CN113445117A - Electrolytic method and device for removing metallic cobalt in polycrystalline diamond compact - Google Patents
Electrolytic method and device for removing metallic cobalt in polycrystalline diamond compact Download PDFInfo
- Publication number
- CN113445117A CN113445117A CN202110726561.XA CN202110726561A CN113445117A CN 113445117 A CN113445117 A CN 113445117A CN 202110726561 A CN202110726561 A CN 202110726561A CN 113445117 A CN113445117 A CN 113445117A
- Authority
- CN
- China
- Prior art keywords
- polycrystalline diamond
- diamond compact
- electrolytic
- cobalt
- removing metallic
- 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.)
- Pending
Links
- 229910003460 diamond Inorganic materials 0.000 title claims abstract description 66
- 239000010432 diamond Substances 0.000 title claims abstract description 66
- 229910017052 cobalt Inorganic materials 0.000 title claims abstract description 57
- 239000010941 cobalt Substances 0.000 title claims abstract description 57
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 title claims abstract description 57
- 238000000034 method Methods 0.000 title claims description 24
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 32
- 239000003792 electrolyte Substances 0.000 claims abstract description 17
- 238000006243 chemical reaction Methods 0.000 claims abstract description 15
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 14
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 14
- 239000001103 potassium chloride Substances 0.000 claims description 7
- 235000011164 potassium chloride Nutrition 0.000 claims description 7
- 239000011780 sodium chloride Substances 0.000 claims description 7
- 239000000758 substrate Substances 0.000 claims description 7
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 6
- 229910052802 copper Inorganic materials 0.000 claims description 6
- 239000010949 copper Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 239000007864 aqueous solution Substances 0.000 claims description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 4
- 239000000741 silica gel Substances 0.000 claims description 4
- 229910002027 silica gel Inorganic materials 0.000 claims description 4
- 239000012153 distilled water Substances 0.000 claims description 3
- 238000009413 insulation Methods 0.000 claims description 2
- 229910052697 platinum Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000008151 electrolyte solution Substances 0.000 claims 1
- 238000005260 corrosion Methods 0.000 abstract description 6
- 230000007797 corrosion Effects 0.000 abstract description 6
- 229910052751 metal Inorganic materials 0.000 description 11
- 239000002184 metal Substances 0.000 description 11
- 230000008901 benefit Effects 0.000 description 6
- 229910045601 alloy Inorganic materials 0.000 description 5
- 239000000956 alloy Substances 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 229910052726 zirconium Inorganic materials 0.000 description 4
- 230000010287 polarization Effects 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- 238000001228 spectrum Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000003411 electrode reaction Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 230000036632 reaction speed Effects 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 238000010008 shearing Methods 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000003841 chloride salts Chemical class 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical class Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F3/00—Electrolytic etching or polishing
- C25F3/02—Etching
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F7/00—Constructional parts, or assemblies thereof, of cells for electrolytic removal of material from objects; Servicing or operating
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
Abstract
The invention discloses an electrolysis method for removing metallic cobalt in a polycrystalline diamond compact, which comprises the following steps: placing an electrolytic cell for electrolyzing the polycrystalline diamond to remove cobalt in an ultrasonic environment for electrolytic reaction; the invention also discloses an electrolysis device for removing metallic cobalt in the polycrystalline diamond compact, which comprises: the electrolytic cell comprises an anode polycrystalline diamond compact, a cathode inert electrode, electrolyte, a power supply and an inner shell. According to the invention, the attachments on the surface of the electrode are removed in time through ultrasonic sound intensity, the corrosion rate is effectively increased, and the cobalt content of the obtained polycrystalline diamond compact is less than 1.03 percent and is lower than the electrolytic cobalt content in a common environment.
Description
Technical Field
The invention relates to the technical field of cobalt removal of diamond compacts. More particularly, the present invention relates to an electrolytic method and apparatus for removing metallic cobalt from polycrystalline diamond compacts.
Background
Polycrystalline Diamond Compacts (PDC) are formed by sintering diamond particles and a sintering catalyst on a cemented carbide substrate at high temperature and high pressure, wherein metallic cobalt is a common sintering catalyst. Because the thermal expansion coefficients of the metal cobalt and the diamond particles are different greatly, the PDC can be damaged by heat in the working process, and the metal cobalt can catalyze the carbon to be converted from the diamond state to the graphite state at high temperature, so that the service life of the PDC is shortened, and therefore, the metal cobalt in the PDC needs to be removed by adopting a necessary means before the PDC is used.
