Flownex SE Error Reports – Flownex Simulation Environment

2025-07-23: Results Report - Continuity Discrepancy on Nodes Connected to Two-Phase Tanks with Associated Steady-State Quality Boundary Condition
2025-04-23: Results Report - All Components of a Type in a Table Only Updates Value of First Component
2025-02-19: Un-Initialized Variable for Fluid Specific Heat Ratio
2025-02-19: Un-Initialized Variable for Minimum Transient Time Step
2023-12-19: The Pump Scaling Factors Are Not Applied Correctly to the Gradient of the Pump Curve for All Scaling Options
2023-07-11: Temperature and Quality and Quality Only Boundary Conditions Are Not Applied Correctly During Transient Events
2023-07-11: Elements Adjacent to First Order Convection Heat Transfer Elements Show Spurious Heat Transfer Results and First Order Convection Heat Transfer is Over Reported When Using the Non-Iterative Transient Solver
2023-07-10: When a Heat Transfer Grading Factor Larger Than One (1) is Specified for Convection Heat Transfer, the Component Fluid Exit Temperature Can Exceed the Wall Temperature
2022-05-27: When a User Volume is Associated with a Solid Node, the Associated Solid Material Specific Heat Value is Always Evaluated at 15 °C
2022-05-20: When the Volumetric Flux Option is Selected in the Run-Time Neutronics Script the Power Distribution Assigned to Each Zone is Incorrect
2021-10-28: The Incorrect Reference Values are Used in the Steiner and Taborek Nucleate Boiling Heat Transfer Coefficient Correlation for Many Two-Phase Fluids
2021-10-28: The Incorrect Heat Flux is Used When Determining the Wall Temperature Associated with Critical Heat Flux
2021-06-14: Nuclear Reactor Element Incremented Secondary Loss Factor
2021-06-09: Shell and Tube Heat Exchanger - Pressure Drop Excluding Elevation Result Incorrect
2021-05-21: Adiabatic Flame – Combustion Products Not Found in Gasses Not Added to Background Fluid