CN106222729B - Overcritical composite plating processing drill method based on mobile anode - Google Patents
Overcritical composite plating processing drill method based on mobile anode Download PDFInfo
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- CN106222729B CN106222729B CN201610587719.9A CN201610587719A CN106222729B CN 106222729 B CN106222729 B CN 106222729B CN 201610587719 A CN201610587719 A CN 201610587719A CN 106222729 B CN106222729 B CN 106222729B
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D15/00—Electrolytic or electrophoretic production of coatings containing embedded materials, e.g. particles, whiskers, wires
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/10—Agitating of electrolytes; Moving of racks
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/12—Electroplating: Baths therefor from solutions of nickel or cobalt
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/003—Electroplating using gases, e.g. pressure influence
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/04—Electroplating with moving electrodes
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D7/00—Electroplating characterised by the article coated
Abstract
The present invention provides a kind of overcritical composite plating tool bit method based on mobile anode, and the key step of this method includes:The matrix material of drill bit is pre-processed, is allowed to the ability for possessing electro-deposition nano-composite plate;The electroplate liquid configured is added into reactor, after sealing, is passed through CO2Gas, surfactant is added, the plating system formed under super critical condition;Setting meets the parameters such as electric current, temperature and the mechanical agitation speed of electro-deposition requirement;The relative position between anode and cathode is adjusted, anode translational speed and stroke is set, switches on power, nano-composite plate is fully deposited to the processed bit face as cathode body;Drill bit after electro-deposition is removed clean, obtaining surface has the drill bit of high-performance composite Nano coating.Bit face tissue made from the method for the present invention is fine and closely woven, and wearability and hardness all have a distinct increment, service life increase.
Description
The application is Application No. 201410412652.6, and the applying date is August in 2014 20, and invention and created name is
The divisional application of the application for a patent for invention of " method of the overcritical composite plating processing drill based on mobile anode ".
Technical field
The present invention relates to electrochemical deposition processing technique field, and in particular to a kind of based on the overcritical compound of mobile anode
The method for electroplating processing drill.
Background technology
Supercritical fluid(Supercritical Fluid)Refer to that pure material is in critical point(Critical pressure and critical
Temperature)During the above, the one kind showed is between liquid and gaseous fluid.In Near The Critical Point, supercritical fluid it is close
Phenomenon jumpy occurs for the physical property of all fluids such as degree, viscosity, solubility, thermal capacity, dielectric constant.CO2Gas has
Environmentally friendly, non-ignitable, nontoxic, inertia, deposit enriches and critical pressure(7.39MPa)With temperature (31.1 DEG C) it is less high the advantages that, because
This supercritical CO2Fluid is widely used.Due to supercritical CO2With relatively low viscosity(0.03-0.1 MPa·s)Higher
Diffusion coefficient(10- 4 cm2·s-1), good condition can be provided in electroforming system for mass transfer.
The moulding material of current industrial drill bit is often using titanium alloy, diamond or Special steel material etc., these materials
The drill bit of material prepares complex process, high expensive and performance is not excellent enough, and uses nano composite material can be preferably
Make up these shortcomings.Industrial drill bit often uses high-speed steel and special steel etc. to be used as matrix material, and the matrix material is generally difficult to
Electrochemical deposition processing is directly carried out, and after using the method for chemical plating to pre-process matrix material, then cause in the base
Nano compound electroplating is carried out on body to be possibly realized.When nano particle uniformly is compounded in into metal matrix material, nano particle exists
The problem of reunion occurred during electroforming and poor macro-uniformity, is very prominent.Shaken mostly using stirring, ultrasound at present
Move, add the modes such as dispersant to handle the agglomeration of nano particle, but because of former mould(Metal parts)It is different, during plating
Electric field, flow field uniformity are whard to control etc., can still cause nanoparticle agglomerates and skewness in nano composite electroforming deposit.Receive
The reunion of rice grain and skewness will cause the cast layer mechanical property difference of different parts huge, have a strong impact on its use
Performance.
