For a list of changes to ChemSep, please visit the ChemSep News page

COCO v3.7 changes and (bug-) fixes

cup To get the latest updates, you can run COCO UPdate (CUP). If you have trouble running CUP, see Updating COCO in the support section.

Changes since version 3.7:

TEA (3.7.0.1): fixed reading of new PCD files to avoid problems with new InChI key storage
COFE (3.7.0.1): fixed an issue with screen update after solving causing occasial painting of streams as if they are not solved at solution
COUSCOUS (3.7.0.1): corrected limiting pressure message for heat exchanger
COUSCOUS: energy measure unit to convert energy stream values to information streams
Help: corrected typing error in Measure Unit help page
Help: energy measure unit
Water (3.7.0.1): allow put_ComponentName to comply with revised ICapeIdentification Errata and Clarifications
COFE (3.7.0.2): allow for not exposing feeds and products in embedded flowsheets as feed- and product-ports (context menu on feed and product streams in embedded flowsheet)
COFE (3.7.0.3): fixed external port issues for embedded units, introduced in 3.7.0.2
COFE (3.7.0.4): printing which units are calculating as part of the solution process, in debug mode
TEA (3.7.0.2): improved flash support for mixtures containing solid-only compounds
TEA: improved flash support in case of single compound and mixtures that contain only one non-solid-only compound
COUSCOUS (3.7.0.2): added a parameter to Compressor for an allowable non-vapor phase fraction before raising a warning
COUSCOUS: added a parameter to Expander for an allowable non-vapor phase fraction before raising a warning
COUSCOUS: Pump that has vapor present in the feed no longer multiplies total feed flow by liquid (and solid) molar volume to calculate max energy requirement. This approach counts vapor as liquid, which is not correct. Instead the max energy requirement is calculated from the total liquid (and solid) flow rate multiplied by liquid (and solid) volume, and vapor is ignored altogether in this calculation.
COUSCOUS: added a parameter to Pump for an allowable vapor phase fraction before raising a warning
COUSCOUS: Turbine that has vapor present in the feed no longer multiplies total feed flow by liquid (and solid) molar volume to calculate max energy production. This approach counts vapor as liquid, which is not correct. Instead the max energy production is calculated from the total liquid (and solid) flow rate multiplied by liquid (and solid) volume, and vapor is ignored altogether in this calculation.
COUSCOUS: added a parameter to Turbine for an allowable vapor phase fraction before raising a warning
COUSCOUS: added a parameter to FixedConversionReactor to suppress warnings related to reaction phases and other present phases
COUSCOUS: correct logic in phase warning generation for FixedConversionReactor
COUSCOUS (3.7.0.3): prevent secondary PMC objects from being renamed by PME
COUSCOUS (3.7.0.4): PropertyTester no longer tries to determine basis and extensive vs intensive for two phase properties - it is correclty assuming that all two phase properties are intensive and without basis
COFE (3.7.0.5): fix incorrect invalidation of unit caused by opening Edit dialog
CORK (3.7.0.1): corrected path to help file
COFE (3.7.0.6): pass unit name to initialization function upon load for better error reporting durinig initialization (was missing unit name under certain circumstances)
COFE: fix for putting simulation context prior to loading unit operations
COUSCOUS (3.7.0.5): fixed issues with BSTR management of port names, causing problems in at least information calculater (evident since fix in 3.7.0.3)
COFE (3.7.0.7): avoid crash upon COM object creation error introduced in 3.7.0.5
COFE: explicit call to InitCommonControls
COFE (3.7.0.8): avoid issues with stream dialog inside unit operation edit dialog in case no streams are connected
COFE (3.7.0.9): fixed potential crash in parametric study
TEA (3.7.0.3): changed decision on single compound super-critical phase labeling (vapor vs liquid, based now on volume)
TEA: corrected single compound enthalpy and entropy flashes
COFE (3.7.0.10): if unit operation is calculated from inside the unit operation dialog, the dialog is updated after calculation (affects balance page and more)
COFE (3.7.0.11): correction on used material count (reporting unused cached materials as used) causing unnecessary solution invalidation as well as incorrectly reporting a material type is in use upon deleting
COFE: fixed incorrect reporting of compounds to be removed upon removing property package in case all compounds are resolved also from a remaining property package
COFE: corrected internal inconsistency on material object data after deletion of a compound

Changes since version 3.6:

TEA (3.6.0.1): fix to initializing properties from outside CAPE-OPEN environment (e.g. ConfigureTEA), introduced in 3.5.0.5
CUP (3.6.0.1): fixed reference to feature name and added debug options
COFE (3.6.0.1): fixes on dependency analysis of parametric study
COUSCOUS (3.6.0.1): initial direction fix in univariate solver
TEA (3.6.0.2): fix to exposing compound constant 'idealGasStateReferencePressure' for CAPE-OPEN 1.1
COFE (3.6.0.2): clearer error upon controller connection failure
COFE: activate log view upon port connection errors so that errors become visible while the problem occurs
CUP (3.6.0.2): fixed UTF16 conversions in path names
COFE (3.6.0.3): fixed issue with printing cut streams in Verbose mode
COFE: modernized formula parser and resolve memory leak
COFE (3.6.0.4): fixed setting unit context on simulation context during unit creation (resolve problems with e.g. setting unit icon as done in e.g. Excel Unit Operation)
JUIcE (3.6.0.1): resizable main window
COFE (3.6.0.5): fixed stream dialog update issues
COFE: moved Edit button in Edit Unit Operation dialog out of tab pages
COFE: added Calculate button to Unit Operation dialog
COFE: added stream dialog to Unit Operation dialog
COFE (3.6.0.6): fixed problem with parameters not updating in unit operation dialog after invoking Edit on the unit operation (introduced in 3.6.0.5)
COFE: fixed failure to update dependent display objects (parameter reports...) when changing a unit parameter from the watch window
COFE (3.6.0.7): additional diagnostics for mass balance errors at flowsheet solution
COFE (3.6.0.8): fixed a crash upon mass balance corrections introduced in 3.6.0.7, and improved diagnostics messages
COFE (3.6.0.9): alternate row colouring option in tables
COFE (3.6.0.10): adjustments to alternate row colour scheme
COFE (3.6.0.11): fixed import data on data series in plotting (unicode detection failed)
COFE (3.6.0.12): adjustments to alternate row colour scheme
TEA (3.6.0.3): fixed check for missing compound data on GetCompoundConstant
TEA: modernized formula parser and resolve memory leak
COFE (3.6.0.13): in stream reports, allow any user specified represntation for zero composition (below zero composition limit)
COFE: in flowsheet reports, allow any user specified represntation for zero composition (below zero composition limit)
Water (3.6.0.1): GetNumPhases incorrectly returned E_NOTIMPL
COFE (3.6.0.14): fixed potential issue with double buffer bitmap allocation for graphs
COFE (3.6.0.15): fixed crash on clicking on unit of measure in parametric study dialog column header (after loading document)
COFE: fixed update of values of parametric study dialog on unit dimension change (after loading document)
TEA (3.6.0.4): removed invalid error on missing boiling point for solid-only compounds on configuration of a property package
TEA (3.6.0.4): removed invalid error on missing boiling point for solid-only compounds on configuration of a property package
COUSCOUS: modernized formula parser and resolve memory leak
CORN: modernized formula parser and resolve memory leak
COFE (3.6.0.16): fixed issue with screen update after drag-and-drop document on COCO
COFE: fixed issue with missing logged messages from solve
Installer: fixed cleanup of help file, xlt template, empty win32 folder

Changes since version 3.5:

COFE (3.5.0.1): not showing message box from COFEStand in case of document load error
COFE: when inserting a unit, loss of mouse capture does not lead to failure to insert unit if mouse is above feasible area
COFE (3.5.0.2): fixed crash on determining stream and unit order, introduced in COFE 3.4.0.9
COUSCOUS (3.5.0.1): disallowing put_value on output parameters
COUSCOUS: sanity check on port count in mixer, splitter, energy mixer, energy splitter and flash
TEA (3.5.0.1): fixed unnecessary logging of error messages during flash iterations
TEA (3.5.0.2): fixed unnecessary logging of error messages during failed flash iterations
COFE (3.5.0.3): allow manual specification of cut streams ("Mark as cut stream" in context menu of stream)
COFE: x86 version no longer auto registers for opening .fsd files; all shell interaction defaults to x64
COUSCOUS (3.5.0.2): fixed access violation in Gibbs reactor, leading to unpredictable results
COFE (3.5.0.4): compact alternatives to stream and unit parameter report objects
COFE: allow no line & fill on report objects
COFE: various corrections on stream reports
COFE (3.5.0.5): fix to initial guesses for energy cut streams (erroneous 'unable to generate guess' message)
COFE: user defined cut streams appear in solve log now for debug level normal and higher
COFE (3.5.0.6): fix on crash on stream reports, introduced in 3.5.0.4
COFE (3.5.0.7): fix for problem to abort embedded flowsheet calculation from its edit window
COFE: fixed crash on paste and delete in stream dialog of embedded flowsheet
TERNYP (3.5.0.1): supporting CO-LaN's flowsheet monitoring specification (deprecating COCO's version - will be removed from a next release)
COFE (3.5.0.8): not logging warning for simulated overall property calculation in case thermo is v1.1 or up
COFE: fix on determination of thermo version on link to external property package from within embedded flowsheet
COFE: supporting CO-LaN's flowsheet monitoring specification (deprecating COCO's version - will be removed from a next release)
COFE: supporting CO-LaN's custom data interface specification
COFE: fixes to ensure unique stream and unit operation naming
COFE: corrected selection of reaction packages via automation and in calculator
COFE (3.5.0.9): fixed RegisterForEvents
COFE (3.5.0.10): fix for crash on solving documents with energy or information streams, introduced 3.5.0.8
COFE: fix for crash on loading embedded flowsheet with reaction packages
COFE (3.5.0.11): fix for unpredictable behaviour upon focus lost during inserting unit operation
CUP (3.5.0.1): fixed connection problem
COFE (3.5.0.12): fix for setting simulation context twice on lazy unit operation creation in solver thread
CUP (3.5.0.2): added CUP version to User-Agent header
COFE (3.5.0.13): added support for CAPE_FLOWSHEET_VALIDATION_STATUS_CHANGED event
COFE (3.5.0.14): correction to ICOFEPropertyManager interface, introduced in 3.4.0.7
COUSCOUS (3.5.0.3): fixes to reduced calculation mode for Gibbs reactor (corrected solution under assumption of full conversion of compounds)
COUSCOUS: upgrade to compiler MSVC 2022
COUSCOUS: fix to constraint projection for CSTR,EquilibriumReactor and Gibbs reactor
COFE (3.5.0.15): using affiliation in document summary as opposed to company, and "date" as opposed to "created"
COFE: upgrade to compiler MSVC 2022
COUSCOUS (3.5.0.4): fixed crash in CSTR, EquilibriumReactor and Gibbs reactor, introduced in 3.5.0.3
TEA (3.5.0.3): added equation 216: A*t^B+C*t^D with t=1-T/TC
TEA: corrected derivative for several equations in case T>=TC
TEA: upgrade to compiler MSVC 2022
TEA (3.5.0.4): removed incorrect check on trivial solution acceptance
TEA: revised conditions on trivial solution composition check
TEA: additional checks on flash correctness in case of use of pseudo properties
TEA: fixed various instances of early loop exit after partial data
TEA: fixed failure to detect flash not converging
COFE (3.5.0.16): restored icon editing ability for win32 version of COFE
COFE (3.5.0.17): COCO automation interface returns IUnknown rather than IDispatch for CAPE-OPEN objects (Python COM client does not like receiving non-functional IDispatch interfaces)
COFE (3.5.0.18): support for pasting full-precision data from Excel, instead of formatted values
COFE: Support for COFEStand /r option
COFEStand (3.5.0.1): added /r option for reset-before-solve
COFEStand: compiler upgrade
TEA (3.5.0.5): postpone reading props.ini until needed
COFE (3.5.0.19): added context menu to document explorer for closing multiple views of same kind (all or all others)
COFE (3.5.0.20): fixed incorrect read error on missing y data in plots
COFE (3.5.0.21): fixed restoring plot series with no symbol or no line (default incorrectly applied)
COFE: fixed persistence of certain aspects of binary plot series
COFE (3.5.0.22): added CLSID to tooltip text of embedded OLE objects to aid in diagnosing "Class not registered" when trying to open embedded object
COFE: allowing to display single phase liquid surface tension in the stream dialog - it is shown as a two phase property in combination with a vapor phase that has the same composition as the liquid phase
COFE: fixed parametric study jobs incorrectly marked as canceled due to full message queue
COFE: fixed memory leak in case of full message queue
COFE: grouping status message to alleviate problems due to full message queue
COFE: fixed internal serialization of stream copier (used in multi-threaded solver, which did not work if a stream copier was present)
Help: updated help on property configuraton for surface tension
COFE (3.5.0.23): fixed missing close clipboard (leaving the clipboard open) when pasting something copied from Excel (problem introduced in 3.5.0.18)
COUSCOUS (3.5.0.5): fixed problems with make up mixer in mass basis
COUSCOUS (3.5.0.6): fixed mode on fixed conversion reactor conversion input parameters
COUSCOUS (3.5.0.7): fixed data type on fixed conversion reactor conversion input parameters
COUSCOUS (3.5.0.8): unit operations now persist their own name and description rather than assuming the PME will do so
TEA (3.5.0.6): fix to restoring name when reading from property bag (instead of depending on PME to restore name)
CORN (3.5.0.1): upgrade to compiler MSVC 2022
Water (3.5.0.1): upgrade to compiler MSVC 2022
TERNYP (3.5.0.2): upgrade to compiler MSVC 2022
OATS (3.5.0.1): upgrade to compiler MSVC 2022
JUIcE (3.5.0.1): upgrade to compiler MSVC 2022
CUP (3.5.0.3): upgrade to compiler MSVC 2022
CORK (3.5.0.1): upgrade to compiler MSVC 2022
Installer: added new CO-LaN type libraries, including v1.1 extensions (Flowsheet monitoring & Custom data)
Installer: properly cleaning up pre-3.5 installation

Changes since version 3.4:

CUP (3.4.0.1): additional HTTP headers to avoid cache
CUP (3.4.0.2): processing COCO features first
CUP: passing installmode to COCO and ChemSep installers
CUP (3.4.0.4): fixes to temporary crypto contexts for checking signatures
COFE (3.4.0.1): renamed Stream Order to Stream Display Order and Unit Operation Order to Unit Display Order
COFE: fixed mole/mass fraction context menu in stream dialog in embedded flowsheet's stream dialog
COFE.chm: stream and unit display order
COFE: corrected issue with log view: missing character after { and } in logged messages
COUSCOUS (3.4.0.1): fix bug that caused pump enery consumption to be 0 if efficiency is specified
COUSCOUS (3.4.0.2): fixed Gibbs reactor in case of no valid reactions
COFE (3.4.0.2): error message is shown in case of failure to edit a property package
COFE (3.4.0.3): added chemical formula consistency check upon loading document
TEA (3.4.0.1): removed erroneous check on doubly loading external calculation routines
COFE (3.4.0.4): added keyboard shortcut Ctrl+Space for Solve Unit
COFE: increased MRU count from 8 to 16
COFE (3.4.0.5): fixed a problem with description in meta file creation, causing crashes on save and copy on some systems
COFE (3.4.0.6): fixed similar problems with description in meta file creation, causing crashes in copying plots, objects, stream content
COUSCOUS (3.4.0.3): fixed Gibbs reactor initial guess in case of reduced feasible reaction space
COUSCOUS: Gibbs reactor resolves issues with ill-conditioned problems very close to feasible boundary by considering full-conversion components
Chemsep1.pcd, Chemsep2.pcd: updated and new compound definitions
COUSCOUS: fixed CSTR initial guess in case of reduced feasible reaction space
COUSCOUS (3.4.0.4): Make-up mixer now defaults to adiabatic - was isothermal. Isothermal is available as optional choice
COUSCOUS: Make-up mixer issues a warning rather than error in case the make-up feed flow is insufficient, and completes with zero make-up purge flow
COFE (3.4.0.7): call to put_SimulationContext prior to Load, InitNew, Initialize as per M&T recommendations
COFE: added AddMixturePropertyDefinition, AddTwoPhasePropertyDefinition, AddTemperatureDependentPropertyDefinition, AddPressureDependentPropertyDefinition to ICOFEPropertyManager interface, implemented on Simulation Context
COUSCOUS (3.4.0.5): fixed crash on receiving simulation context prior to Initialize(), as per COFE (3.4.0.6)
COUSCOUS: fixed conversion reactor now allows for specifying reaction extents
TEA (3.4.0.2): fixed issue with receiving simulation context prior to Initialize(), as per COFE (3.4.0.6)
COUSCOUS (3.4.0.6): fixed various problems with fixed conversion reactor, introduced in 3.4.0.5
COUSCOUS: replaced Brent solver for TOMS 748 in heat exchanger for cocurrent max heat exchange
COUSCOUS (3.4.0.7): fixed problem with fixed conversion reactor, introduced in 3.4.0.5
COFE (3.4.0.8): fixed reloading of dimension dependency for custom properties in stream reports
COFE (3.4.0.9): new Stream Copier unit (available from Insert menu, internal to COFE)
COUSCOUS (3.4.0.8): fixed extent of reaction reporting of Gibbs reactor
COFE (3.4.0.10): fixed problem on user compound mapping dialog after renaming compound in property package
COFE (3.4.0.11): fixed compound mapping issues due to incorrect use of std::unordered_map::emplace
COFE (3.4.0.12): fixed problem with simulation context of reaction packages, introduced in 3.4.0.7
COFE: rebuiling outdated compound map on rename compound
COFE: revalidating all unit operations after exiting flowsheet configuration dialog as some validation errors were not handled
COFE (3.4.0.13): fixed crashes in several error handlers
CORN (3.4.0.1): fixed crash on error handler, fixed improperly sized memory zeroing
COUSCOUS (3.4.0.9): fixed reporting on non-real-valued parameters, fixed improperly sized memory zeroing
COUSCOUS: fixed improper error detection on selecting invalid choice in exclusive option parameter
COUSCOUS: fixed problems after parse error when entering a conversion spec in FCR
COUSCOUS: fixed crash in measure unit in trying to obtain bubble or dew point if no vapor phase is defined
COUSCOUS: fixed issue with setting remaining factor in case sum(factors)>1
TEA (3.4.0.3): fixed selection issue with solid heat capacity routine
TEA: fixed memory leaks
TEA: avoid unnecessary derivative calculations for mass density routine
TEA (3.4.0.4): fixed problem with reading of compound names from PCD file, introduced in 3.4.0.3
COUSCOUS (3.4.0.10): fixed crash on reporting for Gibbs reactor in case no reactions take place
COUSCOUS (3.4.0.11): skipping infeasible initial guess in Gibbs reactor
COUSCOUS: fixed non negativity contraint handling in Gibbs reactor under assumption of fully reacting compounds
COUSCOUS: fixed Gibbs reactor PH flash (adiabatic operation) in case of no reactions
COUSCOUS: fixed Gibbs reactor when fully constraint by vanishing compounds
COFE (3.4.0.13): fix in compound info dialog: information was showing in improper columns in case columns are present for compound that do not appear in the selected package
COFE: fixed compound mapping issues with compound list on ports that is a subset of compound lists in embedded flowsheeet.
COUSCOUS (3.4.0.12): new algorithm for LMTD based co-current heat exchanger
COUSCOUS: new algorithm for LMTD based counter-current heat exchanger
COUSCOUS: fixed cocurrent maximum heat transfer in heat exchanger in case of two non-pure streams
COUSCOUS: fixed Gibbs reactor PH exit flash under no reaction conditions (also in case of fully constrained reactions)
COUSCOUS: using univariate (TOMS 748) instead of Newton solver for implicit compressor configurations
CORN (3.4.0.2): component balance errors and mass balance errors are now handled as warnings
COFE (3.4.0.13): fixed crash on invalid stream layout data
COFE: fixed crash on dropping file on COFE.exe
Installer: removed COSMOtherm LITE
Installer: for unpriviliged user, using Add/Remove Programs again - problems with unnecessary UAC have been resolved in 2020 release of Win10.
water: code clean up

Changes since version 3.3:

COFE (3.3.0.1): fix for crash error message in case of absense of property in balance window
COUSCOUS (3.3.0.1): fix for scenarios under which flash unit operation was not reporting heat duty
TEA (3.3.0.1): fixed problem with density and volume composition derivatives for COSTALD, Rackett, Yen-Woods
COFE (3.3.0.2): fix for solution not being invalidated upon manually specififying energy or information stream
TEA (3.3.0.2): TEA's window title now shows the word TEA
COFE (3.3.0.3): improved mapping for new compound against existing compounds
COFE: double click in select reaction package dialog is shortcut for Select
COFE: double click in select property package dialog is shortcut for Select
COFE: added ability to manually change compound mapping when adding new property packages
COFE: added Replace Property Package button to Flowsheet Settings dialog
COFE: added basis switch to context menu of stream report
COFE (3.3.0.4): fixed problem with GetCompoundConstant error handling
Water (3.3.0.1): fixes to TS and TH flashes
COFE (3.3.0.5): filtering doubles from property selection list when creating graphs
COFE: added several energy functions to list of plottable properties for overall phase
COFE (3.3.0.6): fixed issues with routine points on stream that overlap with stream start or end
COFE: added several energy functions to list of plottable properties for overall phase
COFE: saved a variety of problems pertaining to Flowsheet Unit Operations resulting from an invalid state flag after loading
COFE (3.3.0.7): fixed painting issue in stream dialog for Flowsheet Unit Operation
COFE (3.3.0.8): solved a crash on a stream with zero length
COFE: changed handling of vapor fractions in setting and resetting streams
COFE: fixed crash on zooming rapidly by scroll wheel
COUSCOUS (3.3.0.2): fix for HeatOfCombusionUnit where data was copied between compounds for which both CAS numbers were empty
COUSCOUS (3.3.0.3): reporting ideal energy consumption or generation for pump, compressor, turbine and expander
COUSCOUS: fixed broken conversion reporting on Gibbs reactor
COUSCOUS: replaced chemical formula parser in Gibbs reactor
COUSCOUS: replaced chemical formula parser in Heat Of Combusion unit
COFE (3.3.0.9): support for wiping values in array parameter editor
COFE: fixed issue with mouse capture in array parameter editor
COFE: validation of array element indices prior to setting
COFE: conveying error message upon setting invalid array parameter value during editing
COUSCOUS (3.3.0.4): fixed bounds on parameters introduced in 3.3.0.3
COUSCOUS: fixed sign on ideal energy generation expander
COFE (3.3.0.10): fixed invalid error about overall phase in binary composition plot creation
COUSCOUS (3.3.0.5): fixes for chemical formula parser for Gibbs reactor, Heat Of Combusion unit
COUSCOUS: new ElementalUnit; calculates elemental (atomic) contents and flow rates
COUSCOUS: forcing water LHV in HeatOfCombusionUnit such that HHV for water is 0 J/mol
COUSCOUS (3.3.0.6): renamed elemental mole fraction to elemental mole ratio
COFE (3.3.0.11): error checking on unit operation icon in fsd-embedded xml
COFE: fixed drawing issue in unit operation status pane when sizing dialog
COFE (3.3.0.12): enabled visual styles
COFE (3.3.0.13): fixed crash in loading string list with empty strings
COFE: fixed crash on right click component flow in stream dialog
COUSCOUS (3.3.0.7): fixed problems with Gibbs reactor introduced in 3.3.0.5
COUSCOUS: removed temperature step limiter from Gibbs reactor
TEA (3.3.0.3): fix for UNIFAC model in presence of solid only compounds
TEA: fix for liquid volume models in presence of solid only compounds
COFE (3.3.0.14): fixed confusion in compound ID and compound name for v1.1 property packages
COUSCOUS (3.3.0.7): measure unit performs post-check on temperature in case P-VF flash is used (if feed is at phase boundary)
COUSCOUS: NoOperation uses P-VF flash if feed is at phase boundary (with temperature check), or PH flash for a pure compound stream. Otherwise TP-flash is used.
COUSCOUS: ElementalUnit uses P-VF flash if feed is at phase boundary (with temperature check), or PH flash for a pure compound stream. Otherwise TP-flash is used.
COUSCOUS: HeatOfCombustionUnit uses P-VF flash if feed is at phase boundary (with temperature check), or PH flash for a pure compound stream. Otherwise TP-flash is used.
TEA (3.3.0.4): Fix for finding PCD manager in x64
CORN (3.3.0.1): corrected error message on empty compound list
COUSCOUS (3.3.0.8): no longer trying GetForegroundWindow to try to find nice parent window for ICapeUtilities::Edit - this may lead to a dead lock
COFE (3.3.0.15): fixed error reporting on unit icon read failure
COFE (3.3.0.16): added ICOFEDocument::Import, similar to ICOFEDocument::LoadFromString with file:///
COFE: added ICOFEDocument::Solve, similar to ICOFEDocument::SolveFlowsheet but with exception instead of string output argument
COFE: ICOFEDocument::LoadFromString and ICOFEDocument::SaveToString raise exception on error
COFE: ICOFEDocument::SolveFlowsheet was modified to wait until solution is finished before returning
Water (3.3.0.2): correction to Cv for regions 2 and 5
COFE (3.3.0.17): fixed truncation issues for export parametric study results
COFE (3.3.0.18): correction that caused missing results for parametric jobs because of other parametric jobs failing
COFE: if dependent job fails in parametric study, error message is added to the dependent job to reflect that.
COFE (3.3.0.19): fixed issue with incorrect "solver failure" exception from automation
COFE: more descriptive error message at solver failure via automation
COFE: resolved an issue causing COFE to remain running with automation documents still open
COFE (3.3.0.20): fixed disappearing mole or mass compound flow input to parametric study
COFE (3.3.0.21): fixed issue with double entries in log
Installer: CO-LaN provided CAPE-OPEN type library MSIs are used
Installer: for unpriviliged user, not using Add/Remove Programs anymore due to Win10 problems with unnecessary UAC. Instead adding Uninstall to COCO start menu.

