|Publication number||US3169856 A|
|Publication date||Feb 16, 1965|
|Filing date||May 22, 1962|
|Priority date||May 22, 1962|
|Publication number||US 3169856 A, US 3169856A, US-A-3169856, US3169856 A, US3169856A|
|Inventors||John L Mero|
|Original Assignee||John L Mero|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (4), Referenced by (22), Classifications (11)|
|External Links: USPTO, USPTO Assignment, Espacenet|
Feb. 16, 1965 J 3,169,856
l L. MERO PROCESS FOR SEPARA'I: ON OF NICKEL FROM COBALT IN OCEAN FLOOR MANGANIFEROUS ORE DEPOSITS Filed May 22, 1962.
GRAPH SHOWING COMPARATIVE LEACHING RATES OF MANGANESE AND OF IRON MINERALS LEACHING CURVE FOR Ni-Cu IN Mn PHASE I Mn-Ni LEACHING CUT OFF POINT PERCENT OF METALS LEACHED LEACHING CURVE FOR Co IN Fe PHASE INVENTOR JOHN L. MERO ATTORNEY$ United States Patent 0,
PROCESS FOR SEPARATION OF NECKEL FROM COBALT IN OCEAN FLOOR MANGANKFEROUS ORE DEPOSITS John L. Mero, Berkeley, Caiii. (1091 Via Robles, Lafayette, Calif.) Filed May 22, 1962, Ser. No. 196,777 4 Claims. (ill. 751l9) My invention relates to a process for recovering nickel, cobalt and other metals from ocean floor m'anganiferous ore deposits, and more particularly relates to a process of separating the nickel from the cobalt found in ocean floor manganiferous deposits.
Although termed manganese deposits or manganiferous ore deposits by virtue of the fact that manganese, on a weight basis, is most frequently the major metallic constit- "uent of these ore deposits, the ocean floor mineral deposits contain many other elements of economic interest as shown in the following table:
MAXIMUM, MINIMUM, AND AVERAGE WEIGHT PERCENTAGES OF 27 ELEMENTS IN MANGA- NESE DEPOSITS FROM THE PACIFIC AND AT- LANTIC OCEANS Weight percentages (dry weight basis) Pacific Ocean-Statistics Atlantic Ocea.nStatison 54 Samples ties on 4 Samples Element Minimum Minimum Maximum Average Average 1 As determined by X-ray emission spectrography.
2 Average of 5 samples in which Ag was detected.
3 L.O.I.=L0ss on ignition at 1,100 F. for one hour. The L.O.I. fig ures are based on a total weight of air-dried sample basis.
Ocean floor mineral deposits containing substantial amounts of manganese, nickel, cobalt, and copper were discovered in 1873 by the British Oceanographic Challenger Expedition. Subsequent oceanographic expeditions have recovered samples of these deposits from many 3,169,855 Patented Feb. 16, 1965 Of the many ingredients making up such ore deposits, nickel and cobalt are emphasized because, firom an economic standpoint, they are the most significant metals in most of these sea floor ores. Other metals, normally present, will be recovered as by-products in the production of nickel and cobalt.
Known methods of separating nickel and cobalt as found in natural ores, generally depend on some method of indiscriminately leaching these elements and separating the same after they are in solution together. Such nickelcobalt separations, however, are rather diflicult and expensive to carry out.
The mining of the vast reserves of manganiferous deposits lying over the ocean floor, can best be economically justified, were a more economical process avail-able to efiect a separation and ultimate recovery of the nickel and cob-alt elements.
Accordingly, among the objects of my invention are:
(1) To provide a novel and improved process of separating the nickel from the cobalt as found in ocean floor manganiferous deposits;
(2) Toprovide a novel and improved process of separating the nickel from the cobalt as found in ocean floor manganiferous deposits, which process shall be simple and straight-forward;
' (3) To provide a novel and improved process for separating the nickel from the cobalt as found in ocean floor deposits, which process, at the same time facilitates the recovery of the many other elements involved in such deposits.
