JP2801740B2 - Method for producing flexible vegetable fiberboard - Google Patents

Method for producing flexible vegetable fiberboard

Info

Publication number
JP2801740B2
JP2801740B2 JP12927290A JP12927290A JP2801740B2 JP 2801740 B2 JP2801740 B2 JP 2801740B2 JP 12927290 A JP12927290 A JP 12927290A JP 12927290 A JP12927290 A JP 12927290A JP 2801740 B2 JP2801740 B2 JP 2801740B2
Authority
JP
Japan
Prior art keywords
aqueous emulsion
producing
weight
fiberboard
fiber
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.)
Expired - Lifetime
Application number
JP12927290A
Other languages
Japanese (ja)
Other versions
JPH0425402A (en
Inventor
清人 土井
嘉夫 葛巻
峰昭 穴田
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.)
Mitsui Chemicals Inc
Original Assignee
Mitsui Chemicals Inc
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 Mitsui Chemicals Inc filed Critical Mitsui Chemicals Inc
Priority to JP12927290A priority Critical patent/JP2801740B2/en
Publication of JPH0425402A publication Critical patent/JPH0425402A/en
Application granted granted Critical
Publication of JP2801740B2 publication Critical patent/JP2801740B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、木質または植物質の外観を有し、且つ、可
撓性をも有して曲面での使用が可能であり、または衝撃
吸収性を有し床等のクッション材としても使用可能な可
撓性植物質繊維板の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention has a woody or plant-like appearance, has flexibility, can be used on a curved surface, or has a shock absorbing property. The present invention relates to a method for producing a flexible vegetable fiberboard which has properties and can be used as a cushion material for floors and the like.

〔従来の技術〕[Conventional technology]

植物質繊維を主原料として利用した板状材は、従来よ
りインシュレーションボード、ハードボード、MDFと称
されて生産され、防音材、断熱材、畳心材、家具部材、
自動車用部材、床材等として使用されている。しかし、
これらの植物質繊維板は、主原料として木質繊維を用い
るため、原料の入手が容易であり、経済的にも低価格で
あるとの利点はあるものの、そのバインダーとしてホル
ムアルデヒド系の縮合樹脂を使用してきたため、可撓性
がなく、曲面状での使用が困難であり、また衝撃吸収性
が良くないため、床等のクッション材としての使用にも
難点があった。
Plate materials that use vegetable fiber as the main raw material have been conventionally produced as insulation boards, hardboards, and MDFs.
It is used as an automobile member, floor material, and the like. But,
These vegetable fiber boards use wood fiber as the main raw material, so they are easy to obtain and have the advantage of being economically inexpensive, but use formaldehyde-based condensation resin as their binder. Therefore, there is no flexibility, it is difficult to use it on a curved surface, and it has poor shock absorption, so that it has a problem in use as a cushion material for floors and the like.

一方、可撓性植物性板材としてコルク板や、粒状コル
クを接合した板状物があるが、限定された天然物である
ため、原料の多量入手が困難であったり、経済的な問題
もあり広く使用されるには問題がある。
On the other hand, there is a cork board as a flexible vegetable board material, and a plate-like material obtained by joining granular cork, but since it is a limited natural product, it is difficult to obtain a large amount of raw materials, and there is also an economic problem. There are problems with widespread use.

このような問題点を解消するため、木質繊維に合成ゴ
ムラテックスを混合し、乾燥後、マット状に集積し、加
熱圧締し、屈曲性繊維板を製造する方法や、稲および/
または麦わらの切断片や木材チップ、コルク粒、籾殻等
に合成ゴムラテックスを主剤とし加硫剤を添加した物、
または合成ゴムラテックスを主剤とし加硫剤を添加した
物に更にアミノ系樹脂を加えたものをバインダーとして
接着し、クッション性を有する床材等の用途のボードの
製造方法などの技術が開示されている。
In order to solve such problems, synthetic rubber latex is mixed with wood fiber, dried, then collected in a mat form, heated and pressed to produce a flexible fiberboard, rice and / or rice.
Or a product obtained by adding a vulcanizing agent to a synthetic rubber latex as a main ingredient in a piece of straw, wood chips, cork grains, rice husk, or the like,
Also disclosed are techniques such as a method of manufacturing a board for use as a flooring material having a cushioning property by bonding a material obtained by adding a vulcanizing agent to a synthetic rubber latex as a main component and further adding an amino resin to a binder. I have.

しかしながら、これらの方法では、真に可撓性・衝撃
吸収性を有する繊維板や、可撓性・衝撃吸収性を保持し
充分な耐久性をも有する繊維板の製造には未だ問題があ
る。
However, these methods still have problems in the production of a fiberboard that is truly flexible and shock-absorbing and a fiberboard that retains flexibility and shock-absorbing properties and has sufficient durability.

