Experimental Study and Modeling of Beer Dealcoholization via Reverse Osmosis

Author:

Varga Áron1ORCID,Bihari-Lucena Eszter2345,Ladányi Márta6ORCID,Szabó-Nótin Beatrix7,Galambos Ildikó8,Koris András2ORCID

Affiliation:

1. Department of Research and Development, Pécsi Brewery, Alkotmány utca 94., H-7624 Pécs, Hungary

2. Department of Food Process Engineering, Hungarian University of Agriculture and Life Sciences, Ménesi út 44., H-1118 Budapest, Hungary

3. Department of Agricultural Business and Economics, Hungarian University of Agriculture and Life Sciences, Villányi út 29-43., H-1118 Budapest, Hungary

4. Department of Bioengineering and Fermentation Technology, Hungarian University of Agriculture and Life Sciences, Ménesi út 45., H-1118 Budapest, Hungary

5. ICON PLC, Szépvölgyi út 39., H-1037 Budapest, Hungary

6. Department of Applied Statistics, Hungarian University of Agriculture and Life Sciences, Villányi út 29-43., H-1118 Budapest, Hungary

7. Department of Fruit and Vegetable Processing Technology, Hungarian University of Agriculture and Life Sciences, Villányi út 29-43., H-1118 Budapest, Hungary

8. Department of Soós Ernő Research and Development Center, University of Pannonia, Zrínyi Miklós utca 18., H-8800 Nagykanizsa, Hungary

Abstract

The goals of the present investigation are to study and to model pale lager beer dealcoholization via reverse osmosis (RO). Samples were dealcoholized at a temperature of 15 ± 1 °C. An Alfa Laval RO99 membrane with a 0.05 m2 surface was used. The flux values were measured during the separations. The ethanol content, extract content, bitterness, color, pH, turbidity, and dynamic viscosity of beer and permeate samples were measured. The initial flux values were determined using linear regression. The initial ethanol flux (JEtOH 0) values were calculated from the initial flux values and the ethanol content values. A 2P full factorial experimental design was applied, and the factors were as follows: transmembrane pressure (TMP): 10, 20, 30 bar; retentate flow rate (Q): 120, 180, 240 L/h; JEtOH 0 was considered as the response. The effect sizes of the significant parameters were calculated. The global maximum of the objective function was found using a self-developed Grid Search code. The changes in the analytical parameters were appropriate. The TMP had a significant effect, while the Q had no significant effect on the JEtOH 0. The effect size of the TMP was 1.20. The optimal value of the factor amounted to TMP = 30 bar. The predicted JEtOH 0 under the above conditions was 121.965 g/m2 h.

Funder

the European Union

the Ministry of Culture and Innovation of Hungary from the National Research, Development and Innovation Fund

Publisher

MDPI AG

Subject

Filtration and Separation,Chemical Engineering (miscellaneous),Process Chemistry and Technology

Reference47 articles.

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