EP0203126A1

EP0203126A1 - Beer and process for its manufacture

Info

Publication number: EP0203126A1
Application number: EP85905818A
Authority: EP
Inventors: Klaus Dziondziak
Original assignee: Holsten Brauerei AG
Current assignee: Holsten Brauerei AG
Priority date: 1984-04-11
Filing date: 1985-11-22
Publication date: 1986-12-03
Also published as: US4624286A; DE8411409U1; DE3508777A1; DE3508777C2

Abstract

Bière faiblement alcoolisée ou non alcoolisée, à teneur comprise entre 0,3% et 2,0% en volume de glycérine pour lui donner plus de corps. La bière est produite par fermentation de moût suivie, le cas échéant, de retrait d'alcool. Pour lui donner plus de corps, on ajuste la teneur en glycérine de la bière par une fermentation dans des conditions conduisant à une augmentation de la production de glycérine et/ou par l'addition de glycérine ou d'un liquide contenant de la glycérine.Low-alcoholic or non-alcoholic beer, with a content between 0.3% and 2.0% by volume of glycerin to give it more body. Beer is produced by fermentation of wort followed, if necessary, by alcohol withdrawal. To give it more body, the glycerin content of the beer is adjusted by fermentation under conditions leading to an increase in the production of glycerin and / or by the addition of glycerin or a liquid containing glycerin.

Description

Beer and process for its production

The invention relates to a beer, in particular a low-alcohol or non-alcoholic beer, and a method for the production thereof.

Numerous processes for the production of low-alcohol or non-alcoholic beer are already known, in which at least part of the alcohol is subsequently removed from a beer having a normal alcohol content produced by conventional brewing processes. The process of this type described in DE-OS 14 42 238 provides for the alcohol to be evaporated off in a thin-film evaporator at temperatures below 70 ° C. From DE-AS 12 66 266 a similar process is also known, in which the beer is first subjected to atomization evaporation in a vacuum and then to a subsequent thin-layer evaporation in a vacuum and the residue is cut back and impregnated with carbon dioxide.

Methods for adsorbing alcohol removal from beer are also known from DE-OS 24 05 543 and DE-PS 7 21 249. A process for the production of low-alcohol beer by reverse osmosis is disclosed in DE-OS 23 23 094. In addition, processes for the production of low-alcohol beers by interrupting the fermentation or boiling-out of the beer in the brewing pan have been proposed. Finally, there is also the possibility of extracting alcohol from the beer by high-pressure extraction with liquid CO ₂ . All of the aforementioned methods for removing alcohol from beer have the disadvantage that, in addition to reducing the alcohol content important for full-bodiedness, other substances which influence the overall sensory impression are also removed, so that the taste quality of such low-alcohol or non-alcoholic beers is normal Beers are inferior in their full-bodied character. In addition, reverse osmosis and high-pressure extraction require complex and relatively fault-prone systems and have not been successful in practice because of the technical difficulties.

Even with full beers, diet beers, strong beers, draft beers and simple beers with alcohol contents in the range between about 1.5 and 6.0 percent by weight, depending on the starting materials and fermentation conditions, the beer obtained can be improved in terms of full-bodiedness and other tasty factors, despite the undiminished alcohol content his.

The object of the invention is now to provide a beer, in particular a low-alcohol or non-alcoholic beer, and a method for its production, which results in improved full-bodied character with simple, uncomplicated means and permits production in accordance with the purity requirement.

To achieve this object, the beer is characterized according to the invention by a full-bodied content of 0.3 to 2.0% by volume, preferably 0.4 to 1.5% by volume and in particular 0.5 to 1.2% by volume . % Glycerin.

Even with conventional brewing processes, a small amount of glycerin is formed as a by-product in addition to the ethyl alcohol when fermenting the wort, but this is well below 2 g / l in the beers produced by the previously known brewing processes. It is also known that some special types of yeast, for example Zygosaccharomyces acidi aci ens Nickerson, Saccharomyces rouxii and Saccharomyces mellis, in addition to ethyl alcohol, convert up to 50% of the carbohydrates consumed into glycerol. However, these types of yeast have not been examined for their suitability for beer production or used in brewing processes. Only the surprising finding that low-alcohol or non-alcoholic beers with a glycerol content of between 0.3 and 2.0 vol. % have such a greatly improved full-bodied character that they are practically indistinguishable from the senses of corresponding non-alcohol-reduced beers, it makes sense to create beers with a corresponding content of glycerol added or produced in situ during fermentation.

Advantageous further refinements of the beer are described in subclaims 2 to 4.

The invention further relates to a process for the production of beer, in particular low-alcohol or non-alcoholic beer, by fermentation of a wort and, if appropriate, subsequent extraction of alcohol, which is characterized by the features of patent claim 5.

Advantageous further refinements of the method are described in subclaims 6 to 11.

