JPS6217616B2 - - Google Patents
Info
- Publication number
- JPS6217616B2 JPS6217616B2 JP8588580A JP8588580A JPS6217616B2 JP S6217616 B2 JPS6217616 B2 JP S6217616B2 JP 8588580 A JP8588580 A JP 8588580A JP 8588580 A JP8588580 A JP 8588580A JP S6217616 B2 JPS6217616 B2 JP S6217616B2
- Authority
- JP
- Japan
- Prior art keywords
- beads
- propane
- weight
- dibromophenyl
- bis
- 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
Links
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 52
- 239000003063 flame retardant Substances 0.000 claims description 30
- 239000012508 resin bead Substances 0.000 claims description 27
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims description 24
- 239000012188 paraffin wax Substances 0.000 claims description 18
- 239000007788 liquid Substances 0.000 claims description 17
- 229920001890 Novodur Polymers 0.000 claims description 16
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 16
- PWXTUWQHMIFLKL-UHFFFAOYSA-N 1,3-dibromo-5-[2-(3,5-dibromo-4-prop-2-enoxyphenyl)propan-2-yl]-2-prop-2-enoxybenzene Chemical compound C=1C(Br)=C(OCC=C)C(Br)=CC=1C(C)(C)C1=CC(Br)=C(OCC=C)C(Br)=C1 PWXTUWQHMIFLKL-UHFFFAOYSA-N 0.000 claims description 15
- 150000003014 phosphoric acid esters Chemical class 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 9
- 239000001294 propane Substances 0.000 claims description 8
- 239000004088 foaming agent Substances 0.000 claims description 6
- 239000011324 bead Substances 0.000 description 27
- 238000000034 method Methods 0.000 description 26
- 229920005989 resin Polymers 0.000 description 14
- 239000011347 resin Substances 0.000 description 14
- 238000005187 foaming Methods 0.000 description 11
- 239000004604 Blowing Agent Substances 0.000 description 10
- 239000006260 foam Substances 0.000 description 10
- 238000005470 impregnation Methods 0.000 description 8
- 229910019142 PO4 Inorganic materials 0.000 description 6
- YSMRWXYRXBRSND-UHFFFAOYSA-N TOTP Chemical compound CC1=CC=CC=C1OP(=O)(OC=1C(=CC=CC=1)C)OC1=CC=CC=C1C YSMRWXYRXBRSND-UHFFFAOYSA-N 0.000 description 6
- 239000010452 phosphate Substances 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 5
- 239000000178 monomer Substances 0.000 description 5
- 238000006116 polymerization reaction Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 4
- -1 phosphate ester Chemical class 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- 239000004793 Polystyrene Substances 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 229920002223 polystyrene Polymers 0.000 description 3
- GPTLIJNIIGNCIG-UHFFFAOYSA-N 1,2-dibromo-3-propylbenzene Chemical compound CCCC1=CC=CC(Br)=C1Br GPTLIJNIIGNCIG-UHFFFAOYSA-N 0.000 description 2
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 2
- 239000001273 butane Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- AUTSLLHNWAZVLE-UHFFFAOYSA-N 1,1,2,2,3-pentabromo-3-chlorocyclohexane Chemical compound ClC1(Br)CCCC(Br)(Br)C1(Br)Br AUTSLLHNWAZVLE-UHFFFAOYSA-N 0.000 description 1
- XQKQZOLAVMIQHZ-UHFFFAOYSA-N 1,1-dibromo-3-(3,3-dibromopropoxy)propane Chemical compound BrC(Br)CCOCCC(Br)Br XQKQZOLAVMIQHZ-UHFFFAOYSA-N 0.000 description 1
- PHOBHMJNDXZVSI-UHFFFAOYSA-N 1,2,3,4-tetrabromo-2-chlorobutane Chemical compound BrCC(Br)(Cl)C(Br)CBr PHOBHMJNDXZVSI-UHFFFAOYSA-N 0.000 description 1
