WO2015169132A1 - Method for preparing wc-co powder used for thermal spraying - Google Patents
Method for preparing wc-co powder used for thermal spraying Download PDFInfo
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- WO2015169132A1 WO2015169132A1 PCT/CN2015/075274 CN2015075274W WO2015169132A1 WO 2015169132 A1 WO2015169132 A1 WO 2015169132A1 CN 2015075274 W CN2015075274 W CN 2015075274W WO 2015169132 A1 WO2015169132 A1 WO 2015169132A1
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- powder
- cobalt
- cobalt salt
- coated
- water
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- 239000000843 powder Substances 0.000 title claims abstract description 135
- 238000000034 method Methods 0.000 title claims abstract description 63
- 238000007751 thermal spraying Methods 0.000 title claims description 20
- 229910009043 WC-Co Inorganic materials 0.000 claims abstract description 75
- 150000001868 cobalt Chemical class 0.000 claims abstract description 64
- 239000002243 precursor Substances 0.000 claims abstract description 43
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 41
- 229910017052 cobalt Inorganic materials 0.000 claims abstract description 34
- 239000010941 cobalt Substances 0.000 claims abstract description 34
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims abstract description 33
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 32
- 239000011268 mixed slurry Substances 0.000 claims abstract description 26
- 239000007921 spray Substances 0.000 claims abstract description 26
- UONOETXJSWQNOL-UHFFFAOYSA-N tungsten carbide Chemical compound [W+]#[C-] UONOETXJSWQNOL-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000003763 carbonization Methods 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 230000009467 reduction Effects 0.000 claims abstract description 17
- 238000005469 granulation Methods 0.000 claims abstract description 16
- 230000003179 granulation Effects 0.000 claims abstract description 16
- 238000002156 mixing Methods 0.000 claims abstract description 15
- 239000002245 particle Substances 0.000 claims description 15
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 12
- 229940011182 cobalt acetate Drugs 0.000 claims description 8
- QAHREYKOYSIQPH-UHFFFAOYSA-L cobalt(II) acetate Chemical compound [Co+2].CC([O-])=O.CC([O-])=O QAHREYKOYSIQPH-UHFFFAOYSA-L 0.000 claims description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 6
- 239000002041 carbon nanotube Substances 0.000 claims description 5
- 229910021393 carbon nanotube Inorganic materials 0.000 claims description 5
- 239000007789 gas Substances 0.000 claims description 5
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 239000001257 hydrogen Substances 0.000 claims description 4
- 239000006233 lamp black Substances 0.000 claims description 4
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 claims description 3
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 claims description 3
- 229910001981 cobalt nitrate Inorganic materials 0.000 claims description 3
- 229940044175 cobalt sulfate Drugs 0.000 claims description 3
- 229910000361 cobalt sulfate Inorganic materials 0.000 claims description 3
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 claims description 3
- 238000000227 grinding Methods 0.000 claims description 3
- 239000012071 phase Substances 0.000 abstract description 20
- 229910052751 metal Inorganic materials 0.000 abstract description 12
- 239000002184 metal Substances 0.000 abstract description 12
- 229910052721 tungsten Inorganic materials 0.000 abstract description 11
- 238000005261 decarburization Methods 0.000 abstract description 9
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 abstract description 8
- 239000010937 tungsten Substances 0.000 abstract description 8
- 239000000758 substrate Substances 0.000 abstract description 7
- 239000007791 liquid phase Substances 0.000 abstract description 6
- 238000000498 ball milling Methods 0.000 abstract description 5
- 238000000354 decomposition reaction Methods 0.000 abstract description 5
- 238000005507 spraying Methods 0.000 abstract description 2
- 239000004615 ingredient Substances 0.000 abstract 3
- 239000000203 mixture Substances 0.000 description 22
- 230000008569 process Effects 0.000 description 12
- 230000000704 physical effect Effects 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 5
- 238000009826 distribution Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 238000004458 analytical method Methods 0.000 description 4
- 238000009690 centrifugal atomisation Methods 0.000 description 4
- 239000011195 cermet Substances 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- 238000004904 shortening Methods 0.000 description 4
- 238000005245 sintering Methods 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 229930006000 Sucrose Natural products 0.000 description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 238000005422 blasting Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- -1 pulp Chemical compound 0.000 description 2
- 238000004626 scanning electron microscopy Methods 0.000 description 2
- 238000005204 segregation Methods 0.000 description 2
- 238000007873 sieving Methods 0.000 description 2
- 239000005720 sucrose Substances 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000000445 field-emission scanning electron microscopy Methods 0.000 description 1
- 238000010285 flame spraying Methods 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 238000007749 high velocity oxygen fuel spraying Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000006188 syrup Substances 0.000 description 1
- 235000020357 syrup Nutrition 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/02—Making metallic powder or suspensions thereof using physical processes
- B22F9/06—Making metallic powder or suspensions thereof using physical processes starting from liquid material
- B22F9/08—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/16—Making metallic powder or suspensions thereof using chemical processes
- B22F9/18—Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds
- B22F9/24—Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds starting from liquid metal compounds, e.g. solutions
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C4/00—Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge
- C23C4/04—Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge characterised by the coating material
- C23C4/06—Metallic material
Definitions
- the invention relates to the technical field of thermal spraying materials, in particular to a method for preparing WC-Co powder for thermal spraying.
- WC-Co-based cermet is the most studied and widely used cermet in carbide-based cermet.
- the thermal spray coating of WC-Co cermet is widely used in aerospace, due to its good hardness and toughness. Automotive, metallurgy, machinery and other fields.
- the preparation of WC-Co powder coating by supersonic flame spraying (HVOF) technology is a research hotspot, which can replace the hard chrome technology with high energy consumption and serious pollution to solve the wear resistance of spacecraft and repair worn parts.
- HVOF supersonic flame spraying
- the preparation method of WC-Co powder for metal thermal spraying WC-Co powder includes melting method, sintering-crushing method, plasma spheroidizing method and agglomeration sintering (spray granulation)-crushing method, etc., but melting
- the spray powder produced by the method and the sintering crushing method has irregular morphology, poor sphericity, poor flowability, low powder deposition rate, poor bonding strength between the coating and the substrate, and cracks and even peeling of the coating during use. And the failure, while the production process brings dust and noise pollution to the surrounding environment.
- the equipment is required to be high and the production cost is high.
- the thermal spraying powder with excellent performance can be obtained, the powder has a long holding time in the high-temperature sintering process, consumes a large amount of energy, and the powder after sintering is bonded in a block shape, and needs to be crushed. Grading, prolonging the production cycle, increases production costs.
- a spray granulation method is one of the current industrial production methods of WC-Co powder metal thermal spraying.
- the application numbers are CN201110336004.3, CN201210061980.7, CN201110321680.3 and CN201210370225.7.
- the preparation of WC-Co thermal spray powder by spray granulation method is basically the same.
- a thermally sprayed tungsten carbide-cobalt composite powder with excellent properties was prepared.
- these methods have the problems of adding a molding agent during the preparation process, increasing the subsequent dewaxing process, crushing and sieving, and causing pollution to the environment during the dewaxing process.
- the method provided by the present invention avoids dewaxing, crushing and sieving, shortens the process flow, and uniformly coats the WC grains in the Co phase.
- the present invention provides a method of preparing a WC-Co powder for thermal spraying, comprising the steps of:
- the mixed slurry is ball milled and then spray granulated to obtain a cobalt salt coated WC precursor powder;
- the cobalt salt is coated with a WC precursor powder to carry out reduction carbonization to obtain a WC-Co powder.
- the water-soluble cobalt salt is one or more of cobalt nitrate, cobalt acetate, cobalt chloride and cobalt sulfate.
- the mass ratio of the tungsten carbide, the water-soluble cobalt salt and the carbon source is a:b:c, 50 ⁇ a ⁇ 70, 28 ⁇ b ⁇ 49, 0 ⁇ c ⁇ 2.
- the tungsten carbide has a particle size of 0.1 ⁇ m to 8.0 ⁇ m.
- the carbon source comprises one or more of carbon black, lamp black, carbon nanotubes and organic carbon.
- the mixed slurry has a mass content of cobalt of from 3 wt% to 20 wt%.
- the reduction carbonization is carried out in an atmosphere of a reducing gas
- the reducing gas includes hydrogen and methane.
- the volume ratio of the hydrogen gas to the methane is (90 to 99): (1 to 10).
- the temperature of the reduction carbonization is 950 ° C to 1350 ° C.
- the reduction carbonization time is from 5 min to 60 min.
- the present invention provides a method for preparing a WC-Co powder for thermal spraying, comprising the steps of: mixing tungsten carbide, a water-soluble cobalt salt, a carbon source and water to obtain a mixed slurry; and grinding and mixing the mixed slurry. Thereafter, spray granulation is carried out to obtain a cobalt salt-coated WC precursor powder; the cobalt salt is coated with the WC precursor powder to carry out reduction carbonization to obtain a WC-Co powder.
