CN101503811A - Method for electroplating shaft bushing antifriction layer by metilsulfate plating bath - Google Patents

Method for electroplating shaft bushing antifriction layer by metilsulfate plating bath Download PDF

Info

Publication number
CN101503811A
CN101503811A CNA2009100370652A CN200910037065A CN101503811A CN 101503811 A CN101503811 A CN 101503811A CN A2009100370652 A CNA2009100370652 A CN A2009100370652A CN 200910037065 A CN200910037065 A CN 200910037065A CN 101503811 A CN101503811 A CN 101503811A
Authority
CN
China
Prior art keywords
bush
coating
bearing shell
metilsulfate
plating bath
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CNA2009100370652A
Other languages
Chinese (zh)
Other versions
CN101503811B (en
Inventor
曾育才
唐春保
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiaying University
Original Assignee
Jiaying University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jiaying University filed Critical Jiaying University
Priority to CN2009100370652A priority Critical patent/CN101503811B/en
Publication of CN101503811A publication Critical patent/CN101503811A/en
Application granted granted Critical
Publication of CN101503811B publication Critical patent/CN101503811B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention relates to a method for plating a bush antifriction coating through a methyl sulfonate bath. The method comprises the following steps: (1) cleaning a bush after ultrasonic degreasing, and cleaning a bush upper ring after cathode electroplating degreasing; (2) cleaning the bush after dilute hydrochloric acid activation for 1 to 2 minutes, placing the bush into the methyl sulfonate bath, taking a terne metal containing 10 percent of tin as an anode at a room temperature, carrying out the electroplating for 18 to 22 minutes when the cathode current density is 2 to 3 A/dm<2>, and then cleaning the bush and obtaining a terne copper coating on the inner surface of the bush; and (3) placing the bush into a tinning bath, taking a steel plate as an anode at 75 to 80 DEG C, carrying out the electroplating for 3 to 8 minutes when the cathode current density is 1 to 1.5 A/dm<2>, and obtaining a tin coating on the inner surface of the bush. The methyl sulfonate bath has stable performance and a simple process; the coating has fine crystallization, good hardness and good abrasion resistance; the bush coating has even thickness; as no strong complexing agent and F<-> are contained, wastewater is easily processed; and the method is suitable for plating the bush antifriction coating on large and medium-size diesel engines and combustion engines.

