JPH03106947A - Production of phenolic rein foam - Google Patents
Production of phenolic rein foamInfo
- Publication number
- JPH03106947A JPH03106947A JP24412089A JP24412089A JPH03106947A JP H03106947 A JPH03106947 A JP H03106947A JP 24412089 A JP24412089 A JP 24412089A JP 24412089 A JP24412089 A JP 24412089A JP H03106947 A JPH03106947 A JP H03106947A
- Authority
- JP
- Japan
- Prior art keywords
- phenolic resin
- foam
- resin
- phenol
- carbon dioxide
- 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.)
- Granted
Links
- 239000006260 foam Substances 0.000 title claims abstract description 30
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 title abstract description 8
- 239000005011 phenolic resin Substances 0.000 claims abstract description 33
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 claims abstract description 26
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229920001568 phenolic resin Polymers 0.000 claims abstract description 26
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 13
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 13
- 239000004604 Blowing Agent Substances 0.000 claims abstract description 12
- 239000002253 acid Substances 0.000 claims abstract description 8
- 239000003381 stabilizer Substances 0.000 claims abstract description 8
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 7
- 239000007858 starting material Substances 0.000 claims abstract description 4
- 238000005187 foaming Methods 0.000 claims description 16
- 239000011134 resol-type phenolic resin Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims 1
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 abstract description 12
- 229920005989 resin Polymers 0.000 abstract description 9
- 239000011347 resin Substances 0.000 abstract description 9
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 abstract description 8
- WHOZNOZYMBRCBL-OUKQBFOZSA-N (2E)-2-Tetradecenal Chemical compound CCCCCCCCCCC\C=C\C=O WHOZNOZYMBRCBL-OUKQBFOZSA-N 0.000 abstract description 5
- 229940044654 phenolsulfonic acid Drugs 0.000 abstract description 5
- 229920003987 resole Polymers 0.000 abstract description 5
- 239000003054 catalyst Substances 0.000 abstract description 3
- 150000001299 aldehydes Chemical class 0.000 abstract description 2
- 230000018044 dehydration Effects 0.000 abstract description 2
- 238000006297 dehydration reaction Methods 0.000 abstract description 2
- 235000010483 polyoxyethylene sorbitan monopalmitate Nutrition 0.000 abstract 1
- 239000000249 polyoxyethylene sorbitan monopalmitate Substances 0.000 abstract 1
- 239000011541 reaction mixture Substances 0.000 abstract 1
- AJDIZQLSFPQPEY-UHFFFAOYSA-N 1,1,2-Trichlorotrifluoroethane Chemical compound FC(F)(Cl)C(F)(Cl)Cl AJDIZQLSFPQPEY-UHFFFAOYSA-N 0.000 description 4
- 239000004088 foaming agent Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- CYRMSUTZVYGINF-UHFFFAOYSA-N trichlorofluoromethane Chemical compound FC(Cl)(Cl)Cl CYRMSUTZVYGINF-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 229930040373 Paraformaldehyde Natural products 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 2
- 239000004566 building material Substances 0.000 description 2
- -1 but among these Chemical compound 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 239000002360 explosive Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- IWDCLRJOBJJRNH-UHFFFAOYSA-N p-cresol Chemical compound CC1=CC=C(O)C=C1 IWDCLRJOBJJRNH-UHFFFAOYSA-N 0.000 description 2
- 150000002989 phenols Chemical class 0.000 description 2
- JNYAEWCLZODPBN-JGWLITMVSA-N (2r,3r,4s)-2-[(1r)-1,2-dihydroxyethyl]oxolane-3,4-diol Chemical compound OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O JNYAEWCLZODPBN-JGWLITMVSA-N 0.000 description 1
- QTWJRLJHJPIABL-UHFFFAOYSA-N 2-methylphenol;3-methylphenol;4-methylphenol Chemical compound CC1=CC=C(O)C=C1.CC1=CC=CC(O)=C1.CC1=CC=CC=C1O QTWJRLJHJPIABL-UHFFFAOYSA-N 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 229930185605 Bisphenol Natural products 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 229920001214 Polysorbate 60 Polymers 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 1
- 239000004359 castor oil Substances 0.000 description 1
- 235000019438 castor oil Nutrition 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 229930003836 cresol Natural products 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 229920002866 paraformaldehyde Polymers 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920006324 polyoxymethylene Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 229920000136 polysorbate Polymers 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- 229940029284 trichlorofluoromethane Drugs 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 125000002256 xylenyl group Chemical class C1(C(C=CC=C1)C)(C)* 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、建材用として壁材、天井材,また家具等の材
料として有用な耐熱性、断熱性、難燃性,耐水性を有し
、機械的強度に優れたフェノール樹脂発泡体の製造法に
関する,
[従来の技術]
フェノール樹脂発泡体は、軽量で熱可塑性樹脂製発泡体
に比し,it燃性、耐熱性、機械的強度に優れ、建材分
野、家具等の材料として広く用いられる.
