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Original file line number | Diff line number | Diff line change |
---|---|---|
@@ -1,20 +1,12 @@ | ||
Version 8.6.5 | ||
Version 8.6.6 | ||
|
||
- Includes ThermoC Property Package | ||
- Dynamic Event transitions | ||
- Export PFR Profile to new spreadsheet (Classic UI/CPUI) | ||
- Heat Exchange Profile now available for all Heat Exchanger calculation modes | ||
- Enhanced Heat Exchange Profile Viewer (CPUI) | ||
- New Enthalpy calculation method (Liquid Cp + Excess) | ||
- EOS-based models can now select Experimental Liquid Cp as Enthalpy calculation method | ||
- Changed duration controls for Dynamics Integrator to allow periods higher than 24 hours (Classic UI) | ||
- Fixed issues with Pure Compound Viewer (Classic UI) | ||
- Fixed conversion reactor energy balance (#541) | ||
- Fixed not being able to update kappa parameters for PRSV2 PP | ||
- Fixed Heat Exchanger calculation when specifiyng invalid outlet temperatures | ||
- Fixed Enthalpy calculation from Liquid Cp | ||
- Fixed/added CO2 Normal Boiling Point | ||
- Fixed Excess Enthalpy calculation | ||
- Fixed Pump curves are not being correctly saved (#548) | ||
- Fixed input issue with Pipe Hydraulic Profile on Classic UI (#543) | ||
- German translation fix | ||
- Added Mach number calculation and reporting for gas flow in pipes | ||
- Added slurry viscosity correction for PFR and Pipe Segment (Yoshida et al, https://www.aidic.it/cet/13/32/349.pdf) | ||
- New Modified Bubble-Point solver for Rigorous Columns | ||
- Kinetic/HetCat/Conversion reactions/reactors now support compounds in solid phase | ||
- Surface Tension is now calculated for all liquid phases | ||
- General fixes to Rigorous Column model and solvers | ||
- Fixed issue with Coolprop Incompressibles PP | ||
- Fixed issues with Pump model | ||
- Fixed Solid Cp calculation | ||
- Other minor fixes and enhancements |