JPH02269004A - Dry manufacture of molded board - Google Patents
Dry manufacture of molded boardInfo
- Publication number
- JPH02269004A JPH02269004A JP1089626A JP8962689A JPH02269004A JP H02269004 A JPH02269004 A JP H02269004A JP 1089626 A JP1089626 A JP 1089626A JP 8962689 A JP8962689 A JP 8962689A JP H02269004 A JPH02269004 A JP H02269004A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- molding
- molded
- fibers
- thermosetting resin
- 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.)
- Granted
Links
Landscapes
- Dry Formation Of Fiberboard And The Like (AREA)
- Reinforced Plastic Materials (AREA)
- Moulding By Coating Moulds (AREA)
Abstract
Description
【発明の詳細な説明】
く産業上の利用分野〉
この発F!Aは、乾式法による成me−ドの製造方法に
係り、特に強度の優れ丸底をコードの製造方法に関する
。[Detailed Description of the Invention] Industrial Application Fields> This invention is F! A relates to a method for producing cords using a dry method, and particularly relates to a method for producing cords with excellent strength and round bottoms.
く従来の技術〉
従来よシ、成型ボードは、粉末状のノがラック樹脂やレ
ゾール樹脂を繊維に添加混合させた後。Conventional technology> Conventionally, molded boards are made by adding and mixing powdered resin or resol resin to fibers.
堆積させ、熱ロールプレスや熱風を通気させ予備加熱逃
埋し、−時、マット化品として、その後。The material is deposited, pre-heated and buried by hot roll pressing or hot air aeration, and then matted as a product.
熱圧成型を行い製造されている。Manufactured using hot pressure molding.
上記粉末状樹脂は火災発生の危険性が小さいことが特徴
であるが、繊維への付着が不完全であシ粉塵を発生した
シ、ノMラック樹脂の場合はへキサミンの分解によシ悪
臭が発生する等0作業環境が悪化するという欠点があっ
た。The powdered resin mentioned above is characterized by a low risk of fire outbreak, but it does not adhere to the fibers incompletely and generates dust, and in the case of M-lac resin, it produces a bad odor due to the decomposition of hexamine. There was a drawback that the work environment deteriorated, such as the occurrence of.
上記欠点を解決する為、水溶性レゾール樹脂が用いられ
ている。In order to solve the above drawbacks, water-soluble resol resins are used.
〈発明が解決しようとする課題〉
しかし、水溶性レゾール樹脂は、低分子量(MFI=S
OO未満)では繊維への樹脂の浸透が大きくなるし、高
分子量(Mn±50t)以上)ではゲル化時間が短く繊
維へ均一に分散しなかったシ、製造時における熱風を通
気させる予備加熱処理時(B−ステージ化時)の硬化進
行が着しく、密度ムラが生じる等いずれにしても良好な
強度の成型& −ドが得られないという欠点を有してい
た。<Problems to be solved by the invention> However, water-soluble resol resins have a low molecular weight (MFI=S
If the resin has a high molecular weight (Mn±50t) or more, the gelation time is short and the fibers are not uniformly dispersed. In either case, the curing process progresses slowly (at the time of B-stage formation), density unevenness occurs, etc., and molding and deformation with good strength cannot be obtained.
く課題を解決するための手段〉
本発明者等は、上記実情に鑑みて鋭意検討を行なった結
果熱硬化性樹脂の水性分散液を用いて製造した成型が−
ドが、従来の粉末状あるいは水溶性のフェノール樹脂を
用いて製造した成型が一ドに比べて高強度になることを
見い出し1本発明を液を付着せしめ乾燥させた後、成型
を行うことを特徴とする成型ボードの乾式製造方法を提
供するものである。Means for Solving the Problems> In view of the above circumstances, the present inventors conducted intensive studies and found that moldings produced using an aqueous dispersion of a thermosetting resin -
It was discovered that molding produced using conventional powdered or water-soluble phenolic resin has higher strength than that of 1-do. The present invention provides a method for dry manufacturing a molded board.
本発明における成型ゲートの製造方法は、公知慣用の製
造方法がいずれも採用でき1%に限定されるものではな
い。The method for manufacturing the molded gate in the present invention may be any known and commonly used manufacturing method, and is not limited to 1%.
例えば(1)結合剤として熱硬化性樹脂の水性分散液t
−織繊維付着せしめ、(2)次いで該樹脂の水性分散液
の付着した繊維(以下、含樹脂繊維という。)を乾燥器
等で一定の含水率となる様均−に乾燥せしめる。(3)
こうして得られた材料を堆積させ、呵より材料の予備加
熱処理(B−ステージ化)を行いマツ) 化品を得、(
4)このマット化品を適宜ガス抜きを行いながら黒土成
型を行えばよい。For example, (1) an aqueous dispersion of a thermosetting resin as a binder
(2) Next, the fibers to which the aqueous dispersion of the resin has been adhered (hereinafter referred to as resin-containing fibers) are evenly dried in a drier or the like to a constant moisture content. (3)
The material obtained in this way is deposited, and the material is preheated (B-staged) to obtain a pine (pine) product.
