Reduction-melting combined with a Na₂CO₃ flux recycling process for lead recovery from cathode ray tube funnel glass

Copyright © 2014 Elsevier Ltd. All rights reserved.

Bibliographische Detailangaben
Veröffentlicht in:Waste management (New York, N.Y.). - 1999. - 34(2014), 8 vom: 01. Aug., Seite 1470-9
1. Verfasser: Okada, Takashi (VerfasserIn)
Weitere Verfasser: Yonezawa, Susumu
Format: Online-Aufsatz
Sprache:English
Veröffentlicht: 2014
Zugriff auf das übergeordnete Werk:Waste management (New York, N.Y.)
Schlagworte:Journal Article Cathode-ray tube Crystallization Phase separation Reduction–melting Sodium recovery Carbonates Ions Oxides Powders mehr... Silicates Sodium Compounds Carbon Dioxide 142M471B3J Lead 2P299V784P sodium oxide 3075U8R23D sodium carbonate 45P3261C7T Sodium 9NEZ333N27 sodium silicate IJF18F77L3
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100 1 |a Okada, Takashi  |e verfasserin  |4 aut 
245 1 0 |a Reduction-melting combined with a Na₂CO₃ flux recycling process for lead recovery from cathode ray tube funnel glass 
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500 |a Date Revised 19.11.2015 
500 |a published: Print-Electronic 
500 |a Citation Status MEDLINE 
520 |a Copyright © 2014 Elsevier Ltd. All rights reserved. 
520 |a With large quantity of flux (Na2CO3), lead can be recovered from the funnel glass of waste cathode-ray tubes via reduction-melting at 1000°C. To reduce flux cost, a technique to recover added flux from the generated oxide phase is also important in order to recycle the flux recovered from the reduction-melting process. In this study, the phase separation of sodium and the crystallization of water-soluble sodium silicates were induced after the reduction-melting process to enhance the leachability of sodium in the oxide phase and to extract the sodium from the phase for the recovery of Na2CO3 as flux. A reductive atmosphere promoted the phase separation and crystallization, and the leachability of sodium from the oxide phase was enhanced. The optimum temperature and treatment time for increasing the leachability were 700°C and 2h, respectively. After treatment, more than 90% of the sodium in the oxide phase was extracted in water. NaHCO3 can be recovered by carbonization of the solution containing sodium ions using carbon dioxide gas, decomposed to Na2CO3 at 50°C and recycled for use in the reduction-melting process 
650 4 |a Journal Article 
650 4 |a Cathode-ray tube 
650 4 |a Crystallization 
650 4 |a Phase separation 
650 4 |a Reduction–melting 
650 4 |a Sodium recovery 
650 7 |a Carbonates  |2 NLM 
650 7 |a Ions  |2 NLM 
650 7 |a Oxides  |2 NLM 
650 7 |a Powders  |2 NLM 
650 7 |a Silicates  |2 NLM 
650 7 |a Sodium Compounds  |2 NLM 
650 7 |a Carbon Dioxide  |2 NLM 
650 7 |a 142M471B3J  |2 NLM 
650 7 |a Lead  |2 NLM 
650 7 |a 2P299V784P  |2 NLM 
650 7 |a sodium oxide  |2 NLM 
650 7 |a 3075U8R23D  |2 NLM 
650 7 |a sodium carbonate  |2 NLM 
650 7 |a 45P3261C7T  |2 NLM 
650 7 |a Sodium  |2 NLM 
650 7 |a 9NEZ333N27  |2 NLM 
650 7 |a sodium silicate  |2 NLM 
650 7 |a IJF18F77L3  |2 NLM 
700 1 |a Yonezawa, Susumu  |e verfasserin  |4 aut 
773 0 8 |i Enthalten in  |t Waste management (New York, N.Y.)  |d 1999  |g 34(2014), 8 vom: 01. Aug., Seite 1470-9  |w (DE-627)NLM098197061  |x 1879-2456  |7 nnns 
773 1 8 |g volume:34  |g year:2014  |g number:8  |g day:01  |g month:08  |g pages:1470-9 
856 4 0 |u http://dx.doi.org/10.1016/j.wasman.2014.04.012  |3 Volltext 
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