Chapter 2 Reynolds Transport Theorem (RTT)
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Transcript of Chapter 2 Reynolds Transport Theorem (RTT)
Chapter 2 Reynolds Transport Theorem (RTT)
2.1 The Reynolds Transport Theorem
2.2 Continuity Equation
2.3 The Linear Momentum Equation
2.4 Conservation of Energy
2.1 The Reynolds Transport Theorem (1)
2.1 The Reynolds Transport Theorem (2)
ρ ( ) (inflow if negative) (11-41)net out in
CS
B B B b V n dA
42)-(11 ρ dV bBCV
CV
43)-(11 )(ρρ CSCV
dAnVbdV bdt
d
dt
dB :General sys
2.1 The Reynolds Transport Theorem (3)
Special Case 1: Steady Flow
Special Case 2: One-Dimensional Flow
44)-(11 )(ρ CS
dAnVbdt
dB :flowSteady sys
:flow ldimensiona-One
45)-(11 ρ-ρρin
exiteach for out
exiteach for CV
iiiieeeesys AVbAVbdV b
dt
d
dt
dB
46)-(11 -ρinoutCV
iieesys bmbmdV b
dt
d
dt
dB
2.2 Continuity Equation (1) An Application: The Continuity Equation
47)-(11 )(ρρ0 CS
dAnVdVdt
d :equation Continuity
CV
48)-(11
in
iout
e mm :flowSteady
49)-(11 or AA 221 AVAVVV
:constant stream,Single
22111
2.3 The Linear Momentum Equation (1)
..50)-(11 )V(m
dt
d
dt
Vdm amF
51)-(11 ρdVVdt
dF
sys
52)-(11 )(ρρ)(
CSCV
sys dAnVVdVVdt
d
dt
Vmd
53)-(11 (ρρ )dAnVVdVVdt
dF:General
CSCV
2.3 The Linear Momentum Equation (2)
2.3 The Linear Momentum Equation (3)
Special Cases
54)-(11 )(ρ dAnVVF :flowSteady CS
55)-(11 V -Vρ ie
in
i
out
e
CV
mmdVVdt
dF
:flow ldimensiona-One
56)-(11 V -V ie
in
i
out
e mmF
:flow ldimensiona-oneSteady,
2.3 The Linear Momentum Equation (4)
57)-(11 )V-V(mF :exit)-oneinlet,-(one
flow ldimensiona-oneSteady,
12
58)-(11 )V-V(mF :coordinate x Along x1,x2,x
2.4 Conservation of Energy
2
) V dA
V
2
system
cv cs
shaft normal shear other
dEQ W e dV e
dt t
e u gz
W W W W W
Chapter 3 Flow Kinematics
3.1Conservation of Mass
3.2 Stream Function for Two-Dimensional
Incompressible Flow
3.3 Fluid Kinematics
3.4 Momentum Equation
3.1 Conservation of mass• Rectangular coordinate system
x
y
z
dx
dy
dzo u
v
w xA udydz
yA dxdz
zA wdxdy
surface control thethrough
outflux mass of rateNet 0
surface control theinside
change mass of Rate
x
y
z
dx
dy
dzo u
v
w xA udydz
x(left)A udydz
dydzdx
x
uu
dx
x
22
dxdydzx
u
xuudydz
2
1
x(right)A udydz
dydzdx
x
uu
dx
x
22
dxdydzx
u
xuudydz
2
1
y(bottom)A dxdz
dxdzdy
y
dy
y
22
dxdydzyy
dxdz
2
1
y(top)A dxdz
dxdzdy
y
dy
y
22
dxdydzyy
dxdz
2
1
x
y
z
dx
dy
dzo u
v
w
yA dxdz
z(back)A wdxdy
dxdydz
z
ww
dz
z
22
dxdydzz
w
zwwdxdz
2
1
z(front)A wdxdy
dxdydz
z
ww
dz
z
22
dxdydzz
w
zwwdxdy
2
1
dx
dy
dzo u
v
w
x
y
z
zA wdxdy
Net Rate of Mass Flux
x(left)A udydz
x(right)A udydz
y(bottom)A dxdz
y(top)A dxdz
z(back)A wdxdy
z(front)A wdxdy
dxdydzx
u
xuudydz
2
1
dxdydzx
u
xuudydz
2
1
dxdydzyy
dxdz
2
1
dxdydzyy
dxdz
2
1
dxdydzz
w
zwwdxdz
2
1
dxdydzz
w
zwwdxdy
2
1
CS AdV
dxdydzz
w
zw
yyx
u
xu
Net Rate of Mass Flux
CS AdV
dxdydzz
w
zw
yyx
u
xu
dxdydzz
w
yx
u
Rate of mass change inside the control
volume
dxdydzt
Vdt
V
dxdydzt
0
dxdydzz
w
yx
u
t
0
z
w
yx
u
Continuity Equation
t
0
z
w
yx
u
zk
yj
xi
ˆˆˆ
Vz
w
yx
u
0
Vt
3.2 Stream Function for Two-Dimensional
Incompressible Flow• A single mathematical function (x,y,t) to
represent the two velocity components, u(x,y,t) and (x,y,t).
