JP2005120337A - Acid-curable phenolic resin foam and its manufacturing method - Google Patents

Acid-curable phenolic resin foam and its manufacturing method Download PDF

Info

Publication number
JP2005120337A
JP2005120337A JP2004111490A JP2004111490A JP2005120337A JP 2005120337 A JP2005120337 A JP 2005120337A JP 2004111490 A JP2004111490 A JP 2004111490A JP 2004111490 A JP2004111490 A JP 2004111490A JP 2005120337 A JP2005120337 A JP 2005120337A
Authority
JP
Japan
Prior art keywords
phenolic resin
acid
weight
foam
parts
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.)
Pending
Application number
JP2004111490A
Other languages
Japanese (ja)
Inventor
Masato Nakasone
正人 仲宗根
Hiroshi Uchida
博 内田
Yukimasa Hase
行正 長谷
Katsuaki Tanaka
克明 田中
Fujio Someya
不二夫 染谷
Masaya Kishimoto
昌也 岸本
Kenji Moribe
鎌志 森部
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.)
J Chemical Inc
Original Assignee
J Chemical Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by J Chemical Inc filed Critical J Chemical Inc
Priority to JP2004111490A priority Critical patent/JP2005120337A/en
Publication of JP2005120337A publication Critical patent/JP2005120337A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an acid-curable phenolic resin foam that is well cured even when using a neutralizer to control a drop in pH of the foam during manufacturing the phenolic resin foam, has superior resistance to water absorption, adhesion to a facing material and mechanical strength, and does not cause corrosion and discoloration in the facing material and a reinforcing member, and its manufacturing method. <P>SOLUTION: This manufacturing method of the acid-curable phenolic resin foam is characterized in that, when manufacturing the phenolic resin foam by formulating a foaming agent and an acid curing agent to a phenolic resin composition followed by foaming and curing it, pH change in the composition by adding the acid curing agent to the phenolic resin composition remains in a range of value equal to and lower than that represented by a formula: Y=0.0034X + 2.167. The acid curing agent is consumed with time by neutralization of the acid neutralizer and a filler resulting in pH change, so that, according the formula, a relationship between an elapsed time (X: 0≤X≤120 s) after addition of the acid curing agent to the phenolic resin composition which is adjusted at a fixed temperature and the pH value (Y) is measured at a fixed condition. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、フェノール系樹脂組成物に発泡剤、酸性硬化剤を配合し、発泡、硬化させてフェノール系樹脂発泡体を製造するに際して、フェノール系樹脂組成物に酸性硬化剤を添加したのちの該組成物のpH変化を特定範囲に調整することによって、耐吸水性、面材接着性、機械的強度などに優れ、かつ金属の腐食や変色のない酸性硬化型フェノール系樹脂発泡体を製造する方法及びその発泡体に関するものである。   The present invention includes adding a foaming agent and an acidic curing agent to a phenolic resin composition, and foaming and curing the phenolic resin foam to produce a phenolic resin foam, and then adding the acidic curing agent to the phenolic resin composition. A method for producing an acid curable phenolic resin foam excellent in water absorption resistance, face material adhesion, mechanical strength, etc. and having no corrosion or discoloration of metals by adjusting the pH change of the composition to a specific range And its foam.

酸性硬化型フェノール系樹脂発泡体は、一般にフェノール系樹脂に、希釈剤、可塑剤、充填剤、酸中和剤、硫酸塩などの反応調整剤や整泡剤、分散剤、減粘剤などの界面活性剤、硬化促進剤、遅延剤、着色剤、難燃剤などを添加してなるフェノール系樹脂組成物に発泡剤、酸性硬化剤などを加え、発泡、加熱硬化させて製造される。フェノール系樹脂発泡体は、その難燃性が高く評価され、間仕切りパネル、クリーンルーム用パネルなどの内壁材、金属サイディングなどの外壁材、天井材、屋根下地材、床下断熱材、屋上断熱材、防火扉などの建築材料、メタン、プロパン、ブタンなどの貯蔵タンクのプラント分野、タンク、パイプ配管などの保冷保温用、冷凍冷蔵倉庫などの保冷材等に幅広く使用されている。   Acidic curable phenolic resin foams are generally used in phenolic resins such as diluents, plasticizers, fillers, acid neutralizers, sulfates and other reaction modifiers, foam stabilizers, dispersants, thickeners, etc. It is produced by adding a foaming agent, an acidic curing agent, etc. to a phenolic resin composition obtained by adding a surfactant, a curing accelerator, a retarder, a colorant, a flame retardant, and the like, followed by foaming and heat curing. Phenolic resin foams are highly evaluated for their flame retardancy. Interior wall materials such as partition panels and clean room panels, outer wall materials such as metal siding, ceiling materials, roof base materials, underfloor insulation materials, roof insulation materials, and fire prevention It is widely used for building materials such as doors, storage tank plants such as methane, propane, and butane, cold storage and warming for tanks and pipes, and cold storage for freezers and refrigerators.

しかし、フェノール系樹脂発泡体を製造する際には、生産性を上げるため多量の酸性硬化剤が使用されている。その結果、発泡、硬化後にフェノール系樹脂発泡体中に遊離の酸が多く残存し、発泡体のpH値を酸性側に引き下げ、発泡体を形成しているセル膜を経日的に劣化させたり、破壊を促進したりする。これにより、耐吸水性や機械的強度が低下し、面材の金属表面や樹脂塗膜を腐食するため断熱材製品としての寿命が著しく縮まるという大きな問題があった。   However, when producing a phenolic resin foam, a large amount of an acidic curing agent is used to increase productivity. As a result, a lot of free acid remains in the phenolic resin foam after foaming and curing, the pH value of the foam is lowered to the acidic side, and the cell membrane forming the foam deteriorates over time. , Or promote destruction. As a result, the water absorption resistance and mechanical strength are lowered, and the metal surface of the face material and the resin coating film are corroded.

これらの問題点を解決するためにホルムアルデヒド系樹脂組成物の中でも酸性硬化剤を多く必要とするフェノール系樹脂発泡組成物に、腐蝕防止剤として亜鉛、アルミニウムなどの金属酸化物又は金属粉末を用いる方法(特許文献1及び2)、中和剤としてIIA族の
炭酸塩(特許文献3)及び粒径が10〜500μmのIA、IIA族の炭酸塩を用いる方法
(特許文献4)、炭酸カルシウム、炭酸バリウム、酸化カルシウム、酸化バリウムなどの塩基性粉末物質やタルク、マイカ、パーライト粒、シラスバルーンなどを用いる方法(特許文献5)などが開示されている。
In order to solve these problems, a method of using a metal oxide such as zinc or aluminum or a metal powder as a corrosion inhibitor in a phenolic resin foam composition that requires a large amount of an acidic curing agent among formaldehyde resin compositions (Patent Documents 1 and 2), Group IIA carbonate (Patent Document 3) and a method using IA having a particle size of 10 to 500 μm and Group IIA carbonate (Patent Document 4), calcium carbonate, carbonate A method using a basic powder substance such as barium, calcium oxide or barium oxide, talc, mica, pearlite particles, shirasu balloon or the like (Patent Document 5) is disclosed.

しかし、特許文献1及び2の方法では、フェノール系樹脂と均一に混合することが難しいため、沈殿、凝集などを起こし、フェノール系樹脂の粘度を増粘させたり、発泡注入機の配管を詰まらせたりして生産性を大幅に低下させる。また発泡工程以前に酸性硬化剤と反応するため、フォームを形成するセルが不均一となり耐吸水性、脆性、機械的強度などが低下する。また、フェノール系樹脂中に溶解することなく分散していることにより、中和剤周辺部のみしか中和できないため、フェノール系樹脂発泡体に残留する遊離酸を十分に中和しがたい。そのため、耐腐食性を解決するのには不十分で品質の不安定なフェノール系樹脂発泡体しか得られない。   However, in the methods of Patent Documents 1 and 2, it is difficult to uniformly mix with the phenolic resin, causing precipitation, aggregation, etc., increasing the viscosity of the phenolic resin, or clogging the piping of the foam injection machine. Or drastically reduce productivity. Moreover, since it reacts with the acidic curing agent before the foaming step, the cells forming the foam become non-uniform, resulting in a decrease in water absorption resistance, brittleness, mechanical strength, and the like. Moreover, since it disperse | distributes without dissolving in a phenol-type resin, only the periphery of a neutralizing agent can be neutralized, Therefore It is difficult to fully neutralize the free acid which remains in a phenol-type resin foam. Therefore, only a phenolic resin foam that is insufficient to solve the corrosion resistance and has unstable quality can be obtained.

特許文献3、4の方法では、炭酸が気体となって離脱することにより充分な中和効果が得られるものの、酸性硬化剤と炭酸塩が接触した際、瞬時にpHの上昇が起こり、発泡が急激となって均一な密度調整が困難となり、フォーム(発泡体)にボイドが多数発生するため熱伝導率や機械的強度の低下が著しく実用的でない。   In the methods of Patent Documents 3 and 4, a sufficient neutralization effect is obtained by the separation of carbonic acid as a gas. However, when the acidic curing agent and the carbonate are brought into contact with each other, the pH rises instantaneously and foaming occurs. It becomes abrupt and uniform density adjustment becomes difficult, and many voids are generated in the foam (foam), so the decrease in thermal conductivity and mechanical strength is extremely impractical.

こうした問題を解決するために、メタホウ酸バリウムを配合する方法(特許文献5)が提案されているが、この方法ではフォームが脆くなり耐吸水性が悪化したり、燃焼時に爆裂が大きくフェノール系樹脂発泡体の最大の長所である難燃性が低下する欠点がある。   In order to solve these problems, a method of blending barium metaborate (Patent Document 5) has been proposed. However, this method makes the foam brittle and the water absorption resistance is deteriorated, or the explosion during combustion is large and the phenolic resin. There is a drawback that flame retardancy, which is the greatest advantage of the foam, is reduced.

また、発泡剤として炭酸塩を用い、炭酸塩の分解による発泡及び硬化速度を調整緩和するのに酸性硬化剤としてナフタレンスルホン酸ホルマリン縮合物とアリールスルホン酸の併用比を変えて使用する方法(特許文献6)及びナフタレンスルホン酸ホルマリン縮合物とアリールスルホン酸の混合酸にギ酸、リン酸及び乳酸を配合して使用する方法(特許文献7)が開示されているが、酸性硬化剤の使用量が多いためフォームを形成するセルが脆くなり、機械的強度や耐吸水性が低下する。また、通常に良く使用されるフェノールスルホン酸ではフェノール樹脂と混合した際、瞬時に発泡が起こり未硬化でボイドの多い発泡体しか得られない。このことは特許文献7の比較例にも記載されている。   Also, using carbonate as the foaming agent, and changing the combined ratio of naphthalene sulfonic acid formalin condensate and aryl sulfonic acid as acidic curing agent to adjust and ease the foaming and curing rate by decomposition of carbonate (patent) Document 6) and a method of using formic acid, phosphoric acid and lactic acid in a mixed acid of naphthalene sulfonic acid formalin condensate and aryl sulfonic acid are disclosed (Patent Document 7), but the amount of acidic curing agent used is Since there are many, the cell which forms foam becomes weak, and mechanical strength and water absorption resistance fall. Further, in the case of phenolsulfonic acid which is usually used well, when it is mixed with a phenol resin, foaming occurs instantaneously and only an uncured foam with many voids can be obtained. This is also described in a comparative example of Patent Document 7.

