Recovery of yttrium from fluorescent powder of cathode ray tube, CRT: Zn removal by sulphide precipitation

•Treatment of fluorescent powder of CRT waste.•Factorial experimental designs to study acid leaching of fluorescent powder and the purification of leach liquors.•Recover of yttrium by precipitation using oxalic acid.•Suitable flowsheet to recover yttrium from fluorescent powder. This work is focused...

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Published inWaste management (Elmsford) Vol. 33; no. 11; pp. 2364 - 2371
Main Authors Innocenzi, Valentina, De Michelis, Ida, Ferella, Francesco, Beolchini, Francesca, Kopacek, Bernd, Vegliò, Francesco
Format Journal Article
LanguageEnglish
Published Kidlington Elsevier Ltd 01.11.2013
Elsevier
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Abstract •Treatment of fluorescent powder of CRT waste.•Factorial experimental designs to study acid leaching of fluorescent powder and the purification of leach liquors.•Recover of yttrium by precipitation using oxalic acid.•Suitable flowsheet to recover yttrium from fluorescent powder. This work is focused on the recovery of yttrium and zinc from fluorescent powder of cathode ray tube (CRT). Metals are extracted by sulphuric acid in the presence of hydrogen peroxide. Leaching tests are carried out according to a 22 full factorial plan and the highest extraction yields for yttrium and zinc equal to 100% are observed under the following conditions: 3M of sulphuric acid, 10% v/v of H2O2 concentrated solution at 30% v/v, 10% w/w pulp density, 70°C and 3h of reaction. Two series of precipitation tests for zinc are carried out: a 22 full factorial design and a completely randomized factorial design. In these series the factors investigated are pH of solution during the precipitation and the amount of sodium sulphide added to precipitate zinc sulphide. The data of these tests are used to describe two empirical mathematical models for zinc and yttrium precipitation yields by regression analysis. The highest precipitation yields for zinc are obtained under the following conditions: pH equal to 2–2.5% and 10–12%v/v of Na2S concentrated solution at 10%w/v. In these conditions the coprecipitation of yttrium is of 15–20%. Finally further yttrium precipitation experiments by oxalic acid on the residual solutions, after removing of zinc, show that yttrium could be recovered and calcined to obtain the final product as yttrium oxide. The achieved results allow to propose a CRT recycling process based on leaching of fluorescent powder from cathode ray tube and recovery of yttrium oxide after removing of zinc by precipitation. The final recovery of yttrium is 75–80%.
AbstractList •Treatment of fluorescent powder of CRT waste.•Factorial experimental designs to study acid leaching of fluorescent powder and the purification of leach liquors.•Recover of yttrium by precipitation using oxalic acid.•Suitable flowsheet to recover yttrium from fluorescent powder. This work is focused on the recovery of yttrium and zinc from fluorescent powder of cathode ray tube (CRT). Metals are extracted by sulphuric acid in the presence of hydrogen peroxide. Leaching tests are carried out according to a 22 full factorial plan and the highest extraction yields for yttrium and zinc equal to 100% are observed under the following conditions: 3M of sulphuric acid, 10% v/v of H2O2 concentrated solution at 30% v/v, 10% w/w pulp density, 70°C and 3h of reaction. Two series of precipitation tests for zinc are carried out: a 22 full factorial design and a completely randomized factorial design. In these series the factors investigated are pH of solution during the precipitation and the amount of sodium sulphide added to precipitate zinc sulphide. The data of these tests are used to describe two empirical mathematical models for zinc and yttrium precipitation yields by regression analysis. The highest precipitation yields for zinc are obtained under the following conditions: pH equal to 2–2.5% and 10–12%v/v of Na2S concentrated solution at 10%w/v. In these conditions the coprecipitation of yttrium is of 15–20%. Finally further yttrium precipitation experiments by oxalic acid on the residual solutions, after removing of zinc, show that yttrium could be recovered and calcined to obtain the final product as yttrium oxide. The achieved results allow to propose a CRT recycling process based on leaching of fluorescent powder from cathode ray tube and recovery of yttrium oxide after removing of zinc by precipitation. The final recovery of yttrium is 75–80%.
