Check of ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings
The model has the same number of unknowns and equations: 5664
Check of ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings successful.
| ModelicaTest410 experiment tolerance | ModelicaTest410 tightend tolerance | |
|---|---|---|
| Testrun ID | 20250225034436 | 20250225005809 |
| Simulator | Dymola | Dymola |
| Status | PASS | PASS |
| Run time | 12.31 | 12.77 |
| Workdir | D:/MSL_Nightly/Output/Testruns/Dymola/ModelicaTest_org\ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings\WorkDir | D:/MSL_Nightly/Output/Testruns/Dymola/ModelicaTest\ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings\WorkDir |
| ModelicaTest410 experiment tolerance | ModelicaTest410 tightend tolerance | |
|---|---|---|
| Status | PASS | PASS |
| Task runtime | 2.04 s | 2.01 s |
| Warnings | 0 | 0 |
| Errors | 0 | 0 |
| Open log  | Open log  |
| ModelicaTest410 experiment tolerance | ModelicaTest410 tightend tolerance | |
|---|---|---|
| Status | PASS | PASS |
| Task runtime | 5.11 s | 5.61 s |
| Warnings | 0 | 0 |
| Errors | 0 | 0 |
| Open log  | Open log  | |
| Numerical Jacobians | 2 | 2 |
| Continuous time states | 124 | 124 |
| Number NL equation systems | 2 | 2 |
| Largest NL equation system | 4 | 4 |
| ModelicaTest410 experiment tolerance | ModelicaTest410 tightend tolerance | |
|---|---|---|
| Status | PASS | PASS |
| Task runtime | 5.08 s | 5.09 s |
| Simulation time | 20.00 s | 20.00 s |
| Copy result file path  | Copy result file path  | |
| Open log  | Open log  | |
| Time Events | 2 | 2 |
| State Events | 0 | 0 |
| Jacobian evaluations | 110 | 110 |
| Integrator Steps | 654 | 654 |
| Total CPU time | 4.50 s | 4.51 s |
| CPU time Integration | 4.50 s | 4.51 s |
| CPU time Initialization | 0.00 s | 0.00 s |
check - Open log
Check of ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings
The model has the same number of unknowns and equations: 5664
Check of ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings successful.
check - Open log
Check of ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings
The model has the same number of unknowns and equations: 5664
Check of ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings successful.
translate - Open log
Translation of ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings
The DAE has 5664 scalar unknowns and 5664 scalar equations.
Statistics
Original Model
Number of components: 516
Variables: 4811
Constants: 56 (56 scalars)
Parameters: 1181 (1497 scalars)
Unknowns: 3574 (5670 scalars)
Differentiated variables: 248 scalars
Equations: 2020
Nontrivial: 1420
Translated Model
Constants: 1990 scalars
Free parameters: 153 scalars
Parameter depending: 572 scalars
Continuous time states: 124 scalars
Time-varying variables: 1556 scalars
Alias variables: 2952 scalars
Number of mixed real/discrete systems of equations: 0
Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2}
Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0}
Sizes of nonlinear systems of equations: {15, 15}
Sizes after manipulation of the nonlinear systems: {4, 4}
Number of numerical Jacobians: 2
Initialization problem
Sizes of nonlinear systems of equations: {15, 15}
Sizes after manipulation of the nonlinear systems: {2, 2}
Number of numerical Jacobians: 2
Settings
Advanced.StoreProtectedVariables = true
Sparse solvers enabled: false
Enabled for integrator Jacobian: false
Model sparse and large enough: true.
Sparse solvers are available for dassl, lsodar, cvode, ida, radau, esdirk*, sdirk*.
Enable sparse solvers by setting Advanced.Translation.SparseActivate.
