Summary of the invention
Object of the present invention is exactly electroless plating formula and the technique of a kind of Cobalt-Nickel Alloy Electroplating Films in order to provide.
Another object of the present invention is to provide the adjustable coating of a kind of cobalt-nickel alloy content.
The present invention adopts following technical solution to realize above-mentioned purpose: a kind of electroless cobalt plating nickelalloy plating solution, is characterized in that, plating solution raw materials composition comprises:
Further illustrating as such scheme, described nickel salt is: the one in nickelous chloride, single nickel salt, nickelous nitrate, nickel sulfamic acid or other water soluble nickel salt.
Described cobalt salt is: the one in cobalt chloride, rose vitriol, thionamic acid cobalt or other water soluble cobaltous salt.
Described reductive agent is: the one in formaldehyde, formic acid, formate, Hypophosporous Acid, 50, hypophosphite, hydrazine hydrate, sodium borohydride.
Described complexing agent comprises: one or more in oxysuccinic acid, citric acid, succsinic acid, lactic acid, propionic acid, oxyacetic acid, ammonia, trolamine, glycine, tartrate, EDTA, quadrol, hydroxycarboxylate, aminocarboxylate and organic phosphonate.
Described stablizer is: one or more in lead salts, stearate, Bismuth trinitrate, thiocarbamide, diphenyl thiourea, Sulfothiorine, UPS, potassiumiodide and rare-earth oxide or muriate.
Described pH buffer reagent is: one or more in Sodium phosphate dibasic, SODIUM PHOSPHATE, MONOBASIC, potassium primary phosphate, boric acid, borax, sodium carbonate, Padil.
A kind of electroless cobalt plating nickelalloy technique, it is characterized in that, in plating process, coating bath temperature controls at 60 ~ 95 DEG C, pH value controls 6 ~ 10, can the workpiece of direct catalysis to reductive agent, surface chemical plating cobalt-nickel alloy processing step is: oil removing → microetch → plating, all uses pure water rinsing between every step; This technique is not only applicable to ironware and iron containing substrates, can be used for the material surface such as copper, nickel plating equally.Also can plating to not possessing the metal of catalytic activity or other material, only need carry out the process of plating front activating.
The beneficial effect that the present invention adopts above-mentioned technical solution to reach is:
The present invention can adjust the alloy layer that nickel salt and the ratio of cobalt salt obtain different content of cobalt and nickel according to demand, and the coating using different reductive agent to obtain composition also has difference.
Embodiment
Below in conjunction with specific embodiment, present invention process is described in detail.
A kind of electroless cobalt plating nickelalloy of the present invention plating solution, plating solution raw materials composition comprises:
Plating solution forms described nickel salt, cobalt salt is water-soluble salt.Described nickel salt is the one in nickelous chloride, single nickel salt, nickelous nitrate, nickel sulfamic acid or other water soluble nickel salt.Described cobalt salt is the one in cobalt chloride, rose vitriol, thionamic acid cobalt or other water soluble cobaltous salt.
In plating solution, the ratio of nickel ion and cobalt ion is the most important factor determining that coating forms, the content direct proportionality of nickel ion, cobalt ion in the content of nickel, cobalt and plating solution in coating.Adjustment nickel salt, cobalt salt ratio in the plating solution, can change the proportion of composing of cobalt nickel element in alloy, obtain the alloy layer of different cobalt contents, cobalt contents is adjustable within the scope of 1wt% ~ 100wt%.As in embodiment 1 ~ 3, the consumption of cobalt salt raises gradually, and nickel salt usage ratio reduces, and in gained coating, the ratio of cobalt element improves gradually.Nickel salt consumption is at 0.1 ~ 40g/L, and cobalt salt consumption is at 0.1 ~ 40g/L.
Described reductive agent is the one in formaldehyde, formic acid, formate, Hypophosporous Acid, 50, hypophosphite, hydrazine hydrate, sodium borohydride.The selection of reductive agent can affect coating composition to a certain extent.As selected sodium hypophosphite as reductive agent in following embodiment 1 ~ 3, then what obtain is Co-Ni-P coating.Reductive agent used in amounts will strictly control, and it is slow that reaction at least crossed by reductive agent, and the process time is longer; The excessive then plating solution of reductive agent is unstable.The consumption of reductive agent controls at 5 ~ 30g/L.
Complexing agent and metallic ion coordination complexing, ensure nickel and cobalt ions stable existence in the plating solution, so the choosing of complexing agent then needs to comprise nickel ion complexing agent and cobalt ion complexing agent.Described complexing agent comprise in oxysuccinic acid, citric acid, succsinic acid, lactic acid, propionic acid, oxyacetic acid, ammonia, trolamine, glycine, tartrate, EDTA, quadrol, hydroxycarboxylate, aminocarboxylate and organic phosphonate one or more.Amount of complex is at 10 ~ 60g/L
Described stablizer is one or more in lead salts, stearate, Bismuth trinitrate, thiocarbamide, diphenyl thiourea, Sulfothiorine, UPS, potassiumiodide and rare-earth oxide or muriate.The consumption of stablizer is at 1 ~ 50mg/L.Stabilizing agent dosage is too much unsuitable, and excessive stablizer can have a strong impact on plating solution activity, causes the problem of stopping plating, not plating.Add in addition metal or rare earth class stablizer in plating process may doped with rare-earth elements in coating, change is to a certain extent risen to coating performance.
Described pH buffer reagent is one or more in Sodium phosphate dibasic, SODIUM PHOSPHATE, MONOBASIC, potassium primary phosphate, boric acid, borax, sodium carbonate, Padil.Concrete chooses according to required pH buffering range, between pH 6 ~ 8, selects potassium primary phosphate proper, if between pH 8 ~ 10, selects boric acid, Padil etc. comparatively suitable.Buffer reagent consumption is at 5 ~ 30g/L.
Plating technology: coating bath temperature controls at 60 ~ 95 DEG C, and pH value controls 6 ~ 10, ironware or steel part etc. can the workpiece of direct catalysis to reductive agent, and surface chemical plating cobalt-nickel alloy processing step is: oil removing → microetch → plating, all uses pure water rinsing between every step; This technique is not only applicable to ironware and iron containing substrates, can be used for the material surface such as copper, nickel plating equally.The process of plating front activating need be carried out to the metal or other material that do not possess catalytic activity.
Embodiment 1
Plating solution forms:
Condition controls:
Temperature 80 DEG C, pH 8.5, alr mode: pneumatic blending.
EDS test is carried out to sample, the nickeliferous 70wt% of prepared coating, containing cobalt 23%, phosphorous 7%.
Embodiment 2
Plating solution forms:
Condition controls:
Temperature 85 DEG C, pH 9.0, alr mode: pneumatic blending;
EDS test is carried out to sample, the nickeliferous 48wt% of coating, containing cobalt 46%, phosphorous 6%.
Embodiment 3
Plating solution forms:
Condition controls:
Temperature 90 DEG C, pH 8.5, alr mode: pneumatic blending;
EDS test is carried out to sample, prepares the nickeliferous 5wt% of coating, containing cobalt 91%, phosphorous 4%.
Above-described is only the preferred embodiment of the present invention, it should be pointed out that for the person of ordinary skill of the art, and without departing from the concept of the premise of the invention, can also make some distortion and improvement, these all belong to protection scope of the present invention.