4) This matted product may be subjected to black clay molding while appropriately degassing.
本発明に係る有機繊維とは、有機化合物からなる繊維で
あシ1例えば木質繊維、綿、麻、絹およびウール等の天
然繊維、ナイロン、ポリエステル。The organic fibers according to the present invention are fibers made of organic compounds, such as wood fibers, natural fibers such as cotton, hemp, silk, and wool, nylon, and polyester.
ポリウレタン、レーヨン、トリアセテート等の合成繊維
等が挙げられる。中でもセルロース、リグニン等の木質
繊維が好ましい、これらの有機繊維は単独使用でも二種
以上の併用でもかまわない。Examples include synthetic fibers such as polyurethane, rayon, and triacetate. Among these, wood fibers such as cellulose and lignin are preferred, and these organic fibers may be used alone or in combination of two or more types.
本発明の熱硬化性樹脂の水性分散液とは、公知慣用の熱
硬化性樹脂の水性分散液であシ1例えば該樹脂を合成時
又は合成後に保護コロイドや界面活性剤等の分散剤を用
いて水性媒体に分散せしめた水性分散液が挙げられる。The aqueous dispersion of a thermosetting resin of the present invention is a known and commonly used aqueous dispersion of a thermosetting resin. Examples include aqueous dispersions prepared by dispersing in an aqueous medium.
熱硬化性樹脂の水性分散液は、該樹脂成分が0、1〜2
0μmの微粒子形状tWすることから、木質繊維へ噴霧
混合した場合、材料への浸透が抑制され、優れた接着性
能を有している。%に水性媒体中に該樹脂を分散させる
ためにセルロース系の保護コロイドを用いると、その粘
着性で含水状態においても該樹脂と繊維物質との付着は
完全なものとなるし、含水状態が低下するに伴い粘着性
が減少し繊維物質との均一分散性が特に優れたものとな
るので好ましい。The aqueous dispersion of thermosetting resin has a resin component of 0, 1 to 2
Since it has a fine particle shape TW of 0 μm, when it is sprayed and mixed into wood fibers, penetration into the material is suppressed and it has excellent adhesive performance. When a cellulose-based protective colloid is used to disperse the resin in an aqueous medium, its adhesive property ensures complete adhesion between the resin and the fibrous material even in a hydrated state, and the hydrated state decreases. This is preferred because the tackiness decreases and the uniform dispersibility with the fiber material becomes particularly excellent.
熱硬化性樹脂としては例えば、エリア樹脂、メラミン樹
脂、フェノール樹脂及びこれらの共縮合樹脂や変性樹脂
等が例示される。中でもレゾール型フェノール樹脂が好
ましく、熱圧成型時の該樹脂の流動性がよく;得られる
成型が−ドが高強度でかつフクレ現象が起きにくくなる
点で、150℃におけるゲル化時間が30〜180秒の
レゾール型フェノール樹脂が特に好ましい。Examples of thermosetting resins include area resins, melamine resins, phenol resins, and co-condensed resins and modified resins thereof. Among these, resol-type phenolic resins are preferred, as they have good fluidity during hot-pressure molding; gelation time at 150°C is 30 to 30°C, since the resulting moldings have high strength and are less prone to blistering. Particularly preferred is a 180 second resol type phenolic resin.
該樹脂の水性分散液の有機繊維への付着量は。What is the amount of the aqueous dispersion of the resin attached to the organic fibers?
用いる有機繊維の種類や成型ゲートの目標強度によシ決
定され1%に制限はないが繊維(乾燥重量換算)重量に
対して5〜201量%(41!f脂固形分)であると成
型が−ド製造時における乾燥時間が短かくかつ得られる
ゲートが高強度となるので好ましい。該樹脂の水性分散
液を繊維に付着せしめる方法は解繊された繊維に直接注
ぎ込んで混合する方法、混合攪拌されている繊維にスグ
レー散布しながら混合する方法等が例示されるがこれら
の方法に限定されず、いかなる方法でもよい。It is determined by the type of organic fiber used and the target strength of the molding gate, and there is no limit to 1%, but molding should be 5 to 201% by weight (41!f fat solid content) based on the weight of the fiber (dry weight equivalent). This is preferable because the drying time during the production of the gate is short and the resulting gate has high strength. Examples of methods for adhering the aqueous dispersion of the resin to the fibers include pouring it directly onto the defibrated fibers and mixing them, and mixing the aqueous dispersion of the resin while sprinkling it on the fibers that are being mixed and stirred. Any method may be used without limitation.
