CN1587441A - Process for preparing high purity nickel - Google Patents
Process for preparing high purity nickel Download PDFInfo
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- CN1587441A CN1587441A CNA2004100706482A CN200410070648A CN1587441A CN 1587441 A CN1587441 A CN 1587441A CN A2004100706482 A CNA2004100706482 A CN A2004100706482A CN 200410070648 A CN200410070648 A CN 200410070648A CN 1587441 A CN1587441 A CN 1587441A
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- high purity
- purity nickel
- electrodeposition
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- 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
- C22B23/06—Refining
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/06—Electrolytic production, recovery or refining of metals by electrolysis of solutions or iron group metals, refractory metals or manganese
- C25C1/08—Electrolytic production, recovery or refining of metals by electrolysis of solutions or iron group metals, refractory metals or manganese of nickel or cobalt
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- 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
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
- C22B3/42—Treatment or purification of solutions, e.g. obtained by leaching by ion-exchange extraction
-
- 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
Abstract
The high purity nickel preparing electrodeposition process features the successive technological steps of: adopting hydrochloric acid system with 3N electrolytic aluminum as anode for electric dissolving preparation of pH 1-3 NiCl2 solution; three-stage countercurrent extraction of the electric dissolving solution with anionic extractant; deoiling the counter extracted solution and deeply purification through ion exchange with anionic exchange resin; and final electrodeposition in electrolytic bath to obtain high purity aluminum, with the introduced solution amount after ion exchange purification being equal to pumped out post-electrodeposition liquid. Glow discharge mass spectrum-GDMS analysis shows that the preparation high purity Ni reaches 5N standard, and the preparation process has low cost and no environmental pollution.
Description
Technical field
A kind of method for preparing high purity nickel, relating to a kind of is raw material with the 3N electrolytic nickel, adopts the hydrochloric acid solution system electrodeposition to prepare the method for high purity nickel
Background technology
Further developing of new and high technology requires enough exotic materialss are provided, and has been found that multiple metal can be used as the strategic materials of new and high technology and requires it to purify to very high purity.Preparation, the characteristic of high-purity, ultra-high purity metal and be applied in the modern material science and the engineering field in belong to novel, great-hearted, ever-increasing field.The above high pure metal of 5N is used widely in semiconductor element and ultra-large integrated component production.The production of electronic component, printed circuit board (PCB) approximately needs surplus high purity gallium, indium, arsenic, antimony, cadmium, lead, tin, tellurium, bismuth, sulphur, zinc, copper, selenium, the phosphorus etc. 20 kind of high pure metal and compound thereof, alloy material.
Nickel is generally used for fields such as traditional stainless steel, alloy.In recent years some special dimensions are progressively increasing for the demand of high purity nickel.For example, the superalloy of making by high purity nickel be used for aircraft engine manufacturing, be used for the reactor protecting materials, be used for biomaterial, be used for low expansion alloy; The used in electronic industry high purity nickel is also progressively increasing, and for example a kind of special Rhometal is widely used in lead frame, and another kind of Cu-Ni-Sn alloy is used for Wiring port; High purity nickel also is used for hydrogenation catalyst and other chemicals.When high purity nickel is used for large-scale integrated circuit and wiring material thereof, magneticthin film, special package material, require foreign matter contents such as basic metal, radioactive element, transition metal element, elemental gas very low.
At present, the preparation method of relevant high purity nickel, disclosed document is also seldom.Patent is " WO 03/014421A1's " the Japanese Patent of " high purity nickel production method; high purity nickel; sputtering target material high purity nickel; make plated film with sputtering target material ", a kind of method that adopts soluble anode electrolytic preparation high purity nickel is disclosed, its anode is solvable nickel raw material, the cathode sheath diaphragm bag, adopt precipitation of hydroxide, the method of displacement of nickel foil sheet and preelectrolysis is removed impurity element in the electrolytic solution, purification electrolysis liquid, electrolysis output 5N (99.999%) high purity nickel, the high purity nickel impurity content: O is below 30ppm, C, N, S, P, F is lower than below the 10ppm, all the other impurity content not specified (NS)s.
In addition, the patent No. is the Japanese Patent of " high purity nickel production method, the making plated film high purity nickel " of " P2000-219988A ", discloses a kind of method that adopts soluble anode electrolytic preparation high purity nickel.It is in same electrolyzer, separate with two-layer barrier film between its negative electrode, the anode, adopt resin anion(R.A) exchange purifying electrolysis liquid, and reduce the method for the hydrochloric concentration of electrolytic solution, purification electrolysis liquid with diffusion dialysis or evaporation drying, electrolysis output high purity nickel, the high purity nickel impurity content: below the alkali metal 1ppm, below 10ppm, U, Th are respectively below 1ppb respectively for Fe, Co, Cr, C is below 50ppm, and O is below 100ppm.
