CN115613025A - High-efficiency acid-free pretreatment process for tire bead steel wire - Google Patents

High-efficiency acid-free pretreatment process for tire bead steel wire Download PDF

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CN115613025A
CN115613025A CN202211333742.7A CN202211333742A CN115613025A CN 115613025 A CN115613025 A CN 115613025A CN 202211333742 A CN202211333742 A CN 202211333742A CN 115613025 A CN115613025 A CN 115613025A
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steel wire
acid
deionized water
free pretreatment
wires according
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CN115613025B (en
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陆海
徐一铭
董利明
周黄山
赵国忠
张永平
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JIANGSU SHENGDA TECHNOLOGY CO LTD
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JIANGSU SHENGDA TECHNOLOGY CO LTD
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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
    • C23C22/73Chemical 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 characterised by the process
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D1/00Coating compositions, e.g. paints, varnishes or lacquers, based on inorganic substances
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D133/00Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Coating compositions based on derivatives of such polymers
    • C09D133/04Homopolymers or copolymers of esters
    • C09D133/06Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • C09D133/062Copolymers with monomers not covered by C09D133/06
    • C09D133/064Copolymers with monomers not covered by C09D133/06 containing anhydride, COOH or COOM groups, with M being metal or onium-cation
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
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    • 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
    • C23C22/60Chemical 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 alkaline aqueous solutions with pH greater than 8
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    • 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
    • C23C22/78Pretreatment of the material to be coated
    • 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
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/24Cleaning or pickling metallic material with solutions or molten salts with neutral solutions

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Abstract

The invention discloses a high-efficiency acid-free pretreatment process of a tire bead steel wire, which comprises the steps of polishing and degreasing a tai-acid steel wire, treating the tai-acid steel wire by using a surface treating agent, and treating the tai-acid steel wire by using a treating fluid to reduce the pollution of the treatment process to the environment.

Description

High-efficiency acid-free pretreatment process for tire bead steel wire
Technical Field
The invention relates to the technical field of tire preparation, in particular to a high-efficiency acid-free pretreatment process for a tire bead steel wire.
Background
With the development of light weight and high speed of automobiles, radial tires, which are important components of automobiles, are rapidly applied and developed with the advantages of high speed, energy saving, light weight, long driving range, and the like. The radial tire bears the acting forces of tension, compression, torsion, centrifugation and the like in the use process, and the quality of a tire bead steel wire serving as one of framework materials directly influences the quality of the tire. The currently used bead wire is a tin-plated bronze wire used to reinforce the rim of a tire. The tyre bead is a steel wire ring which is weaved by tyre bead steel wires and isolation rubber, and the outer tyre is tightly and stably fixed on the tyre bead. When an automobile runs, the tire bead and the tire bead edge are stressed greatly, if a tire bead steel wire of a framework material forming the tire bead is corroded, the strength is insufficient, the tire bead is easy to loosen, the tire is burst, and safety accidents occur, so that steel wire manufacturers and tire enterprises pay attention to the problems.
Disclosure of Invention
The invention aims to provide an efficient acid-free pretreatment process for a tire bead wire, which solves the problem that an acidic substance is required to be used in the existing tire bead wire treatment process to pollute the environment.
The purpose of the invention can be realized by the following technical scheme:
an efficient acid-free pretreatment process for a tire bead wire specifically comprises the following steps:
step S1: grinding the tire bead steel wire by using No. 300 abrasive paper, and then grinding by using No. 1000 abrasive paper to obtain a polished steel wire;
step S2: soaking the polished steel wire in a degreasing agent for 50-60s at the temperature of 30-40 ℃ to obtain a degreased steel wire;
and step S3: soaking the degreased steel wire in a surface treating agent for 1-2h at 50-60 ℃, taking out the steel wire until no liquid drops drop, and preserving heat for 1-2h at 110-120 ℃ to obtain a pretreated steel wire;
and step S4: soaking the pretreated steel wire in the treatment fluid, adding a sodium hydroxide solution until the pH value is 10-11, carrying out ultrasonic treatment for 20-30min under the conditions that the frequency is 30-50kHz and the temperature is 40-50 ℃, taking out the steel wire and drying to obtain the tire bead steel wire.
