EP2291453A2 - Formaldehydfreies schleiferzeugnis - Google Patents

Formaldehydfreies schleiferzeugnis

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Publication number
EP2291453A2
EP2291453A2 EP09750049A EP09750049A EP2291453A2 EP 2291453 A2 EP2291453 A2 EP 2291453A2 EP 09750049 A EP09750049 A EP 09750049A EP 09750049 A EP09750049 A EP 09750049A EP 2291453 A2 EP2291453 A2 EP 2291453A2
Authority
EP
European Patent Office
Prior art keywords
oil
abrasive article
article according
resin composition
unsaturated
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.)
Withdrawn
Application number
EP09750049A
Other languages
English (en)
French (fr)
Inventor
Alix Arnaud
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.)
Saint Gobain Abrasifs Technologie et Services SAS
Saint Gobain Abrasives Inc
Original Assignee
Saint Gobain Abrasifs Technologie et Services SAS
Saint Gobain Abrasives Inc
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 Saint Gobain Abrasifs Technologie et Services SAS, Saint Gobain Abrasives Inc filed Critical Saint Gobain Abrasifs Technologie et Services SAS
Publication of EP2291453A2 publication Critical patent/EP2291453A2/de
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L61/00Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24DTOOLS FOR GRINDING, BUFFING OR SHARPENING
    • B24D3/00Physical features of abrasive bodies, or sheets, e.g. abrasive surfaces of special nature; Abrasive bodies or sheets characterised by their constituents
    • B24D3/02Physical features of abrasive bodies, or sheets, e.g. abrasive surfaces of special nature; Abrasive bodies or sheets characterised by their constituents the constituent being used as bonding agent
    • B24D3/20Physical features of abrasive bodies, or sheets, e.g. abrasive surfaces of special nature; Abrasive bodies or sheets characterised by their constituents the constituent being used as bonding agent and being essentially organic
    • B24D3/28Resins or natural or synthetic macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L91/00Compositions of oils, fats or waxes; Compositions of derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L97/00Compositions of lignin-containing materials
    • C08L97/02Lignocellulosic material, e.g. wood, straw or bagasse

Definitions

  • the present invention relates to an abrasive article which is made from a liquid resin composition containing no formaldehyde.
  • Abrasive articles in general contain a multitude of abrasive grains securely bonded to a carrier or to each other via a binder. These articles are widely used for the machining of various materials, especially in cutting, grinding, deburring and polishing operations. Conventionally, abrasive coated abrasives and abrasive bonded abrasives are distinguished.
  • the abrasives applied comprise a support material, generally flexible, on the surface of which are distributed abrasive grains embedded in a binder.
  • the flexible support may be a sheet of paper, a film or a network of fibers, for example a mat, a felt, a fabric or a knit of natural or synthetic fibers, in particular made of glass or a polymer.
  • abrasives can adopt various forms: sheets, strips, discs, ...
  • the manufacture of the coated abrasives comprises the application of a base coat ("make coat") on the support material, the distribution of the grains of abrasives on said layer, the heat treatment of the base adhesive layer in order to partially harden it and the application of a superior adhesive layer ("size coat") which guarantees a firm anchoring of the grains on the support.
  • An additional adhesive layer (“supersize coat”) may be deposited on the upper adhesive layer and the abrasive grains.
  • the base, top and extra adhesive layers are applied in liquid form. They generally consist of a thermosetting resin, in particular a phenol-formaldehyde resin of the resol type or a urea-formaldehyde resin.
  • the agglomerated abrasives consist of abrasive grains bonded together by a binder which provides a three-dimensional structure adapted to ensure the abrasion operations, including the cutting of hard materials such as steel.
  • these abrasives have the appearance of a grinding wheel, a grinding wheel segment and a whetstone.
  • Agglomerated abrasives in the form of "conventional" grinding wheels are most often made of a single region composed of abrasive grains embedded in the binder extending from the bore to the periphery of the grinding wheel.
  • the abrasion region may be at the periphery, in the form of a strip supported by a central core generally of metal, and the abrasive grains consist of a very hard material, for example diamond or cubic boron nitride.
