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
  • C22B23/00—Obtaining nickel or cobalt
  • C22B23/04—Obtaining nickel or cobalt by wet processes
  • C22B23/0476—Separation of nickel from cobalt
  • C22B23/0484—Separation of nickel from cobalt in acidic type solutions
• • 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
  • C22B23/00—Obtaining nickel or cobalt
  • C22B23/04—Obtaining nickel or cobalt by wet processes
  • C22B23/0453—Treatment or purification of solutions, e.g. obtained by leaching
  • C22B23/0461—Treatment or purification of solutions, e.g. obtained by leaching by chemical methods
  • C22B23/0469—Treatment or purification of solutions, e.g. obtained by leaching by chemical methods by chemical substitution, e.g. by cementation
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P10/00—Technologies related to metal processing
  • Y02P10/20—Recycling

Definitions

• the present invention involves a process for separating nickel from cobalt contained in a solution of mixed salts of cobalt and nickel which consists essentially in separating the nickel by using, jointly with a metal more electronegative than nickel, iron for example, a metalloid compound formed from two or more of the following elements: sulphur, selenium, tellurium, antimony and arsenic.
• a second step of the process involves redissolving the separated nickel and then purifying the resulting nickel solution to ultimately obtain the nickel in a commercial metallic form.
• the present invention is specifically directed to an economical process of separating nickel from cobalt and ultimately obtaining a cobalt salt solution substantially free from nickel, and a nickel salt solution substantially free from cobalt. These solutions may be electrolyzed to obtain the corresponding metals.
• a metal may be displaced from solutions containing it by another metal having a greater electromotive force than the metal in solution.
• the metal which performs the displacement of the metal from the solution is more electronegative than the metal in solution.
• the metalloid compound to be employed in the present invention consists of a compound formed entirely from two or more of the following metalloid elements: sulphur, selenium, tellurium, antimony and arsenic. These metalloid compounds are available in the natural state or may be chemically prepared. Examples of natural metalloid compounds are the realgars, orpiments and stibnites. These and other metalloid compounds may also be obtained by chemical synthesis thereof.
• the metalloid compounds have a very noteworthy power for promoting the separation of nickel from a mixed nickel-cobalt salt solution which appears to be directly correlated to the molecular composition of the compounds. For example, a mere mixture of the constituents of'the compounds, even in proportions equal to those that exist in the compound, results in inferior results in the process.
• a mixed saline solution of sulphates or chlorides of cobalt and nickel is heated to a temperature between 50-l00 C. and thoroughly mixed. Copper is then added to the solution in the form of a soluble salt or in the form of a sulphide mixed with the metalloid compound. Then the metalloid compound is added, possibly simultaneously with the copper and the metal more electronegative than nickel.
• the metalloid compound is, for example, arsenic sulphide, and can be mixed with the copper sulphide as indicated above.
• the metal more electronegative than nickel can be iron in a finely divided form.
• Acid is then added to bring the pH of the solution to about 2.5 as rapidly as possible, and thereafter acid additions are made to maintain the pH close to 2.5 throughout the operation. The temperature is maintained between 50-100 C. until the nickel contained in the original solution has almost completely disappeared. The disappearance of the nickel from the solution can be determined in any known manner.
• the solids in the solution are composed essentially of the metalloid compound, copper, nickel (completely or partially combined with the metalloid compounds), a small amount of cobalt which has been precipitated along with the nickel, and anyexcess portion of the metal more electronegative than nickel, such as iron.
• the solids are separated from the solution by filtration, the residue on the filter is washed and the wash liquid added to the filtrate from the filtration step.
• the filtrate contains substantially pure cobalt, practically free from nickel.
• the filtrate can be treated in any well-known manner to eliminate small impurities such as iron, and is finally electrolyzed to extract the metallic cobalt therefrom.
• the second step of the process isi directed toward a solubilization of the nickel in the residue from the above filtration step, and may be performed in any known nianner and in particular by the steps described hereina ter.
• the above residue is suspended in an aqueous medium and gaseous chlorine is bubbled through until the nickel, and possibly any included cobalt, is totally dissolved.
• Theother metals contained in the solids are at least partly dissolved during the chlorination.
• the suspension is then filtered to remove any remaining residue, which residue is normally sulphur, when the starting metalloid compound is a sulphide.
• This filtrate is then strongly acidiand ametallic sulphide, for example iron sulphide, or hydrogen sulphide, is added to precipitate the arsenic and copper in the form of sulphides if the metalloid compound is AS 8
• the solution is again filtered to remove the arsenic and copper sulphides which are returned to the first step of the process to be reused.
• the filtrate from the last mentioned filtration step contains the remaining metals including the nickel and possiblysmall amounts of cobalt.
• This solution is then treated; to precipitate the cobalt and iron as hydroxides in a well known manner.
• the cobalt is obtained in the form of solid cobalt hydroiiide and includes a small amount of nickel.
• a good separation of the nickel is effected by maintaining the pH constant throughout the whole process;
• the pH may vary between 1 and 5, but preferably its value is maintained at about 2.5.
• the pH is increased from 2.5 to 5, the amount of cobalt precipitated along with the nickel, increases.
• the pl-I is reduced from 2.5 to 1, the yield of nickel decreases progressively.
• the regulation of the pH at the desired value and the use of only the exact amount of metal more electronegative than nickel necessary to precipitate the nickel tends to limit the amount of cobalt coprecipitated with the nickel.
• the amount'of metal more electronegative than nickel which is added to the solution can be in an amount ranging from 1 to 5 times the amount of nickel present, on an atomic basis, but preferably the amount of metal added is maintained between 1.1 and 1.3 of the amount of nickel present,on an atomic basis. 7 v i
