CN115125525A - Low-cost hexagonal boron nitride surface chemical nickel plating pre-palladium-free activation method - Google Patents
Low-cost hexagonal boron nitride surface chemical nickel plating pre-palladium-free activation method Download PDFInfo
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- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 title claims abstract description 106
- 229910052759 nickel Inorganic materials 0.000 title claims abstract description 46
- 230000004913 activation Effects 0.000 title claims abstract description 36
- 238000007747 plating Methods 0.000 title claims abstract description 35
- 229910052582 BN Inorganic materials 0.000 title claims abstract description 27
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 238000000034 method Methods 0.000 title claims abstract description 24
- 239000000126 substance Substances 0.000 title claims abstract description 6
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000005530 etching Methods 0.000 claims abstract description 21
- 229910001961 silver nitrate Inorganic materials 0.000 claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims abstract description 10
- 239000001509 sodium citrate Substances 0.000 claims abstract description 7
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 claims abstract description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000002270 dispersing agent Substances 0.000 claims abstract description 3
- 239000000243 solution Substances 0.000 claims description 31
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 238000003756 stirring Methods 0.000 claims description 12
- 239000008367 deionised water Substances 0.000 claims description 11
- 229910021641 deionized water Inorganic materials 0.000 claims description 11
- 229910052763 palladium Inorganic materials 0.000 claims description 9
- 239000003513 alkali Substances 0.000 claims description 7
- IGFHQQFPSIBGKE-UHFFFAOYSA-N Nonylphenol Natural products CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 claims description 6
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical compound CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 claims description 6
- 229940051841 polyoxyethylene ether Drugs 0.000 claims description 6
- 229920000056 polyoxyethylene ether Polymers 0.000 claims description 6
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 5
- 229910017604 nitric acid Inorganic materials 0.000 claims description 5
- 230000007935 neutral effect Effects 0.000 claims description 4
- 230000008569 process Effects 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 2
- 230000003213 activating effect Effects 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 239000012456 homogeneous solution Substances 0.000 claims description 2
- 239000011259 mixed solution Substances 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 2
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 238000001994 activation Methods 0.000 abstract description 26
- 239000000314 lubricant Substances 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 8
- 239000007787 solid Substances 0.000 abstract description 7
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 abstract description 6
- 238000000576 coating method Methods 0.000 abstract description 4
- 238000010327 methods by industry Methods 0.000 abstract description 3
- 239000011248 coating agent Substances 0.000 abstract description 2
- 239000012535 impurity Substances 0.000 abstract description 2
- 238000010924 continuous production Methods 0.000 abstract 1
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 21
- 239000002131 composite material Substances 0.000 description 16
- 239000002245 particle Substances 0.000 description 15
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 5
- 150000002815 nickel Chemical class 0.000 description 5
- 229910052709 silver Inorganic materials 0.000 description 5
- 239000004332 silver Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 238000007772 electroless plating Methods 0.000 description 4
- 239000011159 matrix material Substances 0.000 description 4
- 230000007547 defect Effects 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- -1 silver ions Chemical class 0.000 description 3
- 238000001228 spectrum Methods 0.000 description 3
- NWZSZGALRFJKBT-KNIFDHDWSA-N (2s)-2,6-diaminohexanoic acid;(2s)-2-hydroxybutanedioic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O.NCCCC[C@H](N)C(O)=O NWZSZGALRFJKBT-KNIFDHDWSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 238000010306 acid treatment Methods 0.000 description 2
