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US4137220A Expired / Lapsed US ⏱️ 0.0 years remaining

Preparation of novolak epoxy resins

Assignee: Societa Italiana Resine SpA SIR
•
Filing: 1976-12-06
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Granted: 1979-01-30
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Expires: 1996-12-06
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Abstract

Abstract A Novolak epoxy resin is prepared by adding an aqueous solution of alkali metal hydroxide to a solution of Novolak phenolic resin in epichlorohydrin, distilling off water during said addition in the form of an azeotrope with epichlorohydrin and recycling the latter, while maintaining the reaction medium at 60-80° C and at a pH between 7 and 8 and a water content of from 0.5 to 2.5 wt.% in said medium. The thermosetting resin thus obtained can be used in applications requiring resins with low chlorine contents, low viscosity and high epoxy value.

Inventors

  • 👤 Giorgio Lazzerini
  • 👤 Silvio Vargiu
  • 👤 Mario Pitzalis

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 11:09
CPC Classifications
C; C08; C08G; C08G59/00; C08G59/02; C08G59/04; C08G59/06; C08G59/08

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 199 words
A method for the preparation of a Novolak epoxy resin, which comprises: (a) gradually feeding an aqueous solution of alkali metal hydroxide into a solution in epichlorohydrin of a Novolak phenolic resin definable by the general formula: ##STR3## where the average value of n is from 0 to 5, the ratio between the moles of epichlorohydrin and the number of phenolic hydroxyl groups in said epychlorohydrin solution being from 2.5:1 to 12:1, until the number of moles of alkali metal hydroxide fed in is substantially equivalent to the number of phenolic hydroxyl groups present in said epichlorohydrin solution, while maintaining the reaction medium at boiling point and at a temperature of from 60° to 80° C., distilling off water in the form of an azeotropic mixture with epichlorohydrin and recycling the distilled epichlorohydrin into the reaction medium, the addition of alkali metal hydroxide and the distillation conditions being adjusted so as to maintain in the reaction medium a water content of on the order of from 1 to 2.5 wt.% and a pH value between 7 and 8; (b) distilling off the residual water present in the reaction medium and recovering the Novolak epoxy resin from the reaction products.
Claim 2
Independent Claim 199 words
A method for the preparation of a Novolak epoxy resin, which comprises: (a) gradually feeding an aqueous solution of alkali metal hydroxide into a solution in epichlorohydrin of a Novolak phenolic resin definable by the general formula: ##STR3## where the average value of n is from 0 to 5, the ratio between the moles of epichlorohydrin and the number of phenolic hydroxyl groups in said epychlorohydrin solution being from 2.5:1 to 12:1, until the number of moles of alkali metal hydroxide fed in is substantially equivalent to the number of phenolic hydroxyl groups present in said epichlorohydrin solution, while maintaining the reaction medium at boiling point and at a temperature of from 60° to 80° C., distilling off water in the form of an azeotropic mixture with epichlorohydrin and recycling the distilled epichlorohydrin into the reaction medium, the addition of alkali metal hydroxide and the distillation conditions being adjusted so as to maintain in the reaction medium a water content of on the order of from 1 to 2.5 wt.% and a pH value between 7 and 8; (b) distilling off the residual water present in the reaction medium and recovering the Novolak epoxy resin from the reaction products.
Claim 3
Dependent Claim 25 words
The method of claim 1, wherein said ratio between the moles of epichlorohydrin and the number of phenolic hydroxyl groups is from 6:1 to 8:1.
Claim 4
Dependent Claim 21 words
The method of claim 1, wherein said alkali metal hydroxide is selected from the group consisting of sodium and potassium hydroxide.
Claim 5
Dependent Claim 19 words
The method of claim 1, wherein said aqueous solution contains from 30 to 50 wt.% of alkali metal hydroxide.
Claim 6
Dependent Claim 16 words
The method of claim 1, wherein the distillation pressure is from 100 to 250 mm Hg.
Claim 7
Dependent Claim 27 words
The method of claim 1, wherein said water content is maintained at a value of about 1 wt.% and said pH at a value of about 7.5.
Claim 8
Dependent Claim 41 words
The method of claim 1, wherein said residual water is distilled off at a temperature of from 60° to 80° C., at a pressure of from 100 to 250 mm Hg and for a period of from 10 to 20 minutes.
Claim 9
Dependent Claim 21 words
The method of claim 1, wherein n is from 0 to 1.0 and said Novolak epoxy resin is liquid or semi-solid.
Claim 10
Dependent Claim 22 words
The method of claim 1, wherein n is higher than 1.0 and up to 5 and said Novolak epoxy resin is solid.
Claim 11
Dependent Claim 21 words
The method of claim 1, wherein said Novolak epoxy resin has an epoxy equivalent value substantially equal to the theoretical value.

References Cited (Backward Citations)

US2801227A Cited
US2840541A Cited
US2829124A Cited
US3252850A Cited
US3860561A Cited
US3867346A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-01-29 1982-07-31 1983-01-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-01-29 1986-07-31 1987-01-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-01-29 1990-07-31 1991-01-30 $7700.00 Window Closed / Lapsed

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