Claims
- 1. A method of manufacturing a novolak type phenolic resin, which comprises reacting an oxycarboxylic acid selected from the group consisting of tartaric acid, citric acid and a mixture thereof, with an aldehyde, and reacting the resultant reaction product with a phenol.
- 2. The method as claimed in claim 1, wherein the novolak type phenolic resin has a ratio of (a)/(b) which is 0.05 or higher, where (a) is the number of units, with a carboxyl group, --COOH, and an alcoholic hydroxyl group, --OH, in the oxycarboxylic acid being considered to form one unit, multiplied by the number of moles of the oxycarboxylic acid, and (b) is the number of aldehyde groups contained in one molecule of the aldehyde multiplied by the number of moles of the aldehyde.
- 3. The method as claimed in claim 1, wherein the phenol is selected from the group consisting of phenol, cresol, xylenol, bisphenol A, bisphenol F, pyrocatechol, resorcinol, pyrogallol and a mixture of any two or more of these.
- 4. The method as claimed in claim 1, wherein the aldehyde is selected from the group consisting of formaldehyde, paraformaldehyde, trioxane, tetraoxane, benzaldehyde, salicylaldehyde, p-hydroxybenzaldehyde, terephthalaldehyde and a mixture of any two or more of these.
- 5. The method as claimed in claim 1, wherein the novolak type phenolic resin has a ratio of (a)/(b) which is 0.1 to 1.0 where (a) is the number of aldehyde groups contained in one molecule of the aldehyde multiplied by the number of moles of the aldehyde, and (b) is the number of aromatic rings having a hydroxyl group contained in one molecule of the phenol multiplied by the number of moles of the phenol.
- 6. The method as claimed in claim 1, which is conducted in the absence of any catalyst other than the oxycarboxylic acid.
- 7. The method as claimed in claim 1, wherein the novolak type phenolic resin has a molecular weight distribution, Mw/Mn, of 1.88 or less, determined by gel permeation chromatography, where Mw is the weight-average molecular weight and Mn is the number-average molecular weight of the resin by polystyrene conversion.
- 8. The method as claimed in claim 1, wherein the novolak type phenolic resin has a ratio of (a)/(b) which is 0.1 to 0.8 where (a) is the number of aldehyde groups contained in one molecule of the aldehyde multiplied by the number of moles of the aldehyde, and (b) is the number of aromatic rings having a hydroxyl group contained in one molecule of the phenol multiplied by the number of moles of the phenol.
- 9. A method of manufacturing a novolak type phenolic resin, which comprises reacting an oxycarboxylic acid selected from the group consisting of tartaric acid, citric acid and a mixture thereof, with an aldehyde, reacting the resultant reaction product with a phenol, and after completion of the reaction, washing the resultant reaction mixture with water to remove catalyst and dehydrating and concentrating the resultant mixture.
- 10. The method as claimed in claim 9, wherein the novolak type phenolic resin has a ratio of (a)/(b) which is 0.05 or higher, where (a) is the number of units, with a carboxyl group, --COOH, and an alcoholic hydroxyl group, --OH, in the oxycarboxylic acid being considered to form one unit, multiplied by the number of moles of the oxycarboxylic acid, and (b) is the number of aldehyde groups contained in one molecule of the aldehyde multiplied by the number of moles of the aldehyde.
- 11. The method as claimed in claim 9, wherein the phenol is selected from the group consisting of phenol, cresol, xylenol, bisphenol A, bisphenol F, pyrocatechol, resorcinol, pyrogallol and a mixture of any two or more of these.
- 12. The method as claimed in claim 9, wherein the aldehyde is selected from the group consisting of formaldehyde, paraformaldehyde, trioxane, tetraoxane, benzaldehyde, salicylaldehyde, p-hydroxybenzaldehyde, terephthalaldehyde and a mixture of any two or more of these.
- 13. The method as claimed in claim 9, wherein the novolak type phenolic resin has a ratio of (a)/(b) which is 0.1 to 1.0 where (a) is the number of aldehyde groups contained in one molecule of the aldehyde multiplied by the number of moles of the aldehyde, and (b) is the number of aromatic rings having a hydroxyl group contained in one molecule of the phenol multiplied by the number of moles of the phenol.
- 14. The method as claimed in claim 9, which is conducted in the absence of any catalyst other than the oxycarboxylic acid.
- 15. The method as claimed in claim 9, wherein the novolak type phenolic resin has a molecular weight distribution, Mw/Mn, of 1.88 or less, determined by gel permeation chromatography, where Mw is the weight-average molecular weight and Mn is the number-average molecular weight of the resin by polystyrene conversion.
- 16. The method as claimed in claim 9, wherein the novolak type phenolic resin has a ratio of (a)/(b) which is 0.1 to 0.8 where (a) is the number of aldehyde groups contained in one molecule of the aldehyde multiplied by the number of moles of the aldehyde, and (b) is the number of aromatic rings having a hydroxyl group contained in one molecule of the phenol multiplied by the number of moles of the phenol.
Priority Claims (1)
Number |
Date |
Country |
Kind |
7-304989 |
Oct 1995 |
JPX |
|
Parent Case Info
This is a divisional application of Ser. No. 08/571,736 filed Dec. 13, 1995, now pending.
US Referenced Citations (1)
Number |
Name |
Date |
Kind |
5023311 |
Kubota |
Jun 1991 |
|
Foreign Referenced Citations (1)
Number |
Date |
Country |
1-105243 |
Apr 1989 |
JPX |
Divisions (1)
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Number |
Date |
Country |
Parent |
571736 |
Dec 1995 |
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