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JPS5826370B2 - Method for producing urea-formaldehyde resin foam - Google Patents
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JPS5826370B2 - Method for producing urea-formaldehyde resin foam - Google Patents

Method for producing urea-formaldehyde resin foam

Info

Publication number
JPS5826370B2
JPS5826370B2 JP3936279A JP3936279A JPS5826370B2 JP S5826370 B2 JPS5826370 B2 JP S5826370B2 JP 3936279 A JP3936279 A JP 3936279A JP 3936279 A JP3936279 A JP 3936279A JP S5826370 B2 JPS5826370 B2 JP S5826370B2
Authority
JP
Japan
Prior art keywords
formaldehyde
urea
foam
thiourea
curing
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
Application number
JP3936279A
Other languages
Japanese (ja)
Other versions
JPS55133434A (en
Inventor
敏治 柴原
憲司 小林
幹夫 北原
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals 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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP3936279A priority Critical patent/JPS5826370B2/en
Publication of JPS55133434A publication Critical patent/JPS55133434A/en
Publication of JPS5826370B2 publication Critical patent/JPS5826370B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は尿素−ホルムアルデヒド樹脂発泡体(以後UF
フオームと略称する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a urea-formaldehyde resin foam (hereinafter UF
It is abbreviated as form.

)の製造方法に関し、詳しくはホルムアルデヒド臭の軽
微なUFフオームの改良製造方法に関するものである。
), and specifically relates to an improved method for producing UF foam with a slight formaldehyde odor.

尿素−ホルムアルデヒド初期反応物の水溶液(以後樹脂
液と略称する。
Aqueous solution of urea-formaldehyde initial reactant (hereinafter abbreviated as resin liquid).

)と硬化剤および起泡剤を含む水溶液(以後硬化液と略
称する。
), a curing agent, and a foaming agent (hereinafter abbreviated as curing liquid).

)とを原料とし、機械的方法等により含泡状態とし、こ
れらを混合、硬化させてUFフオームを製造する方法は
公知である。
) is used as a raw material, brought into a foamed state by a mechanical method or the like, and then mixed and cured to produce UF foam.

UFフオームは安価であること、燃えにくいこと、現場
発泡が可能であること、吸水性が良いこと等の特徴を有
し、省エネルギ一時代の住宅用断熱材をはじめとして、
炭坑用充填材、農業用資材その他者方面の用途に需要拡
大が期待されているものである。
UF foam has the characteristics of being inexpensive, non-combustible, capable of foaming on-site, and having good water absorption properties, and has been used as an energy-saving insulation material for homes for an era.
Demand is expected to increase for use as filler material for coal mines, agricultural materials, and other uses.

公知の方法によってUFフオームを製造するさいに、遭
遇する最大の問題点はフオーム化後にホルムアルデヒド
臭が残ることである。
In producing UF foams by known methods, the biggest problem encountered is the formaldehyde odor that remains after foaming.

従来尿素ホルムアルデヒド樹脂のホルムアルデヒド臭を
軽減するために、種々の試みがなされているが、はとん
ど有効な方法は見出されていない。
Various attempts have been made to reduce the formaldehyde odor of urea formaldehyde resins, but no effective method has been found.

各種のホルムアルデヒド捕集剤を樹脂液の製造過程で添
加し、処理することにより樹脂液中の遊離ホルムアルデ
ヒド量を減少させる方法が知られており、これらの方法
により樹脂液中の未反応ホルムアルデヒド分は減少する
が、樹脂液と硬化液とを反応させてフオーム化を行う以
降の過程で発生するホルムアルデヒド分を減少させるこ
とは困難である。
There are known methods for reducing the amount of free formaldehyde in resin liquids by adding various formaldehyde scavengers during the manufacturing process of resin liquids and treating them. However, it is difficult to reduce the formaldehyde content generated in the process after reacting the resin liquid and the curing liquid to form a foam.

即ち樹脂液の製造過程で添加されたホルムアルデヒド捕
集剤は、樹脂液中の未反応ホルムアルデヒドやメチロー
ル基と反応するため、樹脂液中にホルムアルデヒド捕集
剤を安定に含有せしめることは極めて困難である。
That is, the formaldehyde scavenger added during the manufacturing process of the resin liquid reacts with unreacted formaldehyde and methylol groups in the resin liquid, so it is extremely difficult to stably contain the formaldehyde scavenger in the resin liquid. .