• the reaction rate depends upon the amount of the metalloid compound added in proportion to the amount of nickel present. I
• the metalloid compound is added in an amount ranging from 1 to 2 times the amount of nickel present in the solution, on a Weight basis. For example, with all other operating conditions being constant, 98% of the nickel was precipitated at a temperature of about C. in one minute when the weight ratio of arsenic sulphide to nickel present was equal to about 2; and in ten minutes when the ratio of arsenic sulphide to nickel present was equal to about I.
• the eifect of the presence of the addition of copper to the solution to be treated is to increase the speed of the precipitation of the nickel.
• a precipitation of 98% of the nickel in the solution was obtained in ten minutes when no copper was present in the solution; but, with the addition of copper to the solution in a form of soluble salt equal to 100 milligrams for each 7 grams of nickel present, the 98% precipitation of nickel was obtained under the same operating conditions in five minutes.
• the copper may be added in the form of a soluble salt.
• the copper present, orto be added to the solution must be in the range of 0.3-2% byweightof the nickel present in the solution.
• the copper may also be added in the form of copper sulphide simultaneously with the metalloid compound addition; however, when this copper compound is used, the proportion of copper sulphide which must be added, compared to the nickel present, is about 10-25%
• the reaction rate also depends upon the temperature used in the process. The rate increases as the temperature increases, and to render the operation economically interesting and feasible, the temperature must be maintained between 50-l00 C. and is preferably maintained at about 60 v
• the reaction speed also increases as the metal more electronegative than nickel is more finely divided.
• the temperature was maintained at about 60 C and after about ten minutes most ofthe nickel had precipitated, partly in a formcombined with the arsenic sulphide, and partly in a form of metallic nickel.
• the solid residue was filtered from the solution and washed with 15 litres of cold water until only traces of the cobalt were determinable in the wash water.
• the filtrate and wash water were combined and contained 11 grams of nickel and 6J499 grams of cobalt. Therefore, 98.5% of the nickel had been extracted, and 1.76% of the cobalt had been coprecipita'ted with the nickel.
• the filtrate was then further treated in a well-known manner to remove any impurities and electrolyzed to obtain metallic cobalt.
• the washed solid residues from the filtration were then suspended in water and chlorine gas bubbled through until the nickel and cobalt contained in the residues were completely dissolved. After filtration, hydrogen sulphide was then bubbled through the suspension to precipitate the arsenic and copper in the form of sulphides. This suspension was then filtered to remove the arsenic and copper sulphides, which were washed and recycled to the beginning of the process.
• the filtrate containing nickel and cobalt chloride, was then treated in a well-known manner to precipitate the iron. After this treatment, the solution contained 725.9 grams of nickel and 116 grams of cobalt. The cobalt was then separated in the form of a hydroxide which carried along 7 grams of nickel. The cobalt hydroxide and nickel were filtered from the solution and returned to the first step of the process to be reprocessed. The filtrate was substantially pure nickel containing only a few traces of cobalt. This filtrate was electrolyzed to obtain metallic nickel.
• a process for separating nickel from cobalt contained in a solution of mixed salts of cobalt and nickel which comprises adding to said solution a solid metal more electronegative than nickel and a solid metalloid compound consisting essentially of at least two of the members from the group consisting of sulphur, selenium, tellurium, antimony and arsenic, maintaining the pH of the-solution between 1-5; the nickel separating from the solution as a solid material; and separating the solids containing the nickel from the solution containing substantially only cobalt.
• a process for separating nickel from cobalt contained in a mixed solution of the salts of cobalt and nickel which comprises adding to said solution a solid metal more electronegative than nickel and a solid compound consisting essentially of arsenic and sulphur, maintaining the pH of the solution between about 1 to 5 and the temperature of the solution sufliciently high to separate the nickel from the solution as a solid; separating the solids containing the nickel from the solution containing substantially only cobalt.
• a process for separating nickel from cobalt contained in a mixed solution of the salts of cobalt and nickel which comprises adding to said solution a solid metal more electronegative than nickel and a compound consisting essentially of AS283; maintaining the pH of the solution between about 1 to 5 and the temperature of the solution sufliciently high to separate the nickel from the solution as a solid; separating the solids containing the nickel from the solution containing substantially only cobalt.
• a process according to claim 11 including forming an aqueous suspension of the solids containing the nickel, chlorinating the suspension to dissolve the nickel, adding a sulphide compound to the suspension to convert any arsenic and copper in the suspension into sulphides, removing the arsenic and copper sulphides from the suspension, and removing any cobalt from the suspension in the form of a hydroxide to produce a solution of substantially pure nickel.
• a process for separating nickel from cobalt contained in a solution of mixed salts of cobalt and nickel which process consists essentially of adding to said solution a solid metal more electronegative than nickel and a solid metalloid compound formed solely from at least two members from the group consisting of sulphur, selenium, tellurium, antimony and arsenic; said compound being substantially free of nickel and cobalt; maintaining the pH between about 1-5; the nickel in the solution separating as a solid material; and separating the solids containing the nickel from the solution containing substantially only cobalt.

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Manufacturing & Machinery (AREA)
• Materials Engineering (AREA)
• Mechanical Engineering (AREA)
• Metallurgy (AREA)
• Organic Chemistry (AREA)
• Removal Of Specific Substances (AREA)
• Manufacture And Refinement Of Metals (AREA)
• Inorganic Compounds Of Heavy Metals (AREA)

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Cited By (4)

Citations (3)

• 0
  • BE BE566626D patent/BE566626A/xx unknown
• 1958
  • 1958-04-28 GB GB1343558A patent/GB853323A/en not_active Expired
  • 1958-05-05 US US73283858 patent/US2960400A/en not_active Expired - Lifetime

Patent Citations (3)

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