JPH0665413A - Production of phenol resin foamed product - Google Patents

Production of phenol resin foamed product

Info

Publication number
JPH0665413A
JPH0665413A JP24119392A JP24119392A JPH0665413A JP H0665413 A JPH0665413 A JP H0665413A JP 24119392 A JP24119392 A JP 24119392A JP 24119392 A JP24119392 A JP 24119392A JP H0665413 A JPH0665413 A JP H0665413A
Authority
JP
Japan
Prior art keywords
phenol resin
foaming agent
foam
producing
foamed product
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
JP24119392A
Other languages
Japanese (ja)
Inventor
Takashi Oga
隆史 大賀
Shingo Baba
信吾 馬場
Chiaki Tsukamoto
千秋 塚本
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.)
Toyo Tire Corp
Original Assignee
Toyo Tire and Rubber Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyo Tire and Rubber Co Ltd filed Critical Toyo Tire and Rubber Co Ltd
Priority to JP24119392A priority Critical patent/JPH0665413A/en
Publication of JPH0665413A publication Critical patent/JPH0665413A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To provide the improved method for producing the phenol resin foamed product having uniform foams and high heat resistance without decomposing the ozone layer in the atmosphere by employing a new foaming agent, in the method for producing the phenol resin foamed product having a light weight, high heat resistance and high flame retardancy. CONSTITUTION:This method for producing the phenol resin foamed product by mixing a liquid phenolic resin with a foaming agent and an acidic curing agent to foam and cure the liquid phenol resin is characterized by employing a mixture of dichloropentafluoropropane with dichlorofluoroethane in a weight ratio of 80:20 to 20:80.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は軽量で高い断熱性と高い
難熱性を有するフェノール樹脂発泡体の製造法に関し、
更に詳しくは、新規な発泡剤を用いることにより、均一
な気泡を有しかつ高い断熱性をもったフェノール樹脂発
泡体を製造する改良された製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a phenol resin foam which is lightweight and has high heat insulation and high heat resistance,
More specifically, it relates to an improved production method for producing a phenol resin foam having uniform cells and high heat insulation by using a novel foaming agent.

【0002】[0002]

【従来の技術】一般に液状フェノール樹脂よりフェノー
ル樹脂発泡体を得る場合、フェノール樹脂としてはレゾ
ール型やベンジリックエーテル型のフェノール樹脂が用
いられている。発泡剤としてはトリクロロトリフルオロ
エタン(CFC−113),トリクロロモノフルオロメ
タン(CFC−11),ジクロロメタン等のハロゲン化
炭化水素やペンタン,ヘキサン等の炭化水素が一般に用
いられている。添加剤としては整泡剤としての界面活性
剤,難燃剤,中和剤等が用いられている。硬化剤として
は無機酸、有機酸又はその溶液等が用いられている。こ
れらの原料を均一に混合しモールド等に散布又は注入し
発泡硬化させフェノール樹脂発泡体を得る方法が知られ
ている。尚従来技術としては、本発明者の特開平3−2
55142号がある。
2. Description of the Related Art Generally, when a phenol resin foam is obtained from a liquid phenol resin, a resol type or benzylic ether type phenol resin is used as the phenol resin. As the foaming agent, trichlorotrifluoroethane (CFC-113), trichloromonofluoromethane (CFC-11), halogenated hydrocarbons such as dichloromethane and hydrocarbons such as pentane and hexane are generally used. As additives, surfactants as a foam stabilizer, flame retardants, neutralizing agents, etc. are used. As the curing agent, an inorganic acid, an organic acid, a solution thereof or the like is used. A method is known in which these raw materials are uniformly mixed and then sprayed or poured into a mold or the like to foam and cure to obtain a phenol resin foam. Incidentally, as a conventional technique, Japanese Patent Application Laid-Open No. 3-2 of the present inventor is used.
There is 55142.

