Oil extracted from spent coffee grounds as a renewable source for fatty acid methyl ester manufacturing

被引:208
|
作者
Al-Hamamre, Zayed [1 ]
Foerster, Sascha [2 ]
Hartmann, Franziska [2 ]
Kroeger, Michael [2 ]
Kaltschmitt, Martin [2 ,3 ]
机构
[1] Univ Jordan, Fac Engn & Technol, Dept Chem Engn, Amman 11942, Jordan
[2] Deutsch Biomasseforschungszentrum Gemeinnutzige G, D-04347 Leipzig, Germany
[3] Hamburg Univ Technol, Inst Environm Engn & Energy Econ, D-21073 Hamburg, Germany
关键词
Methyl ester; Coffee oil; Spent coffee grounds; Extraction; Polar-nonpolar solvents; WASTE COOKING OIL; BIODIESEL PRODUCTION; VEGETABLE-OILS; TRANSESTERIFICATION; OPTIMIZATION;
D O I
10.1016/j.fuel.2012.01.023
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The effect of different extraction solvents (polar and non-polar) on yield, chemical and physical properties, including free fatty acid content (FFA) or acid value (AV), saponification value (SV), density, viscosity, elemental composition and heating values of oil extracted from spent coffee grounds (SCG) is investigated. The Soxhlet extraction method is utilized for the extraction of oil from spent coffee grounds. Iso-propanol, ethanol, and acetone as polar solvents and toluene, chloroform, hexane and n-pentane as nonpolar solvents are used. For each solvent, the oil yield is recorded for different time spans. The results show that the highest oil yield (15.3%) is achieved using hexane as an extraction solvent after 30 min of extraction time. The AV and SV of the extracted oils vary depending on the extraction solvent. The results indicate that AV of SCG oil extracted with hexane is 3.65% (7.3 mg(KOH)/g). This value is lower than the values for spent coffee oil extracted with the other solvents (ethanol 3.85%, isopropanol 6.4%, chloroform 4.55%, and toluene 4.15%). Free fatty acids (FFA) of the extracted oil are converted into fatty acid methyl ester (FAME) by base-catalyzed esterification. Effects of temperature, the ratio of FFA to the methanol-KOH solution and the reaction time are investigated. With one step alkali-catalyzed transesterification, oil conversion to methyl ester can be enhanced from approx. 55-85% by increasing the reaction time, the reaction temperature and the MeOH-KOH/FFA ratio. However, a complete oil conversion could only be achieved by utilizing a two-steps transesterification process. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:70 / 76
页数:7
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