FLOWNEX SE 8.12.7 (2021)

FLOWNEX SE 8.12.7 (2021)

The latest release of Flownex® for 2021 comes with much anticipated enhancements and fixes to ensure that you can do even more with real world systems simulation.

Some of these include the option to initialise the steady state solver from a previously saved snap, specifying transient actions through tables, python link functionality. With the support of Adobe Flash having come to an end we have updated our video tutorials to now work with HTML5.



Start Steady State from Previous Conditions

A steady state solve can now be initialised from conditions from any saved snap. The user can use this to initialise a steady state solution from a previous steady state solution or from a transient run.

The setting can be activated on the Flow Solver Properties Inputs window, where the related snap can be selected, as seen in Figure 1.

Fig. 1 - Initialise Steady State from Snap Option in Flow Solver Inputs

Action Specifications via Tables

A table can now be used to specify the value of an input at a specified time in an action. The table allows the user to copy and paste data from Excel. Values will be extrapolated if the time values fall outside the range specified in the table.

Fig. 2 - Table Input Option in Actions

Video Tutorials

The video tutorials in the Flownex® startup page that used Adobe Flash has been replaced by HTML5 videos. This was necessitated by Adobe not supporting Flash since 1 January 2021.
Fig. 3 - Flownex Video Tutorials


Caesar II Link

  • The handling of structural only rigids with the CAESAR II importer has been improved. They are now ignored and not imported at all.

Global Parameters

  • The way global parameters are handled with snaps has been improved. The values will be read in from a snap. The number of parameters and the number of associated properties (as well as which properties are associated) will not be changed when reading in a snap.

Python Link

  • The Python API files now contains a function that allows the user to run the Flownex® Designer using Python.

Finned Tube Heat Exchanger

  • Added an improved default Finned Tube Heat Transfer calculation example script for the Finned Tube Heat Exchanger – Fin Side.
  • The description of the input “Tube pass length” has been changed to clarify that this input represents the total primary flow path length.

License Borrowing

  • The maximum number of days a license can be borrowed, as specified in the server license file, is now indicated on the Borrow License dialog, rather than the default 28 days.
Fig. 4 - Number of Days to Borrow License from Server

Energy Solver Convergence Enhancement

  • The warnings associated with node temperature changes were enhanced to facilitate the identification of the non-converged node.
  • An option was added to the Flow Solver settings to exclude nodes with temperature changes as a result of very small mass flows in its associated flow element.
Fig. 5 - Apply Mass Flow Rate Threshold to Transient Temperature Change Residual


Excel Reporting

  • Fixed the problem where the option to “open in Excel” sometimes opened multiple copies of the Excel template.

Parameter Display

  • Fixed the problem where the parameter display did not work correctly during transient, which sometimes caused the application to terminate.

Heat Transfer Correlations

  • Fixed the problem where a warning was shown when the Gnielinski correlation was used that stated that the roughness used in the correlation is different from the Pipe roughness, even when the user specified the option that the roughness from the Pipe should be used.

Isentropic Head Compressor

  • Updated the maximum number of constant speed curves (61 to 101), data elements in a row (61 to 101) and constant blade angle maps (31 to 51) for the Isentropic Head Compressor Chart.

Variable Speed Pump

  • Fixed the pump shut down speed option that did not execute correctly.
  • Fixed the unit problem with pump shut down speed.

Slurry Flow

  • Fixed the vertical slurry frictional pressure drop calculation, which used the mixture density instead of fines density.


  • Changed the two-phase Bend gross secondary loss factor to display results without multiplication factors.

Flow Path Graph

  • Fixed the bug where the unit of a plotted line item is not removed when the Property is changed to a unitless property.

FLOWNEX SE 8.12.6 (2020 – UPDATE 2)

FLOWNEX SE 8.12.6 (2020 – UPDATE 2)

The second update of Flownex® SE for 2020 further expands the possibilities of simulating real-world systems.

Exciting features for this update are a reworked deep solver coupling with Ansys Mechanical for explicit transient co-simulation and automated Nuclear Reactor building script along with many minor enhancements described below.



Ansys Mechanical Coupling

The Ansys Mechanical Flow Solver Coupling component has been improved to allow the simulation of complex 3D conduction and stress in Ansys Mechanical coupled to a flow and heat transfer simulation in Flownex®. This enhancement includes the addition of a deep solver coupling between Flownex® and Ansys Mechanical, allowing data exchange between iterations, full transient co-simulation functionality and unit integration.
Figure 1: Ansys Mechanical Coupling

Nuclear Reactor Builder Scripts

Script Generated Reactor Results

Results in tabular form corresponding to the grid layout of the generated reactor network are written to a text file in the ScriptResults subfolder of the project folder. The tabular results are reported at the end of a steady state run as well as during user specified times and at the end of transient runs. A feature is provided to specify output variables that are reported at every time step. These results are written to a comma separated values (csv) file as a time series residing in the ScriptResults subfolder.

Reactor Generation Script

Various improvements were made to the geometric parameter calculations. Network topology generation for the transitions between different types of reactor zones was extended.

Figure 2: Reactor Generation Script Enhancements



The “Description”, “Minimum” and “Maximum” values have been added to the imported FMU variables. The description will be displayed if it is not blank. Minimum and maximum values will be displayed if they are specified in the FMU and the “Display variable information” property is turned on. A warning is given if the minimum or maximum values for inputs are exceeded.

Figure 3: Description, Minimum and Maximum Values added to Imported FMU’s


The License modules selection have been updated so that it can work for users that do not have write access to their ProgramData folders.


