Thermodynamics I Chapter 6 Entropy Mohsin Mohd Sies Fakulti Kejuruteraan Mekanikal, Universiti Teknologi Malaysia.

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Presentation transcript:

Thermodynamics I Chapter 6 Entropy Mohsin Mohd Sies Fakulti Kejuruteraan Mekanikal, Universiti Teknologi Malaysia

Entropy (Motivation) The preferred direction implied by the 2 nd Law can be better understood and quantified by the concept of entropy. Entropy quantifies the 2 nd Law and imposes the direction of processes. Here we will study entropy and how processes will proceed only in the direction of increasing entropy.

Clausius Inequality E rev E irrev QHQH QHQH QLQL Q L,irrev W W irrev THTH TLTL Consider two heat engines between the same temperatures

Consider of the whole cycle (a) E rev

(b) E irrev

Combined to be: = 0 if reversible < 0 if irreversible > 0 impossible

ENTROPY 1 2 B A Does not depend on path; thermodynamic property! Let's call this property entropy, S [kJ/K]

Entropy, S = extensive property [kJ/K] Specific entropy, s = intensive property [kJ/kg.K] We have actually defined entropy change From statistical thermodynamics, entropy ~ measure of molecular disorder Work is an ordered form of energy (High quality) No entropy transfer along with work transfer Heat is a disordered form of energy (Low quality) Entropy is transferred along with heat transfer “Entropy = zero for pure crystal at 0 K” Third Law of Thermodynamics Entropy with a 0 K reference is called absolute entropy

T-ds Relations To find the relationship between  Q and T so that the integration of  Q/T can be performed - From the 1 st Law (neglecting KE & PE) (a)

- From the definition of enthalpy From (a) (b)

& Can be used for  S of any process (rev. & irrev.) Can be used for open & closed system T-ds Relations

Entropy Change of Pure Substances Can be obtained from Tds Relations in conjunction with other thermodynamic relations For 2 phase substances like water and R-134a, use property tables  S = S 2 – S 1 For ideal gas, from Tds relations Assume C v =constant & integrate

Another relation, Assume C p =constant & integrate

Both equations give the same result Choose according to available data.. Entropy change

Isentropic Processes,  S = 0 For ideal gases, with constant C p & C v

Another one

Combined to become Isentropic process for ideal gas, constant C p, C v

Work for Open Systems Reversible boundary work for closed systems Open system reversible work, from 1 st Law (single inlet/outlet) Reversible work for open system neglecting ke & pe, & rearrange;

Increase in Entropy Principle For reversible processes, entropy of universe (system surrounding) doesn't change, it is just transferred (along with heat transfer) In real processes, irreversibilities cause entropy of universe to increase Heat reservoirs don't have irreversibility To simplify analysis, assume irreversibilities to exist only inside the system under study. Inside the system, entropy transfer and generation occur. irrev 1 2 rev Irreversible cycle since one of the processes is irreversible From Clausius Inequality;

Rearrange Generalize for all processes = when rev > when irrev < impossible S gen =entropy generated = 0 when rev. > 0 when irrev. < 0 impossible

Change of system entropy Transfer of entropy (T where Q is transferred, usually at boundary Entropy generation Entropy Generation for Closed System

S gen is the measure of irreversibilities involved during process  S surrounding or system may decrease (-ve), but  S total (surrounding + system) must be > 0 Entropy of universe always increases (Entropy increase principle) No such thing as entropy conservation principle For a process to occur, S gen > 0

Entropy Generation for Closed System For multiple heat transfers at different temperatures

In rate form In differential form  S gen - depends on the process (friction,  T etc.) - not a property Entropy Generation for Closed System

Entropy Generation for Open Systems Apart from heat, mass flows also carry entropy along with them Q in m in s in m out s out CV

Rate of change of system entropy Rate of entropy transfer Rate of entropy generation Q in m in s in CV Entropy Generation for Open Systems

Steady Flow Process

single inlet/outlet; Steady Flow Process

Reversible adiabatic process = isentropic process Isentropic is not necessarily reversible adiabatic Reversible process S gen = 0 Produces W max Consumes W min

30 ISENTROPIC EFFICIENCIES OF STEADY-FLOW DEVICES The isentropic process involves no irreversibilities and serves as the ideal process for adiabatic devices. The h-s diagram for the actual and isentropic processes of an adiabatic turbine. Isentropic Efficiency of Turbines Also known as Adiabatic Efficiency or 2 nd Law Efficiency

31 Isentropic Efficiencies of Compressors and Pumps The h-s diagram of the actual and isentropic processes of an adiabatic compressor. Compressors are sometimes intentionally cooled to minimize the work input. When kinetic and potential energies are negligible

32 Isentropic Efficiency of Nozzles The h-s diagram of the actual and isentropic processes of an adiabatic nozzle. If the inlet velocity of the fluid is small relative to the exit velocity, the energy balance is Then, A substance leaves actual nozzles at a higher temperature (thus a lower velocity) as a result of friction.