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JPH0464539B2 - - Google Patents
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JPH0464539B2 - - Google Patents

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Publication number
JPH0464539B2
JPH0464539B2 JP59227156A JP22715684A JPH0464539B2 JP H0464539 B2 JPH0464539 B2 JP H0464539B2 JP 59227156 A JP59227156 A JP 59227156A JP 22715684 A JP22715684 A JP 22715684A JP H0464539 B2 JPH0464539 B2 JP H0464539B2
Authority
JP
Japan
Prior art keywords
particles
aggregate
resin composition
foam
phenolic 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.)
Expired - Lifetime
Application number
JP59227156A
Other languages
Japanese (ja)
Other versions
JPS61103942A (en
Inventor
Kimimichi Masui
Shigetoshi Tanaka
Yoshikazu Kobayashi
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.)
Sekisui Kasei Co Ltd
Original Assignee
Sekisui Plastics 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 Sekisui Plastics Co Ltd filed Critical Sekisui Plastics Co Ltd
Priority to JP22715684A priority Critical patent/JPS61103942A/en
Publication of JPS61103942A publication Critical patent/JPS61103942A/en
Publication of JPH0464539B2 publication Critical patent/JPH0464539B2/ja
Granted legal-status Critical Current

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Description

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

(イ) 発明の目的 (産業上の利用分野) この発明は発泡性を有する固形の樹脂組成物を
粒状の骨材の表面に被覆した発泡性を有する粒子
に関する。 (従来の技術) 従来、レゾール型フエノール樹脂初期縮合物と
所要量の分解型発泡剤を混合してなる発泡性樹脂
組成物は、粉末化しても使用され、その粉末の大
きさも100メツシユ以上、カサ比重も1以下が普
通である。 (発明が解決しようとする問題点) しかしながら、この組成物と、他の粒子とを混
合してフエノール樹脂の成形体を得るには、粒子
の大きさが1mm以下、かつカサ比重が上記組成物
と同じ程度でないと均一な混合体となりにくく、
これを加熱発泡しても均一な発泡を有したフエノ
ール樹脂の成形体として得ることはきわめて困難
であるという問題点があつた。 上記事情に鑑み、この発明の発明者らは、フエ
ノール樹脂の成形体を得るに際し、その形状、大
きさ、カサ比重にかかわらず、被覆する発泡性樹
脂組成物と反応性のない骨材粒子に予めその組成
物を被覆しておき、この発泡性樹脂被覆粒子を用
いて型内に充填して加熱等を行なうことにより均
一なフエノール樹脂の発泡成形体が容易に得られ
る事実を見出しこの発明に到達した。 (ロ) 発明の構成 かくしてこの発明によれば、骨材粒子が、固形
のレゾール型フエノール樹脂初期縮合物、分解型
発泡剤を必須成分として含有する固形発泡性樹脂
組成物で被覆されてなることを特徴とする発泡性
樹脂被覆粒子が提供される。 上記の発泡性樹脂被覆粒子は、加熱により、内
側に骨材を含み、外側がレゾール型フエノール樹
脂発泡層に覆われた断熱性粒状物質となる。たと
えばこの発明の粒子を金型等型内に充填して加熱
すれば、骨材粒子がフエノール発泡体中均一に分
散したフエノールの成形体が得られる。 この発明の主原料であるレゾール型フエノール
樹脂初期縮合物とは、フエノール類と過剰のアル
デヒド類とを塩基性触媒の存在下反応させて得ら
れる当該分野で知られたいわゆるレゾール型フエ
ノール樹脂と称せられ、酸性硬化促進剤又は、加
熱により更に重合が進行しうるものを意味する。
かようなレゾール型フエノール樹脂は、反応水を
約20%含んだ液状のものであるが、これを更に脱
水(水分を蒸発)し固形状物(水分を1%前後含
む)とし、次いでこの固形状物を粉砕して、本発
明で使用する粉末状のレゾール型フエノール樹脂
とする。 上記フエノール類とは、フエノールの他に、
3,5−キシレノール、m−クレゾール、2,5
−キシレノール、3,4−キシレノール、2,4
−キシレノール、o−クレゾール、p−クレゾー
ルなどが含まれる。又アルデヒド類とは、ホルム
アルデヒド、パラホルムアルデヒド、ヘキサメチ
レンテトラミン、フルフラール、アセトアルデヒ
ド、アセタール類などが含まれる。この発明に使
用するのに好ましい初期縮合物は、フエノールと
ホルムアルデヒドとの縮合物である。この発明に
おける分解型発泡剤とは、レゾール型フエノール
樹脂初期縮合物に混合した組成物中で加熱硬化時
に分解してガスを発生しうる無機及び有機の発泡
剤を意味する。これらの代表例としては、N−
N′−ジニトロソペンタメチレンテトラミン、ベ
ンゼンスルホニルヒドラジド、アゾビスイソブチ
ロニトリル、アゾジカルボンアミド、パラトルエ
ンスルホニルヒドラジドなどの有機分解型発泡
剤、並びに重炭酸ナトリウム、炭酸アンモニウ
ム、重炭酸アンモニウム、亜硝酸アンモニウム、
アジド化合物(例えばCaN6)などの無機分解発
泡剤が挙げられる。これらは全て粉末状である。 発泡剤の添加量は、所望する最終の発泡体の密
度を主に考慮してその所要量とされるが、レゾー
ル型フエノール樹脂100重量部に対し1〜50重量
部が適当であり、4〜8重量部が好ましい。 この発明の発泡性樹脂組成物には、他の種々の
添加剤例えばクレイ等の充填剤が少量加えられて
いてもよい。これらの添加剤は、レゾール型フエ
ノール樹脂100重量部に対し100重量部以下である
のが好ましい。 この発明における発泡性樹脂組成物は、通常、
その含有成分であるレゾール型フエノール樹脂初
期縮合物、分解型発泡剤(及び他の添加剤)を加
熱ロール等により混練して均一に混合し、粉砕し
て外径1mm以下の粉末形態で使用される。もちろ
ん顆粒化したものを用いてもよい。 骨材としては、有機質もしくは無機質の粒子又
はそれらの混合物が含まれるが、発泡性樹脂組成
物と反応しないものが好ましい。 無機質としては、例えばパーライト、シラスバ
ルーン、ガラスバルーン、ガラス発泡粒、ガラス
綿粒状物、ロツクウール粒状物、スラツグ、粘土
多泡粒、砂、石コウ粒状物、金属性粒状物などが
挙げられる。 有機質としては、合成樹脂粒子及びその発泡粒
子、木粉粒、紙粒などが挙げられるが、通常100
℃以上の耐熱性を有する樹脂が好ましく、例え
ば、レゾール型フエノール樹脂発泡粒、スチレン
−無水マレイン酸共重合樹脂発泡粒、ポリプロピ
レン発泡粒などが挙げられる。 骨材粒子の形状には特に限定はなく、球状、粉
砕された破片状、不定形の何れであつてもよい。
粒子の大きさは粒径1mmの微小粒から粒径40〜50
mmの大粒までいずれでもよい。また骨材粒子の密
度は、特に限定はなく、軽量の発泡成形帯の用途
を考慮したときは、密度1g/cm3以下のものを選
定すればよく、別に高密度の骨材であつてもよ
い。 骨材粒子への発泡性樹脂組成物の被覆方法とし
ては、粉末の発泡性樹脂組成物が溶融付着する程
度の温度範囲、つまり軟化点である約70℃から、
発泡、硬化する約110〜120℃の範囲までの温度に
骨材粒子を加熱し、この状態で発泡性樹脂組成物
(粉末状)を吹付け、ふりかけ等により接触させ
て被覆粒子を得る方法、また逆にこの発泡性組成
物を加熱軟化させて骨材粒子に被覆する方法があ
る。 また別の方法として、結合剤を用いて行なわれ
る。結合剤としては、水、メチルアルコール、ト
ルエン等が一般的である。これらの中で水が最も
好ましい。このような結合剤を使用するとき、例
えば、パン型造粒機中で結合剤を噴霧しながら骨
剤粒子と粉末の発泡性樹脂組成物とを共に転動さ
せればよい。これらの結合剤を使用した場合に
は、被覆造粒後、乾燥工程に付して結合剤を除去
するのが好ましい。これは、例えば水が残留する
と発泡倍率と気泡などに悪影響を与えることがあ
るからである。また結合剤として、発泡時に悪影
響を及ぼさないものであればよい。たとえば他の
結合剤としては、粘着性のあるポリビニルアルコ
ールの3〜5%水溶液、シリコンオイル、動植物
油等を用いてもよい。これらの結合剤を用いたと
きは、この発明の被覆粒子に残留するが、このよ
うな被覆粒子もこの発明に含まれる。 骨材粒子に発泡性樹脂組成物を被覆する被覆量
は、組成物の発泡性、骨材の種類及び形状等によ