すなわち、前者の方法では、使用するバインダーは合
成ゴムラテックスとのみ記載されているが、後述するよ
うに、あらゆる種類の合成ゴムラテックスで充分な可撓
性が得られるものではなく、また合成ゴムラテックスの
みの使用では、耐水性に乏しく、湿度・水分にさらされ
る環境での耐久性に欠ける。後者の方法では、加硫を行
ったり、アミノ系樹脂を加えるので、バインダー自体が
硬くなり、あらゆる種類の合成ゴムラテックスで充分な
る可撓性は得難い。
That is, in the former method, the binder used is described only as a synthetic rubber latex, but as described later, not all types of synthetic rubber latex provide sufficient flexibility, and the synthetic rubber latex is not used. When used alone, it has poor water resistance and lacks durability in an environment exposed to humidity and moisture. In the latter method, vulcanization is performed or an amino resin is added, so that the binder itself becomes hard, and it is difficult to obtain sufficient flexibility with all types of synthetic rubber latex.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

本発明は、廉価に入手し易い植物質繊維を用い、簡便
な方法で繊維板を製造することを目的とし、更に、充分
な可撓性を有し且つ必要に応じ、耐水性・耐久性を併せ
持つ繊維板の製造を目的とする。
An object of the present invention is to produce a fiberboard by a simple method using inexpensive vegetable fiber, and further have sufficient flexibility and, if necessary, water resistance and durability. The purpose is to produce a fiberboard that has both.

〔課題を解決するための手段〕[Means for solving the problem]

本発明は、乾燥硬化後の主ガラス転移点が−20℃から
10℃である組成物の水性エマルジョンを、植物質繊維の
乾燥重量100重量部に対し、固形分として4〜40重量部
混合し、混合後の水分量を20重量%以下となるように調
整した後積層し、積層マットを圧締して成形することを
特徴とする可撓性植物質繊維板の製造方法である。
The present invention has a main glass transition point after drying and curing from -20 ° C.
An aqueous emulsion of the composition at 10 ° C. was mixed with 4 to 40 parts by weight as a solid content based on 100 parts by weight of the dry weight of the vegetable fiber, and the water content after mixing was adjusted to 20% by weight or less. A method for producing a flexible vegetable fiberboard, which comprises laminating afterwards, and pressing and molding a laminated mat.

本発明にいう植物質繊維とは、木材を解繊もしくは粉
砕もしくは切断もしくは研磨して得られる木質ファイバ
ーおよび/または、単子葉植物の茎または種子殻を解繊
もしくは粉砕もしくは切断して得られるファイバーの1
種または2種以上の混合物を80重量%以上含むものが望
ましく、そのほかに微粒のコルク質粒子、有機物もしく
は無機質発泡体、綿、羊毛、絹等の天然繊維、合成繊維
を含有していても構わない。
The plant fiber referred to in the present invention is a wood fiber obtained by fibrillating, pulverizing, cutting, or polishing wood and / or a fiber obtained by fibrillating, pulverizing, or cutting a stem or a seed shell of a monocotyledon. Of 1
It is desirable that the composition contains at least 80% by weight of a seed or a mixture of two or more kinds. In addition, it may contain fine cork particles, organic or inorganic foams, natural fibers such as cotton, wool, silk, and synthetic fibers. Absent.

