JPH0345702B2 - - Google Patents
Info
- Publication number
- JPH0345702B2 JPH0345702B2 JP59005274A JP527484A JPH0345702B2 JP H0345702 B2 JPH0345702 B2 JP H0345702B2 JP 59005274 A JP59005274 A JP 59005274A JP 527484 A JP527484 A JP 527484A JP H0345702 B2 JPH0345702 B2 JP H0345702B2
- Authority
- JP
- Japan
- Prior art keywords
- foamed
- foam
- mold
- particles
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/3461—Making or treating expandable particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2061/00—Use of condensation polymers of aldehydes or ketones or derivatives thereof, as moulding material
- B29K2061/04—Phenoplasts
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
【発明の詳細な説明】
この発明は、ノボラツク型フエノール樹脂発泡
成形体の製造法、ことにノボラツク型フエノール
樹脂を部分的に発泡硬化したいわゆる1次発泡粒
を一旦生成させ、次いで型成形することによるノ
ボラツク型フエノール樹脂発泡成形体の製造法に
関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a novolak type phenolic resin foam molded article, and in particular, a method for producing so-called primary foamed particles in which a novolak type phenolic resin is partially foamed and hardened, and then molding. This invention relates to a method for producing a novolak-type phenolic resin foam molded article.
従来、プラスチツク樹脂の2次発泡性を有する
1次発泡粒としては、ポリスチレン樹脂、ポリオ
レフイン樹脂及びその共重合樹脂などの熱可塑性
樹脂について知られる。しかし、この発明の発明
者らの知る限り、熱硬化性樹脂については、かか
る1次発泡粒は知られていない。これは、熱硬化
性樹脂の場合、一般に加熱して発泡と同時に硬化
をさせることで、発泡の形状を維持して発泡体を
得ており、この際、発泡硬化は短時間で最終まで
進み、部分発泡の状態で止めることが技術的に困
難であり、経済的に有利でないためと考えられ
る。また、熱硬化性樹脂発泡体の発泡粒を均一に
量産することも知られていない。 Conventionally, thermoplastic resins such as polystyrene resins, polyolefin resins, and copolymer resins thereof are known as primary foam particles having secondary foamability of plastic resins. However, as far as the inventors of the present invention know, such primary foam particles are not known for thermosetting resins. This is because thermosetting resins are generally heated and cured at the same time as foaming to maintain the foamed shape and obtain a foam. This is considered to be because it is technically difficult to stop the foaming in a partially foamed state, and it is not economically advantageous. Furthermore, it is not known to uniformly mass-produce foamed beads of thermosetting resin foam.
また一方、1次発泡粒としないで粉粒体のまま
で大型の生形体や複雑な形状の型の成形体を得よ
うとすると、粉粒体の充填量に対して型内の空隙
が大きいため、空隙の上方と下方とでは発泡密度
にばらつきが出やすい。一方、型の空隙が狭い形
状の型は発泡充填ムラができやすい欠点がある。 On the other hand, if you try to obtain a large green body or a molded body with a complicated shape from powder or granules without making them into primary foamed granules, the voids in the mold will be large compared to the amount of powder or granules filled. Therefore, the foam density tends to vary between above and below the void. On the other hand, molds with narrow voids have the disadvantage that foam filling tends to be uneven.
かかる事情のもとにおいて、熱硬化性樹脂の中
から、ノボラツク型フエノール樹脂初期縮合物が
主として粉末であることに着目し、種々検討した
結果、2次発泡性を有する熱硬化性樹脂の1次発
泡粒を簡便に作ることに成功し、かつ型成形にお
いて2次発泡しながら発泡粒が相互に熱融着する
ことを見出し、この発明を完成するに至つた。 Under these circumstances, we focused on the fact that among thermosetting resins, novolac-type phenolic resin initial condensates are mainly powders, and as a result of various studies, we found that primary condensates of thermosetting resins with secondary foamability They succeeded in easily producing foamed beads, and discovered that the foamed beads were thermally fused to each other during secondary foaming during molding, leading to the completion of this invention.