- 230000006399 behavior Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000012512 characterization method Methods 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- IKDUDTNKRLTJSI-UHFFFAOYSA-N hydrazine monohydrate Substances O.NN IKDUDTNKRLTJSI-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 150000003378 silver Chemical class 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- 238000005411 Van der Waals force Methods 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 238000000026 X-ray photoelectron spectrum Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- QDWJUBJKEHXSMT-UHFFFAOYSA-N boranylidynenickel Chemical compound [Ni]#B QDWJUBJKEHXSMT-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000011258 core-shell material Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000005555 metalworking Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002135 nanosheet Substances 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 description 1
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical class [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 230000000153 supplemental effect Effects 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
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- 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
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/18—Pretreatment of the material to be coated
- C23C18/1851—Pretreatment of the material to be coated of surfaces of non-metallic or semiconducting in organic material
- C23C18/1872—Pretreatment of the material to be coated of surfaces of non-metallic or semiconducting in organic material by chemical pretreatment
- C23C18/1886—Multistep pretreatment
- C23C18/1893—Multistep pretreatment with use of organic or inorganic compounds other than metals, first
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- 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
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/31—Coating with metals
- C23C18/32—Coating with nickel, cobalt or mixtures thereof with phosphorus or boron
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Abstract
本发明公开了一种低成本六方氮化硼表面化学镀镍前无钯活化方法,对六方氮化硼进行表面酸碱蚀刻处理,再通过热处理清除表面残留杂质。将热处理后的六方氮化硼置于分散剂溶液中,使其均匀分散。按比例加入硝酸银和柠檬酸钠,在超声振荡中活化处理,然后用无水乙醇清洗并过滤。本发明是一种低成本的活化方法,成本大约为氯化钯活化的1/20,并且其工艺工程简单,活化效果好,能实现后续镍层的均匀包覆;活化产生的纳米银层也是优异的固体润滑剂;活化过程使用常规药品,可以适用于大批量连续生产。The invention discloses a low-cost palladium-free activation method before electroless nickel plating on the surface of hexagonal boron nitride. The hexagonal boron nitride is subjected to acid-base etching treatment on the surface, and then the residual impurities on the surface are removed by heat treatment. The heat-treated hexagonal boron nitride is placed in the dispersant solution to make it uniformly dispersed. Silver nitrate and sodium citrate were added in proportion, activated in ultrasonic vibration, then washed with absolute ethanol and filtered. The invention is a low-cost activation method, the cost is about 1/20 of that of palladium chloride activation, the process engineering is simple, the activation effect is good, and the uniform coating of the subsequent nickel layer can be realized; the nano-silver layer produced by the activation is also Excellent solid lubricant; the activation process uses conventional chemicals, which can be suitable for continuous production in large quantities.
Description
技术领域technical field
本发明涉及一种表面处理方法,特别是涉及一种六方氮化硼表面化学镀镍前的活化方法。The invention relates to a surface treatment method, in particular to an activation method before electroless nickel plating on the surface of hexagonal boron nitride.
背景技术Background technique
随着科技的发展和进步,材料的性能已经不是唯一的追求,也同时对能源的节省有了要求。摩擦磨损造成的损耗是使用设备工具时不可避免的,这直接决定了设备工具的使用寿命,而且造成了很大的能源损失。研究金属基自润滑复合材料是解决这一难题的重要手段。这类复合材料不仅具有金属基体的机械性能,又有固体润滑剂的摩擦学性能。然而,固体润滑剂作为添加剂,很难与金属基体结合。因此,对固体润滑剂进行表面改性是一种有潜力的途径。With the development and progress of science and technology, the performance of materials is not the only pursuit, but also requires energy saving. The loss caused by friction and wear is inevitable when using equipment tools, which directly determines the service life of equipment tools and causes great energy loss. The study of metal matrix self-lubricating composites is an important means to solve this problem. This kind of composite material not only has the mechanical properties of metal matrix, but also has the tribological properties of solid lubricant. However, as an additive, solid lubricant is difficult to combine with metal matrix. Therefore, surface modification of solid lubricants is a potential approach.
与无涂层固体润滑剂粉末相比,微结构改性的复合粉末材料表现出更好的机械和抗磨损性能。有很多方法可以合成带有金属外壳的核壳复合粉末。其中,化学镀被认为是最方便和有效的技术之一。化学镀是在无外加电流的条件下,在镀液中利用还原剂将金属离子还原成金属单质并沉积在具有催化活性的表面上的一种镀覆方法。Compared with uncoated solid lubricant powders, the microstructure-modified composite powder materials exhibited better mechanical and antiwear properties. There are many ways to synthesize core-shell composite powders with metal shells. Among them, electroless plating is considered to be one of the most convenient and effective techniques. Electroless plating is a plating method in which metal ions are reduced into metal elements and deposited on the surface with catalytic activity by using reducing agents in the plating solution under the condition of no applied current.
