JPS6320857B2 - - Google Patents

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Publication number
JPS6320857B2
JPS6320857B2 JP21433184A JP21433184A JPS6320857B2 JP S6320857 B2 JPS6320857 B2 JP S6320857B2 JP 21433184 A JP21433184 A JP 21433184A JP 21433184 A JP21433184 A JP 21433184A JP S6320857 B2 JPS6320857 B2 JP S6320857B2
Authority
JP
Japan
Prior art keywords
molding material
weight
phenolic resin
parts
cellulose
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
Application number
JP21433184A
Other languages
Japanese (ja)
Other versions
JPS6195039A (en
Inventor
Sadamu Takahashi
Masayuki Amano
Naoya Kominami
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.)
Asahi Yukizai Corp
Original Assignee
Asahi Organic Chemicals Industry Co 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 Asahi Organic Chemicals Industry Co Ltd filed Critical Asahi Organic Chemicals Industry Co Ltd
Priority to JP21433184A priority Critical patent/JPS6195039A/en
Publication of JPS6195039A publication Critical patent/JPS6195039A/en
Publication of JPS6320857B2 publication Critical patent/JPS6320857B2/ja
Granted legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

産業上の利用分野 本発明は低発泡体用フエノール樹脂成形材料、
さらに詳しくいえば、食器類、記念品、装飾品、
玩具などの木工製品の代替品となりうる比重0.75
〜1.0の低発泡成形体、その中でも特に発泡成形
が困難とされている形状が複雑な低発泡成形体、
大型の低発泡成形体、あるいは肉厚の厚い低発泡
成形体などを与えるフエノール樹脂成形材料に関
するものである。 従来の技術 従来、食品類、記念品、装飾品、玩具などは主
として木材を使用して成形加工されていたが、近
年これらの木工製品の代替品として、熱可塑性樹
脂や熱硬化性樹脂の成形材料を用いた成形品が市
販されている。しかしながら、この樹脂製の成形
品においては、木材の感触や機能を十分に備えた
ものはまだ得られていない。例えば熱可塑性樹脂
成形材料から得られる成形品は、温湯に浸した場
合、軟らくなつて変形しやすくなるし、また食器
として用いた場合高温の内容物を入れると、熱く
なつて手で持てなくなるなどの欠点を有してい
る。一方、熱硬化性樹脂成形材料、例えばフエノ
ール樹脂成形材料から得られる成形品について
は、熱湯を入れても軟化、変形することはないと
しても、高温の内容物を入れた場合、容器が熱く
なり手で持てなくなるという欠点は避けられな
い。 これに対し、比重0.75〜1.0の低発泡フエノー
ル樹脂成形体は、熱湯を入れても軟化せず、その
容器の表面の温度も高くはならないので、この低
発泡フエノール樹脂成形体は、例えばノボラツク
型フエノール樹脂にヘキサメチレンテトラミンの
ような硬化剤と、加熱により分解して多量のガス
を発生する発泡剤と二価金属酸化物を配合し、加
熱発泡成形することにより製造されている(特公
昭47−24266号公報)。しかしながら、この低発泡
フエノール樹脂成形体は、小型で比較的簡単な形
状の食器、例えば吸物椀、平皿などにする場合に
は問題はないとしても、複雑な形状や、大型又は
肉厚の食器、例えば波目菓子鉢、サラダボール、
腰高菓子皿などにする場合には、内部に巣を生じ
やすく、表面剥離、末端部欠落などの現象が起
り、商品価値を著しく低下させる原因となる。 したがつて、これまで木材に匹敵する比重を有
し、かつ良好な断熱性を示す合成樹脂系成形材料
で、かつ複雑な形状、大型又は肉厚の食器の製造
に適したものの出現が要望されていた。 このような要望にこたえるために、本発明者ら
はフエノール樹脂系成形材料の物性改良に関し
種々研究を重ねた結果、フエノール樹脂の発泡前
後の流動性は、それに充てんされる植物質基材に
関係し、それによつて発泡の際の独立気泡の形成
状態が著しく左右されるという知見を得、それに
基づいてフエノール樹脂100重量部に対して種子
殻セルロース粉末40〜400重量部及び必要量の発
泡剤を配合した低発泡用フエノール樹脂成形材料
を提案した(特開昭59−11339号公報)。 しかしながら、この成形材料においては、吸物
椀、平皿などの比較的容易に成形しうるものにつ
いては圧縮成形によつて通常の使用に耐えうる良
好な外観と十分な強度を有し、かつ比重1.0以下
の低発泡体が得られるが、さらに成形が困難な形
状の複雑なもの、例えば波目菓子鉢のような成形
体については、従来のものと同様の内部に巣を生
じやすく、強度や外観をそこなうという欠点を免
れることはできなかつた。 発明が解決しようとする問題点 本発明の目的は、このような問題点を解決し、
木工製品の代替品となりうる比重0.75〜1.0の低
発泡成形体、その中でも特に発泡成形が困難とさ
れている形状が複雑な低発泡成形体、大型の低発
泡成形体、あるいは肉厚の厚い低発泡成形体など
を容易に発泡成形しうるフエノール樹脂成形材料
を提供することにある。 問題点を解決するための手段 本発明者らは、まず発泡成形体内部に巣ができ
る原因について種々研究を重ね、発泡成形時にお
ける発泡膜の破壊防止には、成形材料の流動性が
重要な要件になるが、また硬化速度を適当に速め
ることにより、成形体内部の巣の発生が減少する
という知見を得た。そこで本発明者らはさらに研
究を進めた結果、樹脂を構成する分子中に存在す
るオルト結合とパラ結合の比が2.0:1ないし
10.0:1の範囲にあるオルト結合に富むノボラツ
ク型フエノール樹脂が所望の硬化速度を有してお
り、このものに、流動性や粘弾性を与える充てん
基材として種子殻セルロース粉末や精製セルロー
スを、また発泡剤として特定範囲の分解温度を有
するものをそれどれ所定の割合で配合したものを
基本組成とする成形材料が前記目的に適合しうる
ことを見出し、この知見に基づいて本発明を完成
するに至つた。 すなわち、本発明は、(A)樹脂を構成する分子中
に存在するオルト結合とパラ結合の比、すなわち
o/p比が2.0〜10.0である、オルト結合に富む
ノボラツク型フエノール樹脂100重量部に対し、
(B)種子殻セルロース粉末及び精製セルロースの中
から選ばれた少なくとも1種の繊維質基材成分10
〜55重量部と、(C)100〜180℃の分解温度をもつ発
泡剤0.5〜5.0重量部を配合したことを特徴とする
低発泡体用フエノール樹脂成形材料を提供するも
のである。 本発明の成形材料においては、(A)成分のノボラ
ツク型フエノール樹脂としてo/p比が2.0〜
10.0、好ましくは2.5〜5.5の範囲にあるものを用
いることが必要である。この比が2.0よりも小さ
いものを用いると得られる成形材料の硬化速度が
遅くなるため、成形難度の高い製品を得る場合に
