CN105925970A - Surface treatment agent used before metal material cathode electrophoresis coating - Google Patents

Surface treatment agent used before metal material cathode electrophoresis coating Download PDF

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Publication number
CN105925970A
CN105925970A CN201610551816.2A CN201610551816A CN105925970A CN 105925970 A CN105925970 A CN 105925970A CN 201610551816 A CN201610551816 A CN 201610551816A CN 105925970 A CN105925970 A CN 105925970A
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Prior art keywords
metal material
processing agent
list processing
coating
before metal
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CN201610551816.2A
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CN105925970B (en
Inventor
魏大力
赵凯利
聂晓霖
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Nanjing Ke Run Industrial Media Limited-Liability Co
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Nanjing Ke Run Industrial Media Limited-Liability Co
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    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/34Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/48Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 not containing phosphates, hexavalent chromium compounds, fluorides or complex fluorides, molybdates, tungstates, vanadates or oxalates
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D13/00Electrophoretic coating characterised by the process
    • C25D13/20Pretreatment

Abstract

The invention discloses a surface treatment agent used before metal material cathode electrophoresis coating. Every liter of the surface treatment agent comprises 80-150mg of water-soluble oligosiloxane, 50mg of zirconyl nitrate, 100mg of titanyl sulfate, 100mg of aluminum nitrate and/or zinc sulfate, 70-80mg of lithium carbonate, 100-120mg of hydrofluoric acid, 80-100mg of oxide nanoparticles with the surface grafted with an amino group and/or a hydroxyl group, 100-150mg of ethanol, 50-100mg of polyethylene glycol with the molecular weight of 300-600, 1-5mg of ferrous sulfate, and the balance of water, wherein the grafting amount of the hydroxyl group on the surface of the oxide nanoparticles is 1.4-5mmol/g, and the grafting amount of the amino group on the surface of the oxide nanoparticles is 0.9-5mmol/g. The surface treatment agent greatly improves the resistance of the metal surface.

