JPH0583574B2 - - Google Patents
Info
- Publication number
- JPH0583574B2 JPH0583574B2 JP15029689A JP15029689A JPH0583574B2 JP H0583574 B2 JPH0583574 B2 JP H0583574B2 JP 15029689 A JP15029689 A JP 15029689A JP 15029689 A JP15029689 A JP 15029689A JP H0583574 B2 JPH0583574 B2 JP H0583574B2
- Authority
- JP
- Japan
- Prior art keywords
- phenolic resin
- resin
- resol
- resol type
- resorcinol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
〔産業上の利用分野〕
本発明は速硬化、低臭気、低収縮性を要求され
るレゾール型フエノール樹脂発泡性組成物に関す
るものである。
〔従来の技術〕
一般にレゾール型フエノール樹脂発泡体の製造
にはフエノール類とアルデヒド類を用いたレゾー
ル型フエノール樹脂が使用されており、これに界
面活性剤、発泡剤、及び酸硬化剤を混合して室温
から100℃の雰囲気温度において製造されている。
レゾール型フエノール樹脂発泡体の硬化性を決
定する因子には、レゾール型フエノール樹脂の特
性、温度、酸硬化剤の種類、及び使用量等があり
そのどれもが重大な意味を有している。
従来、レゾール型フエノール樹脂発泡体の製造
において硬化速度を改善する場合には、主として
温度の調整、硫酸、塩酸等の無機酸及びトルエン
スルホン酸、フエノールスルホン酸等の有機酸の
併用、使用量の調整により対応されているが、こ
れらの対策のみでは満足な発泡体を得ることは難
しい。また、レゾール型アルキルフエノール樹脂
にレゾルシンを予備反応させ、これとレゾール型
フエノール樹脂を併用する方法が提案されている
(特開昭61−95038)が、この方法では硬化速度を
改善する場合には前記と同様の対応をしなければ
ならず、対応を行つても満足な発泡体を得ること
は難しい。更に、水溶液または固体のレゾルシン
をレゾール型フエノール樹脂に添加する方法が提
案されている(特公昭46−41712)が、この方法
においてはレゾルシンのレゾール型フエノール樹
脂との反応能力が高く、常温においても網状構造
を形成するために安定性が著しく悪化し、その使
用は困難である。
〔発明が解決しようとする課題〕
レゾール型フエノール樹脂を速硬化型にする場
合、温度を上げる、酸硬化剤の量を増加する、よ
り強い酸を使用することなどが挙げられるが、こ
の場合硬化時に放出されるアルデヒド、水蒸気が
多く、この臭気のため作業環境が悪化する。更
に、発泡体が一次収縮により変形し、発泡体中の
残存酸が多く他の部材を腐蝕するという問題があ
る。
従つて、速硬化性を要求されるフエノール樹脂
発泡体分野では作業環境を悪化する臭気、及び収
縮による発泡体の変形等の問題を生じ、適当な発
泡体が得られない。本発明は前記した如き、諸欠
点を削除した速硬化性を要求されるレゾール型フ
エノール樹脂発泡性組成物を提供しようとするも
のである。
〔課題を解決するための手段〕
即ち、本発明はレゾール型フエノール系樹脂に
界面活性剤、発泡剤、及び酸硬化剤を配合してな
るフエノール樹脂発泡性組成物において、前記レ
ゾール型フエノール系樹脂としてレゾール型レゾ
ルシン樹脂、レゾール型レゾルシンフエノール樹
脂又はこれらの樹脂とレゾール型フエノール樹脂
との混合物から選ばれるレゾール型レゾルシン系
フエノール樹脂を用い且つ前記レゾール型レゾル
シン系フエノール樹脂中のレゾルシン含有率が2
〜60重量%になるように使用することによつて、
樹脂貯蔵安定性が良好で、発泡硬化速度を速く
し、しかも多量の臭気、発泡体の収縮変化を発現
させることなく発泡体が得られることを見い出し
本発明に到達した。
〔作用〕
本発明で用いられるレゾルシンとアルデヒド類
を用いたレゾール型レゾルシン系フエノール樹脂
の作用は、分子構造中にフエノール性水酸基を
1、3位に有している為、オルト、バラ位の反応
性が高く、この事からその架橋重合反応が速くな
り、反応途中に発生するアルデヒドとも反応し、
また、架橋点の密度が多くなり一次収縮を抑制す
るものと考えられる。しかし、本発明の範囲であ
る樹脂中のレゾルシンが2重量%未満の場合、そ
の効果は期待できない。また、60重量%を越える
場合も同様であり特に一次収縮について顕著であ
る。
本発明のレゾール型レゾルシン系フエノール樹
脂とはレゾルシンとアルデヒド類を縮合させたレ
ゾール型レゾルシン樹脂、それにフエノールを共
縮合させたレゾール型レゾルシンフエノール樹
脂、及びこれらの樹脂とレゾール型フエノール樹
脂との混合物を意味し、レゾルシン2〜60重量%
は、それら樹脂または樹脂混合物中のレゾルシン
の含有率である。
本発明において使用されるレゾルシンとアルデ
ヒド類を用いたレゾール型レゾルシン樹脂は、レ
ゾルシン1モルに対してアルデヒド類1.5〜3モ
ルをアルカリ金属またはアルカリ土類金属触媒の
存在下、10〜100℃好ましくは20〜80℃で、1〜
7時間好ましくは2〜5時間反応させた後、無機
酸または有機酸によりPHを4.0〜8.0に中和され
る。その後、減圧脱水により系内の水分を適当な
量まで除去して得られるものである。レゾルシン
との反応に使用されるアルデヒド類としてはホル
ムアルデヒド、バラホルムアルデヒド、ポリオキ
シメチレン、トリオキサン等が適当である。
本発明に用いられる発泡剤としては、ペンタ
ン、塩化メチレン、トリクロロフルオロエタン、