Changes since version 3.2:

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
COFE: fixed initial font edit box
COFE: changed default font from "MS Sans" to "Arial"
COFE: 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)
COFE: 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
COFE: 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
COFE: 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
COFE: logging each failed unit evaluation in debug verbosity mode to help assess flowsheet initialization failure
COFE: material object no longer accepts zero or negative values for pressure or temperature
COFE: 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
COFE: 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
COFE: bug fix for parametric study where feed streams containing controller set points are parametric inputs
COFE: bug fix for controller feed setpoint virtual parameter feed stream influence on Jacobian
COFE: revision of job queueing for controller unit operations
COFE (3.2.0.13): compiler upgrade
COFE: 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
COFE: added Copy summary (Tool Tip) to context menu of stream and unit
COFE: 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
COFE: fixed inability to pan while solving
COFE: 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
COFE (3.2.0.18): fix to flowsheet unit operation (disabled shortcut to Save leading to crash)
COFE: new compound mapping dialog in flowsheet unit operation
COFE: improvements to compound mapping in flowsheet unit operation
COFE: added title to embedded plots (so that after "take out of flowsheet" plot does not appear without title)
Water (3.2.0.1): corrected chemical formula (was set to CAS number instead of chemical formula)
Water: updated project file to VS 2017
COUSCOUS (3.2.0.8): fixed issue with switching PFR to heat balance mode
COUSCOUS (3.2.0.9): fixed problem with heat exchanger and pure compound stream
COUSCOUS (3.2.0.10): corrected heat balance for PFR - flow rate contribution of inert compounds was not taken into account
COFE (3.2.0.19): fixed error handling on incorrect compounds in XML
COFE: fixed crash upon lengthy operation (such as file drag & drop) while splash screen is visible
Help: fixed kinetic gas theory equation for vapor viscosity
CUP (3.2.0.3): adjustments for 3rd party prerequisite checking
COFE (3.2.0.20): fixed error handling upon non-existent unit operation port
COUSCOUS (3.2.0.11): corrected error handling in FCR
COUSCOUS (3.2.0.12): corrected counter current NTU calculation in heat exchanger for equal Cp streams
Help: updated NTU equations
COFE (3.2.0.21): fixed dialog font size issues
COFE (3.2.0.22): temperature limit states for energy streams are solved in log domain
COFE: forcing update on parameter collections of energy and information streams after editing connected unit
COFE: correction to equality check of real numbers for NaN and infinity
COUSCOUS (3.2.0.13): added option to thermal energy mixer to suppress temperature limits on product port
COUSCOUS: added option to thermal energy splitter to suppress temperature limits on product ports
Help: changed help on energy mixer and energy splitter
COUSCOUS (3.2.0.14): Splitter P+VF flash (introduced in 3.2.0.3) is checked for temperature consistency. For more than 0.1 K difference, the T-P flash is invoked.
COUSCOUS (3.2.0.15): flash unit improvements
COUSCOUS: multiple feed ports to flash unit
Help: added information on switching thermodynamics for stream types
COFE (3.2.0.23): Added the ability to update molecular weights from a property package (Flowsheet settings, compounds)
Help: added help on updating molecular weights
COFE (3.2.0.24): fix on error check CAS numbers (invalid error 'too many digits in CAS number')
TEA (3.2.0.3): fix on error check CAS numbers
CORN (3.2.0.1): fix on error check CAS numbers
COFE (3.2.0.25): fix on values of controlled streams (did not get depersisted into main document when solved in a different thread)
COFE (3.2.0.26): fixed problem with persistence of description string for unit operations and flowsheet monitoring objects
COFE (3.2.0.27): changed terminology for consistency (unit operation properties vs edit unit operation)
Help: changed terminology for consistency (unit operation properties vs edit unit operation)
TEA (3.2.0.5): new temperature equation 18: A+B*(1+ln(T)*(1+C/T))*exp(-C/T)
TEA: new temperature equation 19: A+B*T*ln(T)*exp(-C/T)
TEA: correction on VARIANT data handling for enumeration types
TEA: support for new gc file format
CUP (3.2.0.4): fixed issues with elevation and "another CUP is running"
COFE (3.2.0.28): fixed temporary invalid compound property list after re-ordering compound list (causing amongst other things reaction stoichiometry indices to be incorrect until next load/save)
COFE: after thermo or material type change, reaction packages are revalidated
COUSCOUS (3.2.0.16): fixed invalid caching of compound names
Installer: removed installation of 1.0 type lib
CUP/CheckProxy: updated from .NET 2.0 to .NET 3.5

Changes since version 3.1:

COFE (3.1.0.1): prevent problems due to re-entrancy in painting methods caused by STA threads in 3rd party modules
COFE: fixed problems with stream dialogs no longer updating resulting from a failed update during solving
COFE: fixed layout issue in stream report
COFE: reporting compound names for compositions of phase equilibrium calculation in calculator output
COFE (3.1.0.2): fixed reports with empty numbers after load (introduced in 3.1.0.1)
COFE (3.1.0.3): fixed crash on failure to load property package or reaction package
COFE: fixed problem with redundant calls to UnsetMaterial
OATS (3.1.0.1): persistence support for PPM/TS/RPM based package (based only on exposed manager name)
COFE (3.1.0.4): support for COFEStand command line option
COFE: Changed "Color Schemes" tab to "Appearance"
COFE: Added font selection to "Appearance" tab
COFEStand (3.1.0.0): initial release
CUP (3.1.0.2): avoid trouble with "Another CUP is running" at elevation
COFE (3.1.0.5): fixed problem with parameteric studies that have inputs on information streams that are flowsheet feed streams
COFE (3.1.0.6): slightly larger property dialogs
COFE: bigger font selection list in text dialog
COFE (3.1.0.7): fix pertaining to final solution status COFEStand
COFE (3.1.0.8): crash fix for COFEStand when running via pipe
TEA (3.1.0.1): fixed problems with property values due to perturbations in case of combined property calculations for EOS models
COFE (3.1.0.9): fixed problem pertaining to drop down list sizes within grids
COFE (3.1.0.10): fix for calculating dew- or bubble points from calculator
COFE (3.1.0.11): fixed a problem from partial results of GetCompoundConstant
COFE: corrected P-dependent property handling
COFE: fix for partial missing values for T- and P- dependent properties
COFE: fix for crash upon context menu in array parameter value dialog
TEA (3.1.0.2): fixed use of external equilibrium routines
TEA (3.1.0.3): fixed problems with composition derivatives and solid-only compounds (which now return a value of zero for composition derivatives in phases where they cannot appear)
TEA (3.1.0.4): fixed problem with EOS enthalpy, introduced in 3.1.0.3
TEA (3.1.0.5): fix that allows for exposing enthalpyF and entropyF for systems that define solid-only compounds
COFE (3.1.0.12): controlled and measured stream indices fixed in solver analysis stage
COFE: error handling upon controllers that are not in a loop fixed in solver analysis stage
Water (3.1.0.1): unit conversion correction to density and volume in region 3
COUSCOUS (3.1.0.1): small adjustment in heat of vaporatization of water for HeatOfCombustion unit (to convert between LHV and HHV)
CORN (3.1.0.1): fixed parsing of F (fugacity)
TEA (3.1.0.6): fixed invalid vapor (instead of liquid) assignment in PH flash single phase result
COUSCOUS (3.1.0.2): fixed conversion reactor failed in case of parallel reactions in which a reactant violates the non-negativity contraint in between two reactions
COFE (3.1.0.13): new option in preferences to open a file in a new COFE instances when double clicking in file manager (Windows Explorer) instead of in existing instance
COFE (3.1.0.14): imposing name change on Property Package and Reaction Package in case of change by PME
Chemsep1.pcd: fixed liquid viscosity fit #520 and updated the version to 7v13
COFE (3.1.0.15): imposing property / reaction package name after persistence and loading from manager
COFE: imposing property package name after creation from thermo system or package manager
COUSCOUS (3.1.0.3): allowing omission of cat loading for packed bed in case of no heterogeneous reactions
COUSCOUS: renamed packing parameters for packed bed PFR
Help: clarified PFR parameters
COCO (3.2): compiler update
Installer: fixed registration of COFEPrevHandl64.dll

Changes since version 3.00:

CUP (3.0.0.1): bug fix in obtaining update list
CUP (3.0.0.2): all remote data is validated by hash and signature
CUP (3.0.0.3): fixed problem with obtaining installer info
CUP (3.0.0.4): fixed permission issues while updating CUP
COFE (3.0.0.1): no longer allowing illegal characters to be saved by unit operation as back-parsing them causes the file to fail to load
COFE: fix to crash upon solution for units with virtual information ports
COFE: fixed abort simulation request for embedded flowsheets
COFE (3.0.0.2): fix to crash upon obtaining compound constants for non-existing compounds (version 1.1 property package only)
COFE: fix to allow for saving documents containing embedded COFE documents via OLE
COFE.XLT removed redundant endif in macros
COUSCOUS (3.0.0.1): fixed problems with parameter modes of heater/cooler
COUSCOUS (3.0.0.2): fixed problems with energy port direction of heater/cooler
COUSCOUS (3.0.0.3): fixed input/output mode for heater/cooler parameters
COFE (3.0.0.3): added phase fractions to material stream tool tips
COFE: fixed crash on loading documents with saved calculator views
COFE: fixed writing composition for calculator views when saving
COFE (3.0.0.4): fix in finding CUP to perform auto-updating and manual updating from the Help menu
CUP (3.0.0.5): fixed error reporting in case of failure
COFE (3.0.0.5): fix to restoring unit after solution that fails initial guess
COFE: as interim solution for ChemSep pop-ups in the solution threads, COFE sets ChemSep's SuppressWarnings public parameter to FALSE when a ChemSep unit is loaded into a solution thread
ChemSep1.pcd: extension to IG Cp correlations
TEA (3.0.0.1): fixed problem with reversed editing interaction parameters
installer: fix to removal of registry values specific to current user vs all users (instead of removing classes_root version)
COUSCOUS (3.0.0.4): fixed crash in compound splitter with zero split factors
COUSCOUS (3.0.0.5): fixed report persistence on PFR, HeatOfCombustionUnit
COUSCOUS: fixed loading of output parameter of information calculator
COUSCOUS: fixed loading conversion parameter values of PFR reactor
TEA (3.0.0.2): fixed problems with reading compound mapping external calculation routines
TEA: fixed reading selection of external equilibrium routines
TEA: fixed reading empty strings, leading to problems instantiating external calculation routines
COFE (3.0.0.6): checking for unique stream names in embedded flowsheet prior to saving
COFE: fixed problems with UTF16 file names when saving files
CORN (3.0.0.1): fixed crash on enabling forward reaction in reaction rate wizard
COFE (3.0.0.8): fixed uninitialized stream counter when reloading document that does not contain streams
TEA (3.0.0.3): post-check on single phase supercritical solution
TEA: fixed post check on two-phase supercritical solution
TEA: new phase assignment rules for supercritical solutions
COFE (3.0.0.9): fixed crash on property plots after loading from new document file format if plotting composition, fraction, phase fraction, flow, temperature or pressure
COFE (3.0.0.10): insert preview image into fsd for Windows Explorer preview functionality of fsd files (enhanced meta file, base64 encoded)
COFE Preview Handler (3.0.0.2): adjusted displayed time to local time zone
COFE Preview Handler: fixed registration problems on winXP
COFE (3.0.0.11): fix to dimension preferences for unit operation parameter, in case of parameters of different unit operation instances of same unit with same name but different dimensionality (e.g. controller setpoint parameters of two controllers)
TERNYP (3.0.0.1): fixed plotting equilibrium temperatures
TERNYP: changed mapping algorithm of residue curve map
COFE (3.0.0.12): fix to starting solver in case of multiple dimensionality preferences for the same parameter (introduced in 3.0.0.11)
COFE (3.0.0.13): button for additional advise near "number of threads" in preferences
COFE: printing initial guess residual if converged at initial guess
COFE (3.0.0.13): renamed "Show GUI" to "Edit"
COFE: fixed Save As on log view
COFE: compiler upgrade
COFE: tighter optimization
COFE: logging refactoring
COFE: per-unit operation log lines are grouped into similar lines
ChemSep1.pcd: upper T limit adjustment for liquid viscosity Ethylene Oxide
COUSCOUS (3.0.0.6): compiler upgrade
COFE Preview Handler (3.0.0.3): compiler upgrade
CORN (3.0.0.2): compiler upgrade
CORN: tighter optimization
TEA (3.0.0.4): compiler upgrade
TEA: tighter optimization
TERNYP (3.0.0.1): compiler upgrade
TERNYP: tighter optimization
COFE Preview Handler (3.0.0.4): resolved registration problems for current user installation
COFE (3.0.0.15): logging line ending corrections
CUP (3.0.0.6): avoiding repeated question for proceeding with update after relaunch for elevation
COFE Preview Handler (3.0.0.5): resolved registration issues
COFE (3.0.0.16): unit log groups performance enhancements
COFE: fixed persistence exception handling
COFE: eliminated temp files in zip/xml reading/writing, in favour of in-memory xml
COFE: fixed crash upon persistence due to new logging mechanism
COFE (3.0.0.17): fixed import file into embedded flowsheet
COFE (3.0.0.18): fixed dimensionality selection for unit operation parameters
COUSCOUS (3.0.0.6): fix to Gibbs reactor to prevent crash upon updating conversion report
COFE (3.0.0.19): fixed problem restoring reaction packages from file
COFE (3.0.0.20): fixed issue with missing line separations in log view
COFE (3.0.0.21): fixed reading previously saved dimensionalities from XML
COFE (3.0.0.22): parametric study fixes
COFE (3.0.0.23): fixed rubberband selection adjustments while scrolling
COUSCOUS (3.0.0.7): fixed problems loading information calculators with spaces or other non-alphanumeric characters in output variable name
COFE (3.0.0.24): additional diagnostics info at failure to find initial guess for partition
COFE (3.0.0.25): fixed loading flowsheet comment (File, Properties), stream comments, unit operation comments
COFE (3.0.0.26): work-around for problems resulting from earlier bug leading to saving invalid dimensionality objects
COFE Preview Handler (3.0.0.6): re-enabled XP support
TEA (3.0.0.5): fixed error handling on failure to get T, P, compositon from MO
COUSCOUS (3.0.0.8): flash no longer lowers product pressure below pressure spec in case pressure spec lower than feed spec
COFE (3.0.0.27): fixed tool tip for streams to only show phase fractions when in phase equilibrium
COFE (3.0.0.28): modified run time reference
COFE: fix for crash on wine
COFE (3.0.0.29): added import conversion for unit operation dimensionality for W/m/K
COFE: fixed crash in calculator upon Copy All From Stream (context menu)
TEA (3.0.0.6): implement work-around for range error in Misic-Thodos 1 pure compound vapor thermal conductivity
COFE (3.0.0.30): adjusted find stream and unit to move stream or unit into view rather than centering it
COFE: find stream or unit is invoked when double clicking on error or warning in error/warnings pane
COUSCOUS (3.0.0.9): corrected flash outlet pressure in case of pressure spec (problem introduced in 3.0.0.8)
COFE (3.0.0.31): fixed retaining unit operation error status after failed solve
TEA (3.0.0.7): fixed memory leak
COFE (3.0.0.32): fixed recycle scanner in case of presence of controllers (recycles were potentially undetected leading to infinite loops, COFE stalls)
COFE: marking streams unsolved on reset failed in some cases
COFE: set focus on edit box in log view upon select all as to see selection
COFE (3.0.0.33): fixed incomplete partitioning error on controller that is not part of a recycle
COFE (3.0.0.34): calculator support for compounds constants
COFE: item in CAPE-OPEN selection dialog was not available for selection after changing model class for the item (until dialog was closed and re-opened)
COFE: changed formatting of non-integer dimensionalities
COFE: fixed building of phase list, causing solid and unknown phases to be name-less (and subsequent errors from phases without a name)
COFE (3.0.0.35): fixed post-processing of feed flow rates of flow-constrained feeds at flowsheet solution
COFE (3.0.0.36): fixed error check on post-processing of flow-constraints
COFE (3.0.0.37): fixed error check on post-processing of flow-constraints, introduced in 3.0.0.36
COFE (3.0.0.38): fixed name not unique after pasting unit operation that saves and reloads is own name
COFE: formula parser fixes
COUSCOUS (3.0.0.10): several simplifications in flash
COUSCOUS: flash no longer copies feed composition prior to executing flash (should be implicit in creation of the calculation material, which is a duplicate of the feed)
COUSCOUS: adiabatic flash at zero pressure drop reduces to equilibrium that equals the feed equilibrium (the actual adiabatic flash is skipped)
COUSCOUS: formula parser fixes
COFE (3.0.0.39): invalid CAS numbers are no longer ignored (and error is changed to warning, still logged)
TEA (3.0.0.8): formula parser fixes
TEA: removed heat of vaporization at normal boiling point support (no longer in PCD file)
COFE (3.0.0.40): compiler upgrade
COFE: corrections in XML parser error reporting
COFE: fixed problem with integer parameters exposed from embedded flowsheets
COFE: fixed storing of default unit operation icons
COFE: fixed problem with parallel Newton iterates in case first iteration of line search fails (all subsequent iterations failed)
COFE: adjused switching between simplified and full model evaluations to avoid hysteris in solution approach
COFE/GOOOP32: win32 PMC private GUIs in COFE64 appear in front of instead of behind COFE
COFE Preview Handler (3.0.0.7): compiler upgrade
CORK (3.0.0.1): compiler upgrade
CORN (3.0.0.3): compiler upgrade
COUSCOUS (3.0.0.11): compiler upgrade
JUIcE (3.0.0.1): compiler upgrade
TEA (3.0.0.9): compiler upgrade
CUP (3.0.0.7): compiler upgrade
CUP: scanf format fixes
CUP: fixed problems with special characters in cup.dat path name
TERNYP (3.0.0.2): compiler upgrade
OATS (3.0.0.1): compiler upgrade
Water(3.0.0.1): compiler upgrade
ChemSep1.pcd: improved various Cp (ideal gas) correlations
installer: fixed x64 type library registration issues

Changes since version 2.07:

COFE (2.7.0.1): ensuring menu bar is visible and docked upon initially showing main window
COFE (2.7.0.2): fixed problems with convergence check flow constraint inside recycle
COFE.xlt: added T and P as outputs of equilibrium calculations
TEA (2.7.0.1): repaired mouse selection in IPD edit dialog
TEA: VS upgrade
TEA: using Intel compiler
TEA: switched to UNICODE
TEA: fixed error reporting on missing Wilson parameters
Water (2.7.0.1): VS upgrade
Water: restored XP support
OATS (2.7.0.1): VS upgrade
OATS: updated icon
JUIcE (2.7.0.1): VS upgrade
JUIcE: switched to UNICODE
JUIcE: updated icon
GOOOP32 (2.7.0.1): VS upgrade
CUP (2.7.0.1): VS upgrade
CUP: switched to UNICODE
CUP: updated icon
COUSCOUS (2.7.0.1): VS upgrade
COUSCOUS: using Intel compiler
COUSCOUS: switched to UNICODE
COUSCOUS: correction in string parameter equality test
COUSCOUS: resolved memory leak in PFR
COUSCOUS: resolved x64 pointer error
CORN (2.7.0.1): VS upgrade
CORN: using Intel compiler
CORN: switched to UNICODE
CORN: removed some thread safety issues with static buffers
CORN: fixed reading charge from PCD files
COFE (2.7.0.3): repaired mouse selection in IPD edit dialog
COFE: VS upgrade
COFE: using Intel compiler
COFE: switched to UNICODE
COFE: updated icon
COFE: updated document icon
COFE: fixed error messages on failure to open help
COFE: strings are stored in document file in UNICODE encoding
COFE: reports can be exported as UNICODE text
COFE: x64 pointer fixes
COFE: new unit operation icon caching system
COFE: window styling (preferences)
COFE: new stream selection drop down on toolbar
ConfigureTEA: updated icon
ConfigureCORN: updated icon
CORK (2.7.0.1): VS upgrade
CORK: switched to UNICODE
TERNYP (2.7.0.1): VS upgrade
TERNYP: using Intel compiler
TERNYP: fixed an x64 pointer issue
(un)registration batch files: fixed replacement of Steamer by Water
COFE (2.7.0.4): fixed crash, introduced in 2.7.0.3
TEA (2.7.0.2): fixed problem with updating configuration, introduced in 2.7.0.1
COFE (2.7.0.5): fixed icon issues, introduced in 2.7.0.3
COFE (2.7.0.6): repaired unit icon selection dialog, broken since 2.7.0.3
COFE: fixed crash upon closing compound info dialog, broken since 2.7.0.3
COFE: fixed tool tips, broken since 2.7.0.3
COFE: fixed problems with export of icons, broken since 2.7.0.3
COFE: fixed problem with modelclasses.dat, broken since 2.7.0.3
COFE: fixed problem with pasting numbers, broken since 2.7.0.3
OATS (2.7.0.2): fixed switch for logging AddRef/Release/QueryInterface
CUP (2.7.0.2): fixed file name issues introduced in CUP 2.7.0.1
COFE (2.7.0.7): Newton solver stability enhancement
COFE: fixed crash on icon transformations, broken since 2.7.0.3
OATS (2.7.0.3): conversion to UNICODE
OATS: catching std::exception
OATS: resolved encoding problems with non-ASCII characters
COUSCOUS (2.7.0.2): fixed problem with property tester output, introduced in 2.7.0.1
COFE (2.7.0.8): fixed some uninitialized memory issues
COFE: fixed hash function in new icon engine
COFE: fixed problems with error handling in TP plot window
COFE: fixed index out of range for default plot color in case more than 16 series
COFE: fixed memory leaks upon unexpected end of file while reading controller units
COFE: fixed memory leak for array parameters
COFE: fixed memory leak upon port out of connection points scenario
COFE: fixed memory leak on error condition of obtaining reference state values
COFE: correction for drawing dotted lines around objects
COFE: fixed internal state issues upon recursive calling of MO
COFE: fixed basis check in reaction package wrapper
COFE: fixed error handling on parse error upon data entry in watch window
COUSCOUS (2.7.0.3): fixed some uninitialized memory issues
COUSCOUS: fixed problem with AspenPlus specific dialog handling
COUSCOUS: fixed problem with error message on failing product flashes
COUSCOUS: resolved memory leak under error conditions in Flash unit operation
COUSCOUS: resolved memory leak under error conditions in HeatExchanger unit operation
COUSCOUS: resolved memory leak under error conditions in PFR unit operation
COUSCOUS: corrected phase presence warning for fixed conversion reactor
COUSCOUS: corrected initial guess of backup method HeatExchanger
COUSCOUS: corrected mass based operation of MakeUpMixer
COUSCOUS: logic correction to Brent (1D) solver
COUSCOUS: resolved memory leak in Gibbs reactor
TEA (2.7.0.3): resolved memory leaks in backup flash algorithm
TEA: resolve memory leak on property package configuration
TEA: correction to internal energy flashes in presence of solids
TEA: fix to convergence failure detection in chemical theory model
TEA: corrected error handling missing values GetComponentConstant
TEA: corrected evaluation of temperature dependent equation 2: A+B*T
TEA: fixed error handling on QI failures
TEA: fixed problems reading GC files, introduced in 2.7.0.2
COUSCOUS (2.7.0.4): fixed string allocation problem in Gibbs reactor, leading to subsequent unpredicted behaviour
COFE (2.7.0.9): mouse hook stops forwarding message to prevent message beep upon clicking outside of active edit field
TEA (2.7.0.4): mouse hook stops forwarding message to prevent message beep upon clicking outside of active edit field
props.ini: corrected definition for virialcoefficient property (was invalidly marked as non-mass-basis property)
COFE (2.7.0.10): corrected calculation type error in calculator
COFE (2.7.0.11): repaired plot axes, broken since 2.7.0.8
OATS (2.7.0.4): fixed problem with saving packages; introduced in 2.7.0.3
COFE (2.7.0.12): fixed problem with PH flash (pure product streams) with COFE flowsheet unit operation, thermo 1.0
COFE: COFE flowsheet unit operation logging suppressed (level silent, only errors are logged) during loading and port connections
COFE (2.7.0.13): graphics library update
COFE: compiler update
CORN (2.7.0.2): compiler update
COUSCOUS (2.7.0.5): compiler update
TEA (2.7.0.5): compiler update
COFE (2.7.0.14): support for boolean named value AbortCalculation to allow for interrupting length unit operation calculations at flowsheet solution time
CUP (2.7.0.3): fixed problem with saving proxy data
COFE (2.7.0.15): fixed mass/mole conversion bug when setting mass fractions on MO, in case of compounds that do not have PP order
TEA (2.7.0.6): fixed broken edit compound window (introduced in 2.7.0.1)
JUIcE (2.7.0.2): fixed problems with saving files (introduced in 2.7.0.1)
COFE.xlt: added support for getting phase list, phase fraction and phase composition when embedded in Excel
OATS (2.7.0.5): fixed logging of quotes in interface logging
COFE (2.7.0.16): correction to manually enabling reference state correction
COFE: fixed reading main window in case saved from embedded document
COUSCOUS (2.7.0.6): fixed UA prediction for co-current heat exchangers (was missing)
COUSCOUS: allowing co-current mode for specified temperature or heat duty
COFE (2.7.0.17): fixed several issues with colour scheme dialog
Water (2.7.0.2): spell check
TEA (2.7.0.7): corrected spelling method names and error messages
TEA: added equations 124 (A+B/T+C/T^2+D*T+E*T^2) and 125 (exp(A+B/T+C/T^2+D*T+E*T^2))
TEA: mixture gas viscosity routine sets minimum value of extrapolated pure compound viscosities to 1e-10 (negative and zero values result problems in the mixture models)
COFE (2.7.0.18): fixed issue with sort order selection
COFE: caching of property entries in props.init
CORK (2.7.0.2): fixed spelling errors
CORN (2.7.0.3): fixed spelling errors
TERNYP (2.7.0.2): fixed spelling errors
COUSCOUS (2.7.0.7): fixed pump and compressor zero flow messages (missing unit operation name)
COUSCOUS (2.7.0.8): fixed crash in property tester, introduced in 2.7.0.1
COFE (2.7.0.19): fixed problem in stream dialog with multiple information streams containing data with different dimensions
Water (2.7.0.3: entropy flash fix near lower temperature boundary
Water: switch to functionals and lambdas for iterative solutions
Water: iterative solution refinement for PH and PS flashes
COFE (2.7.0.20): fixed problems with unit operation icon re-assignment
Water (2.7.0.4): adjusted boundaries during iterative refinement
TEA (2.7.0.7): TP flash correction
COUSCOUS (2.7.0.9): fixed problem with heat exchanger in counter current case NTU mode if max heat transfer for cold and hot side is equal
COUSCOUS (2.7.0.10): fixed problem with heat exchanger in counter current case NTU mode if max heat transfer for cold and hot side is equal (correction on 2.7.0.9)
CORN (2.7.0.4): replaced mutex by critical section around parser
COUSCOUS (2.7.0.11): replaced mutex by critical section around parser
COUSCOUS: fixed threading issue with thermo version parameter
COFE (2.7.0.21): added GWh and MWh energy units
COFE: added toolbar buttons for printing
COFE (2.7.0.23): fixed compound mapping upon setting feed composition for flowsheet unit operation
COFE (2.9.9.9): new flowsheet partitioners
COFE: new flowsheet solvers
COFE: new parametric study solvers
COFE: corrections on method names in error messages
COFE: new stream sorters
COFE: new unit sorters
COFE: fixed spelling errors
COFE: fixed preference defaults
COFE: quicker, internal, creation of embedded flowsheet units
COFE: fixes to layout of "never show again" message boxes
COFE: new handling of frame windows with embedded flowsheets (no unnecessary frame creation)
COFE: avoiding toolbar problems resulting from showing in-place or embedded frame windows
COFE: fixed problems with zero-flow bypass, and outlet information streams
COFE: fixed invalidation of document upon entering flowsheet options tab
COFE: fixed problems with setting reference T and P
COFE: flash error reporting v1.1 fix (crash)
COFE: ensuring unique stream names
COFE: ensuring unit operation stream names
COFE: base64 corrections (error check and proper data length check)
COFE: open file format (xml+zip)
COFE: resolved memory leak and port object leak in virtual information port handling
COFE: storing PMCs by ProgID (if available) rather than CLSID
COFE: storing stream connection by port name instead of port index
COFE: fixed pasting rtf data
COFE: fixed problem with copy on Ctrl+C in stream dialog
COFE: performing validate during reset, with named value ResetOnValidate set to true
COFE: parameter selection by name instead of obtaining entire collections (performance improvement)
COFE: fixed crash on loading document with incompletely restored thermo
COFE: dimensional lookup by hash tables (performance)
COFE: fixed crash on stream routing issue
COFE: fixed input selection on parametric plot dialog
COFE: allow for inspection and clearing of user-mapped compounds of embedded flowsheet
COFE: fixed rotation on scaled icons
COFE: faster string comparisons
COFE: hashed phase ID lookups
COFE: optimizations to flowsheet painting (performance)
COFE: fixed units of measure of parametric plot results for multiple axes (all series used unit of measure conversion of first y axis)
COFE: fixed resolution in dialog of parametric study plot series properties
COFE: fixed ability to select overall phase for enthalpy/enthalpyF/entropy/entropyF/volume in T-dependent, P-dependent and binary property plots
COFE: resolved memory leak in external port dialog of embedded flowsheet
COFE: resolved problem with construction of information ports for embedded flowsheet
COFE: responding to AbortSimulation request on embedded flowsheet
COFE: added solution info to status pane
COFE: renamed material type to stream type
COFE: weekly update checking (can be disabled from application preferences)
TEA (2.9.9.9): fixed thread safety issue binary interaction parameter tables
TEA: property bag storage support
TEA: faster string comparisons
TEA: hashed property lookups
OATS (2.9.9.9): new libxml2
CUP (2.9.9.9): new libxml2
CUP: no longer requires admin rights at startup; CUP is restarted with admin rights only when required
CUP: fixed issue with unregistration of files to be replaced
CUP: fixed error reporting on failure to delete files
CUP: fixed error message on COM DLL (un)registration
CORK (2.9.9.9): writing CAT Ids to current user in key in case of no permission to classes root key
COUSCOUS (2.9.9.9): property bag storage support
COUSCOUS: hashed parameter collections (performance)
COUSCOUS: correction in linear dependence checking and reporting of reactions GibbsReactor, CSTR, EquilibriumReactor
COUSCOUS: corrections on indexing in case of eliminated reactions in GibbsReactor, CSTR, EquilibriumReactor
COUSCOUS: correction for groups of linearly dependent kinetic reactions in CSTR
COUSCOUS: faster string comparisons
CORN (2.9.9.9): property bag storage support
CORN: faster string comparisons
Water(2.9.9.9): fixed error codes upon registration failure
Help: corrections to help file
ChemSep1.pcd: updated component data

