JPH0482006B2 - - Google Patents

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Publication number
JPH0482006B2
JPH0482006B2 JP61162687A JP16268786A JPH0482006B2 JP H0482006 B2 JPH0482006 B2 JP H0482006B2 JP 61162687 A JP61162687 A JP 61162687A JP 16268786 A JP16268786 A JP 16268786A JP H0482006 B2 JPH0482006 B2 JP H0482006B2
Authority
JP
Japan
Prior art keywords
weight
foam
parts
surfactant
manufactured
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 - Lifetime
Application number
JP61162687A
Other languages
Japanese (ja)
Other versions
JPS6317920A (en
Inventor
Tsutomu Toyoda
Masatsugu Sekiguchi
Etsuji Iwami
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.)
Resonac Corp
Original Assignee
Hitachi Chemical 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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP61162687A priority Critical patent/JPS6317920A/en
Publication of JPS6317920A publication Critical patent/JPS6317920A/en
Publication of JPH0482006B2 publication Critical patent/JPH0482006B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳现な説明】[Detailed description of the invention]

産業䞊の利甚分野 本発明は埗られる発泡䜓の難燃特性に優れ、か
぀発泡時の液の流動性の優れた発泡甚暹脂組成物
に関する。 埓来の技術 最近、建築甚材料ずくに䜏宅甚倖壁材に察する
難燃性の芁求は厳しさを増しおおり、建蚭省告瀺
第1231号準䞍燃詊隓に同第1372号暡型箱詊隓が远
加されるに至぀た。前蚘建蚭省告瀺第1372号暡型
箱詊隓ずは同第1231号準䞍燃詊隓における残炎、
枩床時間面積、発煙係数の芏制倀を満たした䞊
で、詊隓䜓を倧型化し、燃焌時の発熱量、燃焌埌
の圢状を刀定するずいう倧倉厳しいものである。
工業甚ポリオヌルを原料ずしお発泡させたむ゜シ
アヌレヌト環を有する埓来のむ゜シアヌレヌト発
泡䜓ポリりレタン発泡䜓の䞀皮を甚いた構造
䜓は燃焌埌の圢状倉化が著しく発熱量も倧きいた
め、前蚘第1372号暡型箱型詊隓に合栌するのは難
しい。 䞀方、公知のプノヌル発泡䜓を甚いた構造䜓
は、燃焌埌の圢状倉化は少ないが、燃焌埌の残炎
時間が長いずいう欠点を持぀。埓来む゜シアヌレ
ヌト環を有するむ゜シアヌレヌト発泡䜓ポリり
レタン発泡䜓の䞀皮を成圢するのに䜿甚しおい
る補造蚭備をプノヌル発泡䜓成圢甚に切替える
堎合は、発泡時及び発泡埌の加熱装眮を高枩で䞔
぀長時間加熱できる装眮に倉曎しなければなら
ず、又この装眮を甚いたプノヌル発泡䜓の補造
法も極めお䜜業性の悪いものである。䞀方、炭氎
化物を原料ずしお発泡させた発泡䜓を甚いた構造
䜓は工業甚ポリオヌルを原料ずするむ゜シアヌレ
ヌト発泡䜓を甚いた構造䜓に比べ燃難性は向䞊す
るが、ずくに発泡時の液の流動性が劣るため、パ
ネル補造時に端郚ぞの充おん性が悪く、たた高密
床の発泡䜓しか埗られずコスト高ずなり、生産性
も劣぀おいる。 発明が解決しようずする問題点 本発明はかかる問題点に鑑みおなされたもので
あり、ポリりレタン発泡䜓の優れた䜜業性を生か
しお、埗られる発泡䜓の難燃特性に優れ、か぀発
泡時の液の流動性の優れた発泡甚暹脂組成物を提
䟛するこずを目的ずする。 問題点を解決するための手段 本発明は、炭氎化物の氎溶液及び又はスラリ
ヌ、反応觊媒、む゜シアネヌト化合物、けい玠に
結合したメチル基、
(Industrial Application Field) The present invention relates to a foaming resin composition that provides excellent flame retardant properties of the resulting foam and excellent liquid fluidity during foaming. (Prior art) Recently, flame retardant requirements for building materials, especially residential exterior wall materials, have become more stringent, and a model box test No. 1372 has been added to the Ministry of Construction notification No. 1231 semi-flammability test. It came to this. The Ministry of Construction Notification No. 1372 model box test refers to the afterflame in the same No. 1231 quasi-noncombustible test.
It is a very demanding process that requires meeting the regulatory values for temperature, time, area, and smoke production coefficient, then increasing the size of the test specimen and determining the amount of heat generated during combustion and the shape after combustion.
Structures using conventional isocyanurate foam (a type of polyurethane foam) having isocyanurate rings made from industrial polyol as a raw material undergo significant shape change after combustion and have a large calorific value, so the above-mentioned No. 1372 Passing the model box test is difficult. On the other hand, structures using known phenol foams do not change their shape after combustion, but have the disadvantage of a long afterflame time after combustion. When switching manufacturing equipment that has been conventionally used for molding isocyanurate foam (a type of polyurethane foam) having isocyanurate rings to molding phenol foam, the heating device during and after foaming must be heated to high temperature. In addition, it is necessary to change to a device that can heat for a long time, and the method for producing phenol foam using this device is also extremely inefficient. On the other hand, structures using foams made from carbohydrates have improved flame retardancy compared to structures using isocyanurate foams made from industrial polyols. Due to its poor properties, it is difficult to fill the edges during panel manufacture, and only a high-density foam can be obtained, resulting in high costs and poor productivity. (Problems to be Solved by the Invention) The present invention has been made in view of the above-mentioned problems, and takes advantage of the excellent workability of polyurethane foam to provide a foam that has excellent flame retardant properties and An object of the present invention is to provide a foaming resin composition having excellent liquid fluidity. (Means for Solving the Problems) The present invention provides an aqueous solution and/or slurry of carbohydrates, a reaction catalyst, an isocyanate compound, a methyl group bonded to silicon,

【匏】単䜍及び ―CH2CH2O―単䜍を有し、けい玠に結合したメ
チル基のモル数を、
[Formula] The number of moles of methyl group having units and (-CH 2 CH 2 O)- units and bonded to silicon is X,

