JPH0446076A - Production of porous material - Google Patents
Production of porous materialInfo
- Publication number
- JPH0446076A JPH0446076A JP15611390A JP15611390A JPH0446076A JP H0446076 A JPH0446076 A JP H0446076A JP 15611390 A JP15611390 A JP 15611390A JP 15611390 A JP15611390 A JP 15611390A JP H0446076 A JPH0446076 A JP H0446076A
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- JP
- Japan
- Prior art keywords
- powder
- resin
- sheet
- porous material
- mold
- Prior art date
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Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、特に水濡れ場所の床材として好適に使用され
る多孔性材料の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for producing a porous material that is particularly suitable for use as a flooring material for wet areas.
(従来の技術)
浴室などの水濡れ場所の床材として、無機粉粒体を不飽
和ポリエステル樹脂等の硬化性樹脂で結合した多孔性材
料を使用することは知られている。(Prior Art) It is known to use a porous material in which inorganic powder and granules are bonded with a curable resin such as an unsaturated polyester resin as a flooring material for a place that gets wet with water such as a bathroom.
この種の多孔性材料は、一般に無機粉粒体と不飽和ポリ
エステル樹脂などの硬化性樹脂液とを混合した粉粒体を
、常温プレス機或いは熱プレス機により加圧成形するこ
とにより製造される(例えば実開平2−.11937号
公報参照)。This type of porous material is generally produced by pressure-molding a mixture of inorganic powder and curable resin liquid such as unsaturated polyester resin using a room temperature press machine or a hot press machine. (For example, see Utility Model Application Publication No. 11937/1993).
(発明が解決しようとする課題)
ところが、このように無機粉粒体と硬化性樹脂液とを混
合してこの樹脂液で湿り状態にした粉粒体は、一般に二
次凝集などにより粒度のばらつきが大きくなっている。(Problem to be Solved by the Invention) However, the powder and granules obtained by mixing an inorganic powder and a curable resin liquid and moistening them with the resin liquid generally have variations in particle size due to secondary aggregation, etc. is getting bigger.
このような粉粒体をプレス機により加圧成形する場合は
、粉粒体間に存在する大きな空間が良好に埋められない
。When such granular materials are pressure-molded using a press machine, the large spaces existing between the granular materials cannot be filled satisfactorily.
そのため、得られる多孔性材料の孔径が不揃いとなり、
孔径を一定の範囲に調節することが容易でな(、水濡れ
時の滑り防止や汚れ防止が充分に行えないことがある。As a result, the pore diameters of the resulting porous material become uneven,
It is difficult to adjust the pore diameter within a certain range (or it may not be possible to sufficiently prevent slipping or staining when wet with water).
本発明は、このような従来方法における問題を解決する
ものであり、その目的とするところは、孔径が揃った多
数の微細孔を有し、水濡れ時においても滑り防止や汚れ
防止を確実に行うことのできる多孔性材料の製造方法を
提供することにある。The present invention solves these problems with conventional methods, and its purpose is to have a large number of fine pores with uniform diameters, and to ensure prevention of slipping and staining even when wet with water. An object of the present invention is to provide a method for manufacturing a porous material that can be carried out.
(課題を解決するための手段)
本発明において、請求項1記載の多孔性材料の製造方法
は、無機粉粒体に硬化性樹脂液を混合してこの樹脂液で
湿り状態にされた粉粒体を、弾性変形或いは塑性変形の
可能なシート状物を介して加圧しながら若しくは加圧し
たあと樹脂を硬化させることを特徴とする
請求項2記載の多孔性材料の製造方法は、無機粉粒体に
硬化性樹脂液を混合してこの樹脂液で湿り状態にされた
粉粒体を成形型内で気体不透過性シートで覆い、粉粒体
間の空気を減圧脱気した後、弾性変形或いは塑性変形の
可能なシート状物を介して加圧しながら若しくは加圧し
たあと樹脂を硬化させることを特徴とする。(Means for Solving the Problems) In the present invention, a method for producing a porous material according to claim 1 is characterized in that a curable resin liquid is mixed with an inorganic powder and granules are wetted with the resin liquid. The method for producing a porous material according to claim 2, wherein the resin is cured while or after the body is pressurized through a sheet-like material capable of elastic deformation or plastic deformation. A curable resin liquid is mixed into the body, the powder and granules are moistened with this resin liquid, and then covered with a gas-impermeable sheet in a mold, and after degassing the air between the powder and granules under reduced pressure, the particles are elastically deformed. Alternatively, the resin is cured while or after being pressurized through a sheet-like material that can be plastically deformed.