製造法としては、レゾール樹脂を原料とし、発泡剤とし
てトリクロルモノフル才ロメタン(フロン−11).ト
リクロルトリフルオ口エタン(フロン−113).ペン
タン等が主として用いられていた.
しかし、フロン−11やフロン−113は発泡剤として
極めて優れた性質を有し、人体に対し無害で、引火性、
着火性もなく、工程的には安全な発泡剤ではあるが、こ
のフロン類が地球を取り巻くオゾン層を破壊し、地球の
環境破壊を促進することが分かり、使用量の減少、更に
は使用禁止の必要性が叫ばれつつある.
また,ペンタンはフロンと異なり地球の環境破壊の問題
はないとしても、可燃性の炭化水素ガスであって、漏洩
すれば爆発や火災の危険の極めて大きい物質であり、ま
たその爆発範囲もベンタンが少量であってもその範囲に
入ること、空気より比重が重いため低所に溜り易く安全
上問題のあるガスであることはよく知られているところ
である.
他の発泡剤としては加熱により窒素ガスを放出するアゾ
系化合物の使用が行なわれてきたが、化合物が高価であ
ること、発泡倍率を高くするには多量の使用が必要とな
ること、発泡させるには化合物の分解温度以上の温度に
長時間保持することが必要であること等の点から主とし
て低発泡倍率の発泡体に利用されてきた.
[発明が解決しようとする課題J
本発明は比較的高倍率の発泡体を、大気汚染の原因とな
るフロン類を使用せず、また可燃性で爆発性のあるベン
タン等を使用しないで安全な操業可能な発泡剤を使用し
,フェノール発泡体の有する耐熱性、難燃性,断熱性、
軽量性等の優れた特徴を持ったフェノール発泡体を製造
する方法の開発を目的とする.
[課題を解決するための手段]
本発明は,上記目的を達するために種々検討した結果、
レゾール型フェノール樹脂、発泡剤、整泡剤,D硬化剤
を混合,硬化して、フェノール樹脂発泡体を製造するに
当り、発泡剤の出発原料として液化二酸化炭素をフェノ
ール樹脂1容量部に対し0.3〜15容量部使用して、
フェノール樹脂発泡体を製造することを開発した.
特に,整泡剤を含有したレゾール型フェノール樹脂、酸
硬化剤及びフェノール樹脂l容璽部に対し0.3〜15
容量部の液化二酸化炭素をそれぞれ別々に連続的にフェ
ノール樹脂発泡機に供給すると共に急速に均一に混合し
ながらフェノール樹脂発泡混合物を吐出させ、ついでモ
ールド中で硬化させることにより安全で、大気汚染の全
くないフェノール樹脂発泡体を製造できることを見出し
た.
