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The recovery of sulphuric acid from copper tankhouse electrolyte bleeds - a case study on the development of solvent extraction processes.

Authors :
Stevens G.W.
Minprex 2000 Melbourne, Victoria 11-Sep-0013-Sep-00
Gottliebsen K.
Stevens G.W.
Minprex 2000 Melbourne, Victoria 11-Sep-0013-Sep-00
Gottliebsen K.
Publication Year :
2000

Abstract

The copper solvent extraction-electrowinning process used at the Mount Gordon mine, North Queensland, produces a concentrated sulphuric acid tankhouse bleed. A solvent extraction process has been developed to recover sulphuric acid selectively using a branched long-chain aliphatic tertiary amine, tris(2-ethylhexyl)amine (TEHA), as extractant, Shellsol 2046 as diluent and octanol as modifier. Up to 90% of the sulphuric acid was recovered as a pure aqueous acid stream at a concentration of up to 130 g/l, which can be recycled to the tankhouse circuit. The raffinate's acid concentration was cut from 180 g/l to 18 g/l, reducing the environmental impact of waste disposal. Equilibrium data and simulation results were compared using an alternative extractant, CYANEX 923, a phosphine oxide; both extractants cold be used in the acid recovery process. Pilot scale investigations in a pulsed plate column with TEHA were used to scale the process for industrial application.<br />The copper solvent extraction-electrowinning process used at the Mount Gordon mine, North Queensland, produces a concentrated sulphuric acid tankhouse bleed. A solvent extraction process has been developed to recover sulphuric acid selectively using a branched long-chain aliphatic tertiary amine, tris(2-ethylhexyl)amine (TEHA), as extractant, Shellsol 2046 as diluent and octanol as modifier. Up to 90% of the sulphuric acid was recovered as a pure aqueous acid stream at a concentration of up to 130 g/l, which can be recycled to the tankhouse circuit. The raffinate's acid concentration was cut from 180 g/l to 18 g/l, reducing the environmental impact of waste disposal. Equilibrium data and simulation results were compared using an alternative extractant, CYANEX 923, a phosphine oxide; both extractants cold be used in the acid recovery process. Pilot scale investigations in a pulsed plate column with TEHA were used to scale the process for industrial application.

Details

Database :
OAIster
Notes :
und
Publication Type :
Electronic Resource
Accession number :
edsoai.on1309222646
Document Type :
Electronic Resource