WO2013132754A1 - 樹脂成形品の製造方法、樹脂組成物の製造方法、樹脂成形品、樹脂組成物、低発塵性樹脂粉末および樹脂の低発塵化方法 - Google Patents
樹脂成形品の製造方法、樹脂組成物の製造方法、樹脂成形品、樹脂組成物、低発塵性樹脂粉末および樹脂の低発塵化方法 Download PDFInfo
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- WO2013132754A1 WO2013132754A1 PCT/JP2013/000799 JP2013000799W WO2013132754A1 WO 2013132754 A1 WO2013132754 A1 WO 2013132754A1 JP 2013000799 W JP2013000799 W JP 2013000799W WO 2013132754 A1 WO2013132754 A1 WO 2013132754A1
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- molded product
- liquid paraffin
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/01—Hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L61/00—Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
- C08L61/04—Condensation polymers of aldehydes or ketones with phenols only
- C08L61/06—Condensation polymers of aldehydes or ketones with phenols only of aldehydes with phenols
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
- B29B7/90—Fillers or reinforcements, e.g. fibres
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
- B29B7/94—Liquid charges
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/20—Compounding polymers with additives, e.g. colouring
- C08J3/201—Pre-melted polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L63/00—Compositions of epoxy resins; Compositions of derivatives of epoxy resins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/52—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices with rollers or the like, e.g. calenders
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2065/00—Use of polyphenylenes or polyxylylenes as moulding material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/0005—Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2491/00—Use of waxes as filler
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2300/00—Characterised by the use of unspecified polymers
- C08J2300/24—Thermosetting resins
Definitions
- the present invention relates to a method for producing a resin molded product, a method for producing a resin composition, a resin molded product, a resin composition, a low dusting resin powder, and a method for reducing the dust generation of a resin.
- Patent Document 1 describes a method for reducing dust generation of fine powder that is likely to be scattered as dust during operations of slaked lime, dolomite, calcium carbonate, cement, gypsum, slag, magnesium hydroxide, and the like. Specifically, attempts have been made to reduce the dust generation of the fine powder by mixing a branched polyethyleneimine solution with the fine powder.
- Patent Document 2 describes a method for reducing dust generation of powder whose properties are changed by adding water, such as quick lime, light calcined dolomite, cement, gypsum, slag, coke powder, and diatomaceous earth. . Specifically, attempts have been made to reduce powder dust generation by mixing a branched polyethyleneimine solution using an organic solvent as a solvent with the powder.
- Patent Documents 1 and 2 there is a method for suppressing dust generation of a powdery low molecular weight compound.
- a powdered polymer compound such as a resin.
- thermosetting resins are known to have high polarity in themselves and are difficult to mix with compounds generally used as lubricants.
- JP-A-10-226780 Japanese Patent Laid-Open No. 11-80712 JP 2011-214002 A
- thermosetting resin is usually used in a powder state. At this time, since the thermosetting resin is in the form of powder, there is a problem that it is likely to generate dust and diffuse around. If the thermosetting resin generates dust during use, the resin is dispersed in the work space, for example, the work space is contaminated, powdered resin is mixed in the work device, or resin is mixed in other reagents. was there.
- the present inventors have found that dust generation of a powdered resin can be suppressed by adding liquid paraffin to the thermosetting resin, and have reached the present invention.
- liquid paraffin is added as a lubricant for improving the fluidity and releasability of a resin when a thermoplastic resin is thermoformed.
- a thermosetting resin is not used in combination with such a lubricant because its fluidity is remarkably lowered when heated.
- the present invention has been made in view of the above circumstances, and provides a resin powder in which dust generation during use is suppressed.
- adding liquid paraffin to the thermosetting resin to prepare a low dusting resin powder A step of heating and kneading the low dusting resin powder to obtain a resin molded product, Including
- the step of preparing a low dusting resin powder includes a step of melting the thermosetting resin, adding the liquid paraffin to the molten thermosetting resin, and stirring and mixing the method. Is provided.
- thermosetting resin By adding liquid paraffin to the thermosetting resin, it is possible to suppress dust generation of the resulting resin powder.
- the reason is not necessarily clear, but is considered as follows.
- liquid paraffin is added to the thermosetting resin, static electricity is generated. As a result, it is considered that electrostatic attraction acts between the fine particles, and the fine particles can be prevented from rising.