ここで,レゾール型フェノール樹脂に使用できるフェノ
ール類としては、通常フェノール樹脂の製造原料として
用いられているフェノール、クレゾール、キシレノール
等が挙げられるが、これらの中でも反応性、硬化性の点
でフェノール、メククレゾールが特に好ましい.これら
フェノール類は単独のみならず.これら同士の混合、更
には0−クレゾール、p−クレゾールまたはビスフェノ
ール等と併用しても良い.
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、トリ才キサン等が使
用できる.
この両者を塩基性触媒の存在下に反応させ、脱水濃縮さ
せてレゾール型フェノール樹脂を得る,樹脂固形物とし
ては60〜90%,粘度1.500〜8.000 c
p s / 25℃位が使用するのに便利であり,もし
濃縮度が高いときは少量の水、アルコール,アセトン、
エステル、可塑剤等で適宜希釈して濃度、粘度を調整す
る.
本発明に使用する整泡剤としては、フロン発泡剤使用の
際に使用されていたものとほとんど同じものが用いられ
る.シリコーン系:エチレンオキサイドーブロビレン才
キサイド共重合体:ソルビタン、アルキルフェノールま
たはヒマシ油等のポリオキシアルキレン付加物系等の界
面活性剤が使用できる,
これらは単独又は混合して使用されるが、使用量はフェ
ノール樹脂100重量部に対し、0. 5〜10重量
部である.
酸硬化剤もフロン発泡剤使用の際に使用されていたもの
と同じであって、例えばバラトルエンスルフ才ンm.フ
ェノールスルホン酸等の強酸を使用する.添加量はフェ
ノール樹脂lOO重量部当り5〜40部が好ましい.
発泡剤の出発原料として使用する液化二酸化炭素は,フ
ェノール樹脂l容量部に対し0.3〜15容量部が適当
である.この範囲外では良好な発泡体が得られない.
フェノール樹脂発泡体の製造は、フロンを用いた時とほ
ぼ同一の方法を採用できる.
すなわち、整泡剤を含有する樹脂固形分及び粘度を調整
したレゾール型フェノール樹脂、酸硬化剤および液化二
酸化炭素をそれぞれフェノール樹脂発泡機に付属する定
量ボンブで混合機(ミキシングヘッド)に供給する.ミ
キシングヘッドのスクリューは1.000−10.00
0rpmの高速回転されており、これら原料は瞬時に均
一に混合され、発泡機から押し出される.
本発明のフェノール樹脂発泡体はそのままで使用する場
合よりも、木材、金属、他の合成尉脂等と複合材として
使用することが多い.
したがって、発泡体の発泡率も目的、複合される相手の
材質や強度により変化し、比較的低発泡率(比重0.1
位)から高発泡率(0.005位)まで変化する.この
発泡率の調整は液化二酸化炭素の注入量によって行なう
.
この発泡混合物は常温〜l00℃の温度で硬化され、硬
化時間はだいたい5〜20分である.[実施例]
(実施例l)
四ツロフラスコにフェノール2Kg.37%ホルムアル
デヒド2.93Kg (ホルムアルデヒド/フェノール
二モル比1.7モル)及び触媒として20%力性ソーダ
60gを仕込み、80℃で3時間反応した後、15%硫
酸で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ェノール樹脂は樹脂固形分80%
,粘度2500cps/25℃、重量平均分子量430
であった.
このレゾール型フェノール樹脂lOO重量部に対してト
ウィーンNo.40(ポリオキシエチレンソルビタンモ
ノバルミテート)2重量部を混合し、発泡用フェノール
樹脂とした.
発泡用フェノール樹脂1.6I2/minに対して、6
5%フェノールスルホン酸0.12g/minをフェノ
ール樹脂発泡機の定量ボンブより混合機(ミキシングヘ
ッド)に供給し、スクリュー回転数6.000rpmの
下で液化二酸化炭素2il/minを別ラインより混合
機に柱人し、フェノール樹脂、フェノールスルホン酸及
び二酸化炭素を瞬時に均一に混合し、混合機底口より吐
き出し,幅50cm、長さ25cm.高さ4cmの鉄枠
中に一定量流し込み、これを40℃オープン中で5分間
放置し,発泡硬化を完了してフェノール樹脂発泡体を得
た.
