Is what I did in part C correct or should I say the average enthalpy of the withdrawn vapor just be the saturated vapor value at 100 F?
And I'm really confused on finding quality at this point.
I found my internal energy for Tank B by finding my values at state 2.
u = u_f + x(u_g - u_f)
but I need x so I solve quality in state 2 by using saturated volume values at 20 F and solved for specific volume by using V2 = V_a + V_b = 2 meter cubed. I used the mass of the initial tank and since...
in D, i used the formula to find quality using internal energy values and in E I'm wanting to find mass, so I use the volume of the tank divided by the specific volume of the tank at 50 F which I used the same quality formula after I found the quality.
I've attached all my work and data table I used to answer the questions but there isn't an answer key so I would like a second opinion.
a) The initial specific internal energy is.......Btu/lbm
b) The initial mass is....lbm
c)The average enthalpy of the withdrawn vapor is.....Btu/lbm
d)The final...
I understand that when volume change is zero, there is no work done so dU = W. However, how do I know in this process in a piston cylinder, the volume is constant?
I also have one question. If the first law of thermodynamics is dU = Q - W. Why is w positive in this case?