Description

A kind of list processing agent before metal material cathode electro-coating
Technical field
The present invention relates to a kind of list processing agent before metal material cathode electro-coating, belong to industrial media technology neck Territory.
Background technology
Metal material typically requires before carrying out application and carries out surface process to strengthen the adhesion property between metal and coating, mesh Before, the metal surface treatment technology many employings phosphorization treatment process before application.But, this processing method is owing to having containing zinc, nickel etc. The evil chemical composition such as heavy metal ion and phosphorus, and production produces substantial amounts of phosphatization slag, environment can be caused potentially hazardous. Meanwhile, phosphorization treatment technology power consumption is relatively big, adjusts technique degree of dependence big in the table in front road, and this also can increase the difficulty of cost and management Degree.
As the technology that can substitute conventional phosphatizing processing mode, it is known that have Zirconium compound or Zirconium compound combine Organosilan processing mode.But the metal material surface chemical reaction film layer that existing non-phosphatization processing mode obtains is thin, film layer Sparse the finest and close, thus cause metal material surface resistance low, for having relatively in car body and parts, or other industry For the metal material of labyrinth, it is accordingly required in particular to form fine and close thick and heavy chemical composition coating layer at metal material surface, enter And improve metal surface resistance, so that metal material is when follow-up cathode electro-coating, electrophoretic coating has high throwing power.
The exploitation of a kind of non-phosphatization list processing agent that can be effectively improved metal surface resistance value is necessary.
Summary of the invention
The technical problem to be solved is to provide a kind of list processing before metal material cathode electro-coating Agent, this list processing agent can be greatly improved the resistance value of metal surface.
For solving above-mentioned technical problem, the technical solution adopted in the present invention is:
A kind of list processing agent before metal material cathode electro-coating, in every L list processing agent, by the group of following quality It is grouped into: 80~150mg water soluble oligomer siloxanes, 50mg zirconyl nitrate or fluorine zirconic acid, 100mg titanyl sulfate or fluotitanic acid, 100mg aluminum nitrate and/or zinc sulfate, 70~80mg lithium carbonate or potassium hydroxide or Ammonium bicarbonate food grade, 100~120mg Fluohydric acid. or Nitric acid or sulphuric acid, 80~100mg surface grafting have amino and/or the oxide nano particles of hydroxyl, 100~150mg ethanol, 50 ~Polyethylene Glycol, 1~5mg ferrous sulfate that 100mg molecular weight is 300~600 and water surplus;Wherein, described oxide is received The grafting amount of rice grain surface hydroxyl is 1.4~5mmol/g, and the grafting amount of described oxide nanoparticle surface amino is 0.9 ~5mmol/g, the ratio of described oxide nanoparticle surface hydroxyl and amino grafting amount is 0.3~4.1.
Further preferably, described water soluble oligomer siloxanes is trimer siloxanes, tetramer siloxanes, pentamer silica Alkane or six aggressiveness siloxanes.
Further preferably, described oxide nano particles is nano SiO 2 particle and/or titania nanoparticles And/or zirconium dioxide nanoparticles.
Further preferably, the particle diameter of described nano SiO 2 particle is 5~10nm;Described titania nanoparticles Particle diameter is 6~8nm;The particle diameter of described zirconium dioxide nanoparticles is 5~6nm, and oxide nano particles is under such particle diameter Easily dispersion, is difficult to reunite, the stability of advantageously combined objects system, and is of value to compositions and deposits film forming in metal surface.
Further preferably, described aluminum nitrate or zinc sulfate can also be substituted by the calcium salt of equivalent, manganese salt or iron salt.
Further preferably, the pH value of described list processing agent is 4~5.
Further preferably, described surface grafting has the oxide nano particles of amino and/or hydroxyl to adopt to make with the following method For forming: the oxide nano particles that a certain amount of particle diameter is 5~10nm is placed in ethanol, isopropanol or toluene solvant;Again The desired amount of γ-aminopropyltrimethoxysilane and/or gamma-aminopropyl-triethoxy-silane, described γ-ammonia is added in solvent The addition of propyl trimethoxy silicane and/or gamma-aminopropyl-triethoxy-silane is the 1% of oxide nano particles addition ~1.5%;By mixed material in rotating speed be 1000~1500r/min down cuts 50~60min;By the suspension that obtains in 40~ Agitating heating 12~24h at 60 DEG C, more scrubbed, filter and dried i.e. can get the oxidation of amino and/or hydroxyl modification Thing nano-particle.Containing of control oxide nano grain surface hydroxyl and amino is carried out by controlling the addition of silane coupler Amount, the content ratio of oxide nanoparticle surface hydroxyl and amino just both must can make product in the range of the present invention is limited The film layer of dense regular can be formed at metal material surface, enhancing metal material can also be played simultaneously and adhere to follow-up electrophoretic coating The effect of power.
The method measuring oxide nanoparticle surface hydroxy radical content: to taking out equipped with modified oxide nano particles Filter flask adds dry toluene, with dispersal oxide nano-particle;The pipeline of titration appratus is dried, and in bottle,suction Rapidly join the methyl-magnesium-chloride being stored in constant pressure funnel, use drainage eudiometer to collect the gas V1 generated, Until reaction is completely;Blank assay: measure the gas flow V2 generated when being added without modified oxide nano particles, as the following formula The content of calculating oxide nanoparticle surface hydroxyl:
C O H = P × ( V 1 - V 2 ) m × T × R × 1000 ;
