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Page 1: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Entropy

Page 2: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Content

• Entropy and principle of increasing entropy.• Change of entropy in an ideal gas.

Page 3: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Entropy

• Entropy can be viewed as a measure of molecular disorder, or molecular randomness.

• As a system becomes more disordered, the positions of the molecules become less predictable and the entropy increases. Thus, it is not surprising that the entropy of a substance is lowest in the solid phase and highest in the gas phase.

• In the solid phase, the molecules of a substance continually oscillate about their equilibrium positions, but they cannot move relative to each other, and their position at any instant can be predicted with good certainty.

• In the gas phase, however, the molecules move about at random, collide with each other, and change direction, making it extremely difficult to predict accurately the microscopic state of a system at any instant.

• Associated with this molecular chaos is a high value of entropy.

Page 4: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Clausius Inequality

• Consider an extremely reversible heat engine 1 as shown in the figure, which operates between the temperature limits Tc and Tf. Using equations of Carnot cycles we have,

Page 5: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Clausius Inequality

• Similarly, now consider a thermal machine 2 that operates between the same limits of temperature Tc and Tf, as shown in Figure. According to the principle of Carnot,W1 > W2

• then,Qf1 < Qf2

• And,

• Therefore, to the machine 2,

Page 6: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Clausius Inequality

• From the above equations it follows that

• The above equation is known as Clausius inequality.• Since any reversible cycle can be replaced by a series of cycles of Carnot, Clausius inequality is valid for any thermal machine (or refrigerator) reversible or irreversible, where equality is preserved in reversible cycles and inequality in irreversible cycles.

• Note that with increasing the irreversibility in a given machine, the cyclic integral of dQ/T becomes more negative.

Page 7: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Definition of Entropy

• Once established Clausius inequality, consider a reversible cycle consisting of the processes A and B as shown in schematic form in Fig. According to the Clausius inequality,

• Similarly, for the reversible cycle consisting of processes A and C,

Page 8: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Definition of Entropy

• Comparing the above equations,

• In the above equation shows that ∫(dQ/T)rev becomes the same value along any reversible path between state 2 and state 1.

• Accordingly, this amount depends solely on the initial and final states of the process, and is therefore a thermodynamic property.

• Indeed, the entropy S is defined by the equation,

Page 9: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Definition of Entropy

• That is, the entropy change between any two thermodynamic states can be determined using the expression,

• The above equation, valid for any closed system or constant mass, clearly stated that integration must be performed along a reversible path, if you want to evaluate the entropy difference between two states, and also requires knowledge of ratio dQ/T throughout the reversible process.

• However, since the entropy is a thermodynamic property, the difference S between two states is the same regardless if the process is reversible or irreversible.

Page 10: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Definition of Entropy

• Furthermore, if the process in question is irreversible, the entropy difference between the states 1 and 2 can not be evaluated directly by using the above equation, therefore, the equation that applies generally to any process is

• where equality is preserved in reversible processes and the inequality in irreversible processes.

Page 11: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Definition of Entropy

• It follows from the integration of (dQ / T) along an irreversible trajectory in a given process, do not result in the entropy difference between the initial state and the final state.

• Similarly, it can be added to all reversible adiabatic isentropic process.• That is, all isentropic process is adiabatic, but not all adiabatic process is isentropic; only reversible adiabatic processes are isentropic.

• Furthermore, since entropy is a property, the difference S between two thermodynamic states can be evaluated using the entropy equation for reversible processes, as long as one or more reversible paths connecting the initial and final states of the process (reversible or irreversible) are selected.

Page 12: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

The Increase of Entropy Principle

• Consider an isolated system, namely, a closed system where no energy transfer with the surroundings.

• According to the First Law of Thermodynamics, this system can only acquire those states in which the total internal energy of the system remains constant.

• On the other hand, the Second Law of Thermodynamics establishes, that the isolated state can only acquire those states that the entropy of this increase or remain constant. Namely,

∆S 0

• where equality is preserved in reversible processes and the inequality in irreversible processes.

Page 13: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

The Increase of Entropy Principle

• The above equation is known as the Increase of Entropy Principle and is a quantitative way to establish the second law of thermodynamics.

• In fact, this axiom states that"The entropy of an isolated system increases in all irreversible processes, and the limit remains constant for reversible processes"

• Unlike the energy, entropy is not conserved except reversible processes.

• In other words, the first law states that energy is neither created nor destroyed, while the second law states that entropy is not destroyed, only created.

Page 14: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

The Increase of Entropy Principle

• Since an isolated system can always be formed with any system (open or closed) and its surroundings, the above equation also indicates that

∆S ∆S 0

• Since the surroundings are everything that surrounds a system, often is called universe the set formed by the system and its surroundings. Accordingly,

∆S 0

Page 15: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Entropy as a Function of Other Properties

• For ideal gases:

∆ ln

∆ , ln ln

∆ , ln ln

has absolute zero as the reference temperature

(kJ/kgK) Constant Specific Heat

(kJ/kgK) Constant Specific Heat

(kJ/kgK) Variable Specific Heat ‐ Tables

Page 16: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)

EXAMPLE 7–1 Entropy Change during an Isothermal ProcessA piston–cylinder device contains a liquid–vapor mixture of water at 300 K. During a constant‐pressure process, 750 kJ of heat is transferred to the water. As a result, part of the liquid in the cylinder vaporizes. Determine the entropy change of the water during this process.Data:  = 300 K,  = 750 kJ, ∆ = ?

∆750kJ300K . /

Page 17: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)

EXAMPLE 7–2 Entropy Generation during Heat Transfer ProcessesA heat source at 800 K loses 2000 kJ of heat to a sink at (a) 500 K and (b) 750 K. Determine which heat transfer process is more irreversible.

a)  = 800 K,  = 500 K,  = ‐2000 kJ,  = 2000 kJ, ∆ = ?