Further, the degreasing agent in the step S2 is prepared from the following components: 5-8g/L of sodium carbonate, 5-8g/L of sodium metasilicate pentahydrate, 4-6g/L of sodium gluconate, 5-8g/L of 4A zeolite, 1-3g/L of sodium nitrite and 4-6g/L of lauryl alcohol polyoxyethylene ether, and the solvent is water.
Further, the mass fraction of the sodium hydroxide solution in step S4 is 150%.
Further, the surface treating agent is prepared by the following steps:
step A1: dissolving 2, 2-dimethylolpropionic acid in deionized water, adding sodium hydroxide, stirring for 10-15min at the rotation speed of 300-500r/min and the temperature of 30-40 ℃, adding epoxy chloropropane, reacting for 3-5h, adjusting the pH value of the reaction solution to 6-6.5 to prepare an intermediate 1, uniformly mixing the intermediate 1, 2-thiophenemethylamine and methanol, carrying out reflux reaction for 10-15h at the temperature of 65-70 ℃, and distilling to remove the methanol to prepare an intermediate 2;
the reaction process is as follows:
Figure BDA0003914570370000021
Figure BDA0003914570370000031
step A2: uniformly mixing the intermediate 2, 2-aminobenzimidazole, 1-hydroxybenzotriazole and tetrahydrofuran, reacting for 6-8h at the rotation speed of 200-300r/min and the temperature of 40-50 ℃ to obtain an intermediate 3, uniformly mixing the intermediate 3, acrylic acid, p-toluenesulfonic acid and DMF, and reacting for 8-10h at the rotation speed of 150-200r/min and the temperature of 120-130 ℃ to obtain an intermediate 4;
the reaction process is as follows:
Figure BDA0003914570370000032
step A3: mixing the intermediate 4, p-amino styrene, ethyl acrylate, acrylic acid and deionized water to obtain a monomer solution, adding 1/10 of the monomer solution into an emulsifier, stirring and adding a potassium persulfate aqueous solution under the conditions of a rotation speed of 150-200r/min and a temperature of 65-70 ℃, reacting for 30-40min, adding the rest of the monomer solution, and reacting for 2-3h to obtain the surface treating agent.
Further, the molar ratio of 2, 2-dimethylolpropionic acid to epichlorohydrin in step A1 is 1.
Further, the molar ratio of the intermediate 2, 2-aminobenzimidazole and 1-hydroxybenzotriazole in the step A2 is 1.
Further, the use ratio of the intermediate 4, p-amino styrene, ethyl acrylate, acrylic acid and deionized water in the step A3 is 8g.
Further, the treatment fluid is prepared by the following steps:
step B1: expanding expandable graphite at 900-950 ℃ for 15-20s at high temperature, adding into deionized water, performing ultrasonic treatment at 30-40kHz and 50-60 ℃ for 1-1.5h, filtering and drying to obtain graphite micro-sheets;
and step B2: mixing graphite micro-sheets, nano boron nitride, alumina and ethanol, ball-milling for 15-20min at the rotation speed of 200-300r/min, drying and crushing, sieving with a 100-mesh sieve, and roasting at the temperature of 1500-1600 ℃ for 1-1.5h to obtain composite powder;
and step B3: dispersing the composite powder in deionized water, adding KH560, stirring at a rotation speed of 600-800r/min and a temperature of 85-90 deg.C for 1-1.5h, filtering to remove filtrate, and dispersing the substrate in deionized water to obtain the treatment solution.
Further, the mass ratio of the graphite micro-sheets, the nano boron nitride, the alumina and the ethanol in the step B2 is 3.
Further, the dosage of the KH560 in the step B3 is 5-8% of the composite powder by mass, and the dosage ratio of the substrate to the deionized water is 1g.
