JP2002212306A - Method for agitating mixture for forming open-cell porous material - Google Patents

Method for agitating mixture for forming open-cell porous material

Info

Publication number
JP2002212306A
JP2002212306A JP2001009892A JP2001009892A JP2002212306A JP 2002212306 A JP2002212306 A JP 2002212306A JP 2001009892 A JP2001009892 A JP 2001009892A JP 2001009892 A JP2001009892 A JP 2001009892A JP 2002212306 A JP2002212306 A JP 2002212306A
Authority
JP
Japan
Prior art keywords
stirring
mixture
filler
porous material
forming
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001009892A
Other languages
Japanese (ja)
Inventor
Nobuo Adachi
信夫 足立
Yoshifumi Misumi
欣史 三澄
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toto Ltd
Original Assignee
Toto Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toto Ltd filed Critical Toto Ltd
Priority to JP2001009892A priority Critical patent/JP2002212306A/en
Publication of JP2002212306A publication Critical patent/JP2002212306A/en
Pending legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a method for agitating to obtain a mixture for forming a uniform open-cell porous material by agitating and dispersing a mixture consisting of a compound such as an epoxy, etc., a filler and water in a short time in producing the open-cell porous material made from a resin used as a mold for a slurry molding. SOLUTION: This method for agitating to obtain a mixture for forming a uniform open-cell porous material containing at least the epoxy compound, a curing agent, the filler and water is provided by agitating the above mixture for forming a uniform continuous pore porous material with a reciprocating rotary agitator having a reversing function not a single direction rotation.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、少なくともエポキ
シ化合物、硬化剤、フィラー、水とを含む連続気孔多孔
体形成用混合物の攪拌方法に関する。
The present invention relates to a method for stirring a mixture for forming a continuous porous material containing at least an epoxy compound, a curing agent, a filler, and water.

【0002】[0002]

【従来の技術】陶磁器の鋳込み成形に用いられる型とし
ては、一般的に石膏型や吸水性のある樹脂製連続気孔多
孔質体を有する泥漿鋳込み成形型(以下樹脂製鋳込み成
形型)が知られているが、近年は成形サイクルタイムが
短い樹脂製鋳込み成形型を用いた加圧成形が主流となり
つつある。ここで用いられている成形型は石膏型に比べ
高価であるが、多回数生産(型寿命が非常に長い)や均
質な製品が得られることで価格差を補っている。つまり
均質な製品を多回数生産するほど効率的な生産が可能と
なる事は明白である。樹脂製鋳込み成形型において均質
な製品の多回数生産は、エポキシ等の化合物とフィラー
と水とを均一に混合・分散してえられた連続気孔多孔体
形成用混合物を硬化させて作製する樹脂製連続気孔多孔
体に左右される。従来この連続気孔多孔体形成用混合物
の混合にはプロペラ型やスクリュー型の羽根を回転させ
る一般的な回転攪拌機や窓の入った固定外刃と回転内刃
を持つホモジナイザーが用いられている。
2. Description of the Related Art As a mold used for casting of ceramics, a gypsum mold or a slurry casting mold having a continuous porous porous body made of a resin having a water absorbing property (hereinafter referred to as a resin casting mold) is generally known. However, in recent years, pressure molding using a resin casting mold having a short molding cycle time is becoming mainstream. The mold used here is more expensive than the gypsum mold, but the price difference is compensated for by the multiple production (extremely long mold life) and by obtaining a homogeneous product. In other words, it is clear that the more homogeneous products are produced, the more efficient the production becomes. Multiple production of a homogeneous product in a resin casting mold is performed by uniformly mixing and dispersing a compound such as epoxy, filler, and water, and then curing a mixture for forming a continuous pore porous body, which is made of resin. It depends on the continuous porous material. Conventionally, a conventional rotary stirrer for rotating a propeller-type or screw-type blade or a homogenizer having a fixed outer blade having a window and a rotating inner blade has been used for mixing the mixture for forming a continuous porous material.