【匏】単䜍の モル数を及び―CH2CH2O―単䜍のモル数を
ずしたずきに0.5〜11および〜 1.8であるシリコヌン敎泡剀、界面掻性剀ただ
しシリコヌン敎泡剀を陀くおよび必芁に応じお
難燃剀を含有しおなる発泡甚暹脂組成物に関す
る。 本発明になる発泡甚暹脂組成物に䜿甚する炭氎
化物の氎溶液及び又はスラリヌずは、果糖、ぶ
どう糖、砂糖、麊芜糖、セルロヌス等を単独で、
又は皮以䞊を組み合わせお氎に溶解させた氎溶
液、氎に分散させたスラリヌ又はその氎溶液ずス
ラリヌの混合溶液である。垂販品ずしお入手し埗
るものずしおは、王子コンスタヌチ株匏䌚瀟補、
異性化糖−42、−55およびHCがある。䟋え
ばHCは果糖55.9重量、ぶどう糖39.2重量、
その他の糖分4.9重量を含むものであり、さら
に氎分を党䜓ずしお24.5重量含む混合物であ
る。たた参束工業株匏䌚瀟補、サンクラフト550
は糖成分ずしお果糖55.6重量、ぶどう糖39.3重
量、オリゎ糖5.1重量を含むものであり、さ
らに氎分を党䜓ずしお24.5重量含む混合物であ
る。 本発明における反応觊媒ずしおは、ゞブチルス
ズゞラりレヌト、ゞブチルスズゞオクト゚ヌト等
のスズ化合物、トリ゚チルアミン、トリ゚チレン
ゞアミン、トリ゚タノヌルアミン、−ゞメチル
アミノ−−メチル−−プロパノヌル、−ア
ミノ−−メチル−−プロパノヌル等のアミン
化合物などがある。 本発明に甚いられる界面掻性剀ずしおはノニオ
ン界面掻性剀、アニオン界面掻性剀、カチオン界
面掻性剀および䞡性界面掻性剀のいずれも䜿甚可
胜であり、これらを単独であるいは組み合わせお
䜿甚するこずができる。 ノニオン系界面掻性剀には、日本油脂株匏䌚瀟
補のノニオンLP−20R、ノニオンOP−85R、ノ
ニオンLT−221、ノニオンPT−221、ノニオン
−13P、ノニオンMN−811、ノニオン−206、
ノニオン−208、ノニオン−215、ノニオン
−204、ノニオン−208.5、パヌ゜フトNK−60、
パヌ゜フトNK−100、ノニオンNS−202、ノニ
オンNS−240、ノニオン−206、ノニオンHS−
208、ノニオン−、ノニオン−、ノニオ
ン−10、ノニオン−、ノニオン−、ノ
ニオン−、プロノン102、プロノン201、デむ
スパノヌルLS−100、デむスパノヌル−、ス
タホヌム、スタホヌムFKスタホヌムDL、ス
タホヌムDO、スタホヌムDO−、スタホヌム
、ペネゟヌル−100、カヌボダツシナシリヌ
ズ、䜏友スリヌ゚ム株匏䌚瀟補のFC−170C、FC
−430、FC−431、䞉掋化成工業株匏䌚瀟補のノ
ニポヌル20、ノニポヌル60、ノニポヌル140、ノ
ニポヌル800、ノニポヌル−160、オクタポヌル
45、オクタポヌル80、オクタポヌル100、オクタ
ポヌル400、ノニポヌル゜フトSM−55、ノニポ
ヌル゜フトSMH−30、゚マルミン40、゚マルミ
ン70、゚マルミン240、゚マルミン−380、むオ
ネツトMS−400、むオネツトMO−400、むオネ
ツトDO−200、むオネツト−20、むオネツト
−85、むオネツト−20C、むオネツト−
80C、ニナヌポヌルPE−61、ニナヌポヌルPE−
71、ニナヌポヌルPE−108、ニナヌポヌルNPE
−2700、プロフアンEX−24、プロフアン2012E、
プロフアン1281などが甚いられる。アニオン系界
面掻性剀ずしおは、日本油脂株匏䌚瀟補のダむダ
ポン、トラツクス−45、トラツクス−
45W、トラツクス−40、トラツクス−300、
トラツクス−300、ニナヌレツクスRS、ニナヌ
レツクス、ノニサヌルOK−、ノニサヌル
OK−、ナむリナヌベ、パヌ゜フトSFT、パヌ
゜フトSLT、パヌ゜フトEF、パヌ゜フトELT、
パヌ゜フトEDO、ラピゟヌル−30、ラピゟヌ
ル−90、ポリスタヌ−1060、ポリスタヌ
SMX−、オレオむルザルコシン221P、サンア
ミド−、フむレツト、゜ルノンSS、ロむ
ダル、゜ルノン、䜏友スリヌ゚ム株匏䌚瀟補
のFC−93、FC−95、FC−98、FC−129などが甚
いられる。カチオン系界面掻性剀ずしおは日本油
脂株匏䌚瀟補のカチオンSA、カチオンMA、カ
チオンDTA、カチオンAB、カチオンAB−600、
カチオンABT2−500、カチオンBB、カチオン
FB、カチオンPB−40、カチオンVB、カチオン
F2−20R、カチオンF2−50E、カチオンE2−
40PO、カチオン−207、ナむミヌン−201、
ナむミヌン−202、ナむミヌン−215、ナむミ
ヌン−202、ナむミヌン−220、ナむミヌン
T2−202、ナむミヌンT2−260、ナむミヌンDT−
208、フむレツト、アスフアゟヌル10、䜏友ス
リヌ゚ム株匏䌚瀟補のFC−135などが甚いられ
る。䞡性界面掻性剀ずしおは、日本油脂株匏䌚瀟
補のアノンBF、アノンBL、アノンLGなどがあ
る。 本発明に甚いられるシリコヌン敎泡剀ずしお
は、組成物の盞溶性および流動性の点からけい玠
に結合したメチル基、
[Formula] The number of moles of unit is Y and the number of moles of (-CH 2 CH 2 O)-unit is Z
contains a silicone foam stabilizer, a surfactant (excluding the silicone foam stabilizer) and, if necessary, a flame retardant, where Y+Z/X=0.5 to 11 and Y/Z=0 to 1.8. The present invention relates to a foaming resin composition. The carbohydrate aqueous solution and/or slurry used in the foaming resin composition of the present invention includes fructose, glucose, sugar, maltose, cellulose, etc. alone,
Alternatively, it is an aqueous solution prepared by dissolving two or more types in water, a slurry dispersed in water, or a mixed solution of the aqueous solution and slurry. Commercially available products include Oji Cornstarch Co., Ltd.
There are isomerized sugars F-42, F-55 and HC. For example, HC is fructose 55.9% by weight, glucose 39.2% by weight,
The mixture contains 4.9% by weight of other sugars and 24.5% by weight of water overall. Also manufactured by Sanmatsu Kogyo Co., Ltd., Suncraft 550
is a mixture containing 55.6% by weight of fructose, 39.3% by weight of glucose, and 5.1% by weight of oligosaccharides as sugar components, and further contains 24.5% by weight of water as a whole. Examples of the reaction catalyst in the present invention include tin compounds such as dibutyltin dilaurate and dibutyltin dioctoate, triethylamine, triethylenediamine, triethanolamine, 2-dimethylamino-2-methyl-1-propanol, and 2-amino-2-methyl- Examples include amine compounds such as 1-propanol. As the surfactant used in the present invention, any of nonionic surfactants, anionic surfactants, cationic surfactants and amphoteric surfactants can be used, and these can be used alone or in combination. Nonionic surfactants include Nonion LP-20R, Nonion OP-85R, Nonion LT-221, Nonion PT-221, and Nonion A manufactured by NOF Corporation.
-13P, Nonion MN-811, Nonion E-206,
Nonion P-208, Nonion P-215, Nonion K
-204, Nonion T-208.5, Persoft NK-60,
Persoft NK-100, Nonion NS-202, Nonion NS-240, Nonion-206, Nonion HS-
208, Nonion L-2, Nonion S-2, Nonion S-10, Nonion O-2, Nonion O-6, Nonion T-4, Pronone 102, Pronone 201, Dispanol LS-100, Dispanol K-3, Starhome F, Starhome FK, Starhome DL, Starhome DO, Starhome DO-S, Starhome T, Penezol H-100, Carbo Datsushi series, FC-170C manufactured by Sumitomo 3M Co., Ltd., FC
-430, FC-431, Nonipole 20, Nonipole 60, Nonipole 140, Nonipole 800, Nonipole D-160, Octapol manufactured by Sanyo Chemical Industries, Ltd.
45, Octapol 80, Octapol 100, Octapol 400, Nonipole Soft SM-55, Nonipole Soft SMH-30, Emulmin 40, Emulmin 70, Emulmin 240, Emulmin L-380, Ionets MS-400, Ionets MO- 400, Ionets DO-200, Ionets S-20, Ionets S-85, Ionets T-20C, Ionets T-
80C, New Paul PE-61, New Paul PE-
71, New Paul PE-108, New Paul NPE
-2700, Profan EX-24, Profan 2012E,
Profan 1281 etc. are used. Examples of anionic surfactants include Diapon S, Trax H-45, and Trax H- manufactured by NOF Corporation.
45W, Trax K-40, Trax K-300,
Trax N-300, Nurex RS, Nurex R, Nonisar OK-1, Nonisar
OK-2, Nairiyube, Persoft SFT, Persoft SLT, Persoft EF, Persoft ELT,
Persoft EDO, Rapizol B-30, Rapizol B-90, Polyster A-1060, Polyster
SMX-1, oleoylsarcosine 221P, Sanamide C-3, Fillet L, Solnon SS, Royal M, Solnon P, FC-93, FC-95, FC-98, FC-129 manufactured by Sumitomo 3M Ltd. used. Examples of cationic surfactants include Cation SA, Cation MA, Cation DTA, Cation AB, and Cation AB-600 manufactured by NOF Corporation.
Cation ABT 2 −500, Cation BB, Cation
FB, cation PB-40, cation VB, cation
F 2 −20R, cation F 2 −50E, cation E 2 −
40PO, cation L-207, Naimeen L-201,
Naimeen L-202, Naimeen F-215, Naimeen S-202, Naimeen S-220, Naimeen
T 2 −202, Naimeen T 2 −260, Naimeen DT−
208, Fillet Q, Asfazole 10, FC-135 manufactured by Sumitomo 3M Ltd., etc. are used. Examples of amphoteric surfactants include Anon BF, Anon BL, and Anon LG manufactured by NOF Corporation. The silicone foam stabilizer used in the present invention includes silicon-bonded methyl groups,