In the production method of present existing high purity nickel, in order to solve the peracid problem of electric molten stoste, adopted boiling deacidification and neutralization to fall the way of acid, cause the production cost height, and easy the generation polluted; Solution deep purifies undesirable.Owing to adopt soluble anode that the generation of electrolysis cathode, the mutual pollution condition of anolyte easily takes place, cause high purity nickel foreign matter content height.
Summary of the invention
Purpose of the present invention is exactly the deficiency that exists in the above-mentioned prior art, a kind of peracid problem that can effectively solve electric molten stoste is provided, reduce production costs, decontamination, solution deep purify, and can prevent effectively that electrolysis cathode, anolyte from polluting, reducing the high method for preparing high purity nickel of high purity nickel foreign matter content mutually.
The objective of the invention is to be achieved through the following technical solutions.
A kind of method for preparing high purity nickel is characterized in that its technological process is followed successively by:
A. adopting hydrochloric acid system, is anode with the 3N electrolytic nickel, is negative electrode with corrosion-resistant titanium metal silk screen, the molten preparation NiCl of electricity
2Solution; The molten current density of its electricity is 100A/m
2～200A/m
2, and molten at electricity to Solution H
+Concentration is that 30A/m is adopted in the liquid making of 1g/l～2g/l latter stage
2～70A/m
2The molten liquid making of current density electricity, the PH that makes solution is 1-3;
B. after the solution after the back extraction being fed the active carbon column de-oiling, feed the ion exchange column of the mixed anion exchange resin that is respectively anionite-exchange resin 331, anionite-exchange resin 717, D301 and D401 more successively, carry out deep purifying, exchange flow rate control≤2BV/h, solution purification is reduced to below the 0.001g/l to containing Co, Fe, and solution contains Cu, Pb, Zn is reduced to below the 0.0002g/l;
C. the solution after ion-exchange being purified feeds electrolyzer and carries out electrodeposition, and control electrodeposition pH value of solution value is 1～3, current density 100A/m
2～200A/m
2, 40 ℃～60 ℃ of electric effusion temperature, simultaneously liquid behind the electrodeposition is extracted out, make solution in electrolyzer, weigh circulation, electrodeposition obtains high purity nickel.
A kind of method for preparing high purity nickel is characterized in that adopting after the molten liquid making of electricity anion extractant that the broad liquid of electricity is carried out the extraction of three stage countercurrents, and extraction phase was than 1: 2, and extraction equilibrium is used the pure water back extraction after 10 minutes.
A kind of method for preparing high purity nickel of the present invention is characterized in that adopting anion extractant to consist of 20%～40% tertiary amine, 20%～45% fourth fat, and surplus is a sulfonated kerosene.
A kind of method for preparing high purity nickel of the present invention, the organic phase that it is characterized in that its anion extractant is through after washing purifying, and it is saturated to adopt the 4N high purity hydrochloric acid to make organic phase carry out acid, again to NiCl
2Solution extracts.
A kind of method for preparing high purity nickel of the present invention is characterized in that its solution is the de-oiling of tubular fibre ball.
A kind of method for preparing high purity nickel of the present invention adopts combination anionite-exchange resin, realizes treatment facilities three-dimensional, that intersect, deep purifying solution.
Method of the present invention adopts the high-purity solutions electrodeposition after ion-exchange purifies to prepare high purity nickel, and the high purity nickel sample is analyzed through glow discharge spectrometry-GDMS, reaches the 5N high purity nickel.In the technological process, adopt the low current liquid making and reduce the solution acid content latter stage, successfully solved the peracid problem of electric molten stoste, abandoned the way that acid falls in boiling deacidification and neutralization, not only reduced cost but also prevented the process pollution in the molten liquid making of electricity; Organic phase is through after washing purifying, and it is saturated to adopt high purity hydrochloric acid to make organic phase carry out acid, uses this organic phase to high density NiCl again
2Solution extracts, and has realized that solution deep purifies except that cobalt; Ion exchange process adopts the combination resin anion(R.A), realizes high-purity solutions treatment facilities three-dimensional, that intersect; Realized the mutual linking of electric molten liquid making, solvent extraction, ion-exchange and electrodeposition process, deep purifying solution, and adopt the high purity nickel of the above grade of electrowinning with insoluble anode output 5N.Compare with the soluble anode electrolysis, have only the high-purity N iCl after the purification in the electrowinning with insoluble anode groove
2Solution, thus the generation of soluble anode electrolysis cathode, the mutual pollution condition of anolyte effectively prevented, and the high purity nickel foreign matter content of electrowinning with insoluble anode refining output is lower.Alkali metal is below 0.1ppm, and below 1ppm, below 0.1ppb, C is below 60ppm respectively for U, Th respectively for Fe, Co, Cr, and O is below 100ppm.
