JPH0446071A - Production of porous material - Google Patents
Production of porous materialInfo
- Publication number
- JPH0446071A JPH0446071A JP15610890A JP15610890A JPH0446071A JP H0446071 A JPH0446071 A JP H0446071A JP 15610890 A JP15610890 A JP 15610890A JP 15610890 A JP15610890 A JP 15610890A JP H0446071 A JPH0446071 A JP H0446071A
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- JP
- Japan
- Prior art keywords
- powder
- resin
- mold
- porous material
- pressure
- Prior art date
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Abstract
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. 2-11937).
(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、−S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, in this way, the powder and granule obtained by mixing an inorganic powder and a curable resin liquid and making it wet with this resin liquid have a particle size change due to secondary aggregation in -S. The dispersion is increasing.
このような粉粒体をローラーを用いずに、上型下型など
からなる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 including an upper mold and a lower mold without using rollers, 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く、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 not easy to adjust the pore diameter within a certain range, and 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、ローラー
により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ローラーにより加圧しながら
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. Claim 2, characterized in that the body is covered with a gas-impermeable sheet in a mold, the air between the particles is degassed under reduced pressure, and then the resin is cured while or after being pressurized by a roller. The method for manufacturing porous materials is to mix inorganic powder and granules with a curable resin liquid, cover the powder and granules moistened with the resin liquid with a gas-impermeable sheet in a mold, and then After the air between them is degassed under reduced pressure, the resin is cured while being pressurized by a roller or after being pressurized through a sheet-like material that can be elastically or 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頗以下が好ましい。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
300μm以下が望ましい。最大粒径1000μm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 μm, 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1、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
して硬化促進剤が配合される。In addition, as the curable resin, unsaturated polyester resin,
Organic peroxide, diallyl phthalate resin, epoxy resin, phenol resin, urethane resin 1, vinyl ester resin, epoxy acrylate resin, acrylic resin, etc.
Room-temperature curable or thermosetting resins containing conventional curing agents and catalysts such as amines and acid anhydrides are used, and if necessary, curing accelerators are added.
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、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, the degree of polymerization of the resin, etc. 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撹拌する方
法、或いは無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大木でもよく、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 inorganic powder. Generally, the method of impregnating the In this case, the two may be mixed and then placed in the mold, or the two may be mixed in 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
保持される程度とされ、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 maintains the powder state. 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の範囲で調製される。この際、各種顔料
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 prepared in the range of 0.05 to 0.5. At this time, it may be colored by mixing various pigments. 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、気体不通過性シートで覆われる。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フクシートが
使用される。This granular material is covered with a gas-impermeable sheet in a desired mold such as a peelable plate-shaped mold or a flat box-shaped mold. As the gas-impermeable sheet, a plastic sheet made of polyethylene, polypropylene, polyester, nylon, etc. is used.
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
ンプで吸弓され、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400 mHg以下、モノマー等
の蒸気圧以上とするのが好ましい。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, air inside the mold is sucked 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. The internal pressure is preferably 400 mHg or less and higher than the vapor pressure of monomers, etc.
減圧脱気された粉粒体の入った成形型は、ロール加圧機
に移送され、例えば常温〜150″Cの温度、1〜15
0 kg/c4の圧力でローラー加圧機により加圧され
る。ローラー加圧機としては、一般に上下に配置された
一組以上の回転駆動可能な押圧ロールからなり、上方の
ロールは加熱可能で且つ油圧シリンダーで下方のロール
に押圧可能になされた装置が使用されるが、場合によっ
ては、上方ロールと下型とからなる加圧機を用いてもよ
い。The mold containing the powder and granules that has been degassed under reduced pressure is transferred to a roll press machine and heated at a temperature of, for example, room temperature to 150"C, 1 to 15"C.
Pressure is applied by a roller presser at a pressure of 0 kg/c4. As a roller press machine, a device is generally used that consists of one or more sets of rotatably driven press rolls arranged one above the other, with the upper roll being able to be heated and being able to be pressed against the lower roll by a hydraulic cylinder. However, in some cases, a press machine consisting of an upper roll and a lower die may be used.
