamics
EES for Thermodynamics
Naveed Rehman
Dalton's Law of Partial Pressures
Dalton's Law of Partial Pressures
Ed Erhardt
Engineering Fluid Mechanics 11th Edition Elger Solutions Manual
Engineering Fluid Mechanics 11th Edition Elger Solutions Manual
VeronicaIngramss
Physics Formula list (1)
Physics Formula list (1)
WAYNE FERNANDES
Chemistry notes ideal gas laws
Chemistry notes ideal gas laws
hega coc
Ideal gas law firs tthis one
Ideal gas law firs tthis one
Dr Robert Craig PhD
La actualidad más candente
(20)
Mcconkey Chapter 9 solution
Mcconkey Chapter 9 solution
004 ideal gas_law
004 ideal gas_law
Ch.1
Ch.1
Thermodynamics Problems Chapter 1
Thermodynamics Problems Chapter 1
Ch.5
Ch.5
110 fluid mechanics
110 fluid mechanics
Thermodynamics Chapter 3- Heat Transfer
Thermodynamics Chapter 3- Heat Transfer
Design coaching22
Design coaching22
Termo 7 ca 17 1
Termo 7 ca 17 1
First Law of Thermodynamics: Energy Conservation For Mechanical and Industria...
First Law of Thermodynamics: Energy Conservation For Mechanical and Industria...
EES Functions and Procedures for Forced convection heat transfer
EES Functions and Procedures for Forced convection heat transfer
Thermodynamics Hw #1
Thermodynamics Hw #1
Thermo problem set no. 2
Thermo problem set no. 2
Mc conkey 13-pb
Mc conkey 13-pb
EES for Thermodynamics
EES for Thermodynamics
Dalton's Law of Partial Pressures
Dalton's Law of Partial Pressures
Engineering Fluid Mechanics 11th Edition Elger Solutions Manual
Engineering Fluid Mechanics 11th Edition Elger Solutions Manual
Physics Formula list (1)
Physics Formula list (1)
Chemistry notes ideal gas laws
Chemistry notes ideal gas laws
Ideal gas law firs tthis one
Ideal gas law firs tthis one
Similar a Ch.12
Ch06b entropy
Ch06b entropy
suresh301
Topic 2 kft 131
Topic 2 kft 131
Nor Qurratu'aini Abdullah
Chm3410hwk02 soln.252145237
Chm3410hwk02 soln.252145237
Samandar Yuldoshev
Manual Solution Fermi Thermodynamics
Manual Solution Fermi Thermodynamics
dklajd
Exerc cios resolvidos_-_cap._01-atkins_(a)
Exerc cios resolvidos_-_cap._01-atkins_(a)
Alisson Moreira
heat diffusion equation.ppt
heat diffusion equation.ppt
056JatinGavel
heat diffusion equation.ppt
heat diffusion equation.ppt
056JatinGavel
Transients characteristics
Transients characteristics
Aldo Uribe
Chapter 5 (ideal gas & gas mixture)
Chapter 5 (ideal gas & gas mixture)
Yuri Melliza
Physics
Physics
Decebae Manalo
Thermodynamics lecture 9
Thermodynamics lecture 9
Archit Gadhok
Clausius-clapeyron Equation
Clausius-clapeyron Equation
Dr. E. Sindhuja Elangovan
slides-enbal-2up.pdf
slides-enbal-2up.pdf
ssuser7084f91
Thermodynamics -Basic concepts
Thermodynamics -Basic concepts
selvakumar948
Ch 05 Thermodynamics (1).ppt
Ch 05 Thermodynamics (1).ppt
Ser Louis Fabunan
Ch 05 Thermodynamics.pdf
Ch 05 Thermodynamics.pdf
Agni73
Study of interactions among work, energy, and heat. Calorimetry
Study of interactions among work, energy, and heat. Calorimetry
seep23lecmcm
Statistics Homework Help
Statistics Homework Help
Statistics Homework Helper
Multiple Linear Regression Homework Help
Multiple Linear Regression Homework Help
Statistics Homework Helper
Differential Equations 4th Edition Blanchard Solutions Manual
Differential Equations 4th Edition Blanchard Solutions Manual
qyfuc
Similar a Ch.12
(20)
Ch06b entropy
Ch06b entropy
Topic 2 kft 131
Topic 2 kft 131
Chm3410hwk02 soln.252145237
Chm3410hwk02 soln.252145237
Manual Solution Fermi Thermodynamics
Manual Solution Fermi Thermodynamics
Exerc cios resolvidos_-_cap._01-atkins_(a)
Exerc cios resolvidos_-_cap._01-atkins_(a)
heat diffusion equation.ppt
heat diffusion equation.ppt
heat diffusion equation.ppt
heat diffusion equation.ppt
Transients characteristics
Transients characteristics
Chapter 5 (ideal gas & gas mixture)
Chapter 5 (ideal gas & gas mixture)
Physics
Physics
Thermodynamics lecture 9
Thermodynamics lecture 9
Clausius-clapeyron Equation
Clausius-clapeyron Equation
slides-enbal-2up.pdf
slides-enbal-2up.pdf
Thermodynamics -Basic concepts
Thermodynamics -Basic concepts
Ch 05 Thermodynamics (1).ppt
Ch 05 Thermodynamics (1).ppt
Ch 05 Thermodynamics.pdf
Ch 05 Thermodynamics.pdf
Study of interactions among work, energy, and heat. Calorimetry
Study of interactions among work, energy, and heat. Calorimetry
Statistics Homework Help
Statistics Homework Help
Multiple Linear Regression Homework Help
Multiple Linear Regression Homework Help
Differential Equations 4th Edition Blanchard Solutions Manual
Differential Equations 4th Edition Blanchard Solutions Manual
Más de R G Sanjay Prakash
Kota super thermal power plant
Kota super thermal power plant
R G Sanjay Prakash
Presentation joining processes
Presentation joining processes
R G Sanjay Prakash
Metal casting process
Metal casting process
R G Sanjay Prakash
Lecture 1 metal_forming
Lecture 1 metal_forming
R G Sanjay Prakash
Sheet metal operations1class_
Sheet metal operations1class_
R G Sanjay Prakash
Sheet metal operations1class
Sheet metal operations1class
R G Sanjay Prakash
Presentation joining processes
Presentation joining processes
R G Sanjay Prakash
Plywood manufacturing process
Plywood manufacturing process
R G Sanjay Prakash
Metal casting process
Metal casting process
R G Sanjay Prakash
Lecture 1 metal_forming
Lecture 1 metal_forming
R G Sanjay Prakash
Lathe presentation1 to_be_class_
Lathe presentation1 to_be_class_
R G Sanjay Prakash
Fitting
Fitting
R G Sanjay Prakash
Fitting(2)
Fitting(2)
R G Sanjay Prakash
Course plan intt_pse_psm_jan_2010_to_april_2010
Course plan intt_pse_psm_jan_2010_to_april_2010
R G Sanjay Prakash
Carpentry9333
Carpentry9333
R G Sanjay Prakash
Ch.17
Ch.17
R G Sanjay Prakash
Ch.16
Ch.16
R G Sanjay Prakash
Ch.13
Ch.13
R G Sanjay Prakash
Ch.8
Ch.8
R G Sanjay Prakash
Ch.6
Ch.6
R G Sanjay Prakash
Más de R G Sanjay Prakash
(20)
Kota super thermal power plant
Kota super thermal power plant
Presentation joining processes
Presentation joining processes
Metal casting process
Metal casting process
Lecture 1 metal_forming
Lecture 1 metal_forming
Sheet metal operations1class_
Sheet metal operations1class_
Sheet metal operations1class
Sheet metal operations1class
Presentation joining processes
Presentation joining processes
Plywood manufacturing process
Plywood manufacturing process
Metal casting process
Metal casting process
Lecture 1 metal_forming
Lecture 1 metal_forming
Lathe presentation1 to_be_class_
Lathe presentation1 to_be_class_
Fitting
Fitting
Fitting(2)
Fitting(2)
Course plan intt_pse_psm_jan_2010_to_april_2010
Course plan intt_pse_psm_jan_2010_to_april_2010
Carpentry9333
Carpentry9333
Ch.17
Ch.17
Ch.16
Ch.16
Ch.13
Ch.13
Ch.8
Ch.8
Ch.6
Ch.6
Último
Strategies for Unlocking Knowledge Management in Microsoft 365 in the Copilot...
Strategies for Unlocking Knowledge Management in Microsoft 365 in the Copilot...
Drew Madelung
Workshop - Best of Both Worlds_ Combine KG and Vector search for enhanced R...
Workshop - Best of Both Worlds_ Combine KG and Vector search for enhanced R...
Neo4j
GenCyber Cyber Security Day Presentation
GenCyber Cyber Security Day Presentation
Michael W. Hawkins
Axa Assurance Maroc - Insurer Innovation Award 2024
Axa Assurance Maroc - Insurer Innovation Award 2024
The Digital Insurer
How to Troubleshoot Apps for the Modern Connected Worker
How to Troubleshoot Apps for the Modern Connected Worker
ThousandEyes
Boost Fertility New Invention Ups Success Rates.pdf
Boost Fertility New Invention Ups Success Rates.pdf
sudhanshuwaghmare1
What Are The Drone Anti-jamming Systems Technology?
What Are The Drone Anti-jamming Systems Technology?
Antenna Manufacturer Coco
The 7 Things I Know About Cyber Security After 25 Years | April 2024
The 7 Things I Know About Cyber Security After 25 Years | April 2024
Rafal Los
presentation ICT roal in 21st century education
presentation ICT roal in 21st century education
jfdjdjcjdnsjd
How to convert PDF to text with Nanonets
How to convert PDF to text with Nanonets
naman860154
Powerful Google developer tools for immediate impact! (2023-24 C)
Powerful Google developer tools for immediate impact! (2023-24 C)
wesley chun
The Role of Taxonomy and Ontology in Semantic Layers - Heather Hedden.pdf
The Role of Taxonomy and Ontology in Semantic Layers - Heather Hedden.pdf
Enterprise Knowledge
TrustArc Webinar - Stay Ahead of US State Data Privacy Law Developments
TrustArc Webinar - Stay Ahead of US State Data Privacy Law Developments
TrustArc
2024: Domino Containers - The Next Step. News from the Domino Container commu...
2024: Domino Containers - The Next Step. News from the Domino Container commu...
Martijn de Jong
🐬 The future of MySQL is Postgres 🐘
🐬 The future of MySQL is Postgres 🐘
RTylerCroy
Data Cloud, More than a CDP by Matt Robison
Data Cloud, More than a CDP by Matt Robison
Anna Loughnan Colquhoun
From Event to Action: Accelerate Your Decision Making with Real-Time Automation
From Event to Action: Accelerate Your Decision Making with Real-Time Automation
Safe Software
08448380779 Call Girls In Diplomatic Enclave Women Seeking Men
08448380779 Call Girls In Diplomatic Enclave Women Seeking Men
Delhi Call girls
Strategize a Smooth Tenant-to-tenant Migration and Copilot Takeoff
Strategize a Smooth Tenant-to-tenant Migration and Copilot Takeoff
sammart93
CNv6 Instructor Chapter 6 Quality of Service
CNv6 Instructor Chapter 6 Quality of Service
giselly40
Último
(20)
Strategies for Unlocking Knowledge Management in Microsoft 365 in the Copilot...