Description

The method of electroplating shaft bushing antifriction layer by metilsulfate plating bath
Technical field
The present invention relates to a kind of big-and-middle-sized diesel engine, internal combustion engine bearing ware reducing coating layer electroplating technology, specifically be meant a kind of method that adopts environment-friendly type metilsulfate plating bath electroplating shaft bushing antifriction coating.
Background technology
The Pb-Sn-Cu ternary alloy coating is widely used in big-and-middle-sized diesel engine, internal combustion engine bearing antifriction layer owing to have performances such as good compactness, solidity to corrosion, wear resistance and fatigue resistance.The electroplating technology of existing Pb-Sn-Cu ternary alloy anti-attrition coating all adopts the fluoroborate bath system, and there are some defectives in its plating bath, as the plating bath instability, need prevent that tin atom is to the diffusion of matrix in the alloy layer with the nickel plating grid, yield rate is low, is not suitable for serialization production in enormous quantities; And because of the feasible Pb that contains of the strong complexing action of fluoroboric acid 2+, F -Poisonous wastewater treatment very difficult, the wastewater treatment expense is high and be difficult to realize qualified discharge, the harm environment, existing in recent years a plurality of countries and regions ban use of the electroplating technology of fluoroborate plating bath.
Summary of the invention
Purpose of the present invention just provides a kind of method that adopts the electroplating shaft bushing antifriction layer by metilsulfate plating bath of safety non-toxic environment-friendly type.
The applicant draws by test: concentration of metal ions to the Coating composition influence significantly in the metilsulfate plating bath.When other conditions are constant, improve slicker solder cupric ion concentration separately, slicker solder copper content all obviously rises in the alloy layer.By adjusting the coating that slicker solder cupric ion in the metilsulfate plating bath can obtain different slicker solder copper ratios, increase free methylsulphonic acid concentration, the content of coating tin descends to some extent, and quality of coating obviously descended when free methylsulphonic acid concentration was big.Gelatin can make coating smooth careful even, and Resorcinol can be stablized the plating bath effect, suppresses Sn 2+→ Sn 4+Transform, can also reduce coating fragility, make coating smooth careful; But along with the content of gelatin or Resorcinol increases, the content of tin also increases in the coating, and the content of copper then descends to some extent.
The present invention can realize in the following manner: clean after the oil removing of (1) bearing shell ultrasonic wave, hang on the bearing shell and carry out cleaning after negative electrode is electroplated oil removing; (2) the bearing shell volume ratio is to clean behind the dilute hydrochloric acid activation 1~2min that is made at 1: 3, and bearing shell is put into the metilsulfate plating bath, at room temperature makes anode with the terne metal of stanniferous 10%, cathode current density 2~3A/dm 2To cleaning behind inner surface of bearing bush plating 18~22min, inner surface of bearing bush obtains the slicker solder copper coating; (3) bearing shell that internal surface is coated with the slicker solder copper coating puts into that to contain sodium hydroxide be 10g/L, contain the tin plating electrolyte that sodium stannate is 85g/L, makes anode at 75~80 ℃ of lower steel plates, and cathode current density is 1~1.5A/dm 2The monoblock bearing shell is electroplated 3~8min, and bearing shell obtains tin coating on the surface.
The metilsulfate electroplate liquid formulation is to contain methylsulphonic acid 110~145g/L, methylsulphonic acid lead with Pb in the above-described step (2) 2+Meter 85~110g/L, stannous methanesulfonate are with Sn 2+Meter 8~14g/L, copper methanesulfonate are with Cu 2+Meter 1.5~4g/L, gelatin 2~5.5g/L, Resorcinol 5~8g/L.
Metilsulfate plating solution performance of the present invention is stable, electroplating technology simply need not the electronickelling grid, the coating crystallization is careful, hardness good, wear resisting property is good; Cooperate the frock hanger can make the lower bearing shell thickness of coating even, need not precision work after the plating, be fit to produce in enormous quantities; The metilsulfate plating bath is not owing to contain strong complexing agent and F -, waste water is handled qualified discharge easily, is applicable to big-and-middle-sized diesel engine, oil engine electroplating shaft bushing antifriction layer.
Embodiment
Below in conjunction with embodiment, the present invention is described in further detail, but it is not represented as unique embodiment of the present invention.
The present invention uses methylsulphonic acid, methylsulphonic acid lead, stannous methanesulfonate, copper methanesulfonate concentrated solution, and their concentration is respectively: M CH 3 SO 3 H = 960 g / L , M Pb ( CH 3 SO 3 ) 2 = 905 g / L , M Sn ( CH 3 SO 3 ) 2 = 785 g / L , M Cu ( CH 3 SO 3 ) 2 = 450 g / L .
Typical metilsulfate plating bath preparation: adding concentration in the 1 parts by volume metilsulfate plating bath successively is methylsulphonic acid strong solution 0.145 parts by volume of 960g/L, methylsulphonic acid lead solution 0.223 parts by volume that concentration is 905g/L, stannous methanesulfonate solution 0.03 parts by volume that concentration is 785g/L, methylsulphonic acid copper solutions 0.022 parts by volume that concentration is 450g/L, gelatin solution 0.2 parts by volume that concentration is 20g/L, Resorcinol solution 0.1 parts by volume that concentration is 65g/L, stir with distilled water diluting to 1 parts by volume at last, promptly obtain the metilsulfate plating bath.
Embodiment one
Two-sided lead plating stannum copper alloy coating on the platinized platinum that specification clean by oil removing and that weigh is 3 * 4cm.Convert dilute hydrochloric acid activation 1~2min that 3 volume water are made into 1 volume concentrated hydrochloric acid, the platinized platinum water after the activation cleans, then with above-mentioned metilsulfate plating bath at room temperature anode be the terne metal of stanniferous 10%, cathode current density 2.5A/dm 2, platinized platinum is carried out two-sided plating 20min, obtain the uniform and smooth fine and close slicker solder copper coating in surface.Prepared platinized platinum slicker solder copper coating is thickness 22 μ m after measured, and the slicker solder copper coating is through dissolving and volumetry coating content with acid: tin 7.8%, copper 2.3%, plumbous 89.9%.
Embodiment two
The pot metal inner surface of bearing bush that is 490QZL to 15 specifications simultaneously on the frock hanger is electroplated the slicker solder copper coating.Bearing shell is first to be 12g/L with containing NaOH, contain Na 2CO 3For 25g/L, contain Na 3PO 412H 2O is 60g/L, contain Na 2SiO 3Be the degreasing fluid of 12g/L, under 50 ℃ of temperature, carry out ultrasonic wave oil removing 5min; Go up to hang after the oil removing of bearing shell ultrasonic wave with containing NaOH be 12g/L, contain Na 2CO 3For 25g/L, contain Na 3PO 412H 2O is 35g/L, contain Na 2SiO 3For the electrolytic degreasing liquid of 7g/L, at room temperature make anode, cathode current density 2.5A/dm with steel plate 2Carry out electrolytic degreasing 4min; After bearing shell oil removing is for the second time cleaned, be that 1: 3 dilute hydrochloric acid promptly activates 1min with the dilute hydrochloric acid that 1 volume concentrated hydrochloric acid and 3 volume water are made into volume ratio; Put into 60 after bearing shell after the activation cleans and go up and state the metilsulfate plating bath, at room temperature make anode, cathode current density 2A/dm with the terne metal of stanniferous 10% 2Inner surface of bearing bush is electroplated 22min, obtain canescence slicker solder copper coating, the uniform and smooth densification of coating surface, the bearing shell thickness of coating is 21~23 μ m.
After inner surface of bearing bush is electroplated the slicker solder copper coating, be 10g/L with containing NaOH, contain Na 2SnO 3Be the tin plating electrolyte of 85g/L, make anode at 75 ℃ of lower steel plates, cathode current density is 1A/dm 2The monoblock bearing shell is electroplated 8min, and the bearing shell surface obtains silvery white zinc-plated protective layer, and the surface is uniform and smooth, thickness 1~2 μ m.
Embodiment three
Lead plating tin copper coating on the pot metal inner surface of bearing bush that is 490QZL to 45 specifications simultaneously on the frock hanger.Bearing shell is first to be 12g/L with containing NaOH, contain Na 2CO 3For 25g/L, contain Na 3PO 412H 2O is 60g/L, contain Na 2SiO 3Be the degreasing fluid of 12g/L, under 60 ℃ of temperature, carry out ultrasonic wave oil removing 5min; Go up to hang after the oil removing of bearing shell ultrasonic wave with containing NaOH be 12g/L, contain Na 2CO 3For 25g/L, contain Na 3PO 412H 2O is 35g/L, contain Na 2SiO 3For the electrolytic degreasing liquid of 7g/L, at room temperature make anode, cathode current density 2.5A/dm with steel plate 2Carry out catholyte oil removing 5min; After bearing shell oil removing is for the second time cleaned, be that 1: 3 dilute hydrochloric acid activates 2min with volume ratio; Put into 60 after bearing shell after the activation cleans and go up and state the metilsulfate plating bath, at room temperature make anode, cathodic current 2.5A/dm with the terne metal of stanniferous 10% 2Inner surface of bearing bush is electroplated 18min, obtain canescence slicker solder copper coating, the uniform and smooth densification of coating surface, thickness is 21~23 μ m.
After inner surface of bearing bush is electroplated the slicker solder copper coating, be 10g/L with containing NaOH, contain Na 2SnO 3Be the tin plating electrolyte of 85g/L, make anode at 80 ℃ of lower steel plates, cathode current density is 1.5A/dm 2The monoblock bearing shell is electroplated 3min, and the bearing shell surface obtains silvery white zinc-plated protective layer, and the surface is uniform and smooth, thickness 1~2 μ m.

