JPH023413A - Production of solid epoxy resin - Google Patents

Production of solid epoxy resin

Info

Publication number
JPH023413A
JPH023413A JP1016079A JP1607989A JPH023413A JP H023413 A JPH023413 A JP H023413A JP 1016079 A JP1016079 A JP 1016079A JP 1607989 A JP1607989 A JP 1607989A JP H023413 A JPH023413 A JP H023413A
Authority
JP
Japan
Prior art keywords
epoxy resin
acid
molecular weight
anhydride
ethylene
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
JP1016079A
Other languages
Japanese (ja)
Inventor
Piotr Penczek
ピオトル ペンクゼック
Jerzy Rejdych
ジエルジイ レジデイック
Jolanta Janosik
ジョランタ ジャノシック
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.)
INST CHEM PRZEMYSLOWEJ
Original Assignee
INST CHEM PRZEMYSLOWEJ
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 INST CHEM PRZEMYSLOWEJ filed Critical INST CHEM PRZEMYSLOWEJ
Publication of JPH023413A publication Critical patent/JPH023413A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/02Polycondensates containing more than one epoxy group per molecule
    • C08G59/12Polycondensates containing more than one epoxy group per molecule of polycarboxylic acids with epihalohydrins or precursors thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Epoxy Resins (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Paints Or Removers (AREA)

Abstract

PURPOSE: To produce a solid epoxy resin suitable to obtain a mechanically durable and glassy covering agent by heating a specific polyethylene terephthalate and a specific epoxy resin at a specific temperature in the presence of a catalyst.
CONSTITUTION: A solid epoxy resin is produced by heating polyethylene terephthalate with a terminal carboxyl group with an acid value of 60 to 400 mgKOH/g and an epoxy resin of a low molecular weight or a medium molecular weight with an epoxy number of 0.13 to 0.55 mole/100g until the acid value of the product becomes less than 5mgKOH/g at the temperature of 120-180°C in the presence of a catalyst, especially lithium chloride, a tertiary amine, a tetraalkylammonium or benzyltrialkylammonium chloride. Thereby, the epoxy resin is provided which is suitable to obtain a mechanically durable and glassy covering agent.
COPYRIGHT: (C)1990,JPO

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明の目的は低分子量のエポキシ樹脂の鎖長を長くす
ることにより中分子顔および高・分子間の固体エポキシ
樹脂を製造することである。
Detailed Description of the Invention (Industrial Field of Application) The purpose of the present invention is to produce medium-molecular and high-molecular solid epoxy resins by increasing the chain length of low-molecular-weight epoxy resins. .

(従来の技術) エポキシ樹脂の分子量を増加させる方法としては、ジフ
ェノールやグリコール、アミン、ジカルボン酸のような
、活性水素原子を持つ二官能化合物との反応の結果とし
て低分子量および中分子mのエポキシ樹脂の鎖長を長く
する方法が知られている。ジカルボン酸の他に、分子鎖
の両端にカルボキシル基を有する1、4−ブチレングリ
コールとセバシン酸のポリエステルのような脂肪続ポリ
エルテルジカルボン酸が、この目的のために用いらレタ
(Batzer Il、、 Lehse F、、 5c
hn+id R,:Angew、 Hakron+o1
.Chem、 29/30.388/1973/;にr
eibich U、、 Schmid H,: Pro
gr、 CCo11oidPoly、Sci、62.1
06.1977 >。
(Prior art) A method for increasing the molecular weight of epoxy resins is to increase the molecular weight of low and medium molecular weight m as a result of reaction with bifunctional compounds having active hydrogen atoms, such as diphenols, glycols, amines, and dicarboxylic acids. A method of increasing the chain length of epoxy resin is known. Besides dicarboxylic acids, aliphatic polyester dicarboxylic acids such as polyesters of 1,4-butylene glycol and sebacic acid, which have carboxyl groups at both ends of the molecular chain, have been used for this purpose. Lehse F,, 5c
hn+id R, :Angew, Hakron+o1
.. Chem, 29/30.388/1973/;
eibich U, Schmid H: Pro
gr, CCo11oidPoly, Sci, 62.1
06.1977>.