Changes since version 2.06:

COFE (2.6.0.1): removed SCROLL LOCK indicator from status bar
COFE: fixed problem with version 1.1 property package context material immediately after Edit (material pointer was lingering)
COUSCOUS (2.6.0.1): fix on non-negativity constraint handling in CSTR and equilibrium reactors
COUSCOUS (2.6.0.2): Added Consumes_Thermo_CATID, SupportsThermodynamics10_CATID and SupportsThermodynamics11_CATID for Turbine, StreamConverter, Splitter, SolidSeparator, Pump, PropertyTester, PropertyTester, NoOperation, Mixer, MeasureUnit, MakeUpMixer, HeatOfCombustionUnit, HeatExchanger, GibbsReactor, Flash, FixedConversionReactor, Expander, EquilibriumReactor, CSTR, Compressor, Valve, ComponentSplitter
CORK (2.6.0.1): Added support for Consumes_Thermo_CATID, SupportsThermodynamics10_CATID and SupportsThermodynamics11_CATID
CORN (2.6.0.1): Added Consumes_Thermo_CATID, SupportsThermodynamics10_CATID and SupportsThermodynamics11_CATID for reaction package manager
OATS (2.6.0.1): Added Consumes_Thermo_CATID, SupportsThermodynamics10_CATID and SupportsThermodynamics11_CATID for COULIS unit operation
TERNYP (2.6.0.1): Added Consumes_Thermo_CATID, SupportsThermodynamics10_CATID and SupportsThermodynamics11_CATID
COFE (2.6.0.2): correction to mass/mole conversions of phase fractions in case compounds are not in same order as property package
COUSCOUS (2.6.0.3): refined check on presence of non liquid phases in pump and turbine, checking for vapor phases only
COUSCOUS: pump and turbine determine volumetric flow based on total molar flow multiplied by average molar volume of the liquid phases only. Fail in case only vapor is present
COUSCOUS: corrections to turbine calculations
TEA (2.6.0.1): single-compound mass vapor fraction flash returned improper phase fractions
COFE (2.6.0.3): fix on jpg color tables when importing graphics
COFE: correction in mm H2O pressure conversion
COFE: added inch H2O and inch Hg pressure unit conversions
COFE: dimension choices are in alphabetic order
COFE.xlt: fixes for Office 2010 x64
COUSCOUS (2.6.0.4): fixed link to compound splitter help
COUSCOUS (2.6.0.5): pump and turbine where using aggregation states rather than phase labels for obtaining phase volumes (introduced in 2.6.0.3)
TEA (2.6.0.2): replaced hash map implementations
TEA: Property Package Edit returns S_FALSE in case of Cancel
COFE (2.6.0.3): replaced hash map implementations
COFE: no longer invalidating flowsheet as result of Edits that return S_FALSE (edits that did not make modifications)
COFE: embedded flowsheet returns S_FALSE for edit in case no changes were made during edit
COFE: fixed several places where a unit should be invalidated
COUSCOUS (2.6.0.6): corrections on formula parse errors in heat exchanger edit box
COUSCOUS: all Edit routines return S_FALSE instead of S_OK in case nothing has changed
CORN (2.6.0.2): Reaction Package Edit returns S_FALSE in case of Cancel
COFE (2.6.0.4): fixed out of memory message in case of dragging a single stream without any other streams or unit operations
COFE (2.6.0.5): validation fixes in case of changing types of streams
COFE: the solution state of a unit is invalidated in case a product stream is changed
COFE: JPG library upgraded
TEA (2.6.0.4): a new property package is not accepted if not at least some model has been selected (prevents a lot of warning messages in case the model selection was omitted)
CorkHelper (1.0.0.2): fixed WinXP x86 incompatibility
TEA (2.6.0.5): property lists are returned in a fixed order (was random)
COUSCOUS (2.6.0.7): fixed invalidation of unit operation upon opening dialog
COUSCOUS (2.6.0.8): fixes several bugs in pump and turbine when using thermo version 1.0, introduced in 2.6.0.3
COFE (2.6.0.6): fix preventing information and energy stream content to get wiped at single-ended disconnect
COFE: added unit operation type name to unit operation tool tip
COFE (2.6.0.7): upgraded compiler
CORK (2.6.0.2): upgraded compiler
CorkHelper (1.0.0.3): upgraded compiler
CORN (2.6.0.3): upgraded compiler
ConfigureCORN: upgraded compiler
COUSCOUS (2.6.0.9): upgraded compiler
TEA (2.6.0.6): upgraded compiler
ConfigureTEA: upgraded compiler
CUP (2.6.0.1): upgraded compiler
GOOOP32 (2.6.0.1): upgraded compiler
JUIcE (2.6.0.1): upgraded compiler
OATS/COULIS (2.6.0.2): upgraded compiler
Water (2.6.0.1): upgraded compiler
Water: source code upgraded to VS2012 project
TERNYP (2.6.0.2): upgraded compiler
CORK (2.6.0.3): re-enabled support for XP
COFE (2.6.0.8): re-enabled support for XP
CorkHelper (1.0.0.3): re-enabled support for XP
CORN (2.6.0.4): re-enabled support for XP
ConfigureCORN: re-enabled support for XP
COUSCOUS (2.6.0.10): re-enabled support for XP
TEA (2.6.0.7): re-enabled support for XP
ConfigureTEA: re-enabled support for XP
CUP (2.6.0.2): re-enabled support for XP
GOOOP32 (2.6.0.2): re-enabled support for XP
JUIcE (2.6.0.2): re-enabled support for XP
OATS/COULIS (2.6.0.3): re-enabled support for XP
Water (2.6.0.2): re-enabled support for XP
Water: source code upgraded to VS2012-SP1 project
TERNYP (2.6.0.3): re-enabled support for XP
COUSCOUS (2.6.0.11): fixed problem with input of dimensionality of measure unit
COFE (2.6.0.9): fixes to PNG import routines
COFE: renamed thermo system/property package manager ICapeParameter based edit dialog (was Edit Property Pack)
COFE: fixed a validation error leading to the Solve button being disabled while the flowsheet is in a valid state
TEA (2.6.0.8): allow missing critical volume for compounds, as long as no models depend on it
COFE (2.6.0.10): fixed problems with exporting controller and flow constraint parameters from embedded flowsheets
COFE: solved problems with external parameters of embedded flowsheet unit operation being
COFE (2.6.0.11): fixed problems with prompting for saving changes, likely since 2.6.0.7
COFE (2.6.0.12): an error message is produced in case an embedded flowsheet (as unit operation) employs a flow constraint to control a feed stream
COFE: fixed exposed parameter name for flow constraint and controller parameters exported from embedded flowsheet
TEA (2.6.0.9): allow missing critical compressibility factor for compounds, as long as no models depend on it
TEA (2.6.0.10): fixed type check on import of equilibrium servers
TEA: basis error fix in external equilibrium calculator import
TEA: property resolution error fix in equilibrium calculator import
TEA: present phase fix for external equilibrium calculators
TEA: fix for single phase flashes at very low pressures
TEA: correction for solution of cubic equations of state in case of presence of a double real root
COFE (2.6.0.13): created a bit more space for editing array parameter elements
COFE: default selection is empty in edit text object dialog
COFE: fixed problem with infinite update loop of stream dialog upon failing flash when failing stream is open in multiple stream dialogs
COFE: fixed dimensions of basic properties used for plotting after loading document
COFE: corrected error with determination of property package thermo version support, leading to amongst other problems flash failures when wrapping 1.0 thermo to a 1.1 unit operation
COUSCOUS (2.6.0.12): corrected text in property tester dialog
COUSCOUS (2.6.0.13): fixed setting boolean parameters, broken since 2.6.0.6
COFE (2.6.0.14): more efficient look-ups
COFE: fix for overall MW calculations via CalcProp of overall phase when using 1.1 thermo or thermo that does not support overall MW calculations
COFE: fix for partially returned values in compound constant dialog in case all values are actually missing
COFE: warning when setting all zero compound flow rates on an MO, as this is not proper behaviour for a unit operation
TEA (2.6.0.11): more efficient look-ups
COFE (2.6.0.15): new layout stream type dialog
COFE: colour schemes, applying to streams, stream types, unit operations, label objects
COFE: material template name can no longer be empty
COFE (2.6.0.16): fixed problem with pasting unit operations, introduced in 2.6.0.15
COFE: fixed problem with pasting label objects, introduced in 2.6.0.15
COFE (2.6.0.17): fixed a problem with updating dialog after Edit from Status page of unit operation dialog
COFE (2.6.0.18): fix to initialization of some calculator variables
COFE: truncating log of messages during last run of each unit operation to prevent extremely slow unit operation dialog
COUSCOUS (2.6.0.14): various optimizations to Fixed Conversion Reactor, Gibbs Reactor, Equilibrium Reactor, CSTR
COUSCOUS: correction for enthalpy of reaction in case of multiple reactions with different phases in fixed conversion reactor
COUSCOUS: removed warnings for equilibrium reactor in case a reaction was not performed because the reaction phase is not present (still appears in log)
COUSCOUS: fixed validation errors of Gibbs reactor
COUSCOUS: Gibbs Reactor+Equilibrium Reactor+CSTR: bypass calculations in case no reactions are possible
COUSCOUS: Gibbs Reactor+Equilibrium Reactor+CSTR: elimination of reactions that may not take place
COUSCOUS: Equilibrium Reactor+CSTR: run time error in case system is over determined due to linear combinations of reactions that cannot take place
COUSCOUS: PFR, Heat Exchanger, Fixed Conversion Reactor, Gibbs Reactor, Equilibrium Reactor, CSTR: switched to MKL lapack implementation for linear solvers
COUSCOUS: Gibbs Reactor: several solver modifications
COUSCOUS (2.6.0.15): stability and performance enhancements Gibbs reactor in adiabatic mode
COUSCOUS (2.6.0.16): improved clarity of fixed conversion reactor error message for negative yields
COUSCOUS: checking for round-off error in non-negativity constraint violation of fixed conversion reactor
COUSCOUS: corrected errors in stoichiometry analysis introduced in 2.6.0.14
COUSCOUS (2.6.0.18): fixed memory leaks
COUSCOUS: fixed a CSTR crash
COUSCOUS: fixed a Gibbs Reactor crash
COUSCOUS: in simplified model (initial guess) mode, preventing zero pressure resulting from pressure drop specifications for SolidSeparator, Splitter, ComponentSplitter, CSTR, Expander, FixedConversionReactor, Flash, GibbsReactor, HeaterCooler, HeatExchanger, Mixer, Turbine, Valve
COUSCOUS: Valve, Turbine, Mixer, HeatExchanger, HeaterCooler, GibbsReactor, Flash, FixedConversionReactor, Expander, CSTR, ComponentSplitter, Splitter limit outlet pressure to 1 Pa in case of pressure drop specification that exceeds inlet pressure, and produce a warning
COUSCOUS: PFR: correction on empty item in property calculation list in case of zero pressure drop (simplified mode)
COUSCOUS: HeatExchanger: changed messages upon infeasible operation
COUSCOUS (2.6.0.19): fixed problem with CSTR, EquilibriumReactor and Gibbs Reactor
COUSCOUS (2.6.0.19): fixed problem with CSTR, EquilibriumReactor and Gibbs Reactor
COUSCOUS (2.6.0.20): allowing Gibbs reactor to converge to boundary of feasible region. A warning is issued
COUSCOUS: fixed lingering values in VARIANT in ComponentSplitter
COUSCOUS: fixed saving of reactors with multiple conversion parameters
COUSCOUS: attempt to recover from wrongly saved reactors with multiple conversion parameters
COUSCOUS: fix to constraint handling of Gibbs reactor, Equilibrium reactor and CSTR
COUSCOUS (2.6.0.21): resolved crash in Gibbs reactor
COUSCOUS (2.6.0.22): performing the phase presence check for Fixed Conversion Reactor on reactor product rather than feed (affects warnings only)
COFE (2.6.0.19): replaced linear solvers by MKL lapack
COFE: new line search for Newton solvers
COFE: modified error recovery for Newton solvers
COFE: various other updates to Newton solvers
COFE: adjusted simplified model request usage for finding initial guess
COFE: skipping mass balance checks in simplified model mode
COFE: changed flowsheet validation not to complain about material templates that are ill-configured unless they are used
COFE: warning upon skipping unit solution due to all-zero feed flows is not logged to simulation log anymore; appears only in unit operation log
COFE: corrected printing of total iteration count after convergence of recycle by Newton
COFE: allowing more iterations in the Wegstein divergence test
COFE: fixed problems with writing to log after failed unit calculations (crash)
COFE: fixed decoupling of virtual information port parameters from their matching items upon persistence
COFE: support for two phase properties in calculator using version 1.0 thermo
COFE: allow renaming of data on information stream
COFE: fixed a problem with updating of parameter collections on information streams upon disconnecting/reconnecting
COUSCOUS (2.6.0.23): removed pressure adjustment on negative pressure increase of compressor and expander
COUSCOUS: compressor/expander warn on non-vapor (rather than less than 99.5% vapor) in feed
COUSCOUS: at zero flow the compressor, expander, pump and turbine work adiabatically rather than isothermally
COUSCOUS: added compressor specification types: pressure ratio and volume ratio (a.k.a. compression ratio)
COFE (2.6.0.20): fix to unit operation colour schemes (reset upon solving)
COUSCOUS (2.6.0.24): fixed ProgID registration of compound splitter
COUSCOUS: fixed ProgID registration of thermal energy mixer
COUSCOUS: fixed problem with re-assignment split factor component name in compound splitter dialog
COFE (2.6.0.21): updating port collection after showing unit operation GUI from unit context menu
COFE (2.6.0.22): allowing file:/// prefix on ICOFEDocument::LoadFromString, indicating that a file should be used instead
COFE (2.6.0.23): using hash maps for some compound look-ups
COFE: fixed names compositions and compound flows in flowsheet report
COFE (2.6.0.24): fixed problems with popping up modal dialogs while the splash dialog is still visible
COFE: fixed line weight on solid lines in plots
COUSCOUS (2.6.0.24): changing the thermo version for a unit did not mark the unit as changed
TEA (2.6.0.12): fixed crash on reading GC files with group indices out of range
TEA: added new ChemSep IONICS family definition
TEA: disallowing compounds with non-zero charge
COFE (2.6.0.25): changed the plot pen for solid lines to a geometric pen
COFE: fixed problems with compound mapping COFE Flowsheet Unit Operation
COUSCOUS (2.6.0.26): fixed port naming of mixer, energy mixer, splitter and energy splitter after deleting port
COUSCOUS: heat duty on energy outlet port of flash was not set in case of heat duty specification
COUSCOUS: validation status was not updated for a parameter upon validate
Water (2.6.0.3): complete remake (source only): no ATL, dual MSVC/MinGW, better error checking, smart objects, exception handling, elimination of globals
COFE (2.6.0.26): post-flash check corrections
COFE (2.6.0.27): corrections in phase sorting for 1.0 external thermodynamics (COFE Flowsheet Unit Operation)
COUSCOUS (2.6.0.27): stability enhancements heat exchanger
CORN (2.6.0.5): clearer error messages in formula domain errors, divisions by zero, etc
Water (2.6.0.4): fixed PH and PS flash logic error in region 2
Water: fixed missing solutions in region 5
TEA (2.6.0.13): corrected use of acentric factor in Lee Kesler vapor pressure
TEA: corrected Misic Thodos 1 and Misic Thodos 2 routines for pure compound liquid thermal conductivity
PCD file: removed double compounds
COUSCOUS (2.6.0.28): stability enhancements heat exchanger
TEA (2.6.0.13): added equation 130: exp(A+B/T+C*ln(T)+D*T+E/T^2)
TEA: added equation 230: added equation 230: -B/T^2+C/T+D-2*E/T^3
COFE (2.6.0.28): added unit of measure mapping for W/m2 (from kg/s3)
COFE: fixed formatting problem for stream parameter watch (missing name)
COFE: resolved problem with stale property index list upon reloading a document (such as on import in external flowsheet)
PCD file: fixed correlations
COFE (2.6.0.29): fixed checking version 1.0 phase lists for two-phase identifiers: dropped assumption that two-phase identifiers appear later in the list than both the included single phase identifiers
COUSCOUS (2.6.0.28): fixed parameter modes of heat exchanger after changing specification type
COFE (2.6.0.30): fixed an x64 pointer cast error that could lead to energy and information stream reference problems and subsequent crashes
COFE (2.6.0.31): fixed problem with loading solution on energy feed streams
TEA (2.6.0.14): correction on activity model interaction parameters when energy units are selected (Wilson, NRTL, UNIQUAC)
TEA: check for consistent units of NRTL interaction parameter and NRTL interaction parameter temperature dependence, in case of any non-zero value for temperature dependence
TEA: corrected help on activity interaction parameters
TEA (2.6.0.15): improved dew and bubble point routines
TEA (2.6.0.16): repaired improper energy units correction for (Wilson, NRTL, UNIQUAC); pre-2.6.0.14 implementation was correct. Documentation adjusted properly
installer: added dryer icons
installer: remove Steamer references (leave for uninstall)
installer: add water references

Changes since version 2.05:

