October 17, 2012

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Week 4 Wednesday October 17, 2012 page 1
Carnot’s principle: e≤erev
e is real engine
Increase efficiency of real engines:
๏‚ท
๏‚ท
Lubricate the moving parts
Less parts
Couple 2 reversible engines: Reversible engine A operates off hot reservoir at temperature τH, sends
some heat to cold reservoir at temperature τC, and provides work to operate reversible engine B.
Reversible engine B is provided with work from reversible engine A to pump heat from the cold reservoir
to the hot reservoir. erev(A)≤erev(B). If we reverse engines A and B, then erev(B)≤erev(A). Therefore,
erev(A)=erev(B).
Conclusions:
1. All reversible heat engines operating between the same two temperatures must have the same
efficiency.
2. The efficiency of a reversible engine is the maximum efficiency possible for any heat engine the
operates between these two temperatures.
eirrev≤erev
erev is theoretical
This is true even if work isn’t PV work.
Calculation of reversible e (erev)
erev = f(τH,τC)
(any temperature scale)
thermodynamics uses ideal gas scale (fictitious)
τ C = TC
τ H = TH
T is ideal gas temperature scale
Carnot cycles: States 1,2,3,4 on PV diagram.
Step 1 to 2 is isothermal expansion (doing work).
Step 2 to 3 is adiabatic expansion (T will change).
Step 3 to 4 is isothermal compression.
Step 4 to 1 is adiabatic compression.
q1-2 is not necessarily the same as q3-4
Carnot cycle: 2 adiabats and 2 isotherms, all 4 steps reversible
Assumptions: P-V work only, perfect gas
1st law: dU = dq + dw = dq – PdV since dw = -PdV for a reversible process
dU = CVdT
CVdT = dq – PdV
๐‘›๐‘…๐‘‡
๐‘‘๐‘‰ ๐‘กโ„Ž๐‘’๐‘› ๐‘‘๐‘–๐‘ฃ๐‘–๐‘‘๐‘’ ๐‘’๐‘ฃ๐‘’๐‘Ÿ๐‘ฆ๐‘กโ„Ž๐‘–๐‘›๐‘” ๐‘๐‘ฆ ๐‘‡
๐‘‰
๐ถ๐‘‰๐‘‘๐‘‡ = ๐‘‘๐‘ž −
๐ถ๐‘‰๐‘‘๐‘‡ ๐‘‘๐‘ž ๐‘›๐‘…
=
−
๐‘‘๐‘‰
๐‘‡
๐‘‡
๐‘‰
๐‘ ๐‘–๐‘›๐‘๐‘’ ๐‘‡ ≠ 0, 3๐‘Ÿ๐‘‘ ๐‘™๐‘Ž๐‘ค
๐ถ (๐‘‡)๐‘‘๐‘‡
๐‘‘๐‘ž
๐‘›๐‘…
โˆฎ ๐‘‰
=โˆฎ
−โˆฎ
๐‘‘๐‘‰
๐‘‡
๐‘‡
๐‘‰
โˆฎ
๐‘–๐‘  ๐‘Ž ๐‘๐‘™๐‘œ๐‘ ๐‘’๐‘‘ ๐‘–๐‘›๐‘ก๐‘’๐‘”๐‘Ÿ๐‘Ž๐‘™
๐‘กโ„Ž๐‘’ โˆฎ
๐‘›๐‘…
๐‘‘๐‘‰ ๐‘ก๐‘’๐‘Ÿ๐‘š ๐‘–๐‘  0, ๐‘ ๐‘–๐‘›๐‘๐‘’ ๐‘‰ ๐‘–๐‘  ๐‘Ž ๐‘ ๐‘ก๐‘Ž๐‘ก๐‘’ ๐‘“๐‘ข๐‘›๐‘๐‘ก๐‘–๐‘œ๐‘›
๐‘‰
The closed integral of a product of state functions is 0, like โˆฎ ๐‘ƒ๐‘‰ = 0
โˆฎ ๐‘‘๐‘™๐‘›๐‘‰ = 0 ๐‘ ๐‘–๐‘›๐‘๐‘’ ๐‘‰ ๐‘–๐‘  ๐‘Ž ๐‘ ๐‘ก๐‘Ž๐‘ก๐‘’ ๐‘“๐‘ข๐‘›๐‘๐‘ก๐‘–๐‘œ๐‘›
โˆฎ ๐ถ๐‘‰(๐‘‡)
๐‘‡2
๐‘‡3
๐‘‡4
๐‘‡1
๐‘‘๐‘‡
๐‘‘๐‘‡
๐‘‘๐‘‡
๐‘‘๐‘‡
๐‘‘๐‘‡
= ∫ ๐ถ๐‘‰(๐‘‡)
+ ∫ ๐ถ๐‘‰(๐‘‡)
+ ∫ ๐ถ๐‘‰(๐‘‡)
+ ∫ ๐ถ๐‘‰(๐‘‡)
๐‘‡
๐‘‡
๐‘‡
๐‘‡
๐‘‡
๐‘‡
๐‘‡
๐‘‡
๐‘‡
1
2
3
4
The T1 to T2 term = 0 since it’s isothermal. The T3 to T4 term = 0 since it’s isothermal.
