Abstract:Chemical looping
combustion (CLC) is one of the promising fuel
conversion technologies for carbon capture with low energy penalty.
Devolatilization is an important physical phenomenon occurring during
solid fuel CLC. Devolatilization behavior influences fragmentation,
combustion rate, emission, and particulates generation in fluidized
bed CLC (FB-CLC), thus a critical input for its design. Existing visual
techniques for determining devolatilization time cannot be applied
in CLC conditions because of its flamel… Show more
“…Pragadeesh and co-workers , focused their attention on the evaluation of the devolatilization timeboth for coal and biomassunder CLC conditions. In particular, they proposed a novel technique, called the “color indistinction method” (CIM), for the determination of the devolatilization time (τ d ) in FB-CLC.…”
Section: Effect Of Volatiles On
Bio-clcmentioning
confidence: 82%
“…Specifically, the devolatilization time was defined as the time period between the introduction of the fresh fuel particle into the bed and the time of its disappearance (Figure ). The CIM method successfully determined the devolatilization time of different types of fuel particles, in a range of particle sizes at different bed temperatures (Figure ), as validated by comparison with other techniques …”
Section: Effect Of Volatiles On
Bio-clcmentioning
confidence: 99%
“…Photographs of a 15 mm wood particle at different residence times during devolatilization under CLC conditions at 875 °C [Reproduced from ref . Copyright 2019 American Chemical Society].…”
Section: Effect Of Volatiles On
Bio-clcmentioning
confidence: 99%
“…Devolatilization time of (a) coal and (b) biomass for different particle sizes at 800, 875, and 950 °C [Reproduced from ref . Copyright 2019 American Chemical Society].…”
Section: Effect Of Volatiles On
Bio-clcmentioning
confidence: 99%
“…In addition, fuel particle characteristics have an important role to control, to a certain measure, the amount of unburnt volatiles: for small particles and high volatile contents, carbon slip to AR is almost negligible, but at the expense of lower volatiles conversion. 69 Pragadeesh and co-workers 103,104 focused their attention on the evaluation of the devolatilization timeboth for coal and biomassunder CLC conditions. In particular, they proposed a novel technique, called the "color indistinction method" (CIM), for the determination of the devolatilization time (τ d ) in FB-CLC.…”
Section: ■ Effect Of Volatiles On Bio-clcmentioning
Chemical looping
combustion of solid biomass has the unique potential
to generate energy with negative carbon emissions, while entailing
an energy penalty compared to traditional combustion that is lower
than that of the competing carbon capture technologies. In spite of
these attractive features, research is still needed to bring the technology
to a fully commercial level. The reason relies on a number of technological
challenges mostly related to the oxygen carrier performance, its possible
detrimental interaction with the biomass ash components, and the efficiency
of the gas–solid contact with the biomass volatiles. This review
is focused on these specific challenges which are particularly relevant
when firing biomass rather than coal in a solid-based chemical looping
combustion process. Special attention will be given to the most recent
findings published on these aspects. Related performance evaluation
by modeling, system integration, and techno-economic analysis will
also be briefly reviewed.
“…Pragadeesh and co-workers , focused their attention on the evaluation of the devolatilization timeboth for coal and biomassunder CLC conditions. In particular, they proposed a novel technique, called the “color indistinction method” (CIM), for the determination of the devolatilization time (τ d ) in FB-CLC.…”
Section: Effect Of Volatiles On
Bio-clcmentioning
confidence: 82%
“…Specifically, the devolatilization time was defined as the time period between the introduction of the fresh fuel particle into the bed and the time of its disappearance (Figure ). The CIM method successfully determined the devolatilization time of different types of fuel particles, in a range of particle sizes at different bed temperatures (Figure ), as validated by comparison with other techniques …”
Section: Effect Of Volatiles On
Bio-clcmentioning
confidence: 99%
“…Photographs of a 15 mm wood particle at different residence times during devolatilization under CLC conditions at 875 °C [Reproduced from ref . Copyright 2019 American Chemical Society].…”
Section: Effect Of Volatiles On
Bio-clcmentioning
confidence: 99%
“…Devolatilization time of (a) coal and (b) biomass for different particle sizes at 800, 875, and 950 °C [Reproduced from ref . Copyright 2019 American Chemical Society].…”
Section: Effect Of Volatiles On
Bio-clcmentioning
confidence: 99%
“…In addition, fuel particle characteristics have an important role to control, to a certain measure, the amount of unburnt volatiles: for small particles and high volatile contents, carbon slip to AR is almost negligible, but at the expense of lower volatiles conversion. 69 Pragadeesh and co-workers 103,104 focused their attention on the evaluation of the devolatilization timeboth for coal and biomassunder CLC conditions. In particular, they proposed a novel technique, called the "color indistinction method" (CIM), for the determination of the devolatilization time (τ d ) in FB-CLC.…”
Section: ■ Effect Of Volatiles On Bio-clcmentioning
Chemical looping
combustion of solid biomass has the unique potential
to generate energy with negative carbon emissions, while entailing
an energy penalty compared to traditional combustion that is lower
than that of the competing carbon capture technologies. In spite of
these attractive features, research is still needed to bring the technology
to a fully commercial level. The reason relies on a number of technological
challenges mostly related to the oxygen carrier performance, its possible
detrimental interaction with the biomass ash components, and the efficiency
of the gas–solid contact with the biomass volatiles. This review
is focused on these specific challenges which are particularly relevant
when firing biomass rather than coal in a solid-based chemical looping
combustion process. Special attention will be given to the most recent
findings published on these aspects. Related performance evaluation
by modeling, system integration, and techno-economic analysis will
also be briefly reviewed.
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