本発明において、無機粉粒体としては、石英、カオリン
、クレー、珪砂、天然石粉砕粉などの無機粉粒体、天然
鉱物繊維、ガラスミルドファイバー、アルミナ短繊維、
チタン酸カリウム短繊維、カーボン短繊維、ボイスカー
などの無機短繊維の粉体が用いられる。In the present invention, inorganic powders include inorganic powders such as quartz, kaolin, clay, silica sand, and crushed natural stone powder, natural mineral fibers, glass milled fibers, alumina short fibers,
Powders of inorganic short fibers such as potassium titanate short fibers, carbon short fibers, and voice car are used.
無機粉粒体の最大粒径は1000μ−以下が好ましい。The maximum particle size of the inorganic powder is preferably 1000 μm or less.
なお、無機短繊維の粉体の場合は、繊維の太さが平均で
300μ醜以下が望ましい。最大粒径1000μ−を越
えると、得られる多孔性材料の表面に開孔した孔径が大
きくなり、塵芥などが孔に侵入し汚れやすくなる。In addition, in the case of powder of inorganic short fibers, it is desirable that the average thickness of the fibers is 300 μm or less. When the maximum particle size exceeds 1000 .mu.-, the pores formed on the surface of the resulting porous material become large, and dirt and the like easily enter the pores and become dirty.
また、硬化性樹脂としては、不飽和ポリエステル樹脂、
ジアリルフタレート樹脂、エポキシ樹脂、フェノール樹
脂、ウレタン樹脂、ビニルエステル樹脂、エポキシアク
リレート樹脂、アクリル樹脂などに、有機過酸化物、ア
ミン系、酸無水物等の慣用の硬化剤や触媒を配合した常
温硬化性或いは熱硬化性の樹脂が用いられ、必要に応じ
て硬化促進剤が配合される。In addition, as the curable resin, unsaturated polyester resin,
Room temperature curing made by blending diallyl phthalate resin, epoxy resin, phenol resin, urethane resin, vinyl ester resin, epoxy acrylate resin, acrylic resin, etc. with conventional curing agents and catalysts such as organic peroxides, amines, acid anhydrides, etc. A thermosetting or thermosetting resin is used, and a curing accelerator is added if necessary.
硬化性樹脂は液状で使用され、その粘度は重合性モノマ
ーや樹脂の重合度などにより常温で100ボイズ以下に
調整するのが望ましい。粘度が常温で100ボイズより
も高いと、粉粒体の二次凝集が多くなり、得られる多孔
性材料の孔径が大きくまた不均一になり、塵芥などが孔
に侵入し汚れやすくなる。The curable resin is used in liquid form, and its viscosity is desirably adjusted to 100 voids or less at room temperature, depending on the polymerizable monomer and the degree of polymerization of the resin. If the viscosity is higher than 100 voids at room temperature, secondary aggregation of the powder particles will increase, the resulting porous material will have large and non-uniform pore diameters, and dirt will easily enter the pores and become dirty.
無機粉粒体に硬化性樹脂液を混合する方法としては、無
機粉粒体に少量の硬化性樹脂液を加えこれを攪拌する方
法、或いはm機粉粒体に少量の硬化性樹脂液を噴霧して
含浸させる方法が一般に採られる。この場合、両者の混
合を行った後これを成形型内に入れてもよく、両者の混
合を成形型内で行うようにしてもよい。The method of mixing the curable resin liquid with the inorganic powder is to add a small amount of the curable resin liquid to the inorganic powder and stir it, or to spray a small amount of the curable resin liquid onto the m machine powder. The method of impregnation is generally adopted. In this case, both may be mixed and then put into a mold, or both may be mixed within the mold.
無機粉粒体に硬化性樹脂液を混合する際の混合量は、無
機粉粒体がこの樹脂液で湿り状態にされ粉粒体の状態が
保持焙れる程度とされ、無機粉粒体の種類や粒度、硬化
性樹脂液の種類や粘度、加圧成形条件などを考慮して決
められる。When mixing the curable resin liquid with the inorganic powder, the mixing amount is such that the inorganic powder is moistened with the resin liquid and the powder state is maintained. It is determined by taking into consideration factors such as the particle size, type and viscosity of the curable resin liquid, and pressure molding conditions.