COFE (2.5.0.1): show unit label menu is checked or unchecked
COFE: better performance of v1.0/v1.1 name conversions of compound constants
COFE: logging error in case of failure to obtain list of PPs from TS or PPM
COFE: forcing flowsheet validation upon load (prevents messages about reference states not being calculated upon first paint where report contents gets recalculated)
TEA (2.5.0.1): fixed crash in CalcEquilibrium in case of NULL pointer in phase list
TEA: fixed invalid releasing of BSTR in v1.0 mixture thermal conductivity routine
TEA: fixed crashes on conversions of arrays of BSTR values containing NULL pointers
TEA: fixed error check for pure solid entropy calculation routine
TEA: fixed crash in NULL string in property list from external property calculator
TEA: fixed crash in NULL string in compound ID from external property calculator
TEA: fixed memory leak on failed SetProp calls
TEA: fixed crash in NULL string in equilibrium specification
TEA: fixed crash on passing NULL string as phase label to CalcSinglePhaseProp
TEA: fixed crash on passing NULL string as either of the phase labels to CalcTwoPhaseProp
TEA: correction on missing values in K value routine
TEA: correction on Gibbs free energy when entropy is taken from external V1.1 calculation routine
TEA: fixed obtaining density from external v1.1 calculation for DIPPR 9I calculation routine
TEA: fixed empty string in phase list of internal PropertyRoutine objects
TEA: corrected pure compound heat capacity derivatives from enthalpy calculations
TEA: corrected a problem with the ASOG calculation routine
TEA: fix for missing temperature derivatives of density from equation of state in presence of solid-only compounds
TEA: removed the warning for no Antoine parameters when loading a compound
OATS (2.5.0.1): fixed problem with logging Release calls (with reference count tracking enabled)
COFE (2.5.0.2): exceptions thrown while reading document views no longer prevents loading document
COFE: storing username and time during saving of document; shown in document properties
TEA (2.5.0.2): removed parsing of eantoine.lib (as these represent liquid fugacities rather than vapor pressures)
TEA (2.5.0.3): removed warning for no data for extended Antoine
TEA: corrected default vapor pressure selection method to select extended Antoine in case all other data are missing
TEA (2.5.0.4): avoid some calculations of heat capacity for compounds that are present with zero composition
COUSCOUS (2.5.0.1): conversion output parameters for individual compounds of the reactors can be configured from the added conversions property page
COUSCOUS: fixed life span of dynamic parameters of units (to avoid problems with COSE implementations that keep a lock on a parameter)
COFE (2.5.0.3): correction on persistence of parameters of embedded flowsheets
COUSCOUS (2.5.0.2): fixed loading issue introduced in 2.5.0.1
COFE (2.5.0.4): GOOOP32 is created only when needed for the first time. This prevents goop from being created during registration or when only x64 components are used.
Chemsep1.pcd: many compound revisions, in particular heats of vaporization
COUSCOUS (2.5.0.3): correction for phase order of 3-way flash
COUSCOUS (2.5.0.4): fixed problem loading documents, introduced in 2.5.0.2
COFE (2.5.0.5): correction for selection of plot series
COFE: correction for labels in axis ticks dialog
COUSCOUS (2.5.0.5): corrected unit of measure on mass enthalpy from measure unit
COUSCOUS: added entropy measurements to measure unit
COUSCOUS: fixed obtaining all mass based properties for measure unit in combination with v1.1 thermo
COFE (2.5.0.6): different colour for unit operation that is being edited
COFE: added UO name to status bar text when editing unit
COFE: added Show GUI to unit's context menu
COFE (2.5.0.7): storing position of edit unit operation dialog between usage
COFE: added show GUI button to unit operation status pane
COUSCOUS (2.5.0.6): added enthalpyF measurements to measure unit
CORN (2.5.0.1): added support for fugacity in rate and equilibrium equation expressions
TEA (2.5.0.5): added Clausius Clapeyron heat of vaporization routine (from vapor pressure)
TEA: corrections on HOC + Chemical Theory
TEA: launching PCD manager with selected PCD file (if it exists)
TEA: fixed problem with compound constant list, introduced in 2.5.0.1
TEA: fixed issues pertaining to warnings and errors for gas/liquid models for solid-only compounds
COFE (2.5.0.8): fixed exposed name of parameters of embedded flowsheet
COFE (2.5.0.9): fixed crash on units that expose no method of editing
COFE: fixed crash on passing invalid name property to MO::GetSinglePhaseProp
COFE: fixed error messages for MO::GetSinglePhaseProp
COFE: fixed crash on passing invalid name property to MO::SetSinglePhaseProp
COFE: fixed error messages for MO::SetSinglePhaseProp
COFE: support for internal energy flashes in stream dialog
COFE: support for internal energy flashes in V10 to V11 wrapping
COFE: support for overall internal energy as watch variable
COFE: support for internal energy flashes in calculator
TEA (2.5.0.6): excess enthalpy corrections for Chemical Theory
TEA: correction to temperature derivative of extended Antoine equation
TEA: correction to phase mapping in Gibbs energy calculation routine, for the entropy calculation
TEA: fixed selection of phase mix routine for overall Gibbs energy
TEA: support for internalEnergy, phase calculation routine from U = H - P*V, overall calculation by phase summation
TEA: fixed problem with uninitialized variables in case of using external version 1.1 calculation routines and internal equilibrium routine
TEA: correction to jacobian for VF-HF Newton flash
TEA: support for PU, TU and UVF flashes
TEA: fixed convergence tests for enthalpy and entropy flashes
COFE (2.5.0.10): fixed problem with temperature dependent properties from stream dialog
COFE: stream specified at vapor phase boundary was not flashed at specified vapor fraction after save/load (and solve in background check)
COFE: automatically skipping post calculation mass balance on unit operations that have no material feed or no material product streams
COUSCOUS (2.5.0.7): fixed problem with post-loading of conversion parameters (crash)
TEA (2.5.0.7): fixed crash in enthalpy flash, introduced in 2.5.0.6
COFE (2.5.0.11): changed TRUE to Yes and FALSE to No in boolean parameter value formatting
COFE: switched exponent printing to two rather than three digits by default
COFE: fixed report aligning in case of exponent and no decimal separator
COFE: fixed crash on failure to set integer parameter value
TEA (2.5.0.8): fixed complaints about missing interaction parameters at model selection if no compounds had been selected
TEA: added Prausnitz fugacity model and enthalpy model (added Prausnitz_e_Antoine.lib)
TEA: added model configuration for HOC/CT+Prausnitz+UNIQUAC-Q`'
OATS (2.5.0.2): fixed problem with CopyFromMaterial not returning the original material pointer
COUSCOUS (2.5.0.8): fixed problem with crash on singular matrix in 3rd party routine
COFE (2.5.0.12): bypassing mass balance check on unit operation solution that is bypassed because of zero flow
COFE (2.5.0.13): preferences are no longer removed upon unregistration (which happens at each update)
COFE: unit of measure default selection was not properly restored
COUSCOUS (2.5.0.9): Gibbs reactor configuration from property package was incorrect
COUSCOUS: fixed convergence of Gibbs reactor to solution that violates boundary conditions at invalid initial guess
COFE (2.5.0.14): report view (unit operation dialog) was not read-only
COUSCOUS (2.5.0.10): Gibbs reactor no longer sets minimum flow on compounds that do not take part in any reaction
COUSCOUS: Gibbs reactor's Validate checks for linearly dependent reactions (not allowed, possible in case of user specified reactions only)
COUSCOUS: Equilibrium reactor's Validate checks for linearly dependent reactions in each phase (not allowed)
COUSCOUS: CSTR reaction resolution moved from calculation to validation for better performance
COUSCOUS: CSTR's Validate checks for sets of linearly dependent reactions that include equilibrium reactions (not allowed)
COUSCOUS (2.5.0.11): Fixed conversion reactor skips phase presence check for reaction phase 'Overall'.
COUSCOUS (2.5.0.12): Fixed CSTR problem introduced in 2.5.0.10
COFE (2.5.0.15): fixed that dew and bubble point properties for stream report property selection box are hidden for actual phases and shown for the overall phase
COUSCOUS (2.5.0.13): measure unit measures entropyF
COUSCOUS: add measurement dialog for measure unit shows items in alphabetic order
COUSCOUS: fixed wrong description of the expander
COUSCOUS (2.5.0.14): prevented crash for Gibbs reactor if selected reactive compounds do not allow for any possible reaction
TEA (2.5.0.9): new hashing for property lookup tables
TEA: fixed hangup in bubble point estimations
COUSCOUS (2.5.0.15): fixed problems with energy mixer
COFE (2.5.0.16): new hashing for property lookup tables
COFE: fixed rendering for text objects: left-align, right-align, center-align now work with respect to width of text object, as does text wrapping
COFE (2.5.0.17): fixed printing for text objects
CORN (2.4.0.2): reaction package manager dialog is now sizable
CORN: reaction name is now displayed in top of reaction properties pane
COFE (2.5.0.18): calculator output was showing molar phase fractions when in mass fraction mode
COFE: fixed invalid error message on empty list of property packages from property package manager
COFE: replaced lower case "tp" flashes by upper case "TP" flashes (even though these are equivalent by specification)
COFE: fixed drawing issues in list box of properties tab of flowsheet configuration dialog
COFE: v1.1 flash specification allows empty 4th string (compound specification, if no compound specified)
TEA (2.5.0.10): entropy calculations using activity models had side effects on external material objects
COFE (2.5.0.19): fixed compound mapping during CalcAndGetLnPhi call to PP
COUSCOUS (2.5.0.16): enhancements to numeric derivative determinations in constraint optimizers near feasible region boundaries
Chemsep1.pcd: improved liquid Cps and surface tensions
COUSCOUS (2.5.0.17): stability enhancements equilibrium reactor
COFE (2.5.0.20): support for integer parameters in parametric study
COFE: check on parameter ranges before starting parametric study
CORK (2.5.0.1): fixed error handling upon removing registry entries
CORK: fixed invalid attempts to remove current user registry keys unon unregistering object
CORK/CorkHelper: helper for removing keys using admin rights (all users installation only)
Installer: removed data file eantoine.lib (as these represent liquid reference fugacities rather than vapor pressures)
Installer: added data file Prausnitz_e_Antoine.lib (liquid reference fugacities for Prausnitz model)
Installer: fixed problems with uninstallation of current user install
Installer: next installation will default to single user in case only single user version is already installed

Changes since version 2.04:

COFE (2.4.0.1): message box upon parse error in formula in stream dialog
COFE: context menus for copying warning/error messages from error pane
TEA (2.4.0.1): fix to finding PCD manager
UNIFACLL.GC: corrected name of main group 15
UNIFACLL.GC: fixed problems reading sub group resulting from above correction
COFE (2.4.0.2): fixed invalid out of connections message when attempting to connect a stream to a unit
COFE: corrected ignoring to ignoring for dimensionality changed warnings
COFE: fixed problems with dimensionality clashes of parameters with same name on different unit operations of same type
UNIFACVL.GC: corrected molecular weights of some groups
Chemsep1.pcd: correction to UNIFAC groups of several compounds
COFE (2.4.0.3): ensure not restoring the remove thread copy of the document after failed solve due to incomplete load
COFE (2.4.0.4): corrected abbreviation for pound to lb
Chemsep1.pcd: added MDEA
Synonyms.dat: added synonyms for many compounds
COFE (2.4.0.5): corrected problems with dimensionality parameter plots introduced in 2.4.0.2
COUSCOUS (2.4.0.1): corrected problem with tube heat transfer for PFR
CUP (2.4.0.1): newer zlib version
CUP (2.4.0.2): fixed access violation
COFE (2.4.0.6): corrected problems with dimensionality parametric plots
CUP (2.4.0.3): removal of cached update files that are older than 30 days
COUSCOUS (2.4.0.2): upgraded to Sundials 2.5 solvers
COUSCOUS: bug fix with respect to PFR tube heat transfer
TERNYP (2.4.0.1): upgraded to Sundials 2.5 solvers
COFE (2.4.0.7): fixed uninitialized variable in edit dialog sizing
COFE: fixed wiping backgrounds of list views
COFE: fixed bug with user specified controller scale
COUSCOUS (2.4.0.3): corrected reference count problem on MO's of products of Gibbs reactor on zero flow condition, leading to crash
COUSCOUS: setting value of heat duty parameter in case of zero flow condition
COUSCOUS (2.4.0.4): fixed problem with resetting UA value of heat exchanger in shortcut mode
COFE (2.4.0.8): default number of concurrent threads determined from environment variable NUMBER_OF_PROCESSORS
COFE: added tab for name, description and comments to unit operation dialog
COFE: fixed problem with not finding recycles in presence of controllers
COFE (2.4.0.9): fixed problems with overflow in formula parser when entering large numbers
TEA (2.4.0.2): fixed problems with overflow in formula parser when entering large numbers
CORN (2.4.0.1): fixed problems with overflow in formula parser when entering large numbers
COUSCOUS (2.4.0.5): fixed problems with overflow in formula parser when entering large numbers
CORN (2.4.0.2): reporting absolute balance errors with component balance mismatch messages
TEA (2.4.0.3): fixed problems with partial atomicities in structure formulas when converting to chemical formulas
CORN (2.4.0.3): fixed problems with partial atomicities in structure formulas when converting to chemical formulas
COUSCOUS (2.4.0.6): fixed problem with improper registration of component splitter
COFE (2.4.0.10): fix for invalid conversion of mass flow rates in material objects during removing of property packages
COFE: cancelling editing actions while saving or showing certain modal dialogs
COFE: repainting of view upon cancellation of inserting stream or unit operation
COFE (2.4.0.11): correct minor ticks to major ticks in label of axis tickmark dialog
COFE: corrected problem loading certain graphs from fsd file (resulting failure to loading the entire file)
COUSCOUS (2.4.0.7): added scroll bar to equilibrium, PFR, FCR and Gibbs reactions dialogs
CORK (2.4.0.1): showing both current user and all-users information in object view
CORK: clicking unregister will remove both current user and all-users registration keys
OATS (2.4.0.1): added support for logging reference counts after QueryInterface / AddRef / Release
CUP (2.4.0.6): fixed problem with unclosed file handle and write permission denied, introduced in 2.4.0.3
COUSCOUS (2.4.0.8): fixed display of units of measure in information calculator unit of measure dialog
COUSCOUS: fixed variable with content being passed to GetProperty by HeatExchanger
COUSCOUS: replaced several instances of the Mixture CalcType for Get/SetProp of Temperature and Pressure by NULL/UNDEFINED\
COFE (2.4.0.12): replaced several instances of the Mixture CalcType for Get/SetProp of Temperature and Pressure by NULL/UNDEFINED
COFE: fixed problems with line width in graphs
TEA (2.4.0.4): selecting model set with activity model did not select proper activity model (causing ideal activity to be used)
COFE (2.4.0.13): asking confirmation before following link in link object
COFE: fixed bounding rectangle when copying non-OLE or multiple embedded objects
COFE: fixed bounding rectangle on pasting certain objects
COFE: fixed updating selection count when (un)selecting individual objects
COFE: quicker look-ups for special properties in version 1.0 thermo and thermo from external material (embedded flowsheet)
COFE: replaced several instances of the Mixture CalcType for Get/SetProp of Temperature and Pressure by NULL/UNDEFINED
COFE: correction on dimensionality when copying parametric plot series data to clipboard
COFE: data can be imported and added as scatter series to plots
COFE (2.4.0.13): fix in background drawing Add Data and Calculator dialogs, causing large delays that appear like hangups
COUSCOUS (2.4.0.9): fixed problem with invalid cat loading and porosity
TEA (2.4.0.5): added equation 119: A/T+B+C*T+D*T^2+E*ln(T)
TEA: added equation 219: -A/T^2+C+2*D*T+E/T;
ChemSep.pcd: corrections in group contributions, 2 new compounds
COFE (2.4.0.14): fix to data in plot when editing dimensionless value (crash)
COFE: fixed crash on editing plot and clicking Remove All
COFE: updating plot after editing data series
COFE (2.4.0.15): fixed slow property look-ups in 1.1 material object
COFE: fixed slow property look-ups in version 1.0 property package wrapper routines to version 1.1
COFE: fixed slow property look-ups in wrapped external property package from material
COFE: when editing parameter values and stream values, not showing N/A for missing numbers in the edit box
COUSCOUS (2.4.0.10): preventing integration of PFR below 10 Pa pressure (when pressure drop is too high for specified inlet pressure) to prevent wrong solutions resulting from singularities (very low gas density, vert high gas velocity)
COUSCOUS: several bug fixes in Sundials/Kinsol
TERNYP (2.4.0.2): solved bug in dense solver with perturbed Jacobian
Help: corrected Winterfeld vapor liquid surface tension equation
Help: updated CAPE-OPEN specification documents

Changes since version 2.03:

COFE (2.3.0.1): changed default guess for parameters in information stream to default value, if available
COFE: full path of recent files in File menu on status bar
COFE: correction to obtaining reference states for individual compounds; compositions of non-existent compounds were not initialized (NaN)
COFE: adjusted outer spacing on graphs
COFE: adjusted restoring screen position for multiple monitor support
COFE: showing overall balances in report even if flowsheet not solved (unless feeds or products are not fully specified)
COFE: changed Exclude parameters from report into Include parameter into report for flowsheet report dialog
COFE: fixed failure to maintain maximized status of child windows at creation of new view
COFE: fixed parametric study to be allowed under non-solved conditions
COFE (2.3.0.2): fix for creation of new property packages version 1.0 (using the New button; Documents did not store properly)
OATS (2.3.0.1): fixed returning original object in ICapeUnitPort::GetConnectedObject
OATS: fixed passing original MO implementation in ICapeThermoMaterial::CopyFrom
OATS: fixed suppressing illegal characters in log for unicode strings
CORK (2.3.0.1): corrections for x64 pointer assignments
CORN (2.3.0.1): corrections for x64 pointer assignments
COUSCOUS (2.3.0.1): corrections for x64 pointer assignments
COFE (2.3.0.4): fixed loading saved plot with phase fraction, mole fraction or mass fraction
COFE: corrections for x64 pointer assignments
COFE: more efficient filling of log window
COFE (2.3.0.5): corrected error message in case of failure to set parameter value during solve
COFE: fixed a problem with setting unit parameters from parametric study
TEA (2.3.0.1): fixed failure to properly initialize external property package managers / thermo systems
COFE (2.3.0.6): added label object (simple text object that has same font as labels)
COFE: added Edit to the context menu of a single insertable object
COFE: added hyperlink object (label object with URL to external resource)
COFE (2.3.0.7): links and labels show black on printer and when copied to clipboard
COFE: added pan mode, menu and toolbar button
COFE: all insert actions cancel when initial click is outside view
COFE: when inserting pline, view does not scroll before initial point
COFE: insert stream and unit operation buttons on toolbars indicate insertion status
COFE: fixed mouse capture in various instances of cancelling an action
COFE: inserting streams shows proper line type, reflecting material, energy or information stream
COFE: feed stream properties can now also be output of parametric study
COFE: corrected dimension of mass fraction in parametric study
COFE: support for mass and molar compound flows for parametric study inputs and outputs
COFE: fixed issues with saving document's maximized state
COFE: fixed load issues introduced in COFE 2.0 (default preferences not loaded, unit set not set, simulation context not created)
COFE: fixed crash on print preview window title update
COFE: deactivating print preview for deactivating views
COFE: deactivating print previews upon save prevents crash
COFE: fixed problem with updating scroll boundaries after inserting object
COFE: new docking system of toolbars etc
COFE: fixed problem with unmodified documents being marked modified
COFE: new print preview control
COFE: corrected some aspects of the main view's dynamic context menu
COFE: save report menu in report view
COFE: contex menu in log
COFE: save log as in context menu
COFE: correction to registry cleanup
COFE: regenerating print previews upon page setup or printer setup
COFE: support for stream view printing
COFE: stream view copies EMF to clipboard (in addition to text)
COFE: support for parametric study view printing
COFE: fix to column scaling parametric study view
COFE: parametric study view copies EMF to clipboard (in addition to text)
COFE: support for report view printing
COFE: several corrections to validity check of move location selected streams and units
COFE: manually add routing points to streams
COFE: fixed updating windows and solution status after editing value in watch window
COFE: fixed the connection points for an icon-less unit operation
COFE: fixed a problem with scaling under-sized icon-less units
OATS (2.3.0.2): logging addresses of interface pointers
COFE (2.3.0.8): fixed problems with embedded unit toolbar introduced in 2.3.0.7
COFE: fixed obtaining reference state values for property package from external thermo for embedded unit operations
COFE: fixed solver crash resulting from information streams out of units that are not part of a recycle
COUSCOUS (2.3.0.2): exposing split factors of compound splitter as parameters
COUSCOUS (2.3.0.3): corrected sign of heat duty on outlet energy port pump, compressor
COFE (2.3.0.8): fixed screen update issues in unit report view
COFE: fixed attempt to set output parameters in edit dialog
TEA (2.3.0.2): fixed a problem with infinite loop on invalid PH flash solution (hangup)
TEA: several fixes on keeping track of temporary disabled pseudo properties for cubic EOS calculations during flash calculations
TEA (2.3.0.3): fixed crash in PS flash
TEA: fixed a problem with properties derived from cubic EOS for systems containing solid-only compounds
COFE (2.3.0.10): changed CapeVersion for the COFE flowsheet unit operation from 1.1 to 1.0 (refers to the Unit standard, not the Thermo standard)
OATS (2.3.0.3): changed CapeVersion for for COULIS from 1.1 to 1.0
CORN (2.3.0.2): changed CapeVersion for reaction package manager from 1.1 to 1.0 (refers to the Reactions standard, not the Thermo standard)
COUSCOUS (2.3.0.4): changed CapeVersion for for all unit operations from 1.1 to 1.0
COUSCOUS: exposing conversions for fixed conversion reactor as parameters
COFE (2.3.0.11): toggle stream labels for all selected streams from context menu
toggle unit operation labels for all selected streams from context menu
option of turning of header row(s) in unit parameter report
COFE (2.3.0.12): stream report allows for per-compound composition and compound flow
TEA (2.3.0.4): fixed solution correction in case of trivial TP flash solution resulting single liquid phase
COUSCOUS (2.3.0.5): eliminated many unicode / multibyte conversions
COUSCOUS: added thermal energy mixer
COUSCOUS: added thermal energy splitter
COUSCOUS: fixed crash on error message in information calculator
COFE (2.3.0.13): lower limit to step size in line search
COFE: preventing multiple occurrence of prompt for saving modified document at application exit
COFE (2.3.0.14): warnings can be cleared for single or all units by right clicking in error/warning pane
COFE: zoom by mouse wheel
COFE: pan by middle mouse button
COFE: pan by right mouse button if not hitting anything
COFE: forcing view redraw upon selection change due to right mouse button down
COFE (2.3.0.15): relocating active in-place OLE objects upon zoom
COFE: zoom is corrected by pan for center of view to remain in place
COFE: fixed problems with ownership of property windows
COFE: fixed crash on pure v1.0 property calculation on v1.1 PP
COFE: fixed error on v1.0 2-phase property calculation on v1.1 PP
COFE: fixed selected item counts in multiple views after deleting objects
COFE: fix for stopping editing embedded objects upon view operations
COFE: plots can be embedded in flowsheets
COFE: exiting pan mode upon right click, middle click and left double click
COFE: replace in-place activation of OLE objects by external activation (if supported by the object) while running embedded
COFE: many fixes of bugs introduced in 2.3.0.7 regarding in-place OLE activation
COFE: fixed release of menu resources
COFE: fixed problem with saving / loading property plots
COFE: follow link context menu on link object
COFE: fixed move up icon reference in context menu of objects
COFE: fixes to bugs introduced in 2.3.0.7 for editing embedded COFE objects in foreign applications
COFE: in-sheet editor for label objects
COFE: move unit operation label by mouse
COFE: click on unit label selects unit
COFE: double click unit label means rename unit
COFE: unit name can be edited inside flowsheet
COFE: move stream label along stream by mouse
COFE: stream name can be edited inside flowsheet
COFE: ensuring unique unit operation names on paste
COFE (2.3.0.16): fixed hangup in logging messages with back slashes
COFE (2.3.0.17): fixed naming error in binary plot series
COFE: fixed problem with hangup on reloading solution, introduced in version 2.3.0.15
COFE (2.3.0.18): fixed problems with embedded plots, introduced in version 2.3.0.15
COFE: fixed problems with parameter plots after solution
COFE (2.3.0.19): some adjustments for 10% zoom
COFE: fix for display of undefined value of integer parameter
COFE: fix for setting value of integer parameter to undefined
COFE: restoring status text of active document upon losing focus of menu or toolbar button
COFE: fixed load/store issues with the main toolbar upon crash or kill (incorrect state of solve/stop buttons), introduced in version 2.3.0.7
COFE: fix to aligning of drawing text in unit operation icons, introduced in version 2.3.0.15
COFE: fix to location of logarithmic axis ticks that do not start at power of 10
COFE: embedded plots scale with zoom factor
COFE: fix for stream routing drawing where no route could be found
COFE: fix for creating unique port name of new virtual information ports
COUSCOUS (2.3.0.6): fixed problem with selecting energy stream as input specification for pump
COUSCOUS: fixed a sign error in the thermal energy mixer under cooling conditions
TEA (2.3.0.5): post flash range checks for lower T and P adjusted
TEA: post flash fugacity checks moved to log domain
COUSCOUS (2.3.0.7): fix to 3-way flash middle port flash condition check
COUSCOUS: avoiding PVF product flashes for flash unit in shortcut mode
COUSCOUS: reverting to TP product flashes if PVF product flashes fail or result temperature that is more than 1 K off
TEA (2.3.0.6): fixed post-flash check problem introduced in 2.3.0.5
TEA (2.3.0.6): fixed post-flash check problem introduced in 2.3.0.5
TEA: using the default compound name is now selected by default
TEA: vapor pressure is added to a property package by default
TEA: not registering type lib
COFE (2.3.0.20): checking for a current-user CUP installation when attempting to launch CUP
COFE: fixed problem with error logging of embedded COFE unit operations during load
COFE: flowsheet views did not store show/hide stream/unit label choices
COFE: fixed line drawing errors leading to screen update failures
TEA (2.3.0.7): added equation 150: A+B*T+C*T^2+D*T^3+E/T^2
TEA: added equation 200: E*exp((A*T'+B*T'^1.5+C*T'^2.5+D*T'^5)/(1-T')) (T'=1-Tr)
TEA: added equation 201: E*(A*T'+B*T'^1.5+C*T'^2.5+D*T'^5)/(1-T') (T'=1-Tr)
TEA: added equation 220: A-B/(1+C*T'+D*T'^2+E*T'^3) (T'=Tr-1)
TEA: added equation 221: -B/T^2+C/T+D*E*T^(E-1)
TEA: stability enhancement in resolving TP flash in case of solution containing pseudo properties
TEA: added domain check in Misic and Thodos thermal conductivities
Chemsep1.pcd: many new compound definitions
COUSCOUS (2.3.0.8): not registering type lib
CORN (2.3.0.3): not registering type lib
TERNYP (2.3.0.1): fixed registration key
CUP (2.3.0.2): enhanced proxy check
CUP: check HKEY_CURRENT_USER\Software\CUP for proxy data
CUP: removed test for administration rights
CUP: running with highest available privileges rather than require admin privileges
CUP: new automatic proxy resolution mechanism
CUP: newly installed files are marked readable for all users (solving issues after updates for multi-user systems)
CUP: fixed crash on failed connection test
installer: registering COFE type library
installer: removed registration batch files
installer: installation mode for current user (does not require admin rights)
WaterEthanolExcel.fsd, WaterEthanolScilabAdiabatic.fsd, WaterEthanolScilab.fsd, WaterEthanolMatlab.fsd, FlowsheetingWithCOCOandChemSep.fsd: inserted link to descriptive document
many new example documents

Changes since version 2.02:

