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ENERGY ANALYSIS OF CLOSED SYSTEMS

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Monatomic gas ... gas specific heats of monatomic gases such as argon, neon ... Thus, u and h of monatomic gases can easily be evaluated from Eqn 4-27 and 4-28. ... – PowerPoint PPT presentation

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Title: ENERGY ANALYSIS OF CLOSED SYSTEMS


1
CHAPTER 4
  • ENERGY ANALYSIS OF CLOSED SYSTEMS

2
Introduction
  • In chapter 2, we considered various forms of
    energy and energy transfer, and we developed a
    general relation for conservation of energy
    balance.
  • In chapter 3, we learned how to determine
    thermodynamic properties of substances.
  • In chapter 4, we apply energy balance relation to
    closed systems.

3
Objectives
  • Examine the boundary work or PdV work
  • Develop the general energy balance applied to
    close systems.
  • Define the specific heat at constant volume and
    constant pressure.
  • Relate the specific heats to the calculation of
    the changes in internal energy and enthalpy of
    ideal gases.

4
Common Types of Work Energy
  • The net work done by the system may be in two
    forms
  • Boundary work
  • Shaft work and electrical work as other work,
    that is, work not associated with a moving
    boundary.

5
Boundary Work
  • Expansion and compression work is often called
    boundary work.
  • Temperature of air rises when it is compressed.
  • This is because energy is transferred to the air
    in the form of boundary work.
  • The increase in the energy of the system be equal
    to the boundary work done on the system.

6
  • Boundary Work
  • Boundary work occurs because the mass of the
    substance contained within the system boundary.
  • Consider the gas enclosed in the piston-cylinder
    device shown.
  • Initial pressure of the gas is P, total volume V,
    cross sectional area of piston is A.
  • If the piston is allowed to move a distance ds,
    the differential work done during this process is

7
  • The boundary work is equal to the area under the
    process curve plotted on the pressure-volume
    diagram.
  • Note from the figure
  • - P is the absolute pressure and is always
    positive.
  • Volume change dV is ve during expansion (V
    increase) -ve during compression (V decrease)
  • When dV is positive, Wb is positive.
  • - When dV is negative, Wb is negative.

Pressure-volume diagram
8
Some Typical Processes
Constant volume If the volume is held constant,
dV 0, and the boundary work equation becomes
Constant pressure If the pressure is held
constant, the boundary work equation becomes
P-V diagram for V constant P-V diagram for P
constant
9
  • Constant temperature, ideal gas
  • If the temperature of an ideal gas system is held
    constant, then the equation of state provides the
    pressure-volume relation

Then, the boundary work is
Note The above equation is the result of
applying the ideal gas assumption for the
equation of state.
10
Example 1 Boundary work for a constant-volume
process
  • A rigid tank contains air at 500 kPa and 150C.
    As a result of heat transfer to the surroundings,
    the temperature and pressure inside the tank drop
    to 65C and 400 kPa, respectively. Determine the
    boundary work done during this process.

11
Example 2 Boundary work for a constant-pressure
process
  • A frictionless pistoncylinder device contains 5
    kg of steam at 400 kPa and 200oC. Heat is now
    transferred to the steam until the temperature
    reaches 250oC. If the piston is not attached to a
    shaft and its mass is constant, determine the
    work done by the steam during this process.

12
Example 3 Isothermal compression of an ideal gas
  • A pistoncylinder device initially contains 0.4
    m3 of air at 100 kPa and 80C. The air is now
    compressed to 0.1 m3 in such a way that the
    temperature inside the cylinder remains constant.
    Determine the work done during this process.

13
Quiz 4
  • A mass of 5 kg of saturated water vapor at 300
    kPa is heated at constant pressure until the
    temperature reaches 200?C. Calculate the work
    done by the steam during this process.

14
ENERGY BALANCE FOR CLOSED SYSTEMS
15
Refresh
  • Energy Balance The net change (increase or
    decrease) in the total energy of the system
    during a process is equal to the difference
    between the total energy entering and the total
    energy leaving the system during that process.