かくしてこの発明によれば、ノボラツク型フエ
ノール樹脂初期縮合物と所要量の分解型発泡剤及
び硬化剤とからなる組成物を部分的に発泡、硬化
させて2次発泡性を有するノボラツク型フエノー
ル樹脂発泡粒とし、次いでこれを型内で2次発泡
させ発泡粒を相互に熱融着させつつ成形して、ノ
ボラツク型フエノール樹脂発泡成形体を得ること
を特徴とするノボラツク型フエノール樹脂発泡成
形体の製造法が提供される。 Thus, according to the present invention, a novolak-type phenolic resin foam having secondary foaming properties is obtained by partially foaming and curing a composition comprising a novolak-type phenolic resin initial condensate and a required amount of a decomposable blowing agent and a curing agent. Production of a novolak-type phenolic resin foam molded article, which is characterized in that a novolak-type phenolic resin foam molded article is obtained by forming particles, then secondary foaming them in a mold, and molding the foamed particles while thermally fusing them to each other. law is provided.
この発明の主原料であるノボラツク型フエノー
ル樹脂初期縮合物とは、フエノール類とアルデヒ
ド類とを酸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ノボラツク型フエノー
ル樹脂と称せられ、硬化剤の存在下で更に重合が
進行しうるものを意味する。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、0−クレゾ
ール、p−クレゾールなどが含まれる。また、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、アセトアルデヒド、ヘキサメチレンテ
トラミン、フルフラール等がある。 The novolak type phenolic resin initial condensate, which is the main raw material of this invention, is a so-called novolak type phenolic resin known in the art, which is obtained by reacting phenols and aldehydes in the presence of an acidic catalyst, and is cured. It means that polymerization can proceed further in the presence of the agent. What are phenols?
In addition to phenol, 3,5-xylenol, m-
Cresol, 2,5-xylenol, 3,4-xylenol, 2,4-xylenol, 0-cresol, p-cresol and the like are included. Furthermore, examples of aldehydes include formaldehyde, paraformaldehyde, acetaldehyde, hexamethylenetetramine, and furfural.
これらの樹脂は、常温で粉末状である。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の縮合物である。 These resins are in powder form at room temperature. A preferred precondensate for use in this invention is a condensate of phenol and formaldehyde.
この発明における分解型発泡剤とは、加熱で分
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)などの無機分解型発泡剤が挙げら
れる。これらは全て粉末状である。 The decomposable blowing agent in this invention means inorganic and organic blowing agents that can be decomposed by heating to generate gas. Typical examples of these are N, N'-
Organic decomposable blowing agents such as dinitrosopentamethylenetetramine, benzenesulfonylhydrazide, azobisisobutyronitrile, azodicarbonamide, paratoluenesulfonylhydrazide, as well as sodium bicarbonate, ammonium carbonate, ammonium bicarbonate, ammonium nitrite, and azide compounds Examples include inorganic decomposition type blowing agents such as (eg CaN 6 ). All of these are in powder form.
この発明に用いる硬化剤は、加熱で分解し、ノ
ボラツク型フエノール樹脂初期縮合物と架橋反応
しうる化合物を意味する。このような化合物とし
ては、ホルムアルデヒドと同様にフエノール類と
の反応でフエノール樹脂形成に用いられる化合物
で通常粉末状のものがある。その具体例として
は、ヘキサメチレンテトラミン、パラホルムアル
デヒド、メチラール、ジオキソラン、トリオキサ
ン、テトラオキサン、トリメチロールホスフイ
ン、S−トリアジンなどが挙げられる。 The curing agent used in this invention means a compound that can be decomposed by heating and can undergo a crosslinking reaction with the novolak type phenolic resin initial condensate. Such compounds include, like formaldehyde, compounds that are used to form phenolic resins by reaction with phenols, and are usually in powder form. Specific examples include hexamethylenetetramine, paraformaldehyde, methylal, dioxolane, trioxane, tetraoxane, trimethylolphosphine, S-triazine, and the like.
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、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。 The amount of blowing agent added is determined mainly by considering the desired density of the final foam;
1 to 50 parts by weight per 100 parts by weight is appropriate, and 4
~8 parts by weight is preferred.
硬化剤の添加量は、一般に樹脂100重量部に対
し、1〜30重量部が適当であり、4〜15重量部が
好ましい。 The amount of the curing agent added is generally 1 to 30 parts by weight, preferably 4 to 15 parts by weight, per 100 parts by weight of the resin.
この発明の発泡粒を構成する組成物には、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。これらの充填剤は、樹脂100
重量部に対し50重量部以下であるのが好ましい。 The composition constituting the expanded granules of the present invention may contain small amounts of other various additives, such as fillers such as clay. These fillers are resin 100
It is preferable that the amount is 50 parts by weight or less.
