WO2010082646A1 - 発泡性レゾール型フェノール樹脂成形材料およびその製造方法ならびにフェノール樹脂発泡体 - Google Patents
発泡性レゾール型フェノール樹脂成形材料およびその製造方法ならびにフェノール樹脂発泡体 Download PDFInfo
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- WO2010082646A1 WO2010082646A1 PCT/JP2010/050461 JP2010050461W WO2010082646A1 WO 2010082646 A1 WO2010082646 A1 WO 2010082646A1 JP 2010050461 W JP2010050461 W JP 2010050461W WO 2010082646 A1 WO2010082646 A1 WO 2010082646A1
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- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
- C08J9/14—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
- C08J9/143—Halogen containing compounds
- C08J9/144—Halogen containing compounds containing carbon, halogen and hydrogen only
- C08J9/145—Halogen containing compounds containing carbon, halogen and hydrogen only only chlorine as halogen atoms
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- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0014—Use of organic additives
- C08J9/0028—Use of organic additives containing nitrogen
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- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
- C08J9/14—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
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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
- C08K5/04—Oxygen-containing compounds
- C08K5/05—Alcohols; Metal alcoholates
- C08K5/053—Polyhydroxylic alcohols
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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
- C08K5/16—Nitrogen-containing compounds
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- 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
- C08K5/16—Nitrogen-containing compounds
- C08K5/34—Heterocyclic compounds having nitrogen in the ring
- C08K5/3442—Heterocyclic compounds having nitrogen in the ring having two nitrogen atoms in the ring
- C08K5/3445—Five-membered rings
- C08K5/3447—Five-membered rings condensed with carbocyclic rings
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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
- C08K5/16—Nitrogen-containing compounds
- C08K5/34—Heterocyclic compounds having nitrogen in the ring
- C08K5/3467—Heterocyclic compounds having nitrogen in the ring having more than two nitrogen atoms in the ring
- C08K5/3477—Six-membered rings
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- 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
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2101/00—Manufacture of cellular products
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- 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
- C08J2361/00—Characterised by the use of condensation polymers of aldehydes or ketones; Derivatives of such polymers
- C08J2361/04—Condensation polymers of aldehydes or ketones with phenols only
- C08J2361/06—Condensation polymers of aldehydes or ketones with phenols only of aldehydes with phenols
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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
- C08K2201/00—Specific properties of additives
- C08K2201/002—Physical properties
- C08K2201/005—Additives being defined by their particle size in general
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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
- C08K5/36—Sulfur-, selenium-, or tellurium-containing compounds
- C08K5/41—Compounds containing sulfur bound to oxygen
- C08K5/42—Sulfonic acids; Derivatives thereof
Definitions
- the present invention relates to a foamable resol-type phenol resin molding material, a method for producing the same, and a phenol resin foam. More particularly, the present invention provides a phenolic resin foam having an advantageous appearance, a practical strength and brittleness, a high pH, and good corrosion resistance. The present invention relates to a foamable resol-type phenolic resin molding material that can be produced under curing and a method for producing the same.
- phenolic resin foams have been used in construction and other industrial fields as heat insulating materials because they are excellent in heat insulation, flame retardancy and fire resistance.
- such a phenol resin foam is generally produced by foaming and curing a foamable phenol resin molding material containing at least a liquid resol type phenol resin, a foaming agent and an acid curing agent.
- the said acid hardening agent generally uses inorganic acids, such as sulfuric acid, and organic acids, such as benzenesulfonic acid, toluenesulfonic acid, and xylenesulfonic acid, the obtained phenol resin foam is, for example, rain If the metal member is in contact with the phenol resin foam, or if there is a metal member in the vicinity of the foam, the acid curing agent in the foam is extracted with water. A problem arises that metal members are susceptible to corrosion.
- Patent Document 1 and Patent Document 2 have been proposed to meet such demands, but even when the density is lowered from the viewpoint of weight reduction and cost reduction, the appearance and the above performance Development of a phenolic resin foam that does not deteriorate is desired.
- the technology described in this patent document is based on the basic nitrogen-containing crosslinked cyclic compound used therein, in particular, hexamethylenetetramine is particularly susceptible to the action of a liquid resol-type phenolic resin or an acid curing agent. Therefore, in some cases, the problem of hindering foaming and curing is inherent.
- the present invention has been made under such circumstances, and the object of the present invention is to have a particularly improved appearance, and at a standard density even at a density of 35 kg / m 3 or less.
- a phenolic resin foam that is suppressed to a level that does not cause a practical problem as compared with the mechanical performance (strength and brittleness) of a foam of about 40 kg / m 3 has a high pH, and has good corrosion resistance.
- An object of the present invention is to provide a foamable phenol resin molding material capable of giving a body.
- Another object of the present invention is to provide a method for producing a foamable phenolic resin molding material that does not hinder foaming and curing.
- another object of the present invention is to provide a phenol resin foam having the above-mentioned performance, which is obtained by foaming and curing the foamable phenol resin molding material.
- the present inventors can obtain a foamable phenolic resin molding material by including a nitrogen-containing crosslinked cyclic compound adjusted to a specific particle size. Even when the density of the phenol resin foam is lowered, the strength and brittleness are hardly lowered, the metal foam has a good metal corrosion prevention property, and has an improved appearance.
- the production of molding materials by adding the above nitrogen-containing cross-linked cyclic compound in the mixing of liquid resol type phenolic resin and acid curing agent, problems with foaming and curing of foaming phenolic resin molding materials are eliminated. The present inventors have found that this can be done and have completed the present invention.