If the fermentation of the wort is carried out in the presence of the osmophilic yeasts mentioned in patent claim 10, the fermentation conditions should expediently be chosen so that on the one hand there are beer-typical conditions and on the other hand conditions are observed which increase glycerine production at the expense of alcohol production on ensure. Specially prepared brewing salts can be used for this. In some of these it is advisable to add sugars, particularly starch sugar, which can be fermented by these osmophilic yeasts, since they cannot utilize most of the malt's carbohydrates during fermentation. In this case, the added sugars represent the essential carbon source for the aerobic fermentation. In addition to other beer-typical metabolism products, a ratio of glycerol production to alcohol production of about 1: 0.8 can 0.9 result. During this fermentation, based on the amount of glycerin formed, about a third of this amount of acetic acid and about 4% of this amount of lactic acid, which, however, are largely removed when the alcohol is expelled by vacuum evaporation together with the ethyl alcohol, so that they do not adversely affect the taste properties of the beer obtained.

After the fermentation has ended, the beer obtained can be mixed with beer produced by another process and / or be matured and / or post-fermented with another or the same yeast before or after an alcohol reduction.

The technically and economically simplest process, however, consists in adding either the wort or the beer obtained after fermentation before or after a possible alcohol reduction, glycerol or a liquid containing glycerin in such an amount that within the ge in the claims inserted into the frame, taking into account the full-bodied character, the harmony of taste and the taste properties of the selected glycerin content.

Preferred embodiments of the beer and the corresponding production processes are explained in more detail below with the aid of examples.

example 1

From a commercially available quality beer Pilsener Brauart with mild bitterness, a wort content of 12% by weight, a real extract content of 4% by weight, an alcohol content of about 4% by weight and a bitter value of about 25 EBC units were produced by vacuum distillation, on the one hand, a low-alcohol beer with an alcohol content of 1.5% by weight and, on the other hand, an alcohol-free beer with an alcohol content of less than 0.05% by weight. The received low alcohol beer was 0.5 vol. % and the alcohol-free beer 0.85 vol. % pure glycerin (Merck 4093, EEC No. E 422} added, the beers then with water on the before Alcohol exhaustion existing diluted and recarbonized. The tasting of the beers obtained in this way showed that both experimental beers were superior in smell to the commercially available starting beer and were practically the same in taste and full-bodied and showed better foam durability and foam adhesion with the same foam pattern.

Example 2

In order to produce a non-alcoholic beer which corresponds to the sensor of the Pilsen brewing type of beer used in Example 1, a malt with a protein content of 16% by weight, a color of 6 EBC and a cooking color of 11 EBC (based on congress wort ratios) was used ), a viscosity of the congress wort of at least 1.75 mPas, a meal difference of 3% by weight, a protein solution level of 44% and a content of soluble nitrogen in 100 ml of 12% laboratory wort of over 130 mg after a two-mixing process with a temperature sequence of 50/75/77 ° C. to achieve a low apparent final degree of fermentation of about 25%, a wort with a wort content of 11% by weight and a bitter value of 48 EBC units and produced by pressure fermentation with a bottom-fermenting yeast at fermentation temperatures fermented between 15 and 18 ° C until final fermentation (actual extract content 8% by weight, alcohol content 1.5% by weight) and then subjected to a warm maturation phase of 24 h. The beer obtained was then dealcoholized in a vacuum rotary evaporator at a pressure of about 15 mm Hg and temperatures of about 30 ° C. to a residual alcohol content of about 0.1% by weight, then rediluted to an actual extract content of 4%, with 0 , 65 vol. % Glycerin added and recarbonized. The alcohol-free beer obtained in this way was slightly weaker in smell compared to the commercially available starting beer of example 1, but was better in taste and the same in the quality of the bitter and full-bodied. The foam durability and the foam adhesion were better. In game 3

An alcohol-free beer was produced by the method of Example 2, but now top-fermenting yeast and fermentation temperatures between 20 and 25 ° C were used. The alcohol-free beer obtained in this way, because of its higher content of fermentation by-products, proved to be significantly better in smell compared to the starting beer on the market and was equivalent in the other sensory characteristics. The experimental beer was rated somewhat better overall.

Example 4

The malt according to Example 2 was converted into a wort with a wort content of 14% by weight (thereof 8% by weight by pouring malt and 6% by weight by adding starch sugar) and a bitter value of 48 EBC egg using the same two-mashing method nhei th produced u-πd by pressure fermentation at a fermentation temperature of 25 ° C in the presence of Zygosaccharomyces acidifaciens Nickerson until largely to the final fermentation (based on this yeast) with an actual extract content of 9% by weight, an alcohol content of 1.15%. %, a glycerol content of 1.35% by weight, an acetic acid content of 0.45% by weight and a lactic acid content of 0.05% by weight. The product obtained was subjected to a warm ripening phase of 24 h, then adjusted in a vacuum rotary evaporator to a residual alcohol content of 0.1% by weight and a residual acid content of 400 mg / l, rediluted to an actual extract content of 4.5% and recarbonized . When specifying the actual extract content, it must be taken into account that 1.35% by weight of glycerin corresponds to an actual extract content of about 1% by weight, so that in the absence of glycerol before the alcohol removal at 8% by weight. % and would be 4% by weight after the redilution. This beer also had a mushroom character and proved to be equivalent to the starting beer of Example 1 in its full-bodied character and its other taste properties. Example 5

