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SS GEN-03 Steady State Design 2013and Road Map for Upcoming Years
Marina VelazquezProduct Manager @InvensysOpsMgmt / #SoftwareRevolution
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© 2013 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries.All third party trademarks and service marks are the proprietary marks of their respective owners.
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PRO/II 9.2 (Released May 2013)
•New Security Tool switcher: USB toFlexLM and back
•Library Registration Repair tool•Compiler Migration to VS 2008 IVF 12.0•New Installer: WIX•SimSci SIM4ME Portal 2.2 in Office 2010
•New Security Tool switcher: USB toFlexLM and back
•Library Registration Repair tool•Compiler Migration to VS 2008 IVF 12.0•New Installer: WIX•SimSci SIM4ME Portal 2.2 in Office 2010
•Improved documentation•SimSci PRO/II version shows in the GUItitle bar
•Russian, Chinese and Spanish in languagemodule
•Consolidation of Casebook and Applib files•Run and calculate output values•Warn if .out is out of sync•Compact/Repair•Allow to copy/paste streams and groups ofunits within a file
•New Cut/paste from one block flowsheet toanother
•Find and Replace streams and unitoperations name
•Create HTRI data files from Heat Curves•Ternary Plots add-on does BVLE plots too
•Improved documentation•SimSci PRO/II version shows in the GUItitle bar
•Russian, Chinese and Spanish in languagemodule
•Consolidation of Casebook and Applib files•Run and calculate output values•Warn if .out is out of sync•Compact/Repair•Allow to copy/paste streams and groups ofunits within a file
•New Cut/paste from one block flowsheet toanother
•Find and Replace streams and unitoperations name
•Create HTRI data files from Heat Curves•Ternary Plots add-on does BVLE plots too
•Multiple Head curves for compressors fordifferent Molecular eights
•Depressurization Updates•KGTower 5.1 link update•CAPE OPEN unit operations: Refineryreactors
•Calculate and report ideal Cp/Cv•Controller behavior user default•Update to SimSci SIM4ME Portal 2.2
UsabilityInfrastructure
Updates
Slide 2
•Improved documentation•SimSci PRO/II version shows in the GUItitle bar
•Russian, Chinese and Spanish in languagemodule
•Consolidation of Casebook and Applib files•Run and calculate output values•Warn if .out is out of sync•Compact/Repair•Allow to copy/paste streams and groups ofunits within a file
•New Cut/paste from one block flowsheet toanother
•Find and Replace streams and unitoperations name
•Create HTRI data files from Heat Curves•Ternary Plots add-on does BVLE plots too
•Improved documentation•SimSci PRO/II version shows in the GUItitle bar
•Russian, Chinese and Spanish in languagemodule
•Consolidation of Casebook and Applib files•Run and calculate output values•Warn if .out is out of sync•Compact/Repair•Allow to copy/paste streams and groups ofunits within a file
•New Cut/paste from one block flowsheet toanother
•Find and Replace streams and unitoperations name
•Create HTRI data files from Heat Curves•Ternary Plots add-on does BVLE plots too
•Multiple Head curves for compressors fordifferent Molecular eights
•Depressurization Updates•KGTower 5.1 link update•CAPE OPEN unit operations: Refineryreactors
•Calculate and report ideal Cp/Cv•Controller behavior user default•Update to SimSci SIM4ME Portal 2.2
•Multiple Head curves for compressors fordifferent Molecular eights
•Depressurization Updates•KGTower 5.1 link update•CAPE OPEN unit operations: Refineryreactors
•Calculate and report ideal Cp/Cv•Controller behavior user default•Update to SimSci SIM4ME Portal 2.2
•Data entry improvements•Duplicate Thermo Method•Case specific Kij editingimprovements
•BWRSPURE databanks accessibleNew Heat of Formation correlation
•Component Phase Selection•OLI Chemistry Wizard 3.2•NIST REFPROP Fluid Files•Password protected databanks do notprint protected values in GUI or outputreport