一般に、嵩体積比で無機粉粒体1に対し硬化性樹脂液0
.05〜0.5の範囲で調製するのが好ましい。この際
、各種頭重を混合して着色してもよい。このようにして
、無機粉粒体が硬化性樹脂液で湿り状態にされた粉粒体
が作られる。Generally, the bulk volume ratio is 1 part of inorganic powder to 0 part of curable resin liquid.
.. It is preferable to prepare within the range of 0.05 to 0.5. At this time, various head weights may be mixed and colored. In this way, a powder or granule in which the inorganic powder or granule is moistened with the curable resin liquid is produced.
この粉粒体は、剥離性の板状型や平たい箱状型などの所
望の成形型内で、これに弾性変形或いは塑性変形の可能
なシート状物が載せられ、このシート状物を介して、例
えば常温〜150°Cf7)in、1〜150 kg/
cniの圧力でプレス機等の加圧機により加圧される。This powder or granular material is placed in a desired mold such as a peelable plate-shaped mold or a flat box-shaped mold, and a sheet-like material that can be elastically or plastically deformed is placed thereon. , for example, room temperature to 150°Cf7)in, 1 to 150 kg/
It is pressurized with a pressure machine such as a press machine at a pressure of cni.
硬化性樹脂液はプレス機等により加圧されながら硬化す
る。若しくはプレス機等による加圧後に、例えば常温又
は150″C以下の温度に加熱されて硬化する。プレス
機としては、空気圧又は油圧シリンダーで上下に移動す
る慣用のプレス装置が使用される。The curable resin liquid is cured while being pressurized by a press or the like. Alternatively, after being pressurized by a press or the like, it is heated to, for example, room temperature or a temperature of 150''C or less to harden.As the press, a conventional press device that moves up and down with a pneumatic or hydraulic cylinder is used.
弾性変形の可能なシート状物としては、ゴムシート、プ
ラスチック発泡シート、不織布、フェルト等が用いられ
、塑性変形の可能なシートとしては、高粘性流体を封入
したブラスチンクシート、粘土ペーストのようなペース
ト状シート等が用いられる。Examples of sheets that can be elastically deformed include rubber sheets, plastic foam sheets, nonwoven fabrics, felt, etc. Examples of sheets that can be plastically deformed include brass sheets filled with highly viscous fluid, clay paste, etc. A paste sheet or the like is used.
弾性変形或いは塑性変形の可能なシート状物を成形型内
の粉粒体に載せる際に、成形型内の粉粒体を気体不透過
性シートで覆い、粉粒体間の空気を減圧脱気しておくの
が好ましい。When placing a sheet-like material that can be elastically or plastically deformed onto the powder in the mold, the powder in the mold is covered with a gas-impermeable sheet and the air between the powder and granules is degassed under reduced pressure. It is preferable to keep it.
気体不透過性シートとしては、ポリエチレン、ポリプロ
ピレン、ポリエステル、ナイロン等のプラスチックシー
トが使用される。この気体不透過性シートの縁辺は、粉
粒体の入った成形型の縁上面或いは縁側面にシーラント
やシール枠等により気密にシールされる。そして、成形
型の一部に形成された一個或いは複数個の減圧孔から内
部の空気が真空ポンプで吸引され、それにより粉粒体間
の空気が減圧脱気される。内部の圧力は、400mmH
g以下、モノマー等の1気圧以上とするのが望ましい。As the gas-impermeable sheet, a plastic sheet such as polyethylene, polypropylene, polyester, or nylon is used. The edge of this gas-impermeable sheet is airtightly sealed with a sealant, a sealing frame, or the like to the upper or side surface of the edge of the mold containing the powder or granules. Then, internal air is sucked in by a vacuum pump through one or more decompression holes formed in a part of the mold, thereby depressurizing and deaerating the air between the particles. Internal pressure is 400mmH
It is preferable that the pressure be less than 10 g and 1 atm or more for monomers, etc.
