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Dynamic Simulation and Investigation of the Startup Process of a Postcombustion-Capture Plant
Author(s) -
Thomas Marx-Schubach,
Gerhard Schmitz
Publication year - 2018
Publication title -
industrial and engineering chemistry research
Language(s) - English
Resource type - Journals
eISSN - 1520-5045
pISSN - 0888-5885
DOI - 10.1021/acs.iecr.8b03444
Subject(s) - reboiler , flue gas , power station , process engineering , environmental science , carbon dioxide , pilot plant , volumetric flow rate , process (computing) , process simulation , waste management , flow (mathematics) , computer science , chemistry , heat exchanger , engineering , mechanical engineering , thermodynamics , operating system , physics , geometry , mathematics , organic chemistry , electrical engineering
Carbon capture is an important possibility to reduce carbon dioxide emissions. To be able to study the startup process of such an amine-scrubbing process, a startup model of a postcombustion-capture plant (pcc-plant) was developed in the Modelica language and validated with measured data from a pilot plant in Heilbronn, Germany. Afterward, the process was scaled up in the model to handle the entire flue-gas flow of a 875 MW coal-fired power plant, resulting in three parallel capture plants. A case study was carried out to investigate the startup process of the pcc-plant in detail, indicating that the startup time increased drastically when the plant is operating at partial load. The startup time for a cold start from the beginning of steam flow to a 90% carbon-capture rate is t = 1900 s at full load and t = 11 075 s at 15% load. The total heat demand in the reboiler of one pcc-plant is 326 GJ at full load and 370 GJ at 15% load. Other results show that the startup time increases linearly with increasing t...

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