FSD100MbP?h㈵>d "dfffffr@ϼ@Qiederror: 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 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 <x temperaturepressure compositionflow (@@Q@,@fffffD@@Fpressure temperatureflow compositionphase fraction @<@1233333@FIsentropic efficiencyPressure increase Energy demand @@LJ@.ffffff@F Heat dutyOutlet temperature M@33333V@6$@F Membrane areaTrans membrane pressure ratioDimensionless membrane area @U@Lb@@ I@@FMembrane modulePBio gasAUwNA\t44Bio gasGas separation caseư>MbP?MbP?MbP?K'C:\Program Files\COCO\data\ChemSep1.pcdVCarbon dioxideOCOCO2124-38-9O=C=O \s@)\A@b?@7? 8`k@`k@@A@7F@I??Y=p@<,?@A|th A3aA 8E@ @y2 8 8@3a@`k@ $@? \s@w? 8`k@ \s@iW@̯#( 0>@ k@ \s@ejtA]?@ݿ ?I?`k@ \s@j@3A@VN(7i?`./9@`k@d@5[@@ ?@S>`k@ r@@A@z~`P%@k൓,>I@@@`?KA@}`b^@@o@3c@@h @d Ra?@@`k@`fr@e>?=Jr@`f@ 8@e@@fϿ`Kܵ?`t>`k@r@K7@|~ܿ@ ш@R@A 8f@p@fЇpfܱ?]i`k@ \s@V@)\R@@> 8@o@@ 8 8 8 8 8 8 8C5@@0 8 8 \k@@p@ *È?D 8 8`k@`fr@ ڬ\m1@`"8d@>@?@?@?h?`q@`? 8 8h?}ͺ? 8 8 8?`f:@I?[_/ @`}g@ 8 W?`?ZWaterHOHH2O 7732-18-5O99@ uAz?@O?`fRw@`fq@`q@@2@ ??=^@ I9@qU?AӬ`@ AVA@_tA{J@` 8 8 8$m@`fq@ J{?x?`f:@?Qa@3o@Q:@iX@Y%@ó>@`frp@Q:@eFpAO?| :? :`fq@=:@j)hp࣐a@MоI =@33 @`fq@d0q@@a@eпf'?q@@3@@/@`0;@@`3c?I@@@4?`6l2vG)@`fq@@@h`f`@@Qx2@`T@q@@ 9@e@r>?`ff@ 8`q@Đ@f}@ K? 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L@Ø@ 8,K@x@f9(ɿ%ݿ`NSu +mI@b@@+=??#M@ 8N@@@f@y 1@`VVw?` ,K@`Rc@y@-`? 2 O>I@@@d 8 8 8 8 8 8 8 4@P@~? 8 8 7W@QXa@ a2 @)? 8 8.K@b@ yA@8bX9@@l?z?z?`t? @ ? 8 8փ? ? 8?3?w?L0@ൄ?@,j @d\@w? ?JMethaneCH4CH474-82-8Cg@6QA=?M?=[@jV@jV@@ 0@L2?+?9=@ u?*AWđTA,A$_A@@@-P$ 8 8`f&7@)V@M? ;6?g@p ? 8 V@Gg@iCF@(U?@T@g@e kAq@@ʡ@`_@V@g@j1@@`.@?@M6@@V@d@@ tH oͿ8b?p-V@g@@K2@"@b?@̧I@p@?Т9Ͽ]?yٿY@p@hF@]@31@ V@g@e >o?\@ 8V@@@fp??G?/وվ)V@f@`cU>X?L`^@ 8Q[@@fפ'@}iv@7(>V@$h@@ΧR`TR?`{2Yx>I@@@d 8 8 8 8 8 8 8t4@,@S? 8 8@ \@ _e@ n ⑘@> 8 8 V@g@ 6@&f@Xw@e#yA >?bb}t?ｿ̤e@v@jp@@^Z4 ?`DA4@@`@dp@@3Ï@ =n?pug@ w@M@?@@ɴ!@[? Y@p@ ]?55~@@3ySp@(@h@Q\p@fw {>@ug@u@e nb>@^?`tM@ 8$m@@3@f&@\Ͽ`d Ծ$h@`Fr@{|>k ?zH2OH2Oq= ףp?ffffff?jt2@>H2OH2Oq= 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 gasOxygen74-82-8Methane 0@=[@CH4Bio gasMethane 7783-06-4Hydrogen sulfideZ A@j@H2SBio gasHydrogen sulfide enthalpy.Dmoles?#logFugacityCoefficient.DmolFractionentropy.Dtemperature?enthalpy?vaporPressure.Dtemperature?enthalpy.DmolFraction?logFugacityCoefficiententhalpy.Dpressure?#logFugacityCoefficient.Dtemperatureentropy.Dpressure?enthalpy.Dtemperature?logFugacityCoefficient.Dmoles / molentropy.DmolFraction?entropy? logFugacityCoefficient.Dpressureentropy.Dmoles?@ppp&{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@ vaporPressurevaporPressure.Dtemperatureenthalpyenthalpy.Dmolesenthalpy.DmolFractionenthalpy.Dpressureenthalpy.DtemperaturelogFugacityCoefficientlogFugacityCoefficient.Dmoles#logFugacityCoefficient.DmolFraction logFugacityCoefficient.Dpressure#logFugacityCoefficient.DtemperaturebubblePointTemperaturebubblePointPressuredewPointTemperaturedewPointPressureentropyentropy.Dmolesentropy.DmolFractionentropy.Dpressureentropy.DtemperatureVapor Vapor phaseBio gasVaporLiquid Liquid phaseBio gasLiquid VaporLiquiddefaultdefault material templateBio gas Bio gas feed 4mole fractions for material 1 do not sum up to unityH‰default?