AVEVA PRO/II Simulation 2025.0
AVEVA PROII Simulation 2025.0 | 839.8 mb
AVEVA, a global leader in engineering and industrial software, is pleased to announce the availability of PRO/II Simulation (formerly PRO/II) 2025.0. Designed to perform rigorous heat and material balance calculations for a wide range of chemical processes, AVEVA PRO/II Simulation offers a wide variety of thermodynamic models to virtually every industry.
What's new in AVEVA PRO/II Simulation 2025
AVEVA PRO/II Simulation 2025 introduces the following set of new features and enhancements.
AVEVA PRO/II Simulation 2025 introduces the following set of new features and enhancements.
New Unit Operations
- HDP Feed Synthesis
- FCC Refinery Reactor
- FCC Feed Synthesis
- Component Mapper
Unit Operation Updates
- Pump
. Single pump curve extrapolation using affinity laws
. User option to choose curve interpolation option
. Plot operating point in the pump curve
- CSTR
. Addition of Newton solver
. Initial estimates
. Addition of Space time specification
- Cyclone
. Addition of Li & Wang efficiency model
. User Interface update
- Valve enhancements
- Compressor - User option to choose curve interpolation option
- Column - Addition of Matsui Machine CMR packings
- Pipe heat transfer upgrades
- Depressure - Added control valve to the available valve methods
Integration
- Column - FRI DRP Integration 4.1 for Tray & Packing rating
- AVEVA Engineering (FEED) – Updated to new AVEVA Integration Service Data API
- Spiral Assay – Addition of support to use Assay Web Services
- Support for MySep 3.1.2
Components and Thermodynamic
- Clarity on UNIFAC structural groups for aromatic groups
- DIPPR Lite 2024 databank support
- Addition of supplemental component data bank
- Modified volume shift calculations for water in SRK and PR peneloux
- REFPROP
. Add-on installed by default
. Component search grouping and indication of supported components
Output
- Single unit property table extended to additional units.
Miscellaneous
- Case study specific point entry increased to 2000 points
- Improved phase description for volumetric flows
- Global default distillation points
- Updating of thermosiphon reboiler icon on conversion of old models
- WebView2 based PRO/II Help Viewer replaces AVEVA Help
- Common Diagnostics log path can now be updated in the proii.ini file
- HDP Feed Synthesis
- FCC Refinery Reactor
- FCC Feed Synthesis
- Component Mapper
Unit Operation Updates
- Pump
. Single pump curve extrapolation using affinity laws
. User option to choose curve interpolation option
. Plot operating point in the pump curve
- CSTR
. Addition of Newton solver
. Initial estimates
. Addition of Space time specification
- Cyclone
. Addition of Li & Wang efficiency model
. User Interface update
- Valve enhancements
- Compressor - User option to choose curve interpolation option
- Column - Addition of Matsui Machine CMR packings
- Pipe heat transfer upgrades
- Depressure - Added control valve to the available valve methods
Integration
- Column - FRI DRP Integration 4.1 for Tray & Packing rating
- AVEVA Engineering (FEED) – Updated to new AVEVA Integration Service Data API
- Spiral Assay – Addition of support to use Assay Web Services
- Support for MySep 3.1.2
Components and Thermodynamic
- Clarity on UNIFAC structural groups for aromatic groups
- DIPPR Lite 2024 databank support
- Addition of supplemental component data bank
- Modified volume shift calculations for water in SRK and PR peneloux
- REFPROP
. Add-on installed by default
. Component search grouping and indication of supported components
Output
- Single unit property table extended to additional units.
Miscellaneous
- Case study specific point entry increased to 2000 points
- Improved phase description for volumetric flows
- Global default distillation points
- Updating of thermosiphon reboiler icon on conversion of old models
- WebView2 based PRO/II Help Viewer replaces AVEVA Help
- Common Diagnostics log path can now be updated in the proii.ini file
The following table lists the issues resolved in AVEVA PRO/II Simulation 2025.