り異なるが、通常、骨材粒子1リツトル容量当り
5g重量以上の被覆が必要であり、良好な被覆量
は15〜500gである。この際の被覆状態は、組成
物が均一に骨材粒子に被覆されている程よいが、
成形体を得る場合は別にまだらな被覆状態でも、
なんらかまわない。 なお、得られたこの発明の発泡性樹脂被覆粒子
の、被覆樹脂組成物が部分的に発泡、硬化されて
いる2次発泡性を有する組成物であつてもよい。 (ハ) 発明の効果 この発明にかかる発泡性樹脂被覆粒子は、任意
の形状の発泡成形体とすることができる。たとえ
ば、所望形状を有する型内に、発泡性樹脂組成物
をカサ容積で通常20〜100%充填し、所定温度
(例えば150〜180℃程度)に加熱すれば、容易に
各粒子が膨張し、融着一体化された発泡成形体と
することができる。また、この発明の発泡性樹脂
被覆粒子は、被覆層が固形化されているので、貯
蔵安定性、空気構造、型内への充填で優れてお
り、作業性がよいものである。 ここで得られる発泡成形体は、発泡性樹脂組成
物と骨材粒子を単に混合して発泡させたものとは
異なり、骨材が発泡体中に実質的に均一に分散し
たものである。ここで骨材粒子が実質的に均一に
分散した成形体とは、骨材粒子が成形体の表層部
または中心部のみに偏よつて存在しないことを意
味する。従つて、骨材粒子が実質的に均一に分散
された成形体が得られるため、このような成形体
は寸法安定性が高く、断熱効果が均一であるな
ど、種々の品質特性を有する。なお、発泡成形の
際、カサ容積の20%という低い充填率においても
発泡成形体中に骨材が実質的に均一に分散するこ
とが認められており、このことは、この発明の発
明者らが発見した新規の驚くべき知見の一つであ
る。 かくしてこの発明の一つの観点によれば、発泡
素材として、骨材粒子が、レゾール型フエノール
樹脂初期縮合物、分解発泡剤を必須成分として含
有する発泡性樹脂組成物で被覆したものからな
り、骨剤粒子が実質的に均一に分散されてなるこ
とを特徴とする骨剤粒子含有レゾール型フエノー
ル樹脂発泡成形体が提供される。 この発明の成形体の形状は特に限定されない
が、板状、円筒状等のいずれであつてもよい。例
えば板状であれば、建築用の断熱板として用いれ
ら、円筒状であれば、パイプをカバーする断熱材
として用いることができる。さらにこの成形体は
非常に軽量で、他のもの(たとえば鉄板等)との
接着性に優れているのでサイジングボード等の複
合成形体としても好適なものである。 (実施例) 次のこの発明を実施例で説明するが、これによ
つてこの発明は限定されるものではない。 実施例 1 125℃での流れ70〜100mm、150℃でのゲルタイ
ム85〜105sec、軟化点73℃の粉末レゾール型フエ
ノール樹脂100重量部に対して、10重量部の発泡
剤ジニトロソペンタチレンテトラミンを混合し、
粒状の発泡性レゾール型フエノール樹脂組成物を
得た。 次いで、平均粒径5.0mmφのレゾール型フエノ
ール樹脂球状多泡体を骨剤粒子として、上記樹脂
組成物粉末をパン型造粒機によつて3分間造粒し
た。なお、その際の結合剤としてはメチルアルコ
ール(試薬特級)を使用し、ノズルより霧状に噴
霧した。 なお、造粒時の原料比率としては骨材1000c.c.
(嵩)に対して、結合剤8c.c.、粉末レゾール型フ
エノール樹脂組成物80c.c.(嵩)である。 次にこの工程で得られた被覆粒子を一昼夜風乾
燥し50℃の熱風循環式恒温槽内で3時間乾燥し
た。 この得られた被覆粒子は骨材(レゾール型フエ
ノール樹脂発泡粒)の表面にこげ茶色の発泡性樹
脂組成物粉末が溶解し薄膜となつて融着した状態
のものであり、その粉末は乱雑に扱つても剥離す
るものではなかつた。なお、この被覆はまだ完全
に発泡してなく、平均56μの厚みであつた。 次にこの被覆粒子をタルク粉末上に置き160℃
の熱風循環式恒温槽内で30分間発泡硬化させた。 得られた発泡体は、黄褐色で粒径6〜9mmで表
面に皮を有する球状のものであり、内部(骨材)
にレゾール型フエノール樹脂発泡粒が存在し、外
部に緻密な気泡構造の発泡層レゾール型フエノー
ル樹脂が存在する複合発泡球であつた。 次にこの被覆された複合発泡球を金属製型
(220×220×25mm)に嵩容積でほぼ一杯(100%)
に充填し、蓋を閉じて160℃の熱風循環式恒温槽
内に1時間保持した。その后、型を恒温槽から出
し、発泡成形体を型から取り出した。 この得られた発泡成形体は表面の粉末レゾール
型フエノール樹脂発泡層が更に発泡し、充填粒間
の空隙をすべて緻密な気泡構造の粉末レゾール型
フエノール樹脂発泡層が埋めつくし、その粒間を
完全に結合し、骨材(レゾール型フエノール樹脂
発泡粒)が均一に分散した状態のレゾール型フエ
ノール樹脂発泡成形体であつた。因にこの成形体
の密度は200Kg/m3であつた。 又、上記複合発泡球を金属製型に嵩容積で50%
充填し、加熱成形したものは、骨材が均一に成形
体中に分散した状態のもので、粒間は高倍率に発
泡した黄かつ色を帯びた緻密な気泡構造の粉末レ
ゾール型フエノール樹脂発泡層で埋めつくされた
成形体であり、密度は100Kg/m3であつた。 実施例 2、3及び4 結合剤としてメチルアルコールとトリクロロト
リフルオロエタン(F113)を使用して造粒した
他の例を実施例1を含め第1表に示す。 なお、被覆時の原料比率はいずれも実施例1と
同様である。
(a) Object of the invention (industrial field of application) The present invention relates to foamable particles in which the surface of granular aggregate is coated with a solid foamable resin composition. (Prior Art) Conventionally, a foamable resin composition prepared by mixing a resol-type phenolic resin initial condensate and a required amount of a decomposition-type foaming agent has been used even if it is powdered, and the size of the powder is 100 mesh or more. The bulk specific gravity is also usually 1 or less. (Problems to be Solved by the Invention) However, in order to obtain a molded body of phenolic resin by mixing this composition with other particles, the size of the particles must be 1 mm or less, and the bulk specific gravity must be equal to or less than the composition described above. If the level is not the same, it will be difficult to form a homogeneous mixture.
Even when heated and foamed, it is extremely difficult to obtain a uniformly foamed phenolic resin molded product. In view of the above circumstances, the inventors of the present invention have determined that when obtaining a molded body of phenolic resin, aggregate particles that are not reactive with the foamable resin composition to be coated, regardless of the shape, size, bulk specific gravity, etc. The inventors discovered the fact that a homogeneous phenolic resin foam molded product can be easily obtained by coating the composition in advance, filling a mold with the foamable resin-coated particles, and heating, etc., which led to the present invention. Reached. (B) Structure of the Invention According to the present invention, aggregate particles are coated with a solid foamable resin composition containing a solid resol type phenolic resin initial condensate and a decomposable foaming agent as essential components. Provided are expandable resin-coated particles characterized by: When heated, the expandable resin-coated particles become heat-insulating