1992
DOI: 10.1016/0304-386x(92)90077-d
|View full text |Cite
|
Sign up to set email alerts
|

A hydrometallurgical process to treat carbon steel electric arc furnace dust

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1

Citation Types

0
12
0
2

Year Published

1995
1995
2020
2020

Publication Types

Select...
10

Relationship

0
10

Authors

Journals

citations
Cited by 50 publications
(14 citation statements)
references
References 1 publication
0
12
0
2
Order By: Relevance
“…During the meltdown of scrap, volatile components are fumed off and are collected with particulate matter in the off-gas cleaning system [1,2]. During the metal fusing process, the electric arc furnace (EAF) can reach temperatures of 1600 • C, or even higher, and many components of the charge, including iron, zinc, and lead, are volatilized and entered the vapour phase.…”
Section: Introductionmentioning
confidence: 99%
“…During the meltdown of scrap, volatile components are fumed off and are collected with particulate matter in the off-gas cleaning system [1,2]. During the metal fusing process, the electric arc furnace (EAF) can reach temperatures of 1600 • C, or even higher, and many components of the charge, including iron, zinc, and lead, are volatilized and entered the vapour phase.…”
Section: Introductionmentioning
confidence: 99%
“…In alkaline leaching processes as Amax or Cebedau [24,25] heavy metals like zinc, lead and other are leached in alkaline media whereas iron is not. In acidic processes, the EAF dust is leached by acetic acid [18,26], sulphuric acid [27,28] or hydrochloric acid [29,30]. Several pilot plants were built to test hydrometallurgical technologies such as the Ezinex process [31].…”
Section: Introductionmentioning
confidence: 99%
“…The concentrations of Cu, Zn, Mn, and Fe were 1.45, 0.18, 0.20, and 9.31 g/L, respectively, which are significantly greater than those published in previous reports (Pepe et al, 2007). The metal recovery from the leaching filtrate was preceded by fractional precipitation with the addition of different chemical agents (Barrnitt et al, 1992;Xie et al, 2005). At first, the pH of the leaching filtrate was adjusted to 3.0 with the addition of Ca(OH) 2 to recover Fe as hydroxide.…”
Section: Metal Recovery From the Leachatementioning
confidence: 99%