What is COCO
Sample Flowsheets
Change Log
License
Compliancy testing
Help
Support
Downloads
Links
Contributors
Flowsheeting
Flowsheet Configuration
Streams
Unit operations
Connecting unit operations
Colors and status
Selecting streams and unit operations
Solving the flowsheet
Editing and displaying streams
Flowsheet log
Flowsheet printing
Inserting models
Inserting objects
Flowsheet report
Add-ins
INDEX
64-bit
Acknowledgements
Activity
Adding compounds
Adding series to a plot
Adding streams
Add-ins
Aggregation states
Amagat's law
Antoine
API SRK
Application preferences
Array formulas in Excel
Array Parameter Plot
ASOG
Atom counting
Author
Author report
Automatic calculation
Automatic update
Automation
Azeotrope
Background thread for solving
Balances
Binary plots
Brock-Bird
Brokaw
Bubble point
CAPE OPEN
Check for updates
Chemical compounds
Chemical reactions
ChemSep
Closed recycles
COCO
COCO Update
COFE
COFE_CalculateEquilibrium
COFE_CalculateEquilibriumHeaders
COFE_FormatCompoundConstantDimensionality
COFE_FormatPropertyDimensionality
COFE_GetCompoundCount
COFE_GetCompoundNames
COFE_GetDownStreamUnitName
COFE_GetStreamComposition
COFE_GetStreamCount
COFE_GetStreamFlow
COFE_GetStreamItemDimension
COFE_GetStreamItems
COFE_GetStreamItemValue
COFE_GetStreamMaterialType
COFE_GetStreamNames
COFE_GetStreamPhaseComposition
COFE_GetStreamPhaseFraction
COFE_GetStreamPresentPhases
COFE_GetStreamPressure
COFE_GetStreamTemperature
COFE_GetStreamType
COFE_GetTemplateCount
COFE_GetTemplateNames
COFE_GetUnitOperationCount
COFE_GetUnitOperationNames
COFE_GetUnitPortCount
COFE_GetUpStreamUnitName
COFE_ObtainComponentConstant
COFE_ObtainProperty
COFE_UnitOperationFormatParameterDimensionality
COFE_UnitOperationGetParameterCount
COFE_UnitOperationGetParameterNames
COFE_UnitOperationGetParameterValue
COFE_UnitOperationGetPortDirection
COFE_UnitOperationGetPortNames
COFE_UnitOperationGetPortStreamName
COFE_UnitOperationGetPortType
COFEStand
CO-LaN
Colors
Command line flowsheet solver
Comments
Company
Composition threshold
Compound spitter
Compounds
Compressibility factor
Compressor
ConfigureCORN.exe
ConfigureTEA.exe
Connecting unit operations
Controller
Cooler
CORK
CORN
Corresponding states
CosmoTherm
COSTALD
COULIS
Counting atoms
Counting elements
COUSCOUS
CreateObject
Creating plots
Creation date
CSTR
Cubic equations of state
CUP
Date of creation
DECHEMA
Defaults
Deferred calculation
Density
Description of property package
Dew point
Digulio-Teja
DIPPR 7A
DIPPR 9B-2
DIPPR 9B-3
DIPPR 9B-3
DIPPR 9D
DIPPR 9E
DIPPR 9H
DIPPR 9I
Disclaimer
Disconnecting unit operations
Distillation
Document Explorer
Document Properties
Document title
Double-click unit operations
DownstreamUnit
Edit unit operations
Element counting
Embedding objects
Energy
Energy Measure unit
Energy mixer
Energy splitter
Energy streams
Entering Excel functions
Enthalpy
Enthalpy reference state
EnthalpyF
Entropy
Entropy reference state
EntropyF
Equation of state
Equilibrium calculations
Equilibrium constant
Equilibrium estimation method
Equilibrium reactions
Equilibrium reactor
Estimation method
Excel
Excess enthalpy
Expander
Expression syntax
Extended Antoine
External property calculation routines
Fixed conversion reactor
Flash
Flash calculations
Flory-Huggins
Flow constraint
Flowsheet add-ins
Flowsheet log
Flowsheet monitoring objects
Flowsheet report
Formula syntax
Fugacity
Full path name
Gamma-Phi
GetCompoundConstantDimensionality
GetError
GetObject
GetPropertyDimensionality
GetReactionObject
GetReactionObject
GetReactionPackageCount
GetReactionPackageNames
GetSimulationContext
GetStream
GetStreamCount
GetStreamNames
GetSupportedPhaseList
GetUnit
GetUnit
GetUnitCount
GetUnitNames
Gibbs free energy
Gibbs Minimization Reactor
Graphics objects
Graphs
Group contribution parameters
Hankinson-Thompson
Hayden-O'Connel
Heat capacity
Heat exchanger
Heat of Combustion
Heat of reaction