granular materials containing aggregate on the inside and covered with a resol-type phenolic resin foam layer on the outside. For example, if the particles of the present invention are filled into a mold or the like and heated, a phenol molded body in which aggregate particles are uniformly dispersed in the phenol foam can be obtained. The resol-type phenolic resin initial condensate, which is the main raw material of this invention, is a so-called resol-type phenolic resin known in the art, which is obtained by reacting phenols and excess aldehydes in the presence of a basic catalyst. It means an acidic curing accelerator or a substance that can further progress polymerization by heating.
Such resol type phenolic resin is a liquid containing about 20% reaction water, which is further dehydrated (evaporates water) to form a solid (containing about 1% water), and then this solid The shaped product is pulverized to obtain a powdered resol type phenolic resin used in the present invention. The above phenols include, in addition to phenol,
3,5-xylenol, m-cresol, 2,5
-xylenol, 3,4-xylenol, 2,4
-xylenol, o-cresol, p-cresol, etc. The aldehydes include formaldehyde, paraformaldehyde, hexamethylenetetramine, furfural, acetaldehyde, acetals, and the like. A preferred precondensate for use in this invention is a condensate of phenol and formaldehyde. The decomposable blowing agent in the present invention refers to inorganic and organic blowing agents that can decompose and generate gas during heat curing in the composition mixed with the resol type phenolic resin initial condensate. Representative examples of these include N-
Organic blowing agents such as N′-dinitrosopentamethylenetetramine, benzenesulfonyl hydrazide, azobisisobutyronitrile, azodicarbonamide, paratoluenesulfonyl hydrazide, as well as sodium bicarbonate, ammonium carbonate, ammonium bicarbonate, and ammonium nitrite. ,
Inorganic decomposition blowing agents such as azide compounds (eg CaN 6 ) may be mentioned. All of these are in powder form. The amount of the blowing agent to be added is the required amount, mainly taking into consideration the density of the desired final foam, but it is appropriate to be 1 to 50 parts by weight, and 4 to 50 parts by weight, based on 100 parts by weight of the resol type phenolic resin. 8 parts by weight is preferred. The foamable resin composition of the present invention may contain small amounts of various other additives, such as fillers such as clay. The amount of these additives is preferably 100 parts by weight or less based on 100 parts by weight of the resol type phenolic resin. The foamable resin composition in this invention usually includes:
Its components, such as a resol-type phenolic resin initial condensate and a decomposable blowing agent (and other additives), are kneaded and mixed uniformly using heated rolls, etc., and then pulverized and used in the form of a powder with an outer diameter of 1 mm or less. Ru. Of course, granules may also be used. The aggregate may include organic or inorganic particles or mixtures thereof, but preferably aggregates that do not react with the foamable resin composition. Examples of inorganic materials include perlite, shirasu balloons, glass balloons, glass foam particles, glass cotton particles, rock wool particles, slag, clay foam particles, sand, plaster particles, and metallic particles. Examples of organic substances include synthetic resin particles and foamed particles thereof, wood powder particles, paper particles, etc., but usually 100
Resins having heat resistance of .degree. C. or higher are preferred, and examples thereof include resol type phenolic resin foam beads, styrene-maleic anhydride copolymer resin foam beads, and polypropylene foam beads. There is no particular limitation on the shape of the aggregate particles, and they may be spherical, crushed fragments, or irregularly shaped.
Particle size ranges from microscopic particles with a particle size of 1 mm to particle sizes of 40 to 50.
Any grain size up to mm is fine. The density of the aggregate particles is not particularly limited; when considering the use of lightweight foam molding strips, it is sufficient to select one with a density of 1 g/cm 3 or less, even if the aggregate is of high density. good. The method for coating the aggregate particles with the foamable resin composition is as follows: from the temperature range at which the powdered foamable resin composition melts and adheres, that is, from about 70°C, which is the softening point.
