JPH0374424A - Unsaturated polyester resin composition - Google Patents
Unsaturated polyester resin compositionInfo
- Publication number
- JPH0374424A JPH0374424A JP20781989A JP20781989A JPH0374424A JP H0374424 A JPH0374424 A JP H0374424A JP 20781989 A JP20781989 A JP 20781989A JP 20781989 A JP20781989 A JP 20781989A JP H0374424 A JPH0374424 A JP H0374424A
- Authority
- JP
- Japan
- Prior art keywords
- unsaturated polyester
- resin
- weight
- resin composition
- parts
- 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
Links
- 239000000203 mixture Substances 0.000 title claims abstract description 15
- 229920006337 unsaturated polyester resin Polymers 0.000 title claims description 17
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000000178 monomer Substances 0.000 claims abstract description 22
- 238000004132 cross linking Methods 0.000 claims abstract description 20
- 229920006305 unsaturated polyester Polymers 0.000 claims abstract description 12
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052740 iodine Inorganic materials 0.000 claims abstract description 7
- 239000011630 iodine Substances 0.000 claims abstract description 7
- 229920005989 resin Polymers 0.000 abstract description 31
- 239000011347 resin Substances 0.000 abstract description 30
- 238000001704 evaporation Methods 0.000 abstract description 7
- 150000003440 styrenes Chemical class 0.000 abstract description 7
- 238000002156 mixing Methods 0.000 abstract description 4
- 238000005336 cracking Methods 0.000 abstract description 3
- 238000000465 moulding Methods 0.000 abstract description 3
- 238000001723 curing Methods 0.000 description 19
- 239000002966 varnish Substances 0.000 description 9
- 230000008020 evaporation Effects 0.000 description 6
- -1 accelerators Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000013007 heat curing Methods 0.000 description 4
- 230000020169 heat generation Effects 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000011342 resin composition Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N 4-Methylstyrene Chemical compound CC1=CC=C(C=C)C=C1 JLBJTVDPSNHSKJ-UHFFFAOYSA-N 0.000 description 2
- 239000004342 Benzoyl peroxide Substances 0.000 description 2
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 2
- KFSLWBXXFJQRDL-UHFFFAOYSA-N Peracetic acid Chemical compound CC(=O)OO KFSLWBXXFJQRDL-UHFFFAOYSA-N 0.000 description 2
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 2
- 235000019400 benzoyl peroxide Nutrition 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000006482 condensation reaction Methods 0.000 description 2
- ZQMIGQNCOMNODD-UHFFFAOYSA-N diacetyl peroxide Chemical compound CC(=O)OOC(C)=O ZQMIGQNCOMNODD-UHFFFAOYSA-N 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 150000007519 polyprotic acids Polymers 0.000 description 2
- 150000005846 sugar alcohols Polymers 0.000 description 2
- HGTUJZTUQFXBIH-UHFFFAOYSA-N (2,3-dimethyl-3-phenylbutan-2-yl)benzene Chemical group C=1C=CC=CC=1C(C)(C)C(C)(C)C1=CC=CC=C1 HGTUJZTUQFXBIH-UHFFFAOYSA-N 0.000 description 1
- HGDULKQRXBSKHL-UHFFFAOYSA-N 1,1-bis(2-methylprop-2-enoyloxy)propyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OC(CC)(OC(=O)C(C)=C)OC(=O)C(C)=C HGDULKQRXBSKHL-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- LZDXRPVSAKWYDH-UHFFFAOYSA-N 2-ethyl-2-(prop-2-enoxymethyl)propane-1,3-diol Chemical compound CCC(CO)(CO)COCC=C LZDXRPVSAKWYDH-UHFFFAOYSA-N 0.000 description 1
- FRIBMENBGGCKPD-UHFFFAOYSA-N 3-(2,3-dimethoxyphenyl)prop-2-enal Chemical compound COC1=CC=CC(C=CC=O)=C1OC FRIBMENBGGCKPD-UHFFFAOYSA-N 0.000 description 1
- 239000004641 Diallyl-phthalate Substances 0.000 description 1
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 description 1