【0003】[0003]

【発明が解決しようとする課題】発泡剤として炭化水素
を用いる場合、これらの炭化水素やその誘導体は引火性
が強く、配合,発泡,硬化,キュア等の製造工程におい
て、その引火性のため火災の発生する危険性が高く、こ
れらの工程を行う設備を防爆化する等の必要があるため
設備投資が非常に大きくなる。又これらの工程での作業
には火災を防ぐための細心の注意が必要である。又得ら
れた発泡体はその気泡中に内包する引火性炭化水素やそ
の誘導体のガスのためフェノール樹脂発泡体本来の難燃
性が損なわれる。又気泡中に内包する炭化水素やその誘
導体のガスの熱伝導率がハロゲン化炭化水素やその誘導
体のガスに比べて大きいため、ハロゲン化炭化水素やそ
の誘導体を発泡剤として用いたフェノール樹脂発泡体に
比べ熱伝導率が大きくなり断熱材としての性能も損なわ
れる。発泡剤としてトリクロロトリフルオロエタン(C
FC−113),トリクロロモノフルオロメタン(CF
C−11),ジクロロトリフルオロエタン(HCFC−
123),ジクロロフルオロエタン(HCFC−141
b),ジクロロメタン,ペンタフルオロプロピルアルコ
ール等のハロゲン化炭化水素やその誘導体を用いる場
合、これらの発泡剤は引火点がなく製造工程が安全であ
り、又気体としての熱伝導率が小さいためガスを発泡体
内に閉じ込めた場合得られた発泡体の断熱性も優れたも
のとなる。しかし発泡剤としてCFC−113,CFC
−11等を用いる場合、CFC−113,CFC−11
等は極めて安定な化合物であるため対流圏で分解される
ことなく成層圏まで到達し、成層圏で紫外線により分解
して塩素原子を放出し、この塩素原子が成層圏のオゾン
を分解しオゾン層の破壊を引き起こすという地球レベル
での環境破壊の原因として現在世界的に問題となってお
り、「モントリオール議定書」で特定フロンとして規定
されており、既に製造及び使用量の規制が世界的に進め
られている。このためこのCFC−113,CFC−1
1等の使用は規制に従って削減し、他の発泡剤等に代替
し全廃していく必要がある。又発泡剤としてHCFC−
123,HCFC−141b,ジクロロメタン等を用い
る場合、これらの発泡剤は分子中に水素原子を持ち対流
圏で分解されやすいため成層圏でオゾンを分解する能力
は小さく環境に及ぼす悪影響も小さい。しかしフェノー
ル樹脂発泡体製造用発泡剤としては、これらのみでは気
泡の均一かつ微細な発泡体が得られにくく、CFC−1
13,ペンタン,ヘキサン等と併用し、しかもHCFC
−123,HCFC−141b,ジクロロメタン等の使
用量が全発泡剤使用量の50重量%以下でないと均一且
つ微細な気泡と優れた品質を持った発泡体を得ることは
困難である。これはHCFC−123,HCFC−14
1b等の液状フェノール樹脂への溶解性が良すぎ、又沸
点が低すぎるためと考えられる。従ってこのように併用
系の発泡剤を使用する必要があり、CFC−113,ペ
ンタン,ヘキサン等を使用することによって生ずる前述
の問題を回避することは不可能である。
When a hydrocarbon is used as a foaming agent, these hydrocarbons and their derivatives have a strong flammability, and in the manufacturing processes such as compounding, foaming, curing and curing, the flammability causes a fire. Since there is a high risk of occurrence of equipment and it is necessary to make equipment that performs these processes explosion proof, equipment investment will be extremely large. In addition, the work in these steps requires extreme caution to prevent fire. In addition, the flame retardancy inherent in the phenol resin foam is impaired due to the flammable hydrocarbon or its derivative gas contained in the bubbles of the obtained foam. Further, since the thermal conductivity of the gas of the hydrocarbon or its derivative contained in the bubbles is higher than that of the gas of the halogenated hydrocarbon or its derivative, a phenol resin foam using the halogenated hydrocarbon or its derivative as a foaming agent. The thermal conductivity is higher than that of and the performance as a heat insulating material is impaired. Trichlorotrifluoroethane (C
FC-113), trichloromonofluoromethane (CF
C-11), dichlorotrifluoroethane (HCFC-
123), dichlorofluoroethane (HCFC-141
b), when using a halogenated hydrocarbon such as dichloromethane or pentafluoropropyl alcohol, or a derivative thereof, these foaming agents have no flash point, the manufacturing process is safe, and the thermal conductivity as a gas is small, so a gas is used. When enclosed in a foam, the resulting foam also has excellent heat insulation. However, as a foaming agent, CFC-113, CFC
When -11 or the like is used, CFC-113, CFC-11
Since they are extremely stable compounds, they reach the stratosphere without being decomposed in the troposphere, are decomposed by ultraviolet rays in the stratosphere and release chlorine atoms, and these chlorine atoms decompose ozone in the stratosphere and cause destruction of the ozone layer. As a cause of environmental destruction at the global level, it is currently becoming a global problem, and it is specified as a specified CFC in the "Montreal Protocol", and the regulation of manufacturing and usage has already been advanced worldwide. Therefore, this CFC-113, CFC-1
It is necessary to reduce the use of 1 etc. in accordance with regulations and replace it with another foaming agent etc., and abolish it. HCFC- as a foaming agent
When 123, HCFC-141b, dichloromethane or the like is used, these foaming agents have hydrogen atoms in the molecule and are easily decomposed in the troposphere, so that the ability to decompose ozone in the stratosphere is small and the adverse effect on the environment is also small. However, as a foaming agent for producing a phenolic resin foam, it is difficult to obtain a foam having uniform and fine cells only by these, and CFC-1
HCFC used in combination with 13, pentane, hexane, etc.
It is difficult to obtain a foam having uniform and fine cells and excellent quality unless the amount of -123, HCFC-141b, dichloromethane, etc. used is 50% by weight or less of the total amount of the blowing agent used. This is HCFC-123, HCFC-14
It is considered that the solubility of 1b or the like in the liquid phenol resin is too good and the boiling point is too low. Therefore, it is necessary to use a combined-use foaming agent as described above, and it is impossible to avoid the above-mentioned problems caused by using CFC-113, pentane, hexane and the like.