Heat of vaporization
Heater
Heterogeneous reaction
HHV
Higher Heating Value
Homogeneous reaction
IAPWS-97
ICOFEDocument
ICOFEMaterial
ICOFEStream
Icons
Ideal gas law
Ideal separator
Information Calculator
Information streams
Initial guess
Inproc
Inserting models
Inserting objects
Inserting streams
Inserting unit operations
Inspecting streams
Interaction parameters
Interface specifications
Internal energy
IPD
JUIcE
Kinetic Gas Theory
Kinetics
K-values
Labels
Lee-Kesler
Letsou-Stiel
LHV
License
Lielmezs-Herrick
LoadFromString
Log
Log size
Log verbosity
Logging
Lower Heating Value
Make-up mixer
Manipulating streams
Margules
Marshalling
Mass balance
Mass tolerance
Material streams
MaterialType
Maximum iterations
Maximum Newton iterations
Measure unit
Microsoft Excel
Misic-Thodos
Missing data points in plots
Mixer
Mixing material streams
Mixing thermal energy streams
Model classes
Model sets
Molecular weight
Moving streams and unit operations
Multi-threading
Name of property package
New files
Newton
Nm3
No operation
Normal volume
NRTL
Numerical property package options
OATS
OLE objects
Options
Order of streams
Order of Unit Operations
Out-of-proc
Pachaiyappan et al.
Packed bed
Parametric study
PCD
Peng Robinson
Perturbation
PFR
Phases
Pitzer
Plot types
Plots
Plug-ins
Poynting correction factor
PR
Predefined model sets (TEA)
Preferences
Pressure plot
Printing
Properties
Properties of plots
Property calculations
Property definitions
Property package options
Property package templates
Property packs
Property tester
props.ini
Pseudo properties
Pump
Pure compound data
PX Plot
Rackett
Reaction compounds
Reaction package templates
Reaction packs
Reaction phase
Reaction property calculations
Reaction rate
Reactors
Recycle tolerance
Redlich Kwong
Reference state
References
Registration of CAPE OPEN objects
Regular solution
Reid et al
Relative perturbation
Removing streams
Removing unit operations
Renon and Prausnitz
Reports
Reset
Residue curves and -maps
Riedel
RK
SaveCopy
SaveToString
Scatchard and Hildebrand
SCF
Selection
Separators
ShowMainConfiguration
Simple editing mode (TEA)
Simplified model solutions
Soave Redlich Kwong
Solid-only compounds
Solids separator
Solution warnings and errors
Sorting streams
Sorting Unit Operations
Species
Splitter
Splitting energy streams
Splitting material streams
SRK
Stand-alone flowsheet solver
Status
Steam
Stoichiometry
Stream copier
Stream order
Stream reports
Stream types
StreamConverter
Streams
StreamType
Sub-flowsheets
Supported properties
Surface tension
Symbol list (TEA)
TEA
Temperature Correlation
Temperature plot
Templates
Ternary systems and plots
TERNYP
Testing properties
Thermal conductivity
Thermodynamics
Title
Tolerance
Trivial solutions
Tsonopoulous
Tube reactor
Turbine
TX Plot
Type libraries
UNIFAC
UNIQUAC
Unit operation icons
Unit operation labels
Unit Operation order
Unit operations
Unit parameter reports
Unit reports
Units of measure
Update checking
UpstreamUnit
Utility applications
Utility steam
Valve
Van Laar
Vapor pressure
Virtual information ports
Viscosity
VLE Server
Volume
Warnings
Watches
Water
Wegstein
Wilke
Wilson
Wilson Ideal solution model
Windows registry
Winterfeld et al.
Wiping streams
Yen-Woods
Yoon and Thodos
Zero flow
CONTENT
COCO
COFE
Material Objects
Flowsheeting
Flowsheet configuration
Streams
Unit operations
Connecting unit operations
Colors and status
Selecting streams and unit operations
Solving the flowsheet
Stream display
Flowsheet log
Flowsheet printing
Inserting models
Inserting objects
Flowsheet report
Add-ins
Plots
Parametric studies
Document explorer
Watches
Flowsheets as Unit Operations
Calculator
Automation
Using COFE in Excel
Document Properties
Application Preferences
TEA
COUSCOUS
CORN
ChemSep
CosmoTherm
Water Property Package
Add-ins
Utility applications
64-bit versus 32-bit software
Disclaimer
COCO
COFE
Flowsheet configuration