なお、気体不透過性シートや弾性変形或いは塑性変形の
可能なシート状物は、通常は加圧成形のあと剥離除去さ
れるが、得られる多孔性材料に接着している場合は、こ
れらのシート材料は多孔性材料の裏面となるので、加圧
成形後にこれらのシート材料を剥離除去する必要はない
。Note that gas-impermeable sheets and sheet-like materials that can be elastically or plastically deformed are usually peeled off after pressure forming, but if they are adhered to the resulting porous material, these sheets There is no need to peel away these sheet materials after pressing, as the material becomes the back side of the porous material.
このようにして、硬化性樹脂液が常温或いは加熱により
硬化され、それにより無機粉粒体が硬化性樹脂により結
合され、表面(成形型面に接する側の表面)に孔径の揃
った多数の微細孔が開孔した多孔性材料が得られる。In this way, the curable resin liquid is cured at room temperature or by heating, and as a result, the inorganic powder and granules are bonded by the curable resin, and a large number of fine pores with uniform diameters are formed on the surface (the surface in contact with the mold surface). A porous material with open pores is obtained.
(作用)
本発明方法において、無機粉粒体に硬化性樹脂液を混合
してこの樹脂液で湿り状態にされた粉粒体を、弾性変形
或いは塑性変形の可能なシート状物を介してプレス等に
より加圧すると、粉粒体に二次凝集などによる大きな粒
度のばらつきがあっても、上記シート状物の変形作用に
より粉粒体の全体にかかる押圧力が均一化されて、粉粒
体間に存在する大きな空間が良好に埋められる。その結
果、孔径がよく揃った多孔性材料が得られる。(Function) In the method of the present invention, inorganic powder and granules are mixed with a curable resin liquid, and the powder and granules moistened with the resin liquid are pressed through a sheet-like material that can be elastically or plastically deformed. Even if there is a large variation in particle size due to secondary agglomeration, etc., the pressing force applied to the entire powder or granule is made uniform by the deformation effect of the sheet-like material, and the powder or granule is The large spaces that exist in between are well filled. As a result, a porous material with well-uniformed pore sizes is obtained.
また、この場合、成形型内の粉粒体を気体不透過性シー
トで覆い、粉粒体間の空気を減圧脱気しておくと、加圧
後に常圧に開放された際に復元して開孔が大きくなるこ
とが防止され、より効果的である。しかも粉粒体の間に
空気(酸素)が殆ど存在しな(なるので、硬化反応が酸
素により主書されずに速やかに硬化が進行する。In addition, in this case, if the powder and granules in the mold are covered with a gas-impermeable sheet and the air between the powder and granules is degassed under reduced pressure, it will be restored to its original state when it is released to normal pressure after pressurization. This prevents the openings from becoming larger and is more effective. Moreover, since there is almost no air (oxygen) between the particles, the curing reaction is not dominated by oxygen and the curing proceeds rapidly.
(実施例) 以下、本発明の実施例及び比較例を示す。(Example) Examples and comparative examples of the present invention are shown below.
実施上]
カーボンミルドファイバー繊維(平均繊維長300μ鵠
)と、熱硬化性エポキシ樹脂(40ボイズ)(樹脂エピ
コート828と硬化剤エビキュアYH−306:油化シ
ェルエポキシ社製)とを、嵩体積比で前者1に対し後者
0.30の割合で均一に混合して湿り状態の粉粒体を作
った。In practice] Carbon milled fiber fibers (average fiber length 300 μm) and thermosetting epoxy resin (40 voids) (resin Epikote 828 and curing agent Ebicure YH-306: manufactured by Yuka Shell Epoxy Co., Ltd.) were mixed in a bulk volume ratio. The former was mixed uniformly at a ratio of 1 to the latter at a ratio of 0.30 to prepare a wet powder.
この粉粒体を平たい箱状の成形型に均一に敷き詰め、そ
の上に羊毛フェルト(厚さ20mm)を載せ、これを常
温のプレース機で油圧シリンダー圧力を40 kg /
cjで加圧したあと120°Cに加熱して樹脂を硬化
させ、羊毛フェルトを除去し脱型して、無機粉粒体が硬
化性樹脂で結合され、表面に孔径の揃った微細な孔が開
孔した不透水性の多孔体からなる厚さ6柵の多孔性材料
を製造した。This granular material was evenly spread in a flat box-shaped mold, a wool felt (thickness 20 mm) was placed on top of it, and a hydraulic cylinder pressure of 40 kg/cm was applied using a press machine at room temperature.
