CN1110726A - Technology method of producing nickel foil with electrolysis method - Google Patents
Technology method of producing nickel foil with electrolysis method Download PDFInfo
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- CN1110726A CN1110726A CN 94104417 CN94104417A CN1110726A CN 1110726 A CN1110726 A CN 1110726A CN 94104417 CN94104417 CN 94104417 CN 94104417 A CN94104417 A CN 94104417A CN 1110726 A CN1110726 A CN 1110726A
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Abstract
The electrolytic deposition process for production of nickel foil in any size features that electrolytic nickel is used as anode, rotational titanium drum as cathode, its electrolyte contains NiSO4.7H2O (240-360g/l), NiCl2.6H2O (8-40 g/l) and H3BO3 (30-45 g/l) and has pH value of 1.8-3.4, and the overflow electrolyte after treatment may be cycllically used through controlled loop. Its advantages are high rate of finished products and low cost.
Description
The present invention relates to a kind of processing method of electrolysis production nickel foil, produce the processing method of nickel foil or rather with electrolytic deposition.
Nickel foil is industrial a kind of starting material such as electronics, telecommunication, instrument, in the last few years, demand to thin nickel foil grows with each passing day, range of application is more and more wider, nickel foil generally is it to be bonded on other material use when above-mentioned industrial application, and this just requires nickel foil not only high physical strength will be arranged, homogeneous thickness, and to have higher adhesiveproperties.
The method of producing nickel foil mainly contains two kinds of rolling process and electrolytic process (electrocasting).The forming process that rolling process is produced nickel foil is to thin by thick, produce thin nickel foil (for example thickness is less than 50 microns nickel foil), need repeatedly repeat-rolling, production process is long, the cost height, the width and the thickness of product all are very limited, and the adhesiveproperties of nickel foil is also poor, and the forming process that electrolytic process (electrocasting) is produced nickel foil is thick by being thinned to, but by the galvanic deposit once lumber-preserving, yield rate is higher, and tooling cost is low, especially is particularly suitable for the production of wide and thin nickel foil.
American documentation literature US3,963,587 introduced a kind of from the single nickel salt body lotion processing method of electrolysis production non junction ring-type nickel foil, its negative electrode is the aluminium roller with chromium surface, anode is a SDN nickel, electrolytic solution consist of total nickel 10.0-16.0 ounce/add human relations, muriate is with NiCl
2.6H
20 counts 0.9-4.5 ounce/add human relations, boric acid 4.5-6.0 ounce/add human relations, the PH of electrolytic solution is 3.8-4.1, the temperature of electrolytic solution is 140 °-160 °F, electrolytic solution also needs to add additive methyl benzenesulfonamide (2-MBSA), and cathode current density changes with process, and the ring-type nickel foil that is deposited on the roller takes off with temperature differential method, the thick 100-150 micron of paper tinsel, the girth of ring is the 300-2000 millimeter.
American documentation literature 4,290,858 narrated a kind of from containing 1,3, electrolysis production thickness is the method for 25-100 micron nickel foil in the single nickel salt body lotion of 6-naphthalene trisulfonic acid (NTSA) additive, its electrolytic solution consist of 75-90 gram/liter metallic nickel, 30-40 gram/liter boric acid, 4-6 gram/liter magnesium chloride, the pH value of electrolytic solution is 3.8-4.2, uses stainless steel cathode, anode SDN nickel, the current density of negative electrode is the 50-100 amperes per square meter, and the temperature 45-60 of electrolytic solution ℃ electrolytic solution purifies by ion exchange resin.
The Japanese documentation spy opens flat 1-222084 and has introduced a kind of processing method of producing the metal nickel foil, its electrolytic solution consist of NiSO
4.7H
2O 30 gram/liters, NiCl
2.6H
2O 45 gram/liters, H
3BO350 gram/liter, the pH value of electrolytic solution is 3.5-4.0, the temperature of electrolytic solution is 40-60 ℃, with stainless steel belt negative electrode, also contains brightening agent in the electrolytic solution, the current density 200-1000 amperes per square meter of negative electrode, the thickness of nickel foil is the 1-40 micron.
American documentation literature US3,844,906 have introduced the processing method that a kind of electrolytic process is produced nickel foil, electrolytic solution consist of total nickel 12.0-16.0 ounce/add human relations, NiX
26H
2O 0.11-0.23 mol/add human relations, boric acid 4.5-6.0 ounce/add human relations, the pH value of electrolytic solution is 3.8-4.9, and the current density of negative electrode is 200-500 ampere/square feet, and the temperature of electrolytic solution is 140-160 °F, also is with electrolytic process purifying electrolysis liquid.