- YEVQZPWSVWZAOB-UHFFFAOYSA-N 2-(bromomethyl)-1-iodo-4-(trifluoromethyl)benzene Chemical compound FC(F)(F)C1=CC=C(I)C(CBr)=C1 YEVQZPWSVWZAOB-UHFFFAOYSA-N 0.000 description 1
- VEORPZCZECFIRK-UHFFFAOYSA-N 3,3',5,5'-tetrabromobisphenol A Chemical compound C=1C(Br)=C(O)C(Br)=CC=1C(C)(C)C1=CC(Br)=C(O)C(Br)=C1 VEORPZCZECFIRK-UHFFFAOYSA-N 0.000 description 1
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N 4-Methylstyrene Chemical compound CC1=CC=C(C=C)C=C1 JLBJTVDPSNHSKJ-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- OSDWBNJEKMUWAV-UHFFFAOYSA-N Allyl chloride Chemical compound ClCC=C OSDWBNJEKMUWAV-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- 239000004338 Dichlorodifluoromethane Substances 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- YYQRGCZGSFRBAM-UHFFFAOYSA-N Triclofos Chemical compound OP(O)(=O)OCC(Cl)(Cl)Cl YYQRGCZGSFRBAM-UHFFFAOYSA-N 0.000 description 1
- PQYJRMFWJJONBO-UHFFFAOYSA-N Tris(2,3-dibromopropyl) phosphate Chemical compound BrCC(Br)COP(=O)(OCC(Br)CBr)OCC(Br)CBr PQYJRMFWJJONBO-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- DDTBPAQBQHZRDW-UHFFFAOYSA-N cyclododecane Chemical compound C1CCCCCCCCCCC1 DDTBPAQBQHZRDW-UHFFFAOYSA-N 0.000 description 1
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 1
- 235000019404 dichlorodifluoromethane Nutrition 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 229920006248 expandable polystyrene Polymers 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000010097 foam moulding Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- YAFOVCNAQTZDQB-UHFFFAOYSA-N octyl diphenyl phosphate Chemical compound C=1C=CC=CC=1OP(=O)(OCCCCCCCC)OC1=CC=CC=C1 YAFOVCNAQTZDQB-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920006327 polystyrene foam Polymers 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000010558 suspension polymerization method Methods 0.000 description 1
- 238000010557 suspension polymerization reaction Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- STCOOQWBFONSKY-UHFFFAOYSA-N tributyl phosphate Chemical compound CCCCOP(=O)(OCCCC)OCCCC STCOOQWBFONSKY-UHFFFAOYSA-N 0.000 description 1
- 229960001147 triclofos Drugs 0.000 description 1
- DQWPFSLDHJDLRL-UHFFFAOYSA-N triethyl phosphate Chemical compound CCOP(=O)(OCC)OCC DQWPFSLDHJDLRL-UHFFFAOYSA-N 0.000 description 1
- XZZNDPSIHUTMOC-UHFFFAOYSA-N triphenyl phosphate Chemical compound C=1C=CC=CC=1OP(OC=1C=CC=CC=1)(=O)OC1=CC=CC=C1 XZZNDPSIHUTMOC-UHFFFAOYSA-N 0.000 description 1
- WTLBZVNBAKMVDP-UHFFFAOYSA-N tris(2-butoxyethyl) phosphate Chemical compound CCCCOCCOP(=O)(OCCOCCCC)OCCOCCCC WTLBZVNBAKMVDP-UHFFFAOYSA-N 0.000 description 1
- XHTMGDWCCPGGET-UHFFFAOYSA-N tris(3,3-dichloropropyl) phosphate Chemical compound ClC(Cl)CCOP(=O)(OCCC(Cl)Cl)OCCC(Cl)Cl XHTMGDWCCPGGET-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Description
本発明は難燃性の発泡性スチレン系樹脂ビーズ
組成物に関する。更に詳しくは本発明はスチレン
系樹脂ビーズに発泡剤を含有させ、更に2,2―
ビス(4―アリロキシ―3,5―ジブロモフエニ
ル)プロパンと常温で液体のリン酸エステル又は
常温で液体のハロゲン化パラフインとを付着含浸
させてなる難燃性の発泡性スチレン系ビーズ組成
物に関する。
スチレン系樹脂は装飾品、建材、日用品、構築
物、構造物等多岐にわたる分野、用途に用いられ
ている。特に、近年省エネルギーという観点から
工業用、建築用断熱材として発泡スチレン系樹脂
が大量に使用されるようになつてきている。
この発泡スチレン系樹脂は、通常押出発泡法と
ビーズ発泡法との2つの大別される方法で製造さ
れている。押出発泡法はスチレン系樹脂と発泡剤
を押出機中で混合したのち押出成形することによ
つて発泡成形品を製造する方法であり、またビー
ズ発泡法は先ずスチレン系樹脂ビーズに発泡剤を
含浸させて発泡性ビーズを製造し、次いでこの発
泡性ビーズを金型等の型内で加熱発泡させて発泡
成形品を製造する方法である。
しかるに、スチレン系樹脂は可燃性であり、着
火、燃焼すればその危険は想像を絶するものがあ
る。このため断熱材等に使用される発泡スチレン
系樹脂の難燃化が望まれ、すでに数多くの提案が
