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Oxy-fuel combustion study of biomass fuels in a 20 kWth fluidized bed combustor

Sher, Farooq; Pans, Miguel A.; Sun, Chenggong; Snape, Colin E.; Liu, Hao

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Authors

Farooq Sher

Miguel A. Pans

Chenggong Sun

COLIN SNAPE COLIN.SNAPE@NOTTINGHAM.AC.UK
Professor of Chemical Technology & Chemical Eng

HAO LIU LIU.HAO@NOTTINGHAM.AC.UK
Professor of Energy Engineering



Abstract

Oxy-fuel combustion is one of the promising carbon capture technologies considered to be suitable for future commercial applications with stationary combustion plants. Although more and more biomass and waste are now being burned in stationary combustion plants, research on oxy-fuel combustion of biomass has received much less attention in comparison to oxy-fuel combustion of coal. In this work, a series of tests was carried out in a 20?kWth fluidized bed combustor under oxy-fuel conditions firing two non-woody fuels (miscanthus and straw pellets) and one woody fuel (domestic wood pellet). The effects of the combustion atmosphere (air and oxy-fuel) and oxygen concentration in the oxidant of the oxy-fuel combustion on gas emissions and temperature profiles were systematically studied with the overall excess oxygen coefficient in the combustor being maintained roughly constant throughout the tests. The experimental results showed that replacing the air with an oxy-fuel oxidant of 21?vol% O2 and 79?vol% CO2 resulted in a significant decrease in combustion temperature and ultimately led to the extinction of the biomass flame due to the larger specific heat of CO2 compared to N2. To keep a similar temperature profile to that achieved under the air combustion conditions, the oxygen concentration in the oxidant of O2/CO2 mixture had to be increased to 30?vol%. A drastic decrease in CO emissions was observed for all three biomass fuels (up to 80% reduction when firing straw) under oxy-fuel combustion conditions providing that the oxygen concentration in the oxidant of O2/CO2 mixture was above 25?vol%. NOx emissions were found to decrease with the oxygen concentration in the oxy-fuel oxidant, due to i) the increase of bed temperature, which implies more volatile-N released and converted in the dense bed zone and ii) the less dilution of the gases inside the dense bed zone, which leads to a higher CO concentration in this region enhancing the reduction of NOx. Similar NOx emissions to those obtained with air combustion were found when the oxygen concentration in the oxy-fuel oxidant was kept at 30?vol%. Further analysis of the experimental results showed that the gas emissions when firing the non-woody fuels were controlled mainly by the freeboard temperature instead of the dense bed region temperature due to the characteristically high volatile matter content and fines of this kind of biomass fuels.

Citation

Sher, F., Pans, M. A., Sun, C., Snape, C. E., & Liu, H. (2018). Oxy-fuel combustion study of biomass fuels in a 20 kWth fluidized bed combustor. Fuel, 215, https://doi.org/10.1016/j.fuel.2017.11.039

Journal Article Type Article
Acceptance Date Nov 10, 2017
Online Publication Date Dec 22, 2017
Publication Date Mar 1, 2018
Deposit Date Nov 22, 2017
Publicly Available Date Dec 22, 2017
Journal Fuel
Print ISSN 0016-2361
Electronic ISSN 1873-7153
Publisher Elsevier
Peer Reviewed Peer Reviewed
Volume 215
DOI https://doi.org/10.1016/j.fuel.2017.11.039
Keywords Biomass combustion; Fluidized bed combustion; Oxy-fuel combustion; Carbon capture; Nox; CO emissions
Public URL https://nottingham-repository.worktribe.com/output/918455
Publisher URL http://www.sciencedirect.com/science/article/pii/S0016236117314369

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