成形体内部に巣を生じ、表面剥離、末端部欠落な
どの欠陥を伴い、十分な強度を有し外観の良好な
製品とならない。他方、この比が10.0よりも大き
いものを用いると、得られる成形材料の硬化速度
が速くなりすぎるため、流動性が低下し、予備成
形が困難となる上に、製品の上端部に気泡やかす
れを生じる原因となる。 ノボラツク型フエノール樹脂のo/p比は、赤
外線吸収スペクトル(以下IRスペクトルと略称
する)から求められるもので、IRスペクトルの
770〜735カイザー付近における1,2―置換体の
面外変角振動の特性吸収(オルソ結合の特性吸
収)と、840〜810カイザー付近における1,4―
置換体の面外変角振動の特性吸収(パラ結合の特
性吸収)の強さの比を表わしたもので、以下の測
定方法により求められる。 すなわち、オルト結合に富むノボラツク型フエ
ノール樹脂約1mgを乾燥した約200mgのIRスペク
トル用臭化カリウム粉末と混合し、IRスペクト
ルにおけるオルソ結合の特性吸収の透過率が35±
5%になるように錠剤の厚みを調整する。測定し
て得られたIRスペクトルから、o/p比を次式 オルソ結合/パラ結合=log Ioa/Ia/log Iob/Ib に従つて求める。 ただし、Ioa、Ia、Iob及びIbはそれぞれ図面に
示された方式のベースラインに基づいて求めた透
過率である。 本発明で用いるo/p比が2.0〜10.0の範囲に
あるノボラツク型フエノール樹脂は、例えばフエ
ノール、レゾルシン、m―クレゾールなどのフエ
ノール類1モルに対し、ホルムアルデヒド、アセ
トアルデヒドなどのアルデヒド類0.67〜0.82モル
を、触媒の存在下で加熱反応させ、その生成物を
吸引脱水することによつて得られる。この際の触
媒としては、二価金属の酸化物、塩化物、弱酸と
の塩、例えば酸化マグネシウム、酸化カルシウ
ム、塩化亜鉛、酢酸カルシウムなどが用いられ
る。これらは単独で用いてもよいし、また2種以
上混合して用いてもよい。 次に、本発明における(B)成分の繊維質基材とし
ては、種子殻セルロースや精製セルロースが用い
られる。この種子殻セルロースとしては、例えば
もみ殻、落花生殻、そば殻、豆殻などの粉末が好
適であり、精製セルロースとしては木材パルプ、
リンターパルプなどが好適である。 なお、本発明でいう精製セルロースとは、セル
ロースを含むものを、機械的及び化学的に処理す
ることによつて得られるものであり、例えば精製
セルロースの1種である木材パルプは、木材チツ
プを酸存在下で煮沸し、木材中のセルロース細胞
に接着しているリグニン属を機械的に破壊しかつ
化学的に溶出してセルロースを抽出し、さらにア
ルカリ処理後、漂白して抄紙機によりシート状に
したものを乾燥、粉砕することによつて得られ
る。 この種子殻セルロースは、約120℃以下の低温
における成形材料の流動性を付与する役割を果す
ものであり、これにより成形材料の予備成形を容
易に行うことができる。また精製セルロースはフ
エノール樹脂中に均一に分散され、かつその一部
が溶解されるため、成形材料の粘弾性を向上さ
せ、成形時における気泡膜の強化をもたらす。木
粉などの未精製セルロースでは、このような効果
は得られない。そして、種子殻セルロースと精製
セルロースとを併用すれば、両者の相乗効果が得
られるので有利である。 この繊維質基材は、粉末状で用いるのが好まし
い。その配合量としては、該フエノール樹脂100
重量部に対し、10〜55重量部の範囲が用いられ
る。この量が10重量部未満では成形材料の熱溶融
時における粘弾性が低くなり、その結果発泡過程
で発泡膜がつぶれるため、得られた成形体内部に
連続気泡による巣が生じやすく、良好な成形体が
得られない。一方55重量部を超えると、成形材料
の熱溶融時の流動性が低くなつて、予備成形が困
難で充てん不良となり、良好な成形体が得られな
い。 本発明において(C)成分として使用される発泡剤
は、(A)成分及び(B)成分と混合した状態における分
解温度が100〜180℃のものであることが必要であ
る。このようなものとしては、例えばジニトロソ
ペンタメチレンテトラミン、p―トルエンスルホ
ニルアセトンヒドラゾン、p―トルエンスルホニ
ルヒドラジドなどが好ましく挙げられる。これら
の発泡剤は通常単独で用いられるが、2種以上を
併用して発泡のタイミングを調整することもでき
る。本発明でいう分解温度とは、該発泡剤が前記
の(A)成分及び(B)成分と共存しているときの分解温
度であり、一般に文献などに記載されている発泡
剤単独の分解温度より低くなるのが普通である。 この発泡剤の配合量については、該フエノール
樹脂100重量部に対して0.5〜50重量部の範囲で用
いられる。この好適な配合量は得られる低発泡体
の比重によつて変わるが、通常1.0〜3.0重量部の
範囲で選ばれる。この配合量が0.5重量部未満で
は比重0.75〜1.0の成形体が得られないし、また
5.0重量部を超えると成形体内部や表面に連続気
泡が形成され、強度が低くかつ外観の悪い成形体
を生じる原因となる。 本発明の低発泡体用フエノール樹脂成形材料を
調製するには、o/p比が2.0〜10.0のノボラツ
ク型フエノール樹脂100重量部に、種子殻セルロ
ース粉末又は精製セルロース若しくはその両方か
ら成る繊維質基材10〜55重量部及び該(A)成分及び
(B)成分との共存下における分解温度が100〜180℃
の発泡剤0.5〜5.0重量部を配合し、さらに必要に
応じて硬化剤、硬化触媒、離型剤、着色剤などの
添加剤を適当量添加したのち、適量の溶剤ととも
にミキサー中で混合し、次いで得られた混合物を
加熱ロールで混練後、シート状に引き出し、適当
な粒度に造粒又は粉砕することによつて、所望の
低発泡体用のフエノール樹脂成形材料が得られ
る。 このようにして得られた成形材料の所定量を約
120〜150℃に加熱された金型中に投入し、予備成
形後、約5〜15分間圧縮成形することによつて、
例えば波目菓子鉢などのような複雑な成形体を得
ることができる。 発明の効果 本発明の成形材料は、約150℃以下の低温域に
おいて良好な流動性を示し、かつこの温度領域で
容易に発泡し、強い気泡膜を有する均一に分散さ
れた細かい独立気泡を形成するので、予備成形が
しやすく、比較的成形が困難とされている形状の
複雑な成形体や大型の成形体、あるいは肉厚の厚
い成形体などが容易に成形できる。また、成形体
内部に巣ができたり、表面剥離や末端部欠落のよ
うな望ましくない現象を伴わないので十分な強度
を有する外観の優れた成形体を得ることができ
る。 また、精製セルロースは油分や不純物が含まれ
ていないため、これを使用した場合には、塗装密
着性の優れた製品を与えるという利点がある。 さらに、本発明の成形材料から得られる成形体
は、比重が0.75〜1.0の範囲のもので、水に浮き
軽量であつて断熱性もよく、木質感を有している
ので、食器類、記念品、装飾品、玩具などの木工
類似品の製造材料として好適である。 実施例 次に実施例によつて本発明をさらに詳細に説明
する。 実施例 1 ハイオルソタイプノボラツク型フエノール樹脂
(o/p比=4.0) 700g もみ殻粉末 100g 木材パルプ 200g ジニトロソペンタメチレンテトラミン 8g ヘキサメチレンテトラミン 90g 酸化マグネシウム 20g ステアリン酸 14g 上記配合物をメタノールとともにミキサー中で
混合し、次にこの混合物を80℃に加熱したロール
で約12分間混練し得られたシートを冷却後粉砕し
てフエノール樹脂成形材料を得た。 得られた成形材料をJISK6911に準じ、下記条
件にて円板式流れを測定した結果110mmであつた。 条件:金型温度 140±3℃ 成形圧力 1500Kg 加圧時間 1分 試料量 2g 得られた成形材料530gを使用して金型温度120
〜140℃,成形圧力150Kg/cm2及び加圧時間7分間
の条件にて圧縮成形を行い、波目菓子鉢を成形す
ることができた。 得られた該成形体は比重0.97で木質感を有した
もので、該成形体表面は、光沢を有しカスレ,割
れや気泡などの欠陥が全く見られず、また該成形
体断面にも巣や連通気泡などが全く見られず、内
部気泡構造は均一かつ緻密であり十分な強度と良