  • Functions to retrieve minimum and maximum temperatures and pressures, as well as critical temperatures and pressures from two-phase fluids via Scripts have been added.
  • Added the ability for Scripts to properly work with lists and Snaps – functions were added that get called in the Script before and after loading and saving Snaps. This gives users flexibility to implement their own Snap saving and loading code.

Composite Heat Transfer Component

The “Area multiplication factor” input for the Composite Heat Transfer (CHT) component has been moved to a separate category to indicate that the input is applied to all surfaces.

Figure 4: Area Multiplication Factor Moved to Separate Category



Fixed the problem where many of the modules were missing when using a borrowed license from the server.

Find Dialog

Fixed the problem where the Find dialog did not open the property page for components on closed pages (it appeared that multi edit did not work).


Line Graph: Removed trailing list separator from the ‘Save As CSV’ file rows.


  • Fixed the Solid Properties script, as the script did not compile correctly due to the enthalpy function that was removed.
  • Fixed the problem where properties for two-phase non condensable mixtures returned zero values as results in the Mixed Fluid Properties Script.

Solver Results

Fixed the problem where the Fluid volume and Fluid mass results in the Flow Solver Results window did not update when it was linked to an Action or displayed on the canvas.

Composite Heat Transfer Component

  • Fixed the problem where an error was issued when connecting the Composite Heat Transfer element to non-pipe flow elements because the roughness could not be determined when the Dittus-Boelter option was specified.
  • Fixed the Composite Heat Transfer element StPr chart option not allowing the user to specify the flow area.
  • Fixed the Reynolds number result on the Composite Heat Transfer element for StPr chart input option not displaying correctly.

FLOWNEX SE 8.12.5 (2020 – UPDATE 1)

FLOWNEX SE 8.12.5 (2020 – UPDATE 1)
The new Update to Flownex® SE for 2020 expands the possibilities of simulating real-world systems. Some exciting features included with this release include: built-in functionality to generate system resistance curves within seconds, force calculations for pipe sections, interfacing with CAESAR II for detailed pipe stress analyses, a co-simulation link to the latest version of 6SigmaDCX, along with many other improvements that are listed below.



System Resistance Graphs

The capability has been added to easily plot system resistance graphs. At the click of a button, a parametric run is automatically configured and executed providing the user with an accurate system resistance graph in seconds, as seen in Figure 4. The system resistance graph can be exported as a CSV file in a few clicks and sent to a manufacturer for pump selection. The system resistance graph can also be plotted on a pump chart allowing the user to quickly determine operating points at different pumps speeds.
Figure 3: System Resistance Graph added to Operating Point Plots.
Figure 4- System Resistance Curve and Pump Curve Plot

Force Calculations for Piping Sections

It is not possible to perform structural pipe analysis for water hammer scenarios in most real world systems using hand calculations due to the complex nature of the pressure wave reflections. Flownex® already provides the capabilities to simulate fast transients such as water hammer in these complex systems. In this release, enhancements have been made to the axial pipe force calculations to make them valid for all steady state and transient simulations. This allows users to easily simulate the pipe forces in Flownex® and export the results to structural codes such as ROHR 2 and CAESAR II. Pipe sections for net force calculations can also easily be defined in the “Force Calculation Piping Sections” dialog that is available under the Results menu.
Figure 5. Calculated Pipe Forces in Flownex
The enhanced force calculations are applicable to Pipes, Bends, Valves, the British Standard Orifice, Secondary Loss and the General Empirical Relationship components.

CAESAR II Integration

Flownex® provides a very easy to use interface to work with CAESAR II. By using this interface Flownex® can calculate dynamic loads for pipe stress simulations for water hammer cases or pressure waves. The interface allows a user to import the geometry for a piping system from CAESAR II directly into Flownex®. This saves a user time and also eliminates possible errors that could occur when users need to manually duplicate piping systems in Flownex®. Flownex® also provides an intuitive way to define the piping sections for which users wants the net forces to be calculated. These calculated forces can be automatically exported in a time series that is easily imported into CAESAR II.
Figure 5- Imported Pipeline and Calculated Pipe Forces in Flownex.
Figure 6- Forces Imported to CAESAR II.

6Sigma Link

6Sigma is a world leading tool for data centre simulation and a link to 6Sigma has been added. The link allows users to quickly setup combined simulations and allows both steady state and full transient simulations. Typically, a detailed model of the inside of a data centre can be connected to a complete external cooling model in Flownex®, where all the cooling towers, pumps, heat exchangers etc. is modelled in detail. This allows a complete system simulation that is not available in other software and opens up a whole new spectrum of possible efficiency improvements in both design and operation mythology.
Figure 7- 6Sigma Link Example.

Nuclear Reactor Building Scripts

The ability has been added to build a nuclear reactor using a script. This script reads information from a reactor geometry chart and builds a corresponding reactor. The reactor is built on a separate page in the user interface. Users have access to all of the elements and nodes that defines the reactor.

There are several advantages using this capability. The first advantage is that all the inputs to the elements and nodes that build the reactor can be verified. Furthermore, all internal results are available and finally, the internal connectivity and structure can be manually modified by users if needed.

 Example scripts are available on request. Some components have been added to aid in the reactor building, which include a Porous Flow Element and a Composite Conduction component. They are found in the Reactor Building Blocks category in the Nuclear library, as seen in Figure 9.

Figure 8- Generated Reactor using the Nuclear Reactor Building Scripts.
Figure 9- Composite Conductivity and Porous Flow Element added to Nuclear Library.

Relap Component

The Relap component has been updated to work with newer versions of Relap. Newly updated examples are available on request.

Angled T-Junctions and Y-Junctions

The existing junction functionality has been enhanced to include the ability to model angled T-junctions and Y-junctions, as seen in Figure 1.