• A continuous function (x,y,t) is defined such that
xyu
and
The continuity equation is satisfied exactly
0
xyyxyx
u
Equation of Streamline
• Lines drawn in the flow field at a given instant that are tangent to the flow direction at every point in the flow field.
dyjdxijuirdV ˆˆˆˆ0
dxudyk ˆ
0 dxudy Along a streamline
0
ddyy
dxx
dxx
dyy
Volume flow rate between streamlines
u
v V
21, yxB
11, yxA
22 , yxC1
23
x
y
Flow across AB
21
21
yy
yy dy
yudyQ
Along AB, x = constant, and dyy
d
1221
21
yy ddy
yQ
Volume flow rate between streamlines
u
v V
21, yxB
11, yxA
22 , yxC1
23
x
y
Flow across BC,
21
21
xx
xx dx
xdxQ
Along BC, y = constant, and dxx
d
1221
12
xx ddx
xQ
Stream Function for Flow in a Corner
Consider a two-dimensional flow field
0
w
Ay
Axu
xyu
and
yAxu
xfAxyxfdy
y
dx
dfAy
x
0
dx
df
cAxy
Motion of a Fluid Element
Translation
x
y
z
Rotation
Angular deformationLinear deformation
3.3 Flow Kinematics
Fluid Translation
x
y
z
Fluid particle pathAt t At t+dt
r
rdr
tzyxVVtp ,,,
dtt
Vdz
z
Vdy
y
Vdx
x
VVd pppp
t
V
dt
dz
z
V
dt
dy
y
V
dt
dx
x
V
dt
Vda pppp
p
t
V
z
Vw
y
V
x
Vu
dt
Vda p
p
t
VVV
Dt
VDa p
p
Scalar component of fluid acceleration
t
u
z
uw
y
u
x
uu
Dt
Duaxp
tzw
yxu
Dt
Dayp
t
w
z
ww
y
w
x
wu
Dt
Dwazp
Fluid acceleration in cylindrical coordinates
t
V
z
VV
r
VV
r
V
r
VV
Dt
DVa rr
zrr
rr
rp
2
t
V
z
VV
r
VVV
r
V
r
VV
Dt
DVa z
rrp
t
V
z
VV
V
r
V
r
VV
Dt
DVa zz
zzz
rz
zp
Fluid Rotation
x
y
aa'
b
b'
o
x
y
t
x
t ttoa
00
limlim
txx
ttxx
xx
xt
xtxx
toa
0
lim
t
y
t ttob
00
limlim
tyy
ututy
y
uu
aa'
b
b'
o
x
y
xx
u
yy
uu
y
u
t
ytyyu
tob
0
lim
aa'
b
b'
o
x
y
xx
u
yy
uu
xoa
y
uob
y
u
xoboaz
2
1
2
1
Similarily, considering the rotation of pairs of perpendicular line segments in yz and xz planes, one can obtain
zy
wx
2
1
x
w
z
uy 2
1
Fluid particle angular velocity
zyx kji ˆˆˆ
y
u
xk
x
w
z
uj
zy
wi
ˆˆˆ2
1
wuzyx
kji
V
ˆˆˆ VV
curl
2
1
2
1
V
2 Vorticity: A measure of fluid element rotation
rzrzr
V
rr
rV
rk
r
V
z
Ve
z
VV
reV
11ˆˆ1
ˆ
Vorticity in cylindrical coordinates
Fluid Circulation, c sdV
x
y x
x
u
yy
uu
c
y
xo
b
a
yxyy
uuyx
xxu
yxy
u
x
yxz 2
A zA zC dAVdAsdV
2
Circulation around a close contour
=Total vorticity enclosed
Around the close contour oacb,
Fluid Angular Deformation
x
y
aa'
b
b'
o
x
y
xx
u
yy
uu
dt
d
dt
d
dt
d
dy
du
x
Fluid Linear Deformation
x
y
yy
uu
a a'
bb'
o
x
y
xx
u
t
y
dt
dy
t
yy
0
limdilation of Rate
