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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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16<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>ethanol supply w<strong>as</strong> 120 PJ from EU cereals <strong>and</strong> sugar beet,with imports of sugar cane bio-ethanol.BIOFUEL PROCESSESDifferent crop <strong>products</strong> are used to make biofuels, usingalternative technologies:• Sugar <strong>and</strong> starch fermentation to bio-ethanol.• Vegetable oil transesterification or hydrogenation tobiodiesel.• Anaerobic digestion to biomethane.• Hydrolysis of lignocellulosic <strong>feed</strong>s followed by fermentationto bio-ethanol.• G<strong>as</strong>ification of lignocellulosic <strong>feed</strong>s followed by biodieselsynthesis.Starch in cereal crops <strong>and</strong> sugar in crops such <strong>as</strong> sugarcane <strong>and</strong> sugar beet are <strong>co</strong>nverted to bio-ethanol usingfermentation, leaving the remaining DDGS from cereals <strong>and</strong>pulp from sugar beet for use <strong>as</strong> animal <strong>feed</strong>. Vegetable oilsare extracted from oilseed crops, such <strong>as</strong> rapeseed <strong>and</strong> soybean,<strong>and</strong> <strong>co</strong>nverted to biodiesel using transesterificationor hydrogenation processes, leaving the remaining oilseedcakes or meals for use <strong>as</strong> animal <strong>feed</strong>. Transesterificationof vegetable oils uses methanol <strong>and</strong> gives aglycerine <strong>co</strong>product.While various work h<strong>as</strong> been done to show thatglycerine can be used <strong>as</strong> an animal <strong>feed</strong>, it is unlikely thatit will be used to any significant extent. This is becausepurification of crude glycerine would probably be neededto eliminate the risk from <strong>as</strong>sociated methanol <strong>and</strong> becausethere are alternative higher value markets for glycerol:upgrading for pharmaceutical use, manufacture of chemicals<strong>and</strong> in the EU there are incentives to use crude glycerolfor renewable power generation.Anaerobic digestion is able to utilize a large range of<strong>feed</strong>stocks to produce biog<strong>as</strong>, which can be used to generateheat <strong>and</strong> power, or purified to make biomethane. Thebiomethane can be fed into the g<strong>as</strong> grid or used <strong>as</strong> a biofuel.Anaerobic digestion de<strong>co</strong>mposes the starch, sugar, oil<strong>and</strong> protein in the <strong>feed</strong>stock to produce methane, while theremaining <strong>co</strong>mponents, including phosphate <strong>and</strong> pot<strong>as</strong>h<strong>and</strong> the nitrogen from the protein fraction, are returned tol<strong>and</strong> <strong>as</strong> digestate, or de<strong>co</strong>mposed in an aerobic oxidationunit.Lignocellulosic <strong>feed</strong>stocks such <strong>as</strong> wheat straw, maizestover <strong>and</strong> wood need more aggressive processing to access<strong>co</strong>mponents for biofuels. One option is to use hydrolysisof the <strong>feed</strong>stocks to extract the sugar, for fermentation toethanol. The other option is g<strong>as</strong>ification of the <strong>feed</strong>stockto hydrogen <strong>and</strong> carbon monoxide, followed by synthesisprocesses to produce methanol, ethanol, dimethyl ether ormiddle distillate using Fischer-Tropsch synthesis <strong>and</strong> hydrocracking.The remaining <strong>co</strong>mponents are used <strong>as</strong> fuel todrive the process. These processes all require a large capitalinvestment. Only the sugar-, starch- <strong>and</strong> oilseed-b<strong>as</strong>edprocesses (so called “First-generation” processes) normallyprovide animal <strong>feed</strong> <strong>as</strong> a <strong>co</strong>-product.<strong>Biofuel</strong> production process efficienciesA <strong>co</strong>mparison of biofuel re<strong>co</strong>very <strong>and</strong> energy efficiencylosses for different biofuel processes (Ingledew 1993; Adenet al., 2002; FNR, 2009; Nexant, 2007) is shown in Table 1.The biofuel <strong>co</strong>mponent is the <strong>co</strong>mponent in the <strong>feed</strong>stockthat is used to make the biofuel, <strong>and</strong> different technologiesare used. The extraction efficiency is the proportion of theavailable <strong>feed</strong>stock <strong>co</strong>mponent that is extracted or utilizedfor the biofuel process. For example, in anaerobic digestion,lignin <strong>and</strong> cellulose can not all be utilized in the process.The biofuel selectivity is the proportion of the biofuel<strong>co</strong>mponent that is <strong>co</strong>nverted to biofuel, while the rest is<strong>co</strong>nverted to other by-<strong>products</strong>. The crop energy efficiencyis the proportion of energy in the crop or <strong>feed</strong>stock thatis <strong>co</strong>nverted to useful energy <strong>products</strong> such <strong>as</strong> biofuel oranimal <strong>feed</strong>.Although some potential biofuel is lost in fermentation<strong>and</strong> transesterification technologies due to inefficienciesin vegetable oil extraction <strong>and</strong> in fermentation, there is aloss of only 1 percent to 2.5 percent in the overall energyTABLE 1<strong>Biofuel</strong> re<strong>co</strong>very <strong>and</strong> energy efficiency losses for different biofuel processesParameterCereals <strong>and</strong> sugarcrops<strong>Biofuel</strong> <strong>feed</strong>stockOil seeds Green maize Maize stover <strong>and</strong> straw WoodComponent Starch <strong>and</strong> sugar Vegetable oil Carbon Carbohydrate <strong>and</strong> sugar CarbonComponent extraction Hydrolysis Extraction Anaerobic digestion Hydrolysis G<strong>as</strong>ificationtechnologyComponent extractionefficiency98.5% 80%–96% 81% 58% 100%<strong>Biofuel</strong> productiontechnologyFermentation Trans esterification Anaerobic digestion Fermentation Fischer-TropschprocessProduct Ethanol Fatty acid methyl ester Methane Ethanol Middle distillateComponent selectivity 93% 95% 75% 82% 74%Stoichiometric energy<strong>co</strong>nversion efficiency95.9% 99.7% 90% 96% 69%Crop energy efficiency 97.5% 99.9% 55% 46% 51%

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