Skip to main content
Conference Proceedings

Eighth Mill Operators' Conference

Conference Proceedings

Eighth Mill Operators' Conference

PDF Add to cart

Fluorine Removal From Ok Tedi Copper/Gold Concentrates

The occurrence of fluorine in the copper/gold concentrates produced by Ok Tedi Mining Limited has provided a series of challenges to metallurgists since 1988. Although fluorine is distributed throughout the gangue minerals contained within Ok Tedi ores, its' presence in talc and phlogopite (naturally floating fluorosilicates) has proven to be the predominate sources of fluorine in the final concentrate. Initial treatment for the fluorosilicates consisted of the use of a carboxy-methyl cellulose depressant added to the flotation cleaners. This was superceded in 1998 with the installation of a fluorine reverse flotation process for the removal of naturally floating fluorosilicates from the final concentrate when the fluorine content of the final concentrate exceeds smelter-defined trigger points. The fluorine reverse process is similar to by-product molybdenite concentrate production in that sodium hydrosulfide is used to depress copper/gold flotation whilst allowing the fluorosilicates to float. The process was installed in two parallel modules (to match the existing grinding/flotation modules at Ok Tedi), each consisting of a closed rougher/cleaner circuit configuration. Both rougher and cleaner cells are Jameson Cells from MIM Process Technologies, with the selection based on both processing characteristics and available construction space. This paper discusses both the nature of fluorine in-, and its removal from-, Ok Tedi copper/gold concentrates.
Return to parent product
  • Fluorine Removal From Ok Tedi Copper/Gold Concentrates
    PDF
    This product is exclusive to Digital library subscription
  • Fluorine Removal From Ok Tedi Copper/Gold Concentrates
    PDF
    Normal price $22.00
    Member price from $0.00
    Add to cart

    Fees above are GST inclusive

PD Hours
Approved activity
  • Published: 2002
  • PDF Size: 0.205 Mb.
  • Unique ID: P200304009

Our site uses cookies

We use these to improve your browser experience. By continuing to use the website you agree to the use of cookies.