A method of obtaining coated particles by heating aggregate particles to a temperature in the range of about 110 to 120°C at which they foam and harden, and in this state, spraying a foamable resin composition (powder form) and bringing them into contact with each other by sprinkling, etc. Conversely, there is a method in which the foamable composition is softened by heating and coated on aggregate particles. Another method is to use a binder. Typical binders include water, methyl alcohol, toluene, and the like. Among these, water is most preferred. When such a binder is used, for example, the aggregate particles and the powdered foamable resin composition may be rolled together in a pan-type granulator while spraying the binder. When these binders are used, it is preferable to remove the binders through a drying process after coating and granulation. This is because, for example, if water remains, it may have an adverse effect on the expansion ratio and bubbles. Further, any binder may be used as long as it does not adversely affect the foaming process. For example, other binders that may be used include a 3-5% aqueous solution of sticky polyvinyl alcohol, silicone oil, animal and vegetable oils, and the like. When these binders are used, they remain in the coated particles of the present invention, and such coated particles are also included in the present invention. The amount of coating of the foamable resin composition on the aggregate particles varies depending on the foamability of the composition, the type and shape of the aggregate, etc., but it is usually necessary to coat the aggregate particles with a weight of 5 g or more per 1 liter volume of the aggregate particles. Good coverage is 15-500g. The coating condition at this time is good enough that the composition is evenly coated on the aggregate particles, but
When obtaining a molded product, even if it is covered with a patchy coating,
I don't care. Note that the coating resin composition of the obtained expandable resin-coated particles of the present invention may be a composition having secondary foamability, which is partially foamed and cured. (c) Effects of the Invention The expandable resin-coated particles according to the present invention can be formed into a foam molded article of any shape. For example, if a mold having a desired shape is filled with a foamable resin composition, usually 20 to 100% of its bulk volume, and heated to a predetermined temperature (for example, about 150 to 180°C), each particle will easily expand. It can be made into a fused and integrated foamed molded product. Further, since the expandable resin-coated particles of the present invention have a solidified coating layer, they are excellent in storage stability, air structure, and filling into molds, and have good workability. The foamed molded product obtained here differs from one in which the foamable resin composition and aggregate particles are simply mixed and foamed, and the aggregate is substantially uniformly dispersed in the foamed product. Here, a molded product in which aggregate particles are substantially uniformly dispersed means that the aggregate particles are not concentrated only in the surface layer or center of the molded product. Therefore, a molded body in which the aggregate particles are substantially uniformly dispersed is obtained, so that such a molded body has various quality characteristics such as high dimensional stability and uniform heat insulation effect. In addition, during foam molding, it has been recognized that aggregate is substantially uniformly dispersed in the foam molded product even at a filling rate as low as 20% of the bulk volume, and this fact was confirmed by the inventors of the present invention. This is one of the new and surprising findings discovered by researchers. Thus, according to one aspect of the present invention, the foamed material is made of aggregate particles coated with a foamable resin composition containing a resol type phenolic resin initial condensate and a decomposed foaming agent as