常用固体润滑剂中的六方氮化硼(h-BN)为白色晶体粉末,俗称白石墨。它属于六方晶系、层状结构,层与层之间为较小的分子间范德华力作用,因此剪切强度较低,在摩擦力作用下很容易在接触面形成润滑转移膜,降低摩擦副的摩擦系数、减少磨损。近年来,h-BN被广泛用于模具制造、航空和航天涡轮发动机等领域。相关研究报告显示,由于h-BN与金属/陶瓷基体的润湿性差,以及其热氧化性能不足,因此在摩擦学中开发表面定制的复合涂层方面,h-BN的研究相对最少。此外,h-BN涂层已被证明在高温金属加工润滑方面的应用较差。研究表明,在活性金属(如镍)的基体层中加入h-BN润滑剂颗粒,可以改善h-BN的润湿性能。基于这一观点,通过化学镀镍来改善h-BN的物理和化学行为,以扩大其性能窗口,从而开发出高效的复合涂层系统。Hexagonal boron nitride (h-BN) in common solid lubricants is a white crystalline powder, commonly known as white graphite. It belongs to the hexagonal crystal system and has a layered structure. There is a small intermolecular van der Waals force between the layers, so the shear strength is low. It is easy to form a lubricant transfer film on the contact surface under the action of friction, reducing the friction pair. friction coefficient and reduce wear. In recent years, h-BN has been widely used in mold making, aviation and aerospace turbine engines and other fields. Related research reports show that h-BN has been relatively least studied in developing surface-tailored composite coatings in tribology due to its poor wettability with metal/ceramic substrates and its insufficient thermal oxidation properties. In addition, h-BN coatings have been shown to be poor applications for high temperature metalworking lubrication. Studies have shown that the wetting properties of h-BN can be improved by adding h-BN lubricant particles to the matrix layer of active metals such as nickel. Based on this viewpoint, the physical and chemical behaviors of h-BN were improved by electroless nickel plating to expand its performance window, leading to the development of an efficient composite coating system.
由于h-BN化学性质稳定,且其表面没有缺陷和官能团,因此难以在其表面形成可供化学镀镍的结晶核。然而在传统的化学镀镍的预处理中,钯的价格昂贵,且操作复杂,需要用到具有强腐蚀性的盐酸。虽然其活化效果较好,但在大规模的生产中,消耗比较大,占化学镀总成本的20~40 %,造成的化学镀的成本过高。Because h-BN is chemically stable and has no defects and functional groups on its surface, it is difficult to form crystalline nuclei for electroless nickel plating on its surface. However, in the pretreatment of traditional electroless nickel plating, palladium is expensive and complicated to operate, and highly corrosive hydrochloric acid needs to be used. Although its activation effect is good, in large-scale production, the consumption is relatively large, accounting for 20~40% of the total cost of electroless plating, resulting in high cost of electroless plating.
发明内容SUMMARY OF THE INVENTION
发明目的:针对现有技术中的不足,本发明的目的是提供一种低成本六方氮化硼表面化学镀镍前无钯活化方法,工艺工程简单,纳米银负载均匀,活化效果好,能实现后续镍层的均匀沉积。Purpose of the invention: In view of the deficiencies in the prior art, the purpose of the present invention is to provide a low-cost hexagonal boron nitride surface electroless nickel-plating method without palladium activation, the process engineering is simple, the nano-silver loading is uniform, the activation effect is good, and the Uniform deposition of subsequent nickel layers.
本发明的技术方案如下文所示。The technical solution of the present invention is shown below.
一种低成本六方氮化硼表面化学镀镍前无钯活化方法,其特征在于包括以下步骤:A method for palladium-free activation before electroless nickel plating on the surface of low-cost hexagonal boron nitride, which is characterized by comprising the following steps:
(1)将六方氮化硼放入KOH和NaOH混合溶液中,持续超声搅拌,一次蚀刻处理,一次蚀刻完成后,用去离子水冲洗至中性;(1) Put the hexagonal boron nitride into the mixed solution of KOH and NaOH, continue to ultrasonically stir, perform one etching treatment, and rinse with deionized water until neutral after one etching is completed;
(2)将一次蚀刻的六方氮化硼移至稀硝酸溶液中,中和残留酸碱,并进行二次蚀刻,二次蚀刻完成后,用去离子水冲洗至中性并过滤,再以特定的工艺参数进行热处理;(2) Move the hexagonal boron nitride etched once to the dilute nitric acid solution, neutralize the residual acid and alkali, and perform secondary etching. After the secondary etching is completed, rinse it with deionized water to neutrality and filter, and then use a specific Process parameters for heat treatment;
(3)以壬基酚聚氧乙烯醚(N=40)作为分散剂,并将其加入去离子水中持续搅拌形成均匀溶液,将热处理后的六方氮化硼加入此溶液中,持续超声搅拌使六方氮化硼均匀分散;(3) Using nonylphenol polyoxyethylene ether (N=40) as a dispersant, adding it into deionized water and stirring continuously to form a uniform solution, adding the heat-treated hexagonal boron nitride into the solution, and continuously ultrasonically stirring it to make a uniform solution. Hexagonal boron nitride is uniformly dispersed;
(4)按特定比例加入硝酸银和柠檬酸钠至步骤(3)所述的均匀溶液中,对六方氮化硼进行活化处理,处理结束后用无水乙醇清洗并过滤。(4) adding silver nitrate and sodium citrate to the homogeneous solution described in step (3) in a specific proportion, activating the hexagonal boron nitride, washing with absolute ethanol and filtering after finishing the treatment.