含樹脂scmの流動性や熱圧成型時の成型ビードの離型
性を改良するためには該樹脂の水性分散液にワックス類
を併用してもよい。ワックス類は、特に限定されるもの
ではなく、公知慣用のものがいずれも使用できる0例え
ばa?シラフィンワックス。In order to improve the fluidity of the resin-containing SCM and the releasability of molded beads during hot-pressure molding, waxes may be used in combination with the aqueous dispersion of the resin. The waxes are not particularly limited, and any known and commonly used waxes can be used.For example, a? silaffin wax.
シリコン系ワックス、脂肪酸アマイド類及びその銹導体
があげられ、形態としては、乳化水溶液が好ましい。中
でも、/量うフインの乳化水溶液が特に好ましい、ワッ
クス類の添加量は1通常樹脂(固形分)に対して0.1
−10111%でアシ、含樹脂繊維の流動性を改良し、
かつ得られる成型ボードの離型性に優れる点で好ましく
は1−8!量%である。Examples include silicone wax, fatty acid amides, and their rust conductors, and the preferred form is an emulsified aqueous solution. Among these, an emulsified aqueous solution of weighing fins is particularly preferred, and the amount of wax added is usually 0.1 to 1 resin (solid content).
-10111% improves the fluidity of reeds and resin-containing fibers,
The rating is preferably 1-8 in that the obtained molded board has excellent mold releasability! The amount is %.
耐水性や耐久強度を改良するためには該樹脂の水性分散
液にシランカップリング剤を混合して用いてもよい。シ
ランカップリング剤は特に限定されるものではなく、ビ
ニル系、アミン系、エポキシ系。In order to improve water resistance and durable strength, a silane coupling agent may be mixed with the aqueous dispersion of the resin. Silane coupling agents are not particularly limited, and include vinyl, amine, and epoxy.
クロル糸、メタクリロキシ糸、メルカプト基が例示され
る。中でもアミン系シランカップリング剤が特に好まし
い。シラ/カップリング剤の添加量は、樹脂(固形分)
に対して0.1−5Xji%であシ、得られる成型?−
ドの耐水性や耐久強度の改良効果に優れる点で好ましく
は0.2−3重量%である。Examples include chloro thread, methacryloxy thread, and mercapto group. Among these, amine-based silane coupling agents are particularly preferred. The amount of silica/coupling agent added is based on the resin (solid content).
What molding can be obtained with 0.1-5Xji%? −
The content is preferably 0.2 to 3% by weight since it is excellent in improving the water resistance and durable strength of the resin.
又、熱硬化性樹脂の水性分散液には必要に応じて従来の
粉末状フェノール樹脂を併用してもよい。Furthermore, a conventional powdered phenol resin may be used in combination with the aqueous dispersion of the thermosetting resin, if necessary.
更に、熱硬化性樹脂の水性分散液には上記ワックス類、
シランカップリング剤、粉末状フェノール樹脂の他に1
着色剤、m燃剤、酸化防止剤、防虫剤、防腐剤、撥水撥
油剤、防汚剤、芳香剤等各種の添加剤を必要に応じて併
用してもよい。Furthermore, the aqueous dispersion of thermosetting resin contains the above-mentioned waxes,
In addition to silane coupling agent and powdered phenolic resin, 1
Various additives such as colorants, retardants, antioxidants, insect repellents, preservatives, water and oil repellents, antifouling agents, and fragrances may be used in combination as necessary.
上記ワックス類、シランカップリング剤等各種の添加剤
を用いる場合は、それをあらかじめ該樹脂の水性分散液
に混合した後、l&雑に付着せしめてもよいし、該樹脂
水性分散液と添加剤を各別に同時繊維に付着せしめても
よいし、該樹脂水性分散液を繊維に付着させた後、添加
剤を付着せしめる等任意の方法が採用できる。When using various additives such as the above-mentioned waxes and silane coupling agents, they may be mixed in advance with the aqueous dispersion of the resin and then allowed to adhere to the aqueous resin dispersion and the additives. may be simultaneously attached to the fibers separately, or any method can be adopted, such as attaching the aqueous resin dispersion to the fibers and then attaching the additive.
上記(2)における含樹脂絨維の乾燥は1通常の乾燥器
でも、乾燥用混合機を用いてもよ−。乾燥は含樹脂繊維
の含水率が8〜20%となる様な条件で行うことが好ま
しい。The resin-containing fibers in (2) above may be dried using either an ordinary dryer or a drying mixer. Drying is preferably carried out under conditions such that the moisture content of the resin-containing fibers is 8 to 20%.
上記(3)において材料の堆積には通常の装置がいずれ
も使用できる。この様な装置としては、フリース成形機
、エアフィルター成形機が例示される。In (3) above, any conventional equipment can be used for depositing the material. Examples of such devices include fleece molding machines and air filter molding machines.
予備加熱処理は熱が材料に与えられる方法であれば何ら
限定されるものではなく、赤外線を照射する方法、熱風
を吹きあてる方法等が例示される。The preheating treatment is not limited in any way as long as heat is applied to the material, and examples thereof include a method of irradiating infrared rays and a method of blowing hot air.