High purity nickel of the present invention is investigated impurity element and is comprised Co, Fe, Cu, Zn, As, Cd, Sn, Sb, Pb, Bi, Al, Mn, Mg, Si, P, S totally 16 kinds of impurity elements, and the high-content of single impurity element is lower than 1ppm; The content of main metallic element nickel (decrement) is higher than 99.999%.Preparation high-purity N iCl
2Solution is the prerequisite of development high purity nickel, selects 5 kinds of impurity of Fe, Co, Cu, Pb, Zn of the most difficult removal from 16 kinds of impurity elements, is investigated as the major impurity element, weighs the solution purification degree by purifying back solution foreign matter content.Test shows, selects representational impurity element as main removal of impurities target, has improved detection efficiency.
Description of drawings
Accompanying drawing is a method process flow diagram of the present invention.
Embodiment
A kind of method for preparing high purity nickel, its technological process is followed successively by:
A. adopting hydrochloric acid system, is anode with the 3N electrolytic nickel, is negative electrode with corrosion-resistant titanium metal silk screen, the molten preparation NiCl of electricity
2Solution; Its electrical current density is 100A/m
2～200A/m
2, electricity is molten to Solution H
+Concentration is that 30A/m is adopted in the liquid making of 1g/l～2g/l latter stage
2～70A/m
2The current density liquid making, the pH that makes solution is 1-3; Owing to adopt the low current density liquid making and reduce the solution acid content latter stage in the molten liquid making of electricity, successfully solved the peracid problem of electric molten stoste, abandoned the way that acid falls in boiling deacidification and neutralization, not only reduced cost but also prevented the process pollution.The molten liquid making of electricity prepares NiCl
2The solution impurity content is: Co 0.006g/l～0.009g/l, Cu 0.002g/l, Fe 0.002g/l, Pb 0.001g/l, Zn 0.002g/l.
B. adopting volume percent is 20%～40% tertiary amine, 20%～45% fourth fat, and surplus is that the anion extractant that sulfonated kerosene is formed carries out the extraction of three stage countercurrents with solution, and extraction phase was than 1: 2, and extraction equilibrium is used the pure water back extraction after 10 minutes; Owing to improve Cl in the solution
-Concentration, make impurity such as Fe, Co, Cu, Pb, Zn fully form complex anion.After the solution process anion extractant abstraction impurity removal matter, the content of impurity element reduces, and solution contains Co and is reduced to 0.001g/l, and solution contains Cu, Zn is reduced to 0.0003g/l.
C. the solution after will extracting feeds the active carbon column de-oiling, feed the ion exchange column of the mixed anion exchange resin that is respectively anionite-exchange resin 331,717, D301 and D401 more successively, carry out deep purifying, exchange flow rate control≤2BV/h, solution contains Co, Fe and is reduced to below the 0.001g/l, and solution contains Cu, Pb, Zn is reduced to below the 0.0002g/l; The principle of design of ion exchange system is to guarantee that exchange column system itself does not produce impurity element and pollutes: select for use virgin material to make ion exchange column body and system; Adopt the quantitative delivered solution of anti-pollution volume pump, accurately control the ion exchanged soln flow; Select special anionite-exchange resin, realize that solution deep purifies.
Raffinate oil removing, acid adjustment are carried out ion-exchange after handling, and the exchange current speed control is built in 1BV/h～2BV/h, if flow velocity is too fast, impurity element is fully exchange not, and resin penetrates easily; The exchange flow velocity is too slow, deficiency in economic performance.Content through impurity lead, zinc, copper, iron, cobalt in the solution of exchange back all has reduction.Solution C o0.006g/l～0.009g/l, Cu 0.002g/l, Pb 0.001g/l, Zn 0.002g/l.
D. with the solution after the ion-exchange, feed electrolyzer and carry out electrodeposition, control electrodeposition pH value of solution value is 1～3, current density 100A/m
2～200A/m
2, the electric effusion temperature: 40 ℃～60 ℃, simultaneously liquid behind the electrodeposition is extracted out, make solution in electrolyzer, weigh circulation, electrodeposition obtains high purity nickel.The high purity nickel sample is analyzed through glow discharge spectrometry-GDMS, reaches the 5N high purity nickel.