【0004】[0004]

【課題を解決するための手段】上記課題を解決するため
に鋭意研究した結果、本発明に到達したものである。す
なわちフェノール樹脂発泡体の製造にあたり従来のオゾ
ン破壊係数(ODP:Ozone Deleting Potential)の大
きいハロゲン化炭化水素や引火性の大きい低沸点炭化水
素を使用しないことにより環境破壊や火災発生の危険性
を大幅に改善し、かつ優れた断熱性能を有するフェノー
ル樹脂発泡体の製造方法を確立するに至ったものであ
る。本発明は液状フェノール樹脂,発泡剤,その他添加
剤及び硬化剤よりフェノール樹脂発泡体を製造する方法
において、該発泡剤としてジクロロペンタフルオロプロ
パンとジクロロフルオロエタンの混合物であって、該ジ
クロロペンタフルオロプロパンの混合重量比が80:2
0〜20:80の範囲にある混合物を用いることによっ
て大気中のオゾン層を破壊しない発泡剤の使用に成功し
た。
Means for Solving the Problems As a result of intensive research for solving the above problems, the present invention has been achieved. In other words, in the production of phenolic resin foams, the danger of environmental damage and fire is greatly increased by not using the conventional halogenated hydrocarbons with a high ozone depletion potential (ODP) or low boiling point hydrocarbons with a high flammability. The present invention has led to the establishment of a method for producing a phenolic resin foam having improved heat resistance and excellent heat insulation performance. The present invention relates to a method for producing a phenol resin foam from a liquid phenol resin, a foaming agent, other additives and a curing agent, which is a mixture of dichloropentafluoropropane and dichlorofluoroethane as the foaming agent. The mixing weight ratio of 80: 2
The use of a blowing agent which does not destroy the ozone layer in the atmosphere has been successful by using a mixture in the range 0-20: 80.