Strategies for Unlocking Knowledge Management in Microsoft 365 in the Copilot...
Workshop - Best of Both Worlds_ Combine KG and Vector search for enhanced R...
Workshop - Best of Both Worlds_ Combine KG and Vector search for enhanced R...
GenCyber Cyber Security Day Presentation
GenCyber Cyber Security Day Presentation
Axa Assurance Maroc - Insurer Innovation Award 2024
Axa Assurance Maroc - Insurer Innovation Award 2024
How to Troubleshoot Apps for the Modern Connected Worker
How to Troubleshoot Apps for the Modern Connected Worker
Boost Fertility New Invention Ups Success Rates.pdf
Boost Fertility New Invention Ups Success Rates.pdf
What Are The Drone Anti-jamming Systems Technology?
What Are The Drone Anti-jamming Systems Technology?
The 7 Things I Know About Cyber Security After 25 Years | April 2024
The 7 Things I Know About Cyber Security After 25 Years | April 2024
presentation ICT roal in 21st century education
presentation ICT roal in 21st century education
How to convert PDF to text with Nanonets
How to convert PDF to text with Nanonets
Powerful Google developer tools for immediate impact! (2023-24 C)
Powerful Google developer tools for immediate impact! (2023-24 C)
The Role of Taxonomy and Ontology in Semantic Layers - Heather Hedden.pdf
The Role of Taxonomy and Ontology in Semantic Layers - Heather Hedden.pdf
TrustArc Webinar - Stay Ahead of US State Data Privacy Law Developments
TrustArc Webinar - Stay Ahead of US State Data Privacy Law Developments
2024: Domino Containers - The Next Step. News from the Domino Container commu...
2024: Domino Containers - The Next Step. News from the Domino Container commu...
🐬 The future of MySQL is Postgres 🐘
🐬 The future of MySQL is Postgres 🐘
Data Cloud, More than a CDP by Matt Robison
Data Cloud, More than a CDP by Matt Robison
From Event to Action: Accelerate Your Decision Making with Real-Time Automation
From Event to Action: Accelerate Your Decision Making with Real-Time Automation
08448380779 Call Girls In Diplomatic Enclave Women Seeking Men
08448380779 Call Girls In Diplomatic Enclave Women Seeking Men
Strategize a Smooth Tenant-to-tenant Migration and Copilot Takeoff
Strategize a Smooth Tenant-to-tenant Migration and Copilot Takeoff
CNv6 Instructor Chapter 6 Quality of Service
CNv6 Instructor Chapter 6 Quality of Service
Ch.12
1.
12-1
Chapter 12 THERMODYNAMIC PROPERTY RELATIONS Partial Derivatives and Associated Relations 12-1C z dz ∂x ≡ dx ∂y ≡ dy dz = (∂z ) x + (∂z ) y (∂z)y (∂z)x y y + dy y dy x dx x+dx x 12-2C For functions that depend on one variable, they are identical. For functions that depend on two or more variable, the partial differential represents the change in the function with one of the variables as the other variables are held constant. The ordinary differential for such functions represents the total change as a result of differential changes in all variables. 12-3C (a) (∂x)y = dx ; (b) (∂z) y ≤ dz; and (c) dz = (∂z)x + (∂z) y 12-4C Yes. 12-5C Yes. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
2.
12-2 12-6 Air at
a specified temperature and specific volume is considered. The changes in pressure corresponding to a certain increase of different properties are to be determined. Assumptions Air is an ideal gas. Properties The gas constant of air is R = 0.287 kPa·m3/kg·K (Table A-1). Analysis An ideal gas equation can be expressed as P = RT/v. Noting that R is a constant and P = P(T, v), ⎛ ∂P ⎞ ⎛ ∂P ⎞ R dT RT dv dP = ⎜ ⎟ dT + ⎜ ⎟ dv = − ⎝ ∂T ⎠v ⎝ ∂v ⎠ T v v2 (a) The change in T can be expressed as dT ≅ ΔT = 400 × 0.01 = 4.0 K. At v = constant, (0.287 kPa ⋅ m 3 /kg ⋅ K)(4.0 K) (dP )v = R dT = = 1.276 kPa v 0.90 m 3 /kg (b) The change in v can be expressed as dv ≅ Δv = 0.90 × 0.01 = 0.009 m3/kg. At T = constant, RT dv (0.287 kPa ⋅ m 3 /kg ⋅ K)(400K)(0.009 m 3 /kg) (dP )T =− =− = −1.276 kPa v2 (0.90 m 3 /kg) 2 (c) When both v and T increases by 1%, the change in P becomes dP = (dP)v + (dP )T = 1.276 + (−1.276) = 0 Thus the changes in T and v balance each other. 12-7 Helium at a specified temperature and specific volume is considered. The changes in pressure corresponding to a certain increase of different properties are to be determined. Assumptions Helium is an ideal gas Properties The gas constant of helium is R = 2.0769 kPa·m3/kg·K (Table A-1). Analysis An ideal gas equation can be expressed as P = RT/v. Noting that R is a constant and P = P(T, v ), ⎛ ∂P ⎞ ⎛ ∂P ⎞ R dT RT dv dP = ⎜ ⎟ dT + ⎜ ⎟ dv = − ⎝ ∂T ⎠v ⎝ ∂v ⎠ T v v2 (a) The change in T can be expressed as dT ≅ ΔT = 400 × 0.01 = 4.0 K. At v = constant, (2.0769 kPa ⋅ m 3 /kg ⋅ K)(4.0 K) (dP )v = R dT = = 9.231 kPa v 0.90 m 3 /kg (b) The change in v can be expressed as d v ≅ Δ v = 0.90 × 0.01 = 0.009 m3/kg. At T = constant, RT dv (2.0769 kPa ⋅ m 3 /kg ⋅ K)(400 K)(0.009 m 3 ) (dP )T =− = = −9.231 kPa v2 (0.90 m 3 /kg) 2 (c) When both v and T increases by 1%, the change in P becomes dP = (dP) v + (dP ) T = 9.231 + (−9.231) = 0 Thus the changes in T and v balance each other. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
3.
12-3 12-8 It is
to be proven for an ideal gas that the P = constant lines on a T- v diagram are straight lines and that the high pressure lines are steeper than the low-pressure lines. Analysis (a) For an ideal gas Pv = RT or T = Pv/R. Taking the partial derivative of T with respect to v holding P constant yields ⎛ ∂T ⎞ P T ⎜ ⎟ = ⎝ ∂v ⎠ P R which remains constant at P = constant. Thus the derivative P = const (∂T/∂v)P, which represents the slope of the P = const. lines on a T-v diagram, remains constant. That is, the P = const. lines are straight lines on a T-v diagram. (b) The slope of the P = const. lines on a T-v diagram is equal to P/R, which is proportional to P. Therefore, the high pressure lines are steeper than low pressure lines on the T-v v diagram. 12-9 A relation is to be derived for the slope of the v = constant lines on a T-P diagram for a gas that obeys the van der Waals equation of state. Analysis The van der Waals equation of state can be expressed as 1⎛ ⎞ ⎟(v − b ) a T= ⎜P + 2 R⎝ v ⎠ Taking the derivative of T with respect to P holding v constant, ⎛ ∂T ⎞ 1 v −b ⎜ ⎟ = (1 + 0)(v − b ) = ⎝ ∂P ⎠v R R which is the slope of the v = constant lines on a T-P diagram. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
4.
12-4 12-10 Nitrogen gas
at a specified state is considered. The cp and cv of the nitrogen are to be determined using Table A-18, and to be compared to the values listed in Table A-2b. Analysis The cp and cv of ideal gases depends on temperature only, and are expressed as cp(T) = dh(T)/dT and cv(T) = du(T)/dT. Approximating the differentials as differences about 400 K, the cp and cv values are determined to be ⎛ dh(T ) ⎞ ⎛ Δh(T ) ⎞ cp c p (400 K ) = ⎜ ⎟ ≅⎜ ⎟ ⎝ dT ⎠ T = 400 K ⎝ ΔT ⎠ T ≅ 400 K h h(410 K ) − h(390 K ) = (410 − 390)K (11,932 − 11,347)/28.0 kJ/kg = (410 − 390)K = 1.045 kJ/kg ⋅ K (Compare: Table A-2b at 400 K → cp = 1.044 kJ/kg·K) T ⎛ du (T ) ⎞ ⎛ Δu (T ) ⎞ cv (400K ) = ⎜ ⎟ ≅⎜ ⎟ ⎝ dT ⎠ T = 400 K ⎝ ΔT ⎠ T ≅ 400 K u (410 K ) − u (390 K ) = (410 − 390)K (8,523 − 8,104)/28.0 kJ/kg = = 0.748 kJ/kg ⋅ K (410 − 390)K (Compare: Table A-2b at 400 K → cv = 0.747 kJ/kg·K) PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
5.
12-5 12-11E Nitrogen gas
at a specified state is considered. The cp and cv of the nitrogen are to be determined using Table A-18E, and to be compared to the values listed in Table A-2Eb. Analysis The cp and cv of ideal gases depends on temperature only, and are expressed as cp(T) = dh(T)/dT and cv(T) = du(T)/dT. Approximating the differentials as differences about 600 R, the cp and cv values are determined to be ⎛ dh(T ) ⎞ ⎛ Δh(T ) ⎞ c p (600 R ) = ⎜ ⎟ ≅⎜ ⎟ ⎝ dT ⎠T = 600 R ⎝ ΔT ⎠T ≅ 600 R h(620 R ) − h(580 R ) = (620 − 580)R (4,307.1 − 4,028.7)/28.0 Btu/lbm = = 0.249 Btu/lbm ⋅ R (620 − 580)R (Compare: Table A-2Eb at 600 R → cp = 0.248 Btu/lbm·R ) ⎛ du (T ) ⎞ ⎛ Δu (T ) ⎞ cv (600 R ) = ⎜ ⎟ ≅⎜ ⎟ ⎝ dT ⎠T = 600 R ⎝ ΔT ⎠T ≅ 600 R u (620 R ) − u (580 R ) = (620 − 580)R (3,075.9 − 2,876.9)/28.0 Btu/lbm = = 0.178 Btu/lbm ⋅ R (620 − 580) R (Compare: Table A-2Eb at 600 R → cv = 0.178 Btu/lbm·R) PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
6.