•Data entry improvements•Duplicate Thermo Method•Case specific Kij editingimprovements
•BWRSPURE databanks accessibleNew Heat of Formation correlation
•Component Phase Selection•OLI Chemistry Wizard 3.2•NIST REFPROP Fluid Files•Password protected databanks do notprint protected values in GUI or outputreport
PRO/II 9.2 (Released May 2013)
•SimSci SIM4ME Thermo 3.6 capabilities•Predictive SRK•Extension of Kij’s equations forNRTL and BWRS
•Water options•IF97 water transport properties•New Calculation Method for WaterPartial
•Pressure, Sour Gas-WichertCorrelation
•Penelux liquid density improvements•CAPE OPEN 1.1 (without VLSE flash)
•SimSci SIM4ME Thermo 3.6 capabilities•Predictive SRK•Extension of Kij’s equations forNRTL and BWRS
•Water options•IF97 water transport properties•New Calculation Method for WaterPartial
•Pressure, Sour Gas-WichertCorrelation
•Penelux liquid density improvements•CAPE OPEN 1.1 (without VLSE flash)
Thermo
Slide 3
•Data entry improvements•Duplicate Thermo Method•Case specific Kij editingimprovements
•BWRSPURE databanks accessibleNew Heat of Formation correlation
•Component Phase Selection•OLI Chemistry Wizard 3.2•NIST REFPROP Fluid Files•Password protected databanks do notprint protected values in GUI or outputreport
•Data entry improvements•Duplicate Thermo Method•Case specific Kij editingimprovements
•BWRSPURE databanks accessibleNew Heat of Formation correlation
•Component Phase Selection•OLI Chemistry Wizard 3.2•NIST REFPROP Fluid Files•Password protected databanks do notprint protected values in GUI or outputreport
•SimSci SIM4ME Thermo 3.6 capabilities•Predictive SRK•Extension of Kij’s equations forNRTL and BWRS
•Water options•IF97 water transport properties•New Calculation Method for WaterPartial
•Pressure, Sour Gas-WichertCorrelation
•Penelux liquid density improvements•CAPE OPEN 1.1 (without VLSE flash)
•SimSci SIM4ME Thermo 3.6 capabilities•Predictive SRK•Extension of Kij’s equations forNRTL and BWRS
•Water options•IF97 water transport properties•New Calculation Method for WaterPartial
•Pressure, Sour Gas-WichertCorrelation
•Penelux liquid density improvements•CAPE OPEN 1.1 (without VLSE flash)
PRO/II 9.2.x (9.2.1 released September 2013)
•APPV (9.2.1)•Expose all commands on the toolbarsection (9.2.1)
•APPV (9.2.1)•Expose all commands on the toolbarsection (9.2.1)
•Open file in original version (9.2.1)•Run Unavailable (9.2.1)•Exclude/Include blocks (9.2.1)•Copy/Paste units into excluded blocks(9.2.1)
•Open file in original version (9.2.1)•Run Unavailable (9.2.1)•Exclude/Include blocks (9.2.1)•Copy/Paste units into excluded blocks(9.2.1)
UsabilityInfrastructure
Slide 4
•APPV (9.2.1)•Expose all commands on the toolbarsection (9.2.1)
•Open file in original version (9.2.1)•Run Unavailable (9.2.1)•Exclude/Include blocks (9.2.1)•Copy/Paste units into excluded blocks(9.2.1)
•DIPPR 2013 Database (9.2.2)•NIST 9.1 (9.2.2)•Update PPR78 binaries (9.2.2)
•DIPPR 2013 Database (9.2.2)•NIST 9.1 (9.2.2)•Update PPR78 binaries (9.2.2)
•Spiral CrudeSuite 5.5 Integration (9.2.1)•Spiral CrudeSuite 5.5 Integration (9.2.1)
New FeaturesThermo
PRO/II 2014/2015 (PRO/II 2014 + patches)
•Cloud computing•Win 8 Support•Office 2013 Support•Upgrade to SIM4ME Thermo 3.7•Upgrade to SIM4ME Portal 2.3
•Cloud computing•Win 8 Support•Office 2013 Support•Upgrade to SIM4ME Thermo 3.7•Upgrade to SIM4ME Portal 2.3
•Convert all Excel Spread sheets and ExcelUnit Operation to Office 2010
•Improve controller to allow Modification ofthermo parameters
•Column user interface improvements•Unit Operations user interfaceimprovements
•Block Operations and SequencingImprovements
•Miscellaneous user experienceimprovements
•Utilities Summary•Case Study Improvements
•Convert all Excel Spread sheets and ExcelUnit Operation to Office 2010
•Improve controller to allow Modification ofthermo parameters
•Column user interface improvements•Unit Operations user interfaceimprovements
•Block Operations and SequencingImprovements
