FSD100MbP?h㈵>d{ 9dfffffr@ϼ@QiedJasper
PStarting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Membrane unit, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell: Solver encountered an error value in a target or constraint cell.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Membrane unit, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
error: Cannot edit: failed to edit object: Failed to get output parameters after edit: Failed to get output parameter values from Excel: unexpected format
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
error: calculate failed for unit Membrane unit: Failed to obtain output parameter values: Failed to get output parameter values from Excel: unexpected format
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Membrane unit, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 5 iterations
Solve finished in 6s, 953ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
user abort
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
(last message repeated 1 time)
Saved Bio gas sep 3.fsd
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Application-defined or object-defined error
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Application-defined or object-defined error
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Application-defined or object-defined error
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Application-defined or object-defined error
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Application-defined or object-defined error
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Application-defined or object-defined error
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Application-defined or object-defined error
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Application-defined or object-defined error
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Application-defined or object-defined error
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Membrane unit, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver encountered an error value in a target or constraint cell.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver encountered an error value in a target or constraint cell.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Membrane unit, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Saved Bio gas sep 3.fsd
(last message repeated 1 time)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Membrane unit, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Membrane unit, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Saved Bio gas sep 3.fsd
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Membrane unit, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Saved Bio gas sep 3.fsd
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
user abort
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
(last message repeated 1 time)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 6 iterations
Solve finished in 18s, 94ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Saved Bio gas sep 3.fsd
Restoring flowsheet from file
Loaded Bio gas sep 3.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 2s, 204ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 6 iterations
Solve finished in 14s, 531ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 6 iterations
Solve finished in 14s, 704ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
user abort
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 6 iterations
Solve finished in 15s, 125ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Saved Bio gas sep 3.fsd
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
user abort
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 6 iterations
Solve finished in 14s, 579ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
user abort
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
user abort
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
converged at initial guess
Solve finished in 2s, 47ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
user abort
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
converged in 9 iterations
Solve finished in 11s, 547ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 3.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 2s, 453ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
user abort
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Saved Bio gas sep 3.fsd
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 2 iterations
Solve finished in 5s, 0ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
user abort
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
converged in 10 iterations
Solve finished in 22s, 16ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Saved Bio gas sep 3.fsd
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 8 iterations
Solve finished in 7s, 625ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 7 iterations
Solve finished in 6s, 219ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 6 iterations
Solve finished in 5s, 594ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 4 iterations
Solve finished in 3s, 859ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 797ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Saved Bio gas sep 3.fsd
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 7 iterations
Solve finished in 7s, 110ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Saved Bio gas sep 3.fsd
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model GPModell2: Solver could not find a feasible solution.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Membrane unit, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 6 iterations
Solve finished in 15s, 15ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 3.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 3s, 391ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
error: Cannot edit: failed to edit object: Failed to get output parameters after edit: Failed to get output parameter values from Excel: unexpected format
(last message repeated 1 time)
Saved Bio gas sep 4.fsd
error: Cannot edit: failed to edit object: Failed to get output parameters after edit: Failed to get output parameter values from Excel: unexpected format
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
error: calculate failed for unit Membrane unit: Failed to run solver model InitModell2: Solver could not find a feasible solution.
user abort
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Saved Bio gas sep 4.fsd
(last message repeated 1 time)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 5 iterations
Solve finished in 13s, 953ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 2s, 328ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Saved Bio gas sep 4.fsd
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 5 iterations
Solve finished in 13s, 625ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 7 iterations
Solve finished in 18s, 641ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
error: Cannot edit: failed to edit object: Failed to get output parameters after edit: Failed to get output parameter values from Excel: unexpected format
error: Cannot edit: failed to edit object: Invalid parameters after edit: One or more parameters with duplicate name (Module cut rate th). Parameter names must be unique.