好な外観を有した塗装密着性の良好な非常に優れ
たものであつた。 実施例 2〜6 第1表に示した配合で実施例1と同様にしてフ
エノール樹脂成形材料を得た。得られた成形材料
のそれぞれの円板式流れを第2表に示す。 得られた成形材料530gを使用して実施例1と
同様にして波目菓子鉢を成形することができた。
得られた該成形体の比重及び外観を第2表に示
す。 比較例 1〜5 第1表に示した配合で実施例1と同様にしてフ
エノール樹脂成形材料を得た。得られた成形材料
のそれぞれの円板式流れを第2表に示す。 得られた成形材料530gを使用して実施例1と
同様にして波目菓子鉢を成形することができた。
得られた該成形体の比重及び外観を第2表に示
す。
Industrial Application Field The present invention relates to a phenolic resin molding material for low-foamed products,
More specifically, tableware, souvenirs, decorations,
Specific gravity 0.75, which can be used as a substitute for wooden products such as toys.
~1.0 low foam molded products, especially low foam molded products with complex shapes that are difficult to foam mold.
The present invention relates to a phenolic resin molding material that provides large-sized low-foaming molded products or thick low-foaming molded products. Conventional technology In the past, food items, souvenirs, decorations, toys, etc. were mainly molded using wood, but in recent years molding of thermoplastic resin and thermosetting resin has been used as an alternative to these wood products. Molded products using this material are commercially available. However, molded products made of resin that have the feel and functionality of wood have not yet been obtained. For example, when molded products made from thermoplastic resin molding materials are immersed in hot water, they become soft and easily deformed, and when used as tableware, when high-temperature contents are placed in them, they become too hot to hold in the hand. It has drawbacks such as: On the other hand, molded products obtained from thermosetting resin molding materials, such as phenolic resin molding materials, do not soften or deform even if hot water is poured into them, but if hot contents are poured into the container, the container becomes hot. The disadvantage of not being able to hold it in your hands is inevitable. On the other hand, low-foaming phenolic resin moldings with a specific gravity of 0.75 to 1.0 do not soften even when hot water is poured into them, and the surface temperature of the container does not become high. It is manufactured by combining phenolic resin with a hardening agent such as hexamethylenetetramine, a foaming agent that decomposes when heated and generates a large amount of gas, and a divalent metal oxide, and then heat-foaming the mixture. -24266). However, although this low-foaming phenolic resin molding does not pose a problem when used to make tableware of small and relatively simple shapes, such as soup bowls and flat plates, it is difficult to use the low-foaming phenolic resin moldings when making tableware of complex shapes, large size or thick walls, etc. For example, wavy confectionery bowls, salad bowls,
When used to make waist-high confectionery plates, etc., nests are likely to form inside the plate, causing phenomena such as surface peeling and end portion loss, which significantly reduces the product value. Therefore, there has been a demand for a synthetic resin molding material that has a specific gravity comparable to that of wood, exhibits good heat insulation properties, and is suitable for manufacturing tableware with complex shapes, large size, or thick walls. was. In order to meet these demands, the present inventors have conducted various studies on improving the physical properties of phenolic resin molding materials, and have found that the fluidity of phenolic resin before and after foaming is related to the vegetable base material filled into it. We