本発明にいう主ガラス転移点が−20℃から10℃の水性
エマルジョンとは、ブタジエン、イソプレンの如き共役
ジエンにこれらと共重合するモノマー例えばスチレン、
メチルメタクリレート、アクリロニトリルの如き各種ビ
ニルモノマー類を共重合させたラテックス、天然ゴムラ
テックス、クロロプレンラテックス、ブチルゴムラテッ
クス、アクリル樹脂エマルジョン、エチレン酢酸ビニル
共重合体エマルジョン、ポリ酢酸ビニルエマルジョン、
またはこれら水性エマルジョンにカルボキシル基、N−
メチロール基、N−アルコキシメチル基、グリシジル
基、β−メチルグリシジル基、水酸基、アミノ基、およ
び酸無水物等の架橋し得る反応基を少なくとも1種側鎖
に有する反応性モノマーの少なくとも1種を重合させた
いわゆる変成ラテックス等の1種または2種以上の重合
体等の混合物で、その主ガラス転移点が、−20℃から10
℃のものであり、望ましくは−10℃から5℃、更に望ま
しくは−5℃から5℃のものである。ガラス転移点が−
20℃未満の場合、植物質繊維に水性エマルジョンを混合
した後、散布積層する際、繊維同士が付着し易く、散布
後の厚みや密度が均質とならず、安定的な品質の繊維板
を得るには問題となる。また、ガラス転移点が10℃を越
える場合、得られる繊維板の可撓性が、常用温度で不充
分となり、本発明の目的を満足することができない。ガ
ラス転移点が上記範囲を満足させる範囲内で、水性エマ
ルジョンが、ポリビニルアルコールやセルロース誘導体
やデンプン誘導体の様な水溶性高分子化合物、小麦粉、
無機質粉体の様な充填剤を含有していても構わない。
The aqueous emulsion having a main glass transition point of −20 ° C. to 10 ° C. as referred to in the present invention is a monomer which copolymerizes with conjugated dienes such as butadiene and isoprene, for example, styrene.
Latex, natural rubber latex, chloroprene latex, butyl rubber latex, acrylic resin emulsion, ethylene vinyl acetate copolymer emulsion, polyvinyl acetate emulsion, copolymerized latex of various vinyl monomers such as methyl methacrylate and acrylonitrile,
Alternatively, carboxyl groups, N-
At least one reactive monomer having at least one crosslinkable reactive group such as a methylol group, an N-alkoxymethyl group, a glycidyl group, a β-methylglycidyl group, a hydroxyl group, an amino group, and an acid anhydride in a side chain; A mixture of one or more polymers, such as so-called modified latex, which has been polymerized and whose main glass transition point is from -20 ° C to 10 ° C.
° C, preferably -10 ° C to 5 ° C, more preferably -5 ° C to 5 ° C. Glass transition point is-
When the temperature is lower than 20 ° C., when the aqueous emulsion is mixed with the vegetable fiber and then sprinkled and laminated, the fibers tend to adhere to each other, and the thickness and density after the spraying are not uniform, and a stable quality fiberboard is obtained. Is a problem. On the other hand, when the glass transition point exceeds 10 ° C., the flexibility of the obtained fiberboard becomes insufficient at ordinary temperatures, and the object of the present invention cannot be satisfied. As long as the glass transition point satisfies the above range, the aqueous emulsion is a water-soluble polymer compound such as polyvinyl alcohol, a cellulose derivative, or a starch derivative, flour,
A filler such as an inorganic powder may be contained.

前述の水性エマルジョンのみをバインダーとして使用
した繊維板でも、常態で充分な可撓性と実用的な強度を
有するが、湿度が高い雰囲気で使用する場合や、水がか
かるような用途では耐水性に問題がある。このような用
途として使用する繊維板の耐水性を向上させる方法とし
ては、イソシアネート化合物による変成が望ましい。イ
ソシアネート化合物の添加量は特に限定しないが、イソ
シアネート化合物による変成を行う場合でも、可撓性を
有する繊維板を得るためには、水性エマルジョンとイソ
シアネート化合物の混合物の乾燥硬化後の主ガラス転移
点が−20℃から10℃となるように、水性エマルジョンと
イソシアネート化合物の種類および比率を調整する必要
がある。
The fiberboard using only the above-mentioned aqueous emulsion as a binder has sufficient flexibility and practical strength under normal conditions, but when used in a humid atmosphere or in applications where it is exposed to water, it is water resistant. There's a problem. As a method for improving the water resistance of the fiberboard used for such a purpose, denaturation with an isocyanate compound is desirable. The amount of the isocyanate compound added is not particularly limited, but even in the case of performing denaturation with the isocyanate compound, the main glass transition point after drying and curing of the mixture of the aqueous emulsion and the isocyanate compound is required to obtain a flexible fiberboard. It is necessary to adjust the types and ratios of the aqueous emulsion and the isocyanate compound so that the temperature is from −20 ° C. to 10 ° C.

イソシアネート化合物とは、分子中に2個以上のイソ
シアネート基を有する化合物で、例えば、トリレンジイ
ソシアネート(TDI)、4,4′−ジフェニルメタンジイソ
シアネート(MDI)、ヘキサメチレンジイソシアネート
(HMDI)、キシレンジイソシアネート(XDI)、イソホ
ロンジイソシアネート(IPDI)、ポリメチレンポリフェ
ニルポリイソシアネート(ポリメリックMDI)が例示さ
れる。また、これらのイソシアネート化合物とポリオー
ルを混合したもの、過剰のイソシアネートとポリオール
で予めポリマー化しイソシアネート基が残有するいわゆ
るプレポリマーも使用することができる。
An isocyanate compound is a compound having two or more isocyanate groups in a molecule, for example, tolylene diisocyanate (TDI), 4,4'-diphenylmethane diisocyanate (MDI), hexamethylene diisocyanate (HMDI), xylene diisocyanate (XDI ), Isophorone diisocyanate (IPDI) and polymethylene polyphenyl polyisocyanate (polymeric MDI). In addition, a mixture of these isocyanate compounds and a polyol, or a so-called prepolymer which is polymerized in advance with an excess of isocyanate and polyol and has an isocyanate group remaining can also be used.