- GNQWHYWLSGTMSL-OUKQBFOZSA-N [(e)-3-phenylbut-1-enyl]benzene Chemical compound C=1C=CC=CC=1C(C)\C=C\C1=CC=CC=C1 GNQWHYWLSGTMSL-OUKQBFOZSA-N 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 229920000180 alkyd Polymers 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- QUDWYFHPNIMBFC-UHFFFAOYSA-N bis(prop-2-enyl) benzene-1,2-dicarboxylate Chemical compound C=CCOC(=O)C1=CC=CC=C1C(=O)OCC=C QUDWYFHPNIMBFC-UHFFFAOYSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 239000012933 diacyl peroxide Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000005802 health problem Effects 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 125000005397 methacrylic acid ester group Chemical group 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- GJBRNHKUVLOCEB-UHFFFAOYSA-N tert-butyl benzenecarboperoxoate Chemical compound CC(C)(C)OOC(=O)C1=CC=CC=C1 GJBRNHKUVLOCEB-UHFFFAOYSA-N 0.000 description 1
- CIHOLLKRGTVIJN-UHFFFAOYSA-N tert‐butyl hydroperoxide Chemical compound CC(C)(C)OO CIHOLLKRGTVIJN-UHFFFAOYSA-N 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
Landscapes
- Macromonomer-Based Addition Polymer (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、一般に不飽和ポリエステル樹脂&I!戒物に
関するものであり、特に、加熱成型時の樹脂温度の上昇
を抑制し、配合された架橋性モノマーの蒸発を防止する
とともにクラックの発生がない硬化物を与える不飽和ポ
リエステル樹脂組成物に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention generally relates to unsaturated polyester resin &I! This relates to samurai, and in particular, to an unsaturated polyester resin composition that suppresses the rise in resin temperature during heat molding, prevents the evaporation of the crosslinking monomer blended, and provides a cured product without cracks. It is.
(従来の技術および発明が解決しようとする課題)従来
、不飽和ポリエステル樹脂は、機械的特性、電気的特性
、熱的特性、作業性等に優れた性質を有しているため、
建設資材、輸送機器、ならびに工業材料の分野で広く利
用されている。(Prior art and problems to be solved by the invention) Conventionally, unsaturated polyester resins have excellent mechanical properties, electrical properties, thermal properties, workability, etc.
Widely used in the fields of construction materials, transportation equipment, and industrial materials.
不飽和ポリエステル樹脂は、多塩基酸と多価アルコール
の縮合反応によって得られる不飽和アルキッド樹脂であ
り、主に、架橋性モノマーと共に触媒、促進剤および種
々の充填剤と一緒に配合されて熱硬化性のワニスとして
利用されている。Unsaturated polyester resin is an unsaturated alkyd resin obtained by the condensation reaction of polybasic acid and polyhydric alcohol, and is mainly blended with crosslinking monomers, catalysts, accelerators, and various fillers to be thermoset. It is used as a sexual varnish.
かかる架橋性モノマーの配合量は20〜50重量%であ
るのが一般的であり、価格面の優位さと特性面の優秀さ
からスチレンが最も広く用いられている。しかし、スチ
レンは低分子量であるために、ワニスとしての保存時や
加熱硬化時に揮散してしまい、作業者や地域住民の健康
上問題のあることが指摘されている。この揮散による問
題を解決するための試みとして、特開昭57−8215
号公報に示されるように、架橋性モノマーとしてスチレ
ンダイマーを用いる方法がある。この方法により、スチ
レンの揮散により生ずる問題点は解消し得るが、得られ
る硬化物は軟質であり、経時的にクラックが発生するた
めに、不飽和ポリエステル樹脂硬化物の有する特徴が活
かされなくなってしまうという欠点を有している。The blending amount of such crosslinking monomer is generally 20 to 50% by weight, and styrene is most widely used because of its cost advantage and excellent properties. However, since styrene has a low molecular weight, it volatilizes during storage as a varnish or during heat curing, which has been pointed out to pose health problems for workers and local residents. In an attempt to solve this problem caused by volatilization, Japanese Patent Application Laid-Open No. 57-8215
As shown in the above publication, there is a method using styrene dimer as a crosslinking monomer. Although this method can solve the problem caused by styrene volatilization, the resulting cured product is soft and cracks occur over time, making it impossible to take advantage of the characteristics of the cured unsaturated polyester resin. It has the disadvantage of being stored away.
