chapters
mass and
energy
oftensystems
balance of
m2
surrounding
Meet
3
Token
closed 2
system
closed
heat transfer
transfer
system
wm
F
sealed
system
Vmax
work mass
heat transfer
velocity
hmbetftn.IT
high
E FFn
A
in
nanocrate
impff
ang
funda
i
volume
flow rate
fÉct
Actose
Parallel
pipe
circular
pipe
f To
system
Vang
23 high
Vang
Vhigh
Tax
Δ
change of
3 mean
mefrincipe
f1
in
my_in
r
ink
is
inin
fin
inout
that
Total mass entering Tolls
leaving
yoursystem
Steystate
inlet
mass flow rate
age
system
offptm
inin
Mout
net change in
mass in
0
your
min
lout
min
inout
andDfjus
a nozzle
is a device that is used
velocityof a fluid
at the expenseof
pressurel
Tale
off
Y
that
a fluid
steady state
47mi dff
enit V2
V2
P2
V
AX
P
velocity
at the increase
ofpressure
in
o
ins
A xY
1
1
Velocity
11
13812 P
is a device
used to decreasethe
u
inlet
11
Az
ME
É FgÉsst
is
of
mothers
P2A2 V2
A V
P
Noz
to increase the
Mout
in
Ex Axa
A2
EE.si
iEaa.n eni Az7Ai
Ethy
V1
Inlet
V2
in
nes
adiabatic
5 0
P2
Rethe
ke
ve
he
P
If
hi
9k
jess
hi
he
2
IF
mte
assewseeitaaanging.it
ÉFokpa
83
151
Tsat
20006
71
Table AG 0 S MPa
b i
2855.8 KJ
superheadedvapor
net
Wnet
Emass
Me
infhe VE g e7
all
hi
he
he
state P2
Tsat
h
Agee
ie
We.IE
the we
h
kg
hf
200hPa
1201
a
hfg
3
hf
s
If
g
110
Table AS
21 C
hi
kg If
hg
Turbines
turbine
dame
generator combo
that would be able to enteract
electrical
energy
device that is used to extract
a fluid at the expenseof
energyfrom
a
pressure
gas
liquid
pressure drops across the turbine
increases
velocity
pressure remains the same
velocity decreases
in
in
me
in
in
energy balance
Éin Éout
system 0
If
Éin Eout
Wrout
he Vertgzi
he
Eiga
Wont
compressorsalumb
goal is
to
liquid
increase
opposite to a turbine
4
173
the pressure of
your fluid
thermodynamic POV
shaft
steadstow
in
M
in
cis
in
win
inhi
Win Got
Win
lff mm.at
Ein
tgaD
inhe Bout
he
hi
Fout inTpT_T
any
Gaskets
Tsat
900
Eoft
400
superheated
For
tabes
Table As
saturated
EEalityhf.bg
mintures
x
h2 hi Cp T2 T
Tset
Are
ΔhD
DE
Ii
12 28
either
Ape
If
rake
410
50
12 hfta hf hg
0
f
ffÉ
P
Es
ginegt.SI
steam in
System
conditions
Sketch
adiabatic
turbing
ivIin
in
Properties
1 9008
6
kg
kg
Table
AS_If
kPa
0095
P2
100
A
Ug
V2
he
42
20
0007343 m
3214.5 KJ
h
State
4
9
P
AEang
4 MPa
I
É
Ac Vang
in
P
2
in
piaspetep
physical laws
Ile
power
in 13.62kg's
hf
x
2
35
Uf
1.609
hg hf
KJ
kg
00001043
1.6941
x
g Uf
hf
417.51
2675.0
hg
calculations
P
Ac Vang
x
Evans
13
livflin
62kg8
v
x
h2 his
8885.2kW
into
gas
0
Is
V
RTI
EII
I
Vafx Ic
in
Acx Vang
Yang
Tinet I
met
NEE
Ny
in
Win
in Cp
Ah
T T2
RE
Throttling
ales
T.EE not
rather
Imeek
CPAT
temp
cycles
sP2cccP
at all to stop the flow
goal
a sharp
capillary
tubes
of fluid
drop in pressure
drop
E eFF5aau
state
Is
Refrigeration
goal is here to have
is
steady
or
87885T
THROTTLING
vapor
IEED
41
room
Flat
Cray
42
KIR
Wm
n
temp
minture
in
in
in
Emars
Ñx d
0
DEE
100date
ARE
o
h _has
Ex B
internal
eners
h
ie Pu
Enthalpy
pressure
0
hi
h
in
ha
hs
0
cannot be 0
O
isenthalp.ie
process
skecific
volume
Towhome
21
Pin
V2
12220