JPH0216113A - Process for modifying unsaturated polyester resin - Google Patents

Process for modifying unsaturated polyester resin

Info

Publication number
JPH0216113A
JPH0216113A JP16605488A JP16605488A JPH0216113A JP H0216113 A JPH0216113 A JP H0216113A JP 16605488 A JP16605488 A JP 16605488A JP 16605488 A JP16605488 A JP 16605488A JP H0216113 A JPH0216113 A JP H0216113A
Authority
JP
Japan
Prior art keywords
unsaturated polyester
polyester resin
parts
weight
polymerization initiator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP16605488A
Other languages
Japanese (ja)
Inventor
Kenji Kato
賢二 加藤
Hisakata Koga
尚賢 古賀
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.)
NOF Corp
Original Assignee
Nippon Oil and Fats 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 Nippon Oil and Fats Co Ltd filed Critical Nippon Oil and Fats Co Ltd
Priority to JP16605488A priority Critical patent/JPH0216113A/en
Publication of JPH0216113A publication Critical patent/JPH0216113A/en
Pending legal-status Critical Current

Links

Landscapes

  • Macromonomer-Based Addition Polymer (AREA)

Abstract

PURPOSE:To make is possible to speed up the cycle of operation, to reduce coloration and to improve the heat resistance by curing an unsaturated polyester resin and a specific maleimide compound in the presence of a radical polymerization initiator at ordinary temperatures or under heating. CONSTITUTION:An unsaturated polyester resin (A) is obtained by blending 100pts.wt. (hereinafter merely pts.) unsaturated polyester with 5-70pts. vinyl monomer copolymerizable therewith (e.g. styrene). 100pts. component (A) and 0.5-100pts. maleimide compound of the given formula (wherein R1 is 1-18C alkyl or cycloalkyl; and R2-3 are each H, halogen, methyl or ethyl) (e.g. N- cyclohexylmaleimide) are cured in the presence of 0.1-10pts. radical polymerization initiator (e.g. benzoyl peroxide) at ordinary temperatures, that is, 10-30 deg.C or by heating to 50-200 deg.C.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、改質反応においてサイクルアップが可能であ
り、耐熱性に優れ、且つ着色が少ない不飽和ポリエステ
ル樹脂を得るための不飽和ポリエステル樹脂の改質方法
に関する。
[Detailed Description of the Invention] <Industrial Application Field> The present invention provides an unsaturated polyester resin for obtaining an unsaturated polyester resin that can be cycled up in a modification reaction, has excellent heat resistance, and has little coloring. This invention relates to a method for modifying.

〈従来の技術〉 不飽和ポリエステル樹脂は、熱硬化型の成形材料として
自動車部品、電気部品、浄化槽、バスタブ又は漁船等に
広く用いられている。
<Prior Art> Unsaturated polyester resins are widely used as thermosetting molding materials for automobile parts, electrical parts, septic tanks, bathtubs, fishing boats, and the like.

しかし、従来の硬化物の示す物性値は必らずしも充分で
はなく、成形性の優れた熱可塑性エンジニアリング樹脂
との比較から、より耐熱性に優れ、且つ着色の少ない硬
化物を得るための不飽和ポリエステル樹脂の改質方法が
望まれている。
However, the physical properties of conventional cured products are not necessarily sufficient, and from a comparison with thermoplastic engineering resins that have excellent moldability, it is possible to obtain cured products with better heat resistance and less coloring. A method for modifying unsaturated polyester resins is desired.

従来、不飽和ポリエステル樹脂の耐熱性を向上させるた
めには、不飽和ポリエステルの不飽和度を増加させ架橋
密度を高くする方法又はより耐熱性の高い充填剤を添加
する方法等が用いられている。
Conventionally, in order to improve the heat resistance of unsaturated polyester resins, methods such as increasing the degree of unsaturation of unsaturated polyester to increase crosslinking density, or adding fillers with higher heat resistance have been used. .

