v3.2 [Oct 7, 2016]
- COFE (3.2.0.1): SetMaterialContext was not always called after re-ordering compound list, leading temporary to invalid thermo results from v1.1 property package
- COFE (3.2.0.2): resolved problem with XML based persistence of plots containing logarithmic axes
- COFE (3.2.0.3): fixed problems for COFE unit operation in case of simulation environments that do not implement ICapeCOSEUtilities
- COUSCOUS (3.2.0.1): flashing MeasureUnit product at specified P+VF if feed has a vapor fraction of 0 or 1
- COUSCOUS (3.2.0.2): corrected invalid phase boundary detection introduced in 3.2.0.1
- COUSCOUS (3.2.0.3): flashing Splitter products at specified P+VF if feed has a vapor fraction of 0 or 1 and zero pressure drop
- OATS (3.2.0.1): fixed problem with ResolvePropertyPackage (thermo 1.0)
- COFE (3.2.0.4): fixed route point insert location in stream
- fixed initial font edit box
- changed default font from "MS Sans" to "Arial"
- changed rendering of energy stream to printer (asking printer driver for a "dotted line" - formatting is up to the printer driver, as user style line does not seem to render will on many printers)
- add some extra slack space to printing of text boxes, to prevent truncated text when text exceeds size of box in printer coords (text was measured in screen coords)
- COFE (3.2.0.5): fixed font issues
- fixed issue causing paint failure in single threaded mode
- COFE (3.2.0.6): fixed font size issue
- COFE (3.2.0.7): fixed font size issue
- disabled font effects in font dialogs
- COFE (3.2.0.8): fixed more font size issues
- TEA (3.2.0.1): added equation 132, A+B/(T-E)^0.5+C/(T-E)^0.8+D/(T-E)^3
- TEA (3.2.0.2): adapted equation 104 to ChemSep
- ChemSep1.pcd: corrected compounds that use equation 104 for second virial coefficient (Cyclobutane, Isopryl mercaptan, Glycerol, N-eicosane)
- COFE (3.2.0.9): added context menu for wiping both content and initial values of streams
- logging each failed unit evaluation in debug verbosity mode to help assess flowsheet initialization failure
- material object no longer accepts zero or negative values for pressure or temperature
- ability to add unit operation reports to unit operation tooltip
- COFE (3.2.0.10): removed report title from report in unit operation tooltip
- COFE (3.2.0.11): fixed reports in tooltip removal
- caching report text to prevent unnecessary reevaluation of reports
- COUSCOUS (3.2.0.4): flashing HeatExchanger unit for zero-flow case at PH for pure compound stream to prevent enthalpy balance failure
- TEA (3.2.0.3): added equation 118, exp(A+B/T^E+C*ln(T)+D*T^2)
- COFE (3.2.0.12): bug fix for determination of number of logical cores
- bug fix for parametric study where feed streams containing controller set points are parametric inputs
- bug fix for controller feed setpoint virtual parameter feed stream influence on Jacobian
- revision of job queueing for controller unit operations
- COFE (3.2.0.13): compiler upgrade
- corrected issue with setting virtual information port data in non-recycle units during solve
- COUSCOUS (3.2.0.5): compiler upgrade
- COUSCOUS: Stream heat capacity (Cp) added to measure unit
- COFE (3.2.0.14): insertable info tip object
- added Copy summary (Tool Tip) to context menu of stream and unit
- fixed tool tip over inserted objects
- OATS (3.2.0.3): fixed problem with unit operation name display
- OATS: compiler upgrade
- COFE (3.2.0.15): fixed equal string checking algorithm
- fixed inability to pan while solving
- fixed hangup on loading unit operations with log line grouping
- COUSCOUS (3.2.0.6): fixed issue with make up mixer with mass flow specification
- COUSCOUS: fixed problem with net flow result not being persisted
- CUP (3.2.0.1): fixed crash on invalid remote CUP.dat in silent update check mode
- COUSCOUS (3.2.0.7): fixed partially hidden Wall Roughness label on pressure drop page tab of PFR
- COFE (3.2.0.16): fixed reporting certain solver errors (resulting in false Flowsheet Solved messages)
- COFE (3.2.0.17): additional error checking on flow constrain units in solver process