イソシアネート化合物は一般的に水溶性ではないた
め、水性エマルジョンとの均一な混合に支障を生ずる場
合もある。このような場合、界面活性剤を用いて分散を
行う方法も採れるが、簡便により均一に分散混合させる
ためには、イソシアネート化合物に、単官能アルコール
にアルキレンオキサイドを付加せしめた化合物を作用さ
せ易乳化性としたイソシアネート化合物を用いる方法が
最も望ましい。充分な乳化性を付与するためには、単官
能アルコールの分子量は100以下のものが好ましく、ア
ルキレンオキサイドの付加数は10以上が好ましい。
Since isocyanate compounds are generally not water-soluble, they may interfere with uniform mixing with an aqueous emulsion. In such a case, a method of dispersing using a surfactant may be employed, but in order to easily and uniformly disperse and mix, a compound obtained by adding an alkylene oxide to a monofunctional alcohol is allowed to act on an isocyanate compound to easily emulsify. Most preferred is a method using an isocyanate compound which has been rendered neutral. In order to impart sufficient emulsifiability, the molecular weight of the monofunctional alcohol is preferably 100 or less, and the number of alkylene oxides added is preferably 10 or more.

また、水性エマルジョンを混合した植物繊維を搬送し
たり、圧締する際、配管内面やプレス面が低エネルギー
界面となるよう被覆もしくは離型剤塗布処理されている
場合は余り問題とはならないが、このような処理がなさ
れていない場合は、水性エマルジョンを混合した植物繊
維が、配管内面やプレス面に付着し、安定的な生産や、
均質な物性の繊維板の生産に支障となる。被覆もしくは
離型剤塗布処理は効果の持続性に問題があり、頻繁な処
理が必要となる。HLB値6以上のポリオキシアルキレン
モノアルキルアリルエーテルおよび/またはポリオキシ
アルキレンモノアルキルエーテルおよび/またはポリオ
キシアルキレンモノ脂肪酸エーテルの、燐酸エステルを
水性エマルジョンに混合し使用することで、このような
付着の問題を解消する事ができる。HLB値6未満の場合
は、水性エマルジョンとの混合に問題を生じたり、付着
防止効果が低下する。添加率は、水性エマルジョン固形
分当り10重量%以下が好ましい。
In addition, when conveying or compressing vegetable fibers mixed with an aqueous emulsion, when coating or a release agent is applied so that the inner surface of the pipe or the pressed surface has a low energy interface, there is not much problem, If such treatment is not performed, vegetable fibers mixed with the aqueous emulsion will adhere to the inner surface of the pipe and the press surface, and stable production,
This hinders the production of fiberboard with uniform physical properties. The coating or release agent application treatment has a problem in the persistence of the effect, and requires frequent treatment. The use of a phosphate mixture of a polyoxyalkylene monoalkyl allyl ether and / or a polyoxyalkylene monoalkyl ether and / or a polyoxyalkylene monofatty acid ether having an HLB value of 6 or more mixed with an aqueous emulsion allows use of such an adhesion. The problem can be solved. If the HLB value is less than 6, a problem may occur in mixing with the aqueous emulsion, or the effect of preventing adhesion is reduced. The addition rate is preferably 10% by weight or less based on the solid content of the aqueous emulsion.

植物質繊維に対する水性エマルジョンの混合比率は、
植物質繊維の乾燥重量100重量部に対し、固形分として
4〜40重量部である。4重量部未満では、得られる繊維
板の強度が充分とはならない。また、40重量部%を越え
ると、植物質繊維に水性エマルジョンを混合した後、散
布積層する際、繊維同士が付着し易く、散布後の厚みや
密度が均質とならず、均質な外面で安定的な品質の繊維
板を得るには問題となる。
The mixing ratio of the aqueous emulsion to the vegetable fiber is
The solid content is 4 to 40 parts by weight based on 100 parts by weight of the dry weight of the vegetable fiber. If the amount is less than 4 parts by weight, the strength of the obtained fiberboard will not be sufficient. If the content exceeds 40% by weight, the fibers tend to adhere to each other when the vegetable fiber is mixed with the aqueous emulsion and then sprayed and laminated, and the thickness and density after spraying are not uniform and stable on a uniform outer surface. There is a problem in obtaining a fiberboard of a proper quality.