Selected continuous time states
Statically selected continuous time states
junction1.medium.h
junction1.medium.p
junction2.medium.h
junction2.medium.p
pipe1.mediums[1].h
pipe1.mediums[1].p
pipe1.mediums[2].h
pipe1.mediums[2].p
pipe1.mediums[3].h
pipe1.mediums[3].p
pipe1.mediums[4].h
pipe1.mediums[4].p
pipe1.mediums[5].h
pipe1.mediums[5].p
pipe2.mediums[1].h
pipe2.mediums[1].p
pipe2.mediums[2].h
pipe2.mediums[2].p
pipe2.mediums[3].h
pipe2.mediums[3].p
pipe2.mediums[4].h
pipe2.mediums[4].p
pipe2.mediums[5].h
pipe2.mediums[5].p
pipe3.mediums[1].h
pipe3.mediums[1].p
pipe3.mediums[2].h
pipe3.mediums[2].p
pipe3.mediums[3].h
pipe3.mediums[3].p
pipe3.mediums[4].h
pipe3.mediums[4].p
pipe3.mediums[5].h
pipe3.mediums[5].p
pipe4.mediums[1].h
pipe4.mediums[1].p
pipe4.mediums[2].h
pipe4.mediums[2].p
pipe4.mediums[3].h
pipe4.mediums[3].p
pipe4.mediums[4].h
pipe4.mediums[4].p
pipe4.mediums[5].h
pipe4.mediums[5].p
pipe5.mediums[1].h
pipe5.mediums[1].p
pipe5.mediums[2].h
pipe5.mediums[2].p
pipe5.mediums[3].h
pipe5.mediums[3].p
pipe5.mediums[4].h
pipe5.mediums[4].p
pipe5.mediums[5].h
pipe5.mediums[5].p
pipe6.mediums[1].h
pipe6.mediums[1].p
pipe6.mediums[2].h
pipe6.mediums[2].p
pipe6.mediums[3].h
pipe6.mediums[3].p
pipe6.mediums[4].h
pipe6.mediums[4].p
pipe6.mediums[5].h
pipe6.mediums[5].p
pipe7.mediums[1].h
pipe7.mediums[1].p
pipe7.mediums[2].h
pipe7.mediums[2].p
pipe7.mediums[3].h
pipe7.mediums[3].p
pipe7.mediums[4].h
pipe7.mediums[4].p
pipe7.mediums[5].h
pipe7.mediums[5].p
pipe8.mediums[1].h
pipe8.mediums[1].p
pipe8.mediums[2].h
pipe8.mediums[2].p
pipe8.mediums[3].h
pipe8.mediums[3].p
pipe8.mediums[4].h
pipe8.mediums[4].p
pipe8.mediums[5].h
pipe8.mediums[5].p
pipe9.mediums[1].h
pipe9.mediums[1].p
pipe9.mediums[2].h
pipe9.mediums[2].p
pipe9.mediums[3].h
pipe9.mediums[3].p
pipe9.mediums[4].h
pipe9.mediums[4].p
pipe9.mediums[5].h
pipe9.mediums[5].p
pipe10.mediums[1].h
pipe10.mediums[1].p
pipe10.mediums[2].h
pipe10.mediums[2].p
pipe10.mediums[3].h
pipe10.mediums[3].p
pipe10.mediums[4].h
pipe10.mediums[4].p
pipe10.mediums[5].h
pipe10.mediums[5].p
pipe11.mediums[1].h
pipe11.mediums[1].p
pipe11.mediums[2].h
pipe11.mediums[2].p
pipe11.mediums[3].h
pipe11.mediums[3].p
pipe11.mediums[4].h
pipe11.mediums[4].p
pipe11.mediums[5].h
pipe11.mediums[5].p
pipe12.mediums[1].h
pipe12.mediums[1].p
pipe12.mediums[2].h
pipe12.mediums[2].p
pipe12.mediums[3].h
pipe12.mediums[3].p
pipe12.mediums[4].h
pipe12.mediums[4].p
pipe12.mediums[5].h
pipe12.mediums[5].p
Finished
translate - Open log
Translation of ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings
The DAE has 5664 scalar unknowns and 5664 scalar equations.