- the present invention (1) A foamable resole-type phenol resin molding material containing a liquid resol-type phenol resin, a foaming agent, a foam stabilizer, an acid curing agent and an additive, wherein the additive has a nitrogen-containing cross-linking having an average particle size of 80 ⁇ m or less A foamable resol-type phenolic resin molding material, characterized by being a cyclic compound (2) The foamable resol-type phenol resin molding material according to (1) above, wherein the nitrogen-containing crosslinked cyclic compound is hexamethylenetetramine, (3) The foamable resol-type phenol resin molding material according to (1) or (2), further comprising a plasticizer, (4) The foamable resol-type phenol resin molding material according to any one of (1) to (3) above, wherein the foaming agent comprises isopropyl chloride, (5) A phenolic resin foam characterized by foaming and curing the foamable resol-type phenolic resin molding material according to any one of (1) to (4)
- Foam, (7) A method for producing a foamable resol type phenol resin molding material comprising a liquid resol type phenol resin, a foaming agent, a foam stabilizer, an acid curing agent and an additive, the liquid resol type phenol resin and the acid curing
- a method for producing a foamable resol-type phenolic resin molding material characterized in that a nitrogen-containing crosslinked cyclic compound having an average particle size of 80 ⁇ m or less is added as the additive in the mixing with the agent, (8)
- the method according to (7) above, wherein the nitrogen-containing crosslinked cyclic compound is hexamethylenetetramine
- the method according to (8) above, wherein the nitrogen-containing crosslinked cyclic compound is added in the form of a mixture with a plasticizer for a phenol resin.
- the plasticizer for phenol resin is at least one selected from polyester polyols, polyether polyols and glycols
- the foaming agent comprises isopropyl chloride
- the foaming agent comprises isopropyl chloride
- the foaming agent comprises isopropyl chloride
- liquid resol type phenol resin, foaming agent, foam stabilizer, acid curing A phenol resin molding material that is foamed and cured by injecting the foamable resol-type phenolic resin composition obtained by supplying the agent and additives to the mixer, stirring and mixing between the upper and lower face materials, and heating.
- any one of the above items (9) to (11), wherein the additive obtained by premixing a nitrogen-containing crosslinked cyclic compound and a plasticizer for phenol resin is supplied to a mixer. The method described in Is to provide.
- the foamable resol-type phenolic resin molding material of the present invention a nitrogen-containing crosslinked cyclic compound (additive) adjusted to a specific particle size is used, so the resulting phenolic resin foam has a density of Even if it is low, it has an improved appearance, has little decrease in strength and brittleness, and retains good metal corrosion resistance.
- a nitrogen-containing crosslinked cyclic compound adjusted to a specific particle size used as an additive is added in the mixing of the liquid resol-type phenol resin and the acid curing agent. Since the retention of the nitrogen-containing crosslinked cyclic compound in the prepared molding material is constant, not only can the influence of the liquid resol type phenolic resin and the acid curing agent be slightly suppressed, but also in the molding material due to the volume effect. Since the dispersion is made uniform, variations in foaming and curing can be advantageously eliminated.
- such a nitrogen-containing crosslinked cyclic compound as a mixture in a state where the nitrogen-containing crosslinked cyclic compound is dispersed in a plasticizer for phenol resin having a low compatibility with the nitrogen-containing crosslinked cyclic compound results in the presence of fine particles. Since it is not necessary to deal with the deterioration of powder fluidity and can be applied to powder feedable products, it is possible not only to simplify and reduce the supply device to the mixing head, but also to improve mixing efficiency. It is possible to provide an advantage that the mixing operation can be advantageously performed.
- the phenol resin foam of the present invention is produced by foaming and curing the foamable resol type phenol resin molding material as described above, even if the density is lowered, it is the same as above. Since it can have practical performance, it can contribute to the weight reduction and cost reduction of a building member, for example.
- the foamable resol-type phenol resin molding material of the present invention (hereinafter sometimes simply referred to as “phenol resin molding material”) will be described.
- phenol resin molding material is a foamable resol-type phenolic resin molding material containing a liquid resol-type phenolic resin, a foaming agent, a foam stabilizer, an acid curing agent, and an additive. It is a nitrogen-containing crosslinked cyclic compound having an average particle diameter of 80 ⁇ m or less.
- phenols and their derivatives represented by phenol, cresol, xylenol, paraalkylphenol, paraphenylphenol, resorcin, and aldehydes represented by formaldehyde, paraformaldehyde, furfural, acetaldehyde, sodium hydroxide
- alkali catalyst typified by potassium hydroxide, calcium hydroxide, etc., and then subjecting to neutralization treatment and / or vacuum dehydration treatment as necessary. Etc. can be used.
- the blending ratio of phenols and aldehydes is not particularly limited, and is appropriately set in the range of 1.0: 1.5 to 3.0 on a molar ratio basis. A range of 0: 1.8 to 2.5 is preferred. Moreover, phenols, aldehydes, and catalysts may be used alone or in combination of two or more of the compounds belonging to each.
- the liquid resol type phenolic resin thus prepared has a viscosity of 1,000 to 80,000 mPa ⁇ s, particularly 7,000 to 50,000 mPa ⁇ s at a temperature of 25 ° C., and a moisture content of 4 Those adjusted to a range of ⁇ 16% by mass, particularly 6 to 14% by mass are preferred.
- foaming agent examples include chlorinated aliphatic hydrocarbons such as dichloroethane, propyl chloride, isopropyl chloride, butyl chloride, isobutyl chloride, pentyl chloride, isopentyl chloride, propane, butane, pentane, and hexane.
- chlorinated aliphatic hydrocarbons such as dichloroethane, propyl chloride, isopropyl chloride, butyl chloride, isobutyl chloride, pentyl chloride, isopentyl chloride, propane, butane, pentane, and hexane.
- Typical examples include low boiling point aliphatic hydrocarbons such as heptane, cyclopropane, cyclobutane, cyclopentane, cyclohexane and cycloheptane, ether compounds such as isopropyl ether, and alternative fluorocarbon compounds such as trichloromonofluoromethane and trichlorotrifluoroethane.
- Organic non-reactive foaming agents Such foaming agents may be used alone or in combination of two or more.
- the non-reactive foaming agent here refers to a substance that itself can volatilize under foaming conditions to foam a phenol resin.
- chlorinated aliphatic hydrocarbons or mixtures of low-boiling point aliphatic hydrocarbons mainly composed of the chlorinated aliphatic hydrocarbons, among which isopropyl chloride and normal pentane are used in combination.