テトラフルオロメタン、1,1,2−トリクロロ
−1,2,2−トリフルオロエタン等の揮発性有
機液体が挙げられる。勿論これらは混合物として
用いても良い。
これらの発泡剤は樹脂100重量部に対して5〜
40重量部の範囲で使用することが望ましい。
本発明に用いられる界面活性剤としては、シリ
コーン系エチレンオキサイド、プロピレンオキサ
イド共重合体、ソルビタン、アルキルフエノー
ル、ひまし油等のポリオキシアルキレン付加物な
どの界面活性剤が挙げられる。これらは混合して
使用することも可能であり、その使用量は樹脂
100重量部に対して0.5〜10重量部の範囲で使用す
ることが出来る。
本発明に用いられる酸硬化剤としては、硫酸、
塩酸等の無機酸、及びトルエンスルホン酸、フエ
ノールスルホン酸等の有機酸が挙げられる。これ
らは混合して使用することも可能であり、その使
用量は樹脂100重量部に対して5〜100重量部、好
ましくは10〜50重量部の範囲で使用することが出
来る。
本発明におけるレゾール型フエノール樹脂発泡
体は、レゾルシンとして樹脂中に2〜60重量%含
有するようにレゾール型レゾルシン系フエノール
樹脂を使用し、界面活性剤、発泡剤、及び酸硬化
剤を混合した後、発泡硬化して発泡体が製造され
る。混合は高速撹拌機(ホモデイスパー等)を用
いて2〜60秒間、硬化化反応に合わせた撹拌を行
うか、もしくはスプレー発泡、現場発泡のように
スプレー等による噴霧混合を行つてもよい。だだ
し、被着面がある角度を持つ場合、吹き付けたレ
ゾール型フエノール樹脂発泡性組成物が直ちに発
泡硬化されないとダレ(発泡性樹脂組成物が下方
に移動すること)を起こし、適正な発泡体が得ら
れない。
本発明のレゾール型フエノール樹脂発泡性組成
物を用いると、硬化速度が速くなり、臭気、収縮
等の問題の解決が容易である。発泡硬化は常温〜
100℃の雰囲気温度で実施される。
〔実施例〕
以下実施例をもつて具体的に説明する。
実施例 1
四口フラスコにフエノール2.0Kg、37%ホルム
アルデヒド2.93Kg(モル比1.7モル)及び触媒と
して20%苛性ソーダ60grを仕込み80℃で3時間反
応した後15%硫酸を用いてPHを7.0に中和し、減
圧脱水により樹脂中の水分を5%以下にした。
得られたレゾール型フエノール樹脂は樹脂固形
分80%、粘度3000cps/25℃、重量平均分子量430
であり、これを樹脂Aとして用いた。
更に、四口フラスコにレゾルシン2.0Kg、37%
ホルムアルデヒド2.51Kg(モル比1.7モル)及び
触媒として20%苛性ソーダ60grを仕込み40℃で3
時間反応した後15%硫酸を用いてPHを7.0に中和
し、減圧脱水により樹脂中の水分を10%以下にし
た。
得られたレゾール型レゾルシ樹脂は樹脂固形分
75%、粘度3000cps/25℃、重量平均分子量480で
あり、これを樹脂Bとして用いた。
得られた樹脂A50重量部、樹脂B50重量部、
Tween#
40(ポリオキシエチレンソルビタンパル
ミテート)2重量部、発泡剤として1,1,2−
トリクロロ−1,2,2−トリフルオロエタン20
重量部、更に65%フエノールスルホン酸20重量部
を高速撹拌機(4000〜6000rpm)で10秒間撹拌し
た後、幅50cm、長さ80cmのビニール袋内に入れ、
これを常温(雰囲気25℃)で放置し、発泡硬化を
完了して、レゾール型フエノール樹脂発泡体を得
た。
発泡硬化して発生した臭気は、北川式検知管を
用いて測定し、ビニール袋内のホルムアルデヒド
とフエノールの濃度はそれぞれ1ppm以下、
0.8ppmであつた。また、収縮率(発泡硬化終了
時の長さ×100/1日後の長さ)は2.2%であつ
た。
第1表に以上の結果を示す。
[Industrial Field of Application] The present invention relates to a resol-type phenolic resin foamable composition that is required to have fast curing, low odor, and low shrinkage. [Prior art] Generally, resol type phenolic resin using phenols and aldehydes is used to produce resol type phenolic resin foam, and a surfactant, a blowing agent, and an acid curing agent are mixed with this. It is manufactured at ambient temperatures ranging from room temperature to 100°C. Factors that determine the curability of a resol type phenolic resin foam include the characteristics of the resol type phenolic resin, temperature, the type of acid curing agent, and the amount used, all of which have important significance. Conventionally, in order to improve the curing speed in the production of resol type phenolic resin foams, the main methods were to adjust the temperature, to use inorganic acids such as sulfuric acid and hydrochloric