しかしながら樹脂液と硬化液とを反応させてフオーム化
を行う過程およびフオーム化後のキユアリングの過程で
生成するホルムアルデヒドを有効に捕集するためには、
フオーム化以後の時点まで、ホルムアルデヒド捕集剤を
糸の中に安定に存在せしめることが必要であるとの考え
方にもとづいて、本発明者はフオーム化の時点まで糸の
中にホルムアルデヒド捕集剤を安定に存在させるための
方法について種々検討した結果、硬化液中にホルムアル
デヒド捕集剤を含有せしめる方法が有効であることを見
出した。
However, in order to effectively collect formaldehyde generated during the process of reacting the resin liquid and the curing liquid to form a foam and the curing process after forming the form,
Based on the idea that it is necessary for the formaldehyde scavenger to stably exist in the yarn until after it is formed into a foam, the present inventors have created a formaldehyde scavenger that exists in the yarn until the point of forming the yarn. As a result of various studies on methods for making it exist stably, it was found that a method of including a formaldehyde scavenger in the curing liquid is effective.

本発明者は先に硬化液中にホルムアルデヒド捕集剤とし
て、尿素を含有せしめる方法を発明したが、引き続き各
種のホルムアルデヒド捕集剤の効果について鋭意検討を
重ねた結果、硬化液中に含有せしめる尿素の一部または
全部をチオ尿素で置き換えることにより、ホルムアルデ
ヒド臭の軽減効果がさらに増すことを発見し、本発明を
完成した。
The present inventor had previously invented a method of incorporating urea into the curing liquid as a formaldehyde scavenger, but as a result of continued intensive studies on the effects of various formaldehyde scavengers, the inventor discovered that urea can be incorporated into the curing liquid as a formaldehyde scavenger. The present invention was completed based on the discovery that the effect of reducing formaldehyde odor can be further increased by replacing part or all of thiourea with thiourea.

本発明の目的はすでに記載した通り、フオーム化後のホ
ルムアルデヒド臭の軽微なUFフオームの製造方法を提
供することにある。
As already stated, the object of the present invention is to provide a method for producing a UF foam that has a slight formaldehyde odor after foaming.

本発明は公知の方法に従って樹脂液と硬化液とを反応さ
せてUFフオームを製造する方法において、硬化液中に
チオ尿素またはチオ尿素と尿素を含有せしめることを特
徴とするUFフオームの改良製造方法である。
The present invention is an improved method for producing UF foam, which is characterized in that the curing solution contains thiourea or thiourea and urea in a method of producing UF foam by reacting a resin liquid and a curing liquid according to a known method. It is.

公知のUFフオーム製造方法としては、古くは樹脂液を
発泡させてから硬化液を吹きつける方法も行われたが、
この方法によれば発泡ガン中の樹脂の詰まり等のトラブ
ルが多く、現在では硬化液を発泡させたのち樹脂液を吹
きつける方法が行われる。
In the past, a known method for manufacturing UF foam was to foam a resin liquid and then spray a curing liquid.
This method causes many problems such as clogging of the resin in the foaming gun, and the current method is to foam the curing liquid and then spray the resin liquid.

即ち硬化液に例えば空気を吹き込んで細かい泡をつくり
、この泡に樹脂液を吹きつけることにより均一な気泡構
造を有するUFフオームが得られる。
That is, by blowing air into the curing liquid to create fine bubbles, and then spraying the resin liquid onto the bubbles, a UF foam having a uniform cell structure can be obtained.

具体的には西独シャラムヘミ−社、英国B、1.P、社
等から市販されているUFフオーム用の発泡ガンを使用
し、空気を吹き込んで発泡させた硬化液に、スプレーノ
ズルから樹脂液を噴霧して混合し、これを施工部分の空
間に吹き付け、または導入する。
Specifically, West German Sharamhemy, UK B, 1. Using a foaming gun for UF foam commercially available from P. Co., Ltd., etc., spray the resin liquid from a spray nozzle to the hardening liquid that has been foamed by blowing air into it, mix it, and spray this into the space of the construction area. , or introduce.

得られたフオームは通常自然放置によって硬化、乾燥さ
せる。
The obtained foam is usually left to harden and dry.