  • Agglomerated abrasives are obtained by the process using compression molding techniques, cold or hot.
  • cold compression molding (“CoId Molding
  • Compression the mixture of constituents of the abrasive, in granular form, is introduced into a mold, then a sufficient compressive force is applied, of the order of 15 to 25 N / mm 2 , to bring said mixture to the shape of the mold and ensure that after extraction of the mold, the piece obtained (green part or "green item") has sufficient strength to be manipulated without losing its original shape.
  • the part is then heated in an oven at a temperature to crosslink the binder, this temperature being dependent in particular on the nature of the binder used.
  • Hot compression molding achieves a higher compaction level than cold molding, which results in a smaller pore volume in the final article.
  • the granular mixture introduced into the mold is compacted under pressure and heated simultaneously in order to allow the binder to be better distributed between the abrasive grains and to occupy the empty spaces.
  • the part After being removed from the mold, the part generally undergoes a post-crosslinking heat treatment to improve its operating life and abrasion performance.
  • the mixture of abrasive constituents is usually used in granular form.
  • the granular mixture is prepared by first treating the abrasive grains with a liquid impregnating resin, usually a phenolic resole resin, and then mixing the wet grains with a resin powder, for example a phenolic resin of novolac type, containing a crosslinking agent - powder which will subsequently constitute the binder itself - if necessary additives which are generally also in powder form.
  • a resin powder for example a phenolic resin of novolac type, containing a crosslinking agent - powder which will subsequently constitute the binder itself - if necessary additives which are generally also in powder form.
  • the resulting mixture thus consists of abrasive grains on the surface of which are adhered solid particles of resin and additives. This mixture has a good ability to be uniformly distributed in the mold (called "flowability") and to be shaped under the effect of pressure.
  • thermosetting resins used in the manufacture of coated abrasives and agglomerated abrasives have many advantages in the intended conditions of use, including:
  • Urea-formaldehyde thermosetting resins make it possible to effectively bond the abrasive grains and crosslink at a relatively low temperature which generally does not exceed 100 0 C.
  • WO 2005/108454 A1 discloses a novolac resin and non-formaldehyde hardener composition for reinforcing composite materials.
  • a polymerizable abrasive composition which comprises an aminoplast resin and a reactive diluent which each contain pendant unsaturated groups.
  • US 5,178,646 discloses a binder precursor composition for abrasives, especially coated, which comprises a heat-curable resin having a plurality of pendant methylol groups and a reactive diluent having at least one functional group that reacts with the groups of the resin.
  • the object of the present invention is to provide an abrasive article, applied or agglomerated, which is obtained from a liquid resin composition free of formaldehyde, thus making it possible to have an alternative to resin compositions based on resoles or urea resin. -formaldehyde.
  • the invention proposes to replace the resol or the urea-formaldehyde resin used as an adhesive in the coated abrasives and the resole used as impregnating resin in the agglomerated abrasives with a liquid resin composition which comprises a product resulting from the oxidative cleavage of an unsaturated oil, plant or animal, selected from aldehydes, peroxides and mixtures of these compounds.
  • the product resulting from the oxidative cleavage of an unsaturated oil, plant or animal can be obtained by a process comprising a step of oxidation of the double bonds of the oil followed by a step of cleavage of the oxidation products to form aldehydes and / or peroxides.
  • Examples of vegetable oil include wood oil, including tung oil, sunflower oil, cottonseed oil, palm oil, corn oil, mono-, di- and triglyceride oils such as rapeseed oil, linseed oil, soybean oil, olive oil, castor oil, mustard oil and peanut oil, and phenolic oils such as cashew nut oil.
  • the oil chosen is rapeseed oil.
  • animal oils that may be mentioned include herring oil, sardine oil, whale oil, tallow, especially beef, and lard.
  • the oil may consist of one or more vegetable or animal oils, and a mixture of these oils.
  • the first step of oxidation of the oil can be carried out by any oxidative method for cleaving the unsaturated bonds to form aldehydes and / or peroxides, for example by ozonolysis or using hydrogen peroxide, advantageously associated with a catalyst such as ferrous ions and salts of oxidizing metals.