【0005】本発明に用いる液状フェノール樹脂は特に
限定されるものではなく、フェノール類とアルデヒド類
をアルカリ性触媒の存在下で反応させることによって得
られるレゾール型フェノール樹脂、中性金属塩触媒等の
存在下で反応させることによって得られるベンジリック
エーテル型フェノール樹脂などが挙げられる。本発明の
フェノール樹脂発泡体の製造方法で発泡剤として用いら
れるジクロロペンタフルオロプロパンとジクロロフルオ
ロエタンの混合物の混合比は、重量比で80:20〜2
0:80の範囲の混合比が良く、より好ましくは70:
30〜40:60である。この混合比が80:20より
大きい場合は、液状フェノール樹脂と発泡剤の分散性が
充分でなく、均一な発泡体が得られず断熱性も悪化す
る。一方この混合比が20:80より小さい場合は液状
フェノール樹脂への発泡剤の溶解性が大きくなり、発泡
体の気泡が大きくきめが粗くなり強度,断熱性等の物性
の低下を来す。発泡剤としてのジクロロペンタフルオロ
プロパンとしては1,1−ジクロロ−2,2,3,3−
ペンタフルオロプロパン(HCFC−225ca),
1,3−ジクロロ−1,1,2,2,3−ペンタフルオ
ロプロパン(HCFC−225cb)等全ての異性体の
使用が可能で、これらの異性体の1つを単独で使用する
ことも2つ以上の異性体の任意の割合の混合物を使用す
ることも可能である。又ジクロロフルオロエタンとして
は1,1−ジクロロ−1−フルオロエタン(HCFC−
141b)等が使用可能である。発泡剤の総使用量とし
ては特に限定されるものではないが、液状フェノール樹
脂100重量部に対して1〜60重量部、好ましくは4
〜40重量部とするのがよい。添加剤としては公知の界
面活性剤,難燃剤,中和剤,充填剤,その他の添加剤を
添加することができる。硬化剤としてはリン酸,亜リン
酸,次亜リン酸,ピロリン酸,トリポリリン酸,ポリリ
ン酸,塩酸,硫酸等の無機酸、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
ルホン酸等のアリールスルホン酸やメタンスルホン酸等
のアルキルスルホン酸等の有機酸が用いられるがこれら
に限定されるものではない。又これらの硬化剤は単独で
又は2種以上を併用することも可能であり、水溶液とし
て使用することも他の溶液として使用することも或いは
非溶液として使用することも可能である。この硬化剤の
使用量は特に限定されるものではないが、液状フェノー
ル樹脂100重量部に対して1〜60重量部、好ましく
は5〜30重量部とするのがよい。本発明では以上に述
べた原料を均一に混合し、引き続きモールド等に散布又
は注入し発泡硬化させることによりフェノール樹脂発泡
体が得られる。発泡硬化工程は常温でも加熱雰囲気下で
も行うことが可能である。これらの原料の混合はバッチ
混合する場合はディスパー等の攪拌機が用いられ、連続
的に混合する場合は公知の多成分混合発泡機等が用いら
れる。又混合された原料は例えばモールド中で発泡硬化
され、そのまま脱型した形で製品することも、更に必要
な形状に加工され製品とすることもできる。又混合され
た原料は例えばクラフト紙,水酸化アルミ紙,アスベス
ト紙,アスファルト紙,炭酸カルシウム紙,アルミクラ
フト紙,鉄箔,ステンレス箔,プラスチックフィルムも
しくはシート等の軟質面材や、鋼板,アルミ板,ステン
レス板等の硬質面材の間に注入され、ボード,パネル,
サイディング材等の形で製品とすることもできる。以下
に実施例及び比較例を挙げて本発明について詳しく説明
する。
The liquid phenol resin used in the present invention is not particularly limited, and the presence of a resole type phenol resin obtained by reacting phenols and aldehydes in the presence of an alkaline catalyst, a neutral metal salt catalyst, etc. Examples thereof include a benzylic ether type phenol resin obtained by reacting under the following conditions. The mixing ratio of the mixture of dichloropentafluoropropane and dichlorofluoroethane used as a foaming agent in the method for producing a phenol resin foam of the present invention is 80:20 to 2 by weight.
The mixing ratio in the range of 0:80 is good, and more preferably 70 :.
30-40: 60. When this mixing ratio is greater than 80:20, the dispersibility of the liquid phenol resin and the foaming agent is not sufficient, a uniform foam cannot be obtained, and the heat insulating property deteriorates. On the other hand, when the mixing ratio is less than 20:80, the solubility of the foaming agent in the liquid phenol resin becomes large, the bubbles of the foam become large and the texture becomes rough, and the physical properties such as strength and heat insulating property deteriorate. As dichloropentafluoropropane as a foaming agent, 1,1-dichloro-2,2,3,3-