essential components. A resol type phenolic resin foam molded article containing aggregate particles is provided, which is characterized in that the agent particles are substantially uniformly dispersed. The shape of the molded article of the present invention is not particularly limited, but may be plate-shaped, cylindrical, or the like. For example, if it is plate-shaped, it can be used as a heat insulating board for construction, and if it is cylindrical, it can be used as a heat insulating material for covering pipes. Furthermore, this molded product is very lightweight and has excellent adhesiveness to other objects (for example, iron plates, etc.), so it is suitable as a composite molded product such as a sizing board. (Example) The present invention will be described below with reference to Examples, but the invention is not limited thereto. Example 1 10 parts by weight of the blowing agent dinitrosopentethylenetetramine was added to 100 parts by weight of a powdered resol type phenolic resin with a flow of 70 to 100 mm at 125°C, a gel time of 85 to 105 seconds at 150°C, and a softening point of 73°C. mix,
A granular foamable resol type phenolic resin composition was obtained. Next, the resin composition powder was granulated for 3 minutes using a pan-type granulator using resol-type phenolic resin spherical foam particles having an average particle diameter of 5.0 mm as aggregate particles. In this case, methyl alcohol (special grade reagent) was used as the binder and was sprayed in a mist form from a nozzle. The raw material ratio during granulation is 1000 c.c. of aggregate.
(bulk), the binder was 8 c.c., and the powder resol type phenolic resin composition was 80 c.c. (bulk). Next, the coated particles obtained in this step were air-dried all day and night, and then dried for 3 hours in a hot air circulation constant temperature bath at 50°C. The obtained coated particles are in a state in which dark brown foamable resin composition powder is dissolved and fused to the surface of the aggregate (resol type phenolic resin foamed particles) to form a thin film, and the powder is disordered. It did not peel off even when handled. Note that this coating was not yet completely foamed and had an average thickness of 56 μm. Next, place the coated particles on talc powder at 160°C.
The foam was cured for 30 minutes in a constant temperature bath with hot air circulation. The obtained foam is yellowish brown, has a particle size of 6 to 9 mm, and is spherical with a skin on the surface, and the inside (aggregate)
It was a composite foam sphere in which resol type phenolic resin foam particles were present on the outside, and a resol type phenolic resin foam layer with a dense cell structure was present on the outside. Next, this coated composite foam sphere is placed in a metal mold (220 x 220 x 25 mm) almost full (100%) of its bulk volume.
The container was filled with water, the lid was closed, and the container was kept in a hot air circulation constant temperature bath at 160°C for 1 hour. After that, the mold was taken out of the thermostatic oven, and the foam molded article was taken out from the mold. In this foamed molded product, the powder resol type phenolic resin foam layer on the surface further foams, and the powder resol type phenolic resin foam layer with a dense cell structure fills all the voids between the filled particles, completely filling the spaces between the particles. It was a resol type phenolic resin foam molded article in which the aggregate (resol type phenolic resin foam particles) was uniformly dispersed. Incidentally, the density of this molded body was 200 Kg/m 3 . In addition, the above composite foam ball is placed in a metal mold by 50% of the bulk volume.
The filled and heat molded product has aggregates uniformly dispersed in the molded product, and the intergranular space is a powdered resol type phenolic resin foam with a dense cell structure that is yellow and colored at a high magnification. It was a molded body filled with layers and had a density of 100 Kg/m 3 . Examples 2, 3 and 4 Other examples of granulation using methyl alcohol and trichlorotrifluoroethane (F113) as binders are shown in Table 1, including Example 1. Note that the ratio of raw materials during coating is the same as in Example 1.