The invention has the beneficial effects that: the invention does not use acid substance to process in the process of processing the tire bead steel wire, reduces the pollution to the environment in the processing process, and uses surface processing agent and processing liquid, the surface processing agent uses 2, 2-dimethylolpropionic acid and epoxy chloropropane as raw materials, under the action of sodium hydroxide, hydroxyl on the 2, 2-dimethylolpropionic acid reacts with chlorine atom sites on the epoxy chloropropane to prepare an intermediate 1, the intermediate 1 reacts with 2-thiophene methylamine to prepare an intermediate 2, the intermediate 2 and 2-aminobenzimidazole are dehydrated and condensed to prepare an intermediate 3, the intermediate 3 and acrylic acid are esterified under the action of p-toluenesulfonic acid to prepare an intermediate 1, the intermediate 1, p-amino styrene, ethyl acrylate and acrylic acid are polymerized to form water-soluble polyacrylate to prepare the surface processing agent, the processing liquid uses expandable graphite as raw materials and is roasted at high temperature, the method comprises the steps of ultrasonically treating graphene microchip, nano boron nitride and aluminum oxide in water to obtain graphite microchip, ball-milling and roasting the graphene microchip, nano boron nitride and aluminum oxide to obtain composite powder, treating the surface of the composite powder with KH560 to graft epoxy groups on the surface of the composite powder, dispersing the composite powder in deionized water to obtain a treatment solution, soaking degreased steel wires in a surface treatment agent to treat heteroatoms such as nitrogen, sulfur and oxygen in self molecules, complexing and coordinating the heteroatoms on the surface of metal to form a corrosion inhibition film, attaching a polyacrylate layer on the surface of the corrosion inhibition film, soaking pretreated steel wires in the treatment solution, adjusting the pH value of the treatment solution to be alkaline, reacting amino on the surface of the pretreated steel wires with the epoxy groups on the surface of the powder during treatment, forming a compact base-free layer on the surface of the polyacrylate layer, and further improving the corrosion resistance of the steel wires.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1
An efficient acid-free pretreatment process for a tire bead wire specifically comprises the following steps:
step S1: grinding the tire bead steel wire by using No. 300 abrasive paper, and then grinding by using No. 1000 abrasive paper to obtain a polished steel wire;
step S2: soaking the polished steel wire in a degreasing agent for 50s at the temperature of 30 ℃ to obtain a degreased steel wire;
and step S3: soaking the degreased steel wire in a surface treating agent for 1h at the temperature of 50 ℃, taking out the steel wire until no liquid drops drop, and preserving heat for 1h at the temperature of 110 ℃ to obtain a pretreated steel wire;
and step S4: soaking the pretreated steel wire in the treatment solution, adding a sodium hydroxide solution until the pH value is 10, carrying out ultrasonic treatment for 20min under the conditions of the frequency of 30kHz and the temperature of 40 ℃, taking out the steel wire and drying to obtain the tire bead steel wire.
The degreasing agent in the step S2 is prepared from the following components: 5g/L of sodium carbonate, 5g/L of sodium metasilicate pentahydrate, 4g/L of sodium gluconate, 5g/L of 4A zeolite, 1g/L of sodium nitrite and 4g/L of lauryl alcohol polyoxyethylene ether, and the solvent is water.
The mass fraction of the sodium hydroxide solution in the step S4 is 150%.