植物質繊維と水性エマルジョンの混合方法は、特に限
定しないが、混合後の水分量を20重量%以下となるよう
に調整した後積層する必要がある。水分量が20重量%を
越える場合は、散布積層する際、繊維同士が付着し易
く、前述と同様の問題を生じるばかりでなく、引続き行
う加圧成形操作において、水分が繊維板層間に残存し、
接着強度を低下させ、また、加熱圧締する場合には、解
圧時、気化した水分が繊維板層間から揮散する際接着層
を破壊するいわゆるパンクという現象を生じ易い。
The method of mixing the vegetable fiber and the aqueous emulsion is not particularly limited, but it is necessary to adjust the water content after mixing so as to be 20% by weight or less before laminating. If the water content exceeds 20% by weight, the fibers tend to adhere to each other when scattered and laminated, and not only the same problem as described above occurs, but also water remains between the fiberboard layers in the subsequent pressing operation. ,
In the case of lowering the adhesive strength and heating and pressing, a phenomenon called so-called puncturing, which breaks the adhesive layer when the vaporized moisture volatilizes between the fiberboard layers upon decompression, is likely to occur.

成型する際の圧締方法については、特に限定しない
が、本発明の水性エマルジョンにおいては、その接着作
用は、過剰水分の揮散と、イソシアネート化合物を混合
する場合ではイソシアネート基と水性エマルジョンおよ
び/または植物質繊維との反応によって発現する。した
がって、生産性を考慮すると、加熱し過剰水分の揮散
と、イソシアネート化合物を混合する場合ではイソシア
ネート基と水性エマルジョンおよび/または植物質繊維
との反応を助長することが望ましい。加熱圧締条件は、
加熱温度が70〜200℃が望ましく、初期圧力を2〜8N/mm
2とし、加熱中の板状物の中心層温度が70〜100℃になっ
た時点で圧力を0.2〜1.8N/mm2に低下することが更に望
ましい。加熱温度が70℃未満の場合は、生産性の向上が
期待できないし、200℃以上では、いわゆるパンクを起
こし易い。初期圧力を2〜8N/mm2とし所定厚みまででき
るだけ速く圧縮し、板状物の中心層温度が70〜100℃に
なり繊維板含有水分が揮散し易くなった時点で、厚みが
所定値を越さない範囲で圧力を0.2〜1.8N/mm2に低下し
板外へ除去し易くすることで生産性向上が期待できる。
The pressing method at the time of molding is not particularly limited. However, in the aqueous emulsion of the present invention, the adhesive action is caused by evaporation of excess water and, when an isocyanate compound is mixed, an isocyanate group and an aqueous emulsion and / or a plant. Expressed by the reaction with the quality fiber. Therefore, in consideration of productivity, it is desirable to promote the evaporation of excess moisture by heating and, when mixing an isocyanate compound, the reaction between the isocyanate group and the aqueous emulsion and / or vegetable fiber. The heating and pressing conditions are:
Desirable heating temperature is 70 ~ 200 ℃, initial pressure is 2 ~ 8N / mm
2, and the center layer temperature of the platelet during heating it is further desirable to reduce the pressure to 0.2~1.8N / mm 2 as it becomes 70 to 100 ° C.. If the heating temperature is lower than 70 ° C., no improvement in productivity can be expected, and if the heating temperature is 200 ° C. or higher, so-called puncturing tends to occur. When the initial pressure is 2 to 8 N / mm2 and the material is compressed as quickly as possible to a predetermined thickness, and when the temperature of the center layer of the plate-like material becomes 70 to 100 ° C and the water content of the fiberboard becomes easy to volatilize, the thickness becomes a predetermined value. The productivity is expected to be improved by reducing the pressure to 0.2 to 1.8 N / mm 2 within the range not to exceed, and making it easy to remove outside the plate.

〔実施例〕〔Example〕

以下、実施例を用いて本発明を詳述するが、本発明は
これら実施例により何ら限定されるものではない。尚、
参考例、実施例中の部、%はそれぞれ重量部、重量%を
表す。
Hereinafter, the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples. still,
Parts and% in Reference Examples and Examples represent parts by weight and% by weight, respectively.

