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Program Book - Master Brewers Association of the Americas

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O-62<br />

Bioconversion <strong>of</strong> brewer’s spent grains to bioethanol<br />

GRAEME WALKER (1), Jane White (1), Biju Yohannan (1)<br />

(1) University <strong>of</strong> Abertay, Dundee, Scotland<br />

Spent grains (SG), <strong>the</strong> solid cereal residues remaining after<br />

extraction <strong>of</strong> wort, represent a major by-product <strong>of</strong> brewing<br />

and distilling industries. This lignocelluose-rich biomass may<br />

provide a source <strong>of</strong> sugars for fuel ethanol fermentations and<br />

may <strong>the</strong>refore <strong>of</strong>fer potentially valuable alternatives to current<br />

uses <strong>of</strong> SG as animal feedstock (Walker and White, 2007).<br />

Bioethanol represents a renewable source <strong>of</strong> energy (as opposed<br />

to syn<strong>the</strong>tic ethanol obtained from crude oils), and it can replace<br />

petroleum or can be used as an additive in car engines to increase<br />

fuel combustion, octane number and to reduce <strong>the</strong> emissions <strong>of</strong><br />

toxic and greenhouse gases. This presentation will review <strong>the</strong><br />

challenges and opportunities regarding bioconversion <strong>of</strong> brewer’s<br />

and distiller’s spent grains to bi<strong>of</strong>uels and will also discuss recent<br />

results on brewery SG hydrolysis and fermentation to bioethanol.<br />

Dilute acid and enzyme treatments were developed to convert <strong>the</strong><br />

hemicellulose and cellulose fractions <strong>of</strong> SG from an ale production<br />

process to glucose, xylose and arabinose. Pre-treatment <strong>of</strong> dried,<br />

hammer-milled grains with 0.16 N HNO 3 at 121°C for 15 min was<br />

chosen as <strong>the</strong> most suitable method for solubilizing grains prior to<br />

enzymatic digestion with cellulase and hemicellulase preparations.<br />

Solid loading concentrations (10, 15 and 20% w/v) were compared<br />

and reducing sugar concentrations between 40 and 48 g (100 g SG) –1<br />

were extracted. Hydrolysate, prepared from 20% SG, pre-treated<br />

with 0.16 N HNO 3 , partially neutralized to pH 5–6 and digested with<br />

enzymes for 18 h, contained 27 g L –1 glucose, 16.7 g L –1 xylose and<br />

11.9 g L –1 arabinose. Fermentation <strong>of</strong> this hydrolysate for 48 h by<br />

Pichia stipitis and Kluyveromyces marxianus resulted in ethanol<br />

conversion yields <strong>of</strong> 0.25 and 0.18 g ethanol (g sugar) –1 , respectively.<br />

These non-Saccharomyces yeasts can ferment C5 sugars, unlike<br />

brewing yeast. The fermentation yields, however, were less<br />

when compared with fermentation performance on glucose/<br />

xylose mixtures in syn<strong>the</strong>tic media, suggesting that inhibitory<br />

compounds (possibly furfural) derived from SG were present in<br />

<strong>the</strong> hydrolysate. Our research findings have revealed relatively<br />

straightforward chemical and biotechnological approaches to<br />

convert brewery and distillery spent grains to bioethanol. “Second<br />

generation” bioethanol derived from biowaste material such as<br />

SG represents one <strong>of</strong> <strong>the</strong> most interesting bi<strong>of</strong>uel sources. Several<br />

future challenges remain, however, regarding cost-efficiencies and<br />

energy balances <strong>of</strong> such processes and <strong>the</strong>y will be discussed in this<br />

presentation. References: Walker, GM and White, JS (2007) Fuelling<br />

<strong>the</strong> future. The science behind fuel alcohol yeast fermentations. The<br />

Brewer & Distiller International 6: 23-27.<br />

Graeme Walker graduated with a B.S. degree in brewing and<br />

biochemistry in 1975 and completed his Ph.D. degree in yeast<br />

physiology (1978) both from Heriot Watt University, Edinburgh. His<br />

pr<strong>of</strong>essional career has included Royal Society/NATO postdoctoral<br />

fellow at Carlsberg Foundation, Copenhagen; lecturer (biochemistry)<br />

at Otago University, New Zealand; lecturer (biotechnology) at<br />

Dublin City University; visiting researcher at Case Western Reserve<br />

University in Cleveland, OH; senior lecturer (microbiology) at<br />

Dundee Institute <strong>of</strong> Technology; and reader (biotechnology) at <strong>the</strong><br />