フェノール系樹脂へ分散性の悪い金属酸化物や金属粉末などの酸中和剤を使用すると、発泡注入機等の配管詰まりを起こしたり、また、酸性硬化剤、発泡剤との混合性が悪く作業性が低下する。一方、酸性硬化剤を多量に使用すると遊離酸によりフォーム特性が低下する。また、炭酸塩を酸中和剤に使用すると、酸性硬化剤との接触により炭酸塩の分解に伴う急激な発泡速度を抑制できずに作業性を悪化させるなどの問題が発生する。故に作業性や生産性を低下させずに、耐腐食性、耐吸水性、機械的強度、面材接着性などに優れた酸性硬化型フェノール系樹脂発体の開発が強く求められていた。
特公平4−11583号公報 特公昭62−25689号公報 特開昭58−154734号公報 特開昭59−152931号公報 特開昭63−175042号公報 特開平7−173315号公報 特開平7−188446号公報
If an acid neutralizer such as a metal oxide or metal powder with poor dispersibility is used in a phenolic resin, it may cause clogging of piping such as a foam injection machine, or work with poor mixing with an acidic curing agent or foaming agent. Sex is reduced. On the other hand, if an acidic curing agent is used in a large amount, the foam characteristics are reduced by the free acid. In addition, when carbonate is used as the acid neutralizer, problems such as deterioration of workability occur due to the rapid foaming rate associated with the decomposition of the carbonate due to contact with the acidic curing agent. Therefore, there has been a strong demand for the development of an acid curable phenolic resin foam excellent in corrosion resistance, water absorption resistance, mechanical strength, face material adhesion, and the like, without reducing workability and productivity.
Japanese Examined Patent Publication No. 4-11583 Japanese Examined Patent Publication No. 62-25689 JP 58-154734 A JP 59-152931 A JP 63-175042 A JP 7-173315 A JP-A-7-188446

本発明は、酸性硬化型フェノール系樹脂発泡体製造における上記の問題点に鑑み、表面に面材、特に鉄、ステンレス、アルミ、亜鉛などの金属板材を使用し、あるいは当該金属板材を補強材として使用したフェノール系樹脂発泡体を製造する際に、フォームpHの低下を抑制するため酸中和剤を使用した場合においてもフォームの硬化が十分に進み、耐腐食性、耐吸水性、面材接着性、機械的強度などに優れ、面材、補強材などの腐食や変色のない酸性硬化型フェノール系樹脂発泡体及びその製造方法を提供することを課題とする。   In view of the above-described problems in the production of an acid curable phenolic resin foam, the present invention uses a face plate, particularly a metal plate material such as iron, stainless steel, aluminum, and zinc on the surface, or uses the metal plate material as a reinforcing material. When the used phenolic resin foam is produced, even when an acid neutralizer is used to suppress foam pH reduction, the foam is sufficiently cured, resulting in corrosion resistance, water absorption resistance, and face material adhesion. It is an object of the present invention to provide an acidic curable phenolic resin foam excellent in properties, mechanical strength, etc., and free from corrosion and discoloration of face materials and reinforcing materials, and a method for producing the same.

本発明者らは上記課題を解決するために鋭意検討した結果、フェノール系樹脂組成物に発泡剤、酸性硬化剤を配合し、発泡、硬化させてフェノール系樹脂発泡体を製造するに際して、特に酸中和剤として炭酸塩を使用した場合に炭酸塩の分解抑制剤として硫酸塩をフェノール系樹脂組成物に使用することにより、酸性硬化剤を添加しても炭酸塩の分解に伴う急激な発泡、pHの上昇を抑制することを可能とし、かつフェノール系樹脂組成物に酸性硬化剤を添加した該組成物のpH変化の範囲を限定することにより、作業性及び生産性の低下や意匠性を損なうことなく、耐腐食性、機械的強度、耐吸水性などに優れた酸性硬化型フェノール系樹脂発泡体を製造出来ることを見出し本発明を完成させた。   As a result of intensive studies to solve the above problems, the present inventors have formulated a phenolic resin foam by mixing a foaming agent and an acidic curing agent with a phenolic resin composition, and then foaming and curing it. When carbonate is used as a neutralizer, by using sulfate as a carbonate decomposition inhibitor in the phenolic resin composition, rapid foaming associated with decomposition of carbonate even when an acidic curing agent is added, It is possible to suppress an increase in pH and limit the range of pH change of the composition obtained by adding an acidic curing agent to a phenolic resin composition, thereby impairing workability, productivity reduction and designability. The present invention was completed by finding that an acid-curable phenolic resin foam excellent in corrosion resistance, mechanical strength, water absorption resistance and the like can be produced.

すなわち、本発明は、フェノール系樹脂組成物に発泡剤、酸性硬化剤を配合し、発泡、硬化させてフェノール系樹脂発泡体を製造するに際して、フェノール系樹脂組成物に酸性硬化剤を添加した該組成物のpH値が、式: Y=0.0034X+2.167(式1)
で示される値以下の範囲にあることを特徴とする酸性硬化型フェノール系樹脂発泡体の製造方法である。
上記式1は、フェノール系樹脂組成物中の酸中和剤、充填剤などにより酸性硬化剤が経時的に消費されることで起こるpH変化を、一定温度に調整したフェノール系樹脂組成物に酸性硬化剤を添加した後の経過時間(X)(単位:秒)と、pH値(Y)との関係を一定条件で測定したものである。
具体的には、フェノール系樹脂、酸中和剤、硫酸塩、充填剤などを配合したフェノール系樹脂組成物に酸価200〜300mgKOH/gの酸性硬化剤を添加し、該組成物を20
℃に温調後、ホモディスパー(商品名、特殊機化工業社製ミキサー)で4000rpmで15秒間混合攪拌した直後からの該組成物のpH変化をpHメーター計で測定し、経過時
間(X:秒、0≦X≦120)とpH値(Y)との関係で表したものである。
That is, in the present invention, a phenolic resin composition is blended with a foaming agent and an acidic curing agent, and foamed and cured to produce a phenolic resin foam. The pH value of the composition is the formula: Y = 0.0034X + 2.167 (Formula 1)
It is in the range below the value shown by this, It is the manufacturing method of the acidic curable phenolic resin foam characterized by the above-mentioned.
The above formula 1 is acidic to the phenolic resin composition in which the pH change caused by the consumption of the acidic curing agent over time due to the acid neutralizing agent, filler, etc. in the phenolic resin composition is adjusted to a constant temperature. The relationship between the elapsed time (X) (unit: second) after adding the curing agent and the pH value (Y) is measured under a certain condition.
Specifically, an acidic curing agent having an acid value of 200 to 300 mgKOH / g is added to a phenolic resin composition containing a phenolic resin, an acid neutralizer, a sulfate, a filler, and the like, and the composition is 20
After temperature adjustment to ° C., the pH change of the composition immediately after mixing and stirring at 4000 rpm for 15 seconds with a homodisper (trade name, mixer manufactured by Tokushu Kika Kogyo Co., Ltd.) was measured with a pH meter, and the elapsed time (X: Second, 0 ≦ X ≦ 120) and the pH value (Y).

本発明の酸性硬化型フェノール系樹脂発泡体は、フォーム特性が、密度が10〜500kg/m3、pHが4以上、吸水量が1〜15g/100cm2、であり、フォーム中に硫黄元素とカリウム元素及び/またはナトリウム元素を含むことを特徴とする。
本発明の酸性硬化型フェノール系樹脂発泡体の製造方法では、フェノール系樹脂組成物に、硫酸カリウム、硫酸ナトリウムなどの硫酸塩、更には酸中和剤として金属粉末、アルミニウム化合物、アルカリ金属またはアルカリ土類金属の炭酸塩、重炭酸塩、酸化物、水酸化物からなる群の少なくとも1種を配合することを特徴とする。
The acidic curable phenolic resin foam of the present invention has a foam characteristic of a density of 10 to 500 kg / m 3 , a pH of 4 or more, and a water absorption of 1 to 15 g / 100 cm 2 . It contains potassium element and / or sodium element.
In the method for producing an acid curable phenolic resin foam of the present invention, a phenolic resin composition is further mixed with sulfates such as potassium sulfate and sodium sulfate, and further metal powder as an acid neutralizer, aluminum compound, alkali metal or alkali. It is characterized by blending at least one member selected from the group consisting of carbonates, bicarbonates, oxides and hydroxides of earth metals.

更に、本発明の酸性硬化型フェノール系樹脂発泡体の製造方法では、フェノール系樹脂組成物に発泡剤、酸性硬化剤を添加、混合後のゲル化時間(Y1)と硬化剤量(X1)が式: Y1=−X1+16(式2) で示される値以下の範囲にあることを特徴とする。
ここで示した式2は、液温20℃、乾燥温度65℃の条件下で測定した、ゲル化時間(Y2分)とフェノール系樹脂の固形分100重量部に対する硬化剤量(X1重量部)の関係を表したものである。
ゲル化時間(Y1)と硬化剤量(X1)との関係が上記範囲を充たすには、フェノール系樹脂組成物に硫酸カリウム及び/または硫酸ナトリウムと、炭酸バリウムを添加、混合後、10分以上経過した後に発泡剤、酸性硬化剤を添加、混合する方法を用いるのが好ましい。
Furthermore, in the method for producing an acidic curable phenolic resin foam of the present invention, a foaming agent and an acidic curing agent are added to the phenolic resin composition, the gelation time after mixing (Y 1 ) and the amount of the curing agent (X 1 ) Is in a range equal to or less than the value represented by the formula: Y 1 = −X 1 +16 (Formula 2).
Formula 2 shown here is a gelling time (Y 2 minutes) and a curing agent amount (X 1 weight based on 100 parts by weight of a solid content of a phenolic resin) measured under conditions of a liquid temperature of 20 ° C. and a drying temperature of 65 ° C. Part)).
In order for the relationship between the gelation time (Y 1 ) and the amount of the curing agent (X 1 ) to satisfy the above range, potassium sulfate and / or sodium sulfate and barium carbonate are added to the phenolic resin composition and mixed. It is preferable to use a method in which a foaming agent and an acidic curing agent are added and mixed after a lapse of more than a minute.

また、本発明の酸性硬化型フェノール系樹脂発泡体の製造方法では、フェノール系樹脂組成物に硫酸カリウム及び/または硫酸ナトリウムと、炭酸バリウムを添加、混合後、10分以上経過した後に発泡剤、酸性硬化剤を添加、混合した後の、ゲル化時間(Y2)と
硬化剤量(X2)が式: Y2=−0.75X2+14.5(式3) で示される値以下の
範囲にあることを特徴とする。
ここで示した式3は、式2と同じ条件下で測定したゲル化時間(Y2分)と硬化剤量(
2重量部)の関係を表したものである。
ゲル化時間(Y2)と硬化剤量(X2)との関係が上記範囲を充たすには、1)硫酸カリウム及び/または硫酸ナトリウムを、水溶液又は含水アルコール溶液として添加したり、2)硫酸カリウム及び/または硫酸ナトリウムの水溶液ないしは含水アルコール溶液と、炭酸バリウムとを予め混合した後に添加する方法を用いるのが好ましい。
更には、本発明の酸性硬化型フェノール系樹脂発泡体の製造方法ではフェノール樹脂組成物に発泡剤、酸性硬化剤を添加、混合した後のクリームタイムが10秒以上であると特に好ましい。ここでクリームタイムとは、フェノール系樹脂組成物に発泡剤、酸性硬化剤を始めとする発泡体を構成する成分を全て混合し、発泡性樹脂組成物を調製した時から、該組成物が発泡を開始するまでの時間である。
Further, in the method for producing an acid curable phenolic resin foam of the present invention, potassium sulfate and / or sodium sulfate and barium carbonate are added to and mixed with the phenolic resin composition, and after 10 minutes or more have passed, the foaming agent, After adding and mixing the acidic curing agent, the gelation time (Y 2 ) and the amount of the curing agent (X 2 ) are not more than the values represented by the formula: Y 2 = −0.75X 2 +14.5 (Formula 3) It is in the range.
Formula 3 shown here is the gelation time (Y 2 min) and the amount of curing agent (Y 2 minutes) measured under the same conditions as Formula 2.
X 2 parts by weight).
In order for the relationship between the gelation time (Y 2 ) and the amount of the curing agent (X 2 ) to satisfy the above range, 1) potassium sulfate and / or sodium sulfate can be added as an aqueous solution or a hydrous alcohol solution, or 2) sulfuric acid. It is preferable to use a method of adding an aqueous solution of potassium and / or sodium sulfate or a hydrous alcohol solution and barium carbonate after mixing them in advance.
Furthermore, in the method for producing an acid curable phenolic resin foam of the present invention, it is particularly preferable that the cream time after adding and mixing the foaming agent and the acid curing agent to the phenol resin composition is 10 seconds or more. Here, cream time means that the foaming resin composition is mixed with the phenolic resin composition and all the components constituting the foamed body including the foaming agent and the acidic curing agent are prepared, and the foaming resin composition is foamed. Is the time to start.