【匏】単䜍及 び―CH2CH2O―単䜍を有し、けい玠に結合した
メチル基のモル数を、
[Formula] The number of moles of methyl group having units and (-CH 2 CH 2 O)- units and bonded to silicon is X,

【匏】単䜍 のモル数を及び―CH2CH2O―単䜍のモル数を
ずしたずきに0.5〜11および 〜1.8のものが甚いられる。およびが䞊
蚘の範囲倖においおは発泡時の流動性が劣る。 0.5〜11および〜1.0の範囲の ものがさらに奜たしい。 このようなシリコヌン敎泡剀ずしおは、䟋えば
次匏に瀺されるものがある。 䞊匏においおはアルキレン基等、R′はアル
キル基等、は又は正の数であ
る。 本発明に䜿甚されるシリコヌン敎泡剀ずしお
は、東芝シリコヌン株匏䌚瀟補のTFA−4200、
TSF−4452、TFA−4310、TSF−4445、日本ナ
ニカヌ株匏䌚瀟補のSZ−1605、SZ−1623、SZ−
1610、信越化孊株匏䌚瀟補の−318、−341、
−347、−350Sなどがある。 シリコヌン敎泡剀の各セグメントのモル数
は通垞NMR分光法で枬定される。テトラ
メチルシランのメチル基のピヌクを0ppmずする
ず (a) けい玠に結合するメチル基のピヌクは0.05〜
0.30ppmにあらわれるので、このピヌクの積分
倀をメチル基のプロトン数で割぀た倀をず
する。 (b)
[Formula] Where Y is the number of moles of units and Z is the number of moles of (-CH 2 CH 2 O)- units, those in which Y+Z/X=0.5 to 11 and Y/Z=0 to 1.8 are used. If X, Y and Z are outside the above ranges, the fluidity during foaming will be poor. More preferably, Y+Z/X is in the range of 0.5 to 11 and Y/Z is in the range of 0 to 1.0. Examples of such silicone foam stabilizers include those represented by the following formula. In the above formula, R is an alkylene group, R' is an alkyl group, etc., and m, n, Z, and Y are 0 or a positive number. The silicone foam stabilizer used in the present invention includes TFA-4200 manufactured by Toshiba Silicone Corporation;
TSF-4452, TFA-4310, TSF-4445, SZ-1605, SZ-1623, SZ- manufactured by Nippon Unicar Co., Ltd.
1610, F-318, F-341 manufactured by Shin-Etsu Chemical Co., Ltd.
There are F-347, F-350S, etc. Number of moles of each segment of silicone foam stabilizer X,
Y and Z are usually measured by NMR spectroscopy. If the peak of the methyl group of tetramethylsilane is 0 ppm, (a) the peak of the methyl group bonded to silicon is 0.05~
Since it appears at 0.30 ppm, X is the value obtained by dividing the integral value of this peak by the number of protons in the methyl group, which is 3. (b)