【0003】従来の攪拌装置を用いた攪拌の状態を図面
を用いて説明する。図5は一般的な回転攪拌機に用いら
れている攪拌羽根であり、中央の回転軸2に直線状の1
枚羽根3を取りつけたものである。図6は一般的なプロ
ペラ型回転攪拌機による混合状態を示す図である。攪拌
槽1において、回転軸2に取付けられたプロペラ羽根6
は特定の液攪拌方向7であるため、回転流は攪拌羽根の
軸心から先端近くまでは羽根の回転速度でほぼ同一速度
で回転し、その遠心力の作用で槽壁側の液面が上がり、
軸心部分が下がり、遠心力と釣り合いを保ちながら回転
している。
The state of stirring using a conventional stirring device will be described with reference to the drawings. FIG. 5 shows a stirring blade used in a general rotary stirrer.
The blade 3 is attached. FIG. 6 is a view showing a mixing state by a general propeller type rotary stirrer. In the stirring tank 1, the propeller blades 6 attached to the rotating shaft 2
Is a specific liquid agitation direction 7, so that the rotating flow rotates from the axis of the stirring blade to near the tip at almost the same speed as the rotation speed of the blade, and the centrifugal force raises the liquid level on the tank wall side. ,
The shaft part is lowered and rotating while keeping balance with the centrifugal force.

【0004】[0004]

【発明が解決しようとする課題】しかし、このような流
動状態では回転流のみで、半径方向、軸方向の流れがほ
とんど起こらず、回転攪拌機は内容物に一定方向のみの
回転しか与えられないため、親水性の液体同士の混合に
は問題ないが、液体への固体の均一分散や親水性液体と
疎水性液体の均一な混合は困難である。具体的にはエポ
キシ等の化合物にフィラーと水とを混合した連続気孔多
孔体形成用混合物において、フィラーは樹脂と共に回転
流動作を行なうだけで混合物全体へは分散しづらく、エ
マルジョン生成にも時間を要するという問題があった。
However, in such a flow state, only the rotational flow is generated, and almost no radial or axial flow occurs, and the rotary stirrer can only rotate the contents in a fixed direction. Although there is no problem in mixing hydrophilic liquids, it is difficult to uniformly disperse solids in the liquid or to uniformly mix hydrophilic liquid and hydrophobic liquid. Specifically, in a mixture for forming a continuous porous material in which a filler and water are mixed with a compound such as an epoxy, the filler is hard to disperse throughout the mixture only by performing a rotating flow operation together with the resin, and it takes time to form an emulsion. There was a problem of cost.

【0005】また、固定外刃と回転内刃を持つホモジナ
イザーは内刃の回転による遠心力で攪拌物を外刃の窓か
ら放出しつつ下から混合物を外刃と内刃の間に取り込む
事により親水性液体と疎水性液体の混合、すなわち乳化
やエマルジョン生成には効果的であるが、エポキシなど
の化合物と水と比重の重いフィラーとの混合においては
フィラーの沈降が早いためフィラーの外刃と内刃の間へ
の取り込みが十分でなくフィラーを含む混合体の均一分
散が困難である。また比重の軽いフィラーとの混合にお
いてはフィラーが沈降せず攪拌層内のエポキシなどの化
合物と水の混合物の上層付近に滞留するためフィラーの
外刃と内刃の間への取り込みが十分でなくフィラーを含
む混合体の均一分散が困難である。また構造が複雑であ
り、エポキシ等の化合物である樹脂等粘度の高い物質の
大量混合時におけるメンテナンスも困難である。このた
め連続気孔多孔体形成用混合物を構成するエポキシ等の
化合物と水とフィラーが均一に分散せず、エマルジョン
の生成とフィラーの均一分散が得られず、連続気孔多孔
体形成用混合物を硬化して形成する樹脂製連続気孔多孔
体の強度等の品質にバラツキを与える原因となってい
る。
Further, a homogenizer having a fixed outer blade and a rotating inner blade is capable of discharging the agitated material from the window of the outer blade by centrifugal force caused by the rotation of the inner blade and taking in the mixture between the outer blade and the inner blade from below. It is effective for mixing hydrophilic and hydrophobic liquids, i.e., emulsification and emulsion formation. The incorporation between the inner blades is not sufficient, and it is difficult to uniformly disperse the mixture containing the filler. In addition, when mixed with a filler with a low specific gravity, the filler does not settle and stays near the upper layer of the mixture of water and a compound such as epoxy in the stirring layer, so the filler is not sufficiently taken up between the outer blade and the inner blade. It is difficult to uniformly disperse the mixture containing the filler. Further, the structure is complicated, and it is difficult to perform maintenance when a large amount of highly viscous substance such as resin such as epoxy is mixed. For this reason, the compound such as epoxy and the water and the filler constituting the mixture for forming the continuous porous material are not uniformly dispersed, and the formation of the emulsion and the uniform dispersion of the filler are not obtained. This causes variation in the quality, such as the strength, of the resin continuous porous body formed by the above method.

