Thermodynamics for Mechanical Engineering Problem

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SUMMARY

The discussion centers on a thermodynamics problem involving a closed, rigid tank containing a two-phase liquid-vapor mixture of Refrigerant 22 at an initial temperature of -20°C and a quality of 50.36%. The final pressure is given as 6 bar, and the objective is to determine the final temperature and assess whether the refrigerant transitions to a superheated vapor state. Participants clarified that the specific volume remains constant due to the rigid nature of the tank, and linear interpolation is a valid method for finding the final temperature based on reference tables.

PREREQUISITES
  • Understanding of thermodynamic properties of refrigerants, specifically Refrigerant 22.
  • Familiarity with the concepts of quality and specific volume in phase change processes.
  • Ability to use thermodynamic reference tables for calculations.
  • Knowledge of linear interpolation techniques for estimating thermodynamic properties.
NEXT STEPS
  • Study the properties of Refrigerant 22 in detail, focusing on phase change behavior.
  • Learn how to utilize thermodynamic reference tables effectively for various refrigerants.
  • Explore the concept of specific volume in rigid tanks and its implications in thermodynamic processes.
  • Investigate methods for determining superheated vapor states in thermodynamic systems.
USEFUL FOR

This discussion is beneficial for mechanical engineering students, thermodynamics practitioners, and anyone involved in HVAC systems or refrigeration technology, particularly those working with Refrigerant 22.

Mi77
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Homework Statement


A closed, rigid tank contains a two-phase liquid-vapor mixture of Refrigerant 22 initially at -20 C with a quality of 50.36%. Energy transfer by heat into the tank occurs until the refrigerant is at a final pressure of 6 bar. Determine the final temperature. If the final state is in the superheated vapor region, at what temperature does the tank contain only saturated vapor?

Homework Equations


v = vf + x(vg-vf)

The Attempt at a Solution


Ok so there are two states in this problem. since I have T1 & x=.5036
I looked at the reference tables in the back of my book and used vf, vg, and x to compute v ( v being specific volume). my computed v :: vf<v<vg which makes since because the ref. 22 is in the two-phase liq-vap region.
Since it is being heated , v and T are increasing correct?
I don't know what to do from here.
since P2 is given, I just assumed at P2 it will be in super-heated vapor state and used linear interpolation to find T using v i found from the initial state and the surrounding T's and v's from the table. but I'm pretty sure that is wrong because v is supposed to increase. Really don't know what I'm doing.
 
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How can v increase when the container is rigid? You're assuming specific volume = 1, a fixed number.
 
Mi77 said:
since P2 is given, I just assumed at P2 it will be in super-heated vapor state and used linear interpolation to find T using v i found from the initial state and the surrounding T's and v's from the table. but I'm pretty sure that is wrong because v is supposed to increase. Really don't know what I'm doing.
You did it correctly. The combined volume per unit mass doesn't change, because the tank is rigid. So v doesn't change.

So, now what is your game plan for doing the second part?

Chet
 

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