16
Energy change of a system
(Total energy entering system) (Total energy
leaving system) (Change in the total energy
of the system)
Ein - Eout ?Esystem
? U ? KE ? PE
where ? U m (u2 u1 ) ? KE ½ (m
)(V22 - V12) ? PE mg (z2 z1 )
17
Energy balance for closed system
  • Closed system (control mass) no mass can
    enter or leave a system

0
Heat
Work
Mass
Closed System
18
Various forms of the first law relation for
closed system
General Qnet,in - Wnet,out ?Esystem
Stationary system Q net,in - W net,out
?U ? KE ?PE 0
Per unit mass q - w ?e
19
Example 4 Electric heating of a gas at constant
pressure
  • A piston-cylinder device contains 25 g of
    saturated water vapor that is maintained at a
    constant pressure of 300 kPa. A resistance heater
    within the cylinder is turned on and passes a
    current of 0.2 A for 5 min from a 120 V source.
    At the same time, a heat loss of 3.7 kJ occurs.
    Show that for a closed system the boundary work
    Wb and the change in internal energy ?U can be
    combined in one term, ?H for a constant pressure
    process.

20
  • For a closed system (involve boundary work at
    constant pressure)

Q - W ?U ? KE ?PE 0
Q - Wother - Wb ?U
Q - Wother P(V2 - V2) U2 U1
Since P is constant, PP1 P2
Q - Wother (U2 P2V2) - (U1 P1V1)
Q - Wother H2 - H1
21
Example 5 Unrestrained Expansion of Water
  • A rigid tank is divided into two equal parts by a
    partition. Initially one side of the tank is
    contains 5 kg of water at 200 kPa and 25?C, and
    the other side is evacuated. The partition is
    removed and the water expands into the entire
    tank. The water is allowed to exchange heat with
    its surroundings until the temperature in the
    tank returns to the initial value of 25?C.
    Determine
  • The volume of the tank
  • The final pressure
  • The heat transfer for this process

22
Quiz 5
  • A 0.5-m3 rigid tank contains refrigerant-134a
    initially at 160 kPa and 40 percent quality. Heat
    is now transferred to the refrigerant until the
    pressure reaches 700 kPa. Determine
  • the mass of the refrigerant in the tank
  • the amount of heat transferred.

23
Specific Heat
  • Energy required to raise the temperature of a
    unit mass substance by one degree.
  • Common unit kJ/kg.K or kJ/kg.oC
  • Two kinds of specific heat
  • Specific heat at constant volume, cv
  • Specific heat at constant pressure, cp

24
  • cp is always greater than cv
  • At constant pressure, the system is allowed to
    expand and the energy is required for the
    expansion work.

25
  • In thermodynamics, the specific heats are defined
    as

26
Internal energy, enthalpy and specific heat of
IDEAL GASES
  • Ideal gas Pv RT
  • Using definition of enthalpy and equation of
    state of ideal gas
  • u and h depend only on temperature for an ideal
    gas.
  • cp and cv also depend on temperature only.

27
Integrate these equations (from state1 to state
2)
  • Changes in the internal energy and enthalpy is

28
Ideal gas constant pressure specific heats for
some gases
Complex molecules
Figure 4-24
Monatomic gas
29
  • Specific heats of gases with complex molecules
    (molecules with two or more atoms) are higher and
    increase with temp.
  • Variation of specific heats with temp is smooth
    and linear over small temp intervals.
  • Therefore specific heat functions in Eqn 4-25
    4-26 can be replaced by the constant average
    specific heat values.
  • Then the integrations in these eqns can be
    performed, yielding

30
  • Specific heat values for some common gases are
    listed as a function of T in Table A-2b.
  • cp,avg and cv,avg are evaluated from this table
    at average temp (T1T2)/2

31
  • Another observation from Fig 4-24 is that ideal
    gas specific heats of monatomic gases such as
    argon, neon and helium remain constant over the
    entire temp range.
  • Thus, ?u and ?h of monatomic gases can easily be
    evaluated from Eqn 4-27 and 4-28.

32
  • Three ways to determine internal energy and
    enthalpy for ideal gases
  • 1. Using tabulated u and h data (Table A-17).
  • 2. Using cp and cv as a function of temperature
    (Table A-2c)
  • 3. Using average specific heat (Take the average
    of T1 and T2 Table A-2b)

33
Specific heat relation of ideal gases
  • Relationship between cp and cv obtained by
    differentiating relation h u RT
  • Replace dh by cpdT and du by cvdT, then divide
    by dT

kJ/kg.K
34
Example 5 Evaluation of the ?u of an ideal gas
  • Air at 300 K and 200 kPa is heated at constant
    pressure to 600 K. Determine the change in
    internal energy of air per unit mass, using
  • Data from the air table (Table A-17)
  • The functional form of the specific heat
    (Table A-2c)
  • The average specific heat value (Table A-2b)

35
Problem 4-52
  • A rigid tank contains 10 kg of air at 350 kPa and
    27?C. The air is now heated until its pressure
    doubles. Determine
  • The volume of the tank and
  • The amount of heat transfer

36
  • THANK
  • YOU
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