- the method provided by the invention uses a water-soluble cobalt salt as a cobalt source, and prepares a cobalt salt-coated WC precursor powder by a liquid phase method, so that cobalt is coated on the surface of the WC as a solution ion, and the cobalt salt is coated.
- the WC precursor powder is reduced in carbonization to obtain a WC-Co powder.
- the invention adopts water-soluble cobalt salt and organic carbon instead of forming agent to avoid dewaxing, and does not need to crush and sieve the obtained product, thereby shortening the process flow.
- the method provided by the present invention avoids the direct addition of cobalt metal to segregate the components caused by the uneven mixing.
- the WC-Co powder prepared by the invention has high free carbon content, so that no decarburization phase is generated at high temperature during thermal spraying on the surface of the base material; and the invention can be reduced to carbonized into spherical WC at low temperature.
- Co powder can be used as thermal spray powder, uniform particle size; low energy consumption, low equipment investment; controllable composition, uniform powder composition, no W 2 C, ⁇ -Co 3 W 3 C, ⁇ -Co 6 W in the composition 6 C, metal tungsten, etc.; high sphericity and good fluidity, no decarburization phase and phase decomposition of the sprayed substrate surface.
- FIG. 1 is a schematic flow chart of preparing a WC-Co powder according to an embodiment of the present invention
- Example 2 is a SEM photograph of a precursor powder obtained in Example 2 of the present invention at 2000 magnifications;
- Example 3 is a SEM photograph of 2000 times magnification of WC-Co powder obtained in Example 2 of the present invention.
- Example 4 is an XRD photograph of a cobalt-coated nano WC obtained in Example 2 of the present invention.
- Fig. 6 is a photograph showing a metallographic photograph of a WC-Co powder obtained in the second embodiment of the present invention at a magnification of 1000 and 1500 times.
- the present invention provides a method of preparing a WC-Co powder for thermal spraying, comprising the steps of:
- the mixed slurry is ball milled and then spray granulated to obtain a cobalt salt coated WC precursor powder;
- the cobalt salt is coated with a WC precursor powder to carry out reduction carbonization to obtain a WC-Co powder.
- the invention adopts water-soluble cobalt salt and organic carbon instead of forming agent to avoid dewaxing, and does not need to crush and sieve the obtained product, thereby shortening the process flow.
- the water-soluble cobalt salt is used as the cobalt source, and when the cobalt salt-coated WC precursor powder is prepared by the liquid phase method, the cobalt is uniformly mixed in a molecular form without causing segregation of components.
- the WC-Co powder prepared by the invention has uniform particle size, high sphericity, good fluidity, and uniform and controllable composition, and does not decompose the decarburized camera phase on the surface of the sprayed substrate when used for thermal spraying.
- the present invention mixes tungsten carbide, a water-soluble cobalt salt, a carbon source and water to obtain a mixed slurry.
- tungsten carbide, a water-soluble cobalt salt and a carbon source are preferably added to water and mixed to obtain a mixed slurry.
- the water-soluble cobalt salt is preferably one or more of cobalt nitrate, cobalt acetate, cobalt chloride and cobalt sulfate, more preferably cobalt acetate;
- the carbon source preferably comprises carbon black, lamp black One or more of carbon nanotubes and organic carbon, more preferably carbon black, lamp black, ethylene diamine, fiber, pulp, acetylene black, carbon nanotubes, glucose, polyacrylonitrile, syrup and sucrose One or several; in an embodiment of the invention, the water may be pure water.
- the grain size of the tungsten carbide is preferably from 0.1 ⁇ m to 8.0 ⁇ m, more preferably from 0.2 ⁇ m to 1.0 ⁇ m; in the embodiment of the present invention, the tungsten carbide may have a particle size of from 0.5 ⁇ m to 0.6 ⁇ m.
- the present invention has no particular limitation on the source of the tungsten carbide, the water-soluble cobalt salt, the carbon source and the water, and the tungsten carbide, the water-soluble cobalt salt, the carbon source and the water which are well known to those skilled in the art can be used, for example, the city can be used. Selling goods. Specifically, in the embodiment of the present invention, a commercially available tungsten carbide having a grade of GWC002 may be used.
- the mass ratio of the tungsten carbide, the water-soluble cobalt salt and the carbon source is preferably a:b:c, 50 ⁇ a ⁇ 70, 28 ⁇ b ⁇ 49, 0 ⁇ c ⁇ 2, more preferably 55 ⁇ a ⁇ 65, 30 ⁇ b ⁇ 45, 0.5 ⁇ c ⁇ 1.5;
- the mass ratio of the total mass of the tungsten carbide, the water-soluble cobalt salt and the carbon source to water is preferably 1: (0.5 to 3), more preferably 1: (1 to 2.5), most preferably 1: (1.5 to 2.0);
- the mass content of cobalt in the mixed slurry is preferably from 3% by weight to 20% by weight, more preferably from 5% by weight to 18% by weight, most preferably 6% by weight. % ⁇ 17wt%.
- the mixed slurry is ball milled and then spray granulated to obtain a cobalt salt coated WC precursor powder.
- the method for ball milling and mixing in the present invention is not particularly limited, and a technical solution of ball milling and mixing well known to those skilled in the art may be employed, such as rolling ball milling.
- the time for the ball mill to mix is preferably from 3 h to 12 h, more preferably from 4 h to 12 h, and most preferably from 6 h to 10 h.
- the inlet blasting temperature of the spray granulation is preferably from 180 ° C to 300 ° C, more preferably from 200 ° C to 280 ° C, most preferably from 220 ° C to 260 ° C; and the outlet blasting temperature of the spray granulation is preferably It is 80 ° C to 180 ° C, more preferably 100 ° C to 170 ° C, most preferably 120 ° C to 160 ° C; the centrifugal atomization rotational speed of the spray granulation is preferably from 6000 r / min to 15000 r / min, more preferably 8000 r / From min to 13500 r/min, most preferably from 10,000 r/min to 12000 r/min.
- the present invention reduces carbonization of the cobalt salt-coated precursor to obtain a WC-Co powder.
- the present invention preferably reductively carbonizes the cobalt salt precursor in a reducing gas atmosphere, preferably including hydrogen and methane.
- the volume ratio of the hydrogen gas to the methane is preferably (90 to 99): (1 to 10), more preferably (95 to 99): (1 to 5), and most preferably (98 to 99). : (1 to 2).
- the temperature of the reduction carbonization is preferably 950 ° C to 1350 ° C, more preferably 1100 to 1300 ° C, most preferably 1150 ° C to 1250 ° C;
- the reduction carbonization time is preferably 5 min to 60 min, more preferably It is 10 min to 40 min, and most preferably 20 min to 30 min.
- FIG. 1 is a schematic flow chart of preparing a WC-Co powder according to an embodiment of the present invention.
- a tungsten carbide, a cobalt acetate, and an organic carbon are formulated into a mixed slurry; and the mixed slurry is subjected to ball milling and then spray granulated.
- the coated WC precursor powder is reduced in carbonization to obtain a WC-Co powder.
- the present invention performs scanning electron microscopy scanning analysis on the obtained cobalt salt-coated WC precursor powder and WC-Co powder, and as a result, it can be seen that the cobalt salt-coated WC precursor powder and WC-Co powder obtained by the method provided by the present invention are obtained. Uniform particle size, high sphericity, and thus higher fluidity;
- the WC-Co powder obtained by the invention is subjected to X-ray diffraction analysis, and the results show that the cobalt-coated nano WC-Co component obtained by the method provided by the invention is uniform, and no W 2 C, ⁇ -Co 3 W 3 C, ⁇ -Co 6 W 6 C, metal tungsten, etc.; the content of free carbon is high, so that it does not generate a decarburization phase at a high temperature on the surface of the base material when used for thermal spraying.
- the present invention provides a method for preparing a WC-Co powder for thermal spraying, comprising the steps of: mixing tungsten carbide, a water-soluble cobalt salt, a carbon source and water to obtain a mixed slurry; and grinding and mixing the mixed slurry Thereafter, spray granulation is carried out to obtain a cobalt salt-coated WC precursor powder; the cobalt salt is coated with the WC precursor powder to carry out reduction carbonization to obtain a WC-Co powder.
- the method provided by the invention uses a water-soluble cobalt salt as a cobalt source, and prepares a cobalt salt-coated WC precursor powder by a liquid phase method, so that cobalt is uniformly coated on the surface of the WC in a molecular form, and then the cobalt salt is coated.
- the WC precursor powder is reduced in carbonization to obtain a WC-Co powder.