∆ ∆ ∆

∆2000kJ800K

2.5kJ/K

2000kJ500K

4.0kJ/K

∆ 2.5kJ/K 4.0 kJ/K . /

Page 18: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)b)  = 800 K,  = 750 K,  = ‐2000 kJ,  = 2000 kJ, ∆ = ?

∆ ∆ ∆

∆2000kJ800K

2.5kJ/K

2000kJ750K

2.7kJ/K

∆ 2.5kJ/K 2.7kJ/K . /

The process in part (b) is smaller, and therefore it is less irreversible

Page 19: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)

EXAMPLE 7–3 Entropy Change of a Substance in a TankA rigid tank contains 5 kg of refrigerant‐134a initially at 20°C and 140 kPa. The refrigerant is now cooled while being stirred until its pressure drops to 100 kPa. Determine the entropy change of the refrigerant during this process.

Data:  = 5 kg, R134a,  = 20°C,  = 140 kPa,  = 100 kPa, ∆ = ?

@ , 1.0625kJ/kgK TableA13

constant ⇒ @ , 0.16544 m3/kg Table A13

Page 20: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)

@ 100kPa0.0007258m3/kg0.19255m3/kg

0.16544m3/kg

Table A12

@ 100kPa0.07182kJ/kg0.88008kJ/kgTable A12

0.16554 0.00072580.19255 0.0007258 0.859

0.07182kJ/kg 0.859 0.88008kJ/kg 0.8278kJ/kg∆ 5 kg 0.8278 1.0625 kJ/kgK . /

Page 21: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)

EXAMPLE 7–5 Isentropic Expansion of Steam in a TurbineSteam enters an adiabatic turbine at 5 MPa and 450°C and leaves at a pressure of 1.4 MPa. Determine the work output of the turbine per unit mass of steam if the process is reversible.Data:  = 5 MPa,  = 450°C,  = 1.4 MPa, ∆ = constant,  = ?

∆ ∆ ∆0 0 0

@ , 3317.2kJ/kg TableA6

@ , 6.810kJ/kgK TableA6

Page 22: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)6.810kJ/kgK

@ 1.4MPa2.2835kJ/kgK6.4675kJ/kgKTable A5

@ , 2967.4kJ/kg TableA6 Interpolation

3317.2kJ/kg 2967.4kJ/kg . /

Page 23: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)

EXAMPLE 7–8 Economics of Replacing a Valve by a TurbineA cryogenic manufacturing facility handles liquid methane at 115 K and 5 MPa at a rate of 0.280 m3/s . A process requires dropping the pressure of liquid methane to 1 MPa, which is done by throttling the liquid methane by passing it through a flow resistance such as a valve. A recently hired engineer proposes to replace the throttling valve by a turbine in order to produce power while dropping the pressure to 1 MPa. Using data from Table 7–1, determine the maximum amount of power that can be produced by such a turbine. Also, determine how much this turbine will save the facility from electricity usage costs per year if the turbine operates continuously (8760 h/yr) and the facility pays $0.075/kWh for electricity.

Page 24: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)

Page 25: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)

Data: Liquid  ,  = 115 K,  = 5 MPa,  = 0.280 m3/s,  = 1 MPa, ∆ = constant, 8760 h/yr, $0.075/kWh,  = ?, $/yr = ?

@ , 232.3kJ/kg(Table 7‐1)@ , 4.9945kJ/kgK (Table 7‐1)

@ , 422.15kg/m3(Table 7‐1)@ , 222.8kJ/kg(Table 7‐1 ‐ Interpolation)

422.15kg/m3 0.280m3/s 118.2kg/s

118.2kg/s 232.3 222.8 kJ/kg ,

Page 26: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)∆

1123kW 8760h 0.9837 10 kWh/yr

Saving $/kWh

0.9837 10 kWh/yr 0.075$/kWh

$ , /

Page 27: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)

EXAMPLE 7–9 Entropy Change of an Ideal GasAir is compressed from an initial state of 100 kPa and 17°C to a final state of 600 kPa and 57°C. Determine the entropy change of air during this compression process by using (a) property values from the air table and (b) average specific heats.

a)  = 100 kPa,  = 17°C,  = 600 kPa,  = 57°C, ∆ = ? Using Table A17

∆ ln

Page 28: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)17°C 273 290K57°C 273 330K

@ 1.66802kJ/kgK TableA17

@ 1.79783kJ/kgK TableA17

0.287kJ/kgK TableA1

∆ ln

1.79783 1.66802 kJ/kgK 0.287kJ/kgK ln600kPa100kPa

. /

Page 29: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Examples (textbook)b)  = 100 kPa,  = 17°C,  = 600 kPa,  = 57°C, ∆ = ? Using Table A2b

∆ , ln ln

, @ 1.006kJ/kgK TableA2b interpolation2

17 57 °C2 37°C 273 310K

∆ 1.006kJ/kgK ln57 273 K17 273 K 0.287kJ/kgK ln

600kPa100kPa

. /

Page 30: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Homework 4b

Problems from the textbook (Thermodynamics, Yunus, 8th ed.):• Choose 5 conceptual problems and answer them (those who you consider to provide better understanding to the subject seen in this section)• Chapter 7, problems: 1‐18, 28, 67‐69

• Choose 5 problems and answer them (those who you consider to provide better understanding to the subject seen in this section)• Chapter 7, problems: 19‐27, 29‐58, 70‐98

Page 31: Entropy - ITESM. Entropy.pdf · EXAMPLE 7–1 Entropy Change during an Isothermal Process A piston–cylinder device contains a liquid –vapor ... 2 5= 5 MPa, 6 5= 450°C, 2 6= 1.4

Entropy