中でも130〜150℃の熱風を吹きあてる方法が簡便
であり好ましい。この行程でマット化品が製造されるが
、このマット化品は通常厚さ15〜30鵡見掛比X 0
.05〜0.21!/am テある。Among these, the method of blowing hot air at 130 to 150°C is simple and preferred. A matte product is produced in this process, and this matte product usually has a thickness of 15 to 30 mm and an apparent ratio of 0.
.. 05~0.21! /am I have a question.
本発明の製造方法では、マット化品を一端製造した後熱
圧成型を行なって成型ボードを製造(即ち上記(3)の
行程を経る方法)してもよいし、材料を直接熱圧成型し
て成型が一ドを製造してもよい。In the manufacturing method of the present invention, a molded board may be manufactured by first manufacturing a matted product and then performing hot-pressing molding (that is, a method that goes through the process (3) above), or the material can be directly hot-pressing molded. The molding may be used to manufacture a single head.
熱圧成型時の条件は特に限定されるものではないが1通
常180〜230℃、圧力30〜40略伝。Conditions during hot-press molding are not particularly limited, but are usually 180 to 230°C and a pressure of 30 to 40°C.
加圧時間30〜90秒である。熱圧成型時には適宜ガス
抜きを行なうのは勿論のことである。こうして最終的に
得られる成型ボードは通常2〜3+罵。The pressurization time is 30 to 90 seconds. It goes without saying that degassing should be carried out as appropriate during hot-pressure molding. The final molded board thus obtained is usually 2-3 + cursive.
比重0.70〜1.0&/cm である。The specific gravity is 0.70 to 1.0 cm.
本発明の製造方法で得られる底型M−ドは例えば自動車
の内装材、住宅の内装材、ドアパネル材。The bottom mold M-do obtained by the manufacturing method of the present invention can be used, for example, as an interior material for automobiles, an interior material for houses, and a door panel material.
家具パネル材や天井材等の各1の用途に使用することが
できる。It can be used for furniture panel materials, ceiling materials, etc.
次に本発明の実施例を示す。以下、断わシのない限ル、
「部」は「Jll郡部を「%」は「l麓%」を意味する
ものとする。Next, examples of the present invention will be shown. The following, unless otherwise specified,
``Part'' means ``Jll Gunbu'' and ``%'' means ``1 foot%.''
実施例1
ろらかじめ水希釈して、固形分30%に調整したブライ
オーフェン pE−zol(大日本インキ化学工業(株
)製レゾール型フェノール樹脂の水分散液固形分47%
、平均粒子径2μm、15部℃のゲル化時間90秒)2
7部をスプレー機器を用いて木質繊維(ドライ換算)1
00部に噴霧散布し付着させ良。その後、これを乾燥用
混合機に入れ。Example 1 Breiofen pE-zol (aqueous dispersion of resol type phenolic resin manufactured by Dainippon Ink and Chemicals Co., Ltd., solid content 47%) was diluted with water in advance and adjusted to a solid content of 30%.
, average particle size 2 μm, 15 parts C gelation time 90 seconds)2
7 parts wood fiber (dry equivalent) using spray equipment 1
Spray it on 00 parts and let it adhere. Then put this into a drying mixer.
含水率が12%となる様に調整した。次に、フリース成
形機、エアフィルター成形機を通しこの材料を堆積させ
た後、上部よシ130℃の熱に1に通気させ予備加熱処
理し、厚さ約3on、見掛は比重約o、 1s tz/
an のマット化品金得た。その後。The moisture content was adjusted to 12%. Next, this material is deposited through a fleece molding machine and an air filter molding machine, and then preheated by passing heat at 130°C from the top to 1. The thickness is about 3 on, and the apparent specific gravity is about o. 1s tz/
I got a matte product from an. after that.
温度210℃、圧力30 kg/an 、時間60秒、
ガス抜き1に:15秒後に1回行い熱圧成型し、厚さ2
.5趨、比重0.8017cm の成型ボードを得た。Temperature: 210°C, pressure: 30 kg/an, time: 60 seconds,
Degassing 1: Perform once after 15 seconds and heat-press mold to a thickness of 2.
.. A molded board with 5 lines and a specific gravity of 0.8017 cm was obtained.
作業環境、木質繊維と該樹脂との混合分散性のいずれも
極めて良好であった。成型が一ドの離型性は良好でめっ
た。Both the working environment and the mixing and dispersibility of the wood fibers and the resin were extremely good. Once molded, the mold releasability was good and rare.
実施例2
あらかじめ水希釈して、固形分30%に11&し九グラ
イオーフェン PE−20127flfiKパラフイン
の乳化水溶液(固形分30%)2部を混合し。Example 2 Two parts of an emulsified aqueous solution (solid content: 30%) of 11 & Shiku Glyophen PE-20127flfiK paraffin was diluted with water in advance and mixed with a solid content of 30%.