- the invention adopts water-soluble cobalt salt and organic carbon instead of forming agent to avoid dewaxing, and does not need to crush and sieve the obtained product, thereby shortening the process flow.
- the method provided by the present invention avoids the direct addition of cobalt metal to segregate the components caused by the uneven mixing.
- the WC-Co powder prepared by the invention has high free carbon content, so that no decarburization phase is generated at high temperature during thermal spraying on the surface of the base material; and the invention can be reduced to carbonized into spherical WC at low temperature.
- Co powder can be used as thermal spray powder, uniform particle size; low energy consumption, low equipment investment; controllable composition, uniform powder composition, no W 2 C, ⁇ -Co 3 W 3 C, ⁇ -Co 6 W in the composition 6 C, metal tungsten, etc.; high sphericity and good fluidity, no decarburization phase and phase decomposition of the sprayed substrate surface.
- step 2) After the ball slurry obtained in the step 1) is ball milled for 6 hours, spray granulation is carried out.
- the inlet air temperature is 260 ° C
- the outlet air temperature is 160 ° C
- the centrifugal atomization speed is 12000 r/min. , obtaining a cobalt salt coated WC precursor powder;
- Table 1 shows the physical properties and chemical compositions of the WC-Co powders obtained in the examples of the present invention.
- step 2) After the ball slurry obtained in the step 1) is ball milled for 8 hours, spray granulation is carried out.
- the inlet air temperature is 260 ° C
- the outlet air temperature is 140 ° C
- the centrifugal atomization rotation speed is 10000 r / min. , obtaining a cobalt salt coated WC precursor powder;
- FIG. 2 is a SEM photograph of the precursor powder obtained in Example 2 of the present invention at 2000 times magnification. As can be seen from FIG. 2, the present invention The obtained precursor powder has a uniform particle size and a spherical shape;
- the invention performs scanning electron microscopy scanning analysis on the obtained WC-Co powder, and the result is shown in FIG. 3 is a SEM photograph of 2000 times magnification of the WC-Co powder obtained in Example 2 of the present invention.
- the WC-Co powder prepared by the present invention has uniform particle size and high sphericity.
- FIG. 4 is an XRD photograph of the cobalt-coated nano WC obtained in Example 2 of the present invention, as can be seen from FIG.
- the WC-Co powder component prepared by the invention is uniformly mixed; W2C, ⁇ (Co 3 W 3 C, Co 6 W 6 C), metal tungsten or the like does not appear in the WC-Co powder.
- FIG. 5 is a magnified 5000 of cobalt-coated nano WC-Co powder obtained in Example 2 of the present invention.
- the SEM photograph and the surface distribution of the W and Co elements are doubled, wherein (a) is a SEM photograph of the cobalt-coated nano-WC-Co powder obtained in Example 2 of the present invention at a magnification of 5000 times, and (b) is Example 2 of the present invention.
- the obtained cobalt-coated nano-WC-Co powder is magnified 5000 times under the W element surface distribution photograph
- (c) is a cobalt-coated nano-WC-Co powder obtained in Example 2 of the present invention, magnified 5000 times under the Co element surface distribution photo
- the WC-Co powder prepared by the invention has a uniform distribution of W and Co phases, and the Co phase uniformly coats the WC grains.
- FIG. 6 is a metallographic profile of the cobalt-coated nano-WC-Co powder obtained in Example 2 of the present invention at 1000 and 1500 times magnification.
- Photograph (a) is a photograph of a metallographic cross-section of a cobalt-coated nano-WC-Co powder obtained in Example 2 of the present invention at a magnification of 1000 times, and (b) a magnified cobalt-coated nano-WC-Co obtained in Example 2 of the present invention.
- Table 1 shows the physical properties and chemical compositions of the WC-Co powders obtained in the examples of the present invention.
- step 2) After the mixture slurry obtained in the step 1) is ball-milled for 8 hours, spray granulation is carried out.
- the inlet air temperature is 260 ° C
- the outlet air temperature is 160 ° C
- the centrifugal atomization rotation speed is 10000 r / min. , obtaining a cobalt salt coated WC precursor powder;
- Table 1 shows the physical properties and chemical compositions of the WC-Co powders obtained in the examples of the present invention.
- the WC-Co powder prepared by the invention has uniform particle size, uniform and controllable composition, and does not cause component segregation; and the WC-Co powder prepared by the invention has high free carbon content, so that the body is made. During the thermal spraying process, the sprayed powder does not produce a decarburized phase at high temperatures.
- the present invention provides a method for preparing a WC-Co powder for thermal spraying, comprising the steps of: mixing tungsten carbide, a water-soluble cobalt salt, a carbon source and water to obtain a mixed slurry; The mixed slurry is ball milled and mixed, and then spray granulated to obtain a cobalt salt coated WC precursor powder; the cobalt salt is coated with the WC precursor powder for reduction carbonization to obtain a WC-Co powder.
- the method provided by the invention uses a water-soluble cobalt salt as a cobalt source, and prepares a cobalt salt-coated WC precursor powder by a liquid phase method, so that the cobalt is coated in a solution ion form. On the surface of the WC, the cobalt salt-coated WC precursor powder is reduced and carbonized to obtain a WC-Co powder.
- the invention adopts water-soluble cobalt salt and organic carbon instead of forming agent to avoid dewaxing, and does not need to crush and sieve the obtained product, thereby shortening the process flow.
- the method provided by the present invention avoids the direct addition of cobalt metal to segregate the components caused by the uneven mixing.
- the WC-Co powder prepared by the invention has high free carbon content, so that no decarburization phase is generated at high temperature during thermal spraying on the surface of the base material; and the invention can be reduced to carbonized into spherical WC at low temperature.
- Co powder can be used as thermal spray powder, uniform particle size; low energy consumption, low equipment investment; controllable composition, uniform powder composition, no W 2 C, ⁇ -Co 3 W 3 C, ⁇ -Co 6 W in the composition 6 C, metal tungsten, etc.; high sphericity and good fluidity, no decarburization phase and phase decomposition of the sprayed substrate surface.
- the method for preparing WC-Co powder uses a water-soluble cobalt salt as a cobalt source, and prepares a cobalt salt-coated WC precursor powder by a liquid phase method, so that cobalt is uniformly coated on the surface of the WC in a solution molecular level form. Then, the cobalt salt coated WC precursor powder is reduced and carbonized to obtain a WC-Co powder.
- the WC-Co powder obtained by the invention has uniform particle size, controllable composition, uniform powder composition, no W 2 C, ⁇ -Co 3 W 3 C, ⁇ -Co 6 W 6 C, metal tungsten, etc. in the composition; high sphericity And the fluidity is good, the decarburization phase and the decomposition of the phase do not occur on the surface of the sprayed substrate.
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Abstract
A method for preparing WC-Co powder comprises the following steps: mixing tungsten carbide, water soluble cobalt salt, a carbon source and water to obtain mixed slurry; after ball-milling and even-blending are conducted on the mixed slurry, conducting spray granulation to obtain WC precursor powder coated by the cobalt salt; and conducting reduction and carbonization on the WC precursor powder coated by the cobalt salt, to obtain WC-Co powder. In the method, the water soluble cobalt salt serves as a cobalt source, and the WC precursor powder coated by the cobalt salt is prepared by using a liquid phase method, so that the cobalt is evenly coated on the surface of the WC in a solution molecular form, and reduction and carbonization are conducted on the WC precursor powder coated by the cobalt salt to obtain the WC-Co powder. The WC-Co powder is even in granularity, controllable in ingredients, even in powder ingredients, and free of W2C, η-Co3W3C, η-Co6W6C, metal tungsten and the like in the ingredients; has high degree of sphericity and good mobility; and does not cause the decarburization phase and phase decomposition on the surface of a spraying substrate.
Description
本发明涉及热喷涂材料技术领域,尤其涉及一种制备热喷涂用WC-Co粉末的方法。The invention relates to the technical field of thermal spraying materials, in particular to a method for preparing WC-Co powder for thermal spraying.
WC-Co基金属陶瓷是碳化物基金属陶瓷中研究最多、应用最广的金属陶瓷,其中WC-Co金属陶瓷的热喷涂涂层,由于其良好的硬度和韧性,广泛地应用于航空航天、汽车、冶金、机械等领域。利用超音速火焰喷涂(HVOF)技术制备WC-Co粉末系涂层是研究的热点,可替代能耗高、污染严重的电镀硬铬技术,以解决航天器的耐磨性能及修复磨损部件。WC-Co-based cermet is the most studied and widely used cermet in carbide-based cermet. The thermal spray coating of WC-Co cermet is widely used in aerospace, due to its good hardness and toughness. Automotive, metallurgy, machinery and other fields. The preparation of WC-Co powder coating by supersonic flame spraying (HVOF) technology is a research hotspot, which can replace the hard chrome technology with high energy consumption and serious pollution to solve the wear resistance of spacecraft and repair worn parts.