error: Cannot edit: failed to edit object: Failed to get output parameters after edit: Failed to get output parameter values from Excel: unexpected format
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 2s, 375ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 4.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 2s, 906ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 2s, 453ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 4.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 2s, 422ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 4.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 2s, 734ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 3 iterations
Solve finished in 10s, 109ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 3 iterations
Solve finished in 10s, 125ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 3 iterations
Solve finished in 10s, 62ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 16 iterations
Solve finished in 42s, 265ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 2s, 500ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
8solving Mixer Splitter Membrane unit Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 4 iterations
Solve finished in 12s, 312ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 4.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
0inserted unit operation Excel Unit Operation_6
@INLET stream 2 disconnected from unit Membrane unit, port Feed
QOUTLET stream Purified gas disconnected from unit Membrane unit, port Retentate
EOUTLET stream 4 disconnected from unit Membrane unit, port Permeate
Iconnected stream 2 to unit Excel Unit Operation_6 as INLET at port Feed
Zconnected stream Purified gas to unit Excel Unit Operation_6 as OUTLET at port Retentate
?warning: no route found for stream 4; using most direct route
!(last message repeated 8 times)
?warning: no route found for stream 4; using most direct route
!(last message repeated 2 times)
?warning: no route found for stream 4; using most direct route
Nconnected stream 4 to unit Excel Unit Operation_6 as OUTLET at port Permeate
?warning: no route found for stream 4; using most direct route
(last message repeated 1 time)
?warning: no route found for stream 4; using most direct route
(last message repeated 1 time)
?warning: no route found for stream 4; using most direct route
Restoring flowsheet from file
Loaded Bio gas sep 5.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
Asolving Mixer Splitter Excel Unit Operation_6 Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Excel Unit Operation_6, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
NOUTLET stream 4 disconnected from unit Excel Unit Operation_6, port Permeate
Nconnected stream 4 to unit Excel Unit Operation_6 as OUTLET at port Permeate
Starting solve
Asolving Mixer Splitter Excel Unit Operation_6 Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Excel Unit Operation_6, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Saved Bio gas sep 5.fsd
(last message repeated 1 time)
Starting solve
Asolving Mixer Splitter Excel Unit Operation_6 Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
error: calculate failed for unit Excel Unit Operation_6: Failed to run solver model InitModell1: Application-defined or object-defined error
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, Excel Unit Operation_6, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
Saved Bio gas sep 5.fsd
Starting solve
Asolving Mixer Splitter Excel Unit Operation_6 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 4s, 110ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 5.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
Asolving Mixer Splitter Excel Unit Operation_6 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 4s, 719ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 5.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
Asolving Mixer Splitter Excel Unit Operation_6 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 3s, 360ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 5.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Saved Bio gas sep 5.fsd
Starting solve
Asolving Mixer Splitter Excel Unit Operation_6 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 3s, 265ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 5.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Starting solve
?solving Mixer Splitter Excel membrane model Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 3s, 250ms
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas sep 5.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
Restoring flowsheet from file
Loaded Bio gas separation.fsd
warning: Material object error in CalcProp: CalcSinglePhaseProp failed for phase Vapor: property dewPointTemperature is not configured for the Vapor phase
!(last message repeated 3 times)
?warning: no route found for stream 2; using most direct route
Jwarning: no route found for stream Purified gas; using most direct route
?warning: no route found for stream 4; using most direct route
?warning: no route found for stream 2; using most direct route
!(last message repeated 2 times)
?warning: no route found for stream 4; using most direct route
(last message repeated 1 time)
?warning: no route found for stream 4; using most direct route
Jwarning: no route found for stream Purified gas; using most direct route
!(last message repeated 6 times)
Jwarning: no route found for stream Purified gas; using most direct route
(last message repeated 1 time)
Restoring flowsheet from file
Loaded Bio gas separation.fsd
1inserted unit operation SciLab Unit Operation_7
Restoring flowsheet from file
Loaded Bio gas separation.fsd
>INLET stream 2 disconnected from unit HF Membrane, port Feed
OOUTLET stream Purified gas disconnected from unit HF Membrane, port Retentate
COUTLET stream 4 disconnected from unit HF Membrane, port Permeate
Kconnected stream 2 to unit SciLab Unit Operation_7 as INLET at port Feed
[connected stream Purified gas to unit SciLab Unit Operation_7 as OUTLET at port Retentate
Oconnected stream 4 to unit SciLab Unit Operation_7 as OUTLET at port Permeate
Saved Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 4 iterations
Solve finished in 4s, 609ms
Saved Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 1s, 140ms
Restoring flowsheet from file
Loaded Bio gas separation.fsd
Restoring flowsheet from file
Loaded Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 1s, 406ms
Restoring flowsheet from file
Loaded Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 11s, 438ms
Restoring flowsheet from file
Loaded Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 1s, 125ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
@error: calculate failed for unit SciLab Unit Operation_7: test
@error: calculate failed for unit SciLab Unit Operation_7: test
@error: calculate failed for unit SciLab Unit Operation_7: test
@error: calculate failed for unit SciLab Unit Operation_7: test