これをスプレー機器を用いて木質繊維(ドライ換算)1
00部に噴霧散布し付着させた。その後。Spray this using a spray device to make wood fibers (dry equivalent) 1
00 parts by spraying and adhesion. after that.
これを乾燥用混合機に入れ、含水率が12%となる様に
調整した6次に、フリース成形機、エアフィルター成形
機を通しこの材料を堆積させた後、上部よ、9130℃
の熱風を通気させ予備加熱処理し、厚さ約30隨、見掛
は比重的0.151部cm’のマット化品を得た。その
後、温度210℃、圧力30 kg/an 、時間60
秒、ガス抜きを15秒後に1回行い熱圧成型し、厚さ2
.5 m 、比重0680g/αの成型ボードを:4次
。This was placed in a drying mixer and the moisture content was adjusted to 12%.6 Next, this material was deposited through a fleece molding machine and an air filter molding machine, and the upper part was heated to 9130℃.
A matte product having a thickness of about 30 cm and an apparent specific gravity of 0.151 part cm' was obtained by preheating the product by blowing hot air through it. After that, the temperature was 210°C, the pressure was 30 kg/an, and the time was 60.
After degassing once for 15 seconds, hot-press molding is performed to a thickness of 2.
.. 5 m, molded board with specific gravity 0680 g/α: 4th order.
作業環境、木質繊維と該樹脂との混合分散性はいずれも
極めて良好であった。成型ボードの離型性も極めて良好
であった。Both the working environment and the mixing and dispersibility of the wood fibers and the resin were extremely good. The releasability of the molded board was also extremely good.
実施例3
あらかじめ水希釈して、固形分30%にvI4!!11
゜たブライオーフェン PE−20127部にアミノ系
シランカップリング剤0.04部を混合し、これをスプ
レー機器で木質繊維(ドライ換算)100部に噴霧散布
し付着させた。その後、これを乾燥用混合機に入れ、含
水率が12%となる様に調整した。次に、フリース成形
機、エアフィルター成形機を通しこの材料を堆積させた
後、上部よシ130℃の熱風を通気させ予備加熱処理し
、浮さ約30 ta 、見掛は比1約0.1517ar
t3のマット化品を得九。その後1m度2り0℃、圧力
30kfl/att2゜時間60秒、ガス抜き215秒
後に1回行い熱圧成形型、厚さ2.5 m 、比重0.
801部cm の成型が−ドを得た。Example 3 Dilute with water in advance to make vI4! 30% solids! ! 11
0.04 part of an amino-based silane coupling agent was mixed with 127 parts of Bryophen PE-20 which had been deformed, and the mixture was sprayed onto 100 parts of wood fibers (dry equivalent) using a spray device to make them adhere. Thereafter, this was placed in a drying mixer and the moisture content was adjusted to 12%. Next, this material is deposited through a fleece molding machine and an air filter molding machine, and then preheated by blowing hot air at 130°C through the top, giving a float of about 30 ta and an apparent ratio of about 1 to 0. 1517ar
I got a matte version of t3. After that, the pressure was 30kfl/att2° at 0°C, the pressure was 30kfl/att2°, the time was 60 seconds, and the gas was removed once after 215 seconds.
A molding of 801 parts cm was obtained.
作業環境、木質繊維と該樹脂の混合分散性はいずれも極
めて良好であった。成型が−ドの離型性は良好でめった
。Both the working environment and the mixing and dispersibility of the wood fibers and the resin were extremely good. The releasability of molding was good and satisfactory.
実施例4
あらかじめ水希釈して、固形分30%に調整したグライ
オーフェ7 PE−20127部に/ヂラフィンの乳化
水溶液(固形分30%)2部、アミン系シランカッグリ
ング剤0.04部を混合し、これをスプレー機器で木質
繊維(ドライ換算)100部に噴霧散布し付着させた。Example 4 2 parts of an emulsified aqueous solution of Dirafin (solid content 30%) and 0.04 parts of an amine-based silane cagging agent were mixed with 127 parts of Gleiophe 7 PE-20, which had been diluted with water in advance and adjusted to a solid content of 30%. This was sprayed onto 100 parts of wood fiber (dry equivalent) using a spray device to make it adhere.
その後、これを乾燥用混合機に入れ、含水率が12%と
なる様に調整した。次に、フリース成形機、エアフィル
ター成形機を通しこの材料を堆積させた後、上部より1
30℃の熱風を通気させ予備加熱処理し、厚さ約30n
、見掛は比重的o、 151部m のマット化品を得た
。その後、温度210℃、圧力30kJan2゜時間6
0秒、ガス抜きを15秒後に1回行い熱圧成型し、厚さ
2.5 m 、比重0.80 !!/cm (D成型ボ
ードを得た。Thereafter, this was placed in a drying mixer and the moisture content was adjusted to 12%. Next, after depositing this material through a fleece molding machine and an air filter molding machine,
Preheated by blowing hot air at 30°C to a thickness of approximately 30n.