また、スチレンのような低分子量の架橋性モノマーを架
橋剤とし、有機過酸化物触媒を用いて不飽和ポリエステ
ル樹脂を加熱硬化させる反応は非常に激しい発熱反応で
あるため、反応熱により樹脂温度は200°C以上にま
で上昇する。この際、未反応の低分子量の架橋性モノマ
ーが揮散して、健康上ならびに環境上の問題を誘起する
ことは前述の通りであるが、さらに、硬化時の樹脂の最
高温度が高くなり過ぎるため、離型後に放冷された樹脂
は、内部に応力が蓄積され、クラックが発生し易いとい
う欠点が指摘されている。In addition, the reaction of heating and curing unsaturated polyester resin using a low molecular weight crosslinking monomer such as styrene as a crosslinking agent and an organic peroxide catalyst is an extremely exothermic reaction, so the resin temperature increases due to the heat of reaction. The temperature rises to over 200°C. At this time, unreacted low-molecular-weight crosslinking monomers volatilize, causing health and environmental problems, as mentioned above, but also because the maximum temperature of the resin during curing becomes too high. It has been pointed out that resins that are left to cool after being released from the mold have the disadvantage that stress accumulates inside them and cracks are likely to occur.
そこで本発明の目的は、上述した従来の架橋性モノマー
のもつ問題点を解消して、加熱硬化時の反応熱による樹
脂温度の上昇を抑制し、架橋性モノマーの蒸発を防止す
るとともにクラックの発生を防止し得る不飽和ポリエス
テル樹脂組成物を提供することにある。Therefore, the purpose of the present invention is to solve the above-mentioned problems of conventional crosslinking monomers, suppress the rise in resin temperature due to reaction heat during heat curing, prevent evaporation of crosslinking monomers, and prevent cracks from occurring. An object of the present invention is to provide an unsaturated polyester resin composition that can prevent the above problems.
(課題を解決するための手段)
上記目的を達成するため、本発明者らは種々の検討を重
ねた結果、不飽和ポリエステルと架橋性モノマーとを含
有する不飽和ポリエステル樹脂組成物に低分子量のスチ
レン類オリゴマーを配合することにより硬化時の発熱抑
制、架橋性モノマーの蒸発防止および硬化後のクラック
発生防止が図れることを見い出し、本発明を完成するに
至った。(Means for Solving the Problems) In order to achieve the above object, the present inventors have conducted various studies and found that a low molecular weight The present inventors have discovered that by blending a styrene oligomer, it is possible to suppress heat generation during curing, prevent evaporation of crosslinking monomers, and prevent cracks from occurring after curing, and have completed the present invention.
すなわち、本発明は、不飽和ポリエステルと架橋性モノ
マーとを含有する不飽和ポリエステル樹脂組成物におい
て、硬化時の発熱抑制、架橋性モノマーの蒸発防止およ
び硬化後のクラック発生防止のために低分子量のスチレ
ン類オリゴマーが配合れていることを特徴とする不飽和
ポリエステル樹脂組成物に関するものである。That is, the present invention provides an unsaturated polyester resin composition containing an unsaturated polyester and a crosslinkable monomer, in which a low molecular weight compound is used to suppress heat generation during curing, prevent evaporation of the crosslinkable monomer, and prevent cracking after curing. The present invention relates to an unsaturated polyester resin composition characterized by containing a styrene oligomer.
本発明においては、スチレン類オリゴマーとして、数平
均分子量が300〜1000であり、ヨウ素価が20〜
110 g−1t/100 gのものを用いる。数平均
分子量が300未満では、不飽和ポリエステルの加熱硬
化時に臭気が発生し、好ましくない。一方、1000を
超えると不飽和ポリエステル樹脂との相溶性が低下し、
均一な&Il戒の樹脂が得られず、やはり好ましくない
。In the present invention, the styrene oligomer has a number average molecular weight of 300 to 1000 and an iodine value of 20 to 1000.
