Chapter 5 | 251
(b) Noting that the microscopic energies of flowing and nonflowing fluids are
represented by enthalpy hand internal energy u, respectively, the mass and
energy balances for this uniform-flow system can be expressed as
Mass balance:
Energy balance:
Net energy transfer Change in internal, kinetic,
by heat, work, and mass potential, etc., energies
Combining the mass and energy balances gives
The amount of heat transfer during this process is found from
Steam leaves the pressure cooker as saturated vapor at 175 kPa at all times
(Fig. 5–51). Thus,
The initial internal energy is found after the quality is determined:
Thus,
and
The mass of the system at the final state is m 2 V/v 2. Substituting this
into the energy equation yields
There are two unknowns in this equation, u 2 and v 2. Thus we need to relate
them to a single unknown before we can determine these unknowns. Assum-
ing there is still some liquid water left in the cooker at the final state (i.e.,
saturation conditions exist), v 2 and u 2 can be expressed as
Recall that during a boiling process at constant pressure, the properties of
each phase remain constant (only the amounts change). When these expres-
sions are substituted into the above energy equation, x 2 becomes the only
unknown, and it is determined to be
x 2 0.009
u 2 ufx 2 ufg486.82x 21 2037.7 2 kJ/kg
v 2 vfx 2 vfg0.001x 21 1.0040.001 2 m^3 /kg
Qinam 1
V
v 2
bhea
V
v 2
¬u 2 m 1 u 1 b
U 1 m 1 u 1 (1 kg)(497 kJ/kg)497 kJ
u 1 ufx 1 ufg486.82 1 0.00499 21 2037.7 2 kJ/kg497 kJ/kg
x 1
v 1 vf
vfg
0.0060.001
1.0040.001
0.00499
v 1
V
m 1
0.006 m^3
1 kg
0.006 m^3 /kg
hehg @ 175 kPa2700.2 kJ/kg
QinQ
#
in^ ¢t^1 0.5 kJ/s^2130 60 s^2 900 kJ
Qin(m 1 m 2 )he(m 2 u 2 m 1 u 1 )CV
Qinmehe(m 2 u 2 m 1 u 1 )CV (since W0, kepe0)
EinEout ¢Esystem
minmout¢msystem S me 1 m 2 m 12 CV¬or¬me 1 m 1 m 22 CV
⎭⎪⎬⎪⎫ ⎭⎪⎬⎪⎫
P
he = hg@175 kPa
Sat. vapor
Sat. liquid
Sat. vapor
FIGURE 5–51
In a pressure cooker, the enthalpy of
the exiting steam is hg@ 175 kPa
(enthalpy of the saturated vapor at the
given pressure).