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Program Book - Master Brewers Association of the Americas

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P-90<br />

Differences in <strong>the</strong> evaporation efficiency (AE) <strong>of</strong> common<br />

wort boiling methods and <strong>the</strong>ir effects on <strong>the</strong> resulting wort<br />

MARCUS HERTEL (1), Hans Scheuren (1), Karl Sommer (1)<br />

(1) TU München, Lehrstuhl für Maschinen- und Apparatekunde,<br />

Freising, Germany<br />

An important function <strong>of</strong> <strong>the</strong> boiling <strong>of</strong> wort is <strong>the</strong> calcination<br />

<strong>of</strong> flavors. If <strong>the</strong> total-evaporation is insufficient <strong>of</strong>f-flavors will<br />

occur in beer. Thus a brewer is anxious to have an adequate overall<br />

evaporation. <strong>Brewers</strong> have recognized, that <strong>the</strong> efficiency <strong>of</strong> <strong>the</strong><br />

calcination <strong>of</strong> flavors differs in varying wort boiling systems. As<br />

no one has an explanation for <strong>the</strong>se differences, people in <strong>the</strong><br />

brewing section claimed that wort is too complex and that <strong>the</strong><br />

fluid mechanics in a boiling system cannot be clarified, so that this<br />

efficiency could differ in every wort boiling system in any brewhouse<br />

for each brew. (It is shown elsewhere that this is not true!) That is<br />

<strong>the</strong> reason why total-evaporation is oversized in most breweries.<br />

Because <strong>of</strong> this a dimensionless index was established, <strong>the</strong> so called<br />

evaporation efficiency (AE). With this index every wort boiling<br />

system can be characterized and classified. One disadvantage <strong>of</strong><br />

this method is that <strong>the</strong> AE has to be measured experimentally.<br />

Because <strong>of</strong> this <strong>the</strong> different evaporation mechanisms that underlie<br />

<strong>the</strong> different boiling systems were researched in this work. Based<br />

on <strong>the</strong> basics <strong>of</strong> evaporation, residue-curves were established for<br />

every common wort boiling system under different conditions<br />

(temperature, pressure). These residue curves have been confirmed<br />

with experimental decreasing values <strong>of</strong> flavors during wort boiling<br />

in various boiling systems. It was possible to show that some boiling<br />

systems perform a mixture <strong>of</strong> different types <strong>of</strong> evaporation. Thus<br />

<strong>the</strong> decrease <strong>of</strong> a flavor component does not succeed <strong>the</strong> classical<br />

type <strong>of</strong> residue curves. That could be <strong>the</strong> main reason why it was<br />

misleadingly claimed that <strong>the</strong> calcination <strong>of</strong> compounds in wort<br />

is too complex to be predicted. It is shown that <strong>the</strong> decrease <strong>of</strong><br />

different wort flavor components can be preeminently predicted<br />

with <strong>the</strong> calculated residue curves for every common boiling system.<br />

With <strong>the</strong>se formulas it is now possible to predict <strong>the</strong> AE for every<br />

wort boiling system under every condition. Thus an experimental<br />

determination <strong>of</strong> <strong>the</strong> AE can now be avoided. It is now also possible<br />

to predict a needed overall evaporation individually for every brew<br />

in different boiling systems. An important result is, that <strong>the</strong> AE can<br />

differ strongly with <strong>the</strong> different common boiling technologies.<br />

Because <strong>of</strong> this <strong>the</strong> common boiling systems are suitable for <strong>the</strong><br />

calcinations <strong>of</strong> flavors in a different way. As a result all common<br />

wort boiling technologies are classified based on <strong>the</strong>ir efficiency.<br />

If <strong>the</strong> efficiency <strong>of</strong> a boiling system is known, it is much easier for<br />

brewers to decide which boiling system is <strong>the</strong> most qualified for <strong>the</strong>ir<br />

applications. Fur<strong>the</strong>rmore <strong>the</strong> efficiency <strong>of</strong> a wort boiling system<br />

can differ under different conditions. Because <strong>of</strong> this, existing wort<br />

boiling systems can be highly optimized if some parameters are<br />

adjusted correctly. With this new knowledge this is now possible!<br />

Marcus Hertel was born in 1975 in Nürnberg, Germany. Marcus<br />

has been <strong>the</strong> director <strong>of</strong> <strong>the</strong> Hertel Brauvertrieb GmbH, Nürnberg/<br />

Germany since 2006. Since 2007, he has been <strong>the</strong> director <strong>of</strong> <strong>the</strong><br />

Hertel GmbH Salzburg/Austria. Marcus has been a scientific<br />

assistant at <strong>the</strong> Lehrstuhl für Maschinen- und Apparatekunde<br />

(Chair Pr<strong>of</strong>essor Karl Sommer) Technische Universität München,<br />

Germany, since 2002. Marcus is active in basic research on <strong>the</strong><br />

steaming behavior and recreation kinetics <strong>of</strong> wort aroma compounds.<br />

From 1996 to 2002, Marcus studied brewing science and beverage<br />

technology at <strong>the</strong> Technische Universität München-Weihenstephan,<br />

Germany, obtaining a Dipl.-Ing. degree. Since 2003 he has studied<br />

business economics and economy engineering sciences at <strong>the</strong><br />

Fernuniversität, Hagen, Germany.<br />

P-91<br />

A new method to reduce <strong>the</strong> recreation <strong>of</strong> <strong>of</strong>f-flavors during<br />