12-6 12-12 The state
of an ideal gas is altered slightly. The change in the specific volume of the gas is to be determined using differential relations and the ideal-gas relation at each state. Assumptions The gas is air and air is an ideal gas. Properties The gas constant of air is R = 0.287 kPa·m3/kg·K (Table A-1). Analysis (a) The changes in T and P can be expressed as dT ≅ ΔT = (404 − 400)K = 4 K dP ≅ ΔP = (96 − 100)kPa = −4 kPa The ideal gas relation Pv = RT can be expressed as v = RT/P. Note that R is a constant and v = v (T, P). Applying the total differential relation and using average values for T and P, ⎛ ∂v ⎞ ⎛ ∂v ⎞ R dT RT dP dv = ⎜ ⎟ dT + ⎜ ⎟ dP = − ⎝ ∂T ⎠ P ⎝ ∂P ⎠ T P P2 ⎛ 4K (402 K)(−4 kPa) ⎞ = (0.287 kPa ⋅ m 3 /kg ⋅ K)⎜ − ⎟ ⎜ 98 kPa (98 kPa) 2 ⎟ ⎝ ⎠ = (0.0117 m 3 /kg) + (0.04805 m 3 /kg) = 0.0598 m 3 /kg (b) Using the ideal gas relation at each state, RT1 (0.287 kPa ⋅ m 3 /kg ⋅ K)(400 K) v1 = = = 1.1480 m 3 /kg P1 100 kPa RT2 (0.287 kPa ⋅ m 3 /kg ⋅ K)(404 K) v2 = = = 1.2078 m 3 /kg P2 96 kPa Thus, Δv = v 2 − v1 = 1.2078 − 1.1480 = 0.0598 m3 /kg The two results are identical. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
7.
12-7 12-13 Using the
equation of state P(v-a) = RT, the cyclic relation, and the reciprocity relation at constant v are to be verified. Analysis (a) This equation of state involves three variables P, v, and T. Any two of these can be taken as the independent variables, with the remaining one being the dependent variable. Replacing x, y, and z by P, v, and T, the cyclic relation can be expressed as ⎛ ∂P ⎞ ⎛ ∂v ⎞ ⎛ ∂T ⎞ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ = −1 ⎝ ∂v ⎠T ⎝ ∂T ⎠ P ⎝ ∂P ⎠v where RT ⎛ ∂P ⎞ − RT P P= ⎯⎯→ ⎜ ⎟ = =− v −a ⎝ ∂v ⎠ T (v − a )2 v −a RT ⎛ ∂v ⎞ R v= +a ⎯ ⎯→ ⎜ ⎟ = P ⎝ ∂T ⎠ P P P (v − a) ⎛ ∂T ⎞ v −a T= ⎯ ⎯→ ⎜ ⎟ = R ⎝ ∂P ⎠ v R Substituting, ⎛ ∂P ⎞ ⎛ ∂v ⎞ ⎛ ∂T ⎞ ⎛ P ⎞⎛ R ⎞⎛ v − a ⎞ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ = ⎜− ⎟⎜ ⎟⎜ ⎟ = −1 ⎝ ∂v ⎠T ⎝ ∂T ⎠ P ⎝ ∂P ⎠v ⎝ v − a ⎠⎝ P ⎠⎝ R ⎠ which is the desired result. (b) The reciprocity rule for this gas at v = constant can be expressed as ⎛ ∂P ⎞ 1 ⎜ ⎟ = ⎝ ∂T ⎠v (∂T / ∂P)v P (v − a) ⎛ ∂T ⎞ v −a T= ⎯⎯→ ⎜ ⎟ = R ⎝ ∂P ⎠v R RT ⎛ ∂P ⎞ R P= ⎯ ⎯→ ⎜ ⎟ = v −a ⎝ ∂T ⎠v v − a We observe that the first differential is the inverse of the second one. Thus the proof is complete. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
8.
12-8 The Maxwell Relations 12-14
The validity of the last Maxwell relation for refrigerant-134a at a specified state is to be verified. Analysis We do not have exact analytical property relations for refrigerant-134a, and thus we need to replace the differential quantities in the last Maxwell relation with the corresponding finite quantities. Using property values from the tables about the specified state, ⎛ ∂s ⎞ ? ⎛ ∂v ⎞ ⎜ ⎟ =− ⎜ ⎟ ⎝ ∂P ⎠ T ⎝ ∂T ⎠ P ⎛ Δs ⎞ ? ⎛ Δv ⎞ ⎜ ⎟ ≅−⎜ ⎟ ⎝ ΔP ⎠ T =80°C ⎝ ΔT ⎠ P =1200 kPa ⎛ s1400 kPa − s1000 kPa ⎞ ? ⎛ v 100°C − v 60° C ⎞ ⎜ ⎟ ≅ −⎜ ⎟ ⎜ (1400 − 1000 )kPa ⎟ ⎜ (100 − 60 )°C ⎟ ⎝ ⎠ T =80°C ⎝ ⎠ P =1200kPa (1.0056 − 1.0458)kJ/kg ⋅ K ? (0.022442 − 0.018404)m 3 /kg ≅− (1400 − 1000)kPa (100 − 60)°C − 1.005 × 10 − 4 m 3 /kg ⋅ K ≅ −1.0095 × 10 − 4 m 3 /kg ⋅ K since kJ ≡ kPa·m³, and K ≡ °C for temperature differences. Thus the last Maxwell relation is satisfied. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
9.
12-9 12-15 EES Problem
12-14 is reconsidered. The validity of the last Maxwell relation for refrigerant 134a at the specified state is to be verified. Analysis The problem is solved using EES, and the solution is given below. "Input Data:" T=80 [C] P=1200 [kPa] P_increment = 200 [kPa] T_increment = 20 [C] P[2]=P+P_increment P[1]=P-P_increment T[2]=T+T_increment T[1]=T-T_increment DELTAP = P[2]-P[1] DELTAT = T[2]-T[1] v[1]=volume(R134a,T=T[1],P=P) v[2]=volume(R134a,T=T[2],P=P) s[1]=entropy(R134a,T=T,P=P[1]) s[2]=entropy(R134a,T=T,P=P[2]) DELTAs=s[2] - s[1] DELTAv=v[2] - v[1] "The partial derivatives in the last Maxwell relation (Eq. 11-19) is associated with the Gibbs function and are approximated by the ratio of ordinary differentials:" LeftSide =DELTAs/DELTAP*Convert(kJ,m^3-kPa) "[m^3/kg-K]" "at T = Const." RightSide=-DELTAv/DELTAT "[m^3/kg-K]" "at P = Const." SOLUTION DELTAP=400 [kPa] RightSide=-0.000101 [m^3/kg-K] DELTAs=-0.04026 [kJ/kg-K] s[1]=1.046 [kJ/kg-K] DELTAT=40 [C] s[2]=1.006 [kJ/kg-K] DELTAv=0.004038 [m^3/kg] T=80 [C] LeftSide=-0.0001007 [m^3/kg-K] T[1]=60 [C] P=1200 [kPa] T[2]=100 [C] P[1]=1000 [kPa] T_increment=20 [C] P[2]=1400 [kPa] v[1]=0.0184 [m^3/kg] P_increment=200 [kPa] v[2]=0.02244 [m^3/kg] PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
10.
12-10 12-16E The validity
of the last Maxwell relation for steam at a specified state is to be verified. Analysis We do not have exact analytical property relations for steam, and thus we need to replace the differential quantities in the last Maxwell relation with the corresponding finite quantities. Using property values from the tables about the specified state, ⎛ ∂s ⎞ ? ⎛ ∂v ⎞ ⎜ ⎟ =− ⎜ ⎟ ⎝ ∂P ⎠ T ⎝ ∂T ⎠ P ⎛ Δs ⎞ ? ⎛ Δv ⎞ ⎜ ⎟ ≅− ⎜ ⎟ ⎝ ΔP ⎠ T =800°F ⎝ ΔT ⎠ P = 400psia ⎛ s 450 psia − s 350 psia ⎞ ? ⎛ v 900° F − v 700° F ⎞ ⎜ ⎟ ≅ −⎜ ⎟ ⎜ (450 − 350)psia ⎟ ⎜ (900 − 700 )°F ⎟ ⎝ ⎠ T =800°F ⎝ ⎠ P = 400psia (1.6706 − 1.7009)Btu/lbm ⋅ R ? (1.9777 − 1.6507)ft 3 /lbm ≅− (450 − 350)psia (900 − 700)°F − 1.639 × 10 −3 ft 3 /lbm ⋅ R ≅ −1.635 × 10 −3 ft 3 /lbm ⋅ R since 1 Btu ≡ 5.4039 psia·ft3, and R ≡ °F for temperature differences. Thus the fourth Maxwell relation is satisfied. 12-17 Using the Maxwell relations, a relation for (∂s/∂P)T for a gas whose equation of state is P(v-b) = RT is to be obtained. RT Analysis This equation of state can be expressed as v = + b . Then, P ⎛ ∂v ⎞ R ⎜ ⎟ = ⎝ ∂T ⎠ P P From the fourth Maxwell relation, ⎛ ∂s ⎞ ⎛ ∂v ⎞ R ⎜ ⎟ = −⎜ ⎟ =− ⎝ ∂P ⎠ T ⎝ ∂T ⎠ P P PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
11.
12-11 12-18 Using the
Maxwell relations, a relation for (∂s/∂v)T for a gas whose equation of state is (P-a/v2)(v-b) = RT is to be obtained. RT a Analysis This equation of state can be expressed as P = + 2 . Then, v −b v ⎛ ∂P ⎞ R ⎜ ⎟ = ⎝ ∂T ⎠ v v − b From the third Maxwell relation, ⎛ ∂s ⎞ ⎛ ∂P ⎞ R ⎜ ⎟ =⎜ ⎟ = ⎝ ∂v ⎠ T ⎝ ∂T ⎠ v v − b 12-19 Using the Maxwell relations and the ideal-gas equation of state, a relation for (∂s/∂v)T for an ideal gas is to be obtained. RT Analysis The ideal gas equation of state can be expressed as P = . Then, v ⎛ ∂P ⎞ R ⎜ ⎟ = ⎝ ∂T ⎠ v v From the third Maxwell relation, ⎛ ∂s ⎞ ⎛ ∂P ⎞ R ⎜ ⎟ =⎜ ⎟ = ⎝ ∂v ⎠ T ⎝ ∂T ⎠ v v PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
12.
