Lecture 8 - Entropy Flashcards

1
Q

What is the Clausius inequality?

A

∮ δQ/T <= 0

where ∮ = cyclic or closed integral

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2
Q

Entropy is derived from the Clausius inequality.

A

True

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3
Q

What is the definition of entropy?

A

dS = (δQ/T)internally reversible

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4
Q

Entropy is tabulated for steam and R134a. We can also calculate the entropy of ideal gases like we did for internal energy, u, and enthalpy, h.

A

True

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5
Q

Entropy generation is …

A

An quantitative measure of the irreversibilities associated with a process

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6
Q

What is an isentropic process?

A

An adiabatic, internally reversible process where there is no entropy change of the system

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7
Q

If δQ = 0, we have a ….

A

an isentropic process, so dS = 0 as well

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8
Q

Isentropic processes are idealizations for the best case scenarios for different types of processes.

A

True

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9
Q

Our base/reference state for entropy, internal energy, or enthalpy is …

A

S, U, or H = 0 at 0K

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10
Q

Entropy quantifies the transfer of the different forms of energy into random forms of energy, for example vibrational, kinetic energy of molecules, etc…

A

True

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11
Q

Examples of entropy generation are …

A
  • mechanical friction
  • viscous dissipation
  • mixing of 2 fluids
  • chemical reactions
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12
Q

In mechanical friction, …

A

work is being converted into random thermal energy within the system

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13
Q

What is viscous dissipation?

A

The process whereby velocity shear/ differentials within a fluid are converted through viscosity and friction in the fluid into thermal energy

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14
Q

An example of entropy generation is viscous dissipation. An example of viscous dissipation is pressure drop in pipe flow. Explain.

A

Pressure is a form of mechanical energy. Since there is velocity shear within the pipe flow, the velocity shear becomes thermal energy, which causes the pressure to drop.

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15
Q

Entropy increases in the mixing of two fluids and in chemical reactions because …

A

it is difficult to take the resulting thermal energy or the final state and get back the original state

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16
Q

When calculating entropy, we can use a differential form of the first law applied to a closed stationary system.

The entropy of a closed stationary system is …

A

δQ - δW(int rev)out = dU + dKE + dPE

BUT if the system is stationary, δKE and δPE are 0.
THEREFORE:
δQ - δW = dU

if there is no other type of work, we have:

δQ - δWb = dU
TdS - PdV = dU
where the elements are not per unit mass

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17
Q

What is the first Gibb’s equation?

A

TdS - PdV = dU

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18
Q

Define enthalpy.

A

h = u + Pv

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19
Q

Define flow work.

A

flow work = boundary work = pdv

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20
Q

h = u + Pv

Appropriately apply the product rule to the above.

A

dh = du + Pdv + vdP

21
Q

If we substitute dh = du + Pdv + vdP into the first gibb’s equation, we get …

A
First Gibb's equation (per unit mass):
Tds - Pdv = du
Substituting:
Tds = du + Pdv
Tds = dh - vdP

WE GET THE SECOND GIBB’S EQUATION:
Tds = dh - vdP

22
Q

State Gibb’s Second Equation.

A

Tds = dh - vdP

23
Q

If we divide the first gibb’s equation or the second gibb’s equation by T, we get …

A

Gibb’s Second Equation:
Tds = dh - vdP / T
ds = dh/T - vdP/T

Gibb’s First Equation:
TdS - PdV = dU / T
dS - PdV/T = dU/T

24
Q

If we integrate Gibb’s First or Second law (divided by temperature:

ds = dh/T - vdP/T or ds - Pdv/T = du/T, between two end state, we get …

A

the change in entropy between two states irrespective or reversibility

25
Q

Determination of properties depend on …

A

the path to get from one state to another and not the end states

26
Q

Liquids and solids are in/compressible.

A

incompressible

27
Q

Because liquids and solids are incompressible, …

A

we can approximate the entropy.

28
Q

For liquids and solids, dv = …

A

dv = 0 because liquids ans solids are incompressible

29
Q

du =

A

CvdT

30
Q

For liquids and solids, the relation between Cv and Cp is …

A

Cv = Cp = cte

assume volume expansion/ compression is negligible for liquids

31
Q

For a liquid or a solid, ds =

A

ds = du/T + pdv/T
where pdv = 0, so

ds = du/T
ds = CdT/T
ds = C(T)dT/T

where C is a constant of temperature

INTEGRATING, WE GET

T(s2-s1) = C(T) * ln(T2-T1)

where we can approximate the specific heat as Cv(avg)

32
Q

When we have C(T), we can approximate it as the average specific heat. If we don’t we ..

A

need to know how the specific changes with the solid or liquid

33
Q

If we are dealing with an isentropic process, ds = 0, which implies that the temperature …

A

remains the same

T2 = T1

34
Q

Define enthalpy.

A

dh = Cp*dT

35
Q

If ds = du/T + Pdv/T, if we substitute du for the definition of internal energy and the definition of pressure, according to the ideal gas equation, we get …

A

ds = CvdT/T + RTdv/vT

ds = Cv*dt/T + Rdv/v

36
Q

If ds = dh/T - vdP/T, if we substitute dh for the definition of enthalpy and the definition of volume, according to the ideal gas equation, we get …

A

ds = Cp*dT/T - RTdP/PT

ds = Cp*dT/T - RdP/P

37
Q

How do find the entropy change between two states for an ideal gas?

A

By integrating

ds = Cvdt/T + Rdv/v or ds = CpdT/T - RdP/P

38
Q

If we integrate ds = CpdT/T - RdP/P or ds = Cvdt/T + Rdv/v, we get …

A

s2 - s1 = Cv(T) * ln(T2 - T1) + R * ln(v2 - v1)

s2 - s1 = Cp(T) * ln(T2 - T1) - R * ln(P2 - P1)

39
Q

Cv (T) = Cv(avg) and Cp(T) = Cp(avg) when …

A

we have constant specific heats like for a solid or liquid or for ideal gases like He, Ar, or N2

OR

when we assume the temperature change is relatively small (by about 200 K)

40
Q

For more accurate specific heat values, we use tables of …

A

s^0 = 0∫T Cp(T) dT/T

41
Q

s^0 means …

A

we integrate the entropy from 0 to some temperature in Kelvin

42
Q

To calculate an exact form of entropy change using the tables at the back of a thermodynamics textbook we do …

A

s2 - s1 = s2^0 - s1^0 - R*ln(P2-P1)

43
Q

In an isentropic process for an ideal gas, we can say about the entropy that …

A

s2 = s1

44
Q

Assuming constant specific heats for an isentropic process, we can say, from the equations of entropy change, that ln(T2/T1) = …

A

ln(T2/T1) = -R/Cv * ln(v2/v1)

Or

ln(T2/T1) = R/Cp * ln(P2/P1)

45
Q

k or ᴕ =

The gas constant, R =

A

ᴕ = Cp/Cv

R = Cp - Cv

46
Q

s^0 = 0∫T Cp(T) dT/T = Cp(T) * ln(T2 - T1)

A

True

47
Q

For isentropic processes of ideal gases, we can say that Tv^(k-1) = cte, TP^(1-k2/k1) = cte, and and Pv^k = cte

A

True

48
Q

We use Tv^(k-1) = cte, TP^(1-k2/k1) = cte, and and Pv^k = cte under the assumption that …

A

the process takes place under constant specific heat and so the change in temperature is not that high

49
Q

If you cannot assume constant specific heat, use …

A

the tables at the back of your textbook to find the relative pressure, Pr, and the relative specific volume, vr