obtained the knowledge that this significantly affects the state of closed cell formation during foaming, and based on this, we added 40 to 400 parts by weight of seed husk cellulose powder and the necessary amount of blowing agent to 100 parts by weight of phenolic resin. proposed a low-foaming phenolic resin molding material containing (Japanese Unexamined Patent Publication No. 11339/1983). However, with this molding material, things that can be relatively easily molded, such as soup bowls and flat plates, have a good appearance and sufficient strength to withstand normal use by compression molding, and have a specific gravity of 1.0 or less. However, when it comes to molded products with complex shapes that are difficult to mold, such as wavy confectionery bowls, cavities are likely to form inside the molded products, which deteriorates strength and appearance. There was no way I could escape the drawback of being damaged. Problems to be Solved by the Invention The purpose of the present invention is to solve these problems,
Low-foam molded products with a specific gravity of 0.75 to 1.0 can be used as substitutes for wood products, especially low-foam molded products with complex shapes that are difficult to foam mold, large low-foam molded products, or thick-walled low-foam molded products. It is an object of the present invention to provide a phenolic resin molding material that can be easily foam-molded into foam molded articles. Means for Solving the Problems The present inventors first conducted various studies on the causes of cavities forming inside foam molded products, and found that the fluidity of the molding material is important for preventing the destruction of the foam membrane during foam molding. Although this is a requirement, we have also found that by increasing the curing speed appropriately, the occurrence of cavities inside the molded product can be reduced. Therefore, the present inventors conducted further research and found that the ratio of ortho bonds and para bonds present in the molecules constituting the resin was 2.0:1 or 2.0:1.
A novolac-type phenolic resin rich in ortho bonds in the range of 10.0:1 has the desired curing speed, and seed shell cellulose powder or purified cellulose is added to this as a filling base material that provides fluidity and viscoelasticity. Furthermore, the inventors have discovered that a molding material whose basic composition is a mixture of blowing agents having a decomposition temperature within a specific range in a predetermined ratio can be suitable for the above purpose, and based on this knowledge, the present invention has been completed. It came to this. That is, the present invention provides (A) 100 parts by weight of a novolak-type phenolic resin rich in ortho bonds, in which the ratio of ortho bonds to para bonds present in the molecules constituting the resin, that is, the o/p ratio, is 2.0 to 10.0. On the other hand,
(B) At least one fibrous base material component selected from seed shell cellulose powder and purified cellulose10
The present invention provides a phenolic resin molding material for low-foam objects, characterized in that it contains 0.5 to 5.0 parts by weight of a blowing agent having a decomposition temperature of 100 to 180° C. and (C) 0.5 to 5.0 parts by weight of a blowing agent having a decomposition temperature of 100 to 180°C. In the molding material of the present invention, the o/p ratio of the novolak type phenolic resin as component (A) is 2.0 to 2.0.