参考例−1(乳化性イソシアネート調製) ジエチレングリコールモノメチルエーテル219.0部と
水酸化カリウム4.45部をオートクレーブに入れ、窒素ガ
ス置換後90℃に昇温しエチレンオキサイド1052部を加圧
下に反応させ、更にプロピレンオキサイド211.4部を反
応させた。反応生成物を理論量の燐酸で中和し、濾過し
た。得られた化合物25部を反応容器に入れ、窒素気流下
常温にてCR−300(粗製ジフェニルメタンジイソシアネ
ート 三井東圧化学株式会社製)1000部を添加し混合後
80℃で2時間反応させ易乳化性のイソシアネート化合物
を得た。
Reference Example 1 (Preparation of emulsifying isocyanate) 219.0 parts of diethylene glycol monomethyl ether and 4.45 parts of potassium hydroxide were placed in an autoclave, and after purging with nitrogen gas, the temperature was raised to 90 ° C, and 1052 parts of ethylene oxide were reacted under pressure, and propylene oxide was further added. 211.4 parts were reacted. The reaction product was neutralized with a theoretical amount of phosphoric acid and filtered. Put 25 parts of the obtained compound in a reaction vessel, add 1000 parts of CR-300 (crude diphenylmethane diisocyanate, manufactured by Mitsui Toatsu Chemicals, Inc.) at room temperature under a nitrogen stream and mix.
The mixture was reacted at 80 ° C. for 2 hours to obtain an easily emulsifiable isocyanate compound.

参考例−2(離型剤調製) エマルゲン404(ポリオキシエチレンモノオレイルエ
ーテル、HLB値8.8、花王アトラス社製)2000部に、窒素
気流下70℃に昇温し、撹拌下五酸化燐430部を徐々に添
加し、100℃で3時間反応せしめて、燐酸エステルを得
た。
Reference Example-2 (Preparation of release agent) Emulgen 404 (polyoxyethylene monooleyl ether, HLB value: 8.8, manufactured by Kao Atlas Co., Ltd.) was heated to 70 ° C under a nitrogen stream in 2000 parts and 430 parts of phosphorus pentoxide was stirred. Was slowly added and reacted at 100 ° C. for 3 hours to obtain a phosphoric ester.

実施例−1 蒸煮し機械的に解繊した含水率50%のラワン系木質繊
維1500部に対し、ガラス転移点が−4℃のSMBR系のラテ
ックス(不揮発分45%)200部を均一にスプレー塗布
し、含水率が15%となるように乾燥した。バインダーを
塗布した繊維400gを、30cm角のボックス中に均一厚みに
なるように堆積した後、熱板温度170℃のプレスで4N/mm
2の圧力で2分間圧締し、その後圧力を1N/mm2で3分間
圧締して厚み5mm、密度0.79g/cm3の繊維板を得た。
Example 1 200 parts of SMBR-based latex (non-volatile content: 45%) having a glass transition point of -4 ° C are uniformly sprayed on 1500 parts of steamed and mechanically defibrated Rawan-based wood fiber having a water content of 50%. It was applied and dried to a water content of 15%. 400 g of the fiber coated with the binder was deposited in a 30 cm square box so as to have a uniform thickness.
And pressing 2 min in 2 pressure, to give a thickness 5 mm, the fiber board of a density 0.79 g / cm 3 by pressing after which the pressure in 1N / mm 2 3 minutes.

この繊維板のJIS−Z−2116に規定された方法による
衝撃吸収エネルギーは48kgf・cm/cm2、最小屈曲半径は6
0mmであった。
The impact absorption energy of this fiberboard according to the method specified in JIS-Z-2116 is 48 kgf · cm / cm 2 , and the minimum bending radius is 6
It was 0 mm.

実施例−2 実施例−1と同一のラワン系木質繊維1500部に対し、
SMBR系ラテックス(不揮発分45%)200部と参考例−1
で得た易乳化型イソシアネート化合物を20部に均一に混
合したもの(該混合物のフィルム化後の主ガラス転移点
は1℃であった)を混合後直ちにスプレー塗布し、含水
率が10%となるように乾燥した。バインダーを塗布した
繊維400gを、30cm角のボックス中に均一に厚みになるよ
うに堆積した後、熱板温度170℃のプレスで5分間圧締
し、厚み5mm、密度0.78g/cm3の繊維板を得た。この繊維
板の衝撃吸収エネルギーは46kgf・cm/cm2、最小屈曲半
径は68mmであった。
Example 2 For 1500 parts of the same Lauan wood fiber as in Example 1,
200 parts of SMBR latex (non-volatile content: 45%) and Reference Example-1
A mixture obtained by uniformly mixing 20 parts of the easily emulsified isocyanate compound obtained in (the main glass transition point after film formation of the mixture was 1 ° C.) was sprayed immediately after mixing, and the water content was increased to 10%. Dried to become. The fibers 400g of binder was applied, was deposited to uniformly become thick in box 30cm square, and pressing for 5 minutes at hot plate temperature 170 ° C. of the press, the thickness 5 mm, the fiber density of 0.78 g / cm 3 I got a board. The impact absorption energy of this fiberboard was 46 kgf · cm / cm 2 , and the minimum bending radius was 68 mm.