12-12
⎛ ∂P ⎞ k ⎛ ∂P ⎞ 12-20 It is to be proven that ⎜ ⎟ = ⎜ ⎟ ⎝ ∂T ⎠ s k − 1 ⎝ ∂T ⎠ v Analysis Using the definition of cv , ⎛ ∂s ⎞ ⎛ ∂s ⎞ ⎛ ∂P ⎞ cv = T ⎜ ⎟ = T⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ v ⎝ ∂P ⎠ v ⎝ ∂T ⎠ v ⎛ ∂s ⎞ ⎛ ∂v ⎞ Substituting the first Maxwell relation ⎜ ⎟ = −⎜ ⎟ , ⎝ ∂P ⎠ v ⎝ ∂T ⎠ s ⎛ ∂v ⎞ ⎛ ∂P ⎞ cv = −T ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ s ⎝ ∂T ⎠ v Using the definition of cp, ⎛ ∂s ⎞ ⎛ ∂s ⎞ ⎛ ∂v ⎞ c p = T⎜ ⎟ = T⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂v ⎠ P ⎝ ∂T ⎠ P ⎛ ∂s ⎞ ⎛ ∂P ⎞ Substituting the second Maxwell relation ⎜ ⎟ =⎜ ⎟ , ⎝ ∂v ⎠ P ⎝ ∂T ⎠ s ⎛ ∂P ⎞ ⎛ ∂v ⎞ cp = T⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ s ⎝ ∂T ⎠ P From Eq. 12-46, 2 ⎛ ∂v ⎞ ⎛ ∂P ⎞ c p − cv = −T ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T Also, k cp = k −1 c p − cv Then, ⎛ ∂P ⎞ ⎛ ∂v ⎞ ⎜ ⎟ ⎜ ⎟ k ⎝ ∂T ⎠ s ⎝ ∂T ⎠ P ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎛ ∂v ⎞ =− = −⎜ ⎟ ⎜ ⎟ ⎜ ⎟ k −1 2 ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎝ ∂T ⎠ s ⎝ ∂v ⎠ P ⎝ ∂P ⎠ T ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T Substituting this into the original equation in the problem statement produces ⎛ ∂P ⎞ ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎜ ⎟ = −⎜ ⎟ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ s ⎝ ∂T ⎠ s ⎝ ∂v ⎠ P ⎝ ∂P ⎠ T ⎝ ∂T ⎠ v But, according to the cyclic relation, the last three terms are equal to −1. Then, ⎛ ∂P ⎞ ⎛ ∂P ⎞ ⎜ ⎟ =⎜ ⎟ ⎝ ∂T ⎠ s ⎝ ∂T ⎠ s PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
13.
12-13 12-21 It is
to be shown how T, v, u, a, and g could be evaluated from the thermodynamic function h = h(s, P). Analysis Forming the differential of the given expression for h produces ⎛ ∂h ⎞ ⎛ ∂h ⎞ dh = ⎜ ⎟ ds + ⎜ ⎟ dP ⎝ ∂s ⎠ P ⎝ ∂P ⎠ s Solving the dh Gibbs equation gives dh = Tds + vdP Comparing the coefficient of these two expressions ⎛ ∂h ⎞ T =⎜ ⎟ ⎝ ∂s ⎠ P ⎛ ∂h ⎞ v =⎜ ⎟ ⎝ ∂P ⎠ s both of which can be evaluated for a given P and s. From the definition of the enthalpy, ⎛ ∂h ⎞ u = h − Pv = h-P⎜ ⎟ ⎝ ∂P ⎠ s Similarly, the definition of the Helmholtz function, ⎛ ∂h ⎞ ⎛ ∂h ⎞ a = u − Ts = h − P⎜ ⎟ − s⎜ ⎟ ⎝ ∂P ⎠ s ⎝ ∂s ⎠ P while the definition of the Gibbs function gives ⎛ ∂h ⎞ q = h − Ts = h − s⎜ ⎟ ⎝ ∂s ⎠ P All of these can be evaluated for a given P and s and the fundamental h(s,P) equation. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
14.
12-14 The Clapeyron Equation 12-22C
It enables us to determine the enthalpy of vaporization from hfg at a given temperature from the P, v, T data alone. 12-23C It is assumed that vfg ≅ vg ≅ RT/P, and hfg ≅ constant for small temperature intervals. 12-24 Using the Clapeyron equation, the enthalpy of vaporization of steam at a specified pressure is to be estimated and to be compared to the tabulated data. Analysis From the Clapeyron equation, ⎛ dP ⎞ h fg = Tv fg ⎜ ⎟ ⎝ dT ⎠ sat ⎛ ΔP ⎞ ≅ T (v g − v f ) @300 kPa ⎜ ⎟ ⎝ ΔT ⎠ sat, 300 kPa ⎛ (325 − 275)kPa ⎞ = Tsat @300 kPa (v g − v f ) @300 kPa ⎜ ⎟ ⎜ Tsat @325 kPa − Tsat @275 kPa ⎟ ⎝ ⎠ 3 ⎛ 50 kPa ⎞ = (133.52 + 273.15 K)(0.60582 − 0.001073 m /kg)⎜ ⎜ (136.27 − 130.58)°C ⎟ ⎟ ⎝ ⎠ = 2159.9 kJ/kg The tabulated value of hfg at 300 kPa is 2163.5 kJ/kg. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
15.
12-15 12-25 The hfg
and sfg of steam at a specified temperature are to be calculated using the Clapeyron equation and to be compared to the tabulated data. Analysis From the Clapeyron equation, ⎛ dP ⎞ h fg = Tv fg ⎜ ⎟ ⎝ dT ⎠ sat ⎛ ΔP ⎞ ≅ T (v g − v f ) @120°C ⎜ ⎟ ⎝ ΔT ⎠ sat,120°C ⎛ Psat @125°C − Psat @115°C ⎞ = T (v g − v f ) @120°C ⎜ ⎜ ⎟ ⎟ ⎝ 125°C − 115°C ⎠ ⎛ (232.23 − 169.18)kPa ⎞ = (120 + 273.15 K)(0.89133 − 0.001060 m 3 /kg)⎜ ⎜ ⎟ ⎟ ⎝ 10 K ⎠ = 2206.8 kJ/kg Also, h fg 2206.8 kJ/kg s fg = = = 5.6131 kJ/kg ⋅ K T (120 + 273.15) K The tabulated values at 120°C are hfg = 2202.1 kJ/kg and sfg = 5.6013 kJ/kg·K. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
16.
12-16 12-26E [Also solved
by EES on enclosed CD] The hfg of refrigerant-134a at a specified temperature is to be calculated using the Clapeyron equation and Clapeyron-Clausius equation and to be compared to the tabulated data. Analysis (a) From the Clapeyron equation, ⎛ dP ⎞ h fg = Tv fg ⎜ ⎟ ⎝ dT ⎠ sat ⎛ ΔP ⎞ ≅ T (v g − v f ) @ 50°F ⎜ ⎟ ⎝ ΔT ⎠ sat, 50° F ⎛ Psat @ 60 ° F − Psat @ 40 °F ⎞ = T (v g − v f ) @ 50°F ⎜ ⎜ ⎟ ⎟ ⎝ 60°F − 40°F ⎠ ⎛ (72.152 − 49.776) psia ⎞ = (50 + 459.67 R)(0.79136 − 0.01270 ft 3 /lbm)⎜ ⎜ ⎟ ⎟ ⎝ 20 R ⎠ = 444.0 psia ⋅ ft 3 /lbm = 82.16 Btu/lbm (0.2% error) since 1 Btu = 5.4039 psia·ft3. (b) From the Clapeyron-Clausius equation, ⎛P ⎞ h fg ⎛ 1 1 ⎞ ln⎜ 2 ⎜P ⎟ ≅ ⎟ ⎜ − ⎟ ⎜T T ⎟ ⎝ 1 ⎠ sat R ⎝ 1 2 ⎠ sat ⎛ 72.152 psia ⎞ h fg ⎛ 1 1 ⎞ ⎜ 49.776 psia ⎟ ≅ 0.01946 Btu/lbm ⋅ R ⎜ 40 + 459.67 R − 60 + 459.67 R ⎟ ln⎜ ⎟ ⎝ ⎠ ⎝ ⎠ h fg = 93.80 Btu/lbm (14.4% error) The tabulated value of hfg at 50°F is 82.00 Btu/lbm. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
17.
12-17 12-27 EES The
enthalpy of vaporization of steam as a function of temperature using Clapeyron equation and steam data in EES is to be plotted. Analysis The enthalpy of vaporization is determined using Clapeyron equation from ΔP h fg ,Clapeyron = Tv fg ΔT At 100ºC, for an increment of 5ºC, we obtain T1 = T − Tincrement = 100 − 5 = 95°C T2 = T + Tincrement = 100 + 5 = 105°C P1 = Psat @ 95°C = 84.61 kPa P2 = Psat @ 105°C = 120.90 kPa ΔT = T2 − T1 = 105 − 95 = 10°C ΔP = P2 − P1 = 120.90 − 84.61 = 36.29 kPa v f @ 100°C = 0.001043 m 3 /kg v g @ 100°C = 1.6720 m 3 /kg v fg = v g − v f = 1.6720 − 0.001043 = 1.6710 m 3 /kg Substituting, ΔP 36.29 kPa h fg ,Clapeyron = Tv fg = (100 + 273.15 K)(1.6710 m 3 /kg) = 2262.8 kJ/kg ΔT 10 K The enthalpy of vaporization from steam table is h fg @ 100°C = 2256.4 m 3 /kg The percent error in using Clapeyron equation is 2262.8 − 2256.4 PercentError = × 100 = 0.28% 2256.4 We repeat the analysis over the temperature range 10 to 200ºC using EES. Below, the copy of EES solution is provided: "Input Data:" "T=100" "[C]" T_increment = 5"[C]" T[2]=T+T_increment"[C]" T[1]=T-T_increment"[C]" P[1] = pressure(Steam_iapws,T=T[1],x=0)"[kPa]" P[2] = pressure(Steam_iapws,T=T[2],x=0)"[kPa]" DELTAP = P[2]-P[1]"[kPa]" DELTAT = T[2]-T[1]"[C]" v_f=volume(Steam_iapws,T=T,x=0)"[m^3/kg]" v_g=volume(Steam_iapws,T=T,x=1)"[m^3/kg]" h_f=enthalpy(Steam_iapws,T=T,x=0)"[kJ/kg]" h_g=enthalpy(Steam_iapws,T=T,x=1)"[kJ/kg]" h_fg=h_g - h_f"[kJ/kg-K]" v_fg=v_g - v_f"[m^3/kg]" PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
18.
12-18 "The Clapeyron equation
(Eq. 11-22) provides a means to calculate the enthalpy of vaporization, h_fg at a given temperature by determining the slope of the saturation curve on a P-T diagram and the specific volume of the saturated liquid and satruated vapor at the temperature." h_fg_Clapeyron=(T+273.15)*v_fg*DELTAP/DELTAT*Convert(m^3-kPa,kJ)"[kJ/kg]" PercentError=ABS(h_fg_Clapeyron-h_fg)/h_fg*100"[%]" hfg hfg,Clapeyron PercentError T [kJ/kg] [kJ/kg] [%] [C] 2477.20 2508.09 1.247 10 2429.82 2451.09 0.8756 30 2381.95 2396.69 0.6188 50 2333.04 2343.47 0.4469 70 2282.51 2290.07 0.3311 90 2229.68 2235.25 0.25 110 2173.73 2177.86 0.1903 130 2113.77 2116.84 0.1454 150 2014.17 2016.15 0.09829 180 1899.67 1900.98 0.06915 210 1765.50 1766.38 0.05015 240 2600 2500 hfg calculated by Clapeyron equation 2400 hfg [kJ/kg] 2300 hfg calculated by EES 2200 2100 2000 1900 1800 1700 0 50 100 150 200 250 T [C] PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
19.
