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Narrowly-dispersed phenol-phenolic varnish resin preparation method and narrowly-dispersed phenol-phenolic varnish resin obtained by means of the preparation method

A technology of phenol novolac and manufacturing method, which is applied in the direction of coating, etc., can solve the problems of deterioration of productivity, increase of process, and inability to obtain phenol novolac resin, etc., and achieve the beneficial effects of small environmental burden and cost reduction

Active Publication Date: 2015-10-28
KUKDO CHEM CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Therefore, as a method for producing a narrowly dispersed phenol novolac resin with a low dinuclear content, it has been proposed that after the reaction, dinuclear bodies are extracted using hot water (Patent Document 1), adding a slightly soluble solvent, and then add water-soluble alcohol and water to remove the method of low nucleosomes (Patent Document 2), etc., but these methods do not show the effective use of the removed dinuclear bodies, so as a result, waste relative to phenol novolac Dinuclear component of about 20% by mass in varnish resin
In addition, a method is disclosed in which a phenol novolac resin is synthesized by first resolizing phenols and aldehydes using a basic catalyst, and then adding phenols and an acidic catalyst for novolakization, However, the process is complicated, and the reduction of dinuclear bodies is not sufficient (Patent Document 3)
In addition, a method is disclosed in which a phenol novolak resin is synthesized by condensation reaction of phenols and aldehydes using a hydroxycarboxylic acid having a carboxyl group and an alcoholic hydroxyl group in one molecule as a catalyst, but the decrease in dinuclear body Insufficient and causes a problem of residual catalyst (Patent Document 4)
Furthermore, a production method is also disclosed in which a monomer and a catalyst are added to a phenol novolak resin, and a high molecular weight body of the phenol novolac resin is decomposed by heat treatment to cause low molecular weight and narrow dispersion, thereby obtaining a narrow dispersion Phenol novolak resin, but the yield is very poor, about 10%, not practical (Patent Document 5)
In addition, the following production method has been proposed, wherein, using the process of distilling bisphenol F to obtain high-purity bisphenol F, the distillation residue is directly made into phenol novolak resin, or further polymerized to produce high-molecular phenol novolac Varnish resin, or the production method of general-purpose bisphenol F obtained by mixing crude bisphenol F before recovery with high-purity bisphenol F, but compared with each independent production method, the number of steps increases and the productivity deteriorates significantly. , general-purpose bisphenol F also contains a lot of high molecular weight bodies and has a bad influence on physical properties, or it is impossible to obtain phenol novolac resins with the same molecular weight distribution as general phenol novolac resins. In addition, those with few dinuclear bodies The production of phenol novolac resin is determined by the production of high-purity bisphenol F, and there are many problems in actual production (Patent Document 6)

Method used

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  • Narrowly-dispersed phenol-phenolic varnish resin preparation method and narrowly-dispersed phenol-phenolic varnish resin obtained by means of the preparation method
  • Narrowly-dispersed phenol-phenolic varnish resin preparation method and narrowly-dispersed phenol-phenolic varnish resin obtained by means of the preparation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0067] (preparation process)

[0068] In a stirred tank type reactor equipped with a stirrer, a temperature regulator, a reflux condenser, a total condenser, a decompression device, etc., add 100 parts of bisphenol F and 600 parts of phenol were heated up to 80° C., then 1.55 parts of oxalic acid dihydrate was added, stirred and dissolved for 10 minutes, and 115 parts of 37.5% formalin were added dropwise over 30 minutes. Thereafter, the reaction was continuously performed for 3 hours while maintaining the reaction temperature at 92°C. After the reaction was terminated, the temperature was increased to 110°C for dehydration, and about 90% of the residual phenol was recovered under the recovery conditions of 150°C and 60mmHg, then recovered under the recovery conditions of 160°C and 5mmHg, and then further recovered at 160°C 10 parts of water were dripped over 90 minutes under conditions of C and 80 mmHg to remove residual phenol, and a crude phenol novolac resin was obtained....