At present, the process and device of electrodeposited nanocrystalline composite and micro-workpiece be under supercritical environment
There is finding.Chinese patent literature if Authorization Notice No. is CN 101092716B discloses a kind of trickle plating of supercritical fluid
Moulding process and its device, it is with SCF-CO2The shaping of micro-structure part, the gold as obtained by this method are carried out for plating environment
Category electroplates layer surface depositing homogeneous, without buildup, and cast layer tissue is fine and closely woven smooth, but gained cast layer is single metal, is not suitable for
Composite plating shaping containing nano particle;And for example publication No. is that CN 102146573A Chinese patent literature proposes one kind
The method of preparing nano composite material by supercritical fluid electroforming, it is mainly the electro-deposition system under mechanical agitation subsidiary conditions
Standby metal-base nanometer composite material, Electric Field Distribution is fixed, from the point of view of its parameter setting and anode and cathode are set, it is impossible to column
Or tubulose class negative electrode carries out effective deposition nano-composite plate.
The content of the invention
The purpose of the present invention is:Agglomeration of the nano particle in electroplating process is controlled, is being electroplated for negative electrode drill bit
During can not be coated with nano composite material well, using the overcritical composite plating method based on the mobile anode of matching,
Composite deposite is enabled to become to be uniformly dispersed in negative electrode bit face, surfacing, dense structure, crystal grain is tiny, performance is excellent
It is different.
The technical scheme is that:The side of the overcritical composite plating processing drill based on mobile anode of the present invention
Method, implemented using the overcritical composite plating device based on mobile anode, should the overcritical composite plating dress based on mobile anode
Put including reactor, dc source component, mechanical agitator, carbon dioxide steel cylinder and high-pressure pump;Dc source component bag
Include power supply, anode stub and cathode bar;It is characterized in:The above-mentioned overcritical composite plating device based on mobile anode also includes moving
Dynamic anode assemblies, drive component and the processed drill bit as cathode body;
Above-mentioned mobile anode assemblies include fixed connecting plate and mobile anode;Mobile anode is fixed with fixed connecting plate to be connected
Connect;Drive component includes servomotor, driving leading screw and connecting rod;Driving leading screw is built-in with the elastic conducting electric wire being insulated from
Circle;Servomotor is connected with driving lead screw transmission;The left end of connecting rod is fixedly connected with fixed connecting plate;The right-hand member of connecting rod with
Driving leading screw is fixedly connected;Mobile anode by the elastic conduction coil built in fixed connecting plate, connecting rod, driving leading screw and
Anode stub electrically connects with the positive pole of power supply;Be processed drill bit upper end be fixedly connected with the lower end of cathode bar and by cathode bar with
The negative pole electrical connection of power supply;The mobile anode of above-mentioned mobile anode assemblies can be processed relatively under the driving of drive component
Drill bit upward and downward moves back and forth;
The mobile anode of above-mentioned mobile anode assemblies is provided with 4;This 4 mobile anodes are fixedly installed on fixed connecting plate
Four corners;It is processed drill bit and is provided with 4,4 processed drill bits corresponds to each setting 1 respectively with 4 mobile anodes;
The cylindric pure nickel thin-walled ring that above-mentioned mobile anode is high 2cm, diameter 3cm, thickness are 2mm;It is processed drill bit
The distance between outer wall and inwall of mobile anode be 1cm.
The method of processing drill, comprises the following steps:
1. carrying out chemical plating in advance to the matrix for being processed drill bit, last layer is plated in the matrix surface for being processed drill bit
It is easy to carry out the fine copper or pure nickel of electro-deposition;
2. the binary system electroplate liquid of the hard particles containing nanometer prepared and compound additive is added in reactor, Gu
It is set for the processed drill bit for cathode body;The position of the mobile anode of the mobile anode assemblies of regulation to move anode can be relative
Moved up and down in processed drill bit;Above-mentioned electroplate liquid is the nickel salt solution of sulfur acid nickel and nickel chloride;Nanometer hard particles be
30~60nm of diameter diamond nano-particles;Compound additive is made up of dodecane base class compound and ether compound
Additive;Above-mentioned electroplate liquid also includes the boric acid as electro-deposition sustained release agent that concentration is 30g/L~60g/L;
3. carbon dioxide is passed through into reactor, control temperature in reactor 35~70 DEG C, pressure 8~
In the range of 20MPa, form the ternary using supercritical carbon dioxide emulsion as carrier and electroplate system;
4. set mobile anode relative to the processed drill bit as cathode body move up and down maximum single direction stroke as
5cm;Using at the uniform velocity or simple harmonic motion move mode, average speed control in 1-20mm/s;Electrodeposition time is 1-3 hours;
Nano-composite plate is obtained under the stirring auxiliary of mechanical agitator;
5. electro-deposition finishes, by post processing, the drill bit with nano-composite plate of required performance requirement is obtained.