- thermosetting resin is preferably a phenol resin or an epoxy resin
- the liquid paraffin preferably contains cycloparaffin.
- a step of preparing a low dusting resin powder containing a thermosetting resin and liquid paraffin A step of dry-mixing the low dusting resin powder and the filler to obtain a resin composition; The manufacturing method of the resin composition containing this is provided.
- a method for producing a resin molded product including a step of obtaining a resin molded product from the resin composition obtained by the method for producing a resin composition.
- a resin molded product obtained by the method for producing a resin molded product.
- thermosetting resin Liquid paraffin, Including A low dusting resin powder having an average particle size of 1 ⁇ m or more and 100 ⁇ m or less is provided.
- thermosetting resin by adding liquid paraffin to the molten thermosetting resin, a portion of the obtained resin powder is weighed in a 100 cc plastic cup and dropped from 1 m above the ground at 25 ° C., There is provided a method for reducing the dust generation of a resin, wherein the dust generation amount of the resin powder is reduced as compared with a case where liquid paraffin is not added to a molten thermosetting resin.
- liquid paraffin is added to a thermosetting resin to prepare a low dusting resin powder, and then the low dusting resin powder is heated and kneaded to obtain a resin molded product. Is what you get.
- low dust generation resin powder is obtained by the method demonstrated below.
- the low dusting resin powder can be obtained by melting a thermosetting resin, adding liquid paraffin to the molten thermosetting resin, and stirring and mixing.
- low dust generation indicates that when a powdery resin is used, the powder hardly rises to the surroundings. That is, the low dust-generating resin powder indicates a resin powder that does not easily rise in the work space when used.
- the low dusting resin powder according to the present embodiment by adding liquid paraffin to the molten thermosetting resin, the obtained resin powder is weighed in a 100 cc plastic cup, The dust generation amount of the resin powder when dropped from 1 m above the ground at 25 ° C. can be reduced as compared with the case where liquid paraffin is not added.
- the low dusting resin powder can be obtained by mixing a thermosetting resin and liquid paraffin.
- thermosetting resin is melted, and the melted thermosetting resin and liquid paraffin are stirred and mixed to obtain a resin mixture.
- the resin mixture obtained is pulverized to obtain a low dusting resin powder.
- the mixing temperature of the thermosetting resin and liquid paraffin is preferably 80 ° C. or higher and 250 ° C. or lower. By mixing in this temperature range, the thermosetting resin and liquid paraffin are easily mixed uniformly.
- the dust generation property of the resin powder obtained can be suppressed by mixing these components as uniformly as possible.
- the liquid paraffin to be added is preferably added in an amount of 0.05 to 2% by weight, more preferably 0.1 to 1% by weight, based on the total weight of the thermosetting resin. .
- the amount of liquid paraffin added is in this range, the dust generation of the resulting resin powder can be further suppressed.
- the average particle size of the obtained low dusting resin powder is not uniform, but the particle size is reduced using a sieve. By aligning, it is possible to cause uniform electrostatic interactions. By arranging the particle diameters in this way, it is possible to further suppress the dust generation properties of the obtained resin powder.
- the average particle size of the low dusting resin powder is 1 ⁇ m or more and 500 ⁇ m or less, preferably 1 ⁇ m or more and 100 ⁇ m or less, and more preferably 5 ⁇ m or more and 100 ⁇ m or less. When the average particle size of the low dusting resin powder is within this range, the dusting property of the obtained resin powder can be further suppressed.
- the resin molded product can be manufactured by heat-kneading the low dust-generating resin powder and molding it into a desired shape.
- the resin molded product include, but are not limited to, a grindstone, a casting, a friction material, a rubber molded product, an adhesive tape, a felt, a mold material, a refractory, and a heat insulating agent.
- a filler may be appropriately added according to the use of the resin molded product.
- the heat-kneading may be performed by a kneader such as a roll, a kneader or a twin screw extruder alone, or may be performed in combination with a roll and another kneader.
- a kneader such as a roll, a kneader or a twin screw extruder alone, or may be performed in combination with a roll and another kneader.
- the low dusting resin powder according to the present embodiment includes a thermosetting resin and liquid paraffin.
- the resin powder by which the dust generation property at the time of use was suppressed can be obtained.
- the reason is not necessarily clear, but is considered as follows.
- liquid paraffin is added to the thermosetting resin, static electricity is generated.