Purpose of the present invention just is to work out a kind of high with roll-type rotating cathode continuous electrolysis production machinery intensity from the single nickel salt body lotion, thickness has the processing method than the belt nickel foil of high adhesion uniformly, the single nickel salt bath is formed the simplest in this processing method, the cathode current density height, can be with the electrolytic nickel scrap stock as anode, this process method equipment is simple, low processing cost.
A kind of electrolytic process of the present invention (electrocasting) is produced the processing method of nickel foil, makes anode with electrolytic nickel, electrolytic solution consist of NiSO
4.7H
2O 240-360 gram/liter, NiCl2.6H
2O 8-40 gram/liter, H
3BO
330-45 gram/liter, with rotatable titanium roller or rotatable stainless roller as negative electrode, under the rotation of negative electrode, carry out electrolytic deposition, place in the anode basket as the anodic electrolytic nickel, nickel electrowinning is deposited on the negative electrode, the pH value of electrolytic solution is 1.8-3.4, electrolytic solution overflows from the top of electrolyzer and carries out electrolytic cleaning, filter, after preheating makes the temperature of the electrolytic solution after the purification reach the temperature of electrolytic solution in the electrolyzer, enter electrolyzer from the bottom of electrolyzer, electrolytic solution equates with the flow that the electrolytic solution of preheating after purifying enters electrolyzer from the flow that electrolyzer overflows.
In electrolyting precipitation process, electrolytic solution is that 1-6 rice/be divided into is good in the polar region speed of circulation, and the temperature of electrolytic solution remains between 50-70 ℃ in electrolyting precipitation process, again being good at 61 °-70 ℃, the temperature of electrolytic solution is too low, it is big to be lower than 50 ℃ of nickel foil stress, and easily separates out hydrogen, produces hydrogen embrittlement, temperature is too high, be higher than 70 ℃, the vaporization losses of solution increases, and the composition of electrolytic solution is with NiSO
4.7H
2O 280-330 gram/liter, NiCl
2.6H
2O 10-35 gram/liter, H
3BO
338-45 gram/liter is good.
In electrolyting precipitation process, the size of the current density of negative electrode has remarkable influence to the quality of nickel foil, and at the bad mechanical property of low current density district nickel foil, this causes owing to the nickel foil crystal structure is thick; And in high current density region, the mechanical property of nickel foil descends, this is because the certain concentration polarization of polar region generation under high current density, cause subsalt on negative electrode, to be separated out, the nickel foil crystallization is loose, surface irregularity causes, so the current density of negative electrode is the 800-3000 amperes per square meter in electrolyting precipitation process, is good with the 1400-2200 amperes per square meter again.
The pH value of electrolytic solution also has remarkable influence to the electrolytic deposition of nickel and the quality of nickel foil, anodic current efficiency increases along with reducing of electrolyte PH value, illustrate that increasing acidity helps the anodic dissolving, cathode efficiency reduced when but pH value was low, the mechanical property of nickel foil is not good yet, this separates out on negative electrode and causes owing to hydrogen, it is many more that the high more hydrogen of acidity is separated out, the separating out of hydrogen on the one hand is accompanied by the generation of nickelous cyanide and dissociates, make nickel foil produce certain stress, the mechanical property variation, reduced the current efficiency of negative electrode simultaneously, the tensile strength of nickel foil descended when pH value was high, this is mixed in the nickel foil and causes owing to subsalt precipitation appears in the cathodic area, under same current density, in the low current density district, elongation δ (being unit elongation again) increases along with the increase of PH, in high current density region, elongation δ descends along with the increase of pH value, the pH value of taking all factors into consideration electrolytic solution is controlled at 1.8-3.4, again with at 2.4-3.4 for better, because the height of pH value, quality to nickel foil has bigger influence, so must control the pH value of electrolytic solution, with boric acid is buffer reagent, keeps solution-stabilized pH value, and boric acid can suppress the rapid rising of the pH value that cathodic process causes owing to separating out of nickel effectively, improve cathodic polarization simultaneously in addition, improve the effect of nickel foil performance, thus 30-45 gram/liter boric acid contained in the electrolytic solution, again to contain 38-45 gram/liter boric acid for well.