acid in combination with organic acids such as toluenesulfonic acid and phenolsulfonic acid, and to control the amount used. Although these problems have been addressed through adjustment, it is difficult to obtain a satisfactory foam using only these measures. In addition, a method has been proposed in which a resol type alkyl phenol resin is pre-reacted with resorcin and this is used in combination with a resol type phenol resin (Japanese Patent Application Laid-Open No. 1983-95038), but this method does not work well when improving the curing speed. The same measures as above must be taken, and even if such measures are taken, it is difficult to obtain a satisfactory foam. Furthermore, a method has been proposed in which an aqueous solution or solid resorcin is added to a resol-type phenolic resin (Japanese Patent Publication No. 46-41712), but in this method, resorcin has a high reaction ability with a resol-type phenolic resin, and even at room temperature. Due to the formation of a network structure, the stability is significantly deteriorated and its use is difficult. [Problems to be Solved by the Invention] When making a resol type phenolic resin a fast-curing type, examples include raising the temperature, increasing the amount of acid curing agent, and using a stronger acid. A large amount of aldehyde and water vapor are released, and this odor worsens the working environment. Furthermore, there is a problem in that the foam is deformed due to primary shrinkage, and a large amount of residual acid in the foam corrodes other members. Therefore, in the field of phenolic resin foams that require fast curing properties, problems such as odor that worsens the working environment and deformation of the foam due to shrinkage occur, making it impossible to obtain a suitable foam. The present invention aims to provide a resol type phenolic resin foaming composition which eliminates the above-mentioned drawbacks and is required to have fast curing properties. [Means for Solving the Problems] That is, the present invention provides a phenolic resin foamable composition comprising a resol type phenolic resin mixed with a surfactant, a blowing agent, and an acid curing agent. A resol-type resorcinol-based phenolic resin selected from a resol-type resorcinol resin, a resol-type resorcinol-based phenolic resin, or a mixture of these resins and a resol-type phenolic resin is used as the resol-type resorcinol-based phenolic resin, and the resorcin content in the resol-type resorcinol-based phenolic resin is 2.