10.0, preferably in the range of 2.5 to 5.5. If a material with this ratio smaller than 2.0 is used, the curing speed of the resulting molding material will be slow, which will result in cavities inside the molded product and defects such as surface peeling and end part loss when producing products that are highly difficult to mold. Consequently, a product with sufficient strength and good appearance cannot be obtained. On the other hand, if a material with a ratio greater than 10.0 is used, the resulting molding material will harden too quickly, resulting in decreased fluidity and difficulty in preforming, as well as air bubbles and scratches at the top of the product. This may cause The O/P ratio of novolak type phenolic resin is determined from the infrared absorption spectrum (hereinafter abbreviated as IR spectrum).
Characteristic absorption of out-of-plane bending vibration of the 1,2-substituted substance near 770-735 Kaiser (characteristic absorption of ortho bond) and 1,4- around 840-810 Kaiser.
It expresses the ratio of the strength of the characteristic absorption of out-of-plane bending vibration (characteristic absorption of para bond) of the substituted body, and is determined by the following measurement method. That is, about 1 mg of novolac-type phenolic resin rich in ortho bonds is mixed with about 200 mg of dried potassium bromide powder for IR spectra, and the transmittance of the characteristic absorption of ortho bonds in the IR spectrum is 35±.
Adjust the thickness of the tablet to 5%. From the measured IR spectrum, the o/p ratio is determined according to the following formula: Ortho bond/para bond = log Ioa/Ia/log Iob/Ib. However, Ioa, Ia, Iob, and Ib are transmittances determined based on the baseline of the method shown in the drawings. The novolac type phenolic resin used in the present invention has an O/P ratio in the range of 2.0 to 10.0, for example, 0.67 to 0.82 mol of aldehydes such as formaldehyde and acetaldehyde per 1 mol of phenols such as phenol, resorcinol, and m-cresol. can be obtained by heating and reacting in the presence of a catalyst and dehydrating the product under suction. As the catalyst in this case, divalent metal oxides, chlorides, and salts with weak acids, such as magnesium oxide, calcium oxide, zinc chloride, and calcium acetate, are used. These may be used alone or in combination of two or more. Next, as the fibrous base material of component (B) in the present invention, seed shell cellulose or purified cellulose is used. Suitable examples of this seed husk cellulose include powders such as rice husks, peanut husks, buckwheat husks, and bean husks; examples of refined cellulose include wood pulp,
Linter pulp and the like are suitable. Note that purified cellulose as used in the present invention is obtained by mechanically and chemically treating materials containing cellulose. For example, wood pulp, which is a type of purified cellulose, is obtained by processing wood chips. Cellulose is extracted by boiling in the presence of acid, mechanically destroying the lignin adhering to cellulose cells in the wood, and chemically eluting it, followed by alkaline treatment, bleaching, and making it into sheets using a paper machine. It is obtained by drying and pulverizing it. This seed shell cellulose plays the role of imparting fluidity to the molding material at low temperatures of about 120° C. or lower, thereby making it possible to easily preform the molding material. Further, since purified cellulose is uniformly dispersed in the phenolic resin and partially dissolved, it improves the viscoelasticity of the molding material and strengthens the cell membrane during molding. Such effects cannot be obtained with unrefined cellulose such as wood flour. It is advantageous to use seed husk cellulose and purified cellulose together because a synergistic effect can be obtained between the two. This fibrous base material is preferably used in powder form. The blending amount is 100% of the phenolic resin.