•Miscellaneous user experienceimprovements
•Utilities Summary•Case Study Improvements
UsabilityInfrastructure
Slide 5
•Cloud computing•Win 8 Support•Office 2013 Support•Upgrade to SIM4ME Thermo 3.7•Upgrade to SIM4ME Portal 2.3
•Convert all Excel Spread sheets and ExcelUnit Operation to Office 2010
•Improve controller to allow Modification ofthermo parameters
•Column user interface improvements•Unit Operations user interfaceimprovements
•Block Operations and SequencingImprovements
•Miscellaneous user experienceimprovements
•Utilities Summary•Case Study Improvements
•Convert all Excel Spread sheets and ExcelUnit Operation to Office 2010
•Improve controller to allow Modification ofthermo parameters
•Column user interface improvements•Unit Operations user interfaceimprovements
•Block Operations and SequencingImprovements
•Miscellaneous user experienceimprovements
•Utilities Summary•Case Study Improvements
•Improve Depressurization•Phase Envelope Updates•Case Study Improvements•Heat Curves Updates•Pipe Operations Updates•Pumps/Expanders Updates•Control Valve to calculate cp
•Improve Depressurization•Phase Envelope Updates•Case Study Improvements•Heat Curves Updates•Pipe Operations Updates•Pumps/Expanders Updates•Control Valve to calculate cp
Updates
PRO/II 2014/2015 (PRO/II 2014 release fall 2014 + patches)
•INPLANT as a Unit Operation•INPLANT as a Unit Operation
New Features
•Metals/Mining capabilities (viaChemApps from GTT)
•Links to Custom Models (via gPROMSfrom PSE)
•Link to Cost Estimating Package(CostOS from Numitech)
•Updates to OLI MSE electrolytes
•Metals/Mining capabilities (viaChemApps from GTT)
•Links to Custom Models (via gPROMSfrom PSE)
•Link to Cost Estimating Package(CostOS from Numitech)
•Updates to OLI MSE electrolytes
Third Party Collaboration
Slide 6
•INPLANT as a Unit Operation•Metals/Mining capabilities (viaChemApps from GTT)
•Links to Custom Models (via gPROMSfrom PSE)
•Link to Cost Estimating Package(CostOS from Numitech)
•Updates to OLI MSE electrolytes
•Metals/Mining capabilities (viaChemApps from GTT)
•Links to Custom Models (via gPROMSfrom PSE)
•Link to Cost Estimating Package(CostOS from Numitech)
•Updates to OLI MSE electrolytes
•DIPPR yearly updates•Coal Handling•DIPPR yearly updates•Coal Handling
Thermo
PRO/II beyond 2015
•64 bit computing•Upkeep with cloud and virtualizationtechnologies
•64 bit computing•Upkeep with cloud and virtualizationtechnologies
•Customer driven improvements•Flowsheeting improvements•Multiple head curves for expander andpumps
•Sequencing improvements•VLSE Flash•Steam Ejector•Water Saturation•2 Phase Plug Flow Reactor
•Customer driven improvements•Flowsheeting improvements•Multiple head curves for expander andpumps
•Sequencing improvements•VLSE Flash•Steam Ejector•Water Saturation•2 Phase Plug Flow Reactor
Infrastructure Usability and New Features
Slide 7
•64 bit computing•Upkeep with cloud and virtualizationtechnologies
•Customer driven improvements•Flowsheeting improvements•Multiple head curves for expander andpumps
•Sequencing improvements•VLSE Flash•Steam Ejector•Water Saturation•2 Phase Plug Flow Reactor
•Customer driven improvements•Flowsheeting improvements•Multiple head curves for expander andpumps
•Sequencing improvements•VLSE Flash•Steam Ejector•Water Saturation•2 Phase Plug Flow Reactor
•Chemical Market Needs•Sulphur treatment Capabilities•Hydrates•Multi component slates
•Chemical Market Needs•Sulphur treatment Capabilities•Hydrates•Multi component slates
Thermo
SIM4ME Reports and PORTAL 2014/2015
•Win 8 Support•Office 2013 Support•VS2010 migration
•Win 8 Support•Office 2013 Support•VS2010 migration
•De-pressurising systems output variablesimprovements
•PIPE Output variables improvement•Report transport properties in the portal.•Expose weight rate variables•Expose the calculated heat transfercoefficients of Rigorous
•In SIM4ME Reports, provide stream ratesand composition on a weight basis.