このように形成した1ボキシ樹脂を架橋した後、ゴム状
生成物が得られる。
After crosslinking the 1-boxy resin thus formed, a rubbery product is obtained.

(解決しようとする課題を解決するための手段)現在、
次のことが判明した。即ち、機械的に耐久性のガラス状
被覆剤を得るために適するエポキシ樹脂は、酸価60〜
400ItgKOH/9の末端カルボキシル基を有する
エチレンポリテレフタレートと、エポキシfj60.1
8〜0.55モル/100gの低分子針あるいは中分子
量のエポキシ樹脂とを、触媒を添加し、カルボキシル基
対エポキシ基のモル比を1.5〜3.0にして、生成物
の酸価が54KOH/9未満とするために120〜18
0℃で加熱することにより得られるのである。
(Means for solving the problem to be solved)Currently,
The following was discovered. That is, epoxy resins suitable for obtaining mechanically durable glassy coatings have an acid value of 60 to 60.
Ethylene polyterephthalate with terminal carboxyl groups of 400ItgKOH/9 and epoxy fj60.1
8 to 0.55 mol/100 g of low molecular weight needles or medium molecular weight epoxy resin are added with a catalyst to adjust the molar ratio of carboxyl groups to epoxy groups to 1.5 to 3.0 to increase the acid value of the product. 120 to 18 to make it less than 54KOH/9
It can be obtained by heating at 0°C.

開始成分として、二つの方法のうちの一つにより高分子
量エチレンポリテレフタレートから得られる、カルボキ
シル基を有するニブ・レンボリテレフタレートを用いた
As starting component, carboxyl-containing nib lemboriterephthalate obtained from high molecular weight ethylene polyterephthalate by one of two methods was used.

これらの方法のうちの一つは、高分子かエチレンボリテ
レフタレ−1・を、ジカルボン酸、特にアジピン酸、セ
バシン酸あるいはイソフタル酸と加熱することからなる
One of these methods consists of heating the polymer ethylene boriterephthalate-1 with a dicarboxylic acid, especially adipic acid, sebacic acid or isophthalic acid.

もう一つの方法に従えば、高分子量エチレンポリテレフ
タレートをグリコールとともに加熱し、次に得られたエ
チレンオリゴテレフタレ−1−をジカルボン酸環状無水
物、特にコハク酸、テトラハイドロフタル酸、ヘキサハ
イドロフタル酸、マレイン酸、あるいはフタル酸の無水
物とともに加熱する。
According to another method, high molecular weight ethylene polyterephthalate is heated with glycol and then the resulting ethylene oligoterephthalate is treated with a dicarboxylic acid cyclic anhydride, especially succinic acid, tetrahydrophthalic acid, hexahydrophthalic acid, etc. Heat with acid, maleic or phthalic anhydride.

また、これとは異なった方法で得られる末端カルボキシ
ル基を有するエチレンポリテレフタレートを使用するこ
とも可能である。その、異なった方法とは、低分子針の
出発物質から得る方法であり、例えば、ジメチルテレフ
タレートをtル過剰のグリコールとともに加熱し、そし
て次にジカルボン酸あるいはジカルボン無水物と加熱す
る方法である。
It is also possible to use ethylene polyterephthalate having terminal carboxyl groups obtained by a different method. A different method is to obtain small molecular needle starting materials, such as heating dimethyl terephthalate with an excess of glycol and then heating with a dicarboxylic acid or dicarboxylic anhydride.

末端カルボキシル基を右するエチレンポリテレフタレー
トをエポキシ樹脂とともに加熱している間に、カルボキ
シル基の反応が実際に完了するまで、エステル結合と第
二アルコールの形成を伴なって、カルボキシル基がエポ
キシ基に付加するのがIi!2311された。
While heating the ethylene polyterephthalate with the terminal carboxyl groups together with the epoxy resin, the carboxyl groups convert into epoxy groups with the formation of an ester bond and a secondary alcohol until the reaction of the carboxyl groups is actually completed. Ii to add! 2311 was done.