【匏】単䜍においおはCH3− メチル基のピヌクが0.90〜1.30ppmにあら
われるので、このピヌクの積分倀をメチル基の
プロトン数で割぀た倀をずする。 (c) ―CH2CH2O―単䜍においおは3.10〜
3.90ppmにCH2のピヌクがあらわれるので、こ
のピヌクの積分倀をプロトン数で割぀た倀を
ずする。 以䞊のようにしお求めたから
およびの倀が決定される。 本発明においお必芁に応じお䜿甚される難燃剀
ずしおはトリス−クロロ゚チルフオスプ
ヌト、トリス−クロロプロピルフオスプ
ヌト、塩玠化パラフむン、ヘキサブロムベンれン
等の有機系難燃剀、䞉酞化アンチモン、氎酞化ア
ルミニりム等の無機系難燃剀などがあり、これら
を単独で、又は組み合わせお䜿甚するこずができ
る。 本発明におけるむ゜シアネヌト化合物ずしおは
トリレンゞむ゜シアネヌト、ヘキサメチレンゞむ
゜シアネヌト、む゜ホロンゞむ゜シアネヌト、ゞ
プニルメタン−4′−ゞむ゜シアネヌト、ポ
リメチレンポリプニルむ゜シアネヌト等、これ
らの混合物、これらのむ゜シアネヌトの誘導䜓な
どがあり粟補又は粗補の䜕れのむ゜シアネヌト化
合物も䜿甚でき、プニルむ゜シアネヌト等のモ
ノむ゜シアネヌト化合物を䜵甚するこずもでき
る。 たた本発明になる発泡甚暹脂組成物を甚いお構
造䜓を造る堎合には、該暹脂組成物から埗られる
発泡䜓の少なくずも片面に難燃若しくは䞍燃性の
板又はシヌトが蚭けられるが、この板又はシヌト
ずしおはアルミクラフト玙、アルミニりム箔、銅
箔等の金属箔、アルミアスベストシヌト、朚毛セ
メント板、鉄板、鋌板、ステンレス板、アルミニ
りム板、銅板等の金属板、スレヌト板、ケむ酞カ
ルシりム板、石膏ボヌド、セメント板、ガラス繊
維匷化セメント板等の無機質䞍燃板などがある。 これら難燃若しくは䞍燃性の板又はシヌトは倖
芳䞊又は腐食防止等の理由で塗装をしおも差し支
えがない。塗装に䜿甚する塗料は難燃性を䜎䞋さ
せないよう、その材質又は塗膜の厚みを充分考慮
する必芁があるが、塗膜が薄ければその材質に特
に制限はなく、通垞垂販されおいるカラヌ鉄板で
も充分䞍燃性の板ずしお䜿甚できる。 本発明になる発泡甚暹脂組成物䞭の各成分の配
合割合には特に制限はないが (a) 炭氎化物の氎溶液及び又はスラリヌ
50〜200重量郹 (b) 反応觊媒 0.1〜重量郚 (c) 界面掻性剀ただしシリコヌン敎泡剀を陀
く 0.1〜重量郚 (d) 䞊蚘のシリコヌン敎泡剀 0.1〜重量郚 (e) む゜シアネヌト化合物 50〜200重量郹 (f) 難燃剀遞択的 0.1〜100重量郹 の割合で䜿甚するこずが奜たしく、 (a) 炭氎化物の氎溶液及び又はスラリヌ
50〜150重量郹 (b) 反応觊媒 0.5〜4.0重量郹 (c) 界面掻性剀ただしシリコヌン敎泡剀を陀
く 0.5〜4.0重量郹 (d) 䞊蚘のシリコヌン敎泡剀 0.5〜4.0重量郹 (e) む゜シアネヌト化合物 50〜150重量郹 (f) 難燃剀遞択的 〜50重量郹 の割合で䜿甚するこずがさらに奜たしい。たた䜜
業性の関係で、䟋えば(a)及び(b)の混合物ず(c)
(d)(e)及び(f)の混合物を準備しおおき、この䞡者
を混合し、反応させ発泡させるこずも可胜であ
る。反応枩床は特に制限はないが、10〜50℃が奜
たしく、混合時の撹拌機の回転数も特に制限はな
いが1000〜7000回転分が奜たしい。発泡䜓を成
圢するのに際しおは、特に制限はないが型を䜿甚
するのが奜たしく、䟋えば、䞊郚が開攟され底を
有する型を甚い、この䞋面に難燃若しくは䞍燃性
の板又はシヌトを眮き、型を均䞀な発泡䜓を埗る
のに奜たしい30℃〜90℃に加枩しおおく。次に前
蚘の各材料を撹拌しお混合しお、この型内に流し
蟌む、぀いで難燃若しくは䞍燃性の板又はシヌト
を備え、均䞀な発泡䜓を埗るのに奜たしい30℃〜
90℃に加枩しおおいた䞊型をこの板又はシヌトの
面を溶液の混合物に向けお茉せ、型締めし、発泡
させるこずにより、発泡䜓ず難燃若しくは䞍燃性
の板又はシヌトずが密着した構造䜓を埗るこずが
出来る。ここで難燃若しくは䞍燃性の板又はシヌ
トは発泡䜓の片面又は䞡面の䜕れに蚭けおも良い
が、䞡面に蚭けサンドむツチ構造にしたものの方
が難燃特性を高める䞊で奜たしい。この堎合、発
泡䜓の䞡面に蚭ける難燃若しくは䞍燃の板又はシ
ヌトは同䞀のものでも異皮のものの組み合わせで
も良い。 実斜䟋 実斜䟋  本発明の実斜䟋を説明する。実斜䟋においお
は前蚘の基のモル数を瀺す。 果糖75重量郚、氎道氎25重量郚、䞡性界面掻性
剀日本油脂瀟補、商品名ニツサンアノンBF
1.0重量郚にトリ゚タノヌルアミン1.5重量郚を加
えよく混合し溶液を埗た。 ゞプニルメタンゞむ゜シアネヌト日本ポリ
りレタン瀟補、商品名ミリオネヌトMR−100
80重量郚にシリコヌン敎泡剀日本ナニカヌ瀟
補、商品名敎泡剀SZ−1623、NMR分光法による
枬定倀1.321.0重量郚、ト リス−クロロ゚チルフオスプヌトを20重
量郚を加え混合し溶液を埗た。 流動性を評䟡するためにパネル充おん性等を調
べた。パネルのコヌナヌ郚ぞの充おん性流れ
性を段階評䟡点数が高い充おん性がすぐれ
おいるするもので次のような方法で調べた。 溶液A100重量郚ず溶液B150重量郚を加え、タ
ヌビン矜根の付いた撹拌機を甚いお2000回転分
で秒間撹拌、混合したものを70℃に保枩した平
板パネル䜜成型鉄補、内寞350mm×250mm×高さ
15mmに流し蟌む。90秒埌に脱型しおパネル厚
さ15mmを埗た。パネル充おん性は点であ぀
た。 溶液A100重量郚ず溶液B150重量郚をタヌビン
矜根の付いた撹拌機を甚いお2000回転分で秒
間撹拌、混合したものを25℃に保枩し䞊郚が開攟
され底を有する朚型補箱内寞250mm×250mm×高
さ250mm内に流し蟌み、120秒埌の発泡䜓の高さ
は350mmであ぀た。 溶液A100重量郚ず溶液B150重量郚をタヌビン
矜根の付いた撹拌機を甚いお2000回転分で秒
間撹拌、混合したものを第図のくさび型型枩
床70℃内に流し蟌み、90秒埌に脱型し流れ距離
を枬定したが、この発泡䜓の流れ距離は230mmで
あ぀た。 次に溶液A100重量郚ず溶液B100重量郚を加
え、タヌビン矜根の付いた撹拌機で2000回転分
で秒間撹拌、混合したものを40℃に保枩した䞊
郚が開攟され底を有する朚型220mm×220mm×高
さ15mm内に流し蟌みこれに40℃に保枩した䞊型
を茉せお型締めした。10分埌に脱型しお発泡䜓
厚さ15mmを埗た。この発泡䜓の密床は0.024
cm3、小口吞氎量は90であ぀た。 以䞋、本発明になる発泡甚暹脂組成物を甚いた
難燃性構造䜓の参考䟋を瀺す。 参考䟋  䞊郚が開攟され底を有する朚型内容積220mm
×220mm×15mmの䞋面にカラヌ鉄板厚さ0.27
mmを眮いお型を40℃に加枩しおおく。次に実斜
䟋で甚いた溶液A100重量郚に溶液B150重量郹
を加えタヌビン矜根の付いた撹拌機で2000回転
分で秒間撹拌、混合し、これを䞊蚘型内ぞ流し
蟌み、これに、䞊面にアルミクラフト玙を貌り付
け40℃に加枩した䞊型をアルミクラフト玙を溶液
の混合物に向けお茉せ型締めした。10分埌に脱型
しお発泡䜓厚さ15mmの衚面にカラヌ鉄板厚
さ0.27mm、裏面にアルミクラフト玙が接着した
難燃性構造䜓を埗た。この構造䜓の芯材である発
泡䜓の密床は0.024cm3、小口吞氎量は90
であり、均䞀で埮现なセル構造を有する発泡䜓
で、埓来の発泡䜓ず比べ小口吞氎量、流動性の点
においお遜色ないものであ぀た。この構造䜓を甚
いお建蚭省告瀺第1231号に基づく䞍燃詊隓を行぀
た結果を衚に瀺す。衚から明らかなようにこ
の構造䜓は燃焌埌の倖芳圢状、残炎、発煙係数、
枩床係数、枩床時間面積の各点においお極めお優
れおいた。 たたこの構造䜓はカラヌ鉄板およびアルミクラ
フト玙に察する接着性は優れおいた。 実斜䟋  果糖75重量郚、氎道氎25重量郚、実斜䟋で甚
いたシリコヌン敎泡剀1.0重量郚、ノニオン系界
面掻性剀日本油脂瀟補、商品名ノニオンNS−
2001.0重量郚にトリ゚タノヌルアミン1.5重量
郚を加えよく混合し溶液を埗た。 実斜䟋で埗られた溶液A100重量郚に溶液C150
重量郚を加え、タヌビン矜根の付いた撹拌機を甚
いお2000回転分で秒間撹拌、混合し以䞋参考
䟋ず同様にしお発泡䜓厚さ15mmの衚面にカ
ラヌ鉄板、裏面にアルミクラフト玙が接着した構
造䜓を埗た。この堎合の発泡䜓のパネル充おん性
は点、発泡高さ350mm、流れ距離225mm、発泡䜓
の密床は0.026cm3、小口吞氎量は130で
あり均䞀で埮现なセル構造を有する発泡䜓であ぀
た。たたこの構造䜓を甚いお建蚭省告瀺第1231号
に基づく準䞍燃詊隓を行぀た結果を衚に瀺す。
衚から明らかなように参考䟋ず比べ小口吞氎
量が倧きくな぀おいるが、流動性、燃難性は同等
の結果が埗られた。 比范䟋  果糖75重量郚、氎道氎25重量郚にトリ゚タノヌ
ルアミン1.5重量郚を加えよく混合し溶液を埗
た。 ゞプニルメタンゞむ゜シアネヌト日本ポリ
りレタン瀟補、商品名ミリオネヌトMR−100
80重量郚にシリコヌン敎泡剀東芝シリコヌン瀟
補、商品名TSF−4450、NMR分光法による枬定
倀9.86、1.0重量郚、トリス −クロロ゚チルフオスプヌトを20重量郹
を加え混合し溶液を埗た。 溶液D100重量郚に溶液E150重量郚を加え、タ
ヌビン矜根の付いた撹拌機を甚いお2000回転分
で秒間撹拌、混合し以䞋参考䟋ず同様にしお
発泡䜓厚さ15mmの衚面にカラヌ鉄板、裏面に
アルミクラフト玙が接着した構造䜓を埗た。この
堎合、発泡䜓のパネル充おん性は点、発泡高さ
は290mm、流れ距離は180mm、発泡䜓の密床は
0.035cm3、小口吞氎量は100で均䞀で埮
现なセル構造を有する発泡䜓であ぀た。たたこの
構造䜓を甚いお建蚭省告瀺第1231号に基づく準䞍
燃詊隓を行぀た結果を衚に瀺す。衚から明ら
かなように本比范䟋になる構造䜓はむ゜シアヌレ
ヌト発泡䜓や、プノヌル発泡䜓を甚いた構造䜓
に比べ燃焌埌の倖芳圢状、発煙係数、分埌の排
気枩床の各点においお向䞊しおいるものの、流動
性が劣぀おいた。 比范䟋  ヘテロフオヌム28264フツカヌ瀟補、商品名
21.1重量郚、ヘテロフオヌム29696フツカヌ瀟
補、商品名23.5重量郚、DC−193ダりコヌニ
ング瀟補、商品名重量郚、ポリキダツト41
サンアボツト瀟補、商品名1.42重量郚、フレ
オン11䞉井フロロケミカル瀟補、商品名25重
量郚を混合した溶液にむ゜ネヌト580アツプゞペ
ン瀟補、商品名101重量郚を加えタヌビン矜根
の付いた撹拌機で2000回転分で秒間撹拌、混
合し以䞋参考䟋ず同様にしおむ゜シアヌレヌト
発泡䜓厚さ15mmの衚面にカラヌ鉄板、裏面に
アルミクラフト玙が接着した構造を埗た。この堎
合、発泡䜓のパネル充おん性は〜点、発泡高
さは290mm、くさび型流れ距離は210mm、発泡䜓の
密床は0.035cm3、小口吞氎量は40であ
぀た。たたこの構造䜓を甚いお建蚭省告瀺第1231
号に基づく準䞍燃詊隓を行぀た結果を衚に瀺
す。衚から明らかなように本比范䟋になる構造
䜓の小口吞氎量は参考䟋の発泡䜓に比べすぐれお
いるが、燃焌埌の倖芳倉化は著しくほずんどの発
泡䜓が焌倱しおいた。発煙係数、時間枩床面積の
点においおも著しく劣぀おいた。 比范䟋  ダンプノン110A保土谷化孊瀟補、商品名
100重量郚ずフレオン11䞉井フロロケミカル瀟
補、商品名15重量郚を混合した溶液にダンプ
ノン110B硬化剀保土谷化孊瀟補、商品名40
重量郚、ダンプノン110C敎泡剀保土谷化孊
瀟補、商品名15重量郚を混合した溶液を加えタ
ヌビン矜根の付いた撹拌機で2000回転分で秒
間撹拌、混合し以䞋参考䟋ず同様にしおプノ
ヌル発泡䜓厚さ15mmの衚面にカラヌ鉄板、裏
面にアルミクラフト玙が接着した構造䜓を埗た。
しかし、プノヌル発泡䜓は硬化性が著しく劣る
ため100℃30分でアフタヌキナアを行぀た。この
堎合、発泡䜓のパネル充おん性は点、発泡高さ