现有技术中,WC-Co粉末系金属热喷涂用WC-Co粉末的制备方法包括熔化法、烧结-破碎法、等离子体球化法和团聚烧结(喷雾造粒)-破碎法等,但是熔化法、烧结破碎法生产的喷涂粉末颗粒形貌不规则,球形度较差,流动性能差,粉末沉积率较低,涂层与基体结合强度较差,使用过程中涂层易出现裂纹甚至剥落现象而失效,同时生产过程中给周围环境带来粉尘和噪音污染。对于等离子体球化法,由于整个球化过程是在高温和保护气氛环境中进行的,对设备要求高,生产成本高昂。对于传统团聚烧结-破碎法,虽然也能获得性能优良的热喷涂粉末,但粉末在高温烧结过程中保温时间较长,耗能大,且烧结后的粉末粘结呈块状,需进行破碎、分级,延长了生产周期,使得生产成本升高。In the prior art, the preparation method of WC-Co powder for metal thermal spraying WC-Co powder includes melting method, sintering-crushing method, plasma spheroidizing method and agglomeration sintering (spray granulation)-crushing method, etc., but melting The spray powder produced by the method and the sintering crushing method has irregular morphology, poor sphericity, poor flowability, low powder deposition rate, poor bonding strength between the coating and the substrate, and cracks and even peeling of the coating during use. And the failure, while the production process brings dust and noise pollution to the surrounding environment. For the plasma spheroidization method, since the entire spheroidization process is carried out in a high temperature and protective atmosphere environment, the equipment is required to be high and the production cost is high. For the traditional agglomeration sintering-crushing method, although the thermal spraying powder with excellent performance can be obtained, the powder has a long holding time in the high-temperature sintering process, consumes a large amount of energy, and the powder after sintering is bonded in a block shape, and needs to be crushed. Grading, prolonging the production cycle, increases production costs.
目前发展了一种喷雾造粒法,其是目前工业化生产WC-Co粉末系金属热喷涂方法之一。如申请号为CN201110336004.3、CN201210061980.7、CN201110321680.3和CN201210370225.7均是采用喷雾造粒法进行WC-Co热喷涂粉末的制备,原理基本相同,都能够
制备出性能优异热喷涂碳化钨钴复合粉。但是,这些方法存在制备过程中需要添加成型剂,增加后续脱蜡工艺、破碎和筛分,同时脱蜡过程对环境产生污染等问题。At present, a spray granulation method has been developed, which is one of the current industrial production methods of WC-Co powder metal thermal spraying. For example, the application numbers are CN201110336004.3, CN201210061980.7, CN201110321680.3 and CN201210370225.7. The preparation of WC-Co thermal spray powder by spray granulation method is basically the same.
A thermally sprayed tungsten carbide-cobalt composite powder with excellent properties was prepared. However, these methods have the problems of adding a molding agent during the preparation process, increasing the subsequent dewaxing process, crushing and sieving, and causing pollution to the environment during the dewaxing process.
发明内容Summary of the invention
本发明的目的在于提供一种制备热喷涂用热喷涂用WC-Co粉末的方法,本发明提供的方法避免脱蜡、破碎和筛分,缩短了工艺流程、Co相均匀包覆WC晶粒。It is an object of the present invention to provide a method for preparing WC-Co powder for thermal spraying for thermal spraying. The method provided by the present invention avoids dewaxing, crushing and sieving, shortens the process flow, and uniformly coats the WC grains in the Co phase.
本发明提供了一种制备热喷涂用WC-Co粉末的方法,包括以下步骤:The present invention provides a method of preparing a WC-Co powder for thermal spraying, comprising the steps of:
将碳化钨、水溶性钴盐、碳源和水混合,得到混合料浆;Mixing tungsten carbide, water-soluble cobalt salt, carbon source and water to obtain a mixed slurry;
将所述混合料浆球磨后进行喷雾造粒,得到钴盐包覆WC前驱体粉末;The mixed slurry is ball milled and then spray granulated to obtain a cobalt salt coated WC precursor powder;
将所述钴盐包覆WC前驱体粉末进行还原碳化,得到WC-Co粉末。The cobalt salt is coated with a WC precursor powder to carry out reduction carbonization to obtain a WC-Co powder.
优选的,所述水溶性钴盐为硝酸钴、醋酸钴、氯化钴和硫酸钴中一种或几种。Preferably, the water-soluble cobalt salt is one or more of cobalt nitrate, cobalt acetate, cobalt chloride and cobalt sulfate.
优选的,所述碳化钨、水溶性钴盐和碳源的质量比为a∶b∶c,50≤a≤70,28≤b≤49,0<c≤2。Preferably, the mass ratio of the tungsten carbide, the water-soluble cobalt salt and the carbon source is a:b:c, 50≤a≤70, 28≤b≤49, 0<c≤2.
优选的,所述碳化钨的粒度为0.1μm~8.0μm。Preferably, the tungsten carbide has a particle size of 0.1 μm to 8.0 μm.
优选的,所述碳源包括炭黑、灯黑、碳纳米管和有机碳中的一种或几种。Preferably, the carbon source comprises one or more of carbon black, lamp black, carbon nanotubes and organic carbon.
优选的,所述混合料浆中钴的质量含量为3wt%~20wt%。Preferably, the mixed slurry has a mass content of cobalt of from 3 wt% to 20 wt%.
优选的,所述还原碳化在还原气体的气氛中进行;Preferably, the reduction carbonization is carried out in an atmosphere of a reducing gas;
所述还原气体包括氢气和甲烷。The reducing gas includes hydrogen and methane.
优选的,所述氢气和甲烷的体积比为(90~99)∶(1~10)。Preferably, the volume ratio of the hydrogen gas to the methane is (90 to 99): (1 to 10).
优选的,所述还原碳化的温度为950℃~1350℃。Preferably, the temperature of the reduction carbonization is 950 ° C to 1350 ° C.
优选的,所述还原碳化的时间为5min~60min。
Preferably, the reduction carbonization time is from 5 min to 60 min.
本发明提供了一种制备热喷涂用WC-Co粉末的方法,包括以下步骤:将碳化钨、水溶性钴盐、碳源和水混合,得到混合料浆;将所述混合料浆球磨混匀后进行喷雾造粒,得到钴盐包覆WC前驱体粉末;将所述钴盐包覆WC前驱体粉末进行还原碳化,得到WC-Co粉末。本发明提供的方法以水溶性钴盐作为钴源,采用液相法制备得到钴盐包覆WC前驱体粉末,使得钴以溶液离子形式包覆在WC的表面,再将所述钴盐包覆WC前驱体粉末还原碳化,得到WC-Co粉末。本发明采用水溶性钴盐和有机碳代替成型剂,避免脱蜡,且无需对得到的产品进行破碎和筛分,缩短工艺流程。The present invention provides a method for preparing a WC-Co powder for thermal spraying, comprising the steps of: mixing tungsten carbide, a water-soluble cobalt salt, a carbon source and water to obtain a mixed slurry; and grinding and mixing the mixed slurry. Thereafter, spray granulation is carried out to obtain a cobalt salt-coated WC precursor powder; the cobalt salt is coated with the WC precursor powder to carry out reduction carbonization to obtain a WC-Co powder. The method provided by the invention uses a water-soluble cobalt salt as a cobalt source, and prepares a cobalt salt-coated WC precursor powder by a liquid phase method, so that cobalt is coated on the surface of the WC as a solution ion, and the cobalt salt is coated. The WC precursor powder is reduced in carbonization to obtain a WC-Co powder. The invention adopts water-soluble cobalt salt and organic carbon instead of forming agent to avoid dewaxing, and does not need to crush and sieve the obtained product, thereby shortening the process flow.
而且,本发明提供的方法避免直接添加钴金属使混合不均匀造成的成分偏析。同时本发明制备得到的WC-Co粉末中游离碳含量高,使其在基体材料表面热喷涂过程中,在高温下不产生脱碳相;同时本发明在低温下就可还原碳化成球形WC-Co粉末,可用作热喷涂粉,粒度均匀;能耗低,设备投资小;成分可控,粉末成分均匀、成分中未出现W2C、η-Co3W3C、η-Co6W6C、金属钨等;球形度高及流动性好,喷涂基体表面不发生脱碳相及相的分解。Moreover, the method provided by the present invention avoids the direct addition of cobalt metal to segregate the components caused by the uneven mixing. At the same time, the WC-Co powder prepared by the invention has high free carbon content, so that no decarburization phase is generated at high temperature during thermal spraying on the surface of the base material; and the invention can be reduced to carbonized into spherical WC at low temperature. Co powder, can be used as thermal spray powder, uniform particle size; low energy consumption, low equipment investment; controllable composition, uniform powder composition, no W 2 C, η-Co 3 W 3 C, η-Co 6 W in the composition 6 C, metal tungsten, etc.; high sphericity and good fluidity, no decarburization phase and phase decomposition of the sprayed substrate surface.