After pressurizing with cj, heating to 120°C to harden the resin, removing the wool felt and demolding, the inorganic powder and granules are bonded with a hardening resin, and fine pores with uniform diameter are formed on the surface. A porous material with a thickness of 6 bars consisting of an open, water-impermeable porous body was produced.
この多孔性材料について、滑りにくさ、汚れにくさ、細
孔の直径、細孔の容積を次の方法により測定し評価した
。その結果を第1表に示す。This porous material was evaluated by measuring its slip resistance, stain resistance, pore diameter, and pore volume using the following methods. The results are shown in Table 1.
(1)滑りにくさは、水濡れ状態の多孔性材料の表面に
30唾×50=の合成皮革片を重ね、これに2kgの荷
重を載せ、傾斜法で摩擦係数を測定し、摩擦係数が0.
8以上を○、0.8未満〜0.6を△、0.6未満を×
で表した。(1) Slip resistance was measured by stacking 30 x 50 pieces of synthetic leather on the surface of a porous material in a wet state, placing a 2 kg load on it, and measuring the friction coefficient using the inclination method. 0.
8 or more: ○, less than 0.8 to 0.6: △, less than 0.6: ×
It was expressed as
(2)汚れにくさは、タルク粉末(粒径10μM以下)
を0.2 g /ccの割合に水中に分散させ、この分
散液を100皿×1100ff1Iの多孔性材料の表面
に50cc散布し、タルク粉末が表面に残り、後で洗い
流すことが可能な場合をO、タルク粉末が表面の細孔で
目詰りを起す場合を×で表した。(2) Stain resistance is determined by talc powder (particle size 10μM or less)
was dispersed in water at a rate of 0.2 g/cc, and 50 cc of this dispersion was sprinkled on the surface of a porous material of 100 dishes x 1100 ff1I, and the talc powder remained on the surface and could be washed off later. O indicates that the talc powder causes clogging in the pores on the surface.
(3)細孔の直径は、水銀式ボロンメーターで測定して
、孔径20μ肩以下の孔が95%以上の場合をO1孔径
20μI以下の孔が95%未満の場合を×で表した。(3) The diameter of the pores was measured with a mercury boron meter, and the case where 95% or more of the pores had a pore diameter of 20 μl or less was represented by an x, and the case where the number of pores with a pore diameter of 20 μl or less was less than 95% was represented by an x.
(4)細孔の容積は、水銀式ポロシメーターで測定して
、0.05cc/g以上を○、0.05cc/g未満を
×で表した。(4) The volume of the pores was measured with a mercury porosimeter, and 0.05 cc/g or more was represented by ○, and less than 0.05 cc/g was represented by ×.
ス麓11
大理石粉砕粉(240メツシユパス)を平たい箱状成形
型に均一に敷き詰め、これに硬化剤(バーへキサ3−二
日本油脂社製)を1.5重量%含有する熱硬化性エポキ
シアクリレート樹脂(35ボイズ)を、嵩体積比で前者
1に対し後者0.27の割合で噴霧し含浸した。Foothills 11 Pulverized marble powder (240 mesh passes) is evenly spread in a flat box-shaped mold, and thermosetting epoxy acrylic resin containing 1.5% by weight of a hardening agent (manufactured by Barhexa 3-2 Nippon Oil & Fats Co., Ltd.) A resin (35 voids) was sprayed and impregnated at a bulk volume ratio of 1 to 0.27 of the latter.
その上を粘土ペーストでシート状(厚さ約5mm)に覆
い、これを常温のプレス機で油圧シリンダー圧力10k
g/c+flで加圧したあと粘土ペーストを除去し、1
00°Cに加熱して樹脂を硬化させその後脱型して、無
機粉粒体が硬化性樹脂で結合され、表面に孔径の揃った
微細な孔が開孔した不透水性の多孔体からなる厚さ6m
mの多孔性材料を製造した。Cover the top with clay paste in the form of a sheet (approx. 5mm thick), and press this with a press machine at room temperature to a hydraulic cylinder pressure of 10k.
After applying pressure with g/c+fl, remove the clay paste and
The product is heated to 00°C to harden the resin, then removed from the mold, and the inorganic powder is bonded with a curable resin to form a water-impermeable porous body with fine pores of uniform diameter on the surface. 6m thick
m porous materials were produced.