Pentafluoropropane (HCFC-225ca),
All isomers such as 1,3-dichloro-1,1,2,2,3-pentafluoropropane (HCFC-225cb) can be used, and one of these isomers can be used alone. It is also possible to use mixtures of one or more isomers in any proportion. As dichlorofluoroethane, 1,1-dichloro-1-fluoroethane (HCFC-
141b) or the like can be used. The total amount of the foaming agent used is not particularly limited, but is 1 to 60 parts by weight, preferably 4 parts by weight with respect to 100 parts by weight of the liquid phenol resin.
It is recommended that the amount be ˜40 parts by weight. As the additives, known surfactants, flame retardants, neutralizing agents, fillers and other additives can be added. As a curing agent, phosphoric acid, phosphorous acid, hypophosphorous acid, pyrophosphoric acid, tripolyphosphoric acid, polyphosphoric acid, hydrochloric acid, inorganic acids such as sulfuric acid, phenolsulfonic acid,
Organic acids such as aryl sulfonic acids such as toluene sulfonic acid, xylene sulfonic acid and benzene sulfonic acid, and alkyl sulfonic acids such as methane sulfonic acid are used, but not limited thereto. Further, these curing agents can be used alone or in combination of two or more kinds, and can be used as an aqueous solution, another solution, or a non-solution. The amount of the curing agent used is not particularly limited, but it is preferably 1 to 60 parts by weight, and more preferably 5 to 30 parts by weight with respect to 100 parts by weight of the liquid phenol resin. In the present invention, the phenol resin foam is obtained by uniformly mixing the above-mentioned raw materials, and then spraying or pouring the mixture into a mold or the like and foam-curing. The foaming and hardening step can be performed at room temperature or under a heated atmosphere. When these materials are mixed in a batch, a stirrer such as a disperser is used, and when continuously mixed, a known multi-component mixing and foaming machine is used. Further, the mixed raw materials may be foamed and cured in a mold, for example, and the product may be released from the mold as it is, or further processed into a required shape to obtain a product. The mixed raw materials are, for example, kraft paper, aluminum hydroxide paper, asbestos paper, asphalt paper, calcium carbonate paper, aluminum kraft paper, iron foil, stainless steel foil, soft film such as plastic film or sheet, steel plate, aluminum plate. , Injected between hard surface materials such as stainless steel plates, boards, panels,
It can also be made into a product in the form of a siding material or the like. Hereinafter, the present invention will be described in detail with reference to Examples and Comparative Examples.