過剰のエポキシ基は未反応のまま残り、こうして19だ
生成物はエポキシ樹脂型のものであり、典型的なエポキ
シ樹脂硬化剤によって硬化させることができる。
Excess epoxy groups remain unreacted and thus the product is of the epoxy resin type and can be cured by typical epoxy resin curing agents.

本発明に従う方法において、有利には、カルボキシル基
とエポキシ基の反応の触媒を使用し、特に塩化リチウム
、第三アミン、テトラアルキルアンモニウムあるいは塩
化ベンジルトリアルキルアンモニウムが好ましい。
In the process according to the invention, catalysts for the reaction of carboxyl groups with epoxy groups are advantageously used, in particular lithium chloride, tertiary amines, tetraalkylammonium or benzyltrialkylammonium chloride.

例1. 重量比が48:52の高分子量エチレンポリテ
レフタレートとイソフタル酸を、260℃で加熱し、酸
価が17511!FKOH/gの生成物を1qた。次に
、得られた末端カルボキシル基を有するエチレンポリプ
レフタレート100gを、エポキシ1lIio、25モ
ル/100gのジアンエポキシ樹脂エビジアン2 (E
pidian 2 > 250gと共に0.1gのベン
ジルジメチルアミンを添加して加熱した。酸価が1.5
syKOH/g、エポキシ価が0.10モル/100g
および軟化点が125℃のエポキシ樹脂が得られるまで
160℃で加熱した。
Example 1. High molecular weight ethylene polyterephthalate and isophthalic acid in a weight ratio of 48:52 were heated at 260°C, and the acid value was 17,511! 1 q of FKOH/g product was obtained. Next, 100 g of the obtained ethylene polyprephthalate having a terminal carboxyl group was mixed with epoxy 1lIio, 25 mol/100 g of diane epoxy resin Evidian 2 (E
Added 0.1 g of benzyldimethylamine along with pidian 2 > 250 g and heated. Acid value is 1.5
syKOH/g, epoxy value is 0.10 mol/100g
and heated at 160°C until an epoxy resin with a softening point of 125°C was obtained.

例2.゛ 235℃において、高分子fllチレンボリ
テレフタレート1000gとジエヂレングリコール17
5gを加熱し、均一な・液体を得た。次に、温度を20
0℃にまで下げ、162gの無水マレイン酸を添加し、
そしてWI価が961RgKOl−1/Jとなるまで全
体をこの温度で加熱した。温度を140℃に下げた襖、
塩化リチウムo、oigおよびエポキシ価0.5モル/
1009のエポキシ樹1111t’シアン5 (Epi
dian 5 )の875gを加え、次に、酸価2.3
#I!FKOH/g、エポキシ価0.10モルフ100
gおよび軟化魚87℃のエポキシ樹脂が冑られるまで仝
休をこの温度で加熱した。
Example 2.゛ At 235°C, 1000 g of polymeric full ethylene polyterephthalate and 17 dielene glycol
5g was heated to obtain a homogeneous liquid. Next, increase the temperature to 20
The temperature was lowered to 0°C and 162g of maleic anhydride was added.
The whole was then heated at this temperature until the WI value became 961 RgKOl-1/J. Fusuma with a temperature lowered to 140℃,
Lithium chloride o, oig and epoxy value 0.5 mol/
1009 Epoxy Tree 1111t'Cyan 5 (Epi
dian 5) was added, and then the acid value was 2.3.
#I! FKOH/g, epoxy value 0.10 morph 100
The mixture was heated at this temperature until the epoxy resin at 87°C was melted.

