CN1091452C - Preparation method of phenolic epoxy resin curing agent - Google Patents

Preparation method of phenolic epoxy resin curing agent Download PDF

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Publication number
CN1091452C
CN1091452C CN99115656A CN99115656A CN1091452C CN 1091452 C CN1091452 C CN 1091452C CN 99115656 A CN99115656 A CN 99115656A CN 99115656 A CN99115656 A CN 99115656A CN 1091452 C CN1091452 C CN 1091452C
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China
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acid
catalyst
curing agent
manufacture method
formaldehyde
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Expired - Fee Related
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CN99115656A
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CN1252412A (en
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陈湘
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China Petrochemical Corp
Baling Petrochemical Co Ltd
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YUEYANG PETROCHEMICAL GENERAL
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  • Phenolic Resins Or Amino Resins (AREA)
  • Epoxy Resins (AREA)

Abstract

The invention discloses a method for preparing a phenolic aldehyde type epoxy resin curing agent, which takes dialdehyde A and formaldehyde as raw materials, the molar ratio of the dialdehyde A to the formaldehyde is 1: 0.2-3.2, an acid catalyst is added in batches in a solvent accounting for 25-400% of the total amount of the dialdehyde A and the formaldehyde, the total amount of the acid catalyst is 0.5-2.5% of the weight of bisphenol A, and the reaction is carried out at the temperature of 45-120 ℃ for 2-10 hours to prepare the curing agent with the average molecular weight of 400-2000 and the residual amount of the bisphenol A of 10-20%. The curing agent can solve the problems of poor heat resistance, insufficient curing, poor stability of resin varnish and the like of curing agent resin, has the advantages of good compatibility with epoxy resin, easy mixing, good heat resistance of cured products, high strength and the like, and is widely applicable to epoxy resin curing agents, particularly epoxy copper clad laminates.