なお、空気の代りに窒素、炭酸ガス等の気体を用いたり
、各種の発泡剤を用いる方法ももちろん可能である。
Note that it is of course possible to use a gas such as nitrogen or carbon dioxide instead of air, or to use various foaming agents.

樹脂液は例えば次の要領で製造される。The resin liquid is manufactured, for example, in the following manner.

尿素、ホルマリンに必要に応じて水を加え、初め中性付
近で80〜95℃で反応させる。
Water is added to urea and formalin as needed, and the mixture is initially reacted at 80 to 95°C near neutrality.

反応がある程度進んだ時点でPHを調整して反応を続け
、さらに反応の終期に未反応ホルムアルデヒドを減少さ
せるため少量の尿素を加える。
When the reaction has progressed to a certain extent, the pH is adjusted to continue the reaction, and at the end of the reaction, a small amount of urea is added to reduce unreacted formaldehyde.

必要に応じて水で希釈し、固形分含有率を調節する。Dilute with water as necessary to adjust solids content.

なお、尿素の一部をメラミン、フェノール等で置きかえ
て得られる変性品ももちろん使用できる。
Of course, modified products obtained by replacing a portion of urea with melamine, phenol, etc. can also be used.

また硬化液としては硬化剤、起泡剤、助剤およびチオ尿
素またはチオ尿素および尿素を含んだ水溶液が用いられ
る。
Further, as the curing liquid, an aqueous solution containing a curing agent, a foaming agent, an auxiliary agent, and thiourea or thiourea and urea is used.

硬化剤、起泡剤および助剤としてはすべての公知のもの
が用いられ、硬化剤の例としてはリン酸、硫酸、酢酸、
p−トルエンスルホン酸等の1種または2種以上の混合
物が、起泡剤の例としてはアルキルベンゼンスルホン酸
塩、アルキルナフタレンスルホン酸塩、アルキルジフェ
ニルエーテルスルホン酸塩、高級脂肪酸塩、高級アルコ
ール硫酸エステル塩、ポリオキシエチレンアルキル硫酸
エステル塩、アルキルフェノール・エチレンオキシド付
加物等の界面活性剤の1種または2種以上の混合物があ
げられる。
All known hardeners, foaming agents and auxiliaries can be used; examples of hardeners include phosphoric acid, sulfuric acid, acetic acid,
Examples of foaming agents include alkylbenzene sulfonates, alkylnaphthalene sulfonates, alkyldiphenyl ether sulfonates, higher fatty acid salts, and higher alcohol sulfate ester salts. , polyoxyethylene alkyl sulfate salts, alkylphenol/ethylene oxide adducts, etc., or a mixture of two or more thereof.

また助剤の例としては親水性付与剤としてポリエチレン
グリコール、ポリプロピレングリコール、ポリビニルア
ルコール等が、水質調整剤としてカルシウム、マグネシ
ウム等の塩類があげられる。
Examples of auxiliary agents include polyethylene glycol, polypropylene glycol, polyvinyl alcohol, etc. as hydrophilicity imparting agents, and salts such as calcium and magnesium as water quality conditioners.

チオ尿素またはチオ尿素および尿素(以後単にチオ尿素
等と略称する。
Thiourea or thiourea and urea (hereinafter simply referred to as thiourea, etc.).

)の添加量とフオーム化以降の発生ホルムアルデヒド量
との関係は樹脂液の製造条件、特に樹脂液中の未反応ホ
ルムアルデヒド分の影響をうけるほか、フオーム化の機
械的条件の影響を受けるので、チオ尿素等の添加量を一
義的に決めるのは難しいが、通常樹脂液の固形分に対し
て重量比で1〜20%用いるのが適当である。
) and the amount of formaldehyde generated after foaming is affected by the manufacturing conditions of the resin solution, especially the amount of unreacted formaldehyde in the resin solution, as well as the mechanical conditions of foaming. Although it is difficult to unambiguously determine the amount of urea to be added, it is usually appropriate to use it in an amount of 1 to 20% by weight based on the solid content of the resin liquid.

