Aqueous phenolic resole dispersion containing gum ghatti interfacial agent

Claim 2

An aqueous dispersion containing dispersed particles of a phenolic resole in water, gum ghatti, and a thickening agent, substantially all of said particles having diameters below about 25 microns, wherein the molecular weight of said resole is such that said resole is substantially water-insoluble, wherein said gum ghatti is employed in an amount sufficient to stabilize said dispersion of resole particles in water, and wherein the thickening agent is employed in an amount such that the viscosity of said dispersion at 23° C. is at least about 500 centipoises.

Claim 3

The aqueous dispersion of claim 1 wherein said phenolic resole is the base-catalyzed reaction product of a phenol and formaldehyde, wherein the average diameter of said particles is below about 12 microns, and wherein the proportion of said resole in said dispersion is not greater than about 50 weight percent, based on weight of resole plus water.

Claim 4

The aqueous dispersion of claim 2 wherein said phenolic resole has a weight average molecular weight within the range of from about 400 to about 3000.

Claim 5

The aqueous dispersion of claim 2 wherein said phenol is at least one member of the group consisting of monohydroxybenzene, alkylphenol, and 2,2-bis(4-hydroxyphenyl)propane.

Claim 6

The aqueous dispersion of claim 2 wherein substantially all of said particles have diameters below about 5 microns.

Claim 7

The aqueous dispersion of claim 5 wherein said particles have average diameters below about 3 microns.

Claim 8

The aqueous dispersion of claim 2 wherein said thickening agent is selected from the group consisting of guar gum, gum carrageenan, algin gum, locust bean gum, and water-soluble ethylene-maleic anhydride copolymers.

Claim 9

The aqueous dispersion of claim 2 wherein the gum ghatti is employed in an amount of from about 0.5 to about 5 parts by weight, and wherein the thickening agent is used in an amount of from about 0.1 to about 1 parts by weight, per 100 parts by weight of phenol employed to produce said resole.

Claim 10

A process for producing an aqueous dispersion of phenolic resole particles in water, which process comprises reacting a phenol with an aldehyde in the presence of a basic catalyst for a period of time and at a temperature sufficient to produce a substantially water-insoluble phenolic resole, and dispersing said phenolic resole, in situ, in an aqueous medium containing gum ghatti and a thickening agent, wherein said aqueous medium contains sufficient water to enable a phase inversion to occur during said dispersing step, thereby to produce a dispersion of phenolic resole in water, wherein said gum ghatti is employed in an amount sufficient to form and stabilize said dispersion of phenolic resole particles in water, and wherein said thickening agent is employed in an amount such that the viscosity of said dispersion at 23° C. is at least about 500 centipoises.

Claim 11

A process for producing an aqueous dispersion of phenolic resole particles in water, which process comprises reacting a phenol with an aldehyde in the presence of a basic catalyst for a period of time and at a temperature sufficient to produce a substantially water-insoluble phenolic resole, and dispersing said phenolic resole, in situ, in an aqueous medium containing gum ghatti and a thickening agent, wherein said aqueous medium contains sufficient water to enable a phase inversion to occur during said dispersing step, thereby to produce a dispersion of phenolic resole in water, wherein said gum ghatti is employed in an amount sufficient to form and stabilize said dispersion of phenolic resole particles in water, and wherein said thickening agent is employed in an amount such that the viscosity of said dispersion at 23° C. is at least about 500 centipoises.

Claim 12

The process of claim 9 wherein said aldehyde is formaldehyde.

Claim 13

The process of claim 9 wherein said process includes the steps of: (a) reacting a phenol with an aldehyde in a reaction mixture containing a basic catalyst for a period of time sufficient to produce a resole; (b) adding to said reaction mixture gum ghatti, a thickening agent, and sufficient water to enable the production of a resole-in-water dispersion; and (c) thereafter subjecting the reaction mixture to elevated temperature for a period of time sufficient to increase the weight average molecular weight of said resole to a value within the range of from about 400 to about 3000; provided that the pH of said reaction mixture is below about 9 prior to said step (c).