Further scheme is:The reactor of the above-mentioned overcritical composite plating device based on mobile anode includes main body
And liner;Liner is on the internal perisporium of main body;Air inlet is provided with the left of the upper end of the main body of reactor;The main body of reactor
Leakage fluid dram is provided with the right side of upper end;The body interior of reactor is provided with heating coil;Mechanical agitator is arranged in reactor;Machinery
Agitator is worked using level to intermittent stirring mode;High-pressure pump is used for the carbon dioxide of carbon dioxide steel cylinder memory storage
The air inlet for the main body that gas passes through reactor takes out pressure into main body;
The fixed connecting plate of above-mentioned mobile anode assemblies is the plate body part that is integrally square, four angles of fixed connecting plate
Portion is provided with the breach of arc;Fixed connecting plate is by carrying out insulation, high pressure resistant, acidproof engineering plastics system outside copper frame structure
Into;Mobile anode is metallic conductor part;On the arc notch in four corners that mobile anode is fixedly installed on fixed connecting plate and
Electrically connected with the copper frame structure of fixed connecting plate;
The driving leading screw of drive component is hollow leading screw;Above-mentioned elastic conduction coil is arranged on the hollow of driving leading screw
In position;And the left side of driving leading screw is stretched out in the lower end of the elastic conduction coil;Driving is stretched out in the upper end of the elastic conduction coil
The upper end of leading screw;The elastic conduction coil is insulated with driving leading screw by insulation spacer;Leading screw is driven by its underpart and servo electricity
Machine is connected;Above-mentioned connecting rod outside copper post by carrying out insulation, high pressure resistant, acidproof engineering plastics are made.
Further scheme is:The concentration of above-mentioned nickel salt solution is 300~450g/L;The concentration of Nano diamond particle
For 1~20g/L;The concentration of compound additive is 0.1~2g/L.
Further scheme is:The current density of the power supply output of above-mentioned dc source component is 7A/dm2;Above-mentioned
Mechanical agitator is arranged in reactor;For mechanical agitator level to intermittent stirring, stir speed (S.S.) is 200~500rpm.
Further scheme also has:Above-mentioned compound additive is by lauryl sodium sulfate and polyethylene glycol trimethyl nonyl
Base ether;The concentration of lauryl sodium sulfate is 0.2g/L, and the concentration of polyethylene glycol trimethyl nonyl ethers is 0.8g/L.
The present invention has positive effect:(1)The present invention is by using mobile anodization method, as cathode body
It is processed drill bit and ensure that each to uniformity of its surface in plating so that is electrodeposited in nano combined on processed drill bit
Coating can be smooth, uniform;Simultaneously using horizontal to intermittent stirring mode, so that nano particle has sedimentation in electroplating solution
Trend, further improve uniformity and uniformity during nano combined electroforming.(2) present invention can be in non-smooth metal
The excellent nano-composite plate of forming properties on piece surface.(3) present invention can be according to use demand, by nano particle
Processing, form the nano-composite plate of different performance on metal parts using different nanometer hard materials.(4)The present invention
Overcritical nano compound electroplating can be carried out to multiple processed drill bits as cathode body simultaneously, can prepared efficiently, in batches
Go out the drill bit of the nano composite material of excellent performance.
Brief description of the drawings
Fig. 1 is the schematic diagram of electrotyping forming device of the present invention;
Fig. 2 is the structural representation of mobile anode in Fig. 1, and mobile anode and the quilt as cathode body are also show in figure
The position matching of processing drill.
Reference in above-mentioned accompanying drawing is as follows:
Reactor 1, main body 11, air inlet 11-1, leakage fluid dram 11-2, heating coil 11-3, liner 12;
Mobile anode assemblies 2, fixed connecting plate 21, mobile anode 22;
Drive component 3, servomotor 31;Drive leading screw 32, connecting rod 33;
Dc source component 4, power supply 41, anode stub 42, cathode bar 43;
Mechanical agitator 5;
Carbon dioxide steel cylinder 6;
High-pressure pump 7,
It is processed drill bit 8.
