water if = 7.70 kJ/kg K, = 25 kPa, using the diagram.
Then find the values of , , and if defined.
water, if = 3400 kJ/kg and = 10 MPa, using the diagram.
Then find the values of , , and if defined
In each diagram, list no more than is needed to construct the
phase, but do list the values of the curves/points.
A Carnot-cycle heat pump uses R-134a as refrigerant. Heat is
absorbed from the outside at -10C. It is delivered to the heated
space at 40C. Assume that the R-134a enters the hot-side heat
exchanger as saturated vapor and exits it as saturated liquid.
Show the cycle in the diagram. List the entry to the hot
side heat exchanger as 1, the exit of it as 2, and so on.
Find the quality of the R-134a at the beginning and end of the
isothermal heat addition process at -10C.
Determine the coefficient of performance for the cycle.
Two kilogram ammonia in a piston/cylinder at 50C, 1000 kPa is
expanded in a reversible isothermal process to 100 kPa.
Construct the initial phase of the ammonia in both the
and diagrams. In each diagram, list no more than is needed
to construct the phase, but do list the values of the
curves/points used.
Add the final state to the diagrams and then draw the process
in them as a fat curve. (A ``curve'' might have straight parts.)
Find the work and heat transfer.
Water in a piston/cylinder at 400C, 2000 kPa is expanded in a
reversible adiabatic process. The specific work is measured to be
415.72 kJ/kg out.
Construct the initial phase of the water in both the and
diagrams. In each diagram, list no more than is needed to
construct the phase, but do list the values of the curves/points
used. Watch it: the temperature of the critical point is
374.1C, less than 400C.
Find a second intensive variable for the final state. Then
use table B.1.2, not B.1.1 to find the saturated value(s) needed
to figure out the phase.
Show the final state, and the process line as a fat curve, in
the two diagrams.
Find the final pressure and temperature.
Hardcovers have in B.1.3 = 2945.21 listed incorrectly as
2045.21.