【表】【table】

【表】 実施例 5 発泡性樹脂組成物の粉末は実施例1と同様にし
て調整した。 次いで、平均粒径3.7mmの発泡ガラス(商品
名;セロビーズ、豊田紡織株式会社製)を骨剤と
して上記樹脂組成物粉末をパン型造粒機によつて
被覆した。なお、その際の結合剤としては、水を
使用し、ノズルより霧状に噴霧した。 なお、被覆時の原料比率としては骨材1000c.c.
(嵩)に対して結合剤約10c.c.、レゾール型フエノ
ール樹脂組成物粉末80c.c.(嵩)である。 次にこの工程で得られた被覆粒子を一昼夜風乾
し、65℃の熱風循環式恒温槽内で4時間乾燥し
た。 この得られた被覆粒子は、骨材(発泡ガラス
粒)の表面に発泡性樹脂混合物粉末が結合した状
態のものでありこの被覆は乱雑に扱つても剥離す
るものではなかつた。なお、この被覆はまだ完全
に発泡してなく平均80μの厚みであつた。 次に、この被覆粒子をタルク粒末上に置き160
℃の熱風循環式恒温槽内で30分間発泡硬化させ
た。 得られた発泡体は、黄褐色を帯び、粒径5〜8
mmで表面に皮を有し、内部に発泡ガラス粒が存在
する緻密な気泡構造の発泡層で覆われた球状のレ
ゾール型フエノール樹脂複合発泡球であつた。 実施例6、7及び8 結合剤として水を使用して被覆した他の例を実
施例5を含め第2表に示す。なお、被覆時の原料
比率はいずれも同様である。
[Table] Example 5 A powder of a foamable resin composition was prepared in the same manner as in Example 1. Next, the resin composition powder was coated using a pan-shaped granulator using foamed glass (trade name: Cellobeads, manufactured by Toyota Boshoku Co., Ltd.) having an average particle size of 3.7 mm as an aggregate. Note that water was used as the binder at that time, and was sprayed in a mist form from a nozzle. The raw material ratio for coating is 1000 c.c. of aggregate.
(bulk), the binder is approximately 10 c.c., and the resol type phenolic resin composition powder is 80 c.c. (bulk). Next, the coated particles obtained in this step were air-dried all day and night, and then dried for 4 hours in a hot air circulation constant temperature bath at 65°C. The obtained coated particles had the foamable resin mixture powder bonded to the surface of the aggregate (foamed glass particles), and the coating did not peel off even when handled roughly. Note that this coating was not yet completely foamed and had an average thickness of 80 μm. Next, place this coated particle on top of the talc powder for 160 minutes.
The foam was cured for 30 minutes in a constant temperature bath with hot air circulation at ℃. The obtained foam has a yellowish brown color and a particle size of 5 to 8.
It was a spherical resol type phenolic resin composite foam sphere with a skin on the surface and covered with a foam layer with a dense cell structure containing foamed glass particles inside. Examples 6, 7 and 8 Other examples of coatings using water as a binder are shown in Table 2, including Example 5. Note that the ratio of raw materials during coating is the same in all cases.