- the blending amount of the foaming agent is appropriately selected in the range of usually 1 to 20 parts by mass with respect to 100 parts by mass of the above-mentioned liquid resol type phenolic resin, preferably 5 to 20 parts by mass. If the blending amount is less than 1 part by mass, a foam having the desired density cannot be obtained.
- a gas such as nitrogen gas, oxygen gas, argon gas, carbon dioxide gas, or a mixed gas thereof can be used.
- foam stabilizer Although there is no restriction
- the blending amount of the foam stabilizer is appropriately selected in the range of usually 1 to 5 parts by mass, preferably 2 to 4 parts by mass with respect to 100 parts by mass of the liquid resol type phenolic resin.
- Examples of the acid curing agent in the phenol resin molding material of the present invention include inorganic acids such as sulfuric acid and phosphoric acid, benzenesulfonic acid, ethylbenzenesulfonic acid, paratoluenesulfonic acid, xylenesulfonic acid, naphtholsulfonic acid, phenolsulfonic acid, and the like. However, it is not limited to these examples. These may be used alone or in combination of two or more.
- the blending amount of the acid curing agent is appropriately selected in the range of usually 5 to 50 parts by mass with respect to 100 parts by mass of the liquid resol type phenolic resin, preferably 10 to 30 parts by mass.
- a nitrogen-containing crosslinked cyclic compound is used as an additive as an essential component.
- the particle size of the nitrogen-containing crosslinked cyclic compound needs to be adjusted to an average particle size of 80 ⁇ m or less, and preferably 70 ⁇ m or less, which means an improvement in the degree of mixing and dispersion in the molding material due to the volume effect. From the viewpoint, 50 ⁇ m or less is particularly preferable. When the average particle diameter exceeds 80 ⁇ m, the effect associated with the finer particle cannot be sufficiently expressed.
- the lower limit of the average particle diameter is not particularly limited. In general, when particles become finer, the particles are combined due to agglomeration and powder flowability is deteriorated.
- the foam does not have an extreme adverse effect, and the nitrogen-containing crosslinked cyclic compound does not have an adverse effect. It is suitable for use as a mixture which is mixed and dispersed in a liquid material which has low compatibility and has a minimum viscosity capable of preventing sedimentation and which is compatible with a liquid phenol resin.
- Such a liquid substance is not particularly limited as long as it has the above properties.
- examples of such a liquid substance include polyester polyols, polyether polyols, glycols, among plasticizers that are optional components described below. It is advantageous to select and use at least one of these.
- Such a method is not limited to fine particles, but also applied to particle sizes that can be supplied in powder form with few composite particles, thereby simplifying and reducing the supply device to the mixing head as well as mixing. It is possible to provide an advantage that the mixing operation can be advantageously performed, for example, efficiency can be improved.
- the nitrogen-containing bridged cyclic compound hexamethylenetetramine is particularly preferable in view of availability and effect expression. And even when the density of the foam is lowered by adjusting the particle size of the nitrogen-containing crosslinked cyclic compound to an average particle size of 80 ⁇ m or less and including it in the foamable phenol resin molding material, metal corrosion occurs. It has been found that unexpected effects are exhibited such that the preventive properties are not inhibited, the strength and brittleness are not significantly reduced, and the appearance is conversely improved.
- the blending amount of such a nitrogen-containing crosslinked cyclic compound is usually appropriately selected within the range of 0.1 to 10 parts by mass with respect to 100 parts by mass of the liquid resol type phenol resin, but preferably 0. 3 to 7 parts by mass. If the blending amount is less than 0.1 parts by mass, the intended purpose cannot be achieved, and conversely if it exceeds 10 parts by mass, the curability tends to deteriorate.
- a plasticizer, an inorganic filler, etc. can be contained as needed.
- ⁇ Plasticizer> As a plasticizer that can be contained in the phenolic resin molding material of the present invention as needed, it provides flexibility to the cell walls of the obtained phenolic resin foam, and suppresses deterioration of heat insulation performance over time. What has is used.
- plasticizers examples include polyester polyols, polyether polyols, glycols, triphenyl phosphate, dimethyl terephthalate, and dimethyl isophthalate. These may be used individually by 1 type and may be used in combination of 2 or more type.
- the plasticizer is usually used in the range of 0.1 to 20 parts by mass with respect to 100 parts by mass of the liquid resol type phenol resin.
- the amount of the plasticizer used is in the above range, the effect of imparting flexibility to the cell wall is satisfactorily exhibited without impairing other performances of the obtained phenol resin foam.
- a preferable amount of the plasticizer is 0.5 to 15 parts by mass, and more preferably 1 to 12 parts by mass.
- Inorganic filler As the inorganic filler that can be contained in the phenol resin molding material of the present invention as needed, those that can effectively impart fire resistance and / or corrosion resistance to the obtained phenol resin foam are used.
- inorganic fillers examples include metal hydroxides and oxides such as aluminum hydroxide, magnesium hydroxide, calcium oxide, magnesium oxide, aluminum oxide, and zinc oxide, metal powders such as zinc, calcium carbonate, and magnesium carbonate. And metal carbonates such as barium carbonate and zinc carbonate.
- aluminum hydroxide and / or calcium carbonate are preferable. These may be used alone or in combination of two or more.
- the amount of the inorganic filler is usually appropriately selected within the range of 0.1 to 30 parts by mass with respect to 100 parts by mass of the liquid resol type phenolic resin, and particularly preferably about 1 to 10 parts by mass. It is.
- the present invention also provides a method for producing the aforementioned foamable resol-type phenol resin molding material of the present invention.
- the method for producing a phenol resin molding material of the present invention is a method for producing a foamable resol type phenol resin molding material containing a liquid resol type phenol resin, a foaming agent, a foam stabilizer, an acid curing agent and an additive, In mixing the liquid resol type phenolic resin and the acid curing agent, a nitrogen-containing crosslinked cyclic compound having an average particle size of 80 ⁇ m or less is added as the additive.