得られたフェノール樹脂発泡体の物性は密度2 0 K
g / m ’、吸水量4.5g/loocw”熱伝
導率0.027Kcal/mh’Cであり,外観上も全
体的に均一であった.
(実施例2〜6、比較例1〜2、参考例l)実施例1で
得た整泡剤添加済のレゾール型発泡用フェノール樹脂を
1.6I2/min.65%フェノールスルホン酸0.
l2j2/minの割合で供給すると共に、液化二酸化
炭素供給量、ミキシングヘッドのスクリューの回転数を
変えて実施した結果を第l表に示す.
なお、参考のためフロン−113を使用し,本発明の実
施例とほぼ同一の製品を得る条件を参考例lとして示す
.
(以下余白)
[効 果]
従来、発泡剤として使用されていたトリクロルモノフル
才口メタン(フロン−11).}リクロルトリフル才ロ
エタン(フロン−113)はオゾン層を破壊し、地球の
環境汚染をするとされて使用量の制限、使用禁止の必要
が叫ばれており,フロンを使用しない製造法の開発が要
望されていた.
一方、フロンを使用しないベンタンを発泡剤として使用
する発泡体製造法もあるが,これは爆発の危険があり,
安全上問題があった.[Detailed Description of the Invention] [Industrial Application Field] The present invention has heat resistance, heat insulation, flame retardancy, and water resistance, making it useful as a building material for wall materials, ceiling materials, furniture, etc. [Conventional technology] Phenolic resin foam is lightweight and has excellent flammability, heat resistance, and mechanical strength compared to thermoplastic resin foam. Excellent, widely used in the field of building materials and as a material for furniture, etc. The manufacturing method uses resol resin as a raw material and trichloromonofluoromethane (Freon-11) as a blowing agent. Trichlortrifluoroethane (Freon-113). Pentane etc. were mainly used. However, Freon-11 and Freon-113 have extremely excellent properties as foaming agents, are harmless to the human body, and are not flammable.
Although they are non-flammable and safe foaming agents from a process standpoint, it has been discovered that these fluorocarbons destroy the ozone layer that surrounds the earth and accelerate the destruction of the earth's environment, leading to a reduction in their usage and even a ban on their use. The need for this is becoming increasingly important. Furthermore, although pentane does not cause the problem of global environmental destruction unlike fluorocarbons, it is a flammable hydrocarbon gas that poses an extremely high risk of explosion or fire if it leaks, and the explosive range of pentane is It is well known that even a small amount of gas falls within this range, and that it is a gas that has a higher specific gravity than air, so it tends to accumulate in low places and poses a safety problem. As other foaming agents, azo compounds that release nitrogen gas when heated have been used, but these compounds are expensive, require large amounts to increase the foaming ratio, and are difficult to foam. It has been mainly used for foams with low expansion ratios because it is necessary to maintain the temperature at or above the decomposition temperature of the compound for a long time. [Problem to be Solved by the Invention J] The present invention creates a foam with a relatively high magnification in a safe manner without using fluorocarbons, which cause air pollution, and without using flammable and explosive gases such as bentane. Using a blowing agent that can be operated, the heat resistance, flame retardance, heat insulation properties, and
The purpose of this project is to develop a method for manufacturing phenolic foam with excellent characteristics such as lightness. [Means for Solving the Problem] As a result of various studies to achieve the above object, the present invention has been made based on the following:
When producing a phenolic resin foam by mixing and curing a resol type phenolic resin, a blowing agent, a foam stabilizer, and a D hardening agent, liquefied carbon dioxide is added to 1 part by volume of the phenolic resin as a starting material for the blowing agent. Using .3 to 15 parts by volume,
We have developed a method to produce phenolic resin foam. In particular, 0.3 to 15
Each volume of liquefied carbon dioxide is separately and continuously fed into a phenolic resin foaming machine, and the phenolic resin foaming mixture is discharged while rapidly and uniformly mixed, and then cured in a mold, thereby making it safe and free from air pollution. We have discovered that it is possible to produce a phenolic resin foam completely free of phenolic resin. Here, examples of phenols that can be used in the resol type phenolic resin include phenol, cresol, xylenol, etc., which are usually used as raw materials for producing phenolic resin, but among these, phenol, Mecclesol is particularly preferred. These phenols are used not only individually. These may be mixed with each other, or may be used in combination with 0-cresol, p-cresol, bisphenol, etc. Examples of aldehydes include formaldehyde. Paraformaldehyde, polyoxymethylene, trioxyxane, etc. can be used. Both are reacted in the presence of a basic catalyst and dehydrated and concentrated to obtain a resol type phenol resin, with a resin solid content of 60 to 90% and a viscosity of 1.500 to 8.000 c.