しかしながら、これらの方法には、次のような問題点が
ある。即ち不飽和ポリエステルの不飽和度等を変化させ
ると耐熱性以外の物性、例えば耐衝撃性が低下する等の
欠点が生じること、又充填剤も種々の特性に大きな影響
を与えるため使用量に制限があること等である。
However, these methods have the following problems. In other words, changing the degree of unsaturation of unsaturated polyester causes disadvantages such as a decrease in physical properties other than heat resistance, such as impact resistance, and fillers also have a large effect on various properties, so the amount used must be limited. For example, there is a

〈発明が解決しようとする課題〉 本発明の目的は、耐熱性に優れており1着色が少く、し
かも広範囲の改質条件においても改質可能な不飽和ポリ
エステル樹脂の改質方法を提供することにある。
<Problems to be Solved by the Invention> An object of the present invention is to provide a method for modifying an unsaturated polyester resin that has excellent heat resistance, has little coloration, and can be modified under a wide range of modification conditions. It is in.

〈課題を解決するための手段〉 本発明によれば不飽和ポリエステル及び該不飽和ポリエ
ステルと共重合可能なビニルモノマーからなる不飽和ポ
リエステル樹脂に。
<Means for Solving the Problems> According to the present invention, an unsaturated polyester resin comprising an unsaturated polyester and a vinyl monomer copolymerizable with the unsaturated polyester is provided.

下記一般式(I) (式中R□は炭素数1〜18のアルキル基又はシクロア
ルキル基を示し、R2及びR3は水素原子、ハロゲン原
子、メチル基又はエチル基を示す。)で表わされるマレ
イミド化合物を前記不飽和ポリエステル樹脂100重量
部に対して0.5〜100重量部添加し、ラジカル重合
開始剤存在下において常温硬化又は加熱硬化させること
を特徴とする不飽和ポリエステル樹脂の改質方法が提供
される。
Maleimide represented by the following general formula (I) (wherein R□ represents an alkyl group or cycloalkyl group having 1 to 18 carbon atoms, and R2 and R3 represent a hydrogen atom, a halogen atom, a methyl group or an ethyl group) A method for modifying an unsaturated polyester resin, which comprises adding 0.5 to 100 parts by weight of a compound to 100 parts by weight of the unsaturated polyester resin, and curing at room temperature or heating in the presence of a radical polymerization initiator. provided.

以下本発明を更に詳細に説明する。The present invention will be explained in more detail below.

本発明における不飽和ポリエステルは、無水マレイン酸
、フマル酸等の不飽和二塩基酸又は該不飽和二塩基酸及
び無水フタル酸、イソフタル酸。
The unsaturated polyester in the present invention is an unsaturated dibasic acid such as maleic anhydride or fumaric acid, or the unsaturated dibasic acid and phthalic anhydride or isophthalic acid.

アジピン酸、テトラクロロ無水フタル酸等の飽和二塩基
酸の混合物と、エチレングリコール、プロピレングリコ
ール、1,3−ブチレンゲリコール。
A mixture of saturated dibasic acids such as adipic acid and tetrachlorophthalic anhydride, and ethylene glycol, propylene glycol, and 1,3-butylene gellicol.

ジエチレングリコール、ジプロピレングリコール。Diethylene glycol, dipropylene glycol.

ネオペンチルグリコール、ビスフェノールジオキシエチ
ルエーテル等の多価アルコールとを常法により、好まし
くは1:0.5〜2モル、特に好ましくは1:1の配合
割合で1例えば窒素下。
A polyhydric alcohol such as neopentyl glycol or bisphenol dioxyethyl ether is mixed in a conventional manner, preferably in a ratio of 1:0.5 to 2 mol, particularly preferably 1:1, under nitrogen, for example.

170〜200℃で縮合させることにより得ることがで
きる。また市販の不飽和ポリエステルを使用することも
できる。
It can be obtained by condensation at 170 to 200°C. It is also possible to use commercially available unsaturated polyesters.