【0006】[0006]

【実施例】【Example】

実施例 フェノール100重量部,ホルムアルデヒド37%水溶
液173重量部及び水酸化ナトリウム1重量部を反応容
器に投入し90℃で3時間反応させた後、減圧下に脱水
しレゾール型液状フェノール樹脂を得た。このレゾール
型フェノール樹脂100重量部に整泡剤としてシリコン
系界面活性剤L−5420(日本ユニカー製)2重量
部、発泡剤として、ジクロロペンタフルオロプロパンと
ジクロロフルオロエタンとを表1に示す種々の比率で混
合した発泡剤10重量部を予め混合してプレミックス成
分を調整し、これに硬化剤として65%フェノールスル
ホン酸水溶液15重量部を加えラボミキサーで10秒攪
拌して、300×300×300mmのオープンモール
ド中に流し込み、70℃の雰囲気下で10分間加熱し、
フェノール樹脂発泡体を得た。得られた発泡体の物性
を、表1に示す。
Example 100 parts by weight of phenol, 173 parts by weight of 37% formaldehyde aqueous solution and 1 part by weight of sodium hydroxide were placed in a reaction vessel and reacted at 90 ° C. for 3 hours, followed by dehydration under reduced pressure to obtain a resol type liquid phenol resin. . In 100 parts by weight of this resol-type phenol resin, 2 parts by weight of a silicon-based surfactant L-5420 (manufactured by Nippon Unicar) as a foam stabilizer and dichloropentafluoropropane and dichlorofluoroethane as blowing agents are shown in Table 1. 10 parts by weight of the foaming agent mixed in a ratio were mixed in advance to prepare a premix component, and 15 parts by weight of a 65% phenolsulfonic acid aqueous solution as a curing agent was added thereto, and the mixture was stirred with a lab mixer for 10 seconds to give 300 × 300 × Pour into an open mold of 300 mm and heat in an atmosphere of 70 ° C for 10 minutes,
A phenol resin foam was obtained. Table 1 shows the physical properties of the obtained foam.

【0007】[0007]

【表1】 [Table 1]

【0008】比較例 実施例1において発泡剤としてジクロロペンタフルオロ
プロパン単独、ジクロロフルオロエタン単独、又はジク
ロロペンタフルオロプロパンとジクロロフルオロエタン
とを表1に示す種々の比率で用いる以外は実施例1と同
様にしてフェノール樹脂発泡体を得た。その結果を比較
例1〜4として表1に示す。このフェノール樹脂発泡体
について目視により気泡の状態を観察し、ASTMD1
622に定められた方法で密度を、JISA1412に
定められた方法で熱伝導率を、ASTMD1621に定
められた方法で圧縮強度を、ASTMD2856に定め
られた方法で独立気泡率を測定した。
Comparative Example Similar to Example 1 except that dichloropentafluoropropane alone, dichlorofluoroethane alone, or dichloropentafluoropropane and dichlorofluoroethane were used as the foaming agent in various ratios shown in Table 1. To obtain a phenol resin foam. The results are shown in Table 1 as Comparative Examples 1 to 4. The state of bubbles was visually observed for this phenol resin foam, and ASTM D1
The density was measured by the method specified in 622, the thermal conductivity was measured by the method specified by JISA1412, the compressive strength was measured by the method specified by ASTM D1621, and the closed cell ratio was measured by the method specified in ASTM D2856.

【0009】[0009]