步骤(1)中,h-BN的质量为1~10 g,KOH溶液的浓度为5~20 mol/L,NaOH溶液的浓度为5~20 mol/L,溶液体积为100 mL,蚀刻处理的时间为1~10 h,蚀刻温度为50~100 ℃。蚀刻的主要目的是清洗表面污渍,以及产生的孔隙和缺陷能作为后续活化和镀镍的结晶区域。合适的h-BN体积占比,决定了蚀刻效果的好坏,h-BN的添加量过多会容易成团。由于h-BN化学性质稳定,需要足够浓度的碱溶液才能够成功蚀刻。In step (1), the mass of h-BN is 1-10 g, the concentration of KOH solution is 5-20 mol/L, the concentration of NaOH solution is 5-20 mol/L, the solution volume is 100 mL, and the etching treatment The time is 1~10 h, and the etching temperature is 50~100 °C. The main purpose of etching is to remove surface contamination, and the resulting pores and defects can serve as crystalline regions for subsequent activation and nickel plating. The appropriate volume ratio of h-BN determines the quality of the etching effect. Too much h-BN will easily form agglomerates. Due to the chemical stability of h-BN, a sufficient concentration of alkaline solution is required for successful etching.
步骤(2)中,稀硝酸浓度为0.1~1.5 mol/L,溶液体积与步骤(1)中的碱处理液体积保持一致,蚀刻时间为5~40 min,热处理温度为500~900 ℃,热处理时间为1~10 h,管式炉中抽真空至压强低于5 Pa。酸处理的主要目的是清除残留的碱,以及作为碱处理的额外补充蚀刻。热处理的主要目的是蒸发残留液体和分解残留杂质。In step (2), the concentration of dilute nitric acid is 0.1~1.5 mol/L, the volume of the solution is consistent with the volume of the alkali treatment solution in step (1), the etching time is 5~40 min, the heat treatment temperature is 500~900 ° C, and the heat treatment The time is 1-10 h, and the tube furnace is evacuated until the pressure is lower than 5 Pa. The main purpose of the acid treatment is to remove residual alkali, and as an additional supplemental etch to the alkali treatment. The main purpose of heat treatment is to evaporate residual liquid and decompose residual impurities.
步骤(3)中,壬基酚聚氧乙烯醚(N=40)的浓度为100~500 ppm,溶液体积为100 mL,搅拌时间为10~50 min。添加壬基酚聚氧乙烯醚(N=40)的主要目的是使h-BN均匀分散,减少团聚。也能降低其表面能,防止其与水之间形成薄膜,漂浮在水面。In step (3), the concentration of nonylphenol polyoxyethylene ether (N=40) is 100-500 ppm, the solution volume is 100 mL, and the stirring time is 10-50 min. The main purpose of adding nonylphenol polyoxyethylene ether (N=40) is to uniformly disperse h-BN and reduce agglomeration. It can also reduce its surface energy, preventing it from forming a film with water and floating on the water surface.