  • the oxidation is carried out by ozonolysis.
  • the oxidation products formed are subjected to cleavage to form aldehydes and / or peroxides, and optionally hemiacetals of these aldehydes in the case where the cleavage is carried out in the presence of an alcohol.
  • the conditions necessary to obtain the cleavage of the oxidation products are well known to those skilled in the art; preferably the cleavage is conducted under reducing conditions, for example using a metal such as zinc, advantageously associated with an acid such as acetic acid (see EP-A-1 198 443).
  • the product resulting from the oxidative cleavage is chosen from aldehydes.
  • the product resulting from the oxidative cleavage of the unsaturated oil represents at least 40% by weight of the liquid resin composition, preferably at least 50%, advantageously at least 60% and more preferably at least 65%.
  • the liquid resin composition may further comprise a compound containing at least one hydroxy functional group capable of reacting with the product resulting from the oxidative cleavage of the unsaturated oil. For reasons of simplification, this compound is called "hydroxylated compound".
  • the hydroxylated compound may be chosen from hydroxylated phenolic compounds, substituted or unsubstituted by at least one saturated or unsaturated C 1 -C 15 hydrocarbon group, for example phenol, resorcinol, catechol, hydroxyquinone, phloroglucinol, cardol, cardanol and methylcardol, furanemethanols, for example 2-furanemethanol (or furfurol), and mixtures of these compounds.
  • Natural products, in particular of plant origin, which include the hydroxy compound are within the scope of the present invention.
  • the hydroxylated compound may also be chosen from novolacs.
  • Novolaks are known to those skilled in the art and are obtained by condensation of a phenolic compound and an aldehyde in an aldehyde / phenol compound molar ratio of less than 1, in the presence of an acid catalyst.
  • the phenolic compound used in the constitution of the novolak is chosen from phenol and substituted phenols such as cresols, guaiacol, methoxyphenols, catechol, resorcinol, tert-butylphenol and nonylphenol, and bisphenols such as bisphenol A, naphthols and mixtures of these compounds.
  • the phenol is selected.
  • the aldehyde used in the constitution of the novolak is chosen from alicyclic aldehydes such as formaldehyde, cyclic aldehydes such as furfural, aromatic aldehydes such as benzaldehyde, para-anisaldehyde, ortho-anisaldehyde and veratraldehyde. , and mixtures of these aldehydes.
  • the formaldehyde is chosen.
  • the formaldehyde / phenol molar ratio ranges from 0.2 to less than 1, preferably from 0.35 to 0.9 and more preferably from 0.5 to 0.9.
  • the novolac may be prepared using a known acid catalyst, for example a strong mineral acid such as sulfuric acid, phosphoric acid and hydrochloric acid, or an organic acid such as oxalic acid, salicylic acid or anhydrides such as maleic anhydride.
  • the amount of acid should be sufficient to allow the condensation of the phenolic compound and the aldehyde.
  • the amount of acid used generally represents 0.02 to 1% by weight of the starting phenolic compound, preferably 0.1 to 0.6% in the case of a strong mineral acid, and 0.3 to 3% by weight. weight of the starting phenolic compound in the case of an organic acid.
  • the novolac obtained at the end of the condensation is preferably treated so as to reduce the content of free phenolic compound, for example by distillation under reduced pressure.
  • the novolak has a softening temperature less than or equal to 120 ° C.
  • the hydroxyl compound contains at least two hydroxy functions.
  • the most preferred hydroxyl compounds are resorcinol, cashew nut oil and novolaks.
  • the amount of hydroxyl compound present in the liquid resin composition may be up to 95% by weight of the compound resulting from the oxidative cleavage of unsaturated oil, preferably up to 50% and preferably up to 45%.
  • the liquid resin composition may also comprise an acidic or basic catalyst whose function is to adjust the starting temperature of crosslinking of the resin.
  • the acidic catalyst may be chosen in particular from sulphonic acids, in particular substituted aromatic sulphonic acids such as para-toluene sulphonic acid.
