L5 - EnergyAnalysisClosedSys 2023.pptx

Keith Vaugh
Keith VaughSTEM Education & Design en MAGVA Design + Letterpress
KEITH VAUGH
ENERGY ANALYSIS OF
CLOSED SYSTEMS
Reference text: Chapter 5 - Fundamentals of Thermal-Fluid Sciences, 3rd Edition
Yunus A. Cengel, Robert H. Turner, John M. Cimbala
McGraw-Hill, 2008
Lecture 5
Keith Vaugh BEng (AERO) MEng
KEITH VAUGH
Examine the moving boundary work or P dV work
commonly encountered in reciprocating devices such
as automotive engines and compressors.
Identify the first law of thermodynamics as simply a
statement of the conservation of energy principle for
closed (fixed mass) systems.
Develop the general energy balance applied to closed
systems.
Define the specific heat at constant volume and the
specific heat at constant pressure.
OBJECTIVES
KEITH VAUGH
Relate the specific heats to the calculation of the
changes in internal energy and enthalpy of ideal gases.
Describe incompressible substances and determine the
changes in their internal energy and enthalpy.
Solve energy balance problems for closed (fixed mass)
systems that involve heat and work interactions for
general pure substances, ideal gases, and
incompressible substances.
KEITH VAUGH
MOVING
BOUNDARY WORK
Moving boundary work (PdV work)
The work associated with a moving boundary is
called boundary work
The expansion and compression work in a piston
cylinder device is given by
A gas does a differential amount of
work δWb as it forces the piston to
move by a differential amount ds.
Quasi-equilibrium process
A process during which the system remains nearly
in equilibrium at all times.
KEITH VAUGH
The area under the process curve on
a P-V diagram represents the
boundary work.
The boundary work done
during a process depends
on the path followed as well
as the end states.
The net work done during a
cycle is the difference
between the work done by
the system and the work
done on the system.
KEITH VAUGH
POLYTROPIC,
ISOTHERMAL &
ISOBARIC PROCESSES
Polytropic process: C, n (polytropic exponent) constants
Polytropic process
Polytropic and for ideal gas
When n=1 (Isothermal process)
Constant pressure process (Isobaric process)
KEITH VAUGH
ENERGY
BALANCE FOR
CLOSED SYSTEMS
Energy balance for any system undergoing
any process
Energy balance in the rate form
The total quantities are related to the quantities
per unit time
Energy balance in differential form
Energy balance per unit mass basis
KEITH VAUGH
Energy balance when sign convention is used (i.e. heat input and work output are
positive; heat output and work input are negative)
Energy balance for a cycle
Various forms of the first-law
relation for closed systems when
sign convention is used.
KEITH VAUGH
The first law cannot be proven mathematically, but no process
in nature is known to have violated the first law, therefore this
can be taken as sufficient proof
KEITH VAUGH
ENERGY BALANCE
FOR A CONSTANT
PRESSURE
PROCESS
General analysis for a closed system undergoing a
quasi-equilibrium constant-pressure process Q is to
the system and W is from the system
For a constant pressure expansion
or compression process:
Example 5-5 page 168
expansion or
compression
KEITH VAUGH
The energy required to raise the temperature of a unit mass of a substance by one degree
SPECIFIC HEAT
Specific heat is the energy required to raise
the temperature of a unit mass of a
substance by one degree in a specified
way.
In thermodynamics we are interested in two kinds of specific heats
✓ Specific heat at constant volume, cv
✓ Specific heat at constant pressure, cp
KEITH VAUGH
Specific heat at constant volume, cv
The energy required to raise the temperature of the
unit mass of a substance by one degree as the
volume is maintained constant.
Specific heat at constant pressure, cp
The energy required to raise the temperature of the
unit mass of a substance by one degree as the
pressure is maintained constant.
Constant-volume and constant-
pressure specific heats cv and cp
(values are for helium gas).
KEITH VAUGH
The specific heat of a substance
changes with temperature
The equations in the figure are valid for any
substance undergoing any process.
cv and cp are properties.
cv is related to the changes in internal energy and cp
to the changes in enthalpy.
A common unit for specific heats is kJ/kg · °C or kJ/kg · K
}
}
the change in internal energy with
temperature at constant volume
the change in internal enthalpy with
temperature at constant pressure
Formal definitions of cv and cp
KEITH VAUGH
INTERNAL ENERGY,
ENTHALPY &
SPECIFIC HEATS
An Ideal gas can be defined as a gas whose temperature, pressure and
specific volume are related by
Joule demonstrated mathematically and
experimentally in 1843, that for an Ideal
gas the internal energy is a function of the
temperature only;
of ideal gases
KEITH VAUGH
Using the definition of enthalpy and the equation of state
of an ideal gas
For ideal gases, u, h,
cv, and cp vary with
temperature only.
Internal energy change of an ideal gas
Internal energy change of an ideal gas
KEITH VAUGH
At low pressures, all real gases approach
ideal-gas behaviour, and therefore their
specific heats depend on temperature only.
The specific heats of real gases at low
pressures are called ideal-gas specific
heats, or zero-pressure specific heats, and
are often denoted cp0 and cv0.