By using it at ~60% by weight,
The present invention was achieved by discovering that a foam can be obtained that has good resin storage stability, increases the foam curing speed, and does not generate a large amount of odor or change in shrinkage of the foam. [Function] The action of the resorcinol-based phenolic resin using resorcin and aldehydes used in the present invention is that it has phenolic hydroxyl groups at the 1st and 3rd positions in its molecular structure, so it reacts at the ortho and bala positions. This makes the cross-linking polymerization reaction faster, and it also reacts with aldehyde generated during the reaction.
It is also thought that the density of crosslinking points increases, thereby suppressing primary shrinkage. However, if the amount of resorcin in the resin is less than 2% by weight, which is within the scope of the present invention, the effect cannot be expected. The same applies when the amount exceeds 60% by weight, and the primary shrinkage is particularly noticeable. The resol-type resorcinol-based phenolic resin of the present invention includes a resol-type resorcinol resin in which resorcinol and aldehydes are condensed, a resol-type resorcinol-phenolic resin in which phenol is co-condensed with the resol-type resorcinol resin, and a mixture of these resins and a resol-type phenolic resin. meaning, resorcinol 2-60% by weight
is the content of resorcinol in the resin or resin mixture. The resol-type resorcinol resin using resorcin and aldehydes used in the present invention is prepared by adding 1.5 to 3 mol of aldehyde to 1 mol of resorcin in the presence of an alkali metal or alkaline earth metal catalyst at a temperature of preferably 10 to 100°C. At 20-80℃, 1-
After reacting for 7 hours, preferably 2 to 5 hours, the pH is neutralized to 4.0 to 8.0 with an inorganic or organic acid. Thereafter, water in the system is removed to an appropriate amount by dehydration under reduced pressure. Suitable aldehydes used in the reaction with resorcinol include formaldehyde, paraformaldehyde, polyoxymethylene, trioxane, and the like. The blowing agents used in the present invention include pentane, methylene chloride, trichlorofluoroethane,
Examples include volatile organic liquids such as tetrafluoromethane and 1,1,2-trichloro-1,2,2-trifluoroethane. Of course, these may be used as a mixture. These blowing agents are used in amounts of 5 to 100 parts by weight of resin.
It is desirable to use within the range of 40 parts by weight. Examples of the surfactant used in the present invention include surfactants such as silicone-based ethylene oxide, propylene oxide copolymer, sorbitan, alkylphenol, and polyoxyalkylene adducts such as castor oil. These can also be used in combination, and the amount used depends on the resin.
