(Facility) Copper Cliff Copper Smelter

Plant in Ontario, Canada with commodities Cobalt, Copper, Gold, Nickel, Silver, Sulfur, Sulfuric Acid

Geologic information

Identification information

Deposit ID 10229957
MAS/MILS ID 1220401001
Record type Site
Current site name (Facility) Copper Cliff Copper Smelter
Alternate or previous names Copper Cliff Smelter

Geographic coordinates

Point of reference Plant
Geographic coordinates: -80.99977, 46.49999 (WGS84)
Elevation 244
Location accuracy 1000(meters)
(click for info)

Geographic areas

Country State
Canada Ontario

Commodities

Commodity Importance
Cobalt Secondary
Copper Primary
Gold Secondary
Nickel Secondary
Silver Secondary
Sulfur, Sulfuric Acid Tertiary

Nearby scientific data

Plant (1) -80.99977, 46.49999

Economic information

Economic information about the deposit and operations

Operation type Processing Plant
Development status Plant
Commodity type Both metallic and non-metallic
Significant Yes
Plant type Smelter
Plant subcategory Smelter-Pyrometallurgy

Mineral rights holdings

Type of mineral rights Fee Ownership

Ownership information

  • Type Operator
    Owner Inco Metals Co., Ontario Division
    Home office Canada
    Year 1980
  • Type Owner
    Owner Inco Ltd.
    Interest 100
    Home office Canada
    Year 1980

Production statistics

  • Year 1980
    Description Copper Anodes 132000 Mt
    Importance Item Commodity Group Amount recovered Grade Recovery percentage
    Major Copper Copper 132,000mt
  • Year 1981
    Description Copper Anodes 111000 Mt
    Importance Item Commodity Group Amount recovered Grade Recovery percentage
    Major Copper Copper 111,000mt
  • Year 1982
    Description Copper Anodes 61000 Mt
    Importance Item Commodity Group Amount recovered Grade Recovery percentage
    Major Copper Copper 61,000mt
  • Year 1983
    Description Copper Anodes 67000 Mt
    Importance Item Commodity Group Amount recovered Grade Recovery percentage
    Major Copper Copper 67,000mt
  • Year 1984
    Description Copper Anodes 117000 Mt
    Importance Item Commodity Group Amount recovered Grade Recovery percentage
    Major Copper Copper 117,000mt

Comments on the reserve resource information

  • PART OF MAJOR CU-NI COMPLEX WITH INTERFLOW. CU CONC CAP 1500 MTPD. PRODUCTION RESTRICTED BY COMPLEX SO2 EMISSION LIMITS. TO REDUCE SO2 EMISS. BY 60% TO 265M MTPD BY 94 BY MAJOR CHANGES IN CU-NI PLANT.

Reference information

Links to other databases

Agency Database name Acronym Record ID Notes
U.S. Bureau of Mines Minerals Availability System MAS 1220401001

Bibliographic references

  • Production

    CHARLES RIVER ASSOCIATES SMELTER PROFILE, COPPER CLIFF

  • Production

    SMELTER, SEPTEMBER 9, 1986, P. 1.

  • Deposit

    CANADIAN MINES HANDBOOK 1979-80, PP. 136, 309.

  • Deposit

    PINCOCK, ALLEN & HOLT, INC.; THE DEVELOPMENT OF ENGINEERING,

  • Deposit

    OPERATING AND ENVIRONMENTAL COST DATA FOR INTERNATIONAL

  • Deposit

    COPPER SMELTING AND REFINING OPERATIONS - INCO LTD.,

  • Deposit

    COPPER CLIFF, ONTARIO, CANADA. BUMINES CONTRACT J0290007,

  • Deposit

    MAY 1990; FOR INF., CONTACT S.W. TOWLE, TPO, BUMINES

  • Deposit

    MAFO, DENVER, CO.

  • Deposit

    MINING WEEKLY, MARCH 2, 1992, P. 8.

General comments

Subject category Comment text
Deposit THE COPPER CLIFF SMELTER AND COPPER REFINERY ARE LOCATED AT SUDBURY, ONTARIO. THE OPERATIONS MAKE UP PART OF A LARGE COPPER/NICKEL MINING AND MILLING OPERATION IN THE SUDBURY AREA, CONSIDERED TO BE THE LARGEST IN THE WORLD. THE OPERATION PRODUCES NICKEL, COPPER, PRECIOUS METALS, COBALT, AND SULFURIC ACID. THE SMELTER OPERATION IS COMPLEX, SINCE MOST COPPER/NICKEL OPERATIONS PRODUCE A COMBINED WHITE METAL WHICH IS SEPARATED AT THE REFINERY; THIS SMELTER PRODUCES BOTH COPPER AND VARIOUS NICKEL PRODUCTS WITH INTERNAL PROCESS CROSS FLOWS, THUS IT IS DIFFICULT TO ESTABLISH A CLEAR CUT BREAK BETWEEN COPPER AND NICKEL IN TERMS OF COST OR ENERGY ANALYSES. THE PLANT WILL BE MODERNIZED OVER THE NEXT FOUR YEARS (AS OF 1990) IN ORDER TO ACHIEVE A 60% REDUCTION IN SULFER DIOXIDE EMISSIONS. OTHER CHANGES IN MILLING TECHNOLOGY AND SMELTER PROCESS FLOWS ARE ALSO PLANNED. THE SMELTER FACILITY PERFORMS SOME, BUT VERY LITTLE CUSTOM OR TOLL SMELTING. THE BASIC COPPER CIRCUIT CONSISTS OF DRYING THE COPPER CONCENTRATES FROM AN INITIAL MOISTURE CONTENT OF 8 TO 10%, TO A FINAL VALUE OF 0.1 TO 0.3% PRIOR TO FLASH SMELTING. THE DRIED CONCENTRATE IS SEPARATED FROM THE DRYER OFFGASES IN A BAGHOUSE WITH AN ESTIMATED EFFICIENCY OF 99.9% OFFGASES AND CONVERTER GASES ARE FURTHER CLEANED IN A HOT ELECTOSTATIC PRECIPITATOR. SILICA FLUX IS ADDED TO THE CONCENTRATES PRIOR TO DRYING TO MAXIMIZE BLENDING. THE DRIED FURNACE FEED IS STORED AT EACH END OF THE FURNACE IN SEPARATE BINS, WHICH IN TURN, FEED TWO CONCENTRATE BURNERS LOCATED AT EACH END OF THE FLASH FURNACE. THE FEED IS CARRIED FROM THE BINS BY SCREW CONVEYOR, AND DROPPED TO THE BURNER THROUGH SANKYO IMPACT MEASURING DEVICES, WHICH INDICATE THE FEED RATE TO THE BURNER. THE FLUXED CONCENTRATE FEED MIXTURE IS COMBUSTED AT EACH END OF THE FURNACE WITH PURE TECHNICAL OXYGEN (96%) WHICH MIXES WITH THE CONCENTRATES IN THE BURNER AND INJECTS T THE MIXTURE INTO THE FURNACE. THE LIMITATION ON THE RATIO OF O2 TO CONCENTRATE (0.22 TO 7.0) IS THE HEAT BALANCE AND AND PROTECTION OF THE FURNACE

Reporter information

Type Date Name Affiliation Comment
Reporter 09-JAN-1995 Towle, Stewart W. U.S. Bureau of Mines