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 ๐๐ ๐ ๐๐ ๐กโ๐๐ ๐๐๐ฃ๐๐๐ ๐๐ฃ๐๐๐ฆ๐กโ๐๐๐ ๐๐ฆ ๐ ๐ ๐ถ๐๐๐ = ๐๐ − ๐ถ๐๐๐ ๐๐ ๐๐ = − ๐๐ ๐ ๐ ๐ ๐ ๐๐๐๐ ๐ ≠ 0, 3๐๐ ๐๐๐ค ๐ถ (๐)๐๐ ๐๐ ๐๐ โฎ ๐ =โฎ −โฎ ๐๐ ๐ ๐ ๐ โฎ ๐๐ ๐ ๐๐๐๐ ๐๐ ๐๐๐ก๐๐๐๐๐ ๐กโ๐ โฎ ๐๐ ๐๐ ๐ก๐๐๐ ๐๐ 0, ๐ ๐๐๐๐ ๐ ๐๐ ๐ ๐ ๐ก๐๐ก๐ ๐๐ข๐๐๐ก๐๐๐ ๐ The closed integral of a product of state functions is 0, like โฎ ๐๐ = 0 โฎ ๐๐๐๐ = 0 ๐ ๐๐๐๐ ๐ ๐๐ ๐ ๐ ๐ก๐๐ก๐ ๐๐ข๐๐๐ก๐๐๐ โฎ ๐ถ๐(๐) ๐2 ๐3 ๐4 ๐1 ๐๐ ๐๐ ๐๐ ๐๐ ๐๐ = ∫ ๐ถ๐(๐) + ∫ ๐ถ๐(๐) + ∫ ๐ถ๐(๐) + ∫ ๐ถ๐(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. ∫ ๐3 ๐2 ๐ถ๐(๐) ๐๐ถ ๐๐ป ๐๐ ๐๐ ๐๐ = ∫ ๐ถ๐(๐) = − ∫ ๐ถ๐(๐) ๐ ๐ ๐ ๐ ๐ ๐ป ๐1 ∫ ๐4 ๐ถ๐(๐) ๐ถ ๐๐ป ๐๐ ๐๐ = ∫ ๐ถ๐(๐) ๐ ๐ ๐ ๐ถ ∴โฎ โฎ ๐๐๐๐๐ฃ =0 ๐ 2 3 4 1 ๐๐๐๐๐ฃ ๐๐ ๐๐ ๐๐ ๐๐ =∫ +∫ +∫ +∫ =0 ๐ 1 ๐๐ป 2 ๐ 3 ๐๐ถ 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 ∫ ๐๐ + ∫ ๐๐ = 0 ๐๐ป 1 ๐๐ถ 3 ๐๐ป ๐๐ถ + =0 ๐๐ป ๐๐ถ ๐๐ถ ๐ =− ๐ถ ๐๐ป ๐๐ป ๐๐๐๐ฃ = |๐ค| ๐๐ป + ๐๐ถ ๐ ๐ = =1+ ๐ถ =1− ๐ถ ๐๐ป ๐๐ป ๐๐ป ๐๐ป ๐ ๐๐๐๐ฃ = 1 − ๐ถ ๐๐ป 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 โU = 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.