@error: calculate failed for unit SciLab Unit Operation_7: test
@error: calculate failed for unit SciLab Unit Operation_7: test
@error: calculate failed for unit SciLab Unit Operation_7: test
@error: calculate failed for unit SciLab Unit Operation_7: test
@error: calculate failed for unit SciLab Unit Operation_7: test
@error: calculate failed for unit SciLab Unit Operation_7: test
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, SciLab Unit Operation_7, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 1s, 141ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
Terror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: Qref
Terror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: Qref
Terror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: Qref
Terror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: Qref
Terror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: Qref
Terror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: Qref
Terror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: Qref
Terror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: Qref
Terror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: Qref
Terror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: Qref
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, SciLab Unit Operation_7, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
Saved Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
Werror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: gpcount
Werror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: gpcount
Werror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: gpcount
Werror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: gpcount
Werror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: gpcount
Werror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: gpcount
Werror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: gpcount
Werror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: gpcount
Werror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: gpcount
Werror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: gpcount
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, SciLab Unit Operation_7, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
Saved Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, SciLab Unit Operation_7, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
gerror: calculate failed for unit SciLab Unit Operation_7: Undefined operation for the given operands.
gerror: calculate failed for unit SciLab Unit Operation_7: Undefined operation for the given operands.
gerror: calculate failed for unit SciLab Unit Operation_7: Undefined operation for the given operands.
gerror: calculate failed for unit SciLab Unit Operation_7: Undefined operation for the given operands.
gerror: calculate failed for unit SciLab Unit Operation_7: Undefined operation for the given operands.
gerror: calculate failed for unit SciLab Unit Operation_7: Undefined operation for the given operands.
gerror: calculate failed for unit SciLab Unit Operation_7: Undefined operation for the given operands.
gerror: calculate failed for unit SciLab Unit Operation_7: Undefined operation for the given operands.
gerror: calculate failed for unit SciLab Unit Operation_7: Undefined operation for the given operands.
gerror: calculate failed for unit SciLab Unit Operation_7: Undefined operation for the given operands.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, SciLab Unit Operation_7, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
Zerror: calculate failed for unit SciLab Unit Operation_7: Submatrix incorrectly defined.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, SciLab Unit Operation_7, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
message: TEA warning: PS inside-out flash failed: Post flash PS test failed; entropy target not met (converged to invalid solution)
message: TEA warning: PS inside-out flash failed: Post flash PS test failed; entropy target not met (converged to invalid solution)
user abort
Solve failed
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 4 iterations
Solve finished in 3s, 515ms
Restoring flowsheet from file
Loaded Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
]error: calculate failed for unit SciLab Unit Operation_7: Missing permeability data for CH4
]error: calculate failed for unit SciLab Unit Operation_7: Missing permeability data for CH4
]error: calculate failed for unit SciLab Unit Operation_7: Missing permeability data for CH4
]error: calculate failed for unit SciLab Unit Operation_7: Missing permeability data for CH4
]error: calculate failed for unit SciLab Unit Operation_7: Missing permeability data for CH4
]error: calculate failed for unit SciLab Unit Operation_7: Missing permeability data for CH4
]error: calculate failed for unit SciLab Unit Operation_7: Missing permeability data for CH4
]error: calculate failed for unit SciLab Unit Operation_7: Missing permeability data for CH4
]error: calculate failed for unit SciLab Unit Operation_7: Missing permeability data for CH4
user abort
Solve failed
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 5 iterations
Solve finished in 11s, 860ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 1s, 359ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 4 iterations
Solve finished in 8s, 625ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 1s, 110ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 5 iterations
Solve finished in 4s, 640ms
Saved Bio gas separation.fsd
(last message repeated 1 time)
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: c
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: c
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: c
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: c
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: c
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: c
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: c
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: c
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: c
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: c
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, SciLab Unit Operation_7, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
Saved Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: z
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: z
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: z
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: z
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: z
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: z
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: z
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: z
Qerror: calculate failed for unit SciLab Unit Operation_7: Undefined variable: z
user abort
Solve failed
Saved Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
error: calculate failed for unit SciLab Unit Operation_7: msprintf: Wrong value of input argument 1: data doesn't fit with format.