  • the basic catalyst may be chosen in particular from alkali metal hydroxides and alkaline earth metal hydroxides, preferably sodium hydroxide.
  • the quantity of catalyst introduced into the liquid resin composition may represent up to 10% of the weight of the oxidative cleavage product of the unsaturated oil, preferably at least equal to 0.15%, advantageously from 0.3 to 9% by weight. , 5% and better still ranges from 0.4 to 9%.
  • the introduction of a quantity of catalyst varying from 0.4 to 4% makes it possible to obtain a pot life of the liquid resin composition of the order of 8 to 48 hours.
  • the liquid resin composition may also comprise an amino compound whose function is to increase the rate of crosslinking of the resin composition.
  • the amino compound contains at least one primary or secondary amine function.
  • urea ethylene urea, thiourea, melamine, dicyandiamide, carbohydrazide and acetoacetamide.
  • urea is selected.
  • the amount of amino compound in the resin composition may represent up to 20% of the weight of the product resulting from the oxidative cleavage of the unsaturated oil, preferably up to 17% and advantageously up to 15%.
  • the viscosity of the liquid resin composition depends on the intended application but remains below or equal to 7000 mPa.s, measured at 25 ° C.
  • the liquid resin composition is used to produce coated abrasives.
  • the liquid resin composition comprises the product resulting from the oxidative cleavage of an unsaturated oil and the hydroxyl compound which react during the heat treatment to form a crosslinked product.
  • the amount of hydroxylated compound in the resin composition is at least 5% by weight of the product resulting from the oxidative cleavage of unsaturated oil, preferably at least 10%, and preferably at least 15%.
  • the resin composition contains at least 0.7% by weight of urea relative to the weight of product resulting from the oxidative cleavage of an unsaturated oil and hydroxylated compound, and preferably at least 2%.
  • the resin composition comprises at least 0.15% by weight of catalyst relative to the weight of the product resulting from the oxidative cleavage of an unsaturated oil and hydroxylated compound, preferably at least 0.3%, and advantageously to less 0.4%.
  • the manufacture of the coated abrasives comprises the steps of depositing a base coat ("make coat") on a support material, distributing the grains of abrasives on said layer, subjecting said material to a heat treatment allowing partially cross-linking the resin composition, depositing a top adhesive layer ("size coat”) and subjecting the heat-treated coated material to obtain complete crosslinking of the resin composition. If necessary, an additional adhesive layer may be deposited on the upper adhesive layer and crosslinked by a suitable heat treatment.
  • the support material generally has a moderate to strong flexibility, and may have the appearance of a sheet, especially paper, a film, in particular polymer, or a more or less dense network of natural or synthetic fibers, for example glass fibers and vulcanized fibers.
  • the abrasive grains may be chosen from known grains, for example made of alumina, including sintered aluminas and sintered aluminas obtained by sol-gel, seeded or not with a material of the same crystalline nature, chemically modified or not, d. iron oxide, molybdenum oxide, vanadium oxide, alumina-zirconia, boron-alumina, silicon carbide, aluminum-oxynitride, diamond or cubic boron nitride, and mixtures of such grains.
  • the abrasive grains are alumina.
  • the application of the grains on the base adhesive layer can be done by the usual techniques operating by gravity or electrostatically.
  • the density of the abrasive grains on the support is to be chosen according to the intended application.
  • the liquid resin composition used in the context of the invention can be used to form the base adhesive layer ("make coat"), the upper adhesive layer ("size coat”) or the additional adhesive layer (“supersize coat”).
  • the liquid resin composition serves to form the base adhesive layer and the upper adhesive layer, and optionally the additional adhesive layer.
  • the liquid resin composition has a viscosity of less than or equal to 6000 mPa.s, measured at 25 ° C.
  • the liquid resin composition may further comprise additives, for example wetting agents, fillers, coupling agents, dyes, pigments and antistatic agents.
  • the liquid resin composition When used to form the upper adhesive layer and / or the additional adhesive layer, it advantageously comprises at least one agent which enhances the abrasive performance of the final abrasive.
  • an agent can be chosen from waxes, halogenated organic compounds, halogen salts, metals and metal alloys.
