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Biofuel co-products as livestock feed - Opportunities and challenges

Biofuel co-products as livestock feed - Opportunities and challenges

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144<strong>Biofuel</strong> <strong>co</strong>-<strong>products</strong> <strong>as</strong> <strong>livestock</strong> <strong>feed</strong> – <strong>Opportunities</strong> <strong>and</strong> <strong>challenges</strong><strong>and</strong> can be produced worldwide. While research oncellulosic ethanol h<strong>as</strong> been ongoing for several decades, its<strong>co</strong>mmercial viability h<strong>as</strong> only been demonstrated recently.Fibre <strong>and</strong> storage carbohydrates within gr<strong>as</strong>ses can be<strong>co</strong>nverted to al<strong>co</strong>hol by ye<strong>as</strong>t after enzymatic hydrolysis,but the protein cannot be utilized for ethanol production.Therefore, the use of gr<strong>as</strong>s to produce ethanol, especiallyspecies that <strong>co</strong>ntain appreciable amounts of protein, createsnitrogenous w<strong>as</strong>te for bio-refineries. However, extraction ofprotein prior to enzymatic hydrolysis <strong>and</strong> <strong>co</strong>ncentrated <strong>as</strong>leaf protein can be utilized by <strong>livestock</strong>, thereby reducingprotein <strong>co</strong>sts <strong>and</strong> offsetting the l<strong>and</strong> required for animalproduction (Dale et al., 2009). Forage crops (e.g. reedcanary gr<strong>as</strong>s, timothy <strong>and</strong> alfalfa, <strong>as</strong> well <strong>as</strong> barley, triticale,pearl millet <strong>and</strong> sweet sorghum hays) <strong>and</strong> crop residues (e.g.maize stover <strong>and</strong> bag<strong>as</strong>se, <strong>as</strong> well <strong>as</strong> wheat, barley, triticale<strong>and</strong> rice straws) have been identified <strong>as</strong> potential sourcesof ligno cellulose for bio-ethanol production (Michaud,Bélanger <strong>and</strong> Surprenant, 1997).Information <strong>co</strong>ncerning the <strong>feed</strong>ing value of <strong>co</strong>-<strong>products</strong>from cellulosic ethanol or isobutanol production is currentlyquite limited. Isobutanol h<strong>as</strong> potential because it can be producedin a similar manner to ethanol, but it can be directlyblended with oil-b<strong>as</strong>ed fuels, <strong>and</strong> efficiency of fermentationis identical to ethanol production. While the potential isgreat to develop a whole new series of possible <strong>feed</strong>s foranimals, especially for ruminants, there remain a number ofunknowns. To date, data available includes primarily in vitroor in situ data, with little animal performance data.Treatment of fibrous materials is necessary to <strong>co</strong>nvertcellulose <strong>and</strong> other carbohydrates to forms that can befermented to ethanol or to isobutanol. However, whencellulose-rich biom<strong>as</strong>ses are used <strong>as</strong> an alternative to starchrichmaize grain <strong>as</strong> a source of sugars for ethanol production,large quantities of <strong>co</strong>-<strong>products</strong> need to be disposedof, preferably in a value-added process, possibly <strong>as</strong> animal<strong>feed</strong>. Fortunately, these cellulosic ethanol <strong>co</strong>-<strong>products</strong> areusually high in CP.Ammonia fibre expansion (AFEX) is a pre-treatment processfor cellulosic ethanol <strong>and</strong> may also be used to improveruminant digestibility of <strong>feed</strong>stuffs not traditionally used<strong>as</strong> forages. During AFEX, <strong>co</strong>ncentrated aqueous ammoniais <strong>co</strong>ntacted with biom<strong>as</strong>s under moderate temperatures(80–150 °C) <strong>and</strong> pressure (200–400 psi). After a short(5–30 minute) dwell time, the pressure is explosively rele<strong>as</strong>ed.This process h<strong>as</strong> several physical <strong>and</strong> chemical effects on thelignocellulosic material that improve its digestibility. AFEXresults in cellulose depolymerization <strong>and</strong> partial solubilizationof hemicellulose. Solubilized hemicellulose <strong>and</strong> lignin<strong>co</strong>mponents appear to be moved to the exterior of the cellwalls