Description

A kind of manufacture method of phenol aldehyde type epoxy resin curing agent
The present invention relates to a kind of manufacture method of phenol aldehyde type epoxy resin curing agent, especially a kind of manufacture method that is used for epoxy copper clad laminate and other material layers pressing plate usefulness epoxy curing agent.
In the prior art, seldom relevant for the report of BPA type epoxy curing agent (BPA-novolak) synthetic method, only in Japanese Patent JP61072018, mention with phenol, BPA, 37% formalin synthetic epoxy hardener, be used to solidify bromination BPA Resins, epoxy and make coating foil multilayer layer pressing plate, in Japanese Patent JP61069828, reported synthetic tetra methylol BPA under alkaline condition, under acidic conditions, made epoxy hardener again with the phenol condensation with BPA, 37%HCHO.Epoxy copper clad laminate and other material layers pressing plate mostly are Dyhard RU 100 and the linear phenolic aldehyde of phenol with epoxy curing agent, when veneer sheet is made, usually be dissolved in Resins, epoxy and solidifying agent thereof in the organic solvent such as butanone, add curing catalyst, become epoxy resin varnish, then, this resinous varnish be impregnated in woven fiber glass, make solvent evaporates with the moisture eliminator evaporation again, become semicure impregnation thing, this semicure impregnation thing is added to certain number of plies, the folded at last Copper Foil of going up, under pressurized conditions, heating makes it to solidify, and the lamination veneer sheet that obtains like this carries out machine drill again and is processed into printed circuit board (PCB).In veneer sheet manufacturing technology field, require resin solidification (being activity of curing reaction), cured resin thermotolerance, the stability of the boring processibility of veneer sheet, wet fastness, electrical specification and form and aspect stability thereof, resinous varnish etc. are all good.When being solidifying agent with Dyhard RU 100, do not have problems for machine drill processibility, form and aspect stability and the electrical specification of veneer sheet, but stable not good enough (pot life is short) of cured resin poor heat resistance, resinous varnish; Poor because of Resins, epoxy and Dyhard RU 100 intermiscibility, exist semicure impregnation thing that whiting is arranged, curing can not fully wait defective.When using phenol novolak,, and directly influence quality product, can not obtain the cured article of excellent property also owing to the reason that has free-phenol in the product causes form and aspect stability extreme difference as solidifying agent, thus cause circuit card scrap or influence work-ing life.
The object of the present invention is to provide a kind of manufacture method of phenol aldehyde type epoxy resin curing agent, solidifying agent that makes by this method and Resins, epoxy have good intermiscibility, easily evenly do not have solidifying agent with mixed with resin and separate out phenomenon, improve resin crosslinks density simultaneously, to improve the performance of cured article, particularly improve thermotolerance and wet fastness.
In order to achieve the above object, the present invention has adopted following technological method: be 1: 0.2~3.2 ratio in the mol ratio of dihydroxyphenyl propane and formaldehyde, add weight and be in 25%~400% the solvent of the two total amount, 0.5%~2.5% an acidic catalyst that adds dihydroxyphenyl propane weight in batches, catalyzer is an organic acid, mineral acid, Lewis acid, the mixture of a kind of or its any several arbitrary proportions of storng-acid cation exchange resin or solid acid, reaction is 2 hours~10 hours under 45 ℃~120 ℃ temperature, leave standstill, layering, get the upper strata light liquid, neutralization, washing, at PH is intensification in 6~7 o'clock, remove solvent, getting molecular-weight average is 400~2000, contains the solidifying agent product of residual dihydroxyphenyl propane weight 10%~20%.
In the invention process process, technical scheme can be preferably: formaldehyde can be the formalin solution of Paraformaldehyde 96, trioxymethylene or 37%.Solvent can be low-grade carboxylic acid's classes such as formic acid, acetate, propionic acid; Lower alcohols such as methyl alcohol, ethanol, Virahol; Toluene, ethylbenzene, dimethylbenzene etc. are aromatic hydrocarbon based; Ketones such as ketone, butanone, methyl iso-butyl ketone (MIBK); Ethers such as diox, diisopropyl ether; One or more mixtures of halogenated hydrocarbons such as chloroform, chlorobenzene, Ethylene Dichloride or the like these compounds with arbitrary proportion, the usage quantity of solvent is about 1/3-10 doubly with respect to BPA, and the ideal usage quantity is 1/2-5 times.
In implementing process of the present invention, technical scheme can also be preferably: 1 mole of BPA is better in conjunction with 0.2~3.2 moles of formaldehyde, when exceeding this scope, the resinous varnish poor stability, and when F/P>3.2, molecular-weight average is too high, descends with the Resins, epoxy intermiscibility; When F/P<0.2, unreacted BPA too high levels in the product, and molecular-weight average is low excessively, causes the cured article thermotolerance to reduce.Catalyst levels is 0.5%~2.5% with respect to the BPA usage quantity, if catalyst levels is lower than 0.5%, speed of response is slower, causes molecular weight on the low side, and unreacted BPA content is higher; If catalyst levels is higher than 2.5%, speed of response is too fast, causes molecular weight higher, and product and Resins, epoxy intermiscibility are poor.