Ideal-gas constant-
pressure specific heats for
some gases (see Table A–
2c for cp equations).
u and h data for a number of gases
have been tabulated.
These tables are obtained by choosing
an arbitrary reference point and
performing the integrations by treating
state 1 as the reference state.
In the preparation of ideal-gas
tables, 0 K is chosen as the
reference temperature
KEITH VAUGH
Internal energy and enthalpy change when specific
heat is taken constant at an average value
The relation Δ u = cv ΔT is valid for any kind
of process, constant-volume or not.
For small temperature intervals, the specific heats
may be assumed to vary linearly with temperature.
KEITH VAUGH
Three ways of calculating Δu
By using the tabulated u and h data. This is the easiest
and most accurate way when tables are readily
available.
By using the cv or cp relations (Table A-2c) as a function
of temperature and performing the integrations. This is
very inconvenient for hand calculations but quite
desirable for computerised calculations. The results
obtained are very accurate.
By using average specific heats. This is very simple and
certainly very convenient when property tables are not
available. The results obtained are reasonably accurate
if the temperature interval is not very large.
Three ways of calculating Δu and Δh
KEITH VAUGH
The specific ratio varies with temperature, but this variation is very mild.
For monatomic gases (helium, argon, etc.), its value is essentially constant at 1.667.
Many diatomic gases, including air, have a specific heat ratio of about 1.4 at room temperature.
Specific Heat Relations of Ideal Gases
The relationship between cp, cv and R
} On a molar basis
Specific heat ratio
KEITH VAUGH
Incompressible substance: A substance whose specific volume (or
density) is constant. Solids and liquids are incompressible substances.
INTERNAL ENERGY,
ENTHALPY &
SPECIFIC HEATS
The specific volumes of
incompressible substances
remain constant during a process.
The cv and cp values of incompressible
substances are identical and are
denoted by c.
of solids and liquids
KEITH VAUGH
Internal energy changes
KEITH VAUGH
Enthalpy changes
The enthalpy of a compressed liquid
A more accurate relation than
KEITH VAUGH
Moving boundary work
Wb for an isothermal process
Wb for a constant-pressure process
Wb for a polytropic process
Energy balance for closed systems
Energy balance for a constant-pressure expansion or compression process
Specific heats
Constant-pressure specific heat, cp
Constant-volume specific heat, cv
Internal energy, enthalpy and specific heats of ideal gases
Energy balance for a constant-pressure expansion or compression process
Internal energy, enthalpy and specific heats of incompressible substances (solids and liquids)
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L5 - EnergyAnalysisClosedSys 2023.pptx

  • 1. KEITH VAUGH ENERGY ANALYSIS OF CLOSED SYSTEMS Reference text: Chapter 5 - Fundamentals of Thermal-Fluid Sciences, 3rd Edition Yunus A. Cengel, Robert H. Turner, John M. Cimbala McGraw-Hill, 2008 Lecture 5 Keith Vaugh BEng (AERO) MEng
  • 2. KEITH VAUGH Examine the moving boundary work or P dV work commonly encountered in reciprocating devices such as automotive engines and compressors. Identify the first law of thermodynamics as simply a statement of the conservation of energy principle for closed (fixed mass) systems. Develop the general energy balance applied to closed systems. Define the specific heat at constant volume and the specific heat at constant pressure. OBJECTIVES
  • 3. KEITH VAUGH Relate the specific heats to the calculation of the changes in internal energy and enthalpy of ideal gases. Describe incompressible substances and determine the changes in their internal energy and enthalpy. Solve energy balance problems for closed (fixed mass) systems that involve heat and work interactions for general pure substances, ideal gases, and incompressible substances.
  • 4. KEITH VAUGH MOVING BOUNDARY WORK Moving boundary work (PdV work) The work associated with a moving boundary is called boundary work The expansion and compression work in a piston cylinder device is given by A gas does a differential amount of work δWb as it forces the piston to move by a differential amount ds. Quasi-equilibrium process A process during which the system remains nearly in equilibrium at all times.
  • 5. KEITH VAUGH The area under the process curve on a P-V diagram represents the boundary work. The boundary work done during a process depends on the path followed as well as the end states. The net work done during a cycle is the difference between the work done by the system and the work done on the system.
  • 6. KEITH VAUGH POLYTROPIC, ISOTHERMAL & ISOBARIC PROCESSES Polytropic process: C, n (polytropic exponent) constants Polytropic process Polytropic and for ideal gas When n=1 (Isothermal process) Constant pressure process (Isobaric process)
  • 7. KEITH VAUGH ENERGY BALANCE FOR CLOSED SYSTEMS Energy balance for any system undergoing any process Energy balance in the rate form The total quantities are related to the quantities per unit time Energy balance in differential form Energy balance per unit mass basis
  • 8. KEITH VAUGH Energy balance when sign convention is used (i.e. heat input and work output are positive; heat output and work input are negative) Energy balance for a cycle Various forms of the first-law relation for closed systems when sign convention is used.