- the liquid resol type phenol resin, the foaming agent, the foam stabilizer, the acid curing agent and the additive are as described in the above-described phenol resin molding material of the present invention.
- the nitrogen-containing crosslinked cyclic compound is advantageously added in the form of a mixture with a plasticizer for phenol resin, preferably at least one selected from polyester polyols, polyether polyols and glycols.
- a foamable resol type phenol resin composition obtained by supplying a liquid resol type phenol resin, a foaming agent, a foam stabilizer, an acid curing agent and an additive to a mixer, and stirring and mixing.
- a phenolic resin molding material that is foamed and cured by injecting between the upper and lower face materials and heating is continuously produced, a nitrogen-containing crosslinked cyclic compound and the phenolic plasticizer are premixed. It is preferable to use a method of supplying the additive to the mixer.
- the phenol resin foam of the present invention is produced by foaming and curing the foamable resol-type phenol resin molding material (hereinafter also referred to as “foamable composition”) prepared as described above. Specifically, for example, (1) a molding method for foaming and curing a foamable composition on an endless conveyor belt, (2) a method for foaming and curing by filling the foamable composition in spots, (3) (4) A method in which a foamable composition is filled in a mold and foamed and cured under pressure. (4) A foamable composition is filled in a large space and foamed and cured to form a foam block. In addition to the method of filling and foaming while press-fitting into a cavity, there can be mentioned a method of blowing and curing a foamable composition onto a wall surface of a housing by an on-site spray foaming machine.
- the phenol resin foam is a surface on which a foamable composition is placed on a conveyor belt that continuously moves.
- this is a double conveyor belt type heat curing furnace (internal temperature: normal) 90 ° C. or less, preferably about 60 to 80 ° C.), foamed and cured in a furnace (residence time: about 2 to 10 minutes), formed into a predetermined thickness, and then formed into a predetermined length.
- the face material is not particularly limited and is at least one selected from a glass fiber nonwoven fabric, a spunbond nonwoven fabric, an aluminum foil-clad nonwoven fabric, a metal plate, a metal foil, a plywood, a calcium silicate plate, a gypsum board, and a wood cement board. Species are preferred.
- This face material may be provided on one side of the phenol resin foam or may be provided on both sides. Moreover, when providing in both surfaces, a face material may be the same and may differ. Further, it may be provided later by using an adhesive.
- the phenol resin foam of the present invention thus obtained is usually used in a density range of 20 to 40 kg / m 3 , but in the case of a density of 25 to 35 kg / m 3 adopted from the viewpoint of weight reduction and cost reduction. Although it is slightly inferior to the standard density of about 40 kg / m 3 , it has strength and brittleness that do not impair practicality, has corrosion resistance, and has an excellent appearance.
- Corrosion prevention A phenol resin foam sample of the same size is placed on a 300 mm square galvanized iron plate (thickness 1 mm, plating coverage 120 g / m 2 ) and fixed so as not to slip. The specimen was placed in an accelerated environment of 40 ° C. and 100% RH, and the corrosivity of the contact surface between the galvanized iron plate and the sample after standing for 24 weeks was visually evaluated.
- Viscosity (unit: mPa ⁇ s / 25 ° C.): Measured at a test temperature of 25 ° C. using a Brookfield rotary viscometer according to JIS K 71117-1 (1999).
- Moisture content (unit: mass%): Measured by Karl Fischer automatic volumetric titration in accordance with JIS K 6910 (2007), 5.18.
- Thermal conductivity [unit: W / (m ⁇ K)]: A phenol resin foam sample (200 mm ⁇ 200 mm) was placed between a low temperature plate of 10 ° C. and a high temperature plate of 30 ° C., and JIS A1412-2. According to the heat flow meter method of (1999), the heat conductivity was measured using a thermal conductivity measuring device “HC-074 304” (manufactured by Eihiro Seiki Co., Ltd.).
- Average particle diameter It was measured with a Microtrac particle size distribution measuring apparatus “MT3000” (manufactured by Nikkiso Co., Ltd.).
- Example 1 First, 3 parts by mass of a silicone-based foam stabilizer (trade name “L-5420”, manufactured by Nihon Unicar Co., Ltd.) as a foam stabilizer, and normal pentane as a foaming agent with respect to 100 parts by mass of the liquid resol type phenolic resin prepared above. (Made by SK Sangyo Co., Ltd.) 8 parts by mass were added and mixed, and the temperature of the mixture was adjusted to 5 ° C.
- a silicone-based foam stabilizer trade name “L-5420”, manufactured by Nihon Unicar Co., Ltd.
- normal pentane as a foaming agent with respect to 100 parts by mass of the liquid resol type phenolic resin prepared above.
- the total amount of the mixture obtained 2 parts by mass of hexamethylenetetramine (average particle diameter 11 ⁇ m) as an additive, and 13 parts by mass of xylene sulfonic acid (trade name “Taikatox 110”, manufactured by Teika Co., Ltd.) as an acid curing agent, Were mixed with a pin mixer to prepare a foamable resol type phenolic resin molding material. Subsequently, the molding material is discharged into a metal mold frame (length 300 mm x width 300 mm x height 50 mm) laid with a glass nonwoven fabric, and then immediately put the same glass nonwoven fabric into a sandwich structure. Then, the mold was clamped and placed in a dryer at 80 ° C. and foamed and cured for 7 minutes to prepare a phenol resin foam. The physical properties of this foam are shown in Table 1.
- Example 2 In Example 1, with respect to 100 parts by mass of the liquid resol type phenolic resin, 2 parts by mass of calcium carbonate was further added as an inorganic filler, and the acid curing agent was changed to 14 parts by mass. A phenolic resin foam was produced. The physical properties of this foam are shown in Table 1.
- Example 3 a phenol resin foam was produced in the same manner as in Example 1 except that the average particle diameter of hexamethylenetetramine was changed to 36 ⁇ m.
- the physical properties of this foam are shown in Table 1.