なされ、そのうちのいくつかは実際に工業化され
ている。
例えば押出発泡法による発泡スチレン系樹脂の
難燃化には、難燃剤として2,2―ビス(4―ア
リロキシ―3,5―ジブロモフエニル)プロパン
(特開昭53−125457号公報)ヘキサブロモシクロ
ドデカン(特公昭43−29658号公報)、ペンタブロ
モモノクロロシクロヘキサン(特公昭36−6683号
公報)等が知られている。これらのうち特に2,
2―ビス(4―アリロキシ―3,5―ジブロモフ
エニル)プロパンはスチレン系樹脂に対して特異
な難燃効果を示すため、他の難燃剤に比してその
使用量が少なくてすみ、また樹脂の物性低下が小
さいという利点を有している。
この押出発泡法における難燃化においては、押
出機中で難燃剤と溶融樹脂とを混練することから
該難燃剤の量は任意に使用でき、混合手法特有の
理由に基づく量の制限は特にない。もつともこの
方法において樹脂物性の低下等の理由による難燃
剤の使用量の制約はある。
一方、ビーズ発泡法による発泡スチレン系樹脂
の難燃化には、難燃剤として2―クロロ―1,
2,3,4―テトラブロモブタン(特公昭42−
23091号公報)、ビス(ジクロロプロピル)ジクロ
ロプロピルフオスフエート(特公昭44−16213号
公報)、トリブロムフエニルジブロムプロピルエ
ーテル(特公昭48−32575号公報)トリス(2,
3―ジブロムプロピル)ホスフエート(特公昭33
−6788号公報)等が提案されている。この方法に
おけるビーズの難燃化は、一般にスチレン系モノ
マーからビーズ状重合体に重合する過程で難燃剤
及び発泡剤を添加する重合法、或いは懸濁重合で
製造されたビーズに難燃剤及び発泡剤を含浸させ
る含浸法が用いられている。しかし、これらの方
法は通常100℃以下の温度で行なわれるので、難
燃剤は融点が100℃以下のものに制限を受けてい
る。因みに融点が115〜120℃の2,2―ビス(4
―アリロキシ―3,5―ジブロモフエニル)プロ
パンはスチレン系樹脂に対してすぐれた難燃作用
を奏するか、これを含浸法によつて、スチレン系
樹脂ビーズに付着含浸させようとしても所定量を
付着含浸させることが難しく、所望の難燃性ビー
ズを得ることが難しい。この点を改良する方法と
して処理温度を難燃剤の融点付近まで高くするこ
とが考えられるが、この方法は設備上、経済的に
不利となり、また安定した均一ビーズが得難いと
いう欠陥がある。
また、上記提案の難燃剤はスチレン系樹脂に対
して比較的多量に添加する必要があつたり、耐候
性、耐熱性等の劣るものであつたり、或いは毒性
の強いものであつたりして、真に満足して実用化
し得るものでない。
本発明者は、かかる点に着目し、2,2―ビス
(4―アリロキシ―3,5―ジブロモフエニル)
プロパンを用いてスチレン系樹脂ビーズを難燃化
することについて鋭意検討した結果、2,2―ビ
ス(4―アリロキシ―3,5―ジブロモフエニ
ル)プロパンを特定のリン酸エステル又はハロゲ
ン化パラフインと共に用いると、目的とする難燃
性の発泡性ポリスチレン系樹脂ビーズが得られる
ことを知見し、本発明に到達したものである。
すなわち、本発明はスチレン系樹脂ビーズに(i)
発泡性付与量の発泡剤、(ii)難燃性付与量の2,2
ビス(4―アリロキシ―3,5―ジブロモフエニ
ル)プロパン、及び(iii)該スチレン系樹脂ビーズ
100重量部当り0.05〜2重量部の常温で液体のリ
ン酸エステル及び/又は常温で液体のハロゲン化
パラフインを含有せしめてなる難燃性の発泡性ス
チレン系樹脂ビーズ組成物に関する。
本発明において用いられるスチレン系樹脂ビー
ズとはスチレン重合体、及びスチレンと他の付加
重合性モノマー例えばメチルスチレン、アクリロ
ニトリル、メチルメタクリレート、メチルアクリ
レート、等との共重合体のビーズである。かかる
ビーズは、例えば市販されているスチレン系樹脂
ビーズから容易に入手することができる。
また、本発明においてスチレン系樹脂ビーズに
含有せしめる発泡剤としては例えばプロパン、ブ
タン、ペンタン、シクロヘキサン、ジクロロジフ
ルオロメタン等を挙げることができる。これらの
他にもスチレン系樹脂ビーズの発泡剤として知ら
れているものを用いることはできる。またこれら
は1種以上を用いることができる。
かかる発泡剤を含有せしめる方法としては、ス
チレン系樹脂の重合時に添する方法例えば重合前
のモノマ、重合途中の反応系に添加する等や、ス
チレン系樹脂ビーズの製造後に含浸させる方法等
を用いることができる。これらの方法は発泡性ビ
ーズの製造法として良く知られた方法である。
更に本発明において難燃剤の2,2―ビス(4
―アリロキシ―3,5―ジブロモフエニル)プロ
パンは通常市販されているものを用いることがで
きる。この2,2―ビス―(4―アリロキシ―
3,5―ジブロモフエニル)プロパンは通常テト
ラブロモビスフエノールAと2倍モルないしこれ
より若干過剰量のアリルクロライドとを反応せし
めることによつて得られる。
更にまた、本発明において難燃剤と共に用いら
れる室温で液体のリン酸エステルとしては、例え
ばリン酸トリクレジル、リン酸トリスイソプロピ
ルフエニル、リン酸トリブチル、リン酸トリエチ
ル、リン酸トリオクチル、リン酸トリクロロエチ
ル、リン酸トリスジクロロプロピル、リン酸トリ
ブトキシエチル、リン酸トリス―β―クロロプロ
ピル、リン酸オクチルジフエニル等を挙げること
ができる。これらは1種以上を用いることができ
る。
また、難燃剤と共に用いられる室温で液体のハ
ロゲン化パラフインとしては塩素化パラフイン例
えば塩素含有率40,45,50,65%の塩素化パラフ
イン等が好ましく挙げられる。これらは1種以上
を用いることができる。
常温で液体でないリン酸エステル(例えばリン
酸トリフエニル)或いは常温で液体でないハロゲ
ン化パラフイン(例えば塩素含有率70%以上の塩
素化パラフイン)は、スチレン系樹脂ビーズに所
望量の2,2―ビス(4―アリロキシ―3,5―
ジブロモフエニル)プロパンを含有せしめる作用
が小さく、有用でない。
本発明の発泡性スチレン系樹脂ビーズ組成物
は、スチレン系樹脂ビーズに発泡剤、2,2―ビ
ス(4―アリロキシ―3,5―ジブロモフエニ
ル)プロパン、及び室温で液体のリン酸エステル
及び/又はハロゲン化パラフインを含有せしめる
ことによつて得られるが、発泡剤の量はビーズに
発泡性を付与する量であり通常スチレン系樹脂ビ
ーズ100重量部当り3〜15重量部、好ましくは5
〜7重量部であり、また2,2―ビス(4―アリ
ロキシ―3,5―ジブロモフエニル)プロパンの
量はビーズに難燃性を付与する量であり、通常ス
チレン系樹脂ビーズ100重量部当り0.5〜5重量
部、好ましくは0.8〜2重量部である。2,2ビ
ス(4―アリロキシ―3,5―ジブロモフエニ
ル)プロパンの量が5重量部を超えると発泡スチ
レン系樹脂の物性低下が大きくなる。また室温で
液体のリン酸エステル及び(又は)ハロゲン化パ
ラフイン量はスチレン系樹脂ビーズ100重量部当
り0.05〜2重量部である。0.05重量部より少ない
量では2,2―ビス(4―アリロキシ―3,5―
ジブロモフエニル)プロパンの付着含浸量を増大
させる効果が少なく、また2重量部より多い量で
はスチレン系樹脂発泡体の物性低下が大きく、好
ましくない。
2,2―ビス(4―アリロキシ―3,5―ジブ
ロモフエニル)プロパンと室温で液体のリン酸エ
ステル及び(又は)ハロゲン化パラフインとの重
量比は20:1乃至2:1程度が好ましく、10:1
乃至10:3程度が特に好ましい。室温で液体のリ
ン酸エステル及び(又は)ハロゲン化パラフイン
を併用することによつて、用いた2,2―ビス
(4―アリロキシ―3,5―ジブロモフエニル)