In formula: COHFor oxide nanoparticle surface hydroxy radical content, unit is mmol/g;P is atmospheric pressure, and unit is Pa;V1 generates gas volume for experiment, and unit is m3;V2 is that blank assay generates gas volume, and unit is m3;M is sample matter Amount, unit is g;T is experimental temperature, and unit is K;R is gas constant, and unit is (m3·Pa)/(K·mol)。
The method measuring oxide nanoparticle surface amino content: by a certain amount of modified oxide nano particles, Join in 100ml dehydrated alcohol or isopropanol, ultrasonic 10min, until sample dispersion all with after, add 5~10 thymols Blue indicator solution, with hydrochloric acid-ethanol standard solution titration, solution colour is titration end-point from the faint yellow pink that becomes, with Shi Jinhang blank assay;Blank assay: carry out in the case of being added without modified oxide nano particles.The most according to the following formula Computing function nano-oxide particle surface amino content:
C NH 2 = c × ( V 5 - V 6 ) m ;
In formula:For oxide nanoparticle surface amino content, unit is mmol/g;C is that hydrochloric acid-ethanol solution rubs That concentration, unit is mol/L;V5 is the volume consuming hydrochloric acid-ethanol solution in EXPERIMENTALTitration, and unit is mL;V6 is blank real Testing the volume of consumption hydrochloric acid-ethanol solution, unit is mL.
Hydrochloric acid-ethanol standard solution forming steps is as follows: 1. measure the concentrated hydrochloric acid that 9ml mass concentration is 36%, adds nothing Water-ethanol is diluted to 1000ml, mix homogeneously and get final product;2. it is taken at 270-300 DEG C and is dried the benchmark natrium carbonicum calcinatum 0.1g to constant weight It is placed in conical flask, after adding 50ml deionized water dissolving, adds C.I. 13020 .-bromocresol green mixed indicator 10, with above-mentioned Hydrochloric acid-ethanol solution be titrated to solution colour by green transition be kermesinus be titration end-point, carry out blank assay simultaneously;3. empty White test: carry out in the case of being added without sodium carbonate.It is calculated as follows the molar concentration of hydrochloric acid-ethanol solution:
c = m ( V 3 - V 4 ) × 0.0530 ;
In formula: the actual concentrations of c-hydrochloric acid-ethanol standard titration solution, unit is mol/L;M-benchmark natrium carbonicum calcinatum Quality, unit is g;In V3-experiment, titration consumes hydrochloric acid-ethanol standard solution volume, and unit is mL;V4-blank experiment drips Surely consuming hydrochloric acid-ethanol standard solution volume, unit is mL;0.0530 for (concentration is with 1.00mL Hydrochloric Standard Titration The quality of 1mol/L) suitable benchmark natrium carbonicum calcinatum, unit is g.
Compared to prior art, technical solution of the present invention has the beneficial effect that
The advantage that list processing agent of the present invention has good stability, wettability is good, and the metal material after processing can direct water Wash (illustrating that product of the present invention is strong at metal surface adhesive force, be difficult to come off from metal material surface);Inventive formulation uses poly- Siloxanes substitutes monomeric silanes coupling agent, effectively enhances the stability of system, due to monomeric silanes coupling agent difficulty in system With dispersion, easily assemble agglomerating, thus have impact on performance and the stability of system;It addition, inventive formulation uses is grafted with amino And/or the oxide nano particles of hydroxyl, surface has the oxide nano particles of functional group and shows attachment at metal material Power is strong, is difficult to come off from metal material surface, and follow-up electrophoresis film and the adhesive force of metal material;The present invention joins Product can be made to get off in the calmness that metal material surface is orderly, form the film layer of dense regular, thus improve metal material table The resistance value in face, the resistance value of the metal material surface after using the present invention non-phosphatization list processing agent to process can reach 1.5~2.5 Ohm/every square centimeter, 0.2~0.5 ohm/every square centimeter of the most existing non-phosphatization list processing agent, therefore gold Genus material is when follow-up cathode electro-coating, and electrophoretic coating has high throwing power, and inventive formulation can also improve metal material What surface and follow-up electrophoresis process were formed is coated with intermembranous adhesive force.
Accompanying drawing explanation
Fig. 1 is that after using list processing agent of the present invention to process, metal material shows that the chemical reaction film layer formed is partially schematic Figure;
Fig. 2 is that after using existing non-phosphatization list processing agent to process, metal material shows that the chemical reaction film layer formed local shows It is intended to.
Detailed description of the invention
According to following embodiment, the present invention be may be better understood.But, as it will be easily appreciated by one skilled in the art that reality Execute the content described by example and be merely to illustrate the present invention, and should be also without limitation on basis described in detail in claims Invention.
List processing agent treated metal material of the present invention, including ferrum and/or its alloy material, zinc and/or its alloy material Material, aluminum and/or its alloy material and magnesium and/or its alloy material.
Water soluble oligomer siloxanes employed in list processing agent prescription of the present invention is:
Dynasylan the Hydrosil 2926 and/or Dynasylan Hydrosil 2776 of Dehussa company.
Embodiment 1
Present invention list processing agent before metal material cathode electro-coating, in every L list processing agent, by following quality Component forms: 100mg water soluble oligomer siloxanes (Dynasylan Hydrosil 2926), 50mg zirconyl nitrate, 100mg sulfur Acid oxygen titanium, 100mg aluminum nitrate, 70mgLi2CO3, 100mg sulphuric acid, 80mg surface grafting have the oxidate nano of amino and hydroxyl Grain, 100mg ethanol, 50mg molecular weight are the Polyethylene Glycol of 600, (ferrous sulfate can strengthen the reaction of system to 2mg ferrous sulfate Activity, promotes the generation of reaction and improves reaction efficiency) and water surplus;Wherein, described oxide nanoparticle surface hydroxyl Grafting amount be 5mmol/g, the grafting amount of described oxide nanoparticle surface amino is 5mmol/g, oxide nano particles The ratio of surface hydroxyl and amino grafting amount is 1.