Manufacturing of electrolyzer requires cell body itself and external environment high-purity process of the test not to be produced the impurity element pollution: electrolyzer selects for use virgin material to make; Electrolyzer adopts the sealed construction design, is provided with dustproof top cover, has water-lute to be connected between top cover and the cell body; Cathode-anode plate and current conducting rod assembling are also hung on top cover; Cathode-anode plate and current conducting rod group all adopt pure anticorrosive, thereby effectively prevent the corrosion and the contaminated aqueous solution of acid.Bath voltage, current constant and elimination connect boundary's resistance when guaranteeing operation, and junction of electric circuits all adopts screw to be fastenedly connected, and select the high precision silicon rectifier power source.
Below in conjunction with example method of the present invention is described further.
Embodiment 1
Adopt the 3N electrolytic nickel, at the molten preparation NiCl of hydrochloric acid system electricity
2Solution, its electrical current density is 100A/m
2, the molten H to solution of electricity
+Concentration be 1g/l liquid making adopt 30A/m latter stage
2The current density liquid making, the pH that makes solution is 3; Solution C l
-Concentration reach 6mol/L, the solution impurity content sees Table:
Table 1-original solution impurity content unit: g/l
Serial number name Co Cu Fe Pb Zn
1 original solution 0.009 0.002 0.002 0.001 0.001
Adopting volume percent is the anion extractant of tertiary amine 25%, fourth fat 45%, sulfonated kerosene 30%, after extraction agent washed through high purity water, saturated through the 4mol/l high purity hydrochloric acid again, solution carried out the extraction of three stage countercurrents, extraction phase was than 1: 2, and extraction equilibrium is used the pure water back extraction after 10 minutes; After the solution process anion extractant abstraction impurity removal matter, solution contains Co and is reduced to 0.001g/l by 0.009g/l, and the raffinate solution composition sees Table 2.
Table 2-raffinate impurity content unit: g/l
| Sequence number | Title | Co | ?Cu | ????Fe | ????Pb | ????Zn |
| 1 | Raffinate 2# | 0.001 | ?0.0003 | ????0.001 | ????0.001 | ????0.0003 |
Solution after the extraction is fed the active carbon column de-oiling, feed the ion exchange column of the mixed anion exchange resin that is respectively anionite-exchange resin 331,717, D301 and D401 more successively, carry out concentration purification, exchange flow rate control 2BV/h, exchange back solution composition sees Table 3.
Solution impurity content unit: g/l after the table 3-ion-exchange
| Sequence number | Title | Co | ?Cu | ??Fe | ??Pb | ??Zn |
| 1 | Ion-exchange purifies back liquid | ＜0.0004 | ?0.0001 | ??＜0.0004 | ??＜0.0001 | ??0.0001 |
Electrodeposition technical qualification: control current density 100A/m
2, NiCl
2The pH value of solution value is 3,50 ℃ of electrodeposition temperature.Adopt the high-purity solutions after ion-exchange purifies, carry out electrowinning with insoluble anode and prepare the 5N high purity nickel.Below the high purity nickel alkali metal containing element 0.1ppm, below 1ppm, below 0.1ppb, C is below 60ppm respectively for U, Th respectively for Fe, Co, Cr, and O is below 100ppm.High purity nickel part of impurity elements content sees Table 4.
Table 4 high purity nickel glow discharge spectrometry (GDMS) analytical results:
| Sequence number | Impurity element | 1# sample impurities analysis (ppm) |
| ????1 | ????Cu | ????＜0.8 |
| ????2 | ????Fe | ????0.38 |
| ????3 | ????Co | ????＜0.04 |
| ????4 | ????Pb | ????0.28 |
| ????5 | ????Zn | ????＜0.03 |
| ????6 | ????Cd | ????＜0.01 |
| ????7 | ????Bi | ????＜0.005 |
| ????8 | ????Sb | ????0.14 |
| ????9 | ????Sn | ????＜0.5 |
| ????10 | ????As | ????＜0.8 |
| ????11 | ????Al | ????0.02 |
| ????12 | ????Mg | ????＜0.001 |
| ????13 | ????Mn | ????＜0.005 |
| ????14 | ????Si | ????0.04 |
| ????15 | ????P | ????＜0.01 |
| ????16 | ????S | ????0.1 |
| High purity nickel impurity adds up to | ????＜3 | |
| High purity nickel decrement percentage composition | ????＞99.9997％ | |
Embodiment 2
Adopt the 3N electrolytic nickel, at the molten preparation NiCl of hydrochloric acid system electricity
2Solution, its electrical current density is 150A/m
2, the molten H to solution of electricity
+Concentration be 1.5g/l liquid making adopt 50A/m latter stage
2The current density liquid making, the pH that makes solution is 2; Solution C l
-Concentration reach 6mol/L, the solution impurity content sees Table 5:
Table 5-original solution impurity content unit: g/l
Serial number name Co Cu Fe Pb Zn
1 original solution 0.008 0.003 0.001 0.001 0.001
Adopting volume percent is the anion extractant of tertiary amine 40%, fourth fat 20%, sulfonated kerosene 40%, after extraction agent washed through high purity water, saturated through the 4mol/l high purity hydrochloric acid again, solution carried out the extraction of three stage countercurrents, extraction phase was than 1: 2, and extraction equilibrium is used the pure water back extraction after 10 minutes; After the solution process anion extractant abstraction impurity removal matter, solution contains Co and is reduced to 0.001g/l by 0.008g/l, and the raffinate solution composition sees Table 6.