- Example 4 In Example 1, a phenol resin foam was produced in the same manner as in Example 1 except that the average particle diameter of hexamethylenetetramine was changed to 70 ⁇ m. The physical properties of this foam are shown in Table 1.
- Example 5 3 parts by mass of castor oil ethylene oxide adduct (trade name “D225”, manufactured by Takemoto Yushi Co., Ltd.) as a foam stabilizer and 100 parts by mass of the liquid resol type phenolic resin used in Example 1 and isopropyl chloride as a foaming agent 10 parts by mass of a mixture with normal pentane was added and mixed, and the temperature of the mixture was adjusted to 5 ° C.
- castor oil ethylene oxide adduct trade name “D225”, manufactured by Takemoto Yushi Co., Ltd.
- a foamable resol type phenol resin molding material was prepared by stirring and mixing with a pin mixer. Subsequently, a phenol resin foam was produced in the same manner as in Example 1. Table 1 shows the physical properties of the obtained foam.
- Example 6 Instead of 2 parts by mass of hexamethylenetetramine (average particle size 11 ⁇ m) used in Example 5, polyestermethylene (viscosity: 1200 mPa ⁇ S / 25 ° C.) 5 parts by mass of hexamethylenetetramine (average particle size 5.2 ⁇ m) 2 A phenol resin foam was prepared in the same manner as in Example 5 except that a mixture prepared by adding and mixing parts by mass was used. The physical properties of this foam are shown in Table 1.
- Example 7 The particle size (average particle size: 5.2 ⁇ m) of hexamethylenetetramine used in Example 6 was changed to the particle size (average particle size: 35 ⁇ m, Example 7), particle size (average particle size: 50 ⁇ m, Example 8), and particle size (average particle size).
- Three types of phenolic resin foams were produced in the same manner as in Example 6 except that the thickness was changed to 70 ⁇ m and Example 9). Table 1 shows the physical properties of these foams.
- Example 10 a phenol resin having a density of 40 kg / m 3 was used in the same manner as in Example 5 except that the blending amount of the mixture of isopropyl chloride and normal pentane used as a blowing agent was changed from 10 parts by mass to 8 parts by mass. A foam was made. The physical properties of this foam are shown in Table 1.
- Example 1 In Example 1, two types of phenol were used in the same manner as in Example 1 except that the particle size (average particle size 11 ⁇ m) of hexamethylenetetramine was changed to a particle size (average particle size 90 ⁇ m) and a particle size (average particle size 141 ⁇ m). A resin foam was produced. Table 2 shows the physical properties of these foams.
- Example 3 A phenol resin foam was produced in the same manner as in Example 6 except that the particle size (average particle size: 5.2 ⁇ m) of hexamethylenetetramine used in Example 6 was changed to the particle size (average particle size: 90 ⁇ m). Table 2 shows the physical properties of this foam.
- the foamable resol-type phenol resin molding material of the present invention is a phenol resin foam having a particularly improved appearance, practical strength and brittleness, high pH, and good corrosion resistance. It can be produced under advantageous foaming and curability.
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Abstract