The pH value of present invention list processing agent before metal material cathode electro-coating is 5.
Embodiment 2
Present invention list processing agent before metal material cathode electro-coating, in every L list processing agent, by following quality Component forms: 80mg water soluble oligomer siloxanes (Dynasylan Hydrosil 2926), 70mg water soluble oligomer siloxanes (Dynasylan Hydrosil 2776), 50mg fluorine zirconic acid, 100mg titanyl sulfate, 50mg aluminum nitrate, 50mg zinc sulfate, 70mg Potassium hydroxide, 100mg nitric acid, 100mg surface grafting have amino and the oxide nano particles of hydroxyl, 120mg ethanol, 80mg to divide Son amount is Polyethylene Glycol, 3mg ferrous sulfate and the water surplus of 600;Wherein, the connecing of described oxide nanoparticle surface hydroxyl Branch amount is 1.4mmol/g, and the grafting amount of described oxide nanoparticle surface amino is 3.8mmol/g, oxide nano particles The ratio of surface hydroxyl and amino grafting amount is 0.37.
The pH value of present invention list processing agent before metal material cathode electro-coating is 4.5.
Embodiment 3
Present invention list processing agent before metal material cathode electro-coating, in every L list processing agent, by following quality Component forms: 50mg water soluble oligomer siloxanes (Dynasylan Hydrosil 2926), 100mg water soluble oligomer siloxanes (Dynasylan Hydrosil 2776), 50mg fluorine zirconic acid, 100mg fluotitanic acid, 100mg zinc sulfate, 80mg Ammonium bicarbonate food grade, 120mg Fluohydric acid., 100mg surface grafting have amino and the oxide nano particles of hydroxyl, 150mg ethanol, the 100mg molecular weight to be Polyethylene Glycol, 5mg ferrous sulfate and the water surplus of 600;Wherein, the grafting amount of described oxide nanoparticle surface hydroxyl is 3.7mmol/g, the grafting amount of described oxide nanoparticle surface amino is 0.9mmol/g, oxide nanoparticle surface hydroxyl The ratio of base and amino grafting amount is 4.1.
The pH value of present invention list processing agent before metal material cathode electro-coating is 4.2.
Embodiment 4
Using commercially available Q235 cold-rolled steel sheet (species abundance in Baosteel in Shanghai production), specification is made for (170mm × 100mm × 0.8mm) Set-iron for the present embodiment.
First metal sample is carried out the degreasing cleaning process that metal material shows;Then set-iron is placed in embodiment Soaking 5 minutes in the list processing agent of 1, immediately process with water flushing after immersion, the resistance value on the set-iron surface after process is 1.5 ohm/every square centimeter, after flushing, set-iron is in the case of moistened surface, uses cathode electrophoresis dope HD8000 (to close Western company manufactures) carry out ability cathode electrophoresis process, the model after electrophoretic process uses deionized water rinsing 30 seconds.After washing After electrophoresis, model is dried 20 minutes under the conditions of 180 DEG C, takes out room temperature and dries its film thickness of detection in 20 μm ± 1 μ m Obtaining test piece, test piece specifically detects performance and is shown in Table 1.
Embodiment 5
Using commercially available galvanized steel plain sheet, specification is the metal-like that (170mm × 100mm × 0.8mm) is used as the present embodiment Plate.
First metal sample is carried out the degreasing cleaning process that metal material shows;Then set-iron is placed in embodiment Soaking 2 minutes in the list processing agent of 2, immediately process with water flushing after immersion, the resistance value on the set-iron surface after process is 2.0 ohm/every square centimeter, after flushing, set-iron is in the case of moistened surface, uses cathode electrophoresis dope ECO3000 (manufacture of KCC company) carries out ability cathode electrophoresis process, and the model after electrophoretic process uses deionized water rinsing 30 seconds.After washing Electrophoresis after model under the conditions of 180 DEG C be dried 20 minutes, take out room temperature dry detection its film thickness at 20 μm ± 1 μ m The most i.e. obtaining test piece, test piece specifically detects performance and is shown in Table 1.
Embodiment 6
Using commercially available aluminium sheet, specification is the set-iron that (170mm × 100mm × 0.8mm) is used as the present embodiment.
First metal sample is carried out the degreasing cleaning process that metal material shows;Then set-iron is placed in embodiment Soaking 8 minutes in the list processing agent of 3, immediately process with water flushing after immersion, the resistance value on the set-iron surface after process is 2.5 ohm/every square centimeter, after flushing, set-iron is in the case of moistened surface, uses cathode electrophoresis dope ED6C (PPG Company manufactures) carry out ability cathode electrophoresis process, the model after electrophoretic process uses deionized water rinsing 30 seconds.By the electricity after washing After swimming, model is dried 20 minutes under the conditions of 180 DEG C, and taking-up room temperature is dried its film thickness of detection and in 20 μm ± 1 μ m is Obtaining test piece, test piece specifically detects performance and is shown in Table 1.
Table 1
As shown in Fig. 1~2, the precipitation that list processing agent of the present invention can be orderly in metal surface, the chemical reaction film obtained Layer dense regular, thus cause metal material surface resistance value high, and oxide nano particles is at metal material surface adhesive force By force, difficult drop-off, and the film layer arrangement that existing list processing agent obtains is loose, thus cause metal material surface resistance value low.
List processing agent stability of the present invention is high, wettability is good, and after process, the chemical reaction film layer of metal surface gained has The advantage that film thickness, resistance value are high and corrosion resistance is strong, significantly improves the throwing power in follow-up electrophoretic painting, and with follow-up electricity The adhesion of the film that swimming technique is formed is the strongest.