Embodiment
The present invention is further detailed explanation with reference to the accompanying drawings and detailed description.
(Embodiment 1)
See Fig. 1 and Fig. 2, the overcritical composite plating processing drill method based on mobile anode of the present embodiment, using base
Implement in the overcritical composite plating device of mobile anode, the overcritical composite plating device based on mobile anode is mainly by reacting
Device 1, mobile anode assemblies 2, drive component 3, dc source 4, mechanical agitator 5, carbon dioxide steel cylinder 6 and high-pressure pump 7
Composition.
Reactor 1 is mainly made up of main body 11 and liner 12.Air inlet is provided with the left of the upper end of the main body 11 of reactor 1
11-1;Leakage fluid dram 11-2 is provided with the right side of the upper end of reactor 1;The inside of main body 11 of reactor 1 is provided with heating coil 11-3.Liner
12 on the internal perisporium of main body 11.
Mobile anode assemblies 2 are made up of fixed connecting plate 21 and mobile anode 22.Fixed connecting plate 21 is square to be overall
Plate body part, four corners of fixed connecting plate 21 are provided with the breach of arc.Fixed connecting plate 21 be by copper frame structure outside
Carry out insulation, high pressure resistant, acidproof engineering plastics are made.Mobile 22, anode preferably uses high 2cm, diameter 3cm, thickness in implementing
For 2mm cylindric pure nickel thin-walled ring;4 are preferably used in mobile the present embodiment of anode 22, this 4 mobile anodes 22, which are fixed, to be set
Put on the arc notch in four corners of fixed connecting plate 21 and electrically connected with the copper frame structure of fixed connecting plate 21.
Drive component 3 mainly includes servomotor 31, driving leading screw 32 and connecting rod 33.In the present embodiment of servomotor 31
It is preferred that the DC servo motor using model KT290-A6-50.Driving leading screw 32 is hollow leading screw, is driven in leading screw 32
Empty position is built-in with elastic conduction coil;The left side of driving leading screw 32 is stretched out in the lower end of the elastic conduction coil;The elastic conduction
The upper end of driving leading screw 32 is stretched out in the upper end of coil;And the elastic conduction coil is insulated with driving leading screw 32 by insulation spacer;
Driving leading screw 32 is connected by its underpart and servomotor 31.Connecting rod 33 outside copper post by carrying out insulation, high pressure resistant, acidproof work
Engineering plastics are made.The right-hand member of connecting rod 33 is fixedly connected with driving leading screw 32;And connecting rod 33 is by the right-hand member of its internal copper post
Electrically connected with the lower end of the elastic conduction coil in driving leading screw 32;The fixation of the left end of connecting rod 33 and mobile anode assemblies 2
The right side central of connecting plate 21 is fixedly connected;And connecting rod 33 is by the left end of its internal copper post and the copper of fixed connecting plate 21
Frame structure electrically connects.
Dc source component 4 is made up of power supply 41, anode stub 42 and cathode bar 43.The upper end of anode stub 42 and power supply 41
Positive pole electrically connects, and the lower end of anode stub 42 electrically connects with the upper end of the elastic conduction coil in the driving leading screw 32 of drive component 3;
So as to by anode stub 42, driving leading screw 32 in elastic conduction coil, connecting rod 33, fixed connecting plate 21 copper framework knot
Structure electrically connects mobile anode 22 with the positive pole of power supply 41.The upper end of cathode bar 43 electrically connects with the negative pole of power supply 41, is processed
The upper end of drill bit 8 is fixed with the lower end of cathode bar 43 and electrically connected.It is processed drill bit 8 and is used as cathode body.Drill bit 8 is processed to set
In on the axis in the mobile anode 22 of mobile anode assemblies 2;And it is processed the inwall of the outer wall and mobile anode 22 of drill bit 8
The distance between be 1cm.
Mechanical agitator 5 is arranged in reactor 1;Mechanical agitator 5 is worked using level to intermittent stirring mode, so that
Obtain nano particle has Subsidence trend in electroplating solution, improves uniformity and uniformity during nano combined electroforming.Machinery
Horizontal direction intermittent stirring is stirred, stir speed (S.S.) is 200~500rpm.
Carbon dioxide steel cylinder 6 is used to store carbon dioxide.
