- #1
Xyius
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Hey everyone, I am doing a problem and I am on the "Properties of Pure substances" chapter of the book. These problems basically involve going to lookup tables and reading the values to use in the problem, so I am hoping I can still get some help even though you might not have the thermodynamic tables to look up. :\
A spring loaded piston-cylinder device is initially filled with 0.2 lbm of an R-134a liquid-vapor mixture whose temperature is -30 degrees Fahrenheit and whose quality is 80%. The spring constant in the spring force relation F=ks is 37 lbf/in, and the piston diameter is 12 inches. The R-134a undergoes a process that increases its volume by 40%. Calculate the final temperature and enthalpy of the R-134a.
[tex]Quality=x=\frac{m_{vapor}}{m_{total}}[/tex]
[tex]v_{avg}=v_{f}+xv_{fg}[/tex]
[tex]m=mass[/tex]
[tex]v=specific volume[/tex]
[tex]v_{g}=Specific volume of the gas[/tex]
[tex]v_{f}=Specific volume of the fluid[/tex]
[tex]v_{fg}=v_{g}-v_{f}[/tex]
Since I am not given the mass of the piston I am assuming I can ignore the weight of it. (I do not know if this is valid or not.) Summing the forces in the y direction I get...
[tex]\sum F_{y}=0=ks-PA[/tex]
[tex]ks=PA[/tex]
[tex]s=\frac{PA}{k}=\frac{9.869(\pi (0.5^2))}{37(12)}=0.017ft[/tex]
NOTE: I had to go to the thermodynamic tables and look under -30 degrees F in "Saturated R-134a" to obtain the saturation pressure of 9.869 psia. I also converted 37 lbf/in to lbf/ft and the 6 inch radius to 0.5 ft.
I do not know what this represents though, or if it helps at all with the problem. I am guessing that this is the distance from the springs equilibrium point.
Another thing I can do is find the mass of the gas and liquid using the definition of quality (x). I get 0.16lbm for the gas and 0.04lbm for the liquid. Again, not sure what good this does me either.
Somehow I believe I need to get to the specific volume of state 2 after it has expanded 40%, and then look this value up in the tables.
Any help would GREATLY be appreciated.
Homework Statement
A spring loaded piston-cylinder device is initially filled with 0.2 lbm of an R-134a liquid-vapor mixture whose temperature is -30 degrees Fahrenheit and whose quality is 80%. The spring constant in the spring force relation F=ks is 37 lbf/in, and the piston diameter is 12 inches. The R-134a undergoes a process that increases its volume by 40%. Calculate the final temperature and enthalpy of the R-134a.
Homework Equations
[tex]Quality=x=\frac{m_{vapor}}{m_{total}}[/tex]
[tex]v_{avg}=v_{f}+xv_{fg}[/tex]
[tex]m=mass[/tex]
[tex]v=specific volume[/tex]
[tex]v_{g}=Specific volume of the gas[/tex]
[tex]v_{f}=Specific volume of the fluid[/tex]
[tex]v_{fg}=v_{g}-v_{f}[/tex]
The Attempt at a Solution
Since I am not given the mass of the piston I am assuming I can ignore the weight of it. (I do not know if this is valid or not.) Summing the forces in the y direction I get...
[tex]\sum F_{y}=0=ks-PA[/tex]
[tex]ks=PA[/tex]
[tex]s=\frac{PA}{k}=\frac{9.869(\pi (0.5^2))}{37(12)}=0.017ft[/tex]
NOTE: I had to go to the thermodynamic tables and look under -30 degrees F in "Saturated R-134a" to obtain the saturation pressure of 9.869 psia. I also converted 37 lbf/in to lbf/ft and the 6 inch radius to 0.5 ft.
I do not know what this represents though, or if it helps at all with the problem. I am guessing that this is the distance from the springs equilibrium point.
Another thing I can do is find the mass of the gas and liquid using the definition of quality (x). I get 0.16lbm for the gas and 0.04lbm for the liquid. Again, not sure what good this does me either.
Somehow I believe I need to get to the specific volume of state 2 after it has expanded 40%, and then look this value up in the tables.
Any help would GREATLY be appreciated.