本発明において使用されるフェノール系樹脂とは、フェノール類とアルデヒド類を、必要に応じ反応触媒及び/または第1級アミン類の存在下で反応させて得られる、後述の酸
性硬化剤及び/または加熱によって硬化反応を促がす硬化性官能基、例えばメチロール基、ジメチレンエーテル基、ベンゾオキサジン環などを分子内に有するフェノール系樹脂及びその変性樹脂である。具体的には、例えば塩基性触媒の存在下で反応させて得られるレゾール型フェノール系樹脂、または酸性触媒下で反応させた後、塩基性触媒下で反応させて得られるノボラックレゾール型フェノール系樹脂、又は弱酸性触媒や塩基性及び酸性触媒の組み合わせで形成される弱酸性下で反応させて得られるベンジルエーテル型フェノール系樹脂、又はフェノール類、アルデヒド類及び第1級アミン類を反応させて得られるベンゾオキサジン型フェノール系樹脂、又はこれらの樹脂の製造ないしは製造後に任意の化合物、例えばキシレン樹脂、尿素樹脂、メラミン樹脂、エポキシ樹脂、高吸水性樹脂、尿素系化合物、メラミン系化合物、エポキシ系化合物、フルフラール類、レゾルシン、アルキルレゾルシン、タンニンなどの化合物を混合ないし反応して得られる変性樹脂などがある。これらの中でも、発泡硬化性の観点からレゾール型フェノール系樹脂が好ましい。これらは単独及び/または2種以上を組み合わせて用いても良い。
The phenolic resin used in the present invention is an acidic curing agent described below and / or obtained by reacting phenols and aldehydes in the presence of a reaction catalyst and / or a primary amine as necessary. A phenolic resin having a curable functional group that promotes a curing reaction by heating, such as a methylol group, a dimethylene ether group, and a benzoxazine ring in the molecule, and a modified resin thereof. Specifically, for example, a resol type phenolic resin obtained by reacting in the presence of a basic catalyst, or a novolak resol type phenolic resin obtained by reacting in an acidic catalyst and then reacting in a basic catalyst. Or obtained by reacting a benzyl ether type phenolic resin obtained by reacting under weak acidity or a combination of basic and acidic catalysts, or phenols, aldehydes and primary amines. Benzoxazine type phenolic resin, or any compound after the production of these resins, or after the production thereof, such as xylene resin, urea resin, melamine resin, epoxy resin, superabsorbent resin, urea compound, melamine compound, epoxy compound , Furfurals, resorcin, alkylresorcin, tannin and other compounds And the like are modified resin obtained by response. Among these, a resol type phenol resin is preferable from the viewpoint of foam curability. These may be used alone and / or in combination of two or more.

本発明において使用されるレゾール型フェノール系樹脂はモル比(ホルムアルデヒド/フェノール類)が0.50〜3.00、好ましくは1.00〜2.00、アルカリ触媒とフェノール類のモル比(フェノール類/アルカリ触媒)が0.01以上、数平均分子量が190〜370、含水量が2〜40重量%、不揮発分が50〜96重量%、粘度が800〜300,000mPa・s/23℃の範囲に包含されることが好ましい。   The resol type phenolic resin used in the present invention has a molar ratio (formaldehyde / phenols) of 0.50 to 3.00, preferably 1.00 to 2.00, and a molar ratio of alkali catalyst to phenols (phenols). / Alkali catalyst) is 0.01 or more, the number average molecular weight is 190 to 370, the water content is 2 to 40% by weight, the non-volatile content is 50 to 96% by weight, and the viscosity is 800 to 300,000 mPa · s / 23 ° C. Is preferably included.

本発明において使用される酸性硬化フェノール系樹脂のフェノール類としては、例えばフェノール、クレゾール、エチルフェノール、キシレノール、ビスフェノールA、ビスフェノールF、パラターシャリブチルフェノール、レゾルシン、カテコールなど及びその変性物が挙げられ、アルデヒド類としては、例えばホルムアルデヒド、パラホルムアルデヒド、ポリオキシメチレン、トリオキサン、フルフラール、アセトアルデヒド、グリオキザールなどが挙げられる。また、第1級アミン類としては、例えばメチルアミン、シクロヘキシルアミン、アニリンなどが挙げられる。反応触媒としては、水酸化ナトリウム、水酸化カリウム、水酸化カルシウム、水酸化バリウム、水酸化マグネシウム、炭酸ナトリウム、炭酸カリウム、炭酸水素ナトリウム、炭酸水素カリウム、アンモニア、トリエチルアミンなどの塩基性触媒や、例えば塩酸、硫酸、リン酸、酢酸亜鉛、ホウ酸、蓚酸、ギ酸、乳酸、パラトルエンスルホン酸、メタンスルホン酸などの酸性触媒が挙げられる。かかる反応物や反応触媒は、それぞれ、単独及び/または2種以上を組み合わせて用いても良い。   Examples of the phenolic acid-cured phenolic resin used in the present invention include phenol, cresol, ethylphenol, xylenol, bisphenol A, bisphenol F, paratertiary butylphenol, resorcin, catechol and the like, and modified products thereof. Examples of aldehydes include formaldehyde, paraformaldehyde, polyoxymethylene, trioxane, furfural, acetaldehyde, and glyoxal. Examples of primary amines include methylamine, cyclohexylamine, and aniline. Examples of the reaction catalyst include basic catalysts such as sodium hydroxide, potassium hydroxide, calcium hydroxide, barium hydroxide, magnesium hydroxide, sodium carbonate, potassium carbonate, sodium hydrogen carbonate, potassium hydrogen carbonate, ammonia, triethylamine, Acidic catalysts such as hydrochloric acid, sulfuric acid, phosphoric acid, zinc acetate, boric acid, succinic acid, formic acid, lactic acid, paratoluenesulfonic acid, methanesulfonic acid and the like can be mentioned. These reactants and reaction catalysts may be used alone and / or in combination of two or more.

このフェノール類と組み合わせて用いる他方の原料のアルデヒド類についても、特に制限はなく、従来フェノール系樹脂製造の際に慣用されているものの中から適宜選択して用いることができる。これらのアルデヒド類は単独及び/または2種以上を組み合わせて用いても良い。
前記フェノール類とアルデヒド類の使用割合についても従来のフェノール系樹脂の場合と全く同じであり、フェノール類1モルに対し、アルデヒド類が通常0.5〜3.0モル、好ましくは1.0〜2.0モルの範囲で用いられ、樹脂種に応じ10℃〜還流温度の温度で0.5〜24時間反応後必要に応じ中和、濃縮して製造される。なお、反応触媒(無添加、一括添加又は分割添加)、アルデヒド類の使用(一括、分割)、反応雰囲気(空気、窒素、常圧、減圧、加圧)、反応方法(滴下、一段、二段)などの反応要領については適宜その都度目的に応じて選択される。
The other raw material aldehydes used in combination with the phenols are not particularly limited, and can be appropriately selected from those conventionally used in the production of phenolic resins. These aldehydes may be used alone and / or in combination of two or more.
The use ratio of the phenols and aldehydes is exactly the same as in the case of conventional phenol resins, and the aldehydes are usually 0.5 to 3.0 moles, preferably 1.0 to 1 mole per mole of phenols. It is used in the range of 2.0 mol, and is produced by neutralizing and concentrating as necessary after reaction for 0.5 to 24 hours at a temperature of 10 ° C. to reflux temperature depending on the resin type. Reaction catalyst (no addition, batch addition or split addition), use of aldehydes (lump, split), reaction atmosphere (air, nitrogen, normal pressure, reduced pressure, pressurization), reaction method (dropping, one stage, two stages) The reaction procedure such as) is appropriately selected according to the purpose.

本発明における硫酸塩としては、硫酸カリウム、硫酸水素カリウム、硫酸ナトリウム、硫酸水素ナトリウム、硫酸バリウム、硫酸カルシウム、硫酸アンモニウム、硫酸アルミニウムなどがあり、これらは単独で、または2種以上を併せて使用しても良い。そのうち、硫酸カリウム及び/または硫酸ナトリウムが好適である。これらの硫酸塩の添加量は、酸性硬化型フェノール系樹脂100重量部に対して0.01〜10.0重量部、好ましくは
0.1〜7.0重量部である。更に、硫酸カリウム及び/又は硫酸ナトリウムの場合には2.0重量部以下が特に好ましい。
フェノール系樹脂組成物への硫酸塩の添加は、上記塩化合物の添加のほかに、水酸化ナトリウムと硫酸の添加のように組成物中で硫酸塩を形成するものの添加を包含する。
Examples of the sulfate in the present invention include potassium sulfate, potassium hydrogen sulfate, sodium sulfate, sodium hydrogen sulfate, barium sulfate, calcium sulfate, ammonium sulfate, and aluminum sulfate. These may be used alone or in combination of two or more. May be. Of these, potassium sulfate and / or sodium sulfate is preferred. The addition amount of these sulfates is 0.01-10.0 weight part with respect to 100 weight part of acidic curable phenolic resin, Preferably it is 0.1-7.0 weight part. Furthermore, in the case of potassium sulfate and / or sodium sulfate, 2.0 parts by weight or less is particularly preferable.
The addition of the sulfate to the phenolic resin composition includes the addition of those that form a sulfate in the composition, such as the addition of sodium hydroxide and sulfuric acid, in addition to the addition of the salt compound.

本発明における酸中和剤としては、アルミニウム、亜鉛、クロムなどの金属粉末、酸化アルミニウム、水酸化アルミニウム、硫酸アルミニウムなどのアルミニウム化合物、炭酸カルシウム、炭酸ナトリウム、炭酸水素ナトリウム、炭酸亜鉛、炭酸マグネシウム、炭酸水素カリウム、炭酸カリウム、炭酸バリウム、炭酸アンモニウム、炭酸水素アンモニウム、酸化カルシウム、酸化バリウム、酸化マグネシウム、酸化ナトリウム、水酸化カリウム、水酸化カルシウム、水酸化ナトリウム、水酸化バリウム、水酸化マグネシウムなどのアルカリ金属もしくはアルカリ土類金属の炭酸塩、重炭酸塩、酸化物、水酸化物があり、これらは1種単独であるいは2種以上を混合して使用できるが、そのうち、炭酸バリウムが好適である。これらの酸中和剤の添加量は、酸性硬化型フェノール系樹脂100重量部に対して0.5〜30.0重量部、好ましくは1.0〜20.0重量部である。更に、炭酸バリウムの場合には15.0重量部以下が特に好ましい。   Examples of the acid neutralizing agent in the present invention include metal powders such as aluminum, zinc, and chromium, aluminum compounds such as aluminum oxide, aluminum hydroxide, and aluminum sulfate, calcium carbonate, sodium carbonate, sodium hydrogen carbonate, zinc carbonate, magnesium carbonate, Potassium bicarbonate, potassium carbonate, barium carbonate, ammonium carbonate, ammonium bicarbonate, calcium oxide, barium oxide, magnesium oxide, sodium oxide, potassium hydroxide, calcium hydroxide, sodium hydroxide, barium hydroxide, magnesium hydroxide, etc. There are alkali metal or alkaline earth metal carbonates, bicarbonates, oxides and hydroxides, and these can be used alone or in combination of two or more, of which barium carbonate is preferred. . The addition amount of these acid neutralizing agents is 0.5 to 30.0 parts by weight, preferably 1.0 to 20.0 parts by weight with respect to 100 parts by weight of the acid curable phenolic resin. Furthermore, in the case of barium carbonate, 15.0 parts by weight or less is particularly preferable.

本発明においては、更に、整泡剤、充填剤、希釈剤、硬化促進剤、遅延剤、難燃剤などの、通常フェノール系樹脂発泡体製造時に使用される添加剤を必要に応じて使用することができる。
整泡剤としては、非イオン系界面活性剤、例えばポリオキシエチレンラウリルエーテル、ポリオキシエチレンオレイルエーテル、ポリオキシエチレンオクチルフェニルエーテル、ソルビタンモノラウレート、ソルビタンモノパルミテート、ソルビタンモノステアレートなどに代表されるソルビタン脂肪酸エステル類、ポリオキシエチレンソルビタンモノラウレート、ポリオキシエチレソルビタンモノパルミテート、ポリオキシエチレンソルビタンモノオレエレートなどに代表されるポリオキシエチレンソルビタン脂肪酸エステル類、ポリオキシエチレンジメチルシリコン、ひまし油エチレンオキサイド及びプロピレンオキサイド付加物、エチレンオキサイドープロピレンオキサイドブロック共重合体、ポリシロキサン−ポリオキシアルキレン共重合体、ジメチルポリシロキサン−ポリオキシアルキレン共重合体、エトキシ化ひまし油、エポキシ化大豆油エトキシ化物、シリコーン系界面活性剤等があり、単独でまたは2種以上を併せて使用できる。これらの整泡剤の添加量は、酸性硬化型フェノール系樹脂100重量部に対して0.1〜10.0重量部、好ましくは0.2〜7.0重量部である。
In the present invention, additives that are usually used in the production of phenolic resin foams, such as foam stabilizers, fillers, diluents, curing accelerators, retarders, and flame retardants, are used as necessary. Can do.
Examples of foam stabilizers include nonionic surfactants such as polyoxyethylene lauryl ether, polyoxyethylene oleyl ether, polyoxyethylene octyl phenyl ether, sorbitan monolaurate, sorbitan monopalmitate, and sorbitan monostearate. Sorbitan fatty acid esters, polyoxyethylene sorbitan monolaurate, polyoxyethylene sorbitan monopalmitate, polyoxyethylene sorbitan fatty acid esters represented by polyoxyethylene sorbitan monooleate, polyoxyethylene dimethyl silicon, Castor oil ethylene oxide and propylene oxide adduct, ethylene oxide-propylene oxide block copolymer, polysiloxane-polyoxyalkylene Polymers, dimethylpolysiloxane - polyoxyalkylene copolymers, ethoxylated castor oil, epoxidized soybean oil ethoxylates, there are silicone-based surfactants may be used alone or in combination of two or more. The addition amount of these foam stabilizers is 0.1-10.0 weight part with respect to 100 weight part of acidic curable phenolic resin, Preferably it is 0.2-7.0 weight part.