上記組成物を、部分的に発泡、硬化さすに当つ
て、一般に造粒するのが好ましい。造粒は、たと
えばノボラツク型フエノール樹脂初期縮合物を60
〜90℃程度の温度で溶融し、この中に所要量の発
泡剤と所要量の硬化剤を添加し、さらに所望によ
り充填剤(クレイ、タルク、酸化亜鉛、炭酸カル
シウムなど)を加え、なるべく均一に混合し、次
いで固化させ、適当な大きさに粉砕することによ
つても行うことができる。上記の各原料の混合物
を100℃程度で短時間で軟化溶融させ、固化させ
て、粉砕してもよい。粉砕粒の大きさは、5〜10
メツシユを通過するものが一例である。 It is generally preferable to granulate the above composition before partially foaming and curing it. For granulation, for example, a novolak-type phenolic resin initial condensate is
Melt at a temperature of ~90℃, add the required amount of blowing agent and required amount of hardening agent, and add fillers (clay, talc, zinc oxide, calcium carbonate, etc.) if desired, to make it as uniform as possible. It can also be carried out by mixing, then solidifying, and pulverizing to an appropriate size. A mixture of the above raw materials may be softened and melted at about 100° C. for a short time, solidified, and then pulverized. The size of the crushed grains is 5 to 10
An example is one that passes through a mesh.
このようにして得られた組成物は、加熱により
軟化溶融し組成物の表面張力にて球状とされかつ
部分的に発泡硬化される。この処理は、発泡用の
適当な型内の底部に、非親和性で、かつ熱的に安
定な流動性の粉末物質の層を形成し、その層上又
は層中に前記の造粒組成物の適当量を載置又は混
合して行われる。この様な状態で、必要に応じ振
盪あるいは転動しつつ、適切な温度に加熱すると
組成物が互に融着せず、それぞれ独立したより真
球の発泡粒を得ることができる。これは樹脂組成
物の溶融物の表面張力が、非親和性でかつ熱的に
安定な粉末物質の表面張力よりも大であることに
より達せられるものと推定される。このことは、
この発明者らが見出した新規な知見である。ここ
で非親和性とは、載置又は混合時及びその加熱成
形時を通じて該組成物と実質的に化学反応を起さ
ずかつ該組成物と濡れ難い(実質的に濡れない)
物性を有することを意味する。より具体的には、
載置、混合又は加熱軟化時の組成物中に実質的に
融解や反応せずかつこの液形態の組成物の有する
表面張力より低い表面張力を有するものが適当で
ある。 The composition thus obtained is softened and melted by heating, shaped into a sphere by the surface tension of the composition, and partially foamed and hardened. This process involves forming a layer of a non-compatible, thermally stable, flowable powder material at the bottom of a suitable foaming mold, on or in which layer the granulated composition is added. This is done by placing or mixing an appropriate amount of In this state, if the composition is heated to an appropriate temperature while being shaken or rolled as necessary, the composition will not fuse with each other, and it is possible to obtain foamed beads that are independent and more spherical. It is presumed that this is achieved because the surface tension of the melt of the resin composition is greater than the surface tension of the non-compatible and thermally stable powder material. This means that
This is a new finding discovered by the inventors. Incompatibility here means that the composition does not substantially cause a chemical reaction with the composition and does not get wet easily (substantially does not get wet) with the composition during placement or mixing and during heat molding.
It means having physical properties. More specifically,
Suitable materials are those that do not substantially melt or react in the composition when placed, mixed or softened by heating, and have a surface tension lower than that of the liquid composition.
また熱的に安定とは組成物の成形温度下で軟化
や溶融等の物理的変化を実質的に生じないことを
意味する。 The term "thermally stable" means that physical changes such as softening or melting do not occur substantially at the molding temperature of the composition.
かような粉末としては、有機、無機を問わず
種々の物質を用いることができるが、通常、無機
粉末が好ましく、その具体例としては、クレイ、
タルク、酸化亜鉛、炭酸カルシウム、硫酸カルシ
ウム、カーボンブラツク、酸化アルミニウム、酸
化マグネシウム、酸化鉛等が挙げられる。ただ
し、これ以外にフツ素系やシリコン系の有機高分
子化合物の粉末も好ましい一例として挙げられ
る。なお、特に造粒せず、ノボラツク型フエノー
ル樹脂初期縮合物、発泡剤、硬化剤の混合物(粉
末状や不定形状)を上記の処理に用いてもよい。 As such powder, various substances can be used, whether organic or inorganic, but inorganic powder is usually preferable, and specific examples thereof include clay,
Examples include talc, zinc oxide, calcium carbonate, calcium sulfate, carbon black, aluminum oxide, magnesium oxide, lead oxide, and the like. However, in addition to these, powders of fluorine-based and silicon-based organic polymer compounds are also mentioned as preferred examples. Note that a mixture (in powder form or irregular shape) of a novolak type phenolic resin initial condensate, a foaming agent, and a curing agent may be used in the above treatment without granulation.