Statistics
Original Model
Number of components: 516
Variables: 4811
Constants: 56 (56 scalars)
Parameters: 1181 (1497 scalars)
Unknowns: 3574 (5670 scalars)
Differentiated variables: 248 scalars
Equations: 2020
Nontrivial: 1420
Translated Model
Constants: 1990 scalars
Free parameters: 153 scalars
Parameter depending: 572 scalars
Continuous time states: 124 scalars
Time-varying variables: 1556 scalars
Alias variables: 2952 scalars
Number of mixed real/discrete systems of equations: 0
Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2}
Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0}
Sizes of nonlinear systems of equations: {15, 15}
Sizes after manipulation of the nonlinear systems: {4, 4}
Number of numerical Jacobians: 2
Initialization problem
Sizes of nonlinear systems of equations: {15, 15}
Sizes after manipulation of the nonlinear systems: {2, 2}
Number of numerical Jacobians: 2
Settings
Advanced.StoreProtectedVariables = true
Sparse solvers enabled: false
Enabled for integrator Jacobian: false
Model sparse and large enough: true.
Sparse solvers are available for dassl, lsodar, cvode, ida, radau, esdirk*, sdirk*.
Enable sparse solvers by setting Advanced.Translation.SparseActivate.
Selected continuous time states
Statically selected continuous time states
junction1.medium.h
junction1.medium.p
junction2.medium.h
junction2.medium.p
pipe1.mediums[1].h
pipe1.mediums[1].p
pipe1.mediums[2].h
pipe1.mediums[2].p
pipe1.mediums[3].h
pipe1.mediums[3].p
pipe1.mediums[4].h
pipe1.mediums[4].p
pipe1.mediums[5].h
pipe1.mediums[5].p
pipe2.mediums[1].h
pipe2.mediums[1].p
pipe2.mediums[2].h
pipe2.mediums[2].p
pipe2.mediums[3].h
pipe2.mediums[3].p
pipe2.mediums[4].h
pipe2.mediums[4].p
pipe2.mediums[5].h
pipe2.mediums[5].p
pipe3.mediums[1].h
pipe3.mediums[1].p
pipe3.mediums[2].h
pipe3.mediums[2].p
pipe3.mediums[3].h
pipe3.mediums[3].p
pipe3.mediums[4].h
pipe3.mediums[4].p
pipe3.mediums[5].h
pipe3.mediums[5].p
pipe4.mediums[1].h
pipe4.mediums[1].p
pipe4.mediums[2].h
pipe4.mediums[2].p
pipe4.mediums[3].h
pipe4.mediums[3].p
pipe4.mediums[4].h
pipe4.mediums[4].p
pipe4.mediums[5].h
pipe4.mediums[5].p
pipe5.mediums[1].h
pipe5.mediums[1].p
pipe5.mediums[2].h
pipe5.mediums[2].p
pipe5.mediums[3].h
pipe5.mediums[3].p
pipe5.mediums[4].h
pipe5.mediums[4].p
pipe5.mediums[5].h
pipe5.mediums[5].p
pipe6.mediums[1].h
pipe6.mediums[1].p
pipe6.mediums[2].h
pipe6.mediums[2].p
pipe6.mediums[3].h
pipe6.mediums[3].p
pipe6.mediums[4].h
pipe6.mediums[4].p
pipe6.mediums[5].h
pipe6.mediums[5].p
pipe7.mediums[1].h
pipe7.mediums[1].p
pipe7.mediums[2].h
pipe7.mediums[2].p
pipe7.mediums[3].h
pipe7.mediums[3].p
pipe7.mediums[4].h
pipe7.mediums[4].p
pipe7.mediums[5].h
pipe7.mediums[5].p
pipe8.mediums[1].h
pipe8.mediums[1].p
pipe8.mediums[2].h
pipe8.mediums[2].p
pipe8.mediums[3].h
pipe8.mediums[3].p
pipe8.mediums[4].h
pipe8.mediums[4].p