3309538 Column Reactive distillation model not converge
3907920 Column In a specific file, Column fails to converge when Murphree tray efficiency is specified
3286660 Component & Thermodynamics HF vapour pressure correlation in PRO/II 2024 is wrong
3862372 Compressor In some Compressor units, there is difference between input curve and calculated multiple polytropic head curves
3318430 Documentation In Getting Started manual, path to help files are wrong
3398284 Documentation Pseudo stream temperature is different from associated tray temperature with tray efficiency is given
3894487 Documentation Documentation for multiphase flash algorithm is missing
3861745 Ejector In a specific file, flash fails in ejector when using SRKM thermo method
3407650 Exergy Update Exergy documentation to match calculation
3777141 Flash For a specific file with C3 stream, NIST versus Default flash algorithm gives different results
3826656, 3886315 Flash Grayson-Streed thermo with H2 rich stream generate wrong isothermal curve in Heating curve unit
3757596 Output In XML report, names of some adjusted standard parameters are misspelled
3477285 Refinery Reactor In Reformer, UOM of defines are inconsistent
3479784 Refinery Reactor In Reformer, help links are inconsistent
3782081 Refinery Reactor In wide temperature range, Reformer takes long time to converge
3800461 Refinery Reactor Few Reformer parameters are missing in case study and calculator
3895890, 3911846 UOM User defined Pressure gauge basis is incorrect in in Portuguese OS
3309538 Column Reactive distillation model not converge
3907920 Column In a specific file, Column fails to converge when Murphree tray efficiency is specified
3286660 Component & Thermodynamics HF vapour pressure correlation in PRO/II 2024 is wrong
3862372 Compressor In some Compressor units, there is difference between input curve and calculated multiple polytropic head curves
3318430 Documentation In Getting Started manual, path to help files are wrong
3398284 Documentation Pseudo stream temperature is different from associated tray temperature with tray efficiency is given
3894487 Documentation Documentation for multiphase flash algorithm is missing
3861745 Ejector In a specific file, flash fails in ejector when using SRKM thermo method
3407650 Exergy Update Exergy documentation to match calculation
3777141 Flash For a specific file with C3 stream, NIST versus Default flash algorithm gives different results
3826656, 3886315 Flash Grayson-Streed thermo with H2 rich stream generate wrong isothermal curve in Heating curve unit
3757596 Output In XML report, names of some adjusted standard parameters are misspelled
3477285 Refinery Reactor In Reformer, UOM of defines are inconsistent
3479784 Refinery Reactor In Reformer, help links are inconsistent
3782081 Refinery Reactor In wide temperature range, Reformer takes long time to converge
3800461 Refinery Reactor Few Reformer parameters are missing in case study and calculator
3895890, 3911846 UOM User defined Pressure gauge basis is incorrect in in Portuguese OS
AVEVA PRO/II Simulation 2025.0
AVEVA PRO/II Simulation is a professional simulation tool that offers a comprehensive simulation solution for process design, revamp, and operational analysis. AVEVA PRO/II Simulation performs rigorous mass and energy balances for processes ranging from oil and gas separation to reactive distillation. AVEVA PRO/II Simulation has the power and flexibility to simulate a wide range of processes at steady state, from refining to chemicals. AVEVA PRO/II Simulation provides robust and accurate results based on industry-standard thermodynamic methods and physical property data. AVEVA PRO/II Simulation is a valuable tool allowing engineers and management to enhance the bottom line of their process or plant.
Aveva Pro-II Process Engineering
AVEVA is a global leader in engineering and industrial software driving digital transformation across the entire asset and operations life cycle of capital-intensive industries. The company’s engineering, planning and operations, asset performance, and monitoring and control solutions deliver proven results to over 16,000 customers across the globe. Its customers are supported by the largest industrial software ecosystem, including 4,200 partners and 5,700 certified developers. AVEVA is headquartered in Cambridge, UK, with over 4,400 employees at 80 locations in over 40 countries.
Owner: AVEVA
Product Name: PRO/II Simulation
Version: 2025.0
Supported Architectures: x64
Website Home Page : www.aveva.com
Languages Supported: english
System Requirements: Windows *
Size: 839.8 mb
AVEVA PRO/II Simulation 2025.0
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AVEVA PRO/II Simulation 2025.0