A conventional, commercially available Pilsener Brauart beer with an original wort content of 11.4% by weight, a real extract content of 3.8% by weight and an alcohol content of 3.7% by weight was made with a malt and mashing method of Example 2 produced beer with a wort content of 15% by weight, an actual extract content of 13% by weight and an alcohol content of about 1% by weight and water in a weight ratio of 3: 1: 4 blended. The mixture obtained with a wort content of 6.15% by weight, an actual extract content of 3.05% by weight and an alcohol content of about 1.5% by weight was subjected to a residual alcohol content of about 0.1% by weight in a vacuum rotary evaporator .% adjusted, rediluted with water to the initial volume, with 0.65 vol. % Glycerin added and recarbonized. The beer obtained had a mushroom character and was rated better in terms of smell and quality of bitterness in comparison to the starting beer on the market and rated higher in full-bodied character, while the other taste characteristics were the same. The foam of the experimental beer was more fine-pored and showed better durability and better adhesion. Overall, the experimental beer was preferred.

Example 6

According to a method corresponding to Example 1, but tailored to draft beer, with otherwise identical amounts and qualities of raw materials (original wort content 8% by weight, real extract content 2.7% by weight, alcohol content 2.7% by weight, bitter value 25 EBC- Egg units) a draft beer and then with 0.5 vol. % Glycerin added. The beer obtained in this way had a mushroom character and was judged in terms of smell and taste to be cleaner and better, while the quality of the bitterness, the full-bodied character and the foam values did not result in any significant differences. Overall, the experimental beer was preferred.

Claims

PATENT CLAIMS

Beer, especially low-alcohol or non-alcoholic beer, characterized by a full-bodied content of 0.3 to 2.0 vol. %, preferably 0.4 to 1.5 vol.% and in particular 0.5 to 1.2 vol. % Glycerin.

Low-alcohol or non-alcoholic beer according to Claim 1, characterized in that the total glycerol content consists of glycerol formed in situ by fermentation of the wort in the presence of an increased glycerol-producing yeast.

Low-alcohol or non-alcoholic beer according to claim 1, characterized in that the glycerol content consists predominantly of glycerol introduced into the beer or before or after the alcohol withdrawal in the beer.

Beer according to one of claims 1 to 3, characterized in that it additionally contains 0.05 to 0.5 vol. % preferably 0.1 to 0.3 vol. % of one or more sugar alcohols, in particular erythritol and / or D-arabitol, are contained.

Process for the production of beer, in particular low-alcohol or non-alcoholic beer, by fermentation of a wort and, if appropriate, subsequent alcohol withdrawal, characterized in that to improve the full-bodied character by fermentation under increased glycerin fermentation conditions and / or Addition of glycerin or a liquid containing glycerin has a beer content between 0.3 and 2.0 vol. %, preferably between 0.4 and 1.5 vol. % and in particular between 0.5 and 1, 2 vol. % sets. 6. The method according to claim 5 for the production of a low-alcohol beer, in which a beer produced by conventional brewing methods with an alcohol content of more than 1.5% by weight by evaporation, reverse osmosis, alcohol adsorption or pressure extraction and optionally subsequent dilution and recarbonization to an alcohol content between 0.5 and

1.5% by weight, characterized in that a glyceryl content of between 0.3 and 0.1 vol. % and preferably between 0.4 and 0.7 vol. % complies.

7. The method according to claim 5 for the production of an essentially alcohol-free beer, in which a beer produced by conventional brewing processes with an alcohol content of more than 1.5% by weight is obtained by evaporation, reverse osmosis, alcohol adsorption or pressure extraction and optionally subsequent dilution and recarbonization to an alcohol content of less than 0.5% by weight and preferably less than 0.1% by weight, characterized in that a glycerol content of between 0.5 and 1.8 vol. %, preferably between 0.7 and 1.4 vol. % and in particular between 0.8 and 1.1

Vol. % complies.

8. The method according to any one of claims 5 to 7, characterized gekenn¬ characterized in that a glycerin-containing liquid, for example a beer with sufficient glyceryl content, is introduced into the wort or before or after the alcohol removal in the beer.

9. The method according to any one of claims 5 to 8, in which the beer is subjected to a thin-film evaporation in vacuo, characterized in that the glyceri nhal i liquid is introduced into the evaporated beer before or after any redilution . lo. Process according to one of Claims 5 to 7, characterized in that the fermentation of the wort is carried out in the presence of an osmophilic yeast, in particular Zygosaccharomyces acidifaciens Nickerson, Saccharomyces rouxii or Saccharomyces mellis.

IT. Process according to claim 5 or 10, characterized in that the malt used in the wort, the yeast used and the fermentation conditions are coordinated in such a way that the carbohydrates of the malt are hardly used during fermentation.

12. The method according to claim lo or 11, characterized in that fermentable sugar, especially starch sugar, is introduced into the wort from the osmophilic yeast used