When making anode with electrolytic nickel, under the high cathode current density, be easy to produce anode passivation, must add a certain amount of anode activator nickelous chloride, chlorion produces certain activation to nickel anode, when nickelous chloride content hangs down, it is little that the nickel foil mechanical property is influenced by it, when nickelous chloride content is big, the tensile strength of nickel foil improves along with the increase of nickelous chloride content, nickelous chloride content is when 10-35 gram/liter, cathode efficiency and anodic current efficiency are the most approaching, and nickelous chloride can stabilizing ion concentration in this scope.When nickelous chloride content was increased to 55.6 gram/liters, nickel foil just may come off from negative electrode automatically in deposition process, and along with the increase of nickelous chloride content, nickel foil surface pockmark defective increases.
Strike is produced nickel foil, impurity in the electrolytic solution is to the production technique of nickel foil and the effectively big influence of quality of nickel foil, trace impurity iron, copper, zinc, the existence of nitrate radical and organic impurity, not only influential to the operation of process, and the mechanical property of nickel foil also had a significant impact, in addition, owing to use soluble anode, to produce the anode sludge inevitably, therefore except to raw material sulphuric acid nickel, have outside certain requirement as purity of raw materials such as anodic electrolytic nickels, also must make purifying treatment to electrolytic solution, the method of all knowing with the those of ordinary skill under this area purifies, to handle by charcoal absorption from the electrolytic solution that upper part of the electrolytic cell overflows, remove out organic impurity, carry out the electrolytic cleaning of low current density then, the low current density of its negative electrode is 0.1-0.5 ampere/square decimeter, adopt the undaform negative electrode in the purifying electrolysis groove, used for electrolyte woven dacron behind the electrolytic cleaning removes by filter small solid particulate, electrolytic solution after will purifying again gives heat to 50-70 ℃, be good with 61-70 ℃ again, enter electrolyzer from the bottom of electrolyzer, the flow that the electrolytic solution of purification preheating enters electrolyzer equates with the flow of the electrolytic solution to be clean that overflows from upper part of the electrolytic cell.
In order to be collected in the anode sludge in the electrolyting precipitation process, the anode basket that fills as the anodic electrolytic nickel is surrounded by the anode of being made by woven dacron outward, so that the anode sludge is removed by filter.
The electrolytic deposition of nickel foil is a rotatable titanium roller or rotatable stainless steel roller to be housed as negative electrode in one, electrolytic nickel (containing in the anode basket) is as anode, fill in the electrolyzer of nickel sulfate solution and carry out, be contained in the anode basket is that the scrap stock of electrolytic nickel are processed into alkynes or pie as the anodic electrolytic nickel, the anode basket is made of titanium, nickel sulfate electrolyte is controlled at (50-70 ℃ of certain temperature, be good with 61-70 ℃ again) and the control electrolytic solution speed of circulation certain in the polar region, under certain current density, carry out electrolysis, nickel ion is deposited on the cathode roller of slow rotation, peel off down nickel foil from cathode roller continuously again, wash by the method known to the one of ordinary skill in the art, oven dry, batch nickel foil and become the nickel foil of continuous rolling, in conditions such as current density one regularly, the rotating speed of cathode roller is made in adjusting, and produce the nickel foil of different thickness, the electrolytic solution continuous purification, recycle, anode nickel regular replenishment, pole span can be controlled between 25 millimeters-50 millimeters.
Processing method of the present invention not only can be used for the manufacturing of nickel foil, also can be used for the production of various foils such as Copper Foil, iron foil.
The advantage of the inventive method just is:
1. processing method of the present invention adopted rotatable titanium roller or rotatable stainless steel roller as negative electrode can the continuous production all lengths, the nickel foil of various width, all thickness, the nickel foil of 15 microns, 25 microns, 50 microns, 100 microns of thickness etc. for example, the temperature of electrolytic solution is controlled at 50-70 ℃, electrolytic solution PH is processing condition such as 1.8-3.4, the nickel foil physical strength height of producing, thickness deviation is little to have higher adhesiveproperties again, anodic current efficiency anodic current efficiency height, visual appearance is good, the cleaning of nickel foil smooth surface.
2. the single nickel salt body lotion that processing method of the present invention adopted is formed the simplest, the additive that does not add any organic substance, brightening agent etc., with the scrap stock of electrolytic nickel as anode, cheap, reduced tooling cost, corrosion-resistant as negative electrode with rotatable titanium roller, rotatable stainless steel roller, the life-span is long, adopted big cathode current density, the output height of nickel foil in the unit time.