High-pressure pump 7 is used for the main body 11 that the carbon dioxide of the memory storage of carbon dioxide steel cylinder 6 is passed through into reactor 1
Air inlet 11-1 pressure is taken out into main body 11.
The mobile anode 22 of foregoing mobile anode assemblies 2 surrounds processed drill bit 8 and entered under the driving of drive component 3
The motion of row upward and downward;In the present embodiment, the maximum single direction stroke that mobile anode 22 is processed drill bit 8 relatively is 5cm;Using even
Speed or the move mode of simple harmonic motion, average speed are controlled in 1-20mm/s.
The overcritical composite plating processing drill method based on mobile anode of the present embodiment, with Ni-based benefit processing drill 8
Illustrated exemplified by electro-deposition Nano diamond composite, its processing method mainly includes the following steps that:
1. carrying out chemical plating in advance to the matrix for being processed drill bit 8, one is plated in the matrix surface for being processed drill bit 8
Layer is easy to carry out the metal of electro-deposition;Fine copper or pure nickel may be selected in the metal.In the present embodiment, it is preferred to use in processed drill bit
8 matrix surface plates the uniform copper layer of about 10 μ m-thicks.
2. it is molten to add nickel salt into the reactor 1 of the overcritical composite plating device based on mobile anode of the present embodiment
Liquid, boric acid, Nano diamond particle and compound additive, stir 30 minutes, make that it is sufficiently mixed and nano particle uniformly divides
Dissipate.Boric acid is optionally added, the concentration of boric acid is 30g/L~60g/L as electro-deposition sustained release agent.
Nickel salt solution is the solution of sulfur acid nickel and nickel chloride;Wherein nickel sulfate dosage is 300~400g/L, and nickel chloride is used
Measure as 30~50g/L;Diamond nano-particles, a diameter of 30~60nm, its dosage are 5~15g/L;Described compound additive
Formed for dodecane base class compound and ether compound, wherein dodecane base class compound amount is 0.1~2g/L, ethers
Compound dosage is 0.1~1g/L.
In the present embodiment, additive preferably uses lauryl sodium sulfate and polyethylene glycol trimethyl nonyl ethers.Each material
Concentration be preferably:Nickel sulfate 300g/L, nickel chloride 35g/L, boric acid 40g/L, Nano diamond particle 15g/L, dodecyl
Sodium sulphate 0.2g/L, polyethylene glycol trimethyl nonyl ethers 0.8g/L.
3. start high-pressure pump 7, by the carbon dioxide in carbon dioxide steel cylinder 6 from the main body 11 of reactor 1
Air inlet 11-1 is taken out in the main body 11 for being pressed onto reactor;Control pressure is 13MPa;Make alternating current adding by main body 11 simultaneously
Heat coil 11-3 is heated in the presence of electromagnetic induction, will by the control of the size of the current strength to alternating current
Temperature control preferably 50 DEG C in the present embodiment, under above-mentioned pressure and temperature, is carried out at 35~70 DEG C by mechanical agitator 5
Stir and form the supercritical fluid electroforming solution containing Nano diamond particle.In the present embodiment, carbon dioxide is close
Test pressure in the main body 11 of the reactor 1 closed is 8~20MPa.
4. consolidate as the upper end of the processed drill bit 8 of cathode body and the lower end of the cathode bar 43 of dc source component 4
Fixed electrical connection;The upper end of the cathode bar 43 of dc source component 4 is electrically connected with the negative electrode of the power supply 41 of dc source component 4;
The upper end of the anode stub 42 of dc source component 4 is electrically connected with the anode of power supply 41;By the lower end of anode stub 42 and driving group
The driving leading screw 32 of part 3 is fixedly connected;The servomotor 31 for driving leading screw 32 and drive component 3 is connected;By driving group
The connecting rod 33 of part 3 is fixedly connected with the fixed connecting plate 21 of mobile anode assemblies 2;It is processed drill bit 8 and is located at mobile anode unit
On axis in the mobile anode 22 of part 2;And make the distance between inwall for the outer wall and mobile anode 22 for being processed drill bit 8
For 1cm;
The current density for setting the power supply 41 of dc source component 4 to export is 1~13A/dm2, preferably adopt in the present embodiment
Use 7A/dm2;The maximum single direction stroke for setting the relatively processed drill bit 8 of mobile anode 22 of mobile anode assemblies 2 is 5cm;It is mobile
Mode is using at the uniform velocity or simple harmonic motion, and average speed control is in 1~20mm/s, and Electric Field Distribution is more uniform during causing electroforming.