  • the heat treatment of the support material coated with the liquid resin composition forming the base adhesive layer is generally carried out at a temperature of less than or equal to 150 ° C., preferably less than or equal to 120 ° C. for 1 to 120 minutes, preferably 1 to 60 minutes.
  • the heat treatment for crosslinking the resin composition forming the upper adhesive layer or the additional adhesive layer may be at a temperature of less than or equal to 150 ° C., preferably less than or equal to 120 ° C. for not more than 36 hours, preference at most
  • the abrasives applied according to the invention may be in the form of sheets, strips or discs.
  • the aforementioned liquid resin composition is used to manufacture agglomerated abrasives.
  • the liquid resin composition comprises the product resulting from the oxidative cleavage of an unsaturated oil and optionally the hydroxylated compound.
  • the presence of the hydroxyl compound as described above for the coated abrasives is not mandatory when the solid resin contains functional groups capable of reacting with the product resulting from the oxidative cleavage of an unsaturated oil.
  • the liquid resin composition is first mixed with abrasive grains in a conventional mechanical mixer until the grains are suitably "wetted”, i.e., coated with the resinous composition, and then the binder powder and the additives, also in powder form, until a homogeneous granular mixture is obtained.
  • the liquid resin composition has a viscosity at most equal to 3000 mPa.s, and advantageously greater than or equal to 600 mPa.s.
  • the time required to obtain complete crosslinking of the resin composition in the granular mixture is less than or equal to 36 hours, preferably less than or equal to 20 hours, at temperatures which range between 100 and 200 ° C.
  • the abrasive grains may be any type of abrasive grains already mentioned which form part of the abrasives applied.
  • the abrasive grains are pretreated with an organic compound which improves the adhesion between the grain and the composition liquid resin chosen from compounds containing silicon, for example a silane functionalized with organic groups such as vinylsilane, in particular vinyltriethoxysilane, an aminosilane, in particular gamma-aminopropyltrimethoxysilane, gamma-aminopropylthethoxysilane and diaminopropylethoxysilane, or an epoxysilane.
  • gamma-aminopropyltriethoxysilane is used.
  • the treatment of the abrasive grains with the organic compound containing silicon can be carried out for example by spraying a solution of said compound in a suitable solvent or by dispersing the grains in the aforementioned solution.
  • the treated abrasive grains are dried before being mixed with the liquid resin composition.
  • a liquid organic carrier can be added to the abrasive grain mixture and the resinous composition, which aids in grain wetting and the formation of a uniform grain network, and which is subsequently removed in the course of time. crosslinking step.
  • the organic vehicle may especially be water, an aliphatic alcohol, a glycol, high molecular weight oil fractions of oily or waxy consistency, a mineral oil or any other known vehicle.
  • the binder may be for example a phenol-aldehyde, melamine-aldehyde, urea-aldehyde, polyester, polyimide, epoxy, polyurethane or polybenzimidazole resin.
  • the binder is a resin with a low level of formaldehyde, advantageously a phenol-aldehyde resin of the novolac type, and better still a novolac phenol-formaldehyde resin.
  • the additives are, for example, fillers, crosslinking agents and other compounds which are useful for the manufacture of agglomerated abrasives, in particular bound by an organic resin.
  • the fillers are generally in the form of a finely divided powder comprising particles that may have the appearance of granules, spheres or fibers.
  • sand silicon carbide
  • alumina hollow spheres bauxite
  • chromites magnesite
  • dolomites hollow mullite spheres
  • borides silica fume, titanium dioxide, carbon products (carbon black, coke, graphite, ...), wood flour, clay, talc, hexagonal boron nitride, molybdenum disulfide, feldspar, nepheline syenite and the glass, especially in the form of solid, hollow or hollow beads, and fibers.
  • the fillers represent 0.1 to 30% by weight of the granular mixture.
  • the crosslinking agents may be used when the powder binder is in particular a novolac resin. They may be chosen from compounds known to perform the aforementioned function such as hexamethylenetetramine or precursors thereof.
  • the crosslinking agent is added at a rate of at most 20 parts by weight per 100 parts by weight of novolac resin powder.
