FBC desulfurization process using coal with low sulfur content, high oxidizing conditions and metamorphic limestones

A metamorphic limestone and a dolomite were employed as SO2 sorbents in the desulfurization of gas from coal combustion. The tests were performed in a fluidized bed reactor on a bench and pilot scale. Several parameters such as bed temperature, sorbent type, and sorbent particle size at different Ca...

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Main Authors: S. R. Bragança, J. L. Castellan
Format: Article
Language:English
Published: Brazilian Society of Chemical Engineering 2009-06-01
Series:Brazilian Journal of Chemical Engineering
Subjects:
Online Access:http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322009000200015
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spelling doaj-59ef560fc5974ed99d16d3bbe1d05a5e2020-11-24T22:21:24ZengBrazilian Society of Chemical EngineeringBrazilian Journal of Chemical Engineering0104-66321678-43832009-06-0126237538310.1590/S0104-66322009000200015FBC desulfurization process using coal with low sulfur content, high oxidizing conditions and metamorphic limestonesS. R. BragançaJ. L. CastellanA metamorphic limestone and a dolomite were employed as SO2 sorbents in the desulfurization of gas from coal combustion. The tests were performed in a fluidized bed reactor on a bench and pilot scale. Several parameters such as bed temperature, sorbent type, and sorbent particle size at different Ca/S molar ratios were analyzed. These parameters were evaluated for the combustion of coal with low-sulfur/high-ash content, experimental conditions of high air excess and high O2 level in fluidization air. Under these conditions, typical of furnaces, few published data can be found. In this work, a medium level of desulfurization efficiency (~60%) for Ca/S = 2 was obtained.http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322009000200015DesulfurizationLow SO2 concentrationCoalMetamorphic limestoneFluidized bed combustor
collection DOAJ
language English
format Article
sources DOAJ
author S. R. Bragança
J. L. Castellan
spellingShingle S. R. Bragança
J. L. Castellan
FBC desulfurization process using coal with low sulfur content, high oxidizing conditions and metamorphic limestones
Brazilian Journal of Chemical Engineering
Desulfurization
Low SO2 concentration
Coal
Metamorphic limestone
Fluidized bed combustor
author_facet S. R. Bragança
J. L. Castellan
author_sort S. R. Bragança
title FBC desulfurization process using coal with low sulfur content, high oxidizing conditions and metamorphic limestones
title_short FBC desulfurization process using coal with low sulfur content, high oxidizing conditions and metamorphic limestones
title_full FBC desulfurization process using coal with low sulfur content, high oxidizing conditions and metamorphic limestones
title_fullStr FBC desulfurization process using coal with low sulfur content, high oxidizing conditions and metamorphic limestones
title_full_unstemmed FBC desulfurization process using coal with low sulfur content, high oxidizing conditions and metamorphic limestones
title_sort fbc desulfurization process using coal with low sulfur content, high oxidizing conditions and metamorphic limestones
publisher Brazilian Society of Chemical Engineering
series Brazilian Journal of Chemical Engineering
issn 0104-6632
1678-4383
publishDate 2009-06-01
description A metamorphic limestone and a dolomite were employed as SO2 sorbents in the desulfurization of gas from coal combustion. The tests were performed in a fluidized bed reactor on a bench and pilot scale. Several parameters such as bed temperature, sorbent type, and sorbent particle size at different Ca/S molar ratios were analyzed. These parameters were evaluated for the combustion of coal with low-sulfur/high-ash content, experimental conditions of high air excess and high O2 level in fluidization air. Under these conditions, typical of furnaces, few published data can be found. In this work, a medium level of desulfurization efficiency (~60%) for Ca/S = 2 was obtained.
topic Desulfurization
Low SO2 concentration
Coal
Metamorphic limestone
Fluidized bed combustor
url http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322009000200015
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