Description
(1) 液状レゾール型フェノール樹脂、発泡剤、整泡剤、酸硬化剤および添加剤を含む発泡性レゾール型フェノール樹脂成形材料であって、前記添加剤が、平均粒子径80μm以下の含窒素架橋型環式化合物であることを特徴とする、発泡性レゾール型フェノール樹脂成形材料、
(2) 含窒素架橋型環式化合物が、ヘキサメチレンテトラミンである、上記(1)項に記載の発泡性レゾール型フェノール樹脂成形材料、
(3) さらに、可塑剤を含む、上記(1)または(2)項に記載の発泡性レゾール型フェノール樹脂成形材料、
(4) 発泡剤が、イソプロピルクロリドを含む、上記(1)~(3)項のいずれか1項に記載の発泡性レゾール型フェノール樹脂成形材料、
(5) 上記(1)~(4)項のいずれか1項に記載の発泡性レゾール型フェノール樹脂成形材料を発泡硬化させてなることを特徴とする、フェノール樹脂発泡体、
(6) 密度が20~40kg/m3であって、pHが4.0以上、圧縮強さが10N/cm2以上および脆性が20%以下である、上記(5)項に記載のフェノール樹脂発泡体、
(7) 液状レゾール型フェノール樹脂、発泡剤、整泡剤、酸硬化剤および添加剤を含む発泡性レゾール型フェノール樹脂成形材料を製造する方法であって、前記液状レゾール型フェノール樹脂と前記酸硬化剤との混合において、前記添加剤として平均粒子径80μm以下の含窒素架橋型環式化合物を加えることを特徴とする、発泡性レゾール型フェノール樹脂成形材料の製造方法、
(8) 含窒素架橋型環式化合物が、ヘキサメチレンテトラミンである、上記(7)項に記載の方法、
(9) 含窒素架橋型環式化合物を、フェノール樹脂用可塑剤との混合物の形態で加える、上記(8)項に記載の方法、
(10) フェノール樹脂用可塑剤が、ポリエステルポリオール、ポリエーテルポリオールおよびグリコール類の中から選ばれる少なくとも1種である、上記(9)項に記載の方法、
(11) 発泡剤が、イソプロピルクロリドを含む、上記(7)~(10)項のいずれか1項に記載の方法、および
(12) 液状レゾール型フェノール樹脂、発泡剤、整泡剤、酸硬化剤および添加剤をミキサーに供給し、攪拌・混合して得られた発泡性レゾール型フェノール樹脂組成物を、上下の面材間に注入し、加熱することで発泡・硬化させるフェノール樹脂成形材料を連続的に製造するに際し、含窒素架橋型環式化合物とフェノール樹脂用可塑剤とをプレ混合してなる前記添加剤をミキサーに供給する、上記(9)~(11)項のいずれか1項に記載の方法、
を提供するものである。
[発泡性レゾール型フェノール樹脂成形材料]
本発明の発泡性レゾール型フェノール樹脂成形材料は、液状レゾール型フェノール樹脂、発泡剤、整泡剤、酸硬化剤および添加剤を含む発泡性レゾール型フェノール樹脂成形材料であって、前記添加剤が、平均粒子径80μm以下の含窒素架橋型環式化合物であることを特徴とする。
本発明のフェノール樹脂成形材料における液状レゾール型フェノール樹脂としては特に制限はなく、従来公知の液状レゾール型フェノール樹脂の中から、適宜選択して用いることができる。例えば、フェノール、クレゾール、キシレノール、パラアルキルフェノール、パラフェニルフェノール、レゾルシン等に代表されるフェノール類およびその誘導体と、ホルムアルデヒド、パラホルムアルデヒド、フルフラール、アセトアルデヒド等に代表されるアルデヒド類とを、水酸化ナトリウム、水酸化カリウム、水酸化カルシウム等に代表されるアルカリ触媒の存在下に反応させた後、必要に応じて中和処理および/または減圧脱水処理を施すことにより、調製される液状のレゾール型フェノール樹脂等を用いることができる。なお、フェノール類とアルデヒド類の配合割合については、特に限定はなく、モル比基準にて、通常、1.0:1.5~3.0の範囲で適宜に設定されるが、とりわけ1.0:1.8~2.5の範囲が好適である。また、フェノール類、アルデヒド類および触媒は、それぞれに属する化合物の1種を単独で用いてもよく、あるいは2種以上を併用してもよい。
本発明のフェノール樹脂成形材料における発泡剤としては、例えばジクロロエタン、プロピルクロリド、イソプロピルクロリド、ブチルクロリド、イソブチルクロリド、ペンチルクロリド、イソペンチルクロリド等の塩素化脂肪族炭化水素、プロパン、ブタン、ペンタン、ヘキサン、ヘプタン、シクロプロパン、シクロブタン、シクロペンタン、シクロヘキサン、シクロヘプタン等の低沸点脂肪族炭化水素、イソプロピルエーテル等のエーテル系化合物、トリクロロモノフルオロメタン、トリクロロトリフルオロエタン等の代替フロン系化合物などに代表される有機系非反応型発泡剤が挙げられる。かかる発泡剤は単独で用いてもよく、あるいは2種以上を併用してもよい。なお、ここでいう非反応型発泡剤とは、物質それ自体が発泡条件下に揮発してフェノール樹脂を発泡し得るものをいう。
本発明のフェノール樹脂成形材料における整泡剤としては、特に制限はないが、非イオン性界面活性剤が好適に用いられる。なお、必要に応じて他のアニオン性界面活性剤を単独で、あるいは併用しても差し支えない。かかる非イオン性界面活性剤の例としては、例えばポリシロキサン系、ポリオキシエチレンソルビタン脂肪酸エステル、ヒマシ油エチレンオキシド付加物などが挙げられる。これらは、単独で用いてもよく、2種以上を併用してもよい。また、整泡剤の配合量としては、液状レゾール型フェノール樹脂100質量部に対して、通常、1~5質量部の範囲で適宜に選択されるが、好ましくは2~4質量部である。
本発明のフェノール樹脂成形材料における酸硬化剤としては、例えば硫酸、リン酸等の無機酸や、ベンゼンスルホン酸、エチルベンゼンスルホン酸、パラトルエンスルホン酸、キシレンスルホン酸、ナフトールスルホン酸、フェノールスルホン酸等の有機酸などの使用が一般的であるが、これらの例示に限定されるものではない。これらは、単独で用いてもよく、2種以上を併用してもよい。かかる酸硬化剤の配合量としては、液状レゾール型フェノール樹脂100質量部に対して、通常、5~50質量部の範囲で適宜に選択されるが、好ましくは10~30質量部である。
本発明のフェノール樹脂成形材料においては、必須成分の添加剤として、含窒素架橋型環式化合物が用いられる。この含窒素架橋型環式化合物の粒度は、平均粒子径で80μm以下に調整されていることが必要であり、好ましくは70μm以下であり、体積効果による成形材料中への混合分散度の向上という観点から、50μm以下が特に好ましい。平均粒子径が80μmを超えると、細粒化に伴う効果が十分に発現され得なくなる。なお、平均粒子径の下限については、特に限定されない。一般に粒子が細かくなると凝集作用による粒子の複合化が生じて粉体流動性の悪化を招き、発泡体の連続生産ラインでのミキシングヘッド(高速混合器など)への直接ないし間接(液状レゾール型フェノール樹脂成分または発泡剤成分との直前混合)の定量供給が難しくなることから、かかる細かな粒子の場合には、通常、発泡体に極端な悪影響を与えず、含窒素架橋型環式化合物との相溶性が少なく、かつその沈降を防止し得る最低限の粘度を有し、しかも液状フェノール樹脂との相溶性を有する液状物質に混合分散させた混合物としての使用が好適である。
本発明のフェノール樹脂成形材料においては、必要に応じて、可塑剤や無機フィラーなどを含有させることができる。
本発明のフェノール樹脂成形材料に、必要に応じて含有させることができる可塑剤としては、得られるフェノール樹脂発泡体の気泡壁に柔軟性を付与し、断熱性能の経時的な劣化を抑制する作用を有するものが用いられる。