プロパンのほゞ全量をビーズに付着含浸せしめる
ことができる。2,2―ビス(4―アリロキシ―
3,5―ジブロモフエニル)プロパンと室温で液
体のリン酸エステル及び(又は)ハロゲン化パラ
フインは使用にあたつて両者を予め混合してから
用いても良く、また別々に添加使用しても良い。
本発明の難燃性の発泡性スチレン系樹脂ビーズ
組成物は、通常オートクレーブに、水分散系でス
チレン系樹脂ビーズ、2,2―ビス(4―アリロ
キシ―3,5―ジブロモフエニル)プロパン及び
室温で液体のリン酸エステル及び/又はハロゲン
化パラフイン特に塩素化パラフインを仕込み発泡
剤を圧力して約100℃で含浸処理する方法、或い
はオートクレーブに水懸濁液、触媒(過酸化物)
スチレン系モノマー、2,2―ビス(4―アリロ
キシ―3,5―ジブロモフエニル)プロパン、及
び室温で液体のリン酸エステル及び/又はハロゲ
ン化パラフイン特に塩素化パラフインを、更に必
要に応じて助剤を仕込み、加熱してスチレン系モ
ノマーの重合反応を行ない、重合反応用始後発泡
剤を圧入する懸濁重合法によつて製造することが
できる。とりわけ前者の含浸法が好ましい。
本発明の難燃性の発泡性スチレン系樹脂ビーズ
組成物には更に必要に応じて金属酸化物、酸化防
止剤、充填剤、染剤、安定剤等の他の添加剤をも
含有させることができる。
更に本発明を実施例を掲げて説明する。尚実施
例中の酸素脂数はASTMD―2863の方法による測
定結果である。
実施例 1
容量10のオートクレーブに水3Kg、ポリスチ
レンビーズ1Kg、2,2―ビス(4―アリロキシ
―3,5―ジブロモフエニル)プロパン12g及び
リン酸トリクレジル1.4gを仕込み、100℃に加熱
後、約10Kg/cm3になる迄ブタンガスを圧入した。
約6時間撹拌後、冷却圧抜して発泡性ビーズを取
出し、水洗後常温で乾燥した。
得られた発泡性ビーズの1/10重量部を80℃で5
時間減圧乾燥して、発泡剤及び水分を除去した重
量は101.30gであり、この値を全量に換算すると
1013.0gとなり、添加した2,2―ビス(4―ア
リロキシ―3,5―ジブロモフエニル)プロパン
とリン酸トリクレジルの合計量13.4gの97%がポ
リスチレンビーズに付着含浸していた。
得られた発泡性ビーズを通常の方法で発泡成形
して、密度が0.033g/cm3のポリスチレン発泡体
を得た。この発泡体から200×25×10mmの試験片
を切り出し、JIS―A―9551による燃焼試験を行
つた結果、燃焼時間が1.2秒で判定は合格であつ
た。
比較例 1
リン酸トリクレジルを添加しない以外は、実施
例1と同様に実施した結果、得られた発泡性ビー
ズの1/10重量部の乾燥後の重量は100.54gであ
り、この値を全量に換算すると1005.4gとなり、
ポリスチレンビーズへの付着含浸率は45%であつ
た。
実施例1と同様1に発泡成形して密度が0.030
g/cm3の発泡体を得た。この発泡体は燃焼時間が
3.7秒で判定は不合格であつた。
この結果から、リン酸トリクレジルが難燃剤の
付着含浸量を著しく増大させていることがわか
る。
実施例 2〜8
実施例1と同じ装置、方法によつて、表―1に
示すようにリン酸トリクレジルの添加量を変え
て、或いは他のリン酸エステル若しくは塩素化パ
ラフイン(塩素含有率:40%)を用いて発泡性ビ
ーズを製造した。この発泡性ビーズを用いて実施
例1と同様にして発泡体を得た。発泡性ビーズへ
の付着含浸量及びその割合、更に発泡体の難燃性
(燃焼時間)を表―1に示す。
The present invention relates to flame retardant expandable styrenic resin bead compositions. More specifically, in the present invention, styrene resin beads contain a blowing agent, and 2,2-
A flame-retardant expandable styrenic bead composition formed by adhering and impregnating bis(4-allyloxy-3,5-dibromophenyl)propane with a phosphoric acid ester that is liquid at room temperature or a halogenated paraffin that is liquid at room temperature. . Styrenic resins are used in a wide variety of fields and applications, such as ornaments, building materials, daily necessities, buildings, and structures. In particular, in recent years, expanded styrene resins have come to be used in large quantities as industrial and architectural insulation materials from the viewpoint of energy conservation. This foamed styrene resin is generally manufactured by two methods: extrusion foaming method and bead foaming method. The extrusion foaming method is a method of manufacturing foam molded products by mixing styrene resin and a foaming agent in an extruder and then extrusion molding, while the bead foaming method first involves impregnating styrene resin beads with a foaming agent. This is a method of producing foamed beads by heating and foaming the foamed beads in a mold such as a metal mold. However, styrene resin is flammable, and if it ignites or burns, the danger is unimaginable. For this reason, it is desired to make foamed styrene resins used for insulation materials etc. flame retardant, and many proposals have already been made, some of which have actually been commercialized. For example, to make styrene foam resin flame retardant by the extrusion foaming method, 2,2-bis(4-allyloxy-3,5-dibromophenyl)propane (JP-A-53-125457) and hexabromo are used as flame retardants. Cyclododecane (Japanese Patent Publication No. 43-29658), pentabromomonochlorocyclohexane (Japanese Patent Publication No. 36-6683), and the like are known. Among these, especially 2,