(4) To provide a novel and improved process for separating the nickel from the cobalt as found in ocean floor deposits, which process provide-ssimple but accunate controls for indicating substantially complete separation of such elements from each other.
Additional objects of my invention will be described in conjunction with the accompanying drawing wherein the figure is a graph depicting the principle underlying the present invention.
Following intensive investigation of these ocean floor mineral deposits, I have discovered them to consist of several separate mineral. phases of manganese and of iron. These separate mineral crystallites of manganese and of iron are so fine-grained and so intimately mixed that no known physical process can be employed to separate them. The minor metallic consituents of the ocen floor manganifenou deposits, such as nickel, cobalt, and co er and other elements, are localized in different mineral phases of this material, some elements being contained in the manganese mineral phases and others in the iron mineral phases.
I have found, through my extensive investigations, that the nickel and copper are contained in the manganese mineral phase of this material, apparently in solid solution in the manganese minerals. Cobalt, on the other hand, I have discovered to exist in the iron mineral phases of this material to the exclusion of the manganese phase. This is unlike the situation existing in connection with conventional ore involving nickel and cobalt, in which ores, when the nickel and cobalt are intimately mixed, must be indiscriminately leached from the ore, as the first step in effecting a separation thereof, but which step, unfortunately places them both in solution together, which in turn raises the problem of separation of the nickel from the cobalt.
The present invention is predicated upon the aforementioned discovery of mine relating to the phase characteristics of the ocean floor mineral deposits under consideration herein, and basically involves a process for differentially leaching these metals from the manganiferous ore beiore they are both in solution together, which process is made possible by such discovery.
To accomplish such separation of the nickel room the cobalt in the mangani-ferous deposits found on the ocean floor, the ore is first crushed preferably to about minus forty mesh. The crushed ore material is then mixed with water to form an aqueous slurry which consists of not more than about 40 pence'nt of crushed ore by weight. The amount of crushed ore in this slurry is not critical but should be sufficient'to allow the mixture to act fluid. Leaching gases, which may be sulphur dioxide, nitrogen dioxide or other gases that reduce manganese and iron oxides of a high oxidation state, are then mixed with the aqueou slurry. This may be accomplished by percolating the gas up through the slurry while maintaining the slurry in a constant state of agitation. When the slurry is thus exposed to the gas, the manganese along with the nickel, copper and other mineral elements bound up in the manthe cobalt or iron content of the resulting solution begins ganese phase of the ore, will go into solution in accordance V with the leaching curve of the drawing, designated as Leaching Curve for Ni'-Cu in Mn Phase, while the iron along with the cobalt bound up in the iron phase,
nickel, copper and such other elements in the manganese phase, will go into solution before any appreciable amounts I of thecobalt and such other elements as may be bound up in the i-ronphase; After all the available manganese, nickel, copper, etc., are in solution, additional amounts of gas added to the aqueous slurry, will cause a change in the pH of the slurry toward the'acidic andonly then will much of the cobalt or iron start to dissolve. 1 It is at this point, that the process is stopped and the separation effected, because at this point, the nickel and associated elements are all in solution, while the cobalt and its associated elements are still in solid state. This critical point can thus be controlled by continuous monitoring of the pH of the aqueous slurry.
Another indication of the complete dissolution of the i nickel and other metals associated in the manganese phase,
will be the evolution of leaching gas from the top of the leaching cell. Evolution of such leaching gas or the sudden change in the pH of the slurry, therefore, can be used as controls to prevent the dissolving of the cobalt and other elements associated with the iron phase in the ore material.
This leaching proces may be batch-wise or continuous. At the completion of the leaching operation in a batch process, the leaching gases are stopped and the solution is separated from the tailings. In a continuous process, solution would be continuously drawn off, ore, leaching gases, and Water continuously added and the tailings continuously removed. The pH of the solution and the evolution of leaching gases would be closely monitored to deter mine the rate at which new slurry is added to the system and the rate at which solution is withdrawn.