Many of the junction losses as defined in “Internal Flow Systems, 2nd Edition” by D. S. Miller have been implemented, thereby extending the previous functionality from the limited perpendicular junction options. These junctions are available for selection from pre-defined junction types, as seen in Figure 2.

Figure 1: T-Junction and Y-Junction Components in Flownex®.
Figure 2: Junction Branch Angle Options for Converging T-Junctions.

Mathcad Component

A new Mathcad link has been added to work with Mathcad Prime version 4.0, 5.0 and 6.0.
Figure 10- Mathcad Prime Link

Graph Improvements

Graphs that have been disabled, now shows a red cross on them to easily identify disabled graphs, as seen in Figure 11. The “Save As CSV” option has been added to all graph types and is available on the context menu of a graph, as seen in Figure 12.
Figure 11-Disabled Graph in Flownex®.
Figure 12- “Save As CSV” Option added to Graphs.

Licensing System

The licensing system has been updated to Version 14. Subsequently all users using server licenses will need to install Version 14 of the license server. An installer that does the upgrade is available to download from our website or from Support. There are several fixes in the newer version of the license server. More information about the fixes is available on the RLM website.

Trace Elements

The trace element modelling capability has been significantly expanded. Previous versions only allowed for homogeneous mixing of trace elements on nodes, where users now have the following additional capabilities at their disposal:

  • The ability to filter trace elements from the network.
  • The ability to specify selective throughflow of trace elements between nodes, thus resulting in non-homogenous mixing of trace elements within nodes.
  • The ability to specify trace element sources and sinks on nodes without the precondition that they enter or leave the system via mass sources or sinks defined for the carrier fluid.
  • Modelling trace element decay during transients using the trace element decay constant.

Filtering and selective throughflow of trace elements are specified on flow element components and sources or sinks and decay are specified on node components, as seen in Figure 13.

Figure 13- New Trace Element Input Options on Nodes.

Isentropic Head Compressor

A new compressor type has been added specifically for modelling compressors operating near the critical point of the fluid with significant changes in fluid properties such as the specific heat, making the use of conventional gas flow dimensionless parameters less accurate. The Isentropic Head Compressor uses isentropic head vs. volume flow data at different speeds. Given the volume flow and speed, the isentropic head is interpolated from the characteristic curve, after which real gas entropy tables are used to find the corresponding pressure.
Figure 14- Isentropic Head Compressor in the Turbos and Pumps Library.


Video Tutorials

The video tutorials can now be played with a built-in player in Flownex® eliminating problems of browser compatibility. Adobe Flash player needs to be installed for the player to work.

Result Layers

For gradient result layers, components were not coloured when they had properties smaller than the minimum value or larger than the maximum value. A new option has been added namely: “Gradient <-[MinValue, MaxValue]->”, as seen in Figure 15. With this option the components with properties lower than the minimum value is painted the minimum colour and components with properties higher than the maximum is painted the maximum colour. This option is now set as the default option.
Figure 15- Gradient Option in Result Layers.

Property Grid

Disabled input properties did not allow users to change their units. This has been changed since these fields display valuable information which users may want to view in different units, as seen in Figure 16.
Figure 16- Units Can be Changed for Disabled Properties.
Figure 17- Toggle Button for Properties.

Screenshot Preview

The screenshot preview that displays in Windows Explorer when the preview pane view is activated, has been updated. In the past, the entire Flownex® window area was captured and sometimes it included overlapping windows. Now only the main item inside Flownex® is captured in order to show the most relevant view of the project, as seen in Figure 18. 

Figure 18- Screenshot Preview.

Psychrometric Boundary Condition

The “Not specified” option as a Boundary condition type, has been added to the Psychrometric Boundary Condition. This option has been added so that the specified condition can be unfixed during a transient simulation.
Figure 19- Not Specified Option for the Psychrometric Boundary Condition.

Heat Transfer

The following enhancements has been made to the heat transfer components:

  • Implemented the option to calculate conduction area from the circumference of the connected pipe.
  • Made Kugeler-Schulten correlation available for the Convection element.
  • Implemented second order convection calculation for a Convection element connected to a Node. This allows convection calculations to be done using the mass weighed average upstream temperature of the flow elements connected to the node that the convection calculation is performed on. This functionality should result in faster grid independence for subdivided flow fields such as those used in a reactor geometry.
  • Implemented dispersion for porous flow elements to account for the enhance heat transfer resulting from the disruption of flow in porous media. The dispersion is modelled as increased diffusion heat transfer within the fluid.
  • Implemented length over diameter warning for Dittus-Boelter and two-phase flow applications.
  • Added the Overall convection heat transfer coefficient and Convection coefficient as results for Convection elements.


The following enhancements has been made to the Nuclear components:

  • Second order convection can be specified in the reactor chart.
  • Dispersion can be turned on in the reactor chart.
  • An error will be given when not all reactor ports that are defined in the chart are connected.
  • Added gamma_f0, gamma_m0 and gamma_x0 to the fuel reactivity, moderator reactivity, and Xenon reactivity equations to allow the user to specify a constant offset independent of the prevailing temperatures. 
  • Changed “Cross section x neutron flux” input in die neutronics chart to “Xenon cross section x neutron flux” to clarify the use of the input.
  • Implemented warning that normalized control rod insertion depth when upper or lower limit has been reached.
  • Updated “Reactivity” result description to “Control rod reactivity” to clarify its meaning.
  • Added warning if neutronics parameters such as Normalized Power, Normalized concentrations of neutron precursor isotopes, Normalized concentrations of decay-heat producing isotopes, Iodine concentration or Xenon concentration go negative and are limited to zero.
  • Changed point kinetics error condition to be issued if fission power equal to zero and reactivity greater than the decay neutron fraction, Beta.
  • Updated Kugeler-Schulten calculations to interpolate between Nusselt numbers calculated at Reynolds number = 100 and Nusselt numbers of 4 (at Reynolds number = 0) for Reynolds numbers smaller than 100 to correctly reflect the documented range of applicability of the Kugeler-Schulten correlation.