tyy
tyy
tyy
2
1
ydt
d yy
tyy
txx
utx
x
uutx
x
uu
2
1
t
xx
txx
00 limstrain of Rate
x
uxx
0
z
wzz
0
tx
u
x
tz
w
z
tzz
wtz
z
wwtz
z
ww
2
1
t
zz
tzz
00 limstrain of Rate
yy
uu
a a'
bb'
o
x
y
xx
u
t
VVV
t
0
limrate dilation Volume
zyxzyxVV
Ozyyxzx
tz
wt
yt
x
u
z
w
yx
ut
VVV
t
limrate dilation Volume0
V
zyx
zyx
zyyxzx
V
VV
Rate of shearing strain(Angular deformation)
y
u
xyxxy
zy
wzyyz
x
w
z
uxzzx
x
uVxx
2
3
2
yVyy
2
3
2
z
wVzz
2
3
2
Rate of Strain
Rate of normal strain
3.4 Momentum Equation
z
Vw
y
V
x
VuVd
Dt
VDdmFdFdFd sB
t
V
z
Vw
y
V
x
Vu
Vd
Fd
t
VVV
x
y
z
xxxy
xz
zy
zxzz
direction plane jiij
yy
yzyx
Forces acting on a fluid particle
x
y
z
x-direction
2
dz
zzx
zx
2
dy
yyx
yx
2
dz
zzx
zx
2
dx
xxx
xx
2
dx
xxx
xx
2
dy
yyx
yx
SxdF dydzdx
xdydz
dx
xxx
xxxx
xx
22
+ dxdzdy
ydxdz
dy
yyx
yxyx
yx
22
dxdydz
zdxdy
dz
zzx
zxzx
zx
22
+
Forces acting on a fluid particle
x-direction SxdF dydzdx
xdydz
dx
xxx
xxxx
xx
22
+ dxdzdy
ydxdz
dy
yyx
yxyx
yx
22
dxdydz
zdxdy
dz
zzx
zxzx
zx
22
+
SxdF dxdydzzyxzxyxxx
SxBxx dFdFdF dxdydzzyx
g zxyxxxx
Components of Forces acting on a fluid element
x-direction
Vd
dF
Vd
dF
Vd
dF SxBxx
zyx
g zxyxxxx
Vd
dF
Vd
dF
Vd
dF SyByy
zyx
g zyyyxyy
Vd
dF
Vd
dF
Vd
dF SzBzz
zyx
g zzyzxzz
y-direction
z-direction
Differential Momentum Equation
zyxg zxyxxx
x
zyxg zyyyxy
y
zyxg zzyzxz
z
z
uw
y
u
x
uu
t
u
z
wyx
ut
z
ww
y
w
x
wu
t
w
l element/Vo fluid on the acting Forces
naccleratio Fluid
Momentum Equation:Vector form
Dt
VDg
zxAyxAxxAAAAxSx kji
zk
yj
xi
Vd
dF
ˆˆˆˆˆˆ
A
A
A
zzyzxz
zyyyxy
zxyxxx
k
j
i
ˆ00
0ˆ0
00ˆ
zyxzxyxxx
is treated as a momentum flux
Stress and Strain Relation for a Newtonian Fluid
y
u
xxyyxxy
zy
wyzzyyz
x
w
z
uzxxzzx
x
uVpp xxxx
2
3
2
yVpp yyyy
2
3
2
z
wVpp zzzz
2
3
2
Newtonian fluid viscous stress rate of shearing strain
Surface Forces
zyxVd
dF zxyxxxSx
y
u
xyxyx
x
w
z
uzxzx
x
uVpp xxxx 2
3
2
zxyxxxSx
zyp
xVd
dF
x
w
z
u
zy
u
xyV
x
up
x
3
22
Momentum Equation:Navier-Stokes Equations
x
w
z
u
zy
u
xyV
x
u
xx
pg
Dt
Dux
3
22
y
w
zzV
yyxy
u
xy
pg
Dt
Dy
3
22
Vz
w
zy
w
zyz
u
x
w
xz
pg
Dt
Dwz
3
22
Navier-Stokes Equations
For flow with =constant and =constant
0 V
2
2
2
2
2
2
z
u
y
u
x
u
x
pg
Dt
Dux
2
2
2
2
2
2
zyxy
pg
Dt
Dy
2
2
2
2
2
2
z
w
y
w
x
w
z
pg
Dt
Dwz
3.5 Conservation of Energy
iij
j
Dh Dp udiv k T n
Dt Dt x
Summary of Basic Equations
t
D
Dtg + p
Dh
Dt
Dp
Dtk T
u
x
ij
iji
j
div V
V'
div '
0