Ammonia Rankine cycle heat engine calculation

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Homework Help Overview

The discussion revolves around a Rankine Cycle heat engine utilizing ammonia as the working fluid. The original poster presents a scenario with specific pressures and temperatures, seeking to determine the outlet temperature and mass flow rate required for a specified power output.

Discussion Character

  • Exploratory, Assumption checking, Problem interpretation

Approaches and Questions Raised

  • Participants discuss the relevance of the equations used and the availability of thermodynamic data for ammonia. There are inquiries about the correctness of the original poster's approach and the need for confirmation of calculations.

Discussion Status

The discussion is ongoing, with participants exploring different interpretations of the problem. Some have provided guidance on the use of thermodynamic tables and diagrams, while others are questioning the assumptions made in the analysis.

Contextual Notes

There is mention of the original poster's background and intent, indicating a desire for validation rather than formal educational assistance. The discussion also highlights potential constraints related to the availability of thermodynamic resources.

Biodelta
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Homework Statement
A Rankine Cycle heat engine uses ammonia as a working fluid, turbine entry temperature is 25 Bar at 60 degrees Celsius.

The turbine outlet pressure is 4 Bar, the question is: what is the outlet temperature? and if the output power is 6 Gigawatt (6x10^9 watt) what would the mass flow rate of the ammonia need to be for 6 Gigawatt? output
Relevant Equations
U = Q-W
A Rankine Cycle heat engine uses ammonia as a working fluid, turbine entry temperature is 25 Bar at 60 degrees Celsius.

The turbine outlet pressure is 4 Bar, the question is: what is the outlet temperature? and if the output power is 6 Gigawatt (6x10^9 watt) what would the mass flow rate of the ammonia need to be for 6 Gigawatt? output
 
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What are your thoughts on this so far? What other information/data do you have available? Do you really feel that the Relevant Equation that you listed is the correct one to use?
 
My first approach to solving this has been to use: H'mmm cut and paste from word does not work, I will create a PDF and send that, Regards Stuart, back in a few hours
 
Hello, Attached is my solution which I am looking for confirmation of, it is in PDF attachment.
Thanks for considering this matter.
Regards
Stuart
 

Attachments

Did you not have access to thermodynamic tables on ammonia (analogous to the steam tables) or to a pressure-enthalpy diagram for ammonia like this one: http://industrialheatpumps.nl/en/how_it_works/thermodynamic_cycle/
 
Thanks for that, I am a 67 year old retiree / inventor, and just wanted to get a few questions answered, I am not a student except for a few ideas I have. So my real question is how did the calculation stack up? is it valid? I am just looking at plug and play for this. I am also prepared to pay for a professional opinion.
Cheers
Stuart
 
Biodelta said:
Thanks for that, I am a 67 year old retiree / inventor, and just wanted to get a few questions answered, I am not a student except for a few ideas I have. So my real question is how did the calculation stack up? is it valid? I am just looking at plug and play for this. I am also prepared to pay for a professional opinion.
Cheers
Stuart
The p-H diagram shows that some of the ammonia will condense in the turbine. So your analysis is not correct. You can get your answer however using the p-H diagram.
 

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