Table 6-raffinate impurity content unit: g/l
| Sequence number | Title | Co | ?Cu | ??Fe | ??Pb | ??Zn |
| 1 | Raffinate 2# | 0.001 | ?0.0002 | ??0.0009 | ??0.001 | ??0.0003 |
Solution after the extraction is fed the active carbon column de-oiling, feed the ion exchange column of the mixed anion exchange resin that is respectively anionite-exchange resin 331,717, D301 and D401 more successively, carry out deep purifying, exchange flow rate control 1.5BV/h, exchange back solution composition sees Table 7.
Solution impurity content unit: g/l after the table 7-ion-exchange
| Sequence number | Title | Co | ?Cu | ??Fe | ??Pb | ??Zn |
| 1 | Ion-exchange purifies back liquid | ＜0.0004 | ?0.0001 | ??＜0.0004 | ??＜0.0001 | ??0.0001 |
Adopt this NiCl
2Solution carries out electrowinning with insoluble anode, the electrodeposition technical qualification: current density is 160A/m
2, NiCl
2The pH value of solution value is 2,40 ℃ of electrodeposition temperature.Electrowinning with insoluble anode prepares the 5N high purity nickel.Below the high purity nickel alkali metal containing element 0.1ppm, below 1ppm, below 0.1ppb, C is below 60ppm respectively for U, Th respectively for Fe, Co, Cr, and O is below 100ppm.High purity nickel part of impurity elements content sees Table 7.
Table 7 high purity nickel glow discharge spectrometry (GDMS) analytical results:
| Sequence number | Impurity element | 1# sample impurities analysis (ppm) |
| ????1 | ????Cu | ????＜0.9 |
| ????2 | ????Fe | ????0.35 |
| ????3 | ????Co | ????＜0.05 |
| ????4 | ????Pb | ????0.45 |
| ????5 | ????Zn | ????＜0.03 |
| ????6 | ????Cd | ????＜0.02 |
| ????7 | ????Bi | ????＜0.005 |
| ????8 | ????Sb | ????0.14 |
| ????9 | ????Sn | ????＜0.3 |
| ????10 | ????As | ????＜0.8 |
| ????11 | ????Al | ????0.02 |
| ????12 | ????Mg | ????＜0.005 |
| ????13 | ????Mn | ????＜0.005 |
| ????14 | ????Si | ????0.05 |
| ????15 | ????P | ????＜0.01 |
| ????16 | ????S | ????0.15 |
| High purity nickel impurity adds up to | ????＜3 | |
| High purity nickel decrement percentage composition | ????＞99.9997％ | |
Embodiment 3
Other condition is with embodiment 2, and the anion extractant volume percent is tertiary amine 20%, fourth fat 45%, sulfonated kerosene 35%.
Liquid after the ion-exchange among the employing embodiment 2, exchange back solution composition sees Table 8.
Solution impurity content unit: g/l after the table 8-ion-exchange
| Sequence number | Title | ??Co | ??Cu | ??Fe | ??Pb | ????Zn |
| 1 | Ion-exchange purifies back liquid | ??＜0.0004 | ??0.0001 | ??＜0.0004 | ??＜0.0001 | ????0.0001 |
Adopt this NiCl
2Solution carries out electrowinning with insoluble anode, the electrodeposition technical qualification: current density is 200A/m
2,, NiCl
2The pH value of solution value is 2,60 ℃ of electrodeposition temperature.Electrowinning with insoluble anode prepares the 5N high purity nickel.Below the high purity nickel alkali metal containing element 0.1ppm, below 1ppm, below 0.1ppb, C is below 60ppm respectively for U, Th respectively for Fe, Co, Cr, and O is below 100ppm.High purity nickel part of impurity elements content sees Table 9.