Implemented the ability to specify a solid material volume for “Solid Nodes”, as seen in Figure 16. This provides the ability to account for the thermal mass of solid nodes in an all solid heat transfer network such as those generated by the nuclear reactor model generating script.
Figure 20- Specify Node Solid Volume


Exposed fluid mixture component count so that it can be used in a script.

Heat Exchanger Component

The Effectiveness input on the Heat Exchanger Primary component, as seen in Figure 21, is now a dynamic input and can be changed during transient simulations. An option has been added to change the two-phase region error that is given when the heat exchanger operates in the two-phase region to a warning, instead of an error. This allows users to use the heat exchanger in the two-phase region if required. The new option can be seen in Figure 22.
Figure 21- Effectiveness Input on Heat Exchanger Primary Component.
Figure 22- Treat Heat-Exchanger in Two-Phase Errors as Warnings Option in Flow Solver.


Turbine chart scaling factors are now a value of 1.0 by default on new charts, as seen in Figure 23.
Figure 23- Turbine Chart Scaling Factors for New Charts.


The following enhancements has been made to fluid mixtures:

  • The capability has been added to specify a mass sink with mass fractions specified to nodes that are internal to a network. This allows for the selective removal of fluid components from a fluid stream to model the action of a filter or membrane. This functionality is not available on boundary or edge nodes as the transfer of mass is an advection problem and boundary conditions cannot be propagated in the opposite direction to the flow.
  • Psychrometric results are calculated for all two-phase non-condensable mixtures featuring Water as the two-phase fluid.


The amount of iterations during steady state that is solved before iterative scripts or data transfers start being executed can now be specified in the Flow Solver settings, as seen in Figure 24. The default value is 6 – meaning that the scripts and iterative items will start executing at iteration 7 of the pressure solver (main iterations).
Figure 24- Iterative Scripts Calculations and Data Transfer Settings in the Flow Solver.


The API now provides users with the ability to create copies of components and links. Several functions have been added to the NetworkBuilder interface in order to facilitate this. These functions are documented in the API help file. Examples of how to use these functions have been added to the “NetworkBuilderScripts” demo project located under Demo Networks on the Flownex® Start Page. The Python example “3. Simple Network Builder” has also been updated to show how to use these functions. This example is available in the Help menu under Python Link.


Added the capability to specify an angle for the Louver parallel and opposed 3V blades damper types.



Fixed problems where Flownex® crashed when a user deleted a project and its sub directories in Windows Explorer, after the project was closed but Flownex® still open.

Container Interface

Fixed a bug where flow still occurred even when the level of the Container Interface was at zero. 

Heat Transfer

Limit the emissivity on the Surface Radiation component to values between 0 and 1. 

Iterative Scripts

Fixed the problem where Iterative Scripts did not start running until a certain convergence has been reached.


Fixed the problem where the Temperature guess value specified on a mass sink results in a flow solver error.


Fixed the bug where the K Calculation dialog sometimes showed inputs from a different pipe.


The Steam/Water trap was not added to a default report, this has been fixed.

Results Layers

Fixed the problem with painting Result Layers when a user has disconnected links, as parts of the network was not shown at all.

Shell and Tube Heat Exchanger and Finned Tube Heat Exchanger

Fixed the Pressure Drop Excluding Elevation Result, as the result changed with number of tubes specified in parallel.

Download full release notes here.

FLOWNEX SE 8.10.0 (2019)

FLOWNEX SE 8.10.0 (2019)

Flownex® SE 2019 is pushing the boundaries of thermal fluid system simulation.

We’ve added a few new enhancements and additions, including improvements to our heat exchangers, a custom vortex as well as a whole new appearance and functionalities to our graphs. We’ve also updated a few of our components to allow liquid-gas mixture fluid types.
A NEW student version 2019 is also available to download. 



Adaptive Timestep

Fig. 1 - Adaptive Time Step in Scheduler
An adaptive timestep functionality has been added to the Flownex® solver that automatically refines the timestep size through a transient simulation. This results in small timesteps when fast transients (such as pressure pulses during water hammer) are occurring to accurately predict the solution and larger timesteps when possible to effect shorter solving times. This feature monitors the pressure, energy, mass flow and density of all the components and will automatically reduce the timestep to ensure that the solution remains within the specified accuracy criteria. This allows the user to accurately predict fast transients such as pressure pulses without having to perform a temporal convergence study first. For more information about how the adaptive timestep algorithm is implemented, please refer to the Scheduling chapter of the General User Manual. A button has been added to the toolbar that gives the user quick access to the time step settings. It is located next to the Reset Time button in the Simulation Control section, as seen in Figure 2.
Fig. 2 - Time Step Settings

Cavity Editor

The inputs of the Rotor-Rotor and Rotor-Stator components have been significantly enhanced in order to allow a user to easily specify a complex geometry for the cavity.

The complex geometry can be specified by using the Cavity Editor, which opens when double clicking on a Rotor-Rotor or Rotor-Stator component. The Cavity Editor allows the user to import a background picture for the cavity. The geometry and dimensions can then be defined on the picture in the Cavity Editor, as seen in Figure 2.

Fig. 3 - Rotor-Stator Cavity Editor - Reference Measurements

After a picture has been imported, the user can define the dimensions of the cavity by specifying two points at any location on the drawing. Thereafter, the rotor and stator surface geometries are easily drawn on top of the picture.