上記粉末物質の粒径としては0.005〜2000μmが
適当であり、5〜1000μmが好ましい。樹脂組成
物に対する非親和性でかつ熱的に安定な粉末の使
用量は、樹脂組成物の粒子が、溶融時に互いに融
着しない量を最低必要とする。例えば、組成物の
重量と等量以上が好ましい。この樹脂組成物を部
分的に発泡、硬化を起さす温度と時間は、樹脂組
成物中のノボラツク型フエノール樹脂初期縮合物
の融点(又は軟化点)、発泡剤及び硬化剤の添加
量とを考慮して決められるべきである。別の観点
からいうと、1次発泡粒は、硬化度1〜99%、好
ましくは10〜50%を有し、発泡剤の残存量1%以
上好ましくは10%以上であるように処理温度と時
間を調整されるべきである。 The particle size of the powder material is suitably 0.005 to 2000 μm, preferably 5 to 1000 μm. The amount of the thermally stable powder that has no affinity for the resin composition must be such that the particles of the resin composition do not fuse together when melted. For example, the amount is preferably equal to or greater than the weight of the composition. The temperature and time at which this resin composition is partially foamed and cured are determined by taking into account the melting point (or softening point) of the novolak-type phenolic resin initial condensate in the resin composition and the amounts of the foaming agent and curing agent added. It should be determined by From another point of view, the primary foamed grains have a hardening degree of 1 to 99%, preferably 10 to 50%, and the treatment temperature is adjusted such that the residual amount of the blowing agent is 1% or more, preferably 10% or more. Time should be adjusted.
ここで、1次発泡粒の硬化度は、1次発泡粒を
微粉化しエタノール中に浸漬したエタノール可溶
分の重量パーセントである。これらの適切な値の
一例は実施例で具体的に示されるが、これを参照
して適宜選択採用される。 Here, the degree of hardening of the primary foamed grains is the weight percent of the ethanol-soluble content obtained by pulverizing the primary foamed grains and immersing them in ethanol. Examples of these appropriate values are specifically shown in the examples, and are appropriately selected and adopted with reference to the examples.
この発明の一次発泡粒は、通常球形又はそれに
類似の形状を有し、その直径は1ミリ程度から20
ミリ程度のものがある。しかし、この大きさは、
特に限定されるものではない。 The primary foam beads of the present invention usually have a spherical shape or a similar shape, and the diameter ranges from about 1 mm to 20 mm.
Some are about millimeters in size. However, this size is
It is not particularly limited.
1次発泡粒を用途により得ようとする形状の成
形金型等に充填し、通常の方法により発泡成形さ
れる。なお、型材質としては、成形時の温度(通
常90℃以上)及び成形発泡圧力による融解、破
損、変形しないもの、またタイプとして閉鎖タイ
プで型内の空気の排出できるものであることが望
まれることはいうまでもない。成形金型への充填
量は、カサ充填率で25%以上、好ましくは70%以
上である。成形温度は、通常90℃〜170℃であり、
成形時間は温度に関連して決められるが通常1時
間以内である。 The primary foam particles are filled into a mold or the like having the desired shape depending on the intended use, and foam molding is carried out by a conventional method. The mold material should not melt, break, or deform due to the temperature during molding (usually 90°C or higher) and the foaming pressure, and should also be a closed type that allows the air inside the mold to be exhausted. Needless to say. The amount filled into the mold is 25% or more, preferably 70% or more in terms of bulk filling rate. Molding temperature is usually 90℃~170℃,
The molding time is determined in relation to the temperature, but is usually within 1 hour.
このようにして得られたこの発明のフエノール
発泡粒の2次発泡の特性を生かし得られる発泡成
形体は、大型の成形体や複雑な形状の型に対して
均一な発泡密度のものが容易に得られる。その最
終発泡成形体は最高が60倍程度のものまで得られ
る。又、この得られた発泡成形体に於いて各発泡
粒の相互の熱による接着は強く、破壊はこの接着
面に沿うことは少なく各発泡粒の断面にまたがる
ものである。 The foam molded product obtained in this manner by taking advantage of the secondary foaming characteristics of the phenol foam particles of the present invention can be easily produced with a uniform foam density for large molded products or molds with complex shapes. can get. The final foamed molded product can be up to about 60 times larger. In addition, in the obtained foamed molded product, the foam particles are strongly bonded to each other by heat, and the fractures rarely occur along the bonded surfaces, but span the cross section of each foam particle.