Solidifying agent (BPA-novolak) average molecular mass Mn=400-2000 that the present invention makes, relatively poor with resistance toheat behind the epoxy resin cure when Mn<400, when Mn>2000, with the intermiscibility variation of Resins, epoxy.Unreacted BPA content is lower than 20% among the BPA-novolak of manufacturing of the present invention, if be higher than this scope, then the resistance toheat of cured article descends, and other is all influential such as electric property and intensity.In actual manufacturing processed, reaction times is 2 hours~10 hours, utilize the gel chromatography analyser to survey molecular weight in the reaction and control reaction end, molecular weight reaches 400 and gets final product termination reaction when above, molecular weight was at 400~2000 o'clock, and the residual dihydroxyphenyl propane in the product is correspondingly in 10%~20% scope.
The present invention's technical scheme preferably can be again: an acidic catalyst is organic acids such as oxalic acid, Whitfield's ointment, formic acid, acetate and toluenesulphonic acids; Mineral acids such as hydrochloric acid, rare nitric acid, dilute sulphuric acid, phosphoric acid; Lewis acids such as aluminum chloride, tin chloride, boron trifluoride; Polystyrene, the allylic storng-acid cation exchange resin SK1-B of diethyl, RCP1SOH etc.; A kind of or any several mixtures in these compounds of solid acid such as mordenite, pure aluminium silicate with arbitrary proportion.In fact, available catalyzer of the present invention is a lot of, so long as tart, general equal can the employing.
Compared with prior art, the present invention has following tangible advantage:
1, product of the present invention and Resins, epoxy have good intermiscibility, do not separate out phenomenon so easily evenly do not have solidifying agent with mixed with resin;
2, phenyl ring density height in the molecule of product of the present invention has increased its molecular rigidity, and the thermotolerance of cured article and intensity are increased;
3, this invention products molecule contain great amount of hydroxy group can with epoxy reaction, thereby improve the cross-linking density of resin solidification, make the every performance of epoxy resin cured product especially physical and mechanical properties have obvious improvement.
4, can reach under the situation that molecular weight product of the present invention is lower that to be lower than 20% monomers B PA residual.
Below by specific embodiment the present invention is carried out more detailed description:
Embodiment 1
With BPA228.3g (1mol), 50% formaldehyde 60g (0.9mol) adds in the flask with four necks,round bottom, and on flask, load onto agitator, thermometer, reflux exchanger, in system, add toluene 65g again, the stirring that heats up makes the reactant homodisperse and dissolves half an hour, and temperature maintenance adds the 1.1415g toluenesulphonic acids then at 80 ℃, maintain 80 ℃ of reactions 1 hour, add the 1.1415g toluenesulphonic acids again and keep 80 ℃ of reaction 1h, after adding the 1.1415g toluenesulphonic acids for the third time and keeping 80 ℃ of reaction 1h, in system, add toluene 325g, pure water 200g, fully stirring stops after 20 minutes stirring, and leaves standstill 30 minutes, removes sub-cloud heavy-fluid, pure water 200g will be added in the light liquid, NaOH is an amount of, stirs evenly the back and surveys its pH value, when PH=7, static 30 minutes, divide and go heavy-fluid, light liquid intensification desolventizing, temperature reaches 200 ℃, pressure reaches-removal pressure during 0.1MPa, product is poured out from still, and naturally cooling obtains 237g light yellow solid product.
Embodiment 2~12 working method are with example 1, and processing condition, raw material ratio and test result see Table 1.Table 1
Embodiment F/P Catalyst type and consumption (%) Reaction times (hour) Temperature of reaction (℃) Mn BPA%
1 0.9 E 1.5 3 80 717 17.68
2 0.7 J 1.0 3 60 502 10.79
3 0.4 F 0.5 10 80 615 15.06
4 0.85 M 0.5 5 90 832 16.92
5 1.20 A 0.5+N 0.5 8 75 1015 13.02
6 0.65 O 0.5+I 1.0 3 100 934 17.08
7 0.25 A 0.5+P 1.0 4 110 410 18.72
8 3.0 E 1.5+P 1.0 2 115 854 13.68
9 0.2 B 1.3+L 0.8 4 118 440 18.59
10 1.8 C 1.0+G 1.2 6 95 890 17.42
11 3.2 D 1.0+H 1.0 7 85 997 18.96
12 2.4 K 1.2+B 1.2 3 48 405 19.32
Annotate: 1, A represents that oxalic acid, B represent that Whitfield's ointment, C represent that formic acid, D represent that acetate, E represent that toluenesulphonic acids, F represent that hydrochloric acid, the rare nitric acid of G, H represent that dilute sulphuric acid, I represent that phosphoric acid, J represent that aluminum chloride, K represent that boron trifluoride, L represent that tin chloride, M represent that SK1-B, N represent that RCP1SOH, O represent that mordenite, P represent pure aluminium silicate in the table
2, catalyst levels in the table, its percentage composition is a radix with the dihydroxyphenyl propane consumption.