12-19 12-28 A substance
is heated in a piston-cylinder device until it turns from saturated liquid to saturated vapor at a constant pressure and temperature. The boiling temperature of this substance at a different pressure is to be estimated. Analysis From the Clapeyron equation, ⎛ dP ⎞ h fg (5 kPa ⋅ m 3 )/(0.002 kg) ⎜ ⎟ = = = 14.16 kPa/K Weight ⎝ dT ⎠ sat Tv fg (353 K)(1× 10 −3 m 3 )/(0.002 kg) Using the finite difference approximation, ⎛ dP ⎞ ⎛ P − P1 ⎞ 200 kPa ⎜ ⎟ ≈⎜ 2⎜ ⎟ ⎟ 80°C Q ⎝ dT ⎠ sat ⎝ T2 − T1 ⎠ sat 2 grams Solving for T2, Sat. liquid P2 − P1 (180 − 200)kPa T2 = T1 + = 353 K + = 351.6 K dP / dT 14.16 kPa/K 12-29 A substance is heated in a piston-cylinder device until it turns from saturated liquid to saturated vapor at a constant pressure and temperature. The saturation pressure of this substance at a different temperature is to be estimated. Analysis From the Clapeyron equation, Weight 3 ⎛ dP ⎞ h fg (5 kPa ⋅ m )/(0.002 kg) ⎜ ⎟ = = = 14.16 kPa/K ⎝ dT ⎠ sat Tv fg (353 K)(1× 10 −3 m 3 )/(0.002 kg) 200 kPa Using the finite difference approximation, 80°C Q 2 grams ⎛ dP ⎞ ⎛ P − P1 ⎞ Sat. liquid ⎜ ⎟ ≈⎜ 2 ⎟ ⎝ dT ⎠ sat ⎜ T2 − T1 ⎟ sat ⎝ ⎠ Solving for P2, dP P2 = P1 + (T2 − T1 ) = 200 kPa + (14.16 kPa/K )(373 − 353)K = 483.2 kPa dT PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
20.
12-20 12-30 A substance
is heated in a piston-cylinder device until it turns from saturated liquid to saturated vapor at a constant pressure and temperature. The sfg of this substance at a different temperature is to be estimated. Analysis From the Clapeyron equation, Weight ⎛ dP ⎞ h fg s fg ⎜ ⎟ = = ⎝ dT ⎠ sat Tv fg v fg 200 kPa Solving for sfg, 80°C Q h fg (5 kJ)/(0.002 kg) 2 grams s fg = = = 7.082 kJ/kg ⋅ K Sat. liquid T 353 K Alternatively, ⎛ dP ⎞ 1× 10 -3 m 3 s fg = ⎜ ⎟ v fg = (14.16 kPa/K ) = 7.08 kPa ⋅ m 3 /kg ⋅ K = 7.08 kJ/kg ⋅ K ⎝ dT ⎠ sat 0.002 kg ⎛ ∂ (h fg / T ) ⎞ 12-31 It is to be shown that c p , g − c p , f = T ⎜ ⎟ + v fg ⎛ ∂P ⎞ . ⎜ ⎟ ⎜ ∂T ⎟ ⎝ ∂T ⎠ sat ⎝ ⎠P Analysis The definition of specific heat and Clapeyron equation are ⎛ ∂h ⎞ cp = ⎜ ⎟ ⎝ ∂T ⎠ P ⎛ dP ⎞ h fg ⎜ ⎟ = ⎝ dT ⎠ sat Tv fg According to the definition of the enthalpy of vaporization, h fg hg hf = − T T T Differentiating this expression gives ⎛ ∂h fg / T ⎞ ⎛ ∂h / T ⎞ ⎛ ∂h / T ⎞ ⎜ ⎟ =⎜ g ⎟ −⎜ f ⎟ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂T ⎠ P ⎝ ∂T ⎠P 1 ⎛ ∂h g ⎞ ⎛ ∂h ⎞ ⎟ − g −1⎜ f h h = ⎜ ⎟ + f T ⎜ ∂T ⎟ 2 T ⎜ ∂T ⎟ 2 ⎝⎠P T ⎝ ⎠P T c p, g c p, f h g − h f = − − T T T2 Using Clasius-Clapeyron to replace the last term of this expression and solving for the specific heat difference gives ⎛ ∂ (h fg / T ) ⎞ c p, g − c p, f = T ⎜ ⎟ + v fg ⎛ ∂P ⎞ ⎜ ⎟ ⎜ ∂T ⎟ ⎝ ∂T ⎠ sat ⎝ ⎠P PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
21.
12-21 12-32E A table
of properties for methyl chloride is given. The saturation pressure is to be estimated at two different temperatures. Analysis The Clapeyron equation is ⎛ dP ⎞ h fg ⎜ ⎟ = ⎝ dT ⎠ sat Tv fg Using the finite difference approximation, ⎛ dP ⎞ ⎛ P2 − P1 ⎞ h fg ⎜ ⎟ ≈⎜ ⎟ ⎜ T − T ⎟ = Tv ⎝ dT ⎠ sat ⎝ 2 1 ⎠ sat fg Solving this for the second pressure gives for T2 = 110°F h fg P2 = P1 + (T2 − T1 ) Tv fg 154.85 Btu/lbm ⎛ 5.404 psia ⋅ ft 3 ⎞ = 116.7 psia + ⎜ ⎟(110 − 100)R (560 R)(0.86332 ft 3 /lbm) ⎜ ⎝ 1 Btu ⎟ ⎠ = 134.0 psia When T2 = 90°F h fg P2 = P1 + (T2 − T1 ) Tv fg 154.85 Btu/lbm ⎛ 5.404 psia ⋅ ft 3 ⎞ = 116.7 psia + ⎜ ⎟(90 − 100)R (560 R)(0.86332 ft 3 /lbm) ⎜ ⎝ 1 Btu ⎟ ⎠ = 99.4 psia PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
22.
12-22 12-33 Saturation properties
for R-134a at a specified temperature are given. The saturation pressure is to be estimated at two different temperatures. Analysis From the Clapeyron equation, ⎛ dP ⎞ h fg 225.86 kPa ⋅ m 3 /kg ⎜ ⎟ = = = 2.692 kPa/K ⎝ dT ⎠ sat Tv fg (233 K)(0.36010 m 3 /kg) Using the finite difference approximation, ⎛ dP ⎞ ⎛ P − P1 ⎞ ⎜ ⎟ ≈⎜ 2⎜ ⎟ ⎟ ⎝ dT ⎠ sat ⎝ T2 − T1 ⎠ sat Solving for P2 at −50°C dP P2 = P1 + (T2 − T1 ) = 51.25 kPa + (2.692 kPa/K )(223 − 233)K = 24.33 kPa dT Solving for P2 at −30°C dP P2 = P1 + (T2 − T1 ) = 51.25 kPa + (2.692 kPa/K )(243 − 233)K = 78.17 kPa dT PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
23.
12-23 General Relations for
du, dh, ds, cv, and cp 12-34C Yes, through the relation ⎛ ∂c p ⎞ ⎛ 2 ⎞ ⎜ ⎟ = −T ⎜ ∂ v ⎟ ⎜ ∂P ⎟ ⎜ ∂T 2 ⎟ ⎝ ⎠T ⎝ ⎠P PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
24.
12-24 12-35 General expressions
for Δu, Δh, and Δs for a gas whose equation of state is P(v-a) = RT for an isothermal process are to be derived. Analysis (a) A relation for Δu is obtained from the general relation T2 v2 ⎛ ⎛ ∂P ⎞ ⎞ Δu = u 2 − u1 = ∫ T1 cv dT + ∫v 1 ⎜T ⎜ ⎟ ⎜ ⎝ ∂T ⎟ − P ⎟dv ⎝ ⎠v ⎠ The equation of state for the specified gas can be expressed as RT ⎛ ∂P ⎞ R P= ⎯⎯→ ⎜ ⎟ = v −a ⎝ ∂T ⎠v v − a Thus, ⎛ ∂P ⎞ RT T⎜ ⎟ −P = −P = P−P = 0 ⎝ ∂T ⎠v v −a T2 Substituting, Δu = ∫T1 cv dT (b) A relation for Δh is obtained from the general relation ⎛ ∂v ⎞ ⎞ ⎜v − T ⎛ T2 P2 Δh = h2 − h1 = ∫ T1 c P dT + ∫ P1 ⎜ ⎝ ⎜ ⎟ ⎟dP ⎝ ∂T ⎠ P ⎟ ⎠ The equation of state for the specified gas can be expressed as RT ⎛ ∂v ⎞ R v= +a ⎯ ⎯→ ⎜ ⎟ = P ⎝ ∂T ⎠ P P Thus, ⎛ ∂v ⎞ R v −T⎜ ⎟ = v − T = v − (v − a ) = a ⎝ ∂T ⎠ P P Substituting, c p dT + a(P2 − P1 ) T2 P2 T2 Δh = ∫T1 c p dT + ∫ P1 a dP = ∫T1 (c) A relation for Δs is obtained from the general relation T2 cp P2 ⎛ ∂v ⎞ Δs = s 2 − s1 = ∫ T1 T dT − ∫P1 ⎜ ⎟ dP ⎝ ∂T ⎠ P Substituting (∂v/∂T)P = R/T, T2 cp P2 ⎛R⎞ T2 cp P2 Δs = ∫ T1 T dT − ∫P1 ⎜ ⎟ dP = ⎝ P ⎠P ∫T1 T dT − R ln P1 For an isothermal process dT = 0 and these relations reduce to P2 Δu = 0, Δh = a(P2 − P1 ), and Δs = − Rln P1 PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
25.
12-25 12-36 General expressions
for (∂u/∂P)T and (∂h/∂v)T in terms of P, v, and T only are to be derived. Analysis The general relation for du is ⎛ ⎛ ∂P ⎞ ⎞ du = cv dT + ⎜ T ⎜ ⎟ ⎜ ⎝ ∂T ⎟ − P ⎟dv ⎝ ⎠v ⎠ Differentiating each term in this equation with respect to P at T = constant yields ⎛ ∂u ⎞ ⎛ ⎛ ∂P ⎞ ⎞⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂v ⎞ ⎛ ∂v ⎞ ⎜ ⎟ = 0 + ⎜T ⎜ ⎟ ⎜ ⎝ ∂T ⎠ − P ⎟⎜ ∂P ⎟ = T ⎜ ∂T ⎟ ⎜ ∂P ⎟ − P⎜ ∂P ⎟ ⎟ ⎝ ∂P ⎠ T ⎝ v ⎠⎝ ⎠T ⎝ ⎠v ⎝ ⎠T ⎝ ⎠T Using the properties P, T, v, the cyclic relation can be expressed as ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂v ⎞ ⎛ ∂v ⎞ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ = −1 ⎯ ⎯→ ⎜ ⎟ ⎜ ⎟ = −⎜ ⎟ ⎝ ∂T ⎠v ⎝ ∂v ⎠ P ⎝ ∂P ⎠ T ⎝ ∂T ⎠ v ⎝ ∂P ⎠ T ⎝ ∂T ⎠ P Substituting, we get ⎛ ∂u ⎞ ⎛ ∂v ⎞ ⎛ ∂v ⎞ ⎜ ⎟ = −T ⎜ ⎟ − P⎜ ⎟ ⎝ ∂P ⎠ T ⎝ ∂T ⎠ P ⎝ ∂P ⎠ T The general relation for dh is ⎛ ⎛ ∂v ⎞ ⎞ dh = c p dT + ⎜v − T ⎜ ⎜ ⎟ ⎟dP ⎝ ⎝ ∂T ⎠ P ⎟ ⎠ Differentiating each term in this equation with respect to v at T = constant yields ⎛ ∂h ⎞ ⎛ ⎛ ∂v ⎞ ⎞⎛ ∂P ⎞ ⎛ ∂P ⎞ ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎜ ⎟ = 0 + ⎜v − T ⎜ ⎜ ⎟ ⎟⎜⎟⎝ ∂v ⎟ = v ⎜ ∂v ⎟ − T ⎜ ∂T ⎟ ⎜ ∂v ⎟ ⎝ ∂v ⎠ T ⎝ ⎝ ∂T ⎠ P ⎠ ⎠T ⎝ ⎠T ⎝ ⎠P ⎝ ⎠T Using the properties v, T, P, the cyclic relation can be expressed as ⎛ ∂v ⎞ ⎛ ∂T ⎞ ⎛ ∂P ⎞ ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ = −1 ⎯ ⎯→ ⎜ ⎟ ⎜ ⎟ = −⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂P ⎠ v ⎝ ∂v ⎠ T ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T ⎝ ∂P ⎠ v Substituting, we get ⎛ ∂h ⎞ ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎜ ⎟ =v⎜ ⎟ +T⎜ ⎟ ⎝ ∂v ⎠ T ⎝ ∂v ⎠ T ⎝ ∂P ⎠ v PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
26.
