CN1415640A - Method for preparing line-type bisphenol Aphenolic resin by using aqueous solution process - Google Patents
Method for preparing line-type bisphenol Aphenolic resin by using aqueous solution process Download PDFInfo
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- CN1415640A CN1415640A CN02139389.3A CN02139389A CN1415640A CN 1415640 A CN1415640 A CN 1415640A CN 02139389 A CN02139389 A CN 02139389A CN 1415640 A CN1415640 A CN 1415640A
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- dihydroxyphenyl propane
- distilled water
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- formaldehyde
- phenolic resin
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Abstract
A process for preparing linear biphenol-A phenolic resin by aqueous solution method features that the distilled water is used to replace MIBK solvent, the medium-strong acid or mixed acid is used as catalyst, and the liquid formaldehyde is used to replace solid polyformaldehyde. Its advantages are high output rate, linear structure, less environmental pollution, and low cost.
Description
(1) technical field:
The present invention relates to a kind of preparation method of linear bisphenol A phenolic resin.
(2) background technology:
The synthetic employing of linear bisphenol A phenolic resin (BPA-Novolac is abbreviated as BPN) is solvent method at present.This method adopts methyl iso-butyl ketone (MIBK) (MIBK) as solvent, solid polyformaldehyde, dihydroxyphenyl propane and strongly acidic catalyst (example hydrochloric acid, sulfuric acid etc.) is joined in the solvent together prepare the BPN resin by addition, condensation reaction.The advantage of this synthetic method is that reaction process is controlled easily, can synthesize the BPN resin of higher molecular weight.But this method also has following deficiency: (1) during as industrial production, owing to adopt MIBK as solvent, the cost height, energy consumption is big during recovery; (2) directly all join in the reaction system solid formaldehyde, because formaldehyde has the ability of very strong attack phenyl ring under the strongly acidic catalyst effect, cause probably that four adjacent hydrogen of phenolic hydroxyl group all are substituted in the structure of bisphenol A, form build but not the bisphenol A phenolic resin of line style.
(3) summary of the invention:
The cost height that exists at the synthetic linear bisphenol A phenolic resin of solution method, big, the prepared high deficiency of the linear bisphenol A phenolic resin degree of branching of energy consumption when reclaiming the present invention proposes a kind of method for preparing linear bisphenol A phenolic resin with aqua-solution method.
The present invention is raw materials used distilled water, liquid formaldehyde and middle strong acid or the mixing acid of comprising in preparation.Wherein:
Dihydroxyphenyl propane: liquid formaldehyde (37%)=1: 0.8～1.3 (mol ratios);
Middle strong acid: dihydroxyphenyl propane=10～40: 100 (weight ratios);
Mixing acid: dihydroxyphenyl propane=3～10: 100 (weight ratios);
Dihydroxyphenyl propane: distilled water=100: 100～200 (weight ratio).
During preparation:
(1) dihydroxyphenyl propane, middle strong acid or mixing acid, distilled water are joined in the reaction vessel together and stirs, make it to mix;
(2) water-bath is heated to 60 ℃～100 ℃, be incubated and begin and add liquid formaldehyde with the mode that drips;
(3) after the dropping liquid formaldehyde finishes, continue insulation reaction, until reaching required molecular weight;
(4) after reaction finishes, with the mixed solution sucking-off of middle strong acid or mixing acid and distilled water, so that recycle;
(5) reaction product distilled water wash, and add the sodium bicarbonate neutralization, last vacuum-drying obtains faint yellow transparent solid---linear bisphenol A phenolic resin.
By the BPN resin of method for preparing, its productive rate can reach 103%～110% of BPA consumption.Liquid-phase chromatographic analysis shows that residual BPA content is 10%～20%.Gel permeation chromatography (GPC) analysis revealed, the Mw of aqua-solution method synthetic linear bisphenol A phenolic resin reaches as high as 2800, and its molecular weight dispersion coefficient is between 1.2～2.4.
The present invention adopts (1) distilled water to replace the MIBK solvent, can reduce environmental pollution like this, reduces cost; (2) adopt liquid formaldehyde to replace solid polyformaldehyde, and reinforced with the mode that drips, can make in the reaction system, content of bisphenol A is excessive greatly, guarantees to form linear structure; (3) strong acid or mixing acid guarantee that as catalyzer the color and luster of product is more shallow in the employing; (4) mixed solvent can recycle after reaction finishes.