Based on parts by weight, a range of 10 to 55 parts by weight is used. If this amount is less than 10 parts by weight, the viscoelasticity of the molding material during hot melting will be low, and as a result, the foam membrane will collapse during the foaming process, which will easily cause cavities due to open cells inside the resulting molded product, resulting in poor molding. I can't get a body. On the other hand, if it exceeds 55 parts by weight, the fluidity of the molding material during hot melting becomes low, making preforming difficult and causing poor filling, making it impossible to obtain a good molded body. The blowing agent used as component (C) in the present invention must have a decomposition temperature of 100 to 180° C. when mixed with components (A) and (B). Preferred examples of such compounds include dinitrosopentamethylenetetramine, p-toluenesulfonylacetone hydrazone, and p-toluenesulfonylhydrazide. These foaming agents are usually used alone, but two or more types can also be used in combination to adjust the timing of foaming. The decomposition temperature in the present invention is the decomposition temperature when the blowing agent coexists with the above-mentioned components (A) and (B), and is generally the decomposition temperature of the blowing agent alone as described in literature. It is normal to be lower. The amount of the blowing agent used is in the range of 0.5 to 50 parts by weight per 100 parts by weight of the phenolic resin. This suitable amount varies depending on the specific gravity of the low foam to be obtained, but is usually selected within the range of 1.0 to 3.0 parts by weight. If this amount is less than 0.5 parts by weight, a molded product with a specific gravity of 0.75 to 1.0 cannot be obtained, and
If it exceeds 5.0 parts by weight, open cells will be formed inside or on the surface of the molded product, resulting in a molded product with low strength and poor appearance. To prepare the phenolic resin molding material for low-foamed objects of the present invention, 100 parts by weight of a novolak type phenolic resin having an o/p ratio of 2.0 to 10.0 is added to a fibrous base consisting of seed shell cellulose powder, purified cellulose, or both. 10 to 55 parts by weight of the material and the (A) component and
Decomposition temperature in coexistence with component (B) is 100-180℃
0.5 to 5.0 parts by weight of a blowing agent are added, and if necessary, appropriate amounts of additives such as a curing agent, curing catalyst, mold release agent, and coloring agent are added, and then mixed in a mixer with an appropriate amount of solvent. Next, the resulting mixture is kneaded with heated rolls, drawn out into a sheet, and granulated or pulverized to an appropriate particle size to obtain the desired phenolic resin molding material for low-foaming products. The predetermined amount of the molding material thus obtained is approx.
By putting it into a mold heated to 120-150℃ and compression molding for about 5-15 minutes after preforming,
