Lid-driven Cavity Flow.pdf
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Transcript of Lid-driven Cavity Flow.pdf
Ljd-drjven Cavjty Flow
‣ Domain is a “uniform” grid n×n
j = 4
0,4 1,4 2,4 3,4 4,4
j = 3
0,3 1,3 2,3 3,3 4,3
j = 2
0,2 1,2 2,2 3,2 4,2
j = 1
0,1 1,1 2,1 3,1 4,1
j = 0
0,0 1,0 2,0 3,0 4,0
i = 0 i = 1 i = 2 i = 3 i = 4
�ψ[0][1]
�ψ[2][2]
�ψ[4 ][3]
�ψ[3][0]
�ψ[1][3]
�ψ[3][4 ]
�ψ[0][0]
�ψ[2][1]
�ψ[4 ][2]
�ψ[0][4 ]
�ψ[1][2]
�ψ[3][3]
�ψ[2][0]
�ψ[4 ][1]
�ψ[0][3]
�ψ[2][4 ]
�ψ[1][1]
�ψ[3][2]�ψ[0][2]
�ψ[2][3]
�ψ[4 ][4 ]
�ψ[4 ][0]�ψ[1][0]
�ψ[3][1]
�ψ[1][4 ]
Update boundary condition to zero again when solving the RHS in section C, term (13)(14).
Ljd-drjven Cavjty Flow
‣ Stream function
(1−Δt ∂2
∂x2)(1−Δt ∂
2
∂y2)ψ n+1 =ψ n +Δtω n + (Δt ∂
2
∂x2)(Δt ∂
2
∂y2)ψ n
(1−Δt ∂2
∂x2)× f =ψ n +Δtω n + (Δt ∂
2
∂x2)(Δt ∂
2
∂y2)ψ n
f = (1−Δt ∂2
∂y2)ψ n+1
(1)
(2)
(3)
// Expand RHS with (△t×∂2/∂x2) (△t×∂2/∂y2) first
// Recall (△t×∂2/∂x2) gn
// Solve equation with TDMA
(1−Δt ∂2
∂x2)× f = fi, j
n+1 −ΔtΔx2
( fi−1, jn+1 −2 fi, j
n+1 + fi+1, jn+1)
= −ΔtΔx2
fi−1, jn+1 + (1+ 2Δt
Δx2) fi, j
n+1 −ΔtΔx2
fi+1, jn+1
(4)
(5)
= a× fi−1, jn+1 +b× fi, j
n+1 + c× ΔtΔx2
fi+1, jn+1 (6)
Section A // Expand (1-△t×∂2/∂x2) term on LHS
(1−Δt ∂2
∂y2)×ψi, j
n+1 =ψi, jn+1 −
ΔtΔy2
(ψi, j−1n+1 −2ψi, j
n+1 +ψi, j+1n+1) (7)
= −ΔtΔy2
ψi, j−1n+1 + (1+ 2Δt
Δy2)ψi, j
n+1 −ΔtΔy2
ψi, j+1n+1 (8)
= a×ψi, j−1n+1 +b×ψi, j
n+1 + c× ΔtΔy2
ψi, j+1n+1 (9)
Section B // Expand (1-△t×∂2/∂y2) term of “f ” on LHS
Section C
(Δt ∂2
∂x2)(Δt ∂
2
∂y2)ψ n = (Δt ∂
2
∂x2)gn (10)
gi, jn =
ΔtΔy2
ψi, j−1n −2ΔtΔy2
ψi, jn +
ΔtΔy2
ψi, j+1n
= −a×ψi, j−1n − (b−1)×ψi, j
n − c×ψi, j+1n
(11)
(12)
(Δt ∂2
∂x2)gi, j
n =ΔtΔx2
gi−1,1n −2ΔtΔx2
gi, jn +
ΔtΔx2
gi+1, jn (13)