This work is focused on the recovery of yttrium and zinc from fluorescent powder of cathode ray tube (CRT). Metals are extracted by sulphuric acid in the presence of hydrogen peroxide. Leaching tests are carried out according to a 2(2) full factorial plan and the highest extraction yields for yttrium and zinc equal to 100% are observed under the following conditions: 3M of sulphuric acid, 10% v/v of H2O2 concentrated solution at 30% v/v, 10% w/w pulp density, 70°C and 3h of reaction. Two series of precipitation tests for zinc are carried out: a 2(2) full factorial design and a completely randomized factorial design. In these series the factors investigated are pH of solution during the precipitation and the amount of sodium sulphide added to precipitate zinc sulphide. The data of these tests are used to describe two empirical mathematical models for zinc and yttrium precipitation yields by regression analysis. The highest precipitation yields for zinc are obtained under the following conditions: pH equal to 2-2.5% and 10-12%v/v of Na2S concentrated solution at 10%w/v. In these conditions the coprecipitation of yttrium is of 15-20%. Finally further yttrium precipitation experiments by oxalic acid on the residual solutions, after removing of zinc, show that yttrium could be recovered and calcined to obtain the final product as yttrium oxide. The achieved results allow to propose a CRT recycling process based on leaching of fluorescent powder from cathode ray tube and recovery of yttrium oxide after removing of zinc by precipitation. The final recovery of yttrium is 75-80%.
Highlights: • Treatment of fluorescent powder of CRT waste. • Factorial experimental designs to study acid leaching of fluorescent powder and the purification of leach liquors. • Recover of yttrium by precipitation using oxalic acid. • Suitable flowsheet to recover yttrium from fluorescent powder. - Abstract: This work is focused on the recovery of yttrium and zinc from fluorescent powder of cathode ray tube (CRT). Metals are extracted by sulphuric acid in the presence of hydrogen peroxide. Leaching tests are carried out according to a 2{sup 2} full factorial plan and the highest extraction yields for yttrium and zinc equal to 100% are observed under the following conditions: 3 M of sulphuric acid, 10% v/v of H{sub 2}O{sub 2} concentrated solution at 30% v/v, 10% w/w pulp density, 70 °C and 3 h of reaction. Two series of precipitation tests for zinc are carried out: a 2{sup 2} full factorial design and a completely randomized factorial design. In these series the factors investigated are pH of solution during the precipitation and the amount of sodium sulphide added to precipitate zinc sulphide. The data of these tests are used to describe two empirical mathematical models for zinc and yttrium precipitation yields by regression analysis. The highest precipitation yields for zinc are obtained under the following conditions: pH equal to 2–2.5% and 10–12% v/v of Na{sub 2}S concentrated solution at 10% w/v. In these conditions the coprecipitation of yttrium is of 15–20%. Finally further yttrium precipitation experiments by oxalic acid on the residual solutions, after removing of zinc, show that yttrium could be recovered and calcined to obtain the final product as yttrium oxide. The achieved results allow to propose a CRT recycling process based on leaching of fluorescent powder from cathode ray tube and recovery of yttrium oxide after removing of zinc by precipitation. The final recovery of yttrium is 75–80%.
Author Kopacek, Bernd
Innocenzi, Valentina
Ferella, Francesco
De Michelis, Ida
Beolchini, Francesca
Vegliò, Francesco
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Issue 11
Keywords Zinc removal
Cathode ray tubes (CRT)
Fluorescent powder
Yttrium
WEEE
Hydrogen peroxide
Cathode tube
Lixiviation
Regression analysis
Recycling
Mathematical model
Factorial design
Coprecipitation
Zinc
Language English
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Snippet •Treatment of fluorescent powder of CRT waste.•Factorial experimental designs to study acid leaching of fluorescent powder and the purification of leach...
This work is focused on the recovery of yttrium and zinc from fluorescent powder of cathode ray tube (CRT). Metals are extracted by sulphuric acid in the...
Highlights: • Treatment of fluorescent powder of CRT waste. • Factorial experimental designs to study acid leaching of fluorescent powder and the purification...
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SubjectTerms Applied sciences
Cathode Ray Tube
CATHODE RAY TUBES
Cathode ray tubes (CRT)
Chemical Precipitation
COPRECIPITATION
Electronic Waste
Exact sciences and technology
FLUORESCENCE
Fluorescent powder
HYDROGEN PEROXIDE
INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY
LEACHING
MATERIALS RECOVERY
Other wastes and particular components of wastes
OXALIC ACID
PH VALUE
Pollution
PURIFICATION
REGRESSION ANALYSIS
SODIUM SULFIDES
SOLUTIONS
Sulfides - chemistry
SULFURIC ACID
Waste Products - analysis
Wastes
WEEE
YTTRIUM
Yttrium - isolation & purification
YTTRIUM OXIDES
ZINC
Zinc - isolation & purification
Zinc removal
ZINC SULFIDES
Title Recovery of yttrium from fluorescent powder of cathode ray tube, CRT: Zn removal by sulphide precipitation
URI https://dx.doi.org/10.1016/j.wasman.2013.07.006
https://www.ncbi.nlm.nih.gov/pubmed/23910246
https://search.proquest.com/docview/1443418735
https://www.osti.gov/biblio/22300319
Volume 33
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