lect 6

5
Entropy versible adiabatic can not intersect each other C A B C isotherm RA re two reversible adiabatic and they intersect at B. ersible isotherm. Through AC we can transfer heat to the cycle ABC lic process. From the cycle ABC there is no heat loss but work out p es 2 nd law of thermodynamics. Hence two RA can not intersect each oth p v i f a b RA Rev isotherm Any rev path Through i, f there is a Rev process. We construct two rev adiabatic through i and f, then a rev isothe ab such that: ea under iabf = area under if, First law for if : , Process iabf: = , = p v = Thus any rev path can be substituted by a reversible Zig- zag path, between the same end states, consisting of a rev adiabatic + rev isotherm+ another rev adiabatic.

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Page 1: Lect 6

Entropy

Two reversible adiabatic can not intersect each otherCA

B

C

isotherm

RA

AB and CB are two reversible adiabatic and they intersect at B.AC is a reversible isotherm. Through AC we can transfer heat to the cycle ABC which isA close cyclic process. From the cycle ABC there is no heat loss but work out put. SoThis violates 2nd law of thermodynamics. Hence two RA can not intersect each other.

pv

i

fa b

RA

Rev isothermAny rev path

Through i, f there is aRev process. We constructtwo rev adiabatic throughi and f, then a rev isotherm ab such that:

Area under iabf = area under if,

First law for if : ,

Process iabf:

𝑀𝑖𝑓=π‘€π‘–π‘Žπ‘π‘“ ,π‘ π‘œπ‘žπ‘–π‘“=π‘žπ‘–π‘Žπ‘π‘“

p

v

=

Thus any rev path can be substituted by a reversible Zig-zag path, between the same end states, consisting of a rev adiabatic + rev isotherm+ another rev adiabatic.

Page 2: Lect 6

Clausius theorem

p

v

Any rev cyclic process

RA

Rev isotherm

T1

T2

Lets us consider a smooth close curve which represents a rev cycle. Then we take two Elemental parts from this cycle as shown in the picture (upper part and lower part). The upper part cab represented by an isotherm+ two RA and similarly the lower part of the curve. The upper isotherm is at a temp say T1 and the lower isotherm is at T2. Now this elementary process can be thought of as a Carnot engine which receives heat dq1 at T1 and rejects heat dq2 at T2. So for this elementary cycle Signs of heat transfer then we get . If we add all the elementary cycles such that we cover the entire cyclic process then we get :

dq1

dq2

, hence is called entropy , ds.

R1

R2

a

b,=

Hence entropy is a property, independent of pathSo, or,

Clausius theorem

Page 3: Lect 6

; If then the process is called rev adiabatic and then ds=0Hence s=Const;

T

S

A B

CD

π‘‘π‘ž

π‘‘π‘ž2

RA

AB is a general processEither rev or irreversible,All other processes are rev.

Consider an elemental cycle, as shown in the picture. = heat supplied at,

1βˆ’π‘‘π‘ž2π‘‘π‘žπ‘Žπ‘›π‘¦

≀1βˆ’π‘‘π‘ž2π‘‘π‘žπ‘Ÿπ‘’π‘£

π‘‘π‘ž2π‘‘π‘žπ‘Žπ‘›π‘¦

β‰₯π‘‘π‘ž2π‘‘π‘žπ‘Ÿπ‘’π‘£

π‘‘π‘žπ‘Žπ‘›π‘¦

π‘‘π‘ž2β‰€π‘‘π‘žπ‘Ÿπ‘’π‘£

π‘‘π‘ž2

=

Or,

Or,

Or,

Or,

For a reversible process: For any other process :

For any cyclic process:

, cycle is reversible,, cycle is irreversible and feasible, cycle is impossible

Clausius Inequality

Page 4: Lect 6

Entropy principle

For any process undergone by the system, , if the process is reversible then

For isolated system, dq=0, so,

For irreversible process,

Causes of entropy increase: for a closed system entropy increases due to(a) External interaction, (b) internal irreversibility

𝑑𝑠=𝑑𝑠𝑒π‘₯𝑑+𝑑𝑠𝑖𝑛𝑑 so,

𝑑𝑠𝑑𝑑

=Λ™π‘žπ‘π‘£

𝑇+ ˙𝑠𝑔𝑒𝑛

Entropy change Entropy transfer Entropy generation

dqT𝑠𝑔𝑒𝑛

𝑠2βˆ’π‘ 1

For an open system �̇�𝑖

�̇�˙𝑠𝑔𝑒𝑛

�̇�𝑒

, for steady state

π‘šπ‘– 𝑠𝑖+π‘žπ‘π‘£

𝑇+𝑠𝑔𝑒𝑛=π‘šπ‘’π‘ π‘’+π‘š2𝑠2βˆ’π‘š1 𝑠1 Integral form of the equation

Change of entropy within the CV

system

Page 5: Lect 6

relation

First law and second law combined:

𝑑𝑠=𝑑𝑒𝑇

+𝑝𝑇𝑑𝑣 βˆ«π‘‘π‘ =∫ 𝑑𝑒

𝑇+∫ 𝑅

𝑣𝑑𝑣

π‘‘π‘žπ‘Ÿπ‘’π‘£=𝑇𝑑𝑠

𝑠2βˆ’π‘ 1=βˆ«π‘π‘£π‘‘π‘‡π‘‡

+∫ 𝑅𝑣𝑑𝑣

𝑠2βˆ’π‘ 1=𝑐𝑣 ln (𝑇2

𝑇1)+𝑅 ln( 𝑣2𝑣1 )

1st Tds relation

Only for ideal gases

h=𝑒+𝑝𝑣h𝑑 =𝑑𝑒+𝑝𝑑𝑣+𝑣𝑑𝑝h𝑑 =𝑇𝑑𝑠+𝑣𝑑𝑝

T 2nd Tds relation

𝑑𝑠= hπ‘‘π‘‡βˆ’π‘£π‘‡π‘‘π‘π‘ 2βˆ’π‘ 1=∫

𝑐𝑝𝑑𝑇𝑇

βˆ’βˆ« 𝑅𝑝𝑑𝑝𝑐𝑝 ln (𝑇2

𝑇1)βˆ’π‘… ln(𝑝2𝑝1 )Only for ideal gases