pipe8.mediums[5].h
pipe8.mediums[5].p
pipe9.mediums[1].h
pipe9.mediums[1].p
pipe9.mediums[2].h
pipe9.mediums[2].p
pipe9.mediums[3].h
pipe9.mediums[3].p
pipe9.mediums[4].h
pipe9.mediums[4].p
pipe9.mediums[5].h
pipe9.mediums[5].p
pipe10.mediums[1].h
pipe10.mediums[1].p
pipe10.mediums[2].h
pipe10.mediums[2].p
pipe10.mediums[3].h
pipe10.mediums[3].p
pipe10.mediums[4].h
pipe10.mediums[4].p
pipe10.mediums[5].h
pipe10.mediums[5].p
pipe11.mediums[1].h
pipe11.mediums[1].p
pipe11.mediums[2].h
pipe11.mediums[2].p
pipe11.mediums[3].h
pipe11.mediums[3].p
pipe11.mediums[4].h
pipe11.mediums[4].p
pipe11.mediums[5].h
pipe11.mediums[5].p
pipe12.mediums[1].h
pipe12.mediums[1].p
pipe12.mediums[2].h
pipe12.mediums[2].p
pipe12.mediums[3].h
pipe12.mediums[3].p
pipe12.mediums[4].h
pipe12.mediums[4].p
pipe12.mediums[5].h
pipe12.mediums[5].p
Finished
translate - Continuous time states
- junction1.medium.h
- junction1.medium.p
- junction2.medium.h
- junction2.medium.p
- pipe1.mediums[1].h
- pipe1.mediums[1].p
- pipe1.mediums[2].h
- pipe1.mediums[2].p
- pipe1.mediums[3].h
- pipe1.mediums[3].p
- pipe1.mediums[4].h
- pipe1.mediums[4].p
- pipe1.mediums[5].h
- pipe1.mediums[5].p
- pipe2.mediums[1].h
- pipe2.mediums[1].p
- pipe2.mediums[2].h
- pipe2.mediums[2].p
- pipe2.mediums[3].h
- pipe2.mediums[3].p
- pipe2.mediums[4].h
- pipe2.mediums[4].p
- pipe2.mediums[5].h
- pipe2.mediums[5].p
- pipe3.mediums[1].h
- pipe3.mediums[1].p
- pipe3.mediums[2].h
- pipe3.mediums[2].p
- pipe3.mediums[3].h
- pipe3.mediums[3].p
- pipe3.mediums[4].h
- pipe3.mediums[4].p
- pipe3.mediums[5].h
- pipe3.mediums[5].p
- pipe4.mediums[1].h
- pipe4.mediums[1].p
- pipe4.mediums[2].h
- pipe4.mediums[2].p
- pipe4.mediums[3].h
- pipe4.mediums[3].p
- pipe4.mediums[4].h
- pipe4.mediums[4].p
- pipe4.mediums[5].h
- pipe4.mediums[5].p
- pipe5.mediums[1].h
- pipe5.mediums[1].p
- pipe5.mediums[2].h
- pipe5.mediums[2].p
- pipe5.mediums[3].h
- pipe5.mediums[3].p
- pipe5.mediums[4].h
- pipe5.mediums[4].p
- pipe5.mediums[5].h
- pipe5.mediums[5].p
- pipe6.mediums[1].h
- pipe6.mediums[1].p
- pipe6.mediums[2].h
- pipe6.mediums[2].p
- pipe6.mediums[3].h
- pipe6.mediums[3].p
- pipe6.mediums[4].h
- pipe6.mediums[4].p
- pipe6.mediums[5].h
- pipe6.mediums[5].p
- pipe7.mediums[1].h
- pipe7.mediums[1].p
- pipe7.mediums[2].h
- pipe7.mediums[2].p
- pipe7.mediums[3].h
- pipe7.mediums[3].p
- pipe7.mediums[4].h
- pipe7.mediums[4].p
- pipe7.mediums[5].h
- pipe7.mediums[5].p
- pipe8.mediums[1].h
- pipe8.mediums[1].p
- pipe8.mediums[2].h
- pipe8.mediums[2].p
- pipe8.mediums[3].h
- pipe8.mediums[3].p
- pipe8.mediums[4].h
- pipe8.mediums[4].p
- pipe8.mediums[5].h
- pipe8.mediums[5].p
- pipe9.mediums[1].h
- pipe9.mediums[1].p
- pipe9.mediums[2].h
- pipe9.mediums[2].p
- pipe9.mediums[3].h
- pipe9.mediums[3].p
- pipe9.mediums[4].h
- pipe9.mediums[4].p
- pipe9.mediums[5].h
- pipe9.mediums[5].p
- pipe10.mediums[1].h