unable to find initial guesses for cut stream Permate recycle for solving units Mixer, Compressor, Cooler, SciLab Unit Operation_7, Splitter: Please change or set the initial guess(es) or reset the flowsheet and try again
Solve failed
Saved Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 5 iterations
Solve finished in 4s, 797ms
Saved Bio gas separation.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 813ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 781ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 921ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 5 iterations
Solve finished in 4s, 562ms
Saved Bio gas separation.fsd
Restoring flowsheet from file
&Loaded Bio gas separation Scilab.fsd
Restoring flowsheet from file
&Loaded Bio gas separation Scilab.fsd
Restoring flowsheet from file
&Loaded Bio gas separation Scilab.fsd
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 1s, 219ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 1s, 110ms
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 1s, 94ms
Restoring flowsheet from file
#Loaded BioGasSeparationScilab.fsd
added property volume
added property volume.Dmoles
$added property volume.DmolFraction
!added property volume.Dpressure
$added property volume.Dtemperature
Starting solve
Bsolving Mixer Splitter SciLab Unit Operation_7 Cooler Compressor
-Cutting self-recycle stream Permate recycle
converged in 1 evaluation
Solve finished in 719ms
"Saved BioGasSeparationScilab.fsd
<xtemperaturepressurecompositionflowdddDefaultddsPBio gasAUwNA\t6|6Bio gasGas separation caseư>MbP?MbP?MbP?K'C:\Program Files\COCO\data\ChemSep1.pcdCarbon dioxideOCOCO2124-38-9O=C=O \s@)\A@b?@7? 8`k@`k@@A@7F@I??Y=p@<,?@A|th
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ףp?ffffff?jt2@V瞯<Bio gas124-38-9Carbon dioxide@7F@CO2Bio gasCarbon dioxide 7732-18-5Water2@`fRw@H2OBio gasWater 7727-37-9Nitrogen<@`fVS@N2Bio gasNitrogen 7782-44-7Oxygen?@@V@O2Bio gasOxygen74-82-8Methane0@=[@CH4Bio gasMethane 7783-06-4Hydrogen sulfideZ
A@j@H2SBio gasHydrogen sulfide
????????????vaporpressure.dtemperature??entropy.dtemperature??enthalpy.dmoles??enthalpy??#logfugacitycoefficient.dmolfraction#logfugacitycoefficient.dtemperaturelogfugacitycoefficiententhalpy.dmolfraction??enthalpy.dpressure??entropy.dpressure??enthalpy.dtemperature??entropy.dmolfraction??logfugacitycoefficient.dmoles / molentropy?? logfugacitycoefficient.dpressureentropy.dmoles??volume@@@@
volume.dmoles@@@@volume.dmolfraction@@@@volume.dpressure@@@@volume.dtemperature@@@@@&{429DC999-9073-4549-8647-BA72D6BE7931}Pressure increase??Pressure??
Energy demand??Isentropic efficiency??TotalMassBalancePropertiesFraction??
TotalFlowMass??&{779B2C7A-F54B-4A1D-B345-7FA14B889642}Outlet temperature?? Heat duty??