•De-pressurising systems output variablesimprovements
•PIPE Output variables improvement•Report transport properties in the portal.•Expose weight rate variables•Expose the calculated heat transfercoefficients of Rigorous
•In SIM4ME Reports, provide stream ratesand composition on a weight basis.
Reporting CapabilitiesImprovements
Integration/Infrastructure
Slide 8
•Win 8 Support•Office 2013 Support•VS2010 migration
•De-pressurising systems output variablesimprovements
•PIPE Output variables improvement•Report transport properties in the portal.•Expose weight rate variables•Expose the calculated heat transfercoefficients of Rigorous
•In SIM4ME Reports, provide stream ratesand composition on a weight basis.
•De-pressurising systems output variablesimprovements
•PIPE Output variables improvement•Report transport properties in the portal.•Expose weight rate variables•Expose the calculated heat transfercoefficients of Rigorous
•In SIM4ME Reports, provide stream ratesand composition on a weight basis.
•Report liquid properties if the stream is onlyin vapor phase and vice-versa. Theproperties of all the phases should be visibleeven if the stream selected does not have aparticular phase.
•Report liquid properties if the stream is onlyin vapor phase and vice-versa. Theproperties of all the phases should be visibleeven if the stream selected does not have aparticular phase.
Flexibility and Usability
SIM4ME Reports and PORTAL 2014/2015
•Completely define Spec - vary fromPortal replicating PRO/II
•Make key reactor data available asread/write in Portal
•Access to Reaction data via Portal•Approach temperature for individualreactions to be available in portal andcase study to change
•Allow access to User Added Units viaPortal
•Support UAS parameters in the Portal.•Enable all feasible input parametersthrough the portal.
•Completely define Spec - vary fromPortal replicating PRO/II
•Make key reactor data available asread/write in Portal
•Access to Reaction data via Portal•Approach temperature for individualreactions to be available in portal andcase study to change
•Allow access to User Added Units viaPortal
•Support UAS parameters in the Portal.•Enable all feasible input parametersthrough the portal.
Reporting CapabilitiesImprovements
Integration/Infrastructure
Input Completeness
Slide 9
•Completely define Spec - vary fromPortal replicating PRO/II
•Make key reactor data available asread/write in Portal
•Access to Reaction data via Portal•Approach temperature for individualreactions to be available in portal andcase study to change
•Allow access to User Added Units viaPortal
•Support UAS parameters in the Portal.•Enable all feasible input parametersthrough the portal.
•Completely define Spec - vary fromPortal replicating PRO/II
•Make key reactor data available asread/write in Portal
•Access to Reaction data via Portal•Approach temperature for individualreactions to be available in portal andcase study to change
•Allow access to User Added Units viaPortal
•Support UAS parameters in the Portal.•Enable all feasible input parametersthrough the portal.
VISUAL FLOW 2014/2015
•Win 8 Support•Office 2013 Support•Upgrade to SIM4ME Thermo 3.7•Upgrade to SIM4ME Portal 2.3
•Win 8 Support•Office 2013 Support•Upgrade to SIM4ME Thermo 3.7•Upgrade to SIM4ME Portal 2.3
•Report that provides the back-pressure forall relief valves (including those that do nothave any flow rate)
•Enable isometric diagrams to indicate entireflowsheet.
•Report that provides the back-pressure forall relief valves (including those that do nothave any flow rate)
•Enable isometric diagrams to indicate entireflowsheet.
•Metric UOM For VF managers•Metric UOM For VF managers •Add user-supplied line sizing criteria•Improvements required in Depressuringcalculation
•Enable to predict sound velocity from MWwhen simple thermo is applied.
•Enable a safety valve to represent pluralsafety valves by specifying the number ofthe valves.
•MDI Feature•Containerized option of the databases
Flexibility and Usability
Reporting CapabilitiesImprovements
Integration/Infrastructure
Input Completeness
Slide 10
•Metric UOM For VF managers•Metric UOM For VF managers •Add user-supplied line sizing criteria•Improvements required in Depressuringcalculation
•Enable to predict sound velocity from MWwhen simple thermo is applied.
•Enable a safety valve to represent pluralsafety valves by specifying the number ofthe valves.