- the charge amount of the powder is improved. That is, an electrostatic attractive force due to electric charges acts between the fine particles forming the powder. This force is considered to suppress the rising of each fine particle generated when using the powder and to suppress the dust generation.
- the average particle size of the low dusting resin powder according to this embodiment is 1 ⁇ m or more and 500 ⁇ m or less, preferably 1 ⁇ m or more and 100 ⁇ m or less, and more preferably 5 ⁇ m or more and 100 ⁇ m or less.
- the average particle size of the low dusting resin powder is within this range, the dusting property of the obtained resin powder can be further suppressed.
- thermosetting resin for example, a phenol resin, an epoxy resin, a melamine resin, a urea resin, an oxetane resin, (meth) acrylate resin, unsaturated polyester resin, diallyl phthalate
- a resin or a maleimide resin examples thereof include a resin or a maleimide resin.
- these can also be used individually or in combination of 2 or more types.
- a phenol resin or an epoxy resin is preferable.
- the phenol resin in this embodiment is obtained by reacting phenols and aldehydes in the presence of an alkaline or acidic catalyst, and has at least one phenolic hydroxyl group in the aromatic ring. ing.
- it does not specifically limit as a method of making phenols and aldehydes react, A well-known method is employable.
- phenol resin examples include a phenol resin, a cresol resin, a resorcin resin, a xylenol resin, a naphthol resin, a bisphenol A resin, an aralkyl phenol resin, a biphenyl aralkyl phenol resin, and a modified phenol resin using cashew nut oil having a phenolic hydroxyl group.
- xylene-modified phenol resins containing substances having phenolic hydroxyl groups and various modified phenol resins such as phenol-modified rosin, oil-modified phenol resins modified with terpene oil, rubber-modified phenol resins modified with rubber, etc. can do.
- cresols such as phenol, o-cresol, m-cresol, p-cresol, mixed cresol, 2,3-xylenol, 2,4-xylenol, 2,5-xylenol, 2,6-xylenol, 3,4- Xylenol such as xylenol and 3,5-xylenol, ethylphenol such as o-ethylphenol, m-ethylphenol and p-ethylphenol, butylphenol such as isopropylphenol, butylphenol and p-tert-butylphenol, p-tert-amylphenol Alkylphenols such as p-octylphenol, p-nony
- aldehydes used for obtaining the phenol resin include formaldehyde, paraformaldehyde, trioxane, acetaldehyde, propionaldehyde, polyoxymethylene, chloral, hexamethylenetetramine, furfural, glyoxal, n-butyraldehyde, capro
- the catalyst for obtaining the phenol resin is not particularly limited, and examples thereof include an acid catalyst, a base catalyst, and a transition metal salt catalyst.
- the acid catalyst that can be used include inorganic acids such as hydrochloric acid, sulfuric acid, and phosphoric acids, and organic acids such as oxalic acid, p-toluenesulfonic acid, and organic phosphonic acid.
- the base catalyst include alkali metal hydroxides such as sodium hydroxide, potassium hydroxide and lithium hydroxide, alkaline earth metal hydroxides such as calcium hydroxide and barium hydroxide, ammonia, alkylamine and the like. These amines can be used.
- the transition metal salt catalyst include zinc oxalate and zinc acetate.
- the epoxy resin examples include novolak type epoxy resins such as phenol novolak type epoxy resin and cresol novolak type epoxy resin; bisphenol type epoxy resins such as bisphenol A type epoxy resin and bisphenol F type epoxy resin; N, N-di Aromatic glycidylamine type epoxy resins such as glycidylaniline, N, N-diglycidyltoluidine, diaminodiphenylmethane type glycidylamine, aminophenol type glycidylamine; hydroquinone type epoxy resin; biphenyl type epoxy resin; stilbene type epoxy resin; Methane type epoxy resin; Triphenol propane type epoxy resin; Alkyl-modified triphenol methane type epoxy resin; Triazine core-containing epoxy resin; Diene-modified phenol type epoxy resin; naphthol type epoxy resin; naphthalene type epoxy resin; naphthylene ether type epoxy resin; phenol aralkyl type epoxy resin having phenylene and / or biphenylene
- thermosetting resins may contain other components such as a curing agent, an inorganic filler, a curing accelerator, a coupling agent, and an inorganic flame retardant at the time of use. By doing so, it becomes possible to appropriately prepare a low dusting resin powder suitable for various methods of use, depending on the difference in properties required for the resin mixture.