110 g-1t/100 g is used. If the number average molecular weight is less than 300, an odor will be generated during heat curing of the unsaturated polyester, which is not preferable. On the other hand, when it exceeds 1000, the compatibility with unsaturated polyester resin decreases,
It is not possible to obtain a uniform resin, which is also undesirable.
また、ヨウ素価が20 g −Is/100 g未満で
は、樹脂の架橋密度が低下し、十分な硬度を有する樹脂
が得られないため、好ましくない。一方、110g1g
/100 gを超えると、得られる硬化樹脂は軟質であ
り、経時的にクランクが発生するため、やはり好ましく
ない。Moreover, if the iodine value is less than 20 g -Is/100 g, the crosslinking density of the resin decreases and a resin having sufficient hardness cannot be obtained, which is not preferable. On the other hand, 110g1g
If it exceeds /100 g, the resulting cured resin is soft and cracks occur over time, which is also not preferred.
オリゴマー〇原料として用いるスチレン類としては、ス
チレン、α−メチルスチレン、P−メチルスチレンのよ
うな各種アルキル基置換スチレン等を挙げることができ
、これらは混合物であってもよい、これらのスチレン類
のオリゴマーは、酸触媒等を用いて軽度に重合させるこ
とにより得られる。Styrenes used as raw materials for oligomers include various alkyl group-substituted styrenes such as styrene, α-methylstyrene, and P-methylstyrene, and these may be mixtures. The oligomer is obtained by mild polymerization using an acid catalyst or the like.
また、本発明に用いる不飽和ポリエステルとしては、多
価アルコール類と不飽和多塩基酸の縮合反応により得ら
れる重合物を挙げることができる。Furthermore, examples of the unsaturated polyester used in the present invention include polymers obtained by a condensation reaction of polyhydric alcohols and unsaturated polybasic acids.
具体的には、昭和高分子(株)製の「リボラック150
11RJ、「リボラック1588QTJや日立化成工業
(株)製の「ポリセット9230 Jや日本ユピカ(株
)製の「エビカフ5フ6 J等を挙げることができる。Specifically, “Revolac 150” manufactured by Showa Kobunshi Co., Ltd.
11RJ, ``Revolac 1588QTJ,'' Polyset 9230 J manufactured by Hitachi Chemical Co., Ltd., and ``Ebi Cuff 5F 6 J manufactured by Nippon U-Pica Co., Ltd.''.
更に、本発明に用いる架橋性モノマーとしては、分子内
にオレフィン性二重結合を有する物質であればよく、具
体的にはスチレン、α−メチルスチレン、p−メチルス
チレン等のスチレン類;トリメチロールプロパントリメ
タクリレート、2−ヒドロキシエチルメタクリレート等
のアクリル酸またはメタクリル酸エステル;トリメチロ
ールプロパンアリルエーテル、ジアリルフタレート等の
アリルエーテル等の、不飽和ポリエステル用汎用架橋性
モノマーを挙げることができる。Further, the crosslinkable monomer used in the present invention may be any substance having an olefinic double bond in its molecule, and specifically includes styrenes such as styrene, α-methylstyrene, and p-methylstyrene; trimethylol. General-purpose crosslinking monomers for unsaturated polyesters include acrylic acid or methacrylic acid esters such as propane trimethacrylate and 2-hydroxyethyl methacrylate; and allyl ethers such as trimethylolpropane allyl ether and diallyl phthalate.
次に、本発明の不飽和ポリエステル樹脂組成物を硬化さ
せるのに用いられる硬化剤としては、t−ブチルヒドロ
ペルオキシドやクメンヒドロペルオキシドのようなアル
キルヒドロペルオキシド:過酸化ジ−t−ブチルや過酸
化ジクミルのような過酸化ジアルキル;過酸化ベンゾイ
ルや過酸化アセチルのような過酸化ジアシル;過酢酸t
−ブチルや過安息香酸t−ブチルのような過酸エステル
等を挙げることができる。Next, the curing agent used for curing the unsaturated polyester resin composition of the present invention includes alkyl hydroperoxides such as t-butyl hydroperoxide and cumene hydroperoxide; Dialkyl peroxides such as dicumyl; diacyl peroxides such as benzoyl peroxide and acetyl peroxide; peracetic acid t
Examples include peracid esters such as -butyl and t-butyl perbenzoate.