は230mm、くさび型流れ距離は100mm、発泡䜓の密
床は0.040cm3、小口吞氎量は210であ぀
た。プノヌル発泡䜓の衚面にフラむアビリテむ
が生じるため該発泡䜓ずアルミクラフト玙及びカ
ラヌ鉄板ずの接着は劣぀おいた。 この構造物を甚いお建蚭省告瀺第1231号に基づ
く準䞍燃詊隓を行぀た結果を衚に瀺す。衚よ
り明らかなように本比范䟋の構造䜓は燃焌埌の倖
芳は良奜であ぀たが残炎が長く劣぀おいた。
In the [formula] unit, the peak of CH 3 − (methyl group) appears at 0.90 to 1.30 ppm, so Y is the value obtained by dividing the integral value of this peak by the number of protons of the methyl group, which is 3. (c) (-CH 2 CH 2 O) - 3.10~ in units
Since a CH 2 peak appears at 3.90 ppm, Z is the value obtained by dividing the integral value of this peak by the number of protons, 4. The values of Y+Z/X and Y/Z are determined from X, Y, and Z obtained as described above. Flame retardants used as necessary in the present invention include organic flame retardants such as tris(2-chloroethyl) phosphate, tris(2-chloropropyl) phosphate, chlorinated paraffin, hexabromobenzene, antimony trioxide, and water. There are inorganic flame retardants such as aluminum oxide, and these can be used alone or in combination. Isocyanate compounds in the present invention include tolylene diisocyanate, hexamethylene diisocyanate, isophorone diisocyanate, diphenylmethane-4,4'-diisocyanate, polymethylene polyphenyl isocyanate, mixtures thereof, derivatives of these isocyanates, etc., and purified or crude Any isocyanate compound can be used, and monoisocyanate compounds such as phenyl isocyanate can also be used in combination. In addition, when building a structure using the foaming resin composition of the present invention, a flame-retardant or non-combustible plate or sheet is provided on at least one side of the foam obtained from the resin composition. Or sheets include aluminum kraft paper, metal foil such as aluminum foil, copper foil, aluminum asbestos sheet, wood wool cement board, iron plate, steel plate, stainless steel plate, aluminum plate, metal plate such as copper plate, slate plate, calcium silicate plate. , inorganic noncombustible boards such as gypsum board, cement board, and glass fiber reinforced cement board. These flame-retardant or noncombustible boards or sheets may be painted for reasons such as appearance or corrosion prevention. It is necessary to carefully consider the material or thickness of the paint film used for the paint so as not to reduce its flame retardance, but as long as the paint film is thin, there is no particular restriction on the material, and usually commercially available colors can be used. Even iron plates can be used as sufficiently nonflammable plates. Although there is no particular restriction on the blending ratio of each component in the foamable resin composition of the present invention, (a) an aqueous carbohydrate solution and/or slurry;
50 to 200 parts by weight (b) Reaction catalyst 0.1 to 5 parts by weight (c) Surfactant (excluding silicone foam stabilizers) 0.1 to 5 parts by weight (d) 0.1 to 5 parts by weight of the above silicone foam stabilizers ( e) Isocyanate compound 50-200 parts by weight (f) Flame retardant (selective) Preferably used in a proportion of 0.1-100 parts by weight, (a) Aqueous carbohydrate solution and/or slurry
50 to 150 parts by weight (b) Reaction catalyst 0.5 to 4.0 parts by weight (c) Surfactant (excluding silicone foam stabilizers) 0.5 to 4.0 parts by weight (d) 0.5 to 4.0 parts by weight of the above silicone foam stabilizers ( e) Isocyanate compound 50 to 150 parts by weight (f) Flame retardant (selective) It is more preferably used in a proportion of 5 to 50 parts by weight. In addition, due to workability, for example, a mixture of (a) and (b) and (c),
It is also possible to prepare a mixture of (d), (e) and (f), mix them, react and foam. The reaction temperature is not particularly limited, but is preferably 10 to 50°C, and the rotation speed of the stirrer during mixing is not particularly limited, but is preferably 1000 to 7000 rpm. When molding the foam, there are no particular restrictions, but it is preferable to use a mold. For example, a mold with an open top and bottom is used, and a flame retardant or noncombustible plate or sheet is placed on the bottom surface of the mold. The mold is heated to a temperature of 30°C to 90°C, which is preferable to obtain a uniform foam. Next, the above-mentioned materials are stirred and mixed and poured into the mold, which is then equipped with a flame-retardant or non-combustible plate or sheet, preferably at 30°C to obtain a uniform foam.
The foam and the flame-retardant or noncombustible plate or sheet are bonded by placing an upper mold heated to 90°C with the side of this plate or sheet facing the solution mixture, clamping the mold, and causing foaming. A close-fitting structure can be obtained. Here, the flame-retardant or noncombustible plate or sheet may be provided on either one or both sides of the foam, but it is preferable to provide it on both sides to form a sandwich structure in order to improve flame retardant properties. In this case, the flame-retardant or noncombustible plates or sheets provided on both sides of the foam may be the same or a combination of different types. (Examples) Example 1 An example of the present invention will be described. In the examples, X, Y, and Z represent the number of moles of the above groups. 75 parts by weight of fructose, 25 parts by weight of tap water, amphoteric surfactant (manufactured by NOF Corporation, product name Nitsusan Anon BF)