Embodiment 2

[0073] (preparation process)

[0074] 210 parts of evaporated components obtained in Example 1 were used as bisphenol F, 680 parts of phenol, 1.78 parts of oxalic acid dihydrate, and 115 parts of 37.5% formalin. Exactly the same operation as in Example 1 was performed to obtain a crude phenol novolac resin. Regarding the composition of the obtained crude phenol novolak resin, the amount of 2-nuclear bodies is 52.8 area%, the amount of 3-nuclei bodies is 25.0 area%, the amount of 4-nuclei bodies is 12.7 area%, the amount of 5-nuclei bodies is 5.2 area%, and the amount of 6-nuclei bodies is 5.2 area%. The content above the bulk was 4.3 area%, Mw was 347, and the degree of dispersion (Mw / Mn) was 1.192.

[0075] (distillation process)

[0076] The obtained crude phenol novolac resin was continuously supplied at 10 kg / h to the centrifugal thin film evaporator used in Example 1 for 1 hour, and the evaporated components and phenol novolac resin were continuously extracted. Regardi...

Embodiment 3

[0079] (preparation process)

[0080] 25 parts of evaporated components obtained in Example 2 were used as bisphenol F, phenol was changed to 600 parts, oxalic acid dihydrate was changed to 1.25 parts, and 37.5% formalin was changed to 170 parts. Exactly the same operation as in Example 1 was performed to obtain a crude phenol novolac resin. Regarding the composition of the obtained crude phenol novolak resin, the amount of 2-nuclei was 38.0 area%, the amount of 3-nuclei was 24.5 area%, the amount of 4-nuclei was 20.4 area%, the amount of 5-nuclei was 9.3 area%, and the amount of 6-nuclei was 9.3% by area. The content above the bulk was 7.8 area%, Mw was 403, and the degree of dispersion (Mw / Mn) was 1.195.

[0081] (distillation process)

[0082] To the centrifugal thin-film evaporator used in Example 1, the obtained crude phenol novolak resin was continuously supplied at 31 kg / h, and the evaporated components and phenol novolak resin were continuously extracted. Regarding ...

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Abstract

The invention provides a narrowly-dispersed phenol-phenolic varnish resin preparation method, and the narrowly-dispersed phenol-phenolic varnish resin which is narrow in molecular weight distribution, and takes phenols and aldehydes as raw materials is obtained in high yield. The narrowly-dispersed phenol-phenolic varnish resin preparation method is characterized by comprising following steps of (a) adding phenol and formaldehyde into bisphenol F with the amount of two nuclear bodies being detected to be more than 85 % by area by means of gel permeation chromatography, reacting the above materials in the presence of acid catalyst, and removing acid catalyst, water and unreacted phenol in the obtained reaction product, and obtaining a rough phenol-phenolic varnish resin; (b) removing evaporation component taking the dicaryon as the main component from the rough phenol-phenolic varnish resin by means of a distillation operation, and obtaining a narrowly-dispersed phenol-phenolic varnish resin with the amount of two nuclear bodies being detected to be lower than 20 % by area by means of gel permeation chromatography, and the amount of high molecular weight bodies of more than six nuclear bodies being detected to be lower than 12 % by area by means of gel permeation chromatography.

Description

technical field [0001] The present invention relates to a method for producing a narrowly dispersed phenol novolac resin and the narrowly dispersed phenol novolak resin obtained by the production method. Background technique [0002] Phenol novolac resin has excellent properties as an organic or inorganic substrate bonding material, and is used as a curing agent for epoxy resin compositions for sealing semiconductor devices such as semiconductor elements such as ICs and LSIs, or for heat resistance, Resins for molding materials with excellent electrical insulation properties. With regard to the market trend of electronic equipment in recent years, miniaturization, weight reduction, and high performance are progressing, and in response to this market trend, high integration of semiconductor elements is being carried out year by year. In addition, the surface mounting of semiconductor devices is being promoted. In the high integration of semiconductor elements, the size of se...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G8/10C09D161/06
Inventor 申泰圭李镇洙宅和成刚宫崎徹野弘树吉村康男
Owner KUKDO CHEM CO LTD
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