图1为本发明实施例提供的制备WC-Co粉末的流程示意图;1 is a schematic flow chart of preparing a WC-Co powder according to an embodiment of the present invention;
图2为本发明实施例2得到的前驱体粉末放大2000倍的SEM照片;2 is a SEM photograph of a precursor powder obtained in Example 2 of the present invention at 2000 magnifications;
图3为本发明实施例2得到的WC-Co粉末放大2000倍的SEM照片;3 is a SEM photograph of 2000 times magnification of WC-Co powder obtained in Example 2 of the present invention;
图4为本发明实施例2得到的钴包覆纳米WC的XRD照片;4 is an XRD photograph of a cobalt-coated nano WC obtained in Example 2 of the present invention;
图5为本发明实施列2得到的WC-Co粉末放大5000倍下SEM照片及W、Co元素面分布照片;5 is a SEM photograph and a surface distribution of W and Co elements of the WC-Co powder obtained in the second embodiment of the present invention at a magnification of 5000 times;
图6为本发明实施列2得到的WC-Co粉末放大1000、1500倍下剖面的金相照片。Fig. 6 is a photograph showing a metallographic photograph of a WC-Co powder obtained in the second embodiment of the present invention at a magnification of 1000 and 1500 times.
本发明提供了一种制备热喷涂用WC-Co粉末的方法,包括以下步骤:The present invention provides a method of preparing a WC-Co powder for thermal spraying, comprising the steps of:
将碳化钨、水溶性钴盐、碳源和水混合,得到混合料浆;Mixing tungsten carbide, water-soluble cobalt salt, carbon source and water to obtain a mixed slurry;
将所述混合料浆球磨后进行喷雾造粒,得到钴盐包覆WC前驱体粉末;The mixed slurry is ball milled and then spray granulated to obtain a cobalt salt coated WC precursor powder;
将所述钴盐包覆WC前驱体粉末进行还原碳化,得到WC-Co粉末。The cobalt salt is coated with a WC precursor powder to carry out reduction carbonization to obtain a WC-Co powder.
本发明采用水溶性钴盐和有机碳代替成型剂,避免脱蜡,且无需对得到的产品进行破碎和筛分,缩短工艺流程。本发明以水溶性钴盐作为钴源,采用液相法制备得到钴盐包覆WC前驱体粉末时,钴以分子形式混合均匀,不会造成成分偏析。本发明制备得到的WC-Co粉末粒度均匀,球形度高、流动性好,且成分均匀可控,作为热喷涂用时喷涂基体表面不发生脱碳相机相的分解。The invention adopts water-soluble cobalt salt and organic carbon instead of forming agent to avoid dewaxing, and does not need to crush and sieve the obtained product, thereby shortening the process flow. In the invention, the water-soluble cobalt salt is used as the cobalt source, and when the cobalt salt-coated WC precursor powder is prepared by the liquid phase method, the cobalt is uniformly mixed in a molecular form without causing segregation of components. The WC-Co powder prepared by the invention has uniform particle size, high sphericity, good fluidity, and uniform and controllable composition, and does not decompose the decarburized camera phase on the surface of the sprayed substrate when used for thermal spraying.
本发明将碳化钨、水溶性钴盐、碳源和水混合,得到混合料浆。本发明优选将碳化钨、水溶性钴盐和碳源加入到水中,混匀得到混合料浆。在本发明中,所述水溶性钴盐优选为硝酸钴、醋酸钴、氯化钴和硫酸钴中的一种或几种,更优选为醋酸钴;所述碳源优选包括炭黑、灯黑、碳纳米管和有机碳中的一种或几种,更优选为炭黑、灯黑、乙二胺、纤维、纸浆、乙炔黑、碳纳米管、葡萄糖、聚丙烯腈、糖浆和蔗糖中的一种或几种;在本发明的实施例中,所述水可以为纯水。在本发明中,所述碳化钨的粒度优选为0.1μm~8.0μm,更优选为0.2μm~1.0μm;在本发明的实施例中,所述碳化钨的粒度可以为0.5μm~0.6μm。The present invention mixes tungsten carbide, a water-soluble cobalt salt, a carbon source and water to obtain a mixed slurry. In the present invention, tungsten carbide, a water-soluble cobalt salt and a carbon source are preferably added to water and mixed to obtain a mixed slurry. In the present invention, the water-soluble cobalt salt is preferably one or more of cobalt nitrate, cobalt acetate, cobalt chloride and cobalt sulfate, more preferably cobalt acetate; the carbon source preferably comprises carbon black, lamp black One or more of carbon nanotubes and organic carbon, more preferably carbon black, lamp black, ethylene diamine, fiber, pulp, acetylene black, carbon nanotubes, glucose, polyacrylonitrile, syrup and sucrose One or several; in an embodiment of the invention, the water may be pure water. In the present invention, the grain size of the tungsten carbide is preferably from 0.1 μm to 8.0 μm, more preferably from 0.2 μm to 1.0 μm; in the embodiment of the present invention, the tungsten carbide may have a particle size of from 0.5 μm to 0.6 μm.
本发明对所述碳化钨、水溶性钴盐、碳源和水的来源没有特殊的限制,采用本领域技术人员熟知的碳化钨、水溶性钴盐、碳源和水即可,如可以采用市售商品。具体的,在本发明的实施例中,可以采用市售的牌号为GWC002的碳化钨。
The present invention has no particular limitation on the source of the tungsten carbide, the water-soluble cobalt salt, the carbon source and the water, and the tungsten carbide, the water-soluble cobalt salt, the carbon source and the water which are well known to those skilled in the art can be used, for example, the city can be used. Selling goods. Specifically, in the embodiment of the present invention, a commercially available tungsten carbide having a grade of GWC002 may be used.
在本发明中,所述碳化钨、水溶性钴盐和碳源的质量比优选为a∶b∶c,50≤a≤70,28≤b≤49,0<c≤2,更优选的55≤a≤65,30≤b≤45,0.5≤c≤1.5;所述碳化钨、水溶性钴盐和碳源的总质量与水的质量比优选为1∶(0.5~3),更优选为1∶(1~2.5),最优选为1∶(1.5~2.0);所述混合料浆中钴的质量含量优选为3wt%~20wt%,更优选为5wt%~18wt%,最优选为6wt%~17wt%。In the present invention, the mass ratio of the tungsten carbide, the water-soluble cobalt salt and the carbon source is preferably a:b:c, 50≤a≤70, 28≤b≤49, 0<c≤2, more preferably 55 ≤ a ≤ 65, 30 ≤ b ≤ 45, 0.5 ≤ c ≤ 1.5; the mass ratio of the total mass of the tungsten carbide, the water-soluble cobalt salt and the carbon source to water is preferably 1: (0.5 to 3), more preferably 1: (1 to 2.5), most preferably 1: (1.5 to 2.0); the mass content of cobalt in the mixed slurry is preferably from 3% by weight to 20% by weight, more preferably from 5% by weight to 18% by weight, most preferably 6% by weight. % ~ 17wt%.
得到混合料浆后,本发明将所述混合料浆球磨混匀后进行喷雾造粒,得到钴盐包覆WC前驱体粉末。本发明对所述球磨混匀的方法没有特殊的限制,采用本领域技术人员熟知的球磨混匀的技术方案即可,如可以采用滚动球磨。在本发明中,所述球磨混匀的时间优选为3h~12h,更优选为4h~12h,最优选为6h~10h。After the mixed slurry is obtained, in the present invention, the mixed slurry is ball milled and then spray granulated to obtain a cobalt salt coated WC precursor powder. The method for ball milling and mixing in the present invention is not particularly limited, and a technical solution of ball milling and mixing well known to those skilled in the art may be employed, such as rolling ball milling. In the present invention, the time for the ball mill to mix is preferably from 3 h to 12 h, more preferably from 4 h to 12 h, and most preferably from 6 h to 10 h.
在本发明中,所述喷雾造粒的进风温度优选为180℃~300℃,更优选为200℃~280℃,最优选为220℃~260℃;所述喷雾造粒的出风温度优选为80℃~180℃,更优选为100℃~170℃,最优选为120℃~160℃;所述喷雾造粒的离心雾化转速优选为6000r/min~15000r/min,更优选为8000r/min~13500r/min,最优选为10000r/min~12000r/min。In the present invention, the inlet blasting temperature of the spray granulation is preferably from 180 ° C to 300 ° C, more preferably from 200 ° C to 280 ° C, most preferably from 220 ° C to 260 ° C; and the outlet blasting temperature of the spray granulation is preferably It is 80 ° C to 180 ° C, more preferably 100 ° C to 170 ° C, most preferably 120 ° C to 160 ° C; the centrifugal atomization rotational speed of the spray granulation is preferably from 6000 r / min to 15000 r / min, more preferably 8000 r / From min to 13500 r/min, most preferably from 10,000 r/min to 12000 r/min.
