Abstract:In this work, SO 2 retention via calcium-based sorbents added in a continuous bubbling 17 fluidized bed combustor (~3 kWth) operating in oxy-fuel combustion mode is analyzed. 18Tests were performed at different operating temperatures with three sorbents, two 19 limestones and one dolomite, and with three coals, ranging from lignite to anthracite, to 20 analyze the influence of coal rank, type of sorbent, sorbent particle size, and O 2 /CO 2 21 feeding ratio on the sulfation process. 22It was found that the com… Show more
“…5). Previous studies demonstrated that dolomites are able to reach high sulfation conversions, near 1 with respect to Ca content, both in calcining and noncalcining conditions during oxyfuel combustion in fluidized beds [24], as observed in Fig. 3.…”
Section: Effect Of Reaction Time On Product Layersupporting
The use of Ca-based sorbents in circulating fluidized beds (CFB) allows the in-situ desulfurization in oxy-fuel combustion processes. The sulfation process involves important changes in the sorbent morphology, which could vary depending on the operating conditions and be different to those observed in conventional air combustion. This work analyzes the morphological variations observed during limestone and dolomite sulfation at typical oxy-fuel combustion conditions (high CO 2 concentration, higher temperatures than in air combustion) in CFB combustors (long reaction times).
Sulfated samples prepared in a thermogravimetric analyzer were analyzed by Scanning ElectronMicroscope (SEM). The space limitations due to the higher molar volume of CaSO 4 compared to CaO in the external surface of the particles make that the CaSO 4 product layer trend to grow outwards to form a honeycomb-shaped structure. This structure appeared for limestone at both calcining and non-calcining conditions. A strong effect of the CaSO 4 sintering phenomenon was observed at temperatures above 950 ºC. Moreover, the honeycomb structure was never observed working with dolomite in spite of the high sulfation conversions reached with this sorbent. keywords: CO 2 capture, oxy-fuel combustion, fluidized bed, Ca-based sorbent, desulfurization.
“…5). Previous studies demonstrated that dolomites are able to reach high sulfation conversions, near 1 with respect to Ca content, both in calcining and noncalcining conditions during oxyfuel combustion in fluidized beds [24], as observed in Fig. 3.…”
Section: Effect Of Reaction Time On Product Layersupporting
The use of Ca-based sorbents in circulating fluidized beds (CFB) allows the in-situ desulfurization in oxy-fuel combustion processes. The sulfation process involves important changes in the sorbent morphology, which could vary depending on the operating conditions and be different to those observed in conventional air combustion. This work analyzes the morphological variations observed during limestone and dolomite sulfation at typical oxy-fuel combustion conditions (high CO 2 concentration, higher temperatures than in air combustion) in CFB combustors (long reaction times).
Sulfated samples prepared in a thermogravimetric analyzer were analyzed by Scanning ElectronMicroscope (SEM). The space limitations due to the higher molar volume of CaSO 4 compared to CaO in the external surface of the particles make that the CaSO 4 product layer trend to grow outwards to form a honeycomb-shaped structure. This structure appeared for limestone at both calcining and non-calcining conditions. A strong effect of the CaSO 4 sintering phenomenon was observed at temperatures above 950 ºC. Moreover, the honeycomb structure was never observed working with dolomite in spite of the high sulfation conversions reached with this sorbent. keywords: CO 2 capture, oxy-fuel combustion, fluidized bed, Ca-based sorbent, desulfurization.
“…There are several review papers (Buhre et al, 2005;Tan et al, 2005;Wall, 2007;Wall et al, 2009;Normann et al, 2009;Toftegaard et al, 2010;Davidson and Santos, 2010;Scheffknecht et al, 2011;Stanger and Wall, 2011;Chen et al, 2012;Lockwood, 2014) and books (Zheng, 2011;Toporov, 2014) published in the open literature. All of them have provided comprehensive information about the different aspects of oxy-PC combustion.…”
Section: Oxy-pc Power Plantmentioning
confidence: 99%
“…Simplified schematic flow diagram of oxy-PC coal fired power plant with CO2 capture, including possible locations for flue gas recirculation and O2 addition -adapted fromDavidson and Santos (2010).…”
“…Conversely, the N 2 O emission decreased with the increase in operating temperature. In a subsequent study, de las Obras‐Loscertales et al evaluated SO 2 retention by three different calcium‐based sorbents (a dolomite and two limestones). Tests were respectively performed with three different coal types (lignite, bituminous and anthracite) at different operating temperatures to evaluate the influence of sorbent type and particle size, coal rank, temperature and O 2 /CO 2 feed ratios on sulfation.…”
Section: Oxy Combustion In Fluidized Bedsmentioning
confidence: 99%
“…De las Obras‐Loscertales et al reported experimental results conducted in a 3 kWth BFB furnace under oxy‐combustion atmosphere, where sulfur retention through Ca‐based sorbents and the influence of coal rank were studied. The limestone was observed to have a greater sulfur retention capability when combustion temperature was increased to about 925 °C.…”
Presently, there is no detailed review that summarizes the current knowledge status on oxy-fuel combustion in fluidized bed combustors. This paper reviewed the existing literature in heat transfer, char combustion and pollutant emissions oxy-fuel combustion in fluidized beds, as well as modelling of oxy-fuel in FB boiler and gaps were identified for further research direction.
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