Table 9 high purity nickel glow discharge spectrometry (GDMS) analytical results:
| Sequence number | Impurity element | 2# sample impurities analysis (ppm) |
| ????1 | ????Cu | ????＜0.4 |
| ????2 | ????Fe | ????0.11 |
| ????3 | ????Co | ????0.58 |
| ????4 | ????Pb | ????0.28 |
| ????5 | ????Zn | ????＜0.02 |
| ????6 | ????Cd | ????＜0.07 |
| ????7 | ????Bi | ????＜0.005 |
| ????8 | ????Sb | ????＜0.04 |
| ????9 | ????Sn | ????＜1.1 |
| ????10 | ????As | ????＜0.15 |
| ????11 | ????Al | ????0.004 |
| ????12 | ????Mg | ????＜0.005 |
| ????13 | ????Mn | ????＜0.005 |
| ????14 | ????Si | ????＜0.005 |
| ????15 | ????P | ????0.02 |
| ????16 | ????S | ????0.08 |
| High purity nickel impurity adds up to | ????＜3 | |
| High purity nickel decrement percentage composition | ????＞99.9997％ | |
Embodiment 4
Adopt the 3N electrolytic nickel, at the molten preparation NiCl of hydrochloric acid system electricity
2Solution, its electrical current density is 200A/m
2, electricity is molten to Solution H
+For 70A/m is adopted in the liquid making of 2g/l latter stage
2The current density liquid making, the pH that makes solution is 1; Solution C l
-Concentration reach 6mol/L, the solution impurity content sees Table 7:
Table 7-original solution impurity content unit: g/l
| Sequence number | Title | ????Co | ????Cu | ????Fe | ????Pb | ????Zn |
| 1 | Original solution | ????0.006 | ????0.002 | ????0.002 | ????0.001 | ????0.001 |
Carry out ion-exchange afterwards, the exchange current speed control is built in 1BV/h, and exchange back solution composition sees Table 8.
Solution impurity content unit: g/l after the table 8-ion-exchange
| Sequence number | Title | Co | ????Cu | ????Fe | ????Pb | ????Zn |
| ??1 | Ion-exchange purifies back liquid | ＜0.001* | ????0.0002 | ????＜0.001 | ????0.0002 | ????0.0001 |
Adopt the high-purity solutions after ion-exchange purifies, carry out electrowinning with insoluble anode, the electrodeposition technical qualification: control current density 160A/m
2, NiCl
2The pH value of solution value is 1,50 ℃ of electrodeposition temperature.Electrowinning with insoluble anode prepares the 5N high purity nickel.Below the high purity nickel alkali metal containing element 0.1ppm, below 1ppm, below 0.1ppb, C is below 60ppm respectively for U, Th respectively for Fe, Co, Cr, and O is below 100ppm.High purity nickel part of impurity elements content sees Table 9.
Table 9 high purity nickel glow discharge spectrometry (GDMS) analytical results:
| Sequence number | Impurity element | 2# sample impurities analysis (ppm) |
| ????1 | ????Cu | ????0.38 |
| ????2 | ????Fe | ????0.11 |
| ????3 | ????Co | ????0.6 |
| ????4 | ????Pb | ????0.3 |
| ????5 | ????Zn | ????＜0.02 |
| ????6 | ????Cd | ????＜0.07 |
| ????7 | ????Bi | ????＜0.005 |
| ????8 | ????Sb | ????＜0.04 |
| ????9 | ????Sn | ????＜1.2 |
| ????10 | ????As | ????0.13 |
| ????11 | ????Al | ????0.004 |
| ????12 | ????Mg | ????＜0.005 |
| ????13 | ????Mn | ????＜0.005 |
| ????14 | ????Si | ????＜0.005 |
| ????15 | ????P | ????0.02 |
| ????16 | ????S | ????0.08 |
| High purity nickel impurity adds up to | ????＜3 | |
| High purity nickel decrement percentage composition | ????＞99.9997％ | |
Claims (5)
1. method for preparing high purity nickel is characterized in that its technological process is followed successively by:
A. adopting hydrochloric acid system, is anode with the 3N electrolytic nickel, is negative electrode with corrosion-resistant titanium metal silk screen, the molten preparation NiCl of electricity
2Solution; The molten electrical current density of its electricity is 100A/m
2～200A/m
2, and molten at electricity to Solution H+adopt 30A/m latter stage for the liquid making of 1g/l～2g/l
2～70A/m
2The molten liquid making of current density electricity, the pH that makes solution is 1-3;
B. after the solution after will stripping feeds the active carbon column de-oiling, feed the ion exchange column of the mixed anion exchange resin that is respectively anionite-exchange resin 331,717, D301 and D401 more successively, carry out deep purifying, exchange flow rate control≤2BV/h, solution purification is reduced to below the 0.001g/l to containing Co, Fe, and solution contains Cu, Pb, Zn is reduced to below the 0.0002g/l;
C. the solution after ion-exchange being purified feeds electrolyzer and carries out electrodeposition, and control electrodeposition pH value of solution value is 1～3, current density 100A/m
2～200A/m
2, 40 ℃～60 ℃ of electric effusion temperature, simultaneously liquid behind the electrodeposition is extracted out, make solution in electrolyzer, weigh circulation, electrodeposition obtains high purity nickel.