本発明のフェノール樹脂成形材料に、必要に応じて含有させることができる無機フィラーは、得られるフェノール樹脂発泡体に、効果的に防火性および/または防食性を付与し得るものが用いられる。
本発明はまた、前述した本発明の発泡性レゾール型フェノール樹脂成形材料を製造する方法をも提供する。
[フェノール樹脂発泡体]
本発明のフェノール樹脂発泡体は、前述のようにして調製した発泡性レゾール型フェノール樹脂成形材料(以下、「発泡性組成物」ともいう。)を発泡、硬化させて作製されるものであって、具体的には、例えば(1)エンドレスコンベアベルト上で発泡性組成物を発泡、硬化させる成形方法、(2)スポット的に発泡性組成物を充填して発泡、硬化させる方法、(3)モールド内に発泡性組成物を充填して加圧状態で発泡、硬化させる方法、(4)大きな空間内に発泡性組成物を充填して発泡、硬化させて発泡ブロックを成形する方法、(5)空洞中に圧入しながら充填発泡させる方法の他、現場スプレー発泡機によって発泡性組成物を躯体壁面等に吹き付けて発泡、硬化させる方法などを挙げることができる。
(i)良好○:0~10個
(iiやや良好△:11~20個
(iii)不良×:21個以上
還流器、温度計、攪拌機を備えた三つ口反応フラスコ内にフェノール1600gと50質量%水酸化ナトリウム水溶液38gを仕込み、47質量%ホルマリン2282gを分割投入し、80℃で180分間反応を行なった。その後40℃に冷却し、50質量%パラトルエンスルホン酸水溶液で中和し、減圧・加熱下に脱水濃縮して液状レゾール型フェノール樹脂2830gを得た。この樹脂は粘度15,000mPa・s/25℃、水分率9.2質量%であった。
先ず、上記で準備した液状レゾール型フェノール樹脂100質量部に対し、整泡剤としてシリコーン系整泡剤(商品名「L−5420」、日本ユニカー株式会社製)3質量部、発泡剤としてノルマルペンタン(エスケイ産業株式会社製)8質量部加えて混合し、混合物の温度を5℃に調整した。得られた混合物の全量と、さらに添加剤としてヘキサメチレンテトラミン(平均粒子径11μm)2質量部および酸硬化剤としてキシレンスルホン酸(商品名「テイカトックス110」、テイカ株式会社製)13質量部とをピンミキサーにて撹拌、混合して発泡性レゾール型フェノール樹脂成形材料を調製した。引き続いて、この成形材料を、ガラス不織布を敷いた金属型枠内(縦300mm×横300mm×高さ50mm)に吐出後、直ちに同じガラス不織布を載せてサンドイッチ構造とし、さらに上蓋鉄板を型枠上面に載せた後型締めし、これを80℃の乾燥機中に入れて7分間発泡、硬化させてフェノール樹脂発泡体を作製した。この発泡体の物性を表1に示す。
実施例1において、液状レゾール型フェノール樹脂100質量部に対し、さらに無機フィラーとして炭酸カルシウム2質量部を添加し、また酸硬化剤を14質量部に変更した以外は、実施例1と同様にしてフェノール樹脂発泡体を作製した。この発泡体の物性を表1に示す。
実施例1において、ヘキサメチレンテトラミンの平均粒子径を36μmに変更した以外は、実施例1と同様にしてフェノール樹脂発泡体を作製した。この発泡体の物性を表1に示す。
実施例1において、ヘキサメチレンテトラミンの平均粒子径を70μmに変更した以外は、実施例1と同様にしてフェノール樹脂発泡体を作製した。この発泡体の物性を表1に示す。
実施例1で使用した液状レゾール型フェノール樹脂100質量部に対し、整泡剤としてヒマシ油エチレンオキサイド付加物(商品名「D225」、竹本油脂株式会社製)3質量部および発泡剤としてイソプロピルクロリドとノルマルペンタンとの混合物10質量部を加えて混合し、混合物の温度を5℃に調整した。作製した混合物の全量、さらに添加剤としてヘキサメチレンテトラミン(平均粒子径11μm)2質量部および酸硬化剤としてトルエンスルホン酸:キシレスルホン酸=約2:1(質量比)の混合物13.5質量部をピンミキサーにて撹拌、混合して発泡性レゾール型フェノール樹脂成形材料を調製した。引き続いて、フェノール樹脂発泡体の作製は、実施例1と同様にして実施した。得られた発泡体の物性を表1に示す。
実施例5において使用したヘキサメチレンテトラミン(平均粒子径11μm)2質量部に代えて、ポリエステルポリオール(粘度:1200mPa・S/25℃) 5質量部にヘキサメチレンテトラミン(平均粒子径5.2μm)2質量部を添加、混合して作製した混合物を用いる以外は、実施例5と同様にしてフェノール樹脂発泡体を作製した。この発泡体の物性を表1に示す。
実施例6において用いたヘキサメチレンテトラミンの粒度(平均粒子径5.2μm)を、粒度(平均粒子径35μm、実施例7)、粒度(平均粒子径50μm、実施例8)および粒度(平均粒子径70μm、実施例9)に変更した以外は、実施例6と同様にして3種類のフェノール樹脂発泡体を作製した。これらの発泡体の物性を表1に示す。
実施例5において、発泡剤として用いるイソプロピルクロリドとノルマルペンタンとの混合物の配合量を、10質量部から8質量部に変更する以外は、実施例5と同様にして密度40kg/m3のフェノール樹脂発泡体を作製した。この発泡体の物性を表1に示す。
実施例1において、ヘキサメチレンテトラミンの粒度(平均粒子径11μm)を、粒度(平均粒子径90μm)および粒度(平均粒子径141μm)に変更した以外は、実施例1と同様にして2種類のフェノール樹脂発泡体を作製した。これらの発泡体の物性を表2に示す。
実施例6において用いたヘキサメチレンテトラミンの粒度(平均粒子径5.2μm)を、粒度(平均粒子径90μm)に変更した以外は、実施例6と同様にしてフェノール樹脂発砲体を作製した。この発砲体の物性を表2に示す。
Claims (12)
- 液状レゾール型フェノール樹脂、発泡剤、整泡剤、酸硬化剤および添加剤を含む発泡性レゾール型フェノール樹脂成形材料であって、前記添加剤が、平均粒子径80μm以下の含窒素架橋型環式化合物であることを特徴とする、発泡性レゾール型フェノール樹脂成形材料。
- 含窒素架橋型環式化合物が、ヘキサメチレンテトラミンである、請求項1に記載の発泡性レゾール型フェノール樹脂成形材料。
- さらに、可塑剤を含む、請求項1または2に記載の発泡性レゾール型フェノール樹脂成形材料。
- 発泡剤が、イソプロピルクロリドを含む、請求項1~3のいずれか1項に記載の発泡性レゾール型フェノール樹脂成形材料。
- 請求項1~4のいずれか1項に記載の発泡性レゾール型フェノール樹脂成形材料を発泡硬化させてなることを特徴とする、フェノール樹脂発泡体。
- 密度が20~40kg/m3であって、pHが4.0以上、圧縮強さが10N/cm2以上および脆性が20%以下である、請求項5に記載のフェノール樹脂発泡体。
- 液状レゾール型フェノール樹脂、発泡剤、整泡剤、酸硬化剤および添加剤を含む発泡性レゾール型フェノール樹脂成形材料を製造する方法であって、前記液状レゾール型フェノール樹脂と前記酸硬化剤との混合において、前記添加剤として平均粒子径80μm以下の含窒素架橋型環式化合物を加えることを特徴とする、発泡性レゾール型フェノール樹脂成形材料の製造方法。
- 含窒素架橋型環式化合物が、ヘキサメチレンテトラミンである、請求項7に記載の方法。
- 含窒素架橋型環式化合物を、フェノール樹脂用可塑剤との混合物の形態で加える、請求項8に記載の方法。
- フェノール樹脂用可塑剤が、ポリエステルポリオール、ポリエーテルポリオールおよびグリコール類の中から選ばれる少なくとも1種である、請求項9に記載の方法。
- 発泡剤が、イソプロピルクロリドを含む、請求項7~10のいずれか1項に記載の方法。
