Abstract: An extract of an oak aged alcoholic product is produced by a process using a food grade solvent or a process which does not use a food grade solvent. The process using a good grade solvent includes adding a food grade solvent, such as ethyl acetate, to the oak aged alcoholic product and mixing the two liquids. The resulting mixture is allowed to separate into two layers. A first layer, including the food grade solvent, flavors, color, alcohol (i.e., ethanol) and water, is separated from the second layer, and the solvent is removed. In the process which does not use a food grade solvent, the oak aged alcoholic product has at least some of its wood notes and color removed to produce an intermediate product. Substantially all water and alcohol is then removed from the intermediate product. In another process for producing the extract without a food grade solvent an intermediate proof-adjusting step is added after the step of removing the wood notes and color and before the step of removing the water and alcohol.

Abstract: An extract of an oak aged alcoholic product is produced by adding a food grade solvent, such as ethyl acetate, to the oak aged alcoholic product and mixing the two liquids. The resulting mixture is allowed to separate into two layers, a first layer and a second layer. The first layer, including the food grade solvent, flavors, color, alcohol (i.e., ethanol) and water, is separated from the second layer. The solvent is then removed from the first layer to produce the extract. The extract can be added to a less costly alcoholic beverage, such as grain neutral spirits, or sugar beet spirits, to produce a beverage having the taste of a mature oak aged alcoholic beverage. Also disclosed is an accelerated whisky maturation method, including combining an alcoholic distillate with toasted oak chips, heating and aerating and/or oxygenating the resulting mixture to produce an accelerated oak aged alcoholic product. The toasted oak chips are then removed.

Abstract: An extract of a mature oak aged alcoholic beverage is produced by adding a food grade solvent, such as ethyl acetate, to the alcoholic beverage and mixing the two liquids. The resulting mixture is allowed to separate into two layers, a first layer and a second layer. The first layer, including the food grade solvent, is separated from the second layer. The solvent is then removed from the first layer to produce the extract. The extract can be added to a less costly alcoholic beverage, such as grain neutral spirits, or sugar beet spirits, to produce a beverage having the taste of a mature oak aged alcoholic beverage.

Abstract: A process for manufacturing flavors from the spent mash of a fermentation mixture is provided wherein the spent mash of the fermentation mixture after distillation is separated into two constituent portions, the thin stillage and the wet distillers' grains. The thin stillage portion is then combined with a base to adjust pH thereof to between about 7 and about 11. The pH-adjusted thin stillage portion is then cooked at a temperature between about 130.degree. F. and about 210.degree. F. for a period of about 4 to about 14 hours. The cooked solution is concentrated in an evaporator until about 30% wt. solids level is obtained. The product is then dried to about 5-about 10% wt. moisture content. The product obtained has different flavors, depending on the base added and the pH of the cooking step. If the base is sodium hydroxide, the product has a bland, sweet or yeasty flavor if the pH is 8.5, maple or caramel flavor if the pH is 9.5, and a cracker or nutty flavor if the pH is 10.5.

Abstract: A process for manufacturing flavors from the spent mash of a fermentation mixture is provided wherein the spent mash of the fermentation mixture after distillation is separated into two constituent portions, the thin stillage and the wet distillers' grains. The thin stillage portion is then combined with a base to adjust pH thereof to between about 7 and about 11. The pH-adjusted thin stillage portion is then cooked at a temperature between about 130.degree. F. and about 210.degree. F. for a period of about 4 to about 14 hours. The cooked solution is concentrated in an evaporator until about 30% wt. solids level is obtained. The product is then dried to about 5-about 10% wt. moisture content. The product obtained has different flavors, depending on the base added and the pH of the cooking step. If the base is sodium hydroxide, the product has a bland, sweet or yeasty flavor if the pH is 8.5, maple or caramel flavor if the pH is 9.5, and a cracker or nutty flavor if the pH is 10.5.