= −a× gi−1, jn − (b−1)× gi, j
n − c× gi+1, jn (14)
SectionA = SectionC +ψi, jn +Δtωi, j
n
SectionB = fi, jn+1(afterTDMA)
Ljd-drjven Cavjty Flow
When i = 0 , j = 1 ⇒ ⇒ ⇒
When i = 1 , j = 1 ⇒ ⇒
When i = 2 , j = 1 ⇒ ⇒
When i = 3 , j = 1 ⇒ ⇒
When i = 4 , j = 1 ⇒ ⇒ ⇒
a0ψg +b0ψL=0,1 + c0ψ1,1 = B.C a0 = 0,b0 =1,c0 = 0 b0ψL=0,1 = B.C
a1ψL=0,1 +b1ψ1,1 + c1ψ2,1 = S1,1 a1ψL=0,1 +b1ψ1,1 + c1ψ2,1 = S1,1a2ψ1,1 +b2ψ2,1 + c2ψ3,1 = S2,1 a2ψ1,1 +b2ψ2,1 + c2ψ3,1 = S2,1a3ψ2,1 +b3ψ3,1 + c3ψ4,1 = S3,1 a3ψ2,1 +b3ψ3,1 + c3ψ4,1 = S3,1a4ψ3,1 +b4ψR=4,1 + c4ψg = S4,1 a4 = 0,b4 =1,c4 = 0 b4ψR=4,1 = B.C
b0 c0 0 0 0a1 b1 c1 0 00 a2 b2 c2 00 0 a3 b3 c30 0 0 a4 b4
!
"
#######
$
%
&&&&&&&
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
!
"
#######
$
%
&&&&&&&
=
S0,1 = B.CS1,1S2,1S3,1
S4,1 = B.C
!
"
#######
$
%
&&&&&&&
b0 c0 0 0 0a1 b1 c1 0 00 a2 b2 c2 00 0 a3 b3 c30 0 0 a4 b4
!
"
#######
$
%
&&&&&&&
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
!
"
#######
$
%
&&&&&&&
=
S0,1 = B.CS1,1S2,1S3,1
S4,1 = B.C
!
"
#######
$
%
&&&&&&&
1 c0 /b0 =C[0] 0 0 0a1 b1 c1 0 00 a2 b2 c2 00 0 a3 b3 c30 0 0 a4 b4
!
"
#######
$
%
&&&&&&&
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
!
"
#######
$
%
&&&&&&&
=
S0,1 /b0 = D[0]S1,1S2,1S3,1S4,1
!
"
#######
$
%
&&&&&&&
1 C[0] 0 0 00 b1 −a1C[0] c1 0 00 a2 b2 c2 00 0 a3 b3 c30 0 0 a4 b4
"
#
$$$$$$$
%
&
'''''''
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
"
#
$$$$$$$
%
&
'''''''
=
S0,1 /b0 = D[0]S1,1 −a1D[0]
S2,1S3,1S4,1
"
#
$$$$$$$
%
&
'''''''
1 C[0] 0 0 00 1 c1 / (b1 +a1C[0] )=C[1] 0 00 a2 b2 c2 00 0 a3 b3 c30 0 0 a4 b4
!
"
#######
$
%
&&&&&&&
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
!
"
#######
$
%
&&&&&&&
=
S0,1 /b0 = D[0](S1,1 −a1D[0] / (b1 −a1C[0] )= D[1]
S2,1S3,1S4,1
!