1.5 parts by weight of triethanolamine was added to 1.0 parts by weight and mixed well to obtain solution A. Diphenylmethane diisocyanate (manufactured by Nippon Polyurethane Co., Ltd., trade name Millionate MR-100)
80 parts by weight, 1.0 parts by weight of silicone foam stabilizer (manufactured by Nippon Unicar Co., Ltd., trade name Foam stabilizer SZ-1623, measured value by NMR spectroscopy: Y+Z/X=1.32, Y/Z=0), tris(2-chloroethyl) ) 20 parts by weight of phosphate was added and mixed to obtain solution B. In order to evaluate fluidity, panel filling properties, etc. were investigated. The ability to fill the corners of the panel (flowability) was evaluated on a five-point scale (higher scores indicate better filling ability), and the evaluation was conducted using the following method. Add 100 parts by weight of solution A and 150 parts by weight of solution B, stir for 5 seconds at 2000 rpm using a stirrer equipped with turbine blades, and keep the mixture at 70°C to make a flat panel making mold (made of iron, internal dimension 350 mm). ×250mm×height
15mm). After 90 seconds, the mold was demolded to obtain a panel (thickness: 15 mm). The panel filling property was given a score of 5. 100 parts by weight of solution A and 150 parts by weight of solution B were stirred for 5 seconds at 2000 rpm using a stirrer equipped with a turbine blade, and the mixture was kept at 25°C and placed in a wooden box with an open top and bottom ( The height of the foam was 350 mm after 120 seconds. 100 parts by weight of Solution A and 150 parts by weight of Solution B were stirred for 5 seconds at 2000 rpm using a stirrer equipped with turbine blades, and the mixture was poured into the wedge shape shown in Figure 1 (mold temperature 70°C) and 90% After seconds, the mold was removed and the flow distance was measured, and the flow distance of this foam was 230 mm. Next, 100 parts by weight of solution A and 100 parts by weight of solution B were added and stirred for 5 seconds at 2000 rpm with a stirrer equipped with turbine blades. 220 mm x 220 mm x height 15 mm), placed an upper mold kept at 40°C on top, and clamped the mold. After 10 minutes, the mold was demolded to obtain a foam (thickness: 15 mm). The density of this foam is 0.024
g/cm 3 , and the water absorption amount at the end was 90 g/m. Reference examples of flame-retardant structures using the foamable resin composition of the present invention are shown below. Reference example 1 Wooden mold with open top and bottom (inner volume 220mm
×220mm×15mm) Colored iron plate (thickness 0.27mm) on the bottom surface
mm) and warm the mold to 40℃. Next, 150 parts by weight of solution B was added to 100 parts by weight of solution A used in Example 1, and the mixture was rotated at 2000 rpm using a stirrer equipped with turbine blades.
Stir for 5 seconds to mix, pour this into the above mold, paste aluminum kraft paper on the top surface, heat the upper mold to 40℃, place the aluminum kraft paper towards the solution mixture, and tighten the mold. did. After 10 minutes, the mold was removed to obtain a flame-retardant structure in which a colored iron plate (0.27 mm thick) was adhered to the surface of the foam (15 mm thick), and aluminum kraft paper was adhered to the back side. The density of the foam, which is the core material of this structure, is 0.024g/cm 3 , and the water absorption amount at each end is 90g/cm 3 .
The foam had a uniform and fine cell structure, and was comparable to conventional foams in terms of water absorption and fluidity. Table 1 shows the results of a nonflammability test conducted on this structure based on Ministry of Construction Notification No. 1231. As is clear from Table 1, this structure has an external appearance after combustion, an afterflame, a smoke generation coefficient,
It was extremely excellent in terms of temperature coefficient and temperature time area. This structure also had excellent adhesion to colored iron plates and aluminum kraft paper. Example 2 75 parts by weight of fructose, 25 parts by weight of tap water, 1.0 parts by weight of the silicone foam stabilizer used in Example 1, nonionic surfactant (manufactured by NOF Corporation, trade name: Nonion NS-
200) 1.5 parts by weight of triethanolamine was added to 1.0 parts by weight and mixed well to obtain solution C. Add 150 parts by weight of solution C to 100 parts by weight of solution A obtained in the example.
Add the weight parts and mix by stirring at 2000 rpm for 5 seconds using a stirrer equipped with a turbine blade.Then, do the same as in Reference Example 1 and place a color iron plate on the surface of the foam (thickness 15 mm) and an aluminum plate on the back side. A structure with kraft paper glued was obtained. In this case, the panel filling property of the foam is 5 points, the foam height is 350 mm, the flow distance is 225 mm, the density of the foam is 0.026 g/cm 3 , the water absorption at the end is 130 g/m, and it has a uniform and fine cell structure. It was foam. In addition, Table 1 shows the results of a semi-flammable test conducted on this structure based on Ministry of Construction Notification No. 1231.
