The Methods & Tools Special Interest Group held a conference call on June 14, 2017 to progress the document specifying the interface design for Flowsheet Monitoring. Bill BARRETT (U.S. Environmental Protection Agency), Jasper van BATEN (AmsterCHEM) and Michael HLAVINKA (Bryan Research & Engineering) attended the conference call together with me.
It appears that the design is now frozen, at least prior to a final review to be conducted by the CO-LaN members (but not yet launched). A few minor adjustments have been made to the descriptions of the Use Cases as well as to the detailed description of each method. Version 1.52 of the document has been created following this conference call and will be reviewed / modified by the M&T SIG core group till the next conference call scheduled mid-July 2017. Mainly description of various scenarios as to which interfaces and methods they exercize is further needed (there is only one scenario included in the document so far). It is also necessary to address the modifications of the existing prototypes such as COFE as a PME, TERNHYP and WAR as Flowsheet Monitoring Components. Would be easier for everyone to review the design together with exercizing prototypes.
June 14, 2017 conference call
Flowsheet Monitoring is the ability to access all elements in a flowsheet without interfering with the flowsheet. Flowsheet Monitoring Components are software components that can be plugged into a flowsheet and have access to all thermodynamic property calculation methods, all Streams and all Unit Operations.
Moderator: wbarrett
Return to “Flowsheet Monitoring”
Jump to
- General
- ↳ Howto
- ↳ Process modelling and simulation
- Process Modelling Components
- ↳ ChemSep Property Package
- ↳ ChemSep Unit Operation
- ↳ COUSCOUS Unit Operations (AmsterCHEM)
- ↳ FlowExchange Unit Operation (AmsterCHEM)
- ↳ MATLAB Unit Operation (AmsterCHEM)
- ↳ Microsoft Excel Unit Operation (AmsterCHEM)
- ↳ Python Unit Operation (AmsterCHEM)
- ↳ REFPROP Property Package Manager (AmsterCHEM)
- ↳ Scilab Unit Operation (AmsterCHEM)
- ↳ TEA Thermodynamic server (AmsterCHEM)
- Process Modelling Environments
- ↳ Aspen Hysys (Aspen Technology Inc.)
- ↳ Aspen Plus (Aspen Technology Inc.)
- ↳ COCO (AmsterCHEM)
- ↳ DWSIM
- ↳ gPROMS (Process Systems Enterprise Ltd)
- ↳ Microsoft Excel Thermo Import (AmsterCHEM)
- ↳ Open Modelica
- ↳ PetroSim (KBC Advanced Technologies plc)
- ↳ PRO/II (AVEVA)
- ↳ ProSim Plus (ProSim SA)
- ↳ Python Thermo import (AmsterCHEM)
- ↳ Scilab Thermo import (AmsterCHEM)
- ↳ UniSim Design
- Implementation and development
- ↳ Distribution and installation
- ↳ Process Modelling Components
- ↳ Thermodynamic components
- ↳ Unit Operations
- ↳ Process Modelling Environments
- ↳ CAPE-OPEN Binary Interop Architecture
- CAPE-OPEN Interface specifications
- ↳ Common interfaces
- ↳ Parameters v1.0
- ↳ Business interfaces
- ↳ Thermodynamic v1.0
- ↳ Thermodynamic v1.1
- ↳ Unit Operations v1.0
- ↳ Flowsheet Monitoring
- ↳ Custom Data
- Activities of Special Interest Groups
- ↳ Methods & Tools SIG
- ↳ COBIA: CAPE-OPEN Object Model
- ↳ Flowsheet Monitoring
- ↳ Reporting Common interface
- ↳ Interop SIG
- ↳ Thermo SIG
- ↳ UNIT SIG
- Dissemination actions
- ↳ CAPE-OPEN 2019 Annual Meeting
- ↳ CAPE-OPEN 2018 Annual Meeting
- ↳ CAPE-OPEN 2017 Annual Meeting
- ↳ CAPE-OPEN 2016 Annual Meeting
- ↳ CAPE-OPEN 2013 Annual Meeting
- ↳ CAPE-OPEN 2012 Annual Meeting
- ↳ AIChE 2013 Annual Meeting
- ↳ AIChE 2012 Annual Meeting
- ↳ ICheaP-11
- ↳ ECCE-9
- News