2-Bis(4-allyloxy-3,5-dibromophenyl)propane exhibits a unique flame retardant effect on styrene resins, so it can be used in smaller amounts than other flame retardants. It has the advantage that there is little deterioration in the physical properties of the resin. In flame retardation using this extrusion foaming method, the flame retardant and molten resin are kneaded in an extruder, so any amount of flame retardant can be used, and there is no particular restriction on the amount based on reasons specific to the mixing method. . However, in this method, there are restrictions on the amount of flame retardant used due to reasons such as deterioration of resin properties. On the other hand, when making styrene foam resin flame retardant using the bead foaming method, 2-chloro-1,
2,3,4-tetrabromobutane (Special Publication 1977-
23091), bis(dichloropropyl) dichloropropyl phosphate (Japanese Patent Publication No. 44-16213), tribromphenyl dibromopropyl ether (Japanese Patent Publication No. 48-32575), tris(2,
3-dibromopropyl) phosphate (Special Publication No. 33
-6788 Publication) etc. have been proposed. Flame retardant beads in this method are generally made by adding flame retardants and blowing agents during the process of polymerizing styrenic monomers into bead-shaped polymers, or by adding flame retardants and blowing agents to beads produced by suspension polymerization. An impregnation method is used. However, since these methods are usually carried out at temperatures below 100°C, flame retardants are limited to those with a melting point of 100°C or below. By the way, 2,2-bis(4
-Aryloxy-3,5-dibromophenyl)propane has an excellent flame retardant effect on styrene resins, and even if it is attempted to adhere to and impregnate styrene resin beads by the impregnation method, it will not work if a specified amount is applied. It is difficult to adhere and impregnate, making it difficult to obtain the desired flame retardant beads. One possible method to improve this point is to raise the treatment temperature to around the melting point of the flame retardant, but this method has disadvantages in terms of equipment and economy, and also has the disadvantage that it is difficult to obtain stable and uniform beads. In addition, the flame retardants proposed above need to be added in relatively large amounts to styrene resins, have poor weather resistance and heat resistance, or are highly toxic. It cannot be put into practical use with satisfactory results. The present inventor paid attention to this point, and made 2,2-bis(4-allyloxy-3,5-dibromophenyl)
As a result of intensive studies on making styrene resin beads flame retardant using propane, we found that 2,2-bis(4-allyloxy-3,5-dibromophenyl)propane was used together with a specific phosphate ester or halogenated paraffin. The present invention was achieved based on the finding that the desired flame-retardant expandable polystyrene resin beads can be obtained by using the method. That is, the present invention provides styrene resin beads with (i)
Foaming agent in the amount imparting foaming properties, (ii) 2,2 in the amount imparting flame retardancy