5. starting the servomotor 31 of drive component 3, the mobile anode 21 of mobile anode assemblies 2 is controlled according to the ginseng of setting
Number moves up and down;Mechanical agitator 5 is synchronous to use level to intermittent stirring;Connect the power supply 41 of dc source component 4;Make
Nickel ion is obtained quickly and efficiently to deposit on the processed drill bit 8 as cathode body with Nano diamond particle.The present embodiment
In, electrodeposition time is 1~3 hour.
6. after electroforming, supercritical fluid electroforming solution is led by the leakage fluid dram 11-2 in the main body 11 of reactor 1
Enter in gas-liquid separator, the carbon dioxide and electroforming solution of separation, which are separately recovered in retracting device, to be recycled.
7. processed drill bit 8 is taken out from reactor 1, air-dry clean by pickling again by washing, that is, obtain and quilt
The nano particle that the matrix of processing drill 8 is combined closely is evenly distributed, dense structure, crystal grain are tiny, surfacing, excellent performance
Nano composite material electroformed layer.
Above example is the explanation to the embodiment of the present invention, rather than limitation of the present invention, relevant technology
The technical staff in field without departing from the spirit and scope of the present invention, can also make various conversion and change and obtain
To corresponding equivalent technical scheme, therefore all equivalent technical schemes should be included into the patent protection model of the present invention
Enclose.
Claims (1)
- A kind of 1. overcritical composite plating processing drill method based on mobile anode, using based on the overcritical multiple of mobile anode Electroplanting device is closed to implement;The described overcritical composite plating device based on mobile anode includes reactor(1), dc source group Part(4), mechanical agitator(5), carbon dioxide steel cylinder(6)And high-pressure pump(7);Described dc source component(4)Including Power supply(41), anode stub(42)And cathode bar(43);It is characterized in that:The described overcritical composite plating based on mobile anode Device also includes mobile anode assemblies(2), drive component(3)With the processed drill bit as cathode body(8);Described mobile anode assemblies(2)Including fixed connecting plate(21)With mobile anode(22);Mobile anode(22)With fixation Connecting plate(21)It is fixedly connected;Drive component(3)Including servomotor(31), driving leading screw(32)And connecting rod(33);Driving Leading screw(32)It is built-in with the elastic conduction coil being insulated from;Servomotor(31)With driving leading screw(32)Drive connection;Connection Bar(33)Left end and fixed connecting plate(21)It is fixedly connected;Connecting rod(33)Right-hand member with driving leading screw(32)It is fixedly connected; Mobile anode(22)Pass through fixed connecting plate(21), connecting rod(33), driving leading screw(32)Built-in elastic conduction coil and Anode stub(42)With power supply(41)Positive pole electrical connection;It is processed drill bit(8)Upper end and cathode bar(43)Lower end fix connect Connect and pass through cathode bar(43)With power supply(41)Negative pole electrical connection;Described mobile anode assemblies(2)Mobile anode(22) In drive component(3)Driving under, drill bit can be processed relatively(8)Upward and downward moves back and forth;Described mobile anode assemblies(2)Mobile anode(22)Provided with 4;This 4 mobile anodes(22)It is fixedly installed on Determine connecting plate(21)Four corners;It is processed drill bit(8)Provided with 4,4 processed drill bits(8)With 4 mobile anodes (22)Each setting 1 is corresponded to respectively;Described mobile anode(22)The cylindric pure nickel thin-walled ring for being 2mm for high 2cm, diameter 3cm, thickness;It is processed drill bit (8)Outer wall and mobile anode(22)The distance between inwall be 1cm;The method of processing drill, comprises the following steps:1. to being processed drill bit(8)Matrix carry out in advance chemical plating, in processed drill bit(8)Matrix surface plate one Layer is easy to carry out the fine copper or pure nickel of electro-deposition;2. the binary system electroplate liquid of the hard particles containing nanometer prepared and compound additive is added into reactor(1)In, Gu It is set for the processed drill bit for cathode body(8);The mobile anode assemblies of regulation(2)Mobile anode(22)Position to move Anode(22)Can be relative to processed drill bit(8)Move up and down;Described electroplate liquid is molten for the nickel salt of sulfur acid nickel and nickel chloride Liquid;The diamond nano-particles that nanometer hard particles are 30~60nm of diameter;Compound additive is by dodecane base class compound With the additive of ether compound composition;It is being sustained as electro-deposition for 30g/L~60g/L that described electroplate liquid, which also includes concentration, The boric acid of agent;3. to reactor(1)In be passed through carbon dioxide, control reactor(1)Interior temperature 35~70 DEG C, pressure 8~ In the range of 20MPa, form the ternary using supercritical carbon dioxide emulsion as carrier and electroplate system;4. the mobile anode of setting(22)Relative to the processed drill bit as cathode body(8)Moving up and down maximum single direction stroke is 5cm;Using at the uniform velocity or simple harmonic motion move mode, average speed control in 1-20mm/s;Electrodeposition time is 1-3 hours; In mechanical agitator(5)Stirring auxiliary under obtain nano-composite plate;5. electro-deposition finishes, by post processing, the drill bit with nano-composite plate of required performance requirement is obtained.