University <strong>of</strong> Abertay Dundee, Scotland. He is currently pr<strong>of</strong>essor<br />

and divisional leader for biotechnology and forensic science<br />

at Abertay University, where he directs a yeast research group<br />

investigating growth, metabolism, and stress in industrial yeasts.<br />

He is an active member <strong>of</strong> <strong>the</strong> Institute <strong>of</strong> Brewing & Distilling<br />

and American Society <strong>of</strong> Brewing Chemists. Pr<strong>of</strong>essor Walker has<br />

published over 100 articles in journals, books, and conference<br />

96<br />

proceedings and has also authored <strong>the</strong> textbook “Yeast Physiology<br />

and Biotechnology” published by J. Wiley (1998). He acts in a<br />

consulting capacity for international brewing and biotechnology<br />

companies.<br />

O-63<br />

A financial and engineering analysis <strong>of</strong> energy conservation<br />

strategies with respect to heat generation processes within <strong>the</strong><br />

brewing industry<br />

JOHN MEAD (1)<br />

(1) Emech Control Limited, Auckland, New Zealand<br />

As <strong>the</strong> world moves into <strong>the</strong> era <strong>of</strong> high fossil fuel costs and <strong>the</strong><br />

carbon economy dictates minimization <strong>of</strong> a company’s carbon<br />

footprint <strong>the</strong> need to reutilize valuable energy will become more<br />

and more important. So far most breweries have under-utilized <strong>the</strong><br />

opportunities that <strong>the</strong>ir current plant and processes provide for<br />

energy recycling. The most common energy recovery process to<br />

date has been <strong>the</strong> wort cooling process used to heat hot liquor. The<br />

cooling <strong>of</strong> wort is a brewing process, and <strong>the</strong> subsequent energy<br />

recovery is a by-product <strong>of</strong> this process ra<strong>the</strong>r <strong>the</strong>n a purpose <strong>of</strong><br />

<strong>the</strong> original activity. The purpose <strong>of</strong> this presentation is to explore<br />

energy recovery techniques that may be applicable to <strong>the</strong> brewing<br />

process and to provide an executive analysis <strong>of</strong> <strong>the</strong> engineering<br />

fundamentals in light <strong>of</strong> financial limitations and expected returns.<br />

The presentation will include examples <strong>of</strong> current technologies<br />

available, a commentary on <strong>the</strong>ir potential applications and a<br />

critique <strong>of</strong> <strong>the</strong>ir potential limitations. As breweries expand into<br />

developing countries and existing breweries modify processes<br />

to meet <strong>the</strong>ir new operating environments <strong>the</strong> opportunities to<br />

incorporate <strong>the</strong>se technologies into current processes will generate<br />

results that have an immediate impact on <strong>the</strong> financial bottom line.<br />

With <strong>the</strong> move toward triple bottom line reporting such innovations<br />

will also provide positive results from an environmental standpoint<br />

and allow <strong>the</strong> company to report on non-financial aspects <strong>of</strong> its<br />

operation. It is my intention to discuss technologies that will be<br />

applicable to <strong>the</strong> boiler, general brewing process, refrigeration,<br />

bottling and CIP activates. Examples will be provided as to how such<br />

activities are currently being conducted in both breweries and o<strong>the</strong>r<br />

processing plants. I will also provide a decision-making framework<br />

that can be utilized by conference attendees for assessing <strong>the</strong><br />

benefits <strong>of</strong> proposed energy recovery projects and <strong>the</strong> prioritizing <strong>of</strong><br />

<strong>the</strong>ir implementation.<br />

John Mead has worked in <strong>the</strong> engineering field for 18 years, starting<br />

as a mechanical engineer in <strong>the</strong> motor trade. He spent eight years at<br />

Unilever’s Industrial Chemical division before taking up <strong>the</strong> national<br />

sales managers role at Renold NZ. Currently John is employed as<br />

<strong>the</strong> Australasian sales manager for Emech Control. Emech Control<br />

is a specialized valve and actuation manufacturer who produces<br />

a range <strong>of</strong> valves and controls for a variety <strong>of</strong> customers in process<br />

industries. John’s area <strong>of</strong> expertise is heat and energy recovery. John<br />

holds a number <strong>of</strong> engineering qualifications and has also completed<br />

a BBS and postgraduate qualifications in accounting. He is currently<br />

completing his masters degree in environmental accounting, and his<br />

core area <strong>of</strong> research is in creating economic models that illustrate <strong>the</strong><br />

impact energy issues have on companies operating pr<strong>of</strong>itably and<br />

<strong>the</strong>ir share price.

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