【表】【table】

【表】 実施例 9 発泡性樹脂組成物の粉末は実施例1と同様に調
整した。 次いで平均粒径3.7mmの発泡ガラスを骨材とし
て、上記樹脂組成物粉末をパン型造粒機によつて
被覆した。 なお、その際の結合剤としては、分子量190〜
210のポリエチレングリコールを使用し、ノズル
より噴霧した。なお、被覆時の原料比率として
は、骨材1000c.c.(嵩)に対して結合剤10c.c.、レゾ
ール型フエノール樹脂組成物粉末80c.c.(嵩)であ
る。 次にこの工程で得られた被覆粒子を一昼夜静置
した。 この得られた被覆粒子は、骨材(発泡ガラス
粒)の表面に発泡性樹脂混合物粉末が、結合剤の
存在により付着した状態のものであり、乱雑に取
り扱かつても剥離するものではなかつた。 なお、この被覆は平均55μの厚みであつた。次
に、この被覆粒子をタルク粉末上に置き、160℃
の熱風循環式恒温槽内で30分間発泡硬化させた。 得られた発泡体は、茶色味を帯び粒径6〜9mm
で表皮を有し、内部に発泡ガラス粒が存在して発
泡層の表層で覆われた球状のレゾール型フエノー
ル樹脂複合発泡球であつた。 実施例 10 発泡性樹脂組成物の粉末は実施例1と同様にし
て調整した。 次いで平均粒径3.7mmの発泡ガラスを180℃の熱
風循環式恒温槽内で2時間加熱し、槽内からすば
やく取り出し、あらかじめ60℃の雰囲気に調整さ
れたパン型造粒機内で加熱された上記樹脂組成物
粉末中に投入し被覆した。 なお、被覆時の原料比率としては、骨材として
の発泡ガラス粒1000c.c.(嵩)に対してレゾール樹
脂組成物粉末80c.c.(嵩)である。 この得られた被覆粒子は、骨材(発泡ガラス)
の表面に発泡性樹脂組成物粉末が軟化溶融し付着
したものであつて均一な薄膜となつて被膜を形成
していた。なお、この被膜は乱雑に取り扱つても
剥離するものでなかつた。又、この被膜は、平均
45μの厚みであつた。 次に、この発泡性被覆粒子をタルク粉末上に置
き、160℃の熱風循環式恒温槽内で30分間発泡硬
化させた。 得られた発泡体は、黄褐色を帯び、粒径6〜9
mmで表皮を有し、内部に発泡ガラス粒が存在する
緻密な気泡構造の発泡層で覆われたレゾール型フ
エノール樹脂複合発泡球であつた。
[Table] Example 9 A powder of a foamable resin composition was prepared in the same manner as in Example 1. Next, the resin composition powder was coated using a pan-shaped granulator using foamed glass having an average particle size of 3.7 mm as an aggregate. In addition, the binder at that time should have a molecular weight of 190~
210 polyethylene glycol was used and sprayed from a nozzle. The ratio of raw materials during coating is 1000 c.c. (bulk) of aggregate, 10 c.c. of binder, and 80 c.c. (bulk) of resol type phenolic resin composition powder. Next, the coated particles obtained in this step were allowed to stand overnight. The obtained coated particles had the foamable resin mixture powder attached to the surface of the aggregate (foamed glass particles) due to the presence of a binder, and did not peel off even when handled roughly. . Note that this coating had an average thickness of 55 μm. Next, the coated particles were placed on talc powder and heated to 160°C.
The foam was cured for 30 minutes in a constant temperature bath with hot air circulation. The obtained foam has a brownish color and a particle size of 6 to 9 mm.
It was a spherical resol type phenolic resin composite foam sphere with a skin, foam glass particles inside, and a surface layer of a foam layer. Example 10 A powder of a foamable resin composition was prepared in the same manner as in Example 1. Next, foamed glass with an average particle size of 3.7 mm was heated for 2 hours in a hot air circulation constant temperature bath at 180°C, quickly taken out from the tank, and heated in a pan-shaped granulator pre-adjusted to an atmosphere of 60°C. It was poured into a resin composition powder and coated. The raw material ratio during coating is 1000 c.c. (bulk) of foamed glass particles as aggregate to 80 c.c. (bulk) of resol resin composition powder. This obtained coated particle is aggregate (foamed glass)
The foamable resin composition powder was softened and melted and adhered to the surface of the sample, forming a uniform thin film. Note that this coating did not peel off even when handled roughly. Also, this coating has an average
It was 45μ thick. Next, the expandable coated particles were placed on talc powder and foamed and hardened for 30 minutes in a hot air circulation constant temperature bath at 160°C. The obtained foam has a yellowish brown color and a particle size of 6 to 9.
It was a resol-type phenolic resin composite foam sphere that had a skin of 1.0 mm in diameter and was covered with a foam layer with a dense cell structure containing foamed glass particles inside.