二の多孔性材料について、滑りにくさ、汚れにくさ、細
孔の直径、細孔の容積を次の方法により測定し評価した
。その結果を第1表に示す。Regarding the second porous material, slip resistance, stain resistance, pore diameter, and pore volume were measured and evaluated using the following methods. The results are shown in Table 1.
1五倣l
白雲母粉末(200メツシユバス)と、硬化剤(ベンゾ
イルパーオキサイド)2重量%を含有する熱硬化性不飽
和ポリエステル樹脂のスチレン溶液(1ボイズ)とを、
嵩体積比で前者lに対し後者0.25の割合で均一に混
合して湿り状態の粉粒体を作った。15 copies of muscovite powder (200 mesh baths) and a styrene solution of thermosetting unsaturated polyester resin (1 void) containing 2% by weight of a hardening agent (benzoyl peroxide),
A wet granular material was prepared by uniformly mixing the former at a bulk volume ratio of 1 to 0.25 of the latter.
この粉粒体を平たい箱状の成形型に均一に敷き詰め、そ
の上にウレタンゴムシート(厚さ10m)を載せ、これ
をプレス機で温度80°C1油圧シリンダー圧力50k
g/c−で加圧して樹脂を硬化させ、ウレタンゴムシー
トを除去し脱型して、無機粉粒体が硬化性樹脂で結合さ
れ、表面に孔径の揃った微細な孔が開孔した不透水性の
多孔体からなる厚さ611II11の多孔性材料を製造
した。Spread this powder uniformly in a flat box-shaped mold, place a urethane rubber sheet (thickness 10m) on top of it, and press it with a press at a temperature of 80°C and a hydraulic cylinder pressure of 50k.
The resin is cured by applying pressure at g/c-, the urethane rubber sheet is removed and the mold is demolded, and the inorganic powder is bonded with the curable resin to form a non-woven material with fine pores of uniform diameter on the surface. A porous material made of a water-permeable porous body and having a thickness of 611II11 was produced.
この多孔性材料について、滑りにくさ、汚れにくさ、細
孔の直径、細孔の容積を次の方法により測定し評価した
。その結果を第1表に示す。This porous material was evaluated by measuring its slip resistance, stain resistance, pore diameter, and pore volume using the following methods. The results are shown in Table 1.
夫施桝土
カーボンミルドファイバー(平均繊維長300μm)と
、硬化剤(ヘンシイルバーオキサイド)2重量%を含有
する熱硬化性エポキシアクリレート樹脂(12ボイズ)
とを、嵩体積比で前者1に対し後者0.15の割合で均
一に混合して湿り状態の粉粒体を作った。Thermosetting epoxy acrylate resin (12 voids) containing Fuse Masudo carbon milled fiber (average fiber length 300 μm) and 2% by weight of hardening agent (hensilver oxide)
were uniformly mixed in a bulk volume ratio of 1 to 0.15 of the latter to prepare a wet powder.
この粉粒体を平たい箱状の成形型に均一に敷き詰め、そ
の上をナイロンシートで覆い、その縁辺を成形型の上縁
でシールし、その上に羊毛フェルト(厚さlOam)を
載せ、成形型内を減圧脱気して、これをプレス機で温度
80°C5油圧シリンダー圧力50kg/c+Jで加圧
して樹脂を硬化させ、ナイロンシートと羊毛フェルトを
除去し脱型して、無機粉粒体が硬化性樹脂で結合され、
表面に孔径の揃った微細な孔が開孔した不透水性の多孔
体からなる厚さ6鵬の多孔性材料を製造した。Spread this powder uniformly in a flat box-shaped mold, cover it with a nylon sheet, seal the edges with the upper edge of the mold, place wool felt (thickness 1 Oam) on top of it, and mold it. The inside of the mold is degassed under reduced pressure, and the resin is hardened by pressurizing it with a press machine at a temperature of 80°C and a hydraulic cylinder pressure of 50kg/c+J.The nylon sheet and wool felt are removed and demolded to produce inorganic powder. are combined with a curable resin,
A porous material with a thickness of 6 mm consisting of a water-impermeable porous body with fine pores of uniform pore size on its surface was produced.
この多孔性材料について、滑りにくさ、汚れにくさ、細
孔の直径、細孔の容積を次の方法により測定し評価した
。その結果を第1表に示す。This porous material was evaluated by measuring its slip resistance, stain resistance, pore diameter, and pore volume using the following methods. The results are shown in Table 1.