Fig. 4 - Rotor-Stator Cavity Editor - Rotor Surface Geometry

Other geometric items like the position of bolts, gap and shroud width, as well as defining the discretization is also done easily using this Cavity Editor.

Fig. 5 - Rotor-Stator Cavity Editor - Discretisation

Custom Vortex

Fig. 6 - Customer Vortex Component
A Custom Vortex component has been added to the Rotating Components Library. The custom vortex is a vortex model commonly used in gas turbine cavity modelling. The tangential velocity is specified to produce a velocity profile between that of a forced vortex and free vortex. The radial velocity profile is specified in the following format Cθ= s⋅rn. A custom vortex is characterised by a swirl constant, s, and a vortex weighing factor, n. The custom vortex model provides a simplified cavity model that allows the user to adjust the swirl constant and vortex weighing factor to match the swirl pressure rise seen in empirical measurements.

Heat Exchanger Improvements

The Heat Exchanger components in Flownex® has been updated. These components are now easier to use and a few essential features have been added. The heat exchangers that has been updated is the Shell and Tube Heat Exchanger, Finned Tube Heat Exchanger and the Recuperator, which has been renamed to a Plate Heat Exchanger. The changes make using the heat exchangers for a general application like radiators etc. simpler. Furthermore, fouling factors and fin efficiencies have been added to the heat exchangers where relevant. These can be used to model degradation over time and changes in the condition of the heat exchangers.

Shell and Tube Heat Exchanger

Cosmetic Changes

New icons have been added for the Shell and Tube heat exchanger and the names now clearly indicate the shell side and the tube side.

Fig. 7 - Shell & Tube Heat Exchanger
Input Changes
Shell Side Primary Loss Calculations

The shell side supports specification of the friction factor through a constant value, using a script or using a Fanning friction chart. By default, the Fanning friction factor chart is used. The user can however easily use a correlation from another source in the script defined friction factor specification. These options can be seen in Figure 8.

Fig. 8 - Shell Side Primary Loss Options
Shell Side Heat Transfer Coefficient Calculation

The shell side now supports built in correlations for the heat transfer coefficient calculation, as well as script defined heat transfer coefficient calculation, constant value specification and Stanton Prandtl charts. By default, the Shell Side heat transfer coefficient calculation correlation is used. The user can however easily use a correlation from another source in the script defined heat transfer coefficient calculation, as seen in Figure 9.

Fig. 9 - Shell Side Convection Coefficient Options
Tube Side Primary Loss Calculation

The tube side supports specification of the friction factor through a constant value, Darcy Weisbach correlations, using a script or using a Fanning friction factor chart. By default, the Darcy Weisbach correlation is used, as seen in Figure 10.

Fig. 10 - Tube Side Primary Loss Options
Tube Side Heat Transfer Coefficient Calculation

The tube side supports built in correlations for the heat transfer coefficient calculation, as well as script defined heat transfer coefficient calculation, constant value specification and Stanton Prandtl charts, as seen in Figure 11. By default, the Gnielinski correlation is used for the tube side heat transfer coefficient calculation.

Fig. 11 - Tube Side Convection Coefficient Options
Finned Tube Heat Exchanger
Cosmetic Changes

New icons have been added for the Finned Tube heat exchanger and the names now clearly indicate the fin side and the tube side.

Fig. 12 - Finned Tube Heat Exchanger
Input Changes

Fin Side Geometry

A simplified set of inputs has been added to specify the geometry of a rectangular finned tube heat exchanger with round fins. This is the default option now, as seen in Figure 13.

Fig. 13 - Rectangle HX with Round Fins Inputs

The user now specifies more readily available geometric parameters like the heat exchanger width height and length as well as tube and fin diameters. The older more generic specification is still available.

Fin Side Primary Loss Calculation

The fin side supports specification of the friction factor through a constant value, using a script or using a Fanning friction factor chart. By default, the Fanning friction chart is used. The user can however easily use a correlation from another source in the script defined friction factor specification.

Fin Side Heat Transfer Coefficient Calculation

The shell side now supports script defined heat transfer coefficient calculation, constant value specification and Stanton Prandtl charts. By default, Stanton Prandtl chart is used. The user can however easily use a correlation from another source in the script defined heat transfer coefficient calculation.

Tube Side Primary Loss Calculation

The tube side supports specification of the friction factor through a constant value, Darcy Weisbach correlations, using a script or using a Fanning friction factor chart. By default, the Darcy Weisbach correlation is used.

Tube Side Heat Transfer Coefficient Calculation

The tube side supports built in correlations for the heat transfer coefficient calculation, as well as script defined heat transfer coefficient calculation, constant value specification and Stanton Prandtl charts. By default, the Gnielinski correlation is used for the tube side heat transfer coefficient calculation.

Plate Heat Exchanger
Cosmetic Changes

The Recuperator heat exchanger has been renamed to the Plate Heat Exchanger, which describes the functionality of the heat exchanger better. New icons have been added for this heat exchanger too.

Fig. 14 - Plate Heat Exchanger
Input Changes

Primary & Secondary Side Primary Loss Calculations

Both sides support specification of the friction factor through a constant value, Darcy Weisbach correlations, using a script or using a Fanning friction factor chart. By default, the Darcy Weisbach correlation is used with the addition of friction factor multipliers that can be used in the laminar and turbulent ranges to adjust the friction factor.

Primary & Secondary Side Heat Transfer Coefficient Calculation

Both sides support built in correlations for the heat transfer coefficient calculation, as well as script defined heat transfer coefficient calculation, constant value specification and Stanton Prandtl charts. By default, the Gnielinski correlation is used for the tube side heat transfer coefficient calculation.