本発明の樹脂組成物は、不飽和ポリエステル100重量
部に対してスチレン類のオリゴマーを7〜50重量部加
えることが好ましく、7重量部未満では、加熱硬化時の
樹脂温度の抑制と硬化樹脂のクラック発生防止効果が十
分ではなく、一方50重量部を超えると、樹脂の架橋密
度が低下し、十分な硬度を有する樹脂が得られないため
好ましくない。In the resin composition of the present invention, it is preferable to add 7 to 50 parts by weight of a styrene oligomer to 100 parts by weight of the unsaturated polyester. The effect of preventing crack generation is not sufficient, and on the other hand, if it exceeds 50 parts by weight, the crosslinking density of the resin decreases and a resin having sufficient hardness cannot be obtained, which is not preferable.
また、架橋性モノマーは、不飽和ポリエステル100重
量部に対して7〜30重量部加えることが好ましい、7
重量部未満では、樹脂の混合性が悪くなり、均一な組成
の樹脂が得られなくり、一方30重量部を超えると、加
熱硬化時や保存時に臭気が生ずるため、好ましくない。Further, the crosslinking monomer is preferably added in an amount of 7 to 30 parts by weight based on 100 parts by weight of the unsaturated polyester.
If the amount is less than 30 parts by weight, the mixability of the resin will be poor and a resin with a uniform composition will not be obtained, while if it exceeds 30 parts by weight, an odor will be produced during heat curing or storage, which is not preferable.
更に、硬化剤の使用量は、樹脂組成物に対して0.5〜
5重量%の範囲内で用いる。0.5重量%未満では、樹
脂の硬化に長時間を要するため、実用的ではない、一方
、5重量%を超えて用いても、得られる硬化樹脂の特性
は向上しないため、不経済である。Furthermore, the amount of curing agent used is 0.5 to 0.5 to
It is used within a range of 5% by weight. If it is less than 0.5% by weight, it will take a long time to cure the resin, so it is not practical. On the other hand, if it is more than 5% by weight, the properties of the resulting cured resin will not improve, so it is uneconomical. .
本発明の樹脂組成物は、上記の必須成分の他に、硬化促
進剤、重合禁止剤、充填材等、汎用に使用されているも
のを必要に応じて適宜使用することができる。In addition to the above-mentioned essential components, the resin composition of the present invention may appropriately contain commonly used materials such as a curing accelerator, a polymerization inhibitor, and a filler, as required.
(実施例)
次に本発明を実施例および比較例を挙げて具体的に説明
する。(Example) Next, the present invention will be specifically explained by giving examples and comparative examples.
z嵐班上
昭和高分子(株)製の不飽和ポリエステル(商品名「リ
ボラック150 )IRJ )70重量部に、スチレン
オリゴマー(数平均分子量340;ヨウ素価67g−I
t/100 g) 20重量部と、架橋性モノマーとし
てスチレンモノマー(和光純薬(株)製試薬特級)10
重量部とを配合した0次に、ベンゾイルペルオキシド(
和光純薬(株)製試薬特級)を1重量部添加し、十分に
撹拌混合してワニスを得た。このワニスを18++nφ
X180amの試験管に、100鵬の高さにまで入れ、
ワニス中心部に、デジタル温度計に接続した熱電対をセ
ットした。z Arashiban 70 parts by weight of unsaturated polyester (trade name "Revolac 150" IRJ) manufactured by Kamishowa Kobunshi Co., Ltd., was added with styrene oligomer (number average molecular weight 340; iodine value 67 g-I).
t/100 g) 20 parts by weight, and 10 parts by weight of styrene monomer (special grade reagent manufactured by Wako Pure Chemical Industries, Ltd.) as a crosslinking monomer.