チオ尿素等の添加量が少い場合は発生ホルムアルデヒド
量の低減効果が不十分となり、逆に添加量が多過ぎる場
合はフオームの密度の増大、圧縮強度の低下等を来たし
、いずれも好ましくない。
If the amount of thiourea etc. added is small, the effect of reducing the amount of formaldehyde generated will be insufficient, and if the amount added is too large, the density of the foam will increase, the compressive strength will decrease, etc., both of which are undesirable.

チオ尿素等の添加は硬化液の調製時に硬化剤、起泡剤、
助剤等といっしょに加えて撹拌溶解し、水溶液とすれば
よい。
Addition of thiourea, etc. is a curing agent, foaming agent,
It may be added together with auxiliary agents, stirred and dissolved to form an aqueous solution.

もちろん硬化液の使用時に添加することもできる。Of course, it can also be added when the curing liquid is used.

チオ尿素等を添加した硬化液は通常50℃以下では1ケ
月以上安定であるが、高温になると硬化剤の影響でチオ
尿素等の分解を起す可能性があるので、できるだけ低温
に保存し、早目に使用する方がよい。
Curing liquids containing thiourea, etc. are usually stable at temperatures below 50°C for more than a month, but at high temperatures, thiourea, etc. may decompose due to the effect of the curing agent, so store it at as low a temperature as possible and cure it as soon as possible. Better to use on eyes.

この点で、チオ尿素等の水溶液をフオーム化の直前に混
合すれば最も安全である。
In this respect, it is safest if an aqueous solution of thiourea or the like is mixed immediately before foaming.

本発明によれば硬化液中にチオ尿素等を含有せしめるだ
けの簡便な方法により、ホルムアルデヒド臭の軽微なU
Fフオームが得られ、特に住宅用断熱材、炭坑用充填材
等の用途に顕著な効果をもたらすものである。
According to the present invention, by simply adding thiourea or the like to the curing solution, U.
F form is obtained, which brings about remarkable effects especially in applications such as insulation materials for houses and fillers for coal mines.

以下本発明の方法を実施例により説明する。The method of the present invention will be explained below with reference to Examples.

実施例中の部は重量部を表わす。Parts in the examples represent parts by weight.

実施例 1 尿素36.7部、37%ホルマリン75.4部、水30
部および24%アンモニア水0.3部を撹拌混合しなが
ら、90℃付近で30分ないし1時間反応させた。
Example 1 36.7 parts of urea, 75.4 parts of 37% formalin, 30 parts of water
1 part and 0.3 part of 24% aqueous ammonia were stirred and mixed at around 90°C for 30 minutes to 1 hour.

40%ギ酸を加えてPHを4〜5に調整し、さらに1時
間反応させたのち、20%カセイソーダでPHを8に調
整した。
The pH was adjusted to 4 to 5 by adding 40% formic acid, and after further reaction for 1 hour, the pH was adjusted to 8 with 20% caustic soda.

尿素4.2部を加え、65℃で30分間反応させたのち
直ちに冷却して得られた反応物を同容量の水で希釈し、
樹脂液を調製した。
After adding 4.2 parts of urea and reacting at 65°C for 30 minutes, the reaction product obtained by immediately cooling was diluted with the same volume of water.
A resin liquid was prepared.

85%リン酸13.4部、分岐状ドデシルベンゼンスル
ホン酸ナトリウム8.3部、安定剤3.3部を撹拌混合
したのち、これに別途チオ尿素29.4部を水45.7
部に溶解したものを加えて、さらに撹拌混合したのち水
で容量比10倍に希釈して硬化液を調製した。
After stirring and mixing 13.4 parts of 85% phosphoric acid, 8.3 parts of sodium branched dodecylbenzenesulfonate, and 3.3 parts of a stabilizer, 29.4 parts of thiourea was added to 45.7 parts of water.
After stirring and mixing, the mixture was diluted with water to a volume ratio of 10 to prepare a hardening solution.

上記の樹脂液および硬化液を容量比1対1の割合で用い
、英B、1.P、社より市販されているUPフオーム用
の発泡ガンを使用し、空気を吹き込んで発泡させ、硬化
、乾燥させて本発明のUPフオームを得た。
Using the above resin liquid and curing liquid at a volume ratio of 1:1, English B, 1. Using a foaming gun for UP foam commercially available from P. Co., Ltd., air was blown into the foam, followed by curing and drying to obtain the UP foam of the present invention.