Among the existing cobalt removal methods, the electrolytic cobalt removal method has the advantages of small pollution, mild reaction, low cost and the like. However, in the current electrolytic cobalt removal research, the electrolytic cobalt removal effect is poor, and the wear resistance of the polycrystalline diamond compact cannot be well improved.
Disclosure of Invention
An object of the present invention is to solve at least the above problems and to provide at least the advantages described later.
The invention also aims to provide an electrolysis method for removing metallic cobalt in the polycrystalline diamond compact, the cobalt removal treatment of the polycrystalline diamond compact by adopting the electrolysis method can increase the corrosion efficiency of the metallic cobalt in the diamond layer, remove the attachments on the surface of the anode generated in the electrolysis process in time, and ensure that the cobalt content of the cobalt-removed diamond layer is 1.03%. The invention also provides an electrolysis device for removing the metallic cobalt in the polycrystalline diamond compact.
To achieve these objects and other advantages in accordance with the purpose of the invention, an electrolytic method for removing metallic cobalt from a polycrystalline diamond compact is provided, comprising the steps of: and placing the electrolytic cell for electrolyzing the polycrystalline diamond to remove cobalt in an ultrasonic environment for electrolytic reaction.
Preferably, the conditions of the electrolysis reaction include: the ultrasonic power is 0.1-2.0kW, the working frequency is 20-50kHz, the voltage is 0-8V, the temperature is 20-40 ℃, and the time is 5-40 h.
Preferably, the hard alloy substrate of the polycrystalline diamond compact is treated with a silica gel insulation coating.
Preferably, the polycrystalline diamond compact is used as an anode of the electrolytic cell, the inert electrode is used as a cathode of the electrolytic cell, the electrolyte in the electrolytic cell is composed of a sodium chloride aqueous solution and a potassium chloride aqueous solution, and the cathode and the anode are respectively immersed in the electrolyte after being connected with a power supply.
Preferably, the inert electrode is made of one of stainless steel, copper or platinum.
Preferably, the concentration of sodium chloride in the electrolyte is 1-10g/100mL, and the concentration of potassium chloride is 1-20g/100 mL.
Preferably, after the electrolysis reaction is finished, the polycrystalline diamond compact is taken out, cleaned by using distilled water in an ultrasonic environment, and dried.
The invention also provides an electrolysis device for removing metallic cobalt in the polycrystalline diamond compact, which comprises: the electrolytic cell comprises an anode polycrystalline diamond compact, a cathode inert electrode, electrolyte, a power supply and an inner shell.
Preferably, a heating rod is further arranged in the shell, and the heating rod is connected with a temperature controller.
The invention at least comprises the following beneficial effects:
in the process of carrying out the electrolytic reaction, the invention adopts common inorganic salt as the electrolyte, and has the advantages of environmental protection, safety and good economic benefit compared with other acidic or alkaline electrolytes;
before the electrolytic reaction, the hard alloy substrate is wrapped by silica gel to avoid contacting electrolyte, so that the hard alloy substrate of the polycrystalline diamond composite sheet is prevented from being corroded;
the 'cavity' effect of ultrasonic sound intensity can eliminate uneven local concentration in the electrolytic process, improve the reaction speed, stimulate the formation of new phases and play a role in shearing aggregates;
the ultrasonic wave can play a role in promoting the anode reaction in the electrolytic cobalt removal of the polycrystalline diamond compact;
the ultrasonic wave continuously cleans the surface of the electrode in the electrolytic process, so that the metal cobalt is not covered and shielded by attachments, the dissolving degree of the metal cobalt on the surface is increased, and the reaction rate is accelerated.
Additional advantages, objects, and features of the invention will be set forth in part in the description which follows and in part will become apparent to those having ordinary skill in the art upon examination of the following or may be learned from practice of the invention.