3. technological process apparatus of the present invention is simple, the yield rate height of nickel foil, and tooling cost is low.
Fig. 1 cell construction synoptic diagram
1. be the rotatable titanium roller (-) as negative electrode, the arrow that is drawn is the turning direction of negative electrode.2. for filling the titanium anode basket (+) as the anodic electrolytic nickel, 3. be electrolyzer, 4 is winder, and 5 is nickel foil, 6 the imports that enter electrolyzer (arrow is the electrolytic solution approach axis) for electrolytic solution through purifying preheating, and 7 is the electrolytic solution overflow port of electrolyzer.(arrow is that electrolytic solution overflows direction).
With following embodiment processing method of the present invention is further described, will helps understanding, and not as the qualification to protection domain of the present invention, protection scope of the present invention is decided by claims the present invention and advantage thereof.
Embodiment 1
The cell construction synoptic diagram is seen Fig. 1.Make anode with electrolytic nickel, place as the anodic electrolytic nickel in the anode basket of titanium silk establishment, purity as No. 1 electrolytic nickel of anodic is 99.6%, be processed into bulk by the electrolytic nickel scrap stock, with rotatable titanium roller as negative electrode, rotatable titanium roller as negative electrode is made surface finish smooth finish by pure titanium soil weld through shear spinning
10, the titanium roller is of a size of 350 * 400 millimeters of Φ, and electrolyzer is made by acrylic plastering, electrolytic solution consist of NiSO
4.7H
2O 340 gram/liters, NiCl
2.6H
2O 25 gram/liters, H
3BO
335 gram/liters, used single nickel salt, nickelous chloride is a technical pure, boric acid is chemical pure, the pH value of keeping electrolytic solution is 3.0, electrolytic solution overflows from the top of electrolyzer, handle by charcoal absorption, remove organic impurity, carry out electrolytic cleaning again, the current density of control cathode is 0.3 ampere/square decimeter during electrolytic cleaning, negative electrode in the purifying electrolysis groove adopts the undaform negative electrode, used for electrolyte woven dacron behind the electrolytic cleaning removes by filter small solid particulate, give heat again to 62 ± 1 ℃, enter electrolyzer from the bottom of electrolyzer, the flow that electrolytic solution overflows from the top of electrolyzer equates with the flow that the electrolytic solution that gives heat through electrolytic cleaning enters electrolyzer, dipolar pole span is 50 millimeters, nickel sulfate electrolyte is controlled at 62 ° ± 1 ℃, the speed of circulation of control electrolytic solution in the polar region is 5 meters/minute, the current density of negative electrode is that 2200 amperes per square meter are carried out electrolytic deposition, nickel ion is deposited on the titanium roller as negative electrode of slow rotation, peel off nickel foil from the titanium roller again, wash with deionized water, nickel foil is batched in oven dry, become the nickel foil of continuous rolling, 400 millimeters of the width of nickel foil, 500 meters long, and thickness is 25 microns, thickness deviation＜± 4%, tensile strength 850N/mm
2, the tensile strength and the unit elongation of unit elongation (elongation) δ 3.5%(nickel foil make extensibility δ test on the AG-25TA machine again), bonding force 1.4kgf/cm, yield rate 95%, cathodic electricity efficient 92%, nickel foil purity 99.8%, pin hole＜1 hole/square metre, smooth in appearance, cleaning.
Embodiment 2
Its working method and equipment and embodiment 1 are same, and that only different is the NiSO that consists of of electrolytic solution
4.6H
2O 260 gram/liters, NiCl
2.6H
2O 15 gram/liters, H
3BO
330 gram/liters, the pH value of keeping electrolytic solution is 3.4, the current density of control cathode is 0.25 ampere/square decimeter during electrolytic cleaning, electrolytic solution behind the electrolytic cleaning gives heat to 64 ± 1 ℃, enter electrolyzer from the bottom of electrolyzer, dipolar pole span is 25 millimeters, electrolytic solution is controlled at 64 ° ± 1 ℃, the speed of circulation of control electrolytic solution in the polar region is 4 meters/minute, the current density of negative electrode is that 1200 amperes per square meter are carried out electrolytic deposition, 400 millimeters of the width of nickel foil, thickness are 50 microns, thickness deviation＜± 5%, tensile strength 750N/mm
2, unit elongation (elongation) δ＞4.0%, bonding force 1.2kgf/cm, smooth in appearance, cleaning.