本発明に用いる前記不飽和ポリエステルと共重合可能な
ビニルモノマーとしては例えばスチレン。
Examples of the vinyl monomer copolymerizable with the unsaturated polyester used in the present invention include styrene.

0−クロロスチレン、ビニルトルエン、メタクリル酸メ
チル、ジアリルフタレート、トリアリルシアヌレート、
ジアリルベンゼンホスホネート等を挙げることができ、
これらは単独又は併用して用いることができる。前記ビ
ニルモノマーの配合割合は、前記不飽和ポリエステル1
00重量部に対し、5〜70重量部、特に好ましくは1
0〜60重量部であることが望ましい、また市販の不飽
和ポリエステル樹脂を使用することも可能である。
0-chlorostyrene, vinyltoluene, methyl methacrylate, diallyl phthalate, triallyl cyanurate,
Examples include diallylbenzenephosphonate, etc.
These can be used alone or in combination. The blending ratio of the vinyl monomer is 1 to 1 of the unsaturated polyester.
00 parts by weight, 5 to 70 parts by weight, particularly preferably 1
It is desirable that the amount is 0 to 60 parts by weight, and it is also possible to use commercially available unsaturated polyester resins.

本発明におけるマレイミド化合物は、下記一般式(I)
で表わすことができる。
The maleimide compound in the present invention has the following general formula (I)
It can be expressed as

式中R4は炭素数1〜18の直鎖アルキル基、分枝アル
キル基又はシクロアルキル基を示し、R2及びR3は水
素原子、ハロゲン原子、メチル基又はエチル基を示す。
In the formula, R4 represents a straight-chain alkyl group, a branched alkyl group, or a cycloalkyl group having 1 to 18 carbon atoms, and R2 and R3 represent a hydrogen atom, a halogen atom, a methyl group, or an ethyl group.

前記一般式(I)で示されるマレイミド化合物としては
例えば、N−メチルマレイミド、N−イソプロピルマレ
イミド、N−t−ブチルマレイミド、N−オクタデシル
マレイミド、N−シクロへキシルマレイミド、N−シク
ロヘキシル(α−メチル)マレイミド、N−シクロヘキ
シル(α、β−ジメチル)マレイミド、N−(2−メチ
ル−シクロへキシル−1)マレイミド、N−3−エチル
−シクロへキシル−1−マレイミド、N−シクロドデシ
ルマレイミド、N−ラウリルマレイミド、N−ドデシル
マレイミド等を好ましく挙げることができる。
Examples of the maleimide compound represented by the general formula (I) include N-methylmaleimide, N-isopropylmaleimide, N-t-butylmaleimide, N-octadecylmaleimide, N-cyclohexylmaleimide, N-cyclohexyl (α- methyl)maleimide, N-cyclohexyl(α,β-dimethyl)maleimide, N-(2-methyl-cyclohexyl-1)maleimide, N-3-ethyl-cyclohexyl-1-maleimide, N-cyclododecylmaleimide , N-laurylmaleimide, N-dodecylmaleimide and the like can be preferably mentioned.

前記マレイミド化合物の前記不飽和ポリエステル樹脂1
00重量部当りの添加割合は0.5〜100重量部であ
り、0.5重量部未満では、得られた硬化物の耐熱性の
改良が認められず。
The unsaturated polyester resin 1 of the maleimide compound
The addition ratio per 0.00 parts by weight is 0.5 to 100 parts by weight, and if it is less than 0.5 parts by weight, no improvement in the heat resistance of the obtained cured product will be observed.

100重量部を超えると硬化物の物性が低下するので好
ましくない。
If it exceeds 100 parts by weight, the physical properties of the cured product will deteriorate, which is not preferable.

本発明における、不飽和ポリエステル樹脂の改質方法は
、不飽和ポリエステル樹脂にマレイミド化合物を添加し
、ラジカル重合開始剤の存在下において、常温硬化又は
加熱硬化させる方法である。
The method for modifying an unsaturated polyester resin in the present invention is a method in which a maleimide compound is added to an unsaturated polyester resin, and the mixture is cured at room temperature or by heating in the presence of a radical polymerization initiator.