【0006】さらには、連続気孔多孔体形成用混合物は
時間と共に硬化が進行するため短時間で均一なエマルジ
ョンの生成とフィラーの均一分散が要求される。攪拌時
間が長くなると硬化が進行し、攪拌終了時点で連続気孔
多孔体形成用混合物が高粘性となり所望の連続気孔多孔
体形状を得るために連続気孔多孔体形成用混合物を流し
入れて固化させる容器に流し込みができない場合もあ
る。
Furthermore, since the mixture for forming a continuous porous material is cured with time, it is required to form a uniform emulsion in a short time and to uniformly disperse the filler. When the stirring time becomes longer, the curing proceeds, and at the end of the stirring, the mixture for forming the continuous porous body becomes highly viscous and the mixture for forming the continuous porous body is poured and solidified to obtain a desired continuous porous body shape. In some cases, pouring is not possible.

【0007】本発明は上記課題を解決するためになされ
たもので、本発明の目的は、泥漿鋳込み成形型等に使用
される樹脂製連続気孔多孔体の製造に際して、エポキシ
等の化合物と、硬化剤と、フィラーと水とを含む連続気
孔多孔体形成用混合物を短時間で均一に攪拌する攪拌方
法を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to provide a method for producing a continuous porous porous body made of a resin used for a slurry casting mold or the like, and a method of curing a compound such as epoxy with a compound such as epoxy. It is an object of the present invention to provide a stirring method for uniformly stirring a mixture for forming a continuous pored porous material containing an agent, a filler and water in a short time.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
に本発明は、少なくともエポキシ化合物、硬化剤、フィ
ラー、水とを含む連続気孔多孔体形成用混合物の攪拌方
法であって、前記連続気孔多孔体形成用混合物を一方回
転でなく反転機能を持つ往復回転式攪拌機を用いて攪拌
することを特徴とする。そうすることにより攪拌容器内
に乱流を発生させ、樹脂とフィラーを均一分散・混合す
ることが可能になる。
In order to achieve the above object, the present invention provides a method for stirring a mixture for forming a continuous porous material, which comprises at least an epoxy compound, a curing agent, a filler, and water. It is characterized in that the mixture for forming a porous body is stirred using a reciprocating rotary stirrer having a reversing function instead of one-way rotation. By doing so, a turbulent flow is generated in the stirring vessel, and the resin and the filler can be uniformly dispersed and mixed.

【0009】本発明の好ましい態様として、前記往復回
転式攪拌機が2枚以上あるいは2段以上の攪拌羽根を備
えるようにする。そうすることにより攪拌容器内全体に
乱流を強力に発生させ、含水状態において硬化する多種
類の物質を混合した樹脂を流し込み等が可能な流動性を
持つ時間内に均一分散・混合することが可能になる。
In a preferred embodiment of the present invention, the reciprocating rotary stirrer includes two or more stirring blades or two or more stirring blades. By doing so, a turbulent flow is strongly generated in the whole of the stirring vessel, and it is possible to uniformly disperse and mix the resin within a time having a fluidity capable of pouring a resin in which various kinds of substances that cure in a hydrated state can be poured. Will be possible.

【0010】また、本発明の好ましい態様として、前記
フィラーの比重により攪拌羽根の断面部形状を変更する
ようにする。そうすることにより、上下乱流の方向を変
えフィラーの比重に合わせて沈降防止あるいは浮遊物の
混入の攪拌が可能となる。
In a preferred embodiment of the present invention, the sectional shape of the stirring blade is changed depending on the specific gravity of the filler. By doing so, it is possible to change the direction of the vertical turbulence and to prevent sedimentation or to mix suspended matter according to the specific gravity of the filler.

【0011】また、本発明の好ましい態様として、前記
フィラーの比重が1以上の場合に、前記攪拌羽根の断面
部形状を混合物が上方から下方に向って乱流を起こす形
状になるようにする。そうすることにより、回転軸を中
心に下層へ向かう乱流は攪拌槽底部に衝突して攪拌槽上
層へ向かう乱流となり、沈降しようとするフィラーはこ
の上層へ向かう乱流の流れにより攪拌槽上層に向かって
押し上げられ攪拌槽下層にフィラーが沈降・滞留せず、
かつ乱流により攪拌層内の一定の領域のみならずあらゆ
る領域に分散することが可能になる。
[0011] In a preferred embodiment of the present invention, when the specific gravity of the filler is 1 or more, the cross-sectional shape of the stirring blade is such that the mixture causes a turbulent flow from above to below. By doing so, the turbulent flow toward the lower layer around the rotation axis collides with the bottom of the stirring tank and becomes a turbulent flow toward the upper layer of the stirring tank, and the filler to be settled is caused by the turbulent flow toward the upper layer. And the filler does not settle or stay in the lower layer of the stirring tank.
In addition, the turbulent flow makes it possible to disperse not only in a certain region in the stirring layer but also in any region.