It is convenient to use p s / around 25℃, and if the concentration is high, add a small amount of water, alcohol, acetone,
Adjust concentration and viscosity by appropriately diluting with ester, plasticizer, etc. The foam stabilizer used in the present invention is almost the same as that used when using Freon foaming agents. Silicone type: Ethylene oxide-brobylene oxide copolymer: Surfactants such as sorbitan, alkylphenol, or polyoxyalkylene adducts such as castor oil can be used. These can be used alone or in combination, but The amount is 0.00 parts by weight per 100 parts by weight of phenolic resin. It is 5 to 10 parts by weight. The acid curing agent is also the same as that used when using a fluorocarbon blowing agent, such as balatoluene sulfur acid m. Use a strong acid such as phenolsulfonic acid. The amount added is preferably 5 to 40 parts per 100 parts by weight of phenolic resin. The appropriate amount of liquefied carbon dioxide used as a starting material for the blowing agent is 0.3 to 15 parts by volume per 1 part by volume of phenolic resin. A good foam cannot be obtained outside this range. Phenolic resin foam can be manufactured using almost the same method as when using fluorocarbons. That is, a resol-type phenolic resin containing a foam stabilizer with adjusted resin solid content and viscosity, an acid curing agent, and liquefied carbon dioxide are each supplied to a mixer (mixing head) using quantitative bombs attached to the phenolic resin foaming machine. Mixing head screw is 1.000-10.00
The foam is rotated at a high speed of 0 rpm, and these raw materials are instantly and uniformly mixed and extruded from the foaming machine. The phenolic resin foam of the present invention is often used as a composite material with wood, metal, other synthetic resin, etc., rather than being used as it is. Therefore, the expansion rate of the foam also varies depending on the purpose, the material and strength of the composite material, and the expansion rate is relatively low (specific gravity 0.1
The foaming rate varies from 0.005 to high foaming rate (0.005). This foaming rate is adjusted by adjusting the amount of liquefied carbon dioxide injected. This foamed mixture is cured at a temperature of room temperature to 100°C, and the curing time is approximately 5 to 20 minutes. [Example] (Example 1) 2 kg of phenol was placed in a four-piece flask. 2.93 kg of 37% formaldehyde (formaldehyde/phenol dimolar ratio 1.7 mol) and 60 g of 20% sodium hydroxide as a catalyst were charged, and after reacting at 80°C for 3 hours, the pH was adjusted to 7.0 with 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%.