- pipe10.mediums[1].p
- pipe10.mediums[2].h
- pipe10.mediums[2].p
- pipe10.mediums[3].h
- pipe10.mediums[3].p
- pipe10.mediums[4].h
- pipe10.mediums[4].p
- pipe10.mediums[5].h
- pipe10.mediums[5].p
- pipe11.mediums[1].h
- pipe11.mediums[1].p
- pipe11.mediums[2].h
- pipe11.mediums[2].p
- pipe11.mediums[3].h
- pipe11.mediums[3].p
- pipe11.mediums[4].h
- pipe11.mediums[4].p
- pipe11.mediums[5].h
- pipe11.mediums[5].p
- pipe12.mediums[1].h
- pipe12.mediums[1].p
- pipe12.mediums[2].h
- pipe12.mediums[2].p
- pipe12.mediums[3].h
- pipe12.mediums[3].p
- pipe12.mediums[4].h
- pipe12.mediums[4].p
- pipe12.mediums[5].h
- pipe12.mediums[5].p
translate - Continuous time states
- junction1.medium.h
- junction1.medium.p
- junction2.medium.h
- junction2.medium.p
- pipe1.mediums[1].h
- pipe1.mediums[1].p
- pipe1.mediums[2].h
- pipe1.mediums[2].p
- pipe1.mediums[3].h
- pipe1.mediums[3].p
- pipe1.mediums[4].h
- pipe1.mediums[4].p
- pipe1.mediums[5].h
- pipe1.mediums[5].p
- pipe2.mediums[1].h
- pipe2.mediums[1].p
- pipe2.mediums[2].h
- pipe2.mediums[2].p
- pipe2.mediums[3].h
- pipe2.mediums[3].p
- pipe2.mediums[4].h
- pipe2.mediums[4].p
- pipe2.mediums[5].h
- pipe2.mediums[5].p
- pipe3.mediums[1].h
- pipe3.mediums[1].p
- pipe3.mediums[2].h
- pipe3.mediums[2].p
- pipe3.mediums[3].h
- pipe3.mediums[3].p
- pipe3.mediums[4].h
- pipe3.mediums[4].p
- pipe3.mediums[5].h
- pipe3.mediums[5].p
- pipe4.mediums[1].h
- pipe4.mediums[1].p
- pipe4.mediums[2].h
- pipe4.mediums[2].p
- pipe4.mediums[3].h
- pipe4.mediums[3].p
- pipe4.mediums[4].h
- pipe4.mediums[4].p
- pipe4.mediums[5].h
- pipe4.mediums[5].p
- pipe5.mediums[1].h
- pipe5.mediums[1].p
- pipe5.mediums[2].h
- pipe5.mediums[2].p
- pipe5.mediums[3].h
- pipe5.mediums[3].p
- pipe5.mediums[4].h
- pipe5.mediums[4].p
- pipe5.mediums[5].h
- pipe5.mediums[5].p
- pipe6.mediums[1].h
- pipe6.mediums[1].p
- pipe6.mediums[2].h
- pipe6.mediums[2].p
- pipe6.mediums[3].h
- pipe6.mediums[3].p
- pipe6.mediums[4].h
- pipe6.mediums[4].p
- pipe6.mediums[5].h
- pipe6.mediums[5].p
- pipe7.mediums[1].h
- pipe7.mediums[1].p
- pipe7.mediums[2].h
- pipe7.mediums[2].p
- pipe7.mediums[3].h
- pipe7.mediums[3].p
- pipe7.mediums[4].h
- pipe7.mediums[4].p
- pipe7.mediums[5].h
- pipe7.mediums[5].p
- pipe8.mediums[1].h
- pipe8.mediums[1].p
- pipe8.mediums[2].h
- pipe8.mediums[2].p
- pipe8.mediums[3].h
- pipe8.mediums[3].p
- pipe8.mediums[4].h
- pipe8.mediums[4].p
- pipe8.mediums[5].h
- pipe8.mediums[5].p
- pipe9.mediums[1].h
- pipe9.mediums[1].p
- pipe9.mediums[2].h
- pipe9.mediums[2].p
- pipe9.mediums[3].h
- pipe9.mediums[3].p
- pipe9.mediums[4].h
- pipe9.mediums[4].p
- pipe9.mediums[5].h
- pipe9.mediums[5].p
- pipe10.mediums[1].h
- pipe10.mediums[1].p
- pipe10.mediums[2].h
- pipe10.mediums[2].p
- pipe10.mediums[3].h
- pipe10.mediums[3].p
- pipe10.mediums[4].h
- pipe10.mediums[4].p
- pipe10.mediums[5].h
