US1266775A - Method of separating nickel from nickel-copper alloys. - Google Patents
Method of separating nickel from nickel-copper alloys. Download PDFInfo
- Publication number
- US1266775A US1266775A US10899216A US10899216A US1266775A US 1266775 A US1266775 A US 1266775A US 10899216 A US10899216 A US 10899216A US 10899216 A US10899216 A US 10899216A US 1266775 A US1266775 A US 1266775A
- Authority
- US
- United States
- Prior art keywords
- nickel
- copper
- matte
- solution
- separating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0054—Slag, slime, speiss, or dross treating
Definitions
- My invention relates to a method for separating nickel from nickel-copper matte.
- This matte as is well known, is obtained in large quantities in smelting processes, and is an impure metallic product consisting essentially of nickel-copper, and usually of a substantial percentage of sulfur.
- the nickel salt in the solution may be separated in any well known way, suchas by the addition of lime or by evaporating the liquid.
- the resulting crystals or nickel salt may then be broken up by heat treatment to form the well known nickel oxid, from which metallic nickel may easily be obtained by reduction.
- this trace of copper in the solution may be removed by adding metallic nickel, preferably in granulated or powdered form, which operates to displace the copper in the solution and causes it to be precipitated.
- I may employ a neutral or slightly acid copper solution.
- the nickel. of the metallic matte displaces and precipitates the copper of the solution, leaving a nickel solution, and thereby efi'ecting the desired separation.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
IUNITE I I IWE.
JOSEPH IDI'IAVERNAS, OF NEW BRUNSWICK, NEW JERSEY, ASSIGNOR T0 UNITED STATES NICKEL COMPANY, OF NEW BRUNSWICK, NEW JERSEY, A CORPORATION OF NEW JERSEY.
METHOD OF SEPARATING NIGIIEL FEOM NICKEL-COPPER ALLOY$.
nacawa No Drawing.
To all whom it may concern:
Be it known that I, JosErrI DI-rAvnnNAs, a citizen of the Republic of France, residing in the town of New Brunswick, county of Middlese-X, and State of New Jersey, have invented certain new and useful Improvements in Methods of Separating Nickel from Nickel-Copper Alloys, of which the following is a disclosure.
My invention relates to a method for separating nickel from nickel-copper matte. This matte, as is well known, is obtained in large quantities in smelting processes, and is an impure metallic product consisting essentially of nickel-copper, and usually of a substantial percentage of sulfur.
It has heretofore been proposed to separate the nickel. out of the matte by first roasting the matte, thereby converting the copper into oxid, and then leaching out the copperoXid as copper-sulfate or chlorid, leaving the nickel substantially free of copper. This process has not been found satisfactory because it has been found impossible to leach out all of the copper and, in practice, there always remains two or three per cent. of copper undissolved, however long the acid treatment. Moreover, it was found that if the roasting was carried far enough to make the copper more easily soluble, a large percentage of nickel would be oxidized along with the copper, with the result that it would dissolve with the copper in the subsequent acid treatment, preventing the successful operation of the method.
My improved process diflers radically from that above described, as will be readily seen from the following description.
In practising my improved process, I first roast the matte partially, in order to reduce the sulfur content of the matte. If the sulfur content be no greater than twelve per centum, I can proceed without any roasting; but I prefer to have the content of sulfur reduced to about eight per cent. When sufficiently desulfurized, I then reduce the matte to convert whatever oxids it may contain or which have been formed in the roasting process to deoxidized state, this step being accomplished by suitable reducing gases, or coke, or in any suitable way. The result after the deoxidizing step is a conver- Specification of Letters Patent.
Patented May 21L, I915.
Application filed July 13, 1916. Serial No. 108,992.
sion of the original higlrsulfur matte into a 1ow-sulfur double matte of copper and nickel.
- The nickel salt in the solution may be separated in any well known way, suchas by the addition of lime or by evaporating the liquid. The resulting crystals or nickel salt may then be broken up by heat treatment to form the well known nickel oxid, from which metallic nickel may easily be obtained by reduction.
If in practising my improved process, it is found, as is sometimes the case, that the acid mployed to dissolve the nickel also to a small extent attacks the copper and carries a trace of it into the solution, this trace of copper in the solution may be removed by adding metallic nickel, preferably in granulated or powdered form, which operates to displace the copper in the solution and causes it to be precipitated.
In dissolving the nickel out of the oxidized and substantially reduced matte, I may employ a neutral or slightly acid copper solution. In using such a solution, the nickel. of the metallic matte displaces and precipitates the copper of the solution, leaving a nickel solution, and thereby efi'ecting the desired separation.
I am aware that many modifications may be made to the process above described without departing from the scope of my invention, and I therefore intend to include all equivalent processes within the scope of my claims,
What I claim is:
1. The improvement in methods of extracting nickel from copper-nickel matte, containing sulfur, which consists in roasting the matte to remove part of the sulfur, then reducing the resulting oxide to metallic form, then treating the metallic nickel-copper with an acid adapted to attack and dissolve the nickel, substantially as described.