步骤(4)中,硝酸银的浓度为0.1~10 g/L。柠檬酸钠的浓度是硝酸银的浓度的10~20倍,活化处理的温度为20~60 ℃,活化处理时间为20~100 min。当硝酸银的浓度小于0.1g/L时,活化效果不足,难以在h-BN表面镀镍。当硝酸银的浓度大于10 g/L时,活化效果过强,且粉末中出现较大尺寸的银团簇,会导致镍镀到银团簇上,甚至镍团过大,导致脱落。In step (4), the concentration of silver nitrate is 0.1~10 g/L. The concentration of sodium citrate is 10-20 times that of silver nitrate, the activation temperature is 20-60 ℃, and the activation time is 20-100 min. When the concentration of silver nitrate is less than 0.1 g/L, the activation effect is insufficient, and it is difficult to plate nickel on the surface of h-BN. When the concentration of silver nitrate is greater than 10 g/L, the activation effect is too strong, and large-sized silver clusters appear in the powder, which will lead to nickel plating on the silver clusters, or even the nickel clusters are too large, resulting in shedding.
进一步地,经上述活化处理后的h-BN基体,进行后续的化学镀镍处理。Further, the h-BN substrate after the above activation treatment is subjected to subsequent electroless nickel plating treatment.
有益效果:Beneficial effects:
(1)本发明的活化无需使用昂贵的钯,而且活化效果好,成本更低;(1) the activation of the present invention does not need to use expensive palladium, and the activation effect is good, and the cost is lower;
(2)本发明工艺工程简单,稳定性好,不需要使用对环境和人体有极大危害的氟化物;(2) the process engineering of the present invention is simple, the stability is good, and does not need to use the fluoride that has great harm to the environment and human body;
(3)本发明提供的方法中,活化中产生的纳米银作为活性位点,能够为后续镀镍提供结晶核。而且银作为固体润滑剂的一种,也能为摩擦学行为提供有益影响;(3) In the method provided by the present invention, the nano-silver generated in the activation is used as an active site, which can provide a crystal nucleus for subsequent nickel plating. Moreover, silver, as a solid lubricant, can also provide beneficial effects on tribological behavior;
(4)本发明提供的方法中,纳米银只会在h-BN表面产生,溶液中的银离子并未发生全面的还原反应,从而使大部分银离子得以保存,溶液可重复使用,降低成本。(4) In the method provided by the present invention, nano-silver can only be produced on the surface of h-BN, and the silver ions in the solution do not undergo a comprehensive reduction reaction, so that most of the silver ions are preserved, the solution can be reused, and the cost is reduced .
附图说明Description of drawings
图1是镀镍后h-BN复合粉末表面微观形貌SEM图片。Figure 1 is an SEM image of the surface microstructure of the h-BN composite powder after nickel plating.
图2是镀镍后h-BN复合粉末XRD图谱。Figure 2 is the XRD pattern of the h-BN composite powder after nickel plating.
图3是镀镍后h-BN复合粉末全范围XPS图谱。Figure 3 is the full range XPS spectrum of h-BN composite powder after nickel plating.
图4是镀镍后h-BN复合粉末的Ni 2p XPS窄谱。Figure 4 is the Ni 2p XPS narrow spectrum of h-BN composite powder after nickel plating.
具体实施方式Detailed ways
下面结合实施例对本发明进一步地详细描述。The present invention will be further described in detail below with reference to the embodiments.
实施例1:Example 1:
本实施例的一种低成本六方氮化硼表面化学镀镍前无钯活化方法包括如下步骤。A low-cost palladium-free activation method before electroless nickel plating on the surface of hexagonal boron nitride in this embodiment includes the following steps.
(1)蚀刻处理(1) Etching treatment
将30 g KOH和25 g NaOH加入烧杯中,并加入去离子水至100 mL。随后加入2.5 gh-BN至该溶液中,在75 ℃下持续超声搅拌2 h。完成蚀刻处理后,用去离子水洗至中性。Add 30 g KOH and 25 g NaOH to a beaker and add deionized water to 100 mL. Then 2.5 gh-BN was added to the solution, and ultrasonic stirring was continued at 75 °C for 2 h. After the etching process is completed, rinse with deionized water until neutral.
(2)酸处理和热处理(2) Acid treatment and heat treatment
配置100 mL 0.3 mol/L的稀硝酸溶液,将碱处理后的h-BN放入其中,蚀刻20 min后,用去离子水洗至中性并过滤。随后在700 ℃下热处理1 h。100 mL of 0.3 mol/L dilute nitric acid solution was prepared, and the alkali-treated h-BN was placed in it. After etching for 20 min, it was washed with deionized water until neutral and filtered. It was then heat-treated at 700 °C for 1 h.
