2005
DOI: 10.1016/j.wasman.2004.12.014
|View full text |Cite
|
Sign up to set email alerts
|

Optimizing the APC residue washing process to minimize the release of chloride and heavy metals

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1

Citation Types

2
35
0
5

Year Published

2008
2008
2018
2018

Publication Types

Select...
6
3

Relationship

1
8

Authors

Journals

citations
Cited by 78 publications
(42 citation statements)
references
References 11 publications
2
35
0
5
Order By: Relevance
“…Some of the values given in the literature for CaO, SiO 2 , Al 2 O 3 , Fe 2 O 3 , MgO, Na 2 O, K 2 O, Ti 2 O, SO 3 , P 2 O 5 , MnO and ZnO are indicated in Table 3. Oxide compositions are also given in many other studies, such as Quina et al (2006), Qian et al (2006a,b), Park et al (2005), Carignan et al (2005), Chimenos et al (2005), Stegemann and Buenfeld (2003), Wang et al (2002Wang et al ( , 2004, Rémond et al (2002a), Nishida et al (2001), Polettini et al (2001), Haugsten and Gustavson (2000) and Derie (1996). Although oxide composition may vary, a very high alkali content is generally observed, mainly due to the calcium hydroxide or sodium carbonate usually used for acid gas removal.…”
Section: Characterization Of the Residuesmentioning
confidence: 91%
See 1 more Smart Citation
“…Some of the values given in the literature for CaO, SiO 2 , Al 2 O 3 , Fe 2 O 3 , MgO, Na 2 O, K 2 O, Ti 2 O, SO 3 , P 2 O 5 , MnO and ZnO are indicated in Table 3. Oxide compositions are also given in many other studies, such as Quina et al (2006), Qian et al (2006a,b), Park et al (2005), Carignan et al (2005), Chimenos et al (2005), Stegemann and Buenfeld (2003), Wang et al (2002Wang et al ( , 2004, Rémond et al (2002a), Nishida et al (2001), Polettini et al (2001), Haugsten and Gustavson (2000) and Derie (1996). Although oxide composition may vary, a very high alkali content is generally observed, mainly due to the calcium hydroxide or sodium carbonate usually used for acid gas removal.…”
Section: Characterization Of the Residuesmentioning
confidence: 91%
“…5): (1) Washing processes: The objective in this case is generally to remove the soluble salts by using water as a leachant. This process may be used as a first step in more elaborate methodologies (Chimenos et al, 2005;Mangialardi, 2003;Piantone et al, 2003;Nzihou and Sharrock, 2002;Krebs et al, 2001;Lundtorp et al, 2003;Derie, 1996;Mulder, 1996). Kirby and Rimstidt (1994) studied the dominant chemical reactions between water and a mixture of ESP and bottom ash (BA), and concluded that 10 kg of anhydrous salts can be obtained from a tonne of waste.…”
Section: Separation Methodsmentioning
confidence: 99%
“…The composition of APC fly ash strongly depends on the technology adopted. The semi-dry process used in the gas treatment is highly alkaline due to the lime grout added to neutralize the gases coming from the combustion chamber (Chimenos et al, 2005). High alkalinity promotes the leaching of strongly amphoteric heavy metals, such as lead and zinc (Polettini et al, 2001).…”
Section: Methodsmentioning
confidence: 99%
“…Separation techniques include washing and leaching of the FA by water [54,55] or by means of more sophisticated multiple step procedures [56]. On applying this method, chlorides can be extracted after solution evaporation and salts may be recovered [41,[57][58][59]. Several types of washing technique have been applied in particular for MSWI FA [60]; they displayed that it is possible to wash FA with water or with an acidic water solution.…”
Section: Advances In Materials Science and Engineeringmentioning
confidence: 99%