得到钴盐包覆WC前驱体粉末后,本发明将所述钴盐包覆前驱体还原碳化,得到WC-Co粉末。本发明优选将所述钴盐前驱体在还原气体气氛中进行还原碳化,所述还原气体优选包括氢气和甲烷。在本发明中,所述氢气和甲烷的体积比优选为(90~99)∶(1~10),更优选为(95~99)∶(1~5),最优选为(98~99)∶(1~2)。在本发明中,所述还原碳化的温度优选为950℃~1350℃,更优选为1100~1300℃,最优选为1150℃~1250℃;所述还原碳化的时间优选为5min~60min,更优选为10min~40min,最优选为20min~30min。After obtaining a cobalt salt-coated WC precursor powder, the present invention reduces carbonization of the cobalt salt-coated precursor to obtain a WC-Co powder. The present invention preferably reductively carbonizes the cobalt salt precursor in a reducing gas atmosphere, preferably including hydrogen and methane. In the present invention, the volume ratio of the hydrogen gas to the methane is preferably (90 to 99): (1 to 10), more preferably (95 to 99): (1 to 5), and most preferably (98 to 99). : (1 to 2). In the present invention, the temperature of the reduction carbonization is preferably 950 ° C to 1350 ° C, more preferably 1100 to 1300 ° C, most preferably 1150 ° C to 1250 ° C; the reduction carbonization time is preferably 5 min to 60 min, more preferably It is 10 min to 40 min, and most preferably 20 min to 30 min.
参见图1,图1为本发明实施例提供的制备WC-Co粉末的流程示意图,首先将碳化钨、醋酸钴和有机碳配制成混合料浆;再将混合料浆进行球磨后喷雾造粒,得到钴盐包覆WC前驱体粉末;再将所述钴盐
包覆WC前驱体粉末还原碳化,得到WC-Co粉末。Referring to FIG. 1 , FIG. 1 is a schematic flow chart of preparing a WC-Co powder according to an embodiment of the present invention. First, a tungsten carbide, a cobalt acetate, and an organic carbon are formulated into a mixed slurry; and the mixed slurry is subjected to ball milling and then spray granulated. Obtaining a cobalt salt coated WC precursor powder; and then the cobalt salt
The coated WC precursor powder is reduced in carbonization to obtain a WC-Co powder.
本发明对得到的钴盐包覆WC前驱体粉末和WC-Co粉末进行扫描电镜扫描分析,结果可以看出,本发明提供的方法得到的钴盐包覆WC前驱体粉末和WC-Co粉末的粒度均匀,球形度较高,进而具有较高的流动性;The present invention performs scanning electron microscopy scanning analysis on the obtained cobalt salt-coated WC precursor powder and WC-Co powder, and as a result, it can be seen that the cobalt salt-coated WC precursor powder and WC-Co powder obtained by the method provided by the present invention are obtained. Uniform particle size, high sphericity, and thus higher fluidity;
本发明将得到的WC-Co粉末进行X-射线衍射分析,结果表明,本发明提供的方法得到的钴包覆纳米WC-Co成分均匀,未出现W2C、η-Co3W3C、η-Co6W6C、金属钨等;游离碳的含量较高,使其在用于热喷涂时在基体材料表面,在高温下不产生脱碳相。The WC-Co powder obtained by the invention is subjected to X-ray diffraction analysis, and the results show that the cobalt-coated nano WC-Co component obtained by the method provided by the invention is uniform, and no W 2 C, η-Co 3 W 3 C, η-Co 6 W 6 C, metal tungsten, etc.; the content of free carbon is high, so that it does not generate a decarburization phase at a high temperature on the surface of the base material when used for thermal spraying.
本发明提供了一种制备热喷涂用WC-Co粉末的方法,包括以下步骤:将碳化钨、水溶性钴盐、碳源和水混合,得到混合料浆;将所述混合料浆球磨混匀后进行喷雾造粒,得到钴盐包覆WC前驱体粉末;将所述钴盐包覆WC前驱体粉末进行还原碳化,得到WC-Co粉末。本发明提供的方法以水溶性钴盐作为钴源,采用液相法制备得到钴盐包覆WC前驱体粉末,使得钴以分子形式均匀包覆在WC的表面,再将所述钴盐包覆WC前驱体粉末还原碳化,得到WC-Co粉末。本发明采用水溶性钴盐和有机碳代替成型剂,避免脱蜡,且无需对得到的产品进行破碎和筛分,缩短工艺流程。The present invention provides a method for preparing a WC-Co powder for thermal spraying, comprising the steps of: mixing tungsten carbide, a water-soluble cobalt salt, a carbon source and water to obtain a mixed slurry; and grinding and mixing the mixed slurry Thereafter, spray granulation is carried out to obtain a cobalt salt-coated WC precursor powder; the cobalt salt is coated with the WC precursor powder to carry out reduction carbonization to obtain a WC-Co powder. The method provided by the invention uses a water-soluble cobalt salt as a cobalt source, and prepares a cobalt salt-coated WC precursor powder by a liquid phase method, so that cobalt is uniformly coated on the surface of the WC in a molecular form, and then the cobalt salt is coated. The WC precursor powder is reduced in carbonization to obtain a WC-Co powder. The invention adopts water-soluble cobalt salt and organic carbon instead of forming agent to avoid dewaxing, and does not need to crush and sieve the obtained product, thereby shortening the process flow.
而且,本发明提供的方法避免直接添加钴金属使混合不均匀造成的成分偏析。同时本发明制备得到的WC-Co粉末中游离碳含量高,使其在基体材料表面热喷涂过程中,在高温下不产生脱碳相;同时本发明在低温下就可还原碳化成球形WC-Co粉末,可用作热喷涂粉,粒度均匀;能耗低,设备投资小;成分可控,粉末成分均匀、成分中未出现W2C、η-Co3W3C、η-Co6W6C、金属钨等;球形度高及流动性好,喷涂基体表面不发生脱碳相及相的分解。Moreover, the method provided by the present invention avoids the direct addition of cobalt metal to segregate the components caused by the uneven mixing. At the same time, the WC-Co powder prepared by the invention has high free carbon content, so that no decarburization phase is generated at high temperature during thermal spraying on the surface of the base material; and the invention can be reduced to carbonized into spherical WC at low temperature. Co powder, can be used as thermal spray powder, uniform particle size; low energy consumption, low equipment investment; controllable composition, uniform powder composition, no W 2 C, η-Co 3 W 3 C, η-Co 6 W in the composition 6 C, metal tungsten, etc.; high sphericity and good fluidity, no decarburization phase and phase decomposition of the sprayed substrate surface.
为了进一步说明本发明,下面结合实施例对本发明提供的制备钴包覆纳米WC粉末的方法进行详细地描述,但不能将它们理解为对本
发明保护范围的限定。In order to further illustrate the present invention, the method for preparing the cobalt-coated nano WC powder provided by the present invention will be described in detail below with reference to the examples, but they cannot be understood as
The scope of the invention is limited.
实施例1Example 1
1)将粒度为0.5μm~0.6μm的50Kg碳化钨粉、21Kg醋酸钴和560g碳纳米管溶于质量是固体总质量1.5倍的纯水中,配制成钴含量为10wt%的混合料浆;1) 50Kg tungsten carbide powder having a particle size of 0.5 μm to 0.6 μm, 21 Kg of cobalt acetate and 560 g of carbon nanotubes are dissolved in pure water having a mass of 1.5 times the total mass of the solid, and formulated into a mixed slurry having a cobalt content of 10% by weight;
2)将步骤1)得到的混合料浆经球磨6小时后,进行喷雾造粒,喷雾造粒过程中,进风温度为260℃,出风温度为160℃,离心雾化转速为12000r/min,得到钴盐包覆WC前驱体粉末;2) After the ball slurry obtained in the step 1) is ball milled for 6 hours, spray granulation is carried out. During the spray granulation process, the inlet air temperature is 260 ° C, the outlet air temperature is 160 ° C, and the centrifugal atomization speed is 12000 r/min. , obtaining a cobalt salt coated WC precursor powder;
3)将步骤2)得到的前驱体粉末在1150℃条件下,在H2∶CH4(体积比)=98.5∶1.5的气氛下进行还原碳化60min,得到WC-Co粉末。3) The precursor powder obtained in the step 2) was subjected to reduction carbonization in an atmosphere of H 2 :CH 4 (volume ratio) = 98.5:1.5 at 1150 ° C for 60 minutes to obtain a WC-Co powder.