Graph Improvements
The appearance of the graphs in Flownex® has been updated and the new graphs can be seen in Figure 14.
Fig. 15 - Comparison Between the Old and New Graphs in Flownex

The graphs inputs have been modified such that only basic graph properties are shown when creating a new graph to ease formatting/styling. Additional formatting properties are available when checking the Advanced Formatting properties, as seen in Figure 15.

Fig. 16 - Graph Properties

New graph functionalities include:

  • By default, the Y-Axis will zoom and pan automatically for easy navigation.
  • The X-Axis will auto scale.
  • Line types can be changed to Step, Spline, Scatter Line, Area, Step Area or Spline area.
  • Line graph plotting data can be saved to a CSV file by simply right clicking on the graph.
  • A Crosshair cursor showing all Y-Axis values for a specific X-Axis value has been added.
  • Graphs formatting can be changed without having to solve the network again.
Rotating Components

The Daily and Nece correlation for calculating moment coefficients on disk surfaces was added as an option for the Rotor-Stator and Rotor-Rotor cavities as seen in Figure 16.

Fig. 17 - Friction Coefficient Correlation Options

In the case of the Rotor-Stator cavity, the Daily and Nece correlation allows for four different regimes, including fully interfering boundary layers within very small gap widths. The possibility to modify the Haaser et. al. correlation to be dependent on the gap width to disk diameter ratio was also added.

The Rotor-Stator and Rotor-Rotor cavities were upgraded to allow specifying an inner radius and outer radius for each disk individually, this is specifically useful when modelling cavities with axial inflows/outflows.

The Rotor-Stator and Rotor-Rotor cavities were upgraded to allow a disk surface profile specification that is not strictly rising with radius.

An option was added to all elements connected to vortices and cavities to specify the radius at the connection rather than the radius fraction. This allows the user to easily link the connection radius input to a measurement on a scaled drawing.

An increment result for windage power was added to the Rotor-Stator and Rotor-Rotor cavities. The windage power calculation of the Rotating Channel, Rotating Nozzle, Labyrinth Seal and Rotating Annular Gap was modified to automatically account for windage addition/removal to the element on account of upstream node swirl speeds not equal to that inside the element. Previously the windage power added to these elements was solely attributed to that required to maintain the swirl speed inside the element. This modification may lead to modified results since windage affects gas density.

The windage power calculation on the Forced Vortex component was modified to account for changes in kinetic energy of incoming flow streams that must increase/decrease in order to be equal to the swirl speed of the vortex at the particular connection radius. This modification may lead to modified results since windage affects gas density.

Liquid Gas Mixtures

The following components were extended to allow liquid-gas mixture fluid types, thereby allowing coupling of the secondary air system with the lubrication system:

  • Rotating Channel
  • Rotating Nozzle
  • Nozzle
  • Rotor-Stator Cavity
  • Rotor-Rotor Cavity
  • Forced vortex
  • Free Vortex
Chemical Reactions

The combustion category has been renamed to Chemical Reactions. The existing Adiabatic Flame model is a chemical reaction where the end temperature and composition of the end product of the reaction is determined by the CEA calculations. Another component has been added to the Chemical Reactions library where the user can specify the end temperature of the chemical reaction, namely the Gibbs Free Energy Reactor.

Gibbs Free Energy Reactor
Fig. 18 - Gibbs Free Energy Reactor
The component uses the NASA CEA program to predict the reaction products at the specified end temperature. This component will then calculate the change in Gibbs free energy and enthalpy during the reaction. As part of this enhancement, a Gibbs free energy result has been added on all flow nodes. The first application of this reactor is to model fuel cells and use Flownex® to optimise the surrounding systems. There are however many other possible applications.


Scale Drawings

The setup of measurements in scale drawings has been simplified. The user can now drag and drop properties from components onto measurement points and measurement lines.

If it is a measurement point, the user will be asked to which part of the coordinate (X,Y, or Z) it should be assigned.

Fig. 19 - Coordinates

If the user drags and drops on a line, the property will automatically be associated with the length of the line.

CFX Interface

Errors when using a comma as decimal separator were fixed. The interface is able to handle both a point or a comma as decimal separator.

The option was added to deactivate the simulation when the CFX Generic Interface encounters an error. A user can continue the simulation from the point where the error (can include CFX solver crash) occurred, saving the time it took to reach that point.

Fig. 20 - Deactivate Simulation when Error Occurs Option


The Flownex® Co-Simulation FMU capability has been enhanced. Flownex® now supports state serialization of the FMU. State serialization is however a slow process and therefore it is not recommended unless it is crucial. There is a new option in the FMU configuration to turn state serialization on and off. The option is false by default. An option has also been added to the FMU configuration to hide Flownex® during FMU execution.
Fig. 21 - FMU Configurations
An example of using a Flownex® FMU with CFX has been added as a tutorial (Tutorial 44).

AFT Importer

In the past, the AFT importer always searched for a scenario named Base Scenario or Base Case to import. This has been improved and the first scenario listed in the Scenario Manager section of the file will now be imported. This enhancement fixes issues were scenarios did not have the default Base names.


Functions were added to the network builder to set the page size for any page.

Ansys Mechanical Link

The Ansys mechanical link now allows a user to specify the name of boundary conditions to transfer load data. Specifying the same names for matching boundary conditions and named selections allows the user to use named selections in the link setup.

Fig. 22 - Use Boundary Condition Names


The unit g/mol was added for molar mass.

The unit kN was added for force.


Errors and warnings were displayed in the console version of Flownex®, but were not recorded. The errors and warnings are now recorded to files named FlownexSEConsoleWarnings.txt and FlownexSEConsoleErrors.txt respectively. These files are located inside the project folder.