このフオームの密度は11.8kg/m’、圧縮強度は
0.299 /cyrt−で、JISA−5908に従
って発泡1時間後から24時間の間に発生したホルムア
ルデヒド量を測定した結果は13.8ppmであり、ホ
ルムアルデヒド臭は極めて軽微であった。
The density of this foam is 11.8 kg/m', the compressive strength is 0.299/cyrt-, and the amount of formaldehyde generated during 24 hours from 1 hour after foaming was measured according to JISA-5908, and the result was 13.8 ppm. Yes, and the formaldehyde odor was extremely slight.

比較例 1 実施例1の方法で硬化液調製時にチオ尿素の使用を省略
したほかは実施例1と同様に行った。
Comparative Example 1 The same procedure as in Example 1 was carried out except that the use of thiourea was omitted when preparing the hardening solution.

得られたUFフオームの密度は10.1 kg/ m’
、圧縮強度は0.35 kg/cyiで、J I S
A−5908に従って発泡1時間後から24時間の間に
発生したホルムアルデヒド量を測定した結果は86.4
ppmであり、ホルムアルデヒド臭が顕著であった。
The density of the obtained UF foam is 10.1 kg/m'
, compressive strength is 0.35 kg/cyi, JIS
According to A-5908, the amount of formaldehyde generated during 24 hours from 1 hour after foaming was measured and the result was 86.4.
ppm, and the formaldehyde odor was noticeable.

比較例 2 実施例1の方法で、硬化剤調製時にチオ尿素29.4部
の代りに尿素29.4部を用いたほかは実施例1と同様
に実施した。
Comparative Example 2 The same procedure as in Example 1 was carried out except that 29.4 parts of urea was used instead of 29.4 parts of thiourea when preparing the curing agent.

得られたUFフオームの密度は10.9 kg/ m’
、圧縮強度は0.30 kg/cyrYで、発生ホルム
アルデヒド量は18.5ppmであった。
The density of the obtained UF foam is 10.9 kg/m'
The compressive strength was 0.30 kg/cyrY, and the amount of formaldehyde generated was 18.5 ppm.

実施例 2〜4 実施例1の方法で、硬化剤の調製時にチオ尿素等の添加
量を変更したほかは、実施例1と同様に実施した結果は
次表の通りであった。
Examples 2 to 4 Examples 2 to 4 were carried out in the same manner as in Example 1, except that the amount of thiourea etc. added during the preparation of the curing agent was changed, and the results were as shown in the following table.

Claims (1)

【特許請求の範囲】[Claims] 1 尿素−ホルムアルデヒド初期反応物水溶液と硬化剤
および起泡剤を含む水溶液とを反応させて尿素−ホルム
アルデヒド樹脂発泡体を製造する方法において、硬化剤
および起泡剤を含む水溶液中にチオ尿素またはチオ尿素
と尿素を含有せしめることを特徴とする尿素−ホルムア
ルデヒド樹脂発泡体の製造方法。
1. In a method for producing a urea-formaldehyde resin foam by reacting an aqueous solution of a urea-formaldehyde initial reactant with an aqueous solution containing a curing agent and a foaming agent, thiourea or thiourea is added to the aqueous solution containing a curing agent and a foaming agent. A method for producing a urea-formaldehyde resin foam, characterized by containing urea and urea.
JP3936279A 1979-04-03 1979-04-03 Method for producing urea-formaldehyde resin foam Expired JPS5826370B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3936279A JPS5826370B2 (en) 1979-04-03 1979-04-03 Method for producing urea-formaldehyde resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3936279A JPS5826370B2 (en) 1979-04-03 1979-04-03 Method for producing urea-formaldehyde resin foam

Publications (2)

Publication Number Publication Date
JPS55133434A JPS55133434A (en) 1980-10-17
JPS5826370B2 true JPS5826370B2 (en) 1983-06-02

Family

ID=12550948

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3936279A Expired JPS5826370B2 (en) 1979-04-03 1979-04-03 Method for producing urea-formaldehyde resin foam

Country Status (1)

Country Link
JP (1) JPS5826370B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102005027552A1 (en) * 2005-06-14 2006-12-21 Basf Ag Thermoformable melamine / formaldehyde foams with low formaldehyde emission

Also Published As

Publication number Publication date
JPS55133434A (en) 1980-10-17

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