A matted product with an apparent specific gravity of 151 parts m was obtained. After that, temperature 210℃, pressure 30kJan 2゜hours 6
After 0 seconds and degassing once after 15 seconds, it was hot-press molded to a thickness of 2.5 m and a specific gravity of 0.80! ! /cm (D molded board was obtained.
作業環境、木質繊維と該樹脂の混合分散性はいずれも極
めて良好でめった。成型ボードの離型性も極めて良好で
めった。Both the working environment and the mixing and dispersibility of the wood fiber and the resin were extremely good. The releasability of the molded board was also extremely good.
実施例5
レゾール樹脂の水分散&(固形分47%、平均粒子径2
μm、150℃のゲル化時間50秒)を水希釈して固形
分30%にv4表した後、この27部をスプレー機器を
用いて木質繊維(ドライ換算)100部に噴鯵散布し付
着させた。その後、これを乾燥用混合機に入れ、含水率
が12%となる様に調整した0次に、71)−ス成形機
、エアフィルター成形機を通しこの材料を堆積させ死後
、上部よシ130℃の熱風を通気させ予備加熱処理し。Example 5 Water dispersion of resol resin & (solid content 47%, average particle size 2
μm, gelling time at 150°C for 50 seconds) was diluted with water to give a solid content of 30% v4, and then 27 parts of this was sprayed onto 100 parts of wood fibers (dry equivalent) using a spray device and allowed to adhere. Ta. After that, this material was placed in a drying mixer, and the moisture content was adjusted to 12%.Then, this material was deposited through a 71)-space molding machine and an air filter molding machine, and after death, the upper part was Pre-heated by blowing hot air at ℃.
厚さ約30龍、見掛は比重的0.151/artsのマ
ット化品を得た。その後、温度210℃、圧力3゜kt
r/an2.時間60秒、ガス抜きを15秒後に1回行
い熱圧成型し、厚さ2.5 m、 、比重0.809/
art’の成型ボードを得た。A matted product with a thickness of about 30 mm and an apparent specific gravity of 0.151/arts was obtained. After that, the temperature was 210℃ and the pressure was 3゜kt.
r/an2. Time: 60 seconds, degassing once after 15 seconds, hot-press molding, thickness: 2.5 m, specific gravity: 0.809/
A molded board of art' was obtained.
作業環境、木質繊維と該樹脂の混合分散性はいずれも極
めて良好であった。成型が一ドの離型性は良好であり之
。Both the working environment and the mixing and dispersibility of the wood fibers and the resin were extremely good. The mold releasability after molding is good.
実施例6
レゾール411M¥1の水分散液(固形分47%、平均
粒子径2.5μm、150℃のゲル化時間170秒)を
水希釈して固形分30%にm製した後、この27部を、
スプレー機器を用いて木質繊維(ドライ換算)100部
に噴霧散布し付着させた。その後、これを乾燥用混合機
に入れ、含水率が12%となる様に調整した。次に、フ
リース成形機、エアフィルター成形機を通しこの材料を
堆積させた後、上部よfi130℃の熱風を通気させ予
備加熱処理しlIさ約30鴎、見掛は比重的0.151
/A−IL’のマット化品を得た。その後、温度210
℃、圧力30 kg/x 、時間60秒、ガス抜きを1
5秒後に1回行い熱圧成型し、厚さ2.5 mm 、比
重0.8011/cm の成型ゲートを得た。Example 6 An aqueous dispersion of Resol 411M ¥1 (solid content 47%, average particle diameter 2.5 μm, gelling time at 150°C 170 seconds) was diluted with water to a solid content of 30%, and then this 27 Department,
Using a spray device, 100 parts of wood fibers (dry equivalent) were sprayed and adhered. Thereafter, this was placed in a drying mixer and the moisture content was adjusted to 12%. Next, this material is deposited through a fleece molding machine and an air filter molding machine, and then preheated by blowing hot air at a temperature of 130°C through the upper part.
A matted product of /A-IL' was obtained. Then temperature 210
°C, pressure 30 kg/x, time 60 seconds, degassing 1
After 5 seconds, hot pressure molding was carried out once to obtain a molded gate having a thickness of 2.5 mm and a specific gravity of 0.8011/cm.
作業環境、木質繊維と該樹脂の混合分散性はいずれも極
めて良好であった。成型ゲートの離型性も良好であった
。Both the working environment and the mixing and dispersibility of the wood fibers and the resin were extremely good. The releasability of the molded gate was also good.
比較例1 市販の水溶性レゾール樹脂(固形分50%。Comparative example 1 Commercially available water-soluble resol resin (solid content 50%).
150℃のゲル化時間90秒)を水で希釈して固形分3
0%に調整した後、これをスグレー機器で木質繊維(ド
ライ換算)100部に噴鐸散布し付着させ九個は、実施
例1と同様にしてNさ約301m、見掛は比l約0.1
511/cmのマット化を得た。150℃ gelation time 90 seconds) was diluted with water to reduce the solid content to 3.