  • 9. KEITH VAUGH The first law cannot be proven mathematically, but no process in nature is known to have violated the first law, therefore this can be taken as sufficient proof
  • 10. KEITH VAUGH ENERGY BALANCE FOR A CONSTANT PRESSURE PROCESS General analysis for a closed system undergoing a quasi-equilibrium constant-pressure process Q is to the system and W is from the system For a constant pressure expansion or compression process: Example 5-5 page 168 expansion or compression
  • 11. KEITH VAUGH The energy required to raise the temperature of a unit mass of a substance by one degree SPECIFIC HEAT Specific heat is the energy required to raise the temperature of a unit mass of a substance by one degree in a specified way. In thermodynamics we are interested in two kinds of specific heats ✓ Specific heat at constant volume, cv ✓ Specific heat at constant pressure, cp
  • 12. KEITH VAUGH Specific heat at constant volume, cv The energy required to raise the temperature of the unit mass of a substance by one degree as the volume is maintained constant. Specific heat at constant pressure, cp The energy required to raise the temperature of the unit mass of a substance by one degree as the pressure is maintained constant. Constant-volume and constant- pressure specific heats cv and cp (values are for helium gas).
  • 13. KEITH VAUGH The specific heat of a substance changes with temperature The equations in the figure are valid for any substance undergoing any process. cv and cp are properties. cv is related to the changes in internal energy and cp to the changes in enthalpy. A common unit for specific heats is kJ/kg · °C or kJ/kg · K } } the change in internal energy with temperature at constant volume the change in internal enthalpy with temperature at constant pressure Formal definitions of cv and cp
  • 14. KEITH VAUGH INTERNAL ENERGY, ENTHALPY & SPECIFIC HEATS An Ideal gas can be defined as a gas whose temperature, pressure and specific volume are related by Joule demonstrated mathematically and experimentally in 1843, that for an Ideal gas the internal energy is a function of the temperature only; of ideal gases
  • 15. KEITH VAUGH Using the definition of enthalpy and the equation of state of an ideal gas For ideal gases, u, h, cv, and cp vary with temperature only. Internal energy change of an ideal gas Internal energy change of an ideal gas
  • 16. KEITH VAUGH At low pressures, all real gases approach ideal-gas behaviour, and therefore their specific heats depend on temperature only. The specific heats of real gases at low pressures are called ideal-gas specific heats, or zero-pressure specific heats, and are often denoted cp0 and cv0. Ideal-gas constant- pressure specific heats for some gases (see Table A– 2c for cp equations). u and h data for a number of gases have been tabulated. These tables are obtained by choosing an arbitrary reference point and performing the integrations by treating state 1 as the reference state. In the preparation of ideal-gas tables, 0 K is chosen as the reference temperature
  • 17. KEITH VAUGH Internal energy and enthalpy change when specific heat is taken constant at an average value The relation Δ u = cv ΔT is valid for any kind of process, constant-volume or not. For small temperature intervals, the specific heats may be assumed to vary linearly with temperature.
  • 18. KEITH VAUGH Three ways of calculating Δu By using the tabulated u and h data. This is the easiest and most accurate way when tables are readily available. By using the cv or cp relations (Table A-2c) as a function of temperature and performing the integrations. This is very inconvenient for hand calculations but quite desirable for computerised calculations. The results obtained are very accurate. By using average specific heats. This is very simple and certainly very convenient when property tables are not available. The results obtained are reasonably accurate if the temperature interval is not very large. Three ways of calculating Δu and Δh
  • 19. KEITH VAUGH The specific ratio varies with temperature, but this variation is very mild. For monatomic gases (helium, argon, etc.), its value is essentially constant at 1.667. Many diatomic gases, including air, have a specific heat ratio of about 1.4 at room temperature. Specific Heat Relations of Ideal Gases The relationship between cp, cv and R } On a molar basis Specific heat ratio
  • 20. KEITH VAUGH Incompressible substance: A substance whose specific volume (or density) is constant. Solids and liquids are incompressible substances. INTERNAL ENERGY, ENTHALPY & SPECIFIC HEATS The specific volumes of incompressible substances remain constant during a process. The cv and cp values of incompressible substances are identical and are denoted by c. of solids and liquids
  • 22. KEITH VAUGH Enthalpy changes The enthalpy of a compressed liquid A more accurate relation than
  • 23. KEITH VAUGH Moving boundary work Wb for an isothermal process Wb for a constant-pressure process Wb for a polytropic process Energy balance for closed systems Energy balance for a constant-pressure expansion or compression process Specific heats Constant-pressure specific heat, cp Constant-volume specific heat, cv Internal energy, enthalpy and specific heats of ideal gases Energy balance for a constant-pressure expansion or compression process Internal energy, enthalpy and specific heats of incompressible substances (solids and liquids)

Notas del editor

  1. Wb is positive → for expansion Wb is negative → for compression
  2. Refer to Isobaric process (constant pressure) on slide 6.
  3. True or False, cp is always greater then cv
  4. Refer to Joule experimental arrangement on page 174 of the text
  5. Refer to Joule experimental arrangement on page 174 of the text