次に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。 Next, the present invention will be described with reference to Examples, but the present invention is not limited thereto.
実施例 1
ノボラツク型フエノール−ホルムアルデヒド樹
脂粉末100重量部に対して、5重量部の発泡剤ジ
ニトロソペンタメチレンテトラミン、10重量部の
硬化剤ヘキサメチレンテトラミンを加えた粉状の
樹脂混合物を調整した。なお、この樹脂組成物は
100メツシユ残0.5%の粉体で、融点は81℃であ
り、150℃のゲル化時間は76秒であつた。次いで、
この樹脂混合物粉末を100℃の湯浴上で軟化溶融
させた後冷却し固化させ粒径7〜9メツシユに粉
砕し、顆粒状の樹脂組成物を得た。Example 1 A powdered resin mixture was prepared by adding 5 parts by weight of a blowing agent dinitrosopentamethylenetetramine and 10 parts by weight of a hardening agent hexamethylenetetramine to 100 parts by weight of a novolac type phenol-formaldehyde resin powder. In addition, this resin composition
The powder had a 100 mesh residue of 0.5%, the melting point was 81°C, and the gelation time at 150°C was 76 seconds. Then,
This resin mixture powder was softened and melted on a hot water bath at 100°C, then cooled and solidified, and pulverized to a particle size of 7 to 9 mesh to obtain a granular resin composition.
この顆粒状の樹脂混合物30gを約1000cm2の厚さ
2〜3mmの焼石膏粉末層上に置き、120℃の熱風
循環式恒温槽で10分間発泡硬化させ、発泡粒を得
た。 30 g of this granular resin mixture was placed on an approximately 1000 cm 2 layer of calcined gypsum powder with a thickness of 2 to 3 mm, and foamed and hardened in a hot air circulation thermostat at 120° C. for 10 minutes to obtain foamed granules.
得られた発泡粒は、黄色で粒表面に表皮を有
し、緻密な気泡構造を有する粒径2.5〜4.5mmの球
状のものであり、カサ比重0.21であつた。因にこ
の発泡粒を微粉化して1.0gを20mlのエチルアル
コール(試薬特級)中に25℃で20時間浸漬し、
過してエチルアルコール可溶分を測定した結果、
88.3重量パーセントであつた。 The obtained foamed particles were yellow in color, had a skin on the particle surface, had a dense cell structure, were spherical with a particle size of 2.5 to 4.5 mm, and had a bulk specific gravity of 0.21. Incidentally, 1.0 g of this foamed granule was pulverized and immersed in 20 ml of ethyl alcohol (reagent grade) at 25°C for 20 hours.
As a result of measuring the ethyl alcohol soluble content by
It was 88.3% by weight.
次いで、この得られた発泡粒を粒径3.0〜4.0mm
を篩分し、木製型内にカサ容積で100%充填し、
蓋を閉じて160℃の熱風循環式恒温槽内に45分間
保持した。型を恒温槽から出し、発泡体を型から
取り出した。 Next, the obtained foamed particles are made into particles with a particle size of 3.0 to 4.0 mm.
Sieve and fill 100% of the volume into a wooden mold.
The lid was closed and the mixture was kept in a hot air circulation constant temperature bath at 160°C for 45 minutes. The mold was removed from the thermostatic oven and the foam was removed from the mold.
この得られた発泡体は、1次球状発泡粒が、さ
らに発泡し、その空隙がすべて発泡層で充填され
たもので1次発泡球間の融着も極めて良好なもの
であり、若干茶色味を帯びた比重0.21の緻密な気
泡構造を有する成形体であつた。 The obtained foam is made by further foaming the primary spherical foam particles, and all the voids are filled with the foam layer, and the fusion between the primary foam beads is also very good, and it has a slightly brownish color. The molded product had a dense cell structure with a specific gravity of 0.21.
実施例 2
実施例1と全く同様の樹脂配合混合物を同様の
処方で7〜9メツシユの樹脂配合混合物顆粒に調
整した。Example 2 The same resin mixture as in Example 1 was prepared into 7 to 9 mesh resin mixture granules using the same recipe.
この顆粒状の樹脂混合物を焼石膏粉末を敷きつ
めた型上に置き、120℃の熱風循環式恒温槽内で
30分間発泡硬化させ発泡粒を得た。 This granular resin mixture was placed on a mold lined with calcined gypsum powder, and placed in a hot air circulation thermostat at 120°C.