- the liquid paraffin contained in the low dusting resin powder is not particularly limited, but preferably contains cycloparaffin.
- cycloparaffin is easily mixed with a thermosetting resin to make a resin powder, the degree of suppression of dust generation during use can be further improved.
- liquid paraffin has been known to be used as a lubricant in combination with a thermoplastic resin.
- liquid paraffin is not used in combination with a thermosetting resin.
- the resin molded product according to the present embodiment is prepared by preparing a low dust generation resin powder containing a thermosetting resin and liquid paraffin in the first embodiment, and then dry-mixing the low dust generation resin powder and the filler. The difference is that the resin composition is prepared and manufactured from the obtained resin composition.
- the same method as described in the first embodiment can be used as the method for producing the low dusting resin powder and the low dusting resin powder.
- the dry mix indicates that the low dusting resin powder and the filler are mixed without melting.
- the respective components may be heated, but a form such as heat kneading in which any one is melted and kneaded is not used.
- the resin composition concerning this embodiment can be obtained. According to the present embodiment, by using the low dust-generating resin powder, it is possible to prevent the powder from being diffused and generate dust, so that the work space that has conventionally occurred is contaminated. It is possible to prevent the resin powder from being mixed into other reagents.
- the various fillers are not particularly limited.
- abrasive grains for example, abrasive grains, inorganic fillers, organic fillers, silica sand, curing agents, coupling agents, rubber, base materials, solvents, pigments, fibers, surfactants. , Flocculants, hair materials, foaming agents, glass, aggregates, carbon, acids and the like.
- the resin composition obtained by dry mixing is not particularly limited.
- the resin composition is heat-kneaded, melt-molded, hot-molded, hot-worked, applied to a substrate, or fixed to other production raw materials. It can be used in various methods such as impregnating a substrate.
- the resin molded product containing the low dust generation resin powder which concerns on this embodiment can be obtained.
- the resin composition in the present embodiment can be used as a resin material or a molding material for obtaining various resin molded products described below.
- the resin composition includes, for example, (1) a general grinding wheel, a heavy grinding wheel, a cutting wheel, an offset wheel, a glass cloth treatment, a resin material for obtaining a grinding wheel such as a diamond wheel, (2) a polishing cloth, a polishing paper, Resin materials for obtaining abrasive cloth such as disc sandpaper and abrasive bubbling, (3) Shell mold method (cold coat, semi-hot coat, dry hot coat), organic self-hardness (cold box, phenol urethane, phenol acid curing, Resin materials for obtaining castings such as renocure, furan, organic acid esters), hot boxes, shell adhesives, coating materials, etc.
- friction materials such as brake lining, clutch facing, disc pad, paper clutch facing, brake ring, etc.
- Rubber reinforcement, hot melt adhesive, adhesive tape, Resin materials to obtain rubber such as rubber adhesive, rubber latex, tackifier, pressure sensitive adhesive, metal adhesive, rubber vulcanization, sealing material, etc.
- Electricity such as capacitor coating, insulation varnish, etc.
- Resin materials for obtaining insulating materials (7) Paint bases, oil-modified paints, furniture paints, metal can paints, printing inks, offset printing, dyeing assistants, photoresists, and other paints and printing inks Resin materials, (8) Felt, phenol foam, wood powder molding, phenol resin fiber, hard board, particle board, reinforced wood, insulation board and other organic materials, (9) Beater addition, battery Resin materials for obtaining pulp-impregnated products such as separators, air filters, oil filters, etc.
- Resin materials for obtaining woodworking adhesives such as plywood (special), laminated wood, panel adhesives, (13) impervious carbon products, carbonaceous sealing materials, electric brushes, sliding materials, activated carbon, corrosion resistant joints It can be used as a resin material for obtaining other products such as an agent, an epoxy resin curing agent, casting, and phenol FRP.
- Example 1 Production of low dusting resin powder First, 1000 parts by weight of phenol resin (Sumitite Resin (registered trademark) PR-50731 manufactured by Sumitomo Bakelite Co., Ltd.) in a 3 L cylindrical separable flask was heated to 200 ° C. And melted. In addition, the cylindrical separable flask used here uses what was equipped with the stirring apparatus, the reflux condenser, and the thermometer.