2. will weigh according to right and ask 1 described a kind of method for preparing high purity nickel, it is characterized in that the solution after the electric molten liquid making adopts anion extractant that the broad liquid of electricity is carried out the extraction of three stage countercurrents, extraction phase was than 1: 2, and extraction equilibrium is used the pure water back extraction after 10 minutes.
3. will weigh according to right and ask 1 and 2 described a kind of methods that prepare high purity nickel, it is characterized in that adopting anion extractant by 20%～40% tertiary amine, 20%～45% fourth fat, surplus is formed for yellow kerosene.
4. require 1 described a kind of method for preparing high purity nickel according to right power, the organic phase that it is characterized in that its anion extractant is through after washing purifying, and it is saturated to adopt high purity hydrochloric acid to make organic phase carry out acid, again to NiCl
2Solution extracts.
5. ask 1 described a kind of method for preparing high purity nickel according to right power, it is characterized in that its solution is the de-oiling of tubular fibre ball.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100706482A CN1276129C (en) | 2004-07-28 | 2004-07-28 | Process for preparing high purity nickel |
| US11/658,626 US20090272651A1 (en) | 2004-07-28 | 2005-04-13 | Method for producing high-purity nickel |
| JP2007522898A JP4659829B2 (en) | 2004-07-28 | 2005-04-13 | Method to produce high purity nickel |
| PCT/CN2005/000488 WO2006010305A1 (en) | 2004-07-28 | 2005-04-13 | A method for producing high-purity nickel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100706482A CN1276129C (en) | 2004-07-28 | 2004-07-28 | Process for preparing high purity nickel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1587441A true CN1587441A (en) | 2005-03-02 |
| CN1276129C CN1276129C (en) | 2006-09-20 |
Family
ID=34604510
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100706482A Active CN1276129C (en) | 2004-07-28 | 2004-07-28 | Process for preparing high purity nickel |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US20090272651A1 (en) |
| JP (1) | JP4659829B2 (en) |
| CN (1) | CN1276129C (en) |
| WO (1) | WO2006010305A1 (en) |
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| CN101063210B (en) * | 2006-04-25 | 2010-05-26 | 襄樊化通化工有限责任公司 | Technique for producing high activity nickel cake with regeneration of waste material containing nickle as raw material |
| CN102268691A (en) * | 2011-08-04 | 2011-12-07 | 苏州晶纯新材料有限公司 | Method for producing high-purity nickel |
| CN102643990A (en) * | 2012-05-18 | 2012-08-22 | 南京大学 | Method for removing trace Cu in high-purity Ni by chelate resin |
| CN102995094A (en) * | 2011-09-19 | 2013-03-27 | 代芳 | Method for stabilizing metal ion concentration in electroplating bath |
| CN103046076A (en) * | 2012-12-26 | 2013-04-17 | 浙江华友钴业股份有限公司 | Preparation method of electrodeposited nickel |
| CN103320622A (en) * | 2013-07-18 | 2013-09-25 | 海南金亿新材料股份有限公司 | Technological process for preparing electronic-grade nickel methylsulfonate by utilization of nickel waste material |
| CN103726069A (en) * | 2012-10-13 | 2014-04-16 | 江西江锂科技有限公司 | Production method of novel electrolytic nickel |
| CN104018183A (en) * | 2014-05-30 | 2014-09-03 | 成都易态科技有限公司 | Soluble anode electrolysis production process of nickel |
| CN104611720A (en) * | 2015-01-28 | 2015-05-13 | 江苏理工学院 | Method for producing electrolytic nickel and recovering tin and iron from tin-nickel-iron alloy waste materials |
| CN105441974A (en) * | 2015-11-20 | 2016-03-30 | 金川集团股份有限公司 | Method for producing electrodeposited nickel |
| CN106283108A (en) * | 2016-08-31 | 2017-01-04 | 中南大学 | A kind of spent ion exchange resin is the method for deep copper removal from nickle electrolysis anode solution |
| CN108977669A (en) * | 2018-09-13 | 2018-12-11 | 中南大学 | A method of cadmium in high-concentration sulfuric acid cobalt liquor is removed in depth and recycles cadmium |