(3)活化处理(3) Activation treatment
取0.03 g壬基酚聚氧乙烯醚(N=40)均匀溶于100 mL去离子水中。将处理过的h-BN粉末加入其中,超声搅拌20 min后,加入0.1 g硝酸银和1.3 g柠檬酸钠。在30 ℃超声振荡30 min后进行抽滤,然后用无水乙醇进行3次清洗,最后在40 ℃的真空炉中干燥10 h。Take 0.03 g of nonylphenol polyoxyethylene ether (N=40) and dissolve it in 100 mL of deionized water. The treated h-BN powder was added to it, and after ultrasonic stirring for 20 min, 0.1 g silver nitrate and 1.3 g sodium citrate were added. After ultrasonic vibration at 30 °C for 30 min, suction filtration was performed, then washed with absolute ethanol for 3 times, and finally dried in a vacuum oven at 40 °C for 10 h.
(4)化学镀镍(4) Electroless nickel plating
将活化后的h-BN粉末加入到化学镀镍液中,边搅拌边滴加25 mL水合肼。然后放入75 ℃的水浴锅中,持续搅拌,控制pH值在12附近。持续加热,直到不冒气泡。用去离子水将粉末清洗至中性,然后用无水乙醇冲洗两次。最后在60 ℃的真空炉中干燥10小时。其中镀液的配方如下:硫酸镍:30 g/L,水合肼:50 mL/L,柠檬酸钠:30 g/L,pvp:0.05 g/L。The activated h-BN powder was added to the electroless nickel plating solution, and 25 mL of hydrazine hydrate was added dropwise while stirring. Then put it into a water bath at 75 °C, keep stirring, and control the pH value around 12. Continue heating until no bubbles appear. The powder was washed to neutrality with deionized water, then rinsed twice with absolute ethanol. Finally, it was dried in a vacuum oven at 60 °C for 10 hours. The formula of the plating solution is as follows: nickel sulfate: 30 g/L, hydrazine hydrate: 50 mL/L, sodium citrate: 30 g/L, pvp: 0.05 g/L.
对镀镍后的h-BN复合粉末进行微观结构表征。用SEM对镀镍后的h-BN复合粉末进行表面形貌观察,结果如图1所示。半透明的片状颗粒为h-BN颗粒,而球状的小颗粒则是Ni颗粒。大部分粉体表面都被Ni包覆,只有较少的1-2 μm无镍层h-BN颗粒。由于h-BN原料的粒径小于3 μm,其中存在大量的纳米片状h-BN颗粒。因此可以观察到镀镍层由纳米镍球和纳米片状h-BN颗粒共同沉积,而且粒径大约为3 μm的Ni包覆h-BN粉体的表面镍层较为均匀。The microstructure characterization of the h-BN composite powder after nickel plating. The surface morphology of the h-BN composite powder after nickel plating was observed by SEM, and the results are shown in Figure 1. The translucent flake particles are h-BN particles, and the spherical small particles are Ni particles. Most of the powder surface is coated with Ni, and there are only a few 1-2 μm nickel-free h-BN particles. Since the particle size of the h-BN raw material is less than 3 μm, there are a large number of nano-flaky h-BN particles in it. Therefore, it can be observed that the nickel-plated layer is co-deposited by nano-nickel balls and nano-flaky h-BN particles, and the surface nickel layer of the Ni-coated h-BN powder with a particle size of about 3 μm is relatively uniform.
用XRD对镀镍后的h-BN复合粉末进行组分分析,结果如图2所示。Ni的衍射峰明显比h-BN的强,说明复合粉末的表面大部分都是Ni颗粒。可以看到曲线上存在宽矮的金属银的衍射峰,说明有微量的Ag颗粒作为活性位点,形成了不均匀的层。活性位点越多,越能够促进化学镀镍反应,形成更均匀,更厚的镍层。The composition analysis of the h-BN composite powder after nickel plating was carried out by XRD, and the results are shown in Figure 2. The diffraction peaks of Ni are obviously stronger than those of h-BN, indicating that most of the surfaces of the composite powders are Ni particles. It can be seen that there are broad and short diffraction peaks of metallic silver on the curve, indicating that there are a small amount of Ag particles as active sites, forming an uneven layer. The more active sites, the more it can promote the electroless nickel plating reaction and form a more uniform and thicker nickel layer.