Embodiment 3
Its working method and equipment and embodiment 1 are same, and that only different is the NiSO that consists of of electrolytic solution
4.7H
2O 360 gram/liters, NiCl
2.6H
2O 40 gram/liters, H
3BO
340 gram/liters, the pH value of keeping electrolytic solution is 2.2, the cathode current density of controlling during electrolytic cleaning is 0.45 ampere/square decimeter, electrolytic solution behind the electrolytic cleaning gives heat to 67 ± 1 ℃, enter electrolyzer from the bottom of electrolyzer, dipolar pole span is 50 millimeters, the temperature of electrolytic solution is controlled at 67 ° ± 1 ℃, the speed of circulation of control electrolytic solution in the polar region is 2.5 meters/minute, the current density of negative electrode is that 2600 amperes per square meter are carried out electrolytic deposition, and 400 millimeters of the width of nickel foil, thickness are 100 microns, long 500 meters, thickness deviation＜± 5%, tensile strength 1000N/mm
2, unit elongation (elongation) δ＞3.5%, bonding force 1.3kgf/cm, smooth in appearance, cleaning.
Claims (10)
1, a kind of processing method of method of producing nickel foil with electrolysis is made anode with electrolytic nickel, it is characterized in that, (1) electrolytic solution consist of NiSO
4.7H
2O 240-360 gram/liter, NiCl2.6H
2O 8-40 gram/liter, H
3BO
330-45 gram/liter,
(2) with rotatable titanium roller or rotatable stainless steel roller as negative electrode, under the rotation of negative electrode, carry out electrolytic deposition, place in the anode basket as the anodic electrolytic nickel,
(3) pH1.8-3.4 of electrolytic solution,
(4) electrolytic solution overflows from the top of electrolyzer and carries out electrolytic cleaning, filter, give after heat makes the temperature of the electrolytic solution after the purification reach the temperature of electrolytic solution in the electrolyzer, enter electrolyzer from the bottom of electrolyzer, electrolytic solution equates with the flow that the electrolytic solution that gives heat after purifying enters electrolyzer from the flow that electrolyzer overflows.
2, according to the processing method of a kind of method of producing nickel foil with electrolysis of claim 1, it is characterized in that, in electrolyting precipitation process, electrolytic solution the polar region speed of circulation be 1-6 rice/minute.
3, according to the processing method of a kind of method of producing nickel foil with electrolysis of claim 1, it is characterized in that the temperature of electrolytic solution remains on 50-70 ℃ in electrolyting precipitation process.
4, according to the processing method of a kind of method of producing nickel foil with electrolysis of claim 3, it is characterized in that the temperature of electrolytic solution remains on 61-70 ℃ in electrolyting precipitation process.
5, according to the processing method of a kind of method of producing nickel foil with electrolysis of claim 1, it is characterized in that in the process of electrolytic deposition, the current density of negative electrode is the 800-3000 amperes per square meter.
6, according to the processing method of a kind of method of producing nickel foil with electrolysis of claim 5, it is characterized in that in the process of electrolytic deposition, the current density of negative electrode is the 1400-2200 amperes per square meter.
7, according to the processing method of a kind of method of producing nickel foil with electrolysis of claim 1, it is characterized in that the pH value of electrolytic solution is controlled at 2.4-3.4.
8, according to the processing method of a kind of method of producing nickel foil with electrolysis of claim 1, it is characterized in that, electrolytic solution consist of NiSO
4.7H
2O 280-330 gram/liter, NiCl
2.6H
2O 10-35 gram/liter, H
3BO
338-45 gram/liter,
9, according to the processing method of a kind of method of producing nickel foil with electrolysis of claim 1, it is characterized in that, the electrolytic solution that overflows from upper part of the electrolytic cell passes through activated carbon treatment, current density with negative electrode is after 0.1-0.5 ampere/square decimeter carries out electrolytic cleaning again, filter with woven dacron, give heat to 50-70 ℃.
