The proposed procedure is based on Figure (9.16).
From numerical point of view, the Mach number equal infinity
when left side assumes result in infinity length of possible
extra (the whole flow in the tube is subsonic).
To overcome this numerical problem it is suggested to
start the calculation from
distance from the right hand
side.
Let denote
Figure (9.17) shows the entrance Mach number,
reduces after the maximum length is exceeded.
With
The extra
In a summary of the actions
is done by the following algorithm:
shock location are:
The iteration summary is also shown below
The solution is obtained by an iterative process.
The maximum
for
is 0.821508116.
Hence,
exceed the maximum length
for this entrance Mach number.
The maximum for
is
,
thus the extra tube is
.
The left side is when the shock occurs at
(flow
chocked and no any additional
).
Hence, the value of left side is
.
The right side is when the shock is at the entrance
at which the extra
is calculated for
and
is
Normal Shock
Input: Mx
k = 1.4
Mx
My
Ty/Tx
ρy/ρx
Py/Px
P0y/P0x
8
0.39289
13.3867
5.56522
74.5
0.00848783
Fanno Flow
Input: M
k = 1.4
M
fld
P/P*
P0/P0*
ρ/ρ*
U/U*
T/T*
0.39289
2.44172
2.74611
1.61362
2.35907
0.423896
1.16406
is
Now the solution is somewhere between the negative of left side to the
positive of the right side.9.17
exceeds the maximum
for the supersonic flow.
Accordingly continue.
,
with the
Mach number,
calculated previously,
for supersonic branch for the
against the old one.
If it satisfactory stop or return to stage
(b).
<>
8.0000
1.0000
0.57068
0.32932
1.6706
0.64830
<>
0
0.67426
0.22574
1.3838
0.74664
0.90000
1
0.62170
0.27830
1.5286
0.69119
0.90000
2
0.59506
0.30494
1.6021
0.66779
0.90000
3
0.58217
0.31783
1.6382
0.65728
0.90000
4
0.57605
0.32395
1.6554
0.65246
0.90000
5
0.57318
0.32682
1.6635
0.65023
0.90000
6
0.57184
0.32816
1.6673
0.64920
0.90000
7
0.57122
0.32878
1.6691
0.64872
0.90000
8
0.57093
0.32907
1.6699
0.64850
0.90000
9
0.57079
0.32921
1.6703
0.64839
0.90000
10
0.57073
0.32927
1.6705
0.64834
0.90000
11
0.57070
0.32930
1.6706
0.64832
0.90000
12
0.57069
0.32931
1.6706
0.64831
0.90000
13
0.57068
0.32932
1.6706
0.64831
0.90000
14
0.57068
0.32932
1.6706
0.64830
0.90000
15
0.57068
0.32932
1.6706
0.64830
0.90000
16
0.57068
0.32932
1.6706
0.64830
0.90000
17
0.57068
0.32932
1.6706
0.64830
0.90000
This procedure is rapidly converted to the solution.