- phenol resin Suditite Resin (registered trademark) PR-50731 manufactured by Sumitomo Bakelite Co., Ltd.
- the cylindrical separable flask used here uses what was equipped with the stirring apparatus, the reflux condenser, and the thermometer.
- liquid paraffin MORESCO White P-350P manufactured by MORESCO
- the melt-mixed resin was taken out into a stainless steel vat and cooled at 25 ° C. (room temperature) to obtain a solid resin. Then, the obtained solid resin was pulverized with a ball mill until the average particle diameter became 30 ⁇ m to prepare a powder.
- Dust generation was evaluated in the same manner as in the examples. As a result, the obtained powder generated intense dust.
- thermosetting resin By mixing liquid paraffin with the thermosetting resin, it is possible to obtain a resin powder that is excellent in suppressing dust generation during use as compared with the case where liquid paraffin is not mixed.
- a resin composition was obtained by dry-mixing the filler with respect to the resin powders obtained in the above Examples and Comparative Examples. At this time, the resin powder obtained in the Examples hardly generated dust when dry-mixed with the filler. On the other hand, the resin powder obtained in the comparative example generated intense dust when dry mixed with the filler.
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Abstract
Description
前記低発塵性樹脂粉末を加熱混練して樹脂成形品を得る工程と、
を含み、
低発塵性樹脂粉末を準備する前記工程は、前記熱硬化性樹脂を溶融し、前記溶融した熱硬化性樹脂に、前記流動パラフィンを添加して撹拌混合する工程を含む樹脂成形品の製造方法が提供される。
前記低発塵性樹脂粉末と、充填材とをドライミックスして樹脂組成物を得る工程と、
を含む樹脂組成物の製造方法が提供される。
流動パラフィンと、
を含み、
平均粒径が、1μm以上100μm以下である低発塵性樹脂粉末が提供される。
本実施形態に係る樹脂成形品の製造方法は、熱硬化性樹脂に流動パラフィンを添加して低発塵性樹脂粉末を準備し、その後、低発塵性樹脂粉末を加熱混練して樹脂成形品を得るものである。また、低発塵性樹脂粉末を準備する場合、以下に説明する方法で低発塵性樹脂粉末を得る。低発塵性樹脂粉末は、熱硬化性樹脂を溶融し、溶融した熱硬化性樹脂に、流動パラフィンを添加して撹拌混合することで得ることができる。
低発塵性樹脂粉末は、熱硬化性樹脂と流動パラフィンとを混合することにより得ることが出来る。
次に、上記方法で得られた低発塵性樹脂粉末から樹脂成形品を製造する方法について説明する。
本実施形態において、樹脂成形品は、低発塵性樹脂粉末を加熱混練し、所望の形状に成形することによって製造することができる。樹脂成形品としては、たとえば、砥石、鋳物、摩擦材、ゴム成形品、粘着テープ、フェルト、型材、耐火物および保温剤等が挙げられるものの、これらに限定されない。