For example, complex molded bodies such as wavy confectionery bowls can be obtained. Effects of the Invention The molding material of the present invention exhibits good fluidity in a low temperature range of about 150°C or less, and easily foams in this temperature range, forming uniformly dispersed fine closed cells with a strong cell membrane. Therefore, it is easy to preform, and it is possible to easily mold complex shaped molded products, large molded products, or thick molded products that are relatively difficult to mold. Further, since there are no undesirable phenomena such as the formation of cavities inside the molded product, surface peeling, or loss of end portions, it is possible to obtain a molded product with sufficient strength and an excellent appearance. Further, since purified cellulose does not contain oil or impurities, its use has the advantage of providing a product with excellent paint adhesion. Furthermore, the molded product obtained from the molding material of the present invention has a specific gravity in the range of 0.75 to 1.0, floats on water, is lightweight, has good insulation properties, and has a wood texture, so it can be used for tableware, commemorative items, etc. It is suitable as a manufacturing material for wood products such as goods, decorations, and toys. EXAMPLES Next, the present invention will be explained in more detail with reference to Examples. Example 1 High ortho type novolac type phenolic resin (o/p ratio = 4.0) 700g Rice husk powder 100g Wood pulp 200g Dinitrosopentamethylenetetramine 8g Hexamethylenetetramine 90g Magnesium oxide 20g Stearic acid 14g The above mixture was mixed with methanol. Next, this mixture was kneaded for about 12 minutes using rolls heated to 80°C, and the resulting sheet was cooled and pulverized to obtain a phenolic resin molding material. The disc flow of the obtained molding material was measured according to JISK6911 under the following conditions, and the result was 110 mm. Conditions: Mold temperature 140±3℃ Molding pressure 1500Kg Pressure time 1 minute Sample amount 2g Using the obtained molding material 530g, mold temperature 120
Compression molding was performed under the conditions of ~140°C, molding pressure of 150 Kg/cm 2 , and pressurization time of 7 minutes, and a wavy confectionery bowl could be formed. The obtained molded product had a specific gravity of 0.97 and a woody texture, and the surface of the molded product was glossy and showed no defects such as scratches, cracks, or bubbles, and there were no cavities in the cross section of the molded product. No open air bubbles or the like were observed, and the internal cell structure was uniform and dense, with sufficient strength, good appearance, and excellent paint adhesion. Examples 2 to 6 Phenol resin molding materials were obtained in the same manner as in Example 1 using the formulations shown in Table 1. Table 2 shows the disc flow of each of the molding materials obtained. Using 530 g of the obtained molding material, a wavy confectionery pot could be molded in the same manner as in Example 1.
Table 2 shows the specific gravity and appearance of the molded product obtained. Comparative Examples 1 to 5 Phenol resin molding materials were obtained in the same manner as in Example 1 using the formulations shown in Table 1. Table 2 shows the disc flow of each of the molding materials obtained. Using 530 g of the obtained molding material, a wavy confectionery pot could be molded in the same manner as in Example 1.
Table 2 shows the specific gravity and appearance of the molded product obtained.