The amount of leaching gas required. to complete the dissolution of the, elements in the manganese phase can be determined byca'lculatiombut, in practice, a small excess of gas, isalways required to assure complete dissolution of the manganese, nickel, copper, etc., and thecontrols previously described, are of practical value in determining when these elements have been completely dissolved;
'The rate. at which the manganese, nickel, and associated elements are dissolved will depend somewhat on the tempe'rature, pressure, and agitation of the slurry, but such variables are not critical nor essential features of the process constituting the present invention.
There need be no external control of the pH of the from the cobalt.
to rise rapidly, as illustratedinthe drawing.
' The iron-cobalt tails are then removed from the vessel, dewatered, filtered, and washed,and then treated in a standard manner withacid to leach the cobalt from the iron. The leaching of the cobalt from the iron with acid is a standard process in the metallurgical industry;
The solution of manganese, nickel, copper, etc., can be treated with hydrogen sulphide to precipitate the copper, which is then separated from the remaining manganesenickel solution by standard dewatering and filtering'techniques. Nickel can then be'separated from the manganese by precipitation with hydrogen gas, or the manganese can be firstseparated from the nickel by differential thermal reduction. The separation of the nickel. from the manganese or the manganese from the nickel would be'conducted according to standard procedures. 1
The make up of the manganiferous ores found strewn over the ocean floor, lends itself to other methods of differentially leaching to eifect separation of the nickel One such additional'method which comes to mind, involvessubjecting the ore material to preleaching reduction roasts, The common factor in carrying out the present process, however, is to effect a While I have described my invention in its preferredform and in considerable detail, it will be apparentthat the same is subject to alteration and modification without departing from the underlying principles involved, sear,
1. The method of separating the nickel from cobalt in ocean floor manganiferous deposits, in which the nickel is present in a manganese oxide phase and the cobalt in an iron oxide phase, comprising, breaking up such ore, V I, leaching under reducing conditions in a solution the manganese phase and'included nickel fronljthe iron phase including the cobalt, then removing such manganese phase in solution before any appreciable amount of the elements in the iron phase are dissolved, and processing the same to remove the nickel,
V to remove the cobalt. 2. The method of separating the nickel from cobalt in H ocean floor manganiferous deposits, in which the nickel is present in a manganese oxide phase and the cobaltin an iron oxide phase, comprising,
breaking up. such ore, mixing'said ore in its broken up state with water' to form a slurry,
mixing with said slurry a leachingagent capable of reducing manganese and iron oxides, continuing the addition. of such leaching agent and halting the same before any appreciable amount of the elements in the iron'phase are dissolved, and
then removing the solutionot manganese, and nickel is present in a manganese oxide phase and the'cobalt in,
an iron oxide phase, comprising,
crushing such ore to about minus forty mesh,
and separately processing the iron phase remaining,
mixing said ore in its crushed state with water to form an aqueous slurry,
mixing with said slurry a reducing and leaching agent capable in the presence of water of reducing manan aqueous slurry,
mixing with said slurry a reducing and leaching gas capable in the presence of water of reducing manganese and iron oxides,
continuing the addition of such leaching gas and haltganese and iron oxides, 5 ing the same before any appreciable amount of the continuing the addition of such leaching agent and haltelements in the iron phase are dissolved, and