  • the additives may further comprise agents which assist in the implementation of the process, for example anti-static agents and lubricants.
  • the granular mixture is subjected to a maturing treatment at room temperature for a period of up to 12 hours.
  • the granular mixture is then introduced into a mold equipped with compression means for forming a green part which has sufficient cohesion to be handled and processed in the following steps without substantially changing its shape.
  • the binder at this stage is in the uncrosslinked state.
  • the green part is then heated to a temperature sufficient for the binder to crosslink and give a rigid polymeric network which gives the piece its final shape.
  • the crosslinking can be carried out according to a conventional baking cycle, which consists in bringing the green part to a temperature of the order of 100 ° C. and keeping it at this temperature for 30 minutes to several hours so that the volatile products formed can be evacuated.
  • the room is heated to the final temperature over a period that generally ranges from 10 to 36 hours.
  • the final crosslinking temperature depends in particular on the nature of the resin used, the size and shape of the piece to be treated and the cooking time. In general, the final crosslinking temperature is between 100 and 200 ° C.
  • the thermal crosslinking can be carried out in a controlled atmosphere, preferably with a maximum relative humidity level.
  • the agglomerated abrasives according to the invention may be in the form of grinding wheels, segments of grinding wheels, discs, sharpening stones and articles of any shape and size depending on the intended application.
  • the invention is concerned with agglomerated abrasives which are intended to be implemented in the presence of water, in particular for the machining of metals, in particular steel and aluminum.
  • the crosslinked binder of this type of abrasive has a significant hydrolytic resistance in order to maintain good mechanical properties when it is used in the presence of water, especially in terms of Young's modulus and maximum breaking strength as explained in the examples.
  • liquid resin compositions and coated and agglomerated abrasives are measured under the following conditions:
  • DMA Dynamic Mechanical Analysis
  • peeling The abrasion resistance of abrasive grains (“peeling") is measured as follows: a layer of liquid resin 150 ⁇ m thick is deposited on a cotton or polyester support (15 cm ⁇ 2.5 cm) thickness, and then dust the grains of abrasives. The support is introduced into an oven and heated according to the following temperature cycle:
  • Resin compositions having the composition given in Table 1 are prepared by mixing the aldehydes of RSO and resorcinol, and then adding the catalyst and urea.
  • Liquid resin compositions whose composition is given in Table 2 are also prepared by mixing the aldehydes of RSO and the cashew nut oil (CNSL) or a novolac, possibly furfurol, and then adding the catalyst and urea.
  • the aldehydes of RSO (“Grater Seed OiI" in English) are triglyceride aldehydes obtained by ozonolysis of rapeseed oil under the conditions of Example 1 of Patent EP 1 198 443 A1.
  • Novolacs are sold under the reference Bakelite ® PF5885 (softening temperature: 50-60 0 C) and Bakelite ® PF8505 (softening temperature of the order of 40 0 C) by the company HEXION SPECIALTY CHEMICALS.
  • liquid resin compositions of Examples 1 to 8, 11 and 13-29 and a conventional resin composition, denoted by Reference 1 are applied separately on glass slides to using a filmograph so as to form a layer 200 microns thick.
  • make coat On this layer which serves as a base coat ("make coat") are deposited grains of alumina abrasives (sold under the reference Alumina 57A grit 60 or grit 16 by the company SAINT-GOBAIN CERAMICS AND PLASTICS) and eliminates the excess of grains having not adhered to the layer.
  • alumina abrasives sold under the reference Alumina 57A grit 60 or grit 16 by the company SAINT-GOBAIN CERAMICS AND PLASTICS
  • the glass slides are heated according to the following temperature cycle:
  • the resinous liquid compositions of Examples 1 to 15 have a cross-linking start temperature of at most 160 ° C. (Example 7).
  • the crosslinking start temperature can be decreased by adding urea in the resin compositions (Examples 6 and 7, Examples 8 to 10).