The mixture was foamed and cured for 30 minutes to obtain foamed beads.
得られた発泡粒は、黄色で表面に表皮を有し、
緻密な気泡構造を有する粒径3.5〜6.0mmの球状の
ものであり、カサ比重0.076であつた。又、この
気泡粒を微粉化し、エチルアルコール中に浸漬し
て求めたエチルアルコール可溶分は、44.7重量パ
ーセントであつた。 The foamed granules obtained are yellow in color and have a skin on the surface.
The particles were spherical with a particle size of 3.5 to 6.0 mm and had a dense cell structure, and a bulk specific gravity of 0.076. Further, the ethyl alcohol soluble content, which was determined by pulverizing the bubble particles and immersing them in ethyl alcohol, was 44.7% by weight.
次いで、この得られた発泡粒の粒径3.0〜4.0mm
を篩分し、木製型内にカサ容積で100%充填し、
蓋を閉じて160℃の熱風循環式恒温槽内に45分間
保持した。型を恒温槽から出し、発泡体を型から
取りだした。 Next, the particle size of the obtained expanded particles is 3.0 to 4.0 mm.
Sieve and fill 100% of the volume into a wooden mold.
The lid was closed and the mixture was kept in a hot air circulation constant temperature bath at 160°C for 45 minutes. The mold was removed from the thermostatic oven and the foam was removed from the mold.
この得られた発泡体は、1次球状発泡体がさら
に発泡し、その空隙がすべて発泡層で充填された
もので1次発泡球間の融着も極めて良好なもので
あり、若干茶色味を帯びた比重0.076の緻密な気
泡構造を有する成形体であつた。 The obtained foam is a product in which the primary spherical foam is further foamed, and all the voids are filled with the foam layer, and the fusion between the primary foamed spheres is also very good, and it has a slightly brownish color. The molded product had a dense cell structure with a specific gravity of 0.076.
実施例 3
実施例1と全く同様の樹脂配合混合物を同様の
処方で7〜9メツシユの樹脂配合混合物顆粒に調
整した。Example 3 The same resin mixture as in Example 1 was prepared into 7 to 9 mesh resin mixture granules using the same recipe.
この顆粒状の樹脂混合物を焼石膏粉末を敷きつ
めた型上に置き、140℃の熱風循環式恒温槽で10
分間発泡硬化させ発泡粒を得た。 This granular resin mixture was placed on a mold lined with calcined gypsum powder, and placed in a hot air circulation constant temperature bath at 140℃ for 10 minutes.
The mixture was foamed and cured for a minute to obtain expanded beads.
得られた発泡粒は、黄色で表面に表皮を有し、
緻密な気泡構造を有する粒径3.5〜5.2mmの球状の
ものであり、カサ比重0.070であつた。又、この
発泡粒を微粉化し、エチルアルコール中に浸漬し
て求めたエチルアルコール可溶分は、52.0重量パ
ーセントであつた。 The foamed granules obtained are yellow in color and have a skin on the surface.
The particles were spherical with a particle size of 3.5 to 5.2 mm and had a dense cell structure, and a bulk specific gravity of 0.070. Further, the ethyl alcohol soluble content, which was determined by pulverizing the expanded particles and immersing them in ethyl alcohol, was 52.0% by weight.
次いでこの得られた発泡粒の粒径3.0〜4.0mmを
篩分し、木製型内にカサ容積で100%充填し、蓋
を閉じて160℃の熱風循環式恒温槽内に45分間保
持した。型を恒温槽から出し、発泡体を型から取
りだした。 Next, the resulting foamed particles were sieved to a particle size of 3.0 to 4.0 mm, filled 100% of the bulk volume into a wooden mold, closed with a lid, and held in a hot air circulation constant temperature bath at 160° C. for 45 minutes. The mold was removed from the thermostatic oven and the foam was removed from the mold.
この得られた発泡体は、1次球状発泡体が、さ
らに発泡し、その空隙の83%が発泡層で充填され
たもので1次発泡球間の融着も極めて良好なもの
であり、若干茶色味を帯びたカサ比重0.070の緻
密な気泡構造を有する成形体であつた。 In this obtained foam, the primary spherical foam was further foamed, and 83% of the voids were filled with the foam layer, and the fusion between the primary foamed spheres was also extremely good. It was a brownish molded product having a dense cell structure with a bulk specific gravity of 0.070.
