Patent US3876516A successfully refreshed from Google Patents.
US3876516A
Expired / Lapsed
US
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Copper electrowinning process
Assignee: Consolidation Coal Co
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Filing: 1973-02-14
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Granted: 1975-04-08
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Expires: 1993-02-14
Abstract
Abstract A process and apparatus for electrowinning a high purity copper from an aqueous pregnant liquor acid electrolyte at high efficiency, and high current density in the presence of impurities. Electrolyte is circulated through an external loop system and upwardly between the anodes and cathodes. SO.sub.2, iron, and acid are added to the electrolyte in the external loop to maintain an SO.sub.2 concentration of at least 0.01g/l, an iron concentration of at least 1g/l, and an acid concentration of at least 5g/l as the electrolyte enters the tank. Preferred processes use iron and sulfur dioxide in the electrolyte and carbon electrodes.
Inventors
- 👤 Gerald F Pace
- 👤 Calvin N Armstrong
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 06:11
CPC Classifications
C; C25; C25C; C25C1/00; C25C1/12
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
245 words
A process for efficient electrolysis of an aqueous pregnant liquor electrolyte containing copper producing high purity copper, said process comprising circulating said electrolyte in an external loop electrolyte system from an electrowinning tank which contains the electrolyte and electrodes, at least one electrode being a cathode and at least one electrode being an anode, with the electrodes being immersed in said electrolyte and connected with a means for supplying electrical current so that electrical potential can be impressed between said anode and cathode electrodes through said electrolyte; said tank having parallel side walls substantially perpendicular to said electrodes; circulating said electrolyte through a distributor means in said electrowinning tank uniformly and upwardly between said electrodes overflowing along the entire length of said side walls; maintaining the temperature of said electrolyte above about 70.degree.F with a temperature control means in said external loop; adjusting in said external loop the residual concentration of SO.sub.2 iron, and acid to maintain a concentration of SO.sub.2 of at least about 0.01 gram per liter of electrolyte as it enters the tank, of iron of at least 1.0 g/l of electrolyte as it enters the tank, and of acid of at least 5 g/l of electrolyte as it enters the tank; impressing an electrical voltage of at least 0.4 volts between said anode and cathode electrodes through said electrolyte forming sulfuric acid at the anode and depositing high purity copper at the cathode; and recovering a coherent high purity copper product.
Claim 2
Dependent Claim
245 words
A process for efficient electrolysis of an aqueous pregnant liquor electrolyte containing copper producing high purity copper, said process comprising circulating said electrolyte in an external loop electrolyte system from an electrowinning tank which contains the electrolyte and electrodes, at least one electrode being a cathode and at least one electrode being an anode, with the electrodes being immersed in said electrolyte and connected with a means for supplying electrical current so that electrical potential can be impressed between said anode and cathode electrodes through said electrolyte; said tank having parallel side walls substantially perpendicular to said electrodes; circulating said electrolyte through a distributor means in said electrowinning tank uniformly and upwardly between said electrodes overflowing along the entire length of said side walls; maintaining the temperature of said electrolyte above about 70.degree.F with a temperature control means in said external loop; adjusting in said external loop the residual concentration of SO.sub.2 iron, and acid to maintain a concentration of SO.sub.2 of at least about 0.01 gram per liter of electrolyte as it enters the tank, of iron of at least 1.0 g/l of electrolyte as it enters the tank, and of acid of at least 5 g/l of electrolyte as it enters the tank; impressing an electrical voltage of at least 0.4 volts between said anode and cathode electrodes through said electrolyte forming sulfuric acid at the anode and depositing high purity copper at the cathode; and recovering a coherent high purity copper product.
Claim 3
Dependent Claim
31 words
A process of claim 1 wherein said electrolyte is circulated at a rate sufficient to prevent chemical polarization in the vicinity of said anode and cathode electrodes in said electrowinning tank.
Claim 4
Dependent Claim
48 words
A process of claim 1 wherein the carbon material of said anode electrode is selected from carbon black, coke or graphite and the metal of said anode electrode is selected from platinum, silver, gold, lead, mercury, tin, iron, chromium, zinc, aluminum, magnesium, antimony, silicon, titanium, and combination thereof.
Claim 5
Dependent Claim
136 words
A process of claim 1 for producing a copper product wherein the electrolyte system has an electrowinning tank of rectangular horizontal cross-section wherein the electrodes are substantially rectangular plates suspended in a vertical plane with supporting means at the upper edge of said electrodes which supports the electrodes from vertical tank side-walls which are substantially perpendicular to said electrodes; wherein electrolyte is circulated upwardly into said tank through a distributor means with jets located beneath said electrodes so that the upward electrolyte flow rate is substantially uniform along the side-walls of said tank and the electrolyte leaves said tank near the upper edge of said side-wall at a rate which is substantially uniform along the length of said tank and the electrolyte velocity at said jet is in the range of about 400-800 feet per second.