具体的には、例えば前記不飽和ポリエステル樹脂と前記
マレイミド化合物とを混合、撹拌し均一な溶液とするこ
とが望ましく、これに必要に応じて、例えばガラス繊維
、フィラー、無機物等の充填剤及び/又は補強剤を添加
することもできる。次いで前記溶液に有機過酸化物等の
ラジカル重合開始剤を添加し、50〜200℃の温度範
囲において加熱硬化させる方法又は還元剤等を併用し、
10〜30℃の低温で硬化させる方法等を用いることが
できる。
Specifically, for example, it is desirable to mix and stir the unsaturated polyester resin and the maleimide compound to form a uniform solution, and if necessary, fillers such as glass fibers, fillers, and inorganic substances and/or Or a reinforcing agent can also be added. Next, a radical polymerization initiator such as an organic peroxide is added to the solution, and the method is heated and cured in a temperature range of 50 to 200°C, or a reducing agent is used in combination,
A method of curing at a low temperature of 10 to 30° C. or the like can be used.

前記ラジカル重合開始剤である有機過酸化物としては、
例えば、ベンゾイルペルオキシド、ラウロイルペルオキ
シド、し−ブチルペルオキシベンゾエート、イソプロピ
ルペルオキシジカーボネート、1,1−ビス(し−ブチ
ルプルオキシ)−3゜3.5−1−リメチルシクロヘキ
サン、ジクミルペルオキシド、2,5ジメチル−2,5
−ジ(七−ブチルペルオキシ)ヘキシン−3等の加熱硬
化系の重合開始剤、クメンヒドロペルオキシド/酸化マ
ンガン、メチルエチルケ1ヘンペルオキシド/ナフテン
酸コバルト、アセチルアセトンペルオキシド/酸化第二
鉄、ベンゾイルペルオキシド/ジメチルアニリン等の常
温硬化系の重合開始剤等を挙げることができる。これら
の使用量は、通常不飽和ポリエステル樹脂100重量部
に対して、0.1〜10里量部であることが好ましい。
As the organic peroxide which is the radical polymerization initiator,
For example, benzoyl peroxide, lauroyl peroxide, butyl peroxybenzoate, isopropyl peroxydicarbonate, 1,1-bis(butylpuroxy)-3゜3.5-1-limethylcyclohexane, dicumyl peroxide, 2, 5 dimethyl-2,5
-Heat-curing polymerization initiators such as di(7-butylperoxy)hexyne-3, cumene hydroperoxide/manganese oxide, methyl ethylphene peroxide/cobalt naphthenate, acetylacetone peroxide/ferric oxide, benzoyl peroxide/dimethylaniline Examples include room temperature curing type polymerization initiators such as. The amount of these used is preferably 0.1 to 10 parts by weight per 100 parts by weight of the unsaturated polyester resin.

〈発明の効果〉 本発明の不飽和ポリエステル樹脂の改質方法によれば、
ゲル化から硬化までの時間を短縮出来るので成形のサイ
クルアップが可能になる。さらに得られた成形加工品は
耐熱性が著しく改質されており、且つ着色も少ない等の
利点がある。
<Effects of the Invention> According to the method for modifying unsaturated polyester resin of the present invention,
Since the time from gelation to hardening can be shortened, molding cycles can be increased. Furthermore, the resulting molded product has the advantage of significantly improved heat resistance and less discoloration.

〈実施例〉 つぎに参考例、実施例及び比較例により本発明を更に詳
しく説明するが、本発明はこれらに限定されるものでは
ない。
<Example> Next, the present invention will be explained in more detail with reference examples, examples, and comparative examples, but the present invention is not limited thereto.