Claims (4)

【特許請求の範囲】[Claims] (1)ジカルボン酸を、触媒の存在下に、モル過剰の低
分子量あるいは中分子量のエポキシ樹脂とともに加熱す
ることからなる固体エポキシ樹脂製造方法において、酸
価60〜400mgKOH/gの末端カルボキシル基を
有するエチレンポリテレフタレートとエポキシ価0.1
3〜0.55モル/100gのジアンエポキシ樹脂とを
、可能であれば、触媒、特に塩化リチウム、第三アミン
、テトラアルキルアンモニウムまたは塩化ベンジルトリ
アルキルアンモニウムの存在下で生成物の酸価が5mg
KOH/g未満になるまで120〜180℃で加熱する
ことを特徴とする、前記方法。
(1) A method for producing a solid epoxy resin comprising heating a dicarboxylic acid with a molar excess of a low or medium molecular weight epoxy resin in the presence of a catalyst, which has a terminal carboxyl group with an acid value of 60 to 400 mgKOH/g. Ethylene polyterephthalate and epoxy value 0.1
3 to 0.55 mol/100 g of diane epoxy resin, if possible in the presence of a catalyst, in particular lithium chloride, tertiary amine, tetraalkylammonium or benzyltrialkylammonium chloride, so that the acid number of the product is 5 mg.
The method described above, characterized in that it is heated at 120-180°C until it becomes less than KOH/g.
(2)カルボキシル基1モルに対して1.5〜3.0モ
ルのエポキシ基を使用する、請求項(1)に記載の方法
(2) The method according to claim (1), wherein 1.5 to 3.0 moles of epoxy group are used per mole of carboxyl group.
(3)末端カルボキシル基を有するエチレンポリテレフ
タレートとして、高分子量エチレンポリテレフタレート
とジカルボン酸、特にアジピン酸、セバシン酸あるいは
イソフタル酸とを加熱して得られる生成物を使用する、
請求項(1)または(2)に記載の方法。
(3) As ethylene polyterephthalate having terminal carboxyl groups, a product obtained by heating high molecular weight ethylene polyterephthalate and a dicarboxylic acid, in particular adipic acid, sebacic acid or isophthalic acid, is used;
The method according to claim (1) or (2).
(4)末端カルボキシル基を有するエチレンポリテレフ
タレートとして、高分子量エレチンポリテレフタレート
とグリコールを加熱して得られるエチレンオリゴテレフ
タレートとジカルボン酸の環状無水物、特に、コハク酸
無水物、テトラヒドロフタル酸無水物、ヘキサヒドロフ
タル酸無水物、マレイン酸無水物、あるいはフタル酸無
水物とを加熱して得られる生成物を使用する、請求項(
1)または(2)に記載の方法。
(4) As ethylene polyterephthalate having a terminal carboxyl group, ethylene oligoterephthalate obtained by heating high molecular weight elechin polyterephthalate and glycol and a cyclic anhydride of dicarboxylic acid, especially succinic anhydride and tetrahydrophthalic anhydride , hexahydrophthalic anhydride, maleic anhydride, or phthalic anhydride.
The method described in 1) or (2).
JP1016079A 1988-01-26 1989-01-25 Production of solid epoxy resin Pending JPH023413A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
PL270298 1988-01-26
PL1988270298A PL155390B1 (en) 1988-01-26 1988-01-26 Method of obtaining solid epoxy resins

Publications (1)

Publication Number Publication Date
JPH023413A true JPH023413A (en) 1990-01-09

Family

ID=20040305

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1016079A Pending JPH023413A (en) 1988-01-26 1989-01-25 Production of solid epoxy resin

Country Status (5)

Country Link
JP (1) JPH023413A (en)
DE (1) DE3902311A1 (en)
IT (1) IT1229497B (en)
NL (1) NL8900174A (en)
PL (1) PL155390B1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02274717A (en) * 1989-03-13 1990-11-08 General Electric Co <Ge> Manufacture of polyester/polyepoxide composition having high melt viscosity

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CZ2021507A3 (en) * 2021-11-04 2023-05-17 Synpo, A.S. Epoxy resins

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02274717A (en) * 1989-03-13 1990-11-08 General Electric Co <Ge> Manufacture of polyester/polyepoxide composition having high melt viscosity

Also Published As

Publication number Publication date
DE3902311A1 (en) 1989-08-03
IT1229497B (en) 1991-09-03
NL8900174A (en) 1989-08-16
IT8919142A0 (en) 1989-01-23
PL270298A1 (en) 1989-08-07
PL155390B1 (en) 1991-11-29

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