【0012】また、本発明の好ましい態様として、前記
フィラーの比重が1未満の場合に、前記攪拌羽根の断面
部形状を混合物が下方から上方に向って乱流を起こす形
状になるようにする。そうすることにより、回転軸を中
心に上層へ向かう乱流は攪拌槽内壁に沿って攪拌槽下層
へ向かう乱流となり、浮上しようとするフィラーはこの
下層へ向かう乱流の流れにより攪拌槽下層に向かって押
し下げられ攪拌槽上層にフィラーが浮遊・滞留せず、か
つ乱流により攪拌層内の一定の領域のみならずあらゆる
領域に分散することが可能になる。
In a preferred embodiment of the present invention, when the specific gravity of the filler is less than 1, the shape of the cross section of the stirring blade is such that the mixture causes a turbulent flow from below to above. By doing so, the turbulent flow toward the upper layer around the rotation axis becomes a turbulent flow toward the lower layer of the stirring tank along the inner wall of the stirring tank, and the filler to be floated flows into the lower layer of the stirring tank by the flow of the turbulent flow toward the lower layer. The filler is pushed down so that the filler does not float or stay in the upper layer of the stirring tank, and can be dispersed not only in a certain area but also in any area in the stirring layer by turbulence.

【0013】本発明の好ましい態様においては、前記攪
拌の時には界面活性剤を添加するようにする。そうする
ことにより、フィラーと樹脂の界面自由エネルギーある
いは表面張力を著しく低下させながら乱流を発生させる
ことによって、樹脂のダイラタンシー、チクソトロピー
流動性発現を押さえ、フィラーを均一分散・混合するこ
とが可能になる。
In a preferred embodiment of the present invention, a surfactant is added during the stirring. By doing so, turbulence is generated while significantly lowering the interfacial free energy or surface tension between the filler and the resin, thereby suppressing the dilatancy and thixotropic fluidity of the resin and allowing the filler to be uniformly dispersed and mixed. Become.

【0014】[0014]

【発明の実施の形態】本発明において、樹脂製連続気孔
多孔体とは、エポキシ等の化合物を主体にフィラーと水
とを含水状態のまま混合し固化させた連続気孔を持つ樹
脂層をいう。
BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, a continuous porous resin body is a resin layer having continuous pores obtained by mixing and solidifying a filler and water while containing a compound such as epoxy as a main component.

【0015】本発明において、連続気孔多孔体形成用混
合物とは、エポキシ等の化合物を主体にフィラーと水と
を混合した状態の混合物をいう。
In the present invention, the mixture for forming a continuous porous material means a mixture in which a filler and water are mainly mixed with a compound such as epoxy.

【0016】本発明においてフィラーとはエポキシ化合
物と接着できる材質で珪石粉、珪砂粉、ガラス粉、有機
粉体やマイクロバルーン等をいう。
In the present invention, the filler is a material capable of bonding to the epoxy compound, and includes silica powder, silica sand powder, glass powder, organic powder, microballoons and the like.

【0017】本発明において、界面活性剤とは疎水基と
親水基によって構成される物質で脂肪酸塩、アルキル硫
酸エステル塩、アルキルスルホコハク酸塩等に代表され
る陰イオン界面活性剤やポリオキシエチレンアルキルエ
ーテル、ソルビタン脂肪酸エステル、ポリオキシエチレ
ン脂肪酸エステル等に代表される非イオン界面活性剤を
いう。
In the present invention, a surfactant is a substance composed of a hydrophobic group and a hydrophilic group, and is an anionic surfactant represented by a fatty acid salt, an alkyl sulfate ester salt, an alkyl sulfosuccinate salt or the like, or a polyoxyethylene alkyl. Nonionic surfactants represented by ethers, sorbitan fatty acid esters, polyoxyethylene fatty acid esters and the like.