粉粒体を入れた成形型は、上記のようなローラー加圧機
の上下ロールの間に移送され、油圧シリンダーによる一
定圧力で且つ一定の温度で加圧される。硬化性樹脂はロ
ーラーによる加圧中に硬化する場合と、ローラーによる
加圧後に例えば常温で又は150°C以下の温度に加熱
して硬化させる場合とがある。The mold containing the granular material is transferred between the upper and lower rolls of the roller press machine as described above, and is pressurized by a hydraulic cylinder at a constant pressure and at a constant temperature. The curable resin may be cured while being pressed by a roller, or may be cured after being pressurized by a roller, for example, at room temperature or by heating to a temperature of 150° C. or less.
加圧成形の際に、粉粒体を覆っている気体不透過性シー
トの上に弾性変形或いは塑性変形の可能なシート状物を
載せ、このシート状物を介してローラーにより加圧する
のが、孔径をさらに揃える上で効果的である。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プラ
スチックシート、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。During pressure molding, a sheet-like material that can be elastically or plastically deformed is placed on top of the gas-impermeable sheet covering the powder and granules, and pressure is applied by rollers through this sheet-like material. This is effective in making the pore diameters more uniform. Examples of sheets that can be elastically deformed include rubber sheets, plastic foam sheets, non-woven fabrics, felt, etc. Examples of sheets that can be plastically deformed include plastic sheets filled with highly viscous fluid and pastes such as clay paste. A shaped sheet or the like is used.
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
して湿り状態に形成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、
ローラーにより加圧すると、このローラーの回転により
粉粒体が連続して順次押圧されていき、粉粒体は垂直方
法のみならず水平方向にも良好に移動する。その結果、
粉粒体の間の大きな空間が良好に埋められていき、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, a wet powder formed by mixing a curable resin liquid with an inorganic powder is covered with a gas-impermeable sheet in a mold to prevent air between the powder and granules. After depressurizing and degassing,
When pressure is applied by the roller, the powder and granules are pressed one after another by the rotation of the roller, and the powder and granules move well not only vertically but also horizontally. the result,
The large spaces between the powder and granules are filled well, and a porous material with well-uniformed pore diameters is obtained.
また、粉粒体間の空気が減圧脱気されると、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。Moreover, when the air between the powder particles is degassed under reduced pressure, it is more effective because it is prevented from restoring and enlarging the pores when the pressure is released to normal pressure after pressurization.
しかも粉粒体の間に空気(酸素)が殆ど存在しなくなる
ので、硬化反応が酸素により阻害されずに速やかに硬化
が進行する。Moreover, since almost no air (oxygen) exists between the powder particles, the curing reaction is not inhibited by oxygen and the curing proceeds rapidly.
また、上記粉粒体を弾性変形或いは塑性変形の可能なシ
ート状物を介してローラーにより加圧する場合は、粉粒
体にかかる押圧力が均一化され孔径がさらによく揃った
多孔性材料が得られる。In addition, when the powder and granules are pressed by rollers through a sheet-like material that can be elastically or plastically deformed, the pressing force applied to the powder and granules is made uniform, and a porous material with more uniform pore diameters can be obtained. It will be done.
(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.
1星事ル
アルミナファイパー短繊維(300メツシユバス) 2
500重量部と、硬化側(パーへキサ3門;日本油脂社
製)を1.5重世%含有する熱硬化性エポキシアクリレ
ート樹脂(12ボイズ) 2000重量部とを、嵩体積
比で前者1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。1 star lulumina fiber short fiber (300 mesh bath) 2
500 parts by weight and 2000 parts by weight of a thermosetting epoxy acrylate resin (12 voids) containing 1.5 weight percent of hardening side (Perhexa 3 gates; manufactured by Nippon Oil & Fats Co., Ltd.), the former being 1 in bulk volume ratio. The latter was mixed uniformly at a ratio of 0.25 to the latter 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(約1OOp層)で覆い、そ
の縁辺を成形型の上縁でシリコン系シーラントで気密に
シールし、成形型の一部に形成した減圧孔から成形型内
を真空ポンプで100 mh(ゲージ)に減圧脱気シテ
、コレラ温度100°C1油圧シリンダーの圧力を40
kg / cnJに設定したローラー加圧機に通した
あと100°Cに加熱して樹脂を硬化させ、ポリエステ
ル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6閣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 (approximately 1OOp layer), and seal the edges of the sheet airtightly with a silicone sealant at the upper edge of the mold. The pressure inside the mold was reduced to 100 mh (gauge) using a vacuum pump through the decompression hole formed in a part of the mold, and the cholera temperature was 100°C. The pressure of the hydraulic cylinder was reduced to 40 mh.