mg the Same before y appreclable amount of the then removing the solution of manganese and nickel elements in the iron phase are dissolved, and f h resulting cobaltqmn i1 then removing the solution of manganese and nickel from the r s l ing co alt-iron i 10 References Cited in the file of this patent 4. The method of separating the nickel from cobalt in UNITED STATES PATENTS ocean floor mangamferous deposits, in which the mckel is present in a manganese oxide phase and the cobalt in 2,197,185 Klssock P 1940 an iron oxide phase, comprising 2,816,015 Donaldson 1957 crushing such ore to about minus forty mesh, 15 2345333 Schaufelberger July 291 1958 mixing said ore in its crushed state with water to form 2,913,334 Dean 1959
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2197185 *||Sep 9, 1938||Apr 16, 1940||Alan Kissock||Recovery of metals|
|US2816015 *||Jul 25, 1955||Dec 10, 1957||Quebec Metallurg Ind Ltd||Method for recovering nickel and cobalt from ores|
|US2845333 *||Jun 21, 1955||Jul 29, 1958||Chemical Construction Corp||Process of separating cobalt and nickel values|
|US2913334 *||May 21, 1958||Nov 17, 1959||Dean John G||Process for separating cobalt and nickel from ammoniacal solutions|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US3471285 *||Mar 27, 1967||Oct 7, 1969||Dow Chemical Co||Process for the selective recovery of manganese and iron from ores|
|US3753686 *||Jul 16, 1970||Aug 21, 1973||Kennecott Copper Corp||Recovery of copper, nickel, cobalt and molybdenum from complex ores|
|US3854851 *||Apr 26, 1972||Dec 17, 1974||P Cardwell||Method for separating nickel from cobalt in aqueous solution|
|US3903235 *||Apr 26, 1972||Sep 2, 1975||Deepsea Ventures Inc||Method for separating nickel from cobalt|
|US3906075 *||Oct 10, 1972||Sep 16, 1975||Preussag Ag||Process for extracting a manganese concentrate from maritime manganese ore|
|US3930974 *||May 21, 1973||Jan 6, 1976||Deepsea Ventures, Inc.||Two stage selective leaching of metal values from ocean floor nodule ore|
|US3984520 *||Feb 26, 1974||Oct 5, 1976||Deepsea Ventures, Inc.||Separation of nickel and cobalt and manganese in solution|
|US4020143 *||Aug 26, 1974||Apr 26, 1977||Kennecott Copper Corporation||Use of raw manganese nodules for oxidation leaching of reductively roasted manganese nodules|
|US4123499 *||May 20, 1977||Oct 31, 1978||Chemetals Corporation||Recovering metal values from marine manganese nodules|
|US4138465 *||Dec 13, 1977||Feb 6, 1979||The United States Of America As Represented By The Secretary Of The Interior||Selective recovery of nickel, cobalt, manganese from sea nodules with sulfurous acid|
|US4226836 *||Jan 3, 1979||Oct 7, 1980||University Patents, Inc.||Method for separating molybdenum values from sea nodules|
|US4280986 *||Jul 17, 1980||Jul 28, 1981||University Patents, Inc.||Method for separating metal values from sea nodules|
|US4620964 *||Jun 6, 1985||Nov 4, 1986||Commissariat A L'energie Atomique||Process for the treatment of complex manganese ores, such as marine nodules|
|US4740243 *||Apr 30, 1986||Apr 26, 1988||Ensci, Inc.||Metal value recovery from metal sulfide containing ores|
|US4752332 *||Apr 30, 1986||Jun 21, 1988||Ensci, Inc.||Treating manganese-containing ores with a metal sulfide|
|US4765827 *||Jan 20, 1987||Aug 23, 1988||Ensci, Inc.||Metal value recovery|
|US5834294 *||Jan 11, 1996||Nov 10, 1998||Newmont Gold Co.||Biooxidation process for recovery of metal values from sulfur-containing ore materials|
|US6383458||Jun 2, 1995||May 7, 2002||Newmont Mining Corporation||Biooxidation process for recovery of metal values from sulfur-containing ore materials|
|US6482373||Jun 5, 1995||Nov 19, 2002||Newmont Usa Limited||Process for treating ore having recoverable metal values including arsenic containing components|
|US6696283||Nov 9, 2001||Feb 24, 2004||Newmont Usa Limited||Particulate of sulfur-containing ore materials and heap made therefrom|
|EP0165166A1 *||May 31, 1985||Dec 18, 1985||Commissariat A L'energie Atomique||Process for treating complex manganese ores such as marine nodules|
|WO1996041025A1 *||Jun 4, 1996||Dec 19, 1996||Pacific Nickel Corp.||Process for extraction of nickel and cobalt from laterite ores|
|U.S. Classification||423/150.4, 75/400, 423/DIG.400, 423/41|
|International Classification||C22B47/00, C22B3/00|
|Cooperative Classification||Y10S423/04, C22B47/009, C22B3/00|
|European Classification||C22B3/00, C22B47/00N6|