Drawings
FIG. 1 is an as-received scanning electron micrograph of an untreated PDC according to example 1 of the present invention;
FIG. 2 is a diagram of the distribution of elements of FIG. 1;
FIG. 3 is a diagram of the energy spectrum peak and the content of each element in FIG. 1 and FIG. 2;
FIG. 4 is Tafel anode polarization curve of example 2 of the present invention, in which two curves represent the electrolysis effect in the ultrasonic electrolysis environment and the normal electrolysis environment, respectively;
FIG. 5 is a scanning electron microscope image of the PDC after ultrasonic electrolysis in example 3 of the present invention;
FIG. 6 is a diagram of the corresponding elements of FIG. 5;
FIG. 7 is a diagram of the energy spectrum peaks and contents of the elements in FIGS. 5 and 6;
FIG. 8 is a scanning electron micrograph of a PDC after general electrolysis according to example 4 of the present invention;
FIG. 9 is a graph of the corresponding element distribution of FIG. 8;
FIG. 10 is a diagram of the peak energy spectrum and the content of each element in FIGS. 8 and 9;
FIG. 11 is a schematic view of the structure of an ultrasonic electrolyzing apparatus according to the present invention.
Detailed Description
The invention provides an electrolysis method for removing metallic cobalt from a polycrystalline diamond compact, which comprises the step of placing an electrolytic cell for electrolyzing polycrystalline diamond to remove cobalt in an ultrasonic environment for an electrolysis reaction, wherein the ultrasonic electrolysis method is suitable for the acidic, neutral or alkaline environment. Wherein the electrolytic cell is composed of: taking a PCD layer of the polycrystalline diamond compact as an anode; the copper sheet is taken as a cathode, and the cathode and the anode are respectively immersed in the electrolyte after being connected with a power supply.
In the present invention, the conditions of the electrolysis reaction include: the ultrasonic power is 0.1-2.0kW, the working frequency is 20-50kHz, the voltage is 0-8V, the temperature is 20-40 ℃, and the time is 5-40 h.
In the invention, in order to avoid the corrosion of the hard alloy substrate of the polycrystalline diamond compact, the hard alloy substrate is wrapped by silica gel before the electrolytic reaction is carried out so as to avoid the contact with electrolyte. During electrolysis, all metal catalysts in the PDC composite sheet can be electrolyzed, not only cobalt, which is the most commonly used metal catalyst, and thus, the skilled artisan conventionally considers the process of removing the catalyst as a decobalting treatment.
In the invention, the 'cavity' action of ultrasonic sound intensity can eliminate uneven local concentration in the electrolytic process, improve the reaction speed, stimulate the formation of new phases and play a role in shearing aggregates generated in the electrolytic reaction process. The agglomerates refer to hydroxides or chlorides formed by metal cations generated during electrolysis and anions in a solution, and are agglomerated or flocculent to some extent.
According to the invention, an electrochemical workstation is used for measuring a Tafel anode polarization curve in a long potential interval, and the result shows that the electrolytic reaction of the polycrystalline diamond compact is more violent in an ultrasonic environment, and the ultrasonic wave can play a role in promoting the anode reaction in the electrolytic cobalt removal of the polycrystalline diamond compact.
In the invention, after the electrolytic reaction is finished, the polycrystalline diamond compact is taken out, the surface of the polycrystalline diamond compact is cleaned by distilled water in an ultrasonic environment, and the polycrystalline diamond compact is dried. The surface of the polycrystalline diamond compact electrolyzed in the ultrasonic environment is free of attachments, and the ultrasonic wave continuously cleans the surface of the electrode in the electrolysis process, so that the metal cobalt is not covered and shielded by the attachments, the dissolution degree of the metal cobalt on the surface is increased, and the reaction rate is accelerated.
The present invention is further described in detail below with reference to examples so that those skilled in the art can practice the invention with reference to the description.
It is to be noted that the experimental methods described in the following embodiments are all conventional methods unless otherwise specified, and the reagents and materials are commercially available unless otherwise specified.
Evaluating the influence of ultrasonic waves on the removal of metal cobalt from the polycrystalline diamond by using a volt-ampere linear scanning method of an electrochemical workstation; the porosity after cobalt removal is analyzed and calculated by a femaly scanning electron microscope and ImageJ2x software, and the weight percentages of the elements before and after cobalt removal are determined by a field emission scanning electron microscope
< example 1>
Polycrystalline diamond compacts that have not been subjected to an electrolytic decobalting process are polycrystalline diamond compacts that we have purchased commercially.