参考例1 (不飽和ポリエステル樹脂の調製) 撹拌機、温度計、窒素ガス吹込み管、コンデンサーを取
りつけた500mQの四つロフラスコに無水マレイン9
18g、無水フタル酸178g、プロピレングリコール
167gを添加し、窒素ガスを約100mQ/分の流速
で通じながら、撹拌下において加熱した。1時間で15
0℃まで昇温し更に1時間撹拌をつづけた。その後頁に
反応温度を上昇させ210 ’Cに保ちなから縮合水を
留出させた。
Reference Example 1 (Preparation of unsaturated polyester resin) Anhydrous malein 9 was placed in a 500 mQ four-loop flask equipped with a stirrer, thermometer, nitrogen gas blowing tube, and condenser.
18 g of phthalic anhydride, 178 g of propylene glycol, and 167 g of propylene glycol were added, and the mixture was heated under stirring while passing nitrogen gas at a flow rate of about 100 mQ/min. 15 in 1 hour
The temperature was raised to 0°C, and stirring was continued for an additional hour. Thereafter, the reaction temperature was raised and maintained at 210'C to distill off water of condensation.

次いで反応液の酸価を測定し、酸価40となった時点で
冷却した。次にスチレンモノマー200gを加え均一溶
液となるまで撹拌した。その結果淡黄色の不飽和ポリエ
ステル樹脂を得た。
Next, the acid value of the reaction solution was measured, and when the acid value reached 40, it was cooled. Next, 200 g of styrene monomer was added and stirred until a homogeneous solution was obtained. As a result, a pale yellow unsaturated polyester resin was obtained.

1色見え (不飽和ポリエステル樹脂の調製) フマル酸162g、イソフタル酸100g、プロピレン
グリコール79gおよびネオペンチルグリコール109
gを仕込み、参考例1と同様な方法で酸価30の不飽和
ポリエステルを合成し、次いでスチレンモノマー濃度が
35重量%となるようにスチレンモノマーを添加して不
飽和ポリエステル樹脂を得た6 夫胤■よ 参考例1で調製した不飽和ポリエステル樹脂100重量
部に、N−シクロへキシルマレイシド10重量部を添加
溶解させた。次にベンゾイルペルオキシド1.0重量部
を加え均一に溶解し、JIS  K−6901に従って
硬化反応を行なった。硬化温度及び硬化物の物性値1着
色度、熱変形温度等をあわせて表1に示す。又着色度は
目視でl1lt察を行い、熱変形温度はJ I S  
K−7207に従い別途注形板を作成し、測定した。
One color appearance (preparation of unsaturated polyester resin) 162 g of fumaric acid, 100 g of isophthalic acid, 79 g of propylene glycol and 109 g of neopentyl glycol
An unsaturated polyester with an acid value of 30 was synthesized in the same manner as in Reference Example 1, and then styrene monomer was added so that the styrene monomer concentration was 35% by weight to obtain an unsaturated polyester resin. To 100 parts by weight of the unsaturated polyester resin prepared in Reference Example 1, 10 parts by weight of N-cyclohexyl maleiside was added and dissolved. Next, 1.0 parts by weight of benzoyl peroxide was added and uniformly dissolved, and a curing reaction was performed according to JIS K-6901. Table 1 shows the curing temperature, physical properties of the cured product, degree of coloring, heat deformation temperature, etc. In addition, the degree of coloring was visually inspected, and the heat deformation temperature was determined by JIS.
A casting plate was separately prepared according to K-7207 and measured.

叉胤叢又二↓i 表1に示す不飽和ポリエステル樹脂、マレイミド化合物
及びラジカル重合開始剤を用い、また表1に示す反応条
件によって、実施例1と同様に不飽和ポリエステル樹脂
の改質反応を行い、次いで得られた硬化物の硬度、熱変
形温度及び着色度を測定した。その結果を表1に示す。
A modification reaction of an unsaturated polyester resin was carried out in the same manner as in Example 1 using the unsaturated polyester resin, maleimide compound and radical polymerization initiator shown in Table 1 and under the reaction conditions shown in Table 1. Then, the hardness, heat distortion temperature, and degree of coloring of the obtained cured product were measured. The results are shown in Table 1.