実施例−3〜9/比較例−1〜4 実施例1および2と類似した方法で、繊維板を製造
し、評価した。条件および結果は表−1にまとめて示
す。
Examples -3 to 9 / Comparative Examples -1 to 4 Fiberboards were produced and evaluated in a similar manner to Examples 1 and 2. The conditions and results are summarized in Table 1.

〔発明の効果〕 本発明により、可撓性を有し、且つ必要により耐水性
を有する植物質繊維板が簡便なる方法により、特に作業
性を低下させる事なく製造しうることが明確である。
[Effects of the Invention] It is clear that the present invention makes it possible to produce a flexible and, if necessary, water-resistant vegetable fiberboard by a simple method without lowering workability.

Claims (7)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】乾燥硬化後の主ガラス転移点が−20℃から
10℃である組成物の水性エマルジョンを、植物質繊維の
乾燥重量100重量部に対し、固形分として4〜40重量部
混合し、混合後の水分量を20重量%以下となるように調
整した後積層し、積層マットを圧締して成形することを
特徴とする可撓性植物質繊維板の製造方法。
The main glass transition point after drying and curing is from -20 ° C.
An aqueous emulsion of the composition at 10 ° C. was mixed with 4 to 40 parts by weight as a solid content based on 100 parts by weight of the dry weight of the vegetable fiber, and the water content after mixing was adjusted to 20% by weight or less. A method for producing a flexible vegetable fiberboard, comprising laminating the laminate and pressing the laminated mat to form the laminate.
【請求項2】水性エマルジョンとイソシアネート化合物
を主成分とする混合物で、混合物の乾燥硬化後の主ガラ
ス転移点が−20℃から10℃である混合物のエマルション
を、水性エマルジョンとして用いる請求項(1)に記載
の可撓性植物質繊維板の製造方法。
2. An aqueous emulsion comprising a mixture containing an aqueous emulsion and an isocyanate compound as main components and having a main glass transition point of -20 ° C. to 10 ° C. after drying and curing of the mixture. A) a method for producing a flexible vegetable fiberboard;
【請求項3】イソシアネート化合物として、単官能アル
コールにアルキレンオキサイドを付加せしめた化合物を
イソシアネート化合物に作用させ易乳化性としたものを
用いる請求項(2)に記載の可撓性植物質繊維板の製造
方法。
3. The flexible vegetable fiber board according to claim 2, wherein the isocyanate compound is a compound obtained by adding a compound obtained by adding an alkylene oxide to a monofunctional alcohol to make the isocyanate compound easier to emulsify. Production method.
【請求項4】水性エマルジョンが、合成ゴムラテックス
および/または天然ゴムラテックスおよび/またはアク
リル系エマルジョンの1種または2種以上の混合物であ
る請求項(1)〜(3)のいずれかの項に記載の可撓性
植物質繊維板の製造方法。
4. The method according to claim 1, wherein the aqueous emulsion is one or a mixture of two or more of synthetic rubber latex and / or natural rubber latex and / or acrylic emulsion. A method for producing a flexible vegetable fiberboard according to the above.
【請求項5】水性エマルジョンが、HLB値6以上のポリ
オキシアルキレンモノアルキルエーテルおよび/または
ポリオキシアルキレンモノアルキルアリルエーテルおよ
び/またはポリオキシアルキレンモノ脂肪酸エーテル
の、燐酸エステルを含有する請求項(1)〜(4)のい
ずれかの項に記載の可撓性植物質繊維板の製造方法。
5. An aqueous emulsion containing a phosphoric ester of a polyoxyalkylene monoalkyl ether and / or a polyoxyalkylene monoalkyl allyl ether and / or a polyoxyalkylene monofatty acid ether having an HLB value of 6 or more. The method for producing a flexible vegetable fiberboard according to any one of the above (1) to (4).
【請求項6】植物質繊維が、木材を解繊もしくは粉砕も
しくは切断して得られる木質ファイバーおよび/または
単子葉植物の茎または種子殻を解繊もしくは粉砕もしく
は切断して得られるファイバーの1種または2種以上の
混合物を80重量%以上含むことを特徴とする請求項
(1)〜(5)のいずれかの項に記載の可撓性植物質繊
維板の製造方法。
6. The plant fiber is one of wood fiber obtained by fibrillating, pulverizing or cutting wood and / or fiber obtained by fibrillating, pulverizing or cutting monocotyledon stem or seed shell. Alternatively, the method for producing a flexible vegetable fiberboard according to any one of claims (1) to (5), comprising at least 80% by weight of a mixture of two or more kinds.
【請求項7】圧締に際し、加熱温度が70〜200℃であ
り、初期圧力を2〜8N/mm2とし、加熱中の板状物の中心
層温度が70〜100℃になった時点で圧力を0.2〜1.8N/mm2
に低下することを特徴とする請求項(1)〜(6)のい
ずれかの項に記載の可撓性植物質繊維板の製造方法。
7. A pressure-tightening heating temperature of 70 to 200 ° C., an initial pressure of 2 to 8 N / mm 2 , and a temperature at which the central layer temperature of the plate-like material being heated reaches 70 to 100 ° C. Pressure 0.2-1.8N / mm 2
The method for producing a flexible vegetable fiberboard according to any one of claims (1) to (6), characterized in that:
JP12927290A 1990-05-21 1990-05-21 Method for producing flexible vegetable fiberboard Expired - Lifetime JP2801740B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12927290A JP2801740B2 (en) 1990-05-21 1990-05-21 Method for producing flexible vegetable fiberboard