Parts by weight of benzoyl peroxide (
1 part by weight of Reagent Special Grade (manufactured by Wako Pure Chemical Industries, Ltd.) was added and thoroughly stirred and mixed to obtain a varnish. This varnish is 18++nφ
Put it in a test tube of 180 am to a height of 100 am,
A thermocouple connected to a digital thermometer was set in the center of the varnish.
熱電対をセットしたワニス入りの試験管を、80℃±0
.5℃に温度調節されたオイルバスにワニス部が全て浸
るようにセットし、ワニス中心部の温度変化を観察した
。樹脂の硬化特性評価は、JISに6901 に準じ
て行ない、評価項目とその意味は以下に示す通りである
。A varnished test tube with a thermocouple set at 80℃±0
.. The varnish was set in an oil bath whose temperature was adjusted to 5°C so that the entire varnish was immersed, and temperature changes at the center of the varnish were observed. The curing characteristics of the resin were evaluated according to JIS 6901, and the evaluation items and their meanings are as shown below.
■ ゲル化時間:樹脂の中心温度が65°Cから85°
Cまでに上昇するのに要する時間。■ Gelling time: resin center temperature from 65°C to 85°
The time required to rise to C.
■ 最小硬化時間:樹脂の中心温度が最高点に達するま
でに要する時間。■ Minimum curing time: The time required for the core temperature of the resin to reach its maximum point.
■ 最高発熱温度:樹脂の中心温度が最高点に達した温
度。■ Maximum exothermic temperature: The temperature at which the center temperature of the resin reaches its maximum point.
また、硬化樹脂に発生したクラックは、硬化直後と、硬
化樹脂を試験管からとり出し、室温2o%R11のデシ
ケータ−中に7日間放置した後に目視により観察し、そ
の有無を判定した。In addition, cracks generated in the cured resin were visually observed immediately after curing and after the cured resin was taken out of the test tube and left in a desiccator at room temperature 20% R11 for 7 days, to determine the presence or absence of cracks.
判定の基準は、(A)クラックなし、(B)部分的にク
ラック発生、(C)全体にクラック発生、03段階とし
た。The criteria for evaluation were (A) no cracks, (B) cracks partially, and (C) cracks throughout, grade 03.
また、樹脂の混合の容易さは、硬化剤を添加する前にワ
ニスを室温で30分間放置し、各成分の分離の有無を目
視で判定して行なった。評価の基準は、「分離」もしく
は「非分離」の2段階とした。Furthermore, the ease of mixing the resins was determined by allowing the varnish to stand at room temperature for 30 minutes before adding the curing agent, and visually determining the presence or absence of separation of each component. The evaluation criteria were in two stages: "separation" and "non-separation."
更に、硬化時の樹脂の発熱による架橋性モノマーの蒸発
の有無は、試験管内部を目視により観察するとともに、
発熱時の樹脂の臭気の有無により判断した。結果は、下
記の第1表にまとめて示した。Furthermore, the presence or absence of evaporation of the crosslinking monomer due to the heat generated by the resin during curing can be determined by visually observing the inside of the test tube.
Judgment was made based on the presence or absence of resin odor during heat generation. The results are summarized in Table 1 below.
1遣1:」−
スチレンオリゴマー(数平均分子量340. ヨウ素
価67g−Im/100 g)とスチレンモノマーの使
用量を第1表に示す割合で配合した以外は実施例1と同
様の操作を行なった。樹脂の硬化特性と外観観察の結果
は、第1表にまとめて示した。1: 1: The same procedure as in Example 1 was carried out except that the styrene oligomer (number average molecular weight 340, iodine value 67 g-Im/100 g) and styrene monomer were blended in the proportions shown in Table 1. Ta. The results of resin curing characteristics and appearance observation are summarized in Table 1.
止藍班上
スチレンオリゴマーを用いず、スチレンモノマーを30
重量部用いた以外は実施例1と同様の操作を行なった。30% of styrene monomer without using styrene oligomer
The same operation as in Example 1 was performed except that parts by weight were used.