As is clear from Table 1, the amount of water absorbed at the end was larger than that of Reference Example 1, but the same results were obtained in fluidity and flame retardance. Comparative Example 1 1.5 parts by weight of triethanolamine was added to 75 parts by weight of fructose and 25 parts by weight of tap water and mixed well to obtain a solution D. Diphenylmethane diisocyanate (manufactured by Nippon Polyurethane Co., Ltd., trade name Millionate MR-100)
80 parts by weight, 1.0 part by weight of silicone foam stabilizer (manufactured by Toshiba Silicone Co., Ltd., trade name TSF-4450, measured value by NMR spectroscopy: Y+Z/X=9.86, Y/Z=2), and tris(2-chloroethyl) phosphate. 20 parts by weight were added and mixed to obtain solution E. Add 150 parts by weight of solution E to 100 parts by weight of solution D, stir and mix for 5 seconds at 2000 rpm using a stirrer equipped with a turbine blade. A structure was obtained with a colored iron plate attached to the top and aluminum kraft paper glued to the back. In this case, the panel fillability of the foam is 2 points, the foam height is 290 mm, the flow distance is 180 mm, and the foam density is
The foam had a uniform and fine cell structure with a water absorption of 0.035 g/cm 3 and an end water absorption of 100 g/m. In addition, Table 1 shows the results of a semi-flammable test conducted on this structure based on Ministry of Construction Notification No. 1231. As is clear from Table 1, the structure of this comparative example is better than the structure using isocyanurate foam or phenol foam in terms of external shape after combustion, smoke emission coefficient, and exhaust temperature after 5 minutes. Although it has improved, its liquidity has been poor. Comparative example 2 Heteroform 28264 (manufactured by Futsker, trade name)
21.1 parts by weight, 23.5 parts by weight of Heteroform 29696 (manufactured by Futzker, trade name), 1 part by weight of DC-193 (manufactured by Dow Corning, trade name), Polycat 41
To a solution containing 1.42 parts by weight of Freon 11 (manufactured by Sun Abot Co., Ltd., trade name) and 25 parts by weight of Freon 11 (manufactured by Mitsui Fluorochemical Co., Ltd., trade name), 101 parts by weight of Isonate 580 (manufactured by Abbot Co., Ltd., trade name) was added. Stir and mix for 5 seconds at 2000 rpm with the attached stirrer, and use the same procedure as in Reference Example 1 to obtain a structure in which the isocyanurate foam (thickness 15 mm) has a colored iron plate on the surface and aluminum kraft paper on the back. Ta. In this case, the panel filling property of the foam was 4 to 5 points, the foaming height was 290 mm, the wedge-shaped flow distance was 210 mm, the density of the foam was 0.035 g/cm 3 , and the water absorption at the edges was 40 g/m. Also, using this structure, Ministry of Construction Notification No. 1231
Table 1 shows the results of the quasi-nonflammability test based on No. As is clear from Table 1, the water absorption amount of the structure of this comparative example was superior to that of the foam of the reference example, but the change in appearance after combustion was significant and most of the foam was burned out. It was also significantly inferior in terms of smoke generation coefficient and time-temperature area. Comparative example 3 Danphenon 110A (manufactured by Hodogaya Chemical Co., Ltd., trade name)
Add 40 parts of Danphenone 110B curing agent (manufactured by Hodogaya Chemical Co., Ltd., trade name) to a solution of 100 parts by weight and 15 parts by weight of Freon 11 (manufactured by Mitsui Fluorochemical Co., Ltd., trade name).
A solution containing 15 parts by weight of Danphenon 110C foam stabilizer (manufactured by Hodogaya Chemical Co., Ltd., trade name) was added, and the mixture was stirred for 5 seconds at 2000 rpm with a stirrer equipped with turbine blades. Reference Example 1 is shown below. In the same manner as above, a structure was obtained in which a colored iron plate was adhered to the surface of a phenol foam (thickness 15 mm) and aluminum kraft paper was adhered to the back surface.
However, since the phenol foam has significantly poor curing properties, after-curing was performed at 100°C for 30 minutes. In this case, the panel filling property of the foam was 2 points, the foaming height was 230 mm, the wedge-shaped flow distance was 100 mm, the density of the foam was 0.040 g/cm 3 , and the water absorption at the edges was 210 g/m. Since flyability occurred on the surface of the phenol foam, the adhesion between the foam and the aluminum kraft paper and the colored iron plate was poor. Table 1 shows the results of semi-flammability tests conducted on this structure based on Ministry of Construction Notification No. 1231. As is clear from Table 1, the structure of this comparative example had a good appearance after combustion, but the afterflame was long and inferior.