本发明检测了得到的WC-Co粉末的物理性能和化学组成,结果如表1所示,表1为本发明实施例得到的WC-Co粉末的物理性能和化学成分。The physical properties and chemical compositions of the obtained WC-Co powders were examined. The results are shown in Table 1. Table 1 shows the physical properties and chemical compositions of the WC-Co powders obtained in the examples of the present invention.
实施例2Example 2
1)将粒度0.5μm~0.6μm的50Kg碳化钨粉、29Kg醋酸钴、600g炭黑溶于质量是固体总质量1.8倍的纯水中,配制成钴含量为12wt%的混合料浆;1) 50Kg tungsten carbide powder having a particle size of 0.5μm to 0.6μm, 29Kg of cobalt acetate, and 600g of carbon black are dissolved in pure water having a mass of 1.8 times the total mass of the solid to prepare a mixed slurry having a cobalt content of 12% by weight;
2)将步骤1)得到的混合料浆经球磨8小时后,进行喷雾造粒,喷雾造粒过程中,进风温度为260℃,出风温度为140℃,离心雾化转速为10000r/min,得到钴盐包覆WC前驱体粉末;2) After the ball slurry obtained in the step 1) is ball milled for 8 hours, spray granulation is carried out. During the spray granulation process, the inlet air temperature is 260 ° C, the outlet air temperature is 140 ° C, and the centrifugal atomization rotation speed is 10000 r / min. , obtaining a cobalt salt coated WC precursor powder;
本发明将得到的前驱体粉末进行扫描电镜扫描分析,结果如图2所示,图2为本发明实施例2得到的前驱体粉末放大2000倍的SEM照片,由图2可以看出,本发明得到的前驱体粉末粒径均一,形状为球形;The obtained precursor powder is subjected to scanning electron microscope scanning analysis, and the result is shown in FIG. 2. FIG. 2 is a SEM photograph of the precursor powder obtained in Example 2 of the present invention at 2000 times magnification. As can be seen from FIG. 2, the present invention The obtained precursor powder has a uniform particle size and a spherical shape;
3)将步骤2)得到的前驱体粉末在1250℃条件,在H2∶CH4(体积比)=98.65∶1.35的气氛下进行还原碳化40min,得到WC-Co粉末。3) The precursor powder obtained in the step 2) was subjected to reduction carbonization in an atmosphere of H 2 : CH 4 (volume ratio) = 98.65: 1.35 at 1250 ° C for 40 min to obtain a WC-Co powder.
本发明对得到的WC-Co粉末进行扫描电镜扫描分析,结果如图3
所示,图3为本发明实施例2得到的WC-Co粉末放大2000倍的SEM照片,由图3可以看出,本发明制备得到的WC-Co粉末粒度均匀,球形度高。The invention performs scanning electron microscopy scanning analysis on the obtained WC-Co powder, and the result is shown in FIG.
3 is a SEM photograph of 2000 times magnification of the WC-Co powder obtained in Example 2 of the present invention. As can be seen from FIG. 3, the WC-Co powder prepared by the present invention has uniform particle size and high sphericity.
本发明将得到的WC-Co粉末进行X-射线衍射分析,结果如图4所示,图4为本发明实施例2得到的钴包覆纳米WC的XRD照片,由图4可以看出,本发明制备得到的WC-Co粉末成分混合均匀;WC-Co粉末中未出现W2C、η(Co3W3C、Co6W6C)、金属钨等。The WC-Co powder obtained by the present invention is subjected to X-ray diffraction analysis, and the results are shown in FIG. 4. FIG. 4 is an XRD photograph of the cobalt-coated nano WC obtained in Example 2 of the present invention, as can be seen from FIG. The WC-Co powder component prepared by the invention is uniformly mixed; W2C, η (Co 3 W 3 C, Co 6 W 6 C), metal tungsten or the like does not appear in the WC-Co powder.
本发明将得到的WC-Co粉末进行场发射扫描电镜放大5000倍下元素面分布照片,结果如图5所示,图5为本发明实施例2得到的钴包覆纳米WC-Co粉末放大5000倍下SEM照片及W、Co元素面分布照片,其中(a)为本发明实施例2得到的钴包覆纳米WC-Co粉末放大5000倍下的SEM照片,(b)为本发明实施例2得到的钴包覆纳米WC-Co粉末放大5000倍下W元素面分布照片,(c)为本发明实施例2得到的钴包覆纳米WC-Co粉末放大5000倍下Co元素面分布照片,由图5可以看出,本发明制备得到的WC-Co粉末、W、Co相分布均匀,Co相均匀包覆WC晶粒。The WC-Co powder obtained by the invention is subjected to field emission scanning electron microscopy to enlarge the element surface distribution photograph at 5000 times, and the result is shown in FIG. 5. FIG. 5 is a magnified 5000 of cobalt-coated nano WC-Co powder obtained in Example 2 of the present invention. The SEM photograph and the surface distribution of the W and Co elements are doubled, wherein (a) is a SEM photograph of the cobalt-coated nano-WC-Co powder obtained in Example 2 of the present invention at a magnification of 5000 times, and (b) is Example 2 of the present invention. The obtained cobalt-coated nano-WC-Co powder is magnified 5000 times under the W element surface distribution photograph, (c) is a cobalt-coated nano-WC-Co powder obtained in Example 2 of the present invention, magnified 5000 times under the Co element surface distribution photo, It can be seen from Fig. 5 that the WC-Co powder prepared by the invention has a uniform distribution of W and Co phases, and the Co phase uniformly coats the WC grains.
本发明将得到的WC-Co粉末进行剖面金相分析照片,结果如图6所示,图6为本发明实施例2得到的钴包覆纳米WC-Co粉末放大1000、1500倍下金相剖面照片,其中(a)为本发明实施例2得到的钴包覆纳米WC-Co粉末放大1000倍下金相剖面照片,(b)为本发明实施例2得到的钴包覆纳米WC-Co放大1500倍下金相剖面照片,由图6可以看出,本发明制备得到的WC-Co粉末、WC、Co相分布均匀。The obtained WC-Co powder is subjected to cross-section metallographic analysis photograph, and the result is shown in FIG. 6. FIG. 6 is a metallographic profile of the cobalt-coated nano-WC-Co powder obtained in Example 2 of the present invention at 1000 and 1500 times magnification. Photograph (a) is a photograph of a metallographic cross-section of a cobalt-coated nano-WC-Co powder obtained in Example 2 of the present invention at a magnification of 1000 times, and (b) a magnified cobalt-coated nano-WC-Co obtained in Example 2 of the present invention. The 1500 times lower metallographic cross-section photograph, as can be seen from FIG. 6, the WC-Co powder, WC, and Co phase prepared by the present invention are uniformly distributed.
本发明检测了得到的WC-Co粉末的物理性能和化学组成,结果如表1所示,表1为本发明实施例得到的WC-Co粉末的物理性能和化学成分。The physical properties and chemical compositions of the obtained WC-Co powders were examined. The results are shown in Table 1. Table 1 shows the physical properties and chemical compositions of the WC-Co powders obtained in the examples of the present invention.
实施例3Example 3
1)将粒度为0.5μm~0.6μm的50Kg碳化钨粉、43.5Kg醋酸钴、1.4Kg
蔗糖溶于质量为固体总质量3.0倍的纯水中,配制成钴含量为17wt%的混合料浆;1) 50Kg tungsten carbide powder with a particle size of 0.5μm to 0.6μm, 43.5Kg cobalt acetate, 1.4Kg
The sucrose is dissolved in pure water having a mass of 3.0 times the total mass of the solid, and is formulated into a mixed slurry having a cobalt content of 17% by weight;
2)将步骤1)得到的混合料浆经球磨8小时后,进行喷雾造粒,在喷雾造粒中,进风温度为260℃,出风温度为160℃,离心雾化转速为10000r/min,得到钴盐包覆WC前驱体粉末;2) After the mixture slurry obtained in the step 1) is ball-milled for 8 hours, spray granulation is carried out. In the spray granulation, the inlet air temperature is 260 ° C, the outlet air temperature is 160 ° C, and the centrifugal atomization rotation speed is 10000 r / min. , obtaining a cobalt salt coated WC precursor powder;
3)将步骤2)得到的前驱体粉末在1250℃条件,在H2∶CH4(体积比)=98.5∶1.5的气氛下进行还原碳化30min,得到钴包覆纳米WC-Co粉末。3) The precursor powder obtained in the step 2) was subjected to reduction carbonization in an atmosphere of H 2 : CH 4 (volume ratio) = 98.5 : 1.5 at 1250 ° C for 30 min to obtain a cobalt-coated nano WC-Co powder.