It can be used in a range of 0.5 to 10 parts by weight per 100 parts by weight. The acid curing agent used in the present invention includes sulfuric acid,
Examples include inorganic acids such as hydrochloric acid, and organic acids such as toluenesulfonic acid and phenolsulfonic acid. These can also be used as a mixture, and the amount used can range from 5 to 100 parts by weight, preferably from 10 to 50 parts by weight, based on 100 parts by weight of the resin. The resol type phenolic resin foam in the present invention uses a resol type resorcinol phenolic resin so that the resin contains 2 to 60% by weight as resorcinum, and after mixing a surfactant, a blowing agent, and an acid curing agent. , the foam is cured to produce a foam. Mixing may be performed using a high-speed stirrer (such as Homo Disper) for 2 to 60 seconds in accordance with the curing reaction, or may be mixed by spraying, such as spray foaming or in-situ foaming. However, if the surface to which it is applied has a certain angle, if the sprayed resol type phenolic resin foam composition is not foamed and cured immediately, it will sag (the foamable resin composition moves downward) and the foam will not be properly formed. is not obtained. When the resol type phenolic resin foamable composition of the present invention is used, the curing speed becomes faster and problems such as odor and shrinkage can be easily solved. Foaming hardens at room temperature
Performed at an ambient temperature of 100°C. [Example] The following is a concrete explanation using an example. Example 1 A four-necked flask was charged with 2.0 kg of phenol, 2.93 kg of 37% formaldehyde (mole ratio 1.7 mol), and 60 gr of 20% caustic soda as a catalyst, and after reacting at 80°C for 3 hours, the pH was adjusted to 7.0 using 15% sulfuric acid. The water content in the resin was reduced to 5% or less by dehydration under reduced pressure. The obtained resol type phenolic resin has a resin solid content of 80%, a viscosity of 3000 cps/25°C, and a weight average molecular weight of 430.
This was used as resin A. Furthermore, 2.0Kg of resorcinol, 37% in a four-necked flask.
2.51 kg of formaldehyde (mole ratio 1.7 mol) and 60 gr of 20% caustic soda as a catalyst were prepared and heated at 40°C.
After reacting for an hour, the pH was neutralized to 7.0 using 15% sulfuric acid, and the water content in the resin was reduced to 10% or less by dehydration under reduced pressure. The obtained resol type resorsi resin has a resin solid content
75%, viscosity 3000 cps/25°C, weight average molecular weight 480, and was used as resin B. Resin A 50 parts by weight, Resin B 50 parts by weight,
2 parts by weight of Tween #40 (polyoxyethylene sorbitan palmitate), 1,1,2- as a blowing agent
Trichloro-1,2,2-trifluoroethane 20
parts by weight and further 20 parts by weight of 65% phenolsulfonic acid were stirred for 10 seconds with a high-speed stirrer (4000 to 6000 rpm), and then placed in a plastic bag with a width of 50 cm and a length of 80 cm.
This was left to stand at room temperature (atmosphere 25°C) to complete foaming and curing to obtain a resol type phenolic resin foam. The odor generated by foam curing was measured using a Kitagawa detection tube, and the concentrations of formaldehyde and phenol in the plastic bag were each below 1 ppm.
It was 0.8ppm. Further, the shrinkage rate (length at the end of foaming and curing x 100/length after 1 day) was 2.2%. Table 1 shows the above results.
【表】【table】
【表】
実施例 2〜4、比較例 1〜8
実施例1の方法において、第1表の条件で発泡
体を製造し、物性を測定した。
実施例 5
四口フラスコにフエノール1.0Kg、レゾルシン
1.0Kg、37%ホルムアルデヒド2.72Kg(モル比1.7
モル)及び触媒として20%苛性ソーダ60grを仕込
み80℃で3時間反応した後15%硫酸を用いてPHを
7.0に中和し、減圧脱水により樹脂中の水分を5
%以下にした。
得られたレゾール型フエノール樹脂は樹脂固形
分80%、粘度2800cps/25℃、重量平均分子量460
であり、これを樹脂Cとして用いた。
得られた樹脂Cを実施例1の方法で第1表の条
件で発泡体を製造し、物性を測定した。
比較例 9
特開昭61−95038号公報に記載の実施例1に従
つてフエノール樹脂を製造し、得られた樹脂を樹
脂Dとして実施例1の方法において、第1表の条
件で発泡体を製造し、物性を測定した。
実施例 6
実施例1の配合で樹脂、発泡剤及び界面活性剤
を予め混合し、2成分系として実機スプレーマシ
ン(GRACO社製ハイドラキヤツトVRHC)を使
用し、幅50cm、長さ100cm、角度45゜の石膏ボード
の上に30sec(約1Kg)吐出し、発泡を行つた。そ
の結果を示す。[Table] Examples 2 to 4, Comparative Examples 1 to 8 In the method of Example 1, foams were produced under the conditions shown in Table 1, and their physical properties were measured. Example 5 1.0Kg of phenol and resorcinol in a four-necked flask
1.0Kg, 37% formaldehyde 2.72Kg (molar ratio 1.7
mol) and 60g of 20% caustic soda as a catalyst, reacted at 80℃ for 3 hours, and then adjusted the pH using 15% sulfuric acid.