【0018】以下に本発明の好ましい実施の形態につい
て図を用いて説明する。反転機能を持つ往復回転式攪拌
機を用いた攪拌は図1に示すように、攪拌槽1内に乱流
4を発生させ半径方向、軸方向を含めた攪拌層1内全体
を覆う流動状態が得られるため、フィラーが容易に短時
間で攪拌槽1全体に分散される。更に反転往復を繰り返
す攪拌羽根3から受ける大きなせん断力によってフィラ
ーの分散とエマルジョン生成は促進され、より均一にエ
ポキシ樹脂内へのフィラー分散が可能となる。
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings. Stirring using a reciprocating rotary stirrer having a reversing function generates a turbulent flow 4 in the stirring tank 1 as shown in FIG. 1 to obtain a fluid state covering the whole of the stirring layer 1 including the radial and axial directions. Therefore, the filler is easily dispersed throughout the stirring tank 1 in a short time. Further, the dispersion of the filler and the formation of the emulsion are promoted by the large shearing force received from the stirring blade 3 that repeats the reversing reciprocation, so that the filler can be more uniformly dispersed in the epoxy resin.

【0019】本発明の好ましい実施形態では、図2に示
すような回転軸2に二枚羽根5または二枚以上の羽根を
取り付けた攪拌羽根あるいは図3に示す回転軸2に二段
以上の攪拌羽根を取り付けた攪拌羽根を往復回転式攪拌
機に使用する。これにより攪拌槽内の乱流が更に細分化
されると共に攪拌羽根のせん断力が大きくなり、一分子
中に1個以上のエポキシ環を有するエポキシ化合物とエ
ポキシ化合物と反応してこれを硬化させる硬化剤とフィ
ラーと水および可溶性塩類を含む含水状態において硬化
する複雑混合系樹脂において、複雑混合系樹脂が流し込
み等が可能な流動性を持つ時間内にフィラーを均一分散
・混合することが可能になる。羽根の枚数および段数は
連続気孔多孔質樹脂の量、攪拌層の形状や深さあるいは
直径にあわせて設定する。
In a preferred embodiment of the present invention, a stirring blade having two blades 5 or two or more blades attached to a rotating shaft 2 as shown in FIG. 2 or a stirring blade having two or more stages attached to the rotating shaft 2 shown in FIG. The stirring blade equipped with the blade is used for a reciprocating rotary stirrer. As a result, the turbulent flow in the stirring tank is further subdivided and the shearing force of the stirring blade is increased, and the epoxy compound having one or more epoxy rings in one molecule reacts with the epoxy compound to cure the epoxy compound. It is possible to uniformly disperse and mix the filler in a complex mixed resin that cures in a water-containing state containing an agent, a filler, water and soluble salts, within a time period in which the mixed mixed resin has fluidity that can be poured. . The number of blades and the number of stages are set in accordance with the amount of the continuous porous resin and the shape, depth or diameter of the stirring layer.

【0020】本発明の好ましい実施の形態では、ダイラ
タンシー、チクソトロピー流動性を発現する連続気孔多
孔体形成用混合物に界面活性剤を混合する。ダイラタン
シー、チクソトロピー流動性を発現する際、往復回転式
攪拌機での攪拌開始前あるいは攪拌中に界面活性剤を投
入する。これによって、往復回転式攪拌機の発生させる
上下乱流と攪拌羽根の強力なせん断力とともに界面活性
剤のフィラーと樹脂の界面自由エネルギーあるいは表面
張力低下効果によって、樹脂のダイラタンシー、チクソ
トロピー流動性発現を押さえ、非ダイラタンシー、非チ
クソトロピー流動性発現樹脂と同様の攪拌が可能とな
る。
In a preferred embodiment of the present invention, a surfactant is mixed with the mixture for forming a continuous porous material exhibiting dilatancy and thixotropic fluidity. When dilatancy and thixotropic fluidity are developed, a surfactant is added before or during stirring with a reciprocating rotary stirrer. This reduces the dilatancy and thixotropic fluidity of the resin due to the vertical turbulence generated by the reciprocating rotary stirrer and the strong shearing force of the stirring blades as well as the effect of lowering the surface free energy or the surface tension between the filler and the resin of the surfactant. , Non-dilatancy, non-thixotropic fluidity developing resin can be stirred in the same manner.