【衚】 発明の効果 本発明になる発泡甚暹脂組成物は、埗られる発
泡䜓の難燃特性に優れ、か぀発泡時の液の流動性
の優れた発泡甚暹脂組成物である。
[Table] (Effects of the Invention) The foaming resin composition of the present invention is a foaming resin composition that provides excellent flame retardant properties of the resulting foam and excellent fluidity of the liquid during foaming.

【図面の簡単な説明】[Brief explanation of drawings]

第図は実斜䟋および比范䟋においおくさび型
流れ距離の枬定に甚いた型の略図である。
FIG. 1 is a schematic diagram of the mold used for measuring the wedge-shaped flow distance in Examples and Comparative Examples.

Claims (1)

【特蚱請求の範囲】  炭氎化物の氎溶液及び又はスラリヌ、反応
觊媒、む゜シアネヌト化合物、けい玠に結合した
メチル基【匏】単䜍及び― CH2CH2O―単䜍を有し、けい玠に結合したメチ
ル基のモル数を、【匏】単䜍のモ ル数を及び―CH2CH2O―単䜍のモル数をず
したずき、0.5〜11および〜1.8 であるシリコヌン敎泡剀、界面掻性剀ただしシ
リコヌン敎泡剀を陀くおよび必芁に応じお難燃
剀を含有しおなる発泡甚暹脂組成物。  界面掻性剀がノニオン系界面掻性剀である特
蚱請求の範囲第項蚘茉の発泡甚暹脂組成物。  界面掻性剀がアニオン系界面掻性剀である特
蚱請求の範囲第項蚘茉の発泡甚暹脂組成物。  界面掻性剀がカチオン系界面掻性剀である特
蚱請求の範囲第項蚘茉の発泡甚暹脂組成物。  界面掻性剀が䞡性界面掻性剀である特蚱請求
の範囲第項蚘茉の発泡甚暹脂組成物。  シリコヌン敎泡剀を0.5〜11および 〜1.0であるシリコヌン敎泡剀ずした特蚱 請求の範囲第項蚘茉の発泡甚暹脂組成物。
[Scope of Claims] 1. An aqueous solution and/or slurry of carbohydrates, a reaction catalyst, an isocyanate compound, a methyl group bonded to silicon, having [formula] units and (- CH 2 CH 2 O)- units, When the number of moles of the bonded methyl group is X, the number of moles of the [Formula] unit is Y, and the number of moles of the (-CH 2 CH 2 O)- unit is Z, Y + Z / X = 0.5 to 11 and Y / Z = 0 to 1.8, a surfactant (excluding the silicone foam stabilizer), and optionally a flame retardant. 2. The foaming resin composition according to claim 1, wherein the surfactant is a nonionic surfactant. 3. The foaming resin composition according to claim 1, wherein the surfactant is an anionic surfactant. 4. The foaming resin composition according to claim 1, wherein the surfactant is a cationic surfactant. 5. The foaming resin composition according to claim 1, wherein the surfactant is an amphoteric surfactant. 6. The foaming resin composition according to claim 1, wherein the silicone foam stabilizer is a silicone foam stabilizer in which Y+Z/X=0.5-11 and Y/Z=0-1.0.
JP61162687A 1986-07-10 1986-07-10 Resin composition for expansion Granted JPS6317920A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61162687A JPS6317920A (en) 1986-07-10 1986-07-10 Resin composition for expansion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61162687A JPS6317920A (en) 1986-07-10 1986-07-10 Resin composition for expansion

Publications (2)

Publication Number Publication Date
JPS6317920A JPS6317920A (en) 1988-01-25
JPH0482006B2 true JPH0482006B2 (en) 1992-12-25

Family

ID=15759390

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61162687A Granted JPS6317920A (en) 1986-07-10 1986-07-10 Resin composition for expansion

Country Status (1)

Country Link
JP (1) JPS6317920A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6320314A (en) * 1986-07-11 1988-01-28 Hitachi Chem Co Ltd Expandable resin composition

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5374596A (en) * 1976-12-14 1978-07-03 Toyo Rubber Chem Ind Co Ltd Manufacture of rigid polyurethane foam
US4230822A (en) * 1978-10-10 1980-10-28 W. R. Grace & Co. Flame-retardant polyurethane foams
US4400475A (en) * 1981-12-08 1983-08-23 Patrick James Crehan Polyurethane foams and processes for preparation
US4520139A (en) * 1984-07-26 1985-05-28 Patrick James Crehan Pectin and related carbohydrates for the preparation of polyurethane foams

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Publication number Publication date
JPS6317920A (en) 1988-01-25

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