After passing through a roller pressure machine set at kg / cnJ, it is heated to 100°C to harden the resin, the polyester sheet is removed and the mold is demolded, and the inorganic powder is bonded with a hardening resin and the pore size is formed on the surface. A porous material with a thickness of 6 mm consisting of a water-impermeable porous body with a uniform set of 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。Regarding this porous material, the 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)滑りにくさは、水濡れ状態の多孔性材料の表面に
30mmX50mm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0,0.8未満〜0.6をΔ、0.6未満
を×で表した。(1) Slip resistance was determined by layering a 30mm x 50mm piece of synthetic leather on the surface of a porous material that was wet with water, and then adding 2kg of synthetic leather to the surface.
The friction coefficient was measured by the slope method, and the friction coefficient of 0.8 or more was expressed as 0, less than 0.8 to 0.6 was expressed as Δ, and less than 0.6 was expressed as x.
(2)汚れにくさは、タルク粉末(粒径10μl以下)
を0.2 g /ccの割合に水中に分散させ、この分
散液を100mm X 100mm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○、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 of 10 μl or less)
is dispersed in water at a ratio of 0.2 g/cc, and 50 cc of this dispersion is sprinkled on the surface of a 100 mm x 100 mm porous material. If the talc powder remains on the surface and can be washed off later, mark as ○. , The case where the talc powder caused clogging in the pores on the surface was indicated by ×.
(3)細孔の直径は、水銀式ポロシメーターで測定して
、孔径20μ■以下の孔が95%以上の場合をO1孔径
20μm以下の孔が95%未満の場合を×で表した。(3) The diameter of the pores was measured using a mercury porosimeter, and the case where 95% or more of the pores had a pore diameter of 20 μm or less was expressed as an x, and the case where the percentage of pores with a pore diameter of 20 μm or less was less than 95% was indicated by an “×”.
(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Olo、05cc/g未満を
×で表した。(4) The pore volume was measured with a mercury porosimeter, and 0.05 cc/g or more was expressed as Olo, and less than 0.05 cc/g was expressed as x.
ス崖訓l
マイカ(100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(ジアミノジフェニルメ
タン)を当量配合した熱硬化性エポキシ樹脂(4ボイズ
)(TETRAD−X+三菱ガス化学社製)を、嵩体積
比で前者1に対して後者0.15の割合で噴霧し含浸し
た。Thermosetting epoxy resin (4 voids) (TETRAD-X + Mitsubishi Gas Chemical Co., Ltd.) made by uniformly spreading mica (100 mesh bath) in a flat box-shaped mold and blending an equivalent amount of a hardening agent (diaminodiphenylmethane) with it. ) was sprayed and impregnated at a bulk volume ratio of 1 to 0.15 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、成形型内を300m)Ig(ゲージ
)に減圧脱気して、これを油圧シリンダーの圧力を25
kg / cnlに設定したローラー加圧機に通して
賦形した後、120〜180 ”Cに加熱して樹脂を硬
化させ、ポリエステル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6mmの
多孔性材料を製造した。Cover the top with a polyester sheet, seal the edges with the upper edge of the mold, depressurize the inside of the mold to 300 m) Ig (gauge), and reduce the pressure of the hydraulic cylinder to 25 m).
After shaping through a roller pressure machine set at kg/cnl, the resin is cured by heating to 120-180"C, the polyester sheet is removed and the mold is demolded, and the inorganic powder becomes 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 formed on the 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。Regarding this porous material, the slip resistance, stain resistance, pore diameter, and pore volume were measured and evaluated using the following methods. The results are shown in Table 1.