本発明で使用される発泡剤としては、特定フロン、代替フロンなどのフッ素化合物、塩化メチレンなどのハロゲン化合物、酢酸エチルなどのエステル類、ヘプタン、n−ヘキサン、イソヘキサン、シクロヘキサン、2,3−ジメチルブタン、2−メチルペンタン、2,2−ジメチルブタン、3−メチルペンタン、n−ペンタン、シクロペンタンなどの低沸点の脂肪族炭化水素、イソプロピルエーテルなどのエーテル、メタノール、エタノールなどのアルコール類、メチルエチルケトンなどのケトン類、ジオキソランなどの環状エーテル化合物類、更に酸を作用させることで炭酸ガスや窒素等の気体を発生させるような炭酸カルシウム、炭酸バリウム、炭酸水素ナトリウム、炭酸ナトリウム、アゾジカルボンアミド、アゾビスイソブチロニトリル、パラトルエンスルホニルヒドラジッド等の化学的反応発泡剤があり、これらは単独又は2種以上を併せて使用できる。更にはこれら以外に液化炭酸ガス、空気、窒素、ブタン、アルゴン等の気体もこれらと混合して使用できる。これら発泡剤の添加量は、酸性硬化型フェノール系樹脂100重量部に対して0.2〜20.0重量部、好ましくは0.5〜15.0重量部である。   Examples of the foaming agent used in the present invention include fluorine compounds such as specific CFCs and CFC substitutes, halogen compounds such as methylene chloride, esters such as ethyl acetate, heptane, n-hexane, isohexane, cyclohexane, and 2,3-dimethyl. Low-boiling point aliphatic hydrocarbons such as butane, 2-methylpentane, 2,2-dimethylbutane, 3-methylpentane, n-pentane and cyclopentane, ethers such as isopropyl ether, alcohols such as methanol and ethanol, methyl ethyl ketone Such as ketones, cyclic ether compounds such as dioxolane, and calcium carbonate, barium carbonate, sodium hydrogen carbonate, sodium carbonate, azodicarbonamide, azo which generate gas such as carbon dioxide and nitrogen by the action of acid. Bisisobutyronitrile , There is a chemical reaction foaming agent such as p-toluenesulfonyl hydrazide, which may be used in combination alone or in combination. In addition to these, gases such as liquefied carbon dioxide, air, nitrogen, butane, and argon can be used by mixing them. The addition amount of these foaming agents is 0.2 to 20.0 parts by weight, preferably 0.5 to 15.0 parts by weight with respect to 100 parts by weight of the acid curable phenolic resin.

本発明で使用される酸性硬化剤には、フェノールスルホン酸、トルエンスルホン酸、キシレンスルホン酸、ベンゼンスルホン酸、レゾルシンスルホン酸、メタキシレンスルホン
酸、エチルベンゼンスルホン酸、ナフタレンスルホン酸、ナフトールスルホン酸、アントラセンスルホン酸、オルソクレゾール4スルホン酸、メタクレゾールスルホン酸等の有機スルホン酸類及びこれらとホルマリンとの縮合物の他、γ―ブチロラクトン、トリエチレングリコールジアセテート、トリアセチン、ギ酸メチル等のカルボン酸エステル類、エチレンカーボネート、プロピレンカーボネート等の環状アルキレンカーボーネート類、正リン酸、ポリリン酸、トリポリリン酸、メタリン酸、塩酸等の無機酸類、ギ酸、酢酸、シュウ酸などの有機酸などがあり、これらは単独で又は2種以上を混合して使用できる。その
添加量は、酸性硬化型フェノール系樹脂100重量部に対して200〜300mgKOH/gの酸価のものとして1.0〜20.0重量部で好ましくは2.0〜15.0重量部である。
The acidic curing agent used in the present invention includes phenolsulfonic acid, toluenesulfonic acid, xylenesulfonic acid, benzenesulfonic acid, resorcinsulfonic acid, metaxylenesulfonic acid, ethylbenzenesulfonic acid, naphthalenesulfonic acid, naphtholsulfonic acid, anthracene. In addition to organic sulfonic acids such as sulfonic acid, orthocresol 4 sulfonic acid, and metacresol sulfonic acid, and condensates thereof with formalin, carboxylic acid esters such as γ-butyrolactone, triethylene glycol diacetate, triacetin, and methyl formate, There are cyclic alkylene carbonates such as ethylene carbonate, propylene carbonate, inorganic acids such as orthophosphoric acid, polyphosphoric acid, tripolyphosphoric acid, metaphosphoric acid, hydrochloric acid, organic acids such as formic acid, acetic acid, oxalic acid, etc. These may be used alone, or two or more thereof. The addition amount is 1.0 to 20.0 parts by weight, preferably 2.0 to 15.0 parts by weight as an acid value of 200 to 300 mg KOH / g with respect to 100 parts by weight of the acid curable phenolic resin. is there.

本発明に使用する難燃剤としては、デカブロモジフェニルエーテル、ペンタブロモトルエン、ペンタブロモジフェニルエーテルなどの添加型臭素系難燃剤、テトラブロモ無水フタル酸、ジブロモフェノール、トリブロモフェノールのグリシジルエーテル等の反応型臭素系難燃剤、トリエチルホスフェート、トリクレジルホスフェート、クレジルジフェニルホスフェート、トリフェニルホスフェート、トリブチルホスフェート、キシレルジフェニルホスフェート等のリン酸エステル類、トリス−(クロロエチル)ホスフェート、トリス−(β−クロロプロピル)ホスフェート、トリス−(ジブロモプロピル)ホスフェート、トリス−(2,3−ジブロモクロロプロピル)ホスフェートなどの含ハロゲンリン酸エステル類及び含ハロゲン縮合リン酸エステル類、トリフェニルホスファイトなどの亜リン酸エステル類、リン酸、メタリン酸、ピロリン酸、ポリリン酸等のリン酸類、ホウ素化合物、水酸化アルミニウム、尿素、メラミン、ベンゾグアナミンなどがあり、これらは単独で又は2種以上を併せて使用できる。その添加量は、酸性硬化型フェノール系樹脂100重量部に対して3.0〜200重量部、好ましくは5.0〜90.0重量部である。   Examples of the flame retardant used in the present invention include additive brominated flame retardants such as decabromodiphenyl ether, pentabromotoluene, pentabromodiphenyl ether, and reactive bromines such as tetrabromophthalic anhydride, dibromophenol, and tribromophenol glycidyl ether. Flame retardants, triethyl phosphate, tricresyl phosphate, cresyl diphenyl phosphate, triphenyl phosphate, tributyl phosphate, xyleryl diphenyl phosphate, phosphate esters, tris- (chloroethyl) phosphate, tris- (β-chloropropyl) phosphate , Halogen-containing phosphates such as tris- (dibromopropyl) phosphate, tris- (2,3-dibromochloropropyl) phosphate, and halogen-containing condensed phosphorus There are esters, phosphorous esters such as triphenyl phosphite, phosphoric acids such as phosphoric acid, metaphosphoric acid, pyrophosphoric acid, polyphosphoric acid, boron compounds, aluminum hydroxide, urea, melamine, benzoguanamine, etc. Or in combination of two or more. The addition amount is 3.0 to 200 parts by weight, preferably 5.0 to 90.0 parts by weight, with respect to 100 parts by weight of the acid curable phenolic resin.

また、これら以外にフェノール樹脂系発泡体を製造するに際しては、各種の添加剤を加えて発泡体の性能を改質することができる。例えば、1)フェノール繊維、炭素繊維、アラミド繊維、ガラス繊維、ロックウール繊維などに代表される繊維類(機械的強度や寸法
精度の改善)、2)エチレングリコール、ジエチレングリコール、プロピレングリコール
、ジプロピレングリコール、トリプロピレングリコール等の低分子ポリエチレン及びポリプロピレングリコール類、プロピレングリコールジグリシジルエーテル、ネオペンチルグリコールジグリシジルエーテル、ジプロピレングリコールジグリシジルエーテル類などの脂肪族グリシジルエーテル化合物類、芳香族多価アルコールのジ又はトリグリシジルエーテル化合物類、ポリビニルアルコール、カルボキシメチルセルロース、メチルセルロース、スターチ類等の合成及び天然高分子、アクリル系エマルジョン類(脆性の改質)、3)アセトン、テトラヒドロフラン、1,3ジオキソランなど(粘度の低減)、4)硝酸アンモニウム、硫酸アンモニウム、塩化アンモニウム、リン酸アンモニウム、炭酸アンモニウム、酢酸アンモニウム等のアンモニウ塩類、分子内にアミノ基、アミド基、イミノ基を有する尿素、尿素樹脂、メラミン、メラミン樹脂、チオ尿素、ジシアンジアミド、ベンゾグアナミン、亜硫酸ナトリウム、亜硫酸水素ナトリウム、亜硫酸アンモニウム、亜硫酸水素アンモニウム等の亜硫酸塩類、重亜硫酸塩類(ホルムアルデヒド捕捉)などが挙げられる。その他にに、タルク、マイカ、ワラストナイト、カオリン、シリカ等の無機質充填剤、染料、顔料等の着色剤、紫外線吸収剤なども併用しても良い。その添加量には特に制限はないが、通常、酸性硬化型フェノール系樹脂100重量部に対して0.1〜50.0重量部、好ましくは0.2〜40.0重量部である。
In addition to these, when producing a phenol resin foam, various additives can be added to improve the performance of the foam. For example, 1) Fibers represented by phenol fiber, carbon fiber, aramid fiber, glass fiber, rock wool fiber, etc. (improvement of mechanical strength and dimensional accuracy), 2) ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol Low molecular weight polyethylene such as tripropylene glycol and polypropylene glycols, aliphatic glycidyl ether compounds such as propylene glycol diglycidyl ether, neopentyl glycol diglycidyl ether, dipropylene glycol diglycidyl ether, Or synthetic and natural polymers such as triglycidyl ether compounds, polyvinyl alcohol, carboxymethyl cellulose, methyl cellulose, starches, acrylic emulsions (modified brittleness) 3) Acetone, tetrahydrofuran, 1,3 dioxolane, etc. (decrease in viscosity) 4) Ammonium salts such as ammonium nitrate, ammonium sulfate, ammonium chloride, ammonium phosphate, ammonium carbonate, ammonium acetate, amino groups, amide groups in the molecule , Urea having urea, urea resin, melamine, melamine resin, thiourea, dicyandiamide, benzoguanamine, sodium sulfite, sodium hydrogen sulfite, ammonium sulfite, ammonium hydrogen sulfite and the like, and bisulfites (formaldehyde trapping) It is done. In addition, inorganic fillers such as talc, mica, wollastonite, kaolin and silica, colorants such as dyes and pigments, ultraviolet absorbers and the like may be used in combination. Although there is no restriction | limiting in particular in the addition amount, Usually, it is 0.1-50.0 weight part with respect to 100 weight part of acidic curable phenolic resin, Preferably it is 0.2-40.0 weight part.

本発明で酸性硬化型フェノール系樹脂発泡体に使用される面材は特に限定されるものではなく、クラフト紙、炭カル紙、合板、繊維板、突板等の繊維、アルミニウム箔、亜鉛メッキ鋼鈑、ガルバニウム鋼鈑などの金属、珪カル板、石膏ボードなどの無機の材質のものが利用可能である。   The face material used for the acid curable phenolic resin foam in the present invention is not particularly limited, and the fibers such as kraft paper, charcoal cal paper, plywood, fiber board, and veneer, aluminum foil, galvanized steel sheet Further, metals such as galvanium steel plates, inorganic materials such as quartz plates and gypsum boards can be used.