bis(4-allyloxy-3,5-dibromophenyl)propane, and (iii) the styrenic resin beads
The present invention relates to a flame-retardant expandable styrenic resin bead composition containing 0.05 to 2 parts by weight per 100 parts by weight of a phosphoric acid ester that is liquid at room temperature and/or a halogenated paraffin that is liquid at room temperature. The styrenic resin beads used in the present invention are beads of styrene polymers and copolymers of styrene and other addition polymerizable monomers such as methylstyrene, acrylonitrile, methyl methacrylate, methyl acrylate, and the like. Such beads can be easily obtained, for example, from commercially available styrene resin beads. Further, examples of the blowing agent to be included in the styrene resin beads in the present invention include propane, butane, pentane, cyclohexane, dichlorodifluoromethane, and the like. In addition to these, agents known as foaming agents for styrene resin beads can also be used. Moreover, one or more types of these can be used. Such a blowing agent can be incorporated by adding it during polymerization of styrenic resin, for example by adding it to the monomer before polymerization or to the reaction system during polymerization, or by impregnating it after producing styrenic resin beads. I can do it. These methods are well known methods for producing expandable beads. Furthermore, in the present invention, the flame retardant 2,2-bis(4
-Allyloxy-3,5-dibromophenyl)propane that is normally commercially available can be used. This 2,2-bis-(4-allyloxy-
3,5-dibromophenyl)propane is usually obtained by reacting tetrabromobisphenol A with allyl chloride in an amount ranging from 2 times the mole to a slightly excess amount. Furthermore, the phosphoric acid esters that are liquid at room temperature and are used together with the flame retardant in the present invention include, for example, tricresyl phosphate, trisisopropylphenyl phosphate, tributyl phosphate, triethyl phosphate, trioctyl phosphate, trichloroethyl phosphate, Examples include trisdichloropropyl phosphate, tributoxyethyl phosphate, tris-β-chloropropyl phosphate, and octyldiphenyl phosphate. One or more types of these can be used. Further, as the halogenated paraffin which is liquid at room temperature and is used together with the flame retardant, chlorinated paraffin such as chlorinated paraffin having a chlorine content of 40, 45, 50 or 65% is preferably mentioned. One or more types of these can be used. Phosphate esters that are not liquid at room temperature (e.g., triphenyl phosphate) or halogenated paraffins that are not liquid at room temperature (e.g., chlorinated paraffins with a chlorine content of 70% or more) are added to styrene resin beads in a desired amount of 2,2-bis( 4-Allyloxy-3,5-
The effect of containing (dibromophenyl)propane is small and is not useful. The expandable styrenic resin bead composition of the present invention includes styrenic resin beads, a blowing agent, 2,2-bis(4-allyloxy-3,5-dibromophenyl)propane, and a phosphate ester that is liquid at room temperature. It can be obtained by containing/or halogenated paraffin, but the amount of blowing agent is the amount that imparts foaming properties to the beads, and is usually 3 to 15 parts by weight, preferably 5 parts by weight, per 100 parts by weight of styrene resin beads.