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12927290A JP2801740B2 (en) 1990-05-21 1990-05-21 Method for producing flexible vegetable fiberboard

Publications (2)

Publication Number Publication Date
JPH0425402A JPH0425402A (en) 1992-01-29
JP2801740B2 true JP2801740B2 (en) 1998-09-21

Family

ID=15005486

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12927290A Expired - Lifetime JP2801740B2 (en) 1990-05-21 1990-05-21 Method for producing flexible vegetable fiberboard

Country Status (1)

Country Link
JP (1) JP2801740B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002160206A (en) * 2000-11-24 2002-06-04 Yamaha Corp Wood fiberboard
JP3743285B2 (en) * 2000-12-15 2006-02-08 ヤマハ株式会社 Process for producing semi-cured wood panels and semi-cured wood panels

Also Published As

Publication number Publication date
JPH0425402A (en) 1992-01-29

Similar Documents

Publication Publication Date Title
JP4717215B2 (en) PMDI / resole resin mixed binder for the manufacture of wood composite products
CN109081902B (en) Artificial board adhesive without aldehyde addition and artificial board without aldehyde addition manufactured by using same
KR101713104B1 (en) Lignocellulosic products and methods of forming the same
US8895643B2 (en) Cold-pressed mats of lignocellulosic material having improved cold tack and a process for their production
AU763902B2 (en) Adhesive composition for lignocellulose-type hot-pressed forms, and hot-pressed form production process using the same
RU2279447C2 (en) Employment of polyisocyanates compositions as binders for composite lignocellulose materials
ES2296799T3 (en) POLYISOCIANATE COMPOSITIONS AS A BINDER FOR COMPOUND LIGNOCELLULOSIC MATERIALS.
JPH07197004A (en) Polyisocyanate extended with urea
JPS60260617A (en) Production of uretedione group-containing polyurethane prepolymer and lignocellulose composite material
CA2312365C (en) Adhesive systems and products formed using same and methods for producing said adhesive systems and products
JP2002532293A (en) Extended polymethylene poly (phenylisocyanate) resin binder for the manufacture of wood composite products
JPH11503476A (en) Method for bonding lignocellulosic material
KR20170042633A (en) Continuous process for forming a unitary mat
GB2096626A (en) Organic polyisocyanate-alkylene oxide adhesive composition for preparing lignocellulosic composite products
JP2801740B2 (en) Method for producing flexible vegetable fiberboard
JP5783888B2 (en) Adhesive composition for forming composite material with high water resistance, composite material, production method thereof, and adhesive for forming composite material with high water resistance
CN112549243B (en) Composition, formaldehyde-free artificial board prepared from composition and preparation method of formaldehyde-free artificial board
WO1995005275A1 (en) Organic isocyanates as binders for wood composites
EP0139530A2 (en) Preparation of lignocellulosic composite articles
JPH11124923A (en) Vibration damping sound insulating sheet and vibration damping sound insulating material
JP4596352B2 (en) Adhesive composition for lignocellulosic material, hot-press molded body using the same, and method for producing hot-press molded body
JPS63189563A (en) Production of core material of lightweight tatami bed
JPH0687106A (en) Manufacture of natural wood decorative laminated sheet
MXPA01006023A (en) Extended polymethylene poly(phenylisocyanate) resin binders for the production of wood composite products
MXPA01006020A (en) Process for production of wood composites using a mixed pmdi/solid novolac resin binder

Legal Events

Date Code Title Description
FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 10

Free format text: PAYMENT UNTIL: 20080710

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090710

Year of fee payment: 11

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100710

Year of fee payment: 12

EXPY Cancellation because of completion of term