The polycrystalline diamond compact without electrolytic cobalt removal treatment has the weight percentage of cobalt of 6.13 and the weight percentage of zirconium of 4.16, as shown in figures 1-3.
< example 2>
The polycrystalline diamond compact is used as an anode, copper is used as a cathode, and a saturated calomel electrode is used as a reference electrode. The concentration of sodium chloride in the electrolyte is 1-10g/100mL, and the concentration of potassium chloride is 1-20g/100 mL. The initial potential was set at-8.0V relative to the reference electrode and the final potential was 8.0V. As shown in fig. 4, in a common environment, as the electrode potential increases, the corrosion current density of the polycrystalline diamond compact is basically unchanged and tends to be a horizontal straight line, the electrode reaction is very weak, and the polycrystalline diamond compact is purchased commercially in the common environment. However, when the polycrystalline diamond compact is electrolyzed in an ultrasonic environment, when the electrode potential tends to a positive value, the corrosion current of the anodic polarization curve starts to increase obviously, and the electrode reaction is severe. The higher the current density is, the faster the electrolysis speed is, that is to say, under the ordinary electrolysis condition, the electrolysis speed is almost zero under the tested voltage condition, and under the ultrasonic environment, the electrolysis speed is obviously improved within the voltage range of 0-3V.
< example 3>
The polycrystalline diamond compact is used as an anode, and the copper is used as a cathode. The electrolyte comprises the following components: 3g/100mL of sodium chloride and 5g/100mL of potassium chloride. Electrolyzing under ultrasonic environment, wherein the voltage of the constant voltage source is 3V, and the electrolysis time is 12 h. And cleaning the polycrystalline diamond for 4 hours after electrolysis, and drying for 2 hours. After cobalt removal, the weight percentage of cobalt is 1.03%, the weight percentage of zirconium is 2.14, and no oxide is attached, as shown in fig. 5-7.
< example 4>
The polycrystalline diamond compact is used as an anode, and the copper is used as a cathode. The electrolyte comprises the following components: 3g/100mL of sodium chloride and 5g/100mL of potassium chloride. And electrolyzing under a common environment, wherein the voltage of the constant voltage source is 3.5V, and the electrolysis time is 36 h. And cleaning the polycrystalline diamond for 4 hours after electrolysis, and drying for 2 hours. After cobalt removal, the weight percentage of cobalt is 8.29, the weight percentage of oxygen is 11.04, the cobalt and the zirconium are in cross distribution, the weight percentage of zirconium is 1.44, and the oxide adhesion is obvious, as shown in figures 8-10.
After cobalt removal is completed in examples 3 to 4, the ratio of each element in the polycrystalline diamond compact is shown in table 1.
TABLE 1
As can be seen from fig. 1 to 10 and table 1, the method of the present invention has a good cobalt removal effect on a polycrystalline diamond compact by electrolysis, the corrosion current increase in an ultrasonic environment is significant, the surface porosity is increased, the attachment is reduced, and the cobalt weight percentage is 1.03%, which indicates that the present invention has a good cobalt removal effect.
The invention also provides an electrolysis device for removing metallic cobalt in a polycrystalline diamond compact, as shown in fig. 11, comprising: the electrolytic cell comprises an outer shell 1, medium water 2, an ultrasonic generator 3 and an electrolytic cell, wherein the outer shell 1 is internally filled with the medium water 2, the ultrasonic generator 3 and the electrolytic cell, and the electrolytic cell consists of an anode polycrystalline diamond compact 4, a cathode inert electrode 5, electrolyte 6, a power supply and an inner shell 7. Still be provided with heating rod 8 in the shell 1, heating rod 8 is connected with temperature controller 9.
While embodiments of the invention have been described above, it is not limited to the applications set forth in the description and the embodiments, which are fully applicable to various fields of endeavor for which the invention may be embodied with additional modifications as would be readily apparent to those skilled in the art, and the invention is therefore not limited to the details given herein and to the embodiments shown and described without departing from the generic concept as defined by the claims and their equivalents.
Claims (9)
1. An electrolytic method for removing metallic cobalt from a polycrystalline diamond compact, comprising the steps of: and placing the electrolytic cell for electrolyzing the polycrystalline diamond to remove cobalt in an ultrasonic environment for electrolytic reaction.