Claims (6)

1, a kind of manufacture method of phenol aldehyde type epoxy resin curing agent, with dihydroxyphenyl propane and formaldehyde is raw material, under catalyst action, reacting by heating in solvent, remove solvent, the invention is characterized in: 1. the mol ratio of dihydroxyphenyl propane and formaldehyde is 1: 0.2~3.2, and the add-on of solvent is 25%~400% of dihydroxyphenyl propane and a formaldehyde total amount; 2. add an acidic catalyst, its consumption is 0.5%~2.5% of a dihydroxyphenyl propane weight, and an acidic catalyst is the mixture of a kind of or its any several arbitrary proportions of organic acid, mineral acid, Lewis acid, storng-acid cation exchange resin or solid acid; 3. add an acidic catalyst in batches under 45 ℃~120 ℃ temperature, reacted 2 hours~10 hours, leave standstill, the upper strata light liquid is got in layering, neutralization, washing; 4. be intensification in 6~7 o'clock, remove solvent at PH, get average molecular mass Mn=400~2000, contain the solidifying agent product of residual dihydroxyphenyl propane weight 10%~20%.
2, manufacture method according to claim 1 is characterized in that organic acid catalyst is oxalic acid, Whitfield's ointment, formic acid, acetate and toluenesulphonic acids.
3, the described manufacture method of claim 1 is characterized in that inorganic acid catalyst is hydrochloric acid, rare nitric acid, dilute sulphuric acid and phosphoric acid.
4, require 1 described manufacture method, it is characterized in that lewis acid catalyst is aluminum chloride, boron trifluoride and tin chloride.
5, the described manufacture method of claim 1 is characterized in that cation exchange resin catalyst is allylic storng-acid cation exchange resin SK1-B of polystyrene, diethyl and RCPISOH.
6, manufacture method according to claim 1 is characterized in that solid acid catalyst is mordenite and pure aluminium silicate.
CN99115656A 1999-11-26 1999-11-26 Preparation method of phenolic epoxy resin curing agent Expired - Fee Related CN1091452C (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103506171B (en) * 2012-06-15 2015-11-25 华东理工大学 Modification acid cation exchange resin and uses thereof

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3862260A (en) * 1973-05-07 1975-01-21 Union Carbide Corp Epoxy curing system
JPS57185317A (en) * 1981-05-11 1982-11-15 Hitachi Ltd Epoxy resin composition
JPS58124640A (en) * 1982-01-20 1983-07-25 日立化成工業株式会社 Epoxy resin copper lined laminated board
JPS61243821A (en) * 1985-04-23 1986-10-30 Hitachi Chem Co Ltd Epoxy resin composition for sealing semiconductor
JPH04227624A (en) * 1990-03-27 1992-08-17 Sumitomo Durez Co Ltd Epoxy resin curing agent and epoxy resin composition
JPH08283656A (en) * 1995-04-13 1996-10-29 Mitsui Petrochem Ind Ltd Solid epoxy resin composition for rapidly curable powder coating
EP0835892A1 (en) * 1995-06-27 1998-04-15 Hitachi Chemical Co., Ltd. Epoxy resin composition for printed wiring board and laminated board produced with the use of the same
JPH11181239A (en) * 1997-12-25 1999-07-06 Hitachi Chem Co Ltd Epoxy resin composition, epoxy resin prepreg and metal foil laminated plate

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3862260A (en) * 1973-05-07 1975-01-21 Union Carbide Corp Epoxy curing system
JPS57185317A (en) * 1981-05-11 1982-11-15 Hitachi Ltd Epoxy resin composition
JPS58124640A (en) * 1982-01-20 1983-07-25 日立化成工業株式会社 Epoxy resin copper lined laminated board
JPS61243821A (en) * 1985-04-23 1986-10-30 Hitachi Chem Co Ltd Epoxy resin composition for sealing semiconductor
JPH04227624A (en) * 1990-03-27 1992-08-17 Sumitomo Durez Co Ltd Epoxy resin curing agent and epoxy resin composition
JPH08283656A (en) * 1995-04-13 1996-10-29 Mitsui Petrochem Ind Ltd Solid epoxy resin composition for rapidly curable powder coating
EP0835892A1 (en) * 1995-06-27 1998-04-15 Hitachi Chemical Co., Ltd. Epoxy resin composition for printed wiring board and laminated board produced with the use of the same
JPH11181239A (en) * 1997-12-25 1999-07-06 Hitachi Chem Co Ltd Epoxy resin composition, epoxy resin prepreg and metal foil laminated plate

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