1隻■五
大理石粉砕粉(180メンシユバス)と、硬化剤(メチ
ルエチルケトンパーオキサイド)1重量%を含有する熱
硬化性不飽和ポリエステル樹脂(10ボイズ)とを、嵩
体積比で前者1に対し後者0.15の割合で均一に混合
して湿り状態の粉粒体を作った。1 vessel ■ Five marble crushed powder (180 mensius) and a thermosetting unsaturated polyester resin (10 voids) containing 1% by weight of a hardening agent (methyl ethyl ketone peroxide), with a bulk volume ratio of 1 for the former to 0 for the latter. They were uniformly mixed at a ratio of .15 to produce a wet powder.
この粉粒体を平たい箱状の成形型に均一に敷き詰め、そ
の上をポリエステルシートで覆い、その縁辺を成形型の
上縁でシールし、その上にニトリルゴムシート(厚さ7
am)を載せ、成形型内を減圧脱気して、これをプレス
機で温度60°C2油圧シリンダー圧力30 kg /
dで加圧して樹脂を硬化させ、ポリエステルシートと
ニトリルゴムシートを除去し脱型し、無機粉粒体が硬化
性樹脂で結合され、表面に孔径の揃った微細な孔が開孔
した不透水性の多孔体からなる厚さ6鴫の多孔性材料を
製造した。Spread this powder uniformly in a flat box-shaped mold, cover it with a polyester sheet, seal the edges with the upper edge of the mold, and place a nitrile rubber sheet (thickness 7
am), the inside of the mold was depressurized and degassed, and this was pressed in a press at a temperature of 60°C and a hydraulic cylinder pressure of 30 kg/
d to harden the resin, remove the polyester sheet and nitrile rubber sheet and demold, and the inorganic powder is bonded with a curable resin to form an impermeable surface with fine pores of uniform diameter. A porous material having a thickness of 6 mm was produced.
この多孔性材料について、滑りにくさ、汚れにくさ、細
孔の直径、細孔の容積を次の方法により測定し評価した
。その結果を第1表に示す。This porous material was evaluated by measuring its slip resistance, stain resistance, pore diameter, and pore volume using the following methods. The results are shown in Table 1.
夾五性旦
白雲母粉末(200メツシユバス)を平たい箱状の成形
型に均一に敷き詰め、これに硬化剤(ベンゾイルパーオ
キサイド)2重量%を含有する熱硬化性不飽和ポリエス
テル樹脂のスチレン溶液(1ボイズ)を、嵩体積比で前
者1に対し後者0.25の割合で噴霧し含浸させた。Powdered muscovite mica powder (200 mesh) was evenly spread in a flat box-shaped mold, and a styrene solution of thermosetting unsaturated polyester resin containing 2% by weight of a hardening agent (benzoyl peroxide) (1 Boise) was sprayed and impregnated at a bulk volume ratio of 1 to 0.25 of the latter.
その上をポリエステルシートで覆い、その縁辺を成形型
の上縁でシールし、その上を粘土ペーストでシート状(
厚さ3El11)に覆い、成形型内を減圧脱気して、こ
れを常温のプレス機で油圧シリンダー圧力50 kg
/ cllNで加圧した後、80°Cに加熱して樹脂を
硬化させ、ポリエステルシートと粘土を除去し脱型して
、無機粉粒体が硬化性樹脂で結合され、表面に孔径の揃
った微細な孔が開孔した不透水性の多孔体からなる厚さ
6閣の多孔性材料を製造した。Cover it with a polyester sheet, seal its edges with the upper edge of the mold, and cover it with clay paste to form a sheet (
The inside of the mold was depressurized and degassed, and then pressed in a press machine at room temperature under a hydraulic cylinder pressure of 50 kg.
/ After pressurizing with cllN, heating to 80°C to harden the resin, removing the polyester sheet and clay and demolding, the inorganic powder and granules are bonded with a hardening resin, and the surface has a uniform pore size. A porous material with a thickness of 6 mm consisting of a water-impermeable porous body with minute pores was produced.
この多孔性材料について、滑りにくさ、汚れにくさ、細
孔の直径、細孔の容積を次の方法により測定し評価した
。その結果を第1表に示す。This porous material was evaluated by measuring its slip resistance, stain resistance, pore diameter, and pore volume using the following methods. The results are shown in Table 1.
