CPL - Chalmers Publication Library
| Utbildning | Forskning | Styrkeområden | Om Chalmers | In English In English Ej inloggad.

The Application of a Multistage-Bed Model for Residence-Time Analysis in Chemical-Looping Combustion of Solid Fuel

Pontus Markström (Institutionen för energi och miljö, Energiteknik) ; Nicolas Berguerand (Institutionen för energi och miljö, Energiteknik) ; Anders Lyngfelt (Institutionen för energi och miljö, Energiteknik)
Chemical Engineering Science (0009-2509). Vol. 65 (2010), 18, p. 5055-5066.
[Artikel, refereegranskad vetenskaplig]

The behavior of a 10 kW chemical-looping combustor for solid fuels, normally operated in continuous mode, has been studied by addition of fuel batches. From analysis of gas leaving the air reactor, it was possible to determine the residence time and residence-time distribution of particles in the fuel reactor. Knowing the solids inventory in the fuel reactor, the circulation mass flow could be directly correlated to measured operational data, i.e. pressure drop, temperature and gas flow in air reactor riser. Using results for carbon-capture efficiency and residence-time distribution, a model was developed which could determine a mass-based reaction-rate constant for char conversion. The reaction-rate constant of a Mexican petroleum coke at both 950°C and 970°C was calculated to 8.2 wt%/min and 28.8 wt%/min, respectively. The reaction-rate constant of a South African coal at 950°C was calculated to 26.1 wt%/min. This reaction-rate constant could also be determined independently from the conversion rates of char during the batch tests. The results showed a good agreement between the two approaches, indicating that the model well describes the behavior of the unit. From the determination of the circulation mass flow, and comparison with previous testing with different circulation, it was also possible to estimate the limit for which the ilmenite was unable to supply sufficient oxygen to achieve good conversion. This limit was compared to theoretical limits for ilmenite as well as the limit set by a heat balance. It was concluded that the latter will be the one setting the limit.

Nyckelord: Chemical-looping combustion; Ilmenite; Solid fuel; CO2 capture; Residence time; Reaction rate

Denna post skapades 2010-02-09. Senast ändrad 2016-04-28.
CPL Pubid: 111749


Läs direkt!

Länk till annan sajt (kan kräva inloggning)

Institutioner (Chalmers)

Institutionen för energi och miljö, Energiteknik (2005-2017)


Kemisk energiteknik

Chalmers infrastruktur

Relaterade publikationer

Denna publikation ingår i:

Modeling Aspects of Chemical-Looping Combustion for Solid Fuels

Design, modelling and operation of a 100 kW chemical-looping combustor for solid fuels