本发明检测了得到的WC-Co粉末的物理性能和化学组成,结果如表1所示,表1为本发明实施例得到的WC-Co粉末的物理性能和化学成分。The physical properties and chemical compositions of the obtained WC-Co powders were examined. The results are shown in Table 1. Table 1 shows the physical properties and chemical compositions of the WC-Co powders obtained in the examples of the present invention.
表1本发明实施例得到的WC-Co粉末的物理性能和化学成分Table 1 Physical properties and chemical composition of WC-Co powder obtained by the examples of the present invention
由表1可以看出,本发明制备得到的WC-Co粉末粒度均匀,成分均匀可控,从而不会造成成分偏析;且本发明制备得到的WC-Co粉末中游离碳含量较高,使得机体材料表面在热喷涂过程中,喷涂粉在高温下不产生脱碳相。It can be seen from Table 1 that the WC-Co powder prepared by the invention has uniform particle size, uniform and controllable composition, and does not cause component segregation; and the WC-Co powder prepared by the invention has high free carbon content, so that the body is made. During the thermal spraying process, the sprayed powder does not produce a decarburized phase at high temperatures.
由以上实施例可知,本发明提供了一种制备热喷涂用WC-Co粉末的方法,包括以下步骤:将碳化钨、水溶性钴盐、碳源和水混合,得到混合料浆;将所述混合料浆球磨混匀后进行喷雾造粒,得到钴盐包覆WC前驱体粉末;将所述钴盐包覆WC前驱体粉末进行还原碳化,得到WC-Co粉末。本发明提供的方法以水溶性钴盐作为钴源,采用液相法制备得到钴盐包覆WC前驱体粉末,使得钴以溶液离子形式包覆
在WC的表面,再将所述钴盐包覆WC前驱体粉末还原碳化,得到WC-Co粉末。本发明采用水溶性钴盐和有机碳代替成型剂,避免脱蜡,且无需对得到的产品进行破碎和筛分,缩短工艺流程。It is apparent from the above examples that the present invention provides a method for preparing a WC-Co powder for thermal spraying, comprising the steps of: mixing tungsten carbide, a water-soluble cobalt salt, a carbon source and water to obtain a mixed slurry; The mixed slurry is ball milled and mixed, and then spray granulated to obtain a cobalt salt coated WC precursor powder; the cobalt salt is coated with the WC precursor powder for reduction carbonization to obtain a WC-Co powder. The method provided by the invention uses a water-soluble cobalt salt as a cobalt source, and prepares a cobalt salt-coated WC precursor powder by a liquid phase method, so that the cobalt is coated in a solution ion form.
On the surface of the WC, the cobalt salt-coated WC precursor powder is reduced and carbonized to obtain a WC-Co powder. The invention adopts water-soluble cobalt salt and organic carbon instead of forming agent to avoid dewaxing, and does not need to crush and sieve the obtained product, thereby shortening the process flow.
而且,本发明提供的方法避免直接添加钴金属使混合不均匀造成的成分偏析。同时本发明制备得到的WC-Co粉末中游离碳含量高,使其在基体材料表面热喷涂过程中,在高温下不产生脱碳相;同时本发明在低温下就可还原碳化成球形WC-Co粉末,可用作热喷涂粉,粒度均匀;能耗低,设备投资小;成分可控,粉末成分均匀、成分中未出现W2C、η-Co3W3C、η-Co6W6C、金属钨等;球形度高及流动性好,喷涂基体表面不发生脱碳相及相的分解。Moreover, the method provided by the present invention avoids the direct addition of cobalt metal to segregate the components caused by the uneven mixing. At the same time, the WC-Co powder prepared by the invention has high free carbon content, so that no decarburization phase is generated at high temperature during thermal spraying on the surface of the base material; and the invention can be reduced to carbonized into spherical WC at low temperature. Co powder, can be used as thermal spray powder, uniform particle size; low energy consumption, low equipment investment; controllable composition, uniform powder composition, no W 2 C, η-Co 3 W 3 C, η-Co 6 W in the composition 6 C, metal tungsten, etc.; high sphericity and good fluidity, no decarburization phase and phase decomposition of the sprayed substrate surface.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above description is only a preferred embodiment of the present invention, and it should be noted that those skilled in the art can also make several improvements and retouchings without departing from the principles of the present invention. It should be considered as the scope of protection of the present invention.
本发明提供了的制备WC-Co粉末的方法以水溶性钴盐作为钴源,采用液相法制备得到钴盐包覆WC前驱体粉末,使得钴以溶液分子级形式均匀包覆在WC的表面,再将所述钴盐包覆WC前驱体粉末还原碳化,得到WC-Co粉末。本发明得到的WC-Co粉末粒度均匀、成分可控,粉末成分均匀、成分中未出现W2C、η-Co3W3C、η-Co6W6C、金属钨等;球形度高及流动性好,喷涂基体表面不发生脱碳相及相的分解。
The method for preparing WC-Co powder provided by the invention uses a water-soluble cobalt salt as a cobalt source, and prepares a cobalt salt-coated WC precursor powder by a liquid phase method, so that cobalt is uniformly coated on the surface of the WC in a solution molecular level form. Then, the cobalt salt coated WC precursor powder is reduced and carbonized to obtain a WC-Co powder. The WC-Co powder obtained by the invention has uniform particle size, controllable composition, uniform powder composition, no W 2 C, η-Co 3 W 3 C, η-Co 6 W 6 C, metal tungsten, etc. in the composition; high sphericity And the fluidity is good, the decarburization phase and the decomposition of the phase do not occur on the surface of the sprayed substrate.
Claims (10)
- 一种制备热喷涂用WC-Co粉末的方法,包括以下步骤:将碳化钨、水溶性钴盐、碳源和水混合,得到混合料浆;将所述混合料浆球磨后进行喷雾造粒,得到钴盐包覆WC前驱体粉末;将所述钴盐包覆WC前驱体粉末进行还原碳化,得到WC-Co粉末。A method for preparing a WC-Co powder for thermal spraying, comprising the steps of: mixing tungsten carbide, a water-soluble cobalt salt, a carbon source and water to obtain a mixed slurry; and grinding the mixed slurry to perform spray granulation, A cobalt salt coated WC precursor powder is obtained; the cobalt salt is coated with a WC precursor powder for reduction carbonization to obtain a WC-Co powder.
- 根据权利要求1所述的方法,其特征在于,所述水溶性钴盐为硝酸钴、醋酸钴、氯化钴和硫酸钴中一种或几种。The method according to claim 1, wherein said water-soluble cobalt salt is one or more of cobalt nitrate, cobalt acetate, cobalt chloride and cobalt sulfate.
- 根据权利要求1所述的方法,其特征在于,所述碳化钨、水溶性钴盐和碳源的质量比为a∶b∶c,50≤a≤70,28≤b≤49,0<c≤2。The method according to claim 1, wherein the mass ratio of said tungsten carbide, water-soluble cobalt salt and carbon source is a:b:c, 50 ≤ a ≤ 70, 28 ≤ b ≤ 49, 0 < c ≤ 2.
- 根据权利要求1所述的方法,其特征在于,所述碳化钨的粒度为0.1μm~8.0μm。The method according to claim 1, wherein the tungsten carbide has a particle size of from 0.1 μm to 8.0 μm.
- 根据权利要求1所述的方法,其特征在于,所述碳源包括炭黑、灯黑、碳纳米管和有机碳中的一种或几种。The method of claim 1 wherein the carbon source comprises one or more of carbon black, lamp black, carbon nanotubes, and organic carbon.
- 根据权利要求1所述的方法,其特征在于,所述混合料浆中钴的质量含量为3wt%~20wt%。The method according to claim 1, wherein the mixed slurry has a mass content of cobalt of from 3 wt% to 20 wt%.
- 根据权利要求1所述的方法,其特征在于,所述还原碳化在还原气体的气氛中进行;所述还原气体包括氢气和甲烷。The method according to claim 1, wherein said reducing carbonization is carried out in an atmosphere of a reducing gas; said reducing gas comprises hydrogen and methane.
- 根据权利要求7所述的方法,其特征在于,所述氢气和甲烷的体积比为(90~99)∶(1~10)。The method according to claim 7, wherein the volume ratio of hydrogen to methane is (90 to 99): (1 to 10).
- 根据权利要求1所述的方法,其特征在于,所述还原碳化的温度为950℃~1350℃。The method of claim 1 wherein said reducing carbonization temperature is from 950 ° C to 1350 ° C.
- 根据权利要求1所述的方法,其特征在于,所述还原碳化的时间为5min~60min。 The method according to claim 1, wherein the reduction carbonization time is from 5 min to 60 min.
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