Irreversibility

17
Irreversibility Physics 313 Professor Lee Carkner Lecture 16

description

Irreversibility. Physics 313 Professor Lee Carkner Lecture 16. Exercise #15 Carnot Engine. Power of engine h = 1 – Q H /Q L h = W/Q H Source temp h = 1 – T L /T H Max refrigerator COP For a Carnot refrigerator operating between the same temperatures: - PowerPoint PPT Presentation

Transcript of Irreversibility

Page 1: Irreversibility

Irreversibility

Physics 313Professor Lee

CarknerLecture 16

Page 2: Irreversibility

Exercise #15 Carnot Engine Power of engine

= 1 – QH/QL

= W/QH

Source temp

= 1 – TL/TH

Max refrigerator COP

For a Carnot refrigerator operating between the same temperatures:

Since K < KC (8.2<9.9), refrigerator is possible

Page 3: Irreversibility

Entropy Entropy (S) defined by heat and

temperature

Total entropy around a closed reversible path is zero

Can write heat in terms of entropy:dQ = T dS

Page 4: Irreversibility

General Irreversibility

Since S = Sf - Si

Sf > Si

This is true only for the sum of all entropies

Since only irreversible processes are possible, Entropy always increases

Page 5: Irreversibility

Reversible Processes Consider a heat exchange between a system

and reservoir at temperature T So:

dSs = +dQ/T

dSr = - dQ/T

For a reversible process the total entropy change of the universe is zero

Page 6: Irreversibility

Irreversible Processes

How do you compute the entropy change for an irreversible process?

What is the change in entropy for specific irreversible processes?

Page 7: Irreversibility

Isothermal W to U

Friction or stirring of a system in contact with a heat reservoir

The only change of entropy is heat Q (=W) absorbed by the reservoir

S = W/T

Page 8: Irreversibility

Adiabatic W to U Friction or stirring of insulated

substance

System will increase in temperature

S = dQ/T = CPdT/T = CPln (Tf/Ti)

Page 9: Irreversibility

Heat Transfer Transferring heat from high to low T

reservoir

For any heat reservoir S = Q/T S for cool reservoir = + Q/TC

Assumes no other changes in any other

system

Page 10: Irreversibility

Free Expansion Gas released into a vacuum

Replace with a reversible isothermal

expansion Thus, (dQ/T) = (nRdV/V)

Note: Entropy increases even though temperature

does not change

Page 11: Irreversibility
Page 12: Irreversibility

Entropy Change of Solids

Solids (and most liquids) are incompressible

We can thus write dQ as CdT and dS as (C/T)dT If we approximate C as being constant with T

Note:

If C is not constant with T, need to know (and be able to integrate) C(T)

Page 13: Irreversibility

General Entropy Changes For fluids that under go a change in T, P or V we

can find the entropy change of the system by finding dQ

For example ideal gas:

dQ = CPdT – VdP

dQ = CVdT + PdV

These hold true for any continuous process involving an ideal gas with constant C

Page 14: Irreversibility

Notes on Entropy Processes can only occur such that S

increases

Entropy is not conserved

The degree of entropy increase indicates the degree of departure from the reversible state

Page 15: Irreversibility
Page 16: Irreversibility

Use of Entropy

How can the second law be used?

Example: total entropy for a refrigerator S (reservoir) = (Q + W) /TH

The sum of all the entropy changes must be greater than zero:

Page 17: Irreversibility

Use of Entropy (cont.)

We can now find an expression for the work:

Thus the smallest value for the work is:

Thus for any substance we can look up S1-

S2 for a given Q and find out the minimum amount of work needed to cool it