Claims (7)

1. the list processing agent before metal material cathode electro-coating, it is characterised in that: in every L list processing agent, by such as The component composition of lower quality: 80~150mg water soluble oligomer siloxanes, 50mg zirconyl nitrate or fluorine zirconic acid, 100mg titanyl sulfate Or fluotitanic acid, 100mg aluminum nitrate and/or zinc sulfate, 70~80mg lithium carbonate or potassium hydroxide or Ammonium bicarbonate food grade, 100~120mg Fluohydric acid. or nitric acid or sulphuric acid, 80~100mg surface grafting have amino and/or the oxide nano particles of hydroxyl, 100~ 150mg ethanol, 50~Polyethylene Glycol, 1~5mg ferrous sulfate that 100mg molecular weight is 300~600 and water surplus;Wherein, The grafting amount of described oxide nanoparticle surface hydroxyl is 1.4~5mmol/g, described oxide nanoparticle surface amino Grafting amount is 0.9~5mmol/g, and the ratio of described oxide nanoparticle surface hydroxyl and amino grafting amount is 0.3~4.1.
List processing agent before metal material cathode electro-coating the most according to claim 1, it is characterised in that: described water Dissolubility oligosiloxane is trimer siloxanes, tetramer siloxanes, pentamer siloxanes or six aggressiveness siloxanes.
List processing agent before metal material cathode electro-coating the most according to claim 1, it is characterised in that: described oxygen Compound nano-particle is nano SiO 2 particle and/or titania nanoparticles and/or zirconium dioxide nanoparticles.
List processing agent before metal material cathode electro-coating the most according to claim 3, it is characterised in that: described two The particle diameter of silicon oxide nano-particle is 5~10nm;The particle diameter of described titania nanoparticles is 6~8nm;Described zirconium dioxide The particle diameter of nano-particle is 5~6nm.
List processing agent before metal material cathode electro-coating the most according to claim 1, it is characterised in that: described nitre Acid aluminum or zinc sulfate can also be substituted by the calcium salt of equivalent, manganese salt or iron salt.
List processing agent before metal material cathode electro-coating the most according to claim 1, it is characterised in that: described table The pH value of inorganic agent is 4~5.
List processing agent before metal material cathode electro-coating the most according to claim 1, it is characterised in that: described table Face is grafted with the oxide nano particles of amino and/or hydroxyl and adopts and be prepared from the following method: by a certain amount of particle diameter be 5~ The oxide nano particles of 10nm is placed in ethanol, isopropanol or toluene solvant;The desired amount of γ-ammonia third is added again in solvent Base trimethoxy silane and/or gamma-aminopropyl-triethoxy-silane, described γ-aminopropyltrimethoxysilane and/or γ-ammonia The addition of propyl-triethoxysilicane is the 1%~1.5% of oxide nano particles addition;By mixed material in rotating speed it is 1000~1500r/min down cuts 50~60min;Suspension agitating heating 12~24h at 40~60 DEG C that will obtain, then warp Washing, filtration and dried i.e. can get the oxide nano particles of amino and/or hydroxyl modification.
CN201610551816.2A 2016-07-14 2016-07-14 A kind of surface conditioning agent before the cathode electro-coating for metal material Active CN105925970B (en)

