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Efficiency of an ideal-gas cycle. |
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| Oct10-10, 11:22 PM | #1 |
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Efficiency of an ideal-gas cycle.
1. The problem statement, all variables and given/known data
A possible ideal-gas cycle operates as follows: (i) from an initial state (p1,V1) the gas is cooled at constant pressure to (p1,V2); (ii) the gas is heated at constant volume to (p2,V2); (iii) the gas expands adiabatically back to (p1,V1). Assuming constant heat capacities, show that the thermal eficiency is: 1-ɣ[((V1/V2) - 1) / ((p2/p1) -1)] 2. Relevant equations I used first law of thermal dynamics, n = W/Qh, differential forms of Cv and Cp. change in energy for the complete cycle = 0, therefor W = Qh + Ql. 3. The attempt at a solution Using efficiency = W / heat absorbed. I attempted to find the W and Q of the 3 processes separately. I was using for Isobaric: dW = -Pdv but im pretty sure this is incorrect because no where does it state it is a reversible process. But the book for the class only shows reversible processes for examples and does not actually show a isobaric or isochoric process in any example. I tried using the differential form of Cv and Cp and rearranging them to find dQ, but failed. I have used 4 or 5 sheets of paper, trying every way i could think of to work this problem out. I know im missing something and if someone could just point me in the right direction I would gladly appreciate it and work out the problem on my own. Thanks |
| Oct10-10, 11:35 PM | #2 |
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Welcome to Physics Forums.
You'll also need Q for one leg of the cycle (do you know which leg that is?). |
| Oct10-10, 11:56 PM | #3 |
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Using Qh for heat absorbed and Ql for heat lost I was using the equation as:
n = w/Qh = (Qh +Ql)/Qh = 1 + Ql/Qh. Ql being from (i) and Qh being from (ii). Q = 0 from (iii). Qh = ∫Cv dT Ql = ∫Cp dt + ∫pdV For adiabatic ΔQ = 0 so ΔU = W. Since, you are ending where you started ΔU for the complete cycle should = 0 correct? so ΔU for adiabatic should equal ΔU for isochoric + isobaric. Isobaric: ΔU = Ql + pdV Isochoric: ΔU = Qh ΔU for adiabatic = Ql + Qh - ∫pdV. ΔU = W so W = Ql + Qh - ∫pdV and now i lost myself. Maybe i just need some sleep. Thanks for trying. |
| Oct11-10, 09:24 AM | #4 |
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Efficiency of an ideal-gas cycle.I stated that I wasnt sure how to relate the change in T to p and V, but I forgot about the ideal gas equation. So I just solved for Q's like before and put in pV/R in place of T. Doing that I ended up with n = Qin - Qout / Qin dQin = Cv/R(Vdp + pdV) and pdV = 0 dQout = Cp/R(Vdp + pdV) and Vdp = 0 n = Cv(V2(p2-p1)) - Cp(p1(V2-V1)) / Cv(V2(p2-p1)) because R's cancel out. n = 1 + (-Cp/Cv) *((V2-V1)/V2) * (p1(p2-p1)) sub in ɣ for Cp/Cv and clean up the rest and that shows that n = 1+ɣ[((V1/V2) - 1) / ((p2/p1) -1)] It is very close, only missing a - sign. I am not sure If i did a calculation wrong or that it is purely coincidental that I got this close. Now that part that scares me and why I didnt do this in the beginning is that I complete ignore the adiabatic leg, and all work done. I just simple used heat. It is close to the right answer but I am not convinced I did it correctly. Thanks for your help so far. |
| Oct11-10, 11:12 AM | #5 |
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Recognitions:
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If you are using 1 - Qout/Qin for efficiency you have to take the absolute value of Qout: [tex]|Q_{out}| = C_pP_1(V_1 - V_2)[/tex] That is where you got the signs mixed up. AM |
| Oct11-10, 11:31 AM | #6 |
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thanks, that makes me feel better.
can you explain to me exactly why we take the absolute value? Just so i can understand it and apply it to future problems. thanks again. I think I understand. Work is actually equal to the sum of the heat. By me stating Qin - Qout I am taking the negative out of Qout already. To do it the way I did I should have used n = (Qin + Qout)/ Qin |
| Oct11-10, 03:22 PM | #7 |
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Recognitions:
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AM |
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