L校外上
羊毛フェルトを使用せず、それ以外は実施例1と同様に
行った。The same procedure as in Example 1 was carried out except that the wool felt was not used on the outer surface of L.
比較性l
粘土ペーストを使用せず、それ以外は実施例2と同様に
行った。Comparison 1 The same procedure as in Example 2 was carried out except that clay paste was not used.
ル較且l
ウレタンゴムシートを使用せず、それ以外は実施例3と
同様に行った。Comparison Example 3 The same procedure as in Example 3 was carried out except that the urethane rubber sheet was not used.
(以下余白)
第1表
(発明の効果)
上述の通り、本発明の製造方法によれば、無機粉粒体に
硬化性樹脂液を混合してこの樹脂で湿り状態にされた粉
粒体が、弾性変形或いは望性変形可能なシート状物を介
して加圧されて樹脂が硬化するので、無機旬粒体が硬化
性樹脂で結合され、表面に孔径の揃った微細な孔が開孔
した不透水性の多孔性材料が得られる。(Margins below) Table 1 (Effects of the Invention) As mentioned above, according to the production method of the present invention, the granular material is mixed with an inorganic powder material and a curable resin liquid, and the powder material is moistened with this resin. As the resin is hardened by applying pressure through a sheet-like material that can be elastically or desirably deformed, the inorganic particles are bonded with the hardening resin, and fine pores with uniform diameters are formed on the surface. A water-impermeable porous material is obtained.
二のように表面の孔径が揃うと一定の孔径範囲に設定す
ることが容易となり、水濡れ時の滑り防止や目詰りによ
る汚れ防止が確実に行える。When the pore diameters on the surface are uniform as shown in 2, it becomes easy to set the pore diameter within a certain range, and it is possible to reliably prevent slipping when wet with water and prevent stains due to clogging.
また、粉粒体間の空気を減圧脱気する場合は、硬化が速
まり生産性が向上するという利点がある。Further, when the air between the powder particles is degassed under reduced pressure, there is an advantage that curing is accelerated and productivity is improved.
したがって、本発明方法により得られる多孔性材料は、
浴室、便所、調理室、玄関、ベランダ、シャワールーム
、プールサイド、歩道などにおいて、滑り止め効果を期
待した床材やカウンター、テーブルや吸放湿壁材、防音
建材等に好適に使用することができる。Therefore, the porous material obtained by the method of the present invention is
Suitable for use in bathrooms, toilets, galleys, entrances, balconies, shower rooms, poolsides, walkways, etc., for flooring, counters, tables, moisture absorbing/releasing wall materials, soundproofing building materials, etc. with anti-slip properties. can.
Claims (1)
湿り状態にされた粉粒体を、弾性変形或いは塑性変形の
可能なシート状物を介して加圧しながら若しくは加圧し
たあと樹脂を硬化させることを特徴とする多孔性材料の
製造方法。 2、無機粉粒体に硬化性樹脂液を混合してこの樹脂液で
湿り状態にされた粉粒体を成形型内で気体不透過性シー
トで覆い、粉粒体間の空気を減圧脱気した後、弾性変形
或いは塑性変形の可能なシート状物を介して加圧しなが
ら若しくは加圧したあと樹脂を硬化させることを特徴と
する多孔性材料の製造方法。[Claims] 1. Inorganic powder and granules are mixed with a curable resin liquid, and the powder and granules moistened with the resin liquid are processed through a sheet-like material that can be elastically or plastically deformed. A method for producing a porous material, characterized by curing the resin while or after applying pressure. 2. Mix a curable resin liquid with an inorganic powder, cover the powder moistened with the resin liquid with a gas-impermeable sheet in a mold, and degas the air between the powder and granules under reduced pressure. After that, the resin is cured while being pressurized through a sheet-like material capable of elastic deformation or plastic deformation, or after being pressurized.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15611390A JPH0446076A (en) | 1990-06-14 | 1990-06-14 | Production of porous material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15611390A JPH0446076A (en) | 1990-06-14 | 1990-06-14 | Production of porous material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0446076A true JPH0446076A (en) | 1992-02-17 |
Family
ID=15620599
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15611390A Pending JPH0446076A (en) | 1990-06-14 | 1990-06-14 | Production of porous material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0446076A (en) |
-
1990
- 1990-06-14 JP JP15611390A patent/JPH0446076A/en active Pending
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