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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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6<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>2 440FIGURE 32010 world <strong>feed</strong>stock usage for biodiesel(thous<strong>and</strong> tonnes)2 230Rapeseed oilSoybean oilPalm oilSource: F.O. Licht, 2011211 1615 700Animal fats & yellow gre<strong>as</strong>eSunflower oilOther5 750Animal fats <strong>and</strong> yellow gre<strong>as</strong>eAnimal fats are derived from the rendering process usinganimal tissues <strong>as</strong> the raw material. The raw material is aby-product of the processing of meat animals <strong>and</strong> poultry.The amount of fat produced is directly related to the speciesof animal processed <strong>and</strong> the degree of further processingthat is <strong>as</strong>sociated with the marketing <strong>and</strong> distribution ofthe meat product. Current markets for rendered animal fatsinclude use <strong>as</strong> <strong>feed</strong> ingredients for <strong>livestock</strong>, poultry, <strong>co</strong>mpanionanimals <strong>and</strong> aquaculture. In addition, <strong>products</strong> such<strong>as</strong> edible tallow are used for soap <strong>and</strong> fatty acid production.Industry analysts anticipate that roughly 25 to 30 percentof the rendered animal fat supplies <strong>co</strong>uld be diverted tobiodiesel production given current uses (Weber, 2009).In 2010, an estimated 2.2 million tonne of animal fats<strong>and</strong> yellow gre<strong>as</strong>e w<strong>as</strong> used globally in the production ofbiodiesel (F.O. Licht, 2011), representing 14 percent of thetotal <strong>feed</strong>stocks used in global biodiesel production. EUproducers used 54 percent of animal fats <strong>and</strong> yellow gre<strong>as</strong>eprocessed <strong>as</strong> biodiesel <strong>feed</strong>stock in 2010, followed by Brazil(16 percent) <strong>and</strong> the United States (12 percent).Maize oil from ethanol production processesGrain ethanol production may offer the biodiesel industryits nearest-term opportunity for a significant additive supplyof plant oils for biodiesel production. Historically, maizeoil h<strong>as</strong> not been a viable biodiesel <strong>feed</strong>stock due to itsrelative high <strong>co</strong>st <strong>and</strong> high value <strong>as</strong> edible oil. However, <strong>as</strong>discussed earlier, some dry-mill ethanol plants in the UnitedStates are now removing crude maize oil from the stillageat the back end of the process. The maize oil is typicallymarketed <strong>as</strong> an individual <strong>feed</strong> ingredient or sold <strong>as</strong> a <strong>feed</strong>stockfor further processing (e.g. for biodiesel production).Maize oil <strong>co</strong>uld help to meet <strong>feed</strong>stock market dem<strong>and</strong> intwo ways. First, edible maize oil <strong>co</strong>uld displace other edibleoils that <strong>co</strong>uld then be diverted to biodiesel production.Se<strong>co</strong>nd, non-edible maize oil <strong>co</strong>uld be used directly forbiodiesel production.Biodiesel production processRegardless of the <strong>feed</strong>stock, most biodiesel globally is producedusing one of three <strong>co</strong>mmon manufacturing methods:reaction of the triglycerides with an al<strong>co</strong>hol, using ab<strong>as</strong>e catalyst; reaction of the triglycerides with an al<strong>co</strong>hol,using a strong acid catalyst; or <strong>co</strong>nversion of the triglyceridesto fatty acids, <strong>and</strong> a subsequent reaction of the fattyacids with an al<strong>co</strong>hol using a strong acid catalyst.In the United States <strong>and</strong> elsewhere, biodiesel is <strong>co</strong>mmonlyproduced using the b<strong>as</strong>e-catalyzed reaction of thetriglycerides with al<strong>co</strong>hol. Methanol is currently the mainal<strong>co</strong>hol used <strong>co</strong>mmercially for the production of biodieseldue to its <strong>co</strong>st relative to other al<strong>co</strong>hols, shorter reactiontimes <strong>co</strong>mpared with other al<strong>co</strong>hols, <strong>and</strong> the difficulty <strong>and</strong><strong>co</strong>st of recycling other al<strong>co</strong>hols.Use of acid catalysis is typically limited to the <strong>co</strong>nversionof the fatty acid fraction in high free fatty acid <strong>feed</strong>stocks,or to treat intermediate high fatty acid/ester streams thatcan form in the acidification of the crude glycerin bottomsproduced <strong>as</strong> a <strong>co</strong>-product of the transesterification reaction.Stoichiometrically, 100 kg of triglycerides are reactedwith 10 kg of al<strong>co</strong>hol in the presence of a b<strong>as</strong>e catalystto produce 10 kg of glycerin <strong>and</strong> 100 kg of mono-alkylesters or biodiesel. In practice, an excess amount of al<strong>co</strong>holis used in the reaction to <strong>as</strong>sist in quick <strong>and</strong> <strong>co</strong>mplete<strong>co</strong>nversion of the triglycerides to the esters, <strong>and</strong> the excessal<strong>co</strong>hol is later re<strong>co</strong>vered for re-use. All reactants must beessentially free from water. The catalyst is usually sodiummethoxide, sodium hydroxide or pot<strong>as</strong>sium hydroxide thath<strong>as</strong> already been mixed with the al<strong>co</strong>hol.In some c<strong>as</strong>es, the free fatty acid levels of the <strong>feed</strong>stockutilized are elevated to the point that an esterificationstep, using an acid catalyst, is in<strong>co</strong>rporated into thebiodiesel processing sequence. This stage involves mixingthe high fatty acid material with a solution of methanolthat <strong>co</strong>ntains an acid catalyst, typically sulphuric acid. The<strong>co</strong>ntained fatty acids are then <strong>co</strong>nverted to methyl ester.An excess of methanol <strong>and</strong> H 2 SO 4 is employed to ensure<strong>co</strong>nversion, <strong>and</strong> after reaction <strong>co</strong>mpletion this excess isseparated from the ester ph<strong>as</strong>e. The <strong>co</strong>nversion of the fattyacid to ester results in the formation of water, thus afterthe reaction there is water in the methanol+sulphuric acidmixture. Since this is an equilibrium reaction, the presence

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