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Estimation of measurement uncertainty for the determination of the ...

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Content <strong>of</strong> neutral lipids, %Fatty acid content, %Lipid content <strong>of</strong> extracts, %Table 6. Lipid content <strong>of</strong> <strong>the</strong> extracts from dried sources.C<strong>of</strong>feeresidue,g.D. I. Yordanov, Z. B. Tsonev, T. V. Palichev, Z. A. Mustafa/Petroleum & Coal 55(2) 74-81, 2013 80Temperature<strong>of</strong> drying, CTime <strong>of</strong>drying, h.Rawmaterial <strong>for</strong>extraction,gTime <strong>of</strong>extraction,hProduct,g.Total lipidcontent, %20 150 4 20 2 0.8577 2.2920 20 24 20 2 1.6805 5.6380Sterol esters Triacylglycerols Non identified8070Sterols+Diacylglycerols+FFAMonoacylglycerols+Polar lipids706060505040403030202010100450 W 300 W Dried at 20°C 120-150°C 600WFig. 8. Data <strong>for</strong> <strong>the</strong> content <strong>of</strong> neutral lipids frоmextracts based on <strong>the</strong> results <strong>for</strong> Table 40450 W 300 W Dried at 20°C 120-150°C 600WFig. 9. Lipid content <strong>of</strong> <strong>the</strong> extracts.100Sum <strong>of</strong> unsaturated fatty acidsSum <strong>of</strong> saturated fatty acids9080706050403020100450 W 300 W Dried at 20°C 120-150°C 600WFig. 10. Content <strong>of</strong> <strong>the</strong> unsaturated and saturated fatty acids in <strong>the</strong> extracts.5. Conclusions1. We were per<strong>for</strong>med <strong>the</strong> microwave irradiation processing and drying at 120-150 C <strong>for</strong>4 hours <strong>of</strong> <strong>the</strong> c<strong>of</strong>fee residue from <strong>the</strong> vending machine. The products obtained were usedas raw materials <strong>for</strong> <strong>the</strong> extraction <strong>of</strong> lipids by n-hexane.2. From our study we may conclude that microwave irradiation and heat treatment <strong>of</strong> <strong>the</strong>c<strong>of</strong>fee residue increase <strong>the</strong> amount <strong>of</strong> saturated fatty acids <strong>of</strong> <strong>the</strong> c<strong>of</strong>fee oil.3. The lipid extract derived from <strong>the</strong> processing <strong>of</strong> c<strong>of</strong>fee residue with microwave radiationpower <strong>of</strong> 600W, contains <strong>the</strong> greatest amount <strong>of</strong> lipids (8.07%). This is probably due to<strong>the</strong> flow <strong>of</strong> high-energy cracking under <strong>the</strong> influence <strong>of</strong> powerful microwave radiation to<strong>the</strong> molecules in <strong>the</strong> c<strong>of</strong>fee residue, resulting in increased total lipid content.4. The sample obtained at 600W microwave has <strong>the</strong> balanced composition <strong>of</strong> saturatedand unsaturated fatty acids <strong>of</strong> approximately 50%. This allows us to <strong>of</strong>fer exactly this way<strong>of</strong> handling <strong>the</strong> raw material to obtain <strong>the</strong> biodiesel.

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