- pipe10.mediums[5].p
- pipe11.mediums[1].h
- pipe11.mediums[1].p
- pipe11.mediums[2].h
- pipe11.mediums[2].p
- pipe11.mediums[3].h
- pipe11.mediums[3].p
- pipe11.mediums[4].h
- pipe11.mediums[4].p
- pipe11.mediums[5].h
- pipe11.mediums[5].p
- pipe12.mediums[1].h
- pipe12.mediums[1].p
- pipe12.mediums[2].h
- pipe12.mediums[2].p
- pipe12.mediums[3].h
- pipe12.mediums[3].p
- pipe12.mediums[4].h
- pipe12.mediums[4].p
- pipe12.mediums[5].h
- pipe12.mediums[5].p
translate - Largest NL equation system
- 4
- 4
translate - Largest NL equation system
- 4
- 4
simulate - Open log
Log-file of program ./dymosim
(generated: Tue Feb 25 03:49:22 2025)
dymosim started
... "ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings" simulating
... "dsin.txt" loading (dymosim input file)
... "result.mat" creating (simulation result file)
Integration started at T = 0 using integration method DASSL
(DAE multi-step solver (dassl/dasslrt of Petzold modified by Dassault Systemes))
Error: The following error was detected at time: 2.40834336073673E-12
IF97 medium function visc_dTp: viscosity computed outside the range
of validity of the IF97 formulation: p = 100000 Pa, Tc = -73.1857 K
Failed condition: p <= 500000000.0 and (Tc >= 0.0 and Tc <= 150) or p <= 350000000.0 and (Tc > 150.0 and Tc <= 600) or p <= 300000000.0 and (Tc > 600.0 and Tc <= 900)
The stack of functions is:
Modelica.Media.Water.IF97_Utilities.dynamicViscosity
Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe6.flowModel.states[1].d, pipe6.flowModel.states[1].T, pipe6.flowModel.states[1].p, 0, true)
Modelica.Media.Water.WaterIF97_ph.dynamicViscosity_Unique8(
Modelica.Media.Water.WaterIF97_base.ThermodynamicState(
phase = pipe6.flowModel.states[1].phase,
h = pipe6.flowModel.states[1].h,
d = pipe6.flowModel.states[1].d,
T = pipe6.flowModel.st...
First evaluation failed for non-linear solver.
Error: The following error was detected at time: 2.40834336073673E-12
IF97 medium function visc_dTp: viscosity computed outside the range
of validity of the IF97 formulation: p = 100000 Pa, Tc = -73.1857 K
Failed condition: p <= 500000000.0 and (Tc >= 0.0 and Tc <= 150) or p <= 350000000.0 and (Tc > 150.0 and Tc <= 600) or p <= 300000000.0 and (Tc > 600.0 and Tc <= 900)
The stack of functions is:
Modelica.Media.Water.IF97_Utilities.dynamicViscosity
Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe6.flowModel.states[1].d, pipe6.flowModel.states[1].T, pipe6.flowModel.states[1].p, 0, true)
Modelica.Media.Water.WaterIF97_ph.dynamicViscosity_Unique8(
Modelica.Media.Water.WaterIF97_base.ThermodynamicState(
phase = pipe6.flowModel.states[1].phase,
h = pipe6.flowModel.states[1].h,
d = pipe6.flowModel.states[1].d,
T = pipe6.flowModel.st...
Non-linear solver will silently attempt to handle this problem.
Non-linear solver gave up after attempt: 2
Solver will attempt to handle this problem.
