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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

邮发代号 80-973

2018 Impact Factor: 3.883

Frontiers of Environmental Science & Engineering  2019, Vol. 13 Issue (4): 49   https://doi.org/10.1007/s11783-019-1130-7
  本期目录
Combined Fenton process and sulfide precipitation for removal of heavy metals from industrial wastewater: Bench and pilot scale studies focusing on in-depth thallium removal
Huosheng Li1, Hongguo Zhang2, Jianyou Long3(), Ping Zhang4, Yongheng Chen1()
1. Institute of Environmental Studies at Greater Bay, Key Laboratory for Water Quality and Conservation of Pearl River Delta (Ministry of Education), Guangzhou University, Guangzhou 510006, China
2. Guangzhou University–Linköping University Research Center on Urban Sustainable Development, Guangzhou University, Guangzhou 510006, China
3. School of Environmental Science and Engineering, Guangzhou University, Guangzhou 510006, China
4. School of Chemistry and Chemical Engineering, Guangzhou University, Guangzhou 510006, China
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Abstract

Addition of alkali to pH 10 is effective for precipitation of precipitable metals.

Fenton treatment is effective for substantial removal of Tl, Cd, Cu, Pb, and Zn.

Sulfide precipitation is a final step for removal of trace Tl, Cd, Cu, Pb, and Zn.

Bench and pilot studies demonstrated the effectiveness of this combined technique.

Thallium (Tl) in industrial wastewater is a public health concern due to its extremely high toxicity. However, there has been limited research regarding Tl removal techniques and engineering practices to date. In this investigation, bench and pilot studies on advanced treatment of industrial wastewater to remove Tl to a trace level were conducted. The treatment process involved a combination of hydroxide precipitation, Fenton oxidation, and sulfide precipitation. While hydroxide precipitation was ineffective for Tl+ removal, it enabled the recovery of approximately 70%–80% of Zn as Zn hydroxide in alkaline conditions. The Fenton process provided good Tl removal (>95%) through oxidation and precipitation. Tl was then removed to trace levels (<1.0 µg/L) via sulfide precipitation. Effective removal of other heavy metals was also achieved, with Cd<13.4 µg/L, Cu<39.6 µg/L, Pb<5.32 µg/L, and Zn<357 µg/L detected in the effluent. X-ray photoelectron spectroscopy indicated that Tl2S precipitate formed due to sulfide precipitation. Other heavy metals were removed via the formation of metal hydroxides during hydroxide precipitation and Fenton treatment, as well as via the formation of metal sulfides during sulfide precipitation. This combined process provides a scalable approach for the in-depth removal of Tl and other heavy metals from industrial wastewater.

Key wordsThallium    Pilot    Fenton    Sulfide precipitation    Heavy metal    Industrial wastewater
收稿日期: 2018-12-25      出版日期: 2019-04-26
Corresponding Author(s): Jianyou Long,Yongheng Chen   
 引用本文:   
. [J]. Frontiers of Environmental Science & Engineering, 2019, 13(4): 49.
Huosheng Li, Hongguo Zhang, Jianyou Long, Ping Zhang, Yongheng Chen. Combined Fenton process and sulfide precipitation for removal of heavy metals from industrial wastewater: Bench and pilot scale studies focusing on in-depth thallium removal. Front. Environ. Sci. Eng., 2019, 13(4): 49.
 链接本文:  
https://academic.hep.com.cn/fese/CN/10.1007/s11783-019-1130-7
https://academic.hep.com.cn/fese/CN/Y2019/V13/I4/49
Metal ion Metal concentration (mg/L, Mean±SDa))
Low High
Na 360±14.3 4245±381
K 798±8.82 13390±277
Cd 24.8±3.60 680.5±32.2
Cu 1.59±0.281 2.69±0.0813
Pb 1.35±0.122 8.57±0.431
Zn 346±25.3 1446±16.7
Tl 0.272±0.0235 5.46±0.383
Tab.1  
Fig.1  
Fig.2  
Fig.3  
Fig.4  
Fig.5  
Wastewater Process Cd (mg/L) Cu (mg/L) Pb (mg/L) Zn (mg/L)
Low strength Raw 24.5±3.51 1.85±1.34 1.16±0.265 340±10.5
1st 2.39±1.13 303±9.31 a) 630±20.3 69.8±2.63
2nd 540±21.2 a) 60.3±2.46 a) 50.1±3.54 a) 450±10.6 a)
3rd 10.5±1.21a) 20.4±1.98 a) 2.18±0.134 a) 150±6.18 a)
Effluent 13.4±1.03 a) 15.1±1.25 a) 5.32±0.367 a) 135±5.37 a)
High strength Raw 713±30.8 2.70±1.07 8.57±0.387 1459±102
1st 49.0±2.96 1.90±0.351 2.39±0.187 314±21.6
2nd 80.4±2.37 a) 105±2.64 a) 21.6±1.47 a) 40.4±2.56
3rd 10.3±1.16 a) 20.3±2.73 a) 1.38±0.173 a) 451±30.7 a)
Effluent 10.4±0.597 a) 39.6±4.89 a) 1.45±0.357 a) 357±24.8 a)
Tab.2  
Fig.6  
Fig.7  
Reagents Price ($/t) Dosage (kt/m3) Cost ($/m3)
H2O2 384.62 0.0022 0.85
FeSO4 76.92 0.002 0.15
PAM 2461.54 0.000004 0.01
NaOH 615.38 0.002 1.23
Na2S 792.31 0.001 0.79
H2SO4 138.46 0.002 0.28
3.31 a)
Tab.3  
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