CO2 capture by oxyfuel combustion
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F68407700%3A21220%2F18%3A00325201" target="_blank" >RIV/68407700:21220/18:00325201 - isvavai.cz</a>
Výsledek na webu
<a href="http://dx.doi.org/10.1007/978-981-13-3296-8_5" target="_blank" >http://dx.doi.org/10.1007/978-981-13-3296-8_5</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.1007/978-981-13-3296-8_5" target="_blank" >10.1007/978-981-13-3296-8_5</a>
Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
CO2 capture by oxyfuel combustion
Popis výsledku v původním jazyce
This chapter presents detailed description of oxyfuel combustion plant configuration, discusses specific features and differences between oxyfuel combustion and air combustion, and shows detailed numerical approach for establishing material balance of the oxyfuel combustion process. This numerical approach includes calculation of fluidization medium flow for the case of fluidized bed combustor. Based on experimental data, validation of the model is provided. The text discusses oxyfuel combustion in a fluidized bed, which is generally more complicated especially by the need to maintain proper fluidization conditions. A practical example of a change of the operation mode from air to oxyfuel in a fluidized bed combustor is presented. Last part of the chapter is dedicated to discussing the formation discussion of particular pollutants that need to be removed from the off-gas before the condensation of water vapor to obtain the final CO2 can be performed. The discussion concerns differences in processes of formation and possibilities of reduction of carbon monoxide, sulfur and nitrogen oxides that must be absent in the final CO2 due to the risk of liquid acids formation which can take place under high pressure.
Název v anglickém jazyce
CO2 capture by oxyfuel combustion
Popis výsledku anglicky
This chapter presents detailed description of oxyfuel combustion plant configuration, discusses specific features and differences between oxyfuel combustion and air combustion, and shows detailed numerical approach for establishing material balance of the oxyfuel combustion process. This numerical approach includes calculation of fluidization medium flow for the case of fluidized bed combustor. Based on experimental data, validation of the model is provided. The text discusses oxyfuel combustion in a fluidized bed, which is generally more complicated especially by the need to maintain proper fluidization conditions. A practical example of a change of the operation mode from air to oxyfuel in a fluidized bed combustor is presented. Last part of the chapter is dedicated to discussing the formation discussion of particular pollutants that need to be removed from the off-gas before the condensation of water vapor to obtain the final CO2 can be performed. The discussion concerns differences in processes of formation and possibilities of reduction of carbon monoxide, sulfur and nitrogen oxides that must be absent in the final CO2 due to the risk of liquid acids formation which can take place under high pressure.
Klasifikace
Druh
C - Kapitola v odborné knize
CEP obor
—
OECD FORD obor
20704 - Energy and fuels
Návaznosti výsledku
Projekt
<a href="/cs/project/EF16_019%2F0000753" target="_blank" >EF16_019/0000753: Centrum výzkumu nízkouhlíkových energetických technologií</a><br>
Návaznosti
P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)
Ostatní
Rok uplatnění
2018
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Údaje specifické pro druh výsledku
Název knihy nebo sborníku
CO2 Separation, Purification and Conversion to Chemicals and Fuels
ISBN
9789811332968
Počet stran výsledku
24
Strana od-do
55-78
Počet stran knihy
184
Název nakladatele
Springer Nature Singapore Pte Ltd.
Místo vydání
—
Kód UT WoS kapitoly
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