12-26 12-37E The specific
heat difference cp-cv for liquid water at 1000 psia and 150°F is to be estimated. Analysis The specific heat difference cp - cv is given as 2 ⎛ ∂v ⎞ ⎛ ∂P ⎞ c p − cv = −T ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T Approximating differentials by differences about the specified state, 2 ⎛ Δv ⎞ ⎛ ΔP ⎞ c p − cv ≅ −T ⎜ ⎟ ⎜ ⎟ ⎝ ΔT ⎠ P =1000 psia ⎝ Δv ⎠ T =150°F 2 ⎛ v 175° F − v 125° F ⎞ ⎛ (1500 − 500)psia ⎞ = −(150 + 459.67 R )⎜ ⎟ ⎜ ⎟ ⎜ (175 − 125)°F ⎟ ⎜ ⎟ ⎝ ⎠ P =1000psia ⎝ v 1500 psia − v 500 psia ⎠ T =150° F 2 ⎛ (0.016427 − 0.016177)ft 3 /lbm ⎞ ⎛ 1000 psia ⎞ = −(609.67 R)⎜ ⎟ ⎜ ⎟ ⎜ 50 R ⎟ ⎜ (0.016267 − 0.016317)ft 3 /lbm ⎟ ⎝ ⎠ ⎝ ⎠ = 0.3081 psia ⋅ ft 3 /lbm ⋅ R = 0.0570 Btu/lbm ⋅ R (1 Btu = 5.4039 psia ⋅ ft 3 ) 12-38 The volume expansivity β and the isothermal compressibility α of refrigerant-134a at 200 kPa and 30°C are to be estimated. Analysis The volume expansivity and isothermal compressibility are expressed as 1 ⎛ ∂v ⎞ 1 ⎛ ∂v ⎞ β= ⎜ ⎟ and α = − ⎜ ⎟ v ⎝ ∂T ⎠ P v ⎝ ∂P ⎠ T Approximating differentials by differences about the specified state, 1 ⎛ Δv ⎞ 1 ⎛ v 40°C − v 20°C ⎞ β≅ ⎜ ⎟ = ⎜ ⎟ v ⎝ ΔT ⎠ P = 200kPa v ⎜ (40 − 20)°C ⎝ ⎟ ⎠ P = 200 kPa 1 ⎛ (0.12322 − 0.11418) m 3 /kg ⎞ = ⎜ ⎟ 0.11874 m 3 /kg ⎜ ⎝ 20 K ⎟ ⎠ = 0.00381 K −1 and 1 ⎛ Δv ⎞ 1 ⎛ v 240 kPa − v 180 kPa ⎞ α ≅− ⎜ ⎟ =− ⎜ ⎟ v ⎝ ΔP ⎠ T =30°C v ⎜ (240 − 180)kPa ⎝ ⎟ ⎠ T =30°C 1 ⎛ (0.09812 − 0.13248)m 3 /kg ⎞ =− ⎜ ⎟ 0.11874 m /kg ⎜ 3 ⎝ 60 kPa ⎟ ⎠ = 0.00482 kPa −1 PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
27.
12-27
⎛ ∂P ⎞ ⎛ ∂v ⎞ 12-39 It is to be shown that c p − cv = T ⎜ ⎟ ⎜ ⎟ . ⎝ ∂T ⎠ v ⎝ ∂T ⎠ P Analysis We begin by taking the entropy to be a function of specific volume and temperature. The differential of the entropy is then ⎛ ∂s ⎞ ⎛ ∂s ⎞ ds = ⎜ ⎟ dT + ⎜ ⎟ dv ⎝ ∂T ⎠ v ⎝ ∂v ⎠ T ⎛ ∂s ⎞ c Substituting ⎜ ⎟ = v from Eq. 12-28 and the third Maxwell equation changes this to ⎝ ∂T ⎠ v T cv ⎛ ∂P ⎞ ds = dT + ⎜ ⎟ dv T ⎝ ∂T ⎠v Taking the entropy to be a function of pressure and temperature, ⎛ ∂s ⎞ ⎛ ∂s ⎞ ds = ⎜ ⎟ dT + ⎜ ⎟ dP ⎝ ∂T ⎠ P ⎝ ∂P ⎠ T ⎛ ∂s ⎞ cp Combining this result with ⎜ ⎟ = from Eq. 12-34 and the fourth Maxwell equation produces ⎝ ∂T ⎠ P T cp ⎛ ∂v ⎞ ds = dT − ⎜ ⎟ dP T ⎝ ∂T ⎠ P Equating the two previous ds expressions and solving the result for the specific heat difference, ⎛ ∂v ⎞ ⎛ ∂P ⎞ (c p − cv )dT = T ⎜ ⎟ dP + ⎜ ⎟ dv ⎝ ∂T ⎠ P ⎝ ∂T ⎠ v Taking the pressure to be a function of temperature and volume, ⎛ ∂P ⎞ ⎛ ∂P ⎞ dP = ⎜ ⎟ dT + ⎜ ⎟ dv ⎝ ∂T ⎠ v ⎝ ∂v ⎠ T When this is substituted into the previous expression, the result is ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎡⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂P ⎞ ⎤ (c p − cv )dT = T ⎜ ⎟ ⎜ ⎟ dT + T ⎢⎜ ⎟ ⎜ ⎟ ⎜ ⎟ ⎥ dv ⎝ ∂T ⎠ P ⎝ ∂T ⎠ v ⎣⎝ ∂T ⎠ P ⎝ ∂v ⎠ T ⎝ ∂T ⎠ v ⎦ According to the cyclic relation, the term in the bracket is zero. Then, canceling the common dT term, ⎛ ∂P ⎞ ⎛ ∂v ⎞ c p − cv = T ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ v ⎝ ∂T ⎠ P PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
28.
12-28 12-40 It is
to be proven that the definition for temperature T = (∂u / ∂s ) v reduces the net entropy change of two constant-volume systems filled with simple compressible substances to zero as the two systems approach thermal equilibrium. Analysis The two constant-volume systems form an isolated system shown here For the isolated system dS tot = dS A + dS B ≥ 0 Assume S = S (u , v ) VA =const. Isolated TA system Then, boundary ⎛ ∂s ⎞ ⎛ ∂s ⎞ ds = ⎜ ⎟ du + ⎜ ⎟ dv VB =const. ⎝ ∂u ⎠ v ⎝ ∂v ⎠ u TB Since v = const. and dv = 0 , ⎛ ∂s ⎞ ds = ⎜ ⎟ du ⎝ ∂u ⎠ v and from the definition of temperature from the problem statement, du du = (∂u / ∂s ) v T Then, du A du B dS tot = m A + mB TA TB The first law applied to the isolated system yields E in − E out = dU 0 = dU ⎯ ⎯→ m A du A + m B du B = 0 ⎯ ⎯→ m B du B = −m A du A Now, the entropy change may be expressed as ⎛ 1 1 ⎞ ⎛ T − TA ⎞ dS tot = m A du A ⎜ ⎜T − T ⎟ = m A du A ⎜ B ⎟ ⎜ T T ⎟ ⎟ ⎝ A B ⎠ ⎝ A B ⎠ As the two systems approach thermal equilibrium, lim dS tot = 0 T A → TB PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
29.
12-29 12-41 The internal
energy change of air between two specified states is to be compared for two equations of states. Assumptions Constant specific heats for air can be used. Properties For air at the average temperature (20+300)/2=160°C=433 K, cv = 0.731 kJ/kg⋅K (Table A-2b). Analysis Solving the equation of state for P gives RT P= v −a Then, ⎛ ∂P ⎞ R ⎜ ⎟ = ⎝ ∂T ⎠v v − a Using equation 12-29, ⎡ ⎛ ∂P ⎞ ⎤ du = cv dT + ⎢T ⎜ ⎟ − P ⎥ dv ⎣ ⎝ ∂T ⎠v ⎦ Substituting, ⎛ RT RT ⎞ du = cv dT + ⎜ − ⎟dv ⎝ v −a v −a⎠ = cv dT Integrating this result between the two states with constant specific heats gives u 2 − u1 = cv (T2 − T1 ) = (0.731 kJ/kg ⋅ K)(300 − 20)K = 205 kJ/kg The ideal gas model for the air gives du = cv dT which gives the same answer. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
30.
12-30 12-42 The enthalpy
change of air between two specified states is to be compared for two equations of states. Assumptions Constant specific heats for air can be used. Properties For air at the average temperature (20+300)/2=160°C=433 K, cp = 1.018 kJ/kg⋅K (Table A-2b). Analysis Solving the equation of state for v gives RT v= +a P Then, ⎛ ∂v ⎞ R ⎜ ⎟ = ⎝ ∂T ⎠ P P Using equation 12-35, ⎡ ⎛ ∂v ⎞ ⎤ dh = c p dT + ⎢v − T ⎜ ⎟ ⎥ dP ⎣ ⎝ ∂T ⎠ P ⎦ Substituting, ⎛ RT RT ⎞ dh = c p dT + ⎜ +a− ⎟dP ⎝ P P ⎠ = c p dT + adP Integrating this result between the two states with constant specific heats gives h2 − h1 = c p (T2 − T1 ) + a ( P2 − P1 ) = (1.018 kJ/kg ⋅ K)(300 − 20)K + (0.10 m 3 /kg)(600 − 100)kPa = 335.0 kJ/kg For an ideal gas, dh = c p dT which when integrated gives h2 − h1 = c p (T2 − T1 ) = (1.018 kJ/kg ⋅ K)(300 − 20)K = 285.0 kJ/kg PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
31.