"
#######
$
%
&&&&&&&
Ljd-drjven Cavjty Flow
1 C[0] 0 0 00 1 C[1] 0 00 0 b2 −a2C[1] c2 00 0 a3 b3 c30 0 0 a4 b4
"
#
$$$$$$$
%
&
'''''''
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
"
#
$$$$$$$
%
&
'''''''
=
S0,1 /b0 = D[0](S1,1 −a1D[0] / (b1 −a1C[0] )= D[1]
S2,1 −a2D[1]S3,1S4,1
"
#
$$$$$$$
%
&
'''''''
1 C[0] 0 0 00 1 C[1] 0 00 0 1 c2 / (b2 −a2C[1] )=C[2] 00 0 a3 b3 c30 0 0 a4 b4
"
#
$$$$$$$
%
&
'''''''
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
"
#
$$$$$$$
%
&
'''''''
=
S0,1 /b0 = D[0](S1,1 −a1D[0] / (b1 −a1C[0] )= D[1](S2,1 −a2D[1] ) / (b2 −a2C[1] )= D[2]
S3,1S4,1
"
#
$$$$$$$
%
&
'''''''
1 C[0] 0 0 00 1 C[1] 0 00 0 1 C[2] 00 0 0 b3 −a3C[2] c30 0 0 a4 b4
"
#
$$$$$$$
%
&
'''''''
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
"
#
$$$$$$$
%
&
'''''''
=
S0,1 /b0 = D[0](S1,1 −a1D[0] / (b1 −a1C[0] )= D[1](S2,1 −a2D[1] ) / (b2 −a2C[1] )= D[2]
S3,1 −a[3]D[2]S4,1
"
#
$$$$$$$
%
&
'''''''
1 C[0] 0 0 00 1 C[1] 0 00 0 1 C[2] 00 0 0 1 c3 / (b3 +a3C[2] )=C[3]0 0 0 a4 b4
!
"
#######
$
%
&&&&&&&
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
!
"
#######
$
%
&&&&&&&
=
S0,1 /b0 = D[0](S1,1 −a1D[0] / (b1 −a1C[0] )= D[1](S2,1 −a2D[1] ) / (b2 −a2C[1] )= D[2](S3,1 −a3D[2] ) / (b3 −a3C[2] )= D[3]
S4,1
!
"
#######
$
%
&&&&&&&
Ljd-drjven Cavjty Flow
1 C[0] 0 0 00 1 C[1] 0 00 0 1 C[2] 00 0 0 1 C[3]0 0 0 0 b4 −a4C[3]
"
#
$$$$$$$
%
&
'''''''
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
"
#
$$$$$$$
%
&
'''''''
=
S0,1 /b0 = D[0](S1,1 −a1D[0] / (b1 −a1C[0] )= D[1](S2,1 −a2D[1] ) / (b2 −a2C[1] )= D[2](S3,1 −a3D[2] ) / (b3 −a3C[2] )= D[3]
S4,1 −a4D[3]
"
#
$$$$$$$
%
&
'''''''
1 C[0] 0 0 00 1 C[1] 0 00 0 1 C[2] 00 0 0 1 C[3]0 0 0 0 1
!
"
#######
$
%
&&&&&&&
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
!
"
#######
$
%
&&&&&&&
=
S0,1 /b0 = D[0](S1,1 −a1D[0] / (b1 −a1C[0] )= D[1](S2,1 −a2D[1] ) / (b2 −a2C[1] )= D[2](S3,1 −a3D[2] ) / (b3 −a3C[2] )= D[3](S4,1 −a4D[3] ) / (b4 −a4C[4 ] )= D[4 ]
!
"
#######
$
%
&&&&&&&
1 C[0] =c0b0
0 0 0
0 1 C[1] =c1
b1 −a1C[0]0 0
0 0 1 C[2] =c2
b2 −a2C[2]0
0 0 0 1 C[3] =c3
b3 −a3C[3]0 0 0 0 1
"
#
$$$$$$$$$$$$
%
&
''''''''''''
ψL=0,1
ψ1,1ψ2,1
ψ3,1
ψR=4,1
"
#
$$$$$$$
%
&
'''''''
=
S0,1b0
= D[0]
S1,1 −a1D[0]b1 −a1C[0]
= D[1]
S2,1 −a2D[1]b2 −a2C[1]
= D[2]
S3,1 −a3D[2]b3 −a3C[2]
= D[3]
S4,1 −a4D[3]b4 −a4C[3]
= D[4 ]
"
#
$$$$$$$$$$$$$$$
%
&
'''''''''''''''