2. The improvement in the method of extracting nickel from copper-nickel matte which consists in partly oxidizing the matte, partly reducing the resulting 02nd, and dissolving out the nickel.
3. The improvement in methods of ex tracting nickel from copper-nickel matte containing sulfur which consists in roasting the matte to reduce the sulfur content, then reducing the resultin product, then treating the product With an acid thereby dissolving thenickel, and then adding metallic nickel to the solution for the purpose of precipitating any copper dissolved therein, substantially as described.
4:. The improvement in processes of the kind described Which consists in treating non-oxidized nickel-copper matte with an acid adapted to dissolve the nickel, then treating the solution with metallic nickel thereby precipitating any small percentages of copper in the solution, then drawing off Copies of this patentmay be obtained for five cents each, by addressing the Commissioner Washington, D. 0.
the nickel salts and treating them to produce 15 by roasting, partly reducing the resulting 20 matte, treating the resulting product with an acid adapted to dissolve the nickel, then treating the solution with metallic nickel, thereby precipitating any small percentages of copper in the solution, then drawing oil the nickel salts, and producing metallic nickel therefrom.
JOSEPH DHAVERNAS.
of Patents,
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10899216A US1266775A (en) | 1916-07-13 | 1916-07-13 | Method of separating nickel from nickel-copper alloys. |
US190308A US1273465A (en) | 1916-07-13 | 1917-09-08 | Method of separating nickel from nickel-copper alloys. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10899216A US1266775A (en) | 1916-07-13 | 1916-07-13 | Method of separating nickel from nickel-copper alloys. |
Publications (1)
Publication Number | Publication Date |
---|---|
US1266775A true US1266775A (en) | 1918-05-21 |
Family
ID=3334433
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10899216A Expired - Lifetime US1266775A (en) | 1916-07-13 | 1916-07-13 | Method of separating nickel from nickel-copper alloys. |
Country Status (1)
Country | Link |
---|---|
US (1) | US1266775A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2753259A (en) * | 1950-11-18 | 1956-07-03 | Basf Ag | Processing of nickel-copper mattes |
US2934428A (en) * | 1957-05-08 | 1960-04-26 | Quebec Metallurg Ind Ltd | Method for treating nickel sulphide ore concentrates |
US4241031A (en) * | 1979-02-16 | 1980-12-23 | Amax Inc. | Dissolution of nickeliferous sulfide material in HCl |
-
1916
- 1916-07-13 US US10899216A patent/US1266775A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2753259A (en) * | 1950-11-18 | 1956-07-03 | Basf Ag | Processing of nickel-copper mattes |
US2934428A (en) * | 1957-05-08 | 1960-04-26 | Quebec Metallurg Ind Ltd | Method for treating nickel sulphide ore concentrates |
US4241031A (en) * | 1979-02-16 | 1980-12-23 | Amax Inc. | Dissolution of nickeliferous sulfide material in HCl |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2003514109A5 (en) | ||
TW201229244A (en) | Process for recovering zinc and/or zinc oxide II | |
KR20140006875A (en) | Improved method of ore processing | |
AU2012211033A1 (en) | Improved method of ore processing | |
AU2018248786A1 (en) | Process for the recovery of lithium | |
Chong et al. | Selective reductive leaching of oxidised cobalt containing residue | |
US3962051A (en) | Atmospheric leaching of matte containing iron | |
EP3607101B1 (en) | A method for preparing a leach feed material | |
US4188362A (en) | Process for the treatment of platinum group metals and gold | |
FR2948946A1 (en) | PROCESS FOR LEACHING COBALT FROM COBALT OXIDE ORES | |
US1266775A (en) | Method of separating nickel from nickel-copper alloys. | |
JP2014015647A (en) | Method for recovering cobalt | |
EP0008992A1 (en) | Process for recovering indium | |
US1273465A (en) | Method of separating nickel from nickel-copper alloys. | |
CA2949580A1 (en) | Process for selective acid leaching nickel and cobalt from a mixed hydroxide intermediate | |
US940292A (en) | Method of separating copper, nickel, and other metals from copper-nickel matte. | |
DE2240770A1 (en) | CLEANING NICKEL ROCK | |
JP7365846B2 (en) | Method for producing high purity cobalt sulfate solution and method for producing cobalt sulfate | |
CA2439970C (en) | Recovery of metals from jarosite-containing materials | |
US1047825A (en) | Method or process of treating nickel-copper mattes. | |
US1263727A (en) | Process for extracting copper from its ores. | |
US1167701A (en) | Process of recovering zinc from its ores. | |
US2104076A (en) | Lead recovery | |
US1238298A (en) | Treatment of copper-nickel pyrrhotite. | |
US3674465A (en) | Recovery of nickel from nickel ammonium carbonate systems |