樹脂の硬化特性と外観観察の結果は、第1表にまとめて
示した。The results of resin curing characteristics and appearance observation are summarized in Table 1.
五藍班エ
スチレンモノマーを用いず、スチレンオリゴマー(数平
均分子量340.ヨウ素価67g−1冨/100 g)
を30重量部用いた以外は、実施例1と同様の操作を行
なった。樹脂の硬化特性と外観観察の結果は、第1表に
まとめて示した。Styrene oligomer (number average molecular weight 340, iodine value 67g-1 richness/100g) without using styrene monomer
The same operation as in Example 1 was performed except that 30 parts by weight of . The results of resin curing characteristics and appearance observation are summarized in Table 1.
五藍班1エエ
スチレンオリゴマーの代りにスチレンダイマー(1,3
−ジフェニルブテン−1冨95−%含L EFつ素価1
11 g−I2/100 g)を用い、第1表に示した
割合で配合した以外は実施例1と同様の操作を行なった
。411脂の硬化特性と外観観察の結果は、第1表にま
とめて示した。Five blue group 1 Styrene dimer (1,3
-Diphenylbutene-1 richness 95-% L EF element value 1
11 g-I2/100 g) was used, and the same operation as in Example 1 was performed except that the mixture was blended in the proportions shown in Table 1. The results of hardening characteristics and appearance observation of 411 resin are summarized in Table 1.
(発明の効果〉
以上説明してきたように本発明の不飽和ポリエステル樹
脂組成物は、特定のスチレン頬オリゴマーを配合したこ
とで硬化時の発熱による樹脂温度の上昇を抑制すること
ができ、これにより架橋性モノマーの蒸発を防止すると
ともに、樹脂硬化物のクランク発生を防止する効果が認
められ、成形特にクラックの発生が生じた従来の不飽和
ポリエステル樹脂の代りとして好適な樹脂組成物である
といえる。(Effects of the Invention) As explained above, the unsaturated polyester resin composition of the present invention can suppress the rise in resin temperature due to heat generation during curing by incorporating a specific styrene cheek oligomer. It has been observed that it has the effect of preventing the evaporation of crosslinking monomers as well as the occurrence of cracks in the cured resin, and can be said to be a suitable resin composition as a substitute for conventional unsaturated polyester resins that have been prone to cracking, especially during molding. .
Claims (1)
不飽和ポリエステル樹脂組成物において、数平均分子量
が300〜1000の範囲であり、かつヨウ素価が20
〜110g−I_2/100gの範囲であるスチレン類
オリゴマーが配合されていることを特徴とする不飽和ポ
リエステル樹脂組成物。 2、上記スチレン類のオリゴマーの配合量が、不飽和ポ
リエステル100重量部に対して7〜50重量部の範囲
であり、架橋性モノマーの配合量が、不飽和ポリエステ
ル100重量部に対して7〜30重量部の範囲である請
求項1記載の不飽和ポリエステル樹脂組成物。[Claims] 1. An unsaturated polyester resin composition containing an unsaturated polyester and a crosslinkable monomer, which has a number average molecular weight in the range of 300 to 1000 and an iodine value of 20.
An unsaturated polyester resin composition characterized in that a styrene oligomer in the range of ~110g-I_2/100g is blended. 2. The amount of the styrene oligomer is in the range of 7 to 50 parts by weight per 100 parts by weight of the unsaturated polyester, and the amount of the crosslinking monomer is in the range of 7 to 50 parts by weight per 100 parts by weight of the unsaturated polyester. The unsaturated polyester resin composition according to claim 1, wherein the amount is in the range of 30 parts by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20781989A JPH0374424A (en) | 1989-08-14 | 1989-08-14 | Unsaturated polyester resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20781989A JPH0374424A (en) | 1989-08-14 | 1989-08-14 | Unsaturated polyester resin composition |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0374424A true JPH0374424A (en) | 1991-03-29 |
Family
ID=16546032
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20781989A Pending JPH0374424A (en) | 1989-08-14 | 1989-08-14 | Unsaturated polyester resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0374424A (en) |
-
1989
- 1989-08-14 JP JP20781989A patent/JPH0374424A/en active Pending
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