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Tytuł artykułu

Analysis of the thermodynamic and economic efficiency of supercritical power unit with CFB boiler fed with lignite and air separation unit based on high-temperature membrane technology

Wybrane pełne teksty z tego czasopisma
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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
This paper presents a thermodynamic and economic analysis of the supercritical power unit with OXY type circulating fluidized bed boiler fed with lignite and air separation unit based on a three-end type high-temperature membrane. The fluidized bed boiler model is integrated with the installation of fuel drying, flue gas dehumidifier and the flue gas stream compression unit for further transportation. Models of the CFB boiler with fuel drying installation, air separation unit (ASU) and flue gas compression installation (CCS) were built using GateCycle™ computer program. For the fuel drying process the expanded nitrogen and oxygen mixture stream from the air separation unit was used. Thermodynamic analysis of the power unit assumed examining of certain characteristics of the block as a function of the oxygen recovery rate in the high-temperature membrane and selecting the appropriate calculation point for further economic analysis. Within the economic analysis for a selected operation point of the block the estimated capital expenditures and break-even price of electricity under the assumption that the net present value of investment (NPV) is equal to zero were determined.
Rocznik
Strony
308--313
Opis fizyczny
Bibliogr. 8 poz., rys., tab., wykr.
Twórcy
autor
  • Institute of Power Engineering and Turbomachinery, Silesian University of Technology, Gliwice, Poland
autor
  • Institute of Power Engineering and Turbomachinery, Silesian University of Technology, Gliwice, Poland
Bibliografia
  • [1] R. Castillo. Thermodynamic analysis of a hard coal oxyfuel power plant with high temperature three-end membrane for air separation. Applied Energy, 88:1480–1493, 2011.
  • [2] A. Dryjańska. Analiza sprawności elektrowni na parametry nadkrytyczne z cyrkulacyjnym kotłem fluidalnym typu oxy. Rynek Energii, 1(104):11–15, 2013.
  • [3] H. Stadler et al. Oxyfuel coal combustion by effcient integration of oxygen transport mmembrane. International Journal of Greenhouse Gas Control, 5:7–15, 2011.
  • [4] J. Kotowicz and A. Balicki. Method of increasing the efficiency of a supercritical lignite-fired oxy-type fluidized bed boiler and high-temperature three-end membrane for air separation. In Proceedings of the 25th International Conference ECOS, Perugia, Italy, 26-29 June 2012.
  • [5] J. Kotowicz and K. Janusz-Szymańska. Wpływ systemu separacji CO2 na efektywność elektrowni węglowej na parametry nadkrytyczne. Rynek Energii, 2(93):8–12, 2011.
  • [6] J. Kotowicz, A. Dryjańska, and A. Balicki. Wpływ wybranych parametrów na sprawność kotła cfb typu oxy. Rynek Energii, 2(99):120–126, 2012.
  • [7] Jarosław Milewski, R Bernat, and J. Lewandowski. Reducing co2 emissions from a gas turbine power plant by using a molten carbonate fuel cell. Proceedings of the World Congress on Engineering, 3, 2012.
  • [8] A. Skorek-Osikowska, Ł. Bartela, J. Kotowicz, and M. Job. Thermodynamic and economic analysis of the different variants of a coal-fired, 460 MW power plant using oxy-combustion technology. Energy Conversion and Management, 76:109–120, 2013.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-14b5da3d-3395-47a0-9f31-db67cfc8d026
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