Claims (2)

1, a kind of method of electroplating shaft bushing antifriction layer by metilsulfate plating bath is characterized in that:
(1) cleans after the oil removing of bearing shell ultrasonic wave, hang on the bearing shell and carry out cleaning after the catholyte oil removing;
(2) the bearing shell volume ratio is to clean behind the dilute hydrochloric acid activation 1~2min that is made at 1: 3, and bearing shell is put into the metilsulfate plating bath, at room temperature makes anode with the terne metal of stanniferous 10%, cathode current density 2~3A/dm 2To cleaning behind inner surface of bearing bush plating 18~22min, inner surface of bearing bush obtains the slicker solder copper coating;
(3) bearing shell that internal surface is coated with the slicker solder copper coating puts into that to contain sodium hydroxide be 10g/L, contain the tin plating electrolyte that sodium stannate is 85g/L, makes anode at 75~80 ℃ of lower steel plates, and cathode current density is 1~1.5A/dm 2The monoblock bearing shell is electroplated 3~8min, and the bearing shell surface obtains tin coating.
2, the method for electroplating shaft bushing antifriction layer by metilsulfate plating bath according to claim 1 is characterized in that the metilsulfate electroplate liquid formulation is to contain methylsulphonic acid 110~145g/L, methylsulphonic acid lead with Pb in the step (2) 2+Meter 85~110g/L, stannous methanesulfonate are with Sn 2+Meter 8~14g/L, copper methanesulfonate are with Cu 2+Meter 1.5~4g/L, gelatin 2~5.5g/L, Resorcinol 5~8g/L.
CN2009100370652A 2009-02-04 2009-02-04 Method for electroplating shaft bushing antifriction layer by metilsulfate plating bath Expired - Fee Related CN101503811B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009100370652A CN101503811B (en) 2009-02-04 2009-02-04 Method for electroplating shaft bushing antifriction layer by metilsulfate plating bath