星較透上二±Hoshiki Toru 12±

Claims (1)

【特許請求の範囲】 不飽和ポリエステル及び該不飽和ポリエステルと共重合
可能なビニルモノマーからなる不飽和ポリエステル樹脂
に、下記一般式( I ) ▲数式、化学式、表等があります▼・・・( I ) (式中R_1は炭素数1〜18のアルキル基又はシクロ
アルキル基を示し、R_2及びR_3は水素原子、ハロ
ゲン原子、メチル基又はエチル基を示す。)で表わされ
るマレイミド化合物を前記不飽和ポリエステル樹脂10
0重量部に対して0.5〜100重量部添加し、ラジカ
ル重合開始剤存在下において常温硬化又は加熱硬化させ
ることを特徴とする不飽和ポリエステル樹脂の改質方法
[Claims] An unsaturated polyester resin consisting of an unsaturated polyester and a vinyl monomer copolymerizable with the unsaturated polyester has the following general formula (I) ▲Mathematical formula, chemical formula, table, etc.▼...(I ) (In the formula, R_1 represents an alkyl group or a cycloalkyl group having 1 to 18 carbon atoms, and R_2 and R_3 represent a hydrogen atom, a halogen atom, a methyl group, or an ethyl group.) resin 10
A method for modifying an unsaturated polyester resin, which comprises adding 0.5 to 100 parts by weight to 0 parts by weight, and curing at room temperature or heating in the presence of a radical polymerization initiator.
JP16605488A 1988-07-05 1988-07-05 Process for modifying unsaturated polyester resin Pending JPH0216113A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16605488A JPH0216113A (en) 1988-07-05 1988-07-05 Process for modifying unsaturated polyester resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16605488A JPH0216113A (en) 1988-07-05 1988-07-05 Process for modifying unsaturated polyester resin

Publications (1)

Publication Number Publication Date
JPH0216113A true JPH0216113A (en) 1990-01-19

Family

ID=15824109

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16605488A Pending JPH0216113A (en) 1988-07-05 1988-07-05 Process for modifying unsaturated polyester resin

Country Status (1)

Country Link
JP (1) JPH0216113A (en)

Similar Documents

Publication Publication Date Title
JPS628444B2 (en)
US4348498A (en) Accelerated hardening of unsaturated polyester resins
JP3572125B2 (en) Curing agent composition for unsaturated polyester resin or vinyl ester resin and curing method
JPH0410488B2 (en)
JPH0216113A (en) Process for modifying unsaturated polyester resin
JP2008144103A (en) Colored curing agent composition, curing method of radical polymerizable thermoset resin, and cured product
JPH0931314A (en) Unsaturated polyester resin composition
JPH1087652A (en) Ketone peroxide composition and curing of unsaturated polyester resin using the same
JPH01272613A (en) Unsaturated polyester resin composition
JP2794802B2 (en) Low shrinkage unsaturated polyester resin composition
JPH08157544A (en) Method for cold curing of unsaturated polyester resin and/or vinyl ester resin and cold curing agent composition
JP3328968B2 (en) Unsaturated polyester resin composition
US5216047A (en) Unsaturated polyester resin composition
JPH02281072A (en) Unsaturated polyester resin composition
US5189094A (en) Process for producing thermoset resin
JP2765090B2 (en) Unsaturated polyester resin composition
JPH07252330A (en) Unsaturated polyester resin composition and its curing method
JPS60240723A (en) Production of pale unsaturated polyester resin
JPH10212331A (en) Peroxide composition
JP2003064114A (en) Curing agent composition, thermosetting resin composition, molded and cured article and method for producing the same
JP2001002718A (en) Hardening agent composition, and method for hardening and hardened product using the same
JP2527505B2 (en) Method for producing unsaturated polyester
JPH07173378A (en) Unsaturated polyester resin composition
JPH0129207B2 (en)
JPH0412745B2 (en)