【発明の効果】本発明で発泡剤として使用されるジクロ
ロペンタフルオロプロパン及びジクロロフルオロエタン
は分子中に水素原子を持ち対流圏で分解されやすい為、
成層圏に到達しにくく、成層圏で紫外線により分解して
塩素原子を放出して成層圏のオゾンを分解しオゾン層を
破壊する能力が小さく環境破壊という問題も小さい。又
引火点を持たない為、製造工程での火災の危険性がな
く、製造設備を防爆化する必要がないので設備費用が非
常に安くなる。又ジクロロペンタフルオロプロパンとジ
クロロフルオロエタンの混合物を用いることにより、そ
れぞれの持つ欠点であるフェノール樹脂への分散性の悪
さ及び溶解性の強さを互いに補填し合い、フェノール樹
脂への分散性,溶解性が改良された発泡剤系となり、均
一かつ微細な気泡と優れた物理特性を持つ発泡体が得ら
れるものと考える。又ジクロロペンタフルオロプロパン
とジクロロフルオロエタンの気体状態での熱伝導率が小
さいため、得られたジクロロペンタフルオロプロパン及
びジクロロフルオロエタンを内包する発泡体は断熱性の
優れたものとなる。従って発泡剤としてジクロロペンタ
フルオロプロパンとジクロロフルオロエタンの混合物を
使用することにより上記の多数の品質において従来技術
による品質を大幅に向上させることが可能である。
The dichloropentafluoropropane and dichlorofluoroethane used as the blowing agent in the present invention have hydrogen atoms in the molecule and are easily decomposed in the troposphere.
It is hard to reach the stratosphere, and the ability to decompose ozone in the stratosphere by decomposing chlorine atoms by releasing ultraviolet rays in the stratosphere to destroy ozone in the stratosphere is small and the problem of environmental destruction is small. Also, since it has no flash point, there is no risk of fire in the manufacturing process, and there is no need to make the manufacturing equipment explosion-proof, so the equipment cost is very low. In addition, by using a mixture of dichloropentafluoropropane and dichlorofluoroethane, the disadvantages of dispersibility in phenol resin and solubility are compensated for each other, and the dispersibility and dissolution in phenol resin are compensated for each other. It is believed that the foaming agent system has improved properties, and that a foam having uniform and fine cells and excellent physical properties can be obtained. In addition, since the thermal conductivity of dichloropentafluoropropane and dichlorofluoroethane in the gaseous state is small, the resulting foam containing dichloropentafluoropropane and dichlorofluoroethane has excellent heat insulating properties. Therefore, by using a mixture of dichloropentafluoropropane and dichlorofluoroethane as a blowing agent, it is possible to significantly improve the quality of the prior art in the above many qualities.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 塚本 千秋 兵庫県加古郡稲美町六分一字内ケ池1176番 地 東洋ゴム工業株式会社兵庫事業所兵庫 工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Chiaki Tsukamoto 1176, Uchigaike, 1-6, Inami-cho, Kako-gun, Hyogo Prefecture Toyo Tire & Rubber Co., Ltd. Hyogo Plant Hyogo Factory

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 液状フェノール樹脂と発泡剤と酸性硬化
剤を混合して発泡、硬化させるフェノール樹脂発泡体の
製造法において、該発泡剤としてジクロロペンタフルオ
ロプロパンとジクロロフルオロエタンの混合物であっ
て、該ジクロロペンタフルオロプロパンとジクロロフル
オロエタンの混合重量比が80:20〜20:80の範
囲にある混合物を用いることを特徴とするフェノール樹
脂発泡体の製造方法。
1. A method for producing a phenolic resin foam, which comprises foaming and curing a liquid phenolic resin, a foaming agent and an acidic curing agent by mixing, and a mixture of dichloropentafluoropropane and dichlorofluoroethane as the foaming agent, A method for producing a phenol resin foam, which comprises using a mixture having a mixing weight ratio of the dichloropentafluoropropane and dichlorofluoroethane in the range of 80:20 to 20:80.
JP24119392A 1992-08-17 1992-08-17 Production of phenol resin foamed product Pending JPH0665413A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24119392A JPH0665413A (en) 1992-08-17 1992-08-17 Production of phenol resin foamed product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24119392A JPH0665413A (en) 1992-08-17 1992-08-17 Production of phenol resin foamed product

Publications (1)

Publication Number Publication Date
JPH0665413A true JPH0665413A (en) 1994-03-08

Family

ID=17070600

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24119392A Pending JPH0665413A (en) 1992-08-17 1992-08-17 Production of phenol resin foamed product

Country Status (1)

Country Link
JP (1) JPH0665413A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998030623A1 (en) * 1997-01-08 1998-07-16 Daikin Industries, Ltd. Process for preparing phenol resin foam

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998030623A1 (en) * 1997-01-08 1998-07-16 Daikin Industries, Ltd. Process for preparing phenol resin foam
US6133332A (en) * 1997-01-08 2000-10-17 Daikin Industries, Ltd. Process for producing phenolic resin foams

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