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009100370652A CN101503811B (en) 2009-02-04 2009-02-04 Method for electroplating shaft bushing antifriction layer by metilsulfate plating bath

Publications (2)

Publication Number Publication Date
CN101503811A true CN101503811A (en) 2009-08-12
CN101503811B CN101503811B (en) 2011-01-12

Family

ID=40976184

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009100370652A Expired - Fee Related CN101503811B (en) 2009-02-04 2009-02-04 Method for electroplating shaft bushing antifriction layer by metilsulfate plating bath

Country Status (1)

Country Link
CN (1) CN101503811B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102330129A (en) * 2011-09-09 2012-01-25 江苏飞月轴瓦有限公司 Tin plating process of aluminum base bearing bush
CN102424996A (en) * 2011-12-02 2012-04-25 广东韶配动力机械有限公司 Preparation method of bearing bush with high bearing capacity
CN102748391A (en) * 2012-06-15 2012-10-24 湖北东风佳华汽车部件有限公司 Surface leadless electroplating friction reducing layer of bearing shell, and electroplating process
CN105040053A (en) * 2015-09-22 2015-11-11 太仓市金鹿电镀有限公司 Lead-tin-copper alloy electroplating process
CN115305537A (en) * 2022-09-06 2022-11-08 蔡杰 Copper-tin alloy environment-friendly electroplating process

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102330129A (en) * 2011-09-09 2012-01-25 江苏飞月轴瓦有限公司 Tin plating process of aluminum base bearing bush
CN102330129B (en) * 2011-09-09 2016-08-10 江苏飞月轴瓦有限公司 Tin plating process of aluminum base bearing bush
CN102424996A (en) * 2011-12-02 2012-04-25 广东韶配动力机械有限公司 Preparation method of bearing bush with high bearing capacity
CN102748391A (en) * 2012-06-15 2012-10-24 湖北东风佳华汽车部件有限公司 Surface leadless electroplating friction reducing layer of bearing shell, and electroplating process
CN105040053A (en) * 2015-09-22 2015-11-11 太仓市金鹿电镀有限公司 Lead-tin-copper alloy electroplating process
CN115305537A (en) * 2022-09-06 2022-11-08 蔡杰 Copper-tin alloy environment-friendly electroplating process

Also Published As

Publication number Publication date
CN101503811B (en) 2011-01-12

Similar Documents

Publication Publication Date Title
CN101302635B (en) Steel member acidic electroplating additive for copper pre-plating and pre-plating process
CN101503811B (en) Method for electroplating shaft bushing antifriction layer by metilsulfate plating bath
CN101665962A (en) Alkaline non-cyanide plating solution for copper-plating used on iron and steel base and preparation method thereof
CN103668357A (en) Alkaline cyanide-free high-speed copper plating solution
CN103668374A (en) Method for carrying out one-side copper plating on wide stainless steel band and electroplating bath
CN108060442B (en) Method for preparing zinc-copper composite coating on surface of copper-aluminum composite busbar
CN109957822B (en) Copper alloy electroplating process
CN101760768A (en) Electroplating solution for cyanide-free silver plating and cyanide-free silver plating method
CN102605393B (en) Ni-W-Fe-Co alloy electroplating liquid and electroplating process thereof
CN101710620A (en) Proton exchange membrane fuel cell stainless steel bipolar plate and modification method thereof
CN102677116A (en) Method for dipulse preplating non-cyanide alkaline copper on ferro matrix
CN104611739A (en) Cysteine silver plating solution and electroplating method
CN107190288B (en) Preparation method of HEDP copper-plated pore-free thin layer
CN110923757B (en) Cyanide-free alkali copper electroplating solution and use method thereof
CN105297088A (en) Electroplate liquid for acid copper plating of triphenylmethane dye system and electroplating method
CN104264195A (en) Mercaptoiminazole cyanide-free gold-electroplating solution and electroplating method thereof
CN105177643A (en) Electroplating solution for acidic copper plating by phenol dye system and electroplating method thereof
CN113463146A (en) Electroplating solution and electroplating process for surface of metal tool
CN108130572B (en) Aluminum alloy nickel pre-plating solution
CN102877044A (en) Method for producing environment-friendly lead-free electroless nickel immersion gold
CN105316728A (en) Electroplate liquid and electroplate method for gelatin cyanide-free plated Cu-Sn alloy
CN1978711A (en) Method for preparing alloy coating
CN104233385A (en) Electroplating liquid for non-cyanide plating gold by thiazole and electroplating method thereof
CN105316724A (en) Electroplate liquid and electroplate method for pyrophosphate used for cyanide-free plated Cu-Sn alloy
CN104630843A (en) Plating solution for acid copper plating by phenazine dye system and electroplating method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110112

Termination date: 20150204

EXPY Termination of patent right or utility model