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US3652229A Expired / Lapsed US ⏱️ 0.0 years remaining

Apparatus for production of metal oxides

Assignee: ZANE L BURKE
•
Filing: 1969-03-12
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Granted: 1972-03-28
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Expires: 1989-03-12
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Abstract

Abstract Apparatus for use in a hydrometallurgical system for producing copper or zinc oxide. A closed evaporator tank partially is filled with mild ammonia hydroxide maintained between 214* and 218* F. by recirculation through a heat exchanger external to the evaporator. A pressure of between 5 and 10 p.s.i. is maintained in the evaporator. When a metal-rich ammonia carbonate solution formed by leaching copper or zinc in an oxygenated dissolver tank is injected onto the surface of the ammonia hydroxide, a rapid reaction takes place, causing precipitation of the desired oxide and evaporation of NH3, CO2 and water. The precipitated oxides may be removed either continuously or in batches from the evaporator. The evaporated gases are condensed and reused in the leach solution. Efficient oxygenation in the dissolver is achieved using a novel aerator comprising a hollow carbon rod.

Inventors

  • 👤 Zane L Burke

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 08:32
CPC Classifications
C; C01; C01G; C01G3/00; C01G3/02; C01G9/00; C01G9/02; C01P; C01P2004/00; C01P2004/60; C01P2004/61; C01P2006/00; C01P2006/10; Y; Y10; Y10S; Y10S261/00; Y10S261/72

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 22 words
An apparatus according to claim 1 wherein said evaporator tank comprises a closed vessel having controlled outlet means adjustable to maintain pressure.
Claim 2
Dependent Claim 15 words
An apparatus according to claim 2 wherein said controlled outlet means comprises a throttle valve.
Claim 3
Dependent Claim 50 words
An apparatus according to claim 1 wherein said injection means comprises a supply pipe extending through the wall of said evaporator tank and terminating in a nozzle permitting said metal-rich ammoniacal solution entering said tank through said pipe to drop from said nozzle onto the surface of said basic solution.
Claim 4
Dependent Claim 19 words
An apparatus according to claim 1 further comprising means for removing said precipitated metal oxide from said evaporator tank.
Claim 5
Dependent Claim 50 words
An apparatus according to claim 1 wherein said means for condensing and recovering comprises: a condenser communicating with said controlled outlet means, recovered liquid from said condenser having a temperature above about 130* F., and cooler means for reducing the temperature of said recovered liquid to below about 120* F.
Claim 6
Dependent Claim 26 words
An apparatus according to claim 1 further comprising means for controlling the feed rate of said metal-rich ammoniacal solution through said supply pipe and said nozzle.
Claim 7
Independent Claim 326 words
An apparatus for reducing a copper or zinc-rich ammonia carbonate pregnant solution to the corresponding copper or zinc oxide, said apparatus comprising: a dissolver tank containing copper or zinc source material and an ammonia carbonate solution initially containing few metal ions, means for recirculating said ammonia carbonate solution through said dissolver tank, an aerator for introducing and substantially uniformly distributing air or oxygen into said ammonia carbonate solution within said dissolver tank, whereby said copper or zinc and oxygen combine with said ammonia carbonate to form a cuprous/cupric or zinc pregnant solution, a closed evaporator tank having a generally conical bottom and a height at least one-third greater than its diameter, said tank being capable of withstanding an internal pressure of at least 15 p.s.i., said tank having a first outlet pipe adjacent the apex of said conical bottom for removal therethrough of said oxide, said tank having a second outlet pipe for removal therethrough of gases evaporated in said tank, said tank further having an inlet pipe for continuous injection of said pregnant solution into said tank, a portion of said tank being filled with a basic solution, means for transferring said pregnant solution to said evaporator tank inlet pipe, a heat exchanger external to said tank, pump means for forced recirculation of said basic solution through said heat exchanger and back to said tank below the liquid level therein, thereby maintaining the temperature of said basic solution between 214* and 218* F., throttle valve means controlling the flow of said evaporated gases through said second outlet pipe for maintaining a pressure within said tank of between 5 and 10 p.s.i., and a condenser communicating with said tank via said second outlet pipe, said condenser liquifying the ammonia, CO2 and water evaporated within said tank when said pregnant solution enters said basic solution, whereby pregnant solution injected through said inlet pipe will enter said heated basic solution, said oxide being formed in the resultant reaction.
Claim 8
Dependent Claim 49 words
An apparatus as defined in claim 8 wherein said aerator comprises: a hollow carbon element, and means for introducing air or oxygen under pressure into the hollow interior of said carbon element, said air or oxygen escaping through pores in said carbon in the form of multiple small bubbles.
Claim 9
Dependent Claim 13 words
An apparatus as defined in claim 9 wherein said carbon element is rod-shaped.
Claim 10
Dependent Claim 68 words
An apparatus as defined in claim 8 further comprising: an aeration tank, means for transferring said cuprous/cupric pregnant solution from said dissolver tank into said aeration tank, means for introducing sufficient oxygen into said cuprous/cupric pregnant solution in said aeration tank to convert the cuprous ions in said pregnant solution to cupric ions, and means for transferring the resultant cupric pregnant solution to said evaporator tank inlet pipe.
Claim 11
Dependent Claim 51 words
An apparatus as defined in claim 11 wherein said means for introducing comprises: a hollow carbon element, and means for introducing air or oxygen under pressure into the hollow interior of said carbon element, said air or oxygen escaping through pores in said carbon in the form of multiple small bubbles.
Claim 12
Independent Claim 273 words
A system for reducing metal oxide from a metal-rich ammoniacal liquor, said system comprising: a dissolver tank containing copper or zinc source material and an ammonia carbonate solution initially containing few metal ions, means for recirculating said ammonia carbonate solution through said dissolver tank, an aerator for introducing and substantially uniformly distributing air or oxygen into said ammonia carbonate solution within said dissolver tank, whereby said copper or zinc and oxygen combine with said ammonia carbonate to form a cuprous/cupric or zinc metal-rich ammoniacal liquor, a tank, a boiling ammonia hydroxide solution contained within said tank, a heat exchanger external to said evaporator tank and connected thereto by output and return pipes both terminating below the liquid level of said solution, pump means for forced recirculation of said solution through said heat exchanger to maintain said solution at a boiling temperature in the range of 212* to 225* F., controlled outlet means for maintaining the pressure within said evaporator tank at above about 5 p.s.i., injection means for continuously supplying said metal-rich ammoniacal liquor to said solution, the resultant reaction causing precipitation of said metal oxide, ammonia from said liquor replacing any evaporating from said solution so as to maintain the assay of said solution substantially constant during oxide reduction, an aeration tank, valved conduit means for transferring said metal-rich ammoniacal liquor from said dissolver tank directly to said injection means or via said aeration tank to said injection means, and a condenser communicating with said tank via said outlet means, said condenser liquifying the ammonia, CO2 and water evaporated within said tank when said metal-rich ammoniacal liquor is supplied to said solution.

References Cited (Backward Citations)

US682232A Cited
US1945281A Cited
US2318728A Cited
US2902342A Cited
US3186833A Cited
US3362458A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-03-28 1975-09-27 1976-03-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-03-28 1979-09-27 1980-03-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-03-28 1983-09-27 1984-03-28 $7700.00 Window Closed / Lapsed

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