通过XPS表征探测了镀镍后的h-BN复合粉末的表面元素组成和化学态。从全范围谱图可以观察到,在190.6和398.2 eV分别对应h-BN中的B 1s和N 1s峰(图3)。而C 1s和O1s峰是由于引入了污染源和部分氧化。在368.2 eV处的峰对应于Ag 3d,说明Ag颗粒作为镀镍的催化剂吸附在粉末上。对应于Ni 3p、Ni 3s、Ni 2p3/2、Ni 2p1/2的特征峰分别位于67.5、112.5、855.8、873.2 eV。在高分辨率Ni 2p谱图中(图4),由于部分氧化,在855.8、861.2、879.4 eV处,产生了镍的氧化物的特征峰。而在873.2和852.4 eV处,则分别对应于镍单质和镍硼化合物。说明镍成功镀在h-BN表面。The surface element composition and chemical state of the nickel-plated h-BN composite powders were probed by XPS characterization. From the full-range spectra, it can be observed that the peaks at 190.6 and 398.2 eV correspond to the
实施例2:Example 2:
本实施例的基本步骤与实施例1基本相同,不同之处在于,硝酸银的溶液浓度降低为0.5 g/L。通过SEM观察分析表明,有较多的h-BN表面没有成功镀上镍,而且大尺寸颗粒表面的h-BN纳米片的掺杂量变得更大。说明活化程度不够,形成的镍层存在很多缺陷。The basic steps of this example are basically the same as those of Example 1, except that the solution concentration of silver nitrate is reduced to 0.5 g/L. The SEM observation analysis showed that more h-BN surfaces were not successfully plated with nickel, and the doping amount of h-BN nanosheets on the surface of large-sized particles became larger. It shows that the activation degree is not enough, and the formed nickel layer has many defects.
实施例3:Example 3:
本实施例的基本步骤与实施例1基本相同,不同之处在于,硝酸银的溶液浓度增加为5 g/L。通过SEM观察分析表明,有较多的h-BN表面没有成功镀上镍,而且周围增加了较多的几乎全部由纳米镍组成的镍团。但是3-5 μm的大尺寸h-BN表面镀上了均匀、较厚的镍层。产生这种现象的原因很可能是活化过度,镍团在h-BN表面的生长速度过快,然而h-BN与Ni的机械结合力不足,导致镍团从h-BN表面脱落。The basic steps of this example are basically the same as those of Example 1, except that the concentration of the solution of silver nitrate is increased to 5 g/L. SEM observation and analysis show that there are many h-BN surfaces that are not successfully plated with nickel, and more nickel clusters almost entirely composed of nano-nickel are added around. However, the large size h-BN of 3-5 μm is plated with a uniform and thick nickel layer. The reason for this phenomenon is probably due to excessive activation, and the growth rate of nickel clusters on the surface of h-BN is too fast.
对比例1:Comparative Example 1:
本对比例的基本步骤与实施例1基本相同,不同之处在于,硝酸银的溶液浓度降低为0.1 g/L。通过SEM观察分析表明,大量的h-BN表面没有成功镀上镍,而且很难找到大颗粒的h-BN表面有完整的镍层,说明银离子的浓度太低,导致活化效果太差,没有形成大量的活性位点。The basic steps of this comparative example are basically the same as those of Example 1, except that the solution concentration of silver nitrate is reduced to 0.1 g/L. SEM observation and analysis showed that a large number of h-BN surfaces were not successfully plated with nickel, and it was difficult to find a complete nickel layer on the surface of h-BN with large particles, indicating that the concentration of silver ions was too low, resulting in poor activation effect. forming a large number of active sites.
对比例2:Comparative Example 2:
本对比例的基本步骤与实施例1基本相同,不同之处在于,硝酸银的溶液浓度增加为10 g/L。通过SEM观察分析表明,有大量的h-BN表面没有成功镀上镍,同时复合粉末中存在大量的几乎全部由纳米镍组成的镍团。产生这种现象的原因很可能是活化过度,镍团在h-BN表面的生长速度过快,然而h-BN与Ni的机械结合力不足,导致镍团从h-BN表面脱落。The basic steps of this comparative example are basically the same as those of Example 1, except that the concentration of the solution of silver nitrate is increased to 10 g/L. SEM observation and analysis showed that a large number of h-BN surfaces were not successfully plated with nickel, and there were a large number of nickel clusters almost entirely composed of nano-nickel in the composite powder. The reason for this phenomenon is probably due to excessive activation, and the growth rate of nickel clusters on the surface of h-BN is too fast.
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