@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/,2,2 default0Afffff2t@Tn o$@3?z ?:2F?=M' w?=ѯKp?K0 ?%G?K1#$$?3zD?T~:??&&?Y]?? z ?:2F?=M' w?>ѯKp?M0 ?%G?L1#$$?3zD?T~:??&&?Y]?2 Purified gasBaNBaBFFa ?mole fractions for material Purified gas do not sum up to unity default0Afffff2t@J !@ZS?&j?,V(B? `?@c?=( pU]?4qT?*?if?NVH?E?^ ?Qa }?xJbI??&j?,V(B? `?@c?=( pU]?4qT?*?if?NVH?E?^ ?Qa }?xJbI?24@JD@J@@J 4mole fractions for material 4 do not sum up to unitydefaultAfffff2t@OH?b?cϾ$?X}H?vCM?Ug~?)}?L?_ ?~hVDž?ZR,+?V?T?5ڶ?{\Ti*??hϾ$?]}H?~CM?Ug~?-}?Q?_ ?hVDž?ZR,+?V?T?;ڶ?\Ti*?25("(( default0AQXV}'@Tn o$@3?z ?:2F?=M' w?=ѯKp?K0 ?%G?K1#$$?3zD?T~:??&&?Y]??z ?:2F?=M' w?=ѯKp?K0 ?%G?K1#$$?3zD?T~:??&&?Y]?2Permate recycleP. Q PQQ   defaultAfffff2t@OH?b?cϾ$?X}H?vCM?Ug~?)}?L?_ ?~hVDž?ZR,+?V?T?5ڶ?{\Ti*??hϾ$?]}H?~CM?Ug~?-}?Q?_ ?hVDž?ZR,+?V?T?;ڶ?\Ti*?2 Waste gasPaXPaPa defaultAfffff2t@vel?d#?cϾ$?X}H?vCM?Ug~?)}?L?_ ?~hVDž?ZR,+?V?T?5ڶ?{\Ti*??hϾ$?]}H?~CM?Ug~?-}?Q?_ ?hVDž?ZR,+?V?T?;ڶ?\Ti*?28 default?@j-iar@Tn o$@3?z ?:2F?=M' w?=ѯKp?K0 ?%G?K1#$$?3zD?T~:??&&?Y]??z ?:2F?=M' w?=ѯKp?K0 ?%G?K1#$$?3zD?T~:??&&?Y]?2 Compressor@Compressor - unit increasing the pressure due to the work input.ɝBsIEGr־y1&COUSCOUS0001Pressure spec.Type of pressure specificationPressure increasePressure increasePressure increasePressure Energy 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@?@˕@@xDIsentropic efficiency6Isentropic efficiency at which the compressor operates???Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1 $not all material ports are connectedInletOutlet@@?K(^&? @? @@?:t= @@?:t= @@?:t= @@?:t= @@?:t= @@@CoolerMHeaterCooler - heat or cool stream specifying heat duty or outlet temperaturez,wKJEKBCOUSCOUS0001TypeType of heat duty specification Temperature Heat duty Heat duty Temperature Energy inletOutlet temperature!Temperature of the product stream?fffff2t@r@ _B Heat duty Heat duty@?@sM%0@x@xD Pressure dropPressure drop along the unit?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1(, $not all material ports are connectedInletOutlet b)lb)lb)lb)l@@ ɿ@????@@@@@ɿ@@@Splitter9Splitter - split input stream in number of output streams<3ARby2COUSCOUS0001Number 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 version1.11.01.01.1JP $not all material ports are connectedInletOutlet1Outlet20@@@@@@@ @Mixer6Mixer - mix 2 or more inlet streams to a single outletk!^/E a-&COUSCOUS0001Number of inletsNumber of inlet ports Pressure dropPressure drop along the mixer?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1 $not all material ports are connectedInlet 1Inlet 2Outlet0@@@@@@@ @SciLab Unit Operation_73Unit operation using SciLab script for calculations0 3=GBGABuHDPK;h unit.xmlVmO0_q$kiShbRY ~Ib79NW]8} m%}܋ZD!̙x"d> +ˌ/b.)T"ɚFlB@6r &BBL#z|D`4PSIs0pP"$3Uȓ0!zB( }HT0AroG<~O`m¹{= 3?qt?+KA"`F3XJՍcnw`N\)9P#,T*ٴ.䚱i P[0BC,sy4E-W8 PVe68a"belXwFc^|Di [Vثn|,x%0]M M-R ,v*"VҲz(ҫhgVTǴv7 ! 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