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(MERAF) for the Base Metals Smelting Sector - CCME

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3.2.11. Noranda Inc., Division CCR, Montréal, Québec 90<br />

Figure 19 contains a schematic block flow diagram <strong>for</strong> <strong>the</strong> Copper Refinery<br />

showing <strong>the</strong> general sequence of <strong>the</strong> major unit operations, from <strong>the</strong> receipt of<br />

raw materials to <strong>the</strong> production of metals. When <strong>the</strong>se unit operations are<br />

referred to in <strong>the</strong> text, <strong>the</strong> corresponding words starts with an upper case letter.<br />

This diagram is highly simplified and is included solely to aid in <strong>the</strong> discussion<br />

and understanding of <strong>the</strong> pollution control at <strong>the</strong> facility.<br />

The refinery removes very small quantities of metal impurities from feed<br />

materials to produce high purity copper and o<strong>the</strong>r products. Most of <strong>the</strong> copper<br />

anodes to be refined are received from Noranda’s copper smelters at Rouyn-<br />

Noranda and Murdochville. Anodes are also produced from scrap purchased by<br />

<strong>the</strong> refinery and may be purchased from o<strong>the</strong>r copper producers or refined on a<br />

toll basis.<br />

Anodes are refined by electrorefining in which a solution of sulphuric acid is used<br />

as <strong>the</strong> electrolyte and direct current is applied to dissolve copper at <strong>the</strong> anode.<br />

Impurities including precious and platinum group metals are distributed between<br />

<strong>the</strong> electrolyte and <strong>the</strong> anode slimes. The copper cathode product is plated onto<br />

copper starting sheets. Electrolyte is continuously withdrawn <strong>for</strong> removal of<br />

nickel sulphate and o<strong>the</strong>r impurities such as arsenic, bismuth and antimony. The<br />

nickel sulphate is sold, <strong>the</strong> recovered sulphuric acid is re-used in <strong>the</strong> tankhouse<br />

and <strong>the</strong> impurities are recycled back to <strong>the</strong> smelters. Spent anodes are removed<br />

from <strong>the</strong> cells after 21 days while approximately half of <strong>the</strong> cathodes are removed<br />

from <strong>the</strong> cell every 10 or 11 days. A significant portion of <strong>the</strong> anode is not<br />

dissolved. Spent anodes are remelted and cast into new anodes <strong>for</strong><br />

reprocessing. Off-gases from melting and anode casting are treated by a<br />

baghouse prior to release to <strong>the</strong> atmosphere. Baghouse dust is returned to <strong>the</strong><br />

Horne smelter <strong>for</strong> recycling<br />

Some of <strong>the</strong> cathodes produced are melted and cast into copper billets or o<strong>the</strong>r<br />

shapes <strong>for</strong> <strong>the</strong> market, while most are sold directly. Off-gases from cathode<br />

melting and casting are not treated prior to release to <strong>the</strong> atmosphere.<br />

Anode slimes are washed from <strong>the</strong> spend anodes and removed from <strong>the</strong> cells <strong>for</strong><br />

fur<strong>the</strong>r processing to recover precious, platinum group and specialty metals. The<br />

slimes are first treated to remove tellurium and copper and <strong>the</strong>n smelted in a Top<br />

Blown Rotary Converter (TBRC). Solutions from <strong>the</strong> tellurium recovery stage are<br />

fur<strong>the</strong>r processed to produce metallic tellurium and copper sulphate.<br />

The TBRC produces Doré anodes which are fur<strong>the</strong>r refined to produce metallic<br />

silver, gold and a platinum-palladium concentrate. TBRC slags are milled and<br />

floated to recover a precious metals concentrate while <strong>the</strong> tailings are recycled to<br />

<strong>the</strong> Horne Smelter. Dust, and volatile metals and metal oxides leave <strong>the</strong> TBRC<br />

with <strong>the</strong> off-gas which is treated by wet scrubbing to remove dust and fume.<br />

90 Hatch Associates, Review of Environmental Releases <strong>for</strong> <strong>the</strong> <strong>Base</strong> <strong>Metals</strong> <strong>Smelting</strong> <strong>Sector</strong>,<br />

prepared <strong>for</strong> Environment Canada, dated November 2000<br />

86

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