次に、本発明において、酸性硬化型フェノール系樹脂発泡体を製造する方法としては、前記の組成成分のレゾール型フェノール系樹脂に整泡剤、充填材、酸中和剤、硫酸塩及びその他添加剤などを混合したフェノール系樹脂組成物と発泡剤、酸性硬化剤を高速攪拌で混合しバッチ式で製造する方法、連続的に高速攪拌して製造する方法など、従来公知の方法が利用できる。これらの各操作によって得られる混合物は、エンドレスコンベア上に流出させる成形方法、スポット的に流出させて部分的に発泡させる方法、ある大きさの空洞中に投入して発泡ブロックを作る方法、空洞中に圧入しながら充填発泡させる方法などに用いられる。これらの方法による発泡、硬化温度は30〜100℃、硬化時間は1〜15分の条件であり、また、半硬化状態(プレキュア)でカットした後、更に後硬化(アフターキュア)により硬化を完了させる方法がある。得られたフェノール系樹脂発泡体は、生産性が低下することなく、機械的強度の高い、耐吸水性、耐脆性に優れた高品質の発泡体を形成するものである。主な用途としては、例えば鉄、ステンレス、アルミ、亜鉛等の金属板材、石膏ボード、ロックウールボード等の無機質板、クラフト紙、アスベスト紙、合板等とを複合化して床下材、天井材、屋根下地材、外壁材、内壁材、防火扉などの建材用及びメタン、プロパン、ブタン等の貯蔵タンクなどのプラント分野、重油タンク、パイプ配管などの保冷保温用、冷凍冷蔵倉庫などの保冷材などに幅広く応用される。   Next, in the present invention, as a method for producing an acid curable phenolic resin foam, a foam stabilizer, a filler, an acid neutralizing agent, a sulfate and other additives are added to the resol type phenolic resin having the above-described composition components. Conventionally known methods such as a method in which a phenolic resin composition mixed with an agent and the like, a foaming agent, and an acidic curing agent are mixed by high-speed stirring and manufactured by a batch method, and a method in which high-speed stirring is continuously manufactured are used. The mixture obtained by each of these operations is a molding method that flows out onto an endless conveyor, a method that causes spotting to flow out and partially foams, a method that throws into a cavity of a certain size to make a foam block, It is used for the method of filling and foaming while press-fitting into. Foaming by these methods, curing temperature is 30 to 100 ° C, curing time is 1 to 15 minutes, and after cutting in a semi-cured state (pre-cure), curing is further completed by post-curing (after cure) There is a way to make it. The obtained phenol-based resin foam forms a high-quality foam having high mechanical strength, excellent water absorption resistance and brittleness resistance without lowering productivity. Main applications include metal plates such as iron, stainless steel, aluminum and zinc, inorganic boards such as gypsum board and rock wool board, craft paper, asbestos paper, plywood, etc. For base materials, outer wall materials, inner wall materials, building materials such as fire doors, plant fields such as storage tanks for methane, propane, butane, etc., for cold and warm insulation such as heavy oil tanks, pipe piping, etc. Widely applied.

次に、本発明を実施例により、さらに詳細に説明するが、本発明はこれらの例によってなんら限定されるものではない。   EXAMPLES Next, although an Example demonstrates this invention further in detail, this invention is not limited at all by these examples.


実施例1
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、硫酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム30重量部、クレー30重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、酸中和剤として炭酸バリウム8重量部を添加してフェノール系レゾール樹脂組成物を調製し、6時間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したn−ペンタン 18重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸60重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したのち、ただちにディスポカップを60°の角度で10秒間傾けて予め70℃に温調した両面材クラフト紙を使用したアルミ製モールド(容積:300mm×300mm×50mm)内に均一に散布(注入)した後、モールドの蓋を4箇所で固定し、70℃乾燥機中で10分間加熱した後脱型して酸性硬化型フェノール系樹脂発泡体を作成した。
(3)成形した発泡体を室温20℃、湿度65%の雰囲気下に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。

Example 1
(1) Preparation of phenol-based resole resin composition 4451 g of phenol and 5135 g of a 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes. Then, sulfuric acid was added to adjust the pH to 6.3, and the dehydration rate was 29.0 under reduced pressure. After dehydrating and concentrating to weight percent, 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50 was obtained. Next, 30 parts by weight of aluminum hydroxide, 30 parts by weight of clay, 1.5 parts by weight of silicone foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 100 parts by weight of the resin, and acid neutralizer A phenolic resole resin composition was prepared by adding 8 parts by weight of barium carbonate and allowed to stand for 6 hours.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of the above (1) preliminarily adjusted to 20 ° C., 18 parts by weight of n-pentane preliminarily adjusted to 20 ° C., and preliminarily adjusted to 20 ° C. After adding 60 parts by weight of 67% phenolsulfonic acid having an acid value of 260 mgKOH / g and mixing with a homodisper (trade name, mixer manufactured by Tokushu Kika Kogyo Co., Ltd.) at 5000 rpm for 30 seconds, immediately dispose the disposable cup at an angle of 60 °. After spraying (injecting) uniformly into an aluminum mold (volume: 300 mm x 300 mm x 50 mm) using double-sided kraft paper that has been temperature-controlled at 70 ° C by inclining for 10 seconds, the mold lid is fixed at four locations. After heating for 10 minutes in a dryer at 70 ° C., demolding was performed to produce an acid curable phenolic resin foam.
(3) The molded foam was allowed to stand for 5 days in an atmosphere at room temperature of 20 ° C. and humidity of 65%, and various physical properties were measured in accordance with JIS A-9511.

実施例2
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化カリウム水溶液を添加後
85℃まで昇温させ、同温度で70分間反応させた後、硫酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム30重量部、クレー30重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、酸中和剤として炭酸カルシウム6重量部、5%硫酸ナトリウム水溶液15部を添加してフェノール系レゾール樹脂組成物を調製し、6時間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したシクロペンタン 7.8重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸84重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したのち、ただちにディスポカップを60°の角度で10秒間傾けて予め70℃に温調した両面材亜鉛鋼鈑を使用したアルミ製モールド(容積:300mm×300mm×50mm)に均一に散布した後、蓋を4箇所で固定し、70℃乾燥機中で10分間加熱脱型し酸性硬化型フェノール系樹脂発泡体を作成した。
(3)成形した発泡体を室温20℃、湿度65%に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。
Example 2
(1) Preparation of phenol-based resol resin composition 4451 g of phenol and 5135 g of 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous potassium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, sulfuric acid was added to adjust the pH to 6.3, and the dehydration rate was 29.0 under reduced pressure. After dehydrating and concentrating to weight percent, 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50 was obtained. Next, 30 parts by weight of aluminum hydroxide, 30 parts by weight of clay, 1.5 parts by weight of silicone foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 100 parts by weight of the resin, and acid neutralizer A phenolic resol resin composition was prepared by adding 6 parts by weight of calcium carbonate and 15 parts of a 5% aqueous sodium sulfate solution, and left for 6 hours.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of the above (1) preliminarily adjusted to 20 ° C., 7.8 parts by weight of cyclopentane preliminarily adjusted to 20 ° C., preliminarily warmed to 20 ° C. After charging 84 parts by weight of 67% phenolsulfonic acid having a prepared acid value of 260 mgKOH / g, mixing with a homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.) at 5000 rpm for 30 seconds, and then immediately placing the disposable cup at a 60 ° angle After spraying uniformly on an aluminum mold (volume: 300 mm x 300 mm x 50 mm) using a double-sided galvanized steel plate that has been temperature-controlled at 70 ° C in advance by tilting for 10 seconds, fix the lid at four locations and dry at 70 ° C The mold was heated and demolded in the machine for 10 minutes to prepare an acid curable phenolic resin foam.
(3) The molded foam was allowed to stand at room temperature of 20 ° C. and humidity of 65% for 5 days, and various physical properties were measured according to JIS A-9511.

実施例3
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、シュウ酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム30重量部、クレー30重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、酸中和剤として炭酸バリウム8重量部、5%硫酸カリウム水溶液15部を添加してフェノール系レゾール樹脂組成物を調製し、6時間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したHCHC−141b 18重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸54重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したのち、ただちにディスポカップを60°の角度で10秒間傾けて予め70℃に温調した両面材クラフト紙を使用したアルミ製モールド(容積:300mm×300mm×50mm)に均一に散布した後、蓋を4箇所で固定し、70℃で10分間乾燥後脱型し酸性硬化型フェノール系樹脂発泡体を作成した。
(3)成形した発泡体を室温20℃、湿度65%に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。
Example 3
(1) Preparation of phenol-based resol resin composition 4451 g of phenol and 5135 g of 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, oxalic acid was added to adjust the pH to 6.3, and the dehydration rate was 29. After dehydrating and concentrating to 0% by weight, 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50 was obtained. Next, 30 parts by weight of aluminum hydroxide, 30 parts by weight of clay, 1.5 parts by weight of silicone foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 100 parts by weight of the resin, and acid neutralizer A phenolic resole resin composition was prepared by adding 8 parts by weight of barium carbonate and 15 parts of a 5% aqueous potassium sulfate solution, and left for 6 hours.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of the above (1) preliminarily adjusted to 20 ° C., 18 parts by weight of HCHC-141b preliminarily adjusted to 20 ° C., preliminarily adjusted to 20 ° C. After adding 54 parts by weight of 67% phenolsulfonic acid having an acid value of 260 mgKOH / g, mixing with a homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.) at 5000 rpm for 30 seconds, immediately dispose the disposable cup at a 60 ° angle. After spraying uniformly on an aluminum mold (volume: 300 mm x 300 mm x 50 mm) using double-sided kraft paper that has been temperature-controlled to 70 ° C in advance by inclining for 10 seconds, the lid is fixed at four locations, and 10 minutes at 70 ° C. After drying, it was demolded to produce an acid curable phenolic resin foam.
(3) The molded foam was allowed to stand at room temperature of 20 ° C. and humidity of 65% for 5 days, and various physical properties were measured according to JIS A-9511.

実施例4
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化カリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、硫酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム30重量部、クレー30重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、酸中和剤として炭酸カルシウム8重量部を添加してフェノール系レゾール樹脂組成物を調製し、6時
間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂600重量部、予め20℃に温調したシクロペンタン12重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸42重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したのち、ただちにディスポカップを60°の角度で10秒間傾けて予め70℃に温調したアルミ製モールド(容積:300mm×300mm×50mm、0.5mm亜鉛鋼板を内底部にひいておく)に均一に散布した後、蓋を4箇所で固定し、70℃乾燥機中でで10分間加熱後脱型し酸性硬化型フェノール系樹脂発泡体を作成した。
(3)成形した発泡体を室温20℃、湿度65%に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。
Example 4
(1) Preparation of phenol-based resol resin composition 4451 g of phenol and 5135 g of 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous potassium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, sulfuric acid was added to adjust the pH to 6.3, and the dehydration rate was 29.0 under reduced pressure. After dehydrating and concentrating to weight percent, 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50 was obtained. Next, 30 parts by weight of aluminum hydroxide, 30 parts by weight of clay, 1.5 parts by weight of silicone foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 100 parts by weight of the resin, and acid neutralizer A phenolic resole resin composition was prepared by adding 8 parts by weight of calcium carbonate and allowed to stand for 6 hours.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin of the above (1) preliminarily adjusted to 20 ° C., 12 parts by weight of cyclopentane preliminarily adjusted to 20 ° C., acid value preliminarily adjusted to 20 ° C. Charge 42 parts by weight of 260 mg KOH / g 67% phenol sulfonic acid, mix for 30 seconds at 5000 rpm with a homodisper (trade name, mixer manufactured by Tokushu Kika Kogyo Co., Ltd.), and immediately tilt the disposable cup at an angle of 60 ° for 10 seconds. After spraying uniformly on an aluminum mold (volume: 300 mm x 300 mm x 50 mm, 0.5 mm galvanized steel plate on the inner bottom) preliminarily adjusted to 70 ° C, the lid is fixed at four locations, and 70 ° C It was demolded after heating in a dryer for 10 minutes to produce an acid curable phenolic resin foam.
(3) The molded foam was allowed to stand at room temperature of 20 ° C. and humidity of 65% for 5 days, and various physical properties were measured according to JIS A-9511.