  • the abrasive grains are grains of alumina (marketed under the reference Alumina 57A grit 60 by the company SAINT-GOBAIN CERAMICS AND PLASTICS) treated under the following conditions:
  • RSO aldehydes are triglyceride aldehydes obtained by ozonolysis of rapeseed oil under the conditions of example 1 of patent EP 1 198 443 A1.
  • the resole is a phenol-formaldehyde resole (Bakelite ® sold under the reference 0433SW07 by Hexion Specialty Chemicals).
  • the solid resin is a novolac resin which contains 6.5% by weight hexamine (marketed under the reference Bakelite ® PF8686 by Hexion Specialty Chemicals).
  • the abrasive grains are mixed with the liquid resin composition until the grains are "wetted" uniformly, then the solid resin is added and the mixing conditions are maintained for a time sufficient to obtain a homogeneous granular mixture. The mixture undergoes a ripening step for 6 hours and is sieved (10-18 mesh).
  • test pieces are obtained by molding under cold pressure 75.64 g of the granular mixture obtained under b) in a mold of dimensions 10.224 cm ⁇ 2.591 cm ⁇ 1.27 cm.
  • the green test pieces are removed from the mold, sealed in an aluminum foil and cured in an oven according to the following temperature cycle: 25 to 60 ° C. in 10 minutes
  • test specimens have a pore volume equal to 33%, a grain volume equal to 52% and a binder volume (liquid resin + solid resin composition) equal to 15%. These test specimens are separated into two series: the first series undergoes no treatment, the second series is immersed in boiling water for 150 minutes to simulate the conditions of accelerated aging.
  • R2 Young's modulus after treatment / Young's modulus without treatment.
  • test specimens made with the liquid resin composition according to the invention have ratios R1 and R2 greater than those of the test specimen of Reference 2, which indicates a better hydrolytic resistance.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Materials Engineering (AREA)
  • Polishing Bodies And Polishing Tools (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
EP09750049A 2008-05-06 2009-05-06 Formaldehydfreies schleiferzeugnis Withdrawn EP2291453A2 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0852992A FR2930948B1 (fr) 2008-05-06 2008-05-06 Composition resinique liquide sans formaldehyde pour articles abrasifs
PCT/FR2009/050841 WO2009141568A2 (fr) 2008-05-06 2009-05-06 Article abrasif sans formaldehyde

Publications (1)

Publication Number Publication Date
EP2291453A2 true EP2291453A2 (de) 2011-03-09

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EP09750049A Withdrawn EP2291453A2 (de) 2008-05-06 2009-05-06 Formaldehydfreies schleiferzeugnis

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Country Link
US (1) US8734551B2 (de)
EP (1) EP2291453A2 (de)
FR (1) FR2930948B1 (de)
WO (1) WO2009141568A2 (de)

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WO2025131235A1 (de) * 2023-12-18 2025-06-26 August Rüggeberg Gmbh & Co. Kg Schleifartikel

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5611825A (en) * 1992-09-15 1997-03-18 Minnesota Mining And Manufacturing Company Abrasive articles and methods of making same

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US4903440A (en) * 1988-11-23 1990-02-27 Minnesota Mining And Manufacturing Company Abrasive product having binder comprising an aminoplast resin
US5236472A (en) * 1991-02-22 1993-08-17 Minnesota Mining And Manufacturing Company Abrasive product having a binder comprising an aminoplast binder
US5178646A (en) 1992-01-22 1993-01-12 Minnesota Mining And Manufacturing Company Coatable thermally curable binder presursor solutions modified with a reactive diluent, abrasive articles incorporating same, and methods of making said abrasive articles
ATE138947T1 (de) * 1992-09-15 1996-06-15 Minnesota Mining & Mfg Beschichtete schleifmittel, hergestellt aus beschichtbaren harnstoff-aldehyd- zusammensetzungen, welche einen cokatalysator enthalten, und verfahren zu ihrer herstellung
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US8734551B2 (en) 2014-05-27
US20110113700A1 (en) 2011-05-19
FR2930948B1 (fr) 2013-07-12
FR2930948A1 (fr) 2009-11-13
WO2009141568A2 (fr) 2009-11-26
WO2009141568A3 (fr) 2010-04-08

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