【0021】本発明の好ましい実施の形態では、図1な
らびに図4に示すようにフィラーの比重により攪拌羽根
の断面部形状を交換する事で乱流の方向を任意に上下変
更する。フィラー比重が1以上、好ましくは1.5以上
の場合、台形あるいは三角形の断面部形状を持つ攪拌羽
根を使用する際に、台形短辺面あるいは三角形頂点を下
に向けるように羽根を取り付ける。これにより図1に示
す上から下への乱流4の流動状態にすることでフィラー
の沈降防止が可能となり均一な分散が得られる。
In a preferred embodiment of the present invention, as shown in FIGS. 1 and 4, the direction of the turbulent flow is arbitrarily changed by changing the cross-sectional shape of the stirring blade according to the specific gravity of the filler. When the specific gravity of the filler is 1 or more, preferably 1.5 or more, when using a stirring blade having a trapezoidal or triangular cross-sectional shape, the blade is attached so that the trapezoidal short side surface or the triangular vertex points downward. Thereby, by setting the turbulent flow 4 from the top to the bottom as shown in FIG. 1, the settling of the filler can be prevented, and uniform dispersion can be obtained.

【0022】フィラー比重が1未満、好ましくは0.5
以下の場合、台形あるいは三角形の断面部形状を持つ攪
拌羽根を使用する際に、台形短辺面あるいは三角形頂点
を上に向けるように羽根を取り付ける。これにより図4
に示す下から上への乱流4の流動状態にすることで浮遊
フィラーの取り込みが可能となり均一な分散が得られ
る。
The specific gravity of the filler is less than 1, preferably 0.5
In the following cases, when using a stirring blade having a trapezoidal or triangular cross section, the blade is attached so that the trapezoidal short side surface or the triangular vertex faces upward. As a result, FIG.
By making the turbulent flow 4 flow from the bottom to the top as shown in (1), it is possible to take in the floating filler and obtain a uniform dispersion.

【0023】[0023]

【実施例】[実施例1]表1に示すような調合割合で準
備した材料を蓋なしのステンレス容器に入れプロペラ型
羽根の回転式攪拌機、ホモジナイザーおよび往復回転式
攪拌機で10分間攪拌して3つのエマルジョンスラリー
を得た。このエマルジョンスラリーを形状が10×10
×120mmの直方体で塩化ビニル製の板で四方を囲ん
だ不透水性の型に鋳込み、水が蒸発しないように覆いを
し、30℃の室内に42時間放置して含水状態のまま硬
化させ硬化体を脱型した。試験体は攪拌方法毎に各5ヶ
作製した。 [表1] 得られた硬化体の破断強度をJISK7203(硬質プ
ラスチックの曲げ試験方法:3点曲げ強さ)に準じて測
定し、破断強度およびサンプル破断寸法より曲げ強度を
算出した。材料試験機には(株)島津製作所製オートグ
ラフAG−10KNEを用いた。試験結果を表2に示
す。[表2] 表2に示されるように、往復回転式攪拌機で攪拌し作製
した硬化体は、他の攪拌機で攪拌し作製した硬化体に比
べ格段に曲げ強度が強く、強度のバラツキも少ないこと
がわかった。
[Example 1] Materials prepared in the proportions shown in Table 1 were placed in a stainless steel container without a lid, and stirred for 10 minutes with a rotary agitator of a propeller type blade, a homogenizer, and a reciprocating rotary agitator. Two emulsion slurries were obtained. This emulsion slurry is 10 × 10
Cast into a water-impermeable mold surrounded by a vinyl chloride plate with a rectangular shape of × 120 mm and surrounding it on all sides, cover it so that water does not evaporate, and leave it in a room at 30 ° C for 42 hours to cure it while containing water and cure. I removed my body. Five specimens were prepared for each stirring method. [Table 1] The breaking strength of the obtained cured product was measured according to JIS K7203 (bending test method for hard plastic: three-point bending strength), and the bending strength was calculated from the breaking strength and the sample breaking size. Autograph AG-10KNE manufactured by Shimadzu Corporation was used as a material testing machine. Table 2 shows the test results. [Table 2] As shown in Table 2, it was found that the cured product produced by stirring with a reciprocating rotary stirrer had much higher bending strength and less variation in strength than the cured product produced by stirring with another stirrer.