2. The electrolytic method for removing metallic cobalt from a polycrystalline diamond compact of claim 1, wherein the conditions of the electrolytic reaction comprise: the ultrasonic power is 0.1-2.0kW, the working frequency is 20-50kHz, the voltage is 0-8V, the temperature is 20-40 ℃, and the time is 5-40 h.
3. The electrolytic method for removing metallic cobalt from a polycrystalline diamond compact of claim 1, wherein the cemented carbide substrate of the polycrystalline diamond compact is treated with a silica gel insulation pack.
4. The electrolytic method for removing metallic cobalt from a polycrystalline diamond compact of claim 1, wherein the electrolytic cell uses the polycrystalline diamond compact as an anode and an inert electrode as a cathode, the electrolyte in the electrolytic cell is composed of an aqueous solution of sodium chloride and an aqueous solution of potassium chloride, and the cathode and the anode are respectively immersed in the electrolyte after being connected with a power supply.
5. The electrolytic method for removing metallic cobalt from a polycrystalline diamond compact of claim 4, wherein the inert electrode is one of stainless steel, copper, or platinum.
6. The electrolytic method for removing metallic cobalt from a polycrystalline diamond compact of claim 4, wherein the electrolyte solution comprises sodium chloride at a concentration of 1-10g/100mL and potassium chloride at a concentration of 1-20g/100 mL.
7. The electrolytic method according to claim 4, wherein after the electrolysis reaction is completed, the polycrystalline diamond compact is taken out, cleaned with distilled water in an ultrasonic environment, and dried.
8. An electrolytic device for removing metallic cobalt from a polycrystalline diamond compact, comprising: the electrolytic cell comprises an anode polycrystalline diamond compact, a cathode inert electrode, electrolyte, a power supply and an inner shell.
9. The electrolyzer of claim 8 wherein a heater rod is further disposed within the housing, the heater rod being connected to a temperature controller.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110726561.XA CN113445117A (en) | 2021-06-29 | 2021-06-29 | Electrolytic method and device for removing metallic cobalt in polycrystalline diamond compact |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110726561.XA CN113445117A (en) | 2021-06-29 | 2021-06-29 | Electrolytic method and device for removing metallic cobalt in polycrystalline diamond compact |
Publications (1)
Publication Number | Publication Date |
---|---|
CN113445117A true CN113445117A (en) | 2021-09-28 |
Family
ID=77813850
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110726561.XA Pending CN113445117A (en) | 2021-06-29 | 2021-06-29 | Electrolytic method and device for removing metallic cobalt in polycrystalline diamond compact |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN113445117A (en) |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1962957A (en) * | 2006-11-02 | 2007-05-16 | 中国地质大学(武汉) | Method for ultrasonic electroplating of diamond drilling bit |
CN102134737A (en) * | 2011-04-28 | 2011-07-27 | 上海理工大学 | Method for preparing porous silicon |
US20130001100A1 (en) * | 2011-06-28 | 2013-01-03 | Varel International Ind., L.P. | Ultrasound Assisted Electrochemical Catalyst Removal For Superhard Materials |
CN104862771A (en) * | 2015-05-28 | 2015-08-26 | 吉林大学 | Method for removing partial metal cobalt in polycrystalline diamond compact by electrolytic method |
WO2016049480A1 (en) * | 2014-09-26 | 2016-03-31 | National Oilwell Varco, L.P. | Electrochemical corrosion of catalyst material from pcd elements |
CN108456917A (en) * | 2018-04-19 | 2018-08-28 | 湖南工业大学 | A kind of preparation method of porous tantalum piece |
CN110144618A (en) * | 2019-06-03 | 2019-08-20 | 河南四方达超硬材料股份有限公司 | Method for removing metallic cobalt in polycrystalline diamond compact |
CN110965116A (en) * | 2019-11-27 | 2020-04-07 | 中国民航大学 | Electrolysis ultrasonic cooperative device suitable for precipitation hardening stainless steel descaling |
CN111394780A (en) * | 2020-03-31 | 2020-07-10 | 中国科学院金属研究所 | Device and method for electrochemically dissolving high-temperature alloy waste by using ultrasonic-assisted rotary electrode |