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Publication number Priority date Publication date Assignee Title
CN107587126A (en) * 2017-07-19 2018-01-16 合肥普庆新材料科技有限公司 A kind of nano ceramics silane complex film layer transforming agent containing graphene oxide
CN109423683A (en) * 2017-08-30 2019-03-05 广东新会中集特种运输设备有限公司 The finishing system of container and the coating process of container

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CN102787311A (en) * 2012-07-16 2012-11-21 安徽未来表面技术有限公司 Rare earth-fluorozirconate compounding processing agent technology suitable for catholic electrophoresis pretreatment
CN103031584A (en) * 2012-12-06 2013-04-10 安徽未来表面技术有限公司 Process of silane-zirconium salt conversion treatment before metal cathode electrophoresis coating
CN103397320A (en) * 2013-08-20 2013-11-20 安徽工业大学 Cathodic electrophoresis pre-treatment liquor used on surface of hot-galvanized plate of automobile

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Publication number Priority date Publication date Assignee Title
CN101665934A (en) * 2009-09-27 2010-03-10 大连三达奥克化学股份有限公司 Film treating agent for treatment before electro-coating of die-cast aluminum alloy workpiece and preparation method thereof
CN102787311A (en) * 2012-07-16 2012-11-21 安徽未来表面技术有限公司 Rare earth-fluorozirconate compounding processing agent technology suitable for catholic electrophoresis pretreatment
CN103031584A (en) * 2012-12-06 2013-04-10 安徽未来表面技术有限公司 Process of silane-zirconium salt conversion treatment before metal cathode electrophoresis coating
CN103397320A (en) * 2013-08-20 2013-11-20 安徽工业大学 Cathodic electrophoresis pre-treatment liquor used on surface of hot-galvanized plate of automobile

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107587126A (en) * 2017-07-19 2018-01-16 合肥普庆新材料科技有限公司 A kind of nano ceramics silane complex film layer transforming agent containing graphene oxide
CN109423683A (en) * 2017-08-30 2019-03-05 广东新会中集特种运输设备有限公司 The finishing system of container and the coating process of container
CN109423683B (en) * 2017-08-30 2021-03-23 广东新会中集特种运输设备有限公司 Container coating system and container coating method

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