12-31 12-43 The entropy
change of air between two specified states is to be compared for two equations of states. Assumptions Constant specific heats for air can be used. Properties For air at the average temperature (20+300)/2=160°C=433 K, cp = 1.018 kJ/kg⋅K (Table A-2b) and R = 0.287 kJ/kg⋅K (Table A-1). Analysis Solving the equation of state for v gives RT v= +a P Then, ⎛ ∂v ⎞ R ⎜ ⎟ = ⎝ ∂T ⎠ P P The entropy differential is dT ⎛ ∂v ⎞ ds = c p −⎜ ⎟ dP T ⎝ ∂T ⎠ P dT dP = cp −R T P which is the same as that of an ideal gas. Integrating this result between the two states with constant specific heats gives T2 P s 2 − s1 = c p ln − R ln 2 T1 P1 573 K 600 kPa = (1.018 kJ/kg ⋅ K)ln − (0.287 kJ/kg ⋅ K)ln 293 K 100 kPa = 0.1686 kJ/kg ⋅ K PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
32.
12-32 12-44 The internal
energy change of helium between two specified states is to be compared for two equations of states. Properties For helium, cv = 3.1156 kJ/kg⋅K (Table A-2a). Analysis Solving the equation of state for P gives RT P= v −a Then, ⎛ ∂P ⎞ R ⎜ ⎟ = ⎝ ∂T ⎠v v − a Using equation 12-29, ⎡ ⎛ ∂P ⎞ ⎤ du = cv dT + ⎢T ⎜ ⎟ − P ⎥ dv ⎣ ⎝ ∂T ⎠v ⎦ Substituting, ⎛ RT RT ⎞ du = cv dT + ⎜ − ⎟dv ⎝v − a v − a ⎠ = cv dT Integrating this result between the two states gives u 2 − u1 = cv (T2 − T1 ) = (3.1156 kJ/kg ⋅ K)(300 − 20)K = 872.4 kJ/kg The ideal gas model for the helium gives du = cv dT which gives the same answer. PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
33.
12-33 12-45 The enthalpy
change of helium between two specified states is to be compared for two equations of states. Properties For helium, cp = 5.1926 kJ/kg⋅K (Table A-2a). Analysis Solving the equation of state for v gives RT v= +a P Then, ⎛ ∂v ⎞ R ⎜ ⎟ = ⎝ ∂T ⎠ P P Using equation 12-35, ⎡ ⎛ ∂v ⎞ ⎤ dh = c p dT + ⎢v − T ⎜ ⎟ ⎥ dP ⎣ ⎝ ∂T ⎠ P ⎦ Substituting, ⎛ RT RT ⎞ dh = c p dT + ⎜ +a− ⎟dP ⎝ P P ⎠ = c p dT + adP Integrating this result between the two states gives h2 − h1 = c p (T2 − T1 ) + a ( P2 − P1 ) = (5.1926 kJ/kg ⋅ K)(300 − 20)K + (0.10 m 3 /kg)(600 − 100)kPa = 1504 kJ/kg For an ideal gas, dh = c p dT which when integrated gives h2 − h1 = c p (T2 − T1 ) = (5.1926 kJ/kg ⋅ K)(300 − 20)K = 1454 kJ/kg PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
34.
12-34 12-46 The entropy
change of helium between two specified states is to be compared for two equations of states. Properties For helium, cp = 5.1926 kJ/kg⋅K and R = 2.0769 kJ/kg⋅K (Table A-2a). Analysis Solving the equation of state for v gives RT v= +a P Then, ⎛ ∂v ⎞ R ⎜ ⎟ = ⎝ ∂T ⎠ P P The entropy differential is dT ⎛ ∂v ⎞ ds = c p −⎜ ⎟ dP T ⎝ ∂T ⎠ P dT dP = cp −R T P which is the same as that of an ideal gas. Integrating this result between the two states gives T2 P s 2 − s1 = c p ln − R ln 2 T1 P1 573 K 600 kPa = (5.1926 kJ/kg ⋅ K)ln − (2.0769 kJ/kg ⋅ K)ln 293 K 100 kPa = −0.2386 kJ/kg ⋅ K 12-47 An expression for the volume expansivity of a substance whose equation of state is P (v − a) = RT is to be derived. Analysis Solving the equation of state for v gives RT v= +a P The specific volume derivative is then ⎛ ∂v ⎞ R ⎜ ⎟ = ⎝ ∂T ⎠ P P The definition for volume expansivity is 1 ⎛ ∂v ⎞ β= ⎜ ⎟ v ⎝ ∂T ⎠ P Combining these two equations gives R β= RT + aP PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
35.
12-35
v ⎛ T T T ⎞ 12-48 The Helmholtz function of a substance has the form a = − RT ln − cT0 ⎜1 − ⎟ ⎜ T + T ln T ⎟ . It is to v0 ⎝ 0 0 0 ⎠ be shown how to obtain P, h, s, cv, and cp from this expression. Analysis Taking the Helmholtz function to be a function of temperature and specific volume yields ⎛ ∂a ⎞ ⎛ ∂a ⎞ da = ⎜ ⎟ dT + ⎜ ⎟ dv ⎝ ∂T ⎠ v ⎝ ∂v ⎠ T while the applicable Helmholtz equation is da = − Pdv − sdT Equating the coefficients of the two results produces ⎛ ∂a ⎞ P = −⎜ ⎟ ⎝ ∂v ⎠ T ⎛ ∂a ⎞ s = −⎜ ⎟ ⎝ ∂T ⎠ v Taking the indicated partial derivatives of the Helmholtz function given in the problem statement reduces these expressions to RT P= v v T s = R ln + c ln v0 T0 The definition of the enthalpy (h = u + Pv) and Helmholtz function (a = u−Ts) may be combined to give h = u + Pv = a + Ts + Pv ⎛ ∂a ⎞ ⎛ ∂a ⎞ = a −T⎜ ⎟ −v ⎜ ⎟ ⎝ ∂T ⎠ v ⎝ ∂v ⎠ T v ⎛ T T T ⎞ v T = − RT ln − cT0 ⎜1 − ⎟ ⎜ T + T ln T ⎟ + RT ln v − cT ln T + RT v0 ⎝ 0 0 0 ⎠ 0 0 = cT0 + cT + RT ⎛ ∂s ⎞ c According to ⎜ ⎟ = v given in the text (Eq. 12-28), ⎝ ∂T ⎠ v T ⎛ ∂s ⎞ c cv = T ⎜ ⎟ =T =c ⎝ ∂T ⎠ v T The preceding expression for the temperature indicates that the equation of state for the substance is the same as that of an ideal gas. Then, c p = R + cv = R + c PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
36.
12-36 12-49 An expression
for the volume expansivity of a substance whose equation of state RT a is P = − is to be derived. v − b v (v + b)T 1 / 2 Analysis The definition for volume expansivity is 1 ⎛ ∂v ⎞ β= ⎜ ⎟ v ⎝ ∂T ⎠ P According to the cyclic relation, ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ = −1 ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T ⎝ ∂P ⎠ v which on rearrangement becomes ⎛ ∂P ⎞ ⎜ ⎟ ⎛ ∂v ⎞ ⎝ ∂T ⎠ v ⎜ ⎟ =− ⎝ ∂T ⎠ P ⎛ ∂P ⎞ ⎜ ⎟ ⎝ ∂v ⎠ T Proceeding to perform the differentiations gives ⎛ ∂P ⎞ R a ⎜ ⎟ = + ⎝ ∂T ⎠ v v − b 2v (v + b)T 3 / 2 and ⎛ ∂P ⎞ RT a ⎡ 1 1 ⎤ ⎜ ⎟ =− + 1/ 2 ⎢ 2 − 2 ⎥ ⎝ ∂v ⎠ T (v − b) 2 bT ⎢v ⎣ (v + b) ⎥⎦ RT a 2v + b =− + (v − b) 2 T 1 / 2 v 2 (v + b) 2 Substituting these results into the definition of the volume expansivity produces R a + 1 v − b 2v (v + b)T 3 / 2 β=− v − RT a 2v + b 2 + 1/ 2 2 (v − b) T v (v + b) 2 PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
37.
12-37 12-50 An expression
for the specific heat difference of a substance whose equation of state RT a is P = − is to be derived. v − b v (v + b)T 1 / 2 Analysis The specific heat difference is expressed by 2 ⎛ ∂v ⎞ ⎛ ∂P ⎞ c p − cv = −T ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T According to the cyclic relation, ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ = −1 ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T ⎝ ∂P ⎠ v which on rearrangement becomes −1 ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂P ⎞ ⎜ ⎟ = −⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂T ⎠ v ⎝ ∂v ⎠ T Substituting this result into the expression for the specific heat difference gives 2 −1 ⎛ ∂P ⎞ ⎛ ∂P ⎞ c p − cv = −T ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ v ⎝ ∂v ⎠ T The appropriate partial derivatives of the equation of state are ⎛ ∂P ⎞ R a/2 ⎜ ⎟ = + ⎝ ∂T ⎠v v − b v (v + b)T 3 / 2 ⎛ ∂P ⎞ RT a ⎡ 1 1 ⎤ ⎜ ⎟ =− + 1/ 2 ⎢ 2 − 2⎥ ⎝ ∂v ⎠ T (v − b) 2 bT ⎢v ⎣ (v + b) ⎥ ⎦ RT a 2v + b =− 2 + 1/ 2 (v − b) T v (v + b) 2 2 The difference in the specific heats is then 2 ⎡ R a/2 ⎤ −T ⎢ + 3/ 2 ⎥ ⎢ v − b v (v + b)T ⎣ ⎥ ⎦ c p − cv = RT a 2v + b − + (v − b) 2 T 1 / 2 v 2 (v + b) 2 PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
38.
12-38
RT a 12-51 An expression for the volume expansivity of a substance whose equation of state is P = − v − b v 2T is to be derived. Analysis The definition for volume expansivity is 1 ⎛ ∂v ⎞ β= ⎜ ⎟ v ⎝ ∂T ⎠ P According to the cyclic relation, ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ = −1 ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T ⎝ ∂P ⎠ v which on rearrangement becomes ⎛ ∂P ⎞ ⎜ ⎟ ⎛ ∂v ⎞ ⎝ ∂T ⎠ v ⎜ ⎟ =− ⎝ ∂T ⎠ P ⎛ ∂P ⎞ ⎜ ⎟ ⎝ ∂v ⎠ T Proceeding to perform the differentiations gives ⎛ ∂P ⎞ R a ⎜ ⎟ = + ⎝ ∂T ⎠ v v − b v 2 T 2 and ⎛ ∂P ⎞ RT 2a ⎜ ⎟ =− + 3 ⎝ ∂v ⎠ T (v − b) 2 v T Substituting these results into the definition of the volume expansivity produces R a + 1 v − b v 2T 2 β=− v − RT 2a 2 + 3 (v − b) v T PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
39.