After adjusting to 0%, this was sprayed onto 100 parts of wood fibers (dry equivalent) using a Sugrei machine and adhered to nine pieces. .1
A mattification of 511/cm was obtained.
その後、温度210℃、圧力30 kg/an2.時間
60秒、ガス抜@を15秒後に1回行い熱圧成型し、厚
さ2.5 mm 、比重0.801/an の成型ゲー
トを得た。After that, the temperature was 210°C and the pressure was 30 kg/an2. Heat and pressure molding was performed for 60 seconds and degassing once after 15 seconds to obtain a molded gate with a thickness of 2.5 mm and a specific gravity of 0.801/an.
作業環境は極めて良好であった。木質繊維と該樹脂の混
合分散性は極めて悪かったが、成型が−ト0の離型性は
良好であった。The working environment was extremely good. Although the mixing and dispersibility of the wood fiber and the resin was extremely poor, the mold release property was good when the molding was 0.
比較例2
市販の粉末状ノゲラック樹脂(150℃のゲル化時間9
0秒、へΦサミン10%含有。)8部を木質繊#1(ド
ライ換算)100部に散布混合し付着させた。その後、
フリース成形機、エアフィルター成形機を通し材料を堆
積させた他は、実施例1と同様にして厚さ約30fl、
見掛は比重的0.151部cmのマット化品を得た。そ
の後、温度210℃、圧力30 kl/an2.時間6
0秒、ガス抜きを15秒後に1回行い熱圧成型し、厚さ
2.51比重。Comparative Example 2 Commercially available powdered Nogelac resin (gelling time at 150°C 9
0 seconds, containing 10% hesamine. ) was sprayed and mixed onto 100 parts of wood fiber #1 (dry equivalent) to make it adhere. after that,
The process was the same as in Example 1, except that the material was deposited through a fleece molding machine and an air filter molding machine, with a thickness of about 30 fl,
A matted product with an apparent specific gravity of 0.151 parts cm was obtained. After that, the temperature was 210°C and the pressure was 30 kl/an2. time 6
After 0 seconds and degassing once after 15 seconds, it was hot-press molded to a thickness of 2.51 specific gravity.
0、801/an3の木質系成型ボードを得た。A wood-based molded board of 0.801/an3 was obtained.
粉塵が舞い作業環境は也めて悪かっ九。木質繊維に該樹
脂が均一に付着せず混合分散性が極めて悪かった。又、
粉落ち現象も見られた。成型s?−ドの離型性はやや悪
かった。The working environment was very bad due to the dust. The resin did not adhere uniformly to the wood fibers, resulting in extremely poor mixing and dispersibility. or,
Powder falling phenomenon was also observed. Molding s? - The mold releasability of the mold was somewhat poor.
比較例3
市販の粉末状レゾール樹脂(150℃のゲル化時間90
秒)8部を木質繊維(ドライ換算)100部に散布し混
合し、付着させる。その後、フリース成形機、エアフィ
ルター成形機を通しこの材料を堆積させ九個は、実施例
1と同様にして厚さ約30難、見掛は比重的0.151
17/crIL’のマット化を得た。その後、温度21
0℃、圧力30 ky/an2゜時間60秒、ガス抜き
を15秒後に1回行い熱圧成型し、厚さ2.5 m 、
比g O,80Ji’/cm の木質系成型が−ドを得
た。Comparative Example 3 Commercially available powdered resol resin (gelling time at 150°C 90
Sprinkle 8 parts (second) on 100 parts of wood fiber (dry equivalent), mix, and adhere. Thereafter, this material was deposited through a fleece molding machine and an air filter molding machine, and nine pieces were deposited in the same manner as in Example 1, with a thickness of approximately 30 mm and an apparent specific gravity of 0.151.
A mattification of 17/crIL' was obtained. Then temperature 21
0°C, pressure 30 ky/an2° time 60 seconds, degassing once after 15 seconds, hot pressure molding, thickness 2.5 m,
A wood molding with a ratio g O of 80 Ji'/cm was obtained.
粉塵が舞い作業環境は極めて悪かった。木質繊維に該樹
脂が均一に付着せず混合分散性が極めて悪かった。又、
粉落ち現象も見られた。成型ボードの離型性もやや悪か
った。The working environment was extremely poor with dust flying around. The resin did not adhere uniformly to the wood fibers, resulting in extremely poor mixing and dispersibility. or,
Powder falling phenomenon was also observed. The releasability of the molded board was also somewhat poor.
以下に実施例及び比較例で得た成型ゲートにつき外観、
常態曲げ強度を測定しその結果を第1表に示した。The appearance of the molded gates obtained in Examples and Comparative Examples is shown below.
The normal bending strength was measured and the results are shown in Table 1.
/
第
表
注 $1)常態曲は強度はJIS−A5907に準じた
。/ Notes to the table $1) The strength of normal songs conforms to JIS-A5907.