実施例 4
実施例1と全く同様の樹脂配合混合物を同様の
処方で7〜9メツシユの樹脂配合混合物顆粒に調
整した。Example 4 The same resin mixture as in Example 1 was prepared into 7 to 9 mesh resin mixture granules using the same recipe.
この顆粒状の樹脂混合物を焼石膏粉末を敷きつ
めた型上に置き、130℃の熱風循環式恒温槽で20
分間発泡硬化させ発泡粒を得た。 This granular resin mixture was placed on a mold lined with calcined gypsum powder, and placed in a hot air circulation constant temperature bath at 130℃ for 20 minutes.
The mixture was foamed and cured for a minute to obtain expanded beads.
得られた発泡粒は、黄色で表面に表皮を有し、
緻密な気泡構造を有する粒径3.5〜6.5mmの球状の
ものであり、カサ比重0.066であつた。又、この
気泡粒を微粉化し、エチルアルコール中に浸漬し
て求めたエチルアルコール中に浸漬して求めたエ
チルアルコール可溶分は、49.2重量パーセントで
あつた。 The foamed granules obtained are yellow in color and have a skin on the surface.
The particles were spherical with a particle size of 3.5 to 6.5 mm and had a dense cell structure, and a bulk specific gravity of 0.066. Further, the ethyl alcohol soluble content, which was determined by pulverizing the bubble particles and immersing them in ethyl alcohol, was 49.2% by weight.
次いで、この得られた発泡粒の粒径3.0〜4.0mm
を篩分し、木製型内にカサ容積で100%充填し、
蓋を閉じて160℃の熱風循環式恒温槽内に45分間
保持した。型を恒温槽から出し、発泡体を型から
取りだした。 Next, the particle size of the obtained expanded particles is 3.0 to 4.0 mm.
Sieve and fill 100% of the volume into a wooden mold.
The lid was closed and the mixture was kept in a hot air circulation constant temperature bath at 160°C for 45 minutes. The mold was removed from the thermostatic oven and the foam was removed from the mold.
この得られた発泡体は、1次球状発泡体が、さ
らに発泡し、その空隙の70%が発泡層で充填され
たもので1次発泡球間の融着も極めて良好なもの
であり、若干茶色味を帯びたカサ比重0.066の緻
密な気泡構造を有する成形体であつた。 In this obtained foam, the primary spherical foam is further foamed, and 70% of the voids are filled with a foam layer, and the fusion between the primary foamed spheres is also very good. It was a brownish molded product having a dense cell structure with a bulk specific gravity of 0.066.
実施例 5
実施例1と全く同様の樹脂配合混合物を同様の
処方で7〜9メツシユの樹脂配合混合物顆粒に調
整した。Example 5 The same resin mixture as in Example 1 was prepared into 7 to 9 mesh resin mixture granules using the same recipe.
この顆粒状の樹脂混合物を焼石膏粉末を敷きつ
めた型上に置き、160℃の熱風循環式恒温槽で10
分間発泡硬化させ発泡粒を得た。 This granular resin mixture was placed on a mold lined with calcined gypsum powder, and placed in a hot air circulation constant temperature bath at 160℃ for 10 minutes.
The mixture was foamed and cured for a minute to obtain expanded beads.
得られた発泡粒は、若千茶色味を帯び表面に表
皮を有し、緻密な気泡構造を有する粒径4.5〜6.5
mmの球状のものであり、カサ比重0.052であつた。
又、この発泡体を微粉化し、エチルアルコール中
に浸漬して求めたエチルアルコール可溶分は、
9.6重量パーセントであつた。 The obtained foamed particles have a young brownish color, have a skin on the surface, and have a dense cell structure with a particle size of 4.5 to 6.5.
It had a spherical shape with a bulk specific gravity of 0.052.
In addition, the ethyl alcohol soluble content was determined by pulverizing this foam and immersing it in ethyl alcohol.
It was 9.6% by weight.
次いで、この得られた発泡粒の粒径3.0〜4.0mm
を篩分し、木製型内にカサ容積で100%充填し、
蓋を閉じて160℃の熱風循環式恒温槽内に45分間
保持した。型を恒温槽から出し、発泡体を型から
取りだした。 Next, the particle size of the obtained expanded particles is 3.0 to 4.0 mm.
Sieve and fill 100% of the volume into a wooden mold.
The lid was closed and the mixture was kept in a hot air circulation constant temperature bath at 160°C for 45 minutes. The mold was removed from the thermostatic oven and the foam was removed from the mold.
