Impact of SiO2 and CaO on Cr(VI) formation during heat treatment of Cr(III)-bearing sludge

There is a key issue about formation of highly toxic and easily dissoluble Cr(VI) during heat treatment of Cr-bearing solid waste, resulting in a prominent increase of environmental risk of incineration product. In this study, the effects of CaO and SiO 2 on formation and reduction of Cr(VI) were investigated during heating of Cr-bearing simulated sludge (Cr-SS) and Cr 2 O 3 , exploring Cr(III) oxidation mechanism. The findings indicates that doping CaO significantly promotes Cr(III) oxidation to Cr(VI), and chromium speciation vary with temperature. At 300℃, leaching amount of Cr(VI) in Cr-SS samples increases sharply to 9.3 % of total Cr. In contrast, no Cr(VI) was detected in Cr 2 O 3 samples. Above 300℃, oxidation rates of Cr(III) in different samples of Cr-SS and Cr 2 O 3 exhibit the same trend with temperature increasing. Above 1000℃, new Cr-containing crystalline phases were observed, like CaCr 2 O 4 and Ca 3 (CrO 4 ) 2 . The oxidation rate of Cr(III) is positively connected with the adding amount of CaO. Besides, doping SiO 2 to sludge prominently inhibits Cr(III) oxidation or facilitate Cr(VI) reduction at 600℃-1200℃, which is also confirmed by thermodynamic calculation, attributing to formation of Ca 5 Cr 2 SiO 12 and CaCr 2 O 4 . The number of holes in valence band will be changed through substitution of Cr(III) ions by cations of different valence states, thus facilitate or inhibit Cr(III) oxidation. The ions (<III) can promote Cr(III) oxidation, while ions (>III) can inhibit Cr(III) oxidation and promote Cr(VI) reduction. Introducing SiO 2 or Si-enriched materials to chromium-bearing wastes may be a promising alternative to solve the problem of highly toxic Cr(VI) formation during heat treatment. • Oxidation rate of Cr(III) is positively correlated with the adding amount of CaO. • Content of Cr(VI) in CaO and Cr-SS system reaches peak value at 300℃ and 900℃ respectively. • Multiple chromium species were detected, like CaCrO 4 , Ca 3 (CrO 4 ), CaCr 2 O 4 and Cr 2 O 3 . • Reducing the number of valence band holes of Cr 2 O 3 crystals can inhibit Cr(III) oxidation. • Introducing SiO 2 and controlling temperature are the effective strategies to inhibit Cr(VI) generation.

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Publication Details

Journal
Environmental Technology & Innovation
Published
2025-03-24
DOI
https://doi.org/10.1016/j.eti.2025.104167
Citations
3
Primary Topic
Adsorption and biosorption for pollutant removal
Type
article
Field-Weighted Citation Impact
2.45
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article

Impact of SiO2 and CaO on Cr(VI) formation during heat treatment of Cr(III)-bearing sludge

Jiangyong He, Xiaoyong Fan, Long Yan, Jian Li et al.
3 citations
Environmental Technology & Innovation
Adsorption and biosorption for pollutant removal
2.45
article

Impact of SiO2 and CaO on Cr(VI) formation during heat treatment of Cr(III)-bearing sludge

Jiangyong He, Xiaoyong Fan, Long Yan, Jian Li, Bi Yu Chen, Guohui Dong, Hongrui Ma, Shuaige Shi, Yonglin Yang
article en
3 citations

Abstract

There is a key issue about formation of highly toxic and easily dissoluble Cr(VI) during heat treatment of Cr-bearing solid waste, resulting in a prominent increase of environmental risk of incineration product. In this study, the effects of CaO and SiO 2 on formation and reduction of Cr(VI) were investigated during heating of Cr-bearing simulated sludge (Cr-SS) and Cr 2 O 3 , exploring Cr(III) oxidation mechanism. The findings indicates that doping CaO significantly promotes Cr(III) oxidation to Cr(VI), and chromium speciation vary with temperature. At 300℃, leaching amount of Cr(VI) in Cr-SS samples increases sharply to 9.3 % of total Cr. In contrast, no Cr(VI) was detected in Cr 2 O 3 samples. Above 300℃, oxidation rates of Cr(III) in different samples of Cr-SS and Cr 2 O 3 exhibit the same trend with temperature increasing. Above 1000℃, new Cr-containing crystalline phases were observed, like CaCr 2 O 4 and Ca 3 (CrO 4 ) 2 . The oxidation rate of Cr(III) is positively connected with the adding amount of CaO. Besides, doping SiO 2 to sludge prominently inhibits Cr(III) oxidation or facilitate Cr(VI) reduction at 600℃-1200℃, which is also confirmed by thermodynamic calculation, attributing to formation of Ca 5 Cr 2 SiO 12 and CaCr 2 O 4 . The number of holes in valence band will be changed through substitution of Cr(III) ions by cations of different valence states, thus facilitate or inhibit Cr(III) oxidation. The ions (<III) can promote Cr(III) oxidation, while ions (>III) can inhibit Cr(III) oxidation and promote Cr(VI) reduction. Introducing SiO 2 or Si-enriched materials to chromium-bearing wastes may be a promising alternative to solve the problem of highly toxic Cr(VI) formation during heat treatment. • Oxidation rate of Cr(III) is positively correlated with the adding amount of CaO. • Content of Cr(VI) in CaO and Cr-SS system reaches peak value at 300℃ and 900℃ respectively. • Multiple chromium species were detected, like CaCrO 4 , Ca 3 (CrO 4 ), CaCr 2 O 4 and Cr 2 O 3 . • Reducing the number of valence band holes of Cr 2 O 3 crystals can inhibit Cr(III) oxidation. • Introducing SiO 2 and controlling temperature are the effective strategies to inhibit Cr(VI) generation.

Environmental Technology & InnovationVol. 38
Yulin University (CN), Shaanxi University of Science and Technology (CN)
Clean water and sanitation
Openalex Percentile: Top 13%
Adsorption and biosorption for pollutant removal
2.45
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