実施例5
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化カリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、硫酸を添加してpHを4.5に調整し、減圧下に脱水率5.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.65、粘度が70000mPa・s/23℃の液状フェノール系レゾール樹脂
6800gを得た。次いで、該樹脂100重量部に対してシリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部を添加してフェノール系レゾール樹脂組成物を調製し、6時間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂600重量部、予め20℃に温調したHCFC−141b 21重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸9重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で8000rpmで30秒間混合したのち、ただちにディスポカップを60°の角度で10秒間傾けて予め70℃に温調したアルミ製モールド(容積:300mm×300mm×50mm、0.5mmクラフト紙を内底部にひいておく)に均一に散布した後、蓋を4箇所で固定し、70℃乾燥機中で5分間加熱後脱型した。次いで脱型後のフォームを90℃に加熱したホットプレスで硬化成形し酸性硬化型フェノール系樹脂発泡体を作成した。
(3)成形した発泡体を室温20℃、湿度65%に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。
Example 5
(1) Preparation of phenol-based resol resin composition 4451 g of phenol and 5135 g of 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous potassium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, sulfuric acid was added to adjust the pH to 4.5, and the dehydration rate was 5.0 under reduced pressure. After dehydrating and concentrating to weight percent, 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.65 and a viscosity of 70000 mPa · s / 23 ° C. was obtained. Next, 1.5 parts by weight of a silicone foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone) was added to 100 parts by weight of the resin to prepare a phenolic resole resin composition, which was allowed to stand for 6 hours. .
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin of the above (1) preliminarily adjusted to 20 ° C., 21 parts by weight of HCFC-141b preliminarily adjusted to 20 ° C., acid previously adjusted to 20 ° C. After charging 9 parts by weight of 67% phenolsulfonic acid with a value of 260 mgKOH / g and mixing for 30 seconds at 8000 rpm with a homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.), immediately place the disposable cup at an angle of 60 ° for 10 seconds. After spraying uniformly on an aluminum mold (volume: 300 mm x 300 mm x 50 mm, 0.5 mm kraft paper on the inner bottom) that has been tilted and adjusted to 70 ° C in advance, the lid is fixed at four locations. The mold was removed after heating for 5 minutes in a dryer. Next, the foam after demolding was cured and molded by a hot press heated to 90 ° C. to produce an acid curable phenolic resin foam.
(3) The molded foam was allowed to stand at room temperature of 20 ° C. and humidity of 65% for 5 days, and various physical properties were measured according to JIS A-9511.

実施例6
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、硫酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム30重量部、クレー30重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、酸中和剤として炭酸バリウム6.8重量部を添加してフェノール系レゾール樹脂組成物を調製し10分間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したシクロペンタン 18重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸60重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したのち、ただちにディスポカップを60°の角度で10秒間傾けて予め7
0℃に温調した両面材クラフト紙を使用したアルミ製モールド(容積:300mm×300mm×50mm)内に均一に散布(注入)した後、モールドの蓋を4箇所で固定し、70℃乾燥機中で10分間加熱した後脱型して酸性硬化型フェノール系樹脂発泡体を作成した。
(3)成形した発泡体を室温20℃、湿度65%の雰囲気下に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。
Example 6
(1) Preparation of phenol-based resole resin composition 4451 g of phenol and 5135 g of a 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes. Then, sulfuric acid was added to adjust the pH to 6.3, and the dehydration rate was 29.0 under reduced pressure. After dehydrating and concentrating to weight percent, 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50 was obtained. Next, 30 parts by weight of aluminum hydroxide, 30 parts by weight of clay, 1.5 parts by weight of silicone foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 100 parts by weight of the resin, and acid neutralizer A phenolic resole resin composition was prepared by adding 6.8 parts by weight of barium carbonate and allowed to stand for 10 minutes.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of (1) above, which was previously adjusted to 20 ° C., 18 parts by weight of cyclopentane, which was previously adjusted to 20 ° C., and was previously adjusted to 20 ° C. After charging 60 parts by weight of 67% phenolsulfonic acid having an acid value of 260 mgKOH / g and mixing at 5000 rpm for 30 seconds with a homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.), the disposable cup was immediately adjusted to 10 at an angle of 60 °. Tilt in seconds for 7
After uniformly spraying (injecting) into an aluminum mold (volume: 300 mm x 300 mm x 50 mm) using double-sided kraft paper that has been temperature-controlled at 0 ° C, the mold lid is fixed at four locations, and a 70 ° C dryer The mixture was heated for 10 minutes and then demolded to prepare an acid curable phenolic resin foam.
(3) The molded foam was allowed to stand for 5 days in an atmosphere at room temperature of 20 ° C. and humidity of 65%, and various physical properties were measured in accordance with JIS A-9511.

実施例7
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、50%パラトルエンスルホン酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム92.7重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、9%硫酸カリウム水溶液12重量部、酸中和剤として炭酸バリウム6.8重量部を添加してフェノール系レゾール樹脂組成物を調製し、10分間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したシクロペンタン 7.8重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸60重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したのち、ただちにディスポカップを60°の角度で10秒間傾けて予め70℃に温調した両面材クラフト紙を使用したアルミ製モールド(容積:300mm×300mm×50mm)内に均一に散布(注入)した後、モールドの蓋を4箇所で固定し、70℃乾燥機中で10分間加熱した後脱型して酸性硬化型フェノール系樹脂発泡体を作成した。
(3)成形した発泡体を室温20℃、湿度65%の雰囲気下に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。
Example 7
(1) Preparation of phenol-based resole resin composition 4451 g of phenol and 5135 g of a 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, and then 50% paratoluenesulfonic acid was added to adjust the pH to 6.3. A dehydration rate of 29.0% by weight was obtained by dehydration and concentration to obtain 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50. Next, 92.7 parts by weight of aluminum hydroxide, 1.5 parts by weight of silicone-based foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 12 parts by weight of 9% aqueous potassium sulfate solution with respect to 100 parts by weight of the resin Then, 6.8 parts by weight of barium carbonate as an acid neutralizing agent was added to prepare a phenolic resole resin composition, which was allowed to stand for 10 minutes.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of the above (1) preliminarily adjusted to 20 ° C., 7.8 parts by weight of cyclopentane preliminarily adjusted to 20 ° C., preliminarily warmed to 20 ° C. After charging 60 parts by weight of 67% phenolsulfonic acid having a prepared acid value of 260 mgKOH / g, mixing with a homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.) at 5000 rpm for 30 seconds, and then immediately placing the disposable cup at a 60 ° angle Was sprayed (injected) uniformly into an aluminum mold (volume: 300 mm x 300 mm x 50 mm) using double-sided kraft paper that had been temperature-controlled at 70 ° C by inclining for 10 seconds, and then fixed at four locations on the mold lid Then, after heating for 10 minutes in a dryer at 70 ° C., the mold was removed to produce an acid curable phenolic resin foam.
(3) The molded foam was allowed to stand for 5 days in an atmosphere at room temperature of 20 ° C. and humidity of 65%, and various physical properties were measured in accordance with JIS A-9511.

実施例8
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、50%パラトルエンスルホン酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム92.7重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、事前に用意しておいた9%硫酸カリウム水溶液12重量部と炭酸バリウム6.8重量部の混合液を添加してフェノール系レゾール樹脂組成物を調製し、10分間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したシクロペンタン 18重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸60重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したのち、ただちにディスポカップを60°の角度で10秒間傾けて予め70℃に温調した両面材クラフト紙を使用したアルミ製モールド(容積:300mm×300mm×50mm)内に均一に散布(注入)した後、モールドの蓋を4箇所で固定し、70℃乾燥機中で10分間加熱した後脱型して酸性硬化型フェノール系樹脂発泡体を作成した。
(3)成形した発泡体を室温20℃、湿度65%の雰囲気下に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。
Example 8
(1) Preparation of phenol-based resole resin composition 4451 g of phenol and 5135 g of a 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, and then 50% paratoluenesulfonic acid was added to adjust the pH to 6.3. A dehydration rate of 29.0% by weight was obtained by dehydration and concentration to obtain 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50. Next, 92.7 parts by weight of aluminum hydroxide and 1.5 parts by weight of silicone foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 100 parts by weight of the resin, 9 prepared in advance. A phenolic resole resin composition was prepared by adding a mixed solution of 12 parts by weight of an aqueous potassium sulfate solution and 6.8 parts by weight of barium carbonate, and allowed to stand for 10 minutes.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of (1) above, which was previously adjusted to 20 ° C., 18 parts by weight of cyclopentane, which was previously adjusted to 20 ° C., and was previously adjusted to 20 ° C. After charging 60 parts by weight of 67% phenolsulfonic acid having an acid value of 260 mgKOH / g and mixing at 5000 rpm for 30 seconds with a homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.), the disposable cup was immediately adjusted to 10 at an angle of 60 °. After uniformly spraying (injecting) into an aluminum mold (volume: 300 mm x 300 mm x 50 mm) using a double-sided kraft paper that has been temperature-controlled to 70 ° C in advance by tilting for 2 seconds, the mold lid is fixed at four locations, After heating for 10 minutes in a 70 ° C. dryer, the mold was removed to produce an acid curable phenolic resin foam.
(3) The molded foam was allowed to stand for 5 days in an atmosphere at room temperature of 20 ° C. and humidity of 65%, and various physical properties were measured in accordance with JIS A-9511.

実施例1〜5の結果を表1に、実施例6〜8の結果を表2に示す。表中、pH変化はフェノール系樹脂組成物のpHの変化量を示す。

The results of Examples 1 to 5 are shown in Table 1, and the results of Examples 6 to 8 are shown in Table 2. In the table, pH change indicates the amount of change in pH of the phenolic resin composition.

Figure 2005120337
Figure 2005120337

Figure 2005120337
Figure 2005120337

比較例1
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、PTSを添加してpHを6.3
に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該組成物100重量部に対して水酸化アルミニウム30重量部、クレー30重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、酸中和剤として炭酸バリウム5重量部を添加してフェノール系レゾール樹脂組成物を調製し、6時間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したn−ペンタン18重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸66重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合後、直ぐに炭酸塩の分解が起こり 式: Y=0.0034X+2.167以下の範囲に入らず硬化しないため発泡体が得られなかった。
Comparative Example 1
(1) Preparation of phenol-based resol resin composition 4451 g of phenol and 5135 g of 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, and then PTS was added to adjust the pH to 6.3.
To 69.0 g of a liquid phenolic resol resin having a molar ratio (formaldehyde / phenol) of 1.50. Next, 30 parts by weight of aluminum hydroxide, 30 parts by weight of clay, 1.5 parts by weight of silicone foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 100 parts by weight of the composition, acid neutralizer As a result, 5 parts by weight of barium carbonate was added to prepare a phenolic resole resin composition, which was allowed to stand for 6 hours.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of the above (1) preliminarily adjusted to 20 ° C., 18 parts by weight of n-pentane preliminarily adjusted to 20 ° C., and preliminarily adjusted to 20 ° C. After adding 66 parts by weight of 67% phenolsulfonic acid having an acid value of 260 mgKOH / g and mixing with a homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.) at 5000 rpm for 30 seconds, the carbonate immediately decomposes. Formula: Y = Foam was not obtained because it was not within the range of 0.0034X + 2.167 or less and was not cured.

比較例2
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、キシレンスルホン酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム30重量部、クレー30重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、酸中和剤として炭酸カルシウム6重量部を添加してフェノール系レゾール樹脂組成物を調製し、6時間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したシクロペンタン9.0重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸60重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合中に炭酸塩の分解が急激に起こり 式: Y=0.0034X+2.167以下の範囲に入らず硬化しないため発泡体が得られなかった。
Comparative Example 2
(1) Preparation of phenol-based resol resin composition 4451 g of phenol and 5135 g of 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, then xylene sulfonic acid was added to adjust the pH to 6.3, and the dehydration rate was 29 under reduced pressure. It was dehydrated and concentrated to 0.0% by weight to obtain 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50. Next, 30 parts by weight of aluminum hydroxide, 30 parts by weight of clay, 1.5 parts by weight of silicone foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 100 parts by weight of the resin, and acid neutralizer A phenolic resole resin composition was prepared by adding 6 parts by weight of calcium carbonate and allowed to stand for 6 hours.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of the above (1) preliminarily adjusted to 20 ° C, 9.0 parts by weight of cyclopentane preliminarily adjusted to 20 ° C, preliminarily warmed to 20 ° C 60 parts by weight of 67% phenolsulfonic acid with a prepared acid value of 260 mgKOH / g was charged, and decomposition of carbonate occurred suddenly during mixing for 30 seconds at 5000 rpm with a homodisper (trade name, mixer manufactured by Tokushu Kika Kogyo Co., Ltd.) : Since it did not enter into the range of Y = 0.0034X + 2.167 or less and was not cured, a foam was not obtained.

比較例3
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、蟻酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム30重量部、クレー30重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、酸中和剤として炭酸バリウム8重量部を添加してフェノール系レゾール樹脂組成物を調製し、6時間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したHCFC−141b 18重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸42重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したのち、ただちにディスポカップを60°の角度で10秒間傾けて予め70℃に温調したアルミ製モールド(容積:300mm×300mm×50mm)に均一に散布した後、蓋を4箇所で固定し、70℃乾燥機中で10分間加熱後脱型したが硬化不足のため発泡体が得られなかった。
Comparative Example 3
(1) Preparation of phenol-based resol resin composition 4451 g of phenol and 5135 g of 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, then formic acid was added to adjust the pH to 6.3, and the dehydration rate was 29.0 under reduced pressure. After dehydrating and concentrating to weight percent, 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50 was obtained. Next, 30 parts by weight of aluminum hydroxide, 30 parts by weight of clay, 1.5 parts by weight of silicone foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 100 parts by weight of the resin, and acid neutralizer A phenolic resole resin composition was prepared by adding 8 parts by weight of barium carbonate and allowed to stand for 6 hours.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of the above (1) preliminarily adjusted to 20 ° C., 18 parts by weight of HCFC-141b preliminarily adjusted to 20 ° C., preliminarily adjusted to 20 ° C. After charging 42 parts by weight of 67% phenolsulfonic acid with an acid value of 260 mgKOH / g and mixing with a homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.) for 30 seconds at 5000 rpm, the disposable cup was immediately put at an angle of 60 °. After spraying uniformly on an aluminum mold (volume: 300 mm x 300 mm x 50 mm) that has been preliminarily adjusted to 70 ° C by inclining for 10 seconds, the lid is fixed at four places, heated in a 70 ° C dryer for 10 minutes, and then demolded However, a foam could not be obtained due to insufficient curing.