夫隨桝主
石英粉末(200メツシユバス)と、硬化剤(ペンヅイ
ルバーオキサイド)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1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。A styrene solution of thermosetting unsaturated polyester resin containing 2% by weight of a curing agent (penduyl baroxide) was mixed with quartz powder (200 mesh baths) and a bulk volume ratio of 1 vol. The latter was mixed uniformly at a ratio of 0.25 to the latter 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
でシールして、成形型内を200 mmHg(ゲージ)
に減圧脱気して、これを油圧シリンダーの圧力を50k
g/cIllに設定したローラー加圧機に通して賦形し
た後、80“Cに加熱して樹脂を硬化させ脱型して、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−
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, and adjust the inside of the mold to 200 mmHg (gauge).
The pressure in the hydraulic cylinder is reduced to 50k.
After shaping by passing through a roller press machine set at g/cIll, heat to 80"C to harden the resin and demold, the inorganic powder is bonded with a hardening resin and the surface has uniform pore sizes. 6-thickness made of a water-impermeable porous material with minute pores.
A porous material 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。Regarding this porous material, the slip resistance, stain resistance, pore diameter, and pore volume were measured and evaluated using the following methods. The results are shown in Table 1.
l1衰1
カーボンミルドファイバー(平均繊維長300μm)
と、硬化剤(パーカドノクス16:化薬アクゾ社製)を
1重量%を含有する熱硬化性不飽和ポリエステル樹脂(
12ポイズ)とを、嵩体積比で前者1に対し後者0.1
5の割合で均一に混合して湿り状態の粉粒体を作った。l1 decay 1 carbon milled fiber (average fiber length 300μm)
and a thermosetting unsaturated polyester resin (
12 poise), with a bulk volume ratio of 1 to 0.1 for the latter.
A wet powder was prepared by uniformly mixing the ingredients at a ratio of 5:5 to 5:5.
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10IIII
ll)を載せ、成形型内を100mHg(ゲージ)に減
圧脱気して、これを80°Cに加熱したローラー加圧機
に通し40kg/c+flの油圧シリンダー圧力で加圧
した後、80°Cに加熱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+m++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, and place wool felt (10III thick) on top.
ll), the inside of the mold was depressurized and degassed to 100mHg (gauge), passed through a roller pressure machine heated to 80°C, pressurized with a hydraulic cylinder pressure of 40kg/c+fl, and then heated to 80°C. The resin is cured by heating, the nylon sheet and wool felt are removed and demolded, and the inorganic powder is bonded with a hardening resin to form an impermeable surface with fine pores of uniform diameter. A porous material having a thickness of 6+m++ 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。Regarding this porous material, the slip resistance, stain resistance, pore diameter, and pore volume were measured and evaluated using the following methods. The results are shown in Table 1.
夫権性l
大理石粉砕粉(180メツシユバス)、常温硬化性エポ
キシ樹脂(15ポイズ)(ニスダイン400:積木化学
社製)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。Marble crushed powder (180 mesh bath) and room temperature curable epoxy resin (15 poise) (Nisdyne 400: manufactured by Block Chemical Co., Ltd.) were uniformly mixed in a bulk volume ratio of 1 for the former to 0.15 for the latter. They were mixed to form 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
an)を載せ、成形型内を100 wflg(ゲージ)
に減圧脱気して、これを常温のローラー加圧機に通し2
0kg/c1ilの油圧シリンダー圧力で加圧して常温
で樹脂を硬化させ、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−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
an) and 100 wflg (gauge) inside the mold.
Degassed under reduced pressure and passed through a roller press machine at room temperature 2
The resin is cured at room temperature by pressurizing with a hydraulic cylinder pressure of 0 kg/c1il, the polyester sheet and nitrile rubber sheet are removed and demolded, the inorganic powder is bonded with a hardening resin, and the surface is made of fine particles with uniform pore sizes. A porous material having a thickness of 6 mm and consisting of a water-impermeable porous body with pores opened therein 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。Regarding this porous material, the slip resistance, stain resistance, pore diameter, and pore volume were measured and evaluated using the following methods. The results are shown in Table 1.
