Sindy Heil
Institute of Energy Process Engineering and Chemical Engineering, TU Bergakademie Freiberg, Germany
Christian Brunhuber
Siemens AG, Energy Solutions
Kilian Link
Siemens AG, Energy Solutions
Julia Kittel
Institute of Energy Process Engineering and Chemical Engineering, TU Bergakademie Freiberg, Germany
Bernd Meyer
Institute of Energy Process Engineering and Chemical Engineering, TU Bergakademie Freiberg, Germany
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http://dx.doi.org/10.3384/ecp09430021Published in: Proceedings of the 7th International Modelica Conference; Como; Italy; 20-22 September 2009
Linköping Electronic Conference Proceedings 43:9, p. 77-85
Published: 2009-12-29
ISBN: 978-91-7393-513-5
ISSN: 1650-3686 (print), 1650-3740 (online)
This article describes dynamic models of the carbon dioxide (CO2) -removal units which are coupled with conventional models to form a complete model of an IGCC power plant with CO2 capture.
Therefore some components of the Modelica_Fluid 1.0 library and packages of the Modelica.Media library from Modelica 3.0 were used. Not yet available components were developed.
The results obtained with Dymola 7.1 were compared with steady state simulations calculated with other tools (ChemCAD and Aspen Plus) and a very good agreement was found.
[1] Holt; N.: Gasification Technology Status. Electric Power Research Institute EPRI; California USA; 2006
[2] Schoen; P.: Dynamic Modeling and Control of Integrated Coal Gasification Combined Cycle Units. PhD thesis; Faculty of Mechanical Engineering and Marine Technology; Technical University Delft; 1993
[3] Provost; G. T.; Erbes; M. R.; Zitney; S. E.; Phillips; J. N.; McClintock; M.; Stone; H. P.; Turton; R.; Quintrell; M.; Marasigan; J.: Generic Process Design and Control Strategies Used to Develop a Dynamic Model and Training Software for an IGCC Plant with CO2 Sequestration. International Pittsburgh Coal Conference; Pittsburgh; USA; 2008
[4] Casella; F.; Otter; M.; Proelss; K.; Richter; Ch.; Tummescheit; H.: The Modelica Fluid and Media library for modeling of incom- pressible and compressible thermo-fluid pipe networks. Proceedings of the 5th International Modelica Conference; Wien; 2006
[5] Haldor Topsoe: Sulphur resistant water-gas shift/sour shift; www.topsoe.com; 2009
[6] Perez; A. A. G.: Modelling of a Gas Turbine with Modelica. Department of Automatic Control; Lund Institute of Technology; 2001
[7] Kohl; A.; Nielsen; R.: Gas Purification: 5th Edition; Gulf Publishing Company; Houston; Texas; 1997
[8] National Institute of Standards and Technology (NIST) Chemistry WebBook; http://webbook.nist.gov/chemistry/formser.html (call date: 11-08-09)
[9] Felli; V.: Appendix C: Analysis and simulation of a rectisol-based acid gas purification process. In: A cost-benefit Assessment of Gasification-Based Biorefining in the Kraft Pulp and Paper Industry; 2006
[10] Schroedter; F.; Melzer; W.-M.; Knapp; H.: Investigation of phase equilibria in multi-component mixtures consisting of propane; carbon dioxide; water and various organic solvents. Gas Separation and Purification; Vol. 5; 1991
[11] Sattler; K.: Thermische Trennverfahren; Grundlagen; Auslegung; Apparate. 3. Auflage; WILEY-VCH; Weinheim; 2001