Error: The following error was detected at time: 2.008756569513019E-06
IF97 medium function visc_dTp: viscosity computed outside the range
of validity of the IF97 formulation: p = 104604 Pa, Tc = -23.135 K
Failed condition: p <= 500000000.0 and (Tc >= 0.0 and Tc <= 150) or p <= 350000000.0 and (Tc > 150.0 and Tc <= 600) or p <= 300000000.0 and (Tc > 600.0 and Tc <= 900)
The stack of functions is:
Modelica.Media.Water.IF97_Utilities.dynamicViscosity
Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe8.flowModel.states[7].d, pipe8.flowModel.states[7].T, pipe8.flowModel.states[7].p, 0, true)
Modelica.Media.Water.WaterIF97_ph.dynamicViscosity_Unique8(
Modelica.Media.Water.WaterIF97_base.ThermodynamicState(
phase = pipe8.flowModel.states[7].phase,
h = pipe8.flowModel.states[7].h,
d = pipe8.flowModel.states[7].d,
T = pipe8.flowModel.st...
First evaluation failed for non-linear solver.
Error: The following error was detected at time: 2.008756569513019E-06
IF97 medium function visc_dTp: viscosity computed outside the range
of validity of the IF97 formulation: p = 104604 Pa, Tc = -23.135 K
Failed condition: p <= 500000000.0 and (Tc >= 0.0 and Tc <= 150) or p <= 350000000.0 and (Tc > 150.0 and Tc <= 600) or p <= 300000000.0 and (Tc > 600.0 and Tc <= 900)
The stack of functions is:
Modelica.Media.Water.IF97_Utilities.dynamicViscosity
Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe8.flowModel.states[7].d, pipe8.flowModel.states[7].T, pipe8.flowModel.states[7].p, 0, true)
Modelica.Media.Water.WaterIF97_ph.dynamicViscosity_Unique8(
Modelica.Media.Water.WaterIF97_base.ThermodynamicState(
phase = pipe8.flowModel.states[7].phase,
h = pipe8.flowModel.states[7].h,
d = pipe8.flowModel.states[7].d,
T = pipe8.flowModel.st...
Non-linear solver will silently attempt to handle this problem.
Non-linear solver gave up after attempt: 2
Solver will attempt to handle this problem.
Integration terminated successfully at T = 20
CPU-time for integration : 4.5 seconds
CPU-time for one grid interval : 0.9 milliseconds
CPU-time for initialization : 0.004 seconds
Number of result points : 5004
Number of grid points : 5001
Number of accepted steps : 654
Number of f-evaluations (dynamics) : 1405
Number of crossing function evaluations : 5654
Number of Jacobian-evaluations : 110
Number of model time events : 2
Number of input time events : 0
Number of state events : 0
Number of step events : 0
Minimum integration stepsize : 4.01e-13
Maximum integration stepsize : 4.5
Maximum integration order : 5
Calling terminal section
... "dsfinal.txt" creating (final states)
SUCCESSFUL simulation of ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings
simulate - Open log
Log-file of program ./dymosim
(generated: Tue Feb 25 01:02:58 2025)
dymosim started
... "ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings" simulating
... "dsin.txt" loading (dymosim input file)
... "result.mat" creating (simulation result file)
Integration started at T = 0 using integration method DASSL
(DAE multi-step solver (dassl/dasslrt of Petzold modified by Dassault Systemes))
Error: The following error was detected at time: 2.40834336073673E-12
IF97 medium function visc_dTp: viscosity computed outside the range
of validity of the IF97 formulation: p = 100000 Pa, Tc = -73.1857 K
Failed condition: p <= 500000000.0 and (Tc >= 0.0 and Tc <= 150) or p <= 350000000.0 and (Tc > 150.0 and Tc <= 600) or p <= 300000000.0 and (Tc > 600.0 and Tc <= 900)
The stack of functions is:
Modelica.Media.Water.IF97_Utilities.dynamicViscosity
Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe6.flowModel.states[1].d, pipe6.flowModel.states[1].T, pipe6.flowModel.states[1].p, 0, true)
Modelica.Media.Water.WaterIF97_ph.dynamicViscosity_Unique8(
Modelica.Media.Water.WaterIF97_base.ThermodynamicState(
phase = pipe6.flowModel.states[1].phase,
h = pipe6.flowModel.states[1].h,
d = pipe6.flowModel.states[1].d,
T = pipe6.flowModel.st...
First evaluation failed for non-linear solver.
