Chapter 7 | 387
Under the stated assumptions and observations, the mass and energy
balances for this steady-flow system can be expressed in the rate form as
follows:
Mass balance:
Energy balance:
Rate of net energy transfer Rate of change in internal, kinetic,
by heat, work, and mass potential, etc., energies
Combining the mass and energy balances gives
The desired properties at the specified states are determined from the steam
tables to be
State 1:
State 2:
State 3:
Substituting,
which gives
The rate of entropy generation during this process can be determined by
applying the rate form of the entropy balance on an extended systemthat
includes the mixing chamber and its immediate surroundings so that the
boundary temperature of the extended system is 70F 530 R:
m
#
1 s 1 m
#
2 s 2 m
#
3 s 3
Q
#
out
Tb
S
#
gen^0
S
#
inS
#
out¬¬S
#
gen¬¬dSsystem>dt
m
#
2 22.7 lbm>min
180 Btu>min 3300 18.07m
#
2 1162.3^1300 m
#
22 97.99^4 Btu>min
P 3 20 psia
T 3 130°F
f¬
h 3 hf @ 130°F97.99 Btu>lbm
s 3 sf @ 130°F0.18174 Btu>lbm#R
P 2 20 psia
T 2 240°F
f¬
h 2 1162.3 Btu>lbm
s 2 1.7406 Btu>lbm#R
P 1 20 psia
T 1 50°F
f¬
h 1 hf @ 50°F18.07 Btu>lbm
s 1 sf @ 50°F0.03609 Btu>lbm#R
Q
#
outm
#
1 h 1 m
#
2 h 2 ^1 m
#
1 m
#
22 h 3
m# 1 h 1 m# 2 h 2 m# 3 h 3 Q
#
out^1 since W
#
0, kepe 02
E
#
inE
#
out^
E
#
inE
#
out^ ^ dEsystem/dt^0
m
#
inm
#
out dmsystem>dt^0 S^ m
#
1 m
#
2 m
#
3
⎭⎪⎪⎬⎪⎪⎫ ⎭⎪⎪⎬⎪⎪⎫
0 (steady)
¡
0 (steady)
¡
123
Rate of net entropy
transfer by heat
and mass
123
Rate of entropy
generation
123
Rate of change
in entropy
cen84959_ch07.qxd 4/19/05 10:55 AM Page 387