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Application Number | Priority Date | Filing Date | Title |
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CN201610587719.9A CN106222729B (en) | 2014-08-20 | 2014-08-20 | Overcritical composite plating processing drill method based on mobile anode |
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CN201410412652.6A CN104141161B (en) | 2014-08-20 | 2014-08-20 | The method of overcritical composite plating processing drill based on mobile anode |
CN201610587719.9A CN106222729B (en) | 2014-08-20 | 2014-08-20 | Overcritical composite plating processing drill method based on mobile anode |
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CN201410412652.6A Division CN104141161B (en) | 2014-08-20 | 2014-08-20 | The method of overcritical composite plating processing drill based on mobile anode |
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CN106222729A CN106222729A (en) | 2016-12-14 |
CN106222729B true CN106222729B (en) | 2018-02-06 |
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CN201610595427.XA Active CN106048693B (en) | 2014-08-20 | 2014-08-20 | A kind of overcritical composite plating processing drill method based on mobile anode |
CN201410412652.6A Active CN104141161B (en) | 2014-08-20 | 2014-08-20 | The method of overcritical composite plating processing drill based on mobile anode |
CN201610592998.8A Active CN106087008B (en) | 2014-08-20 | 2014-08-20 | Overcritical composite plating processing drill method of the effect preferably based on mobile anode |
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1064901A (en) * | 1992-01-28 | 1992-09-30 | 胜利石油管理局总机械厂 | Deep-hole sizing chromate plating device and processing method |
JP2004143570A (en) * | 2002-10-28 | 2004-05-20 | Hideo Yoshida | Method and apparatus for producing conductive organic thin film |
CN101092716A (en) * | 2007-04-27 | 2007-12-26 | 江苏技术师范学院 | Superfine electroform technique of supercutical fluid, and equipment |
CN101535531A (en) * | 2006-10-02 | 2009-09-16 | S.E.S.株式会社 | Electroplating method |
CN102146573A (en) * | 2011-03-14 | 2011-08-10 | 江苏技术师范学院 | Method for preparing nano composite material by supercritical fluid electroforming |
CN102560606A (en) * | 2012-03-01 | 2012-07-11 | 梅河口市兴业精密钢管有限公司 | Nanodiamond micro powder composite chromed pump cylinder, production technology and production device |
CN103173842A (en) * | 2013-02-25 | 2013-06-26 | 上海大学 | Device for conducting electroplating process and electroplate liquid development experiment in high-pressure environment |
Family Cites Families (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4661213A (en) * | 1986-02-13 | 1987-04-28 | Dorsett Terry E | Electroplate to moving metal |
EP0563625A3 (en) * | 1992-04-03 | 1994-05-25 | Ibm | Immersion scanning system for fabricating porous silicon films and devices |
JP2935647B2 (en) * | 1995-05-15 | 1999-08-16 | 株式会社荏原製作所 | Electroplating equipment for semiconductor wafers |
CN2403792Y (en) * | 2000-01-28 | 2000-11-01 | 杨聚泰 | Apparatus for auxiliary anode spraying zinc liquid electroplating steel conduit inwall |
IT1318233B1 (en) * | 2000-07-24 | 2003-07-28 | De Nora Elettrodi Spa | MOTORIZED DEVICE FOR THE ADJUSTMENT OF THE INTERELECTRODICAL DISTANCE IN MERCURY CATHODE ELECTROLYSIS CELLS. |