The surface treating agent is prepared by the following steps:
step A1: dissolving 2, 2-dimethylolpropionic acid in deionized water, adding sodium hydroxide, stirring for 10min at the rotation speed of 300r/min and the temperature of 30 ℃, adding epoxy chloropropane, reacting for 3h, adjusting the pH value of a reaction solution to 6 to prepare an intermediate 1, uniformly mixing the intermediate 1, 2-thiophenemethylamine and methanol, carrying out reflux reaction for 10h at the temperature of 65 ℃, and distilling to remove the methanol to prepare an intermediate 2;
step A2: uniformly mixing the intermediate 2, 2-aminobenzimidazole, 1-hydroxybenzotriazole and tetrahydrofuran, reacting for 6 hours at the rotation speed of 200r/min and the temperature of 40 ℃ to obtain an intermediate 3, uniformly mixing the intermediate 3, acrylic acid, p-toluenesulfonic acid and DMF, and reacting for 8 hours at the rotation speed of 150r/min and the temperature of 120 ℃ to obtain an intermediate 4;
step A3: mixing the intermediate 4, p-amino styrene, ethyl acrylate, acrylic acid and deionized water to obtain a monomer solution, adding 1/10 of the monomer solution into an emulsifier, stirring and adding a potassium persulfate aqueous solution under the conditions of a rotation speed of 150r/min and a temperature of 65 ℃, reacting for 30min, adding the rest of the monomer solution, and reacting for 2h to obtain the surface treating agent.
The molar ratio of the 2, 2-dimethylolpropionic acid to the epichlorohydrin in the step A1 is 1.
The molar ratio of the intermediate 2, the 2-aminobenzimidazole and the 1-hydroxybenzotriazole in the step A2 is 1.
The use amount ratio of the intermediate 4, the p-amino styrene, the ethyl acrylate, the acrylic acid and the deionized water in the step A3 is 8g.
The treatment liquid is prepared by the following steps:
step B1: expanding expandable graphite at a high temperature of 900 ℃ for 15s, adding the expandable graphite into deionized water, carrying out ultrasonic treatment for 1h at a frequency of 30kHz and a temperature of 50 ℃, filtering and drying to obtain graphite micro-sheets;
and step B2: mixing graphite micro-sheets, nano boron nitride, alumina and ethanol, ball-milling for 15min at the rotation speed of 200r/min, drying, crushing, sieving with a 100-mesh sieve, and roasting at the temperature of 1500 ℃ for 1h to obtain composite powder;
and step B3: dispersing the composite powder in deionized water, adding KH560, stirring at a rotation speed of 600r/min and a temperature of 85 ℃ for 1h, filtering to remove filtrate, and dispersing a substrate in deionized water to obtain a treatment solution.
The mass ratio of the graphite microchip, the nano boron nitride, the alumina and the ethanol in the step B2 is 3.
The dosage of KH560 in the step B3 is 5% of the composite powder, and the dosage ratio of the substrate to the deionized water is 1g.
Example 2
An efficient acid-free pretreatment process for a tire bead wire specifically comprises the following steps:
step S1: grinding the tire bead steel wire by using No. 300 abrasive paper, and then grinding by using No. 1000 abrasive paper to obtain a polished steel wire;
step S2: soaking the polished steel wire in the degreasing agent for 55s at the temperature of 35 ℃ to obtain a degreased steel wire;
and step S3: soaking the degreased steel wire in a surface treating agent for 1.5h at the temperature of 55 ℃, taking out the steel wire until no liquid drops drop, and preserving heat for 1.5h at the temperature of 115 ℃ to obtain a pretreated steel wire;
and step S4: soaking the pretreated steel wire in the treatment solution, adding a sodium hydroxide solution until the pH value is 10, carrying out ultrasonic treatment for 25min under the conditions of the frequency of 40kHz and the temperature of 45 ℃, taking out the steel wire and drying to obtain the tire bead steel wire.
The degreasing agent in the step S2 is prepared from the following components: 6g/L of sodium carbonate, 6g/L of sodium metasilicate pentahydrate, 5g/L of sodium gluconate, 6g/L of 4A zeolite, 2g/L of sodium nitrite and 5g/L of lauryl alcohol polyoxyethylene ether, and the solvent is water.
The mass fraction of the sodium hydroxide solution in the step S4 is 150%.