∫
๐‘‡3
๐‘‡2
๐ถ๐‘‰(๐‘‡)
๐‘‡๐ถ
๐‘‡๐ป
๐‘‘๐‘‡
๐‘‘๐‘‡
๐‘‘๐‘‡
= ∫ ๐ถ๐‘‰(๐‘‡)
= − ∫ ๐ถ๐‘‰(๐‘‡)
๐‘‡
๐‘‡
๐‘‡
๐‘‡
๐‘‡
๐ป
๐‘‡1
∫
๐‘‡4
๐ถ๐‘‰(๐‘‡)
๐ถ
๐‘‡๐ป
๐‘‘๐‘‡
๐‘‘๐‘‡
= ∫ ๐ถ๐‘‰(๐‘‡)
๐‘‡
๐‘‡
๐‘‡
๐ถ
∴โˆฎ
โˆฎ
๐‘‘๐‘ž๐‘Ÿ๐‘’๐‘ฃ
=0
๐‘‡
2
3
4
1
๐‘‘๐‘ž๐‘Ÿ๐‘’๐‘ฃ
๐‘‘๐‘ž
๐‘‘๐‘ž
๐‘‘๐‘ž
๐‘‘๐‘ž
=∫
+∫
+∫
+∫
=0
๐‘‡
1 ๐‘‡๐ป
2 ๐‘‡
3 ๐‘‡๐ถ
4 ๐‘‡
The state 2 to 3 term = 0 since it’s adiabatic. The state 4 to 1 term = 0 since it’s adiabatic.
1 2
1 4
∫ ๐‘‘๐‘ž +
∫ ๐‘‘๐‘ž = 0
๐‘‡๐ป 1
๐‘‡๐ถ 3
๐‘ž๐ป ๐‘ž๐ถ
+
=0
๐‘‡๐ป ๐‘‡๐ถ
๐‘ž๐ถ
๐‘‡
=− ๐ถ
๐‘ž๐ป
๐‘‡๐ป
๐‘’๐‘Ÿ๐‘’๐‘ฃ =
|๐‘ค| ๐‘ž๐ป + ๐‘ž๐ถ
๐‘ž
๐‘‡
=
=1+ ๐ถ =1− ๐ถ
๐‘ž๐ป
๐‘ž๐ป
๐‘ž๐ป
๐‘‡๐ป
๐‘‡
๐‘’๐‘Ÿ๐‘’๐‘ฃ = 1 − ๐ถ
๐‘‡๐ป
That formula is true for any working substance. It shows that a higher TH will make the process more
efficient. It shows that a lower TC will make the process more efficient.
The cyclic integral equaling 0 means that it’s a state function.
Arbitrary cycle on a PV diagram:
Let a and b be points on the cycle near each other. Let m be a point on the same reversible adiabat as
point a and point n be a point on the same reversible adiabat as point b such that m and n are on the
same reversible isotherm. Let c be the point on the cycle that is also on the same reversible adiabat as
point a. Let d be the point on the cycle that is on the same reversible adiabat as point b. Let point r be a
point on the same reversible adiabat as point c and point s be on the same reversible adiabat as point d
such that r and s are on the same isotherm.
Notice that the area from points a and m to the point where curve ab intersects curve mn is the same
area from points b and n to the point where curve ab instersects curve mn. This means that the area
under path amnb is equal to the area under path ab. The area amnb is thus the reversible work done on
the system. Likewise, the area under ab is also the reversible work done on the system.
wamnb = wab
โˆ†U = q + w and qam = 0 since am is an adiabat
qbn = 0 since bn is an adiabat
qamnb = qmn = qab
qrs = qcd
The cycle is mnsr back to m.
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