この得られた発泡体は、1次球状発泡体が、さ
らに発泡し、その空隙の23%が発泡層で充填され
たもので1次発泡球間に点状に融着し合つた、若
干茶色味を帯びた比重0.052の緻密な気泡構造を
有する成形体であつた。 The resulting foam is a slightly brown color in which the primary spherical foam is further expanded and 23% of the voids are filled with a foam layer, with dots fused between the primary foam spheres. The molded product had a dense cell structure with a specific gravity of 0.052 and was flavorful.
実施例 6
実施例1と全く同様の樹脂配合混合物を同様の
処方で7〜9メツシユの樹脂配合混合物顆粒に調
整した。Example 6 The same resin mixture as in Example 1 was prepared into 7 to 9 mesh resin mixture granules using the same recipe.
この顆粒状の樹脂混合物を焼石膏粉末を敷きつ
めた型上に置き、160℃の熱風循環式恒温槽で30
分間発泡硬化させ発泡粒を得た。 This granular resin mixture was placed on a mold lined with calcined gypsum powder, and placed in a hot air circulation constant temperature bath at 160℃ for 30 minutes.
The mixture was foamed and cured for a minute to obtain expanded beads.
得られた発泡粒は、黄色で表面に表皮を有し、
緻密な気泡構造を有する粒径5.0〜7.0mmの球状の
ものであり、カサ比重0.044であつた。又、この
気泡粒を微粉化し、エチルアルコール中に浸漬し
て求めたエチルアルコール可溶分は、1.2重量パ
ーセントであつた。 The foamed granules obtained are yellow in color and have a skin on the surface.
The particles were spherical with a particle size of 5.0 to 7.0 mm and had a dense cell structure, and a bulk specific gravity of 0.044. Further, the ethyl alcohol soluble content, which was determined by pulverizing the bubble particles and immersing them in ethyl alcohol, was 1.2% by weight.
次いで、この得られた発泡粒の粒径3.0〜4.0mm
を篩分し、木製型内にカサ容積で100%充填し、
蓋を閉じて160℃の熱風循環式恒温槽内に45分間
保持した。型を恒温槽から出し、発泡体を型から
取りだした。 Next, the particle size of the obtained expanded particles is 3.0 to 4.0 mm.
Sieve and fill 100% of the volume into a wooden mold.
The lid was closed and the mixture was kept in a hot air circulation constant temperature bath at 160°C for 45 minutes. The mold was removed from the thermostatic oven and the foam was removed from the mold.
得られた発泡体は、発泡性が少なく発泡粒が全
面的には融着しないが、一応の成形体は得られ
た。 Although the obtained foam had little foamability and the foamed particles were not completely fused, a reasonable molded product was obtained.
Claims (1)
要量の分解型発泡剤及び硬化剤とからなる組成物
を部分的に発泡、硬化させて2次発泡性を有する
ノボラツク型フエノール樹脂発泡粒とし、次いで
これを型内で2次発泡させ発泡粒を相互に熱融着
させつつ成形して、ノボラツク型フエノール樹脂
発泡成形体を得ることを特徴とするノボラツク型
フエノール樹脂発泡成形体の製造法。 2 組成物が部分的に発泡、硬化させる前に造粒
される特許請求の範囲第1項記載の製造法。[Claims] 1. Novolak type phenolic resin foaming having secondary foamability by partially foaming and curing a composition comprising a novolak type phenolic resin initial condensate and required amounts of a decomposable blowing agent and a curing agent. Production of a novolak-type phenolic resin foam molded article, which is characterized in that a novolak-type phenolic resin foam molded article is obtained by forming particles, then secondary foaming them in a mold, and molding the foamed particles while thermally fusing them to each other. Law. 2. The manufacturing method according to claim 1, wherein the composition is granulated before being partially foamed and cured.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59005274A JPS60149439A (en) | 1984-01-14 | 1984-01-14 | Manufacture of expanded novolak type phenol resin molding |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59005274A JPS60149439A (en) | 1984-01-14 | 1984-01-14 | Manufacture of expanded novolak type phenol resin molding |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60149439A JPS60149439A (en) | 1985-08-06 |
| JPH0345702B2 true JPH0345702B2 (en) | 1991-07-11 |
Family
ID=11606652
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59005274A Granted JPS60149439A (en) | 1984-01-14 | 1984-01-14 | Manufacture of expanded novolak type phenol resin molding |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60149439A (en) |
-
1984
- 1984-01-14 JP JP59005274A patent/JPS60149439A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60149439A (en) | 1985-08-06 |
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