Claims (1)

【特許請求の範囲】 1 骨材粒子が、固形のレゾール型フエノール樹
脂初期縮合物、分解型発泡剤を必須成分として含
有する固形発泡性樹脂組成物で被覆されてなるこ
とを特徴とする発泡性樹脂被覆粒子。 2 骨材粒子が、有機質もしくは無機質の粒子又
はそれらの混合物である特許請求の範囲第1項記
載の粒子。 3 有機質粒子が、レゾール型フエノール樹脂発
泡粒又はスチレン−無水マレイン酸共重合樹脂発
泡粒である特許請求の範囲第2項記載の粒子。 4 無機質粒子が、パーライト、シラスバルー
ン、ガラスバルーン、ガラス発泡粒、ガラス綿粒
状物、ロツクウール粒状物又はこれらの破砕物で
ある特許請求の範囲第2項記載の粒子。 5 発泡性樹脂組成物が粉末状で、その大きさは
骨材粒子の大きさより小さいものである特許請求
の範囲第1項記載の粒子。 6 骨材粒子1リツトル容量当りの発泡性樹脂組
成物の使用量が少なくとも5gである特許請求の
範囲第1項記載の粒子。
[Scope of Claims] 1. A foaming property characterized in that aggregate particles are coated with a solid foamable resin composition containing a solid resol type phenolic resin initial condensate and a decomposition type foaming agent as essential components. Resin coated particles. 2. The particles according to claim 1, wherein the aggregate particles are organic or inorganic particles or a mixture thereof. 3. The particles according to claim 2, wherein the organic particles are foamed resol type phenolic resin particles or foamed styrene-maleic anhydride copolymer resin particles. 4. The particles according to claim 2, wherein the inorganic particles are perlite, shirasu balloons, glass balloons, glass foam particles, glass cotton particles, rock wool particles, or crushed products thereof. 5. The particles according to claim 1, wherein the foamable resin composition is in powder form, and the size thereof is smaller than the size of the aggregate particles. 6. The particles according to claim 1, wherein the amount of foamable resin composition used per liter of aggregate particles is at least 5 g.
JP22715684A 1984-10-29 1984-10-29 Particle coated with foamable resin Granted JPS61103942A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22715684A JPS61103942A (en) 1984-10-29 1984-10-29 Particle coated with foamable resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22715684A JPS61103942A (en) 1984-10-29 1984-10-29 Particle coated with foamable resin

Publications (2)

Publication Number Publication Date
JPS61103942A JPS61103942A (en) 1986-05-22
JPH0464539B2 true JPH0464539B2 (en) 1992-10-15

Family

ID=16856370

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22715684A Granted JPS61103942A (en) 1984-10-29 1984-10-29 Particle coated with foamable resin

Country Status (1)

Country Link
JP (1) JPS61103942A (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2220366B1 (en) * 1973-03-05 1976-05-21 Saint Gobain
JPS5056459A (en) * 1973-09-20 1975-05-17
FR2413198A1 (en) * 1977-12-30 1979-07-27 Stratiforme Sa EXPANDED PHENOLIC RESIN PANEL AND ITS MANUFACTURING PROCESS
JPS557859A (en) * 1978-07-03 1980-01-21 Aica Kogyo Co Ltd Light-weight composite

Also Published As

Publication number Publication date
JPS61103942A (en) 1986-05-22

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