•MDI Feature•Containerized option of the databases
•Add user-supplied line sizing criteria•Improvements required in Depressuringcalculation
•Enable to predict sound velocity from MWwhen simple thermo is applied.
•Enable a safety valve to represent pluralsafety valves by specifying the number ofthe valves.
•MDI Feature•Containerized option of the databases
PIPEPHASE 2014/15
•Win 8 Support•Office 2013 Support•PRO/II 9.2 migration•SIM4ME PORTAL 2.3 upgrade
•Win 8 Support•Office 2013 Support•PRO/II 9.2 migration•SIM4ME PORTAL 2.3 upgrade
•Convert all Excel Spread sheets and ExcelUnit Operation to Office 2010
•UOM conversion•Add pictures to PFD•Ability to add names to Properties instead ofnumbers
•Wizard to open PVT data entry
•Convert all Excel Spread sheets and ExcelUnit Operation to Office 2010
•UOM conversion•Add pictures to PFD•Ability to add names to Properties instead ofnumbers
•Wizard to open PVT data entry
UsabilityIntegration/Infrastructure
Slide 11
•Win 8 Support•Office 2013 Support•PRO/II 9.2 migration•SIM4ME PORTAL 2.3 upgrade
•Convert all Excel Spread sheets and ExcelUnit Operation to Office 2010
•UOM conversion•Add pictures to PFD•Ability to add names to Properties instead ofnumbers
•Wizard to open PVT data entry
•Convert all Excel Spread sheets and ExcelUnit Operation to Office 2010
•UOM conversion•Add pictures to PFD•Ability to add names to Properties instead ofnumbers
•Wizard to open PVT data entry
PIPEPHASE 2014/15
•Erosional velocity calculation: Analternative to API 14E
•Handle zero flow in PIPEPHASE sink toallow completion of convergence solution
•Upgrade the Choke and Valves devices toallow users to specify cv (valve flowcapacity coefficient) values
•Add tuning parameters for viscositycorrelation parameters when usingcompositional models
•Viscosity method which includespressure correction
•RAS & NODAL Enhancements
•Erosional velocity calculation: Analternative to API 14E
•Handle zero flow in PIPEPHASE sink toallow completion of convergence solution
•Upgrade the Choke and Valves devices toallow users to specify cv (valve flowcapacity coefficient) values
•Add tuning parameters for viscositycorrelation parameters when usingcompositional models
•Viscosity method which includespressure correction
•RAS & NODAL Enhancements
•Steam Separator•Add PUMP/ESP databases and also provide atool to convert to PP
•Allow gas lift valve option for compositional& condensate fluids.
•Capability to enter tubing profile data•Steam Injection•Add TUFFP mechanistic pressure-dropcorrelation
•Steam Separator•Add PUMP/ESP databases and also provide atool to convert to PP
•Allow gas lift valve option for compositional& condensate fluids.
•Capability to enter tubing profile data•Steam Injection•Add TUFFP mechanistic pressure-dropcorrelation
New FeaturesUpdates
Slide 12
•Erosional velocity calculation: Analternative to API 14E
•Handle zero flow in PIPEPHASE sink toallow completion of convergence solution
•Upgrade the Choke and Valves devices toallow users to specify cv (valve flowcapacity coefficient) values
•Add tuning parameters for viscositycorrelation parameters when usingcompositional models
•Viscosity method which includespressure correction
•RAS & NODAL Enhancements
•Erosional velocity calculation: Analternative to API 14E
•Handle zero flow in PIPEPHASE sink toallow completion of convergence solution
•Upgrade the Choke and Valves devices toallow users to specify cv (valve flowcapacity coefficient) values
•Add tuning parameters for viscositycorrelation parameters when usingcompositional models
•Viscosity method which includespressure correction
•RAS & NODAL Enhancements
•Steam Separator•Add PUMP/ESP databases and also provide atool to convert to PP
•Allow gas lift valve option for compositional& condensate fluids.
•Capability to enter tubing profile data•Steam Injection•Add TUFFP mechanistic pressure-dropcorrelation
•Steam Separator•Add PUMP/ESP databases and also provide atool to convert to PP
•Allow gas lift valve option for compositional& condensate fluids.
•Capability to enter tubing profile data•Steam Injection•Add TUFFP mechanistic pressure-dropcorrelation