共 141 条
- [91] Andrus H E, Chiu J H, Edberg C D, Et al., Alstom's chemical looping combustion prototype for CO<sub>2</sub> capture from existing pulverized coal-fired power plants, Office of Scientific and Technical Information (OSTI), (2012)
- [92] Soukup G, Pfeifer C, Kreuzeder A, Et al., In situ CO<sub>2</sub> capture in a dual fluidized bed biomass steam gasifier-bed material and fuel variation, Chemical Engineering & Technology, 32, 3, pp. 348-354, (2009)
- [93] Aghaalikhani A, Schmid J C, Borello D, Et al., Detailed modelling of biomass steam gasification in a dual fluidized bed gasifier with temperature variation, Renewable Energy, 143, pp. 703-718, (2019)
- [94] Fuchs J, Muller S, Schmid J C, Et al., A kinetic model of carbonation and calcination of limestone for sorption enhanced reforming of biomass, International Journal of Greenhouse Gas Control, 90, (2019)
- [95] Koppatz S, Pfeifer C, Rauch R, Et al., H<sub>2</sub> rich product gas by steam gasification of biomass with in situ CO<sub>2</sub> absorption in a dual fluidized bed system of 8 MW fuel input, Fuel Processing Technology, 90, 7, pp. 914-921, (2009)
- [96] Kraft S, Kuba M, Hofbauer H., The behavior of biomass and char particles in a dual fluidized bed gasification system, Powder Technology, 338, pp. 887-897, (2018)
- [97] Stollhof M, Penthor S, Mayer K, Et al., Influence of the loop seal fluidization on the operation of a fluidized bed reactor system, Powder Technology, 352, pp. 422-435, (2019)
- [98] Strohle J, Orth M, Epple B., Chemical looping combustion of hard coal in a 1 MW<sub>th</sub> pilot plant using ilmenite as oxygen carrier, Applied Energy, 157, pp. 288-294, (2015)
- [99] Thon A, Kramp M, Hartge E U, Et al., Operational experience with a system of coupled fluidized beds for chemical looping combustion of solid fuels using ilmenite as oxygen carrier, Applied Energy, 118, pp. 309-317, (2014)
- [100] Armbrust N, Duelli, Dieter H, Et al., Calcium looping cycle for hydrogen production from biomass gasification syngas: experimental investigation at a 20 kW<sub>th</sub> dual fluidized-bed facility, Industrial & Engineering Chemistry Research, 54, 21, pp. 5624-5634, (2015)