10, according to the processing method of a kind of method of producing nickel foil with electrolysis of claim 1, it is characterized in that, fill the anode of the woven dacron system that is surrounded by as the anode basket of anodic electrolytic nickel outward.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN94104417A CN1042150C (en) | 1994-04-25 | 1994-04-25 | Technology method of producing nickel foil with electrolysis method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN94104417A CN1042150C (en) | 1994-04-25 | 1994-04-25 | Technology method of producing nickel foil with electrolysis method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1110726A true CN1110726A (en) | 1995-10-25 |
| CN1042150C CN1042150C (en) | 1999-02-17 |
Family
ID=5031574
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN94104417A Expired - Lifetime CN1042150C (en) | 1994-04-25 | 1994-04-25 | Technology method of producing nickel foil with electrolysis method |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101864583A (en) * | 2010-05-14 | 2010-10-20 | 昆山延笙电子科技有限公司 | Filter bag used outside platinum titanium mesh |
| CN101037778B (en) * | 2007-02-07 | 2010-11-03 | 吉林大学 | Technical method for sampling prick by electric plating and special device thereof |
| CN102321896A (en) * | 2011-09-09 | 2012-01-18 | 北京工业大学 | Nanocrystalline nickel with high-density twin structure and preparation method thereof |
| CN102995085A (en) * | 2012-11-29 | 2013-03-27 | 烟台晨煜电子有限公司 | Method for producing roughened nickel foil by electrolytic process |
| CN103031578A (en) * | 2012-11-29 | 2013-04-10 | 烟台晨煜电子有限公司 | Electrolysis method for producing nickel foil |
| CN108103533A (en) * | 2017-12-28 | 2018-06-01 | 安徽迈德福新材料有限责任公司 | The technique that a kind of electrodeposition process prepares nickel foil |
| CN108866582A (en) * | 2018-07-13 | 2018-11-23 | 安徽迈德福新材料有限责任公司 | A kind of technique of electrodeposition process preparation roughening nickel foil |
| TWI771606B (en) * | 2019-06-10 | 2022-07-21 | 日商日鐵工材股份有限公司 | Metal foil production apparatus |
| TWI785154B (en) * | 2017-12-08 | 2022-12-01 | 日商日鐵工材股份有限公司 | Metal foil production apparatus and electrode plate mounting body |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1421818A (en) * | 1972-05-08 | 1976-01-21 | Xerox Corp | Nickel electroforming process |
| US4290858A (en) * | 1980-09-23 | 1981-09-22 | The United States Of America As Represented By The United States Department Of Energy | Process for forming a nickel foil with controlled and predetermined permeability to hydrogen |
| JPH01222084A (en) * | 1988-02-29 | 1989-09-05 | Nisshin Steel Co Ltd | Continuous production of metallic foil |
| AT394215B (en) * | 1988-11-15 | 1992-02-25 | Andritz Ag Maschf | METHOD FOR ELECTROLYTICALLY PRODUCING A METAL FILM |
-
1994
- 1994-04-25 CN CN94104417A patent/CN1042150C/en not_active Expired - Lifetime
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101037778B (en) * | 2007-02-07 | 2010-11-03 | 吉林大学 | Technical method for sampling prick by electric plating and special device thereof |
| CN101864583A (en) * | 2010-05-14 | 2010-10-20 | 昆山延笙电子科技有限公司 | Filter bag used outside platinum titanium mesh |
| CN102321896A (en) * | 2011-09-09 | 2012-01-18 | 北京工业大学 | Nanocrystalline nickel with high-density twin structure and preparation method thereof |
| CN102995085A (en) * | 2012-11-29 | 2013-03-27 | 烟台晨煜电子有限公司 | Method for producing roughened nickel foil by electrolytic process |
| CN103031578A (en) * | 2012-11-29 | 2013-04-10 | 烟台晨煜电子有限公司 | Electrolysis method for producing nickel foil |
| CN102995085B (en) * | 2012-11-29 | 2014-12-31 | 烟台晨煜电子有限公司 | Method for producing roughened nickel foil by electrolytic process |
| CN103031578B (en) * | 2012-11-29 | 2016-08-31 | 烟台晨煜电子有限公司 | A kind of electrolytic method producing nickel foil |
| TWI785154B (en) * | 2017-12-08 | 2022-12-01 | 日商日鐵工材股份有限公司 | Metal foil production apparatus and electrode plate mounting body |
| CN108103533A (en) * | 2017-12-28 | 2018-06-01 | 安徽迈德福新材料有限责任公司 | The technique that a kind of electrodeposition process prepares nickel foil |
| CN108866582A (en) * | 2018-07-13 | 2018-11-23 | 安徽迈德福新材料有限责任公司 | A kind of technique of electrodeposition process preparation roughening nickel foil |
| TWI771606B (en) * | 2019-06-10 | 2022-07-21 | 日商日鐵工材股份有限公司 | Metal foil production apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1042150C (en) | 1999-02-17 |
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