KR100526120B1 (en) * | 2000-12-21 | 2005-11-08 | 주식회사 포스코 | Apparatus for adjusting anode gap by using tilting mechanism |
JP4673612B2 (en) * | 2004-02-12 | 2011-04-20 | ダイキン工業株式会社 | Electroplating in the presence of CO2 |
CN101037777B (en) * | 2007-01-30 | 2010-05-19 | 南京航空航天大学 | Precise/ trickle electromoulding machine tool |
CN101225537A (en) * | 2007-10-18 | 2008-07-23 | 上海交通大学 | Automatic brush plating restoration flow plating method |
JP5121481B2 (en) * | 2008-02-01 | 2013-01-16 | 上村工業株式会社 | Surface treatment equipment |
CN201232091Y (en) * | 2008-07-22 | 2009-05-06 | 浙江理工大学 | Quick-speed forming device for electrochemical deposition at numerical control selected area |
CN201574204U (en) * | 2009-12-30 | 2010-09-08 | 运城制版印刷机械制造有限公司 | Titanium bar moving and positioning mechanism of electroplating device |
JP5238854B2 (en) * | 2010-08-27 | 2013-07-17 | 上村工業株式会社 | Electrolytic regeneration treatment equipment |
CN102162118B (en) * | 2011-04-08 | 2013-05-08 | 江苏理工学院 | Manufacturing method of nickel-based diamond slice |
CN102586813B (en) * | 2012-02-03 | 2014-07-16 | 河南理工大学 | Microelectroforming machine tool |
JP5515056B1 (en) * | 2012-11-01 | 2014-06-11 | ユケン工業株式会社 | Plating apparatus, nozzle-anode unit, plating member manufacturing method, and member to be plated fixing apparatus |
CN103898594A (en) * | 2012-12-25 | 2014-07-02 | 大连崇达电路有限公司 | Insoluble anode electroplating copper-tin plating tank |
CN103184471A (en) * | 2013-04-03 | 2013-07-03 | 沈阳建筑大学 | Preparation method of stainless steel based lead dioxide electrode |
CN203582994U (en) * | 2013-12-03 | 2014-05-07 | 湖南特力液压有限公司 | Electroplating device and electroplating apparatus for inner hole of tubular workpiece |
-
2014
- 2014-08-20 CN CN201610587719.9A patent/CN106222729B/en active Active
- 2014-08-20 CN CN201610595427.XA patent/CN106048693B/en active Active
- 2014-08-20 CN CN201410412652.6A patent/CN104141161B/en active Active
- 2014-08-20 CN CN201610592998.8A patent/CN106087008B/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1064901A (en) * | 1992-01-28 | 1992-09-30 | 胜利石油管理局总机械厂 | Deep-hole sizing chromate plating device and processing method |
JP2004143570A (en) * | 2002-10-28 | 2004-05-20 | Hideo Yoshida | Method and apparatus for producing conductive organic thin film |
CN101535531A (en) * | 2006-10-02 | 2009-09-16 | S.E.S.株式会社 | Electroplating method |
CN101092716A (en) * | 2007-04-27 | 2007-12-26 | 江苏技术师范学院 | Superfine electroform technique of supercutical fluid, and equipment |
CN102146573A (en) * | 2011-03-14 | 2011-08-10 | 江苏技术师范学院 | Method for preparing nano composite material by supercritical fluid electroforming |
CN102560606A (en) * | 2012-03-01 | 2012-07-11 | 梅河口市兴业精密钢管有限公司 | Nanodiamond micro powder composite chromed pump cylinder, production technology and production device |
CN103173842A (en) * | 2013-02-25 | 2013-06-26 | 上海大学 | Device for conducting electroplating process and electroplate liquid development experiment in high-pressure environment |
Non-Patent Citations (1)
Title |
---|
深孔镀硬铬和珩磨复合工艺不溶性阳极的设计;陈维范等;《大庆石油学院学报》;19880630;第12卷(第2期);第58~63页 * |
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