COFE (2.2.0.1): correction for mass compositions when opening calculator from stream
COFE: precalculating reference state values to prevent issues with invalid operations during just-in-time reference state value calculations
COFE: reference state correction calculation is part of document validation
COFE: validation explicitly executed during flowsheet solve
COFE (2.2.0.2): fixes to tool tips zoom buttons
COFE: corrected port name in remove virtual information port menu
COFE: fixed naming of indexed virtual information ports
COFE (2.2.0.3): fixes to max index of indexed port parameters
COFE (2.2.0.4): fixed issue with zero-size message box upon closing application
COFE: fixed concurrency issue caused by delayed reference state calculations
COFE (2.2.0.5): fixed problems with ICapePersistStream(Init) implementations that save a total of zero bytes
COFE: fixed problem with parametric results plot
COFE (2.2.0.6): fixed display of stream dialog, calculator and parametric study on Korean (and perhaps other) systems
OATS (2.2.0.1): fixed problem with logging argument to get_Parameters
COFE (2.2.0.7): fixed unit conversions for objects that have no dimensionality
COFE (2.2.0.8): solution status no longer gets invalidated when re-loading the document into the main thread after solving
COFE: updating title of unit operation edit dialog after changing unit name via private GUI
COFE: print range can now be selected from print options
OATS (2.2.0.2): erroneously logged put_value as get_value
TEA (2.2.0.1): calculation routine for liquid entropy from activities could not be selected and was not selected as default (changes will apply to newly created property packages, or edit property package to apply change; the fugacity based entropy was used instead as default)
TEA: new property package no longer displays Custom for model choice in simple mode
TEA (2.2.0.2): fixed composition derivatives vapor viscosity
COFE (2.2.0.9): print options bottom boundary button moved top boundary
COFE (2.2.0.10): fix to colouring of flowsheet items after solution
COFE (2.2.0.11): another fix to colouring of flowsheet items after solution
COFE: unit ID counter increased during flowsheet solutions
COFE (2.2.0.12): fix for label location for units that set their own icon in case not default size
COFE (2.2.0.13): fix: failed to read document in case a unit with icon failed to load
COFE: Added tool tip with port description to port connect selection dialog
COFE (2.2.0.14): fix: verbosity level was set to really silent after aborted solution (fix includes resetting to normal for documents saved this way
COFE: fixed crash on copy in stream dialog
COFE: no longer attempting to calculate overall property for property packages 1.0 that do not expose overall in the phase list
TERNYP (2.2.0.1): upgraded compiler
TERNYP: x64 version
TEA (2.2.0.3): upgraded compiler
TEA: _WIN32_WINNT marked as 0x0403 as per Visual Studio 2010 ATL requirement
TEA: fix on entropy derivatives when using activity models
TEA: x64 version (32-bit calculation and equilibrium routines are supported and are loaded out-of-process)
TEA: memory allocation correction in vapor thermal conductivity routines
TEA: interaction parameter dialog accepts expressions
TEA: edit compound dialog accepts expressions for real inputs
TEA: group contribution dialog accepts expressions
ConfigureTEA: upgraded compiler
Steamer (2.2.0.1): upgraded compiler; the source code is now available as Visual Studio 2010 Professional solution
Steamer: x64 version
OATS (2.2.0.3): upgraded compiler
OATS: updated about box to show full version info
OATS: x64 version (64 bits in-process object should be logged with the 64-bit version; 32-bit in-process objects with the 32-bit version)
OATS: logging whether IPersistStream or IPersistStreamInit of logged PMC is called during Save and Load
OATS: not logging unprintable characters in strings (such as form feeds in reports) to prevent log parsing problems (a warning will be logged)
OATS: when using the New Property Package functionality, the selected property package is saved in the list so that re-creation works
JUIcE (2.2.0.1): upgraded compiler
JUIcE: updated about box to show full version info
COUSCOUS (2.2.0.1): upgraded compiler
COUSCOUS: _WIN32_WINNT marked as 0x0403 as per Visual Studio 2010 ATL requirement
COUSCOUS: x64 version
COUSCOUS: expressions are accepted for real input values
ConfigureCORN: upgraded compiler
CORN (2.2.0.1): upgraded compiler
CORN: _WIN32_WINNT marked as 0x0403 as per Visual Studio 2010 ATL requirement
CORN: x64 version
CORN: fix to Rename buttons
CORN: power law wizard dialog accepts expressions for real numbers
CORN: reaction dialog accepts expresions for stoichiometry numbers
CORK (2.2.0.1): upgraded compiler
CORK: _WIN32_WINNT marked as 0x0500 as per Visual Studio 2010 AFX COMCTL requirement
CORK: x64 version (64-bit in-process objects show only in the 64-bit version; 32-bit in-process objects show only in the 32-bit version)
COFE (2.2.0.15): upgraded compiler
COFE: _WIN32_WINNT marked as 0x0500 as per Visual Studio 2010 AFX COMCTL requirement
COFE: fix on compound check in material object
COFE: upgraded zlib implementation in png import/export
COFE: updated splash and about box to show full version info
COFE: x64 version; 32-bit clients are supported and loaded out of process
COFE: fix on initialization after creation of property packages and reaction packages (using New button)
COFE: removed message at server unregistration
COFE: modified dimension menus to address problems under Wine
COFE: modified text drawing in various places to address problems under Wine
COFE: corrected invalid value in edit box in upper limits inputs parametric study (was showing lower limits)
COFE: modifications to recycle initial guess strategy (solves potential hangup with information cut-streams and speeds up iterating possible guesses significantly)
COFE: automatic reorganization of information streams upon loading caused trouble loading value of information data in some cases
COFE: fixed several issues with storing unit sets
COFE: fixed error reporting on trying to save file with same name as one that is already open
COFE: fixed memory leaks in thread communication
COFE: watch bar input now takes expressions instead of numbers
COFE: flowsheet configuration dialog accepts expressions for numeric real inputs
COFE: flash dialogs accept expressions for real inputs
COFE: calculator accepts expressions for real inputs
COFE: line type with dialog accepts expression
COFE: line end with dialog accepts expression
COFE: parametric study dialog accepts expressions for real inputs
COFE: plot settings dialogs accept expresions for real inputs
COFE: stream dialog accepts expressions for real inputs
COFE: controller input dialog accepts expressions
COFE: flow constraint input dialog accepts expressions
COFE: real parameter input dialogs accept expressions
COFE: plot axis dialog accepts expressions for limits and ticks
COFE: plot range dialogs accept expressions for ranges
COFE: report dialog accepts expression for zero fraction
COFE: text dialog accepts expression for text size
COFE: plot dialogs accept formula for pressure and temperature offsets/values
COFE: selection of mole or mass basis per stream report
COFE: fixed crash upon click in explorer bar when no documents are open
COFE: replaced DDE mechanism for shell open by custom mechanism to avoid Win7 x64 problems
COFE: added find unit operation and find stream menus (center in view and flash)
COFE: fixed flowsheet report for units with solve warnings
COFE: various graphing fixes
COFE: fixed problems with solving flowsheets that are embedded (e.g. in Excel)
GOOOP32 (1.0.0.1): the glue for loading 32-bit in-process objects into 64-bit applications
CUP (2.2.0.1): upgraded compiler
CUP: added version number to window title
CUP: checking that OS version is at least 0x0500 (win2K), or exiting. Older platforms no longer supported
CUP: added 64-bit DLL registration tools
COFE.xlt: issue recalc all after loading document
COFE.xlt: fixed aspect ratio issues in Excel 2010
COFE.xlt: fixed scrollbars on calculation sheets
COFE.xlt: fixed headings on property calculation example sheet
modelClasses.dat: updated for 3rd party unit operations
installer: complete revamp (NSIS based)
installer: CO-LaN type libs no longer optional; registered for both x86 and x64 on x64 systems
CScasebook_MA.fsd, Flash-CosmoThermLite.fsd, FlowsheetingWithCOCOandChemSep.fsd, WaterEthanolExcel.fsd, WaterEthanolScilab.fsd, WaterEthanolMatlab.fsd, WaterEthanolScilabAdiabatic.fsd: updated entropy model
CUP (2.3.0.1): fixed issues with version number formatting

Changes since version 2.01:

COFE (2.1.0.1): Fixed index out of range in paste in stream dialog
COFE: fixed component name mapping error in T and P plots
COFE: fixed problem with entering flash data in calculator
OATS (2.1.0.1): COULIS no longer depends on proper implementation of GetSizeMax for persistence
OATS (2.1.0.2): attempt to log name of object in case of interface argument, as exposed by ICapeIdentification
OATS: correction to IStream::Seek
COFE (2.1.0.2): better error handling in case of problem saving due to inability to locate ports connected to streams
COFE: fixed storage implementation for crash at passing NULL pointer to IStream::Seek
OATS (2.1.0.3): COULIS' get_ConnectedObject now returns the original object, not the logged object. In case the PME makes calls on the returned object, these are no longer logged
COFE (2.1.0.3): solved problem with solution returned at first function evaluation in case of pure compound cut stream at boiling point with wrong phase fractions
COUSCOUS (2.1.0.1): Flash unit no longer performs TP flashes on all outlets if any of the streams has zero flow rate
COFE (2.1.0.4): added electric horse power to power units of measure
COFE (2.1.0.5): modification to life time of sub-menus to prevent problems under WINE
COFE: correction to initial status parametric study event queue causing invalid 'parametric study aborting' message
COFE: simplified problem equations in case of flow controlled feed
TEA (2.1.0.1): corrected RCP correlation into RPP correlation in ideal gas heat capacity selection list
COUSCOUS (2.1.0.2): increased max iterations on internal heat balance of Gibbs reactor
COUSCOUS: gibbs reactor: fixed constraints after failed line search
COFE (2.1.0.6): corrections to embedded flowsheet's product port results handling in case of enthalpy specification
COFE: removed info messages regarding saving and loading of embedded flowsheets
COFE: changed message "At least one compound needs to be present..." from normal level to verbose level
COFE (2.1.0.7): fixed simulated overall calculation of Gibbs free energy
COFE: corrected message "cannot start material at given position" for proper stream type
COFE: corrected a unit-of-measure updating issue that caused an infinite loop in the stream dialog with inclusion of information streams
COFE: fixed problem with stream view showing outdated properties after run
COUSCOUS (2.1.0.3): corrections to constrained projection functions, applies to Gibbs, CSTR and Equilibrium reactors
COUSCOUS: flash unit performs TP outlet flashes for single phase solutions (unless at VF specification)
COUSCOUS: added normal volume to measure unit
TEA (2.1.0.2): fixed column scaling in property calculation routine dialog
TEA: selection dialog allows for selection by double-click
COFE (2.1.0.8): fixed problem with list not being updated after Reset in Parametric study dialog
COFE: fixed issues with moving output items up and down in parametric study dialog
COUSCOUS (2.1.0.4): stability enhancement Gibbs reactor
COUSCOUS: fix in measure unit with multiple compound dependent measured variables
COFE (2.1.0.9): Fixed sizing and labels unit operation parameter report dialog
COFE: memory release error at model class selection fixed
COUSCOUS (2.1.0.5): added HeatOfCombustionUnit, which predicts LHV and HHV of a mixture at 298.15 K and 1 atm
CORN (2.1.0.1): fixed crash on read error PCD file
TEA (2.1.0.3): fixed crash on read error PCD file
COUSCOUS (2.1.0.6): adjusted heat of vaporization value for water used by HeatOfCombustionUnit
COUSCOUS: corrections to HeatOfCombustionUnit
OATS (2.1.0.4): checking validity of BSTR values
COFE (2.1.0.10): added force unit pound-force
COFE: unit conversion objects now recognize dimensional equivalents; alternatives can be selected for derived quantities (e.g. force per area instead of pressure)
COFE: type of an existing stream can be changed from stream's context menu
COFE (2.1.0.11): fixed flow constraint
COFE (2.1.0.12): modifications to the Newton line search termination criteria
COFE: controller has additional input regarding magnitude of measured variable
COFE: modifications to the controller equation residual calculation
COFE: added mole vs mass fractions to context menu of stream view
COFE: added number of significant digits to Stream menu of stream view
COFE: added messages about non-normalized feed streams to document validation
COFE (2.1.0.13): correction to new controller scale variable
COFE (2.1.0.14): fix on crash on closing documents with controllers
COFE (2.1.0.15): stability enhancements on closing document
COFE: fixed problem with renamed compounds in thermo 1.1 based reference state correction
COFE: fixed problem with function call recursion in thermo 1.1 based reference state correction
TEA (2.1.0.4): fixed editing A in correlation A
COFE (2.1.0.15): added 48x48 pixel main icon
COFE: CAPE-OPEN extension library for new property packages is now included in COFE's type lib (for proper marshalling of out-of-process PMCs, pending inclusion in the CAPE-OPEN distribution)
COFE: CAPE-OPEN extension library for flowsheet monitoring objects is now included in COFE's type lib (for proper marshalling of out-of-process PMCs, pending inclusion in the CAPE-OPEN distribution)
COFE: support for creation of new reaction packages instead of selecting from list of existing (only for reaction package managers that implement it, e.g. CORN)
COFE: zoom in/out toolbar buttons
COFE: zoom all function
COFE: icons attached to flowsheet units can be exported to uic file
COFE: allow editing icons attached to flowsheet units using JUIcE
TEA (2.1.0.5): Initialize returns error if property package was not resolved and was not loaded.
CORN (2.1.0.2): Initialize returns error if reaction package was not resolved and was not loaded.
CORN: support for direction creation of new reaction packages (only for applications that support it, e.g. COFE)
OATS (2.1.0.5): allow creation of packages from scratch in supporting applications (e.g. COFE)
OATS: add package dialog now contains check box for logging (default: yes)
OATS: corrected error messages on creation of property packages
OATS: correction to exposed names of imported packages
OATS: overriding name on imported packages at creation
JUIcE (2.1.0.1): fixed problem with window size on large font systems or small displays
JUIcE: corrected overlap error checks
JUIcE: functionality for moving objects by a single grid
JUIcE: modifications to allow calling from within COFE
Installer: fix to default installation location
Installer: fix to registration of *.uic files
Installer: fix to registration of *.fsd files

Changes since version 2.00:

COFE (2.0.0.1): correction to composition override in temperature and pressure plots
COFE: adding default charset flag to screen font creation
COFE: corrected array parameter plot unit operation selection
COFE (2.0.0.2): correction to stream sorting problem causing crash
TEA (2.0.0.1): correction to fugacities for all virial EOS models
Help: several corrections to property formulas
COFE (2.0.0.3): fixed crash upon renaming energy or information stream from stream dialog
COFE (2.0.0.4): validation now fails in case of a material template that does not have a PP selected
COFE: correction in failed to terminate message
COFE: logging of source of highest residual per iteration in debug logging mode
TEA (2.0.0.2): adapted to new PCD format: relative static permittivity instead of heat of formation correlation, charge included,
TEA: new backup PH flash algorithm invoked in case of failing PH flashes
TEA: correction to Winterfeld surface tension routine in absence of one or more compounds
TEA: added equation 123: A+B/T+C*T+D*T^2+E*T^3
TEA: fixed crash in surface tension calculation routine
CORN (2.0.0.1): adapted to new PCD format: charge included
TEA (2.0.0.3): filtering out infeasible solutions (Z<B) for backup analytic cubic EOS solutions
TEA: corrected high pressure correction to vapor viscosity mixture models
TEA: corrected proper selection of compound to be deleted in simple dialog
TEA (2.0.0.4): corrections to liquid thermal conductivity at high pressure
TEA: corrections to vapor thermal conductivity at high pressure
TEA: equation 105 returns 0 for T >= C
TEA: correction for lnPhi and all derived properties for cubic EOS for compounds with zero composition
OATS (2.0.0.1): corrections to IStream::Read function
COFE (2.0.0.5): changes to when unit operation name is obtained, to avoid multi-threading issues
COFE: correction to obtaining reference state values in presence of multiple property packages with various sets of compounds
TEA (2.0.0.5): correction for dlnPhi/dT and all derived properties for cubic EOS for compounds with zero composition
TEA: correction to Hayden-O'Connel estimation for second virial coefficient
TEA: correction to lnPhi, d lnPhi / dT and all derived properties for virial equations of state for compounds with zero composition
TEA: removed composition perturbation of enthalpy
TEA: composition derivatives of entropy no longer by perturbation
COFE (2.0.0.6): prevent crash in document explorer on plot view that closes upon loading document
COFE: fixing IStream::Read and IStream::Write for NULL pointer of amount of bytes transferred
TEA (2.0.0.6): correction to line search in Boston and Britt flash
COUSCOUS(2.0.0.1): correction to line search in Newton solver
COFE (2.0.0.7): modified automation ICofeDocument interfaces to accept BYREF arguments for collection arguments
COUSCOUS(2.0.0.2): fixed uninitialized variable in flash unit
COFE (2.0.0.8): fixed Ctrl+C on view to route to Edit->Copy
TEA (2.0.0.7): use of external equilibrium calculator is disallow in presence of solid-only compounds
TEA: a default Vapor and Liquid phase are presumed for an external equilibrium calculator that does not implement ICapeThermoPhases
TEA (2.0.0.8): correction in v1.1 SetProp on internal material object
COFE (2.0.0.9): fixed error message on invalid property CalcProp to version 1.1 wrapper
COFE.xlt: corrected GetStreamPressure function

Changes since version 1.16:

OATS (1.16.0.1): fix on persistence of out-of-process logged unit operations
OATS: not forwarding requests for IMarshal, IStdMarshal, ICallFactory to facilitate out-of-process PMCs
COFE (1.16.0.1): corrected control focus for tab page windows
COFE: correction on dimensionality of array parameters
COFE: solution of flowsheet will by default be done in background thread
COFE: added parametric study feature
COFE: different icon on plot views
COFE: re-arranged plot menus
COFE: error status return correction for copying text to Windows clipboard
COFE: hiding resolution controls for unit parameter plot as they do not apply
COFE: working with preference for maximized views
COFE: fixed material stream selection in calculator
COFE: sorting of streams in Calculator dialogs, Plot Property Selection dialogs, Stream Report selection, Flowsheet report
COFE: sorting unit operations in Plot Property Selection dialogs, Flowsheet Report, Unit Report Selection dialogs, Flowsheet Unit Operation Parameter list
COFE: fixed tab order in various dialogs
COFE: added sort order and method of streams and units to flowsheet configuration
COFE: closing plot views on deleting last series
COFE: corrected unit conversion for milimole (conversion was equivalent to kmol)
COFE: decimal digits for formatting numbers now accessible from flowsheet options dialog
COFE: fixed calculator for overall property calculations
COFE: Document explorer tree
COFE: working by default with maximized child windows
COFE: correction to cancelling add stream dialog
COFE: streams are now by default in view instead of modal dialog
COFE: whether calculator uses mole fractions depends on document default. Document default is set according to last choice of stream view
COFE: calculator is now a non-modal view
COFE: reformatting of numeric values in calculator, according to documents number of specified decimal values
COFE: correction on saving reports in Cr/Lf conversion
COFE: reports are now a non-modal views
COFE: correction on property lookup tables during re-loading of embedded unit operation
COFE: correction to COFE Flowsheet Unit Operation validation
COFE: safety margin GetSizeMax COFE Flowsheet Unit Operation persistence
COFE: COFE Flowsheet Unit Operation's parameter collection exposes a name via ICapeIdentification
COFE: preferences allow for showing unit's private GUI when double clicking unit
COFE: added watch bar
COFE: modifications to method for setting stream composition: values are clamped to [0,1] range, binary compositions are automatically adjusted (streams with n-2 compositions set to zero are considered binary)
COFE: unit operation parameters can be added to the unit operation's tool tip
COFE: marking the document to be saved after starting solution
COFE: preventing the system from going into sleep mode while flowsheets are solving
COFE: fix for property selection in add series for temparure / pressure plot when switching to / from pure
COFE: fixed drawing error with plots for extremely large values
COFE: fixed memory deallocation problem in exception handlers
COFE: flowsheet unit operation fixed hangup on Edit inside other flowsheeters
COFE: correction on loading embedded flowsheets saved with previous versions
COFE: fixed apparent dead lock on showing child windows of windows that do not yet exist, e.g. on exception handling during windows loading
COFE: replaced temp-file based IStream implementation by memory based implementation
COFE: corrected IStream::Seek implementation
COFE: corrections to version 1.0 to version 1.1 thermo wrapper for external thermo of embedded flowsheet unit: phase list was not obtained properly
COFE: showing full document path in File Properties dialog
COFE: select between CAPE-OPEN version 1.0 and 1.1 implementations when inserting Property Package (defaults to version 1.1)
COFE: added shortcut to creation of new property packages (only available if a custom interface ICapeThermoNewPropertyPackage is implemented by Thermo System or Property Package Manager, contact AmsterCHEM for more information)
COFE: remember last selected PPM for next PPM insertion
COFE: suppressing logging of messages during recycle perturbations (except when in DEBUG log level)
COFE: modification to Wegstein solution method for recycles
COUSCOUS (1.16.0.1): saving report content between sessions
COUSCOUS: fixed warnings about unknown enthalpyNF and entropyNF in property tester
COUSCOUS: fixed malformatted lines at failed composition perturbation in property tester
TEA (1.16.0.1): post-checking vapor fraction flashes for solution that does not involve use of pseudo properties to exclude false super critical solutions
TEA: corrected Hills formula (elements after C and H were in reversed alphabetic order)
TEA: pre-configured model sets can be selected
TEA: renamed "Hankinson and Thompson" to "COSTALD / Hankinson and Thompson"
TEA: replaced temp-file based IStream implementation by memory based implementation
TEA: corrected IStream::Seek implementation
TEA: revision of property package editing dialog; a simple editing mode has been added
TEA: added ICapeThermoNewPropertyPackage for easier creation of new property packages
TEA: corrected composition derivatives for thermal conductivity
CORN (1.16.0.1): corrected Hills formula (elements after C and H were in reversed alphabetic order)

Changes since version 1.15:

Solids.pcd: fixed trailing empty component definition
COFE (1.15.0.1): added horizontal scroll bar to log view
COFE (1.15.0.2): checking for error return on InitNew calls when initializing new external objects
TEA (1.15.0.1): using value of critical pressure instead of saturated pressure for Poynting factor of super critical compounds, with warning
TEA: correction error returns ideal gas entropy routine
TEA: fixed memory leak on error condition in corresponding states calculation routine
TEA: fixed crash on error condition in liquid viscosity calculation routines
TEA: corrected error handling at thermal conductivity mixture calculation routine
TEA: corrected error handling at calc equilibrium balance error on internal MO
TEA: solved memory leak at external v1.1 equilibrium server
TEA: error correction on invalid phase list in CheckTwoPhasePropSpec
TEA: corrected error with composition derivative of entropy from activity and fugacity models
TEA: corrected temperature derivatives for NRTL activity model with temperature dependent interactions
OATS/COULIS (1.15.0.1): fixed invalid log after internal call to InitNew
OATS/COULIS (1.15.0.2): logging class ID of unit operation before creation
TEA (1.15.0.2): corrected error message on fail of SetSinglePhaseProp during CalcSinglePhaseProp
TEA: corrections to calculations of mole number derivative for two-phase properties
TEA: corrected error message on fail of SetTwoPhaseProp during CalcTwoPhaseProp
TEA: corrected failure of logFugacityCoefficient.Dmoles calculations, including CalcAndGetLnPhi
OATS/COULIS (1.15.0.3): corrected error message on type check of long array contained in Variant
Water (1.15.0.1): corrected error message on type check of long array contained in Variant
TERNYP (1.15.0.1): corrected error message on type check of long array contained in Variant
TEA (1.15.0.3): added family for pseudo compounds
TEA: showing <N/A> rather than empty string in Add Compound dialog in case of no formula for compound
TEA: correction for derivative of eq 106 with Tr > 1: returning zero
TEA: added eq 160: exp( (1/Tr)*(A(1-Tr)+B(1-Tr)^1.5+C(1-Tr)^3+D(1-Tr)^6))
TEA: correction to add compounds dialog: default name was not selected in case of filter match
COFE (1.15.0.3): corrections to automation functions: GetPropertyDimensionality, GetCompoundConstantDimensionality
TEA (1.15.0.4): changed new eq from 160 to 212
TEA (1.15.0.5): improvement to numerical differences of S and H from EOS
TEA: a very large negative number (-1e200) rather than -inf is returned for d S / d X at X -> 0
TEA: correction for perturbed DS / DX: -R X ln(X) term is done analytically is perturbation is very inaccurate near X = 0
TEA: property resolution optimized in internal MO's Get/SetSinglePhaseProp
COUSCOUS (1.15.0.1): stability enhancements EquilibriumReactor (new solution algorithm)
COUSCOUS: removed redundant reaction phase control from equilibrium reactor configuration window
COUSCOUS: stability enhancements CSTR (new solution algorithm)
Help: updates on equilibrium reaction basis and tips on reactor types for equilibrium reactors
COUSCOUS (1.15.0.2): modifications to constraint projection algorithms used in CSTR and Equilibrium Reactor
TEA (1.15.0.6): changed new eq 212 to exp( (E/T)*(A(1-T/E)+B(1-T/E)^1.5+C(1-T/E)^3+D(1-T/E)^6)
TEA: added equation 213: (E/T)*(A(1-T/E)+B(1-T/E)^1.5+C(1-T/E)^3+D(1-T/E)^6
IPD files and Antoine.lib: many corrections
TEA (1.15.0.7): for new compounds, selecting the CP IG method with bigger temperature range (if both are available)
TEA: correction in default IPD tables: UNIQUAC model only takes defaults values from UNIQUAC.IPD and UNIQUAC-Q' only takes defaults from UNIQUACP.IPD
COFE (1.15.0.4): several corrections to obtaining errors for version 1.1 reference state correction
COFE: corrected version 1.1 wrapping GetTDependentProperty / GetPDependentProperty wrapping for multiple properties per call for version 1.0 property package
COFE: correction to phase mapping when wrapping 1.1 CalcTwoPhaseProperty call to version 1.0 property package
COFE: replaced empty allocated BSTR by NULL in VARIANT array allocation functions
COFE: correction to version 1.1 CalcEquilibrium wrapper to version 1.0 property package when properties-to-be-calculated list is not empty
COFE: message to log window if stream fails to connect due to lack of connection points at the icon.
COFE: added log messages at deleting stream (for verbose logging level)
COFE: updated consistency between flowsheet validation and enabled state of solve button
COFE: fixed unit and stream tool tips for trailing \r\n
COFE: fixed solve abort message when solving from automation interface
COFE: corrections to put_Mode of parameters that are part of an information or energy stream
COFE: fixed validation status of unit operations after pasting
COFE: added unit operation based on COFE flowsheet
TEA (1.15.0.8): fix when running TEA as external equilibrium server to calcType in SetProp.
TEA: user must confirm replacing user copy of TEAConfig.dat by newer system copy
CORN (1.15.0.1): user must confirm replacing user copy of CORNConfig.dat by newer system copy
COUSCOUS (1.15.0.4): single-phase Gibbs-minimization equilibrium reactor

Changes since version 1.14:

Water (1.14.0.1): adapted PH flash for slight inconsistencies of inverse functions around the saturation line
COFE (1.14.0.1): no longer wiping unit operation's outlet info streams at start of solve, this interferes with proper information streams and data forwarding
COUSCOUS (1.14.0.1): solved bug in Sundials/Kinsol dense solver with perturbed Jacobian
TERNYP (1.14.0.1): solved bug in Sundials/Kinsol dense solver with perturbed Jacobian
TEA (1.14.0.1): correction to Yen & Woods calculation routine (introduced in 1.14); no answers due to critical property check
COFE (1.14.0.2): fixed printing of text objects
COFE: fixed report table size calculations when printing
COFE (1.14.0.3): Fixed hot key for Solve this unit operation menu
TEA (1.14.0.2): Fixed default focus of Add Compound dialog
TEA: Fixed on temperature range check liquid density correlation
TEA: added Amagat routine for solid mixture density / volume
TEA: added T-correlation for pure solid density
TEA: no longer setting phase fraction of non-existing phases for version 1.0 flash after equilibrium calculation
TEA: corrected T-correlation liquid thermal conductivity unit conversion error
TEA: corrected T-correlation vapor thermal conductivity unit conversion error
TEA: corrected temperature out of range check for T-correlation calculation routines for vapor thermal conductivity, liquid thermal conductivity, vapor viscosity, liquid viscosity, Reid et al vapor pressure, liquid heat capacity, vapor pressure
CORN (1.14.0.1): adjusted element balance checking by assuming chemical formula can have fractional element counts (with period as decimal separator)
OATS/COULIS (1.14.0.1): logging error for empty phase label in MO GetProp/SetProp/GetSinglePhaseProp/SetSinglePhaseProp/GetTPFraction
PROPS.INI: modified default property display for solid phases
COFE (1.14.0.4): fix for material object, allows for setting/getting missing values (CapeDoubleMissing)
COFE: more efficient material Set/GetProp implementation
COFE: partial missing values can now be obtained via GetProp
COFE: removed warnings on passing undefined values via material object
CUP (1.14.0.1): relaunching CUP to check for further updates after ChemSep installer exits
COFE (1.14.0.5): fixed memory leak at copy material object
COFE: flow constraint unit for closed recycles
COFE (1.14.0.6): flow constraint unit can be used as first unit in feed stream (to control feed flow)
COFE: flow constraint unit marked as non-reactor; automatically set no-bypass-at-zero-flow flag
COFE: fixed crash on destroying plot window with axis dimensions
COFE: flowsheet reports take into account possibility of feed and product unit operations in balances (unit and flowsheet balances). Unit operations with only a product are considered a feed unit; unit operations with only a feed are considered a product unit. Stream from a feed unit is considered a feed stream. Stream to a product unit is considered a product stream. COCO does not come with feed and product units, but there may be such third-party units.
COFE: unit operation post-calculation mass balance check is now optional per unit operation
COFE: removed warning for underdetermined variable if variable is controlled variable of controller
COFE: fixed check on flow constraint taking part in a recycle
COFE: fix on missing matrix values, bug introduced in 1.14.0.4
TEA (1.14.0.3): added solid heat capacity selection per compound
TEA: fixed ideal gas enthalpy routine for enthalpyNF
TEA: fixed ideal gas enthalpy routine for multiple properties in single call
TEA: fixes for HVF, HFVF, SVF, SFVF flashes
TEA: modified Amagat routine not to calculate pure densities of compounds for which this is not required (zero composition)
TEA: fixed unit conversion error for Cp routines in case of multiple properties in single call
TEA: added solid heat capacity calculation routine (ideal mixing)
TEA: fix for material object, allows for setting/getting missing values (CapeDoubleMissing)
TEA: various optimizations for From Activity calculation routine
TEA: eliminated number of SetProp calls on internal materials (for performance)
TEA: correction to viscosity calculation in DIP9B1, DIP9B2, DIP9B3 thermal conductivity calculations (was performed at wrong pressure)
TEA: more efficient internal material Set/GetProp implementation
TEA: removed support for properties flow and totalFlow of internal material object
TEA: partial missing values can now be obtained via GetProp
TEA: removed warnings on passing undefined values via material object
TEA: fixed interface leak in vapor viscosity mixing calculation routine at failed pure viscosity calculation
TEA: added standardEntropyGas, standardEntropySolid, standardFormationEnthalpySolid
TEA: rewrote a number of T-correlations to give explicit integrals rather than using 10-point Legendre
TEA: rewrote T-correlations to give explicit derivatives rather than using perturbation
TEA: corrected documented form of equation 120 in TEA edit component dialog
TEA: fixed error for equation 207
TEA: fixed BSTR leak in entropy routine
TEA: many strings pre-allocated
TEA: pseudo property calculations for cubic EOS now only applied for external equilibrium calculations and internal multi-compound equilibrium calculations (all other calculations: pseudo property calculations no longer used); this fixes wrong answers for super-critical single compounds flashes
TEA: added solid enthalpy routine for solid-only compounds
TEA: added solid entropy routines (with and without mixing terms) for solid-only compounds
TEA: fixed removing compound data values when editing compound inside property package (or template) configuration
OATS/COULIS (1.14.0.2): accepting NULL pointers for pcbWritten in IStream::Write and pcbRead in IStream::Read
OATS/COULIS: fix to IStream::Seek
CUP (1.14.0.2): fix for MSI installers
CUP (1.14.0.3): fix for MSI installers
COUSCOUS (1.14.0.2): corrected typo description heat exchanger
COUSCOUS: modifications for counter-current UA htx for convergence at very high UA
COUSCOUS: modifications for counter-current UA htx to prevent invalid convergence to maximum heat transfer solution
COUSCOUS: htx correction for calculation of LMTD in case of equal temperature differences
CORN (1.14.0.2): fixed formula parse error introduced in 1.14.0.1
COFE (1.14.0.7): added unit of measure for Gregorian year (a = 365.2425 days)
COFE: more careful temperature step in solving recycles
COFE: corrected typos on menu tooltip descriptors
COFE: fixed a problem with selection of embedded combo boxes that 'drop-down' in upward direction
TEA (1.14.0.4): stability enhancements for pseudo properties
TEA: more elaborate error messages for invalid EOS return values
TEA: more intermediate sanity checks (finite values, etc) in equilibrium calculations to prevent wasted cycles
TEA: underflow check on power of iteration variables in equilibrium calculations
TEA: suppressing warning log from failed inside-out PH if another attempt will follow
TEA: revised flash trivial solution checks: not symmetric EOS fugacity = azeotrope, different Z = azeotrope, same Z and super critical = single phase, same Z and not super critical = discarded
TEA: added post-flash fugacity check
TEA: fixed T and P at solid-only flash
TEA: added synonyms for compounds that can be used during compound selection
TEA: fixed a problem with selection of embedded combo boxes that 'drop-down' in upward direction
TEA: adapted edit compound dialog for solid-only family
TEA: added solids.pcd; small library of solid-only compounds
PR.IPD: correction water/ammonia IPD CAS numbers
COFE (1.14.0.8): fix for serialization with automation
TEA (1.14.0.5): fix for post-flash triviality checks for single compound flash
TEA (1.14.0.6): added T-correlation A+B*T+C*T^2+D*T^3+E/T^2
TEA (1.15.0.0): minor optimizations in cubic EOS initialization
TEA: combined S, H and lnPhi property calls in PH, PS, TH and TS flash to save some EOS evaluations
TEA: reduced work in formatting temperature out of range messages
COFE (1.15.0.0): quicker screen update during flowsheet solution
CUP (1.15.0.0): problem obtaining new COCO installer fixed
Installer: skipping installation of Excel Unit Operation if same version already installed.
Installer: skipping installation of EPA WAR + class libraries if same version already installed.
Installer: no longer failing if HKEY_CLASSES_ROOT\AppID or HKEY_CLASSES_ROOT\CLSID or HKEY_LOCAL_MACHINE\Software do not exist (fix for installation issues at Wine)

Changes since version 1.13:

OATS (1.13.0.6): fixed creation of thermo version 1.0 property packages
OATS (1.13.0.7): fixed buffer overflow when logging long strings
Water (1.13.0.6): fixed units of measure for viscosity
COFE (1.13.0.6): fixed switching tab pages when automatically adding material template at adding multiple property packages
COFE: fixed crash when opening compound flows in stream dialog if no compounds are present
COFE (1.13.0.7): fix for embedded objects containing inserted text
COFE (1.13.0.8): fix on internal reference state active unit
COFE: fix on package defined phase name when obtaining reference state
COFE (1.13.0.9): fix for icon size when changing unit operation icon on non-default sized unit
OATS: (1.13.0.8): option for automatic log location, no user prompt
OATS: option for turning of prompt for automatically opening log when object terminates
COULIS: (1.13.0.8): possibility to configure for a specific unit operation (without asking user) via OATS main window
OATS: fixed indentation in log files for /argval tags
COUSCOUS (1.13.0.6): get_RestrictedToList for parameter did not return VARIANT_TRUE but returned TRUE
COUSCOUS: parameter collection had an empty name
COUSCOUS: failed to release material object after failing to get compound constant
COUSCOUS: PFR dialog did not always re-interpret phase selection
COUSCOUS: added dew- and bubble-point pressures and temperatures to available variables in MeasureUnit
COFE (1.13.0.10): fix to validate (error when property package does not contain compounds)
COFE: error/warning view with clickable errors and warnings
CUP (1.13.0.4): reporting version for newly installed modules
CUP: additional code for registration of Excel Add-ins
COFE (1.13.0.11): objects that were not (properly) Save()d were not initialized using InitNew() when reloading the document
COFE: hitting ESCAPE during mouse actions cancels the action (e.g. cancel insert stream by hitting escape)
COFE: suppressing version 1.0 to version 1.1 CalcEquilibrium wrap on error on internal CalcEquilibrium calls
Water (1.13.0.7): Correction to error message from HRESULT routine
Water: correction to evaluation of multiple T-dependent properties in a single call
Water (1.13.0.8): correction to evaluation of multiple compound constants in a single call
COFE (1.13.0.12): circumvent double attempt at loading document via DDE after double click on fsd file
COFE: correction to mouse/keyboard behaviour after hitting ESC on insert action
COFE: automatic detection of fraction dimension for unit operation parameters (zero dimensionality, but with min and max between 0 and 1 will be fraction, can be formatted as percent etc)
COFE: added unit of measure ppm for fraction
COFE: fixed obtaining parameter specs from array parameters
COFE: file format upgraded
COFE: a composition threshold can be specified for stream reports and the flowsheet report. Compounds are reported as absent (zero composition, zero component flow) when the composition is below the specified value.
COFE: the material object now accepts SetProp, SetSingleProp for phaseFraction in mass basis
COFE: when using v1.1 thermo, stream dialog will allow for mass based vapor fraction flash
TEA (1.13.0.6): liquid entropy calculations are no longer separated from enthalpy calculations (more efficient when obtained in one call)
TEA: adjusted convergence tolerance for cubic EOS (more accurate)
TEA: material object now supports phase fractions in mass basis
TEA: support for mass basis vapor fraction flashes when using thermo v1.1 (not possible in thermo v1.0)
COFE (1.13.0.13): corrections to GetPhaseList of MO when called by PP
COFE: correction to wrapping version 1.1 CalcEquilibrium call to version 1.0 PP: error when firs specification was phaseFraction
COFE: setting phase fraction to 0 caused phases to be marked as not present. Corrected to present. This caused sequences like SetPresentPhases, SetSinglePhaseProp (vapor fraction = 0), CalcEquilibrium to fail
COFE: OLE message pending delay has (Server is Busy dialog time out) has been set from 5 to 60 seconds
COUSCOUS (1.13.0.7): fixed memory leak on obtaining array parameter specs
COUSCOUS: fixed bounds on real array parameter element specs
COUSCOUS: stability enhancement adiabatic CSTR: better problem scaling
COUSCOUS (1.13.0.8): fixed convergence criteria co-current heat transfer after very high UA
COUSCOUS (1.13.0.9): additional stability fixes heat exchangers with high UA
CUP (1.13.0.5): ignoring invalid HTTP 1.0 response line
CUP: proxy authentication, using Basic and Digest schemes. Proxy override required
CUP: proxy override via HKEY_LOCAL_MACHINE\Software\CUP, value "ProxyServer", format: hostname:port
CUP: terminating data connection after expected number of bytes have been received without waiting for socket close event
CUP: when checking for CUP update, ignoring version number in CUP.dat and comparing to CUP internal version instead
CUP (1.13.0.6): correction to base64 routines for authentication
CUP: NTLM Authentication (if user/pass not specified, window logon will be used); proxy override required
CUP: any passwords stored in registry since 1.13.0.5 will be encoded after running CUP
CUP: automatically asking for proxy details in case of connection failure
COFE (1.13.0.14): application preferences dialog (F2)
COFE: new files can be instantiated from template file
COFE: out-of-proc OLE time out can be configured
COFE: messages that have been turned off can be reset
COFE: OLE time out set to large value (1 hour) while invoking ICapeUtilities->Edit
COFE: default plot colors and resolution can be configured
COFE: unitializing unknown phase types to liquid (with warning) in v1.1 property package
COFE: correction to showing key compounds in phase dialog (flowsheet settings)
COFE: corrected Automation function "SaveToString"
COFE (1.13.0.15): correction to loading unit sets (introduced in 1.13.0.14): if you run into problems loading a newly saved document, re-load the default unit set into your document after resetting the application preferences to factory settings; apply the default unit set to the document
TEA (1.13.0.7): fixed crash on invalid derivative specifier for version 1.1 calculation routines
TEA: VF equilibrium calculation did not return an error when failing to obtain VF
TEA: correction to T derivative of surface tension for super critical compounds
TEA: fixed PH flash initial guess
TEA: tea correlation vapor pressure was always using the same - hardcoded - equation. Now uses the actually defined equation
TEA: vapor pressure equation can now be selected per compound
TEA: ideal gas heat capacity equation can now be selected per compound
TEA: new ideal gas heat capacity equation: 3.5 * R (in case no other data is available)
TEA: heat of vaporization equation can now be selected per compound
TEA: vapor-liquid surface tension equation can now be selected per compound
TEA: pure liquid density equation can now be selected per compound
TEA: pure vapor thermal conductivity equation can now be selected per compound
TEA: pure liquid thermal conductivity equation can now be selected per compound
TEA: pure vapor viscosity equation can now be selected per compound
TEA: pure liquid viscosity equation can now be selected per compound
TEA: better check on missing values of sub calculations
TEA: showing family by name when editing compounds
TEA: fixed edit text for compound parameters to show current value as default
TEA: fixes to class assignment in DIPPR 9E thermal conductivity routine
PCD: correction to family numbers (getting family ID for compounds correct in existing documents may require reloading compounds from PCD)
OATS/COULIS (1.13.0.9):
CUP (1.13.0.7): corrected remaining downloading time display (last minute was not showing correctly)
COFE (1.13.0.16): fixed list of supported compound constants in case of partial missing values from version 1.0 PP
COFE: adjusted monitoring interface according to updated interface proposal
COFE: restoring spec list scroll position after update in calculator window
CORK (1.13.0.6): warning for admin rights
TERNYP (1.13.0.6): adjusted monitoring interface according to updated interface proposal

Changes since version 1.12:

CORN: correction on using edit dialog for equilibrium constant; resulting equation appeared in wrong text field
ALL: changed version numbering scheme (1.1.2.0 for version 1.12, but 1.13.0.0 for version 1.13)
Installer: correction on checking loaded modules
COFE: after removing compounds from a PP, stream state was possibly incorrectly set as incomplete
TEA: corrected error detection on failure to save configuration (e.g. when no write access to TEAConfig.dat)
COFE: added message box in case of failure to load property package while loading fsd document
COUSCOUS: fixed problem resulting from renaming output port of info calculator (did not get updated)
COUSCOUS: fixed problem resulting from changing input ports of info calculator
COFE: unit operation port administration was mangled with multiple ports having the same name. This is now checked for and disallowed.
COUSCOUS: information calculator: no longer allowed to have two variables with the same name
TEA: corrected failed presence test of derivative properties from external calculation routines
TEA/CORN: when saving state, replaced rename() by MoveFile() and corrected error description in case of failure
TEA: correction to storing and loading external calculation and equilibrium routines (problem introduced in version 1.12)
COFE: open flowsheet configuration dialog at last used page
COFE: importing dimensionality can take arrays as small as 0 numbers, order if units is m, kg, S, A, K, mole, cd, rad + abs/rel flag
COFE: exporting dimensionality now gives m, kg, S, A, K, mole, cd, rad + abs/rel flag (added abs/rel flag)
OATS: logging dimensionality will show error in case data type is not CapeDoubleArray
COFE: correction on dimensionality check information and energy stream parameters
COUSCOUS: all exported dimensionalities are now 9 elements long: m, kg, S, A, K, mole, cd, rad + abs/rel flag
COUSCOUS: all pressure drops are marked as relative measures
COUSCOUS: information unit variables can now be configured as relative measures
COUSCOUS: improved stability of equilibrium reactor and CSTR reactor (if equilibrium reactors are used)
CUP: added CUP - COCO UPdate
TERNYP: back button added
TERNYP: storing of state between sessions (persistence)
TEA: fixed incorrect liquid density correlation temperature out of range warning
COFE: added barg and psig conversions
OATS (1.13.0.1): function to remove all QueryInterface info nodes from log viewer
OATS: fixed menu accelerators in log viewer (did not work)
OATS: logging of ICapeKineticReactionContext and ICapeElectrolyteReactionContext on unit operations + logging of reaction objects
OATS (1.13.0.2): logging error when attempting to write to output parameter
OATS: logging error when unit operation tries to modify object connected to inlet port
OATS: logging of reaction packages (stand-alone or created via reaction package manager)
OATS: fix on reference count logged material template
OATS: check interface pointers non-NULL before creating logged versions
CORN: releasing reference to reaction properties object and simulation context at Terminate()
COFE: fixed redundant flickering of stream type selector
CORK: no longer complain if HKEY_CURRENT_USER\Software\CLSID does not exist
COFE: wrapping version 1.0 to 1.1 thermo; adding idealGasStateReferencePressure to list of universal constants
TEA: added idealGasStateReferencePressure to available universal constants
COFE: warning on failure to create flowsheet monitoring objects during document loading was not logged
COFE: adapted to newer value of missing double precision numbers (IEEE NaN) while keeping in mind that PMCs may use old value (CapeDoubleEmpty = -DBL_MAX)
CORN/COUSCOUS/TEA/TERNYP: adapted to newer value of missing double precision numbers (IEEE NaN) while keeping in mind that PMEs may use old value (CapeDoubleEmpty = -DBL_MAX)
OATS: checking for both NaN and old value of CapeDoubleEmpty, warning produced for CapeDoubleEmpty usage
TEA: there is now a user copy of TEAConfig.dat in [Application Data]\COCO\data; editing TEA has the effect of modifying the user copy, not the system copy; the user copy will be updated by the system copy if the system copy is newer (e.g. after replaced by a software update)
CORN: there is now a user copy of CORNConfig.dat in [Application Data]\COCO\data; editing CORN has the effect of modifying the user copy, not the system copy; the user copy will be updated by the system copy if the system copy is newer (e.g. after replaced by a software update)
COFE: modelclasses.dat is now saved for the current user in [Application Data]\COCO\data; system and user entries are merged. User entries take precedence.
COFE: defaulticons.dat is now saved for the current user in [Application Data]\COCO\UnitIcons; system and user entries are merged. User entries take precedence.
COFE: unit operation icons from system UnitIcons folders are merged with user UnitIcons folders. User unit icons take precedence over system unit icons with the same name.
COFE: correction on vapor phase existence after dew or bubble point calculation when wrapping version 1.1 equilibrium calculation to version 1.0 property package
TERNYP: added residue curves and residue curve maps
TERNYP: better behaviour during calculation + close window means abort calculation
OATS: substituted E_UNEXPECTED for 0x8000FFFF in log file
OATS: logging error on passing NULL pointer to version 1.1 thermo SetMaterial() (one should use UnsetMaterial instead)
OATS: SEH and C++ exception handling around each external call
TEA: checking for non-NULL material object pointer at SetMaterial
OATS: logging warning in case any object does not expose name; error in case of failure to obtain name
COFE: if monitor is edited, document is marked as not saved if monitor's IsDirty returns S_OK.
TEA: added button to launch ChemSep's PCD manager to Add Compound dialog (if installed at system)
COFE: fix on non-CAPE-OPEN error formatting, introduced in version 1.12
TEA/CORN: DefaultComponentLib.pcd is renamed Chemsep1.pcd
COFE: Reaction Object did not implement ICapeIdentification
COFE: removed support for compound constant 'diffusionCoefficient'
Installer: modified installer not to fail under WINE
COFE: fix to Automation/Excel access to property and compound constant dimensionality strings (introduced in version 1.12)
TEA: IPD files updated; can now read CAS numbers as compound IDs
TEA: Eantoine.lib file updated; can now read CAS numbers as compound ID
COFE: correction on error reporting when failing to set or get parameters
COFE: more information (type, limits, ...) on tooltip for parameter
COFE: fixed stream tool tip text for flow in case of use of mass fractions
TEA: corrected initial T guess for BB PH flash; added backup method for failing PH flashes
TEA: Ideal gas heat capacity correlations are used if available but out of range (warning will be logged)
OATS: calling InitNew for logged unit operation in case the simulation environment fails to do so (and logged as error)
COUSCOUS: fix on loading very old document formats
OATS: fix for get_componentName and get_componentDesc being called before Initialize (plus error being logged)
COFE: material objects now check that information asked directly from the property package is not asked by the property package ("not supported" is returned if it is the property package asking)
CORN: changed title of reaction package dialog
COFE: fixed column with in reaction package page of flowsheet configuration dialog
COUSCOUS: vapor fraction setting did not get filled in in flash dialog
COFE: more elaborate error message for unit operation when virtual information port inlets cannot be obtained
COFE: unit operation with disconnect virtual information inlet port no longer fails (uses current parameter setting)
COFE: fixed memory leak at deleting virtual information port
COFE: zero flow calculation bypass message is now a warning (previously info)
COFE: added additional log messages for ill-specified variables of recycles
COFE: restoring stream after failed solution may caused a solution flow to remain if flow before solution was N/A
COFE: support for enthalpyNF and entropyNF (enthalpy without heat of formation and entropy without entropy of formation)
COFE: added reference state correction for enthalpyNF and entropyNF
COFE: fix on error handling CalcSinglePhaseProp version 1.1 property package
COFE: added (internal) energy to mimicked overall property calculations
COFE: for single-compound material streams, automatically setting composition to unity when opening stream dialog
COFE: for single-compound materials, automatically setting composition to unity in calculator
COFE: correction for calculator: invalid basis for temperature range calculations introduced in v1.12
COFE: binary, T, and P property plots: fixed mixup arising from difference in version 1.0 and version 1.1 property names
COFE: fix to mass based component flows in flowsheet report and stream report
COFE: wiping all outlet streams of a unit operation before Calculate to prevent old values from lingering
COFE: when adding a property package and the default material type already has a property package assigned, prompt for new material type
TEA: correction on FromGammaCalculationRoutine for calculation of entropyF
TEA: corrections on EnthalpyF and EntropyF flashes for wrapping of external calculation routine
TEA: correction on overall entropyF calculation
TEA: support for enthalpyNF and EntropyF (no additional flash types)
TEA: performance improvements
COFE: added more configurable reference state correction for enthalpy and entropy calculations
COFE: no longer making new axis for adding property to plot if dimensions are equivalent (previously: if same dimension object was used)
COUSCOUS: mixer will no longer ask for enthalpy of streams with zero flow
COFE: modifications to insertable unit parameter report in case of single unit operation in report
TEA: fix on composition derivatives of density / volume when using EOS
COFE: support for component flows in stream dialog
Water: IAPWS-97 based steam and water property package
TEA: better interface for loading multiple binary interaction data values at the same time
COUSCOUS: fixed storage size for CSTR, EquilibriumReactor, FixedConversionReactor (all returned too small storage size)
TEA: when editing component temperature correlations, corrected formulas 114 and 116 (Tr rather than T is used)
TEA: correction to temperature correlation calculation routines for vapor viscosity, liquid viscosity, liquid density, liquid thermal conductivity, vapor thermal conductivity, liquid heat capacity in case of equations 114, 116
TERNYP: added units of measure of P and T to dialog labels
EPA/.NET/WAR: added EPA's WAR algorithm + .NET class libraries to installer

Changes since version 1.11:

CORK: progID did not show if VersionIndependentProgID key was not present
TEA/COUSCOUS/CORN: corrected COM error message on unknown HRESULT value
COFE: more error information on fail to save to IStream
COFE: fixed restoring stream reports from file (mixture properties disappeared)
COFE: update compound and phase lists after editing PP
COUSCOUS: a number of unit operation was passing empty phase string for setting overall pressure/temperature on duplicate material object
COFE/TEA: conversion error for "totalFlow" and "flow" for a real phase (mass flows were wrong; correct for overall phase)
COFE: fixed issue with reference state correction
COFE/TEA: fixed issue with inverted phases on two-phase property
COFE: correction to mass phase fractions in stream report and flowsheet report
COFE: flowsheet validation caused solution status flag on unit operations to be set to false
CORK: added CATID for proposed flowsheet monitoring interface
COFE: added Add-in menu with support for flowsheet monitoring objects
COFE: name and description were set on unit operations when loading a document before calling Initalize()
COFE: non-COM or non-CAPE-OPEN units (e.g. controller) are now properly exposed via automation interface
COFE: insert controller menu was not visible for embedded flowsheet documents
COFE: prototype implementation of flowsheet monitoring interface, exposed via Add-in menu
COUSCOUS: fixed description of FCR
COFE: fixed report line drawing for tables with one data row after last header row
COFE: all properties are now wiped after equilibrium calculations. This prevents properties that are not in equilibrium from lingering (previously all properties for all non-overall phases that are not part of the equilibrium specification were wiped before equilibrium calculations)
COUSCOUS: fixed version 1.1 support for enthalpyF flashes
ALL: replaced CLSCTX_INPROC_SERVER by CLSCTX_ALL for all CoCreateInstance calls, allowing for out-of-proc servers
COFE: at document load time, initialize the property lists before loading the unit operations
COFE: fixed missing menu prompts
COFE: on failing to load unit, and user chooses to re-insert unit, InitNew was not called for units with IPersistStreamInit
COFE: correction to IStream::Seek implementation (caused possible invalid STG_E_INVALIDPOINTER return: "Invalid pointer error" when loading objects, specifically called by VB6)
CORN: fix on parse error messages for formulas
COUSCOUS: correction on loading measure unit
COUSCOUS: correction on mole component flow measurement unit-of-measure for measure unit
COUSCOUS: added unit Information Calculator: calculate information output from information inputs
COUSCOUS: fixed heat balance of CSTR
TEA/COFE: corrected data type for GetUniversalConstant (CapeArrayVariant rather than CapeArrayString)
COFE: compressing bitmap objects for document storage, making for smaller document files
COFE: fix to line wrapping for reports: missing last character on wrapped lines
COFE: removed redundant QueryInterface calls for IPersistStreamInit
COUSCOUS: better goal function for CSTR
COUSCOUS: different Newton implementation for CSTR, EquilibriumReactor, HeatExchanger
TEA: fix for buffer overflow at formatting temperature out of range messages for extremely high or low temperatures
COUSCOUS: fixed help on expander
TEA/COFE: performance enhancements have been made
COFE: fixed tick mark at feed and product indicator menu
COFE: exported ICapeIdentification from simulation context
CORN: corrected heat exchanger (UA and co-current max heat transfer modes) for pure compound flows
OATS: added OATS - utility for thermo logging and importing thermo into 64-bit applications
COULIS: added COULIS - utility for unit operation logging
COUSCOUS: fixed heat exchangers for pure component flows (did not solve in the two-phase regions)
COFE: minor adjustments to Newton for solving recycles
COFE: added new recycle solver: lazy Newton (Newton that tries not to update the Jacobian)
COFE: fixed issue where information stream drawn from controller to unit operation fails to connect at controller side
TERNYP: added ternary plugin (TERNYP) for making ternary property and phase diagrams
CORN: parse error in floating point numbers of type ##e+0### or ##E+0### or ##e0### or ##E0###; power had wrong sign in case of presence of leading zero in exponent
COFE: fixed copy/paste for controller unit operation, virtual information ports and report properties
COFE: copy/paste between different versions of COFE no longer works
COFE: added copy / paste to right mouse menus in flowsheet view
COUSCOUS: correction in property tested: missing error message for unexpected number of values in array
CORN: added kinetics to HDA sample template
CORN: correction when restoring reaction package from template
CORN: more elaborate formula parsing error messages
CORN: formula editor dialog
CORN: correction to selection of equilibrium basis; selection of Activity was not detected or applied
COFE.xlt: correction, specification of Overall phase for getting T and P from a stream
COFE: correction to GetLastError reporting
COFE: correction to copying meta file data to clipboard (applications may have responded to paste with 'invalid handle')
COFE: solved crash on message boxes when active window of parent window could not be found
COUSCOUS/CORN/TEA: dropping reference to Simulation Context at Terminate()
COUSCOUS: get_ValStatus for parameters was returning an uninitialized value
TEA: temperature out of range message fixed for T-correlation heat of vaporization
COFE: copying meta file data did not take into account current selection
COFE: modification to recycle initial guess strategy
COFE: correction on not releasing ICapeParameter spec obtained from ICapeArrayParameterSpec::get_ItemsSpecifications
Uninstaller: correction to folder for removing unit operation icons