12-39 12-52 An expression
for the isothermal compressibility of a substance whose equation of state RT a is P = − is to be derived. v − b v 2T Analysis The definition for the isothermal compressibility is 1 ⎛ ∂v ⎞ α=− ⎜ ⎟ v ⎝ ∂P ⎠ T Now, ⎛ ∂P ⎞ − RT 2a ⎜ ⎟ = + 3 ⎝ ∂v ⎠ T (v − b) 2 v T Using the partial derivative properties, 1 1 α=− =− ⎛ ∂P ⎞ − RTv 2a v⎜ ⎟ 2 + ⎝ ∂v ⎠ T (v − b) v 2T ⎛ ∂P ⎞ 12-53 It is to be shown that β = α ⎜ ⎟ . ⎝ ∂T ⎠ v Analysis The definition for the volume expansivity is 1 ⎛ ∂v ⎞ β= ⎜ ⎟ v ⎝ ∂T ⎠ P The definition for the isothermal compressibility is 1 ⎛ ∂v ⎞ α=− ⎜ ⎟ v ⎝ ∂P ⎠ T According to the cyclic relation, ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ = −1 ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T ⎝ ∂P ⎠ v which on rearrangement becomes ⎛ ∂v ⎞ ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎜ ⎟ = −⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂P ⎠ T ⎝ ∂T ⎠ v When this is substituted into the definition of the volume expansivity, the result is 1 ⎛ ∂v ⎞ ⎛ ∂P ⎞ β=− ⎜ ⎟ ⎜ ⎟ v ⎝ ∂P ⎠ T ⎝ ∂T ⎠v ⎛ ∂P ⎞ = − α⎜ ⎟ ⎝ ∂T ⎠ v PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
40.
12-40
cp vα 12-54 It is to be demonstrated that k = =− . cv (∂v / ∂P )s Analysis The relations for entropy differential are dT ⎛ ∂P ⎞ ds = cv +⎜ ⎟ dv T ⎝ ∂T ⎠ v dT ⎛ ∂v ⎞ ds = c p −⎜ ⎟ dP T ⎝ ∂T ⎠ P For fixed s, these basic equations reduce to dT ⎛ ∂P ⎞ cv = −⎜ ⎟ dv T ⎝ ∂T ⎠ v dT ⎛ ∂v ⎞ cp =⎜ ⎟ dP T ⎝ ∂T ⎠ P Also, when s is fixed, ∂v ⎛ ∂v ⎞ =⎜ ⎟ ∂P ⎝ ∂P ⎠ s Forming the specific heat ratio from these expressions gives ⎛ ∂v ⎞ ⎛ ∂T ⎞ ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂P ⎠ v k=− ⎛ ∂v ⎞ ⎜ ⎟ ⎝ ∂P ⎠ s The cyclic relation is ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ = −1 ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T ⎝ ∂P ⎠ v Solving this for the numerator of the specific heat ratio expression and substituting the result into this numerator produces ⎛ ∂v ⎞ ⎜ ⎟ ⎝ ∂P ⎠ T vα k= =− ⎛ ∂v ⎞ ⎛ ∂v ⎞ ⎜ ⎟ ⎜ ⎟ ⎝ ∂P ⎠ s ⎝ ∂P ⎠ s PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
41.
12-41
RT a 12-55 An expression for the specific heat difference of a substance whose equation of state is P = − v − b v 2T is to be derived. Analysis The specific heat difference is expressed by 2 ⎛ ∂v ⎞ ⎛ ∂P ⎞ c p − cv = −T ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T According to the cyclic relation, ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂T ⎞ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ = −1 ⎝ ∂T ⎠ P ⎝ ∂v ⎠ T ⎝ ∂P ⎠ v which on rearrangement becomes −1 ⎛ ∂v ⎞ ⎛ ∂P ⎞ ⎛ ∂P ⎞ ⎜ ⎟ = −⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ P ⎝ ∂T ⎠ v ⎝ ∂v ⎠ T Substituting this result into the expression for the specific heat difference gives 2 −1 ⎛ ∂P ⎞ ⎛ ∂P ⎞ c p − cv = −T ⎜ ⎟ ⎜ ⎟ ⎝ ∂T ⎠ v ⎝ ∂v ⎠ T The appropriate partial derivatives of the equation of state are ⎛ ∂P ⎞ R a ⎜ ⎟ = + 2 2 ⎝ ∂T ⎠ v v − b v T ⎛ ∂P ⎞ RT 2a ⎜ ⎟ =− + 3 ⎝ ∂v ⎠ T (v − b) 2 v T The difference in the specific heats is then 2 ⎡ R a ⎤ ⎢v − b + 2 2 ⎥ ⎣ v T ⎦ c p − cv = −T RT 2a − 2 + 3 (v − b) v T PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
42.
12-42 The Joule-Thomson Coefficient 12-56C
It represents the variation of temperature with pressure during a throttling process. 12-57C The line that passes through the peak points of the constant enthalpy lines on a T-P diagram is called the inversion line. The maximum inversion temperature is the highest temperature a fluid can be cooled by throttling. 12-58C No. The temperature may even increase as a result of throttling. 12-59C Yes. 12-60C No. Helium is an ideal gas and h = h(T) for ideal gases. Therefore, the temperature of an ideal gas remains constant during a throttling (h = constant) process. 12-61E [Also solved by EES on enclosed CD] The Joule-Thompson coefficient of nitrogen at two states is to be estimated. Analysis (a) The enthalpy of nitrogen at 200 psia and 500 R is, from EES, h = -10.564 Btu/lbm. Note that in EES, by default, the reference state for specific enthalpy and entropy is 0 at 25ºC (77ºF) and 1 atm. Approximating differentials by differences about the specified state, the Joule-Thomson coefficient is expressed as ⎛ ∂T ⎞ ⎛ ΔT ⎞ μ=⎜ ⎟ ≅⎜ ⎟ ⎝ ∂P ⎠ h ⎝ ΔP ⎠ h = −10.564 Btu/lbm Considering a throttling process from 210 psia to 190 psia at h = -10.564 Btu/lbm, the Joule-Thomson coefficient is determined to be ⎛ T190 psia − T210 psia ⎞ (499.703 − 500.296) R μ=⎜ ⎟ = = 0.0297 R/psia ⎜ ⎟ (190 − 210) psia ⎝ (190 − 210) psia ⎠ h = −10.564 Btu/lbm (b) The enthalpy of nitrogen at 2000 psia and 400 R is, from EES, h = -55.321 Btu/lbm. Approximating differentials by differences about the specified state, the Joule-Thomson coefficient is expressed as ⎛ ∂T ⎞ ⎛ ΔT ⎞ μ=⎜ ⎟ ≅⎜ ⎟ ⎝ ∂P ⎠ h ⎝ ΔP ⎠ h = −55.321 Btu/lbm Considering a throttling process from 2010 psia to 1990 psia at h = -55.321 Btu/lbm, the Joule-Thomson coefficient is determined to be ⎛ T1999 psia − T2001 psia ⎞ (399.786 - 400.213) R ⎜ μ=⎜ ⎟ = = 0.0213 R/psia ⎟ (1990 − 2010) psia ⎝ (1990 − 2010) psia ⎠ h = −55.321 Btu/lbm PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
43.
12-43 12-62E EES Problem
12-61E is reconsidered. The Joule-Thompson coefficient for nitrogen over the pressure range 100 to 1500 psia at the enthalpy values 100, 175, and 225 Btu/lbm is to be plotted. Analysis The problem is solved using EES, and the results are tabulated and plotted below. Gas$ = 'Nitrogen' {P_ref=200 [psia] T_ref=500 [R] P= P_ref} h=50 [Btu/lbm] {h=enthalpy(Gas$, T=T_ref, P=P_ref)} dP = 10 [psia] T = temperature(Gas$, P=P, h=h) P[1] = P + dP P[2] = P - dP T[1] = temperature(Gas$, P=P[1], h=h) T[2] = temperature(Gas$, P=P[2], h=h) Mu = DELTAT/DELTAP "Approximate the differential by differences about the state at h=const." DELTAT=T[2]-T[1] DELTAP=P[2]-P[1] h = 100 Btu/lbm P [psia] µ [R/psia] 100 0.003675 275 0.003277 450 0.002899 625 0.00254 800 0.002198 975 0.001871 1150 0.001558 1325 0.001258 1500 0.0009699 0.004 0.003 0.002 h = 100 Btu/lbm 0.001 μ [R/psia] 0 -0.001 -0.002 h = 175 Btu/lbm -0.003 -0.004 h = 225 Btu/lbm -0.005 -0.006 0 200 400 600 800 1000 1200 1400 1600 P [psia] PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
44.
12-44 12-63 The Joule-Thompson
coefficient of refrigerant-134a at a specified state is to be estimated. Analysis The enthalpy of refrigerant-134a at 0.7 MPa and T = 50°C is h = 288.53 kJ/kg. Approximating differentials by differences about the specified state, the Joule-Thomson coefficient is expressed as ⎛ ∂T ⎞ ⎛ ΔT ⎞ μ=⎜ ⎟ ≅⎜ ⎟ ⎝ ∂P ⎠ h ⎝ ΔP ⎠ h = 288.53 kJ/kg Considering a throttling process from 0.8 MPa to 0.6 MPa at h = 288.53 kJ/kg, the Joule-Thomson coefficient is determined to be ⎛ T0.8 MPa − T0.6 MPa ⎞ (51.81 − 48.19)°C μ=⎜ ⎜ (0.8 − 0.6)MPa ⎟ ⎟ = = 18.1 °C/MPa ⎝ ⎠ h = 288.53 kJ/kg (0.8 − 0.6)MPa 12-64 Steam is throttled slightly from 1 MPa and 300°C. It is to be determined if the temperature of the steam will increase, decrease, or remain the same during this process. Analysis The enthalpy of steam at 1 MPa and T = 300°C is h = 3051.6 kJ/kg. Now consider a throttling process from this state to 0.8 MPa, which is the next lowest pressure listed in the tables. The temperature of the steam at the end of this throttling process will be P = 0.8 MPa ⎫ ⎬ T2 = 297.52°C h = 3051.6 kJ/kg ⎭ Therefore, the temperature will decrease. T 2 ⎛ ∂ (v / T ) ⎞ 12-65 It is to be demonstrated that the Joule-Thomson coefficient is given by μ = ⎜ ⎟ . c p ⎝ ∂T ⎠ P Analysis From Eq. 12-52 of the text, 1 ⎡ ⎛ ∂v ⎞ ⎤ cp = ⎢T ⎜ ⎟ −v ⎥ μ ⎣ ⎝ ∂T ⎠ P ⎦ Expanding the partial derivative of v/T produces ⎛ ∂v / T ⎞ 1 ⎛ ∂v ⎞ v ⎜ ⎟ = ⎜ ⎟ − 2 ⎝ ∂T ⎠ P T ⎝ ∂T ⎠ P T When this is multiplied by T2, the right-hand side becomes the same as the bracketed quantity above. Then, T 2 ⎛ ∂ (v / T ) ⎞ μ= ⎜ ⎟ c p ⎝ ∂T ⎠ P PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.
Descargar ahora