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| FR2208983B2 (en) * | 1972-12-01 | 1978-06-02 | Nickel Le | |
| CA1064856A (en) * | 1975-02-12 | 1979-10-23 | Alexander Illis | Purification of nickel electrolyte by electrolytic oxidation |
| US4203964A (en) * | 1977-07-20 | 1980-05-20 | Mx-Processer Reinhardt & Co. Ab | Re-extracting metal chloride complex from an organic extraction solution |
| US4956154A (en) * | 1988-03-09 | 1990-09-11 | Unc Reclamation | Selective removal of chromium, nickel, cobalt, copper and lead cations from aqueous effluent solutions |
| DE4110128A1 (en) * | 1990-04-09 | 1991-11-07 | Westinghouse Electric Corp | DECONTAMINATION OF RADIOACTIVELY ATTRACTED METALS |
| US5217585A (en) * | 1991-12-20 | 1993-06-08 | Westinghouse Electric Corp. | Transition metal decontamination process |
| JP2570076B2 (en) * | 1992-10-28 | 1997-01-08 | 住友金属鉱山株式会社 | Manufacturing method of high purity nickel |
| JPH11106842A (en) * | 1997-09-30 | 1999-04-20 | Nippon Mining & Metals Co Ltd | Method for washing copper electrolyte using solvent extraction method |
| JPH11152592A (en) * | 1997-11-18 | 1999-06-08 | Japan Energy Corp | Production of high purity nickel and high purity nickel material for forming thin film |
| JP2000219988A (en) * | 1999-02-01 | 2000-08-08 | Japan Energy Corp | Production of high purity nickel material and high purity nickel material for forming thin film |
| JP3151194B2 (en) * | 1999-03-19 | 2001-04-03 | 株式会社ジャパンエナジー | Cobalt purification method |
| AU2001266950A1 (en) * | 2000-06-30 | 2002-01-14 | Honeywell International, Inc. | Method and apparatus for processing metals, and the metals so produced |
| JP3876253B2 (en) * | 2001-08-01 | 2007-01-31 | 日鉱金属株式会社 | Manufacturing method of high purity nickel |
| JP2004043946A (en) * | 2002-05-21 | 2004-02-12 | Nikko Materials Co Ltd | Method and device for manufacturing high purity metal |
| RU2323007C2 (en) * | 2002-12-27 | 2008-04-27 | Эл Джи Хаусхолд Энд Хелс Кэа, Лтд. | Carbon nano-roll for deodorization |
-
2004
- 2004-07-28 CN CNB2004100706482A patent/CN1276129C/en active Active
-
2005
- 2005-04-13 WO PCT/CN2005/000488 patent/WO2006010305A1/en active Application Filing
- 2005-04-13 JP JP2007522898A patent/JP4659829B2/en active Active
- 2005-04-13 US US11/658,626 patent/US20090272651A1/en not_active Abandoned
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| CN101063210B (en) * | 2006-04-25 | 2010-05-26 | 襄樊化通化工有限责任公司 | Technique for producing high activity nickel cake with regeneration of waste material containing nickle as raw material |
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| CN102643990A (en) * | 2012-05-18 | 2012-08-22 | 南京大学 | Method for removing trace Cu in high-purity Ni by chelate resin |
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| CN104611720A (en) * | 2015-01-28 | 2015-05-13 | 江苏理工学院 | Method for producing electrolytic nickel and recovering tin and iron from tin-nickel-iron alloy waste materials |
| CN105441974A (en) * | 2015-11-20 | 2016-03-30 | 金川集团股份有限公司 | Method for producing electrodeposited nickel |
| CN106283108A (en) * | 2016-08-31 | 2017-01-04 | 中南大学 | A kind of spent ion exchange resin is the method for deep copper removal from nickle electrolysis anode solution |
| CN106283108B (en) * | 2016-08-31 | 2018-04-03 | 中南大学 | A kind of method of spent ion exchange resin deep copper removal from nickle electrolysis anode solution |
| CN108977669A (en) * | 2018-09-13 | 2018-12-11 | 中南大学 | A method of cadmium in high-concentration sulfuric acid cobalt liquor is removed in depth and recycles cadmium |
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| CN115573003A (en) * | 2022-10-12 | 2023-01-06 | 金川集团股份有限公司 | Preparation method of 6N ultra-pure nickel |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4659829B2 (en) | 2011-03-30 |
| JP2008507628A (en) | 2008-03-13 |
| US20090272651A1 (en) | 2009-11-05 |
| WO2006010305A1 (en) | 2006-02-02 |
| CN1276129C (en) | 2006-09-20 |
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