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of the drawing]

図面は、本発明で用いるノボラツク型フエノー
ル樹脂のo/p比の計算方法を説明するための赤
外吸収スペクトル図の1例である。
The drawing is an example of an infrared absorption spectrum diagram for explaining the method for calculating the O/P ratio of the novolak type phenolic resin used in the present invention.

Claims (1)

【特許請求の範囲】 1 (A)樹脂を構成する分子中に存在するオルト結
合とパラ結合の比が2.0:1ないし10.0:1の範
囲にあるオルト結合に富むノボラツク型フエノー
ル樹脂100重量部に対し、(B)種子殻セルロース及
び精製セルロースの中から選ばれた少なくとも1
種の繊維質基材成分10〜55重量部と、(C)100〜180
℃の分解温度をもつ発泡剤0.5〜5.0重量部を配合
したことを特徴とする低発泡体用フエノール樹脂
成形材料。 2 種子殻セルロースがもみ殻、落花生殻、そば
殻及び豆殻の中から選ばれた少なくとも1種であ
る特許請求の範囲第1項記載の成形材料。 3 精製セルロースが木材パルプ及びリンターパ
ルプの中から選ばれた少なくとも1種である特許
請求の範囲第1項記載の成形材料。 4 発泡剤がジニトロソペンタメチレンテトラミ
ン、p―トルエンスルホニルアセトンヒドラゾン
及びp―トルエンスルホニルヒドラジドの中から
選ばれた少なくとも1種である特許請求の範囲第
1項、第2項又は第3項に記載の成形材料。
[Scope of Claims] 1 (A) 100 parts by weight of a novolac-type phenolic resin rich in ortho bonds, in which the ratio of ortho bonds to para bonds present in the molecules constituting the resin is in the range of 2.0:1 to 10.0:1. (B) at least one selected from seed husk cellulose and purified cellulose;
10 to 55 parts by weight of the fibrous base material component of seeds and 100 to 180 parts by weight of (C)
A phenolic resin molding material for low-foamed objects, characterized in that it contains 0.5 to 5.0 parts by weight of a blowing agent having a decomposition temperature of °C. 2. The molding material according to claim 1, wherein the seed husk cellulose is at least one selected from rice husk, peanut husk, buckwheat husk, and bean husk. 3. The molding material according to claim 1, wherein the purified cellulose is at least one selected from wood pulp and linter pulp. 4. Claims 1, 2, or 3, wherein the blowing agent is at least one selected from dinitrosopentamethylenetetramine, p-toluenesulfonylacetone hydrazone, and p-toluenesulfonyl hydrazide. molding material.
JP21433184A 1984-10-15 1984-10-15 Phenolic resin molding material for producing foam having low expansion degree Granted JPS6195039A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21433184A JPS6195039A (en) 1984-10-15 1984-10-15 Phenolic resin molding material for producing foam having low expansion degree

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21433184A JPS6195039A (en) 1984-10-15 1984-10-15 Phenolic resin molding material for producing foam having low expansion degree

Publications (2)

Publication Number Publication Date
JPS6195039A JPS6195039A (en) 1986-05-13
JPS6320857B2 true JPS6320857B2 (en) 1988-04-30

Family

ID=16653981

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21433184A Granted JPS6195039A (en) 1984-10-15 1984-10-15 Phenolic resin molding material for producing foam having low expansion degree

Country Status (1)

Country Link
JP (1) JPS6195039A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4425442A1 (en) * 1994-07-19 1996-01-25 Huels Chemische Werke Ag Process for the production of biodegradable, thermoset foams

Also Published As

Publication number Publication date
JPS6195039A (en) 1986-05-13

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