Error: The following error was detected at time: 2.40834336073673E-12
IF97 medium function visc_dTp: viscosity computed outside the range
of validity of the IF97 formulation: p = 100000 Pa, Tc = -73.1857 K
Failed condition: p <= 500000000.0 and (Tc >= 0.0 and Tc <= 150) or p <= 350000000.0 and (Tc > 150.0 and Tc <= 600) or p <= 300000000.0 and (Tc > 600.0 and Tc <= 900)
The stack of functions is:
Modelica.Media.Water.IF97_Utilities.dynamicViscosity
Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe6.flowModel.states[1].d, pipe6.flowModel.states[1].T, pipe6.flowModel.states[1].p, 0, true)
Modelica.Media.Water.WaterIF97_ph.dynamicViscosity_Unique8(
Modelica.Media.Water.WaterIF97_base.ThermodynamicState(
phase = pipe6.flowModel.states[1].phase,
h = pipe6.flowModel.states[1].h,
d = pipe6.flowModel.states[1].d,
T = pipe6.flowModel.st...
Non-linear solver will silently attempt to handle this problem.
Non-linear solver gave up after attempt: 2
Solver will attempt to handle this problem.
Error: The following error was detected at time: 2.008756569513019E-06
IF97 medium function visc_dTp: viscosity computed outside the range
of validity of the IF97 formulation: p = 104604 Pa, Tc = -23.135 K
Failed condition: p <= 500000000.0 and (Tc >= 0.0 and Tc <= 150) or p <= 350000000.0 and (Tc > 150.0 and Tc <= 600) or p <= 300000000.0 and (Tc > 600.0 and Tc <= 900)
The stack of functions is:
Modelica.Media.Water.IF97_Utilities.dynamicViscosity
Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe8.flowModel.states[7].d, pipe8.flowModel.states[7].T, pipe8.flowModel.states[7].p, 0, true)
Modelica.Media.Water.WaterIF97_ph.dynamicViscosity_Unique8(
Modelica.Media.Water.WaterIF97_base.ThermodynamicState(
phase = pipe8.flowModel.states[7].phase,
h = pipe8.flowModel.states[7].h,
d = pipe8.flowModel.states[7].d,
T = pipe8.flowModel.st...
First evaluation failed for non-linear solver.
Error: The following error was detected at time: 2.008756569513019E-06
IF97 medium function visc_dTp: viscosity computed outside the range
of validity of the IF97 formulation: p = 104604 Pa, Tc = -23.135 K
Failed condition: p <= 500000000.0 and (Tc >= 0.0 and Tc <= 150) or p <= 350000000.0 and (Tc > 150.0 and Tc <= 600) or p <= 300000000.0 and (Tc > 600.0 and Tc <= 900)
The stack of functions is:
Modelica.Media.Water.IF97_Utilities.dynamicViscosity
Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe8.flowModel.states[7].d, pipe8.flowModel.states[7].T, pipe8.flowModel.states[7].p, 0, true)
Modelica.Media.Water.WaterIF97_ph.dynamicViscosity_Unique8(
Modelica.Media.Water.WaterIF97_base.ThermodynamicState(
phase = pipe8.flowModel.states[7].phase,
h = pipe8.flowModel.states[7].h,
d = pipe8.flowModel.states[7].d,
T = pipe8.flowModel.st...
Non-linear solver will silently attempt to handle this problem.
Non-linear solver gave up after attempt: 2
Solver will attempt to handle this problem.
Integration terminated successfully at T = 20
CPU-time for integration : 4.51 seconds
CPU-time for one grid interval : 0.903 milliseconds
CPU-time for initialization : 0.004 seconds
Number of result points : 5004
Number of grid points : 5001
Number of accepted steps : 654
Number of f-evaluations (dynamics) : 1405
Number of crossing function evaluations : 5654
Number of Jacobian-evaluations : 110
Number of model time events : 2
Number of input time events : 0
Number of state events : 0
Number of step events : 0
Minimum integration stepsize : 4.01e-13
Maximum integration stepsize : 4.5
Maximum integration order : 5
Calling terminal section
... "dsfinal.txt" creating (final states)
SUCCESSFUL simulation of ModelicaTest.Fluid.TestComponents.Pipes.DynamicPipesAndFittings