LIU Qinwen, ZHONG Wenqi, LIU Xuejiao, et al. CO2 enrichment characteristics of coal/biomass fluidized oxy-fuel combustion[J]. CIESC Journal, 2018, (12): 5199-5208. DOI: 10.11949/j.issn.0438-1157.20180900.
DOI:
LIU Qinwen, ZHONG Wenqi, LIU Xuejiao, et al. CO2 enrichment characteristics of coal/biomass fluidized oxy-fuel combustion[J]. CIESC Journal, 2018, (12): 5199-5208. DOI: 10.11949/j.issn.0438-1157.20180900.DOI:
CO2 enrichment characteristics of coal/biomass fluidized oxy-fuel combustion
Oxy-fuel combustion with fluidized bed is one of the most promising carbon capture technologies. The oxy-fuel combustion of coal/biomass was simulated in a micro-fluidized bed reactor (inner diameter is 10 mm
combustion temperature is 700-900℃) coupled with an online mass spectrometry
to deeply understand the oxy-fuel combustion behavior. Bituminous coal and rosewood were selected as the samples. The effects of oxygen concentration
combustion temperature and mass ratio of coal to biomass on the combustion characteristics
i.e. the total reaction time
the initial reaction time
CO2 concentration in flue gas and the generation rate of CO2 during particle combustion
were investigated. It was found that the increment of oxygen volume fraction lead to an increase of CO2 yield
the decrease of total reaction time and CO2 concentration in the flue gas. Increasing the combustion temperature could enhance the enrichment of CO2
as a result higher CO2 production by particle combustion and CO2 concentration in the flue gas were obtained. Higher ratio of biomass advanced the initial reaction time and shortened the total reaction time
which resulted in a decrease of CO2 concentration in the flue gas and CO2 production by particle combustion but the rate of CO2 formation is increased.
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Absorption performance and stratification mechanism of biphasic CO2 absorbent[Bmim] [BF4]/MEA aqueous mixtures
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Chemical looping technology for clean and highly efficient coal processes
Chemical looping combustion of coal in a two-stage fuel reactor
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