- 液状レゾール型フェノール樹脂、発泡剤、整泡剤、酸硬化剤および添加剤をミキサーに供給し、攪拌・混合して得られた発泡性レゾール型フェノール樹脂組成物を、上下の面材間に注入し、加熱することで発泡・硬化させるフェノール樹脂成形材料を連続的に製造するに際し、含窒素架橋型環式化合物とフェノール樹脂用可塑剤とをプレ混合してなる前記添加剤をミキサーに供給する、請求項9~11のいずれか1項に記載の方法。
Priority Applications (6)
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EP10731315.7A EP2380931B1 (en) | 2009-01-19 | 2010-01-12 | Expandable resol-type phenolic resin molding material, method for producing the same, and phenolic resin foam |
CA2749760A CA2749760C (en) | 2009-01-19 | 2010-01-12 | Expandable resol-type phenolic resin molding material, method for producing the same, and phenolic resin foam |
CN201080005506.1A CN102300927B (zh) | 2009-01-19 | 2010-01-12 | 发泡性甲阶酚醛树脂型酚醛树脂成型材料及其制备方法以及酚醛树脂发泡体 |
US13/144,973 US20120016047A1 (en) | 2009-01-19 | 2010-01-12 | Expandable resol-type phenolic resin molding material, method for producing the same, and phenolic resin foam |
AU2010205139A AU2010205139C1 (en) | 2009-01-19 | 2010-01-12 | Expandable resol-type phenolic resin molding material, method for producing the same, and phenolic resin foam |
NZ594002A NZ594002A (en) | 2009-01-19 | 2010-01-12 | Expandable resol-type phenolic resin molding material, method for producing the same, and phenolic resin foam |
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JP2009008780 | 2009-01-19 | ||
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JP2009037371A JP5464863B2 (ja) | 2009-01-19 | 2009-02-20 | 発泡性レゾール型フェノール樹脂成形材料およびその製造方法ならびにフェノール樹脂発泡体 |
JP2009-037371 | 2009-02-20 |
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US (1) | US20120016047A1 (ja) |
EP (1) | EP2380931B1 (ja) |
JP (1) | JP5464863B2 (ja) |
KR (1) | KR101623614B1 (ja) |
CN (1) | CN102300927B (ja) |
AU (1) | AU2010205139C1 (ja) |
CA (1) | CA2749760C (ja) |
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KR20150145297A (ko) * | 2014-06-18 | 2015-12-30 | 주식회사 하우솔 | 페놀수지 발포체용 조성물 및 이를 이용하여 제조된 페놀수지 발포폼 보드 |
JP6946038B2 (ja) * | 2017-01-27 | 2021-10-06 | 旭化成建材株式会社 | フェノール樹脂発泡体積層板及びその製造方法 |
KR102356528B1 (ko) * | 2018-07-30 | 2022-01-26 | (주)엘엑스하우시스 | 페놀 수지 발포체, 이의 제조방법 및 이를 포함하는 단열재 |
JP2020124788A (ja) * | 2019-02-06 | 2020-08-20 | 旭化成建材株式会社 | 長尺状断熱材の製造方法 |
WO2021145492A1 (ko) * | 2020-01-17 | 2021-07-22 | (주)엘지하우시스 | 페놀 수지 발포체, 이의 제조방법 및 이를 포함하는 단열재 |
CN112724447A (zh) * | 2020-12-14 | 2021-04-30 | 苏州圣杰特种树脂有限公司 | 一种墙面保温酚醛树脂发泡材料及其制备方法 |
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- 2010-01-12 CN CN201080005506.1A patent/CN102300927B/zh active Active
- 2010-01-12 EP EP10731315.7A patent/EP2380931B1/en active Active
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Also Published As
Publication number | Publication date |
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CA2749760C (en) | 2016-08-16 |
EP2380931B1 (en) | 2014-06-25 |
CN102300927A (zh) | 2011-12-28 |
CN102300927B (zh) | 2014-12-31 |
KR101623614B1 (ko) | 2016-05-23 |
AU2010205139B2 (en) | 2013-02-28 |
KR20110117076A (ko) | 2011-10-26 |
EP2380931A1 (en) | 2011-10-26 |
AU2010205139C1 (en) | 2013-09-05 |
EP2380931A4 (en) | 2013-11-13 |
NZ594002A (en) | 2013-04-26 |
AU2010205139A1 (en) | 2011-07-28 |
US20120016047A1 (en) | 2012-01-19 |
JP2010185061A (ja) | 2010-08-26 |
JP5464863B2 (ja) | 2014-04-09 |
CA2749760A1 (en) | 2010-07-22 |
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