-
2021
- 2021-06-29 CN CN202110726561.XA patent/CN113445117A/en active Pending
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1962957A (en) * | 2006-11-02 | 2007-05-16 | 中国地质大学(武汉) | Method for ultrasonic electroplating of diamond drilling bit |
CN102134737A (en) * | 2011-04-28 | 2011-07-27 | 上海理工大学 | Method for preparing porous silicon |
US20130001100A1 (en) * | 2011-06-28 | 2013-01-03 | Varel International Ind., L.P. | Ultrasound Assisted Electrochemical Catalyst Removal For Superhard Materials |
WO2016049480A1 (en) * | 2014-09-26 | 2016-03-31 | National Oilwell Varco, L.P. | Electrochemical corrosion of catalyst material from pcd elements |
CN104862771A (en) * | 2015-05-28 | 2015-08-26 | 吉林大学 | Method for removing partial metal cobalt in polycrystalline diamond compact by electrolytic method |
CN108456917A (en) * | 2018-04-19 | 2018-08-28 | 湖南工业大学 | A kind of preparation method of porous tantalum piece |
CN110144618A (en) * | 2019-06-03 | 2019-08-20 | 河南四方达超硬材料股份有限公司 | Method for removing metallic cobalt in polycrystalline diamond compact |
CN110965116A (en) * | 2019-11-27 | 2020-04-07 | 中国民航大学 | Electrolysis ultrasonic cooperative device suitable for precipitation hardening stainless steel descaling |
CN111394780A (en) * | 2020-03-31 | 2020-07-10 | 中国科学院金属研究所 | Device and method for electrochemically dissolving high-temperature alloy waste by using ultrasonic-assisted rotary electrode |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Li et al. | Facile synthesis and electrochemical properties of a novel Ni-B/TiC composite coating via ultrasonic-assisted electrodeposition | |
Yao et al. | Preparation and characterization of PbO2–ZrO2 nanocomposite electrodes | |
EP2757179B1 (en) | Chlorine-generating positive electrode | |
Yao et al. | Preparation and properties of PbO2-ZrO2 nanocomposite electrodes by pulse electrodeposition | |
CN103700813B (en) | A kind of Ti base β-PbO 2the preparation method of dimensional stable anode | |
CN102428213A (en) | Method for treating the surface of a metal | |
Yao et al. | Influence of ZrO2 particles on fluorine-doped lead dioxide electrodeposition process from nitrate bath | |
CN105624764A (en) | Preparation method for micro-arc oxidation of ceramic membrane on magnesium alloy | |
Kullaiah et al. | Effect of TiO 2 nanoparticles on hydrogen evolution reaction activity of Ni coatings | |
CN113800606B (en) | Coating titanium anode for treatment of circulating cooling water, preparation method and application | |
CN109440179A (en) | A kind of metal tantalum matrix of roughing in surface and preparation method thereof | |
CN109536964A (en) | A kind of acid etching method of metal oxide electrode Titanium base | |
CN102925929B (en) | Method for producing metal titanium by molten salt electrolysis | |
JPH01294882A (en) | Method for converting manganese diuxide into permanganate | |
Mirseyed et al. | A new insight on the mechanisms of corrosion deactivation of a typical Ti/IrO2+ RuO2+ TiO2 coating in the presence of Ta2O5 in chlor-alkali medium | |
CN113445117A (en) | Electrolytic method and device for removing metallic cobalt in polycrystalline diamond compact | |
CN108060451B (en) | Preparation method of hydrophobic natural fiber composite lead dioxide anode | |
S̆ljukić et al. | Exploration of stable sonoelectrocatalysis for the electrochemical reduction of oxygen | |
CN116837448A (en) | Method and device for efficiently removing metal sintering agent of polycrystalline diamond compact | |
CN111763979A (en) | Preparation method of long-life anode material | |
CN111607805A (en) | Long-life anode material | |
CN111606395A (en) | Preparation method and application of polythiophene modified metal bismuth-doped lead dioxide electrode | |
JP3769492B2 (en) | Performance recovery method of gas diffusion electrode | |
Yao et al. | Preparation and electrocatalytic property of lead dioxide prepared by pulse electrodeposition with different pulse current density | |
CN109628989A (en) | A kind of preparation method of high-chromium alloy ultra-hydrophilic surface |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20210928 |
|
RJ01 | Rejection of invention patent application after publication |