本実施形態に係る低発塵性樹脂粉末は、熱硬化性樹脂と流動パラフィンを含む。こうすることにより、使用時の発塵性が抑制された樹脂粉末を得ることができる。その理由は必ずしも明らかではないが、以下のように考えられる。熱硬化性樹脂に流動パラフィンを添加した際、静電気が発生する。静電気が発生した事に伴い、粉末の帯電量は向上する。すなわち、粉末を形成している各微粒子間に電荷による静電引力が働く。この力によって、粉末を使用する時に発生する各微粒子の舞いあがりが抑制され、発塵性も抑制されるものと考えられる。
フェノール樹脂としては、例えば、フェノール樹脂、クレゾール樹脂、レゾルシン樹脂、キシレノール樹脂、ナフトール樹脂、ビスフェノールA樹脂、アラルキルフェノール樹脂、ビフェニルアラルキルフェノール樹脂、およびフェノール性水酸基を有するカシューナッツ油などによる変性フェノール樹脂などが挙げられる。また、フェノール性水酸基を有する物質を含む、キシレン変性フェノール樹脂、およびフェノール類とロジン、テルペン油などで変性した油変性フェノール樹脂、ゴムで変性したゴム変性フェノール樹脂などの各種変性フェノール樹脂なども使用することができる。
本実施形態における樹脂成形品は、第1の実施形態と、熱硬化性樹脂および流動パラフィンを含む低発塵性樹脂粉末を準備した後、当該低発塵性樹脂粉末と充填材をドライミックスして樹脂組成物を作製し、得られた樹脂組成物から製造する点で異なっている。
まず、低発塵性樹脂粉末を各種充填材と、ドライミックスする。ここで、ドライミックスとは、低発塵性樹脂粉末と充填剤とを、それぞれ溶融することなく混合することを示している。また、低発塵性樹脂粉末を各種充填材とドライミックスする際に、それぞれの成分を加熱してもよいが、いずれかを溶融させて混練する加熱混練のような形態は、用いない。こうすることで、本実施形態に係る樹脂組成物を得ることができる。本実施形態によれば、低発塵性樹脂粉末を用いることで、粉末が周囲に拡散して発塵することを抑制させることができるため、従来生じていた作業空間が汚染される、作業装置に樹脂粉末が混入する、他の試薬類に混入する等といったことを防ぐことができる。
ドライミックスして得られた樹脂組成物は、特に限定されないが、例えば、加熱混練する、溶融成形する、熱間成形する、熱間施工する、基材に塗布する、その他の製造原料に定着させる、基材を含浸させる等の種々の方法に用いることができる。こうすることで、本実施形態に係る低発塵性樹脂粉末を含む樹脂成形品を得ることができる。
(1)低発塵性樹脂粉末の製造
まず、3Lの円筒型セパラブルフラスコ中にフェノール樹脂(住友ベークライト社製スミライトレジン(登録商標)PR-50731)を1000重量部入れ200℃に昇温して溶融した。なお、ここで使用する円筒型セパラブルフラスコは、撹拌装置、還流冷却器および温度計を備えたものを使用する。
作製した粉末を100ccプラスチックカップで一杯分量り取り、25℃で地上1mから落下させた。このように作製した粉末を落下させても、発塵はほぼ発生しなかった。
実施例の粉末の製造において、流動パラフィンを添加せずに比較例の粉末を作製した。
上記実施例および比較例で得られた樹脂粉末に対して、充填材をドライミックスすることで樹脂組成物を得た。このとき、実施例で得られた樹脂粉末は、充填剤とドライミックスする際に、発塵はほぼ発生しなかった。一方、比較例で得られた樹脂粉末は、充填剤とドライミックスする際に、激しく発塵した。
得られた樹脂粉末および樹脂組成物をそれぞれ用いて加熱混練したところ、樹脂成形品を得ることができた。
Claims (25)
- 熱硬化性樹脂に流動パラフィンを添加して低発塵性樹脂粉末を準備する工程と、
前記低発塵性樹脂粉末を加熱混練して樹脂成形品を得る工程と、
を含み、
低発塵性樹脂粉末を準備する前記工程は、前記熱硬化性樹脂を溶融し、前記溶融した熱硬化性樹脂に、前記流動パラフィンを添加して撹拌混合する工程を含む樹脂成形品の製造方法。 - 低発塵性樹脂粉末を準備する前記工程は、前記溶融した熱硬化性樹脂と前記流動パラフィンとを撹拌混合して樹脂混合物を得、次いで前記樹脂混合物を粉砕して、前記低発塵性樹脂粉末を得る工程を含む請求項1に記載の樹脂成形品の製造方法。
- 前記熱硬化性樹脂が、フェノール樹脂またはエポキシ樹脂を含む請求項1または2に記載の樹脂成形品の製造方法。
- 前記流動パラフィンが、シクロパラフィンを含む請求項1乃至3のいずれか一項に記載の樹脂成形品の製造方法。
- 前記熱硬化性樹脂の総重量に対し、0.05重量%以上2重量%以下の前記流動パラフィンを含む請求項1乃至4のいずれか一項に記載の樹脂成形品の製造方法。
- 前記低発塵性樹脂粉末の平均粒径が、1μm以上100μm以下である請求項1乃至5のいずれか一項に記載の樹脂成形品の製造方法。
- 請求項1乃至6のいずれか一項に記載の樹脂成形品の製造方法により得られた樹脂成形品。
- 熱硬化性樹脂および流動パラフィンを含む低発塵性樹脂粉末を準備する工程と、