Claim 6
Dependent Claim
309 words
A process of claim 1 for efficient electrolysis by which coherent copper of high purity can be produced with high efficiency and high current density from an aqueous pregnant liquor electrolyte containing copper, said process comprising circulating said electrolyte through an external loop electrolyte system from an electrowinning tank which contains the electrolyte and electrodes, at least one electrode being a cathode and at least one electrode being an anode, with the electrodes being immersed in said electrolyte and connected with a means for supplying electrical current so that electrical potential can be impressed between said anode and cathode electrodes through said electrolyte; said electrolytic system having a temperature control means, an SO.sub.2 injection means and an electrolyte circulation means; said electrolyte being derived from an aqueous acid leach liquor with SO.sub.2 and iron being added; circulating said electrolyte through a distributor means in said electrowinning tank which circulates said electrolyte uniformly and upwardly between said electrodes by jetting said electrolyte between said electrodes from nozzles with a minimum fluid velocity at the nozzle of at least about 150 ft/sec with a volume calculated to completely displace said electrolyte in an electrolysis zone of the electrowinning tank in the vicinity of said electrodes once every 5 minutes; maintaining the temperature of said electrolyte above about 70.degree.F; adjusting the concentration in said loop to maintain a residual concentration of SO.sub.2 of at least about 0.01 g/l, to maintain an iron concentration of at least 1 g/l and to maintain an acid concentration of least 5 g/l in said electrolyte as it enters said electrowinning tank; impressing an electrical voltage of at least 0.4 volts between said anode and cathode electrodes through said electrolyte forming sulfuric acid at the anode and depositing copper at the cathode; and recovering substantially all of the copper as high purity copper product at the cathode.
Claim 7
Dependent Claim
161 words
IN A PROCESS FOR ELECTROWINNING BY WHICH COHERENT COPPER OF HIGH PURITY CAN BE PRODUCED WITH HIGH EFFECIENCY FROM AN AQUEOUS PREGNANT LIQUOR ELECTROLYTE, SAID ELECTROLYTE BEING PREPARED BY ACID LEACHING A COPPER ORE, THE IMPROVEMENT COMPRISING CIRCULATING SAID ELECTROLYTE THROUGH AN ESTERNAL LOOP ELECTROLYTE SYSTEM AND UPWARDLY BETWEEN AT LEAST ONE CATHODE AND AT LEAST ONE ANODE IMMERSED IN SAID ELECTROLYTE; ADJUSTING IN SAID EXTERNAL LOOP THE CONCENTRATION OF SO2 TO MAINTAIN RESIDUAL CONCENTRATION OF AT LEAST ABOUT 0.01 GRAM PER LITER OF ELECTROLYTE AS IT ENTERS THE TANK OF IRON TO MAINTAIN A CONCENTRATION OF AT LEAST 1.0 G/L OF ELECTROLYTE AS IT ENTERS THE TANK AND ACID TO MAINTAIN A CONCENTRATION OF AT LEAST 5 G/L OF ELECTROLYTE AS IT ENTERS THE TANK; MAINTAINING AN ELECTRICAL VOLTAGE DIFFERENTIAL BETWEEN SAID ANODE AND CATHODE OF AT LEAST 0.4 VOLTS, AND MAINTAINING THE TEMPERATURE OF THE ELECTROLYTE ABOVE ABOUT 70*F AND RECOVERING A COHERENT HIGH-PURITY COPPER PRODUCT AT THE CATHODE.
Claim 8
Dependent Claim
161 words
IN A PROCESS FOR ELECTROWINNING BY WHICH COHERENT COPPER OF HIGH PURITY CAN BE PRODUCED WITH HIGH EFFECIENCY FROM AN AQUEOUS PREGNANT LIQUOR ELECTROLYTE, SAID ELECTROLYTE BEING PREPARED BY ACID LEACHING A COPPER ORE, THE IMPROVEMENT COMPRISING CIRCULATING SAID ELECTROLYTE THROUGH AN ESTERNAL LOOP ELECTROLYTE SYSTEM AND UPWARDLY BETWEEN AT LEAST ONE CATHODE AND AT LEAST ONE ANODE IMMERSED IN SAID ELECTROLYTE; ADJUSTING IN SAID EXTERNAL LOOP THE CONCENTRATION OF SO2 TO MAINTAIN RESIDUAL CONCENTRATION OF AT LEAST ABOUT 0.01 GRAM PER LITER OF ELECTROLYTE AS IT ENTERS THE TANK OF IRON TO MAINTAIN A CONCENTRATION OF AT LEAST 1.0 G/L OF ELECTROLYTE AS IT ENTERS THE TANK AND ACID TO MAINTAIN A CONCENTRATION OF AT LEAST 5 G/L OF ELECTROLYTE AS IT ENTERS THE TANK; MAINTAINING AN ELECTRICAL VOLTAGE DIFFERENTIAL BETWEEN SAID ANODE AND CATHODE OF AT LEAST 0.4 VOLTS, AND MAINTAINING THE TEMPERATURE OF THE ELECTROLYTE ABOVE ABOUT 70*F AND RECOVERING A COHERENT HIGH-PURITY COPPER PRODUCT AT THE CATHODE.
Claim 9
Dependent Claim
28 words
A process of claim 6 wherein a concentration of iron of about at least 3.0 grams per liter is maintained by adjusting the iron concentration of said electrolyte.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1978-04-07 | 1978-10-07 | 1979-04-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-04-07 | 1982-10-07 | 1983-04-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-04-07 | 1986-10-07 | 1987-04-08 | $7700.00 | Window Closed / Lapsed |