The surface treating agent is prepared by the following steps:
step A1: dissolving 2, 2-dimethylolpropionic acid in deionized water, adding sodium hydroxide, stirring for 10min at the rotation speed of 500r/min and the temperature of 35 ℃, adding epoxy chloropropane, reacting for 4h, adjusting the pH value of reaction liquid to 6.5 to prepare an intermediate 1, uniformly mixing the intermediate 1, 2-thiophenemethylamine and methanol, carrying out reflux reaction for 13h at the temperature of 70 ℃, and distilling to remove the methanol to prepare an intermediate 2;
step A2: uniformly mixing the intermediate 2, 2-aminobenzimidazole, 1-hydroxybenzotriazole and tetrahydrofuran, reacting for 7 hours at the rotation speed of 200r/min and the temperature of 45 ℃ to obtain an intermediate 3, uniformly mixing the intermediate 3, acrylic acid, p-toluenesulfonic acid and DMF, and reacting for 9 hours at the rotation speed of 180r/min and the temperature of 125 ℃ to obtain an intermediate 4;
step A3: mixing the intermediate 4, p-amino styrene, ethyl acrylate, acrylic acid and deionized water to obtain a monomer solution, adding 1/10 of the monomer solution into an emulsifier, stirring and adding a potassium persulfate aqueous solution under the conditions of a rotation speed of 180r/min and a temperature of 70 ℃, reacting for 35min, adding the rest of the monomer solution, and reacting for 2.5h to obtain the surface treating agent.
The molar ratio of the 2, 2-dimethylolpropionic acid to the epichlorohydrin in the step A1 is 1.
The molar ratio of the intermediate 2, the 2-aminobenzimidazole and the 1-hydroxybenzotriazole in the step A2 is 1.
The use amount ratio of the intermediate 4, the p-amino styrene, the ethyl acrylate, the acrylic acid and the deionized water in the step A3 is 8g.
The treatment liquid is prepared by the following steps:
step B1: expanding expandable graphite at 930 ℃ for 20s at high temperature, adding the expanded expandable graphite into deionized water, carrying out ultrasonic treatment for 1h at the frequency of 35kHz and the temperature of 55 ℃, filtering and drying to obtain graphite micro-sheets;
and step B2: mixing graphite micro-sheets, nano boron nitride, alumina and ethanol, ball-milling for 20min at the rotation speed of 200r/min, drying and crushing, sieving by a 100-mesh sieve, and roasting for 1h at the temperature of 1550 ℃ to obtain composite powder;
and step B3: dispersing the composite powder in deionized water, adding KH560, stirring for 1.5h at 85 ℃ at a rotation speed of 800r/min, filtering to remove filtrate, and dispersing a substrate in deionized water to obtain a treatment solution.
The mass ratio of the graphite microchip, the nano boron nitride, the alumina and the ethanol in the step B2 is 3.
The dosage of KH560 in the step B3 is 6% of the composite powder, and the dosage ratio of the substrate to the deionized water is 1g.
Example 3
An efficient acid-free pretreatment process for a tire bead wire specifically comprises the following steps:
step S1: grinding the bead wire by using No. 300 abrasive paper, and then grinding by using No. 1000 abrasive paper to obtain a polished steel wire;
step S2: soaking the polished steel wire in the degreasing agent for 60s at the temperature of 40 ℃ to obtain a degreased steel wire;
and step S3: soaking the degreased steel wire in a surface treating agent for 2 hours at the temperature of 60 ℃, taking out the steel wire until no liquid drops drop, and preserving heat for 2 hours at the temperature of 120 ℃ to obtain a pretreated steel wire;
and step S4: soaking the pretreated steel wire in the treatment solution, adding a sodium hydroxide solution until the pH value is 11, carrying out ultrasonic treatment for 30min under the conditions that the frequency is 50kHz and the temperature is 50 ℃, taking out the steel wire and drying to obtain the tire bead steel wire.
The degreasing agent in the step S2 is prepared from the following components: 8g/L of sodium carbonate, 8g/L of sodium metasilicate pentahydrate, 6g/L of sodium gluconate, 8g/L of 4A zeolite, 3g/L of sodium nitrite and 6g/L of lauryl alcohol polyoxyethylene ether, and the solvent is water.
The mass fraction of the sodium hydroxide solution in the step S4 is 150%.