~7 parts by weight, and the amount of 2,2-bis(4-allyloxy-3,5-dibromophenyl)propane is an amount that imparts flame retardancy to the beads, usually 100 parts by weight of styrene resin beads. 0.5 to 5 parts by weight, preferably 0.8 to 2 parts by weight. If the amount of 2,2bis(4-allyloxy-3,5-dibromophenyl)propane exceeds 5 parts by weight, the physical properties of the expanded styrene resin will greatly deteriorate. The amount of phosphoric acid ester and/or halogenated paraffin that is liquid at room temperature is 0.05 to 2 parts by weight per 100 parts by weight of styrene resin beads. In amounts less than 0.05 parts by weight, 2,2-bis(4-allyloxy-3,5-
The effect of increasing the amount of adhesion and impregnation of (dibromophenyl)propane is small, and if the amount is more than 2 parts by weight, the physical properties of the styrenic resin foam will be greatly deteriorated, which is not preferable. The weight ratio of 2,2-bis(4-allyloxy-3,5-dibromophenyl)propane to the phosphoric acid ester and/or halogenated paraffin that is liquid at room temperature is preferably about 20:1 to 2:1, 10:1
A ratio of about 10:3 to 10:3 is particularly preferred. 2,2-bis(4-allyloxy-3,5-dibromophenyl) was used in combination with a phosphoric acid ester and/or a halogenated paraffin, which is liquid at room temperature.
Almost the entire amount of propane can be attached and impregnated onto the beads. 2,2-bis(4-allyloxy-
3,5-Dibromophenyl)propane and the phosphoric acid ester and/or halogenated paraffin that are liquid at room temperature may be used after mixing them in advance, or they may be used by adding them separately. good. The flame-retardant expandable styrenic resin bead composition of the present invention is usually prepared in an autoclave in an aqueous dispersion system including styrenic resin beads, 2,2-bis(4-allyloxy-3,5-dibromophenyl)propane and A method in which phosphoric acid ester and/or halogenated paraffin, especially chlorinated paraffin, which is liquid at room temperature is charged and impregnated at about 100°C with a blowing agent under pressure, or a water suspension and catalyst (peroxide) in an autoclave.
A styrenic monomer, 2,2-bis(4-allyloxy-3,5-dibromophenyl)propane, and a phosphoric acid ester liquid at room temperature and/or a halogenated paraffin, especially a chlorinated paraffin, are further added if necessary. It can be produced by a suspension polymerization method in which a blowing agent is charged and heated to carry out a polymerization reaction of a styrenic monomer, and a blowing agent is press-injected before and after the polymerization reaction. The former impregnation method is particularly preferred. The flame-retardant expandable styrenic resin bead composition of the present invention may further contain other additives such as metal oxides, antioxidants, fillers, dyes, and stabilizers, if necessary. can. Further, the present invention will be explained with reference to examples. The oxygen fat numbers in the examples are the results of measurements according to the method of ASTMD-2863. Example 1 In an autoclave with a capacity of 10, 3 kg of water, 1 kg of polystyrene beads, 12 g of 2,2-bis(4-allyloxy-3,5-dibromophenyl)propane, and 1.4 g of tricresyl phosphate were charged, and after heating to 100°C, Butane gas was pressurized until the pressure reached approximately 10 kg/cm 3 .
After stirring for about 6 hours, the foaming beads were removed by cooling and pressure release, washed with water, and then dried at room temperature. 1/10 part by weight of the obtained expandable beads was heated at 80℃ for 5 minutes.