【0024】[実施例2]次に実施例1と同様の調合に
おいてプロペラ型羽根の回転攪拌機およびホモジナイザ
ーの攪拌で、より均一なフィラーの分散と均一なエマル
ジョン生成までの時間(視感)と連続気孔多孔体形成用混
合物の粘度をB型粘度計にて測定した。結果を表3に示
す。 [表3] 表3に示されるように、均一なフィラーの分散を得るた
めにプロペラ型羽根の回転攪拌機およびホモジナイザー
では長時間攪拌が必要であり、その結果、連続気孔多孔
体形成用混合物の粘度は大幅に上昇し、流し込みに支障
がでることがわかった。
[Example 2] Next, in the same preparation as in Example 1, continuous rotation of the propeller type blade and the homogenizer was performed to obtain a more uniform dispersion of the filler and a continuous time (visual sensation) until uniform emulsion formation. The viscosity of the mixture for forming a porous material was measured with a B-type viscometer. Table 3 shows the results. [Table 3] As shown in Table 3, long-time stirring is required for the propeller-type blade rotary stirrer and the homogenizer in order to obtain a uniform filler dispersion, and as a result, the viscosity of the mixture for forming a continuous porous material greatly increases. Then, it turned out that pouring was hindered.

【0025】[実施例3]次にダイラタンシー流動性が
発現する調合例(表4)と、界面活性剤添加によりダイ
ラタンシー流動性を抑制した結果(表5)を示す。攪拌
機は往復回転式攪拌機を使用した。 [表4] [表5] ダイラタンシー流動性が発現する混合物の場合、往復回
転式攪拌機のみ(界面活性剤なし)ではフィラーの均一分
散、均一なエマルジョン作製が困難であることが曲げ強
度測定値のバラツキからもわかる。ダイラタンシー流動
性が発現する混合物においては、調合時に界面活性剤を
少量加え、往復回転式攪拌機で攪拌することにより均一
なスラリーの作製ができることがわかった。
[Example 3] Next, a formulation example (Table 4) in which dilatancy fluidity is developed and a result (Table 5) in which dilatancy fluidity is suppressed by adding a surfactant are shown. As the stirrer, a reciprocating rotary stirrer was used. [Table 4] [Table 5] In the case of a mixture exhibiting dilatancy flowability, it can be seen from the dispersion of the measured bending strength that it is difficult to uniformly disperse the filler and prepare a uniform emulsion using only a reciprocating rotary stirrer (without a surfactant). It was found that in a mixture exhibiting dilatancy fluidity, a uniform slurry can be prepared by adding a small amount of a surfactant at the time of preparation and stirring with a reciprocating rotary stirrer.

【0026】[0026]

【発明の効果】本発明によれば、泥漿鋳込み成形型に使
用される樹脂製連続気孔多孔体の製造に際して、エポキ
シ等の化合物とフィラーと水からなる混合物を短時間で
均一に攪拌・分散した均質な連続気孔多孔体形成用混合
物を得る攪拌方法を提供することが可能となる。
According to the present invention, a mixture of a compound such as epoxy, a filler, and water is uniformly stirred and dispersed in a short time in the production of a resin continuous porous material used in a slurry casting mold. It is possible to provide a stirring method for obtaining a homogeneous mixture for forming continuous porous media.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の一実施態様である反転機能を持つ往復
回転式攪拌機を用いた攪拌槽内の乱流状態を示す図であ
る。
FIG. 1 is a diagram showing a turbulent state in a stirring tank using a reciprocating rotary stirrer having a reversing function according to an embodiment of the present invention.

【図2】本発明の一実施態様である二枚羽根の攪拌羽根
を示す図である。
FIG. 2 is a diagram showing a two-blade stirring blade according to an embodiment of the present invention.

【図3】本発明の一実施態様である一枚羽根の二段攪拌
羽根を示す図である。
FIG. 3 is a view showing a single-stage two-stage stirring blade according to an embodiment of the present invention.

【図4】本発明一実施態様であるの攪拌羽根の断面部形
状を交換した攪拌槽内の乱流状態を示す図である。
FIG. 4 is a diagram showing a turbulent state in a stirring tank in which a cross-sectional shape of a stirring blade according to an embodiment of the present invention is changed.

【図5】従来の一枚羽根の攪拌羽根を示す図である。FIG. 5 is a view showing a conventional single blade stirring blade.

【図6】従来の一般的な一枚羽根式回転攪拌機を用いた
攪拌槽内の混合状態を示す図である。
FIG. 6 is a view showing a mixing state in a stirring tank using a conventional general single-blade rotary stirrer.