The surface treating agent is prepared by the following steps:
step A1: dissolving 2, 2-dimethylolpropionic acid in deionized water, adding sodium hydroxide, stirring for 15min at the rotation speed of 500r/min and the temperature of 40 ℃, adding epoxy chloropropane, reacting for 5h, adjusting the pH value of reaction liquid to 6.5 to prepare an intermediate 1, uniformly mixing the intermediate 1, 2-thiophenemethylamine and methanol, carrying out reflux reaction for 15h at the temperature of 70 ℃, and distilling to remove the methanol to prepare an intermediate 2;
step A2: uniformly mixing the intermediate 2, 2-aminobenzimidazole, 1-hydroxybenzotriazole and tetrahydrofuran, reacting for 8 hours at the rotation speed of 300r/min and the temperature of 50 ℃ to obtain an intermediate 3, uniformly mixing the intermediate 3, acrylic acid, p-toluenesulfonic acid and DMF, and reacting for 10 hours at the rotation speed of 200r/min and the temperature of 130 ℃ to obtain an intermediate 4;
step A3: mixing the intermediate 4, p-aminostyrene, ethyl acrylate, acrylic acid and deionized water to obtain a monomer solution, adding 1/10 mass of the monomer solution into an emulsifier, stirring and adding a potassium persulfate aqueous solution under the conditions of a rotation speed of 200r/min and a temperature of 70 ℃, reacting for 40min, adding the rest of the monomer solution, and reacting for 3h to obtain the surface treating agent.
The molar ratio of 2, 2-dimethylolpropionic acid to epichlorohydrin in step A1 is 1.
The molar ratio of the intermediate 2, the 2-aminobenzimidazole and the 1-hydroxybenzotriazole in the step A2 is 1.
The use amount ratio of the intermediate 4, the p-amino styrene, the ethyl acrylate, the acrylic acid and the deionized water in the step A3 is 8g.
The treatment liquid is prepared by the following steps:
step B1: expanding expandable graphite at 950 ℃ for 20s at high temperature, adding the expanded graphite into deionized water, carrying out ultrasonic treatment for 1.5h at the frequency of 40kHz and the temperature of 60 ℃, filtering and drying to obtain graphite micro-sheets;
and step B2: mixing graphite micro-sheets, nano boron nitride, alumina and ethanol, ball-milling for 20min at the rotation speed of 300r/min, drying and crushing, sieving by a 100-mesh sieve, and roasting at the temperature of 1600 ℃ for 1.5h to prepare composite powder;
and step B3: dispersing the composite powder in deionized water, adding KH560, stirring at the rotation speed of 800r/min and the temperature of 90 ℃ for 1.5h, filtering to remove filtrate, and dispersing a substrate in deionized water to obtain a treatment solution.
The mass ratio of the graphite microchip, the nano boron nitride, the alumina and the ethanol in the step B2 is 3.
The dosage of the KH560 in the step B3 is 8% of the composite powder, and the dosage ratio of the substrate to the deionized water is 1g.
Comparative example 1
The comparative example was conducted in the same manner as in example 1 without using the treating solution.
Comparative example 2
This comparative example compared with example 1 using thiobenzothiazole in place of the surface treatment agent and was not treated with the treatment liquid.
According to the method of GB/T10124-1988, the bead wires treated in the examples 1-3 and the comparative examples 1-2 are weighed, then soaked in 20mg/L sulfuric acid solution, soaked for 12 hours at the temperature of 25 ℃, taken out, washed by 6 mass percent sodium hydroxide solution and deionized water in sequence, dried and weighed, and the corrosion speed and the corrosion inhibition rate are calculated, and the results are shown in the following table;
Figure BDA0003914570370000121
from the above table, it can be seen that the bead wire treated by the present invention has a good corrosion resistance.
The foregoing is merely exemplary and illustrative of the principles of the present invention and various modifications, additions and substitutions of the specific embodiments described herein may be made by those skilled in the art without departing from the principles of the present invention or exceeding the scope of the claims set forth herein.