尖搭医l
白マイカ粉末(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(バーキュア0:
日本油脂社製) 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。Spread white mica powder (200 mesh baths) evenly in a flat box-shaped mold, and add a hardening agent (Vercure 0:
A styrene solution (1 void) of a thermosetting unsaturated polyester resin containing 2% by weight (manufactured by NOF Corporation) 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、その上に粘土ペーストをシート状(
厘さ5mm)に載せ、成形型内を100 mmJlg(
ゲージ)に減圧脱気して、これを油圧シリンダーの圧力
を50 kg / cdに設定したローラー加圧機に通
して賦形した後、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ペース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
閤の多孔性材料を製造した。Cover it with a polyester sheet, seal its edges with the top edge of the mold, and apply clay paste on top of it in the form of a sheet (
5mm), and the inside of the mold was heated to 100mmJlg (
Gauge), the resin is degassed under reduced pressure, passed through a roller pressure machine with a hydraulic cylinder pressure set to 50 kg/cd, and then heated to 80°C to harden the resin.
Remove the polyester sheet and clay paste and demold,
A 6-thick, water-impermeable porous body made of inorganic powder bound with a curable resin and with fine pores of uniform pore size on its surface.
A porous material 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。Regarding this porous material, the slip resistance, stain resistance, pore diameter, and pore volume were measured and evaluated using the following methods. The results are shown in Table 1.
ル較桝土
成形型内を減圧脱気せず、ローラー加圧機による加圧を
プレス機によ−る加圧に替え、それ以外は実施例1と同
様に行った。The process was carried out in the same manner as in Example 1 except that the inside of the clay molding mold was not degassed under reduced pressure and the pressure applied by the roller press was replaced by pressurization by a press.
且較贋l
成形型内を減圧脱気せず、ローラー加圧機による加圧を
プレス機による加圧に替え、それ以外は実施例2と同様
に行った。Comparison Example 2 was carried out in the same manner as in Example 2, except that the inside of the mold was not depressurized and degassed, and the pressure applied by the roller pressure machine was replaced by the pressure applied by a press machine.
ル較外主
成形型内を減圧脱気せず、ローラー加圧機による加圧を
プレス機による加圧に替え、それ以外は実施例3と同様
に行った。Example 3 was carried out in the same manner as in Example 3 except that the inside of the main mold was not degassed under reduced pressure and the pressure applied by the roller press was replaced by pressurization by a press.
(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、成形型内で気体不透過性シートで覆われ粉粒体
間の空気が減圧脱気された後、−ローラーにより加圧さ
れて樹脂が硬化するので、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. After the air between the particles is degassed under reduced pressure by being covered with a gas-impermeable sheet in the mold, the resin is cured by pressure applied by rollers, so the inorganic particles are bonded with the curable resin. A water-impermeable porous material with fine pores of uniform pore size on the surface is obtained.
こ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 in this way, 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 staining due to clogging.
また、硬化性樹脂の硬化も速くなり、生産性が向上する
。本発明方法はこのような利点を有する。Moreover, the curing of the curable resin becomes faster, improving productivity. The method according to the invention has these advantages.
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
It can be suitably used for flooring, counters, tables, moisture absorbing/releasing wall materials, soundproof building materials, etc. that are expected to have an anti-slip effect, such as in bathrooms, toilets, galleys, entrances, balconies, shower rooms, poolsides, and sidewalks.
Claims (1)
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、ローラー
により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ローラーに
より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. 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 A method for producing a porous material, which comprises degassing the air under reduced pressure, and then curing the resin while or after applying pressure with a roller. 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 pressed by a roller 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 |
|---|---|---|---|
| JP15610890A JPH0446071A (en) | 1990-06-14 | 1990-06-14 | Production of porous material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15610890A JPH0446071A (en) | 1990-06-14 | 1990-06-14 | Production of porous material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0446071A true JPH0446071A (en) | 1992-02-17 |
Family
ID=15620487
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15610890A Pending JPH0446071A (en) | 1990-06-14 | 1990-06-14 | Production of porous material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0446071A (en) |
-
1990
- 1990-06-14 JP JP15610890A patent/JPH0446071A/en active Pending
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