Pressure drop??&{33C43C04-EDAD-41A9-A952-62CDDCF67932}
Pressure drop??&{CA13AF07-5E91-4552-B740-E293397A2056}
Membrane area@@8Q(ref) (1 [Nm3/(h*m^2*bar)] = 1.239E-7 [mol/(s*m^2*Pa)])????Permeate pressure??Feed side pressure drop??Permeate side pressure drop??+Reference permeance Q(ref) [mol/(s*m^2*Pa)]????&{3D330930-C48E-47D6-B9BB-424741D04275}Area@@
Membrane area@@
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volume.Dmolesvolume.DmolFractionvolume.Dpressurevolume.DtemperatureVaporVapor phaseBio gasVaporLiquidLiquid phaseBio gasLiquidVaporLiquiddefaultdefault material templateBio gasBio gas feed4mole fractions for material 1 do not sum up to unityHdefault?@fffffRr@#@K@??Y%=D?{Gzt?m]m?Q?+7E?{Gz?XUŝN?333333?ԫeH?Q?m???Y%=D?zGzt?m]m?Q?+7E?{Gz?XUŝN?333333?ԫeH?Q?m?oEz>85?{?6?&{Jd>G2o>%gȐ>~PaΝ>[t>m>m??Y%=D?{Gzt?m]m?Q?+7E?{Gz?XUŝN?333333?ԫeH?Q?m?fffffRr@?@#@K@?22,2/,2,2default0Afffff2t@NAo$@?w
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Compressor@Compressor - unit increasing the pressure due to the work input.ɝBsIEGr־y1
COUSCOUS0007 Pressure spec.Type of pressure specificationPressure increasePressure increasePressure increasePressurePressure ratioVoume ratioEnergy spec.Type of energy specification
Efficiency
Efficiency
Energy demand
EfficiencyEnergy specification streamPressure increaseCompressor pressure increase??.A _BPressureCompressor outlet pressure?0Aj@ _B
Energy demand!Energy consumed by the compressor@?@7E˕@@xDIsentropic efficiency6Isentropic efficiency at which the compressor operates???Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Pressure ratio9Pressure ratio: outlet pressure divided by inlet pressure3OK%@?? _BVolume ratio8Compression ratio: inlet volume divided by outlet volume`L@?? _BLast run.+++ specifications +++
Pressure increase: 1000000 Pa
Isentropic efficiency: 0.75
+++ optional parameters +++
Pressure: 1101300 Pa
Pressure increase: 1000000 Pa
Pressure ratio: 10.8716683119447
Volume ratio: 5.82502575782445
Energy demand: 104796.742415686 W
Isentropic efficiency: 0.75
$not all material ports are connectedInletOutlet@@?K(^&?
@?
@@?:t=
@@?:t=
@@?:t=
@@?:t=
@@?:t=
@@@CoolerMHeaterCooler - heat or cool stream specifying heat duty or outlet temperaturez,wKJEKB
COUSCOUS0007TypeType of heat duty specificationTemperature Heat duty Heat dutyTemperatureEnergy inletOutlet temperature!Temperature of the product stream?fffff2t@r@ _B Heat duty Heat duty@?@v%0@x@xD
Pressure dropPressure drop along the unit?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++
Heat duty: -94227.0091698671 W
Pressure drop: 0 Pa
+++ optional parameters +++
Outlet temperature: 323.15 K
(,$not all material ports are connectedInletOutlet
b)lb)lb)lb)l@@ ɿ@????@@@@@ɿ@@@Splitter9Splitter - split input stream in number of output streams<3ARby2COUSCOUS0007Number of outletsNumber of outlet ports
Split factors!Split factors for (n - 1) outlets??
Pressure drop Pressure drop along the splitter?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run^+++ specifications +++
Number of outlets: 2
Split factors: [ 0.75]
Pressure drop: 0 Pa
JP$not all material ports are connectedInletOutlet1Outlet20@@@@@@@ @Mixer6Mixer - mix 2 or more inlet streams to a single outletk!^/Ea-COUSCOUS0007Number of inletsNumber of inlet ports
Pressure dropPressure drop along the mixer?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last runD+++ specifications +++
Number of inlets: 2
Pressure drop: 0 Pa
$not all material ports are connectedInlet 1Inlet 2Outlet0@@@@@@@ @SciLab Unit Operation_73Unit operation using SciLab script for calculations0 3=GBGABuOKPK$Ee t|
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unit.xmlPK$E=k;calcPK$Ef {qOgpcross.sciPKzSciLab Unit Operation File2B(Product port "Permeate" is not connectedFeed RetentatePermeate
?0@@?????@.@?.@@ ?@.@@@.@@@.@@@.@@@.@@@.@@@.@@ @"@MS Sans-C6?-C6?h㈵>-C6? (@@Q@,@fffffD@@Fpressuretemperatureflowcompositionphase fraction@<@1233333@FIsentropic efficiencyPressure increase
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Membrane areaTrans membrane pressure ratioDimensionless membrane area@U@Lb@@ I@@FMembrane modulePׁ?ׁ?ׁ?ׁ??__