, viscosity 2500cps/25℃, weight average molecular weight 430
Met. Tween No. 1 for 10 parts by weight of this resol type phenolic resin. 40 (polyoxyethylene sorbitan monobalmitate) was mixed to prepare a foaming phenol resin. For foaming phenolic resin 1.6I2/min, 6
0.12 g/min of 5% phenol sulfonic acid was supplied to the mixer (mixing head) from the metering bomb of the phenol resin foaming machine, and 2 il/min of liquefied carbon dioxide was supplied to the mixer from a separate line at a screw rotation speed of 6.000 rpm. Instantly and uniformly mix the phenol resin, phenolsulfonic acid, and carbon dioxide, and discharge from the bottom of the mixer into a 50 cm width and 25 cm length. A certain amount of the resin was poured into a 4 cm high iron frame, and left in an open environment at 40°C for 5 minutes to complete foaming and curing to obtain a phenolic resin foam. The physical properties of the obtained phenolic resin foam are as follows: density 20K
g/m', water absorption 4.5 g/lookw, thermal conductivity 0.027 Kcal/mh'C, and the overall appearance was uniform. (Examples 2 to 6, Comparative Examples 1 to 2, Reference Example 1) The phenolic resin for resol type foaming obtained in Example 1 with added foam stabilizer was mixed with 1.6I2/min.65% phenol sulfonic acid 0.
Table 1 shows the results obtained by supplying liquefied carbon dioxide at a rate of l2j2/min and varying the amount of liquefied carbon dioxide supplied and the rotational speed of the mixing head screw. For reference, the conditions for obtaining a product almost the same as the example of the present invention using Freon-113 are shown as Reference Example 1. (See margins below) [Effects] Trichlormonofluoric methane (Freon-11), which was conventionally used as a blowing agent. }Lichlortrifluroethane (CFC-113) is said to destroy the ozone layer and pollute the earth's environment, and there are calls for its usage to be limited or banned, and the development of a manufacturing method that does not use CFCs has been called for. It was requested. On the other hand, there is a foam production method that uses bentane as a blowing agent without using CFCs, but this has the risk of explosion.
There was a safety issue.
Claims (2)
硬化剤を混合、硬化して、フェノール樹脂発泡体を製造
するに当り、発泡剤の出発原料として液化二酸化炭素を
フェノール樹脂1容量部に対し0.3〜15容量部使用
することを特徴とするフェノール樹脂発泡体の製造法。(1) In producing a phenolic resin foam by mixing and curing a resol-type phenolic resin, a blowing agent, a foam stabilizer, and an acid curing agent, liquefied carbon dioxide is used as a starting material for the blowing agent and 1 part by volume of the phenolic resin is used. A method for producing a phenolic resin foam, characterized in that 0.3 to 15 parts by volume are used.
硬化剤及びフェノール樹脂1容量部に対し0.3〜15
容量部の液化二酸化炭素をそれぞれ別々に連続的にフェ
ノール樹脂発泡機に供給すると共に急速に均一に混合し
ながらフェノール樹脂発泡混合物を吐出させ、ついでモ
ールド中で硬化させることを特徴とするフェノール樹脂
発泡体の製造法。(2) 0.3 to 15% per volume part of resol type phenolic resin containing foam stabilizer, acid curing agent and phenolic resin
Phenol resin foaming characterized by continuously and separately feeding volume parts of liquefied carbon dioxide to a phenol resin foaming machine, discharging a phenol resin foaming mixture while rapidly and uniformly mixing it, and then curing it in a mold. How the body is manufactured.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24412089A JPH03106947A (en) | 1989-09-20 | 1989-09-20 | Production of phenolic rein foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24412089A JPH03106947A (en) | 1989-09-20 | 1989-09-20 | Production of phenolic rein foam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03106947A true JPH03106947A (en) | 1991-05-07 |
| JPH0549702B2 JPH0549702B2 (en) | 1993-07-27 |
Family
ID=17114059
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24412089A Granted JPH03106947A (en) | 1989-09-20 | 1989-09-20 | Production of phenolic rein foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03106947A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002309030A (en) * | 2001-04-11 | 2002-10-23 | Asahi Kasei Corp | Phenolic foam |
-
1989
- 1989-09-20 JP JP24412089A patent/JPH03106947A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002309030A (en) * | 2001-04-11 | 2002-10-23 | Asahi Kasei Corp | Phenolic foam |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0549702B2 (en) | 1993-07-27 |
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