比較例4
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、50%パラトルエンスルホン酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム92.7重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、9%硫酸カリウム水溶液12重量部、酸中和剤として炭酸バリウム12重量部を添加してフェノール系レゾール樹脂組成物を調製し、10分間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したシクロペンタン 7.8重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸60重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したが、フェノール樹脂固形分に対する炭酸バリウム量が過剰なため、混合中に炭酸塩の分解が急激に起こり 発泡体が得られなかった。
(3)成形した発泡体を室温20℃、湿度65%の雰囲気下に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。
Comparative Example 4
(1) Preparation of phenol-based resole resin composition 4451 g of phenol and 5135 g of a 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, and then 50% paratoluenesulfonic acid was added to adjust the pH to 6.3. A dehydration rate of 29.0% by weight was obtained by dehydration and concentration to obtain 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50. Next, 92.7 parts by weight of aluminum hydroxide, 1.5 parts by weight of silicone-based foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 12 parts by weight of 9% aqueous potassium sulfate solution with respect to 100 parts by weight of the resin Then, 12 parts by weight of barium carbonate as an acid neutralizer was added to prepare a phenol-based resole resin composition, which was allowed to stand for 10 minutes.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of the above (1) preliminarily adjusted to 20 ° C., 7.8 parts by weight of cyclopentane preliminarily adjusted to 20 ° C., preliminarily warmed to 20 ° C. 60 parts by weight of 67% phenolsulfonic acid having a prepared acid value of 260 mgKOH / g was charged and mixed with homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.) at 5000 rpm for 30 seconds. The amount of barium carbonate relative to the phenol resin solid content Because of the excess, carbonate decomposed rapidly during mixing, and no foam was obtained.
(3) The molded foam was allowed to stand for 5 days in an atmosphere at room temperature of 20 ° C. and humidity of 65%, and various physical properties were measured in accordance with JIS A-9511.

比較例5
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、50%パラトルエンスルホン酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム92.7重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量部、9%硫酸カリウム水溶液12重量部、酸中和剤として炭酸バリウム6.8重量部を添加してフェノール系レゾール樹脂組成物を調製し、1分間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したシクロペンタン 7.8重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸60重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したが、放置時間が1分であったため混合中に炭酸塩の分解が急激に起こり 発泡体が得られなかった。
(3)成形した発泡体を室温20℃、湿度65%の雰囲気下に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。
Comparative Example 5
(1) Preparation of phenol-based resole resin composition 4451 g of phenol and 5135 g of a 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, and then 50% paratoluenesulfonic acid was added to adjust the pH to 6.3. A dehydration rate of 29.0% by weight was obtained by dehydration and concentration to obtain 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50. Next, 92.7 parts by weight of aluminum hydroxide, 1.5 parts by weight of silicone-based foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 12 parts by weight of 9% aqueous potassium sulfate solution with respect to 100 parts by weight of the resin Then, 6.8 parts by weight of barium carbonate as an acid neutralizer was added to prepare a phenol-based resol resin composition, which was allowed to stand for 1 minute.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of the above (1) preliminarily adjusted to 20 ° C., 7.8 parts by weight of cyclopentane preliminarily adjusted to 20 ° C., preliminarily warmed to 20 ° C. 60 parts by weight of 67% phenolsulfonic acid having a prepared acid value of 260 mgKOH / g was charged and mixed with a homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.) at 5000 rpm for 30 seconds, but the standing time was 1 minute. During mixing, carbonate decomposition suddenly occurred and no foam was obtained.
(3) The molded foam was allowed to stand for 5 days in an atmosphere at room temperature of 20 ° C. and humidity of 65%, and various physical properties were measured in accordance with JIS A-9511.

比較例6
(1)フェノール系レゾール樹脂組成物の調製
フェノール4451g、41.5重量%ホルマリン水溶液5135gを還流管、攪拌機付き反応缶中に仕込み、攪拌を開始する。触媒として25%水酸化ナトリウム水溶液を添加後85℃まで昇温させ、同温度で70分間反応させた後、50%パラトルエンスルホン酸を添加してpHを6.3に調整し、減圧下に脱水率29.0重量%まで脱水濃縮してモル比(ホルムアルデヒド/フェノール)が1.50の液状フェノール系レゾール樹脂6800gを得た。次いで、該樹脂100重量部に対して水酸化アルミニウム92.7重量部、シリコーン系整泡剤SH−193(東レ・ダウコーニングシリコーン社製)1.5重量
部、9%硫酸カリウム水溶液12重量部、酸中和剤として炭酸バリウム11重量部を添加してフェノール系レゾール樹脂組成物を調製し、10分間放置した。
(2)1000mlディスポカップに、予め20℃に温調した上記(1)のフェノール系レゾール樹脂組成物600重量部、予め20℃に温調したシクロペンタン 7.8重量部、予め20℃に温調した酸価260mgKOH/gの67%フェノールスルホン酸24重量部を仕込み、ホモディスパー(商品名、特殊機化工業社製ミキサー)で5000rpmで30秒間混合したが、硬化剤投入後のpHの落ち込みが少なく、混合中に炭酸塩の分解によるクリームが起こり、発泡体が得られなかった。
(3)成形した発泡体を室温20℃、湿度65%の雰囲気下に5日間放置した後、諸物性をJIS A‐9511に準拠して測定した。
比較例1〜3の結果を表3に、比較例4〜6の結果を表4に示す。表中、pH変化はフェノール系樹脂組成物のpHの変化量を示す。
Comparative Example 6
(1) Preparation of phenol-based resole resin composition 4451 g of phenol and 5135 g of a 41.5 wt% formalin aqueous solution are charged into a reflux tube and a reactor equipped with a stirrer, and stirring is started. After adding a 25% aqueous sodium hydroxide solution as a catalyst, the temperature was raised to 85 ° C. and reacted at the same temperature for 70 minutes, and then 50% paratoluenesulfonic acid was added to adjust the pH to 6.3. A dehydration rate of 29.0% by weight was obtained by dehydration and concentration to obtain 6800 g of a liquid phenolic resole resin having a molar ratio (formaldehyde / phenol) of 1.50. Next, 92.7 parts by weight of aluminum hydroxide, 1.5 parts by weight of silicone-based foam stabilizer SH-193 (manufactured by Toray Dow Corning Silicone), 12 parts by weight of 9% aqueous potassium sulfate solution with respect to 100 parts by weight of the resin Then, 11 parts by weight of barium carbonate as an acid neutralizing agent was added to prepare a phenolic resole resin composition, which was allowed to stand for 10 minutes.
(2) In a 1000 ml disposable cup, 600 parts by weight of the phenolic resole resin composition of the above (1) preliminarily adjusted to 20 ° C., 7.8 parts by weight of cyclopentane preliminarily adjusted to 20 ° C., preliminarily warmed to 20 ° C. 24 parts by weight of 67% phenol sulfonic acid with a prepared acid value of 260 mgKOH / g was added and mixed for 30 seconds at 5000 rpm with a homodisper (trade name, a mixer manufactured by Tokushu Kika Kogyo Co., Ltd.). There was little, and the cream by decomposition | disassembly of carbonate occurred during mixing, and the foam was not obtained.
(3) The molded foam was allowed to stand for 5 days in an atmosphere at room temperature of 20 ° C. and humidity of 65%, and various physical properties were measured in accordance with JIS A-9511.
The results of Comparative Examples 1 to 3 are shown in Table 3, and the results of Comparative Examples 4 to 6 are shown in Table 4. In the table, pH change indicates the amount of change in pH of the phenolic resin composition.

Figure 2005120337
注)
・ 硫黄(S)、カリウム(K)、ナトリウム(Na)の各元素は蛍光X線分析にて測定し
た。
・ フォーム物性の密度はJIS A−9511に準拠して測定した。
・ フォームpHは室温20℃、湿度65%に5日間放置した後、フォーム中央部から
カッターナイフで3〜5mm角にフォームをカットし0.1gを200mlビーカーに
秤り取った。次いで蒸留水100mlを入れ、15分間マグネティックスターラーに
て攪拌した。(攪拌は浮いているフォームを巻き込むぐらいに激しく行なった) 攪拌
終了後、ろ過を行い、ろ液をpHメーター計にて測定した。
・ 鋼鈑の腐蝕性及び鋼鈑表面の変色試験は両面0.5mm厚の亜鉛鋼鈑で接着された
発泡体をポリ袋へ入れ密閉した。次いで、80℃の乾燥機内に1ヶ月間放置後、腐蝕
の進行及び鋼鈑表面の変色を目視にて観察した。
Figure 2005120337
note)
• Each element of sulfur (S), potassium (K), and sodium (Na) was measured by fluorescent X-ray analysis.
-The density of the physical properties of the foam was measured according to JIS A-9511.
The foam pH was left at room temperature of 20 ° C. and humidity of 65% for 5 days, then the foam was cut into 3 to 5 mm square from the center of the foam with a cutter knife, and 0.1 g was weighed into a 200 ml beaker. Next, 100 ml of distilled water was added and the mixture was stirred with a magnetic stirrer for 15 minutes. (Stirring was carried out vigorously enough to involve the floating foam.) After completion of stirring, filtration was performed and the filtrate was measured with a pH meter.
・ In the corrosion test of the steel plate and the discoloration test on the surface of the steel plate, a foam bonded with a 0.5 mm thick zinc steel plate on both sides was placed in a plastic bag and sealed. Next, after standing in a dryer at 80 ° C. for 1 month, the progress of corrosion and the discoloration of the steel plate surface were visually observed.

Figure 2005120337
Figure 2005120337

表1、表2、表3、表4の結果より、本発明の製造方法によるフェノール系樹脂発泡体は、セルおよび硬化の状態も良好でフォーム物性も優れていることが判る。   From the results of Table 1, Table 2, Table 3, and Table 4, it can be seen that the phenolic resin foam produced by the production method of the present invention has good cell and cured conditions and excellent foam properties.

Claims (15)