Neutralize to 7.0 and remove water in the resin by vacuum dehydration.
% or less. The obtained resol type phenolic resin has a resin solid content of 80%, a viscosity of 2800 cps/25°C, and a weight average molecular weight of 460.
This was used as resin C. A foam was produced from the obtained resin C according to the method of Example 1 under the conditions shown in Table 1, and the physical properties were measured. Comparative Example 9 A phenolic resin was produced according to Example 1 described in JP-A-61-95038, and the resulting resin was used as Resin D to produce a foam in the method of Example 1 under the conditions shown in Table 1. It was manufactured and its physical properties were measured. Example 6 The resin, foaming agent, and surfactant were mixed in advance according to the formulation of Example 1, and a two-component system was used using an actual spray machine (Hydracat VRHC manufactured by GRACO), with a width of 50 cm, a length of 100 cm, and an angle of 45°. The foam was discharged for 30 seconds (approximately 1 kg) onto a plasterboard. The results are shown below.
【表】【table】
本発明のレゾール型フエノール樹脂発泡性組成
物は第1表から明らかな様に、樹脂貯蔵安定性が
良好であり、発泡硬化時間が改善され、更に発泡
硬化時間が短いことに依る幣害(臭気、収縮率)
が見られない。
しかも、従来の発泡硬化時間を容易に改善でき
るため、従来の製造機械におけるラインのスピー
ドアツプ及びスプレー発泡、現場発泡での製造が
行える。従つて建材用、家具用等に今後より幅広
く用いることが可能となつた。
As is clear from Table 1, the resol-type phenolic resin foamable composition of the present invention has good resin storage stability, improved foam curing time, and also has no odor caused by the short foam curing time. ,Shrinkage factor)
I can't see it. Moreover, since the conventional foam curing time can be easily improved, the line speed in conventional manufacturing machines can be increased and production can be performed by spray foaming or on-site foaming. Therefore, it has become possible to use it more widely in the future for building materials, furniture, etc.
Claims (1)
発泡剤、及び酸硬化剤を配合してなるフエノール
樹脂発泡性組成物において、前記レゾール型フエ
ノール系樹脂としてレゾール型レゾルシン樹脂、
レゾール型レゾルシンフエノール樹脂又はこれら
の樹脂とレゾール型フエノール樹脂との混合物か
ら選ばれるレゾール型レゾルシン系フエノール樹
脂を用い且つ前記レゾール型レゾルシン系フエノ
ール樹脂中のレゾルシン含有率が2〜60重量%に
なるように使用することを特徴とするレゾール型
フエノール樹脂発泡性組成物。1 Surfactant, resol type phenolic resin,
In the phenolic resin foamable composition containing a blowing agent and an acid curing agent, the resol type phenolic resin includes a resol type resorcinol resin,
A resol type resorcinol phenolic resin selected from a resol type resorcinol phenolic resin or a mixture of these resins and a resol type phenolic resin is used, and the resorcin content in the resol type resorcinol phenolic resin is 2 to 60% by weight. A resol type phenolic resin foamable composition characterized in that it is used for.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15029689A JPH0314843A (en) | 1989-06-13 | 1989-06-13 | Foamable phenol resin composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15029689A JPH0314843A (en) | 1989-06-13 | 1989-06-13 | Foamable phenol resin composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0314843A JPH0314843A (en) | 1991-01-23 |
| JPH0583574B2 true JPH0583574B2 (en) | 1993-11-26 |
Family
ID=15493899
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15029689A Granted JPH0314843A (en) | 1989-06-13 | 1989-06-13 | Foamable phenol resin composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0314843A (en) |
-
1989
- 1989-06-13 JP JP15029689A patent/JPH0314843A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0314843A (en) | 1991-01-23 |
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| LAPS | Cancellation because of no payment of annual fees |