前記低発塵性樹脂粉末と、充填材とをドライミックスして樹脂組成物を得る工程と、
を含む樹脂組成物の製造方法。 - 低発塵性樹脂粉末を準備する前記工程は、前記熱硬化性樹脂を溶融し、前記溶融した熱硬化性樹脂に、前記流動パラフィンを添加して撹拌混合する工程を含む請求項8に記載の樹脂組成物の製造方法。
- 低発塵性樹脂粉末を準備する前記工程は、前記溶融した熱硬化性樹脂と前記流動パラフィンとを撹拌混合して樹脂混合物を得、次いで前記樹脂混合物を粉砕して、前記低発塵性樹脂粉末を得る工程を含む請求項9に記載の樹脂組成物の製造方法。
- 前記熱硬化性樹脂が、フェノール樹脂またはエポキシ樹脂を含む請求項8乃至10のいずれか一項に記載の樹脂組成物の製造方法。
- 前記流動パラフィンが、シクロパラフィンを含む請求項8乃至11のいずれか一項に記載の樹脂組成物の製造方法。
- 前記熱硬化性樹脂の総重量に対し、0.05重量%以上2重量%以下の前記流動パラフィンを含む請求項8乃至12のいずれか一項に記載の樹脂組成物の製造方法。
- 前記低発塵性樹脂粉末の平均粒径が、1μm以上100μm以下である請求項8乃至13のいずれか一項に記載の樹脂組成物の製造方法。
- 請求項8乃至14のいずれか一項に記載の樹脂組成物の製造方法により得られた樹脂組成物。
- 請求項8乃至14のいずれか一項に記載の樹脂組成物の製造方法により得られた樹脂組成物から樹脂成形品を得る工程を含む、樹脂成形品の製造方法。
- 樹脂成形品を得る前記工程は、前記樹脂組成物を加熱混練する工程を含む、請求項16に記載の樹脂成形品の製造方法。
- 樹脂成形品を得る前記工程は、前記樹脂組成物を溶融成形する工程を含む、請求項16に記載の樹脂成形品の製造方法。
- 樹脂成形品を得る前記工程は、前記樹脂組成物を基材に塗布する工程を含む、請求項16に記載の樹脂成形品の製造方法。
- 請求項16乃至19のいずれか一項に記載の樹脂成形品の製造方法により得られた樹脂成形品。
- 熱硬化性樹脂と、
流動パラフィンと、
を含み、
平均粒径が、1μm以上100μm以下である低発塵性樹脂粉末。 - 前記熱硬化性樹脂が、フェノール樹脂またはエポキシ樹脂を含む請求項21に記載の低発塵性樹脂粉末。
- 前記流動パラフィンが、シクロパラフィンを含む請求項21または22に記載の低発塵性樹脂粉末。
- 前記熱硬化性樹脂の総重量に対し、0.05重量%以上2重量%以下の前記流動パラフィンを含む請求項21乃至23のいずれか一項に記載の低発塵性樹脂粉末。
- 溶融した熱硬化性樹脂に流動パラフィンを添加することにより、得られた樹脂粉末を100ccプラスチックカップで一杯分を量り取り、25℃で地上1mから落下させた際の、前記樹脂粉末の発塵量を、溶融した熱硬化性樹脂に流動パラフィンを添加しない場合と比べて低減させる、樹脂の低発塵化方法。
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EP2824146B1 (en) | 2017-09-06 |
CN105419219B (zh) | 2018-04-03 |
AU2013228940A1 (en) | 2014-09-04 |
US20160060424A1 (en) | 2016-03-03 |
MX349012B (es) | 2017-07-06 |
TWI572654B (zh) | 2017-03-01 |
TWI623571B (zh) | 2018-05-11 |
TW201348313A (zh) | 2013-12-01 |
CN104144985A (zh) | 2014-11-12 |
IN2014DN06907A (ja) | 2015-05-15 |
MX2014010703A (es) | 2014-10-13 |
KR20140136976A (ko) | 2014-12-01 |
ES2643506T3 (es) | 2017-11-23 |
US9303139B2 (en) | 2016-04-05 |
EP2824146A1 (en) | 2015-01-14 |
EP2824146A4 (en) | 2015-10-28 |
KR101656593B1 (ko) | 2016-09-09 |
AU2013228940B2 (en) | 2015-11-26 |
MY166338A (en) | 2018-06-25 |
CN105419219A (zh) | 2016-03-23 |
US20150005445A1 (en) | 2015-01-01 |
CN104144985B (zh) | 2016-04-20 |
TW201700567A (zh) | 2017-01-01 |
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