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Technologies for control of sulfur and nitrogen compounds and particulates  157

           operating parameter, grinding the limestone finer resulted in further improvements in
           the SO 2 removal by up to 2.6% (Wang et al., 2005). With respect to sorbent injection
           technology, stream injections after desulfuration by limestone furnace injection have
           also been proposed. Adding stream enhances the heterogeneous condensation of
           fine particles, and they might be more easily removed from the flue gas using a
           high-efficiency demister. This technique also reduces the need for the particulate con-
           trol device downstream (Liu et al., 2011).
              Most of the research on flue gas desulfuration has been focused on the development
           of new adsorbents that can become competitive and marketable in midterm. Adsorbent
           properties such as SO 2 affinity, fast kinetics, high specific surface, and elevated resis-
           tance to multiple regenerations are desirable (Mathieu et al., 2013). Numerous adsor-
           bents have been proposed in the literature. In addition to conventional magnesium and
           calcium oxides, oxides supported by either carbonaceous materials or zeolites result in
           promising SO x adsorbents (Gaudin et al., 2015; Rodríguez et al., 2011; Yu et al.,
           2008).
              Efforts have been driven toward the evaluation of simultaneous abatement of SO x
           and NO x from flue gas derived from industrial processes. Novel sorbents and catalysts
           such as activated coke, the use of microwave reactors with ammonium bicarbonate
           combined with zeolites and electric corona discharge have been recently proposed
           as promising alternatives for combined SO x and NO x removal (Onda et al., 1997;
           Wei et al., 2009).


           6.2.3  Particles removal technologies
           6.2.3.1  What is particulate matter?

           Particulate matter (PM) is a complex mixture of extremely small particles and liquid
           droplets that get into the air. Once inhaled, these particles can affect the heart and lungs
           and cause serious health effects (EPA, 2017).
              The coal industry is facing stringent emission regulations to limit the release of par-
           ticulate matter. PM can contain SO 2 ,NO x , or VOC chemical species or their com-
           pounds, plus water and biogenic organic species. The chemical composition of PM
           varies with coal type, power plant design and location, and also with ambient condi-
           tions such as temperature and wind direction (Zhang, 2016). PM is usually classified
           by particle size because of the wide variation and complexity of its chemical compo-
           sition, which makes it complicated to elaborate a classification of it (Zhang, 2016):
           •  PM 1 particles less than 1 mm in diameter, known as ultrafine or submicron particles.
           •  PM 2.5 particles less than 2.5 mm in diameter, fine particles.
           •  PM 10 particles less than 10 mm in diameter, coarse particles.


           6.2.3.2  PM formation
           The largest particles, called the coarse particles, are mechanically produced by the
           breakup of larger solid particles. These particles can include wind-blown dust from
           agricultural processes, uncovered soil, unpaved roads, or mining operations. Traffic
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