〈発明の効果〉
本発明の成型ボート9の乾式製造方法は、熱硬化性樹脂
の水性分散液を用いるので従来の粉末状ないしは水溶性
フェノール樹脂を用いた成型ゲートに比べて格別顕著に
強度を高めることができ、シランカップリング剤を併用
するとさらに強度を向上でき、ワックス類を併用すると
成型メートの成型時の離型性を向上することができる。<Effects of the Invention> Since the dry manufacturing method of the molded boat 9 of the present invention uses an aqueous dispersion of thermosetting resin, the strength is significantly increased compared to conventional molded gates using powdered or water-soluble phenolic resin. The strength can be further improved by using a silane coupling agent in combination, and the mold releasability during molding of the molding mate can be improved by using a wax in combination.
本発明方法で製造された成型ボードは高強度であるので
、自動車の内装材、住宅の内装材、ドアパネル材、家具
・母ネル材や天井材等の6株の用途に使用することがで
きる。Since the molded board produced by the method of the present invention has high strength, it can be used for six purposes, including automobile interior materials, residential interior materials, door panel materials, furniture/base panel materials, and ceiling materials.
Claims (1)
乾燥させた後、成型を行うことを特徴とする成型ボード
の乾式製造方法。 2、繊維が木質繊維である請求項1記載の製造方法。 3、熱硬化性樹脂が、レゾール型フェノール樹脂である
請求項2記載の製造方法。 4、熱硬化性樹脂は150℃におけるゲル化時間が30
〜180秒のレゾール型フェノール樹脂である請求項2
記載の製造方法。 5、ワックス類を熱硬化性樹脂と併用することを特徴と
する請求項2記載の製造方法。 6、シランカップリング剤を熱硬化性樹脂と併用するこ
とを特徴とする請求項2記載の方法。[Scope of Claims] 1. A dry manufacturing method for a molded board, characterized in that an aqueous dispersion of a thermosetting resin is applied to organic fibers, dried, and then molded. 2. The manufacturing method according to claim 1, wherein the fibers are wood fibers. 3. The manufacturing method according to claim 2, wherein the thermosetting resin is a resol type phenolic resin. 4. Thermosetting resin has a gelation time of 30 at 150°C.
Claim 2, which is a resol-type phenolic resin that lasts for ~180 seconds.
Manufacturing method described. 5. The manufacturing method according to claim 2, characterized in that a wax is used in combination with a thermosetting resin. 6. The method according to claim 2, characterized in that a silane coupling agent is used in combination with a thermosetting resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1089626A JP2718167B2 (en) | 1989-04-11 | 1989-04-11 | Dry manufacturing method of fiberboard |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1089626A JP2718167B2 (en) | 1989-04-11 | 1989-04-11 | Dry manufacturing method of fiberboard |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02269004A true JPH02269004A (en) | 1990-11-02 |
| JP2718167B2 JP2718167B2 (en) | 1998-02-25 |
Family
ID=13975965
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1089626A Expired - Fee Related JP2718167B2 (en) | 1989-04-11 | 1989-04-11 | Dry manufacturing method of fiberboard |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2718167B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008001915A (en) * | 2007-09-13 | 2008-01-10 | Sumitomo Bakelite Co Ltd | Method of manufacturing prepreg and laminate, and apparatus for manufacturing prepreg |
| US8012389B2 (en) | 2005-12-22 | 2011-09-06 | New Zealand Forest Research Institute Limited | Method for producing wood fibre composite products |
| US9511508B2 (en) | 2004-06-23 | 2016-12-06 | New Zealand Forest Research Institute Limited | Method for producing wood fibre pellets |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS50123785A (en) * | 1973-10-08 | 1975-09-29 | ||
| JPS5515897A (en) * | 1978-07-20 | 1980-02-04 | Reichhold Chemicals Canada Ltd | Wood chip board and its preparation |
-
1989
- 1989-04-11 JP JP1089626A patent/JP2718167B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS50123785A (en) * | 1973-10-08 | 1975-09-29 | ||
| JPS5515897A (en) * | 1978-07-20 | 1980-02-04 | Reichhold Chemicals Canada Ltd | Wood chip board and its preparation |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9511508B2 (en) | 2004-06-23 | 2016-12-06 | New Zealand Forest Research Institute Limited | Method for producing wood fibre pellets |
| US10150227B2 (en) | 2004-06-23 | 2018-12-11 | New Zealand Forest Research Institute Limited | Method for producing wood fibre pellets |
| US8012389B2 (en) | 2005-12-22 | 2011-09-06 | New Zealand Forest Research Institute Limited | Method for producing wood fibre composite products |
| JP2008001915A (en) * | 2007-09-13 | 2008-01-10 | Sumitomo Bakelite Co Ltd | Method of manufacturing prepreg and laminate, and apparatus for manufacturing prepreg |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2718167B2 (en) | 1998-02-25 |
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