Preparation of ortho-hydroxybenzyl alcohols

Claim 2

In a process for the preparation of an orthohydroxybenzyl alcohol by (a) reacting a phenol with boric acid to form boric acid esters of said phenol, (b) condensing said boric acid esters with formaldehyde or a formaldehyde-generating compound to form the corresponding ortho-hydroxybenzyl alcohol boric acid esters, and then (c) decomposing said orthohydroxybenzyl alcohol boric acid esters to liberate the corresponding ortho-hydroxybenzyl alcohol therefrom the improvement comprising employing the reactants in step (a) in a ratio of at least 1.1 mols of said phenol per mol of boric acid to form in step (a) boric acid esters of said phenol which comprise phenol orthoborates.

Claim 3

A process as defined in claim 1 wherein the phenol reactant employed in step (a) has the structural formula ##STR5## wherein n is 0, 1, 2 or 3 and R is an alkyl radical having from 1 to 12 carbon atoms, an alkoxy radical having from 1 to 12 carbon atoms or a halogen atom at least one of the ortho-positions relative to the phenolic hydroxyl being free when n is 2 or 3, said process affording the corresponding ortho-hydroxybenzyl alcohol product having the structural formula ##STR6## wherein n and R are defined as above.

Claim 4

A process as defined in claim 1 or 2 wherein the reactants in step (a) are employed in a ratio of from about 1.2 to about 3 mols of said phenol per mol of boric acid.

Claim 5

A process as defined by claim 1 wherein the reactants in step (a) are employed in a ratio of from about 1.5 to about 3 mols of said phenol per mol of boric acid.

Claim 6

A process as defined by claim 1 wherein the ortho-hydroxybenzyl alcohol boric acid esters are decomposed from a solvent solution thereof, said solvent also comprising a phenol/boric acid solvent of esterification.

Claim 7

A process as defined by claim 5, said solvent being an aromatic hydrocarbon.

Claim 8

A process as defined by claim 1 or 5, wherein the amount of formaldehyde employed in step (b) is about 1 mol per mol of boric acid.

Claim 9

A process as defined in claim 1, wherein the temperature employed for the formaldehyde condensation step (b) is between about 20° and about 120° C.

Claim 10

A process as defined in claim 7, wherein an organic solvent is employed during steps (a) and (b) and wherein excess phenol is separated from the ortho-hydroxybenzyl alcohol by treating the reaction mixture obtained at the end of step (b) with an aqueous solution of an alkali metal base, in an amount of from about 0.8 to about 1.2 mols of alkali metal base per mol of boric acid, to form a complex alkali metal salt of the orthohydroxybenzyl alcohol boric acid esters, followed by separation by decantation of the organic phase containing said phenol from the aqueous phase containing the complex and liberation of the ortho-hydroxybenzyl alcohol from its complex.

Claim 11

A process is defined by claim 9, wherein the amount of alkali metal base employed is between about 0.9 and about 1.1 mols per mol of boric acid.

Claim 12

A process as defined by claim 9, wherein the amount of alkali metal base employed is about 1 mol per mol of boric acid.

Claim 13

A process as defined by claim 10, wherein the alkali metal base employed is sodium hydroxide or potassium hydroxide.

Claim 14

A process as defined by claim 10, wherein the ortho-hydroxybenzyl alcohol is liberated by treating the aqueous phase containing the complex with an alkali metal base to afford an aqueous solution of alkali metal borate and of alkali metal salt of the ortho-hydroxybenzyl alcohol.

Claim 15

A process as defined by claim 1 for the preparation of saligenol, wherein phenol and boric acid are reacted in a ratio of from at least 1.1 to about 3 mols of phenol per mol of boric acid, in an organic solvent which forms an azeotrope with the water of esterification, said water being removed by azeotropic distillation; a solution in an organic solvent of the phenyl borate thus formed is then condensed with formaldehyde or a formaldehyde generator, in an amount of about 1 mol of formaldehyde per mol of boric acid, at a temperature of between about 20° and about 120° C.; the reaction mixture obtained after condensation is then treated with an aqueous solution of from about 0.8 to about 1.2 mols of an alkali metal base per mol of boric acid, to form a complex alkali metal salt of saligenol and of boric acid; the resultant organic phase containing excess phenol is separated from the aqueous phase containing the complex alkali metal salt of saliginol and of boric acid; and the aqueous phase containing said complex is treated with an aqueous solution of an alkali metal base, saligenol being liberated therefrom in the form of its alkali metal saligenate.