Changes since version 1.10:

COFE: UnsetMaterial was called for PP version 1.1 after Terminate()
CORN: fixed crash on reaction packages with sub set of total amount of compounds
COFE: fixed crash on GetCompoundConstant when component is not present in PP
COFE: fixed automatic column scaling in stream dialog
COFE: stream dialog now accepts value of zero for flow
COFE: added unit mPa (miliPascal)
COFE: mPa s will format as cP
COFE: added volumetric units liter, mililiter, oil barrel, gallon, cubic centimeter
COFE: J/s will be replaced by Watt (e.g. in thermal conductivity); only for new documents
TEA: asking for confirmation on bail out editing changed property package
TEA: initial focus of add compound dialog to filter control
TEA: when adding compound, unique filter match is automatically selected
COFE: added unit of measure translation for J/mol/K and J/kg/K
COFE: revision of port tab layout
COFE: virtual information ports: information ports that are associated with a parameter value
COFE: double click property package or reaction package invokes Edit
COFE: various actions possible when a unit operation fails to Load
COFE: screen elements are updated if compound is renamed
COFE: screen elements are updated if phase is renamed
COFE: added icons for measuring devices
COUSCOUS: added MeasureUnit to expose material stream value as information stream
COFE: additional checks on ability of setting zero flow bypass solution of energy streams + fix no limit check
COFE: bugfix, hangup when recycle sections contains multiple energy stream recycles
COFE: prevent crash on edit window for unit operations that cannot edit
COFE: hide balance tab on edit window for units with only information ports
COFE: fixed infinite residual with recycle that contains single variable (division by n rather than n-1)
COFE: fixed issue with connection order during loading documents on energy and information streams
COFE: removed balance from flowsheet report for unit operations that only have information ports
COFE: added controller unit operation (not a CAPE-OPEN unit operation, but COFE internal unit operation)
COFE: compound data for boil temp and formula is now stored. GetCompoundList is no longer called on the PP when GetCompoundList is called on MO
COUSCOUS: resolved crash when more compounds in reaction package than in material object at Validate
COFE: normalization of residuals inside Newton
COFE: fixed storing initial guess on information stream (for Reset after saving/loading)
COFE: added type descriptor to CAPE-OPEN insert dialog for each object
COFE: objects that appear with more than one of the target types (e.g. thermo system and property package manager) will appear multiple times in add dialog with proper type descriptor
COFE: black vs dark gray values in stream dialog for values that can or cannot be edited
COFE: change flow by setting overall volume flow in stream dialog
installer: new layout, select all options before starting installation
installer: default install option for ChemSep LITE will be false if full ChemSep is found
CORN: corrected molaliry by molarity in reaction interfaces
TEA: fixed uninitalized liquid fraction for dew- or bubble point calculation using backup method
COFE: stream report was showing mole fractions rather than mass fractions
COFE: flowsheet report was showing mole fractions rather than mass fractions
TEA: added compound constant "charge" (value of 0 for all current TEA compounds)
COUSCOUS: equilibrium reactor crashed if reaction phase was not present at reactor conditions
help: many pages were not found in online (web) version of help

Changes since version 1.09:

COUSCOUS: fix for round-off errors in flash causing negative concentrations in bottom flow
COUSCOUS: fix for crash after deleting a port that is not at the end of a port collection (when removing 3 phase flash option from flash unit operation)
COUSCOUS: unit invalidation is prevented on setting output parameters during calculation time
COUSCOUS: added make-up mixer
COUSCOUS: corrected "S" to "s" and "mole" to "mol" in unit descriptions of reports; removed spaces from unit descriptor
COFE: forcing screen update after editing streams
COFE/TEA/COUSCOUS: preventing ampersand in strings to be drawn as shortcut key underscore (specifically in stream & unit labels)
COFE: fixed crash on reading document that has a unit operation that cannot be created (for example because it is not installed on the system)
COUSCOUS: bug fix for vapor fraction flash specification of flash unit operation introduced in 1.09
COFE: hiding splash screen when running embedded or opening a document from the shell
COFE: maximum length of tool tip when hovering mouse of warnings icon of unit operation (with additional message to check out the solve log for more info)
COFE: enabled DDE shell open
COFE: fixed issue with "File not found" when launching fsd document from shell
COFE: correction on solid fill for unit icon closed poly lines
COFE: new background fill flag for unit icon objects BODY and closed PLINE
COFE: new unit icons: makeup_mixer, pipe1, air_cooler, stirred_vessel, stirred_open, plate_exchanger, shell_tube_exchanger, spiral_exchanger, membrane
COFE: changed icon text element alignment to vertical center
COFE: label element in unit icon files supports rotation flags + correction on reading label
help: added help on unit operation icons and labels
COFE: many (small) corrections to icon files
JUIcE: added JUIcE (Just a Unit ICon Editor)
TEA: resolved uninitialized variable in bubble and dew point pressure calculations (causing convergence to extremely high T after just opening a document)
TEA: resolved issue with uninitalized guess variable in PH inside out flash
COFE: added Configure item to Flowsheet menu when running in embedded environment
CORK: correction on error reporting in case of registry access errors
TEA: trivial solution detection in inside-out flashes
TEA: optional trivial solution check bypass
COFE.xlt: avoid warnings about deleting example sheets, fixed issue with grid lines disappearing in example sheet
COFE: minor modifications to Newton approach for recycles
COFE: changed termination strategy for Wegstein iterations
COFE: decreased default max. successive Newton iteration count to 5
COFE: added option Broyden method instead of full Newton to solve recycles
TEA: correction to compound mapping in GetPDependentProperty
TEA: correction in key compound ID testing for external equilibrium servers
TEA: resolved memory leak
COFE: added title and creation date to document properties
COFE: embedded stream report / unit parameter report / unit report / author report
COFE: textual flowsheet reports
COFE: resolved possible deadlock in updater/listener framework
COFE: correction to display of absent values in stream dialog in case of not all compounds being present in the material
COFE: hiding rows for compounds that do not appear in selected streams in stream dialog
COFE: display of graph coordinates under mouse cursor in status bar
COFE: optional feed and product indicator arrows
CORN: formula parser accepts quoted strings. Compound names that contain non-alpha-numeric characters need to be quoted. Reaction rate wizard adjusted for quoted compound names.
CORN: when editing packages within simulation environment, compounds can be chosen from existing material templates
CORN: allowing empty / missing expressions for rates and equilibrium constants
COFE: changed the labels on the buttons for editing reaction package managers and property package manangers into "Packages"
TEA: GetCompoundList was returning structure formulas rather than chemical formulas
TEA: renamed CorE(quation) into Temperature Correlation
CORN/COFE: assumed are now units of reaction rates that are in mol/s rather than kmol/h. This is foreseeing documentation changes (the reaction package specification is not in SI units)
COFE: corrected plotting error for automatic axes ranges with zero span (min equals max)
CORN: added "Molality", "Concentration", "MoleFraction", "MassFraction", "Fugacity", "Activity" as options for equilibrium constant basis
CORN: mole is no longer accepted as basis for EquilibriumConstant; NULL should be passed
COUSCOUS: equilibrium reactor now interprets concentration bases "Molality", "Concentration", "MoleFraction", "MassFraction", "Fugacity" and "Activity"
COUSCOUS: various fixes to equilibrium reactor
TEA: corrected error on reading compound names with spaces from eantoine.lib, causing erroneous warnings about non-matching names
COUSCOUS: added unit CSTR for single phase kinetic & equilibrium reactions
COUSCOUS: added unit PFR for single phase kinetic reaction
COFE: resolved error in adding property to document twice as a result of difference in name for thermo versions 1.0 and 1.1
CORN: fixed memory exception on evaluating expressions
COUSCOUS: additional remark in COSE log about test results
CORN: correction in power law wizard: forward and backward compounds switched
COFE: automatic assignment of reaction package to newly inserted reactors (if one or more reaction packages are present in the document)
COUSCOUS: fixed crash on assigning reaction package to reactor if no ports connected
COFE: fixed invisible (zero sized) paste rectangle
TEA: resolved issue with BSTR freed too many times in GetComponentConstant
COFE: resolved compound mapping issue in GetComponentConstant
TEA: correction in backup routine of entropy flash solvers
TEA: correction in backup routine for HVF and SVF flash solvers
COFE: added entropy balance to unit operation balance dialog; balances for which the property is does not exist in the document can no longer be selected
TEA: fixed invalid smiles export for compounds for which it is absent (air)
installer: fixed behaviour after problem with administrator test
installer: more explicit messages about failure to pass admin test
COFE/TEA/CORK: adjusted for proper use of LOCAL_MACHINE vs CURRENT_USER registry keys when scanning for CO objects
COFE: fix on axis dimensions for unit parameter plot and reaction data plot
TEA: fixed return value for CheckEquilibriumSpec when a solution type is specified; it returned ok for flashes that are not supported
TEA: fix in pure surface tension calculation routine (complained about missing pure values)
CORN: changed terminology for concentration to molality
TEA: added property enthalpyF, which contains the enthalpy of formation
TEA: absolute entropy is removed from property entropy (affects property gibbsFreeEnergy)
TEA: absolute entropy is removed from property idealGasEntropy
TEA: added property entropyF, which contains absolute entropy term
TEA: added v1.0 flash types "PHF", "THF", "HFVF", "PSF", "SFVF", "TSF" and their equivalents "HFP", "HFT", "VFHF", "SFP", "VFSF", "SFT" (using entropyF and enthalpyF rather than entropy and enthalpy)
TEA: allowing for flash specifications of EnthalpyF and EntropyF for v1.1
COFE: support for enthalpyF and entropyF in all flash operations (using v1.0 notation "HF" and "SF")
COFE: automatic overall calculation for properties enthalpyF and entropyF
COFE: added entropyF and enthalpyF balances to unit operation dialog
COUSCOUS: reactor unit operations can now base their energy balance on either enthalpy (with or without inclusion of heat of reaction) or enthalpyF
COUSCOUS: checking for required properties at Validate: Compressor & Expander (entropy), Fixed conversion reactor & equilibrium reactor (enthalpy or enthalpyF), Flash & Heater/Cooler, HeatExchanger, Mixer, StreamConverter, Valve (enthalpy)
TEA: warning rather than error when temperature is out of range of pure compound surface tension correlation of temperature correlation routine
TEA: warning rather than error when boiling temperature is out of range of pure compound surface tension correlation of Lielmez calculation routine
TEA: added temperate and range to all temperature out of range warning messages
HDA example: added properties to PP that are required for ChemSep update (post calculations for reporting); added stream table; reactor now uses enthalpyF to predict reactor temperature
TEA: after v1.1 flash calculation, overall T and P were not set (should be set if not part of the flash specification)
COFE: unit operation solution warnings can now be accepted
COUSCOUS: corrected GetSizeMax for FixedConversionReactor, EquilibriumReactor, HeatExchanger
COFE: various corrections of persistence on dimensions of plot axes for reaction- and parameter-plots
TEA: fixed bug that caused load of invalid Cp correlation temperature range messages
COFE: bug fix on mapping of pure property calculations from thermo v10 to thermo v11
COFE: correction to symbol hit check when mouse over plot
TEA: fix to initialization of VF flashes: non-finite initial guess replaced by initial guess of FV = 0.5
TEA: alternate temperature guess for PH and PS flash, in case simple guess fails
TEA: fixed error return on missing string values for GetComponentConstant / GetCompoundConstant
COFE: fixed mimicking GetComponentConstantList for version 1.0 property packages for partially missing values
CORN: check for heat of reaction property dependence
COFE: unit operation identification numbers no longer increase by storing / loading the document
COUSCOUS: added maximum possible heat transfer option to HTX (both co- and counter-current)
COFE: streams were invalidly marked as equilibrium at user abort of solve
TEA: revision of van Laar IPD data
COFE: fixed crash on creation of PP that does not have essential interfaces
COFE/TEA/CORN/COUSCOUS: fixed issue with BSTR comparison between "" and NULL
CORN: fixed issue when using thermo v1.1 and sub set of compounds
COFE: when using version 1.1 thermo: more efficient dealing with SetMaterial

Changes since version 1.08:

COFE: fix to GetCompoundConstants for multiple values if any values are missing
TEA: correction to GetCompoundList of TEA MO when passed to external calculation routines. Caused GetCompoundConstant to return improper values when compound list was specified.
COFE: version 1.0 overall calculation request for enthalpy, entropy and volume are automatically mimicked when using v1.1 thermo; this prevent errors as v1.1 thermo does not support overall calculations
COFE: corrected unit operation display color after "Calculate this unit"
TEA: fixed liquid ideal enthalpy calculation routine for v1.0 thermo
TEA: showing thermo v1.1 rather than v1.0 property names in calculation routine selection dialog
COFE: keyboard handling for stream dialog, property dialog, calculator
COFE: column-wise paste for multiple data in stream dialog and calculator
COFE: stream dialog: preventing display for properties for non-existent phases (prevents a lot of errors in the log)
TEA: Property Pack Manager now exports a component name and description through ICapeIdentification
COFE: fix to "Calculator for this stream": no longer pops up repeatedly
COFE: errors caused by calculator are now suppressed from document log
COFE: support for paste in Calculator inputs
COFE: fix in unit operation and stream comments in tooltip
COFE: comment and warning indicators for streams an unit operations with tool tip
COFE: taking into account call to SetPresentPhases before v1.1 CalcEquilibrium (previously all phases were assumed present)
COUSCOUS: calling SetPresentPhases on v1.1 MO before calling v1.1 CalcEquilibrium
TEA: post-checking result for PH, TH, HVF flash by calculating enthalpy at solution and comparing to enthalpy spec. Use backup-flash if inside out flash fails
TEA: post-checking result for PS, TS, SVF flash by calculating entropy at solution and comparing to entropy spec. Use backup-flash if inside out flash fails
TEA: corrected a numeric issue that sometimes caused PH, PS, TH and TS flashes to invalidly converge to the phase boundary
COFE: correction on scanning registry for CAPE-OPEN objects; removed redundant scanning
COFE: added Rankine temperature scale
COFE: releasing all references to parameters before calling Terminate() on ICapeUtilities
COFE: fixed error in reverse phase mapping when using v1.1 thermo
COFE: fix in v1.1 CalcEquilibrium phase & compound name mapping
COUSCOUS: fixed lack of interpretation of new values at closing of flash edit dialog
COUSCOUS: exposing property tester parameters through dialog
installer: showing installation log before rather than after launching COFE
COFE: disallowing setting values or calculating equilibria on inlet streams during Calculate of unit operations; calculating properties on inlet streams will cause a warning
COUSCOUS: property tester v1.1 thermo: adjusted tests for CalcAndGetLnPhi to deal with partial implementation
TEA: corrections to assumptions about present phases for external calculation routines that call CalcEquilibrium v1.1 on material object
TEA: correction to phase and compound mapping for external calculation routines that call CalcEquilibrium v1.1 on material object
TEA: correction to compound mapping for CalcEquilibrium when using external equilibrium calculator
TEA: stability enhancement in EOS pseudo properties calculations
Installer: checking for modules to be installed whether they are loaded in memory before proceeding
COFE: more efficient property lookup
COUSCOUS: added unit operation SolidSeparator
COFE: added icons for filters and cyclones
COFE: bugfix reading old files (no views appeared)
COFE: bugfix: failed to restore plots containing dew- and bubble-point data
TEA: correction on phase mapping for imported v1.0 calculation routine
COFE: solved a crash on closing document while showing debug messages in case of objects that are not released
COFE: modified flash icons to have more connections (existing documents that require extra connection need to reload the flash icon)
COUSCOUS: corrections on error handling of flash unit operation
COUSCOUS: added a three-phase option to the flash unit operation (vapor, lightest liquid, remainder)
COUSCOUS: error produced on many calls instead of crash if Initialize was not called for unit operation
COFE: name was obtained from unit operation in the process of formulating Calculate error. Order of operations is switched so that error is obtained before name.
TEA: correction on T-limits for Argon heat capacity
COFE: added support properties "enthalpyF" and "entropyF" (added to props.ini)
COFE: corrected an issue that caused the solve button to be disabled after loading a file while all validations succeed

Changes since version 1.07:

COFE: correction to ability to select compounds for property selection when creating a plot
COFE: pasting only worked if at least one stream was selected
COFE: adjusted Newton routine to be more efficient for purpose of recycle iterations
COUSCOUS: corrected issue with read/write status for fixed conversion reactor parameters
COUSCOUS: correct text on About page of fixed conversion reactor
COUSCOUS: corrected various error messages
TEA: corrected Brock and Bird surface tension
TEA: corrected .Dmoles for version 1.1 Kvalues
COFE: fixed log lines from repeating in inconvenient places (for example at the start of catching unit operation dependent log)
COUSCOUS: not duplicating the material for enthalpy calculations on outlet (so enthalpy is set on outlet stream) for HeaterCooler, HeatExchanger, StreamConverter, which is a little bit faster
COFE: fixed hangup when adding reaction package
COFE: corrected reference count reporting at end-of-document material loss notification (by -1)
COUSCOUS: added EquilibriumReactor
CORN: corrected appearance of Arrhenius reference temperature in rate wizard
COUSCOUS/COFE/TEA: solved crash at infinite numbers in Jacobian for problems solved by Newton
CORN: solved crash when unsettting context material more than once
COUSCOUS: HeatExchanger: added tolerance and max. iteration parameters, corrected error handling, storing of initial guess from last successful run, default tolerance lower by 2 orders of magnitude
COUSCOUS: prevented crash at empty error message
CORN/TEA/COUSCOUS: better error checks when loading/saving from persistence interfaces
COUSCOUS: additional check on temperature limits for HeaterCooler with inlet energy stream
COUSCOUS: fixed pump/compressor/expander/turbine/fixed conversion reactor/flash for zero flow situation
COFE: fitted compressor/pump/expander icons with additional connection points for energy ports (for existing documents: replace the icons of existing unit operations if additional connection points are required)
COUSCOUS: energy streams for Pump / Compressor / Expander / FixedConversionReactor / Flash
COFE: CAPE-OPEN models can now be assigned a model class; when inserting a model, models are grouped by class
COFE: unit operations that violate mass balance no longer produce error, instead a warning is produced
COFE: showing descriptions of ports and parameters in tool tip
TEA: GetUniversalConstant fixed
TEA: fixed buffer under-allocation by 1 byte during loading of compounds
COFE: corrected description of heat streams in help file
TEA: removed an erroneous inconsistency message between idealGasHeatCapacity and enthalpy or entropy for phases that do not exist or that have no calculation routine selected
TEA: correction to cubic EOS pseudo property calculations resolves property discontinuities
COFE: corrected automatic TP plot labels for presence of component labels for pure compound properties
TEA: corrected ideal gas heat capacity terms (last coefficient was omitted); affects all enthalpy & entropy terms
TEA: allowing pressure & temperature dependent property calculations for any phase specification (correction for v10 / v11 compatibility)
COFE: corrected printing of residual at Newton iterations
COFE: no longer removing assigned reaction pack from unit at change of PP of inlet streams
COFE: solved crash after deleting streams
COFE: solved problems with not updating of items that depend on property packs after changing property pack configuration
COFE: when calculating single unit (Calculate This Unit), only setting solved status if all input streams are marked solved
COFE: allowing for Calculate This Unit even if the unit is marked solved
COFE: adjusting solution status of flowsheet when parameter collection on energy/information stream changes as a result of connecting or disconnecting the stream
CORN: solved memory leak
COFE: fixed hangup in partitioning of flowsheet with isolated group (partition without inlets)
COFE: solve button was disabled for document containing material templates with only 1 compound
COFE: fixed crash on deleting material type that was in use
COFE: completeness state of output streams were not updated for units with zero flow condition bypass. This could - at zero flow condition - cause COFE to hang at next solution attempt
COFE: renaming phases & compounds now marks document as modified
TEA: as a result of speed optimizations of version 1.07, GetCompoundConstant failed to properly return the values for the proper compound during equilibrium calculations involving external calculation routines. CosmoTherm calculation routine suffered from this
TEA: in addition to flash type specifications "TP","TVF","PVF","PH","HVF","TH","PS","SVF" and "TS", the opposites are now also supported, e.g. "PT","VFT","VFP","HP","VFH","HT","SP","VFS" and "ST"
TEA: molal volume and extended Antoine parameters were not exposed when editing compound data
COFE: added support for lbmol
installer: proper error handling on failure to register uninstaller
COUSCOUS: round off error in flash caused possible liquid flow with all zero concentrations
COFE: correct display of units of vanderwaalsVolume and vanderwaalsArea to include /mol
COFE: exposed Automation model
installer: installing tlb file of COFE and optionally installing CAPE-OPEN type libraries
COFE: added Excel template (COFE.xlt) for using COFE inside Excel (+help)
COFE: fixed missing page on phases in help file
TEA: corrected parachors in component data base
TEA: corrected CorE parameters
TEA: added missing component data
COUSCOUS: fixed erroneous assumption in HeaterCooler which caused invalid solution at zero heat duty and non-zero pressure drop (TP flash was performed)
TEA: correction on reading Chao Seader acentric factors for compounds with zero value (H2, CH4)
TEA: correction to idealGas mixture enthalpy calculations: enthalpy.Dpressure failed to properly set results
TEA: corrected a problem with calculation after deleting a compound from a PP
TEA: fixed crash on failure to load external calculation routine v1.1
COFE/TEA/COUSCOUS/CORN: comparison of two empty strings failed in special circumstances
TEA: should now load at Win2000 systems (did not before)
COFE: corrections to enthalpy / entropy reference state implementation: reference state correction was with wrong sign when enthalpy set by user or unit operation and used by property package. Typically caused enthalpy and entropy flashes to give wrong results with reference state correction option on.
COFE: version 1.1 property packages: caching calls to SetMaterial. Postponing calls to UnsetMaterial until required.
COFE: fixed initial guess initialization of composition
TEA: fixed crash on formatting error message with empty calc type
TEA: fixed error return on property not available in GetProp
COFE: when setting vapor fraction of an inlet stream (through VF, H or S flash), vapor fraction guess is stored and used in solution of stream. Solves issues with 1-compound inlet streams at boiling point.
COFE: solution of inlet streams that are marked as being in equilibrium is skipped
COFE: changing from T & P & X as cut stream variables to P & H & X for pure compound streams (solves problems with pure compound recycles at their boiling point)
COUSCOUS: fixed reporting on flash unit operation
COUSCOUS: added P & VF flash option to flash unit operation
COUSCOUS: fixed read/write status of public parameters after loading for flash unit operation
COUSCOUS: fixed possible inability to set new options on old units
COUSCOUS: fixed energy stream option in compressor
COUSCOUS: changing splitter from isothermal to adiabatic operation in case of non-zero pressure drop or single compound operation
COUSCOUS: adjusted range check for temperature on HeaterCooler when using inlet energy stream; bypass check if flash fails and print warning
COUSCOUS: property tester v1.1 thermo: added test for CalcAndGetLnPhi
COUSCOUS: adjusted interpretation of GetCompoundConstant for missing values
COFE/TEA: adjusted response to missing values for GetCompoundConstant
COFE/TEA/CORK: searching user part of registry in addition to system part of registry for CAPE-OPEN objects
COFE: quicker searching for CAPE-OPEN objects in case of multiple categories
CORK: showing location of registry key (current user or system) for selected object.
TEA: corrections to UNIQUAC routine avoiding domain errors
COFE: stream dialog remembers which sections are open
COFE: correction to relative newton perturbation settings
TEA: prompt for automatically removing a property if no calculation routines are defined for it
COFE: fix for loading stand-alone v1.1 property package
TEA: multiple corrections on phase and compound mapping when loading external calculation or equilibrium routines
TEA: corrections on automatic selection of equivalent properties when using external calculation routine (none selected if not support)
COFE: corrected error message on empty CAS number on importing compounds
ChemSep: limits for LITE have been increased to 10 compounds and 150 stages

Changes since version 1.06 beta:

TEA: failing TP flash is now post checked by checking whether outside two phase region by means of dew and bubble calculations; prevents "inside-out TP flash failed"
COFE: removing the port collection (and thereby releasing the port interfaces) immediately before (rather than after) Terminate() on a unit operation
COFE: removed infinite loop in logarithmic axis tick marks introduced in v1.06
COCO: removed beta from version indication
COFE: proper formatting of missing numbers in stream tool tips
COFE: clipboard format of COFE objects adjusted for future format version changes
COFE: fixed tool tip for stream type selection list on toolbar
COFE: bypassing of unit evaluation at zero flow conditions is now optional
COFE: support for energy streams and partial support for information streams
COUSCOUS: removed internal COM interface definitions
TEA: corrected proper specifications of temperature, pressure and composition after equilibrium calculations
COFE: fixed problems with setting values for boolean members of array parameters
COFE: fixed problems related to option members of array parameters
CORN: bugfix, failed to select proper reaction phase
COFE: error messages could have gone wrong due to call to GetName() before obtaining error, resulting in the error of GetName() itself
COFE: memory leaks at error messages fixed
TEA/COUSCOUS: several correction to error reporting
COUSCOUS: checking range on index for parameter collection's Item()
COFE: solved tool tip related crash after deleting object
COFE: implementation of energy and information streams (preliminary - pending the unit SIG discussions on finalizing the format)
COUSCOUS: solved crash in dialog operation of turbine, compressor, expander, flash, pump
COUSCOUS: turbine; added warning for negative energy production
COUSCOUS: corrections to v1.1 thermo version for checking for vapor phases
COFE: correction to calculations on enthalpy balance of unit operation dialog (error introduced in 1.05beta)
COFE: corrections on validation status of document after changes to material templates or property packs
COUSCOUS: efficiency improvement htx: calculation of inlet enthalpy done before rather than inside newton loop
COUSCOUS: htx allows for different material type hookups (as long as corresponding ports match compound lists)
COUSCOUS: all unit operations now check consistent material types at Validate (check is done by compound list only)
COFE: requirement for all materials to hook up to a unit operation to be of the same type is now optional (on by default)
COFE: removed internal unit StreamConverter
COUSCOUS: added unit StreamConverter
COFE: fixed component balance for unit operation dialog in absence of component from outlet stream
COUSCOUS: pump and turbine now check availability of required property 'volume' at Validate()
COFE: fix for missing window titles when opening an fsd by double clicking on disk
COFE: dropped call to get_ValStatus before validation, because unit operation cannot tell whether external influences (such as compounds on stream) have changed unless by call to Validate()
COFE: direct recycles (i.e. going in- and out of the same unit) are now allowed
COFE: tearing algorithm overhaul: better scaling, better tearing, better convergence properties, better memory usage and better stability
COFE: fixed de-selection of insertable objects when CTRL or SHFT down
COUSCOUS: correction to allocation of flash type string argument for v1.0 flash calculations of many outlet ports (was not allocated by SysAllocString())
COFE: corrected heater and cooler icons for additional (energy) ports; existing documents may need to reload icons
DefaultComponentLib.pcd: fixes for the parameters of LDN and HVP for compounds M-dichlorobenzene, Trans-2-pentene, N-heptane, N-decane
DefaultComponentLib.pcd: added CAS number for Air
COFE/TEA: get_PhaseIDs is no longer returning the overall phase as part of the list
COUSCOUS: fixed error value return for v1.1 property tester
COUSCOUS: printing of phase fractions and compositions for all available phases on duplicate of inlet material
COFE: fixed crash when opening component balance for unit without any connected ports
Installer: added un-installation of old DLLs as to remove registration of retired/outdated interfaces
Installer: showing post-installation log
TEA/COFE: memory + speed optimization for compound lists and property storage
TEA: solved error with flash for reduced compound materials
COFE: added total solve (real-) time to final solution output at intermediate verbosity levels
COFE: keeping track of logged messages per unit during solution of unit
COFE: correction after solution ended with single newton step: states are restored from Jacobian perturbation
COFE: checking convergence status after Newton line search
COFE: Newton solution: preventing to evaluate Jacobian if termination targets are met (possibly saves a single Jacobian evaluation)
Updated sample Cavett document
COFE: Fixed copy / paste errors

Changes since version 1.05 beta:

COSMO: COCO now ships with a LITE version of the COSMOlogic's COSMOtherm activity model
ChemSep: new LITE installer with several fixes; flash calculations are now done by the COSE when using external thermo
TEA: evaluating DIP9E at TR=0.99 if TR>0.99
TEA: evaluating CorE liquid thermal conductivity at TR=0.99 if TR>0.99
TEA: added thermal conductivity routine "Sato Riedel"
TEA: for all equations, an error is now returned (rather than the number zero) for non-existing equation numbers in the pure compound data files
TEA: updated equation library
TEA: Pachaiyappan takes TR = 0.99 for TR > 0.99 and B = 3.0 for Tc < 273.15 K.
TEA: UNIFAC bugfix: crash due to wrong indexing at instantiation in the case of unused groups
COUSCOUS: fixed error return upon not getting interface from port in ICapeCollection::Item
COFE: fixed crash upon right click on dimensionality of compositions in stream dialog
COFE: added stream organizing context menus to the stream dialog (when right-clicking stream data or when clicking stream column header)
COFE: decimal tab and fixed font for numeric data in stream dialog
COFE: adjustable number of decimal significant digits for formatting real numbers in the stream dialog
COFE: when renaming a unit or stream, uniqueness of name is checked. In case of name not being unique, user is asked whether to accept or cancel.
COFE: storing main window location and state between sessions
COFE: added Invert Selection menu
COFE: initial empty document is disposed upon opening existing document
COFE: storing plots, plot content and plot window states
COUSCOUS: correction on reference count on array parameter specs returned from get_ItemsSpecifications
COFE: no longer popping up empty list editor for empty array parameter
COFE: correction on window that shows array parameters: read only or output property was not always taken into account
COFE: added interpretation of parameter dimensions J/mol and J/kg
COFE: disabled editing for elements of read-only array parameter
COFE: support for dimensionality on homogeneous double precision array parameter
COFE: fix on constructor of empty dimension object
COFE: support for plots of homogeneous double precision array (matrix, ...) parameters
COFE: lower bound on array parameter indices was previously deduced from SafeArray GetLBound; is now assumed 0
COFE: fixed crash after deleting selected plot axis
COFE: correction to line drawing algorithm for plots
COFE: removed internal COM interface definitions
COFE: added stop button for solution procedure: works same as Ctrl+C: only responds after pending external calculation (unit operation, flash calculation, ...) is finished
COFE: overhaul of stream route-finding algorithms
COFE: removing redundant lines from log views every 100 updates
COFE: fixed the unit icon for the flash unit operation: the connection on the side of the coil was blocked (route finding always failed); documents that use this icon should reload the icon.
COFE: added context menu to change location of label along a a stream
COFE: streams can now be selected by their label
COFE: you can now copy data from a plot to the clipboard (using the Plot menu, selected or all series)
COFE: added author/company/comments to document (File->Properties)
COFE: added optional comment strings to unit operations and streams; comments appear in the tooltip text
COFE: graphs were not updating after solving
ALL: moved to VS2005-SP1 and different set of runtime libraries
TEA: fixed tool tip in interaction parameter dialog
COFE: support for inserting shapes / lines / arrows / images / text / OLE objects into document
COFE: auto-scroll when mouse is outside view during move/size/... action
COFE: bug fix: improper selection status after Delete
COFE: added copy and paste support (flowsheeting objects as well as external objects)
TEA: stability enhancement for bubble point and dew point temperature calculations
TEA: liquid composition resulting from flash is only set if liquid exists, vapor composition resulting from flash is only set if vapor exists
TEA: all warnings of equilibrium calculations are suppressed, unless it is the final iteration (this prevents loads of warnings)
COFE: fixed message box size for occurrence of very long words
TEA: caching a bunch of memory for flash calculations
COFE: fixed material for allowing for 3 or 4 array elements in flash specifications (rather than just 3)
COFE: for thermo 1.0 flash specification, vapor and liquid phases for which concentration is specified but phase fraction is zero are now considered present after a bubble- or dew point calculation
COUSCOUS: pump and turbine no longer produce warnings on non-liquid phases with zero phase fraction
COFE: disallowing ports of type CAPE_INLET_OUTLET due to unclear assumptions about what this means (flow direction, and whether or not data is available before Calculate() and predicted by Calculate()).
COFE: bug fix in editing option parameters that have a list of choices but are not restricted to that list
COFE: removed the editing field for option parameters that are restricted to a list of choices
COFE: correction in obtaining ICapeParameterSpec for a whole class of parameters. Fixed many option parameter issues.
COFE: StreamConverter under zero flow conditions caused crash
COFE: error of connecting different stream types to one unit operation is now postponed until actually connecting, and shown in the log (more intuitive).
COFE: fixed parsing errors in PLINE flags for unit icons
COFE: fixed furnace unit icon to show color while solving (existing documents should reload the icon)
COFE: stream converter now has a purge for compounds that cannot be present at the outlet.
COFE: adjusted stream converter icon for additional ports (for purge); old documents will need to reload icon if purge needs to be hooked up
COFE: stream converter did not properly restore name and description
COFE: added option for inverse automatic axis scale for plots; corrected spacing on inverted axes
COFE: changed hot keys for rotate icon from Ctrl+[ and Ctrl+] to [ and ] (previous hot keys were equivalent with Escape)
COFE: preventing attempts to evaluate flowsheet iterations where Newton makes bad (non-finite or very high) guess for T or P.
TEA: stability improvements on cubic EOS with pseudo props convergence

Changes since version 1.04 beta:

TEA: bugfix: crash after re-loading a PP configuration inside an existing file from a PP template
COFE: added shortcut for equimolar concentrations in context menu of stream dialog
COFE: added shortcut for pasting compositions from clipboard to stream menu
TEA: v1.1 equilibrium specifications now accept an (empty) 4th argument; previously only 3 element long specifications were accepted
TEA: dialog with scroll bars in case of really big lists of messages when checking PP definitions
TEA: major bug fix; when deleting properties from a PP, all properties became labelled internally as EXCESS ENTHALPY
TEA: added PP flag for suppressing warnings
COFE; removed compositions from tool tip text for streams, when more than 15 compounds
COFE; solved crash when picking from an option list without actually making a selection

Changes since version 1.03 beta:

TEA/COFE/COUSCOUS/CORN: support for version 1.1 thermodynamic standard (yet unpublished)
COFE: revised all phase treatment: phase identifiers are now stored internally and for each property pack; phase definition are optionally combined between property packs. There can only be one vapor phase definition. Phases can be renamed.
COFE: major corrections to phase treatment when nPhase > 2
COFE: corrected indexing error on copying compositions from material in calculator
COFE: added phase info dialog in flowsheet configuration window
COFE/TEA/COUSCOUS/CORN: added ECapeThrmPropertyNotAvailableHR to error handlers
COFE: setting/getting mole/molefraction derivatives for pure calcType is not allowed anymore
COFE: added PP defined compound ID to compound info dialog and changed error handling and compound info sequence
COFE/TEA: fixed uninitialized numbers in MO property storage
COFE: property list in calculator is now in alphabetical order
COFE/TEA: fixed issues with uninitialized values in property descriptors
COFE: resolved problem with disabled selection / insertion menus for stream type #3 and up
COFE/TEA: GetPropList now only reports properties that are supported by both PP and MO
TEA: CalcEquilibrium always failed when non-empty property list was passed because calcType was internally not specified. "Mixture" is now assumed.
TEA: changed trivial solution criteria for VL equilibrium server to sum(ln(K)^2)<1e-4
COUSCOUS: many corrections on error messages
COUSCOUS: fixed memory leak in compressor
COUSCOUS: fixed memory leak in expander
COUSCOUS: fixed memory leak in case of error in flash
COUSCOUS: removed redundant property calls from flash
COUSCOUS: corrected error messages for flash
COUSCOUS: pump: corrected error messages
COUSCOUS: pump no longer uses flow_L/rho_L, but total volumetric flow
COUSCOUS: turbine no longer uses flow_L/rho_L, but total volumetric flow
COUSCOUS: compressor/expander: warning about non-vapor phases now appears in COSE log
COUSCOUS: implemented thermo v 1.1
COUSCOUS: property tester: v 1.1 thermo property testing
COUSCOUS: property tester: dropped PerturbXFirst parameter
COUSCOUS: property tester: CheckMissingZeroDerivs default value now is FALSE, all perturbation defaults are factor 10 lower
COUSCOUS: property tester: corrected column of display for scalar property composition derivatives and the corresponding perturbed values
COUSCOUS: abandoned all attempts to obtain enthalpy in J/s or entropy in J/K/s or volume in m3/s by specifying no or TOTAL basis; call to GetProp now specifies mole basis; multiplication with totalFlow in mol/s follows
COFE: solved a resource leak (HWND, 1 per document window)
COFE: added ability to deal with compounds of unknown molecular weight
CORK: CAPE-OPEN Registry Kit; a utility to inspect and manipulate CAPE-OPEN CATIDs and object registration
COFE: implemented PropCheck() on material object
TEA: fixed PropCheck() for externally defined properties
COFE: material object was not released in case of mimic Bubble/Dew T/P calculation that fails on missing vapor phase
COFE: added W/m2/K to list of popular dimensions
COFE: basis TOTAL (empty basis in v1.0 thermo spec for mass/mole based properties) no longer supported by material object
TEA: basis TOTAL (empty basis in v1.0 thermo spec for mass/mole based properties) no longer supported by material object
COFE: more stringent checking on canHaveTotal item in props.ini when parsing property definitions
TEA: solved various memory leaks
TEA: resolved pointer error
COFE: when solving a recycle, an infinite loop was possible in case a unit operation no longer solves at inputs at which it previously did solve (which can happen if initial guesses are remembered between different evaluations)
COFE/TEA/COUSCOUS: numeric singularity could cause infinite loop in Newton
TEA: option to use COSE materials for internal property calculations has been removed; all internal calculations are done using TEA material objects
TEA: correction to pressure derivative of enthalpy from excess enthalpy
TEA: correction to pressure derivative of ideal liquid enthalpy
TEA: various optimizations to the liquid enthalpy routines
TEA: SumOfPhases calculation routine was calculating phase properties on original material, now uses duplicate material
TEA: when editing compound properties in property pack definitions: corrected unit kmol/m3 to m3/kmol
TEA: after determining pressure derivative of entropy all other entropy values were wrong (within the same CalcProp() call)
COFE/TEA: totalFlow and flow properties are now read-only for all phases but overall phase (read/write)
TEA: support for external equilibrium servers (only v1.1 thermo standard, no support for v1.0 thermo standard)
TEA: serious error on internal calcProp calls: phase array was not property converted
TEA: stack overflow after Duplicate on internal material
COFE: all ports are now disconnected before a unit is destroyed
TEA: enthalpy / heatOfVaporization / entropy / gibbsFreeEnergy calculations no longer try to obtain composition when not a mixture calculation
TEA: VLE server, pressure was not set after equilibrium calculation for HVF and SVF flashes
COFE: values for simulated overall properties Enthalpy/Entropy/Volume were put back on the material object with wrong unit
TEA: fixed crash in all surface tension mixing routines except for "Ideal"
TEA: template list is saved after deleting a template
COFE: by default, display of pressure- or temperature-dependent properties is turned off for the stream dialog
TEA: fixed property dependency checks for fugacity for routines "FromGamma" (to include vapor phase logFugacityCoefficient) and "Dechema" (to not include pure compound density and vapor pressure)
TEA: removed support for back-calculating heatOfVaporization from enthalpy (this would make enthalpy available for mixture, and depend on P, both of which are not allowed in v1.1 spec)
TEA: correction on Amagat routine: failed for temperature and pressure derivatives
TEA: corrections to Letsou-Stiel routine: major failure for super critical compounds
TEA: adjusted some property dependency tests for dependence on mixture rather than pure property to facilitate selection of external routines taking care of both pure and mixture
TEA: fixed equation 106 to give 0 for Tr>1.0; also fixed description to show Tr rather than T
COFE: property list was not updated after editing property packs (until re-opening flowsheet configuration window)
COFE: property display is reduced (no Pure for composition derivatives and 2P properties,
TEA: added properties molecularWeight, kvalue, logkvalue, idealGasEntropy, idealGasHeatCapacity
TEA: much more stringent checks on missing values (CapeDoubleEmpty) of sub-calculations
TEA: fixing CAS numbers upon reading from PCD file if the dashes are lacking
TEA: checking valid CAS numbers when checking property pack
COFE: performing sanity checks on all imported CAS numbers
TEA: compounds with missing boiling-point-temperature (such as CO2) and -volume can now be loaded
TEA: several corrections to pure compound information (pcd file)
COFE: ICapeCOSEUtilities is now exporting named value FreeFORTRANChannel
COFE: ICapeCOSEUtilities is now exporting named value DefaultThermoVersion, which is an advice to PMCs (should not be used by PPs) what thermo version to use if both are implemented. Takes a value of "1.0" or "1.1".
COUSCOUS: DefaultThermoVersion is used to find default thermo version. If that fails, thermo version default to 1.0 until first port is connected. In case this port exports ICapeThermoMaterial, version 1.1 is defaulted to.
TEA: error in ideal gas Cp integrals in (enthalpy, entropy were therefore wrong)
TEA/COFE: various fixes in compound mapping between COSE / PP and external routines
TEA/COFE: fixed memory leaks in material objects
TEA/COFE: fixed setting 'flow' on material object for overall when using reduced or modified-order compound set
COUSCOUS: added testing based on 'Mass' rather than 'Mole' basis
COFE: added option to correct enthalpy and entropy (and idealGas versions) for reference state, ideal gas, user defined T
COFE/TEA: mixture molar weight was sum(MW_i*X_i)/sum(X_i) and now is sum(MW_i*X_i); normalization is dropped. Mainly used in mass/mole conversions and display in stream dialog for overall MW; allow now for perturbation in principle X direction with mass basis.
COFE/TEA: corrected mass/mole conversion for property.DmolFraction with property being scalar mixture property (e.g. density.DmolFraction). Chain rule applies for mixture molar weight; this requires calculation of property during mass conversion (during GetProp() call)
COFE/TEA: added 'extensive' indication to props.ini
COFE: corrections to internal dimensionality and unit conversions of .Dmoles properties
COFE/TEA: only mole basis is allowed for .Dmoles for extensive properties
COFE/TEA: corrected mass/mole conversion for property.Dmoles with property being scalar mixture property (e.g. density.Dmoles). Chain rule applies for mixture molar weight; this requires calculation of property during mass conversion (during GetProp() call)
TEA: checking for unique names when renaming compounds
TEA: fixed compound renaming; old name was still used in some cases
TEA: added Dmoles for all properties for which DmolFraction was available. Dmoles is back-calculated from DmolFraction values
COFE: crash when reading document with multiple property packs in which the first one failed to load
COFE: crash after trying to plot series that does not have pp attached (reference to document's log gets destroyed)
TEA: correction to CorE virial EOS component mapping
TEA: correction on all entropy calculations, removed ideal entropy, replaced entropy from gamma by entropy from fugacityCoefficient
TEA: corrected documentation on entropy
COFE: fix for axis scaling in plots with series that has all data missing
TEA: updated eantoine.lib so that names match the ones in the pcd files; suppresses warnings
COFE: fixed small issue with storage of dimensionality preferences
COFE: fixed hotkey for solving individual unit operation
COFE: for MO and simulation context COM objects: force destruction if not properly Release()d, plus reporting to the end-user (COFE will exit if all objects are released)
COFE: several fixes for plots with logarithmic axes, and zero or negative values
TEA: default tolerance has been decreased to 1e-6. The default maximum number of iterations has been increased to 75.
TEA: added implementation for pseudo properties for cubic equations of state, infeasible regions
TEA: implemented inside-out equilibrium calculations for VLE equilibrium server
TEA: added heat capacity calculation routine from Cp = dH/dT. This is now the default Cp routine
TEA: improved consistency check on entropy, enthalpy and heat capacity
COFE: fix, steam dialog was showing mass fraction compositions for non-existing phases
COFE: allow H-VF and S-VF flashes from within the stream viewer
TEA: When CorE Hvap is out of temperature range, it is still used with a warning (previously Pitzer was used instead, but this makes for a discontinuity that is not desired).
COFE: bug fix in maximum number of newton iterations
COUSCOUS: overall enthalpy calculations on a duplicate of an inlet material within AspenPlus 2004.1/patch:CP-4, still results nonsense: the cause seems to be that phase compositions are not copied by AspenPlus' material::Duplicate().
ChemSep: new LITE installer with several fixes

Changes since version 1.02 beta:

Installer: the data\UnitIcons\Vessels folder was not installed, this caused the icons for the flash and the FCR to be missing
COFE/CORN: using the new v1.1 CAPE-OPEN IDL with new definition for ICapeThermoMaterialContext rather than ICapeThermoContext
COFE: fixed memory leak when failing to restore a saved thermo pack
TEA: added universal constant speedOfLightInVacuum and compound constant SMILESformula
COFE/TEA: revised props.ini format and content for compliance with 1.1 thermo standard
COFE/TEA: revised mass/molar/total conversion of material object
CORN: bug fix after initializion failure: initializing as empty reaction package
COFE: added phase information page in flowsheet configuration dialog, will contain the v1.1 phase information
COFE: items no longer show bold or non-bold in the CAPE-OPEN component selection dialog (which used to indicate the version string was set to 1.0)
COFE: added T and P to calculator results of equilibrium calculation
COFE: bug fix: error correction in mimicked properties: removing properties from list at repeated calculation caused results to equal first call (specifically an issue for TX, PX plots, as well as overall enthalpy/entropy plots)
COFE: bug fix in properties available for plotting: mimicked bubble and dew points were not included in the list
COFE: v1.1 thermo still disabled, untested

Changes since version 1.01 beta:

COFE: many BSTR values were over-allocated by one wide character. This is now fixed, and resolves string comparison issues with all PMC implementations that depend on the string length as reported by SysStringLen rather than lstrlenW. This includes all PMCs written in VB 6.0. It resolves problems loading Infochem's Multiflash as well as Aspen Properties 13.2.
COFE/TEA: Changed solubilityIndex and solubilityProduct properties into vector properties (were previously in props.ini as scalar properties)
COFE: added code for being able to read files that stored properties that were previously defined in a wrong format
COFE: bugfix: old documents failed loading in case of properties that were no longer present
COFE: added dewPointTemperature, dewPointPressure, bubblePointTemperature, bubblePointPressure to the list of properties exported by a material if they are mimicked by the PME rather than exported by the property pack used by the material
COFE: corrected display of matrix values in stream dialog when using material types with fewer compounds than available in document
CORN: implemented IPersistStream on instance of reaction package; the reaction package did not yet store itself into the COFE document
CORN: bugfix: crash on passing empty reaction ID
TEA: you can now restore property pack templates from other property pack templates. This is useful for creating copies of property pack templates (create a new one, restore from an existing one)
TEA: bug fix in making property pack name unique: wrong number was used
COFE/TEA: bug fix: crash on suspect value warnings without basis in MO SetProp
COFE/TEA: changed limit for warnings on suspect values in MO SetProp to 1e15 (before: 1e10)
COFE: when plotting T or P series, no longer evaluating series data if used fractions do not add up to unity
COFE: corrected error in drawing lines in plots with missing points
COFE: added context menus to graphs
COCO: several corrections to help file
COFE: added normalize and remainder context menus to composition overrides for temperature and pressure plots
COFE: quicker response to aborting solve using Ctrl+C (derivative and equilibrium calculations are skipped in case of abort)
COFE: possibility to abort calculations in graphs
COFE: added property/equilibrium/reaction property calculator
CORN: added load and store to reaction pack edit dialog (like in TEA)

Changes since version 1.00 beta:

COUSCOUS: invalid registration of the compound splitter is fixed
COFE: memory leak fixed in case of failure of thermo system
COFE, TEA, COUSCOUS: more elaborate error in case of ECapeUnknown and no error interface
TEA: bug fix in pH flash, pS flash: uninitialized T in case of single phase result (error: zero or negative temperature)
TEA: bug fix in TH flash, TS flash: uninitialized P in case of single phase result (error: zero or negative pressure)
COFE: bug fix: parameter spec was obtained using QueryInterface() rather than get_Specification()
COFE: shortcut keys to menus
COFE: added Zoom-in, Zoom-out menus
COFE: added ConfigureTEA and ConfigureCORN to start menu
COFE: bugfix in rotating and flipping unit icons; scaling point was wrongly transformed
COUSCOUS: fixed several error messages
COUSCOUS: work-around for overall enthalpy and entropy if not supplied by material
COCO: help file updated
TEA: get_PhaseIDs is no longer returning the overall phase as part of the list
COFE: dropped requirement of at least 2 compounds per material type, now is at least 1
TEA: dropped requirement of at least 2 compounds per property pack, you can now make a zero compound property pack
COFE: updated document format for future backward compatibility
COFE: revision of material object; properties like enthalpy can now be stored in J/mol, J/kg or J/s; conversion no longer takes place at SetProp, but at GetProp. Solves a lot of issues regarding order of specification.
TEA: revision of material object; properties like enthalpy can now be stored in J/mol, J/kg or J/s; conversion no longer takes place at SetProp, but at GetProp.
TEA: TP flash failure was not always detected
COFE: added possibility to specify overall enthalpy or entropy from the stream dialog
CORN: new reaction rate wizard
COFE: the material object is now able to CalcProp() dewPointPressure, bubblePointPressure, dewPointTemperature, bubblePointTemperature if there is no support for that in the property pack
COFE: the material object is now able to CalcProp() overall enthalpy/entropy/volume if there is no support for that in the property pack
COFE: when using Validate() on the flowsheet, each unit operation's validate is now explicitly called (formerly the results of that were cached)
COFE: bugfix in importing parameter dimensions: crash at less than 6 numbers could have occurred
CORN: accepting no basis as mole basis
COFE: support for plotting reaction properties vs T or P
CORN: many corrections to actual property calculations
CORN: reaction rate & equilibrium constant formulas are now both remembered (only 1 can apply though)
COFE: GetAvailableProps now also adds to the list: pressure, temperature, flow, totalFlow, fraction, phaseFraction
TEA: GetAvailableProps now also adds to the list: pressure, temperature, flow, totalFlow, fraction, phaseFraction
COFE: error check on obtaining unit operation reports
COFE: unit reports are now shown in fixed pitch font (courier)
COFE: revised unit conversion objects
COFE: kg and moles are now supported when appearing together in a unit operation parameter.
COFE: fractions can now be displayed in percents
COFE: plot series did not update when axis unit was changed
COFE: added mass, enthalpy and component balances to unit dialog
ChemSep: new LITE installer with several fixes