Claims (10)

1. The high-efficiency acid-free pretreatment process of the tire bead steel wire is characterized in that: the method specifically comprises the following steps: the method specifically comprises the following steps:
step S1: grinding the tire bead steel wire by using abrasive paper to obtain a polished steel wire;
step S2: soaking the polished steel wire in a degreasing agent to obtain a degreased steel wire;
and step S3: soaking the degreased steel wire in a surface treating agent, soaking, and keeping the temperature and drying to obtain a pretreated steel wire;
and step S4: and soaking the pretreated steel wire in the treatment solution, performing ultrasonic treatment, taking out the steel wire, and drying to obtain the tire bead steel wire.
2. The process for efficient acid-free pretreatment of bead wires according to claim 1, characterized in that: the degreasing agent in the step S2 is prepared from the following components: 5-8g/L of sodium carbonate, 5-8g/L of sodium metasilicate pentahydrate, 4-6g/L of sodium gluconate, 5-8g/L of 4A zeolite, 1-3g/L of sodium nitrite and 4-6g/L of lauryl alcohol polyoxyethylene ether, and the solvent is water.
3. The process for efficient acid-free pretreatment of bead wires according to claim 1, characterized in that: the mass fraction of the sodium hydroxide solution in the step S4 is 150%.
4. The process for efficient acid-free pretreatment of bead wires according to claim 2, characterized in that: the surface treating agent is prepared by the following steps:
step A1: dissolving 2, 2-dimethylolpropionic acid in deionized water, adding sodium hydroxide, stirring, adding epoxy chloropropane, reacting to obtain an intermediate 1, mixing the intermediate 1, 2-thiophenemethylamine and methanol, performing reflux reaction, and distilling to remove methanol to obtain an intermediate 2;
step A2: mixing the intermediate 2, 2-aminobenzimidazole, 1-hydroxybenzotriazole and tetrahydrofuran for reaction to prepare an intermediate 3, and mixing the intermediate 3, acrylic acid, p-toluenesulfonic acid and DMF for reaction to prepare an intermediate 4;
step A3: mixing the intermediate 4, p-aminostyrene, ethyl acrylate, acrylic acid and deionized water to obtain a monomer solution, adding 1/10 mass of the monomer solution into an emulsifier, stirring, adding a potassium persulfate aqueous solution, reacting, adding the rest of the monomer solution, and reacting to obtain the surface treating agent.
5. A process for efficient acid-free pre-treatment of bead wires according to claim 4, characterized in that: the molar ratio of 2, 2-dimethylolpropionic acid to epichlorohydrin in step A1 is 1.
6. A process for efficient acid-free pretreatment of bead wires according to claim 4, characterized in that: the molar ratio of the intermediate 2, the 2-aminobenzimidazole and the 1-hydroxybenzotriazole in the step A2 is 1.
7. A process for efficient acid-free pretreatment of bead wires according to claim 4, characterized in that: the intermediate 4, the p-amino styrene, the ethyl acrylate, the acrylic acid and the deionized water in the step A3 have a use ratio of 8g to 15 g to 1 g.
8. The process for efficient acid-free pretreatment of bead wires according to claim 1, characterized in that: the treatment liquid is prepared by the following steps:
step B1: after the expandable graphite is expanded at high temperature, adding the expandable graphite into deionized water, carrying out ultrasonic treatment, filtering and drying to obtain graphite micro-sheets;
and step B2: mixing and ball-milling graphite micro-sheets, nano boron nitride, alumina and ethanol, drying, crushing and roasting to prepare composite powder;
and step B3: dispersing the composite powder in deionized water, adding KH560, stirring, filtering to remove filtrate, and dispersing the substrate in deionized water to obtain the treatment solution.
9. The process for efficient acid-free pretreatment of bead wires according to claim 8, characterized in that: the mass ratio of the graphite microchip, the nano boron nitride, the alumina and the ethanol in the step B2 is 3.
10. The process for efficient acid-free pretreatment of bead wires according to claim 8, characterized in that: the dosage of KH560 in the step B3 is 5-8% of the composite powder, and the dosage ratio of the substrate to the deionized water is 1g.
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