Convection Coefficient Correlations

Correlations for calculating convection heat transfer to ambient was added to the Composite Heat Transfer component, as well as the Insulated Pipe component.

Correlations for three different convection mechanisms were added, namely free convection over a horizontal cylinder, free convection over a vertical cylinder, or forced convection over a cylinder. The user can select the mechanism that should be used, as seen in Figure 22.

Fig. 23 - Convection Coefficient Correlation Selections


Added Wall Shear Stress result for Pipe elements with Newtonian Fluids.

Material Warnings

Added warnings for low and high limits when interpolating from two-phase tables. Added warning when two-phase critical mass flux cannot be calculated due to low total pressure.

Nuclear Reactor

Improved the checking and issuing of errors for materials in the Advanced Reactor – materials that did not exist issued warnings even when options were active where they were not used.

Several improvements were made to the text based Nuclear results. This includes correcting the generated heat results for solid nodes and solid node volume results. Also, units were added and corrected for heat in several places.

Node Results

Added an energy source result on solid nodes, as well as transient energy source calculation on all node types. A Gibbs free energy result was also added to flow nodes.

Container Interface Components

The Container Interface Top and Container Interface Bottom components were enhanced to allow the specification of height or height fractions on adjacent elements. Previously, elements could only be connected at the bottom or top.

Fig. 24 - Connection Specification Options


Nuclear Reactor

Fixed a problem where the volume on flow nodes were too large when using Darcy Weisbach pressure drop in a nuclear reactor.


Prevent snaps from loading new script code. This could cause the user to lose the current script and it would be reverted to the script that was used when the snap was saved.

Heat Transfer Component

When multiple Composite Heat Transfer elements were connected to a component, the downstream temperature exceeded the wall temperature. This has been fixed.

User Specified Pressure Drop

Fixed the problem with networks using multiple User Specified Pressure Drop Components that did not converge under some conditions.


Fixed incremented pipes giving different results than non-incremented pipes when used with non-Newtonian fluid types.

Positive Displacement Compressor

Fixed the problem where the Polytropic coefficient value was limited between 0 and 1 for the Positive Displacement Compressor.

Charts & Data References

The full name and path of the chart were saved in the chart and then Chinese characters in the path caused a problem with the saving. This was removed and the charts are now better compatible with Chinese characters in file names and folders.

Fixed problems when turbo machinery charts have too many points. This caused losses of data and abnormal program termination. The errors that are issued when there are too many points are now handled gracefully.

Scale Drawings/GIS

Elevation retrieval for nodes on imported GIS networks did not work due to changes to the Google elevation API. The code has been updated to work with the new changes.

There was a problem on scale drawings where IO boxes displaying measurement positions or lengths did not update when measurement items were moved.

Fixed a problem where using groups on scale drawings caused duplicate views of components on the scale drawings.

Excel Input Sheet

Saving of snaps caused Excel Input Sheets to stop functioning. This has been fixed.

Excel Reports

There was a problem where the last time step during a run was not reported to the table with time steps. This has been fixed.

The cyclic option on reports did not always sample data at the correct time – it was sometimes off by a couple of timesteps.

Global Parameters

Fixed the problem where loading snaps created duplicate global parameters. This caused the global parameter list to become very large and caused serious slowdowns in the user interface. A script has been added to remove the duplicate items.


Fixed a problem where checking licenses back in if the roam (borrowing) period is longer than the server license expiration date caused an exception.

Download full release notes here.

FLOWNEX SE 8.9.1 (2018 – UPDATE 1)

FLOWNEX SE 8.9.1 (2018 – UPDATE 1)

We have launched our latest update of Flownex® SE for 2018.

Some of our major enhancements is adding a thermostat and thermostat bypass component, scale drawing measurements, liquid mixtures and more.



Thermostat & Thermostat Bypass

Fig. 1 - Thermostat and Thermostat Bypass
Thermostat and Thermostat Bypass components were added to the Flownex® component library. Thermostats are required in systems that control the heating or cooling of the working fluid close to the desired temperature. This component is typically found in engine cooling systems or airconditioning of buildings. The component level behaviour is therefore similar to a valve that will change its opening as a function of temperature.
A typical thermostat has two flow paths, namely the primary flow path and the bypass flow path, however there are cases without a bypass, and therefore Flownex® allows the modelling of a Thermostat with and without a Thermostat bypass. The opening of the Thermostat is dependent on the inlet static temperature and specified as a chart. The opening of the Thermostat Bypass is obtained from the opening of the Thermostat, also defined by means of a chart. The secondary loss for both the Thermostat and Thermostat Bypass as a function of their respective openings are calculated from the user-defined charts for secondary loss versus opening.
Fig. 2 - Close-loop network with a Thermostat and Thermostat Bypass

Scale Drawing Measurements

The scale drawing functionality has been expanded. A scale drawing ribbon was added to the toolbar with all the scale drawing related functionality.

Fig. 3 - Scale Drawing Ribbon Bar

The user can specify the scale and coordinate system of an imported drawing with two known coordinates on the drawing canvas. This allows the drawing origin to be away from the zero-point on the axis and also simplifies specifying the scale. The drawing scale and coordinate system can be changed at any time and the components will be scaled accordingly.

Fig. 4 - Generate Scale Drawing dialog

Point and line measurements can be drawn on top of the imported picture. The line will determine the correct lengths and coordinates from the scale and coordinate system of the imported drawing.

Fig. 5 - Adding a point or line measurement

The coordinates of the points and length of each line can be connected to any input fields on components. They are connected without data transfer links to avoid cluttering the drawing canvas.

