| Name: |
11eq1 - Stirred pot reactor
process |
| Source: |
Henley, E. J. and Rosen, E.
M., Material and Energy Balance |
| |
Computations, Wiley: New York, 1969 |
| Reference/s |
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| Model: |
11 implicit equations, indep.
variables x1, x2, x3, V, L, s11, s12, s13, s61, s62 and s63 |
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Lower difficulty level |
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Constraints: All the variables
are nonnegative |
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Discontinuities: none |
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Initial estimates: 1.(0.1,
0.2, 0, 500, 500, 970, 30, 0, 970, 30, 0) ; |
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2. (0.1, 0.4, 0.5, 600, 1500,
970, 300, 0, 500, 900, 800) |
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3. (0.3, 0.3, 0.4, 100, 100,
100, 100, 100, 100, 100, 100, 100, 100) |
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| Solved by |
Shacham, M., POLYMATH 5.1,
build 19, April 18, 2001 |
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| Model Eqs. |
Stirred pot reactor process
|POLVER05_1 |
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EXCEL
FILE |
f(x1)=s61-x1*(L+V*2.523) # |
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TEXT
FILE |
f(x2)=s62-x2*(L+V*1.57) # |
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POLYMATH
FILE |
f(x3)=s63-x3*(L+V*0.0329)
# |
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f(V)=2.523*x1+1.57*x2+0.0329*x3-1
# |
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f(L)=x1+x2+x3-1 # |
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f(s11)=s11-970-s51 # |
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f(s12)=s12-30-s52 # |
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f(s13)=s13-s53 # |
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f(s61)=s81+s101+s31-s61 # |
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f(s62)=s82+s102+s32-s62 # |
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f(s63)=s83+s103+s33-s63 # |
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s102=0 # |
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s21=s11/(1+0.211*1.5) # |
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s71=L*x1 # |
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s72=L*x2 # |
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s73=L*x3 # |
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s41=V*2.523*x1 # |
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s42=V*1.57*x2 # |
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s43=V*0.0329*x3 # |
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s51=0.75*s41 # |
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s52=0.75*s42 # |
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s53=0.75*s43 # |
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s81=0.1*s71 # |
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s101=0.9*0.1*s71 # |
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s82=0.5*s72 # |
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s83=0.2*s73 # |
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s103=0.8*0.4*s73 # |
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s22=s12/(1+0.101*1.5)+0.211*s21*1.5/(1+0.101*1.5)
# |
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s31=s21/(1+0.44*2) # |
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s23=s13+0.101*1.5*s22 # |
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s32=s22/(1+0.219*2)+0.44*s31*2/(1+0.219*2)
# |
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s33=s23+0.219*2*s32 # |
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x1(0)=0.1 |
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x2(0)=0.2 |
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x3(0)=0 |
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V(0)=500 |
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L(0)=500 |
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s11(0)=970 |
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s12(0)=30 |
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s13(0)=0 |
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s61(0)=970 |
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s62(0)=30 |
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s63(0)=0 |
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| Variable/function values |
Variable |
Value |
f(x) |
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x1 |
0.1 |
793.85 |
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x2 |
0.2 |
-227 |
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x3 |
0 |
0 |
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V |
500 |
-0.434 |
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L |
500 |
-0.700 |
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s11 |
970 |
-94.613 |
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s12 |
30 |
-117.750 |
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s13 |
0 |
0 |
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s61 |
970 |
-568.584 |
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s62 |
30 |
418.787 |
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s63 |
0 |
209.297 |
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s102 |
0 |
|
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s21 |
736.802 |
|
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s71 |
50 |
|
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s72 |
100 |
|
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s73 |
0 |
|
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s41 |
126.150 |
|
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s42 |
157 |
|
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s43 |
0 |
|
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s51 |
94.613 |
|
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s52 |
117.75 |
|
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s53 |
0 |
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s81 |
5 |
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s101 |
4.5 |
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s82 |
50 |
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s83 |
0 |
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s103 |
0 |
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s22 |
228.570 |
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s31 |
391.916 |
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s23 |
34.628 |
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s32 |
398.787 |
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s33 |
209.297 |
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| Solution |
Variable |
Value |
f(x) |
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x1 |
0.16547930319775 |
0 |
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x2 |
0.36109556119140 |
0 |
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x3 |
0.4734251356109 |
-1.137E-13 |
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V |
630.763337421609 |
0 |
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L |
1554.563311908010 |
0 |
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s11 |
1167.509795711420 |
-1.990E-13 |
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s12 |
298.194278136889 |
0 |
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s13 |
7.368429217898 |
-1.776E-15 |
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s61 |
520.594447913209 |
-1.137E-13 |
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s62 |
918.938282370162 |
-1.137E-13 |
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s63 |
745.793919046246 |
0 |
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s102 |
0 |
|
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s21 |
886.828557319726 |
|
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s71 |
257.248053631316 |
|
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s72 |
561.345911520977 |
|
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s73 |
735.969346755715 |
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s41 |
263.346394281892 |
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s42 |
357.592370849185 |
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s43 |
9.824572290531 |
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s51 |
197.509795711419 |
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s52 |
268.194278136889 |
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s53 |
7.368429217898 |
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s81 |
25.724805363132 |
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s101 |
23.152324826819 |
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s82 |
280.672955760488 |
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s83 |
147.193869351143 |
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s103 |
235.510190961829 |
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s22 |
502.714300068243 |
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s31 |
471.717317723258 |
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s23 |
83.529645678237 |
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s32 |
638.265326609674 |
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s33 |
363.089858733274 |
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