Carnot cycle - Zero Power Extremes

Click For Summary
SUMMARY

The discussion centers on the Carnot cycle's maximum power output, referencing a paper that outlines two extremes of operation. To achieve maximum efficiency, the system's temperature must remain infinitesimally close to thermal equilibrium with its reservoirs during isothermal expansion, allowing for slow heat transfer. Conversely, if the system temperature remains constant during isothermal processes, all heat transfers directly from the hot sink to the cold sink, resulting in zero power output. The participants clarify the implications of irreversible cycles and finite temperature differences between the working fluid and reservoirs, emphasizing that no net work is done under these conditions.

PREREQUISITES
  • Understanding of the Carnot cycle and its components
  • Knowledge of thermodynamic principles, specifically isothermal and isentropic processes
  • Familiarity with heat transfer concepts and equations
  • Basic grasp of thermal equilibrium and temperature differentials
NEXT STEPS
  • Study the implications of irreversible processes in thermodynamics
  • Explore the mathematical modeling of heat transfer rates in thermodynamic cycles
  • Investigate the impact of temperature differentials on efficiency in heat engines
  • Learn about the practical applications of the Carnot cycle in real-world systems
USEFUL FOR

Students of thermodynamics, engineers designing heat engines, and researchers interested in optimizing thermal efficiency in energy systems.

Joshua Pham
Messages
14
Reaction score
0
Hey guys,
I ran into this paper talking about the Maximum power you can obtain from a Carnot cycle: http://aapt.scitation.org/doi/abs/10.1119/1.10023 From what I understood, there are two extremes. To achieve maximum efficiency you have to make sure that the temperature of the system is never more than infinitesmally out of thermal equilibrium with its thermal reservoirs. So during the isothermal expansion, you have heat transfer coming in albeit at a very slow rate because of the negligible temperature difference between the hot reservoir and the system. It then isentropically expands to its low temperature which is infinitesmally higher than the cold reservoir and you get heat transfer out.

The other extreme is when you set the system temperature so that it does not change during the isothermal processes. From the paper this leads to all of the heat going straight from the hot sink to the cold sink and 0 power output. I don't quite understand this bit. Why does all of the heat go straight from the hot to cold sink?
 
Engineering news on Phys.org
Joshua Pham said:
Hey guys,
I ran into this paper talking about the Maximum power you can obtain from a Carnot cycle: http://aapt.scitation.org/doi/abs/10.1119/1.10023 From what I understood, there are two extremes. To achieve maximum efficiency you have to make sure that the temperature of the system is never more than infinitesmally out of thermal equilibrium with its thermal reservoirs. So during the isothermal expansion, you have heat transfer coming in albeit at a very slow rate because of the negligible temperature difference between the hot reservoir and the system. It then isentropically expands to its low temperature which is infinitesmally higher than the cold reservoir and you get heat transfer out.

The other extreme is when you set the system temperature so that it does not change during the isothermal processes. From the paper this leads to all of the heat going straight from the hot sink to the cold sink and 0 power output. I don't quite understand this bit. Why does all of the heat go straight from the hot to cold sink?
Did you mean "during the isentropic process" rather than "during the isothermal process" in the last paragraph?
 
Chestermiller said:
Did you mean "during the isentropic process" rather than "during the isothermal process" in the last paragraph?

No the paper says isothermal processes. I'm still trying to decipher what this means.
 

Attachments

  • Capture.PNG
    Capture.PNG
    33.6 KB · Views: 496
The author is talking about carrying out the cycle irreversibly, so that there is a finite temperature difference between the working fluid and the hot reservoir, and an equal finite temperature difference between the working fluid and the cold reservoir (so that, in both isothermal steps of the cycle, the working fluid is half way between the hot reservoir and the cold reservoir temperature). Under these circumstances, the heat transferred from the hot reservoir to the working fluid is equal to the heat transferred from the working fluid to the cold reservoir. So, no net work is done, and the net effect is a transfer of heat from the hot reservoir to the cold reservoir.
 
Chestermiller said:
The author is talking about carrying out the cycle irreversibly, so that there is a finite temperature difference between the working fluid and the hot reservoir, and an equal finite temperature difference between the working fluid and the cold reservoir (so that, in both isothermal steps of the cycle, the working fluid is half way between the hot reservoir and the cold reservoir temperature). Under these circumstances, the heat transferred from the hot reservoir to the working fluid is equal to the heat transferred from the working fluid to the cold reservoir. So, no net work is done, and the net effect is a transfer of heat from the hot reservoir to the cold reservoir.

Thanks Chestermiller! My lecturer actually drew a picture like this when he attempted to explain it. Where THC and TLC are the high and low temperatures of the system respectively. "To maximise the heat transfer rate in, let THC = TLC. But then Qin = Qout." I don't really understand this statement and I'm still struggling to understand what the paper is saying :frown:
 

Attachments

  • Capture.PNG
    Capture.PNG
    2.5 KB · Views: 549
The heat transfer rate into the working fluid during the expansion is ##k(T_H-T_{HC})## where k is a constant of proportionality; the heat transfer rate out of the working fluid during the compression is ##k(T_{LC}-T_C)##. If ##T_{HC}=T_{LC}=\frac{(T_H+T_C)}{2}##, then ##Q_H=Q_C## and ##W=Q_H-Q_C=0##
 
  • Like
Likes   Reactions: Joshua Pham
Chestermiller said:
The heat transfer rate into the working fluid during the expansion is ##k(T_H-T_{HC})## where k is a constant of proportionality; the heat transfer rate out of the working fluid during the compression is ##k(T_{LC}-T_C)##. If ##T_{HC}=T_{LC}=\frac{(T_H+T_C)}{2}##, then ##Q_H=Q_C## and ##W=Q_H-Q_C=0##

Starting to become clearer. How did you obtain ##T_{LC} = \frac{(T_H + T_C)}{2}## though?
 
Joshua Pham said:
Starting to become clearer. How did you obtain ##T_{LC} = \frac{(T_H + T_C)}{2}## though?
I just assumed the expansion and compression temperatures are the same, and half way between the hot and cold reservoir temperatures, for illustrative purposes.
 
  • Like
Likes   Reactions: Joshua Pham

Similar threads

  • · Replies 2 ·
Replies
2
Views
4K
  • · Replies 67 ·
3
Replies
67
Views
7K
  • · Replies 1 ·
Replies
1
Views
2K
Replies
2
Views
2K
Replies
14
Views
2K
  • · Replies 5 ·
Replies
5
Views
2K
  • · Replies 6 ·
Replies
6
Views
2K
  • · Replies 5 ·
Replies
5
Views
3K
Replies
14
Views
2K
  • · Replies 8 ·
Replies
8
Views
14K