during the process, opening up the structure to facilitateaccess to cellulose by ruminal microbes <strong>and</strong> enzymes.These changes dramatically incre<strong>as</strong>e the rate <strong>and</strong> extent ofboth glucan <strong>and</strong> xylan rele<strong>as</strong>e during enzymatic hydrolysis<strong>co</strong>mpared with untreated material. For cellulosic ethanolproduction, AFEX treatment can incre<strong>as</strong>e ethanol productionfrom high fibre sources. For <strong>livestock</strong> producers, the important<strong>co</strong>nsideration is the <strong>feed</strong>ing value of the remaining <strong>co</strong><strong>products</strong>,although AFEX treatment may also be a means ofimproving digestibility of high-fibre <strong>feed</strong> sources.Bals et al. (2010) extracted 11 forages – including traditionalforages, agricultural residues <strong>and</strong> dedicated energycrops (e.g. switchgr<strong>as</strong>s) – using the AFEX process <strong>and</strong>digested in vitro with rumen inoculum. AFEX treatmentimproved 48-hour NDF digestion for several moderatelyindigestible forages <strong>co</strong>mpared with untreated samples, butshowed no improvement for highly digestible samples such<strong>as</strong> alfalfa <strong>and</strong> maize silage. Of particular interest were maizestover <strong>and</strong> late-harvest switchgr<strong>as</strong>s, <strong>as</strong> AFEX treatmentimproved digestibility by 52 percent <strong>and</strong> 128 percent overuntreated material, where<strong>as</strong> the improvement w<strong>as</strong> 74 percent<strong>and</strong> 70 percent over <strong>co</strong>nventional ammonia treatment,respectively. Weimer et al. (2003) included AFEX-treatedrice straw at modest levels (70 g/kg DM) in a cattle diet<strong>and</strong> found improved milk yields <strong>and</strong> intake <strong>co</strong>mpared withuntreated straw. An unknown at this time is whether <strong>feed</strong>ingsuch <strong>products</strong> <strong>co</strong>uld support the high milk productionneeded to <strong>feed</strong> the world’s future human population.The CP <strong>co</strong>ntent of all treated samples incre<strong>as</strong>ed tomore than 100 g/kg dry forage in the experiments by Balset al. (2010). S<strong>co</strong>tt et al. (2011) showed that AFEX + enzymatichydrolysis of cellulose <strong>and</strong> hemicelluloses incre<strong>as</strong>edthe N <strong>co</strong>ntent <strong>and</strong> disappearance of plant <strong>co</strong>nstituents,but decre<strong>as</strong>ed the <strong>co</strong>ntent of the major structural carbohydrates(ADF <strong>and</strong> NDF). The AFEX + enzymatic hydrolysistreatedforages <strong>co</strong>uld therefore be <strong>co</strong>nsidered for use <strong>as</strong>a non-protein N supplement in <strong>co</strong>mbination with highenergydiets low in ruminally degradable protein.A practical <strong>co</strong>nsideration may be to extract much ofthe leaf protein prior to AFEX or other treatments forcellulosic ethanol production (Dale et al., 2009). Leafprotein properly processed to <strong>co</strong>ncentrate it <strong>and</strong> removeanti-nutritional factors will probably be at le<strong>as</strong>t <strong>as</strong> valuablein <strong>livestock</strong> diets <strong>as</strong> soybean meal protein. Leaf proteinproduced <strong>as</strong> a <strong>co</strong>-product of cellulosic ethanol productioncan be utilized by <strong>livestock</strong> (Kammes et al., 2011).The effects of <strong>co</strong>nservation method on protein extractionefficiency from orchardgr<strong>as</strong>s (OG) <strong>and</strong> switchgr<strong>as</strong>s (SG)were evaluated by Kammes et al. (2011). Two maturitiesof OG <strong>and</strong> SG were harvested with CP <strong>co</strong>ncentrations of171 <strong>and</strong> 44 g/kg DM (immature) <strong>and</strong> 131 <strong>and</strong> 24 g/kgDM (mature) for OG <strong>and</strong> SG, respectively. Leaf juice w<strong>as</strong>extracted with a screw press from fresh, stored or wiltedchopped gr<strong>as</strong>ses. The liquid obtained w<strong>as</strong> pH adjustedwith HCl, treated with or without zinc salts (chloride),with or without heat, <strong>and</strong> then centrifuged to precipi-

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