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

COCO v2.01 changes and (bug-) fixes

cup To get the latest updates, you can run COCO UPdate (CUP), which is available since COCO version 1.13. If you have trouble running CUP, see Updating COCO in the support section.

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

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 corretions 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 absense 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 transfered
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 persistance
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 psuedo properties to exclude false supercritical 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 supercritical 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 NTRL 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 defauls 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 checmical 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 conducitivty 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: psuedo 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, diffent Z = azeotrope, same Z and supercritical = single phase, same Z and not supercritical = 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): possibily 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: surpressing 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 criterium 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 supercritical 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 dowloading time display (last minute was not showing correcly)
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: substitured 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 configuratable 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 exhanger 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 messageboxes 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 releaseing 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 measureing 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 (devision 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 gridlines 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 faillure 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 rerturned 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 tempature 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 equilibruim 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 psuedo 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 isse 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 arhenius 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 opeations 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 partioning 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 faillure to register uninstaller
COUSCOUS: roundoff 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 absense 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 linesearch
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 Tcrit < 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 rightclick 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 compoisition resulting from flash is only set if vapor exists
TEA: all warnings of equilibrium calculations are suppresed, unless it is the final iteration (this prevents loads of warnings)
COFE: fixed message box size for occurance 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 phasefraction 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 criterium 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 orginal 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 Amalgat routine: failed for temperature and pressure derivatives
TEA: corrections to Letsou-Stiel routine: major failure for supercritical 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