<strong>the</strong> whirlpool rest<br />

HEINZ DAUTH (1), Marcus Hertel (1), Karl Sommer (1)<br />

(1) Technische Universität München, Center <strong>of</strong> Life Sciences,<br />

Weihenstephan, Germany<br />

A new approach is presented to reduce <strong>the</strong> content <strong>of</strong> undesired<br />

flavors during <strong>the</strong> whirlpool rest by increasing <strong>the</strong> vaporization rate.<br />

In this case it is not <strong>the</strong> <strong>the</strong>rmodynamic effect <strong>of</strong> evaporation that is<br />

essential, but in fact <strong>the</strong> process <strong>of</strong> vaporescence. This is realized by<br />

constantly evacuating <strong>the</strong> air above <strong>the</strong> wort in <strong>the</strong> whirlpool during<br />

<strong>the</strong> whirlpool rest. With shortened boiling processes, <strong>the</strong> conversion<br />

<strong>of</strong> precursors <strong>of</strong> undesired flavors is <strong>of</strong>ten insufficient. Thus, <strong>of</strong>fflavors<br />

are continuously produced even during <strong>the</strong> whirlpool rest<br />

and cannot be reduced without an additional evaporation, even<br />

with modern practices. The most important flavor in this context<br />

is dimethyl sulfide (DMS). With <strong>the</strong> presented method an increase<br />

in <strong>the</strong> vaporization rate is created by constantly evacuating <strong>the</strong> air<br />

above <strong>the</strong> wort in <strong>the</strong> whirlpool. Test trials have been carried out in<br />

a pilot-plant unit which was equipped with suitable mountings to<br />

permanently exhaust <strong>the</strong> air above <strong>the</strong> wort during <strong>the</strong> whirlpool<br />

rest. Thus, a comparison by gas chromatography between <strong>the</strong><br />

normal rested wort and <strong>the</strong> treated wort was conducted. Samples<br />

were taken in triplicate at different times during <strong>the</strong> whirlpool<br />

rest, to meet statistical requirements. For this, <strong>the</strong> wort was<br />

analyzed before and after a whirlpool rest <strong>of</strong> 30 min., with and<br />

without <strong>the</strong> new suction system. To show that <strong>the</strong> differences in <strong>the</strong><br />

resulting amounts <strong>of</strong> DMS are mainly caused by <strong>the</strong> increase <strong>of</strong> <strong>the</strong><br />

vaporescence, trials were also performed with DMS in pure water,<br />

where no production <strong>of</strong> DMS can occur. The results demonstrate<br />

that <strong>the</strong>re is a significant effect <strong>of</strong> using suction equipment on <strong>the</strong><br />

content <strong>of</strong> DMS after <strong>the</strong> whirlpool rest. This is solely due to <strong>the</strong><br />

higher vaporescence. Because <strong>of</strong> <strong>the</strong> high saturated vapor pressure<br />

<strong>of</strong> DMS in combination with its activity coefficient, <strong>the</strong> mass stream<br />

<strong>of</strong> DMS can be significantly enhanced by permanently exhausting<br />

<strong>the</strong> air above <strong>the</strong> wort during <strong>the</strong> whirlpool rest. This results in a<br />

lower concentration <strong>of</strong> DMS in <strong>the</strong> wort after <strong>the</strong> whirlpool rest. The<br />

influence on o<strong>the</strong>r components (e.g. <strong>the</strong> desirable hop component<br />

linalool) is not significant, because <strong>of</strong> <strong>the</strong>ir lower vapor pressures<br />

and activity coefficients. Shorter boiling times and a higher amount<br />

<strong>of</strong> precursors did not influence <strong>the</strong> quality <strong>of</strong> <strong>the</strong> resulting wort while<br />

using <strong>the</strong> investigated suction system. A patent has been assigned<br />

based on <strong>the</strong>se results.<br />

Dr.-Ing. Heinz Dauth was born in 1964. Dauth graduated as an<br />

engineer for food technology and biotechnology from <strong>the</strong> Technische<br />

Universität München–Weihenstephan in 1993. Afterward Dauth<br />

was appointed as a scientific researcher at <strong>the</strong> Chair <strong>of</strong> Process<br />

Engineering (Pr<strong>of</strong>. Dr.-Ing. K. Sommer) in Weihenstephan, TU<br />

München. He completed his doctoral <strong>the</strong>sis in 1999 in <strong>the</strong> field <strong>of</strong><br />

mechanical process engineering. Since 2003, Dauth has been a<br />

scientific assistant and university lecturer at <strong>the</strong> Chair <strong>of</strong> Process<br />

Engineering (Pr<strong>of</strong>. Sommer), TU München. His main research<br />

interests are bulk solids technology, dispensing technology, process<br />

engineering for specific problems in <strong>the</strong> food and beverage industries,<br />

and <strong>the</strong> formation <strong>of</strong> foam and stability <strong>of</strong> bubbles under <strong>the</strong><br />

influence <strong>of</strong> different gases and mixtures <strong>of</strong> gases dissolved in <strong>the</strong><br />

liquid. He is also responsible for <strong>the</strong> industrial cooperation program<br />

<strong>of</strong> <strong>the</strong> institute. Dauth is also working as an assistant pr<strong>of</strong>essor at <strong>the</strong><br />

Weihenstephan University <strong>of</strong> Applied Sciences, lecturing on process<br />

engineering.<br />

111

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