After drying under reduced pressure for hours and removing the foaming agent and moisture, the weight is 101.30g, and this value is converted to the total amount.
The total amount was 1013.0 g, and 97% of the total amount of 13.4 g of 2,2-bis(4-allyloxy-3,5-dibromophenyl)propane and tricresyl phosphate added was attached to and impregnated with the polystyrene beads. The obtained expandable beads were foam-molded in a conventional manner to obtain a polystyrene foam having a density of 0.033 g/cm 3 . A test piece of 200 x 25 x 10 mm was cut from this foam and subjected to a combustion test according to JIS-A-9551. As a result, the combustion time was 1.2 seconds and the test piece passed the test. Comparative Example 1 The same procedure as in Example 1 was carried out except that tricresyl phosphate was not added. As a result, the weight of 1/10 part by weight of the obtained expandable beads after drying was 100.54 g, and this value was added to the total amount. When converted, it becomes 1005.4g,
The adhesion and impregnation rate on polystyrene beads was 45%. Similar to Example 1, foam molding was performed to obtain a density of 0.030.
A foam of g/cm 3 was obtained. This foam has a burn time of
The judgment was failed in 3.7 seconds. This result shows that tricresyl phosphate significantly increases the amount of adhesion and impregnation of the flame retardant. Examples 2 to 8 Using the same equipment and method as in Example 1, changing the amount of tricresyl phosphate added as shown in Table 1, or adding other phosphate esters or chlorinated paraffin (chlorine content: 40 %) was used to produce expandable beads. A foam was obtained in the same manner as in Example 1 using these expandable beads. Table 1 shows the amount and percentage of impregnation attached to the foam beads, as well as the flame retardancy (burning time) of the foam.
【表】
上表から、リン酸エステル又は塩素化パラフイ
ンを併用すると2,2―ビス(4―アリロキシ―
3,5―ジブロモフエニル)プロパンの付着含浸
率を著しく増大せしめることができ、難燃性の発
泡性ビーズ組成物が得られることがわかる。[Table] From the above table, when phosphate ester or chlorinated paraffin is used together, 2,2-bis(4-allyloxy-
It can be seen that the adhesion and impregnation rate of 3,5-dibromophenyl)propane can be significantly increased and a flame-retardant expandable bead composition can be obtained.
Claims (1)
発泡剤、(ii)難燃性付与量の2,2―ビス(4―ア
リロキシ―3,5―ジブロモフエニル)プロパ
ン、及び(iii)該スチレン系樹脂ビーズ100重量当り
0.05〜2重量部の常温で液体のリン酸エステル及
び/又は常温で液体のハロゲン化パラフインを含
有せしめてなる難燃性の発泡性スチレン系樹脂ビ
ーズ組成物。 2 2,2―ビス(4―アリロキシ―3,5―ジ
ブロモフエニル)プロパンの含有量がスチレン系
樹脂ビーズ100重量当り0.5〜5重量部であること
を特徴とする特許請求の範囲第1項の組成物。[Scope of Claims] 1 Styrenic resin beads, (i) a foaming agent in an amount that imparts foamability, and (ii) an amount of 2,2-bis(4-allyloxy-3,5-dibromophenyl) that imparts flame retardancy. ) propane, and (iii) per 100 weight of said styrenic resin beads.
A flame-retardant expandable styrenic resin bead composition containing 0.05 to 2 parts by weight of a phosphoric acid ester that is liquid at room temperature and/or a halogenated paraffin that is liquid at room temperature. 2. Claim 1, characterized in that the content of 2,2-bis(4-allyloxy-3,5-dibromophenyl)propane is 0.5 to 5 parts by weight per 100 weight of styrene resin beads. Composition of.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8588580A JPS5712048A (en) | 1980-06-26 | 1980-06-26 | Flame-retardant, expandable styrene resin bead composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8588580A JPS5712048A (en) | 1980-06-26 | 1980-06-26 | Flame-retardant, expandable styrene resin bead composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5712048A JPS5712048A (en) | 1982-01-21 |
JPS6217616B2 true JPS6217616B2 (en) | 1987-04-18 |
Family
ID=13871357
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8588580A Granted JPS5712048A (en) | 1980-06-26 | 1980-06-26 | Flame-retardant, expandable styrene resin bead composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5712048A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002523586A (en) | 1998-08-28 | 2002-07-30 | ザ ダウ ケミカル カンパニー | Flame retardant styrene polymer foam with reduced brominated flame retardant |
-
1980
- 1980-06-26 JP JP8588580A patent/JPS5712048A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5712048A (en) | 1982-01-21 |
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