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Applying the Energy BalanceA rigid, well-insulated tank
Chapter 3, Problem 64P(choose chapter or problem)
A rigid, well-insulated tank contains a two-phase mixture of ammonia with \(0.0025 \mathrm{ft}^3\) of saturated liquid and \(1.5 \mathrm{ft}^3\) of saturated vapor, initially at \(40 \mathrm{lbf} / \mathrm{in}^2\) A paddle wheel stirs the mixture until only saturated vapor at higher pressure remains in the tank. Kinetic and potential energy effects are negligible. For the ammonia, determine the amount of energy transfer by work, in Btu.
Questions & Answers
QUESTION:
A rigid, well-insulated tank contains a two-phase mixture of ammonia with \(0.0025 \mathrm{ft}^3\) of saturated liquid and \(1.5 \mathrm{ft}^3\) of saturated vapor, initially at \(40 \mathrm{lbf} / \mathrm{in}^2\) A paddle wheel stirs the mixture until only saturated vapor at higher pressure remains in the tank. Kinetic and potential energy effects are negligible. For the ammonia, determine the amount of energy transfer by work, in Btu.
ANSWER:Step 1 of 3
We have to determine the energy transfer by work in stirring the two-phase mixture of ammonia until only saturated vapor at higher pressure remains in the tank.
The energy transfer by work can be determined using the expression,
where, and account, for the transfer of energy by heat and work
between the system and its surroundings during the process
respectively.
accounts for change in internal energy between
the end states.
Since it is insulated there is no exchange of heat.
Thus,
where,
is the internal energy of the mixture before the stirring and it is given by
where, and are the masses of saturated
liquid and vapour ammonia respectively in kg
and are the internal energies of saturated
liquid and vapour ammonia in kJ
and is internal energy of the mixture after the stirring and it is given by
Now, both the phases of saturated ammonia are at a constant pressure of 40 lbf/in2 or 2.75 bar.
By referring to the table A-14 in the book Fundamentals of Engineering Thermodynamics, 7th Edition. We have the values for and at a constant pressure of 2.75 bar as
m3/kg , 0.4408 m3/kg , 127.26 kJ/kg and 1307.67 kJ/kg