Fig. 6 - Input property link to a measurement on the drawing canvas

Fields associated with the measurements are greyed out. Moving the points or lines will update the coordinates and lengths while keeping the associated fields updated.

Fig. 7 - Input property greyed out when linked to a measurement

The point and line measurements or the components and links drawn on top of a scale drawing picture can be hidden and shown when required with the buttons on the Scale Drawings ribbon tab. The opacity of the background picture can be changed to make it easy to see the measurements on the drawing. The opacity slider on the toolbar is used for this.

Global Parameter Displays on Drawing Canvas

Right-clicking on any property in the input or result grid will display a context menu with a new option called “Display on Canvas”. This allows the user to choose the location where to display this property for all components of the same type. The same context menu of the relevant property on the property grid is used to remove what is displayed on the Drawing canvas.

Fig. 8 - Adding an input or result property using the right-click context menu

In the configuration screen, the user can change the advanced configuration options like the number of significant digits, or whether the caption should be displayed.

Fig. 9 - Configuration screen for the displayed parameters

Script Debugging

The Scripts can be debugged if a debugger is installed on the computer. Visual Studio is recommended for debugging. The Debug button is located on the Script editor.

Fig. 10 - Script editor with the added debugging

After clicking the Debug button then the user will be prompted to select which debugger to use.

Fig. 11 - Prompt to select appropriate debugger

A breakpoint can be placed in the relevant function requiring debugging and the run button can be pressed in the debugger to continue. The debugger will break as soon as your chosen line of code is hit.

Fig. 12 - Breakpoint added to the debugger

Liquid Mixtures

The ability to specify a fluid mixture consisting of multiple liquids was added. The user can select various liquids as pure fluid components in a fluid. The mass fractions for each component are specified similarly for gas mixtures. Flownex® will calculate the mixture thermodynamic properties and the user can specify the mixing rules for the transport properties (viscosity and conductivity) by selecting one of the pre-defined mixing rules or coding a script for custom mixing rules. The mixture will be treated as a single-phase liquid in the Flownex® solver. A Help button was added to direct the user to the appropriate location in the User Manual discussing the mixed fluid theory.
Fig. 13 - Multiple liquid mixture specified in Flownex


Specify Drawing Grid Spacing

The size of the grid on the drawing canvas can be changed on the page inputs. To access the page inputs right-click on a page and choose “Edit Page” on the context menu.

Fig. 14 - Specifying drawing grid spacing

Change Location of Identifier and Description Text

The location of the display can be changed in the project settings under “Drawing Text Settings”.

Fig. 15 - Changing the location of the Identifier and Discription

Added Button to Copy Used Data References to Project Database

A button was added enabling the user to copy all the charts and lookup tables from the databases located in the project to the project database. This is useful when using a company database and it is necessary to send a project to another user that does not have that database.

Fig. 16 - Copy the Data Reference to Project Database

Added Confrim Delete Dialogon Data References & Categories

The user will be asked for confirmation before deleting a data references to prevent accidental deletions.

Fig. 17 - Confirmation dialog before deleting a data reference

Master Database Location

The location for the built-in master database that ships as part of the Flownex® installation was changed. The name for the database folder is now “Master” (it was previously in a folder called “Project” in the installation folder).

Nuclear Reactor

Added friction factor and flow area to Detailed Reactor Output file.


The Python resource files have been updated. Firstly, a getting started guide has been added to assist new users with installing Python and installing the required libraries for using the Flownex API. Another example has also been added to show how Python can be used to automatically build a network from a CSV-file using the API. Furthermore, the Flownex.py file has been updated to automatically determine your Flownex install directly from the registry entries created when Flownex is installed.


The Cooling orifice was removed and will be replaced with a Nozzle in the existing networks.


Drawing Canvas

  • Fixed the problem when pasting a component the component was not always placed at the location where the preview showed.
  • Changed the Ctrl+Drag+Copy mechanism to work the same way as other software.
  • Fixed the problem where background image selection for graphs did not work.
  • Fixed the problem when first Copy-Paste and then undoing of components on geometries left viewless components in the project.

Property Grid

  • Fixed the problem where the Find dialog did not open the property page for components on closed pages (it appeared that multi edit did not work).


  • Fixed the problem when specifying an end time on the main scenario in actions causing the user interface to freeze.

Nuclear Reactor

  • Fixed the problem where the solid material selection drop down box freezes in the general fuel zone in the Nuclear reactor component.
  • Fixed the problem when specifying fractions in the general fuel zone where double precision numbers did not exactly add up to 1.0 for Total solid fraction and Total heat fraction.
  • Fixed the problems when the solution produced NaN results for moderator temperature and reactivity when moderator fraction is set to 0.0.

Flow Solver

  • Fixed convergence criteria for the Two-phase tank component where solving seemed to have converged whilst still solving to converge the Two-phase tank component.
  • Fixed the problem causing the Flow resistance component not to solve when the initial pressure drop is zero.
  • Fixed the problem with the loading of snaps for non-circular pipes and number in parallel not set to unity.
  • Fixed the problem with liquid-gas mixtures during transients with Two-phase tank component not solving.
  • Added a mass fraction relaxation parameter to solver inputs for liquid-gas mixtures.

Flow Solver Components

  • Fixed an error in the Reynolds number calculation for Orifice in pipe transition component.
  • Fixed the problem where the mass fraction boundaries are not correctly applied when specified in the first time step of a transient when changing setting from mass source fraction to mass fraction boundary.
  • Added a warning when the British standard orifice’s solution is in the two-phase regime.
  • Added a warning when two-phase conditions exist at an element outlet when exit temperature is specified.

Download full release notes here.