【符号の説明】[Explanation of symbols]

1…攪拌槽 2…回転軸 3…一枚羽根 4…乱流 5…二枚羽根 6…プロペラ型羽根 7…回転流 DESCRIPTION OF SYMBOLS 1 ... Stirring tank 2 ... Rotating shaft 3 ... Single blade 4 ... Turbulence 5 ... Two blades 6 ... Propeller type blade 7 ... Rotary flow

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4F070 AA46 AC12 AE01 AE08 AE14 FA04 FC02 4J002 CD001 CD051 CH053 CL002 DE028 DJ006 DL006 EV259 FD016 FD142 FD147 FD313 FD319  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4F070 AA46 AC12 AE01 AE08 AE14 FA04 FC02 4J002 CD001 CD051 CH053 CL002 DE028 DJ006 DL006 EV259 FD016 FD142 FD147 FD313 FD319 FD319

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 少なくともエポキシ化合物、硬化剤、フ
ィラー、水とを含む連続気孔多孔体形成用混合物の攪拌
方法であって、前記連続気孔多孔体形成用混合物を一方
回転でなく反転機能を持つ往復回転式攪拌機を用いて攪
拌することを特徴とする連続気孔多孔体形成用混合物の
攪拌方法。
1. A method for agitating a mixture for forming a continuous porous body containing at least an epoxy compound, a curing agent, a filler, and water, wherein the mixture for forming a continuous porous body is reciprocated not having one rotation but a reversing function. A method for stirring a mixture for forming a continuous porous material, which comprises stirring using a rotary stirrer.
【請求項2】 前記往復回転式攪拌機が2枚以上あるい
は2段以上の攪拌羽根を備えていることを特徴とする請
求項1に記載の連続気孔多孔体形成用混合物の攪拌方
法。
2. The method according to claim 1, wherein the reciprocating rotary stirrer has two or more or two or more stages of stirring blades.
【請求項3】 前記フィラーの比重により前記攪拌羽根
の断面部形状を変更することを特徴とする請求項2に記
載の連続気孔多孔体形成用混合物の攪拌方法。
3. The method for stirring a mixture for forming a continuous porous material according to claim 2, wherein the shape of the cross section of the stirring blade is changed depending on the specific gravity of the filler.
【請求項4】 前記フィラーの比重が1以上の場合に、
前記攪拌羽根の断面部形状を前記混合物が攪拌槽内で上
方から下方に向って乱流を起こす形状とすることを特徴
とする請求項3に記載の連続気孔多孔体形成用混合物の
攪拌方法。
4. When the specific gravity of the filler is 1 or more,
The method for stirring a mixture for forming a continuous porous material according to claim 3, wherein the shape of the cross section of the stirring blade is such that the mixture causes a turbulent flow from above to below in the stirring tank.
【請求項5】 前記フィラーの比重が1未満の場合に、
前記攪拌羽根の断面部形状を前記混合物が攪拌槽内で下
方から上方に向って乱流を起こす形状とすることを特徴
とする請求項3に記載の連続気孔多孔体形成用混合物の
攪拌方法。
5. When the specific gravity of the filler is less than 1,
4. The method for stirring a mixture for forming a continuous porous material according to claim 3, wherein the shape of the cross section of the stirring blade is such that the mixture causes a turbulent flow from below to above in the stirring tank.
【請求項6】 前記攪拌の時に界面活性剤を添加するこ
とを特徴とする請求項1乃至5のいずれかに記載の連続
気孔多孔体形成用混合物の攪拌方法。
6. The method for stirring a mixture for forming a continuous porous material according to claim 1, wherein a surfactant is added during the stirring.
JP2001009892A 2001-01-18 2001-01-18 Method for agitating mixture for forming open-cell porous material Pending JP2002212306A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001009892A JP2002212306A (en) 2001-01-18 2001-01-18 Method for agitating mixture for forming open-cell porous material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001009892A JP2002212306A (en) 2001-01-18 2001-01-18 Method for agitating mixture for forming open-cell porous material

Publications (1)

Publication Number Publication Date
JP2002212306A true JP2002212306A (en) 2002-07-31

Family

ID=18877304

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001009892A Pending JP2002212306A (en) 2001-01-18 2001-01-18 Method for agitating mixture for forming open-cell porous material

Country Status (1)

Country Link
JP (1) JP2002212306A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109107411A (en) * 2018-10-26 2019-01-01 临海市朵纳卫浴有限公司 A kind of manufacture of bathroom cabinet plate gluing centrifugation glue mixing device and its impregnation technique

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109107411A (en) * 2018-10-26 2019-01-01 临海市朵纳卫浴有限公司 A kind of manufacture of bathroom cabinet plate gluing centrifugation glue mixing device and its impregnation technique
CN109107411B (en) * 2018-10-26 2023-12-19 浙江朵纳家居股份有限公司 Centrifugal glue mixing device for bathroom cabinet plate gluing manufacture and glue mixing process thereof

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