フェノール系樹脂組成物に発泡剤、酸性硬化剤を配合し、発泡、硬化させてフェノール系樹脂発泡体を製造するに際して、フェノール系樹脂組成物に酸性硬化剤を添加した該組成物のpH値が、式: Y=0.0034X+2.167(式1) で示される値以下の範囲にあることを特徴とする酸性硬化型フェノール系樹脂発泡体の製造方法。
ここで示した式1は、フェノール系樹脂組成物中の酸中和剤、充填剤などにより酸性硬化剤が経時的に消費されることで起こるpH変化を、一定温度に調整したフェノール系樹脂組成物に酸性硬化剤を添加した後の経過時間(X:秒、0≦X≦120)と、pH値(Y)との関係を一定条件で測定したものである。
When a phenolic resin composition is blended with a foaming agent and an acidic curing agent, and foamed and cured to produce a phenolic resin foam, the pH value of the composition obtained by adding the acidic curing agent to the phenolic resin composition is Formula: Y = 0.0034X + 2.167 (Formula 1) It exists in the range below the value shown by these. The manufacturing method of the acid curable phenolic resin foam characterized by the above-mentioned.
Formula 1 shown here is a phenolic resin composition in which pH change caused by consumption of an acidic curing agent over time by an acid neutralizing agent, a filler, etc. in a phenolic resin composition is adjusted to a constant temperature. The relationship between the elapsed time (X: seconds, 0 ≦ X ≦ 120) after adding the acidic curing agent to the product and the pH value (Y) is measured under a certain condition.
硫酸塩を含有することを特徴とする請求項1に記載の酸性硬化型フェノール系樹脂発泡体の製造方法。   The method for producing an acid curable phenolic resin foam according to claim 1, comprising a sulfate. 酸中和剤として金属粉末、アルミニウム化合物、アルカリ金属またはアルカリ土類金属の炭酸塩、重炭酸塩、酸化物、水酸化物からなる群の少なくとも1種を配合することを特徴とする請求項1または2に記載の酸性硬化型フェノール系樹脂発泡体の製造方法。   2. The acid neutralizing agent according to claim 1, wherein at least one member selected from the group consisting of metal powder, aluminum compound, alkali metal or alkaline earth metal carbonate, bicarbonate, oxide, and hydroxide is blended. Or the manufacturing method of the acid curable phenolic resin foam of 2. 硫酸塩が硫酸カリウム及び/または硫酸ナトリウムである請求項1〜3のいずれか1項に記載の酸性硬化型フェノール系樹脂発泡体の製造方法。   The method for producing an acidic curable phenolic resin foam according to any one of claims 1 to 3, wherein the sulfate is potassium sulfate and / or sodium sulfate. 酸中和剤が炭酸バリウムで、発泡剤がシクロペンタンである請求項4に記載の酸性硬化型フェノール系樹脂発泡体の製造方法。   The method for producing an acid curable phenolic resin foam according to claim 4, wherein the acid neutralizer is barium carbonate and the foaming agent is cyclopentane. フェノール系樹脂の固形分100重量部に対する、硫酸カリウム及び/または硫酸ナトリウムの含有量が、2.0重量部以下であり、炭酸バリウムの含有量が15.0重量部以下である請求項4に記載の酸性硬化型フェノール系樹脂発泡体の製造方法。   The content of potassium sulfate and / or sodium sulfate with respect to 100 parts by weight of the solid content of the phenolic resin is 2.0 parts by weight or less, and the content of barium carbonate is 15.0 parts by weight or less. The manufacturing method of the acidic curable phenol-type resin foam of description. フェノール系樹脂組成物に発泡剤、酸性硬化剤を添加、混合後のゲル化時間(Y1)と
硬化剤量(X1)が式: Y1=−X1+16(式2) で示される値以下の範囲にあるこ
とを特徴とする請求項4〜6のいずれか1項に記載の酸性硬化型フェノール系樹脂発泡体の製造方法。
ここで示した式2は、液温20℃、乾燥温度65℃の条件下で測定したゲル化時間(Y1分)とフェノール系樹脂の固形分100重量部に対する硬化剤量(X1重量部)の関係を表したものである。
A foaming agent and an acidic curing agent are added to the phenolic resin composition, and the gelation time (Y 1 ) and the amount of the curing agent (X 1 ) after mixing are represented by the formula: Y 1 = −X 1 +16 (Formula 2) It exists in the range below a value, The manufacturing method of the acid-curable phenolic resin foam of any one of Claims 4-6 characterized by the above-mentioned.
Formula 2 shown here is a gelling time (Y 1 minute) measured under conditions of a liquid temperature of 20 ° C. and a drying temperature of 65 ° C., and the amount of curing agent (X 1 part by weight) relative to 100 parts by weight of the solid content of the phenol resin. ).
フェノール系樹脂組成物に硫酸カリウム及び/または硫酸ナトリウムと、炭酸バリウムを添加、混合後、10分以上経過した後に発泡剤、酸性硬化剤を添加、混合することを特徴とする請求項7に記載の酸性硬化型フェノール系樹脂発泡体の製造方法。   8. The foaming agent and the acidic curing agent are added and mixed after 10 minutes or more have elapsed after adding and mixing potassium sulfate and / or sodium sulfate and barium carbonate to the phenolic resin composition. Of producing an acid-curable phenolic resin foam. フェノール系樹脂組成物に硫酸カリウム及び/または硫酸ナトリウムと、炭酸バリウムを添加、混合後、10分以上経過した後に発泡剤、酸性硬化剤を添加、混合した後の、ゲル化時間(Y2)と硬化剤量(X2)が式: Y2=−0.75X2+14.5(式3) で示される値以下の範囲にあることを特徴とする請求項8に記載の酸性硬化型フェノール系樹脂発泡体の製造方法。
ここで示した式3は、液温20℃、乾燥温度65℃の条件下で測定した、ゲル化時間(Y2分)とフェノール系樹脂の固形分100重量部に対する硬化剤量(X2重量部)の関係を表したものである。
Gelation time (Y 2 ) after adding and mixing foaming agent and acidic curing agent after 10 minutes or more after adding and mixing potassium sulfate and / or sodium sulfate and barium carbonate to phenolic resin composition And the amount of the curing agent (X 2 ) is in the range of the value represented by the formula: Y 2 = −0.75X 2 +14.5 (Formula 3) Of producing a resin-based resin foam.
Equation 3 shown here is the gelling time (Y 2 minutes) and the amount of curing agent (X 2 weights) with respect to 100 parts by weight of the solid content of the phenolic resin, measured under conditions of a liquid temperature of 20 ° C. and a drying temperature of 65 ° C. Part)).
硫酸カリウム及び/または硫酸ナトリウムを、水溶液又は含水アルコール溶液として添
加することを特徴とする請求項9に記載の酸性硬化型フェノール系樹脂発泡体の製造方法。
The method for producing an acid curable phenolic resin foam according to claim 9, wherein potassium sulfate and / or sodium sulfate is added as an aqueous solution or a hydrous alcohol solution.
硫酸カリウム及び/または硫酸ナトリウムの水溶液ないしは含水アルコール溶液と、炭酸バリウムとを予め混合した後に添加することを特徴とする請求項5に記載の酸性硬化型フェノール樹脂発泡体の製造方法。 6. The method for producing an acidic curable phenolic resin foam according to claim 5, wherein an aqueous solution or a hydrous alcohol solution of potassium sulfate and / or sodium sulfate and barium carbonate are added after being mixed in advance. フェノール樹脂組成物に発泡剤、酸性硬化剤を添加、混合した後のクリームタイムが10秒以上であることを特徴とする請求項4、5、10、または11のいずれかに記載の酸性硬化型フェノール系樹脂発泡体の製造方法。 The acid curable mold according to any one of claims 4, 5, 10, or 11, wherein a cream time after adding and mixing a foaming agent and an acidic curing agent to the phenol resin composition is 10 seconds or more. A method for producing a phenolic resin foam. フォーム特性が、密度が10〜500kg/m3、pHが4以上、吸水量が1〜15g
/100cm2、であり、フォーム中に硫黄元素とカリウム元素及び/またはナトリウム
元素を含むことを特徴とする酸性硬化型フェノール系樹脂発泡体。
Foam characteristics with a density of 10 to 500 kg / m 3 , a pH of 4 or more, and a water absorption of 1 to 15 g.
/ 100 cm 2 , and an acidic curable phenolic resin foam characterized by containing sulfur element and potassium element and / or sodium element in the foam.
請求項1〜12のいずれかに記載の製造方法により製造され、フォーム特性が、密度が10〜500kg/m3、pHが4以上、吸水量が1〜15g/100cm2、であり、フォーム中に硫黄元素とカリウム元素及び/またはナトリウム元素を含むことを特徴とする酸性硬化型フェノール系樹脂発泡体。 It is manufactured with the manufacturing method in any one of Claims 1-12, A foam characteristic is a density of 10-500 kg / m < 3 >, pH is 4 or more, and a water absorption is 1-15 g / 100cm < 2 >, In foam An acidic curable phenolic resin foam characterized by containing sulfur element and potassium element and / or sodium element. 両面または片面が、繊維、金属、無機物の群から選ばれる1種以上の面材で被覆されて
なる請求項13または14に記載の酸性硬化型フェノール系樹脂発泡体。

The acid-curable phenolic resin foam according to claim 13 or 14, wherein both surfaces or one surface are coated with one or more kinds of face materials selected from the group consisting of fibers, metals, and inorganic substances.

JP2004111490A 2003-09-26 2004-04-05 Acid-curable phenolic resin foam and its manufacturing method Pending JP2005120337A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004111490A JP2005120337A (en) 2003-09-26 2004-04-05 Acid-curable phenolic resin foam and its manufacturing method

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2003335911 2003-09-26
JP2004111490A JP2005120337A (en) 2003-09-26 2004-04-05 Acid-curable phenolic resin foam and its manufacturing method

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2006346667A Division JP2007131859A (en) 2003-09-26 2006-12-22 Acid-curable phenol resin foam and method for producing the same

Publications (1)

Publication Number Publication Date
JP2005120337A true JP2005120337A (en) 2005-05-12

Family

ID=34622099

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004111490A Pending JP2005120337A (en) 2003-09-26 2004-04-05 Acid-curable phenolic resin foam and its manufacturing method

Country Status (1)

Country Link
JP (1) JP2005120337A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007029222A1 (en) 2005-09-08 2007-03-15 Kingspan Holdings (Irl) Limited Phenolic foam
WO2007029221A1 (en) 2005-09-08 2007-03-15 Kingspan Holdings (Irl) Limited A phenolic foam
JP2007070508A (en) * 2005-09-08 2007-03-22 Nitto Boseki Co Ltd Phenol resin-foamed article and method for producing the same
KR20150134939A (en) * 2014-05-23 2015-12-02 코오롱인더스트리 주식회사 Expandable Phenolic Resin Composition and Phenolic Foam Prepared Thereform
WO2022255292A1 (en) * 2021-05-31 2022-12-08 旭有機材株式会社 Resin composition for phenol foam and foam

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007029222A1 (en) 2005-09-08 2007-03-15 Kingspan Holdings (Irl) Limited Phenolic foam
WO2007029221A1 (en) 2005-09-08 2007-03-15 Kingspan Holdings (Irl) Limited A phenolic foam
JP2007070508A (en) * 2005-09-08 2007-03-22 Nitto Boseki Co Ltd Phenol resin-foamed article and method for producing the same
EP1922356B1 (en) * 2005-09-08 2012-10-03 Kingspan Holdings (IRL) Limited A phenolic foam
US8765829B2 (en) 2005-09-08 2014-07-01 Kingspan Holdings (Irl) Limited Phenolic foam
KR20150134939A (en) * 2014-05-23 2015-12-02 코오롱인더스트리 주식회사 Expandable Phenolic Resin Composition and Phenolic Foam Prepared Thereform
KR102183988B1 (en) * 2014-05-23 2020-11-27 코오롱인더스트리 주식회사 Expandable Phenolic Resin Composition and Phenolic Foam Prepared Thereform
WO2022255292A1 (en) * 2021-05-31 2022-12-08 旭有機材株式会社 Resin composition for phenol foam and foam

Similar Documents

Publication Publication Date Title
JP2007131859A (en) Acid-curable phenol resin foam and method for producing the same
CA2814935C (en) Phenol resin foamed plate
WO2020031863A1 (en) Resin composition for phenolic foam production
JP2021008564A (en) Resin composition for manufacturing phenol foam and phenol foam and its manufacturing method
JP2007070506A (en) Phenol resin-foamed article
JP2007070508A (en) Phenol resin-foamed article and method for producing the same
US20100204351A1 (en) Phenolic novolac foams and compositions for preparing them
JP2005120337A (en) Acid-curable phenolic resin foam and its manufacturing method
JP4878672B2 (en) Foamable phenolic resole resin composition and method for producing the same
JPH07278339A (en) Production of predominantly closed-cell phenolic resin foam
AU2021217298B2 (en) Phenolic Resin Foam Laminate Board
JP4060694B2 (en) Foamable resol-type phenolic resin composition and phenolic resin foam using the same
JP2005054026A (en) Foam with reduced emission of formaldehyde and method for producing the same
JP2873167B2 (en) Method for producing phenolic resin foam
JP4170163B2 (en) Phenol foam raw material composition, phenol foam using the same, and method for producing the same
JP3555012B2 (en) Phenolic resin foamable composition and method for producing foam using the composition
JP2845641B2 (en) Method for producing phenolic resin foam and its application
JP5412018B2 (en) Foamable composition for polyurethane foam, polyurethane foam, and method for producing polyurethane foam
WO2020080149A1 (en) Flame-retardant phenolic-resin composition and flame-retardant material obtained therefrom
JP7221083B2 (en) Method for producing phenolic resin foam
JP2514879B2 (en) Fireproof phenolic resin foamable composition and method for producing foam
WO2023204283A1 (en) Foamed phenolic-resin object and laminate thereof
JP2010138219A (en) Method for producing phenolic resin foam
JP2006152094A (en) Phenol resin foam and its manufacturing process
JP2002338784A (en) Expandable phenolic resol resin composition

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050729

A871 Explanation of circumstances concerning accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A871

Effective date: 20050729

A975 Report on accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A971005

Effective date: 20050812

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20051005

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20051205

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060222

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060424

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060531

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060731

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20061025

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20061124

A911 Transfer to examiner for re-examination before appeal (zenchi)

Free format text: JAPANESE INTERMEDIATE CODE: A911

Effective date: 20070221

A912 Re-examination (zenchi) completed and case transferred to appeal board

Free format text: JAPANESE INTERMEDIATE CODE: A912

Effective date: 20070413