(4) description of drawings:
Accompanying drawing 1 is a line style BPA-Novolac molecular structure;
Accompanying drawing 2 is build BPA-Novolac molecular structures.
(5) embodiment:
Embodiment one:
With dihydroxyphenyl propane, distilled water, phosphoric acid, liquid formaldehyde, sodium bicarbonate preparation preparation linear bisphenol A phenolic resin, its batching is:
Dihydroxyphenyl propane 0.5mol (114.3 gram)
Distilled water 114.3 grams
Phosphoric acid (85%) 26.9 gram
Liquid formaldehyde (37%) 40.5 gram
Sodium bicarbonate 5 grams
The preparation method:
Raw material dihydroxyphenyl propane, phosphoric acid and distilled water are joined in the there-necked flask of the 500ML that thermometer, agitator and constant pressure funnel are housed by proportioning, formaldehyde is joined in the constant pressure funnel.Starting agitator mixes dihydroxyphenyl propane, phosphoric acid and distilled water.Temperature is risen to 85 ± 2 ℃ then, begin to drip formaldehyde, the dropping time is 5 hours.Continue reaction 6 hours, stopped reaction is poured out reaction solution, so that recycle.Add distilled water and sodium bicarbonate then, washed product, until neutrality, and under 100 ℃, vacuum-drying under the 500mmHg, products obtained therefrom is faint yellow transparent solid thing.
Product performance:
Mw=1754.3 Mn=971.06 Pd=1.806 (test of GPC method)
The residual BPA=14.80% of productive rate=105.6% (in BPA) (liquid phase chromatography test)
Softening temperature=113 ℃ (ring and ball method test) hydroxyl equivalent (g/eq)=126.2 (potentiometric titration)
Embodiment two:
With dihydroxyphenyl propane, distilled water, boric acid, sulfuric acid, liquid formaldehyde preparation preparation linear bisphenol A phenolic resin, its batching is:
Dihydroxyphenyl propane 0.5mol (114.3 gram)
Distilled water 114.3 grams
Boric acid 2 grams
Sulfuric acid (98%) 1.5 gram
Liquid formaldehyde (37%) 40.5 gram
Sodium bicarbonate 4 grams
The preparation method:
Raw material dihydroxyphenyl propane, the vitriol oil, boric acid and distilled water are joined in the there-necked flask of the 500ML that thermometer, agitator and constant pressure funnel are housed by proportioning, formaldehyde is joined in the constant pressure funnel.Starting agitator mixes dihydroxyphenyl propane, the vitriol oil, boric acid and distilled water.Temperature is risen to 75 ± 2 ℃ then, begin to drip formaldehyde, the dropping time is 3 hours.Continue reaction 5 hours, stopped reaction is poured out reaction solution, so that recycle.Add distilled water and sodium bicarbonate then, washed product, until neutrality, and under 100 ℃, vacuum-drying under the 500mmHg, products obtained therefrom is faint yellow transparent solid thing.Product performance: Mw=1404.6 Mn=893.22 Pd=1.5726 (test of GPC method) the residual BPA=11.40% of productive rate=103.4% (in BPA) (liquid phase chromatography test) softening temperature=98 ℃ (ring and ball method test) hydroxyl equivalent (g/eq)=129.41 (potentiometric titration).
Claims (3)
1. a method for preparing linear bisphenol A phenolic resin is synthesized with solvent, formaldehyde, dihydroxyphenyl propane, catalyzer, it is characterized in that:
A. make solvent with distilled water;
B. used formaldehyde is liquid formaldehyde;
C. catalyzer is middle strong acid or mixing acid; During preparation:
A. dihydroxyphenyl propane, middle strong acid or mixing acid, distilled water are added in the reaction vessel and stir;
B. water-bath is heated, under keeping warm mode, add liquid formaldehyde with the mode that drips;
C. insulation reaction is to reaching required molecular weight;
D. reaction finishes the mixed solution of back sucking-off acid and distilled water;
E. use the distilled water wash reactant, and the adding sodium bicarbonate is neutralized to neutrality;
F. vacuum-drying.
2. the method for preparing linear bisphenol A phenolic resin according to claim 1 is characterized in that the proportioning of dihydroxyphenyl propane, liquid formaldehyde and middle strong acid or mixing acid is:
Dihydroxyphenyl propane: liquid formaldehyde (37%)=1: 0.8～1.3 (mol ratios);
Middle strong acid: dihydroxyphenyl propane=10～40: 100 (weight ratios);
Mixing acid: dihydroxyphenyl propane=3～10: 100 (weight ratios);
Dihydroxyphenyl propane: distilled water=100: 100～200 (weight ratio).
3. the method for preparing linear bisphenol A phenolic resin according to claim 1 is characterized in that bath temperature is 60 ℃-100 ℃,
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN02139389.3A CN1269862C (en) | 2002-08-28 | 2002-08-28 | Method for preparing line-type bisphenol Aphenolic resin by using aqueous solution process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN02139389.3A CN1269862C (en) | 2002-08-28 | 2002-08-28 | Method for preparing line-type bisphenol Aphenolic resin by using aqueous solution process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1415640A true CN1415640A (en) | 2003-05-07 |
| CN1269862C CN1269862C (en) | 2006-08-16 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN02139389.3A Expired - Lifetime CN1269862C (en) | 2002-08-28 | 2002-08-28 | Method for preparing line-type bisphenol Aphenolic resin by using aqueous solution process |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101538354B (en) * | 2009-04-14 | 2012-08-22 | 天津市职业大学 | Method for utilizing synthesized aspirin waste liquid to prepare water soluble phenol resin |
| CN102137880B (en) * | 2008-09-01 | 2013-02-20 | 可隆工业株式会社 | Novolac and epoxy resin composition |
| CN103626941A (en) * | 2013-11-01 | 2014-03-12 | 南通星辰合成材料有限公司 | Bisphenol a modified phenolic resin and preparation method thereof |
| CN107353377A (en) * | 2017-08-09 | 2017-11-17 | 山东圣泉新材料股份有限公司 | A kind of phenolic resin and preparation method thereof |
| CN108948299A (en) * | 2018-08-17 | 2018-12-07 | 陕西科技大学 | A kind of bisphenol A formaldehyde phenolic resin and its synthetic method |
-
2002
- 2002-08-28 CN CN02139389.3A patent/CN1269862C/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102137880B (en) * | 2008-09-01 | 2013-02-20 | 可隆工业株式会社 | Novolac and epoxy resin composition |
| CN103012742B (en) * | 2008-09-01 | 2014-06-25 | 可隆工业株式会社 | Phenol novolac epoxy resin and epoxy resin composition |
| CN101538354B (en) * | 2009-04-14 | 2012-08-22 | 天津市职业大学 | Method for utilizing synthesized aspirin waste liquid to prepare water soluble phenol resin |
| CN103626941A (en) * | 2013-11-01 | 2014-03-12 | 南通星辰合成材料有限公司 | Bisphenol a modified phenolic resin and preparation method thereof |
| CN103626941B (en) * | 2013-11-01 | 2016-01-20 | 南通星辰合成材料有限公司 | Bisphenol a modified phenolic resin and preparation method thereof |
| CN107353377A (en) * | 2017-08-09 | 2017-11-17 | 山东圣泉新材料股份有限公司 | A kind of phenolic resin and preparation method thereof |
| CN108948299A (en) * | 2018-08-17 | 2018-12-07 | 陕西科技大学 | A kind of bisphenol A formaldehyde phenolic resin and its synthetic method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1269862C (en) | 2006-08-16 |
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Owner name: HONGCHANG ELECTRONIC MATERIALS CO., LTD.; NORTHWES Free format text: FORMER NAME OR ADDRESS: HONGCHANG ELECTRONIC MATERIAL INUSTRY CO., LTD., GUANGZHOU; NORTHWESTERN POLYTECHNICAL UNIVERSITY |
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Address after: No. 1, Yun Po Road, Yun Po Industrial Zone, Luo Gang Town, Guangzhou City, Guangdong Province, zip code: 510530 Co-patentee after: Northwestern Polytechnical University Patentee after: EPOXY BASE ELECTRONIC MATERIAL Corp.,Ltd. Address before: No. 1, Yun Po Road, Yun Po Industrial Zone, Luo Gang Town, Guangzhou City, Guangdong Province, zip code: 510530 Co-patentee before: Northwestern Polytechnical University Patentee before: HONGCHANG ELECTRONIC MATERIAL |
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Granted publication date: 20060816 |