On the efficiency of alkali based sorbents for removal of coal-combustion generated SO₂ and biomass-combustion generated HC1

Acid gas emissions (e.g., SO<sub>2</sub>, HCl and NO<sub>x</sub>) from combustion of solid fuels, such as coal and biomass, have been associated with health-related issues and environmental degradation. As wet flue gas desulfurization is both space- and capital- intensive, in...

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Online Access:http://hdl.handle.net/2047/D20236953
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spelling ndltd-NEU--neu-cj82pd63s2021-05-27T05:11:33ZOn the efficiency of alkali based sorbents for removal of coal-combustion generated SO₂ and biomass-combustion generated HC1Acid gas emissions (e.g., SO<sub>2</sub>, HCl and NO<sub>x</sub>) from combustion of solid fuels, such as coal and biomass, have been associated with health-related issues and environmental degradation. As wet flue gas desulfurization is both space- and capital- intensive, in- furnace dry sorbent injection has been considered over the years to be a viable alternative. However, there is still uncertainty on the best selection of the sorbents for particular fuels and furnace operating conditions. The sulfur content of coals can vary widely from a fraction of 0.5 wt% to 7.5 wt% [1], while their chlorine contents are typically low (≤ 0.3 wt%) [2]. To the contrary the chlorine content of biomass can be high (as high as 0.66%) [3], whereas their sulfur content is typically low (≤ 0.2%) [1]. Since during combustion of solid fuels sulfur typically oxidizes to SO<sub>2</sub> and chlorine typically forms HCl, this study tested the effectiveness of various sorbents to capture the SO<sub>2</sub> emissions of coal and the HCl emissions of biomass. Different sorbents were co-fired with a high-sulfur bituminous coal (Illinois #6, containing 5.5% S) and a high- chlorine raw biomass (corn straw 0.63% Cl), respectively. The two fuels were pulverized to particles with sizes ranging from 75 to 150 μm, which were then blended with pulverized calcium-, sodium- and potassium-containing compounds, with particles ranging from 75 to150 μm, at different proportions. Combustion of the fuels occurred at high heating rates (10<sup>4</sup>4 -10<sup>5</sup> K/s) in a laboratory-scale electrically-heated drop-tube furnace, operated at 1400 K under fuel-lean conditions. The efficiency of different sorbents in reducing SO<sub>2</sub> and HCl emissions in the combustion effluents was evaluated and compared. Results showed that in the cased of both coal and biomass combustion the effectiveness of the alkali-based sorbents for either SO<sub>2</sub> or HCl acid gas removal was that potassium and sodium are better than calcium. Thermodynamic analysis on the reaction of the acid gases with the solid sorbents supported the experimental results.http://hdl.handle.net/2047/D20236953
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description Acid gas emissions (e.g., SO<sub>2</sub>, HCl and NO<sub>x</sub>) from combustion of solid fuels, such as coal and biomass, have been associated with health-related issues and environmental degradation. As wet flue gas desulfurization is both space- and capital- intensive, in- furnace dry sorbent injection has been considered over the years to be a viable alternative. However, there is still uncertainty on the best selection of the sorbents for particular fuels and furnace operating conditions. The sulfur content of coals can vary widely from a fraction of 0.5 wt% to 7.5 wt% [1], while their chlorine contents are typically low (≤ 0.3 wt%) [2]. To the contrary the chlorine content of biomass can be high (as high as 0.66%) [3], whereas their sulfur content is typically low (≤ 0.2%) [1]. Since during combustion of solid fuels sulfur typically oxidizes to SO<sub>2</sub> and chlorine typically forms HCl, this study tested the effectiveness of various sorbents to capture the SO<sub>2</sub> emissions of coal and the HCl emissions of biomass. Different sorbents were co-fired with a high-sulfur bituminous coal (Illinois #6, containing 5.5% S) and a high- chlorine raw biomass (corn straw 0.63% Cl), respectively. The two fuels were pulverized to particles with sizes ranging from 75 to 150 μm, which were then blended with pulverized calcium-, sodium- and potassium-containing compounds, with particles ranging from 75 to150 μm, at different proportions. Combustion of the fuels occurred at high heating rates (10<sup>4</sup>4 -10<sup>5</sup> K/s) in a laboratory-scale electrically-heated drop-tube furnace, operated at 1400 K under fuel-lean conditions. The efficiency of different sorbents in reducing SO<sub>2</sub> and HCl emissions in the combustion effluents was evaluated and compared. Results showed that in the cased of both coal and biomass combustion the effectiveness of the alkali-based sorbents for either SO<sub>2</sub> or HCl acid gas removal was that potassium and sodium are better than calcium. Thermodynamic analysis on the reaction of the acid gases with the solid sorbents supported the experimental results.
title On the efficiency of alkali based sorbents for removal of coal-combustion generated SO₂ and biomass-combustion generated HC1
spellingShingle On the efficiency of alkali based sorbents for removal of coal-combustion generated SO₂ and biomass-combustion generated HC1
title_short On the efficiency of alkali based sorbents for removal of coal-combustion generated SO₂ and biomass-combustion generated HC1
title_full On the efficiency of alkali based sorbents for removal of coal-combustion generated SO₂ and biomass-combustion generated HC1
title_fullStr On the efficiency of alkali based sorbents for removal of coal-combustion generated SO₂ and biomass-combustion generated HC1
title_full_unstemmed On the efficiency of alkali based sorbents for removal of coal-combustion generated SO₂ and biomass-combustion